Company Information

* Company
* Name
* Phone

Key Parameters for Compressor inquiry

Suction Pressure

Discharge Pressure

Flow Rate

Cooling Method

Suction Temperature (℃)
Discharge Temperature(℃)
Power Supply(V/HZ)
Control Requirements
Gas Medium
Additional Remarks (You can also send your datasheet to our email)

Methane Compressor

Methane (CH₄) is the main component of natural gas and coalbed methane. It has a molecular weight of 16.04, a density of 0.717 kg/m³ under standard conditions, and is lighter than air so it tends to accumulate at high points after leakage. Its critical temperature is as low as -82.6°C, and its boiling point is -161.5°C, making the risk of liquefaction under conventional compression extremely low; however, special attention is required in high-pressure cryogenic processes (such as LNG). Methane is highly flammable and explosive, with an explosion limit in air of 5% to 15%. Its safety classification is Ex d IIB T4, imposing strict requirements on equipment sealing and explosion-proof performance. In industry, methane runs through the entire LNG chain—from raw gas boosting, liquefaction and storage, to gasification and distribution—and it is also an important chemical feedstock for ammonia synthesis and methanol production, as well as being used as a high-purity gas in the food and pharmaceutical sectors.
Methane Compressor
Methane Diaphragm Compressor Advantages
  • 01
    Ultimate Purity and Absolute Safety: 
    The static sealing structure of the diaphragm chamber achieves physical isolation between the gas and lubricating oil, ensuring the purity of compressed methane is as high as 99.999%, while completely eliminating gas leakage during operation. This perfectly matches the flammable and explosive nature of methane, providing the highest level of protection for chemical-grade methane, laboratory research, and safety-sensitive areas.
  • 02
    High Pressure Capability and Wide Adaptability: 
    A single stage can achieve a high compression ratio, with a maximum discharge pressure of up to 100 MPa. It can meet ultra-high-pressure requirements ranging from CNG filling and high-pressure bottling to special chemical processes. Its corrosion-resistant material options also allow it to handle methane gas sources containing trace impurities.
Methane Diaphragm Compressor Design Points
  • 01
    Diaphragm Safety Monitoring and Material Upgrade: 

    A three-layer diaphragm structure must be configured with an integrated rupture monitoring and alarm system to ensure immediate interlock shutdown upon diaphragm failure, preventing oil-gas mixing. All flow-wetted parts must be made of 316L stainless steel or a higher-grade material and undergo strict degreasing and cleaning to guarantee gas purity and material compatibility.

  • 02
    Precise Thermal Management and Leak Prevention Design: 

    The discharge temperature of each stage must be strictly controlled, typically not exceeding 120–135°C, to prevent the impact of high temperature on diaphragm life and sealing materials. All static sealing points in the gas path system must adopt metal seals or high-performance sealing elements. Nitrogen purging interfaces must be provided for purging before startup and maintaining pressure after shutdown to prevent the formation of explosive mixtures.

  • 03
    Integrated Safety Interlock System: 

    Methane-specific combustible gas detectors must be installed within the compressor skid scope and interlocked with the main engine Emergency Shutdown (ESD) system and emergency ventilation system. Dual alarms and shutdown interlocks must be set for pressure and temperature parameters to establish an active safety protection system.

