CN206875996U - Coke-oven plant's coke-stove gas utilizes and smoke processing system - Google Patents
Coke-oven plant's coke-stove gas utilizes and smoke processing system Download PDFInfo
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- CN206875996U CN206875996U CN201720556236.2U CN201720556236U CN206875996U CN 206875996 U CN206875996 U CN 206875996U CN 201720556236 U CN201720556236 U CN 201720556236U CN 206875996 U CN206875996 U CN 206875996U
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- 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
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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Abstract
The utility model provides a kind of coke-oven plant's coke-stove gas and utilized to be connected with smoke processing system and its processing method, the raw coke oven gas outlet of coke oven by pipeline with the coal gas processing device；The gas exit of coal gas processing device is connected by pipeline with Coke-oven Gas Boiler；The exhanst gas outlet of coke oven is connected by coke oven exhaust gas flue one with chimney, and the exhanst gas outlet of coke oven is also connected so that coke oven exhaust gas is mixed into the high-temperature flue of Coke-oven Gas Boiler by coke oven exhaust gas flue two with the high-temperature flue of Coke-oven Gas Boiler；And the high-temperature flue of Coke-oven Gas Boiler is connected with denitrification apparatus, waste heat reclaiming flue, air-introduced machine, desulfurizer and chimney successively by pipeline.The utility model is while efficiently coke-stove gas is utilized and effectively controls SO2And NOXDischarge, and overcome several big difficulty in treatment of flue gases of cock oven, ensure that the safe operation of coke oven.
Description
Technical field
Coking industry energy-conserving and emission-cutting technology field is the utility model is related to, more specifically, is related to a kind of coke-oven plant's coke oven
Coal gas utilizes and smoke processing system.
Background technology
In coke-oven plant's process of coking, substantial amounts of by-product coke-stove gas is generated, coke oven conducting self-heating is removed and consumes portion
Divide outside coal gas, still have and largely have more than needed, how this part coke-stove gas efficiently to be utilized, be that coke-oven plant's person skilled compares pass
The problem of heart.
On the other hand, because coke-stove gas calorific value is high, ignition temperature is high, and contains H2The compositions such as S, cause coke-stove gas to fire
Contain substantial amounts of NO in flue gas after burningXAnd SO2.In recent years, as haze situation constantly aggravates and air quality constantly deteriorates,
Control of the country to Air Pollutant Emission Index is more and more tighter, and related specifications also specify that SO in coking industry discharge flue gas2、
NOXConcentration of emission index.So how to control the SO in flue gas2And NOXDischarge capacity is also asking of must take into consideration of coking production
Topic.
In addition, producing the processing of flue gas for coke oven conducting self-heating, following several difficult points are presently, there are：(1) coke oven gives up
Gas temperature degree is relatively low, and typically between 220-280 DEG C, and current most ripe catalytic reduction method (SCR) denitrating catalyst is suitable
It is 320-400 DEG C with temperature, the temperature of flue gases of cock oven is relatively low when causing to use conventional scr denitration technology, and denitration efficiency is low,
Emission request can not be met, flue gases of cock oven is heated into more than 320 DEG C using heating furnace for this many coke-oven plant is re-fed into often
SCR denitration device is advised, but is separately provided a heating furnace and energy waste again be present for heat source, and can increase and once throw
Money and operating cost；(2) coke making process requires that coke oven chimney must remain hot standby state, to ensure that coke oven is kept the safety in production；
(3) the flue gases of cock oven temperature after desulphurization denitration purification necessarily be greater than flue gas dew point temperature, and not preferably less than 130 DEG C.
Therefore, if a kind of coke-oven plant's coke-stove gas utilization and smoke processing system can be designed, efficiently coke-oven plant's pair is being utilized
And can effectively controls SO caused by coke-stove gas burning while product coke-stove gas2And NOX, and overcome coke oven flue desulfurization
Several big difficult points of denitrating system, can necessarily bring considerable economic well-being of workers and staff and environmental benefit, have highly important Practical significance.
Utility model content
In view of the above problems, the purpose of this utility model is to provide a kind of a kind of coke-oven plant's coke-stove gas utilization of offer and cigarette
Gas processing system, denitration process is carried out to solve relatively low should not be directly entered in denitrification apparatus of current coke-oven plant's coke oven exhaust gas temperature
The problem of.
