WO2018192564A1 - 一种生活垃圾热解焚烧装置烟气净化系统 - Google Patents

一种生活垃圾热解焚烧装置烟气净化系统 Download PDF

Info

Publication number
WO2018192564A1
WO2018192564A1 PCT/CN2018/083865 CN2018083865W WO2018192564A1 WO 2018192564 A1 WO2018192564 A1 WO 2018192564A1 CN 2018083865 W CN2018083865 W CN 2018083865W WO 2018192564 A1 WO2018192564 A1 WO 2018192564A1
Authority
WO
WIPO (PCT)
Prior art keywords
flue gas
carbon fiber
dioxin
electromagnetic pulse
induced draft
Prior art date
Application number
PCT/CN2018/083865
Other languages
English (en)
French (fr)
Inventor
陈冠益
马文超
潘敏慧
何啸
台凌宇
颜蓓蓓
钟磊
程占军
杜桂月
李丽萍
Original Assignee
天津大学
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 天津大学 filed Critical 天津大学
Publication of WO2018192564A1 publication Critical patent/WO2018192564A1/zh

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
    • B01D46/023—Pockets filters, i.e. multiple bag filters mounted on a common frame
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/38—Removing components of undefined structure
    • B01D53/40—Acidic components
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/75—Multi-step processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/81—Solid phase processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B01D53/8659—Removing halogens or halogen compounds
    • B01D53/8662—Organic halogen compounds
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44—Details; Accessories
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44—Details; Accessories
    • F23G5/46—Recuperation of heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/006—Layout of treatment plant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
    • F23J15/025—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using filters
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/40—Alkaline earth metal or magnesium compounds
    • B01D2251/404—Alkaline earth metal or magnesium compounds of calcium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/60—Inorganic bases or salts
    • B01D2251/604—Hydroxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10—Inorganic adsorbents
    • B01D2253/102—Carbon
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/93—Toxic compounds not provided for in groups B01D2257/00 - B01D2257/708
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2215/00—Preventing emissions
    • F23J2215/30—Halogen; Compounds thereof
    • F23J2215/301—Dioxins; Furans
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2217/00—Intercepting solids
    • F23J2217/10—Intercepting solids by filters
    • F23J2217/101—Baghouse type
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2217/00—Intercepting solids
    • F23J2217/50—Intercepting solids by cleaning fluids (washers or scrubbers)
    • 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
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • 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
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/30—Technologies for a more efficient combustion or heat usage

