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)

China Chlorine Compressor Suppliers | Durable & Corrosion-Resistant Factory Equipment for Safe Production

Introducing our advanced solution designed for the safe and efficient compression of severely toxic and strongly corrosive chlorine gas. Our system is engineered with a focus on absolute sealing and the use of corrosion-resistant materials, making it an ideal choice for industries requiring high safety standards. We utilize innovative labyrinth seal technology, complemented by nitrogen purge or liquid ring seal technology, to completely eliminate any leakage risks associated with chlorine and other harsh media, including concentrated sulfuric acid, As a leading China supplier and factory, we offer equipment that not only meets the rigorous demands of large-scale continuous production in the chlor-alkali industry but also provides exceptional reliability and adaptability to varying process parameters, such as moisture content. With our product, you can ensure extreme safety and performance in your operations, making it a critical component for secure and successful production processes. Choose us for top-grade solutions to manage your chlorine gas compression needs

    Chlorine Diaphragm Compressor Advantages

    01 Absolutely Oil-Free & Zero Leakage Seal
    The "static seal" structure of the diaphragm compressor ensures that the gas is 100% free from contact with lubricating oil, fully meeting the "absolute oil-free" requirement for chlorine compression. Simultaneously, its embedded diaphragm head or combined oil distribution plate design significantly reduces sealing surfaces. Coupled with high-strength bolt pre-tightening, it achieves zero leakage containment of highly toxic chlorine, preventing the escape of poisonous gas that could harm personnel and the environment, and also preventing external moisture from entering the system and causing corrosion.
    02 Ultra-High Gas Purity Maintenance & Active Safety Protection
    This structure absolutely guarantees that the purity of the compressed chlorine is free from any contamination. The standard three-layer diaphragm rupture alarm system is key to active safety. When any layer of the diaphragm experiences an anomaly, a pressure switch immediately triggers an audible and visual alarm and automatically initiates an interlock shutdown to prevent the incident from escalating. This characteristic makes it especially suitable for electronic-grade high-purity chlorine or chemical processes with stringent cleanliness requirements.

    Key Design Points for Chlorine Diaphragm Compressors

    01 Material Corrosion Resistance
    Material selection is the decisive factor in chlorine compressor design. For dry chlorine with a moisture content strictly controlled to ≤ 0.05% (by weight), carbon steel may be considered for wetted parts. However, for the vast majority of operating conditions where moisture may be present, chlorine reacts with water to form hydrochloric acid, necessitating the use of high-grade corrosion-resistant alloys. Technical agreements typically mandate that all wetted metal parts be made of 316L stainless steel or higher grade materials, with special requirements for welding procedures and surface passivation treatment to address potential stress corrosion cracking induced by chloride ions.
    02 Safety Purge System
    Before startup, the compressor and the entire piping system must be thoroughly purged with high-purity nitrogen or inert gas to expel air and moisture, preventing the formation of explosive mixtures or corrosive environments. The design must integrate dedicated purge and vent connections and valve groups to ensure the operating procedures can be executed simply and reliably.
    03 Diaphragm Cavity & Monitoring
    The diaphragm must be made of a special alloy material resistant to chlorine corrosion. The diaphragm cavity profile needs to be optimized to extend diaphragm life. The system must be equipped with comprehensive temperature and pressure monitoring. The discharge temperature should be controlled within a safe range (typically well below the general limit of 180°C) through efficient inter-stage coolers, with over-limit alarms and shutdowns configured. All electrical instruments must meet an explosion-proof rating of at least Ex d IIB T4 to suit the potentially explosive environment.

    Certificates

    eac
    ce
    iso
    iso2033
    iso2033

    Model Selection

    GZ
    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
    GV
    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
    GL
    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
    GD
    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
    5
    Flow (Nm³/h)
    6
    Inlet pressure (barg)
    10
    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-5/6-10 500 5 0.6 1 1200×700×1100 700 2.2
    2 GZ-7/0.1-6 500 7 0.01 0.6 1200×900×1200 800 3
    3 GZ-1/1.5-8 500 1 0.15 0.8 1200×900×1200 800 4
    4 GV-0.35/100 500 0.35 Atmospheric 10 1200×850×1200 1000 3
    5 GV-23/1 500 23 Atmospheric 0.1 1200×900×1250 900 5.5
    6 GV-70/5-10 1000 70 0.5 1 1200×900×1300 900 7.5
    7 GL-25/15 1000 25 Atmospheric 1.5 2200×1650×1450 3000 7.5
    8 GL-150/0.3-5 2000 150 0.03 0.5 3230×1770×2200 3000 18.5
    9 GL-170/2.5-18 2000 170 0.25 1.8 2900×2000×1700 3000 22
    10 GD-900/(2-6)-12 5000 900 0.2-0.6 1.2 3500×2300×1500 4500 45
    11 GD-600/1.5-5 5000 600 0.15 0.5 3500×2300×1800 4500 45
    12 GD-1306/(5-7)-12 8000 1306 0.5-0.7 1.2 3800×2300×1800 6000 75
    The equipment size and weight are for reference only, and the final design shall prevail.

    Case Study

    Russia

    Russia

    United States

    United States

    Spain

    Spain

    Kazakhstan

    Kazakhstan

    Frequently Asked Questions

    Why is a diaphragm compressor ideal for chlorine compression?
    The static seal structure of a diaphragm compressor ensures that the gas has 100% zero contact with lubricating oil, meeting the strict "absolute oil-free" requirement essential for safe chlorine compression.
    How does the compressor achieve zero leakage for highly toxic chlorine gas?
    It features an embedded diaphragm head or combined oil distribution plate design that minimizes sealing surfaces. Combined with high-strength bolt pre-tightening, it prevents toxic gas escape and external moisture ingress.
    What happens if a diaphragm ruptures during operation?
    The compressor is equipped with a standard three-layer diaphragm rupture alarm system. If any layer fails, a pressure switch immediately triggers an audible and visual alarm and automatically shuts down the system.
    How does moisture content affect material selection for the compressor?
    Dry chlorine (moisture ≤ 0.05%) allows carbon steel wetted parts. However, if moisture is present, it forms corrosive hydrochloric acid, requiring wetted metal components to be made of 316L stainless steel or higher corrosion-resistant alloys.
    Why is a nitrogen purging system required before starting the compressor?
    Purging the compressor and piping with high-purity nitrogen or inert gas before startup expels air and moisture, preventing the formation of highly corrosive environments or explosive mixtures.
    What explosion-proof rating do the electrical instruments meet?
    All electrical instruments and monitoring systems are designed to meet an explosion-proof rating of at least Ex d IIB T4 to ensure safety in potentially explosive processing environments.