Process and apparatus for the production of methanol from condensed carbonaceous material

• US 5,344,848 A
• Filed: 05/27/1993
• Issued: 09/06/1994
• Est. Priority Date: 05/27/1993
• Status: Expired due to Term

• Current Assignee: Meyer Steinberg, Yuanji Dong
• Original Assignee: Meyer Steinberg, Yuanji Dong
• Inventors: Dong, Yuanji, Steinberg, Meyer
• Primary Examiner(s): MARS, HOWARD
• Application Number:
  US08/068,400
• Time in Patent Office: 467 Days
• Field of Search: 518/704
• US Class Current: 518/704
• CPC Class Codes: C07C 29/1518 one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
• CPC Class Codes: C07C 31/04 Methanol
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

An intergrated recycle process for the production of methanol from a process synthesis gas produced by hydrogasification of a condensed carbonaceous feedstock to produce a process gas which is reacted in a steam pyrolysis reactor with additional natural gas and steam to produce said synthesis gas containing hydrogen and carbon monoxide in more than a 2:1 molar ratio which constituents in turn are reacted in a methanol synthesis reactor to produce methanol. The important factor in this process includes the sequence of reactors of the condensed carbonaceous material: a hydrogasification reactor; the stream and natural gas pyrolysis reactor; the methanol synthesis reactor and the recycling to the hydrogasification reactor of the hydrogen-rich gas stream remaining after the methanol synthesis and separation of the methanol product.

Claims

1. An intergrated recycle process for the production of methanol from a condensed carbonaceous feedstock selected from the group consisting of coal, biomass, wood, agricultural products and municipal solid wastes comprising:

a) hydrogasifying said feedstock in a hydrogasification reactor with a recycled hydrogen rich gas stream to produce a process gas stream rich in methane;

b) steam pyrolyzing said process gas stream in a second stage steam pyrolysis reactor in the presence of a catalyst to produce a synthesis gas containing mainly carbon monoxide and hydrogen with small amounts of carbon dioxide;

c) reacting said carbon monoxide and hydrogen synthesis gas in a third stage methanol synthesis reactor in the presence of a catalyst to form a product gas stream containing methanol;

d) removing said methanol from said product gas stream leaving product gas stream rich in hydrogen; and

e) recycling said hydrogen rich product gas stream to supply the hydrogen needs for the above hydrogasifying step.

2. The process of claim 1 further comprising the steps of:

a) recovering thermal energy from synthesis gas stream exiting the steam pyrolysis reactor for use in the present process.

3. The process of claim 1 wherein the hydrogasifying step includes the introduction of steam into the hydrogasification reactor.

4. The process of claim 3 wherein the molar ratio of hydrogen to carbon monoxide in the said synthesis gas is greater than 2 to 1 and as high as 6 to 1.

5. The process of claim 1 wherein the steam pyrolysis reactor catalyst is a nickel based catalyst.

6. The process of claim 1 wherein the methanol synthesis reactor catalyst is a copper based catalyst.

7. The process of claim 1 wherein said hydrogasification reactor is operated at a temperature in the range of 700°

C. to 900°

C. and a pressure range of 10 atmosphere to 100 atmosphere.

8. The process of claim 1 wherein said steam pyrolysis reactor is operated at a temperature in the range of 900°

C. to 1200°

C. and a pressure range of 10 atmosphere and 100 atmosphere.

9. The process of claim 1 comprising the further steps of:

a) expanding the process gas stream produced by the hydrogasification reactor to decrease its pressure and temperature prior to pyrolyzing said process gas stream; and

b) compressing said synthesis gas stream to adjust the temperature and pressure thereof to that needed by the methanol synthesis reactor.

10. The process of claim 9 further comprises the step of purging the inert gases from the process.

11. The process of claim 10 further comprising the step of removing catalyst poisoning impurities from the process prior to feeding any reactants to the pyrolysis reactor.