US4865624A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for steam reforming methanol and a system therefor
Assignee: Taiyo Nippon Sanso Corp
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Filing: 1988-06-28
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Granted: 1989-09-12
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Expires: 2008-06-28
Abstract
Abstract The present invention relates to a steam reforming method of methanol for obtaining hydrogen gas and a system therefor. The present method and present system utilizes a heat transfer medium for regulating the temperature at each step of the process. By optimizing the flow so that the heat transfer medium circulate through the system as heat-exchanging with reactant at each step, temperature of the reactant is regulated at a desirable temperature for proceeding the reaction. Temperature of the decomposition process and the conversion process of methanol is independently regulated.
Inventors
- 👤 Hidetake Okada
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 18:16
CPC Classifications
C; C01; C01B; C01B3/00; C01B3/02; C01B3/22; C01B3/32; C01B3/323; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
214 words
A method for steam reforming methanol to produce a product mixture containing hydrogen comprising the step of heating a methanol-water mixture to form a methanol-steam mixture, wherein the heating step includes a preheating process, a vaporizing process, and a superheating process, and a step of reacting the mixture in the presence of a catalyst for producing hydrogen, wherein the reaction step includes a decomposition process and a conversion process, and wherein the method further comprises: (a) heating the heat transfer medium; (b) feeding a portion of the heated heat transfer medium to the decomposition process and feeding another portion of the heated transfer medium to the superheating process, for indirect heat-exchanging with the methanol-steam mixture; (c) merging the portion of the heat transfer medium from the superheating process with the portion of the heat transfer medium from the decomposition process; (d) feeding the merged portions of the heat transfer medium from the decomposition process and the superheating process to the vaporizing process for indirect heat-exchanging with the methanol-steam mixture; (e) leading a portion of the heat transfer medium from the vaporizing process for re-heating thereof, leading another portion of the heat transfer medium from the vaporizing process to the preheating process and then to the conversion process, and combining the two portions for re-heating.
Claim 2
Independent Claim
214 words
A method for steam reforming methanol to produce a product mixture containing hydrogen comprising the step of heating a methanol-water mixture to form a methanol-steam mixture, wherein the heating step includes a preheating process, a vaporizing process, and a superheating process, and a step of reacting the mixture in the presence of a catalyst for producing hydrogen, wherein the reaction step includes a decomposition process and a conversion process, and wherein the method further comprises: (a) heating the heat transfer medium; (b) feeding a portion of the heated heat transfer medium to the decomposition process and feeding another portion of the heated transfer medium to the superheating process, for indirect heat-exchanging with the methanol-steam mixture; (c) merging the portion of the heat transfer medium from the superheating process with the portion of the heat transfer medium from the decomposition process; (d) feeding the merged portions of the heat transfer medium from the decomposition process and the superheating process to the vaporizing process for indirect heat-exchanging with the methanol-steam mixture; (e) leading a portion of the heat transfer medium from the vaporizing process for re-heating thereof, leading another portion of the heat transfer medium from the vaporizing process to the preheating process and then to the conversion process, and combining the two portions for re-heating.
Claim 3
Dependent Claim
33 words
A method of steam reforming methanol according to claim 1 which further comprises the steps of mixing methanol and water, to form the methanol-water mixture, and separating the hydrogen from the product mixture.
Claim 4
Dependent Claim
54 words
A method of steam reforming methanol according to claim 2 wherein the step of separating hydrogen includes the steps of: (a) cooling the product mixture containing hydrogen; (b) separating the product mixture into a gas stream containing hydrogen and a liquid stream containing water; and (c) adsorptively separating the hydrogen from the gas stream.
Claim 5
Dependent Claim
37 words
A method of steam reforming methanol according to claim 3 which further comprises the steps of: (a) recovering the liquid stream containing water from the separating step; and (b) recycling said liquid stream to the mixing step.
Claim 6
Dependent Claim
29 words
A method of steam reforming methanol according to claim 1 wherein the proportion of methanol and water in the methanol-water mixture is between 1.0 to 1.5 by gram molecule.
Claim 7
Dependent Claim
39 words
A method of steam reforming methanol according to claim 1 wherein a catalytic material having palladium and silica therein, and a catalytic material having copper therein are used as catalysts in the decomposition process and the conversion process, respectively.
Claim 8
Dependent Claim
32 words
A method of steam reforming methanol according to claim 1 wherein the amount of heat transfer medium circulated is sufficient to maintain reaction temperatures in the decomposition process and the conversion process.
Claim 9
Independent Claim
244 words
A system for producing hydrogen by a steam reforming method, the system comprising (i) reformer means having a decomposition part and a conversion part for performing decomposition of a methanol-steam mixture to produce intermediate products and for converting the intermediate products to produce hydrogen, respectively; and (ii) heat exchanger means having a preheating part for preheating a liquid mixture of methanol and water, a vaporizing part for vaporizing the preheated mixture, and a superheating part for superheating the vaporized mixture; wherein the system further comprises: (a) heating means for heating a heat transfer medium; and (b) feeding means for feeding the heat transfer medium through the reformer means and the heat exchanger means, and arranged such that a portion of the heat transfer medium is led to the decomposition part of the reformer means and another portion of the heat transfer medium is led to the superheating part of the heat exchanger means for regulating the temperature thereof; the portions of the heat transfer medium from the decomposition part and the superheating part are led to the vaporizing part of the heat exchanger means to regulate the temperature thereof; and a portion of the heat transfer medium from the vaporizing part is led directly to the heater means and another portion of the heat transfer medium from the vaporizing part is led to the heater means after circulating through the preheating part of the heat exchanger and the conversion part of the reformer means.
Claim 10
Independent Claim
244 words
A system for producing hydrogen by a steam reforming method, the system comprising (i) reformer means having a decomposition part and a conversion part for performing decomposition of a methanol-steam mixture to produce intermediate products and for converting the intermediate products to produce hydrogen, respectively; and (ii) heat exchanger means having a preheating part for preheating a liquid mixture of methanol and water, a vaporizing part for vaporizing the preheated mixture, and a superheating part for superheating the vaporized mixture; wherein the system further comprises: (a) heating means for heating a heat transfer medium; and (b) feeding means for feeding the heat transfer medium through the reformer means and the heat exchanger means, and arranged such that a portion of the heat transfer medium is led to the decomposition part of the reformer means and another portion of the heat transfer medium is led to the superheating part of the heat exchanger means for regulating the temperature thereof; the portions of the heat transfer medium from the decomposition part and the superheating part are led to the vaporizing part of the heat exchanger means to regulate the temperature thereof; and a portion of the heat transfer medium from the vaporizing part is led directly to the heater means and another portion of the heat transfer medium from the vaporizing part is led to the heater means after circulating through the preheating part of the heat exchanger and the conversion part of the reformer means.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-09-11 | 1993-03-13 | 1993-09-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-09-11 | 1997-03-13 | 1997-09-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-09-11 | 2001-03-13 | 2001-09-12 | $7700.00 | Window Closed / Lapsed |