CN102679372A - Coil pipe structure pyrolysis system - Google Patents
Coil pipe structure pyrolysis system Download PDFInfo
- Publication number
- CN102679372A CN102679372A CN2012102021713A CN201210202171A CN102679372A CN 102679372 A CN102679372 A CN 102679372A CN 2012102021713 A CN2012102021713 A CN 2012102021713A CN 201210202171 A CN201210202171 A CN 201210202171A CN 102679372 A CN102679372 A CN 102679372A
- Authority
- CN
- China
- Prior art keywords
- coil pipe
- pyrolysis
- water tank
- chamber
- interface
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Abstract
The invention discloses a coil pipe structure pyrolysis system, which comprises a welding furnace body and a flue gas purification plant, wherein the welding furnace body internally comprises a combustor, a pyrolysis chamber, a reaction chamber, a fusion chamber and a coil pipe in the combustor; and the flue gas purification plant comprises a water tank, a flue gas fan, a coil pipe, a shock cooling water pump, a spray water pump and a chimney. The coil pipe structure pyrolysis system adopts a pyrolysis technology to process medical wastes, the energy cycle is realized by flammable gas generated by the wastes, so that sources can be effectively saved, and the operation cost is lowered. According to the coil pipe structure pyrolysis system disclosed by the invention, the coil pipe is arranged in the combustor of the furnace body, the temperature of burnt flue air is raised and is maintained for more than 2 seconds, and harmful components, such as dioxin, are completely resolved.
Description
Technical field
The present invention relates to the ambulatory vehicle field of engineering technology, specifically, relate to a kind of automobile-used Biohazard Waste treatment facility, be mainly used in Treatment of Medical ' Waste.
Background technology
Present existing medical wastes treatment technologies mainly contains four big types: sanitary landfill method, sterilization, burning and non-burning method.
The less hospital of domestic scale adopts sanitary landfill method more, and external this method has been eliminated, in addition handlebar in the past the hazardous waste of landfill dig out the case of handling again.
The sterilization method is comparative maturity, but because treatment scale is less, tail gas and lime-ash all will pass through strict the processing and could discharge, and the treatable discarded object kind of institute is limited, uses just gradually and reduces.
China mainly adopts the method for high temperature incineration to Treatment of Medical ' Waste at present.High temperature incineration law technology maturity is high, but the investment of high temperature incineration method is big, and the occupied fund cycle is long, and burning has certain requirement to the calorific value of rubbish, has limited its range of application; Especially possibly produce the “ bioxin in the burning process ", atmosphere is produced secondary pollution, the physical and mental health of serious harm surrounding resident.
Non-burning method diffusion levels is low, and the kind of handling Biohazard Waste is many, and the solid residue of generation is harmless, needs less energy supply, and can be used to produce clean energy resource.But non-burning method technology maturity is not very high, and the corresponding standard standard is imperfection also, uses to receive restriction to a certain degree.
?
Summary of the invention
Technical problem to be solved by this invention is; Overcome the deficiency that exists in the prior art; Adopt the non-incineration technology of pyrolytic gasification to handle Biohazard Waste, provide a kind of simple in structure, can effectively economize on resources; The pyrolysis system of the coil arrangement that operating cost is low is used for the harmless treatment of Biohazard Waste.
Coil arrangement pyrolysis system of the present invention is achieved through following scheme:
Said coil arrangement pyrolysis system is made up of welding body of heater and smoke eliminator, comprises the coil pipe in combustion chamber, pyrolysis chamber, reative cell, melter and the combustion chamber in the welding body of heater; Welding body of heater inner top is provided with the pyrolysis chamber, and the below, pyrolysis chamber is provided with reative cell and combustion chamber, and the body of heater inner bottom part is a melter; Pyrolysis chamber's front end is a charging aperture, and the rear end, pyrolysis chamber communicates with reative cell, and pyrolysis chamber and reative cell integral body are the inverted L shape setting; The reative cell bottom communicates with melter, and the space that pyrolysis chamber, reative cell, melter and sidewall of the furnace body surround is the combustion chamber; Coil pipe is set in the combustion chamber, and said coil pipe head end connects the coil pipe intake interface, and tail end connects the coil pipe interface of giving vent to anger, and the furnace wall is provided with coil pipe intake interface and the coil pipe interface of giving vent to anger; Connect combustion gas reuse interface through pipeline; The combustion chamber stove body sidewall sets gradually burner interface and combustion gas reuse interface;
Said smoke eliminator comprises water tank, flue gas blower fan, coil pipe, chilling water pump, spray water pump and chimney; Water tank is arranged at welding body of heater one side, and water tank inside is divided into independently spray section and quench zone by dividing plate; Gas skirt two ends connect the spray section of combustion chamber and water tank respectively after the pyrolysis, and the flue gas blower fan connects the spray section of spray back combustion gas skirt and water tank respectively, and spray back combustion gas skirt connects the coil pipe intake interface; Decompose back combustion gas skirt two ends and connect the give vent to anger quench zone of interface and water tank of coil pipe respectively; Chimney connects the quench zone of water tank.
