GB303165A - - Google Patents

Info

Publication number
GB303165A
GB303165A GB38162/28A GB3816228A GB303165A GB 303165 A GB303165 A GB 303165A GB 38162/28 A GB38162/28 A GB 38162/28A GB 3816228 A GB3816228 A GB 3816228A GB 303165 A GB303165 A GB 303165A
Authority
GB
United Kingdom
Prior art keywords
mains
tar
gas
distillation
carbon content
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
GB38162/28A
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.)
Barrett Co Inc
Original Assignee
Barrett Co Inc
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 Barrett Co Inc filed Critical Barrett Co Inc
Publication of GB303165A publication Critical patent/GB303165A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10CWORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
    • C10C1/00Working-up tar
    • C10C1/04Working-up tar by distillation
    • C10C1/16Winning of pitch

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Working-Up Tar And Pitch (AREA)

Abstract

303,165. Barrett Co., (Assignees of Miller, S. P.). Dec. 29, 1927, [Convention date]. Condensing processes; pitch.-Three collector mains 3, 4, 5, are provided in coke oven or gas retort plant, valves 6, 7, 8, connecting each uptake 2 with any one of the mains. Ammonia liquor is sprayed into the uptakes through nozzles 18 and into the mains through nozzles 19. Tar condensing in each of the mains flows out to separate decanting tanks for removing ammonia liquor and is then pumped to one of three stills 32 which may also receive tar from condensers through which the gases pass after leaving the collector mains. A number of uptakes 48 open into the stills so that gas from a variable number of ovens can be intro. duced. The gas and oil vapour resulting from the distillation pass out through a pipe 55 to condensers. By collecting the gases from independently regulated early, intermediate or late periods of distillation in the respective mains, tars of low, intermediate or 'high free carbon content are obtained and these are separately distilled to provide the appropriate pitches and oils. Further, by employing the total gases from a selected number of ovens for distilling the respective tars, instead of utilizing gas at the appropriate stage of distillation of the fuel, the carbon content of the resulting pitches may be modified. The pitch obtained from the intermediate carbon tar may be blended with such tar or with tar of high or low carbon content. Specifications 289,378, 303,163 and 303,164 are referred to.
GB38162/28A 1927-12-29 1928-12-27 Expired GB303165A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US303165TA 1927-12-29 1927-12-29

Publications (1)

Publication Number Publication Date
GB303165A true GB303165A (en) 1930-03-27

Family

ID=31945832

Family Applications (1)

Application Number Title Priority Date Filing Date
GB38162/28A Expired GB303165A (en) 1927-12-29 1928-12-27

Country Status (1)

Country Link
GB (1) GB303165A (en)

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