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

Categories Air Separation Plant
Model Number: KDONAR-1000Y/1000/35Y
Certification: GB-150 CE ASME ISO9001 TUV
Place of Origin: China
MOQ: 1set
Price: negotiation
Payment Terms: T/T or L/C
Supply Ability: 100sets month
Delivery Time: 60working days after received your payment
Packaging Details: Packed in standard export packing
Brand Name: Tailian
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
  • Product Details
  • Company Profile

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

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

u 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

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