US3723079A - Stabilization of coal - Google Patents

Stabilization of coal Download PDF

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Publication number
US3723079A
US3723079A US00165728A US3723079DA US3723079A US 3723079 A US3723079 A US 3723079A US 00165728 A US00165728 A US 00165728A US 3723079D A US3723079D A US 3723079DA US 3723079 A US3723079 A US 3723079A
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coal
oxygen
percent
water
amount
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US00165728A
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W Seitzer
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Sun Research and Development Co
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Sun Research and Development Co
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L9/00Treating solid fuels to improve their combustion
    • C10L9/02Treating solid fuels to improve their combustion by chemical means
    • C10L9/06Treating solid fuels to improve their combustion by chemical means by oxidation

Definitions

  • the coals used in the process of the invention will be, as indicated, lignitic and subbituminous coals and will include North Dakota lignite, Powder River subbituminous coal, Wyodak coal, and the like. Such coals usually contain from about 20 to 40 percent water as they come from the mine, but for use in subject process they will first be dried to a water level of about I percent to about 10 percent by weight and this is readily done simply by flowing hot flue gas through the coal.
  • the process of the invention is applicable to coal of any size, but will, of course, be of most value with the smaller sizes since they have the greater surface area and are most subject to oxidation.
  • the process of the invention requires that the oxygen treatment be controlled so that its uptake is between about 0.5 percent and about 8 percent by weight of the coal treated.
  • an oxygen uptake of 1 percent corresponds to about 1 pound ofoxygen per 100 pounds of while operable, is somewhat expensive for use in the process.
  • The-oxygen treatment may be carried out by any conventional technique which will distribute the oxygen over the surface of the coal.
  • the dried coal is treated with air in a rotary drum burner, the temperature of treatment being from about C. to about 225 C. Not all of the oxygen in the air will be reactive with the coal since about onehalf of the available oxygen will be carried out of the burner. This is readily compensated for by adjusting air flow, drum rotation speed, and coal volume in accord with known techniques available to the skilled art worker.
  • the oxygen level of the gas used for the oxidation treatment should be at least about 10 percent and as the oxidation proceeds about 45 percent of the oxygen is converted to water, about 45 percent to CO and about 10 percent to CO.
  • the rehydration of the coal with water is readily accomplished by a spraying technique, although when smaller amounts are treated, the coal particles may be simply agitated with the required amount of water to effect distribution on the surface.
  • the amount of water used will be between about 1.5 percent and about 6 percent by weight of the oxygen treated coal.
  • the hot coal emerging from the oxygen treating step is cooled to a temperature between about 150 and about 50 C. by heat exchange with the hot gas oxygen supply, and then the cooled coal is sprayed with water.
  • Empirical techniques are easily employed in the selection of type of spray nozzle, water pressure, time of spray, etc. in order to place from about 1.5 percent to about 6 percent water on the coal.
  • Test Procedure Dried Wyodak coal of 14 mesh size is placed in a stirred container equipped with an oxygen inlet, an outlet which is connected in series to a drying tube, a CuO catalyzed converter at 800 C. to convert CO to C0,, an Ascarite tube for C0, absorption, and then connected through a pump to the input for oxygen recycle.
  • the stirred coal is heated to 200 C. as oxygen is passed through the system and recycled. The amount of oxygen used is measured with appropriate gas flow meters.
  • the oxidized coal is cooled and wetted with the desired amount of water, thorough distribution being obtained by agitation. Then the rehydrated coal is placed in a Dewar flask fitted at the bottom with a sparging tube to pass oxygen through the coal and equipped with a temperature measuring device.
  • the coal (450g) in Dewar flask (70 mm. [.D.) is about 200 mm. in depth and oxygen is passed through it at 63 C. at a rate of ml/min.
  • the time for combustion of the coal to occur is noted as shown by the sudden temperature increase and is taken as a measure of stability.
  • a process for stabilizing dried lignitic and subbituminous coal against spontaneous combustion which comprises treating said dried coal at about to about 225 C. with oxygen in an amount of from about 0.5 percent to about 8 percent by weight of said coal and rehydrating the oxygen treated coal with water in an amount of from about 1.5 percent to about 6 percent by weight of said oxygen treated coal.

Abstract

A process for stabilizing dried lignitic and subbituminous coal against spontaneous combustion which comprises treating said dried coal at about 175* to about 225* C. with oxygen in an amount of from about 0.5 percent to about 8 percent by weight of said coal and rehydrating the oxygen treated coal with water in an amount of from about 1.5 percent to about 6 percent by weight of said oxygen treated coal.

