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US3864277A Expired / Lapsed US ⏱️ 0.0 years remaining

Hard granular activated carbon and preparation from a carbonaceous material a binder and an inorganic activating agent

Assignee: North American Carbon Inc
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Filing: 1972-08-14
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Granted: 1975-02-04
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Expires: 1992-08-14
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Abstract

Abstract A method of manufacturing reconstituted activated carbon by employing chemical activation of a novel mixture of a carbonaceous raw material and a carbonaceous binder material and an activating agent to produce a very hard, granular activated carbon with superior abrasion-resistance.

Inventors

  • 👤 Julius Louis Kovach

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 21:59
CPC Classifications
C; C01; C01B; C01B32/00; C01B32/30; C01B32/354; C01B32/384

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 202 words
A chemical activation process for the manufacture of granular activated carbon comprising the steps of forming a mixture having a consistency permitting the pelleting of granular shaped particles including the following: a ground solid raw carbonaceous starting material possessing an oxygen content of at least approximately 25 percent by weight on a moisture and ash free basis taken from a group consisting of wood, straw and low-rank brown coals, a carbonaceous binder material taken from a group consisting of lignosulphonates and polyvinyl alcohols which are soluble or emulsifiable in water or phosphoric acid solutions, the amount of the binder material being sufficient to contribute at least approximately 24 percent by weight of the total carbon present in the initial mixture formed, and an amount of phosphoric acid sufficient to form a ratio of 100 percent phosphoric acid to the dry basis mixture of the starting material and the binder material of at least 0.35 to 1; forming solid grnaular shaped particles of predetermined size from said mixture; heat treating said shaped particles for a predetermined time at a temperature no greater than approximately 650*C to form a granular activated carbon product having a ball-pan hardness value of approximately 85 percent or greater.
Claim 2
Dependent Claim 202 words
A chemical activation process for the manufacture of granular activated carbon comprising the steps of forming a mixture having a consistency permitting the pelleting of granular shaped particles including the following: a ground solid raw carbonaceous starting material possessing an oxygen content of at least approximately 25 percent by weight on a moisture and ash free basis taken from a group consisting of wood, straw and low-rank brown coals, a carbonaceous binder material taken from a group consisting of lignosulphonates and polyvinyl alcohols which are soluble or emulsifiable in water or phosphoric acid solutions, the amount of the binder material being sufficient to contribute at least approximately 24 percent by weight of the total carbon present in the initial mixture formed, and an amount of phosphoric acid sufficient to form a ratio of 100 percent phosphoric acid to the dry basis mixture of the starting material and the binder material of at least 0.35 to 1; forming solid grnaular shaped particles of predetermined size from said mixture; heat treating said shaped particles for a predetermined time at a temperature no greater than approximately 650*C to form a granular activated carbon product having a ball-pan hardness value of approximately 85 percent or greater.
Claim 3
Dependent Claim 16 words
The process defined in claim 1 wherein said solid raw starting material is ground wood flour.
Claim 4
Dependent Claim 61 words
The method defined in claim 1 including proportioning the amounts of said raw carbonaceous material and said carbonaceous binder material in the mixture to achieve a contribution of carbon in the initial mixture by the binder material of at least approximately 28 percent by weight to achieve a ball pan hardness value of the end product of at least 90 percent.
Claim 5
Dependent Claim 186 words
A granular activated carbon product having a ball pan hardness value of at least 85 and formed by a process comprising the steps of forming a mixture having a consistency permitting the pelleting of solid granular shaped particles comprising a ground naturally occurring carbonaceous starting material possessing an oxygen content of at least 25 percent by weight on a moisture and ash free basis taken from a group consisting of wood, straw and low-rank brown coals, a binder material taken from a group consisting of lignosulphonates and polyvinyl alcohols which are soluble or emulsifiable in water or solutions of phosphoric acid, the amount of said binder material being sufficient to contribute at least approximately 24 percent by weight of the total carbon present, and phosphoric acid in a ratio of 100 percent phosphoric acid to the dry basis total of the starting material and the binder of at least 0.35 to 1; forming granular pellets from said mixture of predetermined size and shape; and heating said formed pellets at a temperature effective to simultaneously carbonize and activate said pellets to form said activAted granular carbon product.
Claim 6
Dependent Claim 186 words
A granular activated carbon product having a ball pan hardness value of at least 85 and formed by a process comprising the steps of forming a mixture having a consistency permitting the pelleting of solid granular shaped particles comprising a ground naturally occurring carbonaceous starting material possessing an oxygen content of at least 25 percent by weight on a moisture and ash free basis taken from a group consisting of wood, straw and low-rank brown coals, a binder material taken from a group consisting of lignosulphonates and polyvinyl alcohols which are soluble or emulsifiable in water or solutions of phosphoric acid, the amount of said binder material being sufficient to contribute at least approximately 24 percent by weight of the total carbon present, and phosphoric acid in a ratio of 100 percent phosphoric acid to the dry basis total of the starting material and the binder of at least 0.35 to 1; forming granular pellets from said mixture of predetermined size and shape; and heating said formed pellets at a temperature effective to simultaneously carbonize and activate said pellets to form said activAted granular carbon product.
Claim 7
Dependent Claim 61 words
The method defined in claim 5 including proportioning the amounts of said raw carbonaceous material and said carbonaceous binder material in the mixture to achieve a contribution of carbon in the initial mixture of the binder material of at least approximately 28 percent by weight to achieve a ball pan hardness value of the end product of at least 90 percent.

References Cited (Backward Citations)

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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) 1978-02-03 1978-08-05 1979-02-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-02-03 1982-08-05 1983-02-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-02-03 1986-08-05 1987-02-04 $7700.00 Window Closed / Lapsed

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