Quick answer: O-rings seal reliably to 150 bar with standard 70A compounds and proper clearance. Above 150 bar dynamic or 200 bar static, add PTFE backup rings and upgrade to 80–90 Shore A. Above 400 bar, use dual backup rings (step-cut or solid), 90 Shore A, and diametral clearance ≤ 0.08 mm. Above 700 bar, switch to PEEK backup rings with solid ring configuration and clearance ≤ 0.05 mm. The primary failure mode — extrusion through the clearance gap — is controlled by the combination of hardness, gap width, and backup ring geometry.
O-rings seal at pressures exceeding 1,000 bar when the gland design prevents the primary failure mode: extrusion. As pressure increases, elastomer is pushed toward the clearance gap between the piston or rod and the bore — if the gap is large enough relative to the material hardness, the elastomer flows into and through the gap, creating permanent leakage. The solution is a three-part engineering response: increase material hardness, minimize clearance gap, and install PTFE backup rings to physically block the gap. Every other aspect of high-pressure gland design serves one of these three objectives.
Extrusion Mechanism: How and Why It Happens
Extrusion is not a sudden event — it is a progressive failure that begins with micro-extrusion at the first pressure excursion and accumulates with each subsequent cycle. The mechanism:
- Pressure is applied and the O-ring is loaded against the sealing surfaces
- The elastomer under the highest stress concentration (at the clearance gap edge) begins to deform into the gap
- On a dynamic seal, the return stroke partially recovers the extruded material — but each cycle leaves a small permanent deformation at the gap edge
- Extruded material accumulates until it forms a thin ribbon extending into the gap — this ribbon is sheared by the next dynamic stroke
- The sheared material cannot return to the O-ring cross-section; the O-ring becomes thinner at the gap edge, reducing contact stress and eventually allowing leakage
Five independent variables control extrusion severity:
| Variable | Effect on Extrusion | Design Response |
|---|---|---|
| Pressure (bar) | Linear relationship — higher pressure = higher extrusion force | Increase hardness; add backup rings above threshold |
| Clearance gap (mm) | Exponential effect — doubling gap multiplies extrusion rate 4–8× | Minimize by tightening bore/rod tolerances |
| Material hardness (Shore A) | Higher hardness resists gap penetration — 90A requires 3–4× more force than 70A to extrude | Specify 80–90 Shore A above 100 bar |
| Temperature (°C) | Higher temperature reduces modulus — 30°C rise roughly halves extrusion resistance | Account for system operating temperature, not ambient |
| Dynamic motion | Reciprocating motion shears extruded ribbon; rotary motion twists it — both accelerate loss | Lower compression rate in dynamic grooves (10–15%) |
Pressure Classification and Design Response
| Pressure Range | Service Class | Primary Extrusion Risk | Required Countermeasures |
|---|---|---|---|
| 0–70 bar | Low | Negligible at standard clearance | Standard 70 Shore A, standard groove |
| 70–150 bar | Medium | Moderate — marginal with 70 Shore A at high temp | 80 Shore A recommended; verify clearance |
| 150–400 bar | High | High with standard design | 80–90 Shore A + single PTFE backup ring |
| 400–700 bar | Very high | Certain without countermeasures | 90 Shore A + dual PTFE backup rings; clearance ≤ 0.08 mm |
| 700–1,000 bar | Ultra high | Extreme | 90 Shore A + dual solid PTFE or PEEK backup rings; clearance ≤ 0.05 mm; split gland |
| > 1,000 bar | Extreme | Beyond standard O-ring capability | Metal-to-metal with elastomeric energizer; specialty seal design |
Material Selection: Hardness and Base Compound
Hardness selection by pressure
Hardness (Shore A) is the single most important material property for extrusion resistance. The physical reason: higher hardness means higher modulus — greater force per unit area is required to deform the material into the clearance gap.
| Pressure Class | Recommended Hardness | Notes |
|---|---|---|
| < 70 bar static | 70 Shore A | Standard; maximum conformability |
| < 70 bar dynamic | 70–80 Shore A | 80 Shore A reduces friction heat |
| 70–150 bar | 80 Shore A | Minimum for sustained medium-pressure service |
| 150–400 bar | 90 Shore A | Standard high-pressure O-ring specification |
| > 400 bar with backup rings | 90 Shore A | Backup rings handle extrusion; O-ring provides sealing force |
Compression set penalty at high hardness: 90 Shore A compounds have higher compression set than 70 Shore A at equivalent temperature conditions. A 70 Shore A NBR at 100°C/70h (ASTM D395 Method B) shows 20–35% compression set; 90 Shore A NBR at the same conditions shows 35–55%. This means high-pressure 90 Shore A seals lose contact force faster over time and require more frequent inspection intervals.