Coil pipe act as the high temperature that utilizes the combustion chamber, flue gas is heated up in coil pipe and stops harmful components such as the above ， bioxin of 2S and decompose fully.
The present invention has following beneficial effect:
1, resource.The present invention adopts pyrolytic technique to handle Biohazard Waste, and the combustible gas that utilizes discarded object self to produce is realized energy circulation, can effectively economize on resources, and reduces operating cost.
2, innoxious.The present invention is provided with coil pipe in combustion chamber of furnace body, gas fume after burning heats up in coil pipe and stops harmful components such as the above ， bioxin of 2S and decomposes fully.
Description of drawings
Fig. 1 is a structural representation of the present invention;
Fig. 2 is a fume pipe interface sketch map of the present invention;
Fig. 3 is a coil arrangement sketch map of the present invention;
Fig. 4 is a flue gas purification system structural representation of the present invention.
The specific embodiment
Below in conjunction with accompanying drawing the present invention is further specified.
Coil arrangement pyrolysis system of the present invention is made up of welding body of heater and smoke eliminator, and is as shown in Figure 1, comprises in the welding body of heater, is made up of the coil pipe 7 in combustion chamber 4, pyrolysis chamber 2, reative cell 3, melter 9 and the combustion chamber.
The body of heater top is provided with manhole 1, is used for overhaul of the equipments.The body of heater front portion is provided with burner interface 8, is used for pyrolysis system initial start burner igniting heating, makes the Biohazard Waste pyrolysis.
Like Fig. 1, shown in Figure 2, the combustion chamber is provided with four air pipe interfaces: the interface of combustion gas inlet pipe 6, flue gas go out the interface of pipe 10, the interface of coil pipe flue gas inlet pipe 12 and the interface that the coil pipe flue gas goes out pipe 11.The combustible gas that combustion gas inlet pipe 6 produces pyrolysis of waste reaction back is introduced combustion chamber 4 burnings; Flue gas goes out pipe and flue gases in the combustion chamber 4 are caused body of heater sprays processing outward; Flue gas after coil pipe flue gas inlet pipe 12 will spray is introduced coil pipe 7, and harmful components such as De bioxin are decomposed in coil pipe 7 fully; The coil pipe flue gas goes out interface tube 11 and the flue gases in the coil pipe 7 are caused body of heater carries out chilling outward and handle.
As shown in Figure 3, coil pipe 7 is by steel pipe 13, and steel pipe tube connector 16 is formed.On the side panel pipe flue gas inlet pipe interface 17 is set therein, flue gas is set on the opposite side coil pipe interface tube 15.Coil pipe 7 is positioned at combustion chamber 4, utilizes the high temperature of combustion chamber 4, and the useless flue gas to 850 of heating ℃ makes useless flue gas stop more than the 2S 850 ℃ of high-temperature regions, guarantees that wherein the De bioxin decomposes fully.
As shown in Figure 4, flue gas purification system is made up of chimney 27, flue gas blower fan 28, flue gas skirt 1, water tank 30, coil pipe 7, flue gas skirt 2 31, flue gas skirt 3 32, spray water pump 33 and chilling water pump 34.Water tank 30 is fixed on the floor compartment, and its inside is divided into independently spray section and quench zone by dividing plate.Flue gas skirt 3 32 two ends connect the spray section of combustion chamber 17 and water tank 30 respectively; Flue gas skirt one 29 two ends connect the spray section of combustion chamber inner coil pipe 18 and water tank 30 respectively; Flue gas skirt 2 31 two ends connect the other end of combustion chamber inner coil pipe 18 and the quench zone of water tank 30 respectively.Chimney 27 connects the quench zone of water tank 30.Water tank 30 inner and upper have evenly been arranged 12 gondola water faucets in spray section; Evenly arranged 6 gondola water faucets at quench zone, an aeration head assembly has been set at quench zone.The aeration head assembly mainly is made up of adpting flange, tube connector, threeway and two aeration heads.
