During the on-site operation of the LNG receiving station, cryogenic ball valves have long faced three major failure pain points: condensed water freezing in the packing area leads to seal failure, extended valve stem misalignment causes abnormal operating torque, and SPE/DPE end Lip-seal seal ring assembly deformation and damage. In response to these industry problems, JH Valve Manufacturing combines the requirements of BS 6364 and API 607 standards and innovatively proposes systematic solutions. Through in-depth analysis of these three core design details, material science (Monel K500 valve stem cryogenic treatment), precision manufacturing (five-axis linkage machining center) and digital simulation (FEA contact stress analysis) are deeply integrated to provide a ball valve solution with reliable operation throughout the life cycle for ultra-low temperature conditions.
Overall design requirements – core technical specifications for cryogenic valves that meet extreme working conditions of -196°C
Cryogenic medium adaptability design (meeting the requirements for ultra-cold fluid transportation such as LNG and liquid nitrogen)
Key medium parameters
- Phase change control: In view of the LNG gasification expansion of 600 times, a double piston effect (DPE) sealing structure is configured
- Ice crystal prevention: Automatic activation of the electric heating system when ambient humidity is > 60% (in compliance with API 675 standard)
- Material compatibility: NACE MR0175 certified, resistant to H2S corrosion (concentration ≤ 5000ppm)
Temperature gradient management
- Thermal bridge blocking technology:
Three-layer composite structure: 1. Vacuum isolation layer (<0.01Pa) 2. Nano aerogel insulation layer (λ=0.018W/m·K) 3. Multi-layer aluminum foil reflective screen (8 layers alternately laminated)
- Cold shrinkage compensation design: The expansion coefficient difference between the valve stem (Monel K500) and the valve body (CF8M) is less than 3%
Safety and reliability guarantee – low leakage valve system certified by ISO 15848
▶ Double sealing protection
| Seal Type | Technical indicators | Test Standards |
| Main seal | Lip-seal dynamic seal resistant to -196℃ | ISO 5208 Grade A |
| Emergency Seal | Graphite + Inconel 718 fireproof combination | API 607 Fire Test |
▶ Fault prevention mechanism
- Anti-icing drainage system:
- 5° precision drainage chute (DN ≥ 200 is processed by laser milling)
- Drainage efficiency>1.5L/min (passed -162℃ condensation water simulation test)
- Intelligent early warning device:
- Frost thickness monitoring sensor (accuracy ±0.1mm)
- Abnormal torque alarm system (automatically cuts off the actuator when the limit is exceeded)
Standardized compliance—— Meet the technical requirements of mainstream LNG projects around the world
▶ Core certification system
- Pressure vessel standard: ASME B16.34 Class 1500 (PN250)
- Low temperature test specification: BS 6364 Type Testing (50 hot and cold cycles)
- Material certification: ASTM A351 Gr.LC3 (-196℃ impact energy ≥34J)
Key structural design
Optimized design of extended bonnet system
Anti-condensation water icing structure
- Gutter design :
- Angle control: 5°±0.5° precision bevel, using five-axis linkage processing (surface roughness Ra≤1.6μm)
- Split type solution: DN≥200 valves use milling slots (6-8 evenly spaced slots), DN<200 valves use integral turning bevels
- Drainage efficiency: Condensate discharge rate ≥ 1.2L/min (-162℃ dynamic test verification)
- Antifreeze material selection :
- The outer surface of the valve cover is sprayed with tungsten carbide coating (thickness 80-100μm, friction coefficient ≤ 0.15)
- The bottom of the drain tank is embedded with a polytetrafluoroethylene guide plate (temperature resistant to -200℃)
Dynamic sealing system
Composite stuffing box components
Four-stage sealing architecture :
- Main sealing layer: Lip-seal fluororubber ring (Shore hardness 75±5, pre-compression 15%-20%)
- Self-compensating structure: One-piece graphite bearing filler (with molybdenum disulfide lubricant)
- Double auxiliary seal:
