CN1583955A - Vertical automatic cokery with cold loading and cold discharge - Google Patents
Vertical automatic cokery with cold loading and cold discharge Download PDFInfo
- Publication number
- CN1583955A CN1583955A CNA2004100443701A CN200410044370A CN1583955A CN 1583955 A CN1583955 A CN 1583955A CN A2004100443701 A CNA2004100443701 A CN A2004100443701A CN 200410044370 A CN200410044370 A CN 200410044370A CN 1583955 A CN1583955 A CN 1583955A
- Authority
- CN
- China
- Prior art keywords
- coke
- coal
- cold
- gas
- heat exchanger
- 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.)
- Granted
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Coke Industry (AREA)
Abstract
This invention is a kind of new-type vertical continuous coke oven, and a high-temperature dry distillation coking device of coal. The main characteristic of this invention is: After the cool furnace roof holds the coal, are urged to fall by the jar of hydraulic pressure of the furnt device, arrange the burnt device, list while being cool by stove bottom finally, dry distillation coal gas a part that course produce melt down and heat, the others support downstream production need; Air after preheating by heat exchanger, is it set up by oblique way fire dish mix burning with coal gas to enter, the high-temperautre waste gas after burning is discharged by the horizontal passway of the waste gas in the top of combustion chamber, retrieve heat energy for the power plant of remaining energy.
Description
Technical field
The present invention is a kind of novel vertical continuous coke oven, belongs to coal high temperature carbonization coking device.
Background technology
The type of furnace of conventional coke making process is mainly the horizontal-chamber type pit kiln of batch production, this kind type of furnace is created in the middle of the 19th century, through the development in century more than one, though significant progress has been arranged at aspects such as throughput, coke quality, heat energy utilization, mechanize levels.But because still there is the disadvantage that environment is caused severe contamination in its inherent batch mode of operation.In the coking production process, production operation such as this type of furnace must at high temperature frequently be opened fire door, coalings, discharged of the coke, quenching, thus cause serious topsoil.In recent years, all transforming existing coking equipment, seek more economical method and produce high-quality coke both at home and abroad to adapt to strict day by day environmental regulation.In conventional coke oven production process, the most serious pollution section be hotly coaling, hot the discharging of the coke.This process contains a large amount of BaP, SO because hot charging heat goes out in the paroxysmal raw gas, coal dust, burnt dirt of institute's loss
2, H
2S, NO
x, atmospheric polluting material such as TSP, these pollutents must be collected improvement.Present improvement method mainly is to join burning, washing and purification association system, coke guide on employing high pressure aqua ammonia (or steam) injection, the coal charger to join dust-removal system, or solve the technology such as process pollution of the discharging of the coke of coalingging with ground station for dust removal, as a coke-oven plant that produces 600000 tons of coke per year, only this item environmental protection investments are up to more than 2,000 ten thousand yuan, but also thoroughly decontamination.On extinguishing technique, what most of coal chemical enterprises adopted is the low wet quenching technology of investment, water sprays cooling to about 1000 ℃ high temperature coke, this process not only can produce pollutents such as containing dust in a large number and enter atmosphere with water vapour, and burnt meeting per ton consumes the above precious water resource of 400kg; Red Jiao per ton has 1.3 * 10 at least
6The KJ sensible heat is wasted; Conventional dry quenching(of coke) technology is to utilize rare gas element to cool off red Jiao, rare gas element after heat absorption is again with the heat transferred boiler, by recirculation blower rare gas element being sent into the dried stove internal recycle that puts out again uses, this device need meet Jiao, fortune is burnt, dress is burnt, dried putting out, coke discharging, control of dust, facility and equipment such as rare gas element circulation and waste heat boiler such as coke breeze storing, it is many that this technology has in the circulation gas dust, flow process is tediously long, facility is numerous and jumbled, invest high, shortcomings such as production cost is big, one cover processing power is the large-scale a complete set of dry coke quenching auxiliary of 60t/h, its investment is up to more than 200,000,000 yuan, only the burnt investment of dry coke quenching ton is just more than 400 yuan, even so, still have a certain amount of CO, SO