To achieve these goals, the utility model is realized by following technical scheme：
A kind of coke-oven plant's coke-stove gas utilizes and smoke processing system, it is characterised in that including at least coke oven, coal gas processing
Device, Coke-oven Gas Boiler, coke oven exhaust gas flue one, coke oven exhaust gas flue two, denitrification apparatus, waste heat reclaiming flue, air-introduced machine,
Desulfurizer and chimney,
The raw coke oven gas outlet of coke oven is connected by pipeline with the coal gas processing device；
The gas exit of coal gas processing device is connected by pipeline with Coke-oven Gas Boiler；
The exhanst gas outlet of coke oven is connected by the coke oven exhaust gas flue one with the chimney, the exhanst gas outlet of the coke oven
Also connected by the coke oven exhaust gas flue two with the high-temperature flue of Coke-oven Gas Boiler so that coke oven exhaust gas is mixed into coke-stove gas
In the high-temperature flue of boiler；And
The high-temperature flue of the Coke-oven Gas Boiler by pipeline successively with the denitrification apparatus, the waste heat recovery cigarette
Road, the air-introduced machine, the desulfurizer and chimney connection.
Preferably, high temperature section economizer, the coke-stove gas are provided with the high-temperature flue of the Coke-oven Gas Boiler
Bypass flue is additionally provided with the high-temperature flue of boiler, the gas approach of the bypass flue is located at the high temperature section economizer
Fume side upstream, the high-temperature flue of the Coke-oven Gas Boiler are also connected by the bypass flue and the coke oven exhaust gas flue two
It is logical.
Preferably, it is provided with smoke regulating valve on the bypass flue.
Preferably, it is additionally provided with coke-oven coal on the pipeline between the coal gas processing device and the Coke-oven Gas Boiler
Gas holder, the gas exit of coke-oven coal gas holder by pipeline respectively with the gas inlet of Coke-oven Gas Boiler and the heating gas of coke oven
Inlet communication.
Preferably, in addition to flue gas heater, the chimney intake of flue gas heater connect with the desulfurizer, flue gas
The flue outlet of heater connects with the chimney.
Preferably, low-temperature zone economizer, closed cycle water heater and sky are provided with the waste heat reclaiming flue
Air preheater；
The water inlet of low-temperature zone economizer is connected with the feedwater interface of external boiler, Coke-oven Gas Boiler low-level (stack-gas) economizer
Delivery port is connected with the water inlet of the high-temperature flue high temperature section economizer of the Coke-oven Gas Boiler；
Connect to form closed cycle by pipeline between the closed cycle water heater and the flue gas heater, it is described
The recirculated water import and export of closed cycle water heater goes out with the recirculated water of the flue gas heater respectively, import is connected, formation
Water circulating pump is additionally provided with closed cycle pipeline；
The air outlet of the air preheater is connected with the burner of the Coke-oven Gas Boiler.
Preferably, valve, Jiao are provided with the coke oven exhaust gas flue one and the coke oven exhaust gas flue two
Deduster is additionally provided with furnace exhaust flue two.
The utility model comprises at least following beneficial effect：
(1) the utility model is connected coke oven exhaust gas flue two with the high-temperature flue of Coke-oven Gas Boiler, so may be used
So that the higher boiler smoke of the temperature coke oven exhaust gas relatively low with temperature to be mixed, mixed flue-gas temperature can control
Within the temperature range of denitrating technique requirement, so mixed flue gas can is directly entered denitrification apparatus, without separately setting
Auxiliary oven carries out heating can to low temperature coke oven exhaust gas meets the requirements of SCR method denitrations, so as to reducining the construction costs and
Reduce occupation of land and space；
(2) bypass flue is provided with the high-temperature flue of Coke-oven Gas Boiler, the gas approach of the bypass flue is positioned at height
On the high-temperature flue of temperature section economizer fume side upstream, and smoke regulating valve is set on bypass flue, cigarette is bypassed by adjusting
High-temperature flue gas flow in road controls mixed flue gas temperature, and then causes denitration reaction be in optimum temperature, realizes and efficiently takes off
Nitre；
(3) a coke-stove gas part caused by coking by coke oven is used for conducting self-heating, another part is used for coke-oven coal steam pot
