CN101985562A - Horizontal coal separating equipment with multiple combustors - Google Patents
Horizontal coal separating equipment with multiple combustors Download PDFInfo
- Publication number
- CN101985562A CN101985562A CN 201010262870 CN201010262870A CN101985562A CN 101985562 A CN101985562 A CN 101985562A CN 201010262870 CN201010262870 CN 201010262870 CN 201010262870 A CN201010262870 A CN 201010262870A CN 101985562 A CN101985562 A CN 101985562A
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- solid matter
- coal
- rotary kiln
- kiln body
- gas
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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
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/04—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of powdered coal
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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
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/28—Other processes
- C10B47/30—Other processes in rotary ovens or retorts
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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
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/28—Other processes
- C10B47/32—Other processes in ovens with mechanical conveying means
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/02—Dust removal
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
Abstract
The invention discloses horizontal coal separating equipment with multiple combustors, comprising a horizontal sealed rotary kiln body, wherein the rotary kiln body is provided with multiple densely arranged combustors inside; one side of the combustors is correspondingly provided with multiple gas inlet pipes and air inlet pipes; the other side of the combustors is provided with corresponding densely arranged radiating pipes; coal propelling and separating channels are formed among the combustors, the gas inlet pipes, the air inlet pipes and the inner wall of the rotary kiln body; the rotary kiln body is provided with a collecting pipe of gases and tar gases separated from coal; the densely arranged radiating pipes are communicated with a flame gas gathering pipe; and the flame gas gathering pipe extends out of the rotary kiln. The equipment can rapidly and efficiently decompose and separate the powdered coal, fully saves and utilizes the energy, greatly improves the utilization ratio and level of the coal resources and brings vast economic and social benefits for the whole society.
Description
Technical field
The invention belongs to the comprehensive utilization of coal material, energy-conserving and emission-cutting technology field, be specifically related to the horizontal separating device of a kind of coal material multi-combustor.
Background technology
In known technology, the coal system of utilization coal gas is arranged, have and utilize the coal preparing natural gas, utilize coal to carry out high temperature, middle temperature, semi-coking, system gas in addition, but above-mentioned processing method is not coal dust to be rolled into a ball caked, will screen the piece material exactly, raw materials cost increases, or institute's aerogenesis calorific value is not high, and added value is little, and economic benefit and social benefit are not remarkable.It is hybrid that the type of heating of stove can be divided into external-heat, internal heat type and the outer heat of interior heat.The heating medium of external-heat stove does not directly contact with raw material, and heat is imported into by the furnace wall; The heating medium of internal heat type stove directly contacts with raw material, because of the difference of heating medium has two kinds of the gentle body heat support methods of solid heat carrier method.
Internal heat type gaseous heat-carrier method is the industrial typical method that has adopted.This method adopts gaseous heat-carrier internal heat type vertical continuous stove, promptly comprises dryer section from top to down, decomposes section and cooling section three parts.(about 25～60mm) from top to bottom move, and directly contact with the burning gas adverse current and are heated for coal low-temperature decomposition brown coal or the type piece that is pressed into by brown coal.About 15% o'clock of the water content of furnace roof raw material removes below the moisture to 1.0% in dryer section, and upstream about 250 ℃ of hot gass are chilled to 80～100 ℃.Dry back raw material is heated to about 500 ℃ in the decomposition section by 600～700 ℃ of oxygen-free burning gas, and thermolysis takes place; Hot gas is chilled to about 250 ℃, and the semicoke of generation enters cooling section and cooled off by cold air.Semicoke is discharged back further water and air cooling.From decomposing section volatile matter of overflowing, obtain tar and pyrolysis water through steps such as condensation, coolings.This type of type of furnace was all once had in Germany, the U.S., the Soviet Union, Czechoslovakia, New Zealand and Japan.
