CN201628457U - Coal oxygen-free drying device and drying system - Google Patents
Coal oxygen-free drying device and drying system Download PDFInfo
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- CN201628457U CN201628457U CN2009202239882U CN200920223988U CN201628457U CN 201628457 U CN201628457 U CN 201628457U CN 2009202239882 U CN2009202239882 U CN 2009202239882U CN 200920223988 U CN200920223988 U CN 200920223988U CN 201628457 U CN201628457 U CN 201628457U
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Abstract
The utility model relates to a coal oxygen-free drying device and a coal oxygen-free drying system. The coal oxygen-free drying device comprises a vertical drying cylinder, a coal inlet, a coal outlet, a gas inlet pipe and a gas outlet pipe, wherein the outer sides of the two side walls of the drying cylinder are respectively provided with hot gas cavities; a certain number of row pipes or row plates are communicated between the two hot gas cavities, so that the coal in the drying cylinder is completely isolated from the hot gas in the hot gas cavities and the row pipes or the row plates; and a steam pipe is led out of the drying device in the drying cylinder. The coal oxygen-free drying system comprises the coal oxygen-free drying device and also comprises a heating system, wherein a thermometer T1 and a thermometer T2 are respectively arranged at the ports of the mouths of the gas inlet pipe and the gas outlet pipe; and a discharge valve and a thermometer T0 are arranged at a discharge hole. By controlling the temperature, the coal oxygen-free drying device and the coal oxygen-free drying system can not only be applicable to drying common coal and coal slime, but also be applicable to drying brown coal and improving the quality of the brown coal; the coal oxygen-free drying device and the coal oxygen-free drying system can not only remove the surface moisture of the brown coal, but also remove part of combined water, and the brown coal is converted from the soft coal to the hard coal and from the hydrophily to the hydrophobicity, thereby facilitating transportation, storage and use and being very beneficial for promotion and implementation.
Description
One, technical field:
The utility model relates to a kind of coal drying and modification technology, particularly relates to a kind of coal anaerobic drying device and drying system.
Two, background technology:
According to statistics, about 26,229 hundred million tons of whole world brown coal reserves account for 24.4% of world's coal gross reserves.The lignite resource amount that China has been found that is 1291.32 hundred million tons, accounts for Chinese coal and possesses 12.7% of stock number.Because it is very shallow apart from the face of land that brown coal form, be suitable for strip mining transformation, therefore cheap.But also there are following distinct issues in brown coal:
1, moisture height, calorific value is low, and the general water content of brown coal is between 30% to 65%, and general calorific value is about 3000kcal/kg.
2, density is low, and easy-weathering is met the water spontaneous combustion, sells radius and is no more than 500 kilometers.
In order to address the above problem, many in the world companies have carried out brown coal drying, upgrading and study on the modification, and minority technology has begun industrialization, and major part is also in the experimental study stage.Most brown coal drying technology is divided into two classes, is the contact drying of dry media with high-temperature flue gas or the vehicular direct contact drying of air with superheated steam.Because brown coal when drying, have fuel gas and separate out,, then be easy to take place the possibility of catching fire or exploding of drying system if adopt with high-temperature flue gas or the vehicular direct contact drying of air.So industrialized brown coal drying mainly is to be the contact drying of dry media with superheated steam at present.But with superheated steam is the contact drying brown coal drying of dry media, because its temperature levels restriction can only remove surface water, can't remove in conjunction with water.If brown coal only remove surface water, do not remove in conjunction with water, dried brown coal the phenomenon of getting damp can occur in long-distance transport or long storage time, therefore relatively be fit to dried brown coal and use immediately, handle such as the raw material drying of the brown coal drying of near coal-mine power plant or near the Coal Chemical Industry project the colliery.Only remove in conjunction with water, the character of brown coal just can change, and can transport as hard coal, deposits and uses.
How can remove brown coal in conjunction with water, thereby realize the brown coal modification, the browning coal is a hard coal, is the great problem that we are faced in clean coal field.
According to discovering, brown coal are heated to 100 degree when above under normal pressure, and most Free water can be evaporated.When brown coal moisture is lower than 15%, if need to continue dry and dehydration, when promptly removing in conjunction with water and since brown coal with combine water stronger adhesion arranged, then need higher temperature and energy to carry out.When brown coal continue to be heated to 180 degree when above under normal pressure, brown coal can be removed in conjunction with water (inherent water).When the brown coal temperature is higher than 150 when spending, hydroxy functional group (mainly is-COOH) decompose, separates out CO2 gas, simultaneously getting rid of in conjunction with water (inherent water) brown coal.Further improve temperature, will cause increasing hydroxy functional group to decompose, thereby the surface nature that causes brown coal changes.
