CN1884913A - Wet sludge drying and incinerating treatment method employing circulating fluidized bed with combined dryer - Google Patents
Wet sludge drying and incinerating treatment method employing circulating fluidized bed with combined dryer Download PDFInfo
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- CN1884913A CN1884913A CN 200510077292 CN200510077292A CN1884913A CN 1884913 A CN1884913 A CN 1884913A CN 200510077292 CN200510077292 CN 200510077292 CN 200510077292 A CN200510077292 A CN 200510077292A CN 1884913 A CN1884913 A CN 1884913A
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- combined dryer
- fluidized bed
- heat
- circulating fluidized
- treatment method
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- 238000000034 method Methods 0.000 title claims abstract description 28
- 238000001035 drying Methods 0.000 title claims abstract description 25
- 239000010802 sludge Substances 0.000 title claims description 32
- 238000010438 heat treatment Methods 0.000 claims abstract description 8
- 239000007789 gas Substances 0.000 claims description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 14
- 239000003546 flue gas Substances 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 9
- 238000002156 mixing Methods 0.000 claims description 6
- 230000005587 bubbling Effects 0.000 claims description 5
- 230000033228 biological regulation Effects 0.000 claims description 3
- 230000003134 recirculating effect Effects 0.000 claims description 2
- 230000001105 regulatory effect Effects 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 11
- 239000012141 concentrate Substances 0.000 abstract description 4
- 239000002131 composite material Substances 0.000 abstract 5
- 239000000779 smoke Substances 0.000 abstract 4
- 239000000446 fuel Substances 0.000 description 10
- 239000002609 medium Substances 0.000 description 9
- 239000003245 coal Substances 0.000 description 8
- 239000010865 sewage Substances 0.000 description 8
- 238000009833 condensation Methods 0.000 description 6
- 230000005494 condensation Effects 0.000 description 6
- 239000000428 dust Substances 0.000 description 6
- 230000008020 evaporation Effects 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 239000001963 growth medium Substances 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 244000000010 microbial pathogen Species 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 210000004681 ovum Anatomy 0.000 description 1
- 230000003071 parasitic effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The invention relates to a cycle fluidizing bed wet mud drying burning method, with composite drier, wherein the invention burns wet mud with water content between 60-90% in the cycle fluidizing bed burning furnace or cycle fluidizing bed boiler, to concentrate the drying and burning in single device; the wet mud is dried in composite drier to be feedback to the hearth to be burnt with cycle ash together, to avoid taking water into tail smoke channel with the high-temperature smoke of hearth, to be leaded out with the fluidizing gas of composite drier, to reduce the heat loss; and the composite drier is arranged with heating coil tube, connected to the tubular heat exchanger of tail smoke channel, to lead in the smoke heat, to be used as the energy to dry wet mud with high-temperature cycle ash; and the discharge gas of composite drier is dedusted and dehumidified to be used as fluidizing gas or fed into hearth to be burnt, without generating smelly gas.
Description
Technical field
The present invention relates to the processing method of a kind of discarded object (wet mud), particularly relate to the wet method for sludge treatment that a kind of mummification of adopting the band combined dryer combines with burning.
Technical background
Mud is the solid residue after the sewage disposal, and sludge quantity accounts for 3 ‰ of sewage load～5 ‰ (in moisture content 97%).Industry of China and sanitary sewage disposal amount increase sharply, and the continuous construction along with sewage treatment plant will produce more mud.The composition of mud is very complicated, except that containing a large amount of moisture, also contains organic matter, various trace elements, pathogenic microorganism and the compositions such as parasitic ovum, heavy metal of common organic matter, difficult degradation.
The method for sludge treatment that with the burning is core process can farthest satisfy minimizing, stabilisation and innoxious requirement.But existing sludge incineration method mostly requires to use earlier special equipment mud to be carried out burn after the preliminary treatment such as mummification again, and mummification is finished system complex with burning in two complete equipments; The mummification equipment energy consumption is big, operating cost height, security requirement height; And burning and drying mud, be easy to generate NOx, need behind incinerator, to be equipped with nitrogen rejection facility; Simultaneously, because sulfur-bearing in the mud also needs to be equipped with desulfurizer behind incinerator.This makes sludge incinerating system complexity, harmless treatment with high costs.
