CN109404936A - A kind of smoke processing system and processing method - Google Patents

A kind of smoke processing system and processing method Download PDF

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Publication number
CN109404936A
CN109404936A CN201811257181.0A CN201811257181A CN109404936A CN 109404936 A CN109404936 A CN 109404936A CN 201811257181 A CN201811257181 A CN 201811257181A CN 109404936 A CN109404936 A CN 109404936A
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CN
China
Prior art keywords
flue gas
combustion furnace
recovery apparatus
heat recovery
desulfurizer
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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.)
Pending
Application number
CN201811257181.0A
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Chinese (zh)
Inventor
刘自金
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
QINGDAO FULUN TECHNOLOGY Co Ltd
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QINGDAO FULUN TECHNOLOGY Co Ltd
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Priority to CN201811257181.0A priority Critical patent/CN109404936A/en
Publication of CN109404936A publication Critical patent/CN109404936A/en
Pending legal-status Critical Current

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00Methods of steam generation characterised by form of heating method
    • F22B1/02Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/18Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00Arrangements of devices for treating smoke or fumes
    • F23J15/02Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00Arrangements of devices for treating smoke or fumes
    • F23J15/02Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/04Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2215/00Preventing emissions
    • F23J2215/20Sulfur; Compounds thereof
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2217/00Intercepting solids
    • F23J2217/50Intercepting solids by cleaning fluids (washers or scrubbers)

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention belongs to fume treatment technical fields, disclose a kind of smoke processing system, the fume collection mechanism including being connected to multiple flue gas generation mechanisms, it is connected to the combustion furnace of fume collection mechanism, it is connected to the deduster of combustion furnace, is connected to the heat recovery apparatus and desulfurizer of deduster;Heat recovery apparatus includes the first pipeline for surrounding the fuel conduit of combustion furnace and the second pipeline for being connected to steam production plant, and the first pipeline, steam production plant are connected to desulfurizer.The present invention is by carrying out high-temp combustion in the fume centralized combustion furnace that generates each workshop, reduce fume treatment cost, gas of the flue gas after high-temp combustion is mostly carbohydrate, pollution level substantially reduces, and reaching low emission or minimum discharge standard after dedusting, desulfurization process, and flue gas is also used as comburant to provide part energy, reduces energy consumption.In addition, heat entrained by the flue gas to combustion furnace discharge is recycled by heat recovery apparatus.

