Home ProductsAir Separation Plant

Cryogenic 900nm³/h Liquid Oxygen /150nm3/h Oxygen 30nm3/h Liquid Argon Plant Air Separation Plant With Low Energy

Cryogenic 900nm³/h Liquid Oxygen /150nm3/h Oxygen 30nm3/h Liquid Argon Plant Air Separation Plant With Low Energy

    • Cryogenic 900nm³/h Liquid Oxygen /150nm3/h Oxygen 30nm3/h Liquid Argon Plant Air Separation Plant With Low Energy
    • Cryogenic 900nm³/h Liquid Oxygen /150nm3/h Oxygen 30nm3/h Liquid Argon Plant Air Separation Plant With Low Energy
    • Cryogenic 900nm³/h Liquid Oxygen /150nm3/h Oxygen 30nm3/h Liquid Argon Plant Air Separation Plant With Low Energy
    • Cryogenic 900nm³/h Liquid Oxygen /150nm3/h Oxygen 30nm3/h Liquid Argon Plant Air Separation Plant With Low Energy
  • Cryogenic 900nm³/h Liquid Oxygen /150nm3/h Oxygen 30nm3/h Liquid Argon Plant Air Separation Plant With Low Energy

    Product Details:

    Place of Origin: China
    Brand Name: Tailian
    Certification: GB-150 CE ASME ISO9001 TUV
    Model Number: KDONAR-1000Y/1000/35Y

    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
    Contact Now
    Detailed Product Description
    Product Name: Oxygen Plant Application: Separate Oxygen From Air
    Liquid Oxygen Output: 900 +-5% Cube Meter Per Hour Feature: Long Service Life Low Energy Consumption
    Standard: ISO9001;2008 CE Cetificate Purity: 99.6%
    Oxygen Output: 150 +-5% Cube Meter Per Hour Liquid Argon Output: 30 +-5% Cube Meter Per Hour

    99.6% Air Separation Plant KDONAR-1000Y/1000/35Y Industrial Oxygen Plant With Low Energy

     

    Plant design basis (need 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 tempt.

    18.4℃

    Ø  Max. Tempt.

    40℃

    Ø  Min. Tempt.

    -1.8℃

    Ø  Summer average tempt.

    30℃

    Ø  Winter average tempt.

    7.5℃

    Earthquake degree:

    6 degree

    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(excluding C2H2)

    ≤5 ppm

    Ø  Mechanical impurity

    ≤10mg/m3

    Recycle water

    Ø  Inlet tempt.

    30℃

    Ø  Inlet pressure

    0.4 MPa(G)

    Ø  Max pressure drop

    0.2 MPa(G)

    Ø  Max tempt. rising

    10℃

    Ø  Turbidity of cooling water

    12 mg/L

    Ø  PH value

    7.2

    Ø  Rigidity

    2.5

    Ø  Fouling factor

    0.0004 m2 hºC/ K.W

    Ø  Total water consumption

    ~260T/h

    Power condition

    Ø  High voltage power

    10,000V±5%  3 phases 3 ways

    Ø  Low voltage power

    380V/220V±5% AC 3 phases 4 ways

    Ø  Frequency

    50±0.5HZ

    Ø  Power amount

    ~2200KW

    Instrument gas ( used for starting)

    Ø  Pressure

    0.5 MPa(G)

    Ø  Tempt.