2Enter atmosphere Deng obnoxious flavour.For the leakage that fire door, bell, upcast etc. are located, present measure only can be frequently repairing or more exchange device.For further reducing the uncontrollable discharge of pollutent, take to strengthen the coking chamber volume, reduce the discharging number of times and the quantity of pollutent by the control number of times of coming out of the stove, as the huge reactor of Germany, pollution-free capacity coke oven of 21 century high yield of Japan or the like.Shortcoming that above-mentioned technology exists all that investment is high, production cost is high, technical difficulty is big etc., these effort only are a kind of simple " treat the head when the head aches, pin cure pin bitterly " ways, can not tackle the problem at its root.Developed country is because environmental regulation is strict day by day, this traditional regenerator coke oven, and the investment cost of environmental protection installation has accounted for 30～40% of whole plant investment, and domestic general coke-oven plant is also 15～20%.Simultaneously, the horizontal-chamber type pit kiln is for guaranteeing that coke quality must adopt cohesiveness coal preferably, high-quality caking coal is in great shortage in the world at present, if do not break through this defective workmanship from technology, can not increase weakly caking coal and non-caking coal proportioning, in time about 30 years, coking industry will be subjected to very big restriction because of the exhaustion of coking coal resource.
In order to solve the defective that above-mentioned conventional pit kiln exists, Ukraine coal chemistry institute once began to carry out testing laboratory's work of continuous stratiform coking in 1974, nineteen eighty-three begins to execute builds the pilot-plant test stove, began to execute in 1988 and build industrial furnace, the back is because of reasons such as insufficient funds, the work of building of executing of industrial furnace is stagnated, and fails to make the research project to realize industrialization.Horizontal quirk structure is adopted in the combustion chamber of this continuous stratiform coking device, effectively controls the body of heater coal gas expense of each section up and down; Its body of heater bottom is provided with regenerator, utilizes the heat preheated air of high-temp waste gas; Extinguishing technique is that medium carries out dry coke quenching with the rare gas element.But still there are some problems in this device: because horizontal quirk intensity is low, for proof strength has increased brick using amount; Horizontal quirk limited coke oven wide to increase; Use the regenerator preheated air, make the coke oven construction complexity and increased investment, and make complicated operationization; Use the rare gas element dry coke quenching, medium-gas constantly increases, and has dust to enter in the gas, causes its complex structure, investment height, takes up space greatly; The sensible heat of heating gas not do not reclaim and the coal supply cloth unreasonable or the like.
Summary of the invention
The present invention is the continuous coke oven of a kind of novel upright structures of design, realize cold conditions the discharge of the coke automatic continuous production technology of fully-closed of cold conditions of coalingging, make coal charge in retort process, realize hot pressing, the consumption that enlarges weak caking coal and non-caking coal is more than 50%, in body of heater, realize simultaneously the indirect dry coke quenching of single hole connection journey, have characteristics such as low input, less energy-consumption, low cost, low pollution, high quality, high labour productivity, floor space are few.This invention is realizing the cleaning production of coal chemical enterprise, and to pollute with source control be principle of design, changes the production model of traditional coal chemical enterprise, effectively solves environment protection that traditional pit kiln exists and the contradiction between investment and the economic benefit.