Description

A kind of smoke processing system and processing method
Technical field
The present invention relates to fume treatment technical field more particularly to a kind of smoke processing system and processing methods.
Background technique
In rubber industry, especially tyre industry, entire manufacture can all generate flue gas in the process, in these flue gases Containing the micro organic component such as H2S, NH3, CS2, mercaptan, organic sulfur compound, amine and inorganic matter, not only to the body of operator Body health causes directly to injure, while also polluted the environment of surrounding, causes bad influence to environment-protecting clean.
Currently, division of labor section is mainly taken to be collected, each workshop section corresponds to a set of corresponding fume treatment auxiliary, at flue gas Equipment is managed by the way of UV photodissociation, using high energy high ozone UV ultraviolet light beam irradiation flue gas and then industrial smoke is cracked, makes to have The degradation under the irradiation of high energy ultraviolet light beam of machine or inorganic polymer malodorous compound strand is changed into low molecular compound, this Processing mode can efficiently remove stench, but limited for the processing of compound contained in flue gas, be difficult poisonous and harmful substance It thoroughly removes, reaches the standard of low emission or minimum discharge, and higher cost.In addition, flue gas cannot be effectively realized again It utilizes, resource utilization is low.
Summary of the invention
The purpose of the present invention is to provide a kind of smoke processing system and processing methods, and realizing reduces harmful substances from flue gases Content, reach the standard of low emission or minimum discharge, reduce processing cost, and realize the recycling of flue gas, improve resource Utilization rate,
To achieve this purpose, the present invention adopts the following technical scheme:
A kind of smoke processing system, the fume collection mechanism including being connected to multiple flue gas generation mechanisms are connected to described The combustion furnace of fume collection mechanism is connected to the deduster of the combustion furnace, is connected to the heat recovery apparatus of the deduster, with And desulfurizer;
The heat recovery apparatus includes that the first pipeline of the fuel conduit around the combustion furnace is produced with steam is connected to Second pipeline of device, first pipeline, steam production plant are connected to the desulfurizer.
Preferably, the ignition temperature in the combustion furnace is more than or equal to 1200 DEG C.
Preferably, the heat recovery apparatus further includes the heat exchanger for being connected to the deduster, the heat exchanger Exhaust outlet be connected to the desulfurizer.
Preferably, the desulfurizer includes tower body, the tower body bottom and top are respectively arranged with air inlet and go out Port is provided with spraying layer and the packing layer below the spraying layer in the tower body.
Preferably, the spraying layer includes water inlet supervisor and is responsible for the multiple water inlet pipes being connected with the water inlet, Spray head is provided on the water inlet supervisor, water inlet pipe.
Preferably, the fume collection mechanism includes the gas gathering mask being arranged in above each flue gas generation mechanism, And each gas gathering mask covers the corresponding flue gas generation mechanism.
Preferably, further include two air-introduced machines, one of them described air-introduced machine be set to the fume collection mechanism and Between the combustion furnace, another described air-introduced machine is set between the heat recovery apparatus and the desulfurizer.
To achieve the above object, the present invention also provides a kind of flue gas processing method, flue gas enters through fume collection mechanism Combustion furnace enters heat recovery apparatus by deduster after burning in the combustion furnace, one into the heat recovery apparatus For partial fume through the first pipeline to the fuel preheating in fuel conduit, another part flue gas is delivered to steam production plant, cooling Flue gas afterwards enters desulfurizer and carries out desulfurization.
Preferably, ignition temperature of the flue gas in the combustion furnace is more than or equal to 1200 DEG C.
Beneficial effects of the present invention:
Smoke processing system provided by the invention, by the fume centralized that generates each workshop to together for vulcanized vehicle Between provide high-temperature steam combustion furnace in carry out high-temp combustion so that no longer need to each workshop generate flue gas individually locate Reason, reduces fume treatment cost, and gas of the flue gas after high-temp combustion is mostly carbohydrate, pollution level is significantly It reduces, and is reaching low emission or minimum discharge standard after dedusting, desulfurization process, and flue gas is also used as comburant to provide Part energy, reduces energy consumption.In addition, by heat recovery apparatus, heat entrained by the flue gas to combustion furnace discharge into Row recycles, and on the one hand preheats to fuel, improves the combustion rate of fuel;On the other hand it for generating high-temperature steam, drops The energy consumption of low combustion furnace.
Flue gas processing method provided by the invention, reduces processing cost, realizes the recycling to flue gas.
Detailed description of the invention
Fig. 1 is the schematic illustration of smoke processing system provided by the invention;
Fig. 2 is the structural schematic diagram of spraying layer provided by the invention.
