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CN106949477B - A kind of processing system of Biohazard Waste and its use technique - Google Patents

A kind of processing system of Biohazard Waste and its use technique Download PDF

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Publication number
CN106949477B
CN106949477B CN201710288028.3A CN201710288028A CN106949477B CN 106949477 B CN106949477 B CN 106949477B CN 201710288028 A CN201710288028 A CN 201710288028A CN 106949477 B CN106949477 B CN 106949477B
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China
Prior art keywords
gas
furnace body
rotating furnace
waste
shell
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CN201710288028.3A
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CN106949477A (en
Inventor
陈侲龙
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Liuhe Peak (tianjin) Polytron Technologies Inc
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Liuhe Peak (tianjin) Polytron Technologies Inc
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • 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

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention provides a kind of processing system of Biohazard Waste and its using technique, successively including pretreatment unit, carbonizing plant, waste gas cracker and exhaust gas processing device;Pretreatment unit is connected by helix transporting device with the feed cap of carbonizing plant;Carbonizing plant includes rotating furnace body and shell, rotating furnace body is in shell, and closed cavity is formed between shell and rotating furnace body, shell is provided with the heating equipment heated to rotating furnace body, and rotating furnace body both ends are connected with discharging lid and feed cap by rotatory sealing;It is connected between one end of waste gas cracker and the discharging lid of rotating furnace body by breather pipe, the other end of waste gas cracker is connected by escape pipe with exhaust gas processing device.The present invention completely solves conventional incineration stove atmosphere pollution such as caused pollution source such as dioxin during Biohazard Waste is handled, so as to realize more preferable fuel service efficiency and environmental protection efficiency.

Description

A kind of processing system of Biohazard Waste and its use technique
Technical field
The invention belongs to Waste Disposal Technology field, a kind of processing system more particularly, to Biohazard Waste and its make Use technique.
Background technology
Hospital produces substantial amounts of different types of discarded object, in addition, health care discarded object can also be by other as urgent Medical treatment and nursing service, blood transfusion or the sources such as center, laboratory, zooscopy, blood bank of dialysing produce.Caused by most of discarded object It is no risk, it is the same that the discarded object of general health care is also similar to household waste.It is essentially from health care Caused when the administration of mechanism and management and maintenance maintenance, remaining health care discarded object is considered as dangerous, may be used also It can produce various communicable health problem.Dangerous Biohazard Waste is typically to carry out burning disposal.
Temperature of the discarded object when incinerator is burned is at a relatively high, if medical refuse incinerator is not by complicated first It will discharge substantial amounts of various poisonous, harmful pollutants during the tail gas treatment device processing entered, including dioxin and furans, again Metal (such as lead, mercury and cadmium), pellet, sour gas (hydrogen chloride, sulfur dioxide), carbon monoxide and nitrogen oxides (composition of haze) etc..These emissions bring serious adverse consequences to the safety of operator, publilc health and environment.Institute Have to just be disposed off before atmosphere is released to this gas, therefore may result in the volume of incinerator operating cost Outer increase.
Incinerator also can always suffer from unnecessary thermal effect loss.All discarded objects are destroyed in order to reach a high temperature Purpose, incinerator, which will typically consume more multiple fuel, can just be burned to higher temperature.Dangerous medical waste is due to its own Infectiousness, general correct way is to reduce artificial operating of contacts as far as possible.So packs of medical wastes will be by It is sent directly into incinerator to burn, but the difference for causing heat demand has been carried out into quilt because the volume of every bag waste material is different from density Burn.The final result of such a situation is increase fuel cost to provide higher temperature to achieve the goal.
There is landfill communicable Biohazard Waste to considerably increase human health and the risk of environmental pollution.It is once discarded Thing is agitated or covered in any way inappropriate, it will further risk occurs.Therefore land-fill method is not one The Biohazard Waste processing mode planted, is not also allowed by thumping majority government.Such as want to take precautions against these risks, while work as and fill out When to bury field be also unique available selection, then effective method is exactly just to destroy or remove medical waste in original place After the infectiousness of thing, just it is transferred to landfill yard and disposes.
