China CO2 Compressor Factory - Reliable Suppliers for Carbon Dioxide Compression in Urea, CCS, Refrigeration, and Pharmaceuticals
Advantages of Carbon Dioxide Diaphragm Compressor
01
Absolutely Oil-Free and 100% Purity Retention
The core of a diaphragm compressor lies in its use of a metal diaphragm to completely physically isolate the compressed gas from the hydraulic oil system. The cylinder requires no lubrication. This means that during the entire compression process, carbon dioxide gas does not come into contact with any grease or oil mist, fundamentally eliminating oil contamination. For food-grade CO₂, electronic-grade CO₂, or CO₂ used in high-end chemical synthesis, this characteristic ensures extremely high cleanliness and chemical purity of the product gas, fully meeting the most stringent application standards.
02
Superior Static Sealing and Intrinsic Safety
The carbon dioxide gas is completely sealed within the "diaphragm cavity" formed by the diaphragm and cylinder head. This is a static sealing structure that theoretically achieves zero leakage. This not only effectively prevents the loss of valuable or hazardous gases, but also completely eliminates the asphyxiation safety risk caused by CO₂ accumulation in low-lying areas due to leakage. Simultaneously, this structure prevents potentially corrosive moist CO₂ from eroding the transmission components, enhancing the operational reliability of the equipment under harsh conditions.
Key Design Points for Carbon Dioxide Diaphragm Compressor
01
Strict Material Selection for Corrosion Protection
Since carbon dioxide forms carbonic acid when co-existing with moisture, which is corrosive to ordinary carbon steel, all flow-wetted components in contact with CO₂—including the cylinder head, diaphragm, gas valves, and piping—must be manufactured from corrosion-resistant materials. Austenitic stainless steels (such as 304, 316L) are typically selected, and strict degreasing, cleaning, and passivation treatments are performed after manufacturing to ensure lasting corrosion resistance and gas purity.
02
Precise Temperature and Pressure Control and Anti-Liquefaction Design
The critical temperature of carbon dioxide is 31.03 °C. During compression, if cooling is insufficient and the gas temperature falls below this critical value while the pressure is high enough, a phase change to liquid is highly likely. Liquid CO₂ inside the compressor can cause a fatal "liquid hammer" phenomenon, damaging the diaphragm and cylinder head. The design must involve carefully calculating and controlling the compression ratio at each stage, and configuring high-efficiency interstage coolers (water-cooled or air-cooled) to ensure that the discharge temperature at each stage is effectively lowered. This strictly confines the operating points of the entire compression path to the gaseous region of CO₂, avoiding the risk of liquefaction.
03
Enhanced Safety Monitoring and Protection System
Given the large coefficient of expansion of CO₂ under high-pressure storage (the pressure of a full cylinder can surge by 314 – 834 kPa for every 1 °C rise in temperature), the system must integrate multiple protections. Key design elements include: setting up accurate and reliable safety valves at each stage to prevent overpressure; equipping a diaphragm rupture detection and alarm device that can immediately alarm and shut down the compressor upon diaphragm failure to prevent gas-oil mixing; and installing gas concentration monitors in areas where CO₂ may accumulate, linked to the ventilation system. The control system (PLC) should integrate real-time monitoring and interlock shutdown functions for parameters such as pressure, temperature, and diaphragm status.
Certificate
Model Selection
ModelG70Z/G95Z/G110Z/G130Z
Piston Stroke70mm~130mm
Maximum Piston Force10KN~30KN
Max Discharge Pressure70Mpa
Flow Range1~500Nm³/h
Motor Power2.2KW~30KW
Crankshaft Speed420rpm
Cooling MethodWater Cooled/Air Cooled
ModelG70V/G95V/G130V
Piston Stroke70mm~130mm
Maximum Piston Force10KN~30KN
Max Discharge Pressure50Mpa
Flow Range1~200Nm³/h
Motor Power2.2KW~30KW
Crankshaft Speed420rpm
Cooling MethodWater-cooled / Air-cooled
ModelG110L/G130L
Piston Stroke110mm~130mm
Maximum Piston Force20KN~40KN
Max Discharge Pressure100Mpa
Flow Range10~1000Nm³/h
Motor Power7.5KW~90KW
Crankshaft Speed420rpm
Cooling MethodWater-cooled / Air-cooled
ModelG110D/G130D/G150D/G180D/G182D/G210D
Piston Stroke110mm~210mm
Maximum Piston Force20KN~160KN
Max Discharge Pressure100Mpa
Flow Range30~2000Nm³/h
Motor Power22KW~200KW
Crankshaft Speed420rpm
Cooling MethodWater-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 | 450 | 3 |
| 2 | GZ-15/10-12 | 500 | 15 | 1 | 1.2 | 1200×700×1100 | 500 | 3 |
| 3 | GZ-20/7-30 | 500 | 20 | 0.7 | 3 | 1200×760×1100 | 750 | 4 |
| 4 | GV-60/8-60 | 1000 | 60 | 0.8 | 6 | 2600×1800×1700 | 3000 | 11 |
| 5 | GV-500/150-200 | 1500 | 500 | 15 | 20 | 2600×1800×1700 | 3000 | 18.5 |
| 6 | GV-160/(6-10)-75 | 2000 | 160 | 0.6-1 | 7.5 | 2600×1800×1700 | 3000 | 22 |
| 7 | GL-20/10-150 | 1500 | 20 | 1 | 15 | 2200×1200×1300 | 3000 | 15 |
| 8 | GL-25/5-150 | 1500 | 25 | 0.5 | 15 | 2200×1200×1300 | 3000 | 15 |
| 9 | GL-45/5-150 | 2000 | 45 | 0.5 | 15 | 2600×1300×1300 | 3000 | 18.5 |
| 10 | GD-40/150 | 4000 | 40 | Atmospheric | 15 | 3500×2000×1700 | 4000 | 37 |
| 11 | GD-300/50-200 | 4000 | 300 | 5 | 20 | 3600×2300×1800 | 4000 | 45 |
| 12 | GD-900/10-140 | 16000 | 900 | 1 | 14 | 4500×4000×2200 | 16000 | 200 |
The equipment size and weight are for reference only, and the final design shall prevail.
Case Study