Directly the wet mud that adds without mummification in incinerator burns, and the cell process such as harmless treatment of drying, burning even the flue gas of mud can be concentrated in the single device to carry out simultaneously, simplifies the sludge incineration treatment process, reduces processing cost; But moisture contained in the wet mud will be discharged burner hearth with burning the high-temperature flue gas that is produced, and take away a large amount of heats, therefore need to add a large amount of auxiliary fuels and just can reach energy balance.
Summary of the invention
The purpose of this invention is to provide a kind of wet sludge drying and incinerating treatment method employing circulating fluidized bed with combined dryer, this method combines the drying and incineration of mud, concentrate in the integrated apparatus and carry out, wet sludge anhydration institute calorific requirement directly comes from the burning liberated heat of mud and auxiliary fuel, and the incinerator after-heat that from flue gas, reclaims, the mud after the mummification burns in burner hearth.
Technical scheme of the present invention is as follows:
Band combined dryer provided by the invention wet sludge drying and incinerating treatment method employing circulating fluidized bed, the wet mud of anhydration and incineration moisture content between 60-90% in circulating fluidized bed incinerator, it is characterized in that, in recirculating fluidized bed high-temp circulating ash loop, combined dryer is set, the high-temp circulating ash that separates from the cyclone separator of circulating fluidized bed incinerator is through the grey distributing valve of heat, a part is directly returned burner hearth through material returning device, and another part enters combined dryer; The economy-combat wet mud of breaing up of putting in bulk is sent into combined dryer, in combined dryer, carry out indirect heat exchange with the direct blending heat exchange of high-temp circulating ash and with heat transferring medium in the heat release coil pipe that is arranged in the combined dryer, be heated, after drying becomes the dewatered sludge that moisture content is 5-20%, return burner hearth with circulating ash again and burn.Described combined dryer is the bubbling fluidized bed formula, and the bottom feeds fluidizing gas, and the heat release coil pipe wherein is set.Described heat release coil pipe links to each other with the pipe heat exchanger of incinerator afterbody, feeds heat transferring medium in the heat release coil pipe, and heat transferring medium absorbs the heat of hot flue gas in pipe heat exchanger, heat release in the heat release coil pipe, the wet mud of heating.Described heat transferring medium is conduction oil or steam.Described heat transferring medium heating is controlled in the 100-260 ℃ of scope with the variations in temperature of heat release.The high-temp circulating ash amount of distributing valve regulation to enter combined dryer by heat ash is controlled at 80-150 ℃ with the delivery temperature of combined dryer.Can strengthen of the adjusting of hot grey distributing valve by in closed circuit, adding inert bed material (as sand) to increase the mode of global cycle ash amount to the delivery temperature of combined dryer.The exhaust of combined dryer is sent combined dryer back to and is recycled as fluidizing gas after dedusting and dehumidifying, perhaps sends into burner hearth and burns.
The present invention is provided with combined dryer in the high-temp circulating ash closed circuit of circulating fluidized bed incinerator, the high-temp circulating ash that cyclone separator separates distributes through the grey distributing valve of heat, a part enters material returning device and directly returns burner hearth, and another part enters combined dryer; Moisture content is broken up the back and is added inlet and add from being located at wet mud on the combined dryer in bulk the putting of the wet mud economy-combat between the 60-90%; Combined dryer is the bubbling fluidized bed formula, and the bottom feeds fluidizing gas; Wherein arrange the heat release coil pipe, heat transferring medium absorbs the heat of hot flue gas in pipe heat exchanger, heat release in the heat release coil pipe, the wet mud of heating; Heat transferring medium is conduction oil or steam.Utilize the heat of the flue gas that heat transferring medium is brought in the heat release coil pipe to heat, dry wet mud, but this part shortage of heat with wet sludge anhydration to moisture content 5-20%, therefore supply by high-temp circulating ash again.
High-temp circulating ash amount by heat ash distributes valve regulation to enter combined dryer is controlled at 80-150 ℃ with the combined dryer delivery temperature, and provide enough heat with wet sludge anhydration to moisture content 5-20%.The grey distributing valve of heat can be mechanical type or pneumatic control formula.Can increase the adjustable range of hot grey distributing valve by in closed circuit, adding inert bed material (as sand) in addition, strengthen its regulating power the combined dryer delivery temperature to increase the mode of global cycle ash amount; Wet mud in combined dryer with the direct blending of circulating ash, with heat release coil pipe indirect heat exchange, be heated, the contained humidity evaporation is dried to the dewatered sludge that moisture content is 5-20%, returns burner hearth with circulating ash by mechanical mode of movement or strength mode and burns.
