Method for producing and regenerating a synthetic CO.sub.2 acceptor

Lancet, Michael S; Curran, George P; Gorin, Everett

Title: Method for producing and regenerating a synthetic CO.sub.2 acceptor

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Abstract

A method for producing a synthetic CO.sub.2 acceptor by feeding a mixture of finely divided silica and at least one finely divided calcium compound selected from the group consisting of calcium oxide and calcium carbonate to a fluidized bed; operating the fluidized bed at suitable conditions to produce pellets of synthetic CO.sub.2 acceptor and recovering the pellets of synthetic CO.sub.2 acceptor from the fluidized bed. Optionally, spent synthetic CO.sub.2 acceptor can be charged to the fluidized bed to produce regenerated pellets of synthetic CO.sub.2 acceptor.

Inventors:

Lancet, Michael S ^[1]; Curran, George P ^[1]; Gorin, Everett ^[2]

Pittsburgh, PA
San Rafael, CA

Issue Date:: 1982-01-01

Research Org.:: Conoco Coal Development Co., Library, PA

OSTI Identifier:: 864212

Patent Number(s):: 4330430

Assignee:: Conoco Inc. (Stamford, CT)

Patent Classifications (CPCs):: B - PERFORMING OPERATIONS B01 - PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL B01J - CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY

C - CHEMISTRY C10 - PETROLEUM, GAS OR COKE INDUSTRIES C10J - PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES

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B - PERFORMING OPERATIONS B01 - PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL B01J - CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY
B01J20/3433 - {of sorbents or filter aids other than those covered by B01J20/3408 - B01J20/3425}
B01J20/3204 - {Inorganic carriers, supports or substrates}
B01J20/103 - {comprising silica}

C - CHEMISTRY C10 - PETROLEUM, GAS OR COKE INDUSTRIES C10J - PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES
C10J3/54 - Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation

B - PERFORMING OPERATIONS B01 - PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL B01J - CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY
B01J20/041 - {Oxides or hydroxides}
B01J20/3236 - {containing metal, other than zeolites, e.g. oxides, hydroxides, sulphides or salts}
B01J20/3078 - {Thermal treatment, e.g. calcining or pyrolizing}

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DOE Contract Number:: EX-76-C-01-1734

Resource Type:: Patent

Country of Publication:: United States

Language:: English

Subject:: method; producing; regenerating; synthetic; acceptor; feeding; mixture; finely; divided; silica; calcium; compound; selected; consisting; oxide; carbonate; fluidized; bed; operating; suitable; conditions; produce; pellets; recovering; optionally; spent; charged; regenerated; compound selected; calcium oxide; fluidized bed; finely divided; calcium carbonate; calcium compound; suitable conditions; divided silica; /502/48/423/

Citation Formats


                    Lancet, Michael S, Curran, George P, and Gorin, Everett. Method for producing and regenerating a synthetic CO.sub.2 acceptor.  United States: N. p., 1982. 
        Web.

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                    Lancet, Michael S, Curran, George P, & Gorin, Everett. Method for producing and regenerating a synthetic CO.sub.2 acceptor.  United States.

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                    Lancet, Michael S, Curran, George P, and Gorin, Everett. Fri .  
        "Method for producing and regenerating a synthetic CO.sub.2 acceptor".  United States.  https://www.osti.gov/servlets/purl/864212.

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@article{osti_864212,

  title        = {Method for producing and regenerating a synthetic CO.sub.2 acceptor},

  author       = {Lancet, Michael S and Curran, George P and Gorin, Everett},

  abstractNote = {A method for producing a synthetic CO.sub.2 acceptor by feeding a mixture of finely divided silica and at least one finely divided calcium compound selected from the group consisting of calcium oxide and calcium carbonate to a fluidized bed; operating the fluidized bed at suitable conditions to produce pellets of synthetic CO.sub.2 acceptor and recovering the pellets of synthetic CO.sub.2 acceptor from the fluidized bed. Optionally, spent synthetic CO.sub.2 acceptor can be charged to the fluidized bed to produce regenerated pellets of synthetic CO.sub.2 acceptor.},

  doi          = {},

  journal      = {},
number       = ,

  volume       = ,

  place        = {United States},

  year         = {1982},

  month        = {1}

}

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