The workflow of this pyrolysis system is: Biohazard Waste enters in the pyrolysis chamber 2 from charging aperture 5, and the burner combustion mouth is pushed in the burner interface 8, and the burner igniting provides heat energy to pyrolysis chamber 2, and Biohazard Waste begins pyrolysis.After pyrolysis was accomplished, its part not have fully by the debirs of pyrolysis and pyrolysis the organic matter residue after intact to be pushed into reative cell 3 to carry out secondary response, be discharged from after the residual residue entering melter 9 further pyrolysis processing after the reaction.The gas that produces in the pyrolytic process after guiding mixes the generation combustible gas, gets into combustion chamber 4 burnings and for follow-up pyrolysis heat energy is provided.After system was stable, the combustible gas that the Biohazard Waste pyrolysis produces was enough kept the subsequent medical pyrolysis of waste, closed burner this moment.
Claims (3)
1. a coil arrangement pyrolysis system is characterized in that, said coil arrangement pyrolysis system is made up of welding body of heater and smoke eliminator, comprises the coil pipe in combustion chamber, pyrolysis chamber, reative cell, melter and the combustion chamber in the welding body of heater; Welding body of heater inner top is provided with the pyrolysis chamber, and the below, pyrolysis chamber is provided with reative cell and combustion chamber, and the body of heater inner bottom part is a melter; Pyrolysis chamber's front end is a charging aperture, and the rear end, pyrolysis chamber communicates with reative cell, and pyrolysis chamber and reative cell integral body are the inverted L shape setting; The reative cell bottom communicates with melter, and the space that pyrolysis chamber, reative cell, melter and sidewall of the furnace body surround is the combustion chamber; Coil pipe is set in the combustion chamber, and said coil pipe one side connects the coil pipe intake interface, and opposite side connects the coil pipe interface of giving vent to anger, and the furnace wall is provided with coil pipe intake interface and the coil pipe interface of giving vent to anger; Connect combustion gas reuse interface through pipeline; The combustion chamber stove body sidewall sets gradually burner interface and combustion gas reuse interface;
Said smoke eliminator comprises water tank, flue gas blower fan, coil pipe, chilling water pump, spray water pump and chimney; Water tank is arranged at welding body of heater one side, and water tank inside is divided into independently spray section and quench zone by dividing plate; Gas skirt two ends connect the spray section of combustion chamber and water tank respectively after the pyrolysis, and the flue gas blower fan connects the spray section of spray back combustion gas skirt and water tank respectively, and spray back combustion gas skirt connects the coil pipe intake interface; Decompose back combustion gas skirt two ends and connect the give vent to anger quench zone of interface and water tank of coil pipe respectively; Chimney connects the quench zone of water tank.
2. coil arrangement pyrolysis system according to claim 1 is characterized in that, said spray water pump connects the spray section gondola water faucet of water tank through pipeline; Said chilling water pump connects the quench zone gondola water faucet of water tank through pipeline.
3. coil arrangement pyrolysis system according to claim 1 is characterized in that said quench zone is provided with the aeration head assembly, and the aeration head assembly connects two aeration heads respectively by threeway and tube connector is formed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210202171.3A CN102679372B (en) | 2012-06-19 | 2012-06-19 | Coil pipe structure pyrolysis system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210202171.3A CN102679372B (en) | 2012-06-19 | 2012-06-19 | Coil pipe structure pyrolysis system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102679372A true CN102679372A (en) | 2012-09-19 |
| CN102679372B CN102679372B (en) | 2015-03-11 |
Family
ID=46811692
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210202171.3A Active CN102679372B (en) | 2012-06-19 | 2012-06-19 | Coil pipe structure pyrolysis system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102679372B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106841546A (en) * | 2017-01-13 | 2017-06-13 | 中国人民解放军军事医学科学院卫生装备研究所 | A kind of analysis method for recalling simulation amendment |
| CN108826982A (en) * | 2018-07-18 | 2018-11-16 | 王同浩 | A kind of aluminium alloy clean manufacturing adds silicon mechanism automatically |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10174958A (en) * | 1996-12-17 | 1998-06-30 | Ohashi Seisakusho:Kk | Deodorizing method in garbage treatment apparatus and apparatus therefor |