Definitions

  • the invention relates to a system for treating and disposing of domestic garbage and utilizing resources, in particular to a flue gas purification system for a domestic waste pyrolysis incineration device.
  • Sanitary landfill is the main way of garbage disposal in China.
  • This treatment method is simple in technology and large in processing capacity, but it takes up too much land resources, and there are problems such as difficult site selection, leachate pollution, greenhouse gas emissions, etc. Resource utilization.
  • the waste heat treatment technology has obvious advantages in reducing capacity, reducing volume and utilizing resources.
  • the new waste incineration technology has received the attention of the state in recent years and will be the main direction of waste disposal and resource utilization in the future.
  • the heat treatment technology essentially oxidizes and decomposes the garbage at high temperature to form a stable solid residue.
  • a large amount of harmful gas is released, and dust and fine particles fly with the wind, resulting in various pollutant indexes in the air.
  • Exceeding the standard and will produce a large number of strong carcinogenic substances, dioxin, which is the main factor that restricts the pyrolysis incineration treatment technology.
  • the dry process purification efficiency is relatively low, and it is used more in the construction of incineration plants in Japan in recent years.
  • the wet purification process has the highest purification efficiency of pollutants and can meet the most stringent emission standards.
  • due to the complicated process and many supporting equipments the one-time investment and operating costs are high. It is widely used in economically developed countries and is not widely used in China.
  • NOx removal the SCR has a NOx removal rate of more than 90%, and the SNCR removal rate of NOx can reach about 50%.
  • cost-efficiency analysis SCR and advanced incineration control systems are roughly equivalent and significantly more expensive than SNCR technology.
  • the flue gas generated by the domestic waste incineration process mainly contains harmful substances such as SO 2 , HCl, NOx, heavy metals and dioxins.
  • dioxin pollution has caused widespread concern among people all over the world, and waste incineration plants are one of the main sources of dioxins, due to the current formation of dioxins.
  • the mechanism has not yet reached a unified consensus, so the control of incineration parameters is only used to suppress the formation of dioxins, and the effect is difficult to determine, so the subsequent treatment of dioxins becomes especially critical.
  • the emission standards for waste incineration flue gas are becoming more and more strict.
  • Dioxins are from the original 1mg/m 3 to 0.5mg/m 3 , and now to 0.1mg/m 3 , for dioxins. There is also a need for new changes in processing.
  • the invention provides a flue gas purification system for a domestic waste pyrolysis incineration device, which can effectively remove pollutants in the incineration flue gas, including CO, SO 2 , NO X , dioxin, etc., especially for the digestible dioxins Multi-stage treatment of British pollutants, the concentration of dioxin in the flue gas is better than the national emission standards, and has played the role of environmental protection.
  • Flue gas purification system for domestic garbage pyrolysis incineration device including quenching tower, electromagnetic pulse dust collector, waste heat utilization and cooling device, carbon fiber filter device, heat exchange device, dioxin chemical catalytic device, water supply system, flue gas pipeline And an induced draft fan; characterized in that the inlet end of the quenching tower is connected with the flue gas pipeline of the domestic garbage pyrolysis incinerator, the outlet end of the quenching tower is connected with the electromagnetic pulse dust collector, and the electromagnetic pulse dust collector is connected with the waste heat utilization and the cooling device.
  • the waste heat utilization and cooling device are connected to the carbon fiber filter device, the carbon fiber filter device is connected to the induced draft fan, the outlet of the induced draft fan is connected to the heat exchange device, and the outlet of the heat exchange device is connected with the dioxin chemical catalytic device, dioxin chemistry
  • the catalytic device is connected to the chimney, and the flue gas is finally discharged into the atmosphere through a series of purification.
  • the upper part of the quenching tower is provided with a spray pipe; after the temperature is lowered, the temperature of the flue gas is 160 ° C - 180 ° C.
  • the electromagnetic pulse dust collector is composed of a plurality of cloth bags, and the pollutants in the flue gas are adsorbed on the surface of the filter bag.
  • the electromagnetic pulse dust collector is provided with a pulse valve.
  • An auxiliary feeding device is installed on the flue gas pipeline between the quenching tower and the electromagnetic pulse dust collector; calcium hydroxide and a reaction auxiliary agent are added to remove various acid gases and dioxins in the flue gas, The flue gas temperature is reduced to 100 ° C - 140 ° C.
  • the waste heat utilization and cooling device is connected between the electromagnetic pulse dust collector and the carbon fiber filter device; the flue gas after the heat energy utilization is re-entered into the cooling device to reduce the flue gas temperature to 40 ° C - 60 ° C.
  • the carbon fiber filter device is composed of an orderly arrangement of a plurality of carbon fiber filter elements.
  • the induced draft fan is located behind the carbon fiber filter device and adopts frequency conversion speed regulation to ensure the furnace pressure required for the pyrolysis incinerator under different working conditions.
  • the heat exchange device is located above the pyrolysis incinerator; the temperature reaches 210 ° C - 250 ° C.
  • the dioxin chemical catalytic device is composed of a plurality of catalyst modules, and the whole is an erected rectangular parallelepiped.
  • the catalyst in the module can catalytically oxidize and decompose dioxin to form harmless substances.
  • the main function of the quenching tower is to cool the flue gas generated by the waste pyrolysis incinerator, wherein the quenching tower is provided with a spray pipe on the upper part, the spray pipe is installed on the upper part of the quenching tower, and the cooling water is sprayed from the spray Sprayed in the shower tube, the flue gas is cooled sharply, and the cooling water is recycled.
  • the electromagnetic pulse dust collector is composed of a plurality of cloth bags, and the pollutants in the flue gas are adsorbed on the surface of the filter bag, which can effectively remove acid and adsorb harmful gases such as dioxins.
  • the electromagnetic pulse dust collector is provided with a pulse valve, each time opening a group of pulse valves to remove the dust of the part of the bag or the filter cylinder controlled by the bag, and the other bags or filter cartridges work normally, after a period of time, the next group The pulse valve is opened to clean the next part of the dust collector.
  • An auxiliary feeding device is installed on the flue gas pipeline between the quenching tower and the electromagnetic pulse dust collector, and calcium hydroxide and a reaction auxiliary agent (activated carbon powder) are added to remove various acid gases in the flue gas and Dioxins.
  • the carbon fiber filter device is composed of a plurality of carbon fiber filter elements arranged in an orderly manner, and can further filter and adsorb harmful gases such as dioxins in the flue gas.
  • the induced draft fan is located after the carbon fiber filter device, and adopts frequency conversion speed regulation, and the first function is to ensure the pressure of the furnace required by the pyrolysis incinerator under different working conditions, and the second is to export the carbon fiber filter device. Flue gas is drawn to the heat exchange device.
