CN105805763A - Medical waste incineration system - Google Patents

Medical waste incineration system Download PDF

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Publication number
CN105805763A
CN105805763A CN201610140910.9A CN201610140910A CN105805763A CN 105805763 A CN105805763 A CN 105805763A CN 201610140910 A CN201610140910 A CN 201610140910A CN 105805763 A CN105805763 A CN 105805763A
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China
Prior art keywords
incineration system
heat exchanger
bag
tower
medical wastes
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Granted
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CN201610140910.9A
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Chinese (zh)
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CN105805763B (en
Inventor
江正云
杨巍
李建康
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Publication of CN105805763B publication Critical patent/CN105805763B/en
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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • 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
    • F23J15/04—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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L15/00—Heating of air supplied for combustion
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2202/00—Combustion
    • F23G2202/10—Combustion in two or more stages
    • F23G2202/103—Combustion in two or more stages in separate chambers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2203/00—Furnace arrangements
    • F23G2203/20—Rotary drum furnace
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2206/00—Waste heat recuperation
    • F23G2206/10—Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00—Specific waste
    • F23G2209/20—Medical materials
    • 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
    • F23J2215/20—Sulfur; Compounds thereof
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2219/00—Treatment devices
    • F23J2219/20—Non-catalytic reduction devices
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2219/00—Treatment devices
    • F23J2219/30—Sorption devices using carbon, e.g. coke
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
    • F23L2900/15043—Preheating combustion air by heat recovery means located in the chimney, e.g. for home heating devices
    • 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
    • Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Abstract

The invention discloses a medical waste incineration system. The medical waste incineration system mainly solves the problems that an existing medical waste incineration system in the prior art is liable to cause cross contamination, medical waste cannot be incinerated in time, loads of a bag-type dust remover are large, and a bag is liable to be burnt to damage. The medical waste incineration system comprises a feeding device, a rotary kiln, secondary combustion chamber, a heat exchange device, a shock cooling device, an adsorption tower, a bag-type dust remover, an induced draught fan, a washing tower and a chimney which sequentially communicate. The feeding device comprises a waste barrel storing area, a cleaning barrel storing area and a lifting discharging table used for lifting a vehicle to the waste barrel storing area. An automatic circulation barrel cleaning machine communicates between the medical waste barrel storing area and the cleaning barrel storing area. The bag-type dust remover comprises a bag bin and a shell. The bag bin is arranged in the shell. A gap is reserved between the bag bin and the shell and communicates with at least one heat exchanger through a pipeline. By means of the above scheme, the purposes that cross contamination does not exist, the loads of the bag-type dust remover are reduced, and a bag is not liable to be burnt to damage are achieved.

