Method and apparatus for separating a synthesis gas

Patent metadata

Field	Value
Publication number	US-10890376-B2
Application number	US-201615772280-A
Country	US
Kind code	B2
Filing date	Oct 28, 2016
Priority date	Oct 30, 2015
Publication date	Jan 12, 2021
Grant date	Jan 12, 2021

Abstract

In a method for separating a synthesis gas containing carbon monoxide and hydrogen, a synthesis gas flow from a synthesis gas source is compressed in a compressor and separated into at least three gaseous products. If there is insufficient synthesis gas, at least three separation products are recycled in the compressor in order to separate said products.

First claim

The invention claimed is:

1. A method for separating a synthesis gas containing carbon monoxide and hydrogen wherein:
i) compressing a synthesis gas flow originating from a synthesis gas source in a compressor;
ii) purifying the compressed synthesis gas in a purification unit to remove water and/or carbon dioxide;
iii) cooling the compressed purified synthesis gas flow;
iv) separating the cooled synthesis gas flow in a separation unit by a separation process selected from the group consisting of scrubbing, distillation at a cryogenic temperature, adsorption, and combinations thereof,
v) producing at least the following three gases in the separation unit: a carbon monoxide-enriched gas, a hydrogen-enriched gas, a residual gas containing carbon monoxide and hydrogen which contains less carbon monoxide than the carbon monoxide-enriched gas and less hydrogen than the hydrogen-enriched gas, and
vi) determining that the synthesis gas flow passed to the compressor is below a threshold or zero, and then introducing at least a portion of at least two the gases selected from the group consisting of the carbon monoxide-enriched gas, the hydrogen-enriched gas, the residual gas, and combinations thereof, at a location downstream of the source and upstream of the purification unit,
wherein at least a portion of at least each of the three gases from stage v) downstream of the source is introduced downstream of the source and upstream of the compressor only if the flow of synthesis gas is below the threshold, or if none of the flow of the synthesis gas comes from the source.

2. The method as claimed in claim 1 , wherein:
a) the compressed synthesis gas is stored while the flow of synthesis gas is above the threshold; and
b) at least a portion of the compressed synthesis gas and at least a portion of at least each of the first three gases from stage v) are passed downstream of the source to be purified in the purification unit and separated in the separation unit while the flow of synthesis gas is below the threshold.

3. The method as claimed in claim 1 , wherein
x % of a nominal output of the carbon monoxide-enriched gas and y % of a nominal output of the hydrogen-enriched gas are passed to the separation unit when the flow of synthesis gas is below a threshold, x and y differing by at most 5%; and/or
y % of the nominal output of the hydrogen-enriched gas and z % of the nominal output of the residual gas are passed to the separation unit when the flow of synthesis gas is below a threshold, y and z differing by at most 5%; and/or
x % of the nominal output of the carbon monoxide-enriched gas z % of the nominal output of the residual gas are passed to the separation unit when the flow of synthesis gas is below a threshold, x and z differing by at most 5%.

4. A method for separating a synthesis gas containing carbon monoxide and hydrogen, the method comprising the steps of:
i) compressing a synthesis gas flow originating from a synthesis gas source in a compressor;
ii) purifying the compressed synthesis gas in a purification unit to remove water and/or carbon dioxide;
iii) cooling the compressed purified synthesis gas flow;
iv) separating the cooled synthesis gas flow in a separation unit by a separation process selected from the group consisting of scrubbing, distillation at a cryogenic temperature, adsorption, and combinations thereof;
v) producing at least the following three gases in the separation unit: a carbon monoxide-enriched gas, a hydrogen-enriched gas, a residual gas containing carbon monoxide and hydrogen which contains less carbon monoxide than the carbon monoxide-enriched gas and less hydrogen than the hydrogen-enriched gas, and
vi) determining that the synthesis gas flow passed to the compressor is below a threshold or zero, and then introducing at least a portion of at least two the gases selected from the group consisting of the carbon monoxide-enriched gas, the hydrogen-enriched gas, the residual gas, and combinations thereof, at a location downstream of the source and upstream of the purification unit,
wherein a portion of the carbon monoxide-enriched gas is stored in a storage unit and the rest of the carbon monoxide-enriched gas is sent to a customer if the flow of synthesis gas is above the threshold and the carbon monoxide-enriched gas originating from the storage unit is sent to the customer if the flow of synthesis gas is below the threshold.

