US3599885A - Process for the treatment of coal to render it suitable for use in coke oven - Google Patents

Process for the treatment of coal to render it suitable for use in coke oven Download PDF

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US3599885A
US3599885A US771934A US3599885DA US3599885A US 3599885 A US3599885 A US 3599885A US 771934 A US771934 A US 771934A US 3599885D A US3599885D A US 3599885DA US 3599885 A US3599885 A US 3599885A
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coal
treatment
dust
surge bin
render
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US771934A
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Lewis Alderman
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Simon Carves Ltd
Carves Simon Ltd
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Carves Simon Ltd
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/08—Non-mechanical pretreatment of the charge, e.g. desulfurization
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/04—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition

Definitions

  • This invention relates to a process for the treatment of coal to render it suitable for use in coke ovens.
  • Such a process has disadvantages when applied 'to the conveying, storing and charging of dry or preheated coal in that the crushing means produce a larger amount of fine coal dust than is desirable thus creating dust nuisances at transfer points and explosive risks during storage.
  • the fine coal dust when introduced into the ovens, causes a significant amount of carryover into the gas-collecting main of the ovens.
  • An object of the present invention is to obviate or'mitigate the aforesaid disadvantages.
  • a process for the treatment of coal to render it suitable for use in coke ovens comprising the steps of thermally drying and heating coal of a size not greater than 1 inch, separating coal which is larger than required from the remainder-of the dried and heated coal, crushing the coal which is larger than required and recycling the crushed coal to the drying and heating stage,
  • the fine coal dust is mixed with oil'prior to being fed into the surge bin.
  • the preheating means is of the-flash type.
  • the apparatus for use in the processfor treating coal in'accordance with the present invention consists of a number of components, each of which is of known and/or conventional construction, and no claim is made to the individual apparatus components per se.
  • the coal-treating apparatus comprises a tippler 10 for delivering uncrushed coal containing, for example, 5 .to percent water onto a conveyor 11. Uncrushed coal may be delivered to this conveyor 1 1 from a stockpile (not shown) or removed from the conveyor 11 to the stockpile by conveyors l2 and 13 respectively.
  • the conveyor 11 delivers the water-containing uncrushed coal to a crusher 14 and crushed coal size 1 inch and/or less, preferably %-0 inch is passedby a conveyor 15 to a series of blending/storage bunkers 16 capable of storing about 48 hours supply of coal for the coke oven battery.
  • the crusher 14 may be omitted if it is not necessary, i.e. if the coal is already of the requisite size, and, inthis instance the conveyors l1 and 15 are one and the same.
  • the coal is fed from the blending/storage bunkers 16 onto one of a pair of parallel endless belt conveyors 17, "l-8'which carries the coal to the first stage 19 of a multistage preheating plant of the flash type.
  • the preheating plant may be two or three stage consisting of two or three thermal drying and heating tubes connected in series depending upon the degree of preheat required.
  • the preheating plant is two stage.
  • a coal crusher 20 is connected to an elutriator 22 of the preheating plant by a chute 21 and takes elutriated coal of a size approximately .4; inch from the elutriator 22 at the top of the first stage drying tube 19 and feeds the .crushed coal backabove a surge bin 27.
  • the larger sized coal is passed from the bottom of the cyclone 24-to the second stage heating tube 28 via a chute 29. This coal is then delivered at a temperature of, for-example, betweenl to 300 C. to a-main preheater cyclone 30 located above'the surge bin 27.
  • coal from the preheater cyclone 30 and the fine coal dust from the secondary cyclone 26 are then passed into the surge bin 27, the fine coal dust from the cyclone 26 passing via a mixerconveyor 31 whereat it is mixed with oil 32 before it enters the surge bin27.
  • the surge-bin 27 is provided with level controllers which control the coal feedfrom the blending/storage bunkers 16 onto the conveying system 17, 18 and is purged with inert gas.
  • Preheated coal is gravity fed from the surge bin 27 into the hoppers ofa charging car 33 wherebythe coal is charged into coking ovens (notshown').
  • the coal on passing from the surge bin .27 to thechargingcar 33, is introduced through telescopic sleeves incorporating filters, which are'the subject of British Pat. application No. l2402/68 filed Mar. 14,1968, and a film of oilas generally'indicated at 34is sprayed over the surface of thecoal ineachhopper to preventcoaldustbeing discharged into the atmosphere when the charging car 33 travels to the ovens.
  • the chargingcar 33 is of the clean air type and is provided with a gas washer and gas ignition equipment in known'manner.
  • the twin conveyors 17, 18' are provided in order tooffset the possibility of breakdown in one conveyor between the main coal storagesbunkers'l6 and the preheating plant.
  • preheating apparatus Whilst the above embodiment refers to preheating'of the .flashtype, other types of preheating apparatus can also be employed, for example, fluidized bed driers or.others which involve thermal drying of the coal.
  • a further advantage of the present invention is that a large storage hopper containing a large amount of preheated coal is dispensed with.
  • the preheating'plant comprises more than-two thermal heating and drying stages then appropriaterecirculation of the coal willbe effected.
  • A- process for the treatment of coal to render it suitable for. use in coke ovens comprising the steps of thermally drying and heating the coal of asize not greater; than 1; inch, separating coalwhich is largertha'n requiredfromthe remainder of the dried and heated coal, crushing the coal which is larger than required andrecycling the crushed coal to' the drying and heating stage, removing'relatively fine coal dust from the coal from which the larger-than-required coal hasbeenseparated, passing the relatively fine coal'dustto a surge bin, andpassing the coalfrom which the relatively fine coal dust has been separated to the surge'bin.
  • a process as claimedin claim. 1 including the step ofmixing oil with the relativelyfine coal dust priorto passing'the latter to the surge bin.