The content of the invention
In view of this, the present invention is directed to propose the processing system of a kind of Biohazard Waste and its using technique, can accomplish compared with Handled under low temperature conditionss in the minimum operating process of harm is reached, completely solve conventional incineration stove and cured in processing The atmosphere pollution such as caused pollution source such as dioxin during treatment discarded object, so as to realize that more preferable fuel uses effect Rate and environmental protection efficiency.
To reach above-mentioned purpose, the technical proposal of the invention is realized in this way:
A kind of processing system of Biohazard Waste, successively including pretreatment unit, carbonizing plant, waste gas cracker and Exhaust gas processing device;
The pretreatment unit is connected by helix transporting device with the feed cap of carbonizing plant;
The carbonizing plant includes rotating furnace body and shell, rotating furnace body in shell, and shell and rotating furnace body it Between form the cavity of closed hot gas water conservancy diversion, shell is provided with the heating equipment heated to rotating furnace body, rotating furnace body both ends Discharging lid and feed cap are connected with by rotatory sealing;
It is connected between one end of the waste gas cracker and the discharging lid of rotating furnace body by breather pipe, waste gas cracking dress The other end put is connected by escape pipe with exhaust gas processing device.
Further, the rotating furnace body is cylindrical cavity and shell is stretched out at both ends, and rotating furnace body passes through end quilt Motor is driven and rotated, and the discharging lid and feed cap of the rotating furnace body are fixedly installed on support, the discharging lid Be provided with exhaust vent, on feed cap respectively by inert gas air inlet and discarded object charging aperture and inertial gas tank, Helix transporting device connects, and is provided with temperature controller and pressure controller in the rotating furnace body, is provided with the rotating furnace body Flow deflector.Biohazard Waste after crushing is after the discarded object charging aperture on feed cap enters rotating furnace body, in flow deflector Lower rotate of effect is moved while going discharging lid direction, is carbonized in moving process, useless after the completion of carbonization post processing Material will be excluded by the sealed drawing mechanism located at rotating furnace body tail end.This sealed drawing mechanism is in order to avoid outside Air (oxygen) enters in reactor.What inert gas air inlet entered is the inert gas of non-combustion characteristics, and persistently leads to Enter, avoid the extraneous air containing oxygen from entering rotating furnace body.The carbonization of Biohazard Waste is in anaerobic or non-in rotating furnace body Carbonization in the environment of normal low oxygen content, and using the mode of indirectly heat, it is right using setting heating equipment on shell The air in closed cavity between shell and rotating furnace body carries out heating so as to be heated to rotating furnace body.
It is fixedly connected, i.e., is rotated with the rotation of rotating furnace body between shell and rotating furnace body;Or shell is fixed on It is motionless on support, and rotating furnace body rotates under motor drive, is connected between shell and rotating furnace body using rotatory sealing.Outside Shell can be various shapes.
Further, the shell is respectively equipped with housing inlet and shell gas outlet in not ipsilateral, in the cavity And temperature controller is equipped with housing inlet, it is provided with air blower at the shell gas outlet, the heat supply on the shell Equipment is any of arc-plasma, infrared heating, conductive heater silk or fuel-fired furnace.
Further, the pretreatment unit includes lift and pulverizer with lifting platform, matches somebody with somebody on the lifting platform For platform scale, capping bucket of the bottom with roller is fixed on lifting platform, and pulverizer drives capping bucket to carry out by lift Material, the lower end discharge outlet of pulverizer are connected with helix transporting device, revolved in the other end and carbonizing plant of helix transporting device The feed cap of rotary furnace body is fixedly connected.
Further, the waste gas cracker includes the interlayer outside combustion chamber and combustion chamber, and the interlayer is provided with the One air inlet and the first air outlet, one end of the combustion chamber be provided with waste gas inlet, the second air inlet and Burner, the other end are provided with waste gas gas outlet and cooling gas air inlet, first air outlet and the second air inlet Mouth is connected by pipeline, and interlayer is provided with temperature controller and pressure controller, and the waste gas gas outlet passes through escape pipe and tail The tail gas air inlet of Flash Gas Compression Skid System is connected.