The internal heat type solid heat carrier method is the typical method of solid thermal carriers internal heat type.Raw material is brown coal, noncaking coal, weak caking coal and resinous shale.Be the pilot plant of 10t/h coal in this Teng Jianyou one cover processing power of Germany Dorr the 1950's, and the thermal barrier of use is solid particulate (little porcelain ball, sand or a semicoke).Because the process product gas does not contain waste gas, so the equipment size of after-treatment system is less, caloric power of gas is higher, can reach 20.5～40.6MJ/m
3Therefore this method has very big processing power because the temperature difference is big, and particle is little, and heat transfer is exceedingly fast.The gained liquid product is more, during the processing high volatile coal, productive rate can reach 30%.L-R method technical process coal low-temperature decomposition is at first with the fritter feed coal of preliminary preheating, mixes in mixing tank with the hot semicoke from separator, and the thermolysis effect takes place.Fall into then in the snubber, stop certain hour, finish thermolysis.The semicoke that comes out from snubber enters the riser tube bottom, is submitted by warm air, and burning-off carbon residue wherein in riser tube elevates the temperature simultaneously, enters then and carries out gas solid separation in the separator.Semicoke returns mixing tank again, so circulation.Volatile matter from mixing tank is overflowed through dedusting, condensation and cooling, recovery oils, obtains the higher coal gas of calorific value.
Current, coal resolving device commonly used mainly is to have two kinds, and having a kind of is the shaft furnace structure, and the inflammable gas that this structure combustion product gases and coal produce makes that the purity of combustible gas is low, and added value is low, also has part to discharge, and causes a large amount of wastes of resource and the pollution of environment.Another kind of shaft kiln is that coal cinder is placed on the dividing plate with holes, coal cinder top having heaters, because of the coal cinder on the dividing plate has certain ulking thickness, can not be by even heating, decomposition, need heat, decompose with the gas circulation that is decomposed, what is more important, because a large amount of existence of coal dividing plate cocycle ventilating pit, coal dust can leak down from ventilating pit, so coal dust need be processed coal-forming group earlier when coal dust need enter shaft kiln, separate so coal dust can not be directly used in the kiln body, this has just correspondingly increased the cost that coal dust decomposes, and has reduced economic benefit.
Summary of the invention
The present invention is for solving the problem that exists in above-mentioned technology and the method, proposed a kind of can be directly with the coal dust separating substances, improve its comprehensive utilization value, energy-saving and emission-reduction, thereby the horizontal separating device of coal material multi-combustor that improves the economic and social benefits.
The horizontal separating device of a kind of coal material multi-combustor, the sealing rotary kiln body that comprises an arranged transversely, described rotary kiln body comprises an opening for feed, discharge port, a plurality of burners of solid matter are set along kiln body direction in the described rotary kiln body, a plurality of air intake ducts of a plurality of gas inlet pipes that a plurality of burners one side correspondence of described solid matter is provided with solid matter and the solid matter parallel with gas inlet pipe, described gas inlet pipe and corresponding burner connection, described solid matter air intake duct and corresponding burner connection, the opposite side of a plurality of burners of described solid matter is provided with corresponding a plurality of solid matter radiating pipes, a plurality of burners of described solid matter are connected with corresponding solid matter radiating pipe, correspondence is provided with a plurality of lighter for ignitions in a plurality of burners of described solid matter, a plurality of burners of described solid matter, radiating pipe, gas inlet pipe, form the coal material between air intake duct and the rotary kiln body inwall and advance split tunnel, described coal material advances split tunnel to be communicated with described opening for feed and discharge port, opening for feed place end is provided with the isolated combustion gas of coal on the described rotary kiln body, the tar gas collection tube, described coal separates combustion gas, the tar gas collection tube advances split tunnel to be communicated with the coal material, the other end is connected with combustion gas dedusting liquid body, described solid matter radiating pipe is communicated with flame gas manifold trunk, and described flame gas manifold trunk stretches out outside the rotary kiln.
Described solid matter gas inlet pipe, air intake duct and discharge port are provided with the support rotary slip ring on the kiln tail, described gas inlet pipe, air intake duct and support rotary slip ring flexibly connect, and described support rotary slip ring is relative with the kiln tail to be rotated, slide.
The coal dust propulsive mechanism of kicking up is set on the described rotary kiln body inwall.
The described coal dust propulsive mechanism of kicking up is the plate of raising that is arranged in a large number on the rotary kiln body inwall.
Between described solid matter radiating pipe, solid matter gas inlet pipe, solid matter air intake duct and the rotary kiln body inwall pipeline supporting mechanism is set.