Description

Unite States atent r 1 Seitzer [54] STABILIZATION OF COAL [75] Inventor: Walter H. Seitzer, Marcus Hook,
[73] Assignee: Sun Research and Development Co.,
Philadelphia, Pa.
[22] Filed: July 23, 1971 [21] Appl. No.: 165,728
[52] US. Cl. ....44/l R, 44/1 G [51] Int. Cl..; ..C10l 5/00 [58] Field of Search ..44/1 R, l G, 6,10 D, 10 E [56] References Cited UNITED STATES PATENTS 1,219,155 3/1917 Rigby 44/1 R [4 1 Mar. 27, 1973 Fernholtz ..44/l G Ford ..44/1O E Primary Examiner-C. F. Dees Attorney-George L. Church et a1.
[57] ABSTRACT 2 Claims, N0 Drawings STABILIZATION or COAL Dried lignitic and subbituminous coals are unstable to storage in that they are subject to air oxidation and combust spontaneously. Thus, in order to enhance storage stability special treatments must often be used. For example, coal piles are often arranged in a particular manner to obtain safe storage; e.g., thin layers which are compacted with sloping sides at a maximum angle of 14, smooth final surfaces, and top surface continually smoothed as coal is removed from the top only. Other approaches to prevent spontaneous combustion during storage involves chemical treatment of the coal; e.g., coating the coal with petroleum products and their emulsions, spraying with calcium bicarbonate or aqueous hydroquinone or amines. Such treatments, however, are either not completely effective or are excessively expensive for a low priced commodity such as coal.
Numerous investigations have been made on the oxidation of coal with an objective toward improving its stability. One such study concluded that use of oxygen to form oxidized zones on the surface and in the interior of the mass of brown coals imparted protection against further oxidation (Szadeczky-Kardoss, E., Ungar., Z. Berg u. Huettenwessen, 77, 241-7, 253-60, 1944). My experimental work confirms this effect with oxygen treatment, but 1 have found this technique to be an incomplete solution to the storage stability problem. In my experiments 1 find that this oxygen treatment coal and thus, the process of the invention will use from about 0.5 pounds to about 8 pounds of oxygen per 100 pounds of coal treated. It will be also understood that air is a suitable source of oxygen and that pure oxygen,
delays somewhat the time until spontaneous combustion might occur, but the treatment does not greatly extend the safe storage period.
1 have now found a means to significantly improve the storage stability of dried lignitic and subbituminous coal and this is accomplished, in accord with my invention, by the process which comprises treating said dried coal at a temperature between about 175 C. and about 225 C. with oxygen in an amount of from about 0.5 percent to about 8 percent by weight of said coal and rehydrating the oxygen treated coal with water in an amount of from about 1.5 percent to about 6 percent by weight of said coal.
The coals used in the process of the invention will be, as indicated, lignitic and subbituminous coals and will include North Dakota lignite, Powder River subbituminous coal, Wyodak coal, and the like. Such coals usually contain from about 20 to 40 percent water as they come from the mine, but for use in subject process they will first be dried to a water level of about I percent to about 10 percent by weight and this is readily done simply by flowing hot flue gas through the coal. The process of the invention is applicable to coal of any size, but will, of course, be of most value with the smaller sizes since they have the greater surface area and are most subject to oxidation.
In carrying out the process of the invention it is important to control the amount of oxidation since I have found that excessive oxygen actually decreases the stability of the dried coal. The process of the invention requires that the oxygen treatment be controlled so that its uptake is between about 0.5 percent and about 8 percent by weight of the coal treated. As a guide in carrying out this controlled oxidation it should be understood that an oxygen uptake of 1 percent corresponds to about 1 pound ofoxygen per 100 pounds of while operable, is somewhat expensive for use in the process.