  • the heat exchange device is located above the pyrolysis incinerator, and the flue gas is sent to the heat exchange device by the induced draft fan to perform temperature rising treatment.
  • the dioxin chemical catalytic device is composed of a plurality of catalyst modules, and the whole is an erected rectangular parallelepiped.
  • the catalyst in the module can catalytically oxidize and decompose dioxin to form harmless water vapor, carbon dioxide, hydrogen chloride and the like.
  • the service life is more than 16,000 hours.
  • the present invention has the following beneficial effects:
  • the system can purify the flue gas discharged from the thermal incineration of domestic garbage even better than the national standard, and consider using the sensible heat in the flue gas to produce low-pressure steam for production and use;
  • the system adopts two-stage treatment of dioxins in flue gas, and the concentration of dioxins after treatment can reach better than national standards;
  • the system will be heated by the flue gas inhalation heat exchange device of the carbon fiber filter device, which is beneficial to the subsequent treatment of the dioxin chemical catalytic device;
  • the system has only two pumps, one air pump and one induced draft fan, which reduces the auxiliary equipment, increases the safety and reliability of the system, and reduces the operating cost of the system;
  • the flue gas purification system of the domestic waste pyrolysis incinerator provided by the invention can effectively remove pollutants in the incineration flue gas, including CO, SO 2 , NO X , dioxin, etc., especially in the flue gas.
  • the concentration of dioxin can meet national standards ( ⁇ 0.03 ng/m 3 ).
  • Figure 1 Schematic diagram of the flue gas purification system of the domestic waste pyrolysis incinerator.
  • FIG. 1 is a schematic structural diagram of a flue gas purification system for a domestic garbage pyrolysis incinerator according to an embodiment of the present invention.
  • the embodiment of the invention provides a flue gas purification system for a domestic waste pyrolysis incinerator, which comprises a quenching tower (2), an electromagnetic pulse dust collector (3), a waste heat utilization and cooling device (4), and a carbon fiber filtering device (5).
  • heat exchange device (7) heat exchange device (7), dioxin chemical catalytic device (8), water supply system, flue gas duct and induced draft fan (6), the inlet end of the quenching tower (2) and the smoke of the domestic waste pyrolysis incinerator a gas pipe connection, an outlet end of the quenching tower (2) is connected to the electromagnetic pulse dust collector (3), and the electromagnetic pulse dust collector (3) is connected with a waste heat utilization and a cooling device (4), and the waste heat utilization Connected to the cooling device (4) and the carbon fiber filtering device (5), the carbon fiber filtering device (5) is connected to the induced draft fan (6), and the flue gas is sent through the induced draft fan (6) After the heating device (7) is warmed up, it enters the dioxin chemical catalytic device (8), and the dioxin chemical catalytic device (8) is connected to the chimney (9), and the flue gas is finally discharged into the atmosphere through a series of purification.
  • a spray pipe (12) is disposed on an upper portion of the quenching tower (2), and the spray pipe (12) is installed at an upper portion of the quenching tower, and cooling water is sprayed from the spray pipe 12.
  • the electromagnetic pulse dust collector (3) is composed of a plurality of bags (13), and the pollutants in the flue gas are adsorbed on the surface of the filter bag, which can effectively remove acid and adsorb harmful gases such as dioxins.
  • the flue gas pipeline between the quenching tower (2) and the electromagnetic pulse dust collector (3) is equipped with an auxiliary dosing device 1 (10), an auxiliary dosing device 2 (11), and a hydroxide is added. Calcium and a reaction aid (activated carbon powder) to remove various acid gases and dioxins in the flue gas.
  • the main parts of the domestic waste pyrolysis incinerator flue gas purification system are equipped with thermocouples, and the PLC automatic control system is used to monitor the temperature change, and at the same time, the dosing of the auxiliary agent and the power of the fan can be controlled.
  • the domestic garbage is thermally decomposed in the pyrolysis incinerator (1).
  • the diameter of the furnace body is 1.2m and the height is 1.88m.
  • the Q235 carbon steel is used, the inner layer is refractory high temperature material, and the outer wall steel plate is 6mm thick.
  • the inner steel plate is 8mm thick, the refractory material layer is 100mm thick, the working time is 8-10h, the processing capacity is 10t/d, and the furnace temperature can reach 700°C-900°C.
  • the flue gas generated by the pyrolysis incineration is sent to the quenching tower (2) through a flue gas duct, and the sprinkling pipe (12) in the quenching tower (2) starts to spray water, and the cooling water sharply changes the flue gas. Cooling, and the cooling water can be recycled. After cooling, the temperature of the flue gas is reduced to 160 °C-180 °C. After cooling, the calcium hydroxide is added to the flue gas pipeline through the auxiliary feeding device 1 (10).
  • the dosage is adjusted by PLC automatic control system, mainly reducing various acid gases and dioxins in flue gas, Calcium hydroxide neutralizes the acid gas, and the activated carbon powder adsorbs dioxins.
  • the temperature is attenuated to 100° C.-140° C., wherein unreacted calcium hydroxide and a reaction auxiliary agent (activated carbon powder) enter the electromagnetic pulse bag filter (3). Adsorbed on the surface of the filter bag, which can effectively remove acid and adsorb harmful gases such as dioxins.
  • the content of particulate matter in the flue gas is reduced to less than 5 mg/m 3 , the NOx is reduced to about 400 mg/m 3 , and the SO 2 is reduced to 100 mg/m 3 . Left and right, dioxin is reduced to 2 to 3 ng/m 3 . Because the temperature required for carbon fiber adsorption is low, the high-temperature flue gas pipeline section of the electromagnetic pulse dust collector (3) is provided with the waste heat recovery and utilization device (4), and the heat energy of the high-temperature flue gas is collected by the heat exchange device. The flue gas after the heat energy is used to enter the cooling device to continue to cool down, so that the flue gas temperature is lowered to 40 ° C -60 ° C.
  • the carbon fiber filtering device (5) is arranged, and the device is composed of a plurality of carbon fiber filter elements arranged in an orderly manner, and the amount of the activated carbon adsorbing material is 150 kg, which can be pickled to further carry out harmful gases such as dioxins in the flue gas. Filtration adsorption, the dioxin content in the treated flue gas is reduced to less than 1 ng / m 3 .
  • the induced draft fan (6) is disposed behind the carbon fiber filtering device (5), and the induced draft fan (6) adopts frequency conversion speed regulation, and the first function thereof is to ensure the garbage pyrolysis incineration device (1) under different working conditions.
  • the required furnace pressure is such that the pyrolysis incinerator is in a negative pressure state; the second is that the carbon fiber filtering device (5) outlet flue gas is sucked into the heat exchange device (7) because of the new type adopted
  • the dioxin catalyst is suitable for a temperature of 180 ° C to 250 ° C, and the flue gas reaches 210 ° C to 250 ° C through the heat exchange device (7), and then enters the dioxin chemical catalytic device (8).
  • the device is composed of a plurality of catalyst modules, and the whole is an erected rectangular parallelepiped.
  • the catalyst is a new deodorized catalyst developed by a company in Shanghai.
  • the catalyst is honeycomb or granular, and the catalyst in the module can be dioxins.