Abstract

The treatment of coal which is of a size, or which is crushed to a size not greater than 1 inch by drying and heating the coal and separating the relatively fine coal dust therefrom before delivering the coal and the coal dust mixed with oil to a surge bin.

Description

United States Patent Inventor Lewis Alderman Romiley, Stockport, England Appl. No. 771,934 Filed Oct. 30, 1968 Patented Aug. 17, 1971 Assignee Simon-Curves Limited Cheshire, England Priority Oct. 31, 1969 Great Britain 49383/67 PROCESS FOR THE TREATMENT OF COAL TO vRENDER IT SUITABLE FOR USE IN COKE OVEN 4 Claims, 1 Drawing Fig.
u.s.c| 241/17, 34/10,34/57,209/11,z41/19 InLCl 1302;21/00 Primary Examiner-Donald G. Kelly Att0rneyHolman & Stern ABSTRACT: The treatment of coal which is of a size, or which is crushed to a size not greater than 1 inch by drying and heating the coal and separating the relatively fine coal dust therefrom before delivering the coal and the coal dust mixed with oil to a surge bin.
PROCESS FOR THE TREATMENT OF COAL TO RENDER IT SUITABLE FOR USE IN COKE OVEN This invention relates to a process for the treatment of coal to render it suitable for use in coke ovens.
It has been previously proposed to feed coal into a series of blending bunkers from which it is conveyed to crushers which reduce the size of the coal to approx. 80-90 percent of Vsinch material. The crushed coal is then conveyed to large elevated storage hoppers situated above the oven battery, and capable of storing about 48 hours supply of coal for the ovens, in order to preserve continuity of feed to 'the ovens should there be a breakdown in the conveying means. The coal is then gravity fed into charging cars running on rails on the oven battery top, these cars charging coal into the ovens as required.
Such a process has disadvantages when applied 'to the conveying, storing and charging of dry or preheated coal in that the crushing means produce a larger amount of fine coal dust than is desirable thus creating dust nuisances at transfer points and explosive risks during storage. In addition the fine coal dust, when introduced into the ovens, causes a significant amount of carryover into the gas-collecting main of the ovens.
An object of the present invention is to obviate or'mitigate the aforesaid disadvantages.
According to the present invention, there is provided a process for the treatment of coal to render it suitable for use in coke ovens, comprising the steps of thermally drying and heating coal of a size not greater than 1 inch, separating coal which is larger than required from the remainder-of the dried and heated coal, crushing the coal which is larger than required and recycling the crushed coal to the drying and heating stage,
removing relatively fine coal dust from the coal from which the larger-than-required coal has been separated, passing the relatively fine coal dust to a surge bin, and passing .the'coal from whichthe relatively fine coal dust has been'separated to the surge bin.
Preferably, the fine coal dust is mixed with oil'prior to being fed into the surge bin.
Preferably also, the preheating means is of the-flash type.
An embodiment of the invention will nowbe describedby way of example with reference to the accompanying drawing which is a flow diagram of the coal-treating process in accordance with the present invention.
The apparatus for use in the processfor treating coal in'accordance with the present invention consists of a number of components, each of which is of known and/or conventional construction, and no claim is made to the individual apparatus components per se.
The coal-treating apparatus comprises a tippler 10 for delivering uncrushed coal containing, for example, 5 .to percent water onto a conveyor 11. Uncrushed coal may be delivered to this conveyor 1 1 from a stockpile (not shown) or removed from the conveyor 11 to the stockpile by conveyors l2 and 13 respectively.
The conveyor 11 delivers the water-containing uncrushed coal to a crusher 14 and crushed coal size 1 inch and/or less, preferably %-0 inch is passedby a conveyor 15 to a series of blending/storage bunkers 16 capable of storing about 48 hours supply of coal for the coke oven battery.
The crusher 14 may be omitted if it is not necessary, i.e. if the coal is already of the requisite size, and, inthis instance the conveyors l1 and 15 are one and the same.