r The-oxygen treatment may be carried out by any conventional technique which will distribute the oxygen over the surface of the coal. In a preferred method, the dried coal is treated with air in a rotary drum burner, the temperature of treatment being from about C. to about 225 C. Not all of the oxygen in the air will be reactive with the coal since about onehalf of the available oxygen will be carried out of the burner. This is readily compensated for by adjusting air flow, drum rotation speed, and coal volume in accord with known techniques available to the skilled art worker. The oxygen level of the gas used for the oxidation treatment should be at least about 10 percent and as the oxidation proceeds about 45 percent of the oxygen is converted to water, about 45 percent to CO and about 10 percent to CO.
The rehydration of the coal with water is readily accomplished by a spraying technique, although when smaller amounts are treated, the coal particles may be simply agitated with the required amount of water to effect distribution on the surface. As indicated, the amount of water used will be between about 1.5 percent and about 6 percent by weight of the oxygen treated coal. In a preferred technique the hot coal emerging from the oxygen treating step is cooled to a temperature between about 150 and about 50 C. by heat exchange with the hot gas oxygen supply, and then the cooled coal is sprayed with water. Empirical techniques are easily employed in the selection of type of spray nozzle, water pressure, time of spray, etc. in order to place from about 1.5 percent to about 6 percent water on the coal.
After the water treatment the stabilized coal is handled, transported and stored by conventional methods and prolonged storage stability of the treated coal is evident.
in order to more fully illustrate the invention the following examples are given:
Test Procedure Dried Wyodak coal of 14 mesh size is placed in a stirred container equipped with an oxygen inlet, an outlet which is connected in series to a drying tube, a CuO catalyzed converter at 800 C. to convert CO to C0,, an Ascarite tube for C0, absorption, and then connected through a pump to the input for oxygen recycle. The stirred coal is heated to 200 C. as oxygen is passed through the system and recycled. The amount of oxygen used is measured with appropriate gas flow meters.
The oxidized coal is cooled and wetted with the desired amount of water, thorough distribution being obtained by agitation. Then the rehydrated coal is placed in a Dewar flask fitted at the bottom with a sparging tube to pass oxygen through the coal and equipped with a temperature measuring device. The coal (450g) in Dewar flask (70 mm. [.D.) is about 200 mm. in depth and oxygen is passed through it at 63 C. at a rate of ml/min. The time for combustion of the coal to occur is noted as shown by the sudden temperature increase and is taken as a measure of stability.
The following tables illustrate the effects of the process:
TABLE I Ex. nov Coal treatment Hours to combustion No oxygen, No water 1 6 l% 0,, No water 6.0 7% 0,, No water 4.8
8% 0,, No water 4.5
No oxygen, 6% water 4.3
4% 0 1.5% water 9 0 4% 0 3% water Never com busts illustrative of the invention:
TABLE 11 Ex. no. Coal Treatment Hours to Combustion 8. No oxygen. 6% water 4.3 9. 4% 0, +6% water Never combusts l0. 7% 0, 6% water Never co'mbusts l l. 8% O, 6% water Never combusts It is clear from the above data that the process of the invention provides a means to prevent spontaneous combustion of coal during storage and makes a valuable contribution to the art.
The invention claimed is:
l. A process for stabilizing dried lignitic and subbituminous coal against spontaneous combustion which comprises treating said dried coal at about to about 225 C. with oxygen in an amount of from about 0.5 percent to about 8 percent by weight of said coal and rehydrating the oxygen treated coal with water in an amount of from about 1.5 percent to about 6 percent by weight of said oxygen treated coal.
2. The process of claim 1 where the amount of water is from about 3 percent to about 6 percent.