Stove produces steam and drags steam turbine power generation, realizes the full utilization on the spot of coke-stove gas；Meanwhile by caused by coke oven flue
Coke oven exhaust gas is mixed into the high-temperature flue of Coke-oven Gas Boiler and then two strands of waste gas of mixing is completed into flue gas desulfurization jointly and taken off
Nitre purified treatment, fume treatment phase is carried out by two sets of independent systems respectively with Coke-oven Gas Boiler flue gas and flue gases of cock oven
Than substantially reducing construction investment and floor space；
(4) heat the flue gas after desulfurizer using the flue gas heat before desulfurizer, by flue gas system itself
Heat exchange realizes the lifting of flue-gas temperature after desulfurizer, but flue gases of cock oven is arranged equivalent to the consumption without external source
Put chimney and be chronically at the hot standby state of safety；
(5) the utility model carries out depth UTILIZATION OF VESIDUAL HEAT IN to the medium temperature flue gas after denitrification apparatus, and obvious heat of smoke is used for into Jiao
The feed-water preheating of producer gas boiler, air preheat and the heating of desulfurization after-purification flue gas, the design of this waste heat reclaiming flue are filled
Point consider that flue-gas temperature is high and exhausted air quantity big (Coke-oven Gas Boiler produces the total of coke oven exhaust gas caused by boiler smoke and coke oven
With) the characteristics of, if according to merely can not be by the flue gas temperature of intimate double flow by way of preheated air in conventional boiler
Degree reduces by 200 DEG C or so, therefore the utility model sets three-level heating surface in waste heat reclaiming flue, that is, sets boiler feedwater pre-
The heating of waste gas absorbs heat energy from waste gas after heat, air preheat and desulfurization, not only efficiently make use of waste gas residual heat, causes again useless
Temperature degree is reduced to desulphurization system requirement condition so as to meet desulfurization requirement；In addition, the setting of all heating surfaces is based on from heat
Mechanics second law, the step that heat energy from waste gas is realized by the level-density parameter of heat-exchange system efficiently utilize.
Brief description of the drawings
By reference to the description below in conjunction with accompanying drawing, and with being more fully understood to of the present utility model, this reality
It will be more apparent and should be readily appreciated that with new other purposes and result.In the accompanying drawings：
Fig. 1 is a kind of Structure and Process schematic diagram of embodiment of the utility model.
In Fig. 1：Coke oven 1, coal gas processing device 2, coke-oven coal gas holder 3, Coke-oven Gas Boiler 4, coke oven exhaust gas flue 1,
Coke oven exhaust gas flue 26, denitrification apparatus 7, waste heat reclaiming flue 8, low-temperature zone economizer 80, closed cycle water heater 81 are empty
Air preheater 82, air-introduced machine 9, desulfurizer 10, chimney 11, high temperature section economizer 12, bypass flue 13, smoke regulating valve 130,
Deduster 14, flue gas heater 15, water circulating pump 16.
Identical label indicates similar or corresponding feature or function in all of the figs.
Embodiment
Specific embodiment of the utility model is described in detail below with reference to accompanying drawing.
See Fig. 1, a kind of coke-oven plant's coke-stove gas utilizes and smoke processing system, including at least coke oven 1, coal gas processing device
2nd, Coke-oven Gas Boiler 4, coke oven exhaust gas flue 1, coke oven exhaust gas flue 26, denitrification apparatus 7, waste heat reclaiming flue 8, air inducing
Machine 9, desulfurizer 10 and chimney 11,
The raw coke oven gas outlet of coke oven 1 is connected by pipeline with coal gas processing device 2；
The gas exit of coal gas processing device 2 is connected by pipeline with Coke-oven Gas Boiler 4；
The exhanst gas outlet of coke oven 1 is connected by coke oven exhaust gas flue 1 with chimney 11, and the exhanst gas outlet of coke oven 1 also passes through
Coke oven exhaust gas flue 26 is connected with the high-temperature flue of Coke-oven Gas Boiler 4 so that the stack gases of coke oven 1 are mixed into Coke-oven Gas Boiler
In 4 back-end ductwork；And
The high-temperature flue of Coke-oven Gas Boiler 4 by pipeline successively with denitrification apparatus 7, waste heat reclaiming flue 8, air-introduced machine 9,
Desulfurizer 10 and chimney 11 connect.