Dynamic seal hardness trade-off: For reciprocating dynamic seals, higher hardness increases friction, heat generation, and rod/bore wear. The trade-off between extrusion resistance (favors hard) and friction/wear (favors soft) determines the practical hardness limit for dynamic service. For most hydraulic cylinders, 90 Shore A is the practical upper limit for reciprocating dynamic service — beyond that, dedicated lip seals or PTFE-based designs are more appropriate.
Base compound selection by service condition
| Material | Hardness Range | Max Temp (continuous) | Chemical Resistance | Pressure Service |
|---|---|---|---|---|
| NBR 90 Shore A | Available | +120°C | Petroleum hydraulics, mineral oil | Standard to 400 bar dynamic; to 700 bar static with backup rings |
| HNBR 90 Shore A | Available | +150°C | Better than NBR in H₂S, amine service | Oil & gas sour service; autoclave hydraulics |
| FKM 90 Shore A | Available | +200°C | Petroleum, aromatic solvents, many chemicals | Chemical-resistant high-pressure static |
| EPDM 90 Shore A | Available | +150°C (dry) | Water, steam, phosphate-ester hydraulics | Water hydraulics, fire-resistant fluid systems |
| HNBR 90 Shore A NACE | Specific compounds | +150°C | H₂S/CO₂ sour gas | NACE MR0175/ISO 15156 qualified service |
Adiabatic heating consideration: At very high pressure with rapid pressurization, the elastomer and compressed fluid can undergo adiabatic temperature rise. For gas systems (nitrogen, CO₂) pressurized rapidly from ambient to >400 bar, localized temperatures at the seal can reach +50 to +100°C above ambient. The O-ring compound must tolerate both the ambient service temperature and the adiabatic peak temperature during pressurization.
Backup Ring Types: Selection and Pressure Range
Backup rings are not a secondary consideration — above 150 bar for dynamic seals and 200 bar for static seals, they are the primary mechanism for extrusion prevention. The O-ring provides sealing force; the backup ring bridges the clearance gap.
Backup ring style comparison
| Style | Installation Method | Max Effective Pressure | Seal Type | Notes |
|---|---|---|---|---|
| Solid flat ring | Split gland (disassembly required) | > 700 bar | Static preferred | No weak point; highest extrusion resistance |
| Scarf-cut ring | Snap-in (expandable) | 400–700 bar | Static and light dynamic | 45° diagonal cut; small gap when installed |
| Spiral-cut ring | Coil-and-slide (no disassembly) | 200–400 bar | Dynamic reciprocating | Small gap at each coil turn — acceptable for dynamic |
| Step-cut ring | Two-step snap-in | 400–500 bar | Static and dynamic | No through gap when installed; better than scarf at high pressure |
| PEEK machined ring | Split gland | > 700 bar | Ultra-high pressure | Harder than PTFE; resists PEEK itself extruding at extreme pressure |
Single vs. dual backup ring selection:
- Single backup ring (low-pressure side only): Effective when pressure direction is fixed — one-directional sealing
- Dual backup rings (both sides of O-ring): Required when pressure direction alternates (double-acting cylinders, pressure-cycling systems) or when pressure exceeds 400 bar
For double-acting hydraulic cylinders, always specify dual backup rings. A single backup ring on the wrong side of a reversed-pressure excursion provides zero protection.
