CN102188934B - High temperature high pressure sterilization hydrolysis curing reaction pot - Google Patents
High temperature high pressure sterilization hydrolysis curing reaction pot Download PDFInfo
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- CN102188934B CN102188934B CN201110094896.0A CN201110094896A CN102188934B CN 102188934 B CN102188934 B CN 102188934B CN 201110094896 A CN201110094896 A CN 201110094896A CN 102188934 B CN102188934 B CN 102188934B
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Abstract
The invention relates to a high temperature high pressure sterilization hydrolysis curing reaction pot, which is used for carrying out spraying, exploding, smashing and hot sorting after organic materials are separated from mixed domestic garbage. The reaction pot comprises a pressure pot body 1, a feeding hole 2, a high pressure valve for the feeding hole 3, a high pressure vale for a discharging hole 4, a spraying and exploding discharging hole 5, a spraying and exploding pressure pipeline for the discharging hole 6, a high temperature and high pressure air inlet valve 7, a high temperature and high pressure air inlet pipeline 8, a support pillar 9, a high temperature and high pressure pipe network distribution center 10, a high temperature and high pressure pipe network outer ring 11, a high temperature and high pressure pipe provided with a hole 12, a material leaking gap 13,a high temperature and high pressure pipe air outlet hole 14 and a pipe network support pillar 15. In the reaction pot provided by the technical scheme of the invention, all the pipes of the high temperature and high pressure gas pipe network in the reaction pot are arranged upwards in the same direction, the tapping angle of each pipe is 60 degrees, the high temperature high pressure gas sprayed in the same direction forms a rotary air flow according to the principle that hot gas is upward, a catalyst and materials in the reaction pot are promoted to be uniformly mixed, the curing reaction on the organic materials is sped up, and the spraying and exploding on the materials are smooth and clean.
Description
Technical field:
The technology of the present invention relates to a kind of reaction pot, is used for the organic hydrolysis control that mixed consumer waste is handled in real time.
Background technology:
Organic substance part during mixed consumer waste is handled, the organic matter maturation process in the high pressure jar of packing into, with high temperature 200 degree, 10 atmospheric saturated steam flowings are transported in the jar, organic waste in sending into jar is hydrolyzed and dewaters, and after the reaction abundance, material enters atmospheric pressure state from the circular discharging opening high pressure conditions in the positive lower end of reaction pot, produces the quick-fried effect of spray and make organic matter play expanded effect, but there is following problem in practice in this facility:
(1) because saturated vapor or high heated drying gas can not evenly be transported to the every nook and cranny fast, so temperature field, pressure field in the pot are uneven; Because catalyst can not evenly mix with material, often also be imperfectly equalized again so react.
(2) when opening the blowdown valve, it is slow that the mid portion flow velocity of outlet leans on pot marginal portion flow velocity soon when outflowing owing to material, the very fast clogging that formed, at this moment because material is sent a pot interior space segment expansion outside, internal pressure reduces, but still is higher than atmospheric pressure far away, so the material that stops up is pressed into the close state of matter, do not flow more, thereby caused the difficulty in the cleaning; And kettle temperature is up to 200 degree, and pot is outer heat-insulation layer, and it is bad to dispel the heat, and generally wants just can carry out the labor cleaning after the couple of days cooling.
The invention technology contents:
1, the characteristics of the technology of the present invention are: a kind of mixed consumer waste autoclave sterilization sterilization hydrolysis slaking reaction pot fast processing equipment that is used for is provided.Described reaction pot can make pot high-pressure hot gas that the female cone pipe network ejects form swirling eddy, and kettle temperature field and pressure field are kept evenly, also can make catalyst and mixing of materials in the pot even; And can not cause material to stop up, thermal diffusivity is good in the pot, and the material cleaning easily.
2, the scheme of the technology of the present invention is: be used for the hydrolysis pot that mixed consumer waste is handled in real time, comprise a pot body, charging aperture, discharging opening, bottom in the described pot body is provided with pipe network type device, this pipe network type device comprises the conical inner body that raises up, with the cylinder pipe that constitutes by gas pipeline, the lower end of described cone pipe network central tube links to each other with the gas pipeline that is positioned at hydrolysis pot outside, described pipe network comprises tubule road and the circular pipe network that is made of some gas pipelines, the blowing angle of every pipe of the High Temperature Gas pipe network in the reaction pot of the technology of the present invention is that 60 degree are arranged to the same direction of upside, make progress principle at the unidirectional high temperature and high pressure gas formation of ejection swirling eddy according to hot gas, impel catalyst and mixing of materials in the pot even, the reaction of organic materials rapid aging, leave the space between the inwall HTHP pipe network outer ring, the bottom of a pan (11), make material behind the hydrolysis flow to discharging opening (4) material to spray quick-fried unimpeded clean along this passage to form passage.Described pipe network type device support column is stainless steel.