Under this baking temperature condition,, cause the pore of brown coal inside to decay and produce crosslinked because a large amount of hydroxy functional group decomposes.Pore decays and can stop moisture to enter pore; Cross-linking reaction then can seal pore, stops the pore that decays to expand when absorbing moisture again.
In addition, when the brown coal temperature is heated to 200 degree when above, its surface area can significantly reduce.The main cause that surface area reduces is that promptly tar is moved to the pore outside by pore inside owing to cause the strong migration of the tar of brown coal inside under the high temperature drying condition.The tar of moving to the pore outside in cooling procedure, thereby since tar condensing pore is sealed, thereby the surface area of brown coal reduces together.
Because said process, promptly pore collapses, and cross-linking reaction and tar migration form sealing to pore, and brown coal become more and more hydrophobic as a result, also can observe the sclerosis of brown coal simultaneously, and this also causes the formation of the rigid structure of brown coal.Its result is exactly that brown coal can be converted to hard coal from cherry coal, is converted to hydrophobicity by hydrophily, thereby can realizes the long-distance transport of brown coal.
Coal damping (Coal Moisture Control is called for short CMC) is the abbreviation of " shove charge moisture content of coal control technology ", is that coking coal materials is removed portion of water before shove charge, keeps the shove charge moisture content of coal to be stabilized in about 6% shove charge coking then.CMC is different from coal preheating and coal drying, and CMC has strict moisture control measure, can guarantee into the stove moisture content of coal constant.Reduce and the stable moisture of controlling the stove coal by direct or indirect heating, do not pursue the moisture of removing people's stove coal to greatest extent, and only moisture stabilization in low relatively level, both can reach the purpose that increases benefit, do not cross the low difficulty that causes the operation of coke oven and recovery system again because of moisture, make the increase of people's stove coal density, coke and chemical products volume increase, coke oven heating with the coal gas amount reduce, effect such as coke quality improves and coking technique is stable.
The coal conditioning technique obtains tremendous development in Japan over nearly 10 years, by in October, 2000, in 47 groups of coke ovens of the existing 15 tame coke-oven plants of Japan, has 28 groups of coke ovens and adopts the CMC technology.Japan has successively developed three generations's coal conditioning technique.
The first generation is the heat kerosene drying mode.Utilize conduction oil to reclaim the waste heat of coke oven flue gas and the sensible heat of coke oven coke oven uprising tube, then, in multi-tube revolving drier, conduction oil carries out indirect to coal charge, thereby makes the coal charge drying.In September nineteen eighty-three, the first cover conduction oil coal humidity control device is constructed and put into operation in the big subsidiary factory of Japan.
The second generation is the steam drying mode.Utilize back pressure vapour after the dry coke quenching steam-electric power or other low-pressure steam in the factory as thermal source, in multi-tube revolving drier, steam carries out the indirect drying to coal.This CMC is early than going into operation at Japanese monarch Jin Chang and Fushan factory the beginning of the nineties in last century.At present, the CMC overwhelming majority in Japan's operation is this kind pattern.
The third generation is the fluidized bed plant of latest generation, is provided with hot-blast stove, adopts coke oven flue waste gas or coke-stove gas to its drying mode that heats.
In recent years, countries such as the U.S., Germany all began to carry out the test and the production practices of shove charge coal humidity control device, all obtained good economic the effect
Because coal has strong wear, there is the heat exchanger serious wear problem in the drying machine in the drying machine of the first generation and second generation drying mode, often needs more switching heat-exchanger.Because there is the big problem of power consumption in fluidized bed drying, third generation drying mode drying cost is higher.
Three, utility model content:
The coal drying technology that coal anaerobic drying device of the present utility model and drying system propose with regard to being based on above-mentioned discovering, this technology is not only applicable to common coal (comprising brown coal) and removes surface water, can also remove brown coal internal junction Heshui, brown coal are converted to hard coal from cherry coal, be converted to hydrophobicity by hydrophily, can realize that brown coal can transport as bituminous coal to deposit and use.Specifically provide a kind of coal anaerobic drying device and drying system.