Claims (1)

  1. 2. The process of claim 1 where the amount of water is from about 3 percent to about 6 percent.
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Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2700554A1 (en) * 1976-01-12 1977-07-14 Edward Koppelman PROCESS FOR PROCESSING LIGNITE-LIKE COAL AS FUEL
US4043763A (en) * 1976-04-12 1977-08-23 Suntech, Inc. Stabilization of dried coal
FR2375875A1 (en) * 1977-01-04 1978-07-28 Schoppe Fritz Suppressing combustion of stored lignite fines - by mixing with a less combustible powder
US4192650A (en) * 1978-07-17 1980-03-11 Sunoco Energy Development Co. Process for drying and stabilizing coal
US4213752A (en) * 1978-11-06 1980-07-22 Suntech, Inc. Coal drying process
EP0081763A2 (en) * 1981-12-10 1983-06-22 Gewerkschaft Sophia-Jacoba Steinkohlenbergwerk Process for converting coal or mixtures thereof into a condition fit for the storage and transport thereof
US4401436A (en) * 1981-12-21 1983-08-30 Atlantic Richfield Company Process for cooling particulate coal
US4402706A (en) * 1981-12-21 1983-09-06 Atlantic Richfield Company Method and apparatus for oxidizing dried low rank coal
US4498905A (en) * 1983-10-31 1985-02-12 Atlantic Richfield Company Method for deactivating and controlling the dusting tendencies of dried particulate lower rank coal
US4501551A (en) * 1983-11-10 1985-02-26 Atlantic Richfield Company Method for producing a dried particulate coal fuel from a particulate low rank coal
US4645513A (en) * 1982-10-20 1987-02-24 Idemitsu Kosan Company Limited Process for modification of coal
EP0325703A1 (en) * 1988-01-22 1989-08-02 Gewerkschaft Sophia-Jacoba Steinkohlenbergwerk Process for the preparation of small size coal or coal mixtures for safe storage, particularly for safe road, rail or sea transport
EP0345387A1 (en) * 1986-12-19 1989-12-13 Shell Oil Company Process for inhibiting the spontaneous oxidation of low rank coal
EP0527045A2 (en) * 1991-08-05 1993-02-10 Robert J. Adams Method for treating coal
EP0758677A1 (en) * 1995-08-15 1997-02-19 Western Syncoal Company Stabilized thermally beneficiated low rank coal and method of manufacture
US20060096167A1 (en) * 2001-10-10 2006-05-11 Dunlop Donald D Process for in-situ passivation of partially-dried coal
US20100037516A1 (en) * 2004-05-03 2010-02-18 Evergreen Energy Inc. Method for thermally upgrading carbonaceous materials
US20100263269A1 (en) * 2001-10-10 2010-10-21 River Basin Energy, Inc. Process for Drying Coal
US8956426B2 (en) 2010-04-20 2015-02-17 River Basin Energy, Inc. Method of drying biomass
US9057037B2 (en) 2010-04-20 2015-06-16 River Basin Energy, Inc. Post torrefaction biomass pelletization
EP3053993A4 (en) * 2013-10-01 2017-03-15 Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) Method for producing modified coal, and modified coal
US9617491B2 (en) 2012-01-06 2017-04-11 Mitsubishi Heavy Industries, Ltd. Coal deactivation treatment device
US9701919B2 (en) 2013-03-04 2017-07-11 Mitsubishi Heavy Industries, Ltd. Coal inactivation processing apparatus
EP3101094A4 (en) * 2014-01-30 2017-09-06 Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) Method of producing modified coal, and modified coal
US9758741B2 (en) 2012-10-09 2017-09-12 Mitsubishi Heavy Industries, Ltd. Coal deactivation processing device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1219155A (en) * 1913-01-11 1917-03-13 Nils Testrup Treatment of lignite and the like.
US1426723A (en) * 1916-09-23 1922-08-22 Margaret J Thompson Process and apparatus for the conversion of peat, lignite, and other carbonaceous substances into artificial coal
US1577902A (en) * 1924-12-22 1926-03-23 Fernholtz Machinery Company Block or briquette of lignite and method of making the same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1219155A (en) * 1913-01-11 1917-03-13 Nils Testrup Treatment of lignite and the like.
US1426723A (en) * 1916-09-23 1922-08-22 Margaret J Thompson Process and apparatus for the conversion of peat, lignite, and other carbonaceous substances into artificial coal
US1577902A (en) * 1924-12-22 1926-03-23 Fernholtz Machinery Company Block or briquette of lignite and method of making the same