In figure:
1, fume collection mechanism;11, gas gathering mask;2, low temperature plasma flue gas processing device;31, the first air-introduced machine;32, Second air-introduced machine;4, combustion furnace;41, fuel conduit;5, deduster;6, heat recovery apparatus;61, the first pipeline;62, the second pipe Road;7, steam production plant;8, desulfurizer;81, tower body;82, packing layer;83, spraying layer;831, water inlet supervisor;832, into Water branch pipe;833, spray head.
Specific embodiment
To further illustrate the technical scheme of the present invention below with reference to the accompanying drawings and specific embodiments.
As shown in Figure 1, a kind of smoke processing system is present embodiments provided, for rubber (especially tire) industry The flue gas that mixing workshop, component workshop, assembly room, curing department, quality inspection workshop and repairing workshop generate is collected processing, It can be certainly also used to the fume treatment of other industry.The smoke processing system includes being connected to multiple flue gas production structures, also It is the fume collection mechanism 1 in each workshop, is connected to the combustion furnace 4 of fume collection mechanism 1, is connected to the deduster of combustion furnace 4 5, it is connected to the heat recovery apparatus 6 and desulfurizer 8 of deduster 5.
Wherein, combustion furnace 4 provides the boiler of high-temperature steam to be original for curing department, and the ignition temperature in combustion furnace 4 is big In equal to 1200 degrees Celsius.Deduster 5 is filtration dust catcher, electrostatic precipitator, dry type or wet scrubber, and structure is The prior art repeats no more.Above-mentioned deduster 5 is connected to the flue gas discharge opening of combustion furnace 4, the flue gas discharge opening row of combustion furnace 4 Flue gas out is dusted by deduster 5.Heat recovery apparatus 6 includes the first pipeline for surrounding the fuel conduit 41 of combustion furnace 4 61 and it is connected to the second pipeline 62 of steam production plant 7, the first pipeline 61 and steam production plant 7 are all connected to desulfurizer 8。
By the fume centralized that generates each workshop to together in the combustion furnace 4 for providing high-temperature steam for curing department High-temp combustion is carried out, so that the flue gas generated to each workshop is no longer needed individually to handle, reduces fume treatment cost, and Gas of the flue gas after high-temp combustion is mostly carbohydrate, and pollution level substantially reduces, and at by dedusting, desulfurization Reach low emission or minimum discharge standard after reason, and flue gas is also used as comburant to provide part energy, reduces energy consumption.Separately Outside, by heat recovery apparatus 6, heat entrained by flue gas that combustion furnace 4 is discharged is recycled, on the one hand to fuel into Row preheating, improves the combustion rate of fuel;On the other hand for generating high-temperature steam, the energy consumption of combustion furnace 4 is reduced.
As shown in Figure 1, fume collection mechanism 1 includes the gas gathering mask 11 being arranged in above each flue gas production mechanism, and every A gas gathering mask 11 covers corresponding flue gas production mechanism.Wherein the structure of gas gathering mask 11 is produced according to corresponding flue gas The structure of mechanism is designed, for example is set as cone barrel or cylindrical shape, as far as possible by corresponding flue gas manufacturing machine Structure is surrounded, so that flue gas is collected to greatest extent, prevents flue gas from spreading around.
As shown in Figure 1, being additionally provided with low temperature plasma flue gas processing device between combustion furnace 4 and fume collection mechanism 1 (DDBD) 2, the flue gas that fume collection mechanism 1 is collected enters low temperature plasma flue gas processing device 2, utilizes generated high energy Electronics, free radical isoreactivity particle irradiation, ionization, cracking flue gas in each component, be allowed to decompose, aoxidize etc. a series of multiple Miscellaneous chemical reaction, to eliminate peculiar smell, stink pollutant that each flue gas production mechanism generates.
In addition, in order to improve gas gathering mask 11 to the collection rate of flue gas, in fume collection mechanism 1 and low temperature plasma flue gas The first air-introduced machine 31 is additionally provided between processing unit 2, and the flue gas of fume collection mechanism 1 can be transported to low temperature etc. from Daughter flue gas processing device 2 guarantees the normal operation of smoke processing system.And between desulfurizer 8 and steam production plant 7 It is additionally provided with the second air-introduced machine 32, so that at negative pressure in combustion furnace 4, not back-fire.
As shown in Figure 1, heat recovery apparatus 6 further includes heat exchanger, the flue gas after 5 dedusting of deduster is entering recuperation of heat It is divided into three tunnels after in device 6, wherein connected ring preheats fuel around the first pipeline 61 of fuel conduit 41 all the way, improves combustion The combustion rate of material;In addition the medium in the heat and heat exchanger in flue gas is swapped, flue gas through over-heat-exchanger all the way Temperature drop to preset temperature or room temperature, preset temperature is set according to actual needs.And it carries and is exchanged with flue gas The medium of heat enters the next step.When the medium in heat exchanger is water, the hot water after heat exchange is carried out with flue gas It enters in the workshop for need hot water or enters in heating system, provide heat for each workshop;When in heat exchanger When medium is compressed gas, the compressed gas that heat is exchanged with flue gas is carry, the high temperature and pressure generated after compressor compresses Gas is transferred heat in water into condenser by indirect exchange, and the hot water of generation enters in the workshop for needing hot water Or enter in heating system, heat is provided for each workshop.