Cold charge of the present invention is cold to go out the full-automatic continuous coke oven of vertical type, it is made up of alternately coking chamber, combustion chamber and furnace roof, chute, dry coke quenching auxiliary, coke discharging device, it is characterized in that, top of combustion chamber is provided with the waste gas horizontal channel, and the waste gas leadout hole that links to each other with the waste gas horizontal channel; The chute position is provided with upright air flue and horizontal gas pipe; Coking chamber and bottom, combustion chamber are dry coke quenching auxiliary and coke discharging device, wherein dry coke quenching auxiliary by high-temperature heat exchanger, in warm interchanger, low temperature heat exchanger and coke cooling channel form.High-temperature heat exchanger is that refractory materials is built by laying bricks or stones, in, low temperature heat exchanger is metal construction, the low temperature heat exchanger place is provided with gas inlet, bottom, coke cooling channel is provided with the cooled coal gas inlet, the type of cooling is the indirect dry coke quenching of single hole connection journey.The coke discharging device by coke extractor, coke discharge box, water seal connect burnt case, scraper conveyor is formed; The coke oven top also is provided with long coal bunker to layout, and coal bunker has funnel, and each funnel is connected with the material distributing machine of the coking chamber side that per two one words are arranged; Coking chamber side top is provided with the side distributing trough, and top is provided with presses coal coke pushing plate, presses coal coke pushing plate by the Driven by Hydraulic Cylinder that is installed on the back timber of coking chamber top; Upright quirk is adopted in the combustion chamber, and these quirks are continuous heating quirk; Top of combustion chamber is provided with the waste gas horizontal channel, is the rapid heating section, and this position is provided with the waste gas leadout hole that links to each other with the waste gas horizontal channel; Coking chamber is divided into the section of coalingging, rapid heating section, retort section from top to bottom, and warm coal gas leadout hole and coal gas of high temperature leadout hole during wherein the retort section place is provided with directly communicate with coking chamber.
This is invented after the furnace roof cold conditions is coaling, descending by the furnace roof Driven by Hydraulic Cylinder, under the condition of secluding air through rapid heating section, retort section, dry coke quenching auxiliary, coke discharging device, discharge by the furnace bottom cold conditions at last, the coal gas part that retort process produces is melted down heating, and all the other produce required for derived product; Air enters flue and coal gas mixed firing through chute after the heat exchanger preheating, the high-temp waste gas after the burning is discharged through the waste gas horizontal channel of top of combustion chamber, gives cogeneration factory and reclaims heat energy.Its detailed process is: coal charge is closed down material distributing machine after being covered with coking chamber top side distributing trough by material distributing machine, then coal is put into the coking chamber top section of coalingging, when needing to press the coal coke pushing, press coal coke pushing plate to push downwards by hydro-cylinder, reach certain stroke and pressure after, enter next circulation; Press the coal process can make the coal charge that is in the plastic stage in the coking chamber be able to hot pressing, effectively improve the consumption of weak caking coal.Coal charge enters the rapid heating section by the section of coalingging, and makes the coal charge quick coking when destructive distillation near coking chamber wall place form duricrust rapidly, so that the coke direct motion, then coal charge further goes downwards to retort section destructive distillation coking.Coke after the maturation enters the coke cooling channel of dry coke quenching auxiliary.The width of coking chamber is decided according to coal, when getting wide coking chamber, for red Jiao is adequately cooled, coke is after retort section enters dry coke quenching auxiliary, become two passages by a passage, so that the heat of coke can be passed to air by heat exchanger wall quickly, coke is in the descending process of shunting, freezing air by low, in the partition wall of warm exchanger wall and high-temperature heat exchanger, indirectly and fully coke is cooled off, promptly absorb red burnt sensible heat, make about preheating of air to 600 ℃ after chute enters combustion chamber and coal gas mixed firing; When getting narrow coking chamber, coke enters dry coke quenching auxiliary by retort section can not establish part flow arrangement; The cooled coal gas inlet is set in the bottom of low temperature heat exchanger, when the indirect cooling of coke is insufficient, cooled coal gas is sent into the direct cooling coke in coke cooling channel; Generally cool off without water vapour, but, when needing to increase CO content in the splitting gas, can spray into the water of requirement at the coke discharge box top if derived product is synthesizing methanol or dme, water vapor is adequately cooled coke first, has second improved the virtual mass of synthetic gas.By above-mentioned measure red Jiao is cooled to below 200 ℃ by about 1000 ℃, this process is called the indirect dry coke quenching of single hole connection journey.The coke that is cooled enters coke discharge box, enters water seal by coke extractor