Technical scheme:
A kind of coal anaerobic drying device comprises vertical drying, is respectively equipped with coal feed point and coal outlet at the drying upper and lower end, and be installed with air inlet pipe on drying top, the bottom is installed with escape pipe; Perhaps be installed with air inlet pipe at drying middle part, top is installed with escape pipe; Perhaps be installed with air inlet pipe in the drying bottom, top is installed with escape pipe; Be respectively equipped with and drying isolation and hot air cavity independent of each other in the outside (along vertical direction) of described vertical drying two side, and two independently be communicated with between the hot air cavity some comb or row plate, described escape pipe, air inlet pipe are communicated with different hot air cavity respectively, the coal that is dried enters drying by gravity from the upper end coal feed point and discharges from the lower end coal outlet, slowly moves from top to bottom.The coal that is positioned at drying is isolated fully with the hot gas that is positioned at hot air cavity and comb or row's plate, thereby guarantees that coal drying is in the anaerobic drying regime in the drying device, guarantees dry security of operation.Also be provided with steam pipe in drying inside, steam pipe is drawn the drying device outside.Steam, flammable other (the containing carbon monoxide) of discharging for steam pipe according to circumstances both can directly have been discharged and entered atmosphere, can process also that the back is discharged or recycling again.
Also laterally be provided with dividing plate in the hot air cavity of the same side, make hot air cavity upper and lower independently of one another, thereby form a plurality of hot air cavity independent of each other.Described hot air cavity is a totally enclosed type, not only with the drying internal insulation, also is isolated from the outside, the hot flue gas of air inlet pipe at first enters the hot air cavity of first sealing, to another hot air cavity, baffling is up or down finally discharged from escape pipe so repeatedly along comb or row's plate current.
Blow-off valve is installed on coal outlet; And thermometer T is installed on coal outlet
0
The flue gas comb that is communicated with between different hot air cavity or row's plate be baffling up or down, and the baffling number of times is 1～20.
A kind of coal anaerobic drying system, comprise described coal anaerobic drying device, also comprise heating system, the heating flue gas efferent duct of heating system is communicated with the air inlet pipe of coal anaerobic drying device, is separately installed with thermometer T at smoke inlet pipe mouth, the flue gas of the drying device mouth of pipe of giving vent to anger
1, T
2, the place is provided with blow-off valve and thermometer T at drying device bottom discharge mouth
0Drying inside at coal anaerobic drying device also is provided with steam pipe, steam pipe is drawn the drying device outside, this steam pipe is drawn the directly discharging of the drying device outside, perhaps make combustible gas and the discharging of steam after separating through the fuel gas separator, the fuel gas after the separation is introduced into the heating system burning.
Described fuel gas separator is a cyclone.
Simultaneously on the escape pipe of coal anaerobic drying device, be provided with breeches pipe, between breeches pipe and the air inlet pipe by the air-introduced machine formation flue gas recirculation that is connected.From the gas that escape pipe is discharged, can all discharge, also only a part is discharged from, and another part is introduced air inlet pipe once more and is done recycling together.
Described heating system comprises combustion furnace, between combustion furnace and flue gas efferent duct the high-temperature flue gas expansion chamber is installed also, the dust in the high-temperature flue gas is eliminated as far as possible being beneficial to environmental protection.
The beneficial effects of the utility model:
1, the problem that exists based on prior art of coal anaerobic drying device of the present utility model and drying system and the coal drying technology that proposes, be not only applicable to common coal and coal slime drying, also be applicable to brown coal drying and upgrading, can not only remove the surface moisture of brown coal during brown coal drying, can also be by control input, output flue-gas temperature, and the final coal temperature of control discharging opening, remove part in conjunction with water.
2, by drying device of the present utility model, brown coal are removed surface water and in conjunction with water, it can be become hard coal by cherry coal, become hydrophobicity by hydrophily, thereby can transport for long-distance.
3, the coal that is dried by airtight circuitous folding pipe does not directly contact with flue gas, has thoroughly solved coal and has separated out and cause the problem of catching fire and exploding owing to fuel gas in dry run.
4, the recycling one side of thermal cycle utilization and tail gas reduces the energy consumption of dry run, also significantly reduces the discharging of tail gas simultaneously.
5, coal anaerobic drying system of the present utility model is taked vertical type drying apparatus, and coal is from top to bottom slowly to move by gravity, has overcome the heat exchanger serious wear problem of the drying machine of the first generation in the coal humidifying technology and second generation drying mode.And the flowing velocity of flue gas is low in the vertical drying machine, overcomes the big problem of third generation drying mode power consumption, is drying mode of new generation, can replace the first, the second and third generation drying mode.