It is remaining that steam production plant 7, in the present embodiment, steam production plant 7 are connected to by the second pipeline 62 all the way For waste heat boiler, high-temperature steam is generated using the high-temperature flue gas that combustion furnace 4 is discharged and is used for curing department, so that combustion furnace 4 mentions The high-temperature steam of confession is reduced, and reduces energy consumption.The structure of waste heat boiler is the prior art, is repeated no more.
The flue gas of the above-mentioned flue gas preheated to fuel, the flue gas through over-heat-exchanger and process waste heat boiler is finally equal It is connected to the second air-introduced machine 32, enters desulfurizer 8 through the second air-introduced machine 32.It, can be to combustion by above-mentioned heat recovery apparatus 6 It burns the high-temperature flue gas that furnace 4 is discharged and carries out waste heat recycling, realize the recycling of flue gas.It should be noted that heat recovery apparatus 6 separates Three tunnels in flue gas flow be not it is identical, adjustment is allocated to the flue gas in three tunnels according to actual needs.
As shown in Figure 1, desulfurizer 8 includes tower body 81, the bottom of tower body 81, which is provided with, is connected to the second air-introduced machine 32 Air inlet, the top of tower body 81 are provided with gas outlet, are provided with 83 He of spraying layer between gas outlet and air inlet in tower body 81 Packing layer 82 below spraying layer 83 is set.Entered through the second air-introduced machine 32 by air inlet by the flue gas of heat recovery apparatus 6 Into tower body 81, from bottom to top flow, and the spray liquid that spraying layer 83 sprays flows from the top to the bottom, and contains in spray liquid containing weight The sodium hydroxide of amount about 3%, the process of desulfurization is mainly that sulfur dioxide reacts with sodium hydroxide solution, and reaction generates sub- Sodium sulphate and water.And filler is set on packing layer 82, further increase the contact area of flue gas and spray liquid, to flue gas into The sufficient desulfurization of row.
Referring to Fig. 2, above-mentioned spraying layer 83 includes multiple water inlet branch that water inlet is responsible for 831 and is connected with water inlet supervisor 831 Pipe 832, water inlet are responsible on 831 and water inlet pipe 832 and are provided with spray head 833, by each spray head 833, so that spray Liquid is equably from top to bottom fallen in tower body 81, adequately and smoke contacts, carries out desulfurization to flue gas.
For above-mentioned smoke processing system, the manufacturing enterprise of rubber industry carries out completely new industrial factory centered on boiler Room layout, the flue gas that all workshops or process generate all are delivered to boiler and carry out high temperature burning handling, then by deduster, The equipment such as heat recovery apparatus are handled, high-efficient, at low cost.And there is very strong specific aim centered on crossing boiler, it throws Rate are used, maintenance cost and consumptive material expense are all relatively low.
By taking 10,000,000 sets of half steel radial tyre of passenger car production lines in rubber tyre industry as an example, cigarette provided in this embodiment Gas processing system and traditional fume treatment process ration, See Figure.As seen from the figure, smoke processing system provided in this embodiment, The flue gas being finally discharged can not only be made to reach minimum discharge standard, and processing cost is substantially reduced.
The present embodiment additionally provides a kind of flue gas processing method, and using above-mentioned smoke processing system, flue gas is received through flue gas Collecting mechanism 1 enters combustion furnace 4, enters heat recovery apparatus 6 by deduster 5 after 1200 DEG C of high-temp combustions in combustion furnace 4, Flue gas into heat recovery apparatus 6, a part is through the first pipeline 61 to the fuel preheating in fuel conduit 41, and a part is through heat Exchanger produces hot water, and residue point a part is delivered to steam production plant 7, and the flue gas after cooling enters the progress of desulfurizer 8 Desulfurization.
The flue gas processing method surrounds the side of boiler processing flue gas convenient for the manufacturing enterprise of rubber industry centered on boiler Formula carries out completely new industrial premises layout, improves fume treatment effect and efficiency, and reduce cost of investment.
Obviously, the above embodiment of the present invention is just for the sake of clearly illustrating examples made by the present invention, and being not is pair The restriction of embodiments of the present invention.For those of ordinary skill in the art, may be used also on the basis of the above description To make other variations or changes in different ways.There is no necessity and possibility to exhaust all the enbodiments.It is all this Made any modifications, equivalent replacements, and improvements etc., should be included in the claims in the present invention within the spirit and principle of invention Protection scope within.