and connects in the burnt case, and concentrate through the cold conditions coke that the scraper conveyor of bottom is sent each coking chamber here and to deliver to Jiao Chang, and water seal connects being provided with of burnt case can effectively block the air admission coking chamber.In the retort section, down the position respectively is provided with a coal gas leadout hole, can be when producing according to the needs of user to derived product, provide composition different coal gas, the coal gas that the middle temperature coal gas leadout hole in stage casing is derived is the low product of cracking degree, mainly include tar, hydro carbons organic compound, be used for the recoveryization product; The coal gas that the coal gas of high temperature leadout hole of hypomere is derived is the high product of cracking degree, mainly be carbon monoxide and hydrogen, this coal gas is drawn about 1000 ℃ of left and right sides high temperature, and then be heated to about 1050 ℃, and make the abundant cracking of coal gas by the cracker that nickel catalyzator is housed, enter waste heat boiler again and reclaim heat, cooling is after desulfurization promptly can be used for products such as dimethyl ether synthesis or methyl alcohol; Firing tunnel in coking furnace enters each flue burning through horizontal gas pipe, gas after the burning is by coking chamber absorption portion heat, after reducing to about 1100 ℃, enter the waste gas horizontal channel of furnace roof, and enter waste gas through the waste gas leadout hole and be in charge of, then enter waste heat boiler through waste gas header again, temperature is reduced to 200～150 ℃, is discharged by chimney after by induced draft fan waste gas being sent into the thionizer desulfurization at last.The high pressure steam that waste heat boiler produces is supplied with the turbine driven set generating.Air is preheating to about 600 ℃ by three sections heat exchangers of high, medium and low temperature, enters flue through chute, guarantees that coal gas is abundant in the flue internal combustion.
The present invention is provided with the rapid heating section at the pars infrasegmentalis of coalingging, and adopts hot-pressing technique in the stove, and the coal charge that will be in the plastic stage carries out compacting, and makes the rapid coking of coal charge form duricrust, solves charge of coke direct motion problem.This technology has solved the difficult problem that vertical coke oven can not refine metallurgical coke.Reducing aspect the investment, this invention does not have four carts, dry coke quenching auxiliary and the corresponding environmental protection facility of the necessary outfit of conventional coke oven institute owing to adopted unique upright structures and the indirect dry coke quenching pattern of single hole connection journey; Compare the burnt investment of ton with the conventional coke oven of the comprehensive band dry coke quenching auxiliary of environmental protection facility and can reduce more than 60%, ton Jiao about 400 yuan, only is equivalent to the investment of conventional dry coke quenching.Aspect cutting down the consumption of energy, this invention is the successional cold conditions production technique of coalingging, discharge of the coke, and does not have the fire door of conventional frequent switching; Combustion chamber headwall thickening reduces the body of heater heat radiation, adopts the sensible heat of interior dry coke quenching technology of stove and heating gas to reclaim technology in addition, and comprehensive energy consumption can reduce more than 6%, has the characteristics of less energy-consumption.Aspect reducing production costs, this invention realizes hot pressing in retort process, and the cheap weakly caking coal or the proportion of non-caking coal can be brought up to about 50%, compare the unit cost of production with conventional coke oven and can reduce by 10～50%.Aspect environment protection; the continuous flow procedure that this invention goes out for the fully-closed cold charge is cold; overcome the serious smoke contamination problem that conventional pit kiln intermittent type hot charging heat goes out; simultaneously because equipment such as no fire doors; adopt hermetically sealed operation; so do not exist fire door to run the cigarette problem of burning with anger, restrained the generation of pollutent from the source, realized the zero release of dust.Aspect raising labour productivity, but the continuous production of this invention can make production process be easy to realize the automatization control of height, and producers can reduce more than 50%, have the high characteristics of labour productivity.Aspect quality product, because coal charge is realized hot pressing in retort process, and each quirk is continuous heating quirk, help reducing relatively coking time, be rapid heating (during the wide 300mm of coking chamber, coking time only is 6～8 hours), adopt the indirect dry coke quenching measure of single hole connection journey in the stove simultaneously, so on the basis of improving the hard coal consumption, still can produce high-intensity coke.Aspect floor space, this invention does not have four big vehicle devices of conventional coke oven, saved push away, block, the quenching car track; Adopt the indirect dry coke quenching of single hole connection journey simultaneously, do not need independent dry coke quenching place; In addition since body of heater to height to development, also be that few reason is taken up an area of in this invention, compare the minimizing floor space with conventional coke oven more than 2/3.