6, in addition, coal anaerobic drying device of the present utility model can also be used for chemical products, industry and municipal sludge drying, the drying of materials such as metal and nonmetallic mineral.
Four, description of drawings:
Fig. 1 is one of coal anaerobic drying device cross-sectional view of the present utility model;
Fig. 1-the 1st, the C portion structure for amplifying schematic diagram of Fig. 1;
Fig. 1-2 is the A-A cross-sectional view of Fig. 1-1;
Fig. 1-the 3rd, certain section perspective view of Fig. 1;
Fig. 2 is two of a coal anaerobic drying device cross-sectional view of the present utility model;
Fig. 2-the 1st, the B-B cross-sectional view of Fig. 2;
Fig. 2-the 2nd, the D-D cross-sectional view of Fig. 2;
Fig. 2-the 3rd, single row's plate structure schematic diagram;
Fig. 2-the 4th, certain section perspective view of Fig. 2;
Fig. 3 is three of a coal anaerobic drying device cross-sectional view of the present utility model;
Fig. 3-the 1st, the left view of Fig. 3;
Fig. 4 is four of a coal anaerobic drying device cross-sectional view of the present utility model;
Fig. 5 is four of a coal anaerobic drying device cross-sectional view of the present utility model;
Fig. 6 is one of coal anaerobic drying system structural representation of the present utility model;
Fig. 7 is two of a coal anaerobic drying system structural representation of the present utility model;
Fig. 8 is three of a coal anaerobic drying system structural representation of the present utility model.
Number in the figure 1 is the external sidewall of hot air cavity, and 2 is support, and 3 is the drying device air inlet pipe, 4 is the drying device escape pipe, and 5 is charging aperture, and 6 is comb, 7 is the drying sidewall, and 8 is the hot gas cavity, and 9 is steam pipe, 10 is discharging opening, and 11 is blow-off valve, and 12 is diaphragm plate, 13 is the fuel gas separator, and 14 is the steam air-introduced machine, and 15 is the fuel gas return pipe, 16 is air inlet pipe, and 17 is escape pipe, and 18 is the escape pipe breeches pipe, 19 is the air exhauster of installing on the escape pipe, 20 is exhaust breeches pipe on the escape pipe, and 21 is combustion furnace, and 22 are the burning blower fan, 23 is the high temperature expansion chamber, 24 are row's plate, and 25 is the flue gas upper return tube, T
0Be discharging opening thermometer, T
2Be escape pipe mouth of pipe thermometer, T
1Be air inlet pipe mouth of pipe temperature
Five, the specific embodiment:
Embodiment one: referring to Fig. 1, Fig. 1-1, Fig. 1-2, Fig. 1-3, a kind of coal anaerobic drying device, comprise vertical drying 7, be respectively equipped with coal feed point 5 and coal outlet 10 at drying 7 upper and lower ends, and be installed with escape pipe 17, bottom or middle part on drying 7 tops and be installed with air inlet pipe 16.
Described vertical drying 7 (about) outside (along vertical direction) of relative two side is respectively equipped with and drying 7 is isolated and hot air cavity independent of each other 8, and at two combs 6 that independently are communicated with some between the hot air cavity 8.
Also laterally be provided with the diaphragm plate 12 of some in two neighbouring hot air cavity 8, make hot air cavity be split into a plurality of hot air cavity independent of each other from the top down.Described hot air cavity 8 is a totally enclosed type, not only with drying 7 internal insulation, also is isolated from the outside, the hot flue gas of air inlet pipe 16 at first enters the hot air cavity of first sealing, to another hot air cavity, baffling is up or down finally discharged from escape pipe 17 so repeatedly along comb or row's plate current.The baffling number of times of the flue gas comb that is communicated with between different hot air cavity is 1～20.
The coal that is dried enters drying by gravity from upper end coal feed point 5 and discharges from lower end coal outlet 10, slowly moves from top to bottom.The coal that is positioned at drying 7 is isolated fully with the hot gas that is positioned at hot air cavity 8 and comb 6, thereby guarantees that coal drying is in the anaerobic drying regime in the drying device, guarantees dry work safety.Also be provided with steam pipe 9 in drying 7 inside, steam pipe is drawn the drying device outside.The steam of discharging for steam pipe, fuel gas compositions such as () carbon monoxide according to circumstances both can directly discharge and enter atmosphere, discharged after also can isolating fuel gas earlier again.
Blow-off valve 11 is installed on coal outlet 10; Thermometer T is installed on coal outlet
0
Present embodiment is not only applicable to the surface water drying to common coal or brown coal, also is applicable to removing brown coal internal crystallization water, and is safe and reliable.
