GB977622A - Carbon black - Google Patents

Carbon black

Info

Publication number
GB977622A
GB977622A GB2461461A GB2461461A GB977622A GB 977622 A GB977622 A GB 977622A GB 2461461 A GB2461461 A GB 2461461A GB 2461461 A GB2461461 A GB 2461461A GB 977622 A GB977622 A GB 977622A
Authority
GB
United Kingdom
Prior art keywords
carbon black
furnace
gases
hood
pict
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB2461461A
Inventor
William Herman Balka
Rice Phillip Lynn
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Lynco Ltd Of Panama S A
Original Assignee
Lynco Ltd Of Panama S A
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Lynco Ltd Of Panama S A filed Critical Lynco Ltd Of Panama S A
Priority to GB2461461A priority Critical patent/GB977622A/en
Publication of GB977622A publication Critical patent/GB977622A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C1/00Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
    • C09C1/44Carbon
    • C09C1/48Carbon black
    • C09C1/50Furnace black ; Preparation thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Pigments, Carbon Blacks, Or Wood Stains (AREA)

Abstract

<PICT:0977622/C1/1> <PICT:0977622/C1/2> <PICT:0977622/C1/3> Carbon black is produced by introducing hydrocarbons and air into the lower end of a furnace having an upper end provided with a restricted opening, partially combusting the hydrocarbons in a combustion zone in said furnace so that the resultant gases pass upwards from said combustion zone through a cracking zone, to and through a hood in said furnace and adjusting the height of the hood so as to vary the volume of the cracking zone according to the desired carbon black particle size, withdrawing the combustion gases through the restricted opening and separating the carbon black from the gases. The temperature of the combustion zone may be 1800-2400 DEG F., of the cracking zone 2200 DEG -2600 DEG F. and in the hood 2600-3000 DEG F. The furnace 10 (see Fig. 2) has a burner 100 having a semi-cylindrical upper section 101 provided with a plurality of spaced parts 125, a semi-cylindrical lower section 102 and conduits extending into the burner through the lower section for introducing gases. The upper section 101 which has a greater radius of curvature than the lower has spaced parts 125 distributed over the whole surface except along the longitudinal side edge portions extending upwardly 5 degrees from the edges. Each of the parts has a straight bore portion 126 (see Fig. 5), whose diameter is preferably 8/10 th the thickness of the plates forming the upper section and whose length is 2/10 th the thickness. The upper flared portion 127 of each bore preferably has a radius of curvature which is 6/10 th the thickness of the plate. The hood is adjusted by winches 91 which are driven by an electric motor 90. A scraper blade 130 is mounted in the burner to remove any deposited carbon black. Liquid hydrocarbons, e.g. oil may be introduced through spray heads 175 supplied by inlets 176. In use the furnace is first preheated to 1800-2400 DEG F. by natural gas. Usually the ratio of air to gas is between 4 to 1 and 8 to 1. As the hood is raised, the size of the particles of carbon black increases. The mixture of carbon black and gases from the furnace 10 (see Fig. 1) is cooled in primary cooler 13 and then moved by fans 14 and 15 to cyclones 16 and secondary cooler 18. The carbon is separated and collected in bins 20 and 24 and the gases exhausted to the atmosphere. The carbon may be pulverized and pelletized and then conveyed to a sizing shaker screen 30, rejected pellets being moved by the blower 32 back to pelletizer 28.
GB2461461A 1961-07-07 1961-07-07 Carbon black Expired GB977622A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2461461A GB977622A (en) 1961-07-07 1961-07-07 Carbon black

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2461461A GB977622A (en) 1961-07-07 1961-07-07 Carbon black

Publications (1)

Publication Number Publication Date
GB977622A true GB977622A (en) 1964-12-09

Family

ID=10214448

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2461461A Expired GB977622A (en) 1961-07-07 1961-07-07 Carbon black

Country Status (1)

Country Link
GB (1) GB977622A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1989006260A1 (en) * 1988-01-11 1989-07-13 Columbian Chemicals Company Non-cylindrical reactor for carbon black production

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1989006260A1 (en) * 1988-01-11 1989-07-13 Columbian Chemicals Company Non-cylindrical reactor for carbon black production
US4927607A (en) * 1988-01-11 1990-05-22 Columbian Chemicals Company Non-cylindrical reactor for carbon black production
AU617710B2 (en) * 1988-01-11 1991-12-05 Columbian Chemicals Company Non-cylindrical reactor for carbon black production

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