Apparatus of hydrocarbon fuel reactors having carbon dioxide separated and purified with space efficiency

Patent metadata

Field	Value
Publication number	US-10010845-B2
Application number	US-201615335592-A
Country	US
Kind code	B2
Filing date	Oct 27, 2016
Priority date	May 26, 2016
Publication date	Jul 3, 2018
Grant date	Jul 3, 2018

Abstract

An apparatus of hydrocarbon fuel reactors separates and purifies carbon dioxide (CO 2 ). Interconnected fluidized beds are applied in chemical-looping combustion. A multi-stage reduction reaction is processed with iron-based oxygen carriers. Three reduction stages using the iron-based oxygen carriers are accurately and completely controlled. Each of the three stages is separately processed in an individual space. Oxygen in the iron-based oxygen carriers can be fully released. High-purity CO 2 is obtained. Hydrogen can be produced as an option. Horizontal connection of three reduction reactors is changed into vertical one. An oxidation reactor is further connected. Thus, the whole structure occupies less area and effectively uses vertical space. Not only small space is effectively used; but also high-volume capacity is obtained. Each of the reactors has better geometry flexibility. The tandem reactor in each layer has less geometric influence and limitation. Therefore, each of the reactors can be resized on its own.

First claim

What is claimed is:

1. An apparatus of hydrocarbon fuel reactors having carbon dioxide (CO 2 ) separated and purified, comprising:
a first reduction reactor,
wherein the said first reduction reactor comprises a first lean bed and a first dense bed, a first orifice located at a side of bottom of said first dense bed, and a first weir located at a side of top of said first lean bed; and

wherein ferric oxide (Fe 2 O 3 ) is added to the said first lean bed and used as an iron-based oxygen carrier; a first stage of a reduction reaction is processed to obtain a gas comprising CO 2 and steam and reduce Fe 2 O 3 to ferroferric oxide (Fe 3 O 4 ); and Fe 3 O 4 rises up in said first lean bed and crosses over said first weir;
a second reduction reactor,
wherein the said second reduction reactor is located below and connected to the said first reduction reactor; while comprises a second lean bed and a second dense bed, a second orifice located at a side of bottom of said second dense bed, and a second weir located at a side of top of said second lean bed; and
wherein Fe 3 O 4 enters the said second dense bed through said first weir and settles down in said second dense bed; CO 2 is passed into said second dense bed and used as a carrier gas to deliver Fe 3 O 4 from said second dense bed into said second lean bed through said second orifice; a second stage of said reduction reaction is processed with a hydrocarbon fuel to obtain a gas comprising CO 2 and steam and reduce Fe 3 O 4 to iron oxide (FeO); and FeO rises up in said second lean bed and crosses over said second weir;

a third reduction reactor,

wherein the said third reduction reactor is located below and connected to the said second reduction reactor; while comprises a third dense bed and a third lean bed, a third orifice located at a side of bottom of said third dense bed, and a third weir located at a side of top of said third lean bed; and
wherein FeO enters the said third dense bed through said second weir and settles down in said third dense bed; CO 2 is passed into said third dense bed and used as a carrier gas to deliver FeO from said third dense bed into said third lean bed through said third orifice; a third stage of said reduction reaction is processed with a hydrocarbon fuel to obtain a gas comprising CO 2 and steam and reduce FeO to iron (Fe); and Fe rises up in said third lean bed and crosses over said third weir; and
an oxidation reactor,

wherein the said oxidation reactor is located at a side of the said first reduction reactor, said second reduction reactor and said third reduction reactor and connected to the said first reduction reactor and said third reduction reactor; while comprises a fourth dense bed and a fourth lean bed, a fourth orifice located at a side of bottom of said fourth dense bed, and a fourth weir located at a side of top of said fourth lean bed;
wherein Fe enters the said fourth dense bed through said third weir and settles down in said fourth dense bed; CO 2 is passed into said fourth dense bed and used as a carrier gas to deliver Fe from said fourth dense bed into said fourth lean bed through said fourth orifice; an oxidation reaction is processed with air to obtain a gas comprising nitrogen and oxygen and turn Fe to Fe 2 O 3 ; Fe 2 O 3 rises up in said fourth lean bed to cross over said fourth weir; Fe 2 O 3 enters and settles down in said first dense bed; CO 2 is passed into said first dense bed and used as a carrier gas to deliver Fe 2 O 3 from said first dense bed into said first lean bed through said first orifice to form a loop; and, thus, said loop is processed by providing said iron-based oxygen carrier into said first reduction reactor; and
at least one heat exchanger to heat up a working medium by said gas consisting of CO 2 and steam; and said working medium is selected from a group of CO 2 and a hydrocarbon fuel.