Abstract

一种生活垃圾热解焚烧装置烟气净化系统：包括急冷塔（2）、电磁脉冲除尘器（3）、余热利用与冷却装置（4）、炭纤维过滤装置（5）、换热装置（7）、二噁英化学催化装置（8）、供水系统、烟气管道和引风机（6）；急冷塔（2）的进口端与生活垃圾热解焚烧装置的烟气管道连接，急冷塔（2）的出口端与电磁脉冲除尘器（3）连接，电磁脉冲除尘器（3）与余热利用与冷却装置（4）连接，余热利用与冷却装置（4）与炭纤维过滤装置（5）连接，炭纤维过滤装置（5）与引风机（6）连接，引风机（6）出口连接换热装置（7），换热装置（7）出口连接二噁英化学催化装置（8），二噁英化学催化装置（8）与烟囱（9）连接，烟气经过一系列净化最终排入大气，够有效地去除焚烧烟气中的污染物，包括CO、SO2、NOX、二噁英等，二噁英浓度满足国家标准。

Description

一种生活垃圾热解焚烧装置烟气净化系统 技术领域
本发明涉及生活垃圾处理处置与资源化利用领域系统，具体地涉及一种生活垃圾热解焚烧装置烟气净化系统。
背景技术
目前我国常用的垃圾处理处置方式有：卫生填埋法、垃圾堆肥法和热处理法等。卫生填埋是我国当前垃圾处理的主要方式，这种处理方式技术简单，处理量大，但占用土地资源过大，存在选址难、渗滤液污染、温室气体排放等问题，且没有对垃圾进行资源化利用。由于生活垃圾中包装材料、纸类和塑料等成分的数量在不断增加，给垃圾堆肥带来了一些问题，且堆肥后容易造成土地盐碱化、产品的市场准入难，使其发展受到限制。而垃圾热处理技术在减容、减量、资源化利用方面具有明显优势，新型垃圾焚烧技术，近年来受到了国家的重视，将是今后垃圾处理处置与资源化利用的主要方向。
热处理技术实质是在高温下将垃圾进行氧化和分解，以形成稳定的固态残渣，但热解焚烧期间会释放出大量的有害气体，粉尘和细小颗粒随风飞扬，致使空气中各种污染物指数超标，而且会产生大量的强致癌物质二噁英，这是目前制约热解焚烧处理技术的主要因素。
为了防止垃圾焚烧处理过程中对环境产生二次污染，必须采取严格的措施，利用烟气净化系统控制垃圾焚烧烟气的排放。烟气中酸性气体的脱除有三种处理工艺：干法、半干法与湿法。半干法净化工艺可达到较高的净化效率，投资和运行费用低，流程简单，不产生废水，欧洲的焚烧厂采用半干法的较多。半干法在国内已有较多成功的应用实例，积累了一定的运行经验，适用于排放标准要求较高的焚烧厂，现在中国在建与待建的多数垃圾焚烧发电厂都选用半干法。干法净化工艺其工艺比较简单，投资低，运行维护方便，但干法工艺净化效率相对较低，在日本近年的焚烧厂建设中采用较多。湿法净化工艺的污染物净化效率最高，可满足最严格的排放标准要求。但由于流程复杂，配套设备较多，一次性投资和运行费用高，在经济发达国家应用较多，在中国得不到广泛应用。就NOx的去除效果而言，SCR对NOx的去除率达到了90％以上，而SNCR对NOx的去除率也可达到50％左右。就成本-效率分析，SCR和先进的焚烧控制系统基本相当，明显比SNCR技术昂贵。自20世 纪80年代末开始，垃圾焚烧厂更多的采用布袋除尘器，其对粉尘的去除效率可达到99.9％以上。我国《生活垃圾焚烧处理工程技术规范》(CJJ90-2009)中明确规定生活垃圾焚烧炉除尘装置必须采用布袋除尘器。而静电除尘器自20世纪70年代起被广泛应用于垃圾焚烧厂。随着环保观念增强，活性炭对二噁英与重金属吸附作用越来越被垃圾焚烧发电厂运用。
生活垃圾焚烧过程产生的烟气中，主要含有SO 2、HCl、NOx、重金属和二噁英类等有害物质。近年来，除了传统的脱硫脱硝以及颗粒物的控制，二噁英污染引起了世界各国人民的普遍关注，而垃圾焚烧厂又是产生二噁英的主要来源之一，由于目前对二噁英的形成机理还没有达成统一的共识，因此仅通过控制焚烧参数来抑制二噁英的生成，其效果很难确定，因此后续对二噁英的处理就变得尤其关键。随着经济的发展，垃圾焚烧烟气排放标准也越来越严格，二噁英从当初的1mg/m 3到0.5mg/m 3，再到如今的0.1mg/m 3，针对二噁英的处理也亟需进行新的变革。
发明内容
本发明提供一种生活垃圾热解焚烧装置烟气净化系统，能够有效地去除焚烧烟气中的污染物，包括CO、SO 2、NO X、二噁英等，尤其针对较难处理的二噁英类污染物进行多段处理，排放烟气中的二噁英浓度优于国家排放标准，起到了环境保护的目的。
本发明的技术方案如下：
