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A bolted flanged joint is one of the most common leak points in any industrial piping system. Even when the pipe, flange, and gasket are correctly specified, the joint can still fail in service because of how the gasket, stud bolt, and nut assembly is selected, stored, installed, and operated. For EPC contractors, refinery maintenance teams, and plant reliability engineers, understanding the typical failure modes is the first step to eliminating chronic leaks and unplanned shutdowns.
In this guide we walk through the most frequent causes of gasket and stud bolt failure observed in refineries, petrochemical plants, power stations, and shipbuilding piping systems, and show how the right material choice and installation discipline prevent them.
A flanged joint only stays tight when the residual gasket stress is maintained over the life of the connection. Three things break that balance: the gasket loses its ability to recover (compression set, creep, chemical attack), the bolts lose preload (yield relaxation, thermal cycling, vibration), or the joint is loaded unevenly from the start (wrong torque pattern, flange misalignment).
In our experience supporting oil and gas, petrochemical, and marine projects, the majority of in-service flange leaks on steel flanges and piping assemblies can be traced back to one of the root causes listed below, not to a defect in the flange or pipe itself.
Once a gasket has been compressed between two flange faces, it takes a permanent compression set. On the next opening, the gasket can no longer conform to the microscopic surface irregularities of the flange faces. Reinstalling a used spiral wound, compressed asbestos-free, or graphite gasket is one of the most common causes of re-leakage after a turnaround. replace the gasket every time the joint is broken.
Raised face (RF), flat face (FF), and ring type joint (RTJ) flanges each require a matching gasket geometry. A full-face gasket on an RF flange wastes bolt load outside the sealing area; a ring gasket on an FF flange has no centering support. Always select the gasket style per ASME B16.20 / B16.21, matched to the flange face and pressure class.
PTFE envelope gaskets begin to creep under bolt load above roughly 260 °C and decompose above 327 °C. In high-temperature services such as steam, hot oil, or refinery flare systems, this creep shows up as progressive loss of gasket stress and eventual blow-out. Switch to spiral wound gaskets with graphite filler, or flexible graphite gaskets, for elevated-temperature service.
On stainless steel or copper nickel flange systems, using a carbon steel inner ring in a spiral wound gasket creates a galvanic couple in the pipe bore. The ring corrodes, contaminates the process fluid, and weakens the seal. Match the inner ring alloy to the piping material (for example 304SS inner ring for 304SS pipe, 90/10 Cu-Ni for Cu-Ni systems).
Ordering gaskets by nominal pipe size alone is a frequent error. A Class 150 gasket for a 6 in line is physically different from a Class 600 gasket of the same NPS. The wrong gasket OD or inner ring diameter leads to either insufficient seating stress or a gasket that sits on the flange bore. Always specify gasket by NPS, pressure class, and material per ASME B16.20 or B16.21.
Tightening bolts sequentially around the flange produces uneven gasket compression: one side is fully loaded while the opposite side remains loose, and the gasket blows out on the weak side. The correct method is a star (cross) pattern in at least three passes — typically 30 %, 60 %, and 100 % of the target torque — followed by a final 360° verification pass, as recommended by ASME PCC-1.
ASME B16.5 flanged joints call for stud bolts with a nut on each end, not hex-head machine bolts. Machine bolts have a shorter thread length, an integral head that can interfere with torque tools, and an uneven load distribution. Stud bolts give balanced elastic behavior and are easier to torque with a calibrated wrench. For pressure piping, always use ASTM A193 stud bolts with ASTM A194 hex nuts.
A193 B7 stud bolts (4140 alloy steel) are the workhorse of the industry, but they lose yield strength above about 450 °C and become brittle below -40 °C. In high-temperature steam or hot reformer service, switch to A193 B16 (up to 540 °C). In cryogenic LNG or low-temperature ethylene service, use A320 L7 or L43. The bolt specification must match the design metal temperature, not just the pipe class.
When bolts are torqued dry, 80–90 % of the applied torque is lost to thread and nut-face friction. The actual bolt stretch — and therefore the gasket load — is only a small fraction of what the torque chart assumes, and the joint is under-loaded. Apply an anti-seize or controlled thread lubricant per ASME PCC-1 before assembly, and recalculate the torque value if the lubricant differs from the chart's assumption.
If the stud bolt sits flush with, or recedes inside, the nut face, the joint has no thread protrusion to absorb vibration and thermal expansion. ASME PCC-1 calls for at least one to three full threads of protrusion past the nut. Calculate the stud bolt length as: flange thickness + gasket thickness + washer thickness + 1.5 × nut height + required protrusion.
Combining B7 and B16 studs, or B7 with B7M, on the same flange is a frequent site error. Different grades have different elastic moduli and yield strengths, so they share load unevenly during thermal cycles. The softer bolts overload, yield, and lose preload, while the harder bolts stay tight. Always fit one flange with a single stud bolt grade and nut grade.
Stainless steel bolts and nuts are prone to galling during assembly. Once the threads are damaged, the bolt cannot develop the design preload. Use a compatible anti-seize compound, slow assembly speeds, and follow the bolt supplier's recommended torque. For critical services, specify B8 / B8M studs with B8 / B8M nuts from the same heat.
Every plant cycle produces differential expansion between the bolt and the flange. Over time the bolt relaxes, gasket stress drops, and the joint begins to weep. Tighten to target torque after the first thermal cycle (hot torque) where the procedure allows, and re-torque during planned turnarounds for chronic-leak services.
Piping connected to reciprocating pumps and compressors experiences continuous vibration that can back the nut off the stud bolt. Add a lock nut, a Nord-Lock style washer, or a belleville washer on critical joints. Where feasible, isolate the flange from vibration with flexible couplings or pipe supports.
Stud bolts stored outdoors, in humid plant air, or in contact with process chemicals can pick up surface corrosion. For high-strength grades (above 10.9 / ASTM A490 equivalent), absorbed hydrogen during acid cleaning or pickling can cause delayed brittle fracture. Store bolts in original packaging, indoors, and avoid acid cleaning of high-strength fasteners.
A reliable flanged joint is the result of four disciplined steps:
As a manufacturer and integrated supplier of industrial piping packages, EZ Steel Industrial supplies the full bolted-joint stack from one source — from the pipe fittings, steel and copper-nickel flanges, to matched stud bolt and nut sets and spiral wound gaskets. Our gaskets, stud bolts, and nuts are produced under ISO 9001 quality management, with full material certificates, hydrostatic and ultrasonic testing on the connecting piping, and traceability from melt to shipment.
For EPC packages, plant maintenance contracts, and shipbuilding orders, we can pre-assemble the gasket and bolt kit to your flange class, stud bolt grade, and torque specification. This eliminates field mismatches and is one of the most practical ways to remove the failure modes listed above from your piping system.
Send your flange class, service temperature, and process fluid details to our engineering team and we will return a recommended gasket, stud bolt, and nut specification with full traceability documentation.
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