- Upper layer: Expanded graphite ring (fire rating ASTM E119)
- Lower layer: modified PTFE sealing ring (30% glass fiber reinforced)
- Pressure self-adaptation: Opposed disc spring set (4 sets of springs, preload adjustable range ±20%)
Coaxiality compensation :
- Bearing packing pad embedded with self-lubricating copper sleeve (radial clearance 0.05-0.1mm)
- Allowable stem eccentricity compensation ±0.8mm (reducing operating torque by 35%)
Innovative design of valve seat seal
SPE end embedded seal
Structural upgrades :
- Closed groove process: groove width tolerance H8, 0.3mm thermal expansion gap reserved in depth direction
- Anti-twist design: Three guide ribs are added to the valve seat support ring (height 0.5mm, spacing 120° evenly distributed)
- Installation verification: The interference of Lip-seal after installation is 0.15-0.25mm (special liquid nitrogen freezing assembly tooling is required)
Performance advantages :
- Friction resistance is reduced by 40% (compared to traditional O-ring structure)
- Seal life increased to 10,000 cycles (ISO 5208 test standard)
Double piston effect at DPE end
- Spring configuration scheme :
- Class 150-600: Single spring back-to-back structure (spring wire diameter Φ1.2mm, material Elgiloy)
- Class 900-1500: Four-spring symmetrical structure (wire diameter Φ2.0mm, pre-compression 30%-35%)
- Friction Control :
- Valve seat support ring surface mirror polished (Ra≤0.4μm)
- Dynamic friction coefficient ≤ 0.08 (test data at -196°C)
Special functional structure
Anti-lock Braking System
- Low Temperature Expansion Compensation:
- The connection between the valve stem and the ball is designed with a 0.5mm axial floating clearance
- The guide groove opening is 20% larger than the conventional structure (to prevent cold jamming)
Emergency pressure relief channel
- Overpressure protection:
- A bidirectional bursting disc is set in the middle cavity of the valve body (bursting pressure is 1.33 times the rated value)
- Pressure relief direction diversion design (media discharge angle 45° downward)
Material Selection Specifications
Material classification and performance requirements
- Main structural materials
- Valve body/valve cover material
- Preferred material: ASTM A351 Gr.CF8M (low carbon 316L stainless steel)
- Low temperature impact energy: CVN≥34J at -196℃ (in accordance with BS 6364 requirements)
- Cryogenic treatment process: -196℃×8h cryogenic + aging treatment
- Alternative: ASTM A522 Type I (9% nickel steel)
- Applicable temperature: -196℃ to +200℃
- Tensile strength ≥690 MPa
- Preferred material: ASTM A351 Gr.CF8M (low carbon 316L stainless steel)
- Moving parts materials
- Valve stem material
- Monel K500 (Nickel-Copper Alloy):
- Low temperature yield strength ≥550 MPa (measured value at -162℃)
- Surface treatment: chemical nickel plating (thickness 30-50μm, HV≥400)
- Inconel 718 (high temperature alloy):
- Applicable to extreme working conditions: -253℃ to +650℃
- Hydrogen embrittlement resistance: NACE MR0175 certified
- Monel K500 (Nickel-Copper Alloy):
Core seal material specifications
- Static sealing material
- Valve seat sealing ring
- Reinforced PTFE:
- Glass fiber filling 25%-30%, friction coefficient ≤0.05
- Temperature range: -200℃ to +260℃
- Flexible Graphite:
- Fire rating: ISO 15848-1 Fire Safe certified
- Compression rate ≥40%, rebound rate ≥15%
- Reinforced PTFE:
- Dynamic sealing material
- Lip-seal materials
- Fluororubber (FKM):
- Low temperature brittle temperature: -40℃ (special formula can reach -60℃)
- Media resistance: passed LNG/liquid oxygen compatibility test
- Polyimide (PI):
- Wear resistance: wear rate ≤ 0.02mm³/N·m
- Thermal expansion coefficient: 4.3×10⁻⁶/℃
- Fluororubber (FKM):
Special treatment process
- Surface strengthening technology
- Ball surface treatment
- High velocity oxygen fuel spraying (HVOF):
- Coating material: WC-12Co (hardness ≥ 1100HV)
- Bonding strength ≥70 MPa (ASTM C633 standard)
- Chemical Vapor Deposition (CVD):
- Deposition layer: Al₂O₃/TiN composite layer (thickness 8-12μm)
- High velocity oxygen fuel spraying (HVOF):
- Low temperature stability treatment
