FIELD: chemical industry, metallurgy for separation of air by low-temperature rectification. SUBSTANCE: part of air after complex cleaning unit is bled and subjected to final compression in compressor of turbo-expander compressor unit 7 to pressure of 13 kgf/sq.cm, after which it is cooled in main heat exchanger to temperature of 293 K and is delivered to suction end of main compressor 1. Nitrogen is delivered to consumer at pressure of first stage of rectification unit. Additional reflux is directed to first stage of rectification without heating. EFFECT: enhanced efficiency. 1 dwg
Title | Year | Author | Number |
---|---|---|---|
METHOD OF PRODUCING PRESSURIZED NITROGEN | 1992 |
|
RU2029204C1 |
AIR SEPARATION METHOD | 1990 |
|
RU2054609C1 |
METHOD FOR LIQUEFYING NATURAL GAS (OPTIONS) | 2022 |
|
RU2775341C1 |
AIR SEPARATION METHOD | 0 |
|
SU979810A1 |
METHOD OF PRODUCTION OF COLD | 1993 |
|
RU2085814C1 |
METHODS FOR TWO-STEP FRACTIONATION SEPARATION OF INERT GASES FROM TAIL GASES AND APPARATUS THEREFOR | 2013 |
|
RU2528786C1 |
DEVICE FOR NEON CONCENTRATION IN AIR MIXTURES CONTAINING NEON | 2009 |
|
RU2441693C2 |
HYDROGEN LIQUEFYING METHOD WITH USE OF HELIUM REFRIGERATION CYCLE AND APPARATUS FOR PERFORMING THE SAME | 2006 |
|
RU2309342C1 |
METHOD OF PRODUCTION OF COLD | 0 |
|
SU1747813A1 |
METHOD AND UNIT OF NATURAL GAS LIQUEFACTION AT THE GAS DISTRIBUTION STATION | 2017 |
|
RU2656068C1 |
Authors
Dates
1997-12-27—Published
1994-06-30—Filed