Apparatus for compressing a wet gas flow

Patent metadata

Field	Value
Publication number	US-9702376-B2
Application number	US-201314394309-A
Country	US
Kind code	B2
Filing date	Apr 2, 2013
Priority date	Apr 16, 2012
Publication date	Jul 11, 2017
Grant date	Jul 11, 2017

Abstract

A method and apparatus for compressing a gas flowing comprising at least 0.1 vol % water, include a compressor containing N compression stages, in which each compression stage includes a compressing means and an exchanger directly or indirectly connected to a water-coolant circuit; and in which at least a first exchanger and a second exchanger, in first and second consecutive or non-consecutive compression stages, are connected in series to the water-coolant circuit. The exchangers, which are not connected in series to the water-coolant circuit, include at their water-coolant output a pressure drop device.

First claim

The invention claimed is:

1. A compression plant for compressing a gas stream comprising a gas stream comprising a wet CO 2 gas stream, the plant comprising a compressor having N compression stages, wherein:
each compression stage comprises a compression means and an exchanger connected directly or indirectly to a cooling water circuit;
at least a first exchanger and a second exchanger of a first and of a second consecutive or non-consecutive compression stages are connected in series to the cooling water circuit; and
at least a third exchanger of a third compression stage, the third exchanger not being connected in series to the cooling water circuit, wherein the at least third exchanger comprises a device that is configured to create a pressure drop at a cooling water outlet of the at least third exchanger.

2. The compression plant as claimed in claim 1 , wherein the shells of the exchangers of the n first compression stages, located on the feed side of the compressor, consist of steel having a chromium content of less than 11% by weight and an absence of a stainless coating, with n≦N−1.

3. The compression plant as claimed in claim 1 , wherein the shells of the exchangers of the n first compression stages, located on the feed side of the compressor, are made of carbon steel, with n≦N−1.

4. The compression plant as claimed in claim 1 , wherein the second exchanger is also connected directly to the water cooling circuit and a temperature regulation system makes it possible to control the mixing of the cooling water resulting from the first exchanger and of the cooling water resulting directly from the cooling water circuit.

5. The compression plant as claimed in claim 1 , wherein the exchanger of the last compression stage, located on the production side of the compressor, is made of stainless steel.

6. The compression plant as claimed in claim 1 , wherein the device that makes it possible to create a pressure drop comprises an orifice or a valve.

7. A process for compressing a gas stream comprising a wet CO 2 gas stream using a compression plant as claimed in claim 1 .

8. The process as claimed in claim 7 , further comprising the steps of:
measuring the temperature of the cooling water T w of the cooling circuit;
comparing T w to the dew point T d of the gas stream entering a second exchanger belonging to one of the N−1 compression stages located on the feed side of the compressor;
and, if the temperature of the water of the cooling circuit T w is such that T w −T d <10° C.:
connecting the cooling water inlet of said exchanger to the cooling water outlet of a first exchanger belonging to said N−1 compression stages, located on the feed side of the compressor, and/or
introducing water external to said compression plant and having a temperature T s >T w directly into the cooling water circuit or directly into said exchanger,
such that the temperature T exch of the water entering said exchanger is T exch −T d ≧10° C.

9. The compression process as claimed in claim 7 , wherein the gas stream is a stream produced by an H 2 PSA, a CO 2 PSA, a membrane separation process, a combustion turbine, an oxy-fuel combustion process, a cement production process, a blast furnace, a hydrogen production process or a refining process.

10. The process as claimed in claim 7 , wherein during a startup period, the process comprises the steps of:
compressing a dry gas at a temperature T g above the dew point T d of the gas stream to be compressed in the compressor having N compression stages until the skin temperature of the n first compression means and of the n first exchangers in contact with the gas stream, located on the feed side of the compressor with n≦N−1, and the temperature of the water from the cooling water circuit are above the dew point T d of the gas stream to be compressed,
replacing the dry gas by said gas stream to be compressed.

11. The process as claimed in claim 10 , wherein the dry gas is nitrogen or carbon dioxide.

12. The process as claimed in claim 7 , wherein during a shutdown period, the process comprises the steps of flushing and purging the compressor with a dry gas.

Assignees

• Air Liquide
• L'Air Liquide Société Anonyme Pour L'Étude Et L'Exploitation Des Procedes Georges Claude

Inventors

• Darde Arthur
• Defaye Cyril
• Morel Thomas

Classifications

• F04D29/5826 Primary

  Cooling at least part of the working fluid in a heat exchanger · CPC title

• F25J2230/30

  Compression of the feed stream · CPC title

• F04B41/06 Primary

  Combinations of two or more pumps · CPC title

• F04D29/023

  especially adapted for elastic fluid pumps · CPC title

• F04D13/14

  the pumps being all of centrifugal type {(deviation valves F04D15/0016)} · CPC title