Description

Medical wastes incineration system
Technical field
The present invention relates to a kind of MEDICAL WASTE TREATMENT system, specifically, relate to a kind of medical wastes incineration system.
Background technology
Hospital wastes are different from house refuse, medical waste thing contains substantial amounts of antibacterial, virus and chemical agent, there is extremely strong infectiousness, bio-toxicity and corrosivity, unprocessed or process halfway medical waste and arbitrarily stack, very easily cause the pollution to water body, soil and air, human body is produced direct or indirect harm, it is also possible to become the source of pestilence；Along with the increase of current population, living standards of the people and medical level improve, medical waste treatment amount also increases year by year.
Existing medical wastes incineration system can not meet effective, quick, the safe disposal of clinical waste；In the process of existing clinical waste, major part adopts double tower deacidification, absorption and bag-type dust, and in this traditional handicraft, discharging turnover barrel is clear, dirty at the same area, it is easy to cause pollution of reporting to the leadship after accomplishing a task；Rotary kiln incineration operating mode is unstable, and doctor is useless can not be burned in time；Combustion room knot ash is serious, and cannot deashing, it is impossible to meets and produces continuously；The sack cleaner now adopted is easily relatively big because of the internal and external walls temperature difference, causes its load relatively big, and during ash discharge, cold air enters sack cleaner and helps oxygen, easily causes the scaling loss of cloth bag.
Summary of the invention
The problem to be solved in the present invention is that existing medical wastes incineration system easily causes that pollution of reporting to the leadship after accomplishing a task, doctor useless can not burn in time, sack cleaner load is relatively big, the easy scaling loss of cloth bag.
In order to solve the problems referred to above, the present invention provides following technical scheme:
Feed arrangement that medical wastes incineration system includes being sequentially communicated, rotary kiln, dual firing chamber, heat-exchanger rig, chilling apparatus, adsorption tower, sack cleaner, air-introduced machine, scrubbing tower, chimney；Feed arrangement include useless bucket storage area, clean bucket storage area, for vehicle being promoted to the lifting discharging platform of useless bucket storage area；Medical treatment is useless is communicated with turnover barrel automatic rinser between bucket storage area, clean bucket storage area.
Further, rotary kiln has charging aperture, and charging aperture is connected to feeding-passage；Described medical wastes incineration system also includes the elevator for clinical waste is poured into feeding-passage；Rotary kiln is provided with and pushes away cylinder for being pushed by clinical waste in charging aperture in rotary kiln；Feeding-passage is provided with double disc.
Specifically, rotary kiln has outlet, and outlet is connected to mucking machine.
Further, heat-exchanger rig includes multiple heat exchanger being sequentially communicated；Heat exchanger is connected to aerator；The heat exchanger being positioned at one end connects with dual firing chamber.
Specifically, chilling apparatus includes being sequentially communicated a temperature-reducing tower, extracting tower, secondary flash cold column；Temperature-reducing tower and secondary flash cold column have been respectively communicated with alkali liquor configuration case；Extracting tower is communicated with Sal Nitri ash bin；One time temperature-reducing tower connects with the heat exchanger being positioned at the other end, and secondary flash cold column connects with adsorption tower.
Further, sack cleaner includes cloth bag bin, shell；Cloth bag bin is arranged in the enclosure, has gap between cloth bag bin and shell, and gap and at least one heat exchanger pass through pipeline communication.
Specifically, sack cleaner has outlet, and its outlet is connected to for the ashes of clinical waste after burning are made the blender of solid.
Specifically, dual firing chamber is vertical dual firing chamber；Heat exchanger is air heat exchanger；Activated carbon it is provided with in adsorption tower；Blender is forced stirrer；Mucking machine is spiral tapping machine；Elevator is multi-rope hoist；Heat exchanger can have the heat exchanger of heat exchange function for other；Other materials with adsorption function can be set in adsorption tower；Blender is alternatively other types blender；Mucking machine can be other types blender；Elevator other can carry the elevator of multiple turnover barrel.
Compared with prior art, the method have the advantages that the turnover barrel of cleaning and the turnover barrel not cleaned are laid respectively in useless bucket storage area, clean bucket storage area by the present invention, stop it is placed cross-contamination jointly that bring, realized automatically cleaning and separated by turnover barrel automatic rinser；The useless bucket storage area of medical treatment, clean bucket storage area saved use space for setting up and down.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
