CN203498235U - Sludge magnetized pyrolysis treatment device and sludge treatment method - Google Patents
Sludge magnetized pyrolysis treatment device and sludge treatment method Download PDFInfo
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- CN203498235U CN203498235U CN201190000786.7U CN201190000786U CN203498235U CN 203498235 U CN203498235 U CN 203498235U CN 201190000786 U CN201190000786 U CN 201190000786U CN 203498235 U CN203498235 U CN 203498235U
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- inner barrel
- mud
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- disposal plant
- sludge
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- 238000000197 pyrolysis Methods 0.000 title claims abstract description 34
- 239000010802 sludge Substances 0.000 title abstract description 22
- 238000000034 method Methods 0.000 title abstract description 13
- 238000010438 heat treatment Methods 0.000 claims abstract description 5
- 230000005415 magnetization Effects 0.000 claims description 24
- 238000002485 combustion reaction Methods 0.000 claims description 17
- 239000002184 metal Substances 0.000 claims description 11
- 239000000919 ceramic Substances 0.000 claims description 8
- 238000007789 sealing Methods 0.000 claims description 8
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 7
- 238000007599 discharging Methods 0.000 abstract description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 abstract description 4
- 239000001301 oxygen Substances 0.000 abstract description 4
- 239000000779 smoke Substances 0.000 abstract description 2
- 150000002013 dioxins Chemical class 0.000 abstract 1
- 238000010336 energy treatment Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 238000000746 purification Methods 0.000 abstract 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 12
- 239000000463 material Substances 0.000 description 8
- 229910052799 carbon Inorganic materials 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 5
- 238000001035 drying Methods 0.000 description 4
- 238000003672 processing method Methods 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000000750 progressive effect Effects 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000037237 body shape Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- -1 oxonium ion Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/20—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having rotating or oscillating drums
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/10—Treatment of sludge; Devices therefor by pyrolysis
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
- F23G5/0276—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
-
- 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
- F23G7/001—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for sludges or waste products from water treatment installations
-
- 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
- F23L2900/00001—Treating oxidant before combustion, e.g. by adding a catalyst
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/40—Valorisation of by-products of wastewater, sewage or sludge processing
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Gasification And Melting Of Waste (AREA)
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a sludge magnetized pyrolysis treatment device. The sludge magnetized pyrolysis treatment device comprises a rotating cylinder (1) and a seat body (2) for supporting the rotating cylinder to rotate, wherein the rotating cylinder (1) comprises an outer cylinder body (3) and an inner cylinder body (4) arranged in the outer cylinder body, a burning machine (6) is arranged on the side of a discharging port (5) of the inner cylinder body to heat the inner cylinder body, an air supply device (7) is also arranged on the side of the discharging port (5) to supply air for the inner cylinder body (4) and control the oxygen supply quantity, and an air magnetizing device (8) is arranged on the air supply device (7). Meanwhile, the utility model also provides a sludge magnetized pyrolysis treatment method. As the air magnetizing device and the burning machine are adopted for heating, the smoke gas quantity is reduced. Moreover, the production quantity of dioxins is greatly reduced, the difficulty of tail gas purification is reduced, and the thermal sludge treatment speed is increased so as to reduce the energy consumption and treatment cost.
Description
Technical field:
The present invention relates to a kind of method that mud magnetization pyrolysis processing disposal plant and sludge treatment are disposed.
Background technology:
The mud that municipal wastewater factory produces and some industrial sludge, the following several method of basic employing is processed and is disposed at present: landfill method, high temperature incineration method.Landfill method because land resources day by day in short supply, there is the problems such as secondary pollution hidden danger, be considered to the filtering technique of sludge treatment; High temperature incineration method is because energy consumption is high, running cost is high, invest that large, dioxin growing amount is large, qualified discharge is difficult and be difficult to apply.
Summary of the invention:
The object of the present invention is to provide a kind of mud magnetization pyrolysis processing disposal plant, this mud magnetization pyrolysis processing disposal plant is not only simple in structure, reasonable in design, and is conducive to improve pyrolyzing sludge speed, reduces pyrolyzing sludge temperature.