Wet mud contained humidity major part is evaporated out in combined dryer, draws from the combined dryer top with the combined dryer fluidizing gas; The combined dryer exhaust is isolated after fine powder and dust, cooler condensation go out condensed water through pulverized-coal collector, through the blower fan pressurization, sends combined dryer back to as the combined dryer fluidizing gas and recycles again, perhaps sends into burner hearth and burns; Isolated fine powder of pulverized-coal collector and dust are sent burner hearth back to by mechanical mode of movement or strength mode and are burned, and the condensed water that the cooler condensation goes out is sent sewage treatment plant back to and handled.
Its principle is:
The drying process of wet mud carries out in combined dryer, the heat that utilizes the burning of mud that high-temp circulating ash brings into and auxiliary fuel to produce, also from flue gas, reclaim the fume afterheat of incinerator simultaneously, the mummification mud that wets, wet mud is the graininess dewatered sludge of 5-20% by mummification, return burner hearth with circulating ash again and burn, burn in the high-temperature flue gas that produces and only contain a small amount of water vapor, the heat of discharging burner hearth significantly reduces; Most of moisture in the wet mud is discharged with the lower combined dryer exhaust of temperature with the form of steam, steam is condensed into water in cooler, can send sewage treatment plant back to handles, combined dryer exhaust through the dedusting dehumidifying can recycle in closed circulation, also can send into the burner hearth burning disposal, the gas that peculiar smell is arranged that produces in the time of can both avoiding sludge drying is discharged in the environment.
Band combined dryer provided by the invention wet sludge drying and incinerating treatment method employing circulating fluidized bed has following advantage: break through that first mummification is burned again, two patterns that process is independently carried out separately, the drying and incineration of mud is combined, concentrate in the incorporate device and carry out, simplify the anhydration and incineration treatment process of wet mud greatly, simplified anhydration and incineration equipment; Wet sludge anhydration institute calorific requirement is from the waste heat and the burning liberated heat that comes from mud and auxiliary fuel of the hot flue gas of incinerator: hot particle directly contacts in combined dryer with wet mud, fully blending, strengthened heat transfer, made that wet mud is heated rapidly, drying; Wet simultaneously mud also with heat release coil pipe indirect heat exchange, absorb the heat that from hot flue gas, reclaims that heat transferring medium is brought into, thereby made full use of the fume afterheat of incinerator; For the pure burning of wet mud, adopt method of the present invention, the wet moisture percentage in sewage sludge upper limit that can allow to pure burning improves 2-3 percentage point, makes moisture content 73-75% and following wet mud can not add auxiliary fuel and burns; Add the burning of the wet mud of high-moisture percentage of auxiliary fuel for needs, adopt method of the present invention, can reduce the addition of auxiliary fuel, save operating cost; Moisture major part contained in the wet mud is no longer with burning the high-temperature flue gas discharging that produces, but concentrate in the cryogenic gas of combined dryer discharge, reduced the thermal loss of system, reduced the consumption of incinerator auxiliary fuel or improved the upper limit need not add the wet moisture percentage in sewage sludge that auxiliary fuel burns; The gas that produces in the sludge drying recycles or sends into burner hearth after treatment and burns, and makes the gas that does not discharge peculiar smell in the processing procedure.
Description of drawings
Accompanying drawing 1 is the method schematic diagram of the embodiment of the invention 1.
Accompanying drawing 2 is method schematic diagrames of the embodiment of the invention 2.