Described flame gas manifold trunk is connected with coal dust drying and preheating mechanism away from an end of solid matter radiating pipe.
Because the horizontal airtight rotary kiln body that the kiln form makes basic horizontal into is decomposed in the setting that the present invention will use always, the intravital gas inlet pipe of rotary kiln, air intake duct is brought air and combustion gas into the burner of solid matter, lighter for ignition is lighted gas mixture, flame source of the gas source after the burning constantly enters the solid matter radiating pipe, the a large amount of heat that produces is by the conduction of solid matter radiating pipe wall, be radiated burner, on the coal dust in the cavity that forms between radiating pipe and the rotary kiln body inwall, absorbed fully by the coal dust that is provided with on the rotary kiln body inwall coal dust that propulsive mechanism kicks up of kicking up, coal dust heats up and decomposes, just in advancing split tunnel, the coal material resolves into combustion gas, the coal that tar gas and calorific value are higher, combustion gas separates combustion gas with tar gas by described coal, the tar gas collection tube is connected with rotary kiln combustion gas dedusting liquid body outward, with the combustion gas that decomposes, tar gas is collected, dedusting, separate, pressurized liquefied.Described solid matter blast main, solid matter gas inlet pipe are provided with the solid matter form, are convenient to fully absorb high temperature and have decomposed the interior heat of coal dust, have made full use of the heat energy that system produces on the one hand, make the temperature of coal dust slowly reduce simultaneously, finally are convenient to store and utilize.Between described solid matter radiating pipe, solid matter blast main, solid matter gas inlet pipe and the rotary kiln body inwall pipeline supporting mechanism is set, further improves bonded reliability and stability between burner and the rotary kiln body; Described flame gas manifold trunk is connected with coal dust drying and preheating mechanism away from an end of solid matter radiating pipe, remaining a large amount of heat energy in the flame gas of assurance after by flame gas manifold trunk is heated up by coal dust preabsorption is dry, improved rate of energy, also improve simultaneously the temperature that enters the preceding coal dust of rotary kiln body greatly, reduced the water content of coal dust.The present invention can fully save and utilize the energy with fine coal decomposition and separation quickly and efficiently, has improved the utilization ratio of coal resource widely and has utilized level, will bring a large amount of economic benefits and social benefit for entire society.
Description of drawings:
The present invention is described further below in conjunction with accompanying drawing:
Fig. 1 is a structural representation of the present invention.
Fig. 2 be among Fig. 1 A-A to sectional view;
Fig. 3 be among Fig. 1 B-B to sectional view.
Embodiment:
As Fig. 1, Fig. 2, shown in Figure 3: the horizontal separating device of a kind of coal material multi-combustor, the sealing rotary kiln body 1 that comprises an arranged transversely, described rotary kiln body 1 comprises an opening for feed 2 and discharge port 3, a plurality of burners 4 of solid matter are set along kiln body direction in the described rotary kiln body 1, a plurality of burners one side correspondence of described solid matter is provided with a plurality of gas line 5 of solid matter and a plurality of solid matter blast mains 6 parallel with gas line, described solid matter gas line 5 is communicated with the burner 4 of solid matter, described solid matter blast main 6 is communicated with the burner 4 of solid matter, the opposite side correspondence of a plurality of burners 4 of described solid matter is provided with a plurality of radiating pipes 7 of solid matter, a plurality of burners 4 of described solid matter are communicated with corresponding solid matter radiating pipe 7, a plurality of burners 4 correspondences of described solid matter are provided with a plurality of lighter for ignitions 8, described solid matter radiating pipe 7, solid matter burner 4, solid matter gas line 5, the cavity that forms between solid matter blast main 6 and rotary kiln body 1 inwall advances split tunnel 9 for the coal material, described coal material advances split tunnel 9 to be communicated with described opening for feed 2 and discharge port 3, the combustion gas outside the rotary kiln body 1 is stretched out in opening for feed 2 place end settings on the described rotary kiln body 1, tar gas collection tube 10, described coal separates combustion gas, tar gas collection tube 10 advances split tunnel 9 to be communicated with the coal material, the other end is connected with combustion gas dedusting liquid body 11, described solid matter radiating pipe 7 is communicated with flame gas manifold trunk 12, and described flame gas manifold trunk 12 stretches out outside the rotary kiln 1.The gas inlet pipe 5 of solid matter in the rotary kiln body 1, the burner 7 that the air intake duct 6 of solid matter is brought combustion gas and air into solid matter is lighted gas mixture in the solid matter burner 4 by lighter for ignition 8, flame source of the gas source after the burning constantly enters solid matter radiating pipe 7, the a large amount of heat that produces is by the conduction of solid matter radiating pipe 7 walls, be radiated on the coal dust in the cavity that forms between burner and rotary kiln body 1 inwall, absorbed fully by the coal dust that is provided with on rotary kiln body 1 inwall coal dust that propulsive mechanism 13 kicks up of kicking up, coal dust heats up and decomposes, just in advancing split tunnel 9, the coal material resolves into combustion gas, tar gas and higher calorific value coal, combustion gas separates combustion gas with tar gas by described coal, tar gas collection tube 10 is connected with the combustion gas dedusting liquid body 11 of rotary kiln outer 1, with the combustion gas that decomposes, tar gas is collected, dedusting, separate, pressurized liquefied.