一种生活垃圾热解焚烧装置烟气净化系统，包括急冷塔、电磁脉冲除尘器、余热利用与冷却装置、炭纤维过滤装置、换热装置、二噁英化学催化装置、供水系统、烟气管道和引风机；其特征是急冷塔的进口端与生活垃圾热解焚烧装置的烟气管道连接，急冷塔的出口端与所述电磁脉冲除尘器连接，电磁脉冲除尘器与余热利用与冷却装置连接，余热利用与冷却装置与所述炭纤维过滤装置连接，炭纤维过滤装置与所述引风机连接，引风机出口连接换热装置，换热装置出口连接二噁英化学催化装置，二噁英化学催化装置与烟囱连接，烟气经过一系列净化最终排入大气。
所述急冷塔内上部布有喷淋管；经过降温后烟气温度为160℃-180℃。
所述电磁脉冲除尘器内由许多布袋组成，烟气中的污染物吸附在滤袋表面。
所述电磁脉冲除尘器设有脉冲阀。
所述急冷塔和所述电磁脉冲除尘器之间的烟气管道上安装有助剂投加装置；投加氢氧化钙和反应助剂，去除烟气中的各种酸性气体及二噁英，烟气温度减到100℃-140℃。
所述电磁脉冲除尘器和所述炭纤维过滤装置之间连接余热利用与冷却装置；热能利用后的烟气再进入冷却装置，使烟气温度降至40℃-60℃。
所述炭纤维过滤装置由若干个炭纤维滤芯有序排列组成。
所述引风机位于所述炭纤维过滤装置后，采用变频调速，保证在不同工况下热解焚烧装置所需要的炉堂压力。
所述换热装置位于热解焚烧炉的上方；温度达到210℃-250℃。
所述二噁英化学催化装置是由若干个催化剂模块组合而成，整体为一竖立的长方体，模块内的催化剂能将二噁英催化氧化分解，生成无害物质。
具体说明如下：
所述急冷塔主要作用是对垃圾热解焚烧装置产生的烟气进行降温处理，所述急冷塔内上部布有喷淋管，所述喷淋管安装在急冷塔上部，冷却水从所述喷淋管中喷洒下来，对烟气进行急剧降温，冷却水循环利用。
所述电磁脉冲除尘器内由许多布袋组成，烟气中的污染物吸附在滤袋表面，可有效除酸、吸附二噁英等有害气体。
所述电磁脉冲除尘器设有脉冲阀，每次开一组脉冲阀来除去它所控制的那部分布袋或滤筒的灰尘，而其他的布袋或滤筒正常工作，隔一段时间后下一组脉冲阀打开，清理下一部分所述除尘器。
所述急冷塔和所述电磁脉冲除尘器之间的烟气管道上安装有助剂投加装置，投加氢氧化钙和反应助剂(活性炭粉末)，去除烟气中的各种酸性气体及二噁英。
所述炭纤维过滤装置由若干个炭纤维滤芯有序排列组成，可进一步对烟气中二噁英等有害气体进行过滤吸附。
所述引风机位于所述炭纤维过滤装置后，采用变频调速，其作用一是保证不同工况下所述热解焚烧装置所需要的炉堂压力，二是将所述炭纤维过滤装置出口烟气抽吸到所述换热装置。
所述换热装置位于所述热解焚烧炉的上方，烟气由所述引风机送入所述换热装置，进行升温处理。
所述二噁英化学催化装置是由若干个催化剂模块组合而成，整体为一竖立的长方体，模块内的催化剂能将二噁英催化氧化分解，生成无害的水蒸汽、二氧化碳、氯化氢等物质，使用寿命为16000小时以上。
与现有技术相比，本发明具有以下有益效果：
1、本系统能够将生活垃圾热焚烧排放的烟气净化达到甚至明显优于国家标准，并可考虑利用烟气中的显热来生产低压蒸汽供工厂生产生活使用；
2、本系统采用两级处理烟气中二噁英的方法，处理后二噁英浓度可达到优于国家标准；
3、本系统将经过炭纤维过滤装置的烟气吸入换热装置进行升温，利于后续的二噁英化学催化装置处理；
4、本系统只有两个水泵，一个气泵和一个引风机，减少辅助设备，增加该系统的安全可靠性，降低该系统的运行成本；
5、对焚烧烟气进行了较为彻底的净化，减少了烟气的排放，降低了环境污染。
6、本发明提供的生活垃圾热解焚烧装置烟气净化系统能够有效地去除焚烧烟气中的污染物，包括CO、SO 2、NO X、二噁英等，尤其是排放烟气中的二噁英浓度可满足国家标准(<0.03ng/m 3)。
附图说明
图1：生活垃圾热解焚烧装置烟气净化系统的结构示意图。
其中，1、生活垃圾热解焚烧炉；2、急冷塔；3、电磁脉冲除尘器；4、余热利用与冷却装置；5、炭纤维过滤装置；6、引风机；7、换热装置；8、二噁英化学催化装置；9、烟囱；10、助剂投加装置1；11、助剂投加装置2；12、喷淋管；13、布袋。
具体实施方式
下面结合附图对本发明作进一步说明：
以下结合附图和具体实施例对本发明提出的生活垃圾热解焚烧装置烟气净化系统作进一步详细说明。根据下面说明和权利要求书，本发明的优点和特征将更清楚。需说明的是，附图均采用非常简化的形式且均使用非精准的比率，仅用以方便、明晰地辅助说明本发明实施例的目的。
请参考图1，图1为本发明实施例提供的生活垃圾热解焚烧装置烟气净化系统的结构示意图。
