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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)

Ethylene compressors

Ethylene (C₂H₄), known as the "industrial grain" of the petrochemical industry, is the organic basic raw material with the largest global production volume. This gas is colorless with a slightly sweet odor, has an extremely low critical temperature (9.21°C), can be liquefied under pressure at room temperature, and is highly prone to phase change during compression. It is also flammable and explosive, with an explosion limit of 3.1% to 32% in air. By virtue of its reactive double bond, ethylene serves as the core starting point for downstream products such as polyethylene and synthetic rubber, imposing extremely high requirements on the performance and reliability of compression equipment.
Ethylene compressors
Ethylene Diaphragm Compressor Advantages:
  • 01
    Absolutely Oil-Free & Ultra-High Purity Assurance: 
    The diaphragm isolation technology ensures that the gas is 100% free from contact with lubricating oil during compression, achieving a compression purity of over 99.999%. This is critical for "polymer-grade" ethylene used as a polymerization feedstock, where even trace oil contamination can affect catalyst activity, leading to product quality degradation or even polymerization failure.
  • 02
    Static Seal Zero Leakage & Intrinsic Safety: 
    The entire gas chamber employs a static seal structure, fundamentally eliminating the possibility of gas leakage. For ethylene, which has a wide explosion limit and high hazard level, this feature provides the highest level of safety assurance, effectively preventing the accumulation of flammable gas in the plant area and meeting the most stringent safety production and environmental protection requirements.
Key Design Points for Ethylene Diaphragm Compressors:
  • 01
    Precise Anti-Liquefaction & Temperature Control Design: 

    Given that the critical temperature of ethylene (9.21°C) is close to ambient temperature, it is highly prone to liquefaction during compression and cooling, which can cause "liquid slugging." The design must include accurate thermodynamic calculations to ensure that the discharge temperature and the gas temperature after inter-stage cooling always remain above the dew point at the corresponding partial pressure, with a sufficient safety margin. The cooling system must be efficient and reliable to prevent gas condensation within the chamber or piping.

  • 02
    High-Pressure & Material Compatibility Design: 

    To meet the demands of processes such as ultra-high-pressure polyethylene synthesis, the compressor must adopt a multi-cylinder series arrangement or a specially reinforced structure to achieve discharge pressures exceeding 100 MPa. Materials for wetted parts are typically selected as 316L stainless steel or higher-grade alloys to ensure high-pressure strength while providing excellent chemical inertness, preventing any adverse reactions with ethylene. The use of copper and its alloys is strictly prohibited to avoid catalyzing the formation of hazardous polymers from ethylene.

  • 03
    Multi-Layered Safety Monitoring & Protection System: 

    A three-layer diaphragm structure is standard, equipped with a diaphragm rupture monitoring and alarm device. If the inner diaphragm is damaged, the system can immediately trigger an alarm and safely shut down. The system must integrate interlocks such as high discharge temperature and pressure alarms, as well as oil pressure protection. For process connections, nitrogen purge connections should beto allow for inerting and purging of the system before startup, ensuring safe operation.

Certificate

eac
ce
iso
iso2033
iso2033
MODEL SELECTION
Ethylene 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
C2H4 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 Ethylene 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
Oil Free Ethylene Diaphragm 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
18
Flow(Nm3/h)
5.3
Inlet pressure(barg)
12.5
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-18/5.3-12.5 500 18 0.53 1.25 1000×800×1100 800 5.5
2 GZ-30/20-60 500 30 2 6 1100×800×1100 800 7.5
3 GZ-22/7-30 1000 22 0.7 3 1200×800×1100 800 11
4 GV-20/7-150 1000 20 0.7 15 1400×800×1100 900 11
5 GV-118/(34.5-44.5)-55 1000 118 3.45-4.45 5.5 1400×800×1100 1000 11
6 GV-160/(0.35-10.5)-30 2000 160 0.035-1.05 3 2600×1800×1600 3000 18.5
7 GL-55/3 1000 55 Atmospheric 0.3 2200×1800×1600 2800 11
8 GL-130/0.3-0.5 1500 130 0.03 0.05 2300×1800×1600 2800 11
9 GL-40/0.2-25 2000 40 0.02 2.5 2300×1800×1600 2800 18.5
10 GD-180/2.3-61.3 4500 180 0.23 6.13 3800×2300×1800 6000 45
11 GD-1076/(17-24)-125 10000 1076 1.7-2.4 12.5 4200×3200×2200 12000 132
12 GD-945/11.7-126 15000 945 1.17 12.6 4200×3500×2200 12000 160
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
Ethylene Piston Compressor Advantages:
  • 01
    Broad Pressure Adaptability & High Compression Efficiency: 