Cited By (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2700554A1 (en) * 1976-01-12 1977-07-14 Edward Koppelman PROCESS FOR PROCESSING LIGNITE-LIKE COAL AS FUEL
US4043763A (en) * 1976-04-12 1977-08-23 Suntech, Inc. Stabilization of dried coal
FR2375875A1 (en) * 1977-01-04 1978-07-28 Schoppe Fritz Suppressing combustion of stored lignite fines - by mixing with a less combustible powder
US4192650A (en) * 1978-07-17 1980-03-11 Sunoco Energy Development Co. Process for drying and stabilizing coal
US4213752A (en) * 1978-11-06 1980-07-22 Suntech, Inc. Coal drying process
EP0081763A3 (en) * 1981-12-10 1984-08-29 Gewerkschaft Sophia-Jacoba Steinkohlenbergwerk Process for producing finely grained storage and transportation equipped coal or coal mixtures
EP0081763A2 (en) * 1981-12-10 1983-06-22 Gewerkschaft Sophia-Jacoba Steinkohlenbergwerk Process for converting coal or mixtures thereof into a condition fit for the storage and transport thereof
US4402706A (en) * 1981-12-21 1983-09-06 Atlantic Richfield Company Method and apparatus for oxidizing dried low rank coal
US4401436A (en) * 1981-12-21 1983-08-30 Atlantic Richfield Company Process for cooling particulate coal
US4645513A (en) * 1982-10-20 1987-02-24 Idemitsu Kosan Company Limited Process for modification of coal
US4498905A (en) * 1983-10-31 1985-02-12 Atlantic Richfield Company Method for deactivating and controlling the dusting tendencies of dried particulate lower rank coal
US4501551A (en) * 1983-11-10 1985-02-26 Atlantic Richfield Company Method for producing a dried particulate coal fuel from a particulate low rank coal
EP0345387A1 (en) * 1986-12-19 1989-12-13 Shell Oil Company Process for inhibiting the spontaneous oxidation of low rank coal
EP0325703A1 (en) * 1988-01-22 1989-08-02 Gewerkschaft Sophia-Jacoba Steinkohlenbergwerk Process for the preparation of small size coal or coal mixtures for safe storage, particularly for safe road, rail or sea transport
DE3801800C1 (en) * 1988-01-22 1989-08-24 Gewerkschaft Sophia-Jacoba, 5142 Hueckelhoven, De
EP0527045A2 (en) * 1991-08-05 1993-02-10 Robert J. Adams Method for treating coal
EP0527045A3 (en) * 1991-08-05 1993-03-10 Robert J. Adams Method for treating coal
US5254139A (en) * 1991-08-05 1993-10-19 Adams Robert J Method for treating coal
US5468265A (en) * 1991-08-05 1995-11-21 Rja Associates Method for treating coal
US5863304A (en) * 1995-08-15 1999-01-26 Western Syncoal Company Stabilized thermally beneficiated low rank coal and method of manufacture
EP0758677A1 (en) * 1995-08-15 1997-02-19 Western Syncoal Company Stabilized thermally beneficiated low rank coal and method of manufacture
AU707213B2 (en) * 1995-08-15 1999-07-08 Western Syncoal Company Stabilized thermally beneficiated low rank coal and method of manufacture
US6090171A (en) * 1995-08-15 2000-07-18 Western Syncoal Company Stabilized thermally beneficiated low rank coal and method of manufacture
US20060096167A1 (en) * 2001-10-10 2006-05-11 Dunlop Donald D Process for in-situ passivation of partially-dried coal
US7695535B2 (en) 2001-10-10 2010-04-13 River Basin Energy, Inc. Process for in-situ passivation of partially-dried coal
US20100263269A1 (en) * 2001-10-10 2010-10-21 River Basin Energy, Inc. Process for Drying Coal
US8197561B2 (en) 2001-10-10 2012-06-12 River Basin Energy, Inc. Process for drying coal
US20100037516A1 (en) * 2004-05-03 2010-02-18 Evergreen Energy Inc. Method for thermally upgrading carbonaceous materials
EP2287279A1 (en) * 2004-05-03 2011-02-23 Evergreen Energy Inc. Method and apparatus for thermally upgrading carbonaceous materials
US9057037B2 (en) 2010-04-20 2015-06-16 River Basin Energy, Inc. Post torrefaction biomass pelletization
US8956426B2 (en) 2010-04-20 2015-02-17 River Basin Energy, Inc. Method of drying biomass
US9988588B2 (en) 2010-04-20 2018-06-05 River Basin Energy, Inc. Post torrefaction biomass pelletization
US9617491B2 (en) 2012-01-06 2017-04-11 Mitsubishi Heavy Industries, Ltd. Coal deactivation treatment device
US9758741B2 (en) 2012-10-09 2017-09-12 Mitsubishi Heavy Industries, Ltd. Coal deactivation processing device
US9701919B2 (en) 2013-03-04 2017-07-11 Mitsubishi Heavy Industries, Ltd. Coal inactivation processing apparatus
EP3053993A4 (en) * 2013-10-01 2017-03-15 Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) Method for producing modified coal, and modified coal
RU2639873C2 (en) * 2013-10-01 2017-12-25 Кабусики Кайся Кобе Сейко Се (Кобе Стил,Лтд.) Method of manufacturing modified coal and modified coal
US9994783B2 (en) 2013-10-01 2018-06-12 Kobe Steel, Ltd. Method for producing modified coal, and modified coal
EP3101094A4 (en) * 2014-01-30 2017-09-06 Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) Method of producing modified coal, and modified coal
US10005977B2 (en) 2014-01-30 2018-06-26 Kobe Steel, Ltd. Method of producing modified coal, and modified coal
RU2666535C2 (en) * 2014-01-30 2018-09-11 Кабусики Кайся Кобе Сейко Се (Кобе Стил, Лтд.) Method of producing modified coal and modified coal

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