Backup ring material selection
| Material | Hardness | Max Temp | Key Property | Application |
|---|---|---|---|---|
| Virgin PTFE | 55–65 Shore D | +260°C | Lowest friction; chemical resistance | General purpose; pharmaceutical; chemical |
| Glass-filled PTFE (25% glass) | 60–70 Shore D | +260°C | Reduced creep vs. virgin PTFE | Hydraulics > 200 bar; better dimensional stability |
| Bronze-filled PTFE (40% bronze) | 65–75 Shore D | +260°C | Best thermal conductivity; lowest creep | High-load dynamic; heat dissipation needed |
| Carbon-filled PTFE (25% carbon) | 60–70 Shore D | +260°C | Low friction; good wear resistance | Rotary and reciprocating dynamic |
| PEEK (polyetheretherketone) | 85–90 Shore D | +250°C | Hardest anti-extrusion ring; resists PEEK extruding | Ultra-high pressure (> 700 bar); cryogenic |
| UHMWPE | 60–70 Shore D | +80°C | Low cost; adequate for low-temp water | Water hydraulics at lower pressure |
PTFE creep at high temperature: Virgin PTFE backup rings creep (cold flow) under sustained compressive load at elevated temperature. At +150°C, a virgin PTFE backup ring compressed between the O-ring groove shoulder and the bore surface can deform plastically, losing contact with the groove shoulder and creating an extrusion path. Glass-filled or bronze-filled PTFE provides significantly better creep resistance for high-temperature service (oil and gas, hydraulics above +100°C).
Groove Geometry for High-Pressure Service
Groove width with backup rings
Adding backup rings requires wider grooves to accommodate the additional rings without excessive compression on the O-ring. Groove width (W) as a multiple of O-ring cross-section diameter (CS):
| Configuration | Groove Width (W) |
|---|---|
| O-ring only, static | 1.15–1.25 × CS |
| O-ring only, dynamic | 1.25–1.35 × CS |
| O-ring + 1 backup ring | 1.45–1.65 × CS |
| O-ring + 2 backup rings | 1.80–2.10 × CS |
Groove width tolerance: High-pressure grooves require tighter width tolerances than standard grooves because excess width allows the backup ring to tilt rather than remaining flat — a tilted backup ring leaves a gap at its edges. For pressures above 400 bar, groove width tolerance should be +0.00/−0.05 mm rather than the standard ±0.10 mm.
Clearance gap limits by pressure
The diametral clearance gap between the rod/piston and the bore is the parameter most directly responsible for extrusion. Maximum allowable clearance (total diametral gap, both sides combined):
| System Pressure | Maximum Diametral Clearance (70 Shore A) | Maximum Diametral Clearance (90 Shore A) | With Backup Rings |
|---|---|---|---|
| < 70 bar | 0.40 mm | 0.50 mm | Not required |
| 70–150 bar | 0.20 mm | 0.30 mm | Recommended |
| 150–400 bar | 0.10 mm | 0.15 mm | Required (single) |
| 400–700 bar | 0.05 mm | 0.08 mm | Required (dual) |
| > 700 bar | 0.03 mm | 0.05 mm | Required (dual solid) |
These values apply at the maximum operating temperature — thermal expansion of the bore or rod material must be accounted for. Steel bores and aluminum pistons have different thermal expansion coefficients; at +150°C, the gap calculated at room temperature changes.
Compression rate for high-pressure grooves
| Application Type | Compression Rate | Gland Fill (%) | Notes |
|---|---|---|---|
| Static high-pressure | 20–25% | 85–95% | Higher compression increases initial contact stress |
| Dynamic reciprocating (< 400 bar) | 10–15% | 80–90% | Lower compression limits friction heat generation |
| Dynamic reciprocating (> 400 bar) | 12–18% | 82–92% | Backup rings handle extrusion; O-ring compression can be moderate |
| Rotary (< 150 bar) | 8–12% | 80–88% | Lowest compression tolerable; friction is primary concern |
Gland fill at pressure: At high operating pressures, elastomers compress under hydrostatic load. An NBR O-ring at 500 bar fills approximately 2–3% more of the gland volume than at atmospheric pressure due to bulk modulus compression of the elastomer. Gland design should not fill the groove to 100% at atmospheric — leave the 85–95% fill limit to accommodate pressure-induced volumetric change and prevent gland hydraulic lock.