Mud magnetization pyrolysis processing disposal plant of the present invention, comprise rotating cylinder and support the pedestal that rotating cylinder rotates, it is characterized in that: described rotating cylinder comprises outer cylinder body and is located at the inner barrel in outer cylinder body, described inner barrel discharge port side is provided with combustion engine with heating inner barrel, in this discharge port side, be also provided with air supply device with to inner barrel air feed with control oxygen-supplying amount, described air supply device is provided with air magnetizing apparatus.
Above-mentioned air magnetizing apparatus consists of permanent magnet and non-magnetic vent-pipe, and permanent magnet is fixed on vent-pipe both sides, the N utmost point that a side is permanent magnet, and the S utmost point that opposite side is permanent magnet, the magnetic line of force that the permanent magnet that air is placed during by vent-pipe produces magnetizes.
In above-mentioned inner tube wall, be evenly distributed with the Ceramic Balls that can freely rotate in metal sash, described metal sash is welded on inner tube wall.
Above-mentioned combustion engine bocca stretches in the portfire body being arranged in inner barrel discharge port lateral body.
Above-mentioned air supply device is roots blower, but is not limited only to roots blower, on the air intake pipeline section within roots blower leads to rotary barrel, is provided with air magnetizing apparatus.
Above-mentioned inner barrel opening for feed side is connected with shaftless helixseal feeding unit.
In above-mentioned inner barrel charging lateral body, be provided with fire damper.
Above-mentioned inner barrel outer wall is wrapped with thermofin.
Above-mentioned outer cylinder body circumferential sectors is provided with spring aligning device to support fixedly inner barrel, guarantees its running right alignment.
Above-mentioned inner barrel discharge port is connected with star-like sealing dumping device.
Another object of the present invention is to provide a kind of mud magnetization pyrolysis processing method of disposal, and this mud magnetization pyrolysis processing method of disposal is conducive to improve pyrolyzing sludge speed, reduces pyrolyzing sludge temperature.
Mud magnetization pyrolysis processing method of disposal of the present invention, it is characterized in that: before sewage sludge feed, first with combustion engine, rotation rotating cylinder inwall is carried out to preheating, reach 400 degree, then start charging, mud is from the hopper feed of equipment, through shaftless helixseal feeding unit, enter inner barrel, the metal sash that mud is attached Spiral distribution on the inner barrel inwall of Ceramic Balls is constantly along circumference lifting and fall forward, realize mud tumbling motion forward, the drying section moisture of material between opening for feed and fire damper is dried substantially, it between fire damper and portfire, is pyrolysis section, progressive toward discharge port from the space of inner barrel inwall and portfire outer wall at portfire position mud, finally by star-like sealing dumping device, discharged, in cylinder, mud is from drying, and then the organic decomposes of long molecular chain becomes inflammable gas and the carbon of short molecular chain, can loom be decomposed completely by controlling oxygen-supplying amount and heat supplied, carbon burns completely, also can make carbon incomplete combustion, produce activated carbon, even can make organic not exclusively pyrolysis, produce organic mud.
The advantage of apparatus of the present invention and method:
1, apparatus of the present invention are furnished with air magnetizing apparatus by air feed system, thereby have improved pyrolyzing sludge speed, have reduced pyrolyzing sludge temperature, have both reduced dioxin growing amount, have reduced again running cost.
2, adopt shaftless helixseal feeding unit, solved that charging is easily stopped up, charging is discontinuous and the poor problem of stopping property.
3, apparatus of the present invention adopt star-like sealing dumping device, are to consist of ripe in the industry star-like discharging (ash) valve, have solved the poor problem of discontinuous and close property envelope of slagging tap.
4, apparatus of the present invention combustion engine bocca is provided with portfire to rotating cylinder, makes to slag tap not disturbed by air-flow dust, has guaranteed that pyrolysis and combustion section operating mode is stable simultaneously.
5, apparatus of the present invention rotating cylinder metal inner surface is furnished with the Ceramic Balls that has self-cleaning function that can freely rotate in fixed space, can accumulation of heat again can be every magnetic, strengthened magnetization airflow function, stablized operating mode, solved a mud wall built-up difficult problem simultaneously, guaranteed that the mud of water ratio in 25%～85% so large scope can obtain normal processing.