In the above-mentioned technical solutions, caused raw coke oven gas is cooled by pipeline into coal gas processing device 2 in coke oven 1
And purified treatment, the coke-stove gas after the processing of coal gas processing device 2 are admitted to Coke-oven Gas Boiler 4 and are used as coke-oven coal steam pot
The main fuel of stove 4.Waste gas caused by coke oven 1 is sent into by coke oven exhaust gas flue 26 in the high-temperature flue of Coke-oven Gas Boiler 4.
Flue-gas temperature in the high-temperature flue of Coke-oven Gas Boiler 4 is high, more than the denitration temperature requirement of denitrification apparatus 7, and coke oven exhaust gas
Temperature it is then relatively low, typically between 220-280 DEG C, the temperature requirement of conventional scr denitration method can not be met, by the boiler of high temperature
The coke oven exhaust gas of flue gas and low temperature is mixed so that mixed EGT is not less than 320 DEG C, reaches the work of denitration process
Skill requirement, flue gas, which can be sent directly into denitrification apparatus 7, carries out denitration reaction, auxiliary without separately setting compared with conventional method
Heating furnace is helped to carry out the requirement that heating can meets SCR denitration to coke oven exhaust gas.Flue gas after denitration is introduced into waste heat recovery
In flue 8, because the flue-gas temperature after denitration is still higher, therefore waste heat reclaiming flue 8 is set to reclaim flue gas heat.Cigarette
Gas heat release in waste heat reclaiming flue 8 cools to reach the preferred temperature needed for the sulfur removal technology of downstream, waste heat off-gas recovery flue 8
Flue gas out enters air-introduced machine 9, by air-introduced machine 9 boost after enter desulfurizer 10 in carry out desulfurization process, finally again from
Discharged in chimney 11.
In another technical solution, high temperature section economizer 12, coke oven are provided with the high-temperature flue of Coke-oven Gas Boiler 4
Bypass flue 13 is additionally provided with the high-temperature flue of gas boiler 4, the gas approach of bypass flue 13 is located at high temperature section economizer
12 fume side upstream, the high-temperature flue of Coke-oven Gas Boiler are also connected by bypass flue 13 with coke oven exhaust gas flue 26, burnt
The tie point of furnace exhaust flue 26 and the high-temperature flue of Coke-oven Gas Boiler 4 is arranged on the fume side upstream of denitrification apparatus 7, this
Sample first mixes the high-temperature flue gas in bypass flue 13 with the coke oven exhaust gas of coke oven exhaust gas flue 26, tentatively improves coke oven exhaust gas
Temperature, then with high temperature section economizer 12 export boiler smoke mix then together enter denitrification apparatus.
In another technical solution, smoke regulating valve 130 is provided with bypass flue 13.Smoke regulating valve 130 is used for
The high-temperature flue gas flow in bypass flue 13 is controlled to adjust the mixed flue gas temperature before denitrification apparatus 7, before denitrification apparatus 7
Mix waste gas temperature control is at 350 DEG C or so, to ensure the Effec-tive Function of denitrification apparatus 7.
In another technical solution, coke oven is additionally provided with the pipeline between coal gas processing device and Coke-oven Gas Boiler
Gas chamber 3, the gas exit of coke-oven coal gas holder 3 by pipeline respectively with the gas inlet of Coke-oven Gas Boiler 4 and coke oven 1 plus
Heating gas inlet communication.Coke-oven coal gas holder can be cached coal gas, weaken gas yield and composition fluctuation to subsequent user
Adverse effect, the coal gas part cached in coke-oven coal gas holder 3, which is admitted in Coke-oven Gas Boiler 4, is used as coke-oven coal steam pot
The main fuel of stove 4, another part are admitted to the heating fuel as coke oven 1 in coke oven 1, can so realize coke oven by-product gas
Full utilization on the spot.
In another technical solution, in addition to flue gas heater 15, the air inlet and desulfurizer of flue gas heater 15
10 connections, the gas outlet of flue gas heater 15 connects with chimney 11.Because the flue-gas temperature after desulfurization process is about 90-
110 DEG C, and the hot standby temperature of the requirement of fume emission chimney 11 is generally 130 DEG C, therefore on the exhaust pass of desulfurizer 10
Flue gas heater 15 is set, the flue gas after desulfurization is sent to chimney 11 to 130 DEG C or so again, finally by the row of chimney 11 to
Air.
