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WO1996015208B1 - Method for coking coal - Google Patents

Method for coking coal

Info

Publication number
WO1996015208B1
WO1996015208B1 PCT/US1995/014184 US9514184W WO9615208B1 WO 1996015208 B1 WO1996015208 B1 WO 1996015208B1 US 9514184 W US9514184 W US 9514184W WO 9615208 B1 WO9615208 B1 WO 9615208B1
Authority
WO
WIPO (PCT)
Prior art keywords
coke
coal
recited
continuously producing
wall
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.)
Ceased
Application number
PCT/US1995/014184
Other languages
French (fr)
Other versions
WO1996015208A1 (en
Filing date
Publication date
Priority claimed from US08/336,399 external-priority patent/US5607556A/en
Priority to UA97062735A priority Critical patent/UA43874C2/en
Priority to RU97110211/04A priority patent/RU2144555C1/en
Priority to EP95941354A priority patent/EP0791039A4/en
Priority to RO97-00855A priority patent/RO119309B1/en
Priority to BR9509631A priority patent/BR9509631A/en
Priority to SK583-97A priority patent/SK58397A3/en
Priority to CA002205047A priority patent/CA2205047C/en
Application filed filed Critical
Priority to KR1019970702941A priority patent/KR100338398B1/en
Priority to AU42719/96A priority patent/AU4271996A/en
Priority to CZ971379A priority patent/CZ137997A3/en
Priority to PL95320193A priority patent/PL184382B1/en
Priority to MX9703379A priority patent/MX9703379A/en
Publication of WO1996015208A1 publication Critical patent/WO1996015208A1/en
Publication of WO1996015208B1 publication Critical patent/WO1996015208B1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Abstract

This invention discloses a new method for the production of coke from coals. In the present invention, coke is continuously produced by heating a moving charge of coal inside the annular cross-section (13) defined by two concentric tubes (11, 12). The coking chamber (13), which includes a large diameter tube (11) and a concentric smaller diameter tube (12), is force fed with a coal such as metallurgical coal. The coal is bi-directionally heated along a controlled temperature gradient between the inner wall of the small diameter tube (12) and the outer wall of the large diameter tube (11). The coal is transformed to coke as it travels longitudinally along the axis of both tubes. Coke is discharged from the chamber at the end opposite to which it was charged and is cooled before being exposed to the atmosphere. Gases generated during the coking process are collected and treated. All of these operations are accomplished in a closed system to prevent pollution.

Claims

UAMENDED CLAIMS[received by the International Bureau on 14 May 1996 (14.05.96); original claims 1-20 replaced by new claims 1-10 (3 pages)]
1. A method for continuously producing coke from coal comprising: providing at least one elongated coking chamber having an annulus formed by an outer wall of a small tube and an inner wall of a large tube; force feeding coal in a charging end of said coking chamber and compacting the coal against the outer wall of the small tube and the inner wall of the large tube; and continuously carbonizing said coal into coke in the absence of oxygen by heating a forced stream of coal in the annulus of said elongated coking chamber, said coal is bi-directionally heated in said annulus by conductive heat as said coal passes through said elongated coking chamber, wherein said carbonization occurs from each of said walls in order to form a cleavage essentially in a middle portion of said annulus.
2. A method of continuously producing coke as recited in claim 1, wherein said coal is delivered to said coking chamber through a lockhopper device.
15
3. A method of continuously producing coke as recited in claim 1, further comprising discharging said coke from the coking chamber into a quenching chamber wherein said coke is cooled below an ignition point of said coke .
4. A method of continuously producing coke as recited in claim 3, wherein said coke is cooled by steam.
5. A method of continuously producing coke as recited in claim 3, further comprising discharging the cooled coke into the atmosphere through a lockhopper device.
6. A method of continuously producing coke as recited in claim 1, further comprising collecting and treating gases generated during the carbonization of said coal .
7. A method of continuously producing coke as recited in claim 1, wherein said coal is forced into said elongated coking chamber at the charging end by a pushing piston so that the compacting of the coal forces said coke out of a discharge end of said elongated coking chamber. 1 6
8. A method of continuously producing coke as recited in claim 1, wherein heat for conductively heating said coal is applied by directing products of combustion against said walls.
9. A method of continuously producing coke as recited in claim 8, wherein the products of combustion are first applied to the wall of the small tube and then directed to the wall of the large tube.
10. A method of continuously producing metallurgical coke as recited in claim 9, further comprising increasing the thermal energy in the products of combustion before directing the products to the wall of the large tube.
1 7
STATEMENT UNDER ARTICLE 19
Applicant submits substitute pages 9-11 in place of old pages 9-13.
PCT/US1995/014184 1994-11-09 1995-11-03 Method for coking coal Ceased WO1996015208A1 (en)

Priority Applications (12)

