Partial oxidation reformer-reforming exchanger arrangement for hydrogen production
First Claim
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1. A process for preparing syngas, comprising:
- partially oxidizing a first hydrocarbon portion with oxygen in a partial oxidation reactor to produce a first reactor effluent;
cooling the first reactor effluent to a temperature from 650°
to 1000°
C., said cooling including direct heat exchange with water introduced into the first reactor effluent as a quench fluid;
supplying the cooled first reactor effluent to a reforming exchanger;
passing a second hydrocarbon portion with steam through a catalyst zone in the reforming exchanger to form a second reactor effluent, wherein the first and second hydrocarbon portions are supplied in a weight ratio of from 40;
60 to 60;
40;
discharging the second reactor effluent from the catalyst zone to form an admixture with the first reactor effluent;
passing the admixture across the catalyst zone in indirect heat exchange therewith to cool the admixture and heat the catalyst zone; and
collecting the cooled admixture from the reforming exchanger.
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Abstract
Low-energy hydrogen production is disclosed. A reforming exchanger is placed in parallel with a partial oxidation reactor in a new hydrogen plant with improved efficiency and reduced steam export, or in an existing hydrogen plant where the hydrogen capacity can be increased by as much as 20–30 percent with reduced export of steam from the hydrogen plant.
21 Citations
19 Claims
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1. A process for preparing syngas, comprising:
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partially oxidizing a first hydrocarbon portion with oxygen in a partial oxidation reactor to produce a first reactor effluent; cooling the first reactor effluent to a temperature from 650°
to 1000°
C., said cooling including direct heat exchange with water introduced into the first reactor effluent as a quench fluid;supplying the cooled first reactor effluent to a reforming exchanger; passing a second hydrocarbon portion with steam through a catalyst zone in the reforming exchanger to form a second reactor effluent, wherein the first and second hydrocarbon portions are supplied in a weight ratio of from 40;
60 to 60;
40;discharging the second reactor effluent from the catalyst zone to form an admixture with the first reactor effluent; passing the admixture across the catalyst zone in indirect heat exchange therewith to cool the admixture and heat the catalyst zone; and collecting the cooled admixture from the reforming exchanger. - View Dependent Claims (2, 3, 4, 5, 6, 7, 9, 10, 11, 17, 18, 19)
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8. An apparatus for producing syngas, comprising:
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partial oxidation reactor means for partially oxidizing a first hydrocarbon portion with oxygen to produce a first reactor effluent; means for cooling the first reactor effluent to a temperature from 650°
to 1000°
C., said cooling means including means for introducing water into the first reactor effluent as a quench fluid for direct heat exchange;means for supplying the cooled first reactor effluent to a reforming exchanger; means for passing a second hydrocarbon portion with steam through a catalyst zone in the reforming exchanger to form a second reactor effluent, wherein the first and second hydrocarbon portions are supplied in a weight ratio of from 40;
60 to 60;
40;means for discharging the second reactor effluent from the catalyst zone to form an admixture with the first reactor effluent; means for passing the admixture across the catalyst zone in indirect heat exchange therewith to cool the admixture and heat the catalyst zone; means for collecting the cooled admixture from the reforming exchanger; and means for shift converting the collected admixture to increase hydrogen content.
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12. A process for preparing a hydrogen-rich syngas, comprising:
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partially oxidizing a first hydrocarbon portion with oxygen in a non-catalytic partial oxidation reactor to produce a first reactor effluent having a temperature greater than 1000°
C.;cooling the first reactor effluent to a temperature from 650°
to 1000°
C.;said cooling including; direct heat exchange with water introduced into the first reactor effluent as a quench fluid; and indirect heat exchange in a cross exchange downstream from the direct heat exchange and upstream from the reforming exchanger comprising heating the second hydrocarbon portion upstream from the catalyst zone; supplying the cooled first reactor effluent to a reforming exchanger; passing a second hydrocarbon portion with steam through a catalyst zone in the reforming exchanger to form a second reactor effluent, wherein the first and second hydrocarbon portions are supplied in a weight ratio of from 40;
60 to 60;
40;discharging the second reactor effluent from the catalyst zone to form an admixture with the first reactor effluent; passing the admixture across the catalyst zone in indirect heat exchange therewith to cool the admixture and heat the catalyst zone; and collecting the cooled admixture from the reforming exchanger. - View Dependent Claims (13, 14, 15, 16)
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Specification