The waste gas that waste gas cracker obtains after being carbonized by the method directly burnt in carbonizing plant carries out thermal cracking. Because the temperature in combustion chamber is very high, if the air or oxygen for playing combustion-supporting effect is directly entered in combustion chamber, due to extraneous temperature Spend relatively low, very big influence can be caused to the temperature in combustion chamber, therefore the first air that combustion-supporting gas is first passed through on interlayer enters Gas port enters interlayer, and the temperature in interlayer derives from combustion chamber, after combustion-supporting gas is preheated in interlayer, from the first air Then gas outlet discharge is entered in combustion chamber through piping by the second air inlet.Due to waste gas inlet, the second air Air inlet and burner are respectively positioned on same one end of combustion chamber, and the waste gas in rotating furnace body is firing after entering from waste gas inlet Lighted at burner, the burning of sufficiently high temperature can effectively reduce in whole carbonisation caused all volatile compounds and Noxious material gas.
Further, absorbent solution is filled inside the exhaust gas processing device, top is provided with spraying mechanism, tail gas air inlet With tail gas gas outlet, the tail gas air inlet is located at below spraying mechanism, and tail gas gas outlet is located above spraying mechanism.
Exhaust gas processing device includes cooler and absorption plant, and the absorption plant includes venturi tower and scrubbing tower, institute The lower end for stating venturi tower and scrubbing tower communicates, and cooler cools to the solution in absorption plant, venturi tower and washing The upper end of tower is equipped with spraying mechanism, respectively the first jet head sets and the second jet head sets, and the first jet head sets and the second jet head sets are equal Connected by circulating pump and pipeline with the absorbent solution of absorption plant bottom, be tail gas gas import below the first jet head sets, institute State tail gas air inlet with waste gas gas outlet by exhaust pipe to be connected, the upper end in scrubbing tower positioned at the second jet head sets is provided with tail Gas gas outlet.
The upper end of scrubbing tower, which is located above the second jet head sets, is provided with the 3rd jet head sets, and running water is conveyed water by pipeline To the first jet head sets and the 3rd jet head sets.Exhaust gas processing device also includes grug feeding jar, and the grug feeding jar is passed through by drug feeding pipeline Scrubbing tower, drug feeding pipeline are provided with dosing pump, and the dosing pump is controlled by pH value sensor and conductivity sensor, the pH value Sensor and conductivity sensor are located on the pipeline for the circulating pump being connected with the second jet head sets.
Present invention also offers a kind of technique of the processing system using Biohazard Waste as described above:
Inside is fixed on lifting platform equipped with the capping bucket of Biohazard Waste and bottom with roller, and lift, which drives, to be risen Feeding of the platform completion to pulverizer drops, and Biohazard Waste is delivered to the rotation of carbonizing plant after rubbing by helix transporting device In rotary furnace body;
It is continually fed into the inert gas of non-burning characteristic in rotating furnace body by inert gas air inlet, the heat supply on shell Equipment heats to rotating furnace body, when the carburizing temperature for reaching Biohazard Waste, the Biohazard Waste i.e. carbon in rotating furnace body Change, during caused waste gas by exhaust vent enter waste gas cracker combustion chamber in, by burner when, give up Gas is converted into free of contamination waste gas by thoroughly thermal cracking, enters exhaust gas processing device from waste gas gas outlet, is filled in vent gas treatment The tail gas after the cyclic absorption final purification of alkaline solution is put, is arranged with the temperature less than 100 DEG C by tail gas gas outlet Go out.
Further, the inert gas for the non-burning characteristic being passed through in the rotating furnace body is nitrogen, and the flow of nitrogen is 0.01m3/ min to 50m3/min。
Further, the rotating speed of the rotating furnace body is 0.05~5rpm, and rotating furnace body internal temperature is 150~650 DEG C, Time of the Biohazard Waste in rotating furnace body is 0.5~6h.