In above-mentioned accompanying drawing, the component names that accompanying drawing labelling is corresponding is as follows:
1-rotary kiln, 2-dual firing chamber, 3-adsorption tower, 4-sack cleaner, 5-air-introduced machine, 6-scrubbing tower, 7-chimney, 8-feeding-passage, 9-elevator, 10-pushes away cylinder, 11-double disc, 12-mucking machine, 13-heat exchanger, 14-aerator, temperature-reducing tower of 15-, 16-extracting tower, No. bis-flash cold columns of 17-, 18-alkali liquor configuration case, 19-Sal Nitri ash bin, 20-cloth bag bin, 21-shell, 22-blender, 23-turnover barrel automatic rinser, 24-promotes discharging platform, and 25-gives up bucket storage area, 26-clean bucket storage area.
Detailed description of the invention
Below in conjunction with drawings and Examples, the invention will be further described, and embodiments of the present invention include but not limited to the following example.
Embodiment 1
As it is shown in figure 1, medical wastes incineration system include being sequentially communicated feed arrangement, rotary kiln 1, dual firing chamber 2, heat-exchanger rig, chilling apparatus, adsorption tower 3, sack cleaner 4, air-introduced machine 5, scrubbing tower 6, chimney 7；Feed arrangement include useless bucket storage area 25, clean bucket storage area 26, for vehicle being promoted to the lifting discharging platform 24 of useless bucket storage area 25；Medical treatment is useless is communicated with turnover barrel automatic rinser between bucket storage area 25, clean bucket storage area 26；Sack cleaner 4 has outlet, and its outlet is connected to for the ashes of clinical waste after burning are made the blender 22 of solid；For save use the useless bucket storage area 25 of medical treatment in space the present embodiment, clean bucket storage area 26 be setting up and down；Turnover barrel and the turnover barrel not cleaned of cleaning are laid respectively in useless bucket storage area 25, clean bucket storage area 26 by the present invention, have stopped it is placed cross-contamination jointly that bring, realize automatically cleaning and separated by turnover barrel automatic rinser 23.
Rotary kiln 1 has charging aperture, and charging aperture is connected to feeding-passage 8；Described medical wastes incineration system also includes the elevator 9 for clinical waste is poured into feeding-passage 8；Rotary kiln 1 has outlet, and outlet is connected to mucking machine 12；Heat-exchanger rig includes multiple heat exchanger 13 being sequentially communicated；Heat exchanger 13 is connected to aerator 14；The heat exchanger 13 being positioned at one end connects with dual firing chamber 2；In the present embodiment, heat exchanger 13 is two, and time actually used, the quantity of heat exchanger 13 is determined according to actual needs.
A temperature-reducing tower 15 that chilling apparatus includes being sequentially communicated, extracting tower 16, secondary flash cold column 17；Temperature-reducing tower 15 and secondary flash cold column 17 have been respectively communicated with alkali liquor configuration case 18；Extracting tower 16 is communicated with Sal Nitri ash bin 19；Slaked lime can replace with the material of other concrete deacidification functions；One time temperature-reducing tower 15 connects with the heat exchanger 13 being positioned at the other end, and secondary flash cold column 17 connects with adsorption tower 3.
Wherein, dual firing chamber 2 is vertical dual firing chamber, and vertical dual firing chamber increases the capacity of dual firing chamber 2, makes flue gas obtain secondary and fully burns, and flue gas residence time is longer, reaches 4s；Being provided with spiral ash hoist bottom dual firing chamber 2, the outlet of spiral ash hoist is connected to forced stirrer；Heat exchanger 13 is air heat exchanger；It is provided with activated carbon in adsorption tower 3；Blender 22 is forced stirrer；Mucking machine 12 is spiral tapping machine；Elevator 9 is multi-rope hoist, and optional two-sided, twin-tub exchange promotes feeding, also can feeding in time when ensureing to meet mechanical breakdown with this；Heat exchanger 13 can have the heat exchanger 13 of heat exchange function for other；Other materials with adsorption function can be set in adsorption tower 3；Blender 22 is alternatively other types blender 22；Mucking machine 12 can be other types blender 22；Elevator 9 other can carry the elevator 9 of multiple turnover barrel.
Embodiment 2
The difference of the present embodiment and embodiment 1 is in that, rotary kiln 1 is provided with and pushes away cylinder 10 for being pushed by clinical waste in charging aperture in rotary kiln 1；Feeding-passage 8 is provided with double disc 11；Clinical waste passes through double disc 11, push away cylinder 10 and will be located in the clinical waste of charging aperture and push in rotary kiln 1, it is to avoid rotary kiln 1 fed material from being blocked.