Burner hearth 1 cyclone separator 2 hot grey distributing valve 3 material returning devices 4
Combined dryer 5 is broken up device 6 wet mud and is added inlet 7 pulverized-coal collectors 8
Cooler 9 blower fans 10 back-end ductworks 11 pipe heat exchangers 12
Heat release coil pipe 13 wet mud A dewatered sludge B combined dryer exhaust C
Dust D condensed water E is through the gas F heat transferring medium G of dedusting dehumidifying
The specific embodiment
Embodiment 1
Independent anhydration and incineration moisture content is 60% wet mud A in circulating fluidized bed incinerator, and wet mud A is added inlet 7 addings from the wet mud that is located on the combined dryer 5, adds the fashionable device 6 of breaing up that adds on the inlet 7 that is installed in and breaks up; Combined dryer 5 is arranged in the circulating fluidized bed incinerator circulating ash closed circuit, and the high-temp circulating ash that cyclone separator 2 separates is through the grey distributing valve 3 of mechanical type heat, and a part enters material returning device 4 and directly returns burner hearth 1, and another part enters combined dryer 5; Combined dryer 5 is the bubbling fluidized bed formula, and the bottom feeds fluidizing gas, wherein is provided with heat release coil pipe 13; Heat release coil pipe 13 links to each other with pipe heat exchanger 12 in the incinerator back-end ductwork 11, heat transferring medium G (steam) absorbs the heat that burning that flue gas takes out of produces in pipe heat exchanger 12, be heated to 150 ℃, again heat release in heat release coil pipe 13, the wet mud of heating, steam is cooled to 100 ℃; Add sand from burner hearth 1 bottom, increase the global cycle amount, and regulate the high-temp circulating ash amount that enters combined dryer 5, combined dryer exhaust C temperature is controlled at about 80 ℃ by the grey distributing valve 3 of heat; Wet mud A in combined dryer 5 with the direct blending of circulating ash, and be heated, the contained humidity evaporation, it is 20% dewatered sludge B that wet mud A is dried to moisture content, returns burner hearth 1 with circulating ash by the strength mode and burns; Combined dryer exhaust C draws from its top, after pulverized-coal collector 8 is isolated dust D, cooler 9 condensations and gone out condensed water E, through blower fan 10 pressurizations, sends combined dryer 5 back to as the combined dryer fluidizing gas and recycles again; Pulverized-coal collector 8 isolated dust D send burner hearth back to and burn, and the condensed water E that cooler 9 condensations go out sends sewage treatment plant back to and handles.
Embodiment 2
Adding coal in circulating fluidized bed incinerator is 90% wet mud A as auxiliary fuel anhydration and incineration moisture content, and wet mud A is added inlet 7 and adds from being located at wet mud on the combined dryer 5, adds the fashionable device 6 of breaing up that adds on the inlet 7 that is installed in and breaks up; Combined dryer 5 is arranged in the circulating fluidized bed incinerator circulating ash closed circuit, the high-temp circulating ash that cyclone separator 2 separates is through the grey distributing valve 3 of pneumatic control formula heat, a part enters material returning device 4 and directly returns burner hearth 1, and another part enters combined dryer 5; Combined dryer 5 is the bubbling fluidized bed formula, and the bottom feeds fluidizing gas, wherein is provided with heat release coil pipe 13; Heat release coil pipe 13 links to each other with pipe heat exchanger 12 in the incinerator back-end ductwork 11, heat transferring medium G (conduction oil) absorbs the heat that burning that flue gas takes out of produces in pipe heat exchanger 12, be heated to 260 ℃, again heat release in heat release coil pipe 13, the wet mud of heating, conduction oil is cooled to 220 ℃; Regulate the high-temp circulating ash amount that enters combined dryer 5 by the grey distributing valve 3 of heat, combined dryer exhaust C temperature is controlled at about 150 ℃; Wet mud A in combined dryer 5 with the direct blending of circulating ash, and be heated, the contained humidity evaporation, it is 15% dewatered sludge B that wet mud A is dried to moisture content, returns burner hearth 1 with circulating ash by mechanical mode of movement and burns; Combined dryer exhaust C draws from its top, after pulverized-coal collector 8 is isolated dust D, cooler 9 condensations and gone out condensed water E, again through blower fan 10 pressurizations, sends into burner hearth 1 and burns; Pulverized-coal collector 8 isolated dust D send burner hearth 1 back to and burn, and the condensed water E that cooler 9 condensations go out sends sewage treatment plant back to and handles.