    Piston compressors can cover a wide range of pressure requirements from medium to high pressure, flexibly adapting to different process pressure levels through multi-stage compression. Their high volumetric efficiency makes them suitable for handling large-scale flow rates, meeting the immense demands of million-ton ethylene plants for feedstock gas boosting and recycle gas compression.

  • 02
    Highly Mature Technology & Maintenance Convenience: 

    As the most classic compressor type in the industrial field, the piston-type ethylene compressor boasts the broadest application cases and deepest technical accumulation, with fully verified operational reliability. Its relatively standardized structure and mature procedures for replacing wearing parts and performing maintenance help reduce the complexity and cost of long-term operation and maintenance.

Key Design Points for Ethylene Piston Compressors:
  • 01
    Strict Inter-stage Cooling & Gas-Liquid Separation Design: 
    Preventing liquefaction is the lifeline of ethylene piston compressor design. Multi-stage compression must be adopted, with efficient inter-stage coolers and high-efficiency gas-liquid separators configured at the outlet of each stage. The core of the design lies in accurately calculating the pressure ratio for each stage, ensuring that the outlet temperature of the cooler is absolutely higher than the dew point of ethylene at that stage's pressure, and thoroughly separating any liquid droplets that may form, strictly preventing liquid ethylene from entering the next stage cylinder and causing catastrophic "liquid slugging."
  • 02
    Optimized Structure Selection & Seal Type: 
    For medium to large flow rates, a horizontal opposed balanced structure is preferred, offering good dynamic balance and low vibration, suitable for long-term continuous operation. Depending on gas purity requirements, an oil-free lubrication design or labyrinth seal type can be selected to minimize lubricating oil contamination of the process gas. The packing system must be designed with a nitrogen buffer seal to prevent gas leakage and purge any leaked ethylene to a safe area.
  • 03
    Comprehensive Safety & Operating Condition Adaptability Configuration: 
    All electrical instruments must comply with the Ex d IIC T2 group explosion-proof rating to suit the explosive environment of ethylene. Filters and separators should be installed upstream of the compressor inlet to ensure clean, dry intake gas. The system must be equipped with a complete set of safety valves, with relieved gas routed to a flare system or recovery unit. Considering that ethylene may carry trace heavy components or operate under special conditions, the materials of key pressure-containing parts should possess good comprehensive mechanical properties. For processes that may involve low temperatures, materials meeting the requirements for low-temperature Charpy impact toughness must be selected.

Certificate

eac
ce
iso
iso2033
atex
MODEL SELECTION
Ethylene Piston Compressor
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
C2H4 Piston Compressor
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
Ethylene Reciprocating Compressor
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
C2H4 Reciprocating Compressor
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) (MPag) (MPag) (kW)
1 ZW-2.1/0.15-15 110 0.015 1.5 22
2 ZW-0.9/6-25 330 0.6 2.5 30
3 ZW-0.63/3-200 120 0.3 20 37
4 VW-7.2/1-22 800 0.1 2.2 132
5 VW-6/20 330 atm 2 75
6 VW-6.8/30 370 atm 3 75
7 DW-9.5/6 600 0.005 0.6 75
8 DW-12.5/29.9-53 21000 2.39 5.3 355
9 DW-8.8/4 -18 2050 0.4 1.8 132
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)

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