Described solid matter gas inlet pipe 5, air intake duct 6 are provided with on the kiln tail with discharge port 3 and support rotary slip ring 17, and described gas inlet pipe 5, air intake duct 6 and support rotary slip ring 17 are connected, and described support rotary slip ring 17 is relative with the kiln tail to be rotated, slide.
The setting of the gas inlet pipe 5 of solid matter and the air intake duct 6 of solid matter is convenient to fully absorb the heat in the high temperature coal dust, has made full use of the heat energy that system produces on the one hand, makes the temperature of coal dust slowly reduce simultaneously, finally is convenient to store and utilize.
The coal dust propulsive mechanism 13 of kicking up is set on described rotary kiln body 1 inwall, and the plate of raising that is arranged in a large number on the rotary kiln body inwall 1 advances coal dust to travel forward on the one hand, on the other hand coal dust is more convenient for evenly absorbing a large amount of heat in rotation advances.
Between described solid matter radiating pipe 7, solid matter gas inlet pipe 5, solid matter air intake duct 6 and rotary kiln body 1 inwall pipeline supporting mechanism 14 is set, further improves bonded reliability and stability between burner and the rotary kiln body.
Described flame gas manifold trunk 12 is connected with coal dust drying and preheating mechanism 16 by pipeline 15 away from an end of solid matter radiating pipe 7, remain in the flame gas of assurance after by flame gas manifold trunk 12 a large amount of heat energy by coal dust preabsorption, be dried, improve rate of energy, also improved the temperature that enters the coal dust before the rotary kiln body 1 simultaneously greatly.
Claims (8)
1. horizontal separating device of coal material multi-combustor, the sealing rotary kiln body rotary kiln body that comprises an arranged transversely, described rotary kiln body comprises an opening for feed, discharge port, a plurality of burners of solid matter are set along kiln body direction in the described rotary kiln body, a plurality of air intake ducts of a plurality of gas inlet pipes that one side correspondence of described solid matter burner is provided with solid matter and the solid matter parallel with gas inlet pipe, described gas inlet pipe and corresponding burner connection, described solid matter air intake duct and corresponding burner connection, the opposite side correspondence of a plurality of burners of described solid matter is provided with a plurality of solid matter radiating pipes, a plurality of burners of described solid matter are connected with corresponding solid matter radiating pipe, correspondence is provided with a plurality of lighter for ignitions in a plurality of burners of described solid matter, a plurality of burners of described solid matter, radiating pipe, gas inlet pipe, form the coal material between air intake duct and the rotary kiln body inwall and advance split tunnel, opening for feed place end is provided with the isolated combustion gas of coal on the described rotary kiln body, the tar gas collection tube, described coal separates combustion gas, the tar gas collection tube advances split tunnel to be communicated with the coal material, the other end is connected with combustion gas dedusting liquid body, described solid matter radiating pipe is communicated with flame gas manifold trunk, and described flame gas manifold trunk stretches out outside the rotary kiln.
2. the horizontal separating device of coal material multi-combustor as claimed in claim 1, it is characterized in that: described solid matter gas inlet pipe, air intake duct and discharge port are provided with the support rotary slip ring on the kiln tail, and described gas inlet pipe, air intake duct and support rotary slip ring flexibly connect.