- Deep cold aging process
- Process parameters: -196℃ liquid nitrogen immersion → +100℃ aging → secondary deep cooling
- Effect: Retained austenite content <3%, dimensional stability increased by 50%
Material Verification and Certification
- Checklist of mandatory items
- Low temperature impact test: -196℃ Charpy V-notch impact (ASTM E23)
- Intergranular corrosion test: ASTM A262 Practice E (boiling nitric acid environment)
- Phase change analysis: DSC differential scanning calorimetry (detection of -200℃ material phase change point)
- Industry certification requirements
- International General Certification:
- PED 2014/68/EU (EU Pressure Equipment Directive)
- NACE MR0103 (Acidic Environment Material Certification)
- Chinese Standard: GB/T 24925 (Technical Requirements for Cryogenic Valves)
Thermal management key design
Thermal bridge blocking technology
- Multi-layer composite insulation structure
- Vacuum insulation layer
- Vacuum degree ≤ 0.01Pa (helium mass spectrometer leak detection verification)
- Vacuum layer thickness: ≥8mm when DN≤100, ≥12mm when DN>100
- Nano aerogel filling:
- Thermal conductivity ≤ 0.018 W/m·K (measured value at -196℃)
- Water repellency ≥99% (prevent condensation water from penetrating)
- Reflective screen optimization:
- 8 layers of alternating aluminum foil (thickness 0.05mm, interval 1mm)
- Radiant heat resistance increased by 60% (compared to single-layer structure)
- Extended bonnet thermal gradient control
- Cold blocking design:
- The height of the extended section of the valve cover is ≥ 250mm (BS 6364 minimum requirement)
- Heat conduction suppression efficiency ≥85% (-196℃ to packing area temperature difference >120℃)
Temperature monitoring system
- Smart sensor networks
- Multi-point temperature measurement arrangement
- Measurement point distribution:
- Valve body cavity (direct contact with the medium)
- Stuffing box bottom (monitoring low temperature conduction)
- Actuator connection (anti-icing warning)
- Sensor Type:
- PT100 platinum resistance (accuracy Class A, ±0.15℃)
- Fiber Bragg grating sensor (anti-electromagnetic interference, resolution 0.1℃)
- Measurement point distribution:
- Dynamic thermal compensation algorithm
- Predictive Adjustment:
- Adaptive heating based on medium flow rate (response time < 3 seconds)
- Temperature fluctuation control ≤±2℃ (steady state condition)
Condensate management design
- Active anti-icing system
- Electric heating configuration
- Power density: 8-12 W/m (DN50-DN300 universal design)
- Heating material: Flexible graphite-based heating film (temperature resistance -200℃ to +250℃)
- Drainage structure enhancement:
- Spiral diversion groove design (drainage efficiency increased by 40%)
- Surface super hydrophobic coating (contact angle >150°, in line with ISO 27448 standard)
- Intelligent humidity control
- Environmental Monitoring Module:
- Humidity sensor accuracy: ±3% RH (0-100% range)
- Automatic start-stop threshold: Ambient humidity > 65% to start anti-icing mode
Thermal Management Validation Standards
- Type test requirements
- BS 6364 Thermal Cycle Test:
- 50 cycles of -196℃↔+50℃, no condensation on the outer surface of the valve
- The temperature of the packing area is always > -20℃
- API 607 Fire Test:
- After burning at 650℃ for 30 minutes, the insulation layer integrity rate is ≥90%
- Online monitoring indicators
- Heat flux control: ≤15 W/m² (-196℃ stable condition)
- Energy efficiency: Electric heating system power consumption ≤ 10% of rated value
Verification and testing
Core test items
- Low temperature performance verification
- Test standard : BS 6364 Type Testing
- Temperature range: -196°C (liquid nitrogen) to +50°C (ambient temperature)
- Number of cycles: 50 complete hot and cold cycles (each cycle ≤ 4 hours)
- Acceptance criteria:
- Stem seal leakage rate ≤10 ppm (ISO 15848-1 AH grade)
- Stuffing box area temperature>-20℃ (infrared thermal imaging verification)
- Test Equipment :
- Liquid nitrogen low temperature test chamber (temperature control accuracy ±2℃)
- Helium mass spectrometer leak detector (sensitivity ≤ 1×10⁻⁶ Pa·m³/s)