Description of drawings
To be that cold charge is cold go out the full-automatic continuous coke oven structural representation of vertical type with accompanying drawing.
Embodiment
The furnace roof of this invention is provided with side distributing trough 5, fire-regulating hole 2, start material distributing machine 4 when coalingging, after coal charge is covered with side distributing trough 5 by material distributing machine 4, close down material distributing machine 4, press coal coke pushing plate 1 to get lodged in discharge opening 6 places of side distributing trough 5 this moment, mention pressure coal coke pushing plate 1 by hydro-cylinder, coal in the side distributing trough 5 is discharged in the coking chamber 8 top sections of coalingging 3 immediately, when needing to press the coal coke pushing, press coal coke pushing plate 1 to push downwards by hydro-cylinder, reach certain stroke and pressure after, will press on the coal coke pushing plate 1 and carry, the discharge opening 6 of stifled upside distributing trough 5 is promptly finished a circulation again.Coal charge enters rapid heating section 28 by the section of coalingging 3, reaches the plastic stage rapidly, and then coal charge further goes downwards to retort section 25 destructive distillation cokings.Discharge out of the furnace through the coal gas leadout hole of retort section 25 by coking chamber 8 dried distilled raw gas, the low coal gas of cracking degree that the middle temperature coal gas leadout hole 26 in coking chamber 8 stage casings is derived is used for the recoveryization product, what the coal gas of high temperature leadout hole 24 of hypomere was derived is the high coal gas of cracking degree, mainly be carbon monoxide and hydrogen, this coal gas is that high temperature is drawn, temperature up to 1000 ℃ about, by further intensification cracking, and after waste heat boiler reclaims heat, be used for products such as dimethyl ether synthesis or methyl alcohol.Firing tunnel in coking furnace enters flue 9 burnings by horizontal gas pipe 11, gas after the burning is by coking chamber 8 absorption portion heats, after reducing to about 1100 ℃, entering waste gas by waste gas horizontal channel 27 through waste gas leadout hole 7 is in charge of, then enter waste heat boiler by waste gas header, temperature is reduced to 200～150 ℃, is discharged by chimney after by induced draft fan waste gas being sent into the thionizer desulfurization at last.The high pressure steam that waste heat boiler produces is supplied with the turbine driven set generating.Freezing air enters heat exchanger through gas inlet 16, through low temperature heat exchanger 20 and in the metal wall 21 indirect cooling cokes of warm interchanger 14, then enter high-temperature heat exchanger 13, further absorb red Jiao's heat indirectly by partition wall 23, after being preheating to about 600 ℃, upright air flue 10 by chute district 12 enters flue 9, guarantees that coal gas is abundant in flue 9 internal combustion.Ripe coke in the retort section 25 enters the coke cooling channel 22 in the dry coke quenching auxiliary, shunt descending, fully heat is passed to air indirectly by heat exchanger, cooled coal gas enters coke cooling channel 22 by cooled coal gas inlet 15, directly absorb red burnt sensible heat,, can spray into an amount of water at the coke discharge box top if when needing to increase CO content in the synthetic splitting gas, water vapor is adequately cooled coke first, has second improved the virtual mass of synthetic gas; At last coke is cooled to below 200 ℃.The cold conditions coke enters coke discharge box 19, enters water seal by coke extractor 18 and connects in the burnt case 17, and concentrate through the coke that the scraper conveyor of bottom is sent each coking chamber here and to deliver to Jiao Chang.
Claims (6)
1, cold charge is cold goes out the full-automatic continuous coke oven of vertical type, it is made up of alternately coking chamber, combustion chamber and furnace roof, chute, dry coke quenching auxiliary, coke discharging device, it is characterized in that top of combustion chamber is provided with the waste gas horizontal channel, and the waste gas leadout hole that links to each other with the waste gas horizontal channel; The chute position is provided with upright air flue and horizontal gas pipe; Coking chamber and bottom, combustion chamber are dry coke quenching auxiliary and coke discharging device, wherein dry coke quenching auxiliary by high-temperature heat exchanger, in warm interchanger, low temperature heat exchanger and coke cooling channel form, the type of cooling is the indirect dry coke quenching of single hole connection journey.