Certificate

eac
ce
iso
iso2033
iso2033
MODEL SELECTION
Methane Diaphragm Compressor
Model G70Z/G95Z/G110Z/G130Z Piston Stroke 70mm~130mm Maximum Piston Force 10KN~30KN
Maximum Discharge Pressure 70Mpa Flow Range 1~500Nm3/h Motor Power 2.2KW~30KW
Crankshaft Speed 420rpm Cooling Method Water Cooled/Air Cooled
CH4 Diaphragm Compressor
Model G70V/G95V/G130V Piston Stroke 70mm~130mm Maximum Piston Force 10KN~30KN
Maximum Discharge Pressure 50Mpa Flow Range 1~200Nm³/h Motor Power 2.2KW~30KW
Crankshaft Speed 420rpm Cooling Method Water-cooled / Air-cooled
High Pressure Methane Diaphragm Compressor
Model G110L/G130L Piston Stroke 110mm~130mm Maximum Piston Force 20KN~40KN
Maximum Discharge Pressure 100Mpa Flow Range 10~1000Nm³/h Motor Power 7.5KW~90KW
Crankshaft Speed 420rpm Cooling Method Water-cooled / Air-cooled
CH4 Compressor
Model G110D/G130D/G150D/
G180D/G182D/G210D
Piston Stroke 110mm~210mm Maximum Piston Force 20KN~160KN
Maximum Discharge Pressure 100Mpa Flow Range 30~2000Nm³/h Motor Power 22KW~200KW
Crankshaft Speed 420rpm Cooling Method Water-cooled / Air-cooled
G
Diaphragm type compressor
Z
Piston stroke 70mm
52
Flow(Nm3/h)
40
Inlet pressure(barg)
56
Outlet pressure(barg)
No. Model Cooling water Flow Inlet pressure Outlet pressure Dimensions L×W×H Weight Motor Power
(L/h) (Nm³/h) (MPa) (MPa) (≈mm) (≈kg) (kW)
1 GZ-52/40-56 500 52 4 5.6 1200×700×1100 900 3
2 GZ-15/10-12 500 15 1 1.2 1200×700×1100 900 3
3 GZ-150/15-40 3000 150 1.5 4 2030×1045×1700 2500 30
4 GV-10/16-250 1000 10 1.6 25 1400×900×1200 1000 7.5
5 GV-10/(15-20)-160 1000 10 1.5-2 16 1400×900×1200 1000 7.5
6 GV-30/4-250 1000 30 0.4 25 2400×1700×1300 3000 15
7 GL-20/12-160 1000 20 1.2 16 2200×1800×1300 3000 7.5
8 GL-70/5-35 1500 70 0.5 3.5 2000×1800×1200 3000 15
9 GL-60/0.05-4 4000 60 0.005 0.4 2400×1800×1600 3000 15
10 GD-220/12-90 4000 220 1.2 9 3000×2000×1800 4000 37
11 GD-130/8-300 6500 130 0.8 30 3500×2300×1800 4500 45
12 GD-500/20-250 9000 500 2 25 3800×2300×2000 100000 75
The equipment size and weight are for reference only, and the final design shall prevail.

CASE STUDY

  • home-pictures
    Russia
  • nitrogen-gas-is-generated
    UNITED STATES
  • nitrogen-gas-is-generated2
    Spain
  • nitrogen-pressure-generated
    Kazakhstan
Advantages of Methane Reciprocating Compressors
  • 01
    High Flow Rate and Economic Efficiency: 

    Reciprocating compressors, especially the balanced-opposed type (D-type), can deliver a wide capacity range from thousands to tens of thousands of cubic meters per hour with high volumetric efficiency. They are well-suited for large-flow, continuous industrial applications such as natural gas pipeline boosting, feed gas processing in liquefaction plants, and large gas-fired power plants, offering excellent economies of scale.

  • 02
    Wide Compression Ratio Range and Technical Maturity: 

    They have a broad pressure adaptation range, covering from medium pressure to ultra-high pressure (e.g., 25 MPa and above), with mature and reliable technical routes. Depending on the required purity level, lubricated, micro-lubricated, or oil-free designs can be adopted, providing proven solutions for complex operating conditions such as BOG recompression in large LNG receiving terminals and associated gas recovery in oil and gas fields.