Claims (9)

1. a kind of smoke processing system, which is characterized in that the fume collection mechanism including being connected to multiple flue gas generation mechanisms (1), it is connected to the combustion furnace (4) of the fume collection mechanism (1), is connected to the deduster (5) of the combustion furnace (4), is connected Heat recovery apparatus (6) and desulfurizer (8) in the deduster (5);
The heat recovery apparatus (6) include around the combustion furnace (4) fuel conduit (41) the first pipeline (61) be connected to In the second pipeline (62) of steam production plant (7), first pipeline (61), steam production plant (7) are all connected to described Desulfurizer (8).
2. smoke processing system according to claim 1, which is characterized in that the ignition temperature in the combustion furnace (4) is big In equal to 1200 DEG C.
3. smoke processing system according to claim 1, which is characterized in that the heat recovery apparatus (6) further includes connection Heat exchanger in the deduster (5), the exhaust outlet of the heat exchanger are connected to the desulfurizer (8).
4. smoke processing system according to claim 1, which is characterized in that the desulfurizer (8) includes tower body (81), Tower body (81) bottom and top are respectively arranged with air inlet and air outlet, are provided with spraying layer (83) in the tower body (81) With the packing layer (82) being located at below the spraying layer (83).
5. smoke processing system according to claim 4, which is characterized in that the spraying layer (83) includes water inlet supervisor (831) and with the water inlet supervisor (831) the multiple water inlet pipes (832) being connected, the water inlet supervisor (831), water inlet branch Spray head (833) are provided on pipe (832).
6. smoke processing system according to claim 1, which is characterized in that the fume collection mechanism (1) includes setting Gas gathering mask (11) above each flue gas generation mechanism, and each gas gathering mask (11) covers the corresponding flue gas Generation mechanism.
7. smoke processing system according to claim 1, which is characterized in that further include two air-introduced machines, one of institute It states air-introduced machine to be set between the fume collection mechanism (1) and the combustion furnace (4), another described air-introduced machine is set to institute It states between heat recovery apparatus (6) and the desulfurizer (8).
8. a kind of flue gas processing method, using such as described in any item smoke processing systems of claim 1-7, which is characterized in that Flue gas enters combustion furnace through fume collection mechanism, enters heat recovery apparatus by deduster after burning in the combustion furnace, into Enter the part of smoke in the heat recovery apparatus through the first pipeline to the fuel preheating in fuel conduit, another part flue gas is defeated It send to steam production plant, the flue gas after cooling enters desulfurizer and carries out desulfurization.
9. flue gas processing method according to claim 8, which is characterized in that ignition temperature of the flue gas in the combustion furnace More than or equal to 1200 DEG C.
CN201811257181.0A 2018-10-26 2018-10-26 A kind of smoke processing system and processing method Pending CN109404936A (en)

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Application Number Priority Date Filing Date Title
CN201811257181.0A CN109404936A (en) 2018-10-26 2018-10-26 A kind of smoke processing system and processing method

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112062102A (en) * 2020-08-10 2020-12-11 宁夏奥斯化工有限公司 Sodium sulfide production process and production device
CN113267054A (en) * 2020-02-15 2021-08-17 来宾市永泰金属有限公司 Heat energy circulating device for casting equipment

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1605401A (en) * 2003-10-10 2005-04-13 中国科学院过程工程研究所 Flue gas purifying and waste heat recovery method and apparatus in bitumen concrete loading
CN102658012A (en) * 2012-05-18 2012-09-12 重庆紫光天化蛋氨酸有限责任公司 Method and device for treating high-concentration malodorous gas
DE102014114052A1 (en) * 2014-09-26 2016-03-31 Elringklinger Ag Honeycomb block and heat exchanger elements produced therefrom, in particular for flue gas purification systems of power plants
CN205897879U (en) * 2016-08-08 2017-01-18 中冶华天南京工程技术有限公司 System is used multipurposely to heating furnace waste heat
CN106377977A (en) * 2016-11-07 2017-02-08 天津海泰环保科技发展股份有限公司 Comprehensive treatment device of rubber waste gas
CN108343978A (en) * 2017-07-28 2018-07-31 北京化工大学 A kind of catalytic oxidation system and method for low calorie fuels

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1605401A (en) * 2003-10-10 2005-04-13 中国科学院过程工程研究所 Flue gas purifying and waste heat recovery method and apparatus in bitumen concrete loading
CN102658012A (en) * 2012-05-18 2012-09-12 重庆紫光天化蛋氨酸有限责任公司 Method and device for treating high-concentration malodorous gas
DE102014114052A1 (en) * 2014-09-26 2016-03-31 Elringklinger Ag Honeycomb block and heat exchanger elements produced therefrom, in particular for flue gas purification systems of power plants
CN205897879U (en) * 2016-08-08 2017-01-18 中冶华天南京工程技术有限公司 System is used multipurposely to heating furnace waste heat
CN106377977A (en) * 2016-11-07 2017-02-08 天津海泰环保科技发展股份有限公司 Comprehensive treatment device of rubber waste gas
CN108343978A (en) * 2017-07-28 2018-07-31 北京化工大学 A kind of catalytic oxidation system and method for low calorie fuels

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113267054A (en) * 2020-02-15 2021-08-17 来宾市永泰金属有限公司 Heat energy circulating device for casting equipment
CN112062102A (en) * 2020-08-10 2020-12-11 宁夏奥斯化工有限公司 Sodium sulfide production process and production device

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