3. the horizontal separating device of coal material multi-combustor as claimed in claim 1 is characterized in that: the coal dust propulsive mechanism of kicking up is set on the described rotary kiln body inwall.
4. the horizontal separating device of coal material multi-combustor as claimed in claim 3 is characterized in that: the described coal dust propulsive mechanism of kicking up is the plate of raising that is arranged in a large number on the rotary kiln body inwall.
5. as claim 1,2, the horizontal separating device of 3 or 4 described coal material multi-combustors, it is characterized in that: between described solid matter radiating pipe, air isocon and the rotary kiln body inwall pipeline supporting mechanism is set.
6. as claim 1,2, the horizontal separating device of 3 or 4 described coal material multi-combustors, it is characterized in that: described flame gas manifold trunk is connected with coal dust drying and preheating mechanism away from an end of solid matter radiating pipe.
7. the horizontal separating device of coal material multi-combustor as claimed in claim 5 is characterized in that: described flame gas manifold trunk is connected with coal dust drying and preheating mechanism away from an end of solid matter radiating pipe.
8. the horizontal separating device of coal material multi-combustor as claimed in claim 1 is characterized in that: described solid matter gas inlet pipe, solid matter air intake duct, solid matter burner, solid matter lighter for ignition, solid matter flame gas radiating pipe are formed the cell cube of a plurality of burning heating.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010262870 CN101985562B (en) | 2010-08-19 | 2010-08-19 | Horizontal coal separating equipment with multiple combustors |
| PCT/CN2010/077032 WO2012022060A1 (en) | 2010-08-19 | 2010-09-17 | Horizontal coal decomposition device with multiple burners |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010262870 CN101985562B (en) | 2010-08-19 | 2010-08-19 | Horizontal coal separating equipment with multiple combustors |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101985562A true CN101985562A (en) | 2011-03-16 |
| CN101985562B CN101985562B (en) | 2011-09-14 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010262870 Active CN101985562B (en) | 2010-08-19 | 2010-08-19 | Horizontal coal separating equipment with multiple combustors |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN101985562B (en) |
| WO (1) | WO2012022060A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104845647A (en) * | 2015-05-05 | 2015-08-19 | 郭秀梅 | Low-rank coal quality-improving pyrolysis equipment |
| US9988577B2 (en) | 2012-02-21 | 2018-06-05 | Xixia Dragon Into Special Material Co., Ltd. | Sleeve-type coal material decomposition apparatus |
| CN113604233A (en) * | 2021-07-09 | 2021-11-05 | 华北电力大学 | Toothed cage type multi-chamber organic solid waste pyrolysis reactor and pyrolysis method thereof |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101985558B (en) * | 2010-08-19 | 2012-01-04 | 西峡龙成特种材料有限公司 | Coal decomposing equipment |
| CN115261035A (en) * | 2022-07-04 | 2022-11-01 | 深圳嘉信量子科技集团有限公司 | Garbage dry distillation system and method |
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| CN2498158Y (en) * | 2001-08-29 | 2002-07-03 | 东南大学 | Pyrolyzer for producing moderate gas from biological materials |
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| US9988577B2 (en) | 2012-02-21 | 2018-06-05 | Xixia Dragon Into Special Material Co., Ltd. | Sleeve-type coal material decomposition apparatus |
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| CN113604233A (en) * | 2021-07-09 | 2021-11-05 | 华北电力大学 | Toothed cage type multi-chamber organic solid waste pyrolysis reactor and pyrolysis method thereof |
| CN113604233B (en) * | 2021-07-09 | 2024-02-02 | 华北电力大学 | Tooth cage type multi-chamber organic solid waste pyrolysis reactor and pyrolysis method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2012022060A1 (en) | 2012-02-23 |
| CN101985562B (en) | 2011-09-14 |
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Effective date of registration: 20150228 Address after: 474500, Henan County, Nanyang province Xixia County town of red stone village industrial agglomeration area Patentee after: Henan Longcheng Coal Efficient Technology Application Co., Ltd. Address before: 474500, Xixia County, Henan province Nanyang County Industrial Park Patentee before: Xixia Longcheng Special Material Co., Ltd. |