Optimized heat exchange in a CO2 de-sublimation process

Patent metadata

Field	Value
Publication number	US-9766011-B2
Application number	US-201615182494-A
Country	US
Kind code	B2
Filing date	Jun 14, 2016
Priority date	Nov 28, 2012
Publication date	Sep 19, 2017
Grant date	Sep 19, 2017

Abstract

The present invention is a process for removing carbon dioxide from a compressed gas stream including cooling the compressed gas in a first heat exchanger, introducing the cooled gas into a de-sublimating heat exchanger, thereby producing a first solid carbon dioxide stream and a first carbon dioxide poor gas stream, expanding the carbon dioxide poor gas stream, thereby producing a second solid carbon dioxide stream and a second carbon dioxide poor gas stream, combining the first solid carbon dioxide stream and the second solid carbon dioxide stream, thereby producing a combined solid carbon dioxide stream, and indirectly exchanging heat between the combined solid carbon dioxide stream and the compressed gas in the first heat exchanger.

First claim

What is claimed is:

1. A process for removing carbon dioxide from a compressed gas stream, the process comprising the steps of:
cooling the compressed gas stream having carbon dioxide in a first heat exchanger to a first temperature that is above the frosting point of carbon dioxide to form a cooled compressed gas stream;
cooling the cooled compressed gas stream in a second heat exchanger to a second temperature that is below the frosting point of carbon dioxide, wherein only a portion of the carbon dioxide within the cooled compressed gas stream de-sublimates thereby forming a first solid CO 2 stream and a CO 2 depleted gas stream;
withdrawing the first solid CO 2 stream from the second heat exchanger;
withdrawing the CO 2 depleted gas stream from the second heat exchanger;
expanding the CO 2 depleted gas stream, such that the carbon dioxide within the CO 2 depleted gas stream de-sublimates to form a second CO 2 solid stream and a cold CO 2 depleted gas stream;
combining the first solid CO 2 stream with the second solid CO 2 stream to form a final solid CO 2 stream;
introducing the cold CO 2 depleted gas stream to the second heat exchanger and the first heat exchanger in succession in order to provide a first portion of refrigeration to the first and second heat exchangers;
pressurizing the final solid CO 2 stream to a pressure that is at or exceeds the triple point of carbon dioxide to produce a pressurized solid CO 2 stream;
melting the pressurized solid CO 2 stream in a melting heat exchanger to produce a liquid CO 2 stream;
heating the liquid CO 2 stream in the first heat exchanger to form a warmed CO 2 fluid; and
providing a second portion of refrigeration to the first and second heat exchangers using a reverse Rankine refrigeration cycle having a refrigerant, wherein the reverse Rankine refrigeration cycle comprises the steps of:
(a) compressing the refrigerant in a compressor;
(b) condensing the refrigerant;
(c) expanding the refrigerant;
(d) vaporizing the refrigerant;

wherein step (b) occurs in the melting heat exchanger, at a temperature near the CO 2 triple point such that the refrigerant condenses,
wherein step (c) further comprises sending the condensed refrigerant to an expansion device such that the condensed refrigerant is reduced in temperature and forms a mixed phase stream, separating the mixed phase stream into a gas refrigerant stream and a liquid refrigerant stream, sending the liquid refrigerant stream to the second heat exchanger for vaporization therein,
wherein step (d) occurs in the second heat exchanger,
wherein only a portion of the refrigerant provides refrigeration within the second heat exchanger.

2. A process for removing carbon dioxide from a compressed gas stream, the process comprising the steps of:
cooling the compressed gas stream having carbon dioxide in a first heat exchanger to a first temperature that is above the frosting point of carbon dioxide to form a cooled compressed gas stream;
cooling the cooled compressed gas stream in a second heat exchanger to a second temperature that is below the frosting point of carbon dioxide, wherein a portion of the carbon dioxide within the cooled compressed gas stream de-sublimates thereby forming a first solid CO 2 stream and a CO 2 depleted gas stream;
withdrawing the first solid CO 2 stream from the second heat exchanger;
withdrawing the CO 2 depleted gas stream from the second heat exchanger;
expanding the CO 2 depleted gas stream, such that the carbon dioxide within the CO 2 depleted gas stream de-sublimates to form a second CO 2 solid stream and a cold CO 2 depleted gas stream;
combining the first solid CO 2 stream with the second solid CO 2 stream to form a final solid CO 2 stream;
introducing the cold CO 2 depleted gas stream to the second heat exchanger and the first heat exchanger in succession in order to provide a first portion of refrigeration to the first and second heat exchangers;
pressurizing the final solid CO 2 stream to a pressure that is at or exceeds the triple point of carbon dioxide to produce a pressurized solid CO 2 stream;
melting the pressurized solid CO 2 stream in a melting heat exchanger to produce a liquid CO 2 stream;
heating the liquid CO 2 stream in the first heat exchanger to form a warmed CO 2 fluid; and
providing a second portion of refrigeration to the first and second heat exchangers using a reverse Rankine refrigeration cycle having a refrigerant, wherein the reverse Rankine refrigeration cycle comprises the steps of:
(a) compressing the refrigerant in a compressor;
(b) condensing the refrigerant;
(c) expanding the refrigerant;
(d) vaporizing the refrigerant;

wherein step (b) occurs in the melting heat exchanger, wherein the refrigerant is condensed near −56.6° C.,
wherein step (d) occurs in the second heat exchanger,
wherein between steps (c) and (d), the refrigerant is split into a gas stream and a liquid stream, with the liquid stream being sent to the second heat exchanger for vaporization within the second heat exchanger, such that only a portion of the refrigerant provides refrigeration within the second heat exchanger.

3. The process as claimed in claim 1 , wherein the gas refrigerant stream is combined with the refrigerant from step (d) downstream the second heat exchanger.

4. The process as claimed in claim 1 , wherein the gas refrigerant stream is combined with the refrigerant from step (d) downstream the second heat exchanger and upstream the first heat exchanger, such that the gas refrigerant stream provides refrigeration to the first exchanger but not the second heat exchanger.

5. The process as claimed in claim 2 , wherein the gas refrigerant stream is combined with the refrigerant from step (d) downstream the second heat exchanger.

6. The process as claimed in claim 2 , wherein the gas refrigerant stream is combined with the refrigerant from step (d) downstream the second heat exchanger and upstream the first heat exchanger, such that the gas refrigerant stream provides refrigeration to the first exchanger but not the second heat exchanger.

Assignees

• Air Liquide
• Newvistas Capital Llc

Inventors

• Baxter Larry
• Terrien Paul
• Tessier Pascal
• Hoeger Christopher

Classifications

• B01D2257/504

  Carbon dioxide · CPC title

• B01D53/002

  by condensation · CPC title

• F25J2270/90

  External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration · CPC title

• B01D2258/0283

  Flue gases · CPC title

• F25J3/067 Primary

  separation of carbon dioxide (production of carbon dioxide in general C01B32/00) · CPC title