The coal is fed from the blending/storage bunkers 16 onto one of a pair of parallel endless belt conveyors 17, "l-8'which carries the coal to the first stage 19 of a multistage preheating plant of the flash type. I
The preheating plant may be two or three stage consisting of two or three thermal drying and heating tubes connected in series depending upon the degree of preheat required.
In the present embodiment, the preheating plant is two stage.
A coal crusher 20 is connected to an elutriator 22 of the preheating plant by a chute 21 and takes elutriated coal of a size approximately .4; inch from the elutriator 22 at the top of the first stage drying tube 19 and feeds the .crushed coal backabove a surge bin 27. The larger sized coal is passed from the bottom of the cyclone 24-to the second stage heating tube 28 via a chute 29. This coal is then delivered at a temperature of, for-example, betweenl to 300 C. to a-main preheater cyclone 30 located above'the surge bin 27.
The coal from the preheater cyclone 30 and the fine coal dust from the secondary cyclone 26 are then passed into the surge bin 27, the fine coal dust from the cyclone 26 passing via a mixerconveyor 31 whereat it is mixed with oil 32 before it enters the surge bin27.
The surge-bin 27 is provided with level controllers which control the coal feedfrom the blending/storage bunkers 16 onto the conveying system 17, 18 and is purged with inert gas. Preheated coal is gravity fed from the surge bin 27 into the hoppers ofa charging car 33 wherebythe coal is charged into coking ovens (notshown'). The coal, on passing from the surge bin .27 to thechargingcar 33, is introduced through telescopic sleeves incorporating filters, which are'the subject of British Pat. application No. l2402/68 filed Mar. 14,1968, and a film of oilas generally'indicated at 34is sprayed over the surface of thecoal ineachhopper to preventcoaldustbeing discharged into the atmosphere when the charging car 33 travels to the ovens. The chargingcar 33is of the clean air type and is provided with a gas washer and gas ignition equipment in known'manner.
The twin conveyors 17, 18' are provided in order tooffset the possibility of breakdown in one conveyor between the main coal storagesbunkers'l6 and the preheating plant.
Whilst the above embodiment refers to preheating'of the .flashtype, other types of preheating apparatus can also be employed, for example, fluidized bed driers or.others which involve thermal drying of the coal.
It will be apparent that the process described above provides an.-arrangem'ent whereby coal can betreated in such a way that undue emission of fine material is reduced to a very low-level, due to avoidance'of overcrushing of inherent fine material'andtreatmentof'this material within the process. This factor minimizes dust nuisance'at transfer points, considerably reduces explosion risks and keeps, carry over of fine material into the. collecting main of the coke oven battery to a minimum.
A further advantage of the present invention is that a large storage hopper containing a large amount of preheated coal is dispensed with.
If the preheating'plant comprises more than-two thermal heating and drying stages then appropriaterecirculation of the coal willbe effected.
What] claim is:
l. A- process for the treatment of coal to render it suitable for. use in coke ovens, comprising the steps of thermally drying and heating the coal of asize not greater; than 1; inch, separating coalwhich is largertha'n requiredfromthe remainder of the dried and heated coal, crushing the coal which is larger than required andrecycling the crushed coal to' the drying and heating stage, removing'relatively fine coal dust from the coal from which the larger-than-required coal hasbeenseparated, passing the relatively fine coal'dustto a surge bin, andpassing the coalfrom which the relatively fine coal dust has been separated to the surge'bin.
2 A process as claimedin claim. 1 includingthe step ofmixing oil with the relativelyfine coal dust priorto passing'the latter to the surge bin.
3. A process as claimed in claim 1, including the step of further heating the coal from which the relatively fine coal crushing the coal to produce the coal of a size not greater than dust has been removed prior to passing the said coal to the 1 inch. surge bin.
4. A process as claimed in claim 1, including the step of

