Hydraulic vs. Mechanical Snubbers: How to Choose for Your Application

Hydraulic and Mechanical Snubbers both serve the same fundamental purpose: allow normal thermal movement with low resistance while restraining the piping system during a dynamic event. They operate on different principles, and those differences must be evaluated alongside the required load capacity, thermal travel, dynamic response, and installation geometry when selecting a device. 

This comparison specifically addresses Fronek Anchor/Darling hydraulic snubbers and DynA/Damp non-locking mechanical snubbers. Other manufacturers’ mechanical snubbers may operate differently. 

 Hydraulic Snubber
Hydraulic Snubber

Hydraulic Snubbers

The Fronek hydraulic snubber is a manifold design hydraulic component consisting of a high-pressure main cylinder, a flow control section with dual-stage velocity-sensitive poppet valves, and a spring-energized reservoir. Under normal operating conditions, the poppet valves remain open, and the piston moves freely in either direction with no restriction to fluid flow for all piston velocities up to the activation velocity. When piston velocity reaches the activation threshold, the poppet valve closes, substantially restricting hydraulic flow and resisting rapid movement. Controlled movement remains possible through the designed bleed path.  When the disturbance subsides and the valve resets, low-resistance movement resumes. Activation velocity and bleed rate are important selection and functional-test parameters. 

Note: “Movement is blocked” suggests an absolute rigid lock. Fronek’s published operating description identifies a controlled bleed rate after activation. 

Key operational characteristics:

  • Designed for continuous operation up to 200°F with brief transients to a maximum of 300°F at the snubber. 
  • Seven sizes with cylinder bores of 1.5 to 8 inches
  • Normal load range of 3,000 to 130,000 lbs
  • Available in 6, 12, and 18-inch strokes
  • Spherical self-aligning ball bushings allow for plus or minus 5 degrees of angular motion or misalignment
  • Pressurized reservoir allows mounting in any spatial orientation
  • Virtually no resistance to normal thermal movements of piping
  •  Standard settings are not intended to control low-amplitude, high-frequency vibration: suitability requires evaluation of the actual motion and activation characteristics. 

Snubber temperature must be distinguished from pipe operating temperature. The thermal conditions at the snubber body, seals, and fluid govern its suitability; pipe temperature alone does not establish the snubber’s operating temperature. 

Mechanical Snubber
Mechanical Snubber

Mechanical Snubbers

The Fronek mechanical snubber uses an oscillatory-type escapement mechanism to restrict pipe movement to a constant velocity when a dynamic disturbance attempts to displace piping or equipment. It is a non-locking, velocity-limiting device that is always engaged and responds to dynamic disturbances instantly. It permits gradual thermal movements virtually unrestricted while providing a damping force proportional to the magnitude of the disturbance during a dynamic event.

Key operational characteristics:

  • Continuous operation at 150°F with brief transients to 350°F
  • 40 years of virtually maintenance-free operation
  • Radiation-resistant lubrication
  • Corrosion-resistant materials
  • Suitable for ASME Section III construction
  • Instantaneous dynamic response
  • No hydraulic fluid required; mechanical snubbers use only grease
  • Seven models with load ratings from 400 lbs (AD-40) to 125,000 lbs (AD-12500), each in four configurations

Note: Load ratings stated above apply to commercial units only. For nuclear applications, consult the applicable load capacity data sheet or design report.

💡Engineering Takeaway: Load capacity alone does not prove vibration control. Check response at the expected frequency and motion.

How the Two Differ in Application

Hydraulic Snubber Mechanical Snubber
Operating principle Velocity-sensitive poppet valve closes above activation threshold, restricting flow while permitting controlled bleed  Oscillatory escapement mechanism limits the rate of relative movement without rigid lock-up 
Activation mechanism Dual-stage velocity-sensitive poppet valves Oscillatory-type escapement, always engaged
Normal thermal movement Low resistance within specified drag limits below activation velocity Permits gradual thermal movement with low resistance within specified drag limits 
Continuous operating temperature Up to 200°F with brief transients to 300°F Published values: 150°F continuous / 350°F brief transient; verify applicable model and approved limits 
Load range 3,000 to 130,000 lbs (seven standard sizes) 400 to 125,000 lbs (seven models, commercial; nuclear consult data sheet)
Fluid requirement Requires approved hydraulic fluid  No fluid required 
Maintenance Applicable examinations and functional testing, with attention to fluid level, leakage, seals, and performance  40 years of virtually maintenance-free operation
Orientation Pressurized reservoir allows mounting in any spatial orientation Confirm permitted orientation and attachment arrangement for the selected model 
Low-amplitude, high-frequency vibration Standard settings are not intended for this duty; engineering review required  Suitability is not established by the escapement principle alone; engineering review required 

 

Fluid Requirements for Hydraulic Snubbers

SF-1154 is a silicone-based hydraulic fluid used in hydraulic snubbers. It is used in hydraulic snubbers with nuclear applications where thermal stability and resistance to radiation-induced degradation are important. Mechanical snubbers do not require this fluid. But their specified lubrication remains important to reliable operation. 

SF-1154 is compatible with all major hydraulic snubber and dynamic restraint makes and models. It is manufactured in Germany and is the established quality standard across the nuclear sector. Specifying a hydraulic snubber in an application where the correct fluid cannot be sourced or maintained within the required timeline is a practical constraint that must be evaluated as part of the selection decision.

💡 Field Note: Check usable stroke at both hot and cold positions. Set installation length to preserve required travel.

For questions on hydraulic and mechanical snubber selection for a specific application, schedule a meeting with Fronek’s engineering team, contact us, or request a quote. Providing the required loads, thermal movements, dynamic-event or vibration data, operating environment, and installation dimensions will help our team evaluate the appropriate configuration. 

10CFR50 and Snubber Testing: What Nuclear Plants Are Required to Do and Why It Matters

Nuclear plants operating in the United States are subject to Title 10, Code of Federal Regulations, Part 50, referred to as 10CFR50. For snubbers, this regulation defines the quality assurance and testing framework governing how snubbers are manufactured, installed, tested, and maintained throughout the operating life of the plant.

What 10CFR50 Covers for Snubbers

10CFR50 is the primary federal regulation governing the domestic licensing of nuclear power plants, administered by the Nuclear Regulatory Commission(NRC). Two provisions apply directly to snubbers.

10CFR50 Appendix B establishes the Quality Assurance Criteria for Nuclear Power Plants. It defines the requirements governing how safety-related components are designed, fabricated, inspected, tested, and documented. Any hydraulic or mechanical snubber installed in a safety-related application must be manufactured under a quality program that meets these requirements.

Fronek Anchor/Darling’s quality program meets the requirements of 10CFR50 Appendix B, along with:

  • ASME NQA-1 (as mandated by Nuclear Components and Assemblies -4000)
  • NCA-3800
  • ANSI/ASME N45.2
ASME NS Certificate of Accreditation
ASME NS Certificate of Accreditation

Fronek has held an ASME NS Certificate of Accreditation since the early 1980s, enabling the manufacture of component and pipe supports in accordance with Section III of the ASME Boiler and Pressure Vessel Code. The scope covers welded and non-welded Class 1, 2, 3, and MC supports with design responsibility for nuclear facilities worldwide.

NRC Bulletin 75-05: The Regulatory Basis for Snubber Functional Testing

The functional testing requirements for snubbers at nuclear plants trace directly to NRC Inspection and Enforcement Bulletin No. 75-05. As documented in Fronek’s functional testing technical bulletin, Bulletin 75-05 became the primary document for licensee action on snubber testing.

The bulletin established that while the failure of a single suppressor would not normally defeat the design function of the restraint system, periodic testing of a representative sample from the total population is necessary to assess operational capability on a continuing basis.

As a requirement of the bulletin, each licensee operating a power reactor facility under NRC authorization was required to:

  • Review the design and installation of the hydraulic restraint systems
  • Review the design requirements each suppressor is intended to meet, including velocity, acceleration, load, and release rate
  • Describe testing performed on hydraulic suppressors by both the licensee and supplier prior to installation
  • Describe surveillance programs and test procedures enforced or planned to be enforced for operability throughout the facility’s life

The reports submitted in response to Bulletin 75-05, combined with additional performance data, contributed to the NRC circulars and ultimately to the functional test and inspection criteria now part of licensee operating technical specifications.

Hydraulic Snubber
Hydraulic Snubber

Operational Design Criteria: What the Functional Test Confirms

Every Fronek hydraulic snubber is individually tested before shipment against three operational design criteria that apply to all bore sizes:

Criterion Requirement
Free movement Piston moves freely in either direction with poppet valves fully open at all velocities at or below 10 inches per minute. Tolerance: plus or minus 2 inches per minute.
Lock-up Poppet valves close when piston velocity reaches 10 inches per minute in both compression and extension strokes. Tolerance: plus or minus 2 inches per minute.
Bypass release rate After valve closure, the orifice permits continued piston movement in either direction at 4 to 6 inches per minute at rated design capacity.

These three parameters are what every functional test is designed to confirm. A unit that fails any one of these criteria requires an operability determination and may trigger an extent-of-condition review covering similar units across the plant.

💡 Engineering Takeaway: A factory acceptance value is not automatically a universal field criterion. Use the model-specific procedure and the plant’s approved surveillance basis.

HSSA Size and Rated Capacity Reference

The hydraulic shock and sway arrestor units are available in the following standard catalog sizes. Load rating and bore size are the primary selection parameters for a given installation:

HSSA Size Cylinder Bore Rated Capacity
3 1.50 in 3,000 lbs
10 2.50 in 10,000 lbs
20 3.25 in 20,000 lbs
30 4.00 in 30,000 lbs
50 5.00 in 50,000 lbs
70 6.00 in 70,000 lbs
130 8.00 in 130,000 lbs
200 10.00 in 200,000 lbs

The restraint designer establishes the as-installed loading and movement conditions by formal calculation and selects the standard unit with load and movement capabilities greater than the calculated requirements, accounting for capacity reduction due to column action of the overall strut length.

How Fronek Tests Each Unit Before It Ships

The factory testing procedure, documented in Fronek’s functional testing technical bulletin, confirms all three criteria above before a unit leaves the facility:

  • The cylinder is placed horizontally in a calibrated test stand with a force transducer and velocity instrumentation package
  • A bind test is run before fluid charging to confirm piston rod alignment and freedom of movement
  • The cylinder is charged with fluid and a minimum pressure of 4,500 psi is applied for at least 20 seconds while fluid containment is visually checked
  • The poppet valve closure test is run in each direction of stroke by incrementally increasing piston velocity until valve activation is confirmed
  • The bypass release rate is checked in each direction under rated force conditions
  • The unit stands on clean paper after testing for a final visual leakage check

This sequence is applied to every unit individually, not on a sampling basis.

Why Temperature Normalization Is Required During Field Testing

The performance characteristics of a hydraulic shock and sway arrestor vary with temperature due to changes in fluid viscosity and density. As confirmed in Fronek’s functional testing technical bulletin, empirical analysis has established the following:

  • Activation velocity varies by approximately 0.2 inches per minute per degree Fahrenheit across a test range of 60 to 95 degrees Fahrenheit
  • Bypass release rate varies by approximately 0.05 inches per minute per degree Fahrenheit across the same range

A unit tested at a field temperature significantly different from the factory calibration temperature will produce results that appear to fall outside the acceptance range even when the unit is performing correctly. Failure to normalize test results to the initial factory calibration criteria produces incorrect failure analysis. This is a documented source of erroneous functional test failures in the field.

💡 Field Note: Record unit temperature and the approved correction method with the test data. An uncorrected reading can lead to an incorrect acceptance decision.

Replacement Parts and Code of Service Ordering

For nuclear plants ordering replacement parts or replacement cylinders for safety-related snubbers, the code of service designation on the purchase order determines the quality requirements the part must meet. Fronek’s replacement parts ordering requirements specify that each order must include one of the following designations:

  • ASME Section III
  • 10CFR50 Appendix B
  • ANSI N45.2
  • Commercial grade

Ordering a safety-related replacement part under a commercial grade designation, or omitting the code of service entirely, means the part will not be manufactured to the documentation and traceability requirements that 10CFR50 Appendix B demands. This is one of the most common ordering errors on replacement parts for aging nuclear snubber populations and one of the most straightforward to prevent. For plants reviewing their legacy snubber populations, the considerations involved are covered in detail in Why Old Nuclear Plants Are Replacing Aging Piping Snubbers.

Summary

10CFR50 Appendix B governs the quality assurance requirements for every safety-related snubber manufactured for a nuclear plant. NRC Bulletin 75-05 established the functional testing framework licensees are required to implement. The three operational design criteria, free movement below 10 inches per minute, lock-up at 10 inches per minute, and a bypass release rate of 4 to 6 inches per minute at rated capacity, are what every functional test confirms. Temperature normalization of test results is required for accurate pass/fail determination. Correct code of service designation on replacement parts orders ensures a replacement component meets the same quality standard as the original.

For questions on snubber quality requirements, functional test criteria, or replacement parts ordering under 10CFR50 Appendix B, schedule a meeting with Fronek’s engineering team, contact us, or request a quote.

Case Study: Three Recent Engagements on Aging Snubbers in the Nuclear Fleet

The three cases below are drawn from active nuclear plant engagements, and each reflects a different aspect of the obsolescence, parts scarcity, and maintenance burden driving plants to reassess their installed snubber populations. 

For a broader overview of why aging nuclear fleets are moving away from legacy hardware, refer to this blog: Why Old Nuclear Plants Are Replacing Aging Piping Snubbers. 

Hydraulic Snubber
Hydraulic Snubber

Case 1 – Obsolete Part Number: When a Database Record No Longer Corresponds to a Buildable Part

Background

A nuclear plant issued a request for a rear bracket assembly against a specific part number. On review, that part number had no active record in the manufacturer’s system.

The Challenge

An obsolete part number on an RFQ does not always mean the part itself is gone; it may mean the number was superseded, revised, or incorrectly transcribed from an aging drawing. Quoting against a non-existent part number produces a purchase order that cannot be fulfilled. The correct response is to identify what the plant actually needs before a quote goes out.