3, the technology of the present invention has following advantage:
(1) the technology of the present invention is by being provided with pipe network type device in pot body bottom, cloth is to become the gas pipeline of the netted arrangement of awl on cone, and on gas pipeline, have aperture, arrange at the same direction degree angles, the place ahead 60 that make progress, under the effect of high-pressure hot gas, formed swirling eddy in the pot, thereby solved uneven temperature problem in the reaction pot, the catalyst in the reaction pot can evenly be mixed with material.
(2) the pipe network type device of the technology of the present invention can make the air-flow rotation, and the air-flow of rotation has played mechanical stirring action, so more can make pressure field, temperature field and material field distribution in the reaction pot even.
(3) the taper net of the technology of the present invention comprises the brailer that thin gas pipeline constitutes, and this structure can make the material behind the hydrolysis slide along constant speed along the cone surrounding, no longer has the differential phenomenon, so can not cause material to stop up, does not need to clear up reaction pot again.
(4) the technology of the present invention has a plurality of apertures on awl net and gas pipeline, has guaranteed that the outgoing air-flow can be mapped to each corner of reaction pot.The pore size of the range decision aperture that should reach in reaction pot according to aperture outgoing air-flow has guaranteed that like this jet-stream wind can be mapped to the position that should reach on the reaction pot inwall, produces even temperature field, pressure field and material field thereby form swirling eddy.
(5) the area summation of the online aperture of opening of all awls of the technology of the present invention equals the outside gas pipeline sectional area for the gas transmission of hydrolysis pot, the gas pipeline that had so both guaranteed the awl net bears pressure can be not excessive, guaranteed again not cause pot inner pressure to reduce after air-flow arrives reaction pot.
(6) the technology of the present invention is evenly distributed on all circular net of cone with aperture, and the aperture on each root pipe network also is evenly distributed, the opening angle of aperture is that 60 degree are the rotary irradiating shape from air-flow and the Taper Pipe net that aperture penetrates on the pipe network, further like this even of the interior temperature field of reaction pot, pressure field and material field that guaranteed.
Description of drawings:
Accompanying drawing is the hydrolysis Cooker structure schematic diagram of embodiment.
Number description:
Pressure cooker body (1), charging aperture (2), charging aperture high pressure valve (3), discharging opening high pressure valve (4), spray quick-fried discharging opening (5), discharging opening spray detonation pressure solenoid road (6), HTHP air intake valve (7), HTHP admission line (8), support column (9), HTHP pipe network shunt centre (10), HTHP pipe network outer ring (11), HTHP pipe with holes (12), leak material space (13), HTHP pipe venthole (14), webmaster support column (15);
The specific embodiment:
Embodiment to the technology of the present invention describes below with reference to accompanying drawing.
The advantage of the technology of the present invention is: a kind of hydrolysis oxidation reaction pot that is used for the mixed consumer waste fast processing is provided.Described reaction pot can make pot high-pressure hot gas that the female cone pipe network ejects form swirling eddy, and kettle temperature field and pressure field are kept evenly, also can make catalyst and mixing of materials in the pot even; And can not cause material to stop up, thermal diffusivity is good in the pot, and the material cleaning easily.
The scheme of the technology of the present invention is: be used for the hydrolysis pot that mixed consumer waste is handled in real time, comprise a pot body, charging aperture, discharging opening, the bottom of described pot body is provided with pipe network type device, this pipe network type device comprises the conical inner body of projection on 3, with the cylinder pipe that constitutes by gas pipeline, the lower end of described cone pipe network central tube links to each other with the gas pipeline that is positioned at hydrolysis pot outside, described pipe network comprises tubule road and the circular pipe network that is made of some gas pipelines, the blowing angle of every pipe of the High Temperature Gas pipe network in the reaction pot of the technology of the present invention is that 60 degree are arranged to the same direction of upside, make progress principle at the unidirectional high temperature and high pressure gas formation of ejection swirling eddy according to hot gas, impel catalyst and mixing of materials in the pot even, the reaction of organic materials rapid aging, leave the space between the bottom of a pan inwall and the HTHP pipe network outer ring (11), make material behind the hydrolysis flow to discharging opening (4) material to spray quick-fried unimpeded clean along this passage to form passage.Described pipe network type device support column is stainless steel.
