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US3852216A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing coarse particles of active carbon in a fluidized bed with added inert particles

Assignee: Takeda Pharmaceutical Co Ltd
•
Filing: 1972-08-31
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Granted: 1974-12-03
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Expires: 1992-08-31
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Abstract

Abstract Process for producing coarse particles of active carbon having an average particle size of 2 to 20 mm by means of a fluidized bed in a reactor in which particles of carbon or carbonaceous material are mixed with a finely powdered inert material having a preferable particle size of 0.08 to 1.0 mm and caused to move upward at low speed by passing a high temperature gas containing steam through the mixture forming the fluidized bed, thereby to obtain activation of the carbonization of the carbon particles with good effect.

Inventors

  • 👤 N Ninomiya
  • 👤 D Kunii

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 04:57
CPC Classifications
C; C01; C01B; C01B32/00; C01B32/30; C01B32/354; C01B32/36; C01B32/366

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 262 words
A PROCESS FOR PRODUCING COARSE PARTICLES OF ACTIVE CARBON WHICH CONSISTS ESSENTIALLY OF CONTINOUSLY SUPPLYING TO A FLUIDIZED BED, PARTICLES OF CARBON OR A CARBONACEOUS MATERIAL FROM THE GROUP CONSISTING OF COKE, CHARCOAL, AND COAL HAVING AN AVERAGE PARTICLE SIZE OF 2 TO 20 MM WITH A FINELY POWDERED INERT MATERIAL HAVING A PARTICLE SIZE OF FROM 0.05 TO 2.0 MM, WHICH INERT MATERIAL DOES NOT INTERFERE WITH THE REACTION AND CAN BE READILY SEPARATED FROM THE ACTIVE CARBON THUSPRODUCED, SAID INET MATERIAL BEING PRESENT IN AN AMOUNT OF 1 TO 4 TIMES BY VOLUME OF THE CARBON OR CARBONACEOUS PARTICLES, INTRODUCING A COMBUSTION GAS, A WASTE GAS OR A HOT WASTE GAS OF A TEMPERATURE WITHIN THE RANGE OF 600* TO 20000*C CONTAINING 20 TO 80 PERCENT BY VOLUME OF STEAM INTO THE MIXTURE OF PARTICLES AND INERT MATERIAL SO AS TO EXECUTE THE ACTIVATION OR THE CARBONIZATION AND ACTIVATION OF SAID PARTICLES WHILE THE MIXTURE IS FORMING A FLUIDIZED BED IN THE REACTOR, TAKING OUT THE PRODUCED COARSE PARTICLES OF ACTIVE CARBON TOGETHER WITH THE INERT MATERIAL FROM THE REACTOR, SEPARATING THE PRODUCED COARSE PARTICLES OF ACTIVE CARBON FROM THE INERT MATERIAL, AND RECYCLING SAID INERT PARTICLES TO SAID FLUIDIZED BED; AND WHEREIN IN SAID PROCESS BOTH THE PARTICLES OF CARBON OR CARBONACEOUS MATERIAL AND THE INERT MATERIAL ARE INTRODUCED TO THE LOWER PORTION OF THE FLUIDIZED BED AND TAKEN OUT FROM THE UPPER PORTION OF THE FLUIDIZED BED TO THE OUTSIDE WHILE THE GAS FLOWS TO PASS THROUGH THE FLUIDIZED BED FROM THE LOWER PORTION TO THE UPPER PORTION.
Claim 2
Dependent Claim 262 words
A PROCESS FOR PRODUCING COARSE PARTICLES OF ACTIVE CARBON WHICH CONSISTS ESSENTIALLY OF CONTINOUSLY SUPPLYING TO A FLUIDIZED BED, PARTICLES OF CARBON OR A CARBONACEOUS MATERIAL FROM THE GROUP CONSISTING OF COKE, CHARCOAL, AND COAL HAVING AN AVERAGE PARTICLE SIZE OF 2 TO 20 MM WITH A FINELY POWDERED INERT MATERIAL HAVING A PARTICLE SIZE OF FROM 0.05 TO 2.0 MM, WHICH INERT MATERIAL DOES NOT INTERFERE WITH THE REACTION AND CAN BE READILY SEPARATED FROM THE ACTIVE CARBON THUSPRODUCED, SAID INET MATERIAL BEING PRESENT IN AN AMOUNT OF 1 TO 4 TIMES BY VOLUME OF THE CARBON OR CARBONACEOUS PARTICLES, INTRODUCING A COMBUSTION GAS, A WASTE GAS OR A HOT WASTE GAS OF A TEMPERATURE WITHIN THE RANGE OF 600* TO 20000*C CONTAINING 20 TO 80 PERCENT BY VOLUME OF STEAM INTO THE MIXTURE OF PARTICLES AND INERT MATERIAL SO AS TO EXECUTE THE ACTIVATION OR THE CARBONIZATION AND ACTIVATION OF SAID PARTICLES WHILE THE MIXTURE IS FORMING A FLUIDIZED BED IN THE REACTOR, TAKING OUT THE PRODUCED COARSE PARTICLES OF ACTIVE CARBON TOGETHER WITH THE INERT MATERIAL FROM THE REACTOR, SEPARATING THE PRODUCED COARSE PARTICLES OF ACTIVE CARBON FROM THE INERT MATERIAL, AND RECYCLING SAID INERT PARTICLES TO SAID FLUIDIZED BED; AND WHEREIN IN SAID PROCESS BOTH THE PARTICLES OF CARBON OR CARBONACEOUS MATERIAL AND THE INERT MATERIAL ARE INTRODUCED TO THE LOWER PORTION OF THE FLUIDIZED BED AND TAKEN OUT FROM THE UPPER PORTION OF THE FLUIDIZED BED TO THE OUTSIDE WHILE THE GAS FLOWS TO PASS THROUGH THE FLUIDIZED BED FROM THE LOWER PORTION TO THE UPPER PORTION.
Claim 3
Dependent Claim 53 words
A process according to claim 1 wherein the carbon or carbonaceous material is selected from the group consisting of coconut shell charcoal, sawdust charcoal, charcoal, coke and anthracite coal and wherein the inert material is selected from the group consisting of alumina, silica, silica-alumina, a thermostable metal oxide, sodium chloride and potassium chloride.
Claim 4
Dependent Claim 29 words
A process according to claim 1 wherein the gas is a combustion gas obtained from the combustion of heavy oil, kerosene, natural gaS, coal, tar, tar oil and sawdust.
Claim 5
Dependent Claim 20 words
A process according to claim 1 wherein the inert material has a particle size of from 0.08 to 1.0 mm.

References Cited (Backward Citations)

GB704810A Cited
DE1119238B Cited
US3565827A Cited
US3541025A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1977-12-02 1978-06-03 1978-12-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1981-12-02 1982-06-03 1982-12-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1985-12-02 1986-06-03 1986-12-03 $7700.00 Window Closed / Lapsed

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