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28000m3/H Cryogenic Air Separation Plant , Large Scale Cryogenic Air Separation Unit

China National Air Separation Engineering Co., Ltd.
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    Buy cheap 28000m3/H Cryogenic Air Separation Plant , Large Scale Cryogenic Air Separation Unit from wholesalers
     
    Buy cheap 28000m3/H Cryogenic Air Separation Plant , Large Scale Cryogenic Air Separation Unit from wholesalers
    • Buy cheap 28000m3/H Cryogenic Air Separation Plant , Large Scale Cryogenic Air Separation Unit from wholesalers
    • Buy cheap 28000m3/H Cryogenic Air Separation Plant , Large Scale Cryogenic Air Separation Unit from wholesalers
    • Buy cheap 28000m3/H Cryogenic Air Separation Plant , Large Scale Cryogenic Air Separation Unit from wholesalers

    28000m3/H Cryogenic Air Separation Plant , Large Scale Cryogenic Air Separation Unit

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    Brand Name : CNASEC
    Certification : TUV, CE
    Payment Terms : T/T, L/C
    Supply Ability : 10 sets per year
    Delivery Time : 10 months
    • Product Details
    • Company Profile

    28000m3/H Cryogenic Air Separation Plant , Large Scale Cryogenic Air Separation Unit

    28000m3/H Cryogenic Air Separation Plant , Large Scale Cryogenic Air Separation Unit

    28000m3/h Air Separation Plant, large scale air separation unit, air separator

    ASU Technical Performace Parameter


    Design case:

    ProductOutput,Nm3/hPurity %Pressure at cold box outlet/Temperature Mpa/(℃)Pressure at Battery outlet/Temperature Mpa/(℃)
    Gaseous Oxygen28,00099.6% O20.015/24.93.0/≤42
    Liquid Oxygen30099.6% O20.15/-181.7-
    Gaseous Nitrogen28,000≤5ppm O20.007/24.9-
    Liquid Nitrogen100≤5ppm O20.2/-193-
    Pressure Nitrogen600≤5ppm O20.434/24.9

    As sealing gas for

    oxygen compressor

    Liquid

    Argon

    1,000

    ≤5ppm

    O2+N2

    0.16/-183.8

    Note: Nm3/h means at the condition of 0℃, 1.013bar(A)

    Liquid product Nm3/h data refers its gaseous state transferred


    • Plant features

    1. Continuous operation period between two defrost≥2 years

    2. Time required for defrost~36 hours

    3. Time required for start-up (from the start-up of expander to attainment of oxygen purity)
      ~36 hours

    4. The instrument air need to be provided by user during start-up, will be provided by ASU itself when running.

    5. Utility Consumption List see next page.

    Unit power consumption(without oxygen compression)0.384Kwh/Nm3 O­2­ ±4%

    {28000+(300+100+1000)X3}/12365=0.384

    Unit power consumption (with oxygen compression) 0.555Kwh/Nm3 O­2­ ±4%

    {28000+(300+100+1000)X3}/17865=0.555

    Note: -Power refers to shaft power as per primary design

    - Liquid product output taken as 3 time gaseous output for calculation

    - Electrical heaters for oil lubrication system, oil pumps and smoke fan motor for oxygen compressor as well as turbo expander are not included.

    - Final figures depend on final design of the Air Separation plant and the compressors chosen after final design.


    • Capablility of ASU design & fabrication

    We can design, manufacture and complete air separation plant according to end users' climatic, geologic and water quality conditions, as well as their different purity and quantity requirements for oxygen, nitrogen and argon. We have the capability to design and fabricate air separation plant with capacity from 10,000Nm3/h to 100,000Nm3/h.





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