Further, the temperature in the combustion chamber is 600~1200 DEG C, and the time in combustion chamber is more than or equal to 0.7s。
Relative to prior art, the processing system of Biohazard Waste of the present invention and its had using technique following excellent Gesture:
The processing system of Biohazard Waste of the present invention and its using technique, it is useless to handle medical treatment using carbonization technique Gurry, Biohazard Waste by pretreatment, carbonization, thermal cracking and vent gas treatment these closely and continuity link is matched somebody with somebody Close, realize nontoxic, the environmentally friendly, safety operation in processing procedure;Carbonizing plant is the ring in the inert gas of non-burning characteristic It is carbonized under border, compared to traditional incinerator, this technique will not produce dioxin and other environmentally harmful chemical combination Thing so that solid Biohazard Waste carbonization avoids the formation of pollution source into pollution-free residue, more environmentally-friendly.
Brief description of the drawings
The accompanying drawing for forming the part of the present invention is used for providing a further understanding of the present invention, schematic reality of the invention Apply example and its illustrate to be used to explain the present invention, do not form inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is the structural representation of the processing system of the Biohazard Waste described in the embodiment of the present invention.
Description of reference numerals:
1- lifts;2- pulverizers;3- covers bucket;4- helix transporting devices;5- rotating furnace bodies;6- shells;601- shells Air inlet;602- shells gas outlet;7- feed caps;8- discharging lids;9- inert gas air inlets;10- discarded object charging apertures;11- Inertial gas tank;12- exhaust vents;13- combustion chambers;1301- waste gas inlets;The air inlets of 1302- second; 1303- waste gas gas outlet;1304- cooling gas air inlets;14- interlayers;The air inlets of 1401- first;The air of 1402- first Gas outlet;15- burners;16- tail gas air inlets;17- tail gas gas outlet;18- venturi towers;19- scrubbing towers;20- first sprays Head group;The jet head sets of 21- second;The jet head sets of 22- the 3rd;23- coolers;24- grug feeding jars.
Embodiment
It should be noted that in the case where not conflicting, the feature in embodiment and embodiment in the present invention can phase Mutually combination.
In the description of the invention, it is to be understood that term " " center ", " longitudinal direction ", " transverse direction ", " on ", " under ", The orientation or position relationship of the instruction such as "front", "rear", "left", "right", " vertical ", " level ", " top ", " bottom ", " interior ", " outer " are Based on orientation shown in the drawings or position relationship, it is for only for ease of the description present invention and simplifies description, rather than instruction or dark Show that the device of meaning or element there must be specific orientation, with specific azimuth configuration and operation, thus it is it is not intended that right The limitation of the present invention.In addition, term " first ", " second " etc. are only used for describing purpose, and it is not intended that instruction or hint phase To importance or the implicit quantity for indicating indicated technical characteristic.Thus, the feature for defining " first ", " second " etc. can To express or implicitly include one or more this feature.In the description of the invention, unless otherwise indicated, " multiple " It is meant that two or more.
In the description of the invention, it is necessary to illustrate, unless otherwise clearly defined and limited, term " installation ", " phase Even ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected, or be integrally connected;Can To be mechanical connection or electrical connection;Can be joined directly together, can also be indirectly connected by intermediary, Ke Yishi The connection of two element internals.For the ordinary skill in the art, above-mentioned term can be understood by concrete condition Concrete meaning in the present invention.
Describe the present invention in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
A kind of processing system of Biohazard Waste, successively including pretreatment unit, carbonizing plant, waste gas cracker and Exhaust gas processing device;
The pretreatment unit is connected by helix transporting device 4 with the feed cap 7 of carbonizing plant;
The carbonizing plant includes rotating furnace body 5 and shell 6, and rotating furnace body 5 is in shell 6, and shell 6 and revolving burner The cavity of closed hot gas water conservancy diversion is formed between body 5, shell 6 is provided with the heating equipment heated to rotating furnace body 5, revolving burner The both ends of body 5 are connected with discharging lid 8 and feed cap 7 by rotatory sealing;
It is connected between one end of the waste gas cracker and the discharging lid 8 of rotating furnace body 5 by breather pipe, waste gas cracking The other end of device is connected by escape pipe with exhaust gas processing device.