本发明实施例提供一种生活垃圾热解焚烧装置烟气净化系统，其包括急冷塔(2)、 电磁脉冲除尘器(3)、余热利用与冷却装置(4)、炭纤维过滤装置(5)、换热装置(7)、二噁英化学催化装置(8)、供水系统、烟气管道和引风机(6)，所述急冷塔(2)的进口端与生活垃圾热解焚烧装置的烟气管道连接，所述急冷塔(2)的出口端与所述电磁脉冲除尘器(3)连接，所述电磁脉冲除尘器(3)与余热利用与冷却装置(4)连接，所述余热利用与冷却装置(4)与所述炭纤维过滤装置(5)连接，所述炭纤维过滤装置(5)与所述引风机(6)连接，烟气经过所述引风机(6)送入换热装置(7)升温后，进入所述二噁英化学催化装置(8)，所述二噁英化学催化装置(8)与烟囱(9)连接，烟气经过一系列净化最终排入大气。
所述急冷塔(2)内上部布有喷淋管(12)，所述喷淋管(12)安装在所述急冷塔上部，冷却水从所述喷淋管12中喷洒下来。
所述电磁脉冲除尘器(3)内由许多布袋(13)组成，烟气中的污染物吸附在滤袋表面，可有效除酸、吸附二噁英等有害气体。
所述急冷塔(2)和所述电磁脉冲除尘器(3)之间的烟气管道上安装有助剂投加装置1(10)、助剂投加装置2(11)，投加氢氧化钙和反应助剂(活性炭粉末)，去除烟气中的各种酸性气体及二噁英。
所述生活垃圾热解焚烧装置烟气净化系统的各个主要部位都安装有热电偶，运用PLC自动化控制系统来监控温度变化，同时还可以控制助剂的投加、风机的功率等。
当本系统正常运行时，生活垃圾在所述热解焚烧炉(1)中进行热分解，炉体直径1.2m，高度1.88m，采用Q235碳钢，内层是耐火高温材料，外壁钢板6mm厚，内胆钢板8mm厚，耐火材料层厚100mm，每天工作时长8-10h，处理量10t/d，炉内温度可达700℃-900℃。热解焚烧所产生的烟气通过烟气管道送入所述急冷塔(2)，所述急冷塔(2)中的所述喷淋管(12)开始喷水，冷却水对烟气进行急剧冷却，并且冷却水可以循环利用，经过降温后烟气温度降为160℃-180℃，降温后在烟气管道中通过助剂投加装置1(10)加投氢氧化钙，通过助剂投加装置2(11)加投活性炭粉末；石灰泵和活性炭粉泵额定功率均为0.75kw，投加量由PLC自动化控制系统进行调节，主要降低烟气中的各种酸性气体及二噁英，氢氧化钙中和酸性气体，活性炭粉末吸附二噁英。烟气经过急冷降温、投加助剂反应后，温度衰减到100℃-140℃，其中未反应的氢氧化钙及反应助剂(活性炭粉末)，进入所述电磁脉冲布袋除尘器(3)，吸附在滤袋表面，可有效除酸、吸附二噁英等有害气体，烟气中的颗粒物含量降低到5mg/m 3以下，NOx降低到400mg/m 3左右，SO 2降低到100mg/m 3左右， 二噁英降低到2～3ng/m 3。因为炭纤维吸附所需温度较低，所述电磁脉冲除尘器(3)出口的高温烟气管道段设所述余热回收利用装置(4)，将高温烟气中热能用换热装置收集起来，热能利用后的烟气再进入冷却装置继续降温，使烟气温度降至40℃-60℃。烟气冷却后进入所述炭纤维过滤装置(5)，该装置由若干个炭纤维滤芯有序排列组成，活性炭吸附材料用量150kg，可酸洗，进一步对烟气中二噁英等有害气体进行过滤吸附，处理完的烟气中二噁英含量降低到1ng/m 3以下。所述引风机(6)设置在所述炭纤维过滤装置(5)后方，所述引风机(6)采用变频调速，其作用一是保证不同工况下垃圾热解焚烧装置(1)所需要的炉堂压力，使热解焚烧炉中处于负压状态；二是将所述炭纤维过滤装置(5)出口烟气抽吸到所述换热装置(7)中，因为所采用的新型脱二噁英催化剂适用温度为180℃-250℃，烟气经过所述换热装置(7)达到210℃-250℃，然后进入所述二噁英化学催化装置(8)。该装置由若干个催化剂模块组合而成，整体为一竖立的长方体，催化剂采用的是上海某公司开发的新型脱二噁英催化剂，催化剂为蜂窝状或颗粒状，模块内的催化剂能将二噁英催化氧化分解，生成无害的水蒸汽、二氧化碳、氯化氢等物质，使用寿命为16000小时以上。经过处理后的烟气可达到表1所示效果，符合《生活垃圾焚烧污染控制标准》(GB18485-2014)中对于生活垃圾焚烧炉排放烟气污染物限值的要求，最后通过烟囱(9)排入大气。
表1处理后烟气污染物指标
Figure PCTCN2018083865-appb-000001
显然，本领域的技术人员可以对本发明进行各种改动和变形而不脱离本发明的精神和范围。这样，倘若本发明的这些修改和变型属于本发明权利要求及其等同技术的范围之内，则本发明也意图包含这些改动和变型在内。