How It Was Resolved

Fronek’s engineering team flagged the obsolete number and proposed the likely current equivalent pending confirmation from the plant. The site engineer cross-referenced the part number against the plant’s own asset records, confirmed a single-digit transcription error in the original request, and provided the original installation drawing to close the loop. The quotation was issued against the correct part number, and the plant requested that the drawing reference be added to the part description going forward, a documentation fix that prevents the same search from recurring on the next order. 

💡  Key Insight: Validate the part number and drawing before quoting legacy hardware.

Engineering Consideration

A part number carried forward from a 1970s or 1980s drawing into a plant’s computerized maintenance management system may have undergone multiple revision cycles since its original installation. Confirming current equivalency before quoting is a standard step in Fronek’s application review process. For plants working through legacy part identification, Fronek’s replacement parts and replacement cylinders pages provide current configuration equivalents for Bergen-Paterson and other legacy designs. 

Mechanical Snubbers
Mechanical Snubbers

Case 2 – Parts Scarcity: Inter-Utility Exchange for an AD-500 Series Mechanical Snubber

Background

A nuclear plant had an urgent operational need for AD-500 series mechanical snubbers. The new manufacturing lead time for that design was approximately three months, beyond what the plant’s schedule could accommodate.

The Challenge

We typically manufacture nuclear-grade snubbers to order rather than maintain them in stock. When new manufacturing lead time exceeds a plant’s operational requirement, the only practical options are a qualified rebuild from another utility or a sourced unit from the industry’s established exchange program. Neither option is straightforward; traceability documentation, radiation status confirmation, and qualification records must all be in order before a unit can transfer between plants.

How It Was Resolved

Fronek identified a nuclear plant operating a qualified Anchor Darling rebuild shop, one of the few remaining outside the original manufacturer, that had two rebuilt and tested AD-501 units available. Both units were confirmed as low-radioactivity (low-RAD), meaning their radiation levels had been measured and cleared for handling and reuse under standard controls. Serial numbers were traced back to the original purchase order for documentation continuity, and Fronek supported the paperwork, including an industry-standard transfer letter, required to complete the inter-utility transfer under the nuclear industry’s established Exchange Program. The transfer provided a bridge unit while the new manufacture order proceeded on its standard timeline.

Engineering Consideration

The AD-500 series case is a direct illustration of how thin the remaining supply of original 1980s-era mechanical hardware has become across the nuclear fleet. For plants carrying mechanical snubbers of this generation, new manufacture is not always an option on a compressed timeline, and exchange program availability is not guaranteed. For plants considering conversion from mechanical to hydraulic units, the engineering considerations are covered in The Real Cost of Improper Snubber Selection.

Case 3 – Maintenance Reality: Supporting a Legacy Hydraulic Fleet Without Complete Assemblies

Background

A nuclear plant contacted Fronek needing either a complete safety-related BP-70 hydraulic snubber assembly or the parts and fluid required to rebuild an existing unit in place.

The Challenge

For hydraulic snubbers this old, complete safety-related units usually aren’t sitting on the shelf. The usual approach is to keep seals, fluid, and spare internal parts on hand to maintain the existing units between outages. Full rebuilds or replacements are typically planned for an outage. 

How It Was Resolved

Fronek had 70 Kip seal kits, SF-1154 silicone-based hydraulic fluid, and the majority of the internal rebuild components on hand. The one gap was the main cylinder heads, which require separate fabrication. The plant was provided with the available components to proceed with an in-place rebuild while the cylinder heads were manufactured.

Engineering Consideration

This engagement reflects the day-to-day maintenance reality for plants still running original 1970s and 1980s hydraulic hardware. Complete assemblies are the exception. Keeping units operational between outages depends on parts depth, particularly seals, fluid, and wear components, rather than complete unit availability. Fronek’s replacement parts inventory is maintained specifically to support this kind of between-outage servicing for legacy hydraulic populations. For the quality and certification framework governing replacement components, refer to Fronek’s Standards and Specifications.

Summary

Case Core Issue Resolution
Case 1 – Obsolete Part Number Part number in plant database had no active manufacturer record Current equivalent confirmed; drawing reference added to prevent recurrence
Case 2 – Parts Scarcity New manufacturer lead time exceeded plant schedule for AD-500 series mechanical unit Low-RAD rebuilt units sourced through inter-utility exchange program with full traceability documentation
Case 3 – Legacy Hydraulic Maintenance Complete safety-related assembly unavailable for BP-70 design Seal kits, fluid, and internal components supplied for in-place rebuild; cylinder heads manufactured separately

Each of these three cases required a different response, a records check, a connection to another utility’s rebuild inventory, and a parts search against a design that has not been manufactured as a complete assembly in decades. Taken together, they reflect the condition of the nuclear fleet’s oldest snubber populations: obsolete records, a diminishing pool of original mechanical hardware, and a maintenance load that does not ease between outages.

For plants working through a part number search, evaluating a rebuild against a replacement, or assessing what remains available for a legacy snubber population, schedule a meeting with Fronek’s engineering team, contact us, or request a quote before the next outage window closes.

Why Old Nuclear Plants Are Replacing Aging Piping Snubbers

What Forty Years in Service Does to a Snubber Population

Most piping snubbers operating in nuclear plants today were installed during original construction in the 1970s and 1980s. As plants move into subsequent license renewal and plan for sixty or eighty years of operation, that original hardware is reaching the point where conventional maintenance is no longer straightforward. The following covers five reasons plants are increasingly retiring legacy hydraulic and mechanical piping snubber (also known as dynamic pipe restraints) populations rather than continuing to rebuild them. 

Snubber Replacement Parts
Snubber Replacement Parts

1. Obsolescence

Part numbers, drawings, and assembly specifications from the 1970s and 1980s have gone through decades of engineering revisions and, in a significant number of cases, they’ve been discontinued. A part number recorded in a plant’s database does not always correspond to anything a manufacturer can currently produce.

Fronek’s engineering team has received RFQs for part numbers that have become obsolete, requiring detailed technical investigation to confirm an equivalent before a quotation can be issued. For plants working through legacy part identification, Fronek’s replacement parts and replacement cylinders pages provide current configuration equivalents for Bergen-Paterson and other legacy designs. A single-digit discrepancy between a plant’s records and the manufacturer’s current catalog is enough to stall an order until the conflict is resolved.

Hydraulic Snubber Assembly
Hydraulic Snubber Assembly

2. Corrosion

A large portion of original snubber installations are located outdoors or in high-heat, high-humidity environments, with limited access for condition assessment between outages. Forty or more years of that exposure on pins, housings, and mounting hardware has an impact on various snubber parts, in ways that are not visible without disassembly.

In severe cases, corrosion has advanced to the point where a unit cannot be safely disassembled for rebuilding without risking component-level damage. What was initially scoped as a routine rebuild becomes a full replacement decision once the unit is opened.   

💡  Pre-outage field verification and a defined inspection plan reduce surprises. Photograph the installation, record identifying information, verify clearances and attachment geometry, and identify access or radiological constraints before committing to scope and schedule.

3. Maintenance Burden

The serviceability of a legacy snubber often cannot be determined from external inspection. A full teardown is required to assess which internal components remain within acceptable tolerances and which do not. When degraded parts are not in inventory, they must be manufactured from scratch. A job scoped as a two-week rebuild can extend to two months when custom fabrication of internal components is required. Carried across a large population of aging units, that uncertainty creates significant planning risk for a maintenance program. Refer to Fronek’s Standards and Specifications for the quality and certification framework that governs replacement component manufacturing.

Snubber Assemblies for a Power Plant
Snubber Assemblies for a Power Plant

4. Legacy Mechanical Units

Mechanical snubbers were the standard design through the 1970s and 1980s. Prominent manufacturers from this period included Pacific Scientific, Anchor/Darling, and Basic-PSA, among others. Many of those original designs have been out of production for decades, although their products remain installed at several utilities. 

Units of the same model number may have been rebuilt or modified differently over the years, meaning parts that appear interchangeable based on nameplate data may not function identically in service.

When a new manufacturer is not available on the required timeline, rebuilt low-radiation replacement units sourced from other utilities through industry exchange programs are one option. It is not uncommon for a specific mechanical design to have gone unbuilt since the mid-1980s. For plants considering a conversion, the engineering considerations involved are covered in The Real Cost of Improper Snubber Selection. 

💡  The best time to resolve a legacy-snubber decision is before the outage schedule is fixed. Early identification permits the plant to compare repair scope, replacement lead time, engineering review, and contingency options on the same basis.

5. Outage-Driven Replacement Decisions

Snubbers can only be pulled, inspected, or replaced during a scheduled outage. That maintenance window, typically every eighteen to twenty-four months, is the only practical opportunity to act on a legacy unit. Functional testing requirements under 10CFR 50 (which sets the rules for building and running nuclear reactors and other large nuclear facilities in the United States) add further scheduling constraints to an already compressed window.
An uncertain rebuild timeline is difficult to reconcile with a fixed return-to-service date. When the rebuild scope cannot be defined until the unit is disassembled, the schedule risk often tips the decision toward a new unit rather than restoring a legacy one, particularly for mechanical designs where parts availability is already constrained.

Summary

The pressures described above are not unusual for plants operating hardware well beyond their original design life. Obsolete part numbers, corroded internals, uncertain rebuild timelines, and a fixed maintenance calendar combine to make the rebuild-versus-replace decision more complex than it once was.

For plants evaluating a legacy snubber population ahead of an outage, whether the question is rebuild feasibility, parts availability, or equivalent specification for an obsolete unit, schedule a meeting with Fronek’s engineering team, contact us, or request a quote before the outage window closes.

How Fronek Supports Snubber Projects at Every Stage – Three Case Studies From The Field

Hydraulic Snubber Being Assembled

Background

Snubber design support does not look the same at every stage of a project. An RFQ with almost no data attached, requires a different kind of engineering response before fabrication or a phone call in the middle of an outage-driven rebuild. The three cases below are drawn from actual customer engagements handled by Fronek Anchor/Darling Enterprises. Each one required application review, whether that was drawing markups, technical consultation, retrofit assistance, or custom configuration, at the point in the project where it was actually needed.

Problem

In all three engagements, the information available at the start of each request was insufficient to specify a correct snubber configuration. The first involved an alternate quote request built around a competitor’s part number with no load or displacement data attached. The second required confirming fit, hardware compatibility, and installation position before drawings went to the client, then catching a bracket count discrepancy when the markups came back. The third involved aging mechanical units that could not be rebuilt on the outage schedule, requiring a technically justified conversion to hydraulic replacements – sized from actual field conditions.

Engineer Evaluating Deliverables
Engineer Evaluating Deliverables

Case 1 – Alternate Quote: From a Part Number to a Specification

A distributor’s sales representative submitted a RFQ asking Fronek to quote an alternative to a competitor’s unit, identified only as “ASC C-201,” with a note that additional information could be provided on request.

The Challenge

An alternate quote is only as good as the engineering behind it. Without engineering details such as –

  • The actual design load  
  • The expected thermal displacement at the installation point

Matching a competitor’s unit is guesswork. And guesswork on a snubber selection produces the same misfits at installation that a poorly considered original selection does. Fronek’s engineering team requested the load and displacement data before recommending a configuration. 

How It Was Resolved

Using the confirmed design load of 14,700 lbs (approximately 15 Kips) and a net thermal displacement of 3.174 inches in the z-plane, Fronek recommended a Fig. 511AD 20 Kip x 6″ hydraulic snubber with one structural attachment and a pipe clamp. 

And because the unit being replaced was a 10-inch-stroke Grinnell, the same 511AD built as a 20 Kip x 12″ was offered in case the client preferred the additional stroke for future flexibility and operating margin. 

Both options were passed to the quotations team for lead time and pricing before being returned to the client.

Engineering Support Applied

  • Application Review: Confirmed the actual design load and thermal displacement before recommending a configuration, rather than matching a catalog number to a competitor’s part.
  • Custom Configuration: Two-stroke options were presented: the calculated minimum and an upsized alternative, based on the client’s operating margin preference.
Hydraulic Snubber designed for LNG Facility
Hydraulic Snubber designed for LNG Facility

Case 2 – Drawing Review: Catching a Bracket Count Before Fabrication

An approval drawing and client data sheets for a hydraulic snubber replacement job were forwarded internally from PT&P’s sales team to Fronek Anchor/Darling’s engineering team, requesting confirmation that a matching unit could be supplied before the drawings went out to the client for approval.

The Challenge

Two things had to be resolved before fabrication could begin:

First, whether Fronek’s standard hydraulic snubber would fit the available space and be able to function correctly in the client’s preferred hot/cold position. 

Second, once the client’s markups came back, whether the assembly list and the drawing itself agreed on hardware requirements across all three units. 

How It Was Resolved

Fronek confirmed that a 10 Kip x 6″ hydraulic snubber fits the allotted space. 

As the unit’s pin size matched the existing Grinnell hardware, Fronek recommended the client leave the clamp and end brackets in place if they were not deteriorated, simplifying the replacement to the snubber body alone. 

Fronek also asked whether the client required the unit to be positioned in the hot or cold position before drawings were finalized. 

When the client’s markups came back, a review of the revised assembly sheet against the drawings identified a discrepancy on two of the three units. One unit showed an end bracket on the drawing that was not called out on the assembly list. A second unit showed two end brackets on the drawing, against a note for only one. Both discrepancies were flagged before the job was released to fabrication. The client confirmed that one end bracket was required across all three units, and the assembly sheet was corrected accordingly.

Engineering Support Applied

  • Application Review: Confirmed stroke, fit, hot and cold installation position, and pin compatibility with existing field hardware before approving the design for the client’s review.
  • Drawing Markups: Caught an end-bracket count discrepancy between the assembly list and the drawing on two of three units before fabrication began. Refer to The Snubber Terminology Guide for a detailed explanation of how pin-to-pin, preset, and attachment hardware interact in a snubber assembly.
Sway Strut
Sway Strut

Case 3 – Retrofit: Replacing Mechanical Units on an Outage Schedule

A utility’s piping SME requested an overhaul quote for four aging piping snubbers, a combination of 20 Kip hydraulic units and AD-1600L mechanical units, ahead of a scheduled spring outage, with a four-week turnaround targeted from removal to reinstallation. 