2, cold charge according to claim 1 is cold goes out the full-automatic continuous coke oven of vertical type, it is characterized in that, described coke discharging device by coke extractor, coke discharge box, water seal connect burnt case, scraper conveyor is formed.
3, cold charge according to claim 2 is cold goes out the full-automatic continuous coke oven of vertical type, it is characterized in that, the coke oven top also is provided with long coal bunker to layout, and coal bunker has funnel, and each funnel is connected with the material distributing machine of the coking chamber side that per two one words are arranged; Coking chamber side top is provided with the side distributing trough, and top is provided with presses coal coke pushing plate.
4, cold charge according to claim 3 is cold goes out the full-automatic continuous coke oven of vertical type, it is characterized in that, described coking chamber is divided into the section of coalingging, rapid heating section and retort section from top to bottom, and warm coal gas leadout hole and coal gas of high temperature leadout hole during wherein the retort section place is provided with directly communicate with coking chamber.
5, cold charge according to claim 4 is cold goes out the full-automatic continuous coke oven of vertical type, it is characterized in that, described high-temperature heat exchanger is that refractory materials is built by laying bricks or stones, in, low temperature heat exchanger is metal construction, the low temperature heat exchanger place is provided with gas inlet, bottom, coke cooling channel is provided with the cooled coal gas inlet, and the type of cooling is the indirect dry coke quenching of single hole connection journey.
6, go out the full-automatic continuous coke oven of vertical type according to each cold charge of claim 1-5 is cold, it is characterized in that the combustion chamber adopts upright quirk, these quirks are continuous heating quirk.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100443701A CN1249201C (en) | 2004-05-31 | 2004-05-31 | Vertical automatic cokery with cold loading and cold discharge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100443701A CN1249201C (en) | 2004-05-31 | 2004-05-31 | Vertical automatic cokery with cold loading and cold discharge |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1583955A true CN1583955A (en) | 2005-02-23 |
| CN1249201C CN1249201C (en) | 2006-04-05 |
Family
ID=34601749
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100443701A Expired - Fee Related CN1249201C (en) | 2004-05-31 | 2004-05-31 | Vertical automatic cokery with cold loading and cold discharge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1249201C (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101792675A (en) * | 2010-04-08 | 2010-08-04 | 徐列 | Coke oven and coking process method |
| CN102250629A (en) * | 2011-06-13 | 2011-11-23 | 山西利华新科技开发有限公司 | Coking furnace capable of recycling heat energy and coking method |
| CN101709220B (en) * | 2009-11-16 | 2013-03-13 | 中冶焦耐(大连)工程技术有限公司 | Coke dry quenching furnace with annular air flue and inclined flue |
| CN103087728A (en) * | 2012-08-06 | 2013-05-08 | 山西鑫立能源科技有限公司 | Continuous coking device of coal pyrolysis furnace |
| CN103756691A (en) * | 2014-01-29 | 2014-04-30 | 刘运良 | Coke oven capable of horizontally heating continuously and vertically extracting coke |
| CN106590699A (en) * | 2015-10-20 | 2017-04-26 | 晏廷书 | Coke quenching technology |
| CN108704435A (en) * | 2018-06-01 | 2018-10-26 | 中国环境科学研究院 | A kind of coal chemical enterprise exhaust gas/pollutant energy-saving and emission-reduction method and device |
| CN110408412A (en) * | 2019-08-23 | 2019-11-05 | 华泰永创(北京)科技股份有限公司 | A kind of air preheating type heat recovery coke oven |
-
2004
- 2004-05-31 CN CNB2004100443701A patent/CN1249201C/en not_active Expired - Fee Related