Application Number Priority Date Filing Date Title
UA97062735A UA43874C2 (en) 1994-11-09 1995-03-11 METHOD OF CONTINUOUS COKE PREPARATION AND COXING DEVICE
MX9703379A MX9703379A (en) 1994-11-09 1995-11-03 Method for coking coal.
KR1019970702941A KR100338398B1 (en) 1994-11-09 1995-11-03 Coking Method of Coal
RO97-00855A RO119309B1 (en) 1994-11-09 1995-11-03 Process and installation for producing coke from coal
BR9509631A BR9509631A (en) 1994-11-09 1995-11-03 Process and apparatus for the continuous production of coal coke
SK583-97A SK58397A3 (en) 1994-11-09 1995-11-03 Method for coking coal
CA002205047A CA2205047C (en) 1994-11-09 1995-11-03 Method for coking coal
RU97110211/04A RU2144555C1 (en) 1994-11-09 1995-11-03 Method of continuous production of coke and device for coking
EP95941354A EP0791039A4 (en) 1994-11-09 1995-11-03 Method for coking coal
AU42719/96A AU4271996A (en) 1994-11-09 1995-11-03 Method for coking coal
CZ971379A CZ137997A3 (en) 1994-11-09 1995-11-03 Coal coking process
PL95320193A PL184382B1 (en) 1994-11-09 1995-11-03 Coal coking process

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/336,399 US5607556A (en) 1994-11-09 1994-11-09 Method for coking coal
US08/336,399 1994-11-09

Publications (2)

Publication Number Publication Date
WO1996015208A1 WO1996015208A1 (en) 1996-05-23
WO1996015208B1 true WO1996015208B1 (en) 1996-07-04

Family

ID=23315914

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1995/014184 Ceased WO1996015208A1 (en) 1994-11-09 1995-11-03 Method for coking coal

Country Status (16)

Country Link
US (1) US5607556A (en)
EP (1) EP0791039A4 (en)
JP (1) JP2758383B2 (en)
KR (1) KR100338398B1 (en)
CN (1) CN1078233C (en)
AU (2) AU689942B2 (en)
BR (1) BR9509631A (en)
CA (1) CA2205047C (en)
CZ (1) CZ137997A3 (en)
MX (1) MX9703379A (en)
PL (1) PL184382B1 (en)
RO (1) RO119309B1 (en)
RU (1) RU2144555C1 (en)
SK (1) SK58397A3 (en)
UA (1) UA43874C2 (en)
WO (1) WO1996015208A1 (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6077399A (en) * 1998-03-24 2000-06-20 Calderon Energy Company Of Bowling Green, Inc. Method for producing uniform quality coke
FR2804205B1 (en) * 2000-01-21 2002-05-03 Thide Environnement THERMOLYSIS OVEN, ESPECIALLY WASTE AND / OR BIOMASS, WITH SPATIALLY INHOMOGENEOUS HEATING
CN1100112C (en) * 2000-09-22 2003-01-29 冶金工业部鞍山热能研究院 Hot air blowing coking coal grading and moisture controlled coal preparation process
UA90089C2 (en) * 2006-02-08 2010-04-12 Григорий БЕРЕЗИН Method for production of coke from the non-coking ranks of coal and the apparatus for its realization
RU2359006C1 (en) * 2008-05-05 2009-06-20 Сергей Романович Исламов Method of coal processing
US20120047975A1 (en) * 2010-09-01 2012-03-01 Albert Calderon Method and apparatus for continuously carbonizing materials
CN101984022B (en) * 2010-10-26 2011-08-10 西峡龙成特种材料有限公司 External heating coal decomposing equipment with multiple pipes
US20130032510A1 (en) * 2011-08-01 2013-02-07 Albert Calderon Advanced method and apparatus to process Bitumen containing impurities
CN102585863B (en) * 2012-02-21 2014-01-15 西峡龙成特种材料有限公司 Sleeve type coal material decomposition device
RU2553116C1 (en) * 2013-12-23 2015-06-10 Общество С Ограниченной Ответственностью "Промышленные Инновационные Технологии Национальной Коксохимической Ассоциации" (Ооо "Проминтех Нка") Method of metallurgical coke production
CN110713839B (en) * 2019-11-13 2024-07-16 宁波蓝乾设备制造有限公司 Vertical biomass pyrolysis carbonization furnace
CN114933911B (en) * 2022-03-28 2023-05-23 中国五冶集团有限公司 Method for building clean heat recovery coke oven gas collecting tube

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1018331A (en) * 1911-10-10 1912-02-20 Walther Mathesius Hot-blast stove.
US1953040A (en) * 1931-03-28 1934-03-27 Combustion Utilities Corp Process and apparatus for carbonizing solid fuel
US2224823A (en) * 1938-07-05 1940-12-10 Du Pont Method for devolatilizing charcoal
US2922752A (en) * 1957-03-07 1960-01-26 Cabot Godfrey L Inc Continuous carbonization process and apparatus
IT1062095B (en) * 1975-05-09 1983-06-25 Lampl Helma PROCESS AND EQUIPMENT FOR THE PYROLYSIS OF CASCAMI
CA1095696A (en) * 1976-12-22 1981-02-17 Richard F. Buswell Catalytic reaction apparatus
US4469488A (en) * 1980-05-27 1984-09-04 Albert Calderon Method for gasifying coal
US4389283A (en) * 1980-10-29 1983-06-21 Albert Calderon Method for making coke via induction heating
EP0194067B2 (en) * 1985-03-05 1994-05-11 Imperial Chemical Industries Plc Steam reforming hydrocarbons
NL9101408A (en) * 1991-08-20 1993-03-16 Stork Contiweb BURNER UNIT.
US5356530A (en) * 1992-10-16 1994-10-18 Albert Calderon Method for upgrading petroleum residuum and heavy crude oil

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