    ≤30 ℃

    Ø  Dew point

    <-40℃

    Ø  Flow

    300m3/h

    Ø  Requirement

    oil free

     

    Annex 2. Main parameter

    Capacity and purity(out of cold box):

    Designed working condition 1

    Medium

    capacity (Nm3/h)

    purity

    pressure(MpaG)

    Luquid O2

    1,050

    ≥99.6%O2

    ~0.16

    N2

    1000

    ≤3ppmO2

    ~0.008

    Liquid argon

    35

    ≤2ppmO2,≤3ppmN2

    ~0.16

    Designed working condition

    Medium

    capacity (Nm3/h)

    purity

    pressure(MpaG)

    Luquid O2

    900

    ≥99.6%O2

    ~0.16

    O2

    150

    ≥99.6%O2

    0.02

    Luquid N2

    160

    ≤3ppmO2

    0.2

    Liquid argon

    30

    ≤2ppmO2,≤3ppmN2

    ~0.16

    Remarks:Nm3/h is under condition of 0℃ , 760mmHg.(same as below);
        Pressure is measured on the level of ground.

     

     

    Running period between 2 defrosting times )

    >2 YEARS

    Defrosting time

    ~36 hr

    Starting time
    from start the turbine to get the production ( excluding commissioning for argon)

    ~24 hr

     

     

     

     

    Power consumption

    NO.

    Equipment

    Motor power(rated power)kW

    Normal working condition

    Shaft power kW

    Voltage stage

    Remarks

    1.  

    Raw air compressor

    1850

    1552

    10KV

     

    2.  

    Air precooling unit

    73

    58

    380/220V

     

    3.  

    Electric heater

    200

    average:85

    380/220V

    One for running and one for standby, Discontinuous running

    4.  

    Chiller

    56

    47

    380/220V

     

    5.  

    Oil pump of turbine expansion

    3

    2

    380/220V

    One for running and one for standby

    6.  

    Liquid argon pump of cold box

    2.2

    0.8

    380/220V

    One for running and one for standby

    7.  

    Liquid storage system

    Liquid oxygen delivery pump

    15

    10

    380/220V

    Discontinuous running

    Liquid N2 delivery pump

    15

    10

    380/220V

    Discontinuous

    Liquid argon delivery pump

    15

    10

    380/220V

    Discontinuous

    8.  

    Instrument control system

     

    average:10

    380/220V

     

    Plant average power consumption(calculate as shaft power,exclude liquid strorage system and utilities):~1754.8kW

     

     

     

    Annex 3 Description of the process:

    1. Design principle of this plant is based on the different boiling point of each gas in the air. Air is compressed, precooled and got removal of H2O and CO2, then to be cooled in the main heat exchanger until it is liquified. After rectification, production oxygen and nitrogen can be collected.
    2. This plant is of MS purification of air with boosting turbine expander process. It is a common air separation plant , which adopts complete stuff filling and rectification for argon making.
    3. Raw air goes to air filter for removal of dust and mechanical impurity and enters air turbine compressor where air is compressed to 0.59MPaA. Then it goes into air precooling system, where air is cooled to 17 ℃. After that, it flows to 2 molecular sieve adsorbing tank, which are running in turn, to be got removal of H2O, CO2 and C2H2.
    •  
      1. After purified, air mixes with expanding reheated air. Then it is compressed by middle pressure compressor to be divided into2 streams. One part goes to main heat exchanger to be cooled to -260K, and sucked from the middle part of main heat exchanger to enter expansion turbine. Expanded air returns to main heat exchanger to be reheated, after that, it flows to air boosting compressor. The other part of air is boosted by high temperature expander, after cooling, it flows to the low temperature boosting expander. Then it goes to cold box to be cooled to ~170K. Part of it would still be cooled, and flows to bottom of lower column via heat exchanger. And other air is sucked to low tempt. expander. After expanded, it is divided into 2 parts. One part goes to the bottom of lower column for rectification, the rest returns to main heat exchanger, then it flows to air booster after being reheated.
      2. After primary rectification in lower column, liquid air and pure liquid nitrogen can be collected in lower column. Waste liquid nitrogen, liquid air and pure liquid nitrogen flows to upper column via liquid air and liquid nitrogen cooler. It is rectified in upper column again, after that, liquid oxygen of 99.6% purity can be collected at the bottom of upper column, and is delivered out of the cold box as production.
      3. Part of argon fraction in upper column is sucked to crude argon column. There are 2 parts of crude argon column. The reflux of second part is delivered to the top of first one via liquid pump as reflux. It is rectified in crude argon column to get 98.5% Ar. 2ppm O2 crude argon. Then it is delivered to the middle of pure argon column via evaporator. After rectification in pure argon column, (99.999%Ar) liquid argon can be collected at the bottom of pure argon column.
      4. Waste nitrogen from top of upper column flows out of the cold box to purifier as regenerative air, rest goes to cooling tower.
      5. Nitrogen from top of assistant column of upper column flows out of cold box as production via cooler and main heat exchanger. If no need nitrogen, then it could be delivered to water cooling tower. For cold capacity of water cooling tower is not sufficient, a chiller needs to be installed.
    • Flow feature:
    •  
    • The design principle of this plant is to ensure safety, energy saving and easy operation and         maintenance. The technology is leading position in the world.
      • Buyer needs lots of liquid production, so we supply middle pressure air recycle process to save the investment and power consumption.
      • We adopts recycle air compressor and high, low tempt. expansion process to save power consumption.
    • It adopts DCS computer control technology to control main panel, local panel at the same time. This system can monitor the entire process of the plant.

