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01Ultimate 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.
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02High 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.
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01Diaphragm 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.
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02Precise 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.
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03Integrated 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.
| 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 | |
| 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 | |
| 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 | |
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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 | |
| 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 |
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01High 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.
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02Wide 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.
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01Oil-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."
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02Explosion-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.
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03Pulsation 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.
| 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 |
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Drive mode
Electric motor, diesel engine, natural gas engine
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Piston stroke
92mm, 95mm, 105mm, 120mm
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Piston force
25KN, 45KN, 65KN
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| Number of compression stages 1/2/3/4 | Number of cylinder banks 2/3/4 |
| Crankshaft speed 740 rpm, 980 rpm | Power 15KW-220KW |
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Drive mode
Electric motor, diesel engine, natural gas engine
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| 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 | |
| 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 |
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Drive mode
Electric motor, diesel engine, natural gas engine
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| 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 |
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