High-Pressure Dynamic Seals: Speed, Heat, and Lubrication
Dynamic sealing at high pressure generates heat at the seal contact zone proportional to contact pressure × sliding velocity × friction coefficient. At pressure above 200 bar with reciprocating motion:
- Contact stress at the O-ring-to-rod interface exceeds 10–15 MPa
- At 0.3 m/s surface speed, heat generation at the contact zone can raise local temperature 30–60°C above fluid temperature
- This localized heating degrades material faster than ambient temperature would suggest — compound selection should be based on the contact zone temperature, not the system temperature
Practical guidelines for high-pressure dynamic sealing:
- Surface speed limit: < 0.5 m/s for reciprocating O-ring seals above 200 bar; above this, specify lip seals, wiper seals, or spring-energized PTFE
- Bronze-filled PTFE backup rings: Thermal conductivity 3–5× higher than virgin PTFE — conducts heat away from the contact zone; specify for > 300 bar dynamic service
- Lubrication: Flooded lubrication (submersed seal in fluid) dramatically reduces friction compared to wiping conditions — maintain lubrication at seal contact zone
- Compression rate for dynamic: 10–15% maximum — higher compression increases contact stress linearly, which increases friction heat quadratically
Surface Finish Requirements for High-Pressure Grooves
Surface finish on the sealing surfaces (bore, rod, groove walls and base) becomes increasingly critical as pressure rises. Rough surfaces damage the O-ring on installation and during dynamic service; excessively smooth surfaces reduce the elastohydrodynamic lubricant film in dynamic applications.
| Pressure Class | Rod/Bore Sealing Surface (Ra) | Groove Base and Walls (Ra) | Notes |
|---|---|---|---|
| < 70 bar (dynamic) | 0.4–0.8 μm | 1.6–3.2 μm | Standard honed finish |
| 70–200 bar (dynamic) | 0.2–0.4 μm | 0.8–1.6 μm | Improved hone or ground finish |
| 200–500 bar (dynamic) | 0.1–0.2 μm | 0.4–0.8 μm | Hard chrome or precision grind |
| > 500 bar (dynamic) | 0.05–0.1 μm | 0.2–0.4 μm | Superfinish; Rz < 1.0 μm |
| Static (all pressures) | 0.4–1.6 μm | 0.8–3.2 μm | Less critical; no sliding wear |
Groove edge radius at high pressure: Sharp groove edges (r < 0.05 mm) cut the O-ring during installation and under pressure cycling. For high-pressure service, specify groove edge radius of 0.10–0.25 mm. The lead-in chamfer on the housing bore should be 15–20° at pressures above 200 bar.
Common High-Pressure Design Mistakes and How to Avoid Them
Mistake 1 — Too much initial compression: Over-compressing (>25% for static, >15% for dynamic) accelerates compression set, increases friction heat, and can cause the O-ring to hydraulically lock in the groove. Use the compression rates above, not maximum possible compression.
Mistake 2 — Ignoring thermal expansion in the gap calculation: A steel rod in an aluminum bore at +150°C has different diametral clearance than at room temperature. Aluminum expands ~2.3× faster than steel — if the room-temperature clearance is 0.10 mm, the clearance at +150°C may be 0.30 mm. Always calculate gap at maximum operating temperature.
Mistake 3 — Single backup ring in a double-acting cylinder: A double-acting cylinder reverses pressure direction on every stroke. A single backup ring on one side provides zero extrusion protection when pressure reverses. Always use dual backup rings for double-acting service.
Mistake 4 — Backup ring on the high-pressure side: Backup rings work by physically blocking the clearance gap on the low-pressure side. Installed on the high-pressure side, the backup ring is loaded toward the O-ring, not toward the gap — providing no extrusion protection and adding compression set risk to the O-ring.
Mistake 5 — Using spiral-cut backup rings above their pressure rating: Spiral-cut PTFE rings have a continuous helical gap around their circumference. At pressures above 400 bar, the O-ring extrudes through the helical gap rather than through the bore clearance — the spiral-cut ring provides false confidence. For > 400 bar, use step-cut or solid rings.
Mistake 6 — Ignoring backup ring creep at high temperature: Virgin PTFE creep at +150°C can reduce the effective backup ring thickness by 5–10% over 1,000 hours. For sustained high-temperature service, specify glass-filled or bronze-filled PTFE to maintain backup ring dimensional stability.