Russia

UNITED STATES

Spain

Kazakhstan
Frequently Asked Questions (FAQ)
Q1: Why is a diaphragm compressor ideal for food-grade and electronic-grade Carbon Dioxide?
A: Diaphragm compressors physically isolate the CO₂ gas from the hydraulic oil system using a metal diaphragm. This ensures 100% oil-free compression, preventing any grease contamination and preserving the high purity required for food, electronic, and pharmaceutical applications.
Q2: How does the compressor prevent corrosion caused by Carbon Dioxide?
A: When CO₂ mixes with moisture, it forms corrosive carbonic acid. To prevent damage, all flow-wetted components (such as cylinder heads, diaphragms, and valves) are made from high-grade corrosion-resistant materials, primarily austenitic stainless steels like 304 or 316L, which undergo strict passivation treatments.
Q3: What is "liquid hammer" in CO₂ compression, and how is it prevented?
A: Liquid hammer occurs if CO₂ liquefies under high pressure and low temperatures (below its critical point of 31.03°C), causing mechanical shock. It is prevented by carefully calculating the compression ratio at each stage and using high-efficiency interstage coolers to keep the gas operating strictly within the gaseous phase.
Q4: What happens if a diaphragm ruptures during compressor operation?
A: The compressor is equipped with a diaphragm rupture detection and alarm system. In the event of a failure, it immediately triggers an alarm and shuts down the system automatically to prevent gas leakage or mixing between the gas and hydraulic oil.
Q5: Are these CO₂ diaphragm compressors safe to operate in confined spaces?
A: Yes, because they feature static sealing that ensures zero leakage. To enhance safety, the design integrates safety valves, gas concentration monitors linked to the ventilation system, and PLC-controlled interlocks to automatically manage risk.




