Method and appliance for separating a mixture containing carbon dioxide by cryogenic distillation

Patent metadata

Field	Value
Publication number	US-9851142-B2
Application number	US-201314431219-A
Country	US
Kind code	B2
Filing date	Sep 24, 2013
Priority date	Sep 25, 2012
Publication date	Dec 26, 2017
Grant date	Dec 26, 2017

Abstract

In a method for separating at least one lighter impurity of a gaseous mixture containing at least 30% mol of carbon dioxide, a liquid ( 101 ) enriched with carbon dioxide is drawn off into a vat of a distillation column ( 25 ), at least part ( 27 ) of the liquid enriched with carbon dioxide is vaporized and then heated to a first temperature higher than the boiling temperature thereof in the exchanger and leaves the exchanger at the hot end thereof, and at least part of the vaporized and heated liquid is sent from the hot end of the exchanger at the first temperature, without being cooled in the exchanger and without having been compressed, to the lower part of the distillation column, where it participates in the distillation while enriching itself.

First claim

The invention claimed is:

1. A method for separating at least one lighter impurity of a gaseous mixture containing at least 30% mol of carbon dioxide comprising:
i) cooling the gaseous mixture in a heat exchanger, the heat exchanger comprising a hot end, the gaseous mixture entering the heat exchanger at the hot end, and the cooled gaseous mixture or a fluid derived from the gaseous mixture, this fluid containing at least 60% carbon dioxide, being separated by a distillation column, the distillation column having a head and a bottom part,
ii) removing a liquid enriched in carbon dioxide from the distillation column,
iii) drawing off a gas depleted in carbon dioxide and enriched in at least one lighter impurity at the head of the column and reheating this drawn off gas in the heat exchanger,

sending at least a part of the liquid enriched in carbon dioxide to the heat exchanger wherein at least one part of the liquid sent to the heat exchanger is vaporized and then super-heated to a first temperature in the heat exchanger and leaves from the heat exchanger at the hot end thereof, and at least a part of the vaporized and heated liquid is sent from the hot end of the heat exchanger at the first temperature, without being cooled in the heat exchanger and without having been compressed, to the bottom part of the distillation column, thereby becoming enriched in at least one lighter impurity, wherein the at least part of the liquid enriched in carbon dioxide that has been vaporized and then super-heated is divided into two parts, one part being returned to the column at the first temperature and the other part constituting at least a part of a final product.

2. The method of claim 1 , wherein the first temperature is at least 5° C. higher than the boiling point.

3. The method of claim 1 , wherein first temperature is higher than 0° C.

4. The method of claim 3 , wherein the first temperature is higher than 10° C.

5. The method of claim 1 , wherein the gaseous mixture goes into the heat exchanger at the hot end thereof at a temperature between 2 and 10° C. higher than the first temperature.

Assignees

• L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude

Inventors

• Darde Arthur
• Leclerc Mathieu

Classifications

• Y02C10/12

  Cross-Sectional Technologies · mapped topic

• F25J2245/02

  Recycle of a stream in general, e.g. a by-pass stream · CPC title

• F25J2240/90

  Hot gas waste turbine of an indirect heated gas for power generation · CPC title

• F25J2235/80

  the fluid being carbon dioxide · CPC title

• F25J2235/02

  using a pump in general or hydrostatic pressure increase · CPC title