Above-mentioned rotating furnace body 5 is cylindrical cavity and shell 6 is stretched out at both ends, and rotating furnace body 5 is by end by motor Drive is rotated, and the discharging lid 8 and feed cap 7 of the rotating furnace body 5 are fixedly installed on support, on the discharging lid 8 Provided with exhaust vent 12, stored up respectively by inert gas air inlet 9 and discarded object charging aperture 10 with inert gas on feed cap 7 Tank 11, helix transporting device 4 are connected, and temperature controller and pressure controller, the rotating furnace body are provided with the rotating furnace body 5 Flow deflector is provided with 5.
Above-mentioned shell 6 is respectively equipped with housing inlet 601 and shell gas outlet 602 in not ipsilateral, in the cavity with And temperature controller is equipped with housing inlet 601, air blower is provided with the shell gas outlet 602, on the shell 6 Heating equipment is any of arc-plasma, infrared heating, conductive heater silk or fuel-fired furnace.
Above-mentioned pretreatment unit includes lift 1 and pulverizer 2 with lifting platform, and pound is equipped with the lifting platform Scale, capping bucket 3 of the bottom with roller are fixed on lifting platform, and pulverizer 2 drives capping bucket 3 to carry out feeding by lift 1, The lower end discharge outlet of pulverizer 2 is connected with helix transporting device 4, is revolved in the other end and carbonizing plant of helix transporting device 4 The feed cap 7 of rotary furnace body is fixedly connected.
Above-mentioned waste gas cracker includes the interlayer 14 outside combustion chamber 13 and combustion chamber, and it is empty that the interlayer 14 is provided with first The air outlet 1402 of gas air inlet 1401 and first, one end of the combustion chamber 13 are provided with the sky of waste gas inlet 1301, second Gas air inlet 1302 and burner 15, the other end are provided with waste gas gas outlet 1303 and cooling gas air inlet 1304, and described first Air outlet 1402 is connected with the second air inlet 1302 by pipeline, and interlayer 14 is provided with temperature controller and pressure control Device processed, the waste gas gas outlet 1303 are connected by escape pipe with the tail gas air inlet 16 of exhaust gas processing device.
Absorbent solution is filled inside above-mentioned exhaust gas processing device, top is provided with spraying mechanism, tail gas air inlet 16 and tail gas Gas outlet 17, the tail gas air inlet 16 are located at below spraying mechanism, and tail gas gas outlet 17 is located above spraying mechanism.
The use technique of the processing system of Biohazard Waste:
Pretreatment:
Inside is fixed on lifting platform equipped with the capping bucket 3 of Biohazard Waste and bottom with roller, is matched somebody with somebody on lifting platform Standby platform scale, can claim Biohazard Waste weight.Lift 1 will cover the feed hopper that the deduction of bucket 3 is subsequently poured into pulverizer 2 In, double blade type devices equipped with extraordinary arrangement in pulverizer 2, Biohazard Waste will be twisted into the broken of 5mm~150mm sizes Piece, the feed hopper of pulverizer 2 are provided with isolation shield, prevent pathogenic Biohazard Waste from being spilt when rubbing process and carrying out so as to pollute To surrounding environment.Biohazard Waste after rubbing will be transferred in the rotating furnace body 5 of carbonizing plant by helix transporting device 4. Helix transporting device 4 is fixedly connected with the feed cap 7 of rotating furnace body in carbonizing plant 5, and discarded object charging is provided with feed cap 7 Mouth 10.
Carbonization:
After Biohazard Waste after crushing enters rotating furnace body 5, rotated in the presence of flow deflector while going out Expect the movement of the direction of lid 8, be carbonized in moving process, carbonisation is set by the way of indirectly heat on shell 6 Heating equipment, heating equipment heat for the air between rotating furnace body 5 and shell 6 in closed cavity, and then heat passes It is directed in rotating furnace body 5, the temperature inside rotating furnace body 5 is 150 DEG C~650 DEG C;Nitrogen is connected with rotating furnace body 5, nitrogen Flow is 0.01m3/ min~50m3/ min, 0.5~6h of carbonization time, Biohazard Waste are carbonized in nitrogen environment.Shell When being passed through air by housing inlet 601 in 6, shell gas outlet 602 is to close, and air constantly enters shell 6 and rotation In the cavity that rotary furnace body 5 is formed, with being constantly passed through and the continuous rising of empty cavity temperature, heat reach revolving burner for air In body 5, when the temperature controller at housing inlet 601 detects that the temperature in cavity reaches requirement, housing inlet 601 Stopping is passed through air.Because empty cavity temperature raises, pressure becomes big, therefore relief valve is provided with shell gas outlet 602, is pressing Power can carry out pressure release when larger.