Claims (3)

  1. 2. A process as claimed in claim 1 including the step of mixing oil with the relatively fine coal dust prior to passing the latter to the surge bin.
  2. 3. A process as claimed in claim 1, including the step of crushing the coal to produce the coal of a size not greater than 1 inch.
  3. 4. A process as claimed in claim 1, including the step of further heating the coal from which the relatively fine coal dust has been removed prior to passing the said coal to the surge bin.
US771934A 1967-10-31 1968-10-30 Process for the treatment of coal to render it suitable for use in coke oven Expired - Lifetime US3599885A (en)

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BE (1) BE723290A (en)
DE (1) DE1806943A1 (en)
FR (1) FR1590365A (en)
GB (1) GB1232030A (en)
NL (1) NL139597B (en)
SE (1) SE360670B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4014104A (en) * 1975-06-23 1977-03-29 Continental Oil Company Drying of lignite using nonaqueous solvents
US4139419A (en) * 1976-01-21 1979-02-13 Hutni Projekt Praha, Projekcni A Inzenyrska Organizace Arrangement for dosing a coal charge to a coking battery
US4193554A (en) * 1977-10-08 1980-03-18 Klockner-Humboldt-Deutz Ag Method and apparatus for the drying and fine-grinding of coal
US4268271A (en) * 1979-11-26 1981-05-19 Atlantic Richfield Company Reduction of the fouling potential of high sodium coal

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4391702A (en) * 1977-10-07 1983-07-05 Nippon Steel Corporation Method for classification of coals for coke production
JPS5454102A (en) * 1977-10-07 1979-04-28 Nippon Steel Corp Classification and selective crushing of coal for coke manufacturing
BR8006070A (en) * 1979-09-26 1981-04-07 Charbonnages De France TREATMENT PROCESS BY DRYING AND / OR HEATING GRANULATED AND / OR PULVERULENT COMBUSTIBLE MATERIAL AND INSTALLATION FOR THE EXECUTION OF THE PROCESS
FR2465774A1 (en) * 1979-09-26 1981-03-27 Charbonnages De France Drying and heating granular or powdered fuels - with splitting of recycled gases so that flow through dust remover is constant

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1576335A (en) * 1925-01-16 1926-03-09 Combustion Eng Corp Pulverization of coal
US2132656A (en) * 1936-01-23 1938-10-11 Comb Eng Co Inc Flash drying control
US2430085A (en) * 1943-07-09 1947-11-04 Pittsburgh Midway Coal Mining Process of preparing coal for use in colloidal fuels
US2803587A (en) * 1956-05-15 1957-08-20 Jung Frederic William Method of heat treatment, separation, and coking coal

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1576335A (en) * 1925-01-16 1926-03-09 Combustion Eng Corp Pulverization of coal
US2132656A (en) * 1936-01-23 1938-10-11 Comb Eng Co Inc Flash drying control
US2430085A (en) * 1943-07-09 1947-11-04 Pittsburgh Midway Coal Mining Process of preparing coal for use in colloidal fuels
US2803587A (en) * 1956-05-15 1957-08-20 Jung Frederic William Method of heat treatment, separation, and coking coal

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4014104A (en) * 1975-06-23 1977-03-29 Continental Oil Company Drying of lignite using nonaqueous solvents
US4139419A (en) * 1976-01-21 1979-02-13 Hutni Projekt Praha, Projekcni A Inzenyrska Organizace Arrangement for dosing a coal charge to a coking battery
US4193554A (en) * 1977-10-08 1980-03-18 Klockner-Humboldt-Deutz Ag Method and apparatus for the drying and fine-grinding of coal
US4268271A (en) * 1979-11-26 1981-05-19 Atlantic Richfield Company Reduction of the fouling potential of high sodium coal

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FR1590365A (en) 1970-04-13
SE360670B (en) 1973-10-01
GB1232030A (en) 1971-05-19
DE1806943A1 (en) 1969-08-21
NL139597B (en) 1973-08-15
NL6815558A (en) 1969-05-02
BE723290A (en) 1969-04-01

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