The technology of the present invention has following advantage:
(1) the technology of the present invention is by being provided with pipe network type device in pot body bottom, cloth is to become the gas pipeline of the netted arrangement of awl on cone, and on gas pipeline, have aperture, arrange at the same direction degree angles, the place ahead 60 that make progress, under the effect of high-pressure hot gas, formed swirling eddy in the pot, thereby solved uneven temperature problem in the reaction pot, the catalyst in the reaction pot can evenly be mixed with material.
(2) the pipe network type device of the technology of the present invention can make the air-flow rotation, and the air-flow of rotation has played mechanical stirring action, so more can make pressure field, temperature field and material field distribution in the reaction pot even.
(3) the taper net of the technology of the present invention comprises the brailer that thin gas pipeline constitutes, and this structure can make the material behind the hydrolysis slide along constant speed along the cone surrounding, no longer has the differential phenomenon, so can not cause material to stop up, does not need to clear up reaction pot again.
(4) the technology of the present invention has a plurality of apertures on awl net and gas pipeline, has guaranteed that the outgoing air-flow can be mapped to each corner of reaction pot.The pore size of the range decision aperture that should reach in reaction pot according to aperture outgoing air-flow has guaranteed that like this jet-stream wind can be mapped to the position that should reach on the reaction pot inwall, produces even temperature field, pressure field and material field thereby form swirling eddy.
(5) the area summation of the online aperture of opening of all awls of the technology of the present invention equals the outside gas pipeline sectional area for the gas transmission of hydrolysis pot, the gas pipeline that had so both guaranteed the awl net bears pressure can be not excessive, guaranteed again not cause pot inner pressure to reduce after air-flow arrives reaction pot.
(6) the technology of the present invention aperture is evenly distributed on all circular net of cone, and the aperture on each root pipe network also is evenly distributed, the opening angle of aperture is that 60 degree are the rotary irradiating shape from air-flow and the Taper Pipe net that aperture penetrates on the pipe network, further like this even of the interior temperature field of reaction pot, pressure field and material field that guaranteed.
The content that is not described in detail in the technology of the present invention specification belongs to this area professional and technical personnel's known technology.The technology of the present invention is not limited to the protection content that claim and specific embodiment are addressed, so long as any invention of creating out according to the design of the technology of the present invention all should belong within the protection domain of the technology of the present invention.
Claims (8)
1. autoclave sterilization sterilization hydrolysis slaking reaction pot, after mixed consumer waste sub-elects organic materials, the choosing of the quick-fried pulverizing heat of described autoclave sterilization sterilization hydrolysis slaking reaction pot spray is handled, and comprises pressure cooker body (1), charging aperture (2), charging aperture high pressure valve (3), discharging opening high pressure valve (4), spray quick-fried discharging opening (5), discharging opening spray detonation pressure solenoid road (6), HTHP air intake valve (7), HTHP admission line (8), support column (9), HTHP pipe network shunt centre (10), HTHP pipe network outer ring (11), HTHP pipe with holes (12), leak material space (13), HTHP pipe venthole (14), webmaster support column (15); HTHP pipe network outer ring (11) and every HTHP pipe with holes (12) in this reaction pot, each tube-surface blowing angle is to the same direction perforate of upper side 60 degree; HTHP pipe venthole (14) shape becomes same direction to arrange, form swirling eddy according to the hot gas principle that makes progress ejecting unidirectional high temperature and high pressure gas, impel catalyst and mixing of materials in the pot even, the reaction of organic materials rapid aging, leave Lou material space between the bottom of a pan inwall and the HTHP pipe network outer ring (11), make the material behind the hydrolysis flow to discharging opening high pressure valve (4) along this passage to form passage, material sprays quick-fried unimpeded clean in the reaction pot.
2. reaction pot according to claim 1, it is characterized in that: an end that constitutes three support columns of triangular supports is connected with the middle part of described HTHP admission line (8) respectively, the other end of three support columns (9) is connected with the inwall in the bottom of a pan respectively, and these three support columns (9) are fixed on described HTHP admission line (8) bottom of pressure cooker body (1).
3. reaction pot according to claim 2, it is characterized in that: an end that constitutes three pillars of HTHP pipe network support column (15) is connected with described HTHP pipe network outer ring (11) respectively, the other end of three pillars is connected with the inwall in the bottom of a pan respectively, and these three pillars are fixed on described HTHP pipe network outer ring (11) bottom of pressure cooker body (1).
