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US4139416A Expired / Lapsed US ⏱️ 0.0 years remaining

Carbonaceous material with high characteristics of surface area and activity and process for producing the same

Assignee: Centro Sperimentale Metallurgico SpA
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Filing: 1977-08-01
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Granted: 1979-02-13
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Expires: 1997-08-01
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Abstract

Abstract A carbonaceous material with high characteristics of surface area and activity is produced in a continuous process by heating and drying ground pit coal at 200 to 300° C. for 15 to 120 minutes in air, and then heating in two further stages in fluidized bed reactors. The first of these further stages is 400 to 600° C. for 10 to 60 minutes while the second is 800 to 1100° C. for 10 to 60 minutes. Tar is condensed from the offgases of the first further stage and the residual gas is divided and 10 to 95% recycled to the first further stage. Similarly, 10 to 95% of the off-gases from the second further stage are recycled.

Inventors

  • 👤 Luigi Palumbo
  • 👤 Angelo Colletta

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 08:49
CPC Classifications
C; C10; C10B; C10B49/00; C10B49/02; C10B49/04; C10B49/08; C10B49/10; C01; C01B; C01B32/00; C01B32/30; C01B32/312; C01B32/336; C21; C21B; C21B13/00; C21B13/0066; C21C; C21C7/00; Y; Y02; Y02P; Y02P10/00; Y02P10/10; Y02P10/134; Y02P10/20

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 384 words
A continuous process for the production of carbonaceous material with high properties of surface area, porosity and surface activity, comprising grinding pit coal, drying and heating the ground coal in a first stage at a temperature of 200° to 300° C. for 15 to 120 minutes by fluidizing the ground coal with gas consisting essentially of 50 to 100% by volume air, 0 to 50% by volume steam and 0 to 50% by volume nitrogen in addition to that present in said air thereby to produce a dried and heated material; heating said material by fluidization in a second heating stage with a fluidizing gas that is initially 0 to 20% by volume air, 0 to 50% by volume steam, and 50 to 100% by volume nitrogen in addition to that present in any supplied air, at 400° to 600° C. for 10 to 60 minutes, thereby to produce a further heated material and off-gases; cooling said off-gases to produce condensed tar and residual gases; passing the further heated material from said second heaating stage to a third heating stage, still further heating the material by fluidization in said third heating stage with a fluidizing gas that is initially 0 to 70% by volume air and 30 to 100% nitrogen in addition to that present in any supplied air, at 800° to 1100° C. for 10 to 60 minutes with the production of off-gases; recycling to said second heating stage as fluidizing gas 10 to 95% by volume of said residual gases; recycling to said third heating stage as fluidizing gas 10 to 95% by volume of said off-gases from said third heating stage; replacing said fluidizing gases in said second and third heating stages substantially entirely with said recycled residual gases and off-gases, respectively, by the time said process is fully on-steam; and cooling said still further heated material below a temperature of 100° C. to produce a particulate carbonaceous material having the following properties: ______________________________________ average size of the particles 0.4 to 3.0 mm lump density 0.20 to 0.76 g/cm.sup.3 composition in per cent by weight: volatile matter 1.0 - 3.0 ash 6.0 - 12.0 total sulphur 0.2 - 1.0 carbon 80 - 90 hydrogen 1.0 - 2.0 heat value 6000 - 8000 kcal/kg surface area 30 - 300 m.sup.2 /g. ______________________________________
Claim 2
Dependent Claim 384 words
A continuous process for the production of carbonaceous material with high properties of surface area, porosity and surface activity, comprising grinding pit coal, drying and heating the ground coal in a first stage at a temperature of 200° to 300° C. for 15 to 120 minutes by fluidizing the ground coal with gas consisting essentially of 50 to 100% by volume air, 0 to 50% by volume steam and 0 to 50% by volume nitrogen in addition to that present in said air thereby to produce a dried and heated material; heating said material by fluidization in a second heating stage with a fluidizing gas that is initially 0 to 20% by volume air, 0 to 50% by volume steam, and 50 to 100% by volume nitrogen in addition to that present in any supplied air, at 400° to 600° C. for 10 to 60 minutes, thereby to produce a further heated material and off-gases; cooling said off-gases to produce condensed tar and residual gases; passing the further heated material from said second heaating stage to a third heating stage, still further heating the material by fluidization in said third heating stage with a fluidizing gas that is initially 0 to 70% by volume air and 30 to 100% nitrogen in addition to that present in any supplied air, at 800° to 1100° C. for 10 to 60 minutes with the production of off-gases; recycling to said second heating stage as fluidizing gas 10 to 95% by volume of said residual gases; recycling to said third heating stage as fluidizing gas 10 to 95% by volume of said off-gases from said third heating stage; replacing said fluidizing gases in said second and third heating stages substantially entirely with said recycled residual gases and off-gases, respectively, by the time said process is fully on-steam; and cooling said still further heated material below a temperature of 100° C. to produce a particulate carbonaceous material having the following properties: ______________________________________ average size of the particles 0.4 to 3.0 mm lump density 0.20 to 0.76 g/cm.sup.3 composition in per cent by weight: volatile matter 1.0 - 3.0 ash 6.0 - 12.0 total sulphur 0.2 - 1.0 carbon 80 - 90 hydrogen 1.0 - 2.0 heat value 6000 - 8000 kcal/kg surface area 30 - 300 m.sup.2 /g. ______________________________________
Claim 3
Dependent Claim 24 words
A method as claimed in claim 1, in which said residual gas recycled to said second heating stage is about 95% by volume thereof.
Claim 4
Dependent Claim 25 words
A process as claimed in claim 1, in which said off-gas recycled to said third heating stage is equal to about 70% by volume thereof.

References Cited (Backward Citations)

US3086923A Cited
US2815316A Cited
US3140241A Cited
US3184397A Cited
US3051628A Cited
US3375175A Cited
US3444046A Cited
US3414480A Cited
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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) 1982-02-12 1982-08-14 1983-02-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-02-12 1986-08-14 1987-02-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-02-12 1990-08-14 1991-02-13 $7700.00 Window Closed / Lapsed

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