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Steam Generating Slurry Gasifier for the Catalytic Gasification of a Carbonaceous Feedstock

Inactive Publication Date: 2009-07-02
SURE CHAMPION INVESTMENT LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0008]In a fourth aspect, a process is provided for converting a carbonaceous material into a first plurality of gases comprising methane and one or more of hydrogen, carbon monoxide, carbon dioxide, hydrogen sulfide, ammonia and other higher hydrocarbons, the process comprising the steps of: providing a gasifier apparatus having a fluidized bed gasifier and a slurry gasifier according to the first aspect; supplying a particulate composition comprising a carbonaceous material and a gasification catalyst to the fluidized bed gasifier, wherein the gasification catalyst, in the presence of steam and under suitable temperature and pressure, exhibits gasification activity whereby the first plurality of gases is formed; supplying an aqueous carbonaceous slurry, enriched oxygen gas and optionally a syngas to the slurry gasifier; reacting the aqueous carbonaceous slurry in the slurry gasifier in the presence of oxygen and under suitable temperature and pressure so as to generate a second plurality of gases comprising steam, hydrogen and carbon monoxide; introducing the second plurality of gases into the fluidized bed gasifier; reacting the particulate composition in the fluidized bed gasifier in the presence of the second plurality of gases, and under suitable temperature and pressure, to form the first plurality of gases; and at least partially separating the first plurality of gases to produce a stream comprising a predominant amount of one of the gases in the first plurality of gases, wherein the gasification catalyst comprises a source of at least one alkali metal and is present in an amount sufficient to provide, in the particulate composition, a ratio of alkali metal atoms to carbon atoms ranging from about 0.01 to about 0.08; and the aqueous carbonaceous slurry comprises a mixture of carbonaceous material and water at a weight ratio ranging from about 5:95 to about 60:40.

Problems solved by technology

Such methods have the disadvantages of requiring an additional fuel source for the boiler, while producing an exhaust comprising additional acid gases (e.g, carbon dioxide, sulfur dioxide, nitrous oxides), which must be treated and exhausted to the atmosphere or otherwise sequestered.

Method used

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  • Steam Generating Slurry Gasifier for the Catalytic Gasification of a Carbonaceous Feedstock
  • Steam Generating Slurry Gasifier for the Catalytic Gasification of a Carbonaceous Feedstock
  • Steam Generating Slurry Gasifier for the Catalytic Gasification of a Carbonaceous Feedstock

Examples

Experimental program
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Effect test

example 1

[0079]Catalyzed and Slurry Feedstock Preparation

[0080]As-received coal (Powder River Basin) can be stage-crushed to maximize the amount of material having particle sizes ranging from about 0.85 to about 1.4 mm. Fines (<0.85 mm) can be separated from the crushed materials by vibratory screening and directed for preparation of the slurry feedstock.

[0081]The crushed coal can be slurried with an aqueous solution of potassium carbonate, dewatered, and dried via a fluid bed slurry drier to yield a catalyzed feedstock containing 185 lb coal (88 wt %), 14.9 lb catalyst (7 wt %), and 10.5 lb moisture (5 wt %). The coal fines separated at the crushing stage can be slurried with water to a composition of 75 wt % water (263 lb) and 25 wt % coal fines (88 lb) by weight and subsequently can be used as the slurry feedstock for the slurry gasifier.

example 2

[0082]Catalytic Gasification

[0083]The slurry feedstock of Example 1 can be provided to a fluidized bed gasification reactor (slurry gasifier) fed by an enriched oxygen source (96 lb / hr) and a syngas source (17.7 w % H2, 82.3% CO; 75.48 lb / hr). Typical gasification conditions for the slurry gasifier would be: total pressure 550 psi, and temperature, 1700-1900° F.; char would be generated at a rate of 12.1 lb / hr.

[0084]The resulting exhaust (561.6 lb / hr) from the slurry gasifier would contain steam (277.5 lb / hr), hydrogen (12.89 lb / hr), CO (62.27 lb / hr), CO2 (187.84 lb / hr) and methane (11.06 lb / hr), and could be provided to a second fluidized bed gasification reactor (catalytic gasifier) supplied with the catalyzed feedstock (210 lb / hr) of Example 1. The catalyzed feedstock would be introduced under a positive pressure of nitrogen (45.8 lb / hr). Typical conditions for the catalytic gasifier would be: total pressure, 500 psi and temperature, 1200° F. The effluent of the catalytic gasifie...

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Abstract

Steam generating gasification reactors for providing high-pressure and high-temperature steam for catalytic gasification of a carbonaceous feedstock can be based on oxygen blown gasification reactors adapted for processing a slurry feedstock comprising at least 40% water. The exhaust from the slurry gasifier comprises at least steam, carbon monoxide and hydrogen. The slurry composition and the oxygen to fuel ratio can be varied to control the ratio of carbonaceous gases in the generator exhaust. By directing substantially all of exhaust gases produced from the slurry gasification reactor through the catalytic gasifier and subsequent gas separation and sequestration processes, a greatly higher energy efficiency and decreased carbon footprint can be realized.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS[0001]This application claims priority under 35 U.S.C. §119 from U.S. Provisional Application Ser. No. 61 / 017,321 (filed Dec. 28, 2007), the disclosure of which is incorporated by reference herein for all purposes as if fully set forth.FIELD OF THE INVENTION[0002]The present invention relates to a steam generating slurry gasifier which produces steam and synthesis gas from an aqueous carbonaceous feed slurry. Further, the invention relates to processes for preparation gaseous products, and in particular, methane via the catalytic gasification of carbonaceous feedstocks in the presence of steam and synthesis gas generated by the slurry gasifier.BACKGROUND OF THE INVENTION[0003]In view of numerous factors such as higher energy prices and environmental concerns, the production of value-added gaseous products from lower-fuel-value carbonaceous feedstocks, such as petroleum coke and coal, is receiving renewed attention. The catalytic gasification of...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C10J3/60
CPCC10J3/463C10L3/102C10J3/82C10J2300/0903C10J2300/093C10J2300/094C10J2300/0943C10J2300/0959C10J2300/0973C10J2300/0986C10J2300/1807C10J2300/1823C10J2300/1846C10J2300/1853C10J2300/1884C10K1/004C10K1/101C10K1/122C10K1/143C10K1/16C10K1/165C10K3/02C10L3/08C10J3/721
Inventor LAU, FRANCIS S.ROBINSON, EARL T.
Owner SURE CHAMPION INVESTMENT LTD
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