5. The method as claimed in claim 4 , wherein if the flow of synthesis gas is below the threshold, all the carbon monoxide-enriched gas passed to the customer originates from the storage unit and possibly all the carbon monoxide-enriched gas originating directly from the separation unit without passing through the storage unit is passed upstream of the compressor and downstream of the source.

6. The method as claimed in claim 1 , wherein the synthesis gas is a residual gas from an acetylene production unit.

7. A method for separating a synthesis gas containing carbon monoxide and hydrogen, the method comprising the steps of:
i) compressing a synthesis gas flow originating from a synthesis gas source in a compressor;
ii) purifying the compressed synthesis gas in a purification unit to remove water and/or carbon dioxide;
iii) cooling the compressed purified synthesis gas flow;
iv) separating the cooled synthesis gas flow in a separation unit by a separation process selected from the group consisting of scrubbing, distillation at a cryogenic temperature, adsorption, and combinations thereof;
v) producing at least the following three gases in the separation unit: a carbon monoxide-enriched gas, a hydrogen-enriched gas, a residual gas containing carbon monoxide and hydrogen which contains less carbon monoxide than the carbon monoxide-enriched gas and less hydrogen than the hydrogen-enriched gas, and
determining that the synthesis gas flow passed to the compressor is below a threshold or zero, and then introducing at least a portion of at least two the gases selected from the group consisting of the carbon monoxide-enriched gas, the hydrogen-enriched gas, the residual gas, and combinations thereof, at a location downstream of the source and upstream of the purification unit,
wherein if the flow of synthesis gas is above the threshold, a portion of the synthesis gas is stored in a storage unit and if the flow of synthesis gas is below the threshold, the synthesis gas is passed from the storage unit to the compressor.

8. The method as claimed in claim 1 , wherein if the synthesis gas flow is zero, the separation unit is only fed by gases produced by the separation unit.

9. A method for separating a synthesis gas containing carbon monoxide and hydrogen, the method comprising the steps of:
i) compressing a synthesis gas flow originating from a synthesis gas source in a compressor;
ii) purifying the compressed synthesis gas in a purification unit to remove water and/or carbon dioxide;
iii) cooling the compressed purified synthesis gas flow;
iv) separating the cooled synthesis gas flow in a separation unit by a separation process selected from the group consisting of scrubbing distillation at a cryogenic temperature, adsorption, and combinations thereof;
v) producing at least the following three gases in the separation unit; a carbon monoxide-enriched gas, a hydrogen-enriched gas, a residual gas containing carbon monoxide and hydrogen which contains less carbon monoxide than the carbon monoxide-enriched gas and less hydrogen than the hydrogen-enriched gas, and
vi) determining that the synthesis gas flow passed to the compressor is below a threshold or zero, and then introducing at least a portion of at least two the gases selected from the group consisting of the carbon mon

Assignees

• Air Liquide

Inventors

• Demolliens Bertrand
• Hernandez Antoine
• Tsevery Jean-Marc

Classifications

• F25J2280/02

  Control in general, load changes, different modes ("runs"), measurements · CPC title

• F25J2250/30

  External or auxiliary boiler-condenser in general, e.g. without a specified fluid or one fluid is not a primary air component or an intermediate fluid · CPC title

• C01B2203/043

  Regenerative adsorption process in two or more beds, one for adsorption, the other for regeneration · CPC title

• C01B2203/146

  At least two purification steps in series · CPC title

• F25J2210/42

  Nitrogen · CPC title