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101709220B (en) * | 2009-11-16 | 2013-03-13 | 中冶焦耐(大连)工程技术有限公司 | Coke dry quenching furnace with annular air flue and inclined flue |
| CN101792675A (en) * | 2010-04-08 | 2010-08-04 | 徐列 | Coke oven and coking process method |
| CN101792675B (en) * | 2010-04-08 | 2013-12-25 | 徐列 | Coke oven and coking process method |
| CN102250629A (en) * | 2011-06-13 | 2011-11-23 | 山西利华新科技开发有限公司 | Coking furnace capable of recycling heat energy and coking method |
| CN102250629B (en) * | 2011-06-13 | 2013-09-04 | 山西利华新科技开发有限公司 | Coking furnace capable of recycling heat energy and coking method |
| CN103087728A (en) * | 2012-08-06 | 2013-05-08 | 山西鑫立能源科技有限公司 | Continuous coking device of coal pyrolysis furnace |
| CN103087728B (en) * | 2012-08-06 | 2014-04-30 | 山西鑫立能源科技有限公司 | Continuous coking device of coal pyrolysis furnace |
| CN103756691A (en) * | 2014-01-29 | 2014-04-30 | 刘运良 | Coke oven capable of horizontally heating continuously and vertically extracting coke |
| CN106590699A (en) * | 2015-10-20 | 2017-04-26 | 晏廷书 | Coke quenching technology |
| CN108704435A (en) * | 2018-06-01 | 2018-10-26 | 中国环境科学研究院 | A kind of coal chemical enterprise exhaust gas/pollutant energy-saving and emission-reduction method and device |
| CN108704435B (en) * | 2018-06-01 | 2020-10-02 | 中国环境科学研究院 | Energy-saving and emission-reducing method and device for waste gas/pollutants of coking enterprise |
| CN110408412A (en) * | 2019-08-23 | 2019-11-05 | 华泰永创(北京)科技股份有限公司 | A kind of air preheating type heat recovery coke oven |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1249201C (en) | 2006-04-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101942313B (en) | Huadian type process and device for dry distillation of oil shale | |
| CN102679728B (en) | Energy-saving environment-friendly type smelting furnace | |
| CN101792676A (en) | Movable slide bed tunnel type coke oven and use method thereof | |
| CN104762095B (en) | A kind of complete alternation low temperature distillation device and technique for producing semi-coke | |
| CN204174158U (en) | A kind of external-heat low-temperature pyrolysis stove | |
| CN100451133C (en) | Method and apparatus for producing directly reduced iron with coke oven gas | |
| CN102363730A (en) | Oil shale dry-wet mixing method dry distillation technology and heat accumulating type external firing shale oven | |
| CN102424757B (en) | Gas heat carrier low-temperature retort furnace and dry quenching method | |
| CN1249201C (en) | Vertical automatic cokery with cold loading and cold discharge | |
| CN101531906A (en) | Method for electrical heating continuous coal pyrogenation coking and coking furnace thereof | |
| CN201520739U (en) | Continuous vertical closed gasification furnace | |
| CN102827619B (en) | Integrated gas retort | |
| CN204803378U (en) | Rotary hearth furnace | |
| CN102766476B (en) | Multi-layer upright tower type duff dust and oil shale distillation plant with stirring function and process | |
| CN105349160A (en) | Continuous vertical porous dry distillation furnace for straw | |
| CN1242024C (en) | Heat transfer room type heat recovery coke-oven | |
| CN1056170C (en) | Continuous coking process and equipment thereof | |
| CN202415452U (en) | Gas heat carrier low-temperature gas retort | |
| CN101519595B (en) | Coal-carbonifying device | |
| CN202576523U (en) | Energy-saving and environment-friendly smelting furnace | |
| CN102079982B (en) | Production method of formed coke | |
| CN2595807Y (en) | Vertical continuous coking furnace | |
| CN211497498U (en) | Novel medium-low temperature pyrolysis furnace for mixed coal | |
| CN205784513U (en) | External combustion vertical roasting stove | |
| CN101665851A (en) | Three-step metal reducing method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20060405 Termination date: 20190531 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |