Oxycombustion systems and methods with thermally integrated ammonia synthesis

Patent metadata

Field	Value
Publication number	US-10106430-B2
Application number	US-201314143737-A
Country	US
Kind code	B2
Filing date	Dec 30, 2013
Priority date	Dec 30, 2013
Publication date	Oct 23, 2018
Grant date	Oct 23, 2018

Abstract

Oxycombustion systems and oxycombustion methods include thermally integrated ammonia synthesis. The oxycombustion systems may include an air separation unit that separates air into an oxygen stream and a nitrogen stream. An ammonia synthesis unit synthesizes ammonia from a hydrogen feed and the nitrogen stream to form a crude ammonia stream. An ammonia separation unit condenses the crude ammonia stream and separates the ammonia from any unreacted nitrogen and hydrogen to form a purified ammonia stream. An oxycombustion reactor combusts a fuel from a fuel feed stream in the presence of the oxygen stream from the air separation unit to generate hot water or steam. At least one thermal integration may be present in the oxycombustion systems and may be chosen from a reactor thermal linkage of the ammonia synthesis unit with the oxycombustion reactor, a separator thermal linkage of the air separation unit with the ammonia separation unit, or both.

First claim

What is claimed is:

1. A thermally-integrated oxycombustion system comprising:
an air separation unit that separates an air feed stream into an oxygen stream and a nitrogen stream;
an ammonia synthesis unit that synthesizes ammonia from a hydrogen feed stream and the nitrogen stream from the air separation unit to form a crude ammonia stream containing the ammonia and, optionally, unreacted nitrogen and hydrogen;
an ammonia separation unit that condenses at least a portion of the crude ammonia stream formed in the ammonia synthesis unit and separates the ammonia from unreacted nitrogen and hydrogen to form a purified ammonia stream;
an oxycombustion reactor that combusts a fuel from a fuel feed stream in the presence of the oxygen stream from the air separation unit to produce combustion heat;
a flue-gas treatment system that treats a flue gas formed by the combustion of the fuel in the oxycombustion reactor with ammonia separated in the ammonia separation unit to remove pollutants from the flue gas and output carbon dioxide;
a carbon dioxide capture unit that captures the carbon dioxide generated in the flue-gas treatment system; and
a plurality of thermal integrations comprising:
a reactor thermal linkage of the ammonia synthesis unit and the oxycombustion reactor;
a separator thermal linkage of the air separation unit and the ammonia separation unit;
an air-separator capture-unit thermal linkage of the air separation unit and the carbon dioxide capture unit directing heat from the air separation unit to the carbon dioxide capture unit; and
an ammonia-separator capture-unit thermal linkage of the ammonia separation unit and the carbon dioxide capture unit directing heat from the ammonia separation unit to the carbon dioxide capture unit.

2. The thermally-integrated oxycombustion system of claim 1 , wherein the reactor thermal linkage of the ammonia synthesis unit with the oxycombustion reactor comprises a boiler loop that transfers combustion heat to the ammonia synthesis unit from the oxycombustion reactor, from flue gas formed in the oxycombustion reactor, from hot water or steam that has been heated from the combustion heat, or a combination thereof.

3. The thermally-integrated oxycombustion system of claim 1 , wherein the separator thermal linkage of the air separation unit with the ammonia separation unit comprises a separator loop that transfers heat to the air separation unit from the ammonia separation unit.

4. The thermally-integrated oxycombustion system of claim 1 , wherein the purified ammonia stream is in fluidic communication with the flue-gas treatment system and at least a portion of the ammonia separated in the ammonia separation unit is used in the flue-gas treatment system to remove the pollutants from the flue gas.

5. The thermally-integrated oxycombustion system of claim 1 , further comprising a urea synthesis unit that synthesizes urea to produce a urea stream from carbon dioxide captured in the carbon dioxide capture unit and the ammonia in the purified ammonia stream.

6. The thermally-integrated oxycombustion system of claim 5 , wherein at least one of the urea stream and the purified ammonia stream is in fluidic communication with the flue-gas treatment system and at least a portion of the ammonia in the purified ammonia stream or at least a portion of the urea in the urea stream, or both, is used to remove pollutants from the flue gas in the flue-gas treatment system.

7. The oxycombustion system of claim 5 , further comprising a urea synthesis thermal linkage of the urea synthesis unit and the oxycombustion reactor.

8. The thermally-integrated oxycombustion system of claim 7 , wherein:
both the purified ammonia stream and the urea stream and are in fluidic communication with the flue-gas treatment system; and
both ammonia in the purified ammonia stream and urea in the urea stream are used to remove pollutants from the flue gas in the flue-gas treatment system.

Assignees

• Saudi Arabian Oil Co

Inventors

• Younes Mourad
• Niass Tidjani

Classifications

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title

• C01C1/0417 Primary

  characterised by the synthesis reactor, e.g. arrangement of catalyst beds and heat exchangers in the reactor · CPC title

• Y02P20/129

  Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines · CPC title

• B01J12/00

  Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor (B01J3/08, B01J8/00, B01J19/08 take precedence) · CPC title

• F23L7/007

  Supplying oxygen or oxygen-enriched air · CPC title