     

     

     

    Annex 4. Scope of supply

    1. Raw material filter

    1set

    (note:determined by final design)

    Manufacturer

    Wuxi

    Type

    Self cleaning

    Process capacity

    ~27000m3/h

    Filter efficiency

    ≥99.8 %

    Filter resistance

    ≤0.65KPa

    Installation type

    vertical

    Filter material

    foliage fibre

    (note:determined as manufacturer’s final list)

    Q.T.

    Ø  FILTER HOST BODAY

    1

    Ø  Counter blowing and control system

    1

    Ø  Filter bucket

    1

    Ø  Spare parts

    1

    Image (for reference, determined by final design)

     

     

     

    1.     centrifugal oil free air compressor

    1 set

    Technical parameter(note:determined by final design)

    Manufacturer

    Atlas or Ingersoll

    Medium

    Air

    cooling water inlet temp.

    ≤30 ℃

    cooling water inlet pressure.

    0.4 Mpa

    Discharge capacity

    13800m3/h

    Discharge pressure

    1.1MPa(A)

    Compressing stage

    3

    Motor power

    1850KW

    Shaft power

    1552KW

    Cooling water consumption

    161m3/h

    Discharge tempt.

    ≤40 ℃

    Discharge oil content

    100% oil free

    Regulation scope

    70 %~100 %

    SCOPE OF SUPPLY(note:determined as manufacturer’s final list)

    Q.T.

    • Compressor body

    1

    • Pedestal and anchor bolt

    1

    • Main motor

    1

    • Coupling and cover

    1

    • Fuel supply system

    1

    Complete lub. system(incl:oil pump,heater ,auxiliary oil pump,filter,cooler,oil smoke discharger,bottom plate and anchor bolts, etc.)

    •  

    1

    • Gas cooler

    1

    • Return flow valves, vent valves, outlet valves

    1

    • Venting valves

    1

    • Valves within the system

    1

    • Corrugated pipes expansion joint on inlet and outlet pipes

    1

    • Anti tremble system

    1

    • Primary element,local instrument and necessary connector and root valves.

    1

    • Primary instrument to transformer for shaft vibration, shaft displacement 

    1

    • Local instrument control panel

    1

    • Spare parts and special tool

    1

    Image (for reference, determined by final design)

     

         
     
     

     

     
    1. Air precooling system

    1set

    Technical parameter(note:determined by final design)

    Manufactory

    Siade

    Model

    SDYL-13800/10

    Process air

    ~13800m3/h

    Air inlet working pressure

    ~1.1MPa(A)

    Air inlet tempt.

    ≤40℃

    Air outlet tempt.

    ~8℃

    Motor power

    ~75KW

    Cooling water inlet pressure

    0.4MPa

    Cooling water inlet tempt.