6, apparatus of the present invention thermofin adopts lightweight heat-proof material, greatly reduces weight of equipment, has reduced driving power consumption.
Accompanying drawing explanation:
Fig. 1 is the organigram of apparatus of the present invention;
Fig. 2 is the A-A sectional view of Fig. 1.
Embodiment:
Mud magnetization pyrolysis processing disposal plant of the present invention, comprise rotating cylinder 1 and support the pedestal 2 that rotating cylinder rotates, described rotating cylinder 1 comprises outer cylinder body 3 and is located at the inner barrel 4 in outer cylinder body, described inner barrel 4 discharge port sides 5 are provided with combustion engine 6 with heating inner barrel, in these discharge port 5 sides, be also provided with air supply device 7 with to inner barrel air feed with control oxygen-supplying amount, described air supply device is provided with air magnetizing apparatus 8, air magnetizing apparatus consists of permanent magnet and non-magnetic vent-pipe that (this vent-pipe can be rectangle vent-pipe, circular vent-pipe etc. all can), permanent magnet is fixed on vent-pipe both sides, one side is the N utmost point of permanent magnet, opposite side is the S utmost point of permanent magnet, the magnetic line of force that the permanent magnet that air is placed during by vent-pipe produces magnetizes, owing to having adopted the heating of air magnetizing apparatus and combustion engine, make material magnetization pyrolysis, pyrolysis temperature can be reduced to 400 ℃ (common sludge pyrolysis temperature is more than 600 ℃), exhaust gas volumn reduces more than 25% than high temperature incineration, and greatly reduce dioxin growing amount, reduced tail gas clean-up difficulty, improve sludge disposal speed.Thereby reduction energy consumption, has reduced processing, cost of disposal.Really realized " resource utilization, minimizing, innoxious, stabilization " that sludge treatment is disposed.
In above-mentioned inner tube wall, be evenly distributed with the Ceramic Balls 9 that can freely rotate in metal sash, described metal sash is welded on inner tube wall, apparatus of the present invention rotating cylinder metal inner surface is furnished with the Ceramic Balls that has self-cleaning function that can freely rotate in fixed space, can accumulation of heat again can be every magnetic, strengthened magnetization airflow function, stablized operating mode, solved a mud wall built-up difficult problem simultaneously, guaranteed that the mud of water ratio in 25%～85% so large scope can obtain normal processing.
Above-mentioned combustion engine 6 boccas stretch in portfire 10 bodies that are arranged in inner barrel discharge port lateral body.Owing to being provided with portfire, making to slag tap not disturbed by air-flow dust, has guaranteed that pyrolysis and combustion section operating mode is stable simultaneously.
Above-mentioned air supply device is roots blower (but being not limited to roots blower), and roots blower system is provided with blower fan and air magnetizing apparatus, and magnetization air feed inlet mouth is positioned at rotating cylinder discharge port side upper end.Because pyrolyzing sludge burn to need oxygen debt oxygen supply, it is by roots blower magnetization air feed and control oxygen-supplying amount it is controlled magnetic air air demand and realize by adjusting rotation speed of fan.The air of roots blower air outlet, under the strong magnetic field action of magnetizing assembly, oxygen wherein forms orderly electronegative oxonium ion, in importing cylindrical shell, through magnetization pyrolysis, mud organic substance matter molecule is broken down into gas, water, inorganics, and produces the chain reaction of other molecular breakdown simultaneously.Mud is broken down into after inorganics gradually, the burning segment of cylindrical shell can decrement to the inorganic lime-ash of surplus zero water ratio only.Apparatus of the present invention borrow organic substance molecule anoxic magnetic force decomposition principle (400 ℃) to substitute traditional heat-flash oxidizing fire (600～800 ℃), save oil consumption energy consumption, and because burning mostly occurs under inorganics state, thereby can greatly reduce the quantity discharged of the obnoxious flavoures such as dioxin.
Feed hopper 12 of the present invention is long vertebral body shape, guarantees the smooth and easy continuously of blanking.Opening for feed top also has smoke exhaust pipe, is connected to secondary combustion apparatus.
Above-mentioned inner barrel opening for feed side is connected with shaftless helixseal feeding unit 13, adopts shaftless helixseal feeding unit, has solved that charging is easily stopped up, charging is discontinuous and the poor problem of stopping property.