The Challenge

Once the units arrived and were disassembled, one AD-1600L mechanical unit proved corroded well past the point of economical repair. The spare part needed to rebuild the second mechanical unit carried a 12-to 14-week lead time, well outside the outage window. A like-for-like rebuild was not going to happen on the client’s schedule, which meant Fronek’s

engineering team needed to propose and technically justify an alternative, then reflect it correctly in the drawings before the client’s installation crew and third-party engineering firm signed off. 

How It Was Resolved

After a phone call to work through the client’s piping movement data, Fronek recommended replacing both mechanical units with equivalent hydraulic snubbers sized for actual field conditions. A cold pin-to-pin dimension of 75-1/4″, an expected movement of 5-1/2″, and an anticipated load of 6.0 Kips supported a 10 Kip hydraulic snubber with a 12″ stroke for each unit, built with a new structural attachment to replace the mounting hardware originally used by the mechanical struts.

The two hydraulic units that had been submitted separately for rebuild required only minor parts replacement and were completed on the original schedule. Once site measurements confirmed the true pin-to-pin dimensions, 73″ and 74,” against the preliminary drawing basis, Fronek issued corrected drawings with the piston rod set-point specified at +4 inches rather than mid-stroke, to accommodate approximately 6 inches of expected thermal displacement in the direction of pipe movement. The client’s maintenance department received an installation procedure ahead of the outage date.

Engineering Support Applied

  • Retrofit Assistance: Assessed rebuild feasibility unit by unit and proposed hydraulic replacements once the mechanical snubbers were found impractical to rebuild on the outage schedule.
  • Technical Consultation: Worked through the client’s actual piping movement data on a direct call to size the replacement, rather than defaulting to a like-for-like part swap.
  • Custom Configuration: A new structural attachment was engineered to mate with the hydraulic replacement to the mounting hardware originally built for a mechanical unit.
  • Drawing Markups: Pin-to-pin dimensions were corrected to site-measured values, and the preset was moved off mid-stroke to reflect the true thermal displacement in each direction.

For a broader look at what improper snubber selection costs when these steps are not taken, refer to The Real Cost of Improper Snubber Selection.

Summary

Case Support Provided Outcome
Industrial Distributor Application review translated a competitor’s part number into load- and displacement-based sizing, with two configuration options. Alternate snubber recommendation and lead times were delivered ahead of the client’s quote deadline.
Mining Client Application review confirmed fit and hardware compatibility; drawing markup caught an end-bracket mismatch on two of the three tagged units. Corrected assembly sheet issued; job proceeded to paint and shipment on the original schedule.
Utility Client Technical consultation and retrofit assistance replaced a non-repairable mechanical unit; drawing markups corrected pin-to-pin and set-point. Hydraulic replacement engineered and drawings corrected; units shipped ahead of the scheduled outage.

In each of these cases, the support Fronek provided was not a single deliverable. It was engineering judgment applied at whatever stage the project actually needed it, from a first RFQ with almost no data attached, to a markup review before fabrication, to a phone call in the middle of an outage-driven rebuild.

To discuss a specific snubber application, request a drawing review, or get engineering support on a retrofit, contact the Fronek Anchor/Darling team or request a quote.

How Fronek Supports Engineers’ Design from Inquiry to Installation

Field Engineer Evaluation
Field Engineer Evaluation

A significant portion of Fronek Anchor/Darling’s engineering work takes place before a purchase order exists. Application reviews, drawing markups, technical consultations, retrofit evaluations, none of it appears on an invoice, but each step directly determines whether a snubber fits the job it is being asked to do. 

This article covers five ways Fronek’s engineering team gets involved in a design, from first inquiry through fabrication. 

Field Engineer On-Site Inspection
Field Engineer On-Site Inspection

1. Application Reviews

Every RFQ that reaches Fronek’s engineering desk is reviewed against the actual application before a quotation is prepared. That means evaluating the design load, the expected thermal movement, and the available installation space, not just matching a part number off a data sheet or a competitor’s catalog.

A figure that looks close on paper, does not always hold up once the numbers are run. When a request comes in to match or substitute a competitor’s unit with little more than a part number to work from, Fronek’s team asks for the design load and the net thermal displacement at the installation point before recommending anything. A mismatch caught at this stage costs nothing to correct. A mismatch found after a unit ships carries consequences covered in detail in The Real Cost of Improper Snubber Selection. 

Field Services Team On-Site
Field Services Team On-Site

2. Drawing Markups

Once a design is confirmed, the drawings go through a detailed review before fabrication begins. Fronek’s engineering team checks pin-to-pin dimensions against the actual attachment/bracket take-outs, confirms hot and cold installation positions on the drawing, and cross-checking the assembly list against the relevant drawings.

When the assembly list and the drawing do not agree, the discrepancy is marked up and returned for clarification before any fabrication work starts. That step adds time on paper. It eliminates re-orders, field fit-up problems, and rework after shipment. 

Mechanical Snubber
Mechanical Snubber
 Hydraulic Snubbers
Hydraulic Snubbers

3. Technical Consultation

Not every question requires a formal quotation. Engineers, maintenance planners, and procurement contacts frequently need a direct answer before a project reaches the RFQ stage, whether a hydraulic snubber is a viable substitute for an aging mechanical unit, what the practical difference is between preset and lock-up velocity, or whether an existing clamp and end bracket can be reused on a replacement assembly.

Fronek’s engineering team handles these questions regularly, often in a direct conversation rather than a formal written exchange. Resolving an application question before an order is placed is substantially easier than identifying an error six weeks later when the part arrives on

site. For a detailed reference on snubber dimensional terminology, refer to The Snubber Terminology Guide.

4. Retrofit Assistance

Plants operating piping systems, especially the ones that are twenty or thirty years old, rarely have drawings that still reflect what is actually installed. When a snubber reaches the point where spare parts are no longer available, or corrosion has taken a unit past the point of economical repair, Fronek evaluates what can be rebuilt, what needs to be replaced, and where the original design is no longer practical to reproduce.

Retrofit work typically involves sizing a replacement from the actual cold pin-to-pin dimension, the expected thermal movement, and the confirmed load, and in many cases, designing a new structural attachment where the original mounting hardware does not carry over cleanly. This process is covered in detail in the case study When Snubber Records Go Missing, which illustrates what happens when original selection documentation is no longer available.

5. Custom Configurations

Standard catalog numbers do not fit every application. Fronek sizes each unit to the actual design load and thermal displacement at the specific installation point, and where additional stroke provides operational margin or future flexibility, that option is presented rather than assumed.

Custom configurations also include non-standard structural attachments, pin sizes matched to existing hardware, and finish-specifications outside the standard catalog. The engineering basis for the snubber itself does not change; the configuration around it is built to fit the job. For applications involving silicone-based hydraulic fluid requirements specific to the operating temperature range, fluid selection is reviewed as part of the configuration process.

Summary

Each of the five activities above is standard engineering practice, the work required to confirm that a snubber fits its installation, performs as designed under both thermal and dynamic conditions, and does not create an unanalyzed restraint condition in the field. For a broader look at what incorrect snubber selection costs when these steps are skipped, refer to The Real Cost of Improper Snubber Selection.

To discuss a specific snubber application, review an existing installation, or request an engineering evaluation, contact the Fronek Anchor/Darling team or request a quote.

When Terminology Matters in the Field – Case Study Showcasing Snubber Specification Challenges

 Hydraulic Snubber - Factory Preset Reference
Hydraulic Snubber – Factory Preset Reference

Background

Snubber specification errors are often predictable and preventable. A specification may appear complete on paper, allowing procurement to move forward, but critical issues often emerge only when the snubber arrives on site. Common problems include an incorrectly installed length or insufficient stroke to accommodate the actual thermal movement of the piping system. By this stage, the consequences extend far beyond replacing a single component. It includes expedited re-orders, field rework, and schedule impact that could have been avoided at the specification stage.

The three cases below are drawn from actual customer engagements handled by Fronek Anchor/Darling. Each one involved a hydraulic snubber specification that was incomplete or ambiguous at the time of order. In each case, Fronek’s engineering team identified the gap before fabrication and resolved it through direct technical clarification. The cases span industrial, geothermal, and refining applications, but the terminology risks they illustrate are common across every sector where snubbers are used.

Problem

In all three engagements, the purchase order or RFQ contained specification data that appeared complete on the surface. Pin-to-pin dimensions were listed, stroke values were referenced, and assembly types were identified. The problems were not missing fields. They were dimensional values that had been carried forward from catalog references rather than derived from the actual installation geometry, assembly configurations where a critical take-out dimension had not been calculated, and stroke approvals that had not been validated against the actual thermal displacement at the installation point. 

Hydraulic Snubber
Hydraulic Snubber

Case 1 — When a Catalog Dimension Is Not an Installation Dimension

A purchase order was placed for a series of hydraulic snubbers. The customer’s data sheet referenced a pin-to-pin dimension of 23-1/4″. That figure matched a value published in the Fronek product catalog, which raised an immediate engineering flag.

The catalog value of 23-1/4″ represents the snubber’s pin-to-pin at mid-stroke, which is the factory standard preset position. A customer referencing that catalog dimension does not necessarily require the snubber at that preset. In many cases, the value is carried over from the catalog as a reference point, without being validated against the actual installation envelope.

Fronek’s engineering team flagged the ambiguity before the order was processed:

“Can you confirm whether the client specifically requires a pin-to-pin length of 23-1/4″, or if they are referencing that value from the catalog? The 23-1/4″ represents the snubber at mid-stroke, but this needs to be confirmed against the actual installation envelope before we proceed.”

The clarification confirmed the customer was referencing the catalog value, not specifying a fixed installation constraint. The correct pin-to-pin was established based on the actual structural attachment geometry and the pipe’s thermal displacement in the cold position. The snubber was ordered at the appropriate preset to accommodate field conditions, not at the catalog default.

Terminology Applied

  • Pin-to-Pin: Confirmed as the governing installation dimension, not the cylinder length alone. All attachment hardware take-outs were included in the final dimension.
  • Preset Position: Set to place the rod at a position ensuring adequate stroke in both the direction of thermal growth and thermal contraction.
  • Cold Position: Defined as the installed condition at ambient temperature, from which thermal displacement in the hot direction is measured.
Hydraulic Snubber Assemblies for an LNG Processing Facility
Hydraulic Snubber Assemblies for an LNG Processing Facility

Case 2 — Type B Assemblies and the Missing Clamp Take-Out

Fronek received an RFQ for seven hydraulic snubbers for an industrial customer. The data sheet specified two snubber types, SN3 and SNB4, both configured as Type B assemblies. Type B snubbers include a pipe clamp as part of the assembly.

Calculating pin-to-pin for a Type B assembly requires the clamp take-out: the dimension from the pipe centerline to the clevis pin hole on the clamp side. Without this value, pin-to-pin cannot be reliably calculated, even when the structural attachment side is fully defined.

Fronek’s engineering review identified the gap before responding to the customer:

“For Snubbers SN3 and SNB4, they’re looking for Type ‘B’ which comes with a clamp. I need to know what the clamp take-out is to approximate the pin-to-pin. I’m still waiting on the clamp take-out measurement to finalize the P2P.”

The clamp take-out was obtained prior to order finalization. Pin-to-pin was then calculated correctly for all seven snubbers, incorporating the structural attachment take-out on the structure side and the clamp take-out on the pipe side.

Terminology Applied

  • Pin-to-Pin: Dependent on take-out at both ends. Structural attachment and clamp hardware dimensions are both required. Neither alone is sufficient.
  • Stroke: Confirmed against the expected thermal displacement at each installation point to ensure the preset would leave adequate travel in both directions.
Hydraulic Snubber Field Installation
Hydraulic Snubber Field Installation

Case 3 — Stroke Approval Without Displacement Analysis

A geothermal power generation customer engaged Fronek for a multi-unit snubber supply across several load ratings with varying stroke requirements. Technical data sheets were exchanged and reviewed collaboratively before fabrication.

During the drawing review, the customer’s engineering team raised questions about stroke adequacy for one of the specified units. A 6-inch stroke was proposed, and the customer confirmed approval. The discussion also identified a broader issue: the engineering group was not fully familiar with how snubber dimensional parameters interact with installation geometry.

Approving a stroke value is only meaningful when the underlying calculation has been performed. Thermal displacement in the direction of the snubber axis, at the correct installation point, must be established before a stroke can be validated.

The 6-inch stroke was confirmed through a collaborative data sheet review, validating the travel against anticipated thermal displacement at each installation point. Separately, Fronek’s engineering team developed and delivered a dedicated technical training session for the customer’s group, covering snubber selection, installation parameters, and dimensional terminology, including stroke, preset, cold, and hot position, and pin-to-pin.

Terminology Applied

  • Stroke: Confirmed at 6 inches for the applicable units, validated against thermal displacement in the snubber axis direction.
  • Cold/Hot Position: The basis for the displacement calculation. Cold (shutdown) to hot (operating) defines the thermal travel the snubber must accommodate.
  • Lock-Up Velocity: Reviewed during training as part of hydraulic snubber selection guidance for geothermal applications, where thermal transients are slow but seismic exposure is a design consideration. 

The terminology gaps identified in this engagement are covered in depth in The Snubber Terminology Guide. A reference built around the parameters that caused specification errors in all three cases above.

Summary

Case Core Terminology Risk Outcome
Case 1 – Industrial Refinery Catalog P2P referenced as installation P2P Correct P2P established against the field geometry. Snubber ordered at the proper preset.
Case 2 – Industrial P2P calculation is incomplete without a clamp take-out. Type B assembly requires both end dimensions. Clamp take-out obtained. P2P confirmed for all seven units before the order.
Case 3 – Geothermal Stroke approved without underlying displacement analysis. The team lacked dimensional terminology familiarity. Stroke confirmed by analysis. Technical training session delivered to close the knowledge gap.