Embodiment two: referring to Fig. 2, Fig. 2-1, Fig. 2-2, Fig. 2-3, Fig. 2-4, number identically with embodiment one, meaning is identical, and something in common does not repeat, and different is: change described comb into as Fig. 2-3 described row's plate 24.
Embodiment three: referring to Fig. 3, Fig. 3-1, number identical with embodiment one, meaning is identical, something in common does not repeat, different is: air inlet pipe 16 is positioned at drying 7 middle parts, the downward baffling discharging of the hot air cavity at hot gas sequence of flow self-desiccation tube middle part, and then upwards draw flue gas return pipe 25 by the hot air cavity of drying bottom and be communicated in the hot air cavity of air inlet pipe 16 tops, baffling upwards successively finally flows to escape pipe 17 again.Present embodiment is fit to the surface water drying to common coal or brown coal, also is fit to chemical industry certainly, and metal and nonmetallic mineral etc. carries out drying.
Embodiment four: referring to Fig. 4, number identically with embodiment one, meaning is identical, something in common does not repeat, different is: air inlet pipe 16 is positioned at drying 7 tops, and the hot air cavity on hot gas sequence of flow self-desiccation tube top is baffling discharging successively downwards, finally flows to the escape pipe 17 of drying bottom.Present embodiment is fit to the surface water drying to common coal or brown coal, also is fit to chemical industry certainly, and metal and nonmetallic mineral etc. carries out drying.
Embodiment five: referring to Fig. 5, number identical with embodiment one, meaning is identical, something in common does not repeat, different is: left and right each independently both be communicated with comb between the hot air cavity, the row's of being connected with plate again, its layout structure be mixed-arrangement how also, be presented at each independent hot air cavity about the about 1/3 section row's of the employing plate connection in drying device top in Fig. 5, each independent hot air cavity about the comb connection is adopted for about 2/3 section in the bottom.
Embodiment six: referring to Fig. 6, a kind of coal anaerobic drying system, comprise embodiment one described coal anaerobic drying device, also comprise heating system, the heating flue gas efferent duct of heating system is communicated with the air inlet pipe 16 of coal anaerobic drying device, is separately installed with thermometer T at smoke inlet pipe mouth, the flue gas of the drying device mouth of pipe of giving vent to anger
1, T
2, the place is provided with blow-off valve and thermometer T at drying device bottom discharge mouth
0, also being provided with steam pipe 9 in the drying inside of coal anaerobic drying device, steam pipe is drawn the drying device outside, and this steam pipe is drawn the directly discharging of the drying device outside.
On the escape pipe 17 of coal anaerobic drying device, be provided with simultaneously breeches pipe (return duct) 18, between breeches pipe 18 and the air inlet pipe 16 by the air-introduced machine 19 formation flue gas recirculation that is connected.
Described heating system comprises combustion furnace, between combustion furnace and flue gas efferent duct the high-temperature flue gas expansion chamber is installed also, the dust in the high-temperature flue gas is eliminated as far as possible being beneficial to thermal cycle.
Embodiment seven: referring to Fig. 7, number identical with embodiment five, meaning is identical, something in common does not repeat, different is: be communicated in fuel gas separator 13 after each steam pipe 9 gathers and make combustible gas and steam after separating, steam is discharged from by air intake machine 14, and the residue fuel gas is introduced into the heating system burning by return pipe 15.Described fuel gas separator 13 is a cyclone.
Embodiment eight: referring to Fig. 8, number identically with embodiment five, meaning is identical, and something in common does not repeat, and different is: from the gas that escape pipe is discharged, all discharge or do the vent gas treatment that is beneficial to environmental protection.The flue gas of discharging at the flue gas escape pipe does not constitute circulation with smoke inlet pipe, and this mode can improve the input temp of smoke inlet pipe as far as possible.
Claims (10)
1. a coal anaerobic drying device comprises vertical drying, is respectively equipped with coal feed point and coal outlet at the drying upper and lower end, and be installed with air inlet pipe on drying top, the bottom is installed with escape pipe; Perhaps be installed with air inlet pipe at drying middle part, top is installed with escape pipe; Perhaps be installed with air inlet pipe in the drying bottom, top is installed with escape pipe; It is characterized in that: be respectively equipped with in the outside of described vertical drying two side with drying and isolate and hot air cavity independent of each other, and, coal and hot air cavity in the drying and comb or the interior hot gas of row's plate are isolated fully at two comb or the row's plates that independently are communicated with some between the hot air cavity; Described escape pipe, air inlet pipe are communicated with different hot air cavity respectively, also are provided with steam pipe in drying inside, and steam pipe is drawn the drying device outside.