Embodiment 3
The present embodiment difference from embodiment 1 and embodiment 2 is in that, sack cleaner 4 includes cloth bag bin 20, shell 21；Cloth bag bin 20 is arranged in shell 21, has gap between cloth bag bin 20 and shell 21, and gap and at least one heat exchanger 13 pass through pipeline communication；Gap introduces the thermal air of heat exchanger 13 conversion, cloth bag bin 20 is made to keep permanent steady, it is to avoid its inwall or outer wall condensation produce dewing corrosion cloth bag bin 20, increase the filter area of cloth bag bin 20 simultaneously, reduce its load, can steady and continuous work when deashing.
Embodiment 1-3 is in use, lifting discharging platform 24 will be equipped with the vehicle of clinical waste and is promoted to useless bucket storage area 25, multiple turnover barrels equipped with clinical waste are proposed to pour clinical waste therein into feeding-passage 8 by elevator 9, under double disc 11 with the effect pushing away cylinder 10, clinical waste enters in rotary kiln 1 and burns, and the solid residue in rotary kiln 1 is exported outside rotary kiln 1 by mucking machine 12；For thoroughly decomposing the oxious component in flue gas, enter in vertical dual firing chamber from rotary kiln 1 flue gas out and burn further, and to keep dual firing chamber 2 flue-gas temperature be 850～1200 DEG C, the time of staying is not less than 3s, simultaneously for ensureing that in dual firing chamber 2 exiting flue gas, oxygen content reaches 6%～10% dry flue gas, reduces fuel consumption, send in dual firing chamber 2 after secondary wind is preheated to 160 DEG C, vertical dual firing chamber top is provided with emergent chimney 7 and water-cooled valve, and the flue gas after dual firing chamber 2 burning enters in air heat exchanger；Air heat exchanger is multiple, adds heat exchange area, makes air heat-exchange become 160 DEG C～250 DEG C, helps oxygen and cloth bag bin 20, casing heating for burning, simultaneously by interval, flue-gas temperature heat exchange to 800 DEG C～850 DEG C, creates conditions for follow-up gas cleaning；Flue gas in air heat exchanger passes sequentially through temperature-reducing tower 15, extracting tower 16, a secondary flash cold column 17；Temperature-reducing tower 15 and secondary flash cold column 17 form double tower cooling and are quenched, flue gas is initially entered a temperature-reducing tower 15 and is lowered the temperature at 550 DEG C-600 DEG C by water, gas, atomization, flue gas enters back in extracting tower 16, extracting tower 16 carries out dry-process deacidification by adding slaked lime, secondary flash cold column 17 is entered back into after deacidification, again by water, gas, atomization cooling, controlling exit gas temperature is 160 DEG C-180 DEG C；Flue gas in secondary flash cold column 17 enters adsorption tower 3, is adsorbed by activated carbon, again purifying smoke, and the flue gas after purification enters in bag-type dust collector；
Purifying smoke again, flue gas after purification enters in bag-type dust collector, bag-type dust collector is provided with two layers of cloth bag bin 20 wall, the thermal air changed by air heat exchanger is introduced in the middle of two layers of cloth bag bin 20 wall, bag-type dust collector has forced stirrer, and bag-type dust collector is connected by air-introduced machine 5 and scrubbing tower 6；Scrubbing tower 6 adopt the cooling water in a temperature-reducing tower 15 and secondary flash cold column 17 carry out alkali liquor configuration and the tail gas before discharge is carried out wet method deacidification again.For preventing equipment corrosion, air-introduced machine 5 and scrubbing tower 6 material selection 316L rustless steel make, and the exit of scrubbing tower 6 is connected to chimney 7, and the flue gas after processing directly is discharged；
Secondary flash cold column 17 takes water and compression air two-phase flow system, atomizes water into very small water smoke with compression air, makes water smoke completely vaporize within the time of 1.5 seconds so that flue-gas temperature is also down to 200 DEG C from 550 DEG C in 1.5s；Secondary flash cold column 17 adopts complete dry type to run, and does not produce any liquid in tower；Constant voltage operation, i.e. compressed-air actuated constant pressure, compression air and the flow of water and the pressure of atomized water are automatically adjusted with the fluctuation of outlet temperature, to ensure that exit gas temperature is constant in set point.
According to above-described embodiment, the present invention just can be realized well.What deserves to be explained is; under premise based on said structure design, for solving same technical problem, even if some making in the present invention are without substantial change or polishing; the essence of the technical scheme adopted is still the same with the present invention, therefore it should also be as in protection scope of the present invention.