- Life and reliability testing
- Opening and closing life test
- Test conditions:
- Total pressure difference (Class 1500 corresponds to 22 MPa)
- Frequency: 10 times/minute (including start-stop shock)
- Acceptance Criteria:
- After ≥10,000 cycles, the wear of the sealing surface is ≤0.05mm
- Operating torque fluctuation range <±15%
- Test conditions:
Key test methods
- Phase change working condition simulation test
- LNG flash steam working condition simulation
- Test medium: LNG (-162℃) and natural gas mixed flow
- Test parameters:
- Flow velocity ≥ 30 m/s (simulating transient flow in pipeline)
- Pressure fluctuation range: ±20% rated value
- Performance requirements:
- Zero leakage of valve seat seal (bubble method detection)
- There is no resonance phenomenon in the valve body (vibration acceleration < 2g)
- Extreme environment adaptability test
- High humidity icing test:
- Spray water volume: 3 L/h (humidity>90% environment)
- Duration: 72 hours continuous operation
- Acceptance Result:
- The drainage trough is not blocked by ice (visual inspection + flow monitoring)
- Valve stem operating force increase ≤ 10%
Certification and Compliance
- International certification system
- Fire test certification (API 607 standard):
- Combustion temperature: 650℃~760℃
- Duration: 30 minutes
- Pass conditions:
- External leakage rate <100 ppm
- Seal integrity maintained (no structural failure)
- Material Certification :
- ASTM A351 Gr.LC3 (-196℃ Charpy impact energy ≥34J)
- NACE MR0175 (Hydrogen Sulfide Stress Corrosion Resistance Certification)
- China Standard Test
- GB/T 24925 cryogenic valve test:
- Low temperature sealing test: -196℃ pressure maintenance for 30 minutes
- Flow capacity test: Cv value error ≤ ±5%
Installation and maintenance specifications

Installation Specifications
- Pre-installation checks
- Key inspection items
- Cleanliness of valve body interior: particle size ≤ 25 μm (ISO 4406 16/14 grade)
- Sealing surface protection: Lip-seal anti-oxidation coating integrity (UV fluorescence detection)
- Material certificate verification: ASTM A351/EN 10204 3.1 certification
- Alignment requirements :
- Flange parallelism deviation ≤ 0.2mm/m
- Stem verticality error <0.5° (calibrated by laser centering instrument)
- Special low temperature installation process
- Cold preload technology:
- Bolt preload is 20% higher than normal temperature (using hydraulic torque wrench)
- Seat spring pre-compression adjustment: additional 10% compression under low temperature conditions
- Thermal Stress Avoidance:
- Pipeline compensator installation spacing ≤ 3 times the pipe diameter
- Forced jointing is prohibited (allowed cold tightening amount ≤ 1.5mm)
Operation and maintenance management specifications
- Preventive Maintenance Program
- Monitoring cycle
| Project | Cycle | Standard Methods |
| Packing leakage detection | per month | Infrared imaging + soap bubble method |
| Operating torque record | Quarterly | Digital torque sensor ±1% accuracy |
| Drain dredging | each year | Endoscopic visual inspection |
- Lubrication management :
- Stem grease: Perfluoropolyether (PFPE) based grease, temperature resistant -100℃~+260℃
- Grease injection frequency: every 500 openings and closings or 6 months (whichever comes first)
- Fault emergency handling
- Ice jam treatment process:
- Enable electric heating system (heating rate ≤ 5℃/min)
- Manual turning device assists rotation (maximum applied torque ≤ 150% of rated value)
- Inject IPA isopropyl alcohol thawing agent (purity ≥ 99.9%)
- Sealing failure response:
- Online replacement of Lip-seal technology (no need to release media)
- Emergency plugging fixture installation time ≤ 30 minutes
FAQ:
Q1:Why is CF8M the preferred material for the cryogenic valve body?
A1: CF8M (low-carbon 316L) significantly improves its low-temperature toughness through the double vacuum melting process. Its -196℃ impact energy is more than three times higher than that of conventional 304 stainless steel. It also has excellent resistance to chloride ion corrosion and is perfectly suited to the working conditions of LNG receiving stations.