| CN2632508Y (en) * | 2003-06-06 | 2004-08-11 | 吴桐 | Movable medical refuse incinerator systems on board |
| CN2636094Y (en) * | 2003-05-30 | 2004-08-25 | 徐长忠 | Refuse pyrolysis treatment device |
| CN2655052Y (en) * | 2003-09-26 | 2004-11-10 | 徐国文 | Environmental protection horizontal incinerator for hospital refuse |
| CN201155763Y (en) * | 2007-12-11 | 2008-11-26 | 北京机电院高技术股份有限公司 | Vehicle mounted chemical dangerous articles burning processing unit |
| CN102012032A (en) * | 2010-12-29 | 2011-04-13 | 中国科学院广州能源研究所 | Medical waste complete incineration device |
| CN202868688U (en) * | 2012-06-19 | 2013-04-10 | 中国人民解放军军事医学科学院卫生装备研究所 | Pyrolysis system provided with coil pipe structure |
-
2012
- 2012-06-19 CN CN201210202171.3A patent/CN102679372B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10174958A (en) * | 1996-12-17 | 1998-06-30 | Ohashi Seisakusho:Kk | Deodorizing method in garbage treatment apparatus and apparatus therefor |
| CN2636094Y (en) * | 2003-05-30 | 2004-08-25 | 徐长忠 | Refuse pyrolysis treatment device |
| CN2632508Y (en) * | 2003-06-06 | 2004-08-11 | 吴桐 | Movable medical refuse incinerator systems on board |
| CN2655052Y (en) * | 2003-09-26 | 2004-11-10 | 徐国文 | Environmental protection horizontal incinerator for hospital refuse |
| CN201155763Y (en) * | 2007-12-11 | 2008-11-26 | 北京机电院高技术股份有限公司 | Vehicle mounted chemical dangerous articles burning processing unit |
| CN102012032A (en) * | 2010-12-29 | 2011-04-13 | 中国科学院广州能源研究所 | Medical waste complete incineration device |
| CN202868688U (en) * | 2012-06-19 | 2013-04-10 | 中国人民解放军军事医学科学院卫生装备研究所 | Pyrolysis system provided with coil pipe structure |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106841546A (en) * | 2017-01-13 | 2017-06-13 | 中国人民解放军军事医学科学院卫生装备研究所 | A kind of analysis method for recalling simulation amendment |
| CN108826982A (en) * | 2018-07-18 | 2018-11-16 | 王同浩 | A kind of aluminium alloy clean manufacturing adds silicon mechanism automatically |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102679372B (en) | 2015-03-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105258131A (en) | Environment-friendly efficient waste incinerator | |
| CN103438461B (en) | A kind of integral type pyrolysis restoring system and waste disposal method | |
| CN203718791U (en) | Household garbage incinerator | |
| CN204240362U (en) | Incinerator | |
| CN104373942B (en) | Incinerator | |
| CN102679372B (en) | Coil pipe structure pyrolysis system | |
| CN102679373B (en) | Vehicle-mounted medical waste pyrolyzing furnace | |
| CN202868688U (en) | Pyrolysis system provided with coil pipe structure | |
| CN102454997A (en) | High-thermal-cracking-rate burning processing and secondary pollutant eliminating method of medical wastes | |
| CN204648247U (en) | A kind of portable ill domestic animal pyrolysis charring treating apparatus | |
| CN202868693U (en) | Vehicle-mounted medical waste pyrolyzing furnace | |
| CN103697481A (en) | Pyrolysis-gas-recyclable medical waste pyrolysis treatment device | |
| CN110186055A (en) | A kind of waste incinerator purifying dioxin flue gas | |
| CN104014576B (en) | A kind of multifunctional solid waste treatment equipment and method thereof | |
| CN104896480B (en) | A kind of bilingual processing unit of rubbish | |
| CN101387401A (en) | There-waste heat recoverer | |
| CN204358731U (en) | City low-temperature carbonization burning domestic garbage flue gas innocuity disposal system | |
| CN104930522A (en) | Multi-phase vertical high-temperature suspension-burning harmless incineration boiler | |
| CN205191591U (en) | High -efficient waste incinerator of environmental protection | |
| CN204756951U (en) | Innoxious incineration boiler of heterogeneous vertical high temperature suspension firing | |
| CN100491829C (en) | Garbage treating plant with low energy consumption and treating method thereof | |
| CN101516536B (en) | A deposited industrial waste thermodecomposition apparatus and decomposition method using thereof | |
| CN111503637A (en) | Process and device for pyrolyzing household garbage by low-nitrogen combustion | |
| CN204730210U (en) | The bilingual treating apparatus of a kind of rubbish | |
| CN216431737U (en) | Material guiding structure for waste incineration and tail gas treatment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170103 Address after: 300161 Hedong District, Tianjin, East Road, No. 106 Patentee after: Sanitary Equipment Inst., Academy of Military Medical Sciences PLA Patentee after: BEIJING HUILONG NEW TECHNOLOGY CO., LTD. Address before: 300161 Hedong District, Tianjin, East Road, No. 106 Patentee before: Sanitary Equipment Inst., Academy of Military Medical Sciences PLA |