In above-mentioned inner barrel charging lateral body, be provided with fire damper 14, fire damper is circular steel plate, when material feeding is fallen, before fire damper, can directly not contact with the flame after fire damper.
Above-mentioned inner barrel outer wall is wrapped with thermofin 15, and this thermofin adopts lightweight heat-proof material, greatly reduces weight of equipment, has reduced driving power consumption, is also conducive to guarantee that envrionment temperature is no more than 40 ℃.
Above-mentioned outer cylinder body circumferential sectors is provided with spring aligning device 16 to support fixedly inner barrel, guarantees its running right alignment.
Above-mentioned inner barrel discharge port is connected with star-like sealing dumping device 17, and this star-like sealing dumping device system consists of star-like discharging (ash) valve or star-shaped dust-discharging valve+flange connect of mature technology in the industry, has solved the poor problem of discontinuous and close property envelope of slagging tap.
The gearing driving device 18 that is located at outer cylinder body periphery can make cylindrical shell running maintain high accurancy and precision, stability of rotation.
Mud magnetization pyrolysis processing method of disposal of the present invention, before sewage sludge feed, first with combustion engine, rotation rotating cylinder inwall is carried out to preheating, reach 400 degree, then start charging, mud is from the hopper feed of equipment, through shaftless helixseal feeding unit, enter inner barrel, the metal sash that mud is attached Spiral distribution on the inner barrel inwall of Ceramic Balls is constantly along circumference lifting and fall forward, realize mud tumbling motion forward, the drying section moisture of material between opening for feed and fire damper is dried substantially, it between fire damper and portfire, is pyrolysis section, progressive toward discharge port from the space of inner barrel inwall and portfire outer wall at portfire position mud, finally by star-like sealing dumping device, discharged, in cylinder, mud is from drying, and then the organic decomposes of long molecular chain becomes inflammable gas and the carbon of short molecular chain, can loom be decomposed completely by controlling oxygen-supplying amount and heat supplied, carbon burns completely, also can make carbon incomplete combustion, produce activated carbon, even can make organic not exclusively pyrolysis, produce organic mud.
The present invention is when processing, can make the mud of water ratio 25%～85% process after disposal by this device, by controlling the duty parameters such as air demand, temperature, residence time of material, can produce as required the byproducts such as not moisture and organic inorganic flour sand, fertilizer raw material, activated carbon.
The remarkable advantage of apparatus of the present invention and method:
1, apparatus of the present invention are furnished with air magnetizing apparatus by air feed system, thereby have improved pyrolyzing sludge speed, have reduced pyrolyzing sludge temperature, have both reduced dioxin growing amount, have reduced again running cost.
2, adopt shaftless helixseal feeding unit, solved that charging is easily stopped up, charging is discontinuous and the poor problem of stopping property.
3, apparatus of the present invention adopt star-like sealing dumping device, are to consist of ripe in the industry star-like discharging (ash) valve, have solved the poor problem of discontinuous and close property envelope of slagging tap.
4, apparatus of the present invention combustion engine bocca is provided with portfire to rotating cylinder, makes to slag tap not disturbed by air-flow dust, has guaranteed that pyrolysis and combustion section operating mode is stable simultaneously.
5, apparatus of the present invention rotating cylinder metal inner surface is furnished with the Ceramic Balls that has self-cleaning function that can freely rotate in fixed space, can accumulation of heat again can be every magnetic, strengthened magnetization airflow function, stablized operating mode, solved a mud wall built-up difficult problem simultaneously, guaranteed that the mud of water ratio in 25%～85% so large scope can obtain normal processing.
6, apparatus of the present invention thermofin adopts lightweight heat-proof material, greatly reduces weight of equipment, has reduced driving power consumption.
Claims (9)
1. a mud magnetizes pyrolysis processing disposal plant, comprise rotating cylinder and support the pedestal that rotating cylinder rotates, it is characterized in that: described rotating cylinder comprises outer cylinder body and is located at the inner barrel in outer cylinder body, described inner barrel discharge port side is provided with combustion engine with heating inner barrel, in this discharge port side, be also provided with air supply device with to inner barrel air feed with control oxygen-supplying amount, described air supply device is provided with air magnetizing apparatus, in described inner barrel charging lateral body, is provided with fire damper.