In each case, the risk was not structural failure. It was a specification error that would have produced the wrong device or an incorrect installation. The cost of that error, in expedited re-orders, field rework, and schedule impact, would have far exceeded the cost of the clarification that prevented it.

To discuss a specific snubber specification, confirm pin-to-pin, preset, or stroke requirements, or request a technical review of an existing installation, contact the Fronek Anchor/Darling team or request a quote.

 

The Snubber Terminology Guide – What the Numbers on the Nameplate Actually Mean

A  snubber quotation, data sheet, or installation drawing contains its own specialized vocabulary. Engineers who work with these devices every day treat the terms as second nature. However, for maintenance planners, procurement teams, plant managers, and engineers new to piping support design, these terms are often overlooked or misunderstood, with real consequences in the field. This guide defines the terms that appear on every snubber data sheet, drawing, and purchase order, and explains how they interact in practice. 

1. Core Dimensional Terminology

Term Definition
Pin-to-Pin (PP) Length The overall installed length of the snubber assembly is measured from the centerline of the structure-side pin to the centerline of the pipe-side pin. This is the governing dimension that determines whether the snubber fits the available space between the structural attachment and the pipe clamp.
Preset Position The rod extension at which the snubber leaves the factory. Because the snubber must accommodate both cold (shutdown) and hot (operating) pipe positions, the rod is set to a specific point to ensure adequate stroke is available in both directions. Preset position is expressed either as an absolute rod extension measurement or as the resulting pin-to-pin length at the preset.
Cold Position The physical position of the pipe, and therefore the snubber rod, is determined when the system is at normal shutdown temperature. This is typically the as-installed condition. The snubber is preset so that the cold position corresponds to the factory preset extension.
Hot Position The physical position of the pipe when the system is at operating temperature. Thermal growth displaces the pipe from the cold position to the hot position. The snubber rod extends or retracts to follow this displacement. The difference between cold and hot positions, in the direction of the snubber axis, is the thermal displacement the snubber must accommodate without bottoming out.
Stroke The total available travel of the snubber rod is measured from its fully retracted position to its fully extended position. The available stroke must be sufficient to ensure the snubber never bottoms out in either direction during thermal cycling. 
Lock-Up Velocity The rod velocity above which the snubber’s damping mechanism engages, and the device transitions from free movement to load-bearing restraint. For a hydraulic snubber, lock-up is a true velocity threshold; below it, the snubber follows thermal displacement freely; above it, the snubber arrests dynamic motion. Too high, and the snubber fails to engage during a seismic event; too low, and normal vibration or pressure transients cause unintended restraint.
Schematic Diagram of Hydraulic Snubber
Schematic Diagram of Hydraulic Snubber

2. How These Terms Interact in Practice

Pin-to-Pin Drives the Installation

The structural attachment and the pipe clamp define a fixed envelope. The pin-to-pin length of the snubber assembly, including the rod, cylinder, clevis ends, and pins, must fit within that envelope at the cold-installed position. This is why pin-to-pin is the primary dimension on a data sheet, not cylinder bore or rod diameter.

Note – The cold position pin-to-pin dimension equals the sum of: cylinder body length + rod extension at preset + attachment hardware take-out at each end. If any element is estimated incorrectly, the snubber will not fit at the installation point.

Preset Enables Bidirectional Stroke

A snubber preset at its midpoint, 3 inches of extension on a 6-inch stroke device, has 3 inches of travel available in both directions. A snubber preset near its maximum extension has nearly all of its stroke available for retraction but almost none for extension. Preset must be calculated to leave adequate stroke in both the direction of thermal growth and the direction of thermal contraction.

Lock-Up Velocity Is Application-Specific

Fronek’s standard hydraulic snubbers are calibrated with a lock-up velocity in the range of approximately 8–12 inches per minute (IPM), which is appropriate for the vast majority of nuclear and industrial piping applications. Certain systems may require a different activation threshold based on operating conditions. 

A geothermal plant experiencing slow thermal transients and seismic loading may require a different lock-up profile than a refinery steam line subjected to rapid pressure transients, water hammer, or high-frequency vibration. Where application-specific requirements exist, custom lock-up velocities can be engineered, calibrated, and tested to meet the design criteria.

 Mechanical Snubber
Mechanical Snubber

3. Terms That Commonly Cause Field Problems

Three common misunderstandings account for the majority of snubber installation and specification errors encountered in the field:

Confusing pin-to-pin with cylinder length

A snubber quotation specifies pin-to-pin, not the cylinder body alone. The hardware take-out at each clevis end must be included. A customer who measures the cylinder and orders accordingly will receive a snubber that is too long by the total attachment take-out.

Ordering at the wrong preset

 If the cold-position thermal displacement is not confirmed before ordering, the factory preset may leave insufficient stroke in one direction. The snubber may bind during thermal growth or bottom out, becoming an unintended fixed restraint at the limits of travel.

Misapplying lock-up velocity across device types

 Mechanical snubbers engage based on acceleration, not velocity. They are not interchangeable with hydraulic snubbers in all environments, and their effective lock-up behavior differs. Specifying a mechanical unit in a sustained-vibration environment, or a hydraulic unit with the wrong silicone-based fluid for the temperature range, produces a device that fails to perform as designed.

Note – A snubber installed at the wrong preset, in the wrong orientation, or at the wrong pin-to-pin will fail silently until the pipe tells you something is wrong.

Summary

Understanding snubber terminology is essential to ensuring the device can be installed correctly, functions as designed, and allows the piping system to perform as intended under both thermal and dynamic loading. The table above provides a reference for the terms that appear most frequently in specifications, data sheets, and field installations.

For a more detailed look at what improper snubber selection costs in practice, read The Real Cost of Improper Snubber Selection.

To discuss a specific snubber specification, review an installation, or confirm pin-to-pin, preset, or stroke requirements, contact the Fronek Anchor/Darling team or request a quote.

The Hidden Costs of Lost Snubber Selection Data: A Refinery Case Study

Background 

A major refinery operating an extensive steam piping network flagged seventeen hydraulic snubbers on 650 PSIG and 200 PSIG steam headers for evaluation. The units serve a seismic and dynamic restraint function on critical high-energy piping.

The seventeen snubbers consisted of two physical configurations: 

  • Eight shorter units installed on the 200 psig steam headers (Group A) and 
  • Nine longer units installed on the 650 psig steam headers (Group B). 

When Fronek Anchor/Darling was engaged to support the replacement program, the plant had no access to original design documentation. No drawings, no load ratings, no stroke specifications, and in several cases, no confirmed manufacturer identity were on file. 

What Was Found in the Field

For Group A, nameplate analysis conducted by Fronek’s engineering team produced a working identification with moderate confidence. Based on available evidence, the “BE” designation is believed to represent Basic Engineers, the original manufacturer, and the size designation “2 x 5” was interpreted as a 2-inch bore with a 5-inch stroke. This provided a usable, though not fully verified, engineering baseline for specifying equivalent replacement hardware.

For Group B, the nameplate information available in the field did not contain sufficient detail to establish load ratings, stroke lengths, or device type with any engineering confidence.

As Jawad Uppal, P.Eng, PMP, Engineering Manager at Fronek Anchor Darling, noted:

“For the other nine snubbers, the nameplate information provided does not contain sufficient detail for us to reliably establish or even venture a reasonable estimate of the original load rating and stroke length. In the absence of historical drawings, design documentation, or manufacturer records, the most technically defensible approach would be to perform a pipe stress analysis.” 

Solution

The absence of original selection documentation required a multi-phase remediation effort: 

  1. PT&P’s Field Services division was engaged to coordinate the site visit, collecting dimensional data, confirming stroke requirements, and capturing 3D scan isometrics using LiDAR technology for undocumented piping geometry.
  2. A full pipe stress analysis was initiated for all nine Group B snubbers by PTP  to determine load demand and establish code-compliant replacement specifications. 
  3. For Group A, nameplate-derived sizing assumptions required engineering verification before any replacement hardware could be ordered.
  4. No replacement hardware was specified or ordered for Group B until the stress analysis was complete. The units remained in service in their current, unconfirmed state pending the outcome of the analysis.

With PT&P’s in-house field services, pipe stress analysis, and LiDAR scanning capabilities, the plant received a fully coordinated engineering response. Which was faster and more reliable than managing multiple external contractors across the same scope.

Cost Impact

Cost Category Description Severity
Engineering Re-analysis Full pipe stress analysis required for 9 units with no usable selection baseline HIGH
Field Mobilization Site visit to collect dimensional data, stroke measurements, and 3D scan isometrics MODERATE
Documentation Recovery Manufacturer ID via nameplate analysis; partial success on 8 of 17 units MODERATE
Replacement Risk Without confirmed design loads and stroke requirements, replacement hardware may be undersized, oversized, or improperly configured, potentially compromising system performance.  CRITICAL
Schedule Delay A multi-week coordination cycle before replacement hardware can be specified or ordered HIGH

 

Summary

The cumulative cost of this engineering re-analysis, field measurement, mobilization, coordination efforts, and procurement delays significantly exceeded what proper upfront selection engineering would have required. Original snubber selection documentation should be treated as a long-term engineering asset throughout the lifecycle of the facility. Its absence creates a liability that surfaces at inspection, not at installation.

When selection data is missing, the technically defensible response is analysis, not assumption. Specifying a replacement based on estimated load ratings compounds the original error. Nameplate analysis can partially recover lost data, but only with engineering judgment and only for some units. It is not a substitute for documented design records.

To discuss a specific snubber application, review an existing installation, or request an engineering evaluation, contact the Fronek Anchor/Darling team or request a quote.

The Real Cost Of Improper Snubber Selection

The Real Cost Of Improper Snubber Selection 

Improper snubber selection is one of the most underappreciated sources of long-term cost in piping systems, in both commercial and industrial plants and nuclear facilities. The consequences are rarely visible at the time of installation. They develop over months or years and typically surface as a cracked weld, a degraded equipment nozzle, or an unplanned outage that costs significantly more than the correct device would have. This article covers five principal failure modes associated with incorrect snubber selection and the cost implications of each.

1. Structural Damage Risks

A hydraulic snubber is a velocity-sensitive device. It permits slow thermal movement to pass freely and locks up within milliseconds when the pipe accelerates dynamically. A mechanical snubber uses springs and pawl-and-ratchet mechanisms to achieve similar behavior. Selecting the wrong type or load rating results in a device that either fails to arrest the dynamic event or transmits forces that the structure was never designed to withstand.

Undersized Load Capacity

When the snubber’s rated capacity falls below the actual seismic or dynamic load, the device fails to arrest pipe motion during the event. The pipe displaces freely, transmitting shock loads into adjacent structures, hangers, and equipment connections. In nuclear applications, this failure mode can compromise the seismic qualification of the entire support design. 

Note – An undersized snubber under dynamic load is an active failure point. The load that exceeds rated capacity transfers directly into the structure.

Oversized or Over-Constrained Installation

An oversized or poorly positioned snubber can produce equally damaging results. A snubber with excessive stiffness transfers loads into the piping system including attachment hardware, pins and lugs, which were not anticipated in the stress analysis. Pipe stress engineers account for snubber stiffness in their models. If the installed unit behaves differently than modeled, the entire stress calculation may be invalid. 

2. Weld Cracking

Weld cracking is the failure mode most frequently observed in the field following improper snubber selection, and it typically takes time to manifest. Two primary mechanisms are involved: fatigue accumulation from repeated dynamic loading and constraint-induced stress from a snubber that binds during normal thermal cycling.

Fatigue from Dynamic Load Cycling

Piping systems in power generation and industrial plants go through a continuous cycle that includes startup, shutdown, load following, and pressure transients. When a snubber is improperly selected and repeatedly transmits higher-than-analyzed loads, the welded connections at pipe supports and structural attachments accumulate fatigue cycles faster. The pipe does not fail during a single event. It fails after thousands of cycles, with each one contributing incremental damage until a crack appears during maintenance inspection.

Thermal Binding and Constraint-Induced Stress

A snubber installed with insufficient stroke, incorrect preset position, or the wrong orientation will bind as the pipe thermally expands. Rather than moving freely through the slow thermal displacement, the snubber becomes a rigid restraint. The pipe then carries the thermal growth as a constrained stress concentrated at the nearest welds.

This condition is particularly damaging at small-bore branch connections and socket welds, where stress concentration factors are already heightened. If a snubber cannot move freely during normal thermal expansion, it behaves like a rigid support instead of allowing the pipe to expand and contract as designed. 

3. Pipe Movement Issues

Thermal displacement and dynamic restraint represent fundamentally different design requirements. The snubber exists precisely because a single support cannot address both simultaneously. When this distinction is not reflected in the selection, or when the stroke is undersized, the consequences extend beyond the snubber itself.

Insufficient Stroke

A snubber preset at mid-stroke with 6 inches of total travel provides only 3 inches of movement in each direction. If the pipe grows 4 inches thermally, the snubber bottoms out before full displacement is reached, creating an unanalyzed restraint condition. Continued pipe movement against a bottomed-out snubber risks rod bending or mounting bracket fracture.

Stroke selection must be based on the actual thermal displacement at the installation point in the direction of the snubber’s axis. Lateral (side to side) displacement at a point where the snubber is oriented longitudinally (lengthwise) has no impact on stroke adequacy.

Hydraulic Snubber
Hydraulic Snubber
Mechanical Snubber
Mechanical Snubber

4. Mechanical vs. Hydraulic: Selecting the Right Device Type

Parameters Mechanical Snubbers Hydraulic Snubbers
Operating Principle Ratchet-based locking mechanism that responds to acceleration Viscous dampers that respond proportionally to velocity
Suitable For Low-frequency dynamic (seismic) events Most power plant applications
Limitations Not suited to sustain vibration environments, ratchet can engage unintentionally and accumulate constraint over time Seals and Hydraulic fluid can degrade over time due to improper evaluation of the operating environment – thereby rendering reduces service life of the snubber.
Misapplication Risk Unintended ratchet engagement and progressive constraint buildup in high-vibration environments Failure to perform or active constraint of normal pipe movement if incorrect fluid is specified

5. Long-Term Maintenance Costs

The purchase price of a snubber, including a nuclear-grade unit, represents a small fraction of the cost associated with an incorrect selection. Maintenance costs are where the full financial consequences of improper selection are realized.