Claims (8)
1, a kind of wet sludge drying and incinerating treatment method employing circulating fluidized bed with combined dryer, the wet mud of anhydration and incineration moisture content between 60-90% in circulating fluidized bed incinerator or CFBB, it is characterized in that, in recirculating fluidized bed high-temp circulating ash loop, combined dryer is set, the high-temp circulating ash that separates from the cyclone separator of circulating fluidized bed incinerator distributes through the grey distributing valve of heat, a part is directly returned burner hearth through material returning device, and another part enters combined dryer; The economy-combat wet mud of breaing up of putting in bulk is sent into combined dryer, in combined dryer with the direct blending of high-temp circulating ash, with the heat transferring medium indirect heat exchange that is arranged in the heat release coil pipe in the combined dryer, be heated, after drying becomes the dewatered sludge that moisture content is 5-20%, return burner hearth with circulating ash again and burn.
2, press the wet sludge drying and incinerating treatment method employing circulating fluidized bed of the described band combined dryer of claim 1, it is characterized in that described combined dryer is the bubbling fluidized bed formula, the bottom feeds fluidizing gas, and is provided with the heat release coil pipe.
3, press the wet sludge drying and incinerating treatment method employing circulating fluidized bed of the described band combined dryer of claim 1, it is characterized in that, described heat release coil pipe links to each other with pipe heat exchanger in the incinerator back-end ductwork, feed heat transferring medium in the heat release coil pipe, heat transferring medium absorbs the heat of flue gas in pipe heat exchanger, heat release in the heat release coil pipe, the wet mud of heating.
4, press the wet sludge drying and incinerating treatment method employing circulating fluidized bed of the described band combined dryer of claim 3, it is characterized in that described heat transferring medium is conduction oil or steam.
5, press the wet sludge drying and incinerating treatment method employing circulating fluidized bed of the described band combined dryer of claim 4, it is characterized in that, described heat transferring medium heating is controlled in the 100-260 ℃ of scope with the variations in temperature of heat release.
6, press the wet sludge drying and incinerating treatment method employing circulating fluidized bed of the described band combined dryer of claim 1, it is characterized in that, high-temp circulating ash amount by the heat ash distributes valve regulation to enter combined dryer is controlled at 80-150 ℃ with the combined dryer delivery temperature.
7, press the wet sludge drying and incinerating treatment method employing circulating fluidized bed of the described band combined dryer of claim 6, it is characterized in that, by in closed circuit, adding inert bed material, strengthen the regulating power of hot grey distributing valve to the combined dryer delivery temperature to increase the mode of global cycle ash amount.
8, press the wet sludge drying and incinerating treatment method employing circulating fluidized bed of the described band combined dryer of claim 1, it is characterized in that, described combined dryer exhaust is sent combined dryer back to and is recycled as fluidizing gas after dedusting and dehumidifying, perhaps sends into burner hearth and burns.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200510077292XA CN100453905C (en) | 2005-06-21 | 2005-06-21 | Wet sludge drying and incinerating treatment method employing circulating fluidized bed with combined dryer |
| PCT/CN2006/001415 WO2006136105A1 (en) | 2005-06-21 | 2006-06-21 | A combined dryer and a method and an equipment for incinerating the wet sludge with the combined dryer |
| JP2008517303A JP4755250B2 (en) | 2005-06-21 | 2006-06-21 | Combined dryer, wet sludge incineration apparatus with combined dryer, and method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200510077292XA CN100453905C (en) | 2005-06-21 | 2005-06-21 | Wet sludge drying and incinerating treatment method employing circulating fluidized bed with combined dryer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1884913A true CN1884913A (en) | 2006-12-27 |