Claims (8)

1. a medical wastes incineration system, it is characterised in that: the feed arrangement that includes being sequentially communicated, rotary kiln (1), dual firing chamber (2), heat-exchanger rig, chilling apparatus, adsorption tower (3), sack cleaner (4), air-introduced machine (5), scrubbing tower (6), chimney (7)；Feed arrangement include useless bucket storage area (25), clean bucket storage area (26), for vehicle being promoted to the lifting discharging platform (24) of useless bucket storage area；Medical treatment is useless is communicated with turnover barrel automatic rinser (23) between bucket storage area (25), clean bucket storage area (26).
2. medical wastes incineration system according to claim 1, it is characterised in that: rotary kiln (1) has charging aperture, and charging aperture is connected to feeding-passage (8)；Described medical wastes incineration system also includes the elevator (9) for clinical waste is poured into feeding-passage (8)；Rotary kiln (1) is provided with and pushes away cylinder (10) for being pushed by clinical waste in charging aperture in rotary kiln (1)；Feeding-passage (8) is provided with double disc (11).
3. medical wastes incineration system according to claim 2, it is characterised in that: rotary kiln (1) has outlet, and outlet is connected to mucking machine (12).
4. medical wastes incineration system according to claim 3, it is characterised in that: heat-exchanger rig includes multiple heat exchanger (13) being sequentially communicated；Heat exchanger (13) is connected to aerator (14)；The heat exchanger (13) being positioned at one end connects with dual firing chamber (2).
5. medical wastes incineration system according to claim 4, it is characterised in that: a temperature-reducing tower (15) that chilling apparatus includes being sequentially communicated, extracting tower (16), secondary flash cold column (17)；Temperature-reducing tower (15) and secondary flash cold column (17) have been respectively communicated with alkali liquor configuration case (18)；Extracting tower (16) is communicated with Sal Nitri ash bin (19)；One time temperature-reducing tower (15) connects with the heat exchanger (13) being positioned at the other end, and secondary flash cold column (17) connects with adsorption tower (3).
6. medical wastes incineration system according to claim 5, it is characterised in that: sack cleaner (4) includes cloth bag bin (20), shell (21)；Cloth bag bin (20) is arranged in shell (21), has gap between cloth bag bin (20) and shell (21), and gap and at least one heat exchanger (13) pass through pipeline communication.
7. medical wastes incineration system according to claim 6, it is characterised in that: sack cleaner (4) has outlet, and its outlet is connected to for the ashes of clinical waste after burning are made the blender (22) of solid.
8. the medical wastes incineration system according to claim 3 or 7, it is characterised in that: dual firing chamber (2) is vertical dual firing chamber；Heat exchanger (13) is air heat exchanger；Adsorption tower is provided with activated carbon in (3)；Blender (22) is forced stirrer；Mucking machine (12) is spiral tapping machine；Elevator (9) is multi-rope hoist.
CN201610140910.9A 2016-03-14 2016-03-14 Medical wastes incineration system Active CN105805763B (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106524193A (en) * 2016-12-27 2017-03-22 安徽金鼎锅炉股份有限公司 Incineration treatment system for oily sludge
CN109442436A (en) * 2018-10-16 2019-03-08 常熟重型机械制造有限公司 A kind of low heat value organic waste liquid burning processing system and method
CN113375164A (en) * 2021-07-06 2021-09-10 江阴市锦绣江南环境发展有限公司 Incineration system easy to arrange

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CN103557526A (en) * 2013-11-01 2014-02-05 上海灿州环境工程有限公司 Complete equipment of hazardous waste and medical waste incinerator and incineration method of hazardous waste and medical waste
CN205957191U (en) * 2016-03-14 2017-02-15 江正云 Medical waste system of burning

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JP2000240932A (en) * 1999-02-22 2000-09-08 Miura Co Ltd Refuse incineration device equipped with removing means for dioxins
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Publication number Priority date Publication date Assignee Title
CN106524193A (en) * 2016-12-27 2017-03-22 安徽金鼎锅炉股份有限公司 Incineration treatment system for oily sludge
CN109442436A (en) * 2018-10-16 2019-03-08 常熟重型机械制造有限公司 A kind of low heat value organic waste liquid burning processing system and method
CN113375164A (en) * 2021-07-06 2021-09-10 江阴市锦绣江南环境发展有限公司 Incineration system easy to arrange
CN113375164B (en) * 2021-07-06 2024-04-12 江阴市锦绣江南环境发展有限公司 Incineration system easy to arrange

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