Key Design Points for Methane Reciprocating Compressors
  • 01
    Oil-Free Lubrication and Interstage Cooling to Prevent Liquid Slugging:
    To ensure methane purity and prevent lubricating oil from entering the process system, oil-free piston rings and packing made of PTFE or carbon composite materials should be used. Efficient interstage coolers and gas-liquid separators must be designed. Although methane has a low critical temperature and does not easily liquefy under normal conditions, this effectively controls the discharge temperature, reduces power consumption, and prevents liquid carryover or condensation of heavy components in the intake gas that could cause "liquid slugging."
  • 02
    Explosion-Proof Sealing and Buffer Isolation: 
    The drive motor and all electrical components must meet the Ex d IIB T4 explosion-proof classification. The piston rod packing system should be designed with a nitrogen buffer seal to direct trace amounts of process gas leakage to a safe vent or flare system, preventing combustible gas from entering the crankcase. For low-temperature BOG compressors, the distance piece must adopt an extended design and be equipped with nitrogen isolation facilities.
  • 03
    Pulsation Suppression and Vibration Control: 
    Due to the low density of methane, gas flow pulsation is likely to occur during compressor operation. Pulsation dampeners or surge bottles must be designed and installed near the suction and discharge ports of each stage. Pipeline vibration analysis should be performed in accordance with standards such as API 618 to ensure the piping system and foundation are stable, thereby ensuring long-term, safe, and stable operation of the equipment and reducing the risk of fatigue failure.

Certificate

eac
ce
iso
iso2033
atex
MODEL SELECTION
CH4 Piston Compressors
Piston stroke 80mm, 95mm Piston force 10KN~25KN
Power 7.5KW-55KW Number of cylinder banks 1/2
Crankshaft speed 740 rpm, 980 rpm Number of compression stages 1/2/3/4
Drive mode
Electric motor, diesel engine, natural gas engine
Methane Reciprocating Compressors
Piston stroke
92mm, 95mm, 105mm, 120mm
Piston force
25KN, 45KN, 65KN
Number of compression stages 1/2/3/4 Number of cylinder banks 2/3/4
Crankshaft speed 740 rpm, 980 rpm Power 15KW-220KW
Drive mode
Electric motor, diesel engine, natural gas engine
Methane Piston Compressors
Piston stroke 92mm~315mm Piston force 45KN~660KN
Number of compression stages 1/2/3/4 Number of cylinder banks 4
Crankshaft speed 300rpm~980rpm Power 160KW-3000KW
Drive mode Electric motor, diesel engine, natural gas engine
CH4 Reciprocating Compressors
Piston stroke 92mm~315mm Piston force 25KN~200KN
Number of compression stages 1/2/3/4 Number of cylinder banks 2
Crankshaft speed 300rpm~980rpm Power 30KW-1000KW
Drive mode
Electric motor, diesel engine, natural gas engine 
Z
Vertical type
W
Oil-free / F: Air-cooled
2.1
Actual volume flow (m3/min)
0.15
Inlet pressure(barg)
15
Outlet pressure(barg)
S/N Model Flow Inlet pressure Outlet pressure Motor power
(Nm³/h) (Mpa) (MPa) (kW)
1 ZW-2.1/0.15-15 120 0.015 1.5 22
2 ZW-0.9/6-25 310 0.6 2.5 30
3 ZW-0.63/3-200 130 0.3 20 37
4 VW-10/8 600 Atm 0.8 75
5 VW-15/13 780 Atm 1.3 132
6 VW/20/8 1020 Atm 0.8 132
7 D-1.47/10-300 800 1 30 185
8 D-1.1/10-300 600 1 30 160
9 DW-30/16 - 20-30 27000 1.6-2.0 3 900
10 MW-154/6 10500 0.05 0.6 1100
11 MW-6/15-21 6000 1.5-2.0 2.1 185
12 M-40/3-7 9000 0.3 0.7 450
The equipment size and weight are for reference only, and the final design shall prevail.

CASE STUDY

  • home-pictures
    Russia
  • nitrogen-gas-is-generated
    UNITED STATES
  • nitrogen-gas-is-generated2
    Spain
  • nitrogen-pressure-generated
    Kazakhstan

INQUIRY GUIDE FORM

Company Information

Company*

Name*

Phone*

Key Parameters for Compressor Inquiry

Suction Pressure

Discharge Pressure

Flow Rate

Cooling Method

Suction Temperature (℃)

Discharge Temperature (℃)

Power Supply(V/HZ)

Control Requirements

Gas Medium

Additional Remarks (You can also send your datasheet to our email)

RELATED PRODUCTS