2. mud according to claim 1 magnetizes pyrolysis processing disposal plant, it is characterized in that: described air magnetizing apparatus consists of permanent magnet and non-magnetic vent-pipe, permanent magnet is fixed on vent-pipe both sides, one side is the N utmost point of permanent magnet, opposite side is the S utmost point of permanent magnet, and the magnetic line of force that the permanent magnet that air is placed during by vent-pipe produces magnetizes.
3. mud magnetization pyrolysis processing disposal plant according to claim 1 and 2, is characterized in that: in described inner tube wall, be evenly distributed with the Ceramic Balls that can freely rotate in metal sash, described metal sash is welded on inner tube wall.
4. mud magnetization pyrolysis processing disposal plant according to claim 3, is characterized in that: described combustion engine bocca stretches in the portfire body being arranged in inner barrel discharge port lateral body.
5. mud magnetization pyrolysis processing disposal plant according to claim 4, is characterized in that: described air supply device is roots blower, but is not limited only to roots blower, on the air intake pipeline section within roots blower leads to rotary barrel, is provided with air magnetizing apparatus.
6. mud magnetization pyrolysis processing disposal plant according to claim 5, is characterized in that: described inner barrel opening for feed side is connected with shaftless helixseal feeding unit.
7. mud magnetization pyrolysis processing disposal plant according to claim 6, is characterized in that: inner barrel outer wall is wrapped with thermofin.
8. mud magnetization pyrolysis processing disposal plant according to claim 7, is characterized in that: described outer cylinder body circumferential sectors is provided with spring aligning device to support fixedly inner barrel, guarantees its running right alignment.
9. mud magnetization pyrolysis processing disposal plant according to claim 8, is characterized in that: described inner barrel discharge port is connected with star-like sealing dumping device.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/CN2011/084138 WO2013086742A1 (en) | 2011-12-16 | 2011-12-16 | Sludge magnetization pyrolyzing treatment device and sludge treatment method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203498235U true CN203498235U (en) | 2014-03-26 |
Family
ID=48611839
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201190000786.7U Expired - Lifetime CN203498235U (en) | 2011-12-16 | 2011-12-16 | Sludge magnetized pyrolysis treatment device and sludge treatment method |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN203498235U (en) |
| WO (1) | WO2013086742A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111453967A (en) * | 2020-03-11 | 2020-07-28 | 广州市晶科电器有限公司 | Sludge reduction equipment |
| CN116474726A (en) * | 2023-05-16 | 2023-07-25 | 北京沃太斯环保科技发展有限公司 | Biochar device for repairing heavy metal contaminated soil |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004237278A (en) * | 2002-12-09 | 2004-08-26 | Nippon Steel Corp | Waste melting furnace |
| CN100534649C (en) * | 2005-05-12 | 2009-09-02 | 刘文治 | Cleansed handling domestic garbage |
| CN201195708Y (en) * | 2008-03-11 | 2009-02-18 | 中国石油天然气股份有限公司 | Sludge pyrolysis treatment device |
| JP2011085377A (en) * | 2009-10-16 | 2011-04-28 | Masanobu Matsunaga | Rotary organic matter decomposing apparatus |
| CN201842746U (en) * | 2010-10-22 | 2011-05-25 | 上海图盛投资咨询有限公司 | Magnetic gas pyrolysis device for organic sludge treatment |
-
2011
- 2011-12-16 CN CN201190000786.7U patent/CN203498235U/en not_active Expired - Lifetime
- 2011-12-16 WO PCT/CN2011/084138 patent/WO2013086742A1/en active Application Filing
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111453967A (en) * | 2020-03-11 | 2020-07-28 | 广州市晶科电器有限公司 | Sludge reduction equipment |
| CN116474726A (en) * | 2023-05-16 | 2023-07-25 | 北京沃太斯环保科技发展有限公司 | Biochar device for repairing heavy metal contaminated soil |
| CN116474726B (en) * | 2023-05-16 | 2024-01-02 | 北京沃太斯环保科技发展有限公司 | Biochar device for repairing heavy metal contaminated soil |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2013086742A1 (en) | 2013-06-20 |
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