2. The apparatus according to claim 1 ,
wherein said first, said second and said third stages of said reduction reaction are processed at a temperature of 400˜950 celsius degrees (° C.).

3. The apparatus according to claim 1 ,
wherein said first, said second and said third lean beds are staggered and dislocated with said first, said second and said third dense beds.

4. The apparatus according to claim 1 ,
wherein the said first, said second and said third reduction reactors have different geometric dimensions according to the differences of reducing reaction kinetics processed in said first, said second and said third reduction reactors.

5. The apparatus according to claim 1 ,
wherein the said first, said second and said third reduction reactors are vertically connected and stacked.

6. The apparatus according to claim 1 ,
wherein the said fourth lean bed utilizes steam to process said oxidation reaction with Fe; then hydrogen (H 2 ) is obtained; and Fe is turned into Fe 2 O 3 .

7. The apparatus according to claim 1 ,
wherein, after crossing said first weir, Fe 3 O 4 in said first lean bed enters said second dense bed through a channel located at bottom or a side.

8. The apparatus according to claim 1 ,
wherein, after crossing said second weir, FeO in said second lean bed enters said third dense bed through a channel located at bottom or a side.

9. The apparatus according to claim 1 ,
wherein said working medium to be heated is CO 2 ; is supplied to said first, said second and said third reduction reactors; and is used as a carrier gas in said first, said second and said third dense bed.

10. The apparatus according to claim 1 ,
wherein said working medium to be heated is CO 2 ; is supplied to said oxidation reactor; and is used as a carrier gas in said fourth dense bed.

11. The apparatus according to claim 1 ,
wherein said working medium to be heated is said hydrocarbon fuel; is supplied to a reduction reactor selected from a group of said first reduction reactor and said second reduction reactor; and is used as a reduction gas in a corresponding lean bed selected from a group of said first lean bed and said second lean bed.

12. The apparatus according to claim 1 ,
wherein said working medium to be heated is said hydrocarbon fuel; is supplied to said first and said second reduction reactors; and is used as a reduction gas in said first and said second lean beds.

13. The apparatus according to claim 1 ,
wherein said heat exchanger is located between said first reduction reactor and said second reduction reaction.

14. The apparatus according to claim 1 ,
wherein said heat exchanger is located between said second reduction reactor and said third reduction reactor.

15. The apparatus according to claim 1 ,
wherein said heat exchanger is located between said first reduction reactor and said second reduction reaction and between said second reduction reactor and said third reduction reactor.

16. An apparatus of hydrocarbon fuel reactors having carbon dioxide (CO 2 ) separated and purified, comprising:
a first reduction reactor,
wherein the said first reduction reactor comprises a first lean bed and a first dense bed, a first orifice located at a side of bottom of said first dense bed, and a first weir located at a side of top of said first lean bed; and

wherein ferric oxide (Fe 2 O 3 ) is added to the said first lean bed and used as an iron-based oxygen carrier; a first stage of a reduction reaction is processed to obtain a gas comprising CO 2 and steam and reduce Fe 2 O 3 to ferroferric oxide (Fe 3 O 4 ); and Fe 3 O 4 rises up in said first lean bed and crosses over said first weir;
a second reduction rea

Assignees

• Iner Aec Executive Yuan

Inventors

• Chyou Yau-Pin
• Chen Po-Chuang
• Chien Hsiu-Yun
• Wu Keng-Tung
• Huang Ching-Ying

Classifications

• C01B31/20

  Chemistry & Metallurgy · mapped topic

• B01J2208/00256

  in a heat exchanger for the heat exchange medium separate from the reactor · CPC title

• B01J8/08 Primary

  with moving particles (with fluidised particles B01J8/18) · CPC title

• B01J8/087

  Heating or cooling the reactor · CPC title

• B01J8/26 Primary

  with two or more fluidised beds, e.g. reactor and regeneration installations · CPC title