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High Purity 1400nm3/h Liquid O2 / 2000nm3/h Liquid N2 Air Separation Plant Oxygen/nitrogen Generating Machine

High Purity 1400nm3/h Liquid O2 / 2000nm3/h Liquid N2 Air Separation Plant Oxygen/nitrogen Generating Machine

    • High Purity 1400nm3/h Liquid O2 / 2000nm3/h Liquid N2 Air Separation Plant Oxygen/nitrogen Generating Machine
    • High Purity 1400nm3/h Liquid O2 / 2000nm3/h Liquid N2 Air Separation Plant Oxygen/nitrogen Generating Machine
    • High Purity 1400nm3/h Liquid O2 / 2000nm3/h Liquid N2 Air Separation Plant Oxygen/nitrogen Generating Machine
  • High Purity 1400nm3/h Liquid O2 / 2000nm3/h Liquid N2 Air Separation Plant Oxygen/nitrogen Generating Machine

    Product Details:

    Place of Origin: China
    Certification: ISO9001;2008 CE cetificate
    Model Number: KDON-1400Y/2000

    Payment & Shipping Terms:

    Minimum Order Quantity: 1set
    Price: negotiation
    Packaging Details: Packed in standard export packing
    Delivery Time: 60working days after received your payment
    Payment Terms: T/T or L/C
    Supply Ability: 100sets month
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    Detailed Product Description
    Product Name: Oxygen Plant Application: Separate Oxygen From Air
    Oxygen Output: 1400 +-5% Cube Meter Per Hour Feature: Long Service Life Low Energy Consumption
    Standard: ISO9001;2008 CE Cetificate O2 Purity: 99.6%
    N2 Capacity: 2000nm3/h N2 Purity: <3ppm O2

    99.6% Air Separation Plant KDON-1400Y/2000 Liquid Industrial Oxygen Plant With Low Energy

     

     

    Consumption

     

    1. lant design basis (It needs buyer’s confirmation)

     

    Design point of Atmosphere

    Ø  Atmosphere pressure

    101.3kPa(A)

    Ø  Atmosphere tempt.

    30℃

    Ø  Relative humidity

    75%

    Ø  O2 contained in air

    20.95% O2

    Atmosphere tempt.

    Ø  Annual average temp.

    18.4℃

    Ø  Max. Tempt.

    40℃

    Ø  Min. Tempt.

    -1.8℃

    Ø  Summer average temp.

    30℃

    Ø  Winter average temp.

    7.5℃

    Earth shake degree

    <6degree

    Altitude:

    50m

    Impurity in air

    Ø  CO2

    ≤350 ppm

    Ø  SO2

    ≤0.44 mg/m3

    Ø  H2S

    ≤2.3 mg/ m3

    Ø  CH4

    ≤5.2mg/ m3

    Ø  C2H2

    ≤0.03 ppm

    Ø  CnHm(except C2H2)

    ≤5 ppm

    Ø  Dust content

    ≤10mg/m3

    Recycling water

    Ø  Inlet temp.

    30℃

    Ø  Inlet pressure

    0.4 MPa(G)

    Ø  Maximum pressure drop

    0.2 MPa(G)

    Ø  Maximum temperature rise

    10℃

    Ø  Cooling water turbidity

    12 mg/L

    Ø  PH value

    7.2

    Ø  General hardness

    2.5

    Ø  Fouling factor

    0.0004 m2 hºC/ K.W

    Power condition

    Ø  High voltage power

    10,000V±5% three phases three wires

    Ø  Low voltage power

    380V/220V±5% AC three phases four wires

    Ø  Frequency

    50±0.5HZ

    Instrument gas ( used for starting)

    Ø  Pressure

    0.5 MPa(G)

    Ø  Temp.

    ≤30 ℃

    Ø  Dew point

    <-40℃

    Ø  Flow

    300m3/h

    Ø  Requirement

    Oil freeFlow

     

     

    2. Main parameter

     

    Capacity and purity(outlet cold box):

    Design condition Ⅰ

    Media

    capacity(Nm3/h)

    purity

    pressure(MpaG)

    LO2

    1400

    ≥99.6% O2

    ~0.16

    N2

    2000

    ≤3 ppm O2

    ~0.012

    Design condition Ⅱ

        LO2

    1000

    ≥99.6% O2

    ~0.16

    O2

    400

    ≥99.6% O2

    ~0.034

    LN2

    400

    ≤3 ppm O2

    ~0.2

    Note:Nm/h means under the condition of 0℃ and 760mmHg,

        Liquid production converts to gas capacity

    Pressure is calculated as 0 m altitude from the exit of cold box

     

     

    Running period between 2 defrosting times

    >2 years

    Defrosting time

    ~36 hours

    Starting time
    from start the turbine to get the production

    ~16 hours

     

     

     

    Power consumption table

    No.

    Equipment

    Motor power(fixed power)kW

    Normal working condition

    Shaft power kW

    Voltage degree

    Notice

    1.

    Raw air compressor

    2235

    2114

    10KV

    Samsung

    2.

    Air pre-cooling system

    Cooling water pump motor

    15

    10

    380/220V

    One in use one standby

    Condensing water pump motor

    11

    6

    380/220V

    One in use one standby

    Water chiller

    35

    25

    380/220V

    Spares

    3.

    Cryogenic  chiller

    60

    54

    380/220V

     

    4.

    MS purification system

    Heater

    210

    Average:80

    380/220V

    Switching operation

    5.

    Expander oil pump

    3

    2

    380/220V

    One in use one standby

    6.

    Liquid storage system

    LO2 transportation pump

    15

    10

    380/220V

    Intermittent operation

    LN2 transportation pump

    15

    10

    380/220V

    Intermittent operation

    7.

    Instrument system

     

    average:10

    380/220V

     

    Oxygen plant systems average electricity consumption(shaft power calculation, excluding liquid storage systems and utilities consumption):~2266kW

     

     

    Description of the process:

     

    Ø  KDON-1400Y/2000 complete set of Liquid air separation plant is based on the air different boiling point of each component, pressurized air, pre-cooling, through molecular sieves to remove H2O and CO2,in the intermediate pressure heat exchanger is cooled to liquefaction temperature, then enters into the distillation column to participate rectification, thereby obtaining liquid oxygen, nitrogen products.

    Ø  This plant is of MS purification of air with boosting turbine expander process

    ◆  Raw air goes to air filter for removal of dust and mechanical impurity and enters air turbine compressor where air is compressed to ~1.1MpaA. Then goes to Air pre-cooling system, temp. drop to around 10℃ then enters into two sets of switching operation MS absorber, get rid of H2O,CO2,C2H2 e etc. impurity. After purified air through expander boosting then goes into cold box. Air which after boosting separates to two parts, one part via heat exchange cool to ~250K then extract and enter into cryogenic chiller cooled to around ~243K then goes to main heat exchanger continue cooling, after cooled air extract from middle of heat exchanger, goes into expander for expansion, one part of air which after expansion goes into heat exchanger then re-heat goes out of cold box, another part enters into upper column directly; another part of air through reflux gas cooled to liquid type, via cryogenic expander expansion then send to lower column

    Ø  Air via lower column Preliminary rectification,get liquid air from lower column,waste liquid N2 and pure liquid N2. Get liquid air, waste liquid N2 and pure liquid N2 from lower column,via liquid air liquid N2 sub cooler cooling throttle to upper column. Through upper column further rectification,get 99.6% liquid O2 from bottom of upper column,as product out of cold box. From top of accessory column get some N2, after re-heat as product goes out of cold box.

    Ø  Get waste N2 from top of upper column,through sub cooler and main heat exchanger re-heat goes out of cold box,get some part of waste N2 enter into MS purification system,as re-generation gas,others vent.

    • Supporting unit selection and description
    • Raw air compressor

    Compressor uses turbine air compressor,The compressed air free of oil, to ensure the use of molecular sieve  properties, was not subject to oil pollution and failure to ensure the safe and normal operation.

    Air pre-cooling units, cryogenic refrigeration units

     

    Uses imported semi-hermetic screw refrigeration compressor, can be adapted to the harsh

    working conditions, and once you make a mistake and cause damage to the compressor,

    the ease of maintenance. Compressor has high and low pressure and overheating

    protection function from the main refrigeration components are used the most advanced

    Danfoss company's products, making the device reliable operation; cold by the thermal

    expansion valve to regulate, laminated evaporator for efficient heat, heat exchangers, high

    efficiency, compact structure, etc..

     

    Molecular sieve purification system (automatic switching)

    Purifier uses dual adsorption structure, one set in running, another regeneration.

    MS uses 13X-4X8 Head Ball-type MS forCO2 and H2Oadsorption capacity, ensure clean air into the column, so that the whole distillation column runs longer. Use of foreign advanced technology purifiers electric heating for effective control, interlock, to prevent electric heater and the heating temperature is too high and dry damaged heating pipes, effectively extending the life of the heater.

    Distillation column

    Distillation column uses highly efficient boosting turbo-expander, allowing device is stable operation;Sieve plate column with aluminum structure and efficient aluminum plate-fin structure and the main cold main heat exchanger, so that the entire device is compact. Cold box welded seal structure, the outer surface elegant appearance. Internal and external anti-corrosion measures taken.

     

     

    Scope of supply

     

    Self clean air filter

    One set

    Technical data(Notice:according to final design data)

    Manufacturer

    Wuyi

    Type

    Self clean

    Process air volume

    ~34000m3/h

    Filtering efficiency

    ≥99.8 %

    Filtering resistance

    ≤0.65KPa

    Installation type

    Vertical

    Filtering material

    Plant fibre

    Scope of supply(Notice:according to factory final supply)

    quantity

    Ø  Filter body

    1

    Ø  Cleaning system and control system

    1

    Ø  Cartridge

    1

    Ø  Spare parts

    1

     

     

    Centrifugal oil free air compressor

    One set

    Technical data(notice:according to final design data)

    Manufacturer

    Samsung or IHI

    Compression media

    Air

    Cooling water inlet temp.

    ≤30 ℃

    Cooling water supply pressure

    0.4 Mpa

    Design exhaust flow

    17000m3/h

    Exhaust pressure

    1.1MPa(A)

    Compression stages

    Three stages

    Main motor power

    2235KW

    Shaft power

    2114KW

    Cooling water consumption

    218m3/h

    Exhaust temp. (after cooler)

    ≤40 ℃

    Exhaust oil content

    100% oil free

    Adjustment range

    70 %~100 %

    Scope of supply(Notice:according to factory final scope of supply)

    quantity

    Compressor(Include inlet vanes,volute,gear box,Main drive gear shaft,high low speed rotor,bearing,sealer,main oil pump tec.)

    1

    • Compressor frame and anchor bolt

    1

    Main motor(Two-pole, asynchronous)include water cooler,Anti-condensation heater.

    1

    coupling and guard

    1

    Complete set of lub. system(include:oil tank,heater,Auxiliary pump,filter,cooler,hoods,base and anchor bolt etc.)

    1

    system of gas, oil, water pipes and pipe accessories

    1

    • Gas cooler

    1

    return valve, vent valve, outlet valve

    1

    vent silencer

    1

    • System valves

    1

    Inlet and outlet pipeline bellows pipe expansion joints

    1

    Anti-surge device

    1

    • One time measuring element,local instrument and required connect joints and root valve

    1

    shaft vibration, axial displacement of one time measuring element

    1

    • Local instrument and electric control panel

    1

    • Spare parts and special tools

    1

     

     

     

    Air cooling system

    One set

    Technical data(Notice:according to final design data)

    Manufacturer

    Siad

    Processing air volume

    ~17000 Nm3/h

    Air working pressure

    ~1.1MPa (A)

    Air inlet temp.

    < 105 ℃

    Air outlet temp.

    ~17℃

    Cooling water consumption

    Upper portion

    ~10m3/h

    Lower portion

    ~50m3/h

    Scope of supply

    Spec.

    Quantity

    • Air cooling tower, platform and ladder

    Lower part sieve plate+ upper part stuff packing

    1

    • Water cooling tower, platform and ladder

    Stuff packing

    1

    • Cooling water pump(one in use one standby)

    Motor power~15 KW

    2

    chilled water pump(one in use one standby)

    Motor power~11KW

    2

    • Water filter

    4

    • Valve and pipeline accessories

    1

    • Water chiller(Spare)

    Germany bitzer compressor

    1

    Shaft power

    ~25KW

    Motor power

    ~35KW

     

     

     

    Air cryogenic unit

    One group

    Technical data(notice:according to final design data)

    Manufacturer

    Siad

    Type

    UFD-16800/16

    Processing air volume

    ~16800m3/h

    Inlet pressure

    ~1.44MPa(G)

    Air inlet temp.

    253K

    Air outlet temp.

    243K

    Motor power

    ~60KW

    Shaft power

    ~54KW

    Circulating Water Pressure

    0.4MPa

    Circulating Water Temp.

    ≤30℃

    Circulating Water volume

    ~48t/h

    Scope of supply(notice: according to final factory supply)

    Quantity

    Imported refrigeration compressor

    1

    Ø  Condenser

    1

    Ø  Evaporator

    1

    Ø  Pipeline valve

    1

    Refrigeration Control Components

    1

    Ø  Electric control panel

    1

    Ø  Operation instrument board

    1

    Notice:above equipments as whole set skid-mounted design

    Photo(Notice:according to final factory supply,photo for reference only)

     

     

     

     

    MS purification system

    One set

    Technical data(Notice:according to final design data)

    Manufacturer

    Siad

    Type

    HXK-17000/11

    Processing air volume

    ~17000 Nm3/h

    Air working pressure

    ~1.1 MPa(A)

    Air inlet temp.

    <17 ℃>

    Air outlet temp.

    <24 ℃>

    MS re-generation temp.

    ~165℃

    Working time

    4 hours

    Scope of supply

    Spec.

    Quantity

    • MS adsorber

    Vertical Bunk Beds

    2

    Mocular sieve(UOP-13XAPG)

    Enough

    Silicone(WHA-103 Activated Alumina)

    Enough

    Ø  Vent silencer

    1

    Ø  Valve and pipeline accessories

    1

    Ø  Special tools

    1

    Ø  Spare parts

    1

    Ø  Electric Heater(One in use and one standby)

    vertical

    2

    Power~210 KW/set

    Average power consumption~80 KW

    Photo(Notice:according to final factory supply,photo for reference only)

                                                

     

     

    High temp. boosting turbine expansion group

    One set

    Technical data(Notice:according to final design data)

    Manufacturer

    Sichuan or Hangyang

    Working media

    air

    Flow

    ~9300Nm3/h

    Inlet pressure

    ~1.54Mpa(A)

    Outlet pressure

    ~0.12(A)

    Inlet temp.

    ~142K

    Boosting volume

    ~9300 Nm3/h

    Booster inlet pressure

    ~1.05MPa(A)

    Booster inlet temp.

    <40℃>

    Scope of supply:(notice:according to factory final supply)

    Quantity

    Ø  Expander body

    1

    Ø  Booster(assembled with main machine)

    1

    Ø  Oil supply equipment

    1

    Ø  Filter

    1

    Ø  Gas cooler

    1

    Ø  Base frame

    1

    Emergency shut off valve and Nozzle adjustment mechanism

    1

    Ø  Special tools

    1

    Ø  Spare parts(include rotor)

    1

    tachometer and speed probe,one time measurement element local instrument and required connect joint, root valve

    1

    Photo(Notice:according to final factory supply,photo for reference only)

     

     

    Cryogenic turbo-expander group

    set

    Technical data(notice:according to final design data)

    Manufacturer

    Jiangyang or Xida

    Flow:

    ~4800Nm3/h

    Inlet pressure

    1.02MPa(A)

    Outlet pressure

    0.6MPa(A)

    Inlet temp.

    ~120K

    Scope of supply:(notice:according to factory final supply)

    quantity

    Turbine expander

    1

    Local instrument panel

    1

    Filter

    1

    Special tools

    1

    Spare parts(include rotor)

    1

    Photo(Notice:according to final factory supply,photo for reference only)

     

     

    Liquid storage system

    One set

    Manufacturer

    Siad

    Scope of supply:

    Spec.

    Quantity

    Liquid O2 storage tank(assembling at site)

    (buyer supply)

    Vertical,perlite insulation

    1

    Effective volume  300 m3

    Design pressure  normal pressure

    Liquid N2 storage tank(assembling at site)

    (buyer supply)

    Vertical,perlite insulation

    1

    Effective volume  300 m3

    Design pressure  normal pressure

    Liquid O2 filling pump(imported)

    Centrifugal type

    1

    Transportation flow  18 m3/h

    Working pressure  0.6 MPa(G)

    Liquid N2 filling pump(imported)

    Centrifugal type

    1

    Transportation flow  18 m3/h

    Working pressure  0.6 MPa(G)

    Photo(Notice:according to final factory supply,photo for reference only)

     

     

    Liquid O2 capacity 1400nm3/h
    Liquid N2 capacity 2000nm3/h
    Liquid O2 purity >99.6%
    Liquid N2 purity <3ppm O2
    Process air volume 0-34000m3/h
    Filtering resistance <0.65kpa
    Starting time 0-16hours
    Defrosting time 0-36hours

     

     

    High Purity 1400nm3/h Liquid O2 / 2000nm3/h Liquid N2 Air Separation Plant Oxygen/nitrogen Generating Machine

    Contact Details
    HANG ZHOU TAI LIAN CRYOGENIC EQUIPMENT CO., LTD.

    Contact Person: Mr. Yao junming

    Send your inquiry directly to us (0 / 3000)

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