Inspection and Surveillance Burden

Nuclear plants are required to perform functional testing on snubbers at defined intervals under 10CFR 50. A snubber that fails functional testing triggers an operability determination, an extent-of-condition review, and potentially accelerated testing of all similar devices. A single failed unit can initiate a fleet-wide evaluation. An incorrect device selection, particularly one that has been cycling under constraint or binding against thermal movement, increases failure rates and drives inspection costs disproportionately.

Unplanned Outage Costs

When a snubber failure or weld crack is discovered during operation, the plant must choose between continued operation under a degraded support condition and an unplanned outage to carry out repairs. For a nuclear unit, an unplanned outage at peak demand can cost $1M or more per day in replacement power. For a refinery, costs are comparable or higher. These figures represent the true cost of an incorrect snubber selection, not the cost of the device.

Repeat Failures and Root Cause Complexity

When a failed snubber is replaced with a device of the same incorrect specification, the failure will recur.Finding the real cause of the problem can be difficult because the effects often don’t appear until months or even years after the snubber was incorrectly selected.. By the time weld cracks are identified, the engineering basis for the original selection may no longer be available. Correcting the installation then requires a full re-analysis of the support design.

What Gets Triggered By A Wrong Selection

The table below summarizes the cost categories associated with each failure mode. Severity ratings reflect typical commercial and nuclear industrial experience.

Failure Category Primary Consequence Cost Severity
Structural Damage Unanalyzed restraint forces; bracket fracture; support failure under load Critical
Weld Cracking Fatigue accumulation; constraint-induced stress at branch connections Critical
Pipe Movement Snubber bottoming out; binding on thermal growth; loss of design basis High
Maintenance Costs Failed surveillance; unplanned outage; repeat root cause analysis High

Correct snubber selection requires load analysis, displacement data, geometry confirmation, and a thorough understanding of the dynamic environment at the installation point. Addressing these requirements during the engineering phase costs significantly less than correcting them after field consequences develop.

To discuss a specific snubber application, review an existing installation, or request an engineering evaluation, contact the Fronek Anchor/Darling team or request a quote today.

Why Outage Season Is Critical for the Snubber Industry

What Happens During an Outage?

Most industrial plants are designed to run continuously for long periods of time, sometimes years, with minimal interruption. But eventually, every facility reaches the point where systems need to be inspected, repaired, tested, or upgraded. 

An outage is essentially a planned shutdown of a plant or process system so maintenance and inspections can be performed safely. In industries like nuclear, fossil power, petrochemical, and heavy process manufacturing, outages are major events involving hundreds – sometimes thousands – of personnel working around the clock.

Imagine trying to renovate an entire city while also racing against a stopwatch that costs millions of dollars per day. That’s outage season.

During these shutdowns:

  • Insulation gets removed
  • Valves are rebuilt
  • Piping systems are inspected
  • Welds are examined
  • Supports are tested
  • Components that are normally inaccessible suddenly become reachable

This is also the time when many piping support components – including snubbers – finally get their moment in the spotlight.

For most of the year, snubbers quietly sit in the background doing their job without attracting much attention. But during an outage, they quickly become one of the many critical components, utilities need to evaluate before the plant can safely return to service.

And much like your car making strange noises the week before a road trip, this is usually when hidden problems decide to reveal themselves.

Why Snubbers Matter During Outages

Snubbers are designed to live difficult lives.

They operate in environments involving:

  • Heat
  • Vibration
  • Moisture
  • Corrosion
  • Radiation (in nuclear facilities)
  • Years of continuous service

Over time, seals can age, hydraulic fluid can degrade, corrosion can develop, and mechanical components can wear. Most of these issues are not obvious during normal operation – which is exactly why outage inspections are so important.

During outages, utilities often perform:

  • Visual inspections,
  • Functional testing,
  • Maintenance evaluations,
  • In some cases full rebuilds or replacements

A snubber that fails inspection can create significant operational concerns. If a snubber cannot properly restrain dynamic movement during a transient event, the piping system may no longer behave as originally designed during seismic activity, water hammer, or other abnormal conditions.

In simpler terms: the component nobody noticed for five years suddenly becomes extremely important at 2:00 AM during outage week three.

This is especially true in nuclear facilities, where snubber programs are heavily managed and documented under strict inspection and testing requirements.

For outage teams, snubbers are not just “pipe accessories.” They are safety-related dynamic restraints that directly impact system operability and startup readiness.

 How Outages Drive the Snubber Industry

Outages are one of the primary drivers of activity within the snubber industry.

Why?

Because outages compress years of maintenance-needs into very short windows of time.

A plant may operate continuously for 18–24 months, but during a refueling or maintenance outage, utilities suddenly need:

  • Inspections completed
  • Engineering evaluations issued
  • Failed snubbers rebuilt
  • Replacement units manufactured
  • Testing performed
  •  Documentation finalized – all on extremely aggressive schedules.

During peak outage seasons, snubber vendors, rebuild shops, field service teams, QA departments, and engineering groups often shift into full sprint mode. Expedited orders become common, machine shops extend working hours, and everyone starts using phrases like:

“How quickly can you turn this around?”

In many cases, outage schedules are so tight that even relatively small delays can ripple into major startup impacts.

That urgency is what makes the outage environment unique.

Outside of outage season, snubber work can feel methodical and planned. During outages, however, the industry becomes highly schedule-driven and reactive. Components that have been quietly installed for decades suddenly require immediate engineering attention.

It is not uncommon for a snubber discovered in poor condition on Monday to require engineering review, rebuild, testing, documentation, and shipment before the weekend.

The Critical Path Problem

One of the biggest challenges during outages is something known as the “critical path.”

The critical path refers to activities that directly affect when a plant can restart operation. If one critical task gets delayed, the entire outage schedule can begin to slide.

And this is where snubbers can unexpectedly become very important.

For example:

  • A failed snubber may require engineering evaluation,
  • Replacement hardware may need to be fabricated,
  • Support clearances may need verification,
  • Functional testing may need to be repeated before startup approval is granted.

Even though snubbers are relatively small compared to massive turbines, boilers, or reactors, they can still impact overall outage schedules if issues are discovered late in the process.

This is one reason utilities place significant emphasis on outage planning, preventative maintenance, and long-term asset management programs. Identifying problems early helps avoid costly surprises during the outage itself.

Because in the outage world, discovering a failed component on Day 2 is manageable.

Discovering it on the final weekend before startup? That’s when entire conference rooms suddenly become very interested in pipe supports.

At the end of the day, outages are about reliability, safety, and returning systems to operation as efficiently as possible. Snubbers may not always be the most visible components in a plant, but during outage season, they often become some of the most important.

What is a Pipe Snubber? – The Explain-It-Like-I’m-5 Version

Imagine holding a garden hose while water is flowing through it. Most of the time, the hose moves slowly and gently as pressure changes. But if someone suddenly turns the valve on or off very quickly, the hose can violently jerk and shake. 

Industrial piping systems behave the same way. 

Piping systems are designed to move. As temperatures/pressures change during normal operation, pipes naturally expand and contract. This movement is completely normal and is something engineers account for when designing a system. 

The issue starts when the piping experiences sudden or violent movement

Events like water hammer, rapid valve closures, or equipment trips can create sudden dynamic forces that cause piping to shake violently, damaging pipe supports, welds, flanges, and nearby equipment. 

 

That’s where a pipe snubber (also known as a dynamic pipe restraint) comes in. 

A snubber is a restraint device that allows slow thermal movement during normal operation, but locks up and resists sudden movement during an abnormal event. In simple terms, it acts very similar to the shock absorbers on a car or seat belts— flexible during normal conditions, but resistant during sudden impact. 

This is what makes snubbers unique compared to rigid pipe supports. A rigid pipe support constantly restricts movement, whereas a snubber only reacts when movement becomes too rapid. 

 

So why not just rigidly support the pipe everywhere?  

Because piping systems need to move during normal operation. If a high-temperature pipe were fully restrained, thermal expansion could create very large stresses in the piping system, supports, and connected equipment. Snubbers solve this problem by allowing slow thermal movement while still protecting the system during sudden transient events. 

Thermal expansion occurs slowly over time and is considered a low-speed or “static” type of movement. Events such as seismic activity, water hammer, or valve slam occur very quickly and are considered “dynamic” movement.

 

Figure 2 – Typical hydraulic and mechanical snubber installation on process piping.

Snubbers are commonly used in systems that carry fluid at high pressure, high temperature — or both — such as steam, feedwater, or process piping in power and industrial plants. These systems must be able to expand and contract during normal operation while still being protected against dynamic events. 

For example, in a steam power plant, a long steam line may grow several inches as it heats up during startup. The snubber allows this slow movement naturally, but would resist sudden pipe movement caused by a steam hammer or seismic event. 

Snubbers are especially common in nuclear, fossil power, petrochemical, aerospace, and other critical process industries where piping reliability and system safety are essential.

Figure 3 – Exploded view of a hydraulic snubber assembly.

Think of the diagram above as the “insides” of a typical hydraulic snubber. The main cylinder holds a piston, while the reservoir is filled with hydraulic fluid that manages how things move. During normal thermal expansion, fluid travels slowly through the control assembly, letting the pipes drift naturally. But if the pipe tries to jerk away, the flow restriction locks up to stop the fast motion. Other parts, like the rod ends and extension pieces, act as the connectors that hook the snubber to the building and the piping itself. 

In simple terms, a snubber acts like a “smart restraint” for a piping system — flexible during normal thermal movement, but strong during sudden dynamic events. This allows piping systems to operate safely without introducing excessive stresses during normal plant operation.

Any Angle, Any Load: The Versatility of Fronek Anchor/Darling’s Hydraulic Snubbers

A photo of hydraulic snubbers manufactured by Fronek Anchor/DarlingOrientation, Load Capacity, and Nuclear Maintenance

Nuclear power plants are congested, complex environments. A typical containment building is a 3D puzzle of piping, cable trays, and heavy machinery. In such a dense layout, finding the perfect spot to mount a support structure is rarely easy. Support components must fit the plant design, not force it to change. Fronek Anchor/Darling adds value through exceptional versatility in mounting, alignment, and configuration options.

Spatial Independence: Pressurized Reservoirs for Complex Containment

In the congested corridors of a nuclear power plant, structural mounting points are rarely convenient to reach. Traditional hydraulic supports often rely on gravity-fed reservoirs, which impose a strict “vertical-only” orientation to prevent air ingestion and pump cavitation. This limitation frequently forces engineers to compromise, requiring expensive supplemental steel or complex offsets to maintain a functional upright posture.

Fronek Anchor/Darling eliminates these geometric constraints through a positively pressurized reservoir system. By maintaining a constant internal head pressure, the hydraulic circuit remains fully primed regardless of its physical orientation. This allows the snubber to be installed horizontally, vertically, or at any oblique angle required to reach a specific structural beam or embedded plate.

Engineering Advantages for Nuclear Retrofits:

  • Elimination of “Air Pockets”: Pressurization ensures the valve block is always submerged in fluid, preventing the “dead zone” often found in gravity units installed at slight inclines.
  • Streamlined ALARA (As Low As Reasonably Achievable) Planning: High-flexibility mounting allows technicians to install units in more accessible locations, reducing “Time-in-Motion” and radiation exposure.
  • Dynamic Consistency: Whether inverted or upright, the lock-up and bleed rates remain identical, providing the predictable response required for compliance with ASME Section III, Division 1, Subsection NF.

Solving the Misalignment Puzzle

In the real world, piping runs are rarely perfectly straight, and structural attachment points are rarely perfectly aligned. Thermal expansion can also cause pipes to twist or skew slightly. A rigid connection that cannot accommodate these angles will bind, causing stress concentrations that can damage the snubber or the pipe.

To address this, Fronek units are equipped with spherical, self-aligning ball bushings. These precision-engineered bushings allow for ±5° of angular motion or misalignment. This built-in tolerance ensures that the snubber forces remain linear along the cylinder’s axis, preventing side-loading that could wear out seals or bend the piston rod.

Scalability: From 3,000 to 130,000 Pounds

No two piping systems have identical support requirements. A small drain line has vastly different mass and energy potential than a main coolant loop. Fronek offers a scalable menu of options to meet the full spectrum of plant needs.

The product line includes seven sizes with cylinder bores ranging from 1 1/2 to 8 inches. In terms of holding capacity, these units cover a normal load range of 3,000 lbs. to 130,000 lbs.

Additionally, to accommodate varying thermal expansion, they are available in stroke lengths of 6, 12, and 18 inches. This wide variety ensures that engineers can select the right-sized component for every application, avoiding unnecessary cost and weight from over-engineering.

FAQ: Specifications and Solutions: Common Questions Answered

Q. Can Fronek hydraulic snubbers be mounted upside down?

Yes, they feature a pressurized hydraulic reservoir, allowing them to be mounted in any orientation.

Q. What is the load capacity range for Fronek hydraulic snubbers?

These units have a normal load range of 3,000 lbs. to 130,000 lbs.

Q. Are replacement parts available for nuclear-rated snubbers?

Yes, replacement parts and replacement cylinders are available for both commercial and nuclear applications.

Q. How do these snubbers handle pipe misalignment?

They are equipped with spherical, self-aligning ball bushings that allow for ±5° of angular motion or misalignment.

Lifecycle Management: Replacement Parts for Nuclear 

A nuclear plant is a long-term investment, often operating for 40 to 60 years. Supply chain stability is critical. Fronek supports the lifecycle of these assets by ensuring that replacement parts and replacement cylinders are available for both commercial and nuclear applications.

This commitment to aftermarket support enables utilities to maintain their safety systems indefinitely without replacing entire assemblies due to minor wear, ensuring sustainable, cost-effective operations.