Application Examples with Design Specifications
Hydraulic press (500 bar, static)
- O-ring material: NBR 90 Shore A
- Backup rings: Dual solid glass-filled PTFE, one each side
- Diametral clearance: 0.04 mm at operating temperature (+80°C)
- Groove width: 2.0 × CS (to accommodate dual backup rings)
- Compression rate: 22% (static)
- Expected service life: > 5 years without replacement
Injection molding machine tie rod (350 bar, reciprocating dynamic)
- O-ring material: HNBR 90 Shore A (better compression set resistance than NBR at +120°C mold temperature)
- Backup rings: Single step-cut bronze-filled PTFE
- Diametral clearance: 0.08 mm at +120°C
- Compression rate: 13% (dynamic)
- Surface speed: 0.25 m/s
- Expected service life: 18–24 months (previously 6 months with NBR 70A without backup)
Wellhead control valve (700 bar, H₂S/CO₂ sour gas service, +150°C)
- O-ring material: HNBR 90 Shore A, NACE MR0175/ISO 15156 qualified compound
- Backup rings: Dual solid PEEK (higher hardness than PTFE prevents backup ring extrusion at 700 bar)
- Diametral clearance: 0.03 mm at +150°C
- Surface finish: Ra 0.2 μm (honed bore), Ra 0.2 μm (polished rod)
- Rapid gas decompression (RGD) qualification: NACE TM0297 tested
- Expected service life: Annual replacement per API well servicing standard; no field failure between intervals
Hydraulic sealing resources: High-pressure gland design rarely stands alone — compound selection, clearance control, and backup-ring geometry must be validated together before production tooling is cut. For material selection specific to hydraulic systems, see our high-pressure hydraulic O-rings page with pressure-class tables for NBR, HNBR, FKM and polyurethane, including when to upgrade from 70 Shore A to 90 Shore A and where HNBR replaces NBR in hot-oil service. When system pressure exceeds 10–14 MPa in reciprocating service, pair the O-ring with PTFE backup rings to block extrusion into the diametral clearance gap; at higher pressures, step-cut or solid PEEK rings become mandatory rather than optional insurance. For general petroleum-oil hydraulic service below +120°C, NBR O-rings remain the cost-effective baseline — verify groove squeeze with the compression calculator before issuing the BOM. If your assembly mixes North American and metric equipment, cross-check dash numbers on the size chart hub so cylinder glands and manifold ports reference the same nominal ID and cross-section.
Rapid Gas Decompression (RGD) Design for High-Pressure Gas Seals
Rapid gas decompression (RGD), also called explosive decompression, is a failure mode unique to high-pressure gas service. It occurs when gas that has dissolved into the elastomer under pressure comes out of solution faster than it can diffuse out when pressure is dropped quickly.
How RGD happens
- Gas dissolves into the O-ring under high pressure (Henry's Law)
- When pressure drops rapidly, dissolved gas forms bubbles inside the elastomer
- Bubbles expand and create internal tensile stress
- If the elastomer cannot relieve the stress, internal cracks and blisters form
- The seal loses structural integrity and leaks
RGD resistance by material
| Material | Gas Permeability | RGD Resistance | Typical Application |
|---|---|---|---|
| NBR | High | Poor | Not recommended for high-pressure gas |
| HNBR | Moderate | Good | Sour gas, CO₂ injection |
| FKM | Low | Very good | High-pressure gas valves, CO₂ service |
| FFKM | Very low | Excellent | Severe RGD conditions |
Design measures to reduce RGD risk
- Slow decompression: Reduce pressure at ≤ 1 bar/minute if process allows
- Soft elastomer: Lower-hardness compounds (70–75 Shore A) deform around bubbles rather than cracking
- Lower gas permeability: FKM or HNBR instead of NBR
- Avoid sharp edges: Internal cracks initiate at stress concentrators
- Test to NACE TM0297: Standard test is 50 rapid decompression cycles at rated pressure
For critical gas service, specify RGD-qualified compounds and validate with NACE TM0297 testing.
FAQ
Q1: At what pressure do I need backup rings?
For dynamic (reciprocating) seals, backup rings are recommended above 150 bar and required above 200 bar. For static seals (flanges, face seals, threaded connections), backup rings are recommended above 200 bar and required above 350 bar. At pressures below the threshold with proper clearance and 80–90 Shore A hardness, a standard O-ring without backup can seal reliably — but a backup ring adds cost of only a few cents per seal and provides extrusion insurance for margin applications.
Q2: Can I use a 70 Shore A O-ring for high-pressure service?
70 Shore A is generally reliable to approximately 100 bar static and 70 bar dynamic with proper clearance control. Above those levels, extrusion risk increases rapidly with 70 Shore A material. In an emergency substitution where 90 Shore A is unavailable, tightening the clearance gap (reducing bore tolerance) partially compensates for lower hardness — but this is a temporary measure, not a design approach. For any application above 100 bar, specify 80–90 Shore A.
Q3: What is the difference between spiral-cut and step-cut backup rings?