| CN100453905C CN100453905C (en) | 2009-01-21 |
Family
ID=37583193
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB200510077292XA Expired - Fee Related CN100453905C (en) | 2005-06-21 | 2005-06-21 | Wet sludge drying and incinerating treatment method employing circulating fluidized bed with combined dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100453905C (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101713543B (en) * | 2009-02-24 | 2011-08-31 | 刘沪滨 | Sludge incinerator with no auxiliary fuel |
| CN102531324A (en) * | 2008-10-29 | 2012-07-04 | 中国科学院工程热物理研究所 | Wet sludge drying and incinerating treatment device |
| CN101943413B (en) * | 2009-07-10 | 2014-11-05 | 中国科学院工程热物理研究所 | Integral sludge incineration process control system |
| CN104176898A (en) * | 2014-08-29 | 2014-12-03 | 凤阳海泰科能源环境管理服务有限公司 | Sludge drying system and method |
| CN106287747A (en) * | 2016-08-18 | 2017-01-04 | 哈尔滨工业大学 | The outer heat drying of sludge roller is integrated with Incineration in CFB and exhaust gas cleaner |
| CN108579384A (en) * | 2018-05-10 | 2018-09-28 | 哈尔滨工业大学 | A kind of sludge treatment equipment of compound desiccation and burning coupled electricity-generation |
| CN110207104A (en) * | 2019-05-27 | 2019-09-06 | 国粤（深圳）科技投资有限公司 | A kind of outer fossil fuel of furnace burns preceding pretreatment unit |
| CN110422988A (en) * | 2019-09-02 | 2019-11-08 | 宝莹环保科技(杭州)有限公司 | Calcirm-fluoride wet mud process for producing device |
| CN111623352A (en) * | 2020-05-08 | 2020-09-04 | 东南大学 | Self-sustaining incineration system and method for low-calorific-value high-ash sludge |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JPS6025686B2 (en) * | 1979-05-16 | 1985-06-19 | 日本フア−ネス工業株式会社 | Sewage sludge incinerator |
| CN2173355Y (en) * | 1993-10-21 | 1994-08-03 | 哈尔滨工业大学 | Industrial mud circulation fluidized-bed incinerator |
| JPH08166115A (en) * | 1994-12-14 | 1996-06-25 | Mitsubishi Heavy Ind Ltd | Current selection/drier |
| CN1138676A (en) * | 1995-06-16 | 1996-12-25 | 东方锅炉厂 | Garbage incineration furnace |
| DE10341610B8 (en) * | 2003-09-10 | 2007-09-27 | Lentjes Gmbh | Process for the incineration of solid waste |
| CN1559939A (en) * | 2004-03-10 | 2005-01-05 | 沈阳戴维国际机电设备有限公司 | Process for treating sludge of sewage treatment plant by circulating fluidizing burning method |
| CN1616885A (en) * | 2004-12-06 | 2005-05-18 | 无锡华光锅炉股份有限公司 | Method and its device for burning mixed mud in circulating fluidized bed boiler |
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- 2005-06-21 CN CNB200510077292XA patent/CN100453905C/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102531324A (en) * | 2008-10-29 | 2012-07-04 | 中国科学院工程热物理研究所 | Wet sludge drying and incinerating treatment device |
| CN101713543B (en) * | 2009-02-24 | 2011-08-31 | 刘沪滨 | Sludge incinerator with no auxiliary fuel |
| CN101943413B (en) * | 2009-07-10 | 2014-11-05 | 中国科学院工程热物理研究所 | Integral sludge incineration process control system |
| CN104176898A (en) * | 2014-08-29 | 2014-12-03 | 凤阳海泰科能源环境管理服务有限公司 | Sludge drying system and method |
| CN104176898B (en) * | 2014-08-29 | 2015-10-28 | 凤阳海泰科能源环境管理服务有限公司 | A kind of sludge drying system and method |
| CN106287747A (en) * | 2016-08-18 | 2017-01-04 | 哈尔滨工业大学 | The outer heat drying of sludge roller is integrated with Incineration in CFB and exhaust gas cleaner |
| CN108579384A (en) * | 2018-05-10 | 2018-09-28 | 哈尔滨工业大学 | A kind of sludge treatment equipment of compound desiccation and burning coupled electricity-generation |
| CN108579384B (en) * | 2018-05-10 | 2021-08-17 | 哈尔滨工业大学 | Sludge treatment device for combined drying and incineration coupled power generation |
| CN110207104A (en) * | 2019-05-27 | 2019-09-06 | 国粤（深圳）科技投资有限公司 | A kind of outer fossil fuel of furnace burns preceding pretreatment unit |
| CN110422988A (en) * | 2019-09-02 | 2019-11-08 | 宝莹环保科技(杭州)有限公司 | Calcirm-fluoride wet mud process for producing device |
| CN111623352A (en) * | 2020-05-08 | 2020-09-04 | 东南大学 | Self-sustaining incineration system and method for low-calorific-value high-ash sludge |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100453905C (en) | 2009-01-21 |
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