In another technical solution, low-temperature zone economizer 80, the heating of closed cycle water are provided with waste heat reclaiming flue 8
Device 81 and air preheater 82；
The water inlet of low-temperature zone economizer 80 is connected with the feedwater interface of external boiler, the delivery port of low-temperature zone economizer 80
It is connected with the water inlet of the high-temperature flue high temperature section economizer 12 of Coke-oven Gas Boiler 4；
Connect to form closed cycle by pipeline between closed cycle water heater 81 and flue gas heater 15, closed cycle
The recirculated water import and export of water heater 81 goes out with the recirculated water of flue gas heater 15 respectively, import is connected, the closed cycle of formation
Water circulating pump 16 is additionally provided with pipeline, to overcome the resistance on closed cycle pipeline；
The air outlet of air preheater 82 is connected with the burner of Coke-oven Gas Boiler 4.
In the above-mentioned technical solutions, low-temperature zone economizer 80 is used to preheat the boiler feedwater after deoxygenation,
The high temperature section that feedwater in low-temperature zone economizer 80 after preheating is sent in the back-end ductwork of Coke-oven Gas Boiler 4 saves
Coal device 12；Pass through pipe between the flue gas heater 15 set on the exhaust pass of closed cycle water heater 81 and desulfurizer 10
Road connects to form closed cycle, the recirculated water import and export circulation with flue gas heater 15 respectively of closed cycle water heater 81
Water goes out, import is connected, and the heat in waste heat reclaiming flue 8 is transferred in flue gas heater 15, to heat the flue gas after desulfurization；
The setting of water circulating pump 16 can overcome the resistance on closed cycle pipeline；Air preheater 82 is then used to cold air being preheated to
Coke-oven Gas Boiler designs wind-warm syndrome.This design can carry out depth recovery to the medium temperature fume afterheat after denitrification apparatus 7
Utilize, obvious heat of smoke is used for feed-water preheating, air preheat and the heating of desulfurization after-purification waste gas of Coke-oven Gas Boiler.This
The design of waste heat reclaiming flue 8 has taken into full account that flue-gas temperature is high and big (the boiler smoke caused by Coke-oven Gas Boiler of exhaust gas volumn
With coke oven caused by coke oven exhaust gas summation) the characteristics of, if according in conventional boiler merely by way of preheated air without
The flue-gas temperature of intimate double flow is reduced by 200 DEG C or so by method, thus the present invention set in waste heat reclaiming flue three-level by
Hot face, that is, boiler feedwater preheating, air preheat and the heating of flue gas after desulfurization is set to absorb smoke heat energy, it is not only efficiently sharp
With fume afterheat, flue-gas temperature is caused to be reduced to desulphurization system requirement condition so as to meet desulfurization requirement again；In addition, it is all by
The setting in hot face is based on from the second law of thermodynamics, and the step that smoke heat energy is realized by the level-density parameter of heat-exchange system is high
Effect utilizes.
In another technical solution, valve is provided with coke oven exhaust gas flue 1 and coke oven exhaust gas flue 26, just
Valve in the case of often on coke oven exhaust gas flue 1 is closed, the valve opening on coke oven exhaust gas flue 26, and coke oven comes out useless
Gas enters in the high-temperature flue of Coke-oven Gas Boiler 4 from coke oven exhaust gas flue 26；When there are abnormal conditions in system, coke oven exhaust gas
Valve on flue 26 is closed, and the valve opening on coke oven exhaust gas flue 1, coke oven exhaust gas does not enter back into Coke-oven Gas Boiler 4
High-temperature flue and without denitration and desulfurization process, but directly discharged from chimney 11.Also set up on coke oven exhaust gas flue 26
There is deduster 14, to carry out dust removal process to the coke oven exhaust gas in coke oven exhaust gas flue 26, prevent from influenceing the effect of lower procedure
Fruit.
Described in an illustrative manner above with reference to accompanying drawing according to coke-oven plant's coke-stove gas of the present utility model utilization and flue gas
Processing system.It will be understood by those skilled in the art, however, that the coke-oven plant's coke-stove gas proposed for above-mentioned the utility model
Using with smoke processing system, various improvement can also be made on the basis of the utility model content is not departed from.Therefore, this reality
It should be determined with new protection domain by the content of appended claims.
