99.6% Air Separation Plant Industrial KDON-350/800 Oxygen Plant With Low Energy Consumption

Atmosphere pressure       96kPa(A)
Atmosphere tempt.    25
Relative humidity 75%
O2 contained in air    20.95%O

Annual average tempt.                                18.4
Max. Tempt.                                       45
Min. Tempt.                                        -15
Average tempt. in Summer                           25
Average tempt. in Winter                             -15

Earth shake :  6 Mcalli degree

 Sea level:       425m

 Impurity in atmosphere:
CO2       ≤300 ppm
SO2       ≤0.44 mg/m3
H2S       ≤2.3 mg/m3
CH4       ≤5.2mg/m3
C2H2     ≤0.03 ppm
CnHm(Except C2H2)     ≤5 ppm
Dust content       ≤10mg/m3

1.6 Recycling water

Inlet tempt.   30
Inlet pressure      0.4 MPa(G)
Max. pressure drop    0.2 MPa(G)
Max. tempt. rising       10
Turbidity of cooling water   12 mg/L
PH value       7.2

Total hardness       2.5
Fouling factor 0.0004 m2 hºC/ kW

       Water consumption: 180T/h Recycling water   25T/h(not incl. O2 compressor)

Power supply
HV power supply               10kV±5%
LV power supply                380V/220V±5%
Frequency                      50±0.5Hz

     Loaded power                      330KW(Name plate not iccl.

O2compressor)

2.  Main technical parameters

2.1 Output and purity, pressure(out of the cold box)

O2 output                             350m³/h±5%

O2 purity                             ≥99.6%O₂

O2 pressure                           0.034MPa(G)

N2 output                             800m³/h±5%

N2 purity                             ≤10ppmO₂

N2 pressure                           0.012 MPa(G)

Product output status(at 0,101.325Kpa)

 Start pressure                        0.65MPa(G)

 Continuous operation period between two defrosting times   12months

 Start time                            24 Hours

Specific power consumption            0.64kWh/mO₂(not incl. O2 compressor)

3. Process description:

KDON-350/500 air separation plant is of low pressure process.

Raw air comes from air, goes through air filter for removal of dust andother mechanical particle and  enters non-lub air compressor to be compressed by two stage compressor to approx.  0.65MPa(g).It goes through cooler and enters precooling unit to be cooled to 510. Then it goes to switch-over MS purifier for removal of moisture, CO2, carbon hydrogen.  Purifier consists of two molecular sieve filled vessels. One is in use while anther is under regeneration by waste nitrogen from the cold box and through heater heating.

After purified, small part of it is used as bearing gas for turbine expander, other enters cold box to be cooled by reflux(pure oxygen, pure nitrogen and waste nitrogen) in main heat exchanger. Part of air is abstracted from the middle part of main heat exchanger and goes to expansion turbine for production of cold. Most of expanded air goes through subcooler which is cooled by oxygen from upper column to be delivered to upper column. Small part of it goes through bypass to waste nitrogen pipe directly and is reheated to go out of the cold box. The other part of air continues to be cooled to near liquid air tempt to lower column.

In lower column air,air is separated and liquified as liquid nitrogen and liquid air. Part of liquid nitrogen s abstracted from the top of the lower column. Liquid air after subcooled and throttled is delivered to the middle part of upper column as reflux.

Product oxygen is abstracted fr