Universal Mounting & Scalability with Fronek Anchor/Darling. Unlike gravity-dependent systems, Fronek’s pressurized hydraulic reservoir allows mounting in any orientation and supports a wide load range, suitable for auxiliary to main steam lines.

Need a custom fit for a heavy load? Contact our team to discuss our range of hydraulic snubbers and replacement parts to find the exact specification for your project.

 

Sealing the Deal: The Critical Interaction Between Hydraulic Fluid Chemistry and Snubber Seal Life

Extend Hydraulic Snubber Lifespan: The Chemistry You Can’t Ignore for Fronek Anchor/Darling Quality

125 Kip Mechanical Snubber-Largest Made at Fronek Anchor/Darling
125 Kip Mechanical Snubber-Largest Made at Fronek Anchor/Darling

Fronek Anchor/Darling, a leading supplier of high-performance hydraulic and mechanical restraints, knows that the longevity and reliability of your piping systems rely on every component. A seemingly small detail, the compatibility between the snubber’s hydraulic fluid and its seals is one of the most critical factors determining snubber service life and performance.

The continuous operability of a hydraulic snubber—a device designed to permit slow, thermal movement while arresting rapid, potentially destructive motion from seismic events —relies heavily on its elastomeric seals. These seals maintain the integrity of the snubber’s hydraulic pressure boundary. If the fluid’s chemical composition is incompatible with the seal material, the consequences can be disastrous for the snubber’s performance and catastrophic for maintaining the integrity of the piping system. 

In safety-related environments, such as ASME Nuclear Support (“NS) certified applications, equipment must operate with absolute reliability. Understanding the chemical interaction between the snubber’s fluid and its seals is vital to maximizing system uptime and reducing maintenance costs.

SF1154 Hydraulic Fluid: The Critical Chemistry Behind Nuclear Snubber Safety

For Fronek Anchor/Darling, the reliability of hydraulic piping restraints relies on more than just hardware; it hinges on the chemistry of the hydraulic medium. In safety-related applications, we exclusively use SF1154, a methylphenyl polysiloxane silicone fluid originally developed by General Electric and currently manufactured by Momentive Performance Materials (MPM) in Leverkusen, Germany.

Because the fluid’s performance is integral to the snubber’s performance, SF1154 is classified as a safety-related item. Understanding the unique properties of this fluid is essential for maintaining the operational integrity of nuclear piping systems.

Why SF1154 Viscosity and Composition Determine Snubber Performance

The hydraulic fluid within a snubber serves a dual purpose: it acts as a pressurized medium to transmit loads during seismic events (in the active state), and it relies on its viscous properties to allow thermal movement (in the passive state). SF1154 is specifically selected for these functions due to its stability and radiation resistance.

The Role of Viscosity: The operational performance of a hydraulic snubber is fundamentally linked to fluid viscosity. The fluid must work in concert with the physical dimensions of the snubber’s internal flow controls to assure appropriate activation during a system seismic event.

Critical Characteristic: Fronek Anchor/Darling’s team understands that fluid kinematic viscosity is a vital design characteristic. The viscosity’s nominal value, its tolerance range, and temperature characteristics are tightly controlled to ensure that snubber activation only occurs when necessary. 

Newtonian Behavior: SF1154 is a classic Newtonian fluid, meaning its physical properties, such as density, viscosity, and bulk modulus, vary predictably with temperature.

Chemical Composition and Stability: SF1154 is a copolymer manufactured through a proprietary process that controls the length of polymeric chains and the ratio of methyl to phenyl groups. Fronek Anchor/Darling verifies the specific chemical composition of each batch of fluid received from the manufacturer using Fourier Transform Infrared Spectroscopy (FTIR) to ensure traceability to the fluid initially qualified for nuclear use.  

The Interaction Between SF1154 and Ethylene Propylene Seals

The service life of hydraulic snubbers is highly dependent on the compatibility between the fluid and its elastomeric seals. If the fluid chemistry is incompatible with the seal material, it can lead to swelling, shrinking, or chemical degradation, ultimately causing snubber failure.

To prevent these failure modes, Fronek Anchor/Darling utilizes seals made from ethylene-propylene material, which is ideally suited to nuclear-grade silicone fluids such as SF1154.

  • Preventing Degradation: Incompatible fluids can leach plasticizers from seals (which results in material shrinkage and increased hardness issues) or be absorbed by the seal (causing material swelling). By strictly adhering to the SF1154 specification, Fronek Anchor/Darling maintains the seal’s elasticity, which helps prevent fluid leakage. 
  • Radiation Resistance: SF1154 was selected during initial qualification because its physical characteristics remain stable up to 1 x 10^8 Rads of irradiation, a critical factor for components installed in nuclear containment areas. 

Commercial Grade Dedication and Shelf Life Extension

Testing area for snubbers at Fronek Anchor/Darling. The company has maintained this dedicated area since 1978.
Testing area for snubbers at Fronek Anchor/Darling. The company has maintained this dedicated area since 1978.

Because SF1154 is a commercial-grade product, Fronek Anchor/Darling implements a rigorous 10CFR50-Appendix B dedication practices to ensure the fluid performs its safety-related function. 

Dedication Process: Procurement of SF1154 is accomplished directly from the manufacturer or authorized distributors, and the fluid’s critical characteristics are verified at receipt through the dedication process. This includes:

  1. Chemical Verification: Using FTIS to confirm the chemical composition of a controlled sample traceable to the original environmentally qualified fluid.
  2. Physical Testing: Verifying Refractive Index and Kinematic Viscosity at 25°C.
  3. Visual Inspection: Verifying that the fluid is clear with no haze or particulate contamination.

Extended Shelf Life. The fluid manufacturer recommends a “use before” date predicated on four years from the date of its manufacture. Historical data and recent testing indicate that the shelf life of SF1154 is essentially indefinite. Fronek Anchor/Darling has confirmed that the chemical composition remains stable for at least two decades. As part of Fronek Anchor/Darling’s dedication program, the shelf life of the fluid may be extended up to ten years from the date of manufacture through the distinct cycles of viscosity and chemical composition re-verification.

By strictly controlling the procurement, testing, and dedication of SF1154, Fronek Anchor/Darling ensures that every hydraulic snubber delivered to the nuclear industry will reliably perform its safety-related function.  

The Three Ways Incompatible Fluid Attacks Seals

Incompatible fluid chemistry directly impacts the seal’s fundamental properties through physical and chemical reactions, accelerating seal material degradation:

  • 1. Swelling (Increase in Volume): The seal material absorbs elements from the fluid, leading to excessive swelling. This can cause the seal to soften, lose physical strength, and extrude from the seal cavity under pressure, resulting in rapid wear and failure.
  • 2. Shrinking (Decrease in Volume): Conversely, essential components (like plasticizers) in the seal material can be leached out by the fluid. This causes the seal to shrink, harden, and lose flexibility, resulting in reduced sealing force and reduced adhesion to its mating surface, leading to breakage.
  • 3. Chemical Degradation: The use of fluid additives or breakdown products (often accelerated by high operating temperatures) can chemically attack the polymer chains of the seal. This can cause the material to harden or become brittle, resulting in a loss of elasticity needed to maintain a dynamic seal.

The consequences of these reactions include increased friction, loss of sealing ability, and ultimately, hydraulic snubber failure.

Proactive Measures to Lengthen Snubber Service Life

To ensure your hydraulic snubbers perform their critical safety function for their entire service life, adherence to the following maintenance principles is strongly recommended:

  1. Strict Compatibility Matching: Always confirm that the hydraulic fluid’s base oil and additives are compatible with the specific seal material used in Fronek Anchor/Darling snubbers, using SF1154 fluid. Never substitute fluids or introduce potentially harmful additives.
  2. Temperature Control: Excessive heat accelerates fluid and seal degradation. Fronek Anchor/Darling recommends maintaining fluid operating temperatures (under non-accident conditions) to less than 150°F.

Choose Fronek Anchor/Darling for Hydraulic Fluid and Seal Compatibility….Every Time

Don’t let fluid incompatibility compromise the safety and performance of your critical piping restraints. Contact our hydraulic fluid experts for a comprehensive review of your hydraulic fluid and seal material compatibility to extend the service life of your hydraulic snubbers and guarantee their performance under extreme conditions.

 

Connect, Learn and Innovate: The Value of SNUG for Snubber Users and Fronek Anchor/Darling Customers

SNUG logoFor engineers, operators, and maintenance professionals managing critical piping systems, few industry events offer the focused value of the Snubber User Group (SNUG) conference. As a dedicated provider of high-quality shock control devices, Fronek Anchor Darling recognizes the essential role SNUG plays in advancing industry knowledge and best practices.

Here is why attending the next SNUG conference is a crucial investment for anyone relying on snubbers—especially those utilizing Fronek Anchor Darling’s innovative hydraulic technology.

What is the Snubber User Group (SNUG)?

The Snubber User Group (SNUG) is a vital, independent forum dedicated to the discussion, operation, maintenance, and technical aspects of snubbers. These critical components, such as the high-performance hydraulic and mechanical snubbers manufactured by Fronek Anchor/Darling, protect piping systems from sudden, high-force events like water hammer and steam hammer, as well as seismic activity, while allowing for slow, normal thermal expansion.

SNUG provides a unique platform for end-users, primarily those in nuclear, fossil power, and petrochemical plants, to share real-world experiences, challenges, and solutions related to snubber technology and programs.

 Why SNUG is Essential for Snubber Professionals

SNUG offers benefits that directly translate into operational excellence and cost savings for your plant.

1. Real-World Case Studies and Best Practices

The heart of SNUG is the peer-to-peer exchange. Attendees present their successful solutions and lessons learned on topics such as:

  • In-Service Inspection (ISI) Program Optimization: Learn how to streamline testing, minimize false failures, and comply with regulatory requirements more efficiently.
  • Troubleshooting Snubber Failures: Hear directly from peers about standard failure modes and effective repair or replacement strategies.
  • Snubber Program Management: Discover best-in-class methods for documentation, inventory control, and outage planning.

2. Direct Engagement with Industry Experts

SNUG is where end-users, consultants, and manufacturers meet. This environment is perfect for:

  • Technical Problem-Solving: Get one-on-one time with technical experts to discuss specific site challenges, design issues, or difficult-to-inspect snubbers.
  • Understanding Regulatory Changes: Stay ahead of evolving ASME and NRC guidelines that directly impact your snubber program.

3. Shaping the Future of Snubber Technology

User feedback drives innovation. By participating in SNUG, you contribute to the collective knowledge that helps manufacturers, including Fronek Anchor/Darling, continually improve snubber design and supporting services.

Plan Your Attendance, and Learn During Valuable Conference Sessions

Planning Detail SNUG Summer 2026 Conference & Trade Show
Event Focus Snubber program administration, licensing, code compliance, and hands-on field work, featuring a dedicated Trade Show with vendors (including Fronek Anchor Darling).
Dates July 13, 14 & 15, 2026 (Monday to Wednesday)
Location Indianapolis, Indiana
Hotel/Venue To be determined. Hotel information, location, and a room reservation link will be updated on the SNUG website.
Registration Check the official SNUG website for updated registration links.
Attendee Cost Free for Member Utility Representatives. Nonmember utilities may attend up to two conferences as guests.

Fronek Anchor/Darling: Your Trusted Partner in Shock Control

The Fronek Anchor/Darling Team at SNUG
The Fronek Anchor/Darling Team at SNUG.

Fronek Anchor/Darling has a long history of designing and manufacturing durable hydraulic and mechanical snubbers and dynamic restraints for the most demanding applications, including nuclear and traditional power generation.

Our commitment to quality ensures that our snubbers, such as the widely trusted Fig. 510AD/511AD Hydraulic Snubber and the DynA/Damp Mechanical Snubber, provide reliable pipe restraint when it matters most. Learn more about our hydraulic snubbers guide.

“At Fronek Anchor Darling, we see SNUG as an invaluable partner in our mission. By listening to the feedback and challenges shared at the conference, we ensure our snubber technology and field services remain aligned with the real-world needs of our customers.”

Scott Hart, General Manager, Fronek Anchor Darling

Suppose you operate or maintain Fronek Anchor/Darling snubbers. In that case, SNUG is the perfect venue to deepen your expertise in our specific products, helping you prolong service life and deliver the best performance.

The knowledge gained at SNUG directly contributes to improved plant safety, regulatory compliance, and reduced maintenance costs. It is the single most valuable event for snubber professionals seeking to elevate their program’s effectiveness.

Stay informed on the dates and location for the next SNUBBER USER GROUP (SNUG) CONFERENCE 2026  to secure your spot and start planning your educational and networking opportunities.

Hydraulic Snubbers Guide

Hydraulic Snubbers Guide

The style “AD” Hydraulic Shock Arrestor is a manifold design hydraulic component consisting of a high pressure main cylinder, a flow control section which contains dual stage velocity sensitive poppet valves, and a spring energize reservoir.

Application:
For use on piping systems or equipment when unrestrained thermal movement must be allowed, but which must be restrained during impulsive or cyclic disturbance. The unit is not effective against low amplitude, high frequency movement. The preferred usage with standard settings is to prevent destructive results due to earthquakes, flow transients, or wind load. Special settings are available to absorb the continuous thrust resulting from safety valve blow-off or pipe rupture.

Size Range:
PTP offers seven sizes with cylinder bores of 1 1/2 to 8 inches. These units have a normal load range of 3,000 lbs. to 130,000 lbs. All are made to include reservoirs in 6, 12, or 18 inch strokes, except the 1 1/2 inch size. The 1 1/2 inch size is offered only in 6 & 12 inch strokes only. Snubbers, as they are sometimes referred to, are available with remote reservoirs.

Size Selection:
The selection of size depends on the anticipated force and thermal movement of the protected piping or equipment. It is recommended that the selected cylinder stroke be a minimum of the anticipated thermal movement, plus 20%.

