Method and device for stripping a gas from a gas mixture using a venturi ejector

Patent metadata

Field	Value
Publication number	US-10173165-B2
Application number	US-201314430968-A
Country	US
Kind code	B2
Filing date	Oct 1, 2013
Priority date	Oct 5, 2012
Publication date	Jan 8, 2019
Grant date	Jan 8, 2019

Abstract

Method for extracting a gas from a gas mixture by:
during a purification step, bringing a first sorption medium into contact with the gas mixture in order to extract the gas from the gas mixture, whereby an enriched first sorption medium is formed in which the gas is at least partially sorbed; during a regeneration step, bringing a second sorption medium into contact with the enriched first sorption medium in order to extract the gas from the enriched liquid first sorption medium; whereby for the contact in the purification step and/or in the regeneration step use is made of a separate venturi ejector.

First claim

The invention claimed is:

1. Method for extracting a gas from a gas mixture, wherein the method comprises the following steps:
the provision of a liquid first sorption medium, which upon contact with the gas mixture can at least partially sorb the gas to be extracted;
during a purification step, bringing this first sorption medium into contact with the gas mixture by guiding them together through a purification stage to have the gas to be extracted at least partially sorbed from the gas mixture by the first sorption medium due to the mutual contact, in order to be left with a purified gas mixture with less gas to be extracted and an enriched liquid first sorption medium in which the gas to be extracted from the gas mixture is at least partially sorbed;
the provision of a gaseous second sorption medium that can at least partially extract the gas to be extracted from the enriched liquid first sorption medium upon contact with this enriched liquid sorption medium;
during a regeneration step, bringing this gaseous second sorption medium into contact with the enriched liquid first sorption medium formed during the aforementioned purification step by guiding them together through a regeneration stage, whereby, due to the mutual contact, the sorbed gas to be extracted in the enriched first sorption medium is at least partially sorbed by the second sorption medium and whereby at the output of the regeneration stage an at least partially regenerated liquid first sorption medium is formed that can be reused for a subsequent purification step;
whereby use is made of a venturi ejector with a liquid input and a gas input for the regeneration step, and whereby the enriched liquid first sorption medium originating from the purification step is supplied under pressure to the liquid input of this venturi ejector and the gaseous second sorption medium is drawn in via the gas input of this venturi ejector for the contact between the enriched first sorption medium and the second sorption medium.

2. Method according to claim 1 , wherein use is made of a separate venturi ejector with a liquid input and a gas input for the purification step, whereby the first sorption medium is supplied under pressure to the liquid input of this venturi ejector and the gas mixture to be purified is drawn in via the gas input of this venturi ejector for the contact between the first sorption medium and the gas mixture.

3. Method according to claim 1 , wherein the liquid first sorption medium is reused after the aforementioned regeneration step for a subsequent purification step.

4. Method according to claim 1 , wherein it makes use of a circuit in which the liquid first sorption medium is guided around from a first reservoir through the purification stage in which the enriched first sorption medium is received from where it is driven by means of a second pump through the regeneration stage that leads to the aforementioned first reservoir in which the regenerated first sorption medium is received.

5. Method according to claim 4 , wherein the method proceeds according to a continuous process whereby the liquid first sorption medium is guided around the circuit from the first reservoir via the purification stage and then back to the first reservoir via the regeneration stage, such that the gas mixture to be purified is continuously supplied to the purification stage and the purified gas from this purification stage is removed and the gaseous second sorption medium is drawn in continuously via the gas input of the venturi ejector of the regeneration stage.

6. Method according to claim 1 , wherein the second sorption medium is drawn in via an either or not adjustable flow restriction by the venturi ejector of the regeneration stage to reduce the partial pressure of the gas to be extracted in the second sorption medium.

7. Method according to claim 1 , wherein the first liquid sorption medium is heated for an endothermic extraction of the gas to be extracted, or cooled for an exothermic extraction of the gas to be extracted.

8. Method according to claim 1 , wherein the pressure of the gas mixture with the gas to be extracted differs from the pressure of the gaseous second sorption medium.

9. Method according to claim 1 , wherein the gas mixture to be purified is an untreated biogas that contains at least one of CO 2 and H 2 S.

10. Method according to claim 9 , wherein the first sorption medium is a liquid mixture of a more or less concentrated amine, amino salt or amino acid.

11. Method according to claim 1 , wherein the first sorption medium is a liquid mixture of a liquid and solid particles.

12. Method according to claim 11 , wherein the solid particles are iron oxide particles to remove H 2 S from the gas mixture to be purified by binding the sulphur to the iron into FeS that can be removed by filtering.

13. Method according to claim 9 , wherein the second sorption medium is ambient air.

14. Method according to claim 1 , wherein the gas mixture to be purified is a moist gas that must be dried and the first sorption medium is a hygroscopic liquid.

Assignees

• Atlas Copco Airpower Nv
• Atlas Copco Airpower Nv

Inventors

• Heirman Peter
• Aalderink Geurt

Classifications

• B01D53/18

  Absorbing units; Liquid distributors therefor (B01D3/16, B01D3/26, B01D3/30 take precedence; packing elements B01J19/30, B01J19/32) · CPC title

• B01D2252/2028

  Polypropylene glycol, ethers or esters thereof · CPC title

• Y02C10/06

  Cross-Sectional Technologies · mapped topic

• B01D2252/20494

  Amino acids, their salts or derivatives · CPC title

• B01D53/1425 Primary

  Regeneration of liquid absorbents · CPC title