Spiral-cut backup rings have a continuous helical gap around the circumference that allows installation without disassembly (coil to insert). Step-cut backup rings have a single interlocking step joint that provides a much smaller gap when installed. For pressures below 300 bar, spiral-cut is adequate and preferred for its installation convenience. For 300–700 bar, step-cut is preferred because the smaller gap resists O-ring extrusion through the backup ring joint itself. For > 700 bar, only solid rings (requiring split gland) provide zero gap.
Q4: Can PTFE backup rings handle cryogenic service?
Yes. PTFE is one of the few polymers that remains functional at cryogenic temperatures — it retains dimensional stability and stiffness (modulus actually increases) at −200°C. For cryogenic high-pressure service (LNG transfer, liquid hydrogen, LOX), PTFE backup rings are standard. PEEK backup rings are also suitable for cryogenic service. NBR and FKM O-rings cannot be used at cryogenic temperatures — the O-ring must be spring-energized PTFE with the PTFE backup ring providing anti-extrusion support.
Q5: Do backup rings replace the need for tight clearances?
No — they are complementary requirements, not alternatives. Backup rings prevent the O-ring from extruding through the clearance gap. However, if the clearance gap is very large (> 0.20 mm), the backup ring itself can extrude or deform into the gap at high pressure, especially at elevated temperature. The backup ring works within a designed clearance range — typically with the backup ring bridging a gap of 0.03–0.15 mm. Excessive clearance overloads the backup ring and eventually causes backup ring extrusion, followed by O-ring extrusion. Tighten clearance to the design limits even when backup rings are installed.
Q6: Why does dynamic sealing require lower compression than static?
In a dynamic seal, friction at the O-ring-to-rod interface generates heat proportional to contact pressure × velocity. Contact pressure depends on both the initial compression (squeeze) and the system pressure. Higher initial compression increases base contact pressure, which increases friction heat at zero system pressure. When system pressure is added, total contact pressure is already elevated by the initial squeeze. For a 90 Shore A O-ring at 15% compression in a 350 bar system, the effective contact stress at the rod interface may reach 8–12 MPa — sufficient to generate significant heat at velocities above 0.2 m/s. Static seals have no velocity component, so friction heat is not a factor and higher compression (20–25%) is used to increase the initial contact stress margin.
Q7: Can I reuse backup rings after disassembly?
Solid PTFE backup rings that have not been extruded or deformed can be reused if they pass dimensional inspection — check that thickness is within ±0.05 mm of original dimension (creep reduces thickness over time). Spiral-cut and step-cut rings that show any permanent deformation at the joint should be replaced. PEEK rings are dimensionally stable and can typically be reused if undamaged. General guideline: backup rings cost less than $0.10–2.00 each — replace them at every seal change rather than risk failure from re-using a creep-deformed ring.
Q8: What is rapid gas decompression (RGD) and which O-ring compounds resist it?
Rapid gas decompression (RGD), also called explosive decompression, occurs in high-pressure gas service (CO₂, nitrogen, natural gas, H₂S) when system pressure is released quickly. During pressurization, gas dissolves into the elastomer under Henry's Law — at 400 bar CO₂, NBR absorbs significant CO₂ volume into the polymer network. When pressure drops rapidly (valve opening or line break), the dissolved gas nucleates into bubbles within the elastomer faster than it can diffuse out. The expanding bubbles create internal tensile stress that fractures the elastomer from within — blisters, internal cracks, and surface cratering are the visible signs. Compounds resistant to RGD are formulated with lower permeability (FKM and HNBR outperform NBR) and higher tear strength (resist crack propagation). Qualification testing follows NACE TM0297 (50 rapid cycles from rated pressure to near-ambient; no cracking or permanent deformation > specified limits). For CO₂ injection wells and high-pressure gas valves, specify RGD-qualified FKM or HNBR compounds — standard NBR O-rings will fail within the first few decompression events.
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Designing a high-pressure sealing system? Contact our engineering team with your pressure class, fluid type, temperature, dynamic vs. static service, and clearance dimensions — we provide compound selection, backup ring configuration recommendations, and groove design review. We supply NBR, HNBR, and FKM O-rings to 90 Shore A with matched PTFE and PEEK backup ring sets from MOQ 1 piece; 7–15 day lead time, 3–5 day express for stocked compounds.
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Related engineering resources: Hydraulic Seals | Extrusion & Backup Rings | Compression Calculator | Backup Ring Products