Basic Operation:
The piston rod is free to move in either direction with no restrictions to the fluid flow for all piston velocities up to the activation velocity. At activation velocity the poppet valve, internal to the snubber, closes. Closure of the poppet in either tension or compression greatly reduces the fluid flow through grooves in the poppet at rated design capacity of the unit is termed the “ bleed rate”. When the applied velocity of the unit becomes zero the poppet valve opens once again, allowing free piston movement.

Standard Design Features:
– Piping and/or equipment movement is controlled by tamperproof dual stage flow control poppets designed with self-cleaning orifices.
– Furnished as a complete, compact and efficient unit, ready for immediate use.
– Manifold configuration requiring no external piping.
– Large restraining forces compared to size.
– Functions in restraining tension and compression loads.
– Designed for continuous operation up to 200°F with brief transients to a maximum of 300°F.
– Stroke position is measured from a machined groove located at the piston rod wrench flats.
– Fluid Level in the unit, thereby eliminating estimate of reserve fluid level.

Optional Design Features:
– Remote Reservoir Mounting
– The snubber’s pressurized reservoir can be remotely mounted for inaccessible locations.
– Integral Relief Valve- A non-adjustable valve, which is factory preset at 133%, or 200% of rated load.
– Protective Boot- Installed over piston rod for protection against corrosive or outdoor environments.
– Rigid Stud Application- When no thermal growth is anticipated after lock-up, an optional poppet valve, without bleed, can be furnished. Must be ordered with optional integral relief valve.

Hydraulic Snubber Equation

Factory Pre-set:
The units are shipped from the factory complete, tested, reservoir filled to capacity and piston rod preset to mate with pin to pin installation dimension. To determine factory pre-set dimension perform the following calculations.

Most hydraulic snubbers have a piston which is relatively unconstrained in motion at low displacement rates. At high displacement rates the piston “locks up”, that is, the force required to move the piston increases substantially, usually as a result of the closing of a valve.

Some of the features include:

– External pressurized hydraulic reservoir for positioning flexibility in any spatial orientation.
– Allows free thermal movement of piping under normal operations.
– Restrains shock loading, both in tension and compression.
– System’s movement is controlled by a flow control device.

Hydraulic Shock and Sway Arrestor GE SF 1154 Silicone Fluid

Bergen-Paterson HSSA NF Hydraulic Arrestors are supplied with General Electric SF 1154 fluid to meet all snubber applications. SF 1154 methyl phenyl polysiloxane silicone fluid is a clear, light straw colored liquid, which possesses even better heat stability than the dimethyl polysiloxane (SF96-XXX) silicone materials, which were previously supplied as the standard fluids in non-radiation applications. SF 1154 has outstanding heat resistance which is combined with low volatility and high flash point to provide a normal useful service temperature range of -40°F to +500°F. In addition, SF 1154 has excellent high temperature heat transfer characteristics which minimize localized heat spot- ting sources and aid energy dissipation during cyclic loading conditions.

The SF 1154 silicone fluid working in conjunction with unique chemical conversion dry film lubricants forms a lubrication system in the Hydraulic Arrestor which minimizes wear and prolongs service life. This system helps reduce the high break-in wear associated with new equipment and sets up the dual-seal cast iron piston rings as an excellent high pressure metallic seal.

The high energy (heat or radiation) resistance of the fluid is a result of the chemical structure of the silicone oxygen molecule. Where organic hydrocarbons fluids are based on a backbone of carbon-to-carbon atoms, the silicone fluid has a backbone of silicone-oxygen linkages similar to the Si-0 linkages in other high temperature materials (quartz, glass and sand). It is this Si-0 linkage that contributes to the outstanding broad-temperature characteristics and general inertness of the silicone fluid.

 

Some of the outstanding properties of the silicone fluid are:

  1. Low Viscosity Temperature Change –
    All fluids change viscosity with temperature change but GE SF 1154 silicone fluid exhibits a much smaller change than non silicone fluids.
  2. Wide Temperature Range –
    SF 1154 has a useful range of -40° to 500° F. which far surpasses conventional fluids.
  3. Excellent Thermal Stability-
    SF 1154 has shown excellent stability when exposed to very high temperatures.
  4. Excellent Oxidation Stability –
    Due to the absence of copper-induced oxidation, the sludging that normally occurs with mineral oils, especially at high temperatures, is eliminated. No evidence of sludging has been reported in service.

 

  1. Chemical Inertness –
    SF 1154 fluid is chemically inert to most common materials.
  2. Non-Flammability-
    SF 1154 is self-extinguishing. The flash point is in excess of 550°F, along with a fire point exceeding 650°F and an auto ignition temperature in the range of 880°F to 900°F.
  3. Excellent Shear Stability –
    Silicone fluids have unusually high resistance to breakdown by mechanical shearing. The shear stability of silicone fluids can be as much as 20 times that of quality petroleum oils, providing long life. SF 1154 normally does not require change during the design life of the Arrestor.
  4. Excellent Heat Conductivity –
    The thermal conductivity of SF 1154 is relatively constant over its wide temperature range, making it ideal as a working fluid for Hydraulic Arrestors.
  5. Non-Corrosive-
    GE SF 1154 contains no acid-producing chemicals to cause staining or corrosion.

 

  1. Radiation Resistance –
    GE SF 1154 is rated serviceable at 1 X 108 roentgens, which far exceeds normal nuclear plant design radiation levels.

 

TYPICAL PROPERTIES* of SF 1154 SILICONE FLUID

 

1. Nominal Viscosity @ 77°F 175 190 centistokes
2. Viscosity Temperature Coefficient .78
3. Specific Gravity @77°F 1.050
4. Pour Point -40°F
5. Flash Point >550°F
6. Fire Point >650°F
7. Auto Ignition Temperature 880°F 900°F
8. Specific Heat BTU/lb/°F .39
9. Radiation Resistance 1 X 108 Roentgens Min.
10. Toxicity Low to None
11. Storage Life Indefinite
12. Bulk Modulus @ 100° F 245,000 psi

 

*The properties listed are typical and should not be used as specification limits. Specific details and test properties may be obtained from the General Electric Company, Waterford, New York.

 

Due to the inertness and stability of SF 1154 fluid, apparent discoloration noted during seal overhaul can be removed prior to filling, by filtration. The discoloration or streaking of dark particles dispursed in the fluid are normal wear and film particles resulting from wearing in and honing surfaces. Filtration of the fluid through a 10 micron filter element will remove the particles and restore the fluid to cleanliness levels as originally provided during filling and final testing at the factory.

 

SF 1154 fluid is soluble in most alcohols and glycols except Ethylene and Propylene glycols, glycerine and carboway 300. It is also soluble in most hydrocarbon and vegetable oils along with hydrocarbon solvents. The fluid as with the Ethylene-Propylene seals used in the Hydraulic Arrestor should not come into contact with these solvents. If contaminated, discard and recharge the Arrestor with clean fluid.

Hydraulic Shock and Sway Arrestor Recommended Practice for Parts Inspection During Snubber Overhaul

This technical bulletin has been designed to supplement previously published Bergen-Paterson Technical Maintenance Manuals for the Hydraulic Shock and Sway Arrestor (HSSA). When used in conjunction with the Technical Manual, the maintenance technician is afforded a tool by which he can make economic related proposals or decisions concerning repair or replacement of HSSA components. Damage to the individual components can be precluded during overhaul when the steps in the manual are properly followed. However, injury or deterioration of the parts during installation or while in service could detrimentally effect the performance of the Snubber if the same components are reassembled into the unit without proper repair or in some cases, replacement. The inspection guidelines that follow highlight prime areas of concern for the Snubber components. They will ensure maximum functional operability and fluid containment integrity during future in-service use. Figures 1, 2 and 3 can be referenced as an aid in identifying hardware parts for both the Manifold and External Pipe configuration units. The following instruments should be used for final inspection and in particular when doubt persists in the technician’s mind as to a part’s acceptability.

  1. Flat Machinist’s Surface Plate.
  2. Surface Comparitor/Surface Profilometer.
  3. Dial Bore Gauges.
  4. Plug Gauges.

1 – PISTON ROD

After wiping the rod clean, inspect the chrome plated surface for paint, nicks or minor imperfections and/or chips. Surface imperfections can be found by using a surface profilometer or by running the edge of a thumbnail along the length of the rod and feeling for rough spots. The plated surface can be smoothed where necessary with crocus cloth. If any imperfections extend below the chrome plating, discard the part. The surface finish on rod should be maintained at 8-16 microinches.

 

A check should also be made for rod straightness. Rotate the piston between ‘V’ blocks and indicate the concentricity with a .001″ indicator. The piston rod can also be rotated across a smooth and clean surface plate to inspect for straightness. A deformed rod is indicated by the following:

 

  1. Indicator readings in excess of .002″ per foot.
  2. Light (evidence of a gap) showing between the rod and plate surface.
  3. A slight flopping motion as the rod rolls. NOTE: The straightness of the rod must be maintained within .002″ per foot. Replace rods not meeting the straightness specification.

2 – CYLINDER TUBE

Inspect the inside wall and sealing surfaces for imperfections as above. A sharp ended brass rod can be used to feel for imperfections deep within the tube. Imperfections can be removed using a flexible honing tool. Honing should not increase the tube I.D. by more than .005″ above the nominal diameter. This can be checked using a dial bore gauge. If pitting or nicks persist after honing, discard the part. The surface finish must be maintained between 10 and 20 microinches with a cross hatched pattern remaining on the bore after honing.

3 – PISTON LAND and 4- TUBE ENDS

Visually inspect the tube ends and ‘O’ Ting contact surfaces for nicks or rough spots. Smooth with crocus cloth. If imperfections persist discard the part. The surface finish should equal not exceed a maximum of 100 microinches in these areas.

5 – PISTON RINGS

Discard and replace any piston ring that is nicked or worn.

6 – RESERVOIR PISTON and 7 – RESERVOIR TUBE

Inspect for imperfections on tube contact surfaces. Smooth as required with crocus cloth without penetrating through the plated surfaces. Aluminum pistons may be cleaned up on stepped diameters below the largest outside diameter. The largest piston outside diameter should not be less than .010″ to .014″ below nominal size. The surface finish should equal 80 microinches max. If nicks or rough spots persist on the largest diameter, discard the part. Surface finishes on seal contact surfaces must not exceed 63 microinches.

8 – RESERVOIR BIAS SPRING and 9 – POPPET SPRINGS

Inspect for mechanical breakage or corrosion. If either is evident discard and replace the part.

10 – HEADS, 11 – CAPS, 12 – BEARINGS, 13 – PORT PLUGS, 14 – CONNECTOR TUBES, and Other Machined Components.

Inspect all sealing surfaces (ie surfaces contacting an ‘O’ ring or packings) for paint and surface imperfections. A light amount of crocus cloth wiping is acceptable. If nicks or scars persist, discard and replace the part. Surface finishes should not exceed:

  1. 100 microinch max. on static sealing surfaces.
  2. 62 microinch max. on packing sealing surfaces.
  3. 32 microinch max. on bearing sliding surfaces.

15 – VALVE SEAT and 16 – POPPET

Wipe parts clean of all foreign materials. Inspect valve seats and conical surfaces of the poppets for scars or marks other than the coined bleed grooves. If any of these imperfections are evident, replace the part.

 

PISTON and ROD BEARING ALIGNMENT

Correct alignment can be checked by stroking the piston rod in a final assembled main cylinder prior to filling with fluid. The technician should be able to freely slide the piston rod back and forth by hand*. This check should be performed so that the technician may develop a “feel” for proper alignment and relative freedom of movement. Actual resistance tests are made on assembled units after they have been filled with hydraulic fluid. Failure of the unit to perform as such will indicate improper assembly of the components (provided each component has passed its individual inspection). Check for proper and even torquing of the tie rods and glands and retaining bolts. Also check for correct alignment between the rod bearing and those bearings that do not pilot into the cylinder head.

*This applies to Snubber bore sizes 1-1/2″ dia. thru 6″ dia. Larger bore sizes may require more than one technician to slide the piston rod.

Reservoir Assembly of a snubber
Flow control assembly of a snubber
Main cylinder assembly of a snubber

Hydraulic Shock Functional Testing and Sway Arrestor and Performance Criteria

The Nuclear Regulatory Commission Inspection and Enforcement Bulletin No. 75-05 has become the primary document for licensee action regarding snubber testing. As stated in the document itself: “…the installation of hydraulic suppressors provides a system for the restraint of category systems and components against excessive movement during seismic and fluid system transient conditions. Although in such a restraint system the failure or inoperability of a single Suppressor would not normally defeat the design function of the restraint system, it is desirable to provide for the periodic testing of a representative sample from the total population of Suppressors to assess the operational capability of the restraint system on a continuing basis.”

 

A requirement of the bulletin was that the licensee operating a power reactor facility, under NRC authorization:

  1. Review the design and installation of the hydraulic restraint systems.
  2. Review the design requirements which the various suppressors are to meet and note the differences between the design and purchase requirements. Illustrations of the requirements are velocity, acceleration, load, release rate, etc.
  3. Describe the testing performed on the hydraulic suppressors by both the licensee and supplier prior to installation to assure their operation in accordance with the design specifications.
  4. Describe the surveillance programs including test procedures enforced by the licensee or planned to be enforced for the operability of the hydraulic suppressors to meet the design specifications throughout the life of the facility.

As a result of the reports made to the NRC as requirement of Bulletin No. 75-05, and as additional information regarding suppressor installation and performance became available the issuance of NRC circulars such as Inspection and Enforcement Circular No. 75-05 and others contributed to the present functional test and inspection criteria now part of licensee operating technical specifications. As an aid to the various licensees operating with Bergen-Paterson hydraulic shock and sway arrestors, and engineering review of Bulletin No. 75-05 was made and comments offered and published to the field. This bulletin is a discussion of the engineering review.