2. coal anaerobic drying device according to claim 1 is characterized in that: the different hot air cavity of the same side is provided with dividing plate, makes hot air cavity upper and lower independently of one another.
3. coal anaerobic drying device according to claim 1 is characterized in that: blow-off valve is installed on coal outlet.
4. coal anaerobic drying device according to claim 1 is characterized in that: thermometer is installed on coal outlet.
5. coal anaerobic drying device according to claim 1 is characterized in that: the flue gas comb that is communicated with between different hot air cavity or row's plate be baffling up or down, and the baffling number of times is 1～20.
6. coal anaerobic drying system, comprise the described coal anaerobic drying device of claim 1, also comprise heating system, it is characterized in that: the hot flue gas efferent duct of heating system is communicated with the air inlet pipe of coal anaerobic drying device, is separately installed with thermometer T at smoke inlet pipe mouth, the flue gas of the drier mouth of pipe of giving vent to anger
1, T
2, the place is provided with blow-off valve and thermometer T at drier bottom discharge mouth
0, also being provided with steam pipe in the drying inside of coal anaerobic drying device, steam pipe is drawn the drying device outside, and this steam pipe is drawn the directly discharging of the drier outside, is perhaps introduced heating system again and carries out exhaust combustion.
7. coal anaerobic drying system according to claim 6 is characterized in that: simultaneously on the escape pipe of coal anaerobic drying device, be provided with breeches pipe, between breeches pipe and the air inlet pipe by the air-introduced machine formation flue gas recirculation that is connected.
8. coal anaerobic drying system according to claim 6 is characterized in that: steam pipe is communicated in the fuel gas separator and makes combustible gas and the discharging of steam after separating, and the fuel gas after the separation is introduced into the heating system burning.
9. coal anaerobic drying system according to claim 8 is characterized in that: described fuel gas separator is a cyclone.
10. coal anaerobic drying system according to claim 6 is characterized in that: described heating system comprises combustion furnace, between combustion furnace and flue gas efferent duct the high-temperature flue gas expansion chamber is installed also.
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| CN2009202239882U CN201628457U (en) | 2009-10-12 | 2009-10-12 | Coal oxygen-free drying device and drying system |
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| CN2009202239882U CN201628457U (en) | 2009-10-12 | 2009-10-12 | Coal oxygen-free drying device and drying system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101762145B (en) * | 2009-10-12 | 2011-09-07 | 郑州拉姆顿清洁能源工程技术有限公司 | Coal anaerobic drying device and drying system |
| CN102840748A (en) * | 2012-09-21 | 2012-12-26 | 山西鑫立能源科技有限公司 | Hot water gas dehydration device for low rank bituminous coal |
| CN104039455A (en) * | 2011-05-20 | 2014-09-10 | 克劳迪亚斯·彼得斯工程有限责任公司 | Installation and method for the mill drying and storage of brown coal |
| CN107289772A (en) * | 2016-03-30 | 2017-10-24 | 中国石油化工股份有限公司 | The water lift drying means of mobile bed drying tower and feed coal |
-
2009
- 2009-10-12 CN CN2009202239882U patent/CN201628457U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101762145B (en) * | 2009-10-12 | 2011-09-07 | 郑州拉姆顿清洁能源工程技术有限公司 | Coal anaerobic drying device and drying system |
| CN104039455A (en) * | 2011-05-20 | 2014-09-10 | 克劳迪亚斯·彼得斯工程有限责任公司 | Installation and method for the mill drying and storage of brown coal |
| CN102840748A (en) * | 2012-09-21 | 2012-12-26 | 山西鑫立能源科技有限公司 | Hot water gas dehydration device for low rank bituminous coal |
| CN102840748B (en) * | 2012-09-21 | 2014-08-13 | 山西鑫立能源科技有限公司 | Hot water gas dehydration device for low rank bituminous coal |
| CN107289772A (en) * | 2016-03-30 | 2017-10-24 | 中国石油化工股份有限公司 | The water lift drying means of mobile bed drying tower and feed coal |
| CN107289772B (en) * | 2016-03-30 | 2020-05-19 | 中国石油化工股份有限公司 | Moving bed drying tower and method for drying raw coal by lifting water |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20101110 Effective date of abandoning: 20091012 |