The final remaining solid matter of carbonation stage is:The stable carbon dust of property and original or itself can not be carbonized Object, such as glassy metal;Gaseous matter is:Vapor and contaminative waste gas.The stable carbon dust of property and it is original or The object that itself can not be carbonized will be excluded by the sealed drawing mechanism located at the discharge end of rotating furnace body 5.Waste gas is then by setting Entered in the exhaust vent 12 set on discharging lid 8 and thermal cracking is carried out in waste gas cracker.
Waste gas cracks:
Waste gas cracker includes the interlayer 14 for carrying out the combustion chamber 13 of waste gas cracking and being preheated to combustion-supporting gas, Enter combustion chamber 13 after combustion-supporting gas preheating, waste gas enters combustion chamber 13, and burner 15 is lighted to it, and temperature can reach 600 DEG C~1200 DEG C, the residence time is no less than 0.7s, all basic, normal, high in carbonizing plant in the environment of such high temperature The gases that thermophase discharges, it can all switch to carbon dioxide, acid compound gas, water and ashes.
One end of combustion chamber 13 is provided with cooling gas air inlet 1304, when the temperature in combustion chamber 13 is too high, is passed through cold But gas cools for combustion chamber 13.
Vent gas treatment:
Tail gas initially enters venturi tower 18, and the position that venturi tower 18 is located above tail gas air inlet 16 is provided with first Jet head sets 20 carry out spray-absorption to the tail gas of entrance, and then tail gas enters scrubbing tower 19, by the second spray in scrubbing tower 19 The spray of head group 21 and the 3rd jet head sets 22 is further absorbed for tail gas, and the cooled device 23 of absorbing liquid cools down, can Increase the assimilation effect of tail gas.
Exhaust gas processing device is also provided with grug feeding jar 24, and grug feeding jar 24 is passed through scrubbing tower 19, chemical feed pipe by drug feeding pipeline Road is provided with dosing pump, and dosing pump is controlled by pH value sensor and conductivity sensor, pH value sensor and conductivity sensor On the pipeline for the circulating pump being connected with the second jet head sets 21.
Tail gas after absorption is discharged from tail gas gas outlet 17.The tail gas main component finally discharged be carbon dioxide, Vapor and the residual substance for being substantially lower than Environmental Protection Agency's defined discharge standard, such as SO2
Above-mentioned technique can use batch processing or continuous processing.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all essences in the present invention God any modification, equivalent substitution and improvements made etc., should be included in the scope of the protection with principle.

Claims (8)

  1. A kind of 1. processing system of Biohazard Waste, it is characterised in that:Include pretreatment unit, carbonizing plant, waste gas successively to split Solve device and exhaust gas processing device;
    The pretreatment unit is connected by helix transporting device (4) with the feed cap (7) of carbonizing plant;
    The carbonizing plant includes rotating furnace body (5) and shell (6), rotating furnace body (5) in shell (6), and shell (6) with The cavity of closed hot gas water conservancy diversion is formed between rotating furnace body (5), shell (6) is provided with the confession heated to rotating furnace body (5) Hot equipment, rotating furnace body (5) both ends are connected with discharging lid (8) and feed cap (7) by rotatory sealing;
    The shell (6) is respectively equipped with housing inlet (601) and shell gas outlet (602) in not ipsilateral, in the cavity And housing inlet (601) place is equipped with temperature controller, shell gas outlet (602) place is provided with air blower, described outer Heating equipment on shell (6) is any of arc-plasma, infrared heating, conductive heater silk or fuel-fired furnace;
    The rotating furnace body (5) is cylindrical cavity and shell (6) is stretched out at both ends, and rotating furnace body (5) is electronic by end Machine drive rotated, the discharging lid (8) and feed cap (7) of the rotating furnace body (5) are fixedly installed on support, it is described go out Material lid (8) is provided with exhaust vent (12), is fed respectively by inert gas air inlet (9) and discarded object on feed cap (7) Mouth (10) is connected with inertial gas tank (11), helix transporting device (4), and temperature controller is provided with the rotating furnace body (5) And pressure controller, the rotating furnace body (5) is interior to be provided with flow deflector;
    It is connected between one end of the waste gas cracker and the discharging lid (8) of rotating furnace body (5) by breather pipe, waste gas cracking The other end of device is connected by escape pipe with exhaust gas processing device.