 

Design requirements which the various suppressors are intended to meet should be taken from the architect-engineer job specifications. These would normally specify a piston rod velocity range during which rod lock-up actuation should take place. Regarding piston rod velocity during the bypass mode of operation, it is well to point out that the bypass system was originally incorporated into the control valve design simply as a means to insure reopening of the valve and unlocking of the restraint under any possible imposed operating condition. The concept of a piston rod velocity range during the bypass mode of operation was originally not a specific design requirement, but rather an operational characteristic that came out as a result during functional testing of the units. With the Bergen-Paterson units manufacturing control was placed on this velocity range as a means to achieve operational uniformity. The architect-engineer would be appraised of this bypass velocity rate in his review for product approval but, as was the case in many job specifications, it was not called for as a specific requirement.

 

The HSSA units are made available as standard catalog products in the following sizes:

 

HSSA SIZE CYLINDER BORE RATED CAPACITY
3 1.50″ 3,000 lbs.
10 2.50″ 10,000 lbs.
20 3.25″ 20,000 lbs.
30 4.00″ 30,000 lbs.
50 5.00″ 50,000 lbs.
70 6.00″ 70,000 lbs.
130 8.00″ 130,000 lbs.
200 10.00″ 200,000 lbs.

 

In application, the restraint designer establishes the “as installed” loading and movement conditions by formal calculation and normally makes his unit size and stroke selection based on the standard available unit having load and movement capabilities greater than his requirements, taking into account the necessary capacity reduction to account for column action of the overall strut length. As a plant operator, it must be assumed that the size selection made during the plant design phase has been reviewed and approved as being adequate for the calculated imposed loading conditions.

 

Each individual unit is tested to demonstrate fluid containment integrity and operational characteristics. It is necessary to describe both the design criteria and testing procedure with relation to a time frame because the manufacturing technique, testing apparatus, and procedures were changed when the manifold configuration model replaced the external pipe configuration model:

 

OPERATIONAL DESIGN CRITERIA

(Applies to all Bore Sizes)

 

  1. Piston shall be free to move in either direction with poppet valves remaining fully open for all piston velocities 10 inches per minute and slower. Tolerance plus or minus 2 inches per minute.1 (applies to all models).
  2. Poppet valves shall be designed for closure when piston velocity reaches 10 inches per minute for both compression and extension stroke. Tolerance on velocity for closure shall be plus or minus 2 inches per minute. (applies to all models).
  3. Orifice shall permit continued piston movement in either direction after valve closure at a rate of 4 to 6 inches per minute at rated design capacity.”

 

1 Tolerance on rates are established as a target goal to maintain uniformity of production. These values are arbitrary and have been selected as ultimate performance targets. The acceptance range is established by periodic review of individual test and phenomenon. The results on all units in a production run and the range is mutually established and reduced as improved manufacturing techniques are employed. The acceptance range at time of manufacture becomes the functional test and performance acceptance criteria enforced by Bergen-Paterson Quality Control Personnel.

 

 

CURRENT TESTING CRITERIA

(Applicable to all units tested after October, 1972 Serial Numbers F84806 thru F98991, G12039 and up)

The assembly, final test requirement and operational characteristics for each individual unit is governed by specific procedures. Briefly described, the operational characteristics are established by physical test of each fully assembled unit. As part of the final assembly of the major components, the cylinder is set horizontally in a calibrated test stand. The cap end of the cylinder is bracketed to the test stand base and the piston rod is coupled in line to the piston rod of a power driven 8 inch bore hydraulic cylinder which is used to stroke the unit being tested. The velocity of the 8 inch bore unit can be varied by manually controlling the volume of fluid pumped for each direction of stroke. A force transducer and terminal display signal system is calibrated to: display force in pounds for both tension and compression and rod velocity is taken as a direct reading from a velocity instrument package integral to the test stand. The first check made is for piston rod alignment and binding. Prior to the cylinder being charged with fluid, the unit is stroked using an automatic “bind test” controlled drive setting on the test stand for the particular size unit being tested. Excessive resistance to movement would be indicated by the opening of a fluid pressure switch and the shutting down of the pump motor. Newer test equipment makes use of direct load instrumentation and reports resistance to movement or “drag” load directly in pounds force.

The cylinder is then charged during an extension stroke of the piston and the valve manifold attached and filled by a pouring operation. A temporary test fitting is attached to the valve and at least 4500 psi fluid pressure is applied for a minimum of 20 seconds during which fluid containment is visually checked.

The reservoir is then mounted and fluid filling is performed under pressure thru the normal field filling alemite fitting. The unit is now in its fully assembled and filled condition.

After random stroking of the unit, the poppet valve closure test is conducted for each direction of stroke by slowly increasing the piston velocity and noting the velocity at the time of an instantaneous increase in fluid pressure denoting valve closure “activation”.

The bypass “release” rate of flow in each direction is then checked by first applying a high velocity rate to close the valve and then establishing the rated force capacity of the unit. As the unit is stroked thru under the rated force condition, the velocity is checked and noted.

The unit is cleaned off and allowed to stand for a period of time on clean paper and then checked for evidence of leakage.

 

FORMER TESTING PROCEDURE

(Applicable to all units tested prior to October 1972)

 

Applies to all models except units made prior to June 1969. These can be identified as being units with external piping to the accumulator with the following serial numbers:

487278 thru 487820

and F60635 thru F81302

For these specific units, the bypass rate is approximately: 15 inches per minute for 2.50″ Bore Units 10 inches per minute for 3.25″ & 4.00″ Bore Units

 

The operational characteristics of the assembled unit is established by determining the control valve fluid flow characteristics at the various phases of operation. This is done by setting up each individual control valve in a fluid test stand and physically capturing and measuring the fluid flow volume over a specific time period and comparing the results to establish minimum- maximum flow rates at the test pressure that are equivalent to flow rates at actual design rated pressure. These values were originally determined by calculations and then by physical experiment using valves from units whose fully assembled characteristics had been established as being within the piston velocity tolerance ranges for the various phases of operation such as valve closure and bypass rates. The cylinder is filled with fluid prior to mounting of valve using a piston stroking operation and the valve is then mounted and filled using a pouring operation. The fluid containment integrity of the cylinders with valve body attached is established by applying 3500 psi fluid pressure thru the valve port to which the accumulator is normally attached and visually checking for leaks over a specific time period. The accumulator is then attached and charged with fluid, the unit is cleaned and allowed to stand for a period of time and then checked visually for leakage.

In addition to the above described testing procedures performed on each individual unit, dynamic testing has been performed on some selected units to demonstrate operational characteristics during shock loading and vibration conditions.

As a general consideration, it is well to point out that the piston rod velocity of 10 inches per minute was established as a standard by Bergen-Paterson in order to maintain uniformity. This value was selected as being greater than any normally anticipated thermal growth rate and less than any expected imposed shock loading. In reality, this condition should be considered as a velocity range and it is suggested that for normal piping installations, the accepted actuation velocity range should be approximately 5 to 20 inches per minute and approximately 2 to 20 inches per minute for bypass “release” rate at unit design load. These ranges are valid at an ambient temperature of 68-70°F. During review of test results it has been determined that the performance characteristics of the hydraulic shock and sway arrestor vary due to temperature considerations. As a result of temperature, variances have been noted in viscosity and fluid density. Although it was always known that hydraulic units would be temperature sensitive, empirical analysis has shown that the effect is approximately .2 inches per minute of performance variance per “F., between the test range of 60° to 95 °F in activation and .05 ipm per °F for release rate. The temperature effect must be considered when performing functional tests to meet the NRC criteria. Failure to normalize the test results to the initial factory calibration criteria will result in erroneous failure analysis should a unit fall out of the acceptance range. Figures 1 and 2 illustrate the effect of temperature and its application to Bergen-Paterson’s manufacturing acceptance criteria.

Another consideration of functional testing is repeatability. As with any fluid device, repeatability of performance must be accounted for. The hydraulic shock and sway arrestor has demonstrated a functional repeat of activation and release rate calibration results within 2 3 inches per minute of normalized calibrated results. Repeatability is a function of:

  1. Fluid velocity and shock perturbations within the hydraulic cylinder and flow control section.
  2. Load application technique.
  3. Terminal readout repeatability.
  4. Inertia of the test system, etc.

 

A testing technique should be developed to supplement the Licensee’s test procedure. This will ensure uniformity of testing and an increased reliability in Snubber performance.

 

Graph showcasing the release date of H.S.S.A and temperature effect calibration limits

Graph showcasing the release date of H.S.S.A and temperature effect calibration limits

Ethylene-Propylene Elastomers Used in Hydraulic Shock and Sway Arrestors

The elastomer compounds selected for use in the hydraulic shock and sway arrestors are chosen to perform in nuclear power plant environments. The environments include:

  1. High temperature
  2. Radiation
  3. Steam and humidity in accordance with specifications

 

In addition, the seal must retain the working fluid of the arrestor to enable it to be operational at any time.

To date there are no known elastomers that can meet the forty (40) year design life criteria specified by most users. However, the objective is to provide an adequate seal material that will provide the longest possible life and minimal maintenance.

To appreciate the difficulty of seal selection, it is necessary to understand the conditions which deteriorate the seal to a point where it is no longer considered functional. Both radiation and high temperature are the most detrimental of environmental conditions. Both are energy sources which work on the elastomer’s molecular structure eventually causing chain scission and modification of the mechanical properties. Of the Ethylene-Propylene family, compound E740-75 exhibits the best radiation resistance. Ethylene-Propylene as a generic material has excellent high-temperature resistance and is usually applied in applications between -65°F and +300°F for continuous service. These temperature limits are general and must be considered in conjunction with the media the elastomer must seal.

A methylphenyl polysiloxane silicone fluid (1154) is used as the working fluid in HSSA units. This material has been tested in high temperature and radiation environments in conjunction with various EP seal compounds and has been found most compatible with the following:

 

E4248 A 75 (E740-75)
E4207 A 90 (E652-90)
E740-75
E93 B1 (E740-75)

 

These compounds are expressly used in static, dynamic, scraping and auxiliary sealing applications throughout the Hydraulic Arrestor. Compound E740-75 is generally requested in radiation environments but is in reality strictly an ‘O’ ring compound. Compound E4248 A 75 is the packing compound equivalent to E740-75. The manufacturing process involved in dynamic packing molding requires a modification of the ‘O’ ring compound to produce acceptable seals. E4248 A 75 does exhibit the same response to radiation, heat and fluid as it’s counterpart E740-75. In a similar manner, compound E4207 A 90 is equivalent to ‘O’ ring compound E652-90. However, this 90 durometer elastomer is not used in the fluid media of the Arrestor and is restricted to scraping or auxiliary sealing service. Compound E93 B1 is again equivalent to E740-75 and the seals molded from it are used in the quick fill (filler plug) fitting used on all HSSA unit pressurized reservoirs.

Another consideration is seal selection is durometer-Shore A hardness. The major portion of the life span of a snubber is spent in static service. For hydraulic snubbers, this means low or no pressure to activate pressure-responsive seals. Low durometers are selected to maintain an adequate pressure seal. In scraping or auxiliary sealing service, such as rod wipers and back up washers, high durometer materials are sought. These components are chosen to have a Shore A 90 durometer hardness, to safeguard against seal extrusion and to wipe the piston rod clean of normal debris.

The useful shelf and service lives of the Ethylene-Propylene seal is a function of the storage and various environmental conditions. The average shelf life of the E-P seals furnished by Bergen-Paterson is expected to be between 5 and 10 years but is dependent upon the following:

 

  1. Ambient temperature not exceeding 120°F (49°C)
  2. Exclusion of air (oxygen)
  3. Exclusion of contamination
  4. Exclusion of light (particularly sunlight)
  5. Exclusion of ozone-generating electrical devices
  6. Exclusion of radiation

 

Generally, polyethylene bags stored in larger cardboard containers or polyethylene lined craft paper bags ensure optimal storage life.

The service life of the seal commences with installation and is again considered in the 5-10 year category, but is dependent upon radiation and heat energy doses. The following figure illustrates radiation effects.

 

Compound E740-75 Radiation Test Data

Physical Properties Original 107Rads 108Rads
Hardness, Shore A; pts. (chg. pts.) 70 +3 +9
Tensil Strength, psi (chg. %) 2080 +3 -18
Elongation, % (chg. %) 233 -17 -18
Modulus @ 100%, psi (chg. %) 554 +46 —
TR-10,°F -59 -60 —
Compression Set, 25% Deflection 93 Days @RT
% of Original Deflection
6.7 28.6 90.5

 

All values are typical and should not be used for specification limits.

 

The radiation dosage limit for ‘O’ rings may be as high as 1 X 108 Rads or as low as 1 X 107 Rads for packings, but 1 X 107 Rads is expected to be the maximum normal acceptable radiation dosage. In terms of years, at normal plant design radiation levels, the service life approaches 10 years. In addition, temperature effects also determine service life. Operating below temperature limits of +200°F should provide optimum life, whereas exceeding that limit impairs service life. The other factor to be considered in service life is mechanical wear. Some applications may dictate replacement of dynamic packings at earlier scheduled intervals than others due to wear alone.

 

Ethylene – Propylene materials are generally compatible with the following material:

  1. Phosphate-ester base hydraulic fluids
  2. Steam (to 400°F)
  3. Water/hot water
  4. Silicone oils and greases
  5. Dilute acids
  6. Dilute alkalies
  7. Ketones
  8. Alcohols

 

These materials are not compatible with:

  1. Petroleum oils
  2. Di-ester base lubricants

 

When in contact with these materials, the Ethylene-Propylene compounds are severely degraded and/or destroyed due to excess swell, loss of mechanical properties, or disintegration.

 

Whenever a solvent is used to clean components of the hydraulic arrestor all traces (wetting) of the material should be removed prior to installation of new seals to assure that no contamination exists. There are numerous solvents available in the market and specific information regarding compatability of these with the Ethylene-Propylene seals may be obtained from the Product Engineering Department.

 

To summarize, the environment of the seal dictates its total life. In some cases 20 years may elapse from the time the seal was originally manufactured until it is retired from service. The 5 10 year storage and service lives, respectively, are projections based upon past history of similar elastomer compounds and service history of the Ethylene-Propylene seals themselves. The seal performance witnessed to date indicates that these projections are acceptable.

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