Claims (10)

  1. 一种生活垃圾热解焚烧装置烟气净化系统，包括急冷塔、电磁脉冲除尘器、余热利用与冷却装置、炭纤维过滤装置、换热装置、二噁英化学催化装置、供水系统、烟气管道和引风机；其特征是急冷塔的进口端与生活垃圾热解焚烧装置的烟气管道连接，急冷塔的出口端与所述电磁脉冲除尘器连接，电磁脉冲除尘器与余热利用与冷却装置连接，余热利用与冷却装置与所述炭纤维过滤装置连接，炭纤维过滤装置与所述引风机连接，引风机出口连接换热装置，换热装置出口连接二噁英化学催化装置，二噁英化学催化装置与烟囱连接，烟气经过一系列净化最终排入大气。
  2. 如权利要求1所述的装置，其特征是所述急冷塔内上部布有喷淋管；经过降温后烟气温度为160℃-180℃。
  3. 如权利要求1所述的装置，其特征是所述电磁脉冲除尘器内由许多布袋组成，烟气中的污染物吸附在滤袋表面。
  4. 如权利要求1所述的装置，其特征是所述电磁脉冲除尘器设有脉冲阀，每次开一组脉冲阀来除去它所控制的那部分布袋或滤筒的灰尘，而其他的布袋或滤筒正常工作，隔一段时间后下一组脉冲阀打开，清理下一部分所述除尘器。
  5. 如权利要求1所述的装置，其特征是所述急冷塔和所述电磁脉冲除尘器之间的烟气管道上安装有助剂投加装置；投加氢氧化钙和反应助剂，去除烟气中的各种酸性气体及二噁英，烟气温度减到100℃-140℃。
  6. 如权利要求1所述的装置，其特征是在所述电磁脉冲除尘器和所述炭纤维过滤装置之间连接余热利用与冷却装置；热能利用后的烟气再进入冷却装置，使烟气温度降至40℃-60℃。
  7. 如权利要求1所述的装置，其特征是所述炭纤维过滤装置由若干个炭纤维滤芯有序排列组成。
  8. 如权利要求1所述的装置，其特征是所述引风机位于所述炭纤维过滤装置后，采用变频调速，保证在不同工况下热解焚烧装置所需要的炉堂压力。
  9. 如权利要求1所述的装置，其特征是所述换热装置位于热解焚烧炉的上方；温度达到210℃-250℃。
  10. 如权利要求1所述的装置，其特征是所述二噁英化学催化装置是由若干个催化剂模块组合而成，整体为一竖立的长方体，模块内的催化剂能将二噁英催化氧化分解，生成无害物质。
PCT/CN2018/083865 2017-04-21 2018-04-20 一种生活垃圾热解焚烧装置烟气净化系统 WO2018192564A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201710266670.1 2017-04-21
CN201710266670.1A CN107120660A (zh) 2017-04-21 2017-04-21 一种生活垃圾热解焚烧装置烟气净化系统

Publications (1)

Publication Number Publication Date
WO2018192564A1 true WO2018192564A1 (zh) 2018-10-25

Family

ID=59725935

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2018/083865 WO2018192564A1 (zh) 2017-04-21 2018-04-20 一种生活垃圾热解焚烧装置烟气净化系统

Country Status (2)

Country Link
CN (1) CN107120660A (zh)
WO (1) WO2018192564A1 (zh)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107120660A (zh) * 2017-04-21 2017-09-01 天津大学 一种生活垃圾热解焚烧装置烟气净化系统
CN108654367A (zh) * 2018-06-14 2018-10-16 山西普丽环境工程股份有限公司 一种应用催化剂的二噁英脱除装置
CN108980841A (zh) * 2018-06-14 2018-12-11 中国航天员科研训练中心 一种密闭环境系统中的固体废物高温氧化装置及方法
CN109173661A (zh) * 2018-08-31 2019-01-11 南宁市绿城环保设备有限责任公司 一种用于垃圾焚烧烟气处理装置
CN114110613A (zh) * 2021-11-25 2022-03-01 内蒙古恒星化学有限公司 有机硅废料的焚烧方法及系统