  2. 2. the processing system of Biohazard Waste according to claim 1, it is characterised in that:The pretreatment unit includes band There are the lift (1) and pulverizer (2) of lifting platform, platform scale is equipped with the lifting platform, bottom carries the capping bucket (3) of roller It is fixed on lifting platform, pulverizer (2) drives capping bucket (3) to carry out feeding by lift (1), and pulverizer is brought out under (2) It is connected at material mouth with helix transporting device (4), the charging of rotating furnace body in the other end and carbonizing plant of helix transporting device (4) Lid (7) is fixedly connected.
  3. 3. the processing system of Biohazard Waste according to claim 1, it is characterised in that:The waste gas cracker includes Interlayer (14) outside combustion chamber (13) and combustion chamber, the interlayer (14) are provided with the first air inlet (1401) and the first sky Gas gas outlet (1402), one end of the combustion chamber (13) are provided with waste gas inlet (1301), the second air inlet (1302) With burner (15), the other end is provided with waste gas gas outlet (1303) and cooling gas air inlet (1304), and first air goes out Gas port (1402) is connected with the second air inlet (1302) by pipeline, and interlayer (14) is provided with temperature controller and pressure control Device processed, the waste gas gas outlet (1303) are connected by escape pipe with the tail gas air inlet (16) of exhaust gas processing device.
  4. 4. the processing system of Biohazard Waste according to claim 3, it is characterised in that:Inside the exhaust gas processing device Fill absorbent solution, top is provided with spraying mechanism, tail gas air inlet (16) and tail gas gas outlet (17), the tail gas air inlet (16) below spraying mechanism, tail gas gas outlet (17) are located above spraying mechanism.
  5. 5. a kind of technique of the processing system of Biohazard Waste using as described in any one of Claims 1 to 4, its feature exist In:
    Inside is fixed on lifting platform equipped with the capping bucket (3) of Biohazard Waste and bottom with roller, and lift (1) drives Lifting platform completes the feeding to pulverizer (2), and Biohazard Waste is delivered to carbonization after rubbing by helix transporting device (4) In the rotating furnace body (5) of device;
    The inert gas of non-burning characteristic is continually fed into rotating furnace body (5) by inert gas air inlet (9), on shell (6) Heating equipment rotating furnace body (5) is heated, when the carburizing temperature for reaching Biohazard Waste, Biohazard Waste is rotating Be carbonized in body of heater (5), during caused waste gas enter the combustion chamber (13) of waste gas cracker by exhaust vent (12) Interior, when by burner, waste gas is converted into free of contamination waste gas by thoroughly thermal cracking, enters from waste gas gas outlet (1303) Exhaust gas processing device, the cyclic absorption in exhaust gas processing device Jing Guo absorbent solution are arranged eventually through tail gas gas outlet (17) Go out.
  6. 6. technique according to claim 5, it is characterised in that:The non-burning characteristic being passed through in the rotating furnace body (5) Inert gas is nitrogen, and the flow of nitrogen is 0.01m3/ min to 50m3/min。
  7. 7. technique according to claim 5, it is characterised in that:The rotating speed of the rotating furnace body (5) is 0.05-5rpm, rotation Rotary furnace body (5) internal temperature is 150~650 DEG C, and time of the Biohazard Waste in rotating furnace body (5) is 0.5~6h.
  8. 8. technique according to claim 5, it is characterised in that:Temperature in the combustion chamber (13) is 600~1200 DEG C, And the time in combustion chamber (13) is more than or equal to 0.7s.
CN201710288028.3A 2017-04-27 2017-04-27 A kind of processing system of Biohazard Waste and its use technique Active CN106949477B (en)

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