Q2:Why is Monel alloy used instead of stainless steel for the valve stem?
A2: The yield strength of Monel K500 at -162°C is 550MPa, which is 40% higher than that of 17-4PH stainless steel. In addition, the nickel-copper alloy has natural corrosion resistance to hydrogen sulfide in liquefied natural gas, avoiding the risk of stress corrosion cracking (SCC).
Q3:Why must ultra-low temperature valves be designed with multi-layer insulation structures? Why is traditional insulation cotton not applicable?
A3: The multi-layer vacuum + aerogel + reflective screen structure can reduce heat conduction to 1/20 of conventional materials, while traditional glass wool will produce gaps due to shrinkage at -196℃, and the thermal insulation performance will drop sharply after absorbing water (thermal conductivity increases by more than 5 times). BS 6364 clearly requires that the outer surface temperature of the valve must be higher than the dew point to prevent ice from affecting operation.
Q4:How to avoid stuffing box freezing and jamming through thermal management design?
A4: Three points must be met at the same time:
The height of the extended section of the valve cover is ≥ 250mm as specified in BS 6364 (blocking the conduction of cold air)
The packing gland is equipped with an annular electric heating (maintaining temperature>-20℃)
Self-lubricating graphite filler (friction coefficient ≤ 0.1 at -196℃)
Q5:What are the differences between BS 6364 and ISO 28921 in low temperature testing? Which standard should be met first?
A5: BS 6364 requires more stringent hot and cold cycles (50 times vs. 30 times for ISO) and clearly defines the temperature gradient of the valve cover. Priority should be given to meeting the standards of the country where the project is located: European projects implement BS 6364, and ISO 28921 is optional in the Asia-Pacific region. Both standards require a leakage rate ≤ ISO 15848-1 AH level.
Q6:How to verify the sealing reliability of the valve under LNG flash vaporization conditions?
A6: A three-stage testing method is required:
Static sealing test: Maintain pressure at -162℃ for 1 hour, leakage rate ≤0.1 mL/min
Dynamic flash simulation: Rapid pressure reduction (down to 0.5 MPa within 1 second) to detect whether the sealing surface is detached
10,000 times life verification: Simulates 20 openings and closings per day throughout the year
Q7:Why does the pre-tightening force of the low-temperature valve bolts need to be increased by 20% compared to normal temperature? Will it cause damage to the sealing surface?
A7: Due to the shrinkage effect of the material, the shrinkage rate of 316L stainless steel at -196℃ is about 0.3%. The preload compensation can maintain the flange sealing pressure. Through finite element analysis, it is verified that the 20% increment can keep the gasket compression in the safe range of 18%-22% (ASME PCC-1 standard), and the PTFE gasket can avoid overload.
Q8:How to determine whether Lip-seal needs to be replaced? Are there any quantitative detection indicators?
A8: Three judgment conditions:
The width of the valve stem reciprocating friction mark is greater than 50% of the sealing surface width
Dynamic leakage rate > 100 ppm (ISO 15848-1 BH class)
Operating torque increase > 25% (compared to initial value)
It is recommended to use endoscope + friction acoustic emission detection technology for accurate judgment.
Learn more about Ball Valves《Complete Guide to Selecting Zero-Leakage Ball Valves: 30+ Types》
Summarize
This technical document systematically solves the industry problems such as low-temperature ball valve seal failure and abnormal operating torque through innovative solutions such as the 5° precision bevel drain groove design of the extended valve cover, the Lip-seal composite packing system and the four-spring back-to-back valve seat structure. Combined with vacuum multi-layer insulation (λ≤0.018 W/m·K) and 50 times of -196℃ hot and cold cycle verification, it achieves the high standard requirement of BS 6364 with a leakage rate of ≤10ppm. JH Valve Manufacturing Co., Ltd. strictly follows the NACE MR0175 corrosion-resistant material specification, API 607 fire test and ASME B16.34 design standard, and adopts full-process cryogenic treatment (-196℃×8h) and digital assembly process to provide ball valve products with full life cycle reliability guarantee for ultra-low temperature conditions such as LNG and liquid hydrogen.