Claims (7)
1. a kind of coke-oven plant's coke-stove gas utilizes and smoke processing system, it is characterised in that including at least coke oven, coal gas processing dress
Put, be Coke-oven Gas Boiler, coke oven exhaust gas flue one, coke oven exhaust gas flue two, denitrification apparatus, waste heat reclaiming flue, air-introduced machine, de-
Sulphur device and chimney,
The raw coke oven gas outlet of coke oven is connected by pipeline with the coal gas processing device；
The gas exit of coal gas processing device is connected by pipeline with Coke-oven Gas Boiler；
The exhanst gas outlet of coke oven is connected by the coke oven exhaust gas flue one with the chimney, and the exhanst gas outlet of the coke oven is also logical
The coke oven exhaust gas flue two is crossed to connect with the high-temperature flue of Coke-oven Gas Boiler so that coke oven exhaust gas is mixed into the coke-stove gas
In the high-temperature flue of boiler；And
The high-temperature flue of the Coke-oven Gas Boiler by pipeline successively with the denitrification apparatus, the waste heat reclaiming flue, institute
State air-introduced machine, the desulfurizer and chimney connection.
2. coke-oven plant's coke-stove gas as claimed in claim 1 utilizes and smoke processing system, it is characterised in that the coke-oven coal
High temperature section economizer is provided with the high-temperature flue of gas boiler, bypass is additionally provided with the high-temperature flue of the Coke-oven Gas Boiler
Flue, the gas approach of the bypass flue are located at the fume side upstream of the high temperature section economizer, the Coke-oven Gas Boiler
High-temperature flue also connected by bypass flue with the coke oven exhaust gas flue two.
3. coke-oven plant's coke-stove gas as claimed in claim 2 utilizes and smoke processing system, it is characterised in that the bypass cigarette
Smoke regulating valve is provided with road.
4. coke-oven plant's coke-stove gas as claimed in claim 1 utilizes and smoke processing system, it is characterised in that at the coal gas
Coke-oven coal gas holder is additionally provided with pipeline between reason device and the Coke-oven Gas Boiler, the gas exit of coke-oven coal gas holder leads to
Piping respectively with the gas inlet of Coke-oven Gas Boiler and the heating gas inlet communication of coke oven.
5. coke-oven plant's coke-stove gas as claimed in claim 2 utilizes and smoke processing system, it is characterised in that also including flue gas
Heater, the gas approach of flue gas heater connect with the desulfurizer, the exhanst gas outlet of flue gas heater and the chimney
Connection.
6. coke-oven plant's coke-stove gas as claimed in claim 5 utilizes and smoke processing system, it is characterised in that the waste heat returns
Receive in flue and be provided with low-temperature zone economizer, closed cycle water heater and air preheater；
The water inlet of low-temperature zone economizer is connected with the boiler feedwater interface of outside, the delivery port of low-temperature zone economizer and Jiao
The water inlet of the high-temperature flue high temperature section economizer of producer gas boiler is connected；
Connect to form closed cycle by pipeline between the closed cycle water heater and the flue gas heater, the enclosed
The recirculated water import and export of circulating water heater goes out with the recirculated water of the flue gas heater respectively, import is connected, the enclosed of formation
Water circulating pump is additionally provided with circulation line；
The air outlet of air preheater connects with the burner of the Coke-oven Gas Boiler.
7. coke-oven plant's coke-stove gas as claimed in claim 1 utilizes and smoke processing system, it is characterised in that the coke oven gives up
Valve is provided with gas flue one and the coke oven exhaust gas flue two, dedusting is additionally provided with the coke oven exhaust gas flue two
Device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720556236.2U CN206875996U (en) | 2017-05-18 | 2017-05-18 | Coke-oven plant's coke-stove gas utilizes and smoke processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720556236.2U CN206875996U (en) | 2017-05-18 | 2017-05-18 | Coke-oven plant's coke-stove gas utilizes and smoke processing system |
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| CN206875996U true CN206875996U (en) | 2018-01-12 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107014217A (en) * | 2017-05-18 | 2017-08-04 | 中冶华天南京工程技术有限公司 | Coke-oven plant's coke-stove gas is utilized and smoke processing system and its processing method |
-
2017
- 2017-05-18 CN CN201720556236.2U patent/CN206875996U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107014217A (en) * | 2017-05-18 | 2017-08-04 | 中冶华天南京工程技术有限公司 | Coke-oven plant's coke-stove gas is utilized and smoke processing system and its processing method |
| CN107014217B (en) * | 2017-05-18 | 2023-09-26 | 中冶华天南京工程技术有限公司 | Coke oven gas utilization and flue gas treatment system of coking plant and treatment method thereof |
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