    ≤30℃

    Cooling water consumption

    ~50t/h

    Scope of supply(based on final design)

    Q.T.

    Ø  imported compressor

    1

    Ø  condenser

    1

    Ø  evaporator

    1

    Ø  pipes and valves

    1

    Ø  refrigerating self control element

    1

    Ø  computer control panel

    1

    Ø  operation panel

    1

    Ø  water separator

    1

    Ø  automatic drainer

    1

     

    Image (for reference, determined by final design)

     

     

     

     

     

     
    1. Chiller

    1 set

    Technical parameter(note:determined by final design)

    Manufactory

    KAIDE

    Model

    UFD-13800/14D

    Air process

    ~13800m3/h

    Inlet pressure

    ~1.46MPa(G)

    Air inlet tempt.

    250K

    Air outlet tempt.

    240K

    Motor power

    ~56KW

    Shaft power

    ~47KW

    Water inlet pressure

    0.4MPa

    Water inlet tempt.

    ≤30℃

    Water capacity

    ~15t/h

    Scope of supply((note:determined as manufacturer’s final list)

    Q.T.

    Ø  Imported compressor

    1

    Ø  imported compressor

    1

    Ø  condenser

    1

    Ø  evaporator

    1

    Ø  pipes and valves

    1

    Ø  refrigerating self control element

    1

    Ø  computer control panel

    1

     

    Image (for reference, determined by final design)

     

     

     

     

     

     

    1. MS purification system

    1 set(auto switch)

    Technical parameter(note:determined by final design)

    Manufactory

    kaide

    Model

    HXK-13800/10

    Air process

    ~13800 Nm3/h

    Inlet pressure

    ~1.1MPa(A)

    Air inlet tempt.

    10 ℃

    Air outlet tempt.

    17 ℃

    M.S. regeneration tempt.

    ~165℃

    Working time

    4 hours

    Scope of supply (note:determined as manufacturer’s final list)

    Q.T.

    Ø  MS absorber

    2

    Ø  Filter

    1

    Ø  Electric heater

    1

    Ø  Auto switch valve

    1

     

    Image (for reference, determined by final design)

     

     

    1. Distillation column

    1 set

    Technical parameter(note:determined by final design)

    Manufactory

    Kaide

    Model

    FONAr-1000Y/1000/35Y

    Type

    Double column rectification

    Size

    ~4400×4400×50000mm

    Scope of supply

    Specification

    Q.T.

    • Intermediate pressure heat exchanger

    Al-plate-fin type

    1

    • Upper column

    Regular stuff packing

    1

    • Condenser-evaporator(together with lower column)

    Al-plate-fin type

    1

    • Lower column

    counter flow sieve plate type

    1

    • LN2 air subcooler

    Al-plate-fin type

    1

    • Crude argon column Ⅰ

    Regular packing stuff

    1

    • Crude argon column Ⅱ(Incl. crude argon condenser)

    Regular packing stuff

    1

    • Pure argon column  (Incl. condenser and evaporator)

    Regular packing stuff

    1

    • Liquid crude argon pump

    6060M. liquid argon column,power 5.5KW

    2

    • Cold box

    1

    • Valves in pipes in cold box

    1

    • Valves in pipes outside of cold box

    1

    • Valves, pipes, supports in & out of the cold box

    1

    • Platform form and ladder,rails, etc

    1

    • Filter for instrument air

    1

    • Filter for expansion air

    2

    • Injection evaporator for liquid

    1

    • Venting N2 silencer

    1

    • Venting O2 silencer

    1

    • Special tool

    1

    • Spare parts

    1

    Image (for reference, determined by final design)

     

     

     

     

     
    1. High tempt. expansion turbine

    1 SET

    Technical parameter(note:determined by final design)

    Manufacturer

    Hangyang or Sizhuan

    Medium

    AIR

    Expansion capacity

    ~7600Nm3/h

    Inlet pressure of expansion turbine

    ~1.5Mpa(A)

    Outlet pressure of expansion turbine

    ~0.117Mpa(A)

    Inlet tempt. of expansion turbine

    ~147K

    Boosting capacity

    ~7600 Nm3/h

    Inlet pressure of booster

    ~1.07MPa(A)

    Inlet tempt. of booster

    313K

    scope of supply

    Q.T.

    Ø  Expansion turbine body

    1

    Ø  Booster(assembly with main machine)

    1

    Ø  Oil supply

    1

    Ø  Filter

    1

    Ø  Air cooler

    1

    Ø  Bottom plate

    1

    Ø  Emergency shut valve and spray mouth adjusting mechanism

    1

    Ø  Special tool

    1

    Ø  SPARE PARTS

    1

    Ø  Rotating speed meter and detective and joint

    1

    Image (for reference, determined by final design)

     

     

     

     

    1. Lower tempt. turbine expander with booster 

    1 set

    Technical parameter(note:determined by final design)

    Manufacturer

    Jiangyang or xida

    Expansion capacity:

    ~3625Nm3/h

    Inlet pressure of expansion turbine

    1.056MPa(A)

    Outlet pressure of expansion turbine

    0.568MPa(A)

    Inlet tempt. of expansion turbine

    ~108.5K

    Scope of supply:(note:determined as manufacturer’s final list)

    Q.T.

    Main body of expansion turbine

    1

    Local panel

    1

    Filter

    1

    Special tool

    1

    Spare parts

    1

    Image (for reference, determined by final design)

     

     

     

    1. Liquid storage system

    1 set

    Manufacturer

    Kai de

    Scope of supply:

    Specification

    QUANTITY

    LOX tank (assembled at site, prepared by buyer)

    Vertical,Perlite insulation

    1

    Efficient volume  300 m3

    Design pressure  Normal pressure

    N2 tank  (assembled at site, prepared by buyer)

    Vertical,Perlite insulation

    1

    Efficient volume  50m3

    Design pressure  0.2 MPa(G)

    LAr tank   (prepared by buyer)

    Vertical,Perlite insulation

    1

    Efficient volume 15 m3

    Design pressure 0.8MPa(G)

    LOX truck filling pump(imported)

    centrifugal

    1

    Delivery flow rate  18 m3/h

    Working pressure  0.6 MPa(G)

    LN2 truck filling pump(imported)

    centrifugal

    1

    Delivery flow rate 18 m3/h

    Working pressure 0.6 MPa(G)

    L Ar truck filling pump(imported)

    centrifugal

    1

    Delivery flow rate 18 m3/h

    Working pressure 0.6 MPa(G)

    Image (for reference, determined by final design)

     

     

    Annex 4 Instrument system

    Design principle

    1. It should be able to control and supervise the whole process of the air separation plant to ensure the long stable roperation and easy maintenance.
    2. It is of central control room(DCS) with local control panel and field control to ensure the reliability and advance.
    3. There are 2 21”  screen operation tables. It has supervision, display, or operation, adjusting, memory start interlock and protecting function. It can stop or start automaticly according to technological requirement, to open or close the calves. It also can be operated by manual to start,  stop or change the operation mode.
    4. there are two printers in central control room recoording main parameters in the whole process of production and operation of the workers and system fault if it is over limitation separately.
    5. Local control anels can dispay parcial parameters and operaion conditions, warning, etc.
    6. Instrument power supply:1 circuit is of 380V AC,another 220VACand 24VDC.DCS system is supported by uninterrupted power. Instrument control power supply is by power supply panel of instrument control system.
    7. Online analyzing room is provided in instrument pane Online analyzing technological data enters DCS system to display , recording, warning, etc. There is a manual valve analyzing panel.

    Ø

     

     

     

     

     

     

     

     

     

     

     

    1. Instrument selection

     

    DCS system

    Zhejiang Zhong Kong.

    UPS

    Santak.

    On line analyzing instrument

    complete (electric and gas line will be within terminal and standard gas and pretreatment device provided).

     

    Regulating valves

    Zhejiang or simular products

    Butterfly valve of M.S. purifier

    USA Bray

    Pressure, pressure difference transformer and flow transmitter

    EJA or similar brand

    2 positions 3 ways and 2 positions 5 ways solenoid valves

    SMC,PARKERor similar brand

    Local flow meter

    glass rotor flow meter,

    Air flow measuring element

    orifice

    Temp. measuring

    Pt100 with graduation and resistance within cold box is of double platinum resistance temperature sensor.

    Local and field panel indication

    spring tube pressure gauges.

    Local tempt, indication

    double metal temperature meter.

     

     

     

     

     

     

     

     

     

     

     

    Scope of supply for instrument system (note:Depends on real supply of good based on final design)

    Q.T.

     

    Ø  DCS(Distributed Control System)

    1

     

    19” color LCD operating desk

    2

     

    Printer 

    1

     

    Control station (incl. all kind of  I/O card)

    1

     

    Terminal board and communication cable

    1

     

    System software(incl. technical paper)

    1

     

    Ø  Main instrument

     

    UPS un-interrupted power supply(10KVA,15MINS s/b battery)

    1

     

    Pressure and pressure differential transformer

    60

     

    All kinds of ragulating valve

    17

     

    Switch over butterfly valves

    10

     

    Pt resistance

    60

     

    Orifice plate

    9

    Ø  Analyzer instrument

     

    double metal tempt. meter, pressure gauge, joint. Etc.

    1

     

    Ø  Instrument panel

     

    DCS panel

    1

     

    Online analyzer panel

    1

     

    (all with wire and pipes. Outside purchased will be with that panel.)

     

             

     

    Ø  Analyzer instrument(incl. panel and pretreatment device and standard gas, etc.)

    Q.T.

    CO2 analyzer (0~10ppmCO2)(imported)

    1

    Pure O2 analyzer (98~100%O2)     ( imported )

    1

    Trace O2 analyzer (0~10ppmO2)   ( imported )

    2

    Trace moisture analyzer (0~100ppmH2O)( imported )

    1

    Thermal conductance Ar analyzer (0~15%Ar)

    1

    Thermal conductance Ar analyzer (80~100%Ar)

    1

    Constant O2 analyzer (0~5%O2)

    1

    (note:Depends on real supply of good based on final design)For ref.

     

     

     

    Annex 5 Electric control system

    Design principle

    It must be fit for reliable, easy operation and process requirement.

    Motor control ,  protection  and measuring  must be in accordance with China relative standards.

    1 way incoming cable for high voltage

    HV motor uses liquid soft starter. Busbar voltage will not less than 85% of it.

    HV system control is protected by computer comprehensive protection measuring control device.

    There is local panel for motor with necessary electric meters and signal and operation element.

    LV power resource has two incoming lines, among which one is as S/B.

    When LV motor start, LV busbar voltage drop will not be lower than 15%.

    Ø  MS heater tempt, is regulated by closed-loop power regulation.

     
     
    •  

    Liquid O2 output 900nm3/h
    O2 output 150nm3/h
    Liquid N2 output 160nm3/h
    Liquid argon output 30nm3/h
    Liquid O2 purity >99.6%
    O2 purity >99.6%
    Liquid N2 purity <3ppmO2
    Liquid argon purity <2ppmO2,<3ppmN2

    Cryogenic 900nm³/h Liquid Oxygen /150nm3/h Oxygen 30nm3/h Liquid Argon Plant Air Separation Plant With Low Energy

     

     

     

     

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

    Contact Person: Mr. Yao junming

    Send your inquiry directly to us (0 / 3000)

    Best Products
    Other Products