4. reaction pot according to claim 1 and 2, it is characterized in that: the area summation of the HTHP pipe network outer ring (11) on the HTHP pipe network in the reaction pot, HTHP pipe with holes (12), the aperture of opening equals the sectional area of reaction pot HTHP admission line (8).
5. reaction pot according to claim 1 and 2 is characterized in that: described HTHP pipe venthole (14) is evenly distributed on the HTHP pipe network.
6. reaction pot according to claim 1 and 2 is characterized in that: the high-temperature high-pressure air flow that ejects from described HTHP pipe venthole (14) and the bullet surface of HTHP pipe network are the rotation shape, form swirling eddy like this in reaction pot.
7. reaction pot according to claim 1 and 2 is characterized in that: described HTHP pipe network is a metal material.
8. reaction pot according to claim 7 is characterized in that: described HTHP pipe network is a stainless steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110094896.0A CN102188934B (en) | 2011-04-15 | 2011-04-15 | High temperature high pressure sterilization hydrolysis curing reaction pot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110094896.0A CN102188934B (en) | 2011-04-15 | 2011-04-15 | High temperature high pressure sterilization hydrolysis curing reaction pot |
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| CN102188934A CN102188934A (en) | 2011-09-21 |
| CN102188934B true CN102188934B (en) | 2013-07-24 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201110094896.0A Active CN102188934B (en) | 2011-04-15 | 2011-04-15 | High temperature high pressure sterilization hydrolysis curing reaction pot |
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Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103599732B (en) * | 2013-10-30 | 2015-11-25 | 沈阳迈维科技有限公司 | A kind of X-ray high-temperature high-pressure catalytic reaction stove |
| CN106007814A (en) * | 2016-07-18 | 2016-10-12 | 宋春刚 | Feed and organic fertilizer puffing method and in-tank stirring puffing equipment |
Citations (7)
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| JP2003170145A (en) * | 2001-12-11 | 2003-06-17 | Nippon Denka Koki Kk | Method and system for treating organic waste |
| CN1448211A (en) * | 2002-03-29 | 2003-10-15 | 中国石油化工股份有限公司 | Gas-solid reactor |
| CN2583991Y (en) * | 2002-12-15 | 2003-11-05 | 鲁来斌 | Rotation steam type cymbopogon goeringii puffing apparatus |
| CN101041596A (en) * | 2007-03-01 | 2007-09-26 | 袁少峰 | Hydrolytic decomposition pot and technology thereof |
| CN101081400A (en) * | 2007-07-05 | 2007-12-05 | 浙江大学 | Device for the high-temperature hydrolyzing processing of organic solid waste |
| CN101406895A (en) * | 2008-12-05 | 2009-04-15 | 郑顺潮 | Hydrolytic reaction pot for realtime processing mixed consumer waste |
| CN201632261U (en) * | 2010-04-12 | 2010-11-17 | 杨辉 | Hydrolytic-hydrothermal oxidizing reaction kettle for agriculture and animal husbandry wastes and household refuses |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004250288A (en) * | 2003-02-20 | 2004-09-09 | Katsusuke Kayama | Inflammable waste recycling resource machine (pressurized and magnetized vapor treatment) |
-
2011
- 2011-04-15 CN CN201110094896.0A patent/CN102188934B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003170145A (en) * | 2001-12-11 | 2003-06-17 | Nippon Denka Koki Kk | Method and system for treating organic waste |
| CN1448211A (en) * | 2002-03-29 | 2003-10-15 | 中国石油化工股份有限公司 | Gas-solid reactor |
| CN2583991Y (en) * | 2002-12-15 | 2003-11-05 | 鲁来斌 | Rotation steam type cymbopogon goeringii puffing apparatus |
| CN101041596A (en) * | 2007-03-01 | 2007-09-26 | 袁少峰 | Hydrolytic decomposition pot and technology thereof |
| CN101081400A (en) * | 2007-07-05 | 2007-12-05 | 浙江大学 | Device for the high-temperature hydrolyzing processing of organic solid waste |
| CN101406895A (en) * | 2008-12-05 | 2009-04-15 | 郑顺潮 | Hydrolytic reaction pot for realtime processing mixed consumer waste |
| CN201632261U (en) * | 2010-04-12 | 2010-11-17 | 杨辉 | Hydrolytic-hydrothermal oxidizing reaction kettle for agriculture and animal husbandry wastes and household refuses |
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| CN102188934A (en) | 2011-09-21 |
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