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4502349B2 (ja) * 2001-02-23 2010-07-14 三井造船株式会社 排ガス処理装置および排ガス処理方法
CN101797472A (zh) * 2009-05-04 2010-08-11 上海蓝鸟环境科技发展有限公司 一种烟气处理工艺
CN103994447A (zh) * 2014-06-18 2014-08-20 江苏安琪尔废气净化有限公司 气固液一体化焚烧系统
CN105627335A (zh) * 2016-02-05 2016-06-01 江苏全能机电装备工程股份有限公司 焚烧尾气超净处理方法
CN205815444U (zh) * 2016-06-03 2016-12-21 上海第升环保科技有限公司 一种用于焚烧尾气中二噁英和臭气处理的装置
CN107120660A (zh) * 2017-04-21 2017-09-01 天津大学 一种生活垃圾热解焚烧装置烟气净化系统

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW386894B (en) * 1997-06-20 2000-04-11 Von Roll Umwelttechnik Ag Process and plant for deNOxing combustion off-gas
CN102961953A (zh) * 2012-03-09 2013-03-13 明峰 用“电离”技术治理工业锅炉烟气污染系统
CN203628674U (zh) * 2013-07-08 2014-06-04 上海灿州环境工程有限公司 一种危险废物焚烧炉成套装置
CN104815512B (zh) * 2015-05-27 2016-05-04 成都虹华环保科技股份有限公司 一种循环水洗式的废气处理装置

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4502349B2 (ja) * 2001-02-23 2010-07-14 三井造船株式会社 排ガス処理装置および排ガス処理方法
CN101797472A (zh) * 2009-05-04 2010-08-11 上海蓝鸟环境科技发展有限公司 一种烟气处理工艺
CN103994447A (zh) * 2014-06-18 2014-08-20 江苏安琪尔废气净化有限公司 气固液一体化焚烧系统
CN105627335A (zh) * 2016-02-05 2016-06-01 江苏全能机电装备工程股份有限公司 焚烧尾气超净处理方法
CN205815444U (zh) * 2016-06-03 2016-12-21 上海第升环保科技有限公司 一种用于焚烧尾气中二噁英和臭气处理的装置
CN107120660A (zh) * 2017-04-21 2017-09-01 天津大学 一种生活垃圾热解焚烧装置烟气净化系统

Also Published As

Publication number Publication date
CN107120660A (zh) 2017-09-01

Similar Documents

Publication Publication Date Title
WO2018192564A1 (zh) 一种生活垃圾热解焚烧装置烟气净化系统
CN102120130B (zh) 一种半干法处理污泥焚烧尾气的成套装置及方法
WO2021114084A1 (zh) 一种垃圾焚烧节能烟气超低净化系统
CN108636098A (zh) 一种城市生活垃圾焚烧烟气的超低排放净化装置及其方法
CN101822942B (zh) 一种固体废物焚烧烟气中二噁英、重金属湿法净化方法
CN205055820U (zh) 垃圾焚烧尾气的净化处理系统
CN111729490A (zh) 一种活性炭再生过程中废气处理工艺
CN212188526U (zh) 一种污泥处理后的烟气处理系统
CN201899980U (zh) 一种半干法处理污泥焚烧尾气的成套装置
CN108452663A (zh) 固废物焚烧烟气净化处理方法
CN215388629U (zh) 用于垃圾焚烧烟气的污染物协同净化系统
CN214809730U (zh) 垃圾焚烧烟气净化系统
CN113776061A (zh) 一种危废焚烧烟气净化与余热回收装置及其方法
CN113587117A (zh) 一种无害化处置污泥的系统及方法
CN210278758U (zh) 一种生活垃圾焚烧炉烟气超净排放处理装置
CN106139840A (zh) 含低浓度voc废气的净化装置及方法
CN204619702U (zh) 一种含低浓度voc废气的净化装置
CN102895856A (zh) 一种垃圾焚烧烟气净化的设备及其净化工艺
WO2006076849A1 (fr) Procede de nettoyage pour convertir un gaz residuaire en un gaz residuaire organique industriel pouvant etre utilise en circulation
CN110841447A (zh) 一种垃圾焚烧烟气的湿法-scr联合净化方法及系统
CN116422311A (zh) 一种活性炭的热再生装置及再生方法
CN116293721A (zh) 一种贵金属焚烧及尾气净化工艺
CN212651583U (zh) 一种双循环式活性炭分离解析的垃圾焚烧烟气处理系统
CN212091626U (zh) 一种焚烧炉烟道气多污染物干式净化装置
CN113813771A (zh) 一种pan基碳纤维生产废气净化方法

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 18787492

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 18787492

Country of ref document: EP

Kind code of ref document: A1

32PN Ep: public notification in the ep bulletin as address of the adressee cannot be established

Free format text: NOTING OF LOSS OF RIGHTS PURSUANT TO RULE 112(1) EPC (EPO FORM 1205A DATED 20/05/2020)

122 Ep: pct application non-entry in european phase

Ref document number: 18787492

Country of ref document: EP

Kind code of ref document: A1