CN105013802A - Organic solid waste high-temperature carbonization and drying system with waste heat utilization device - Google Patents
Organic solid waste high-temperature carbonization and drying system with waste heat utilization device Download PDFInfo
- Publication number
- CN105013802A CN105013802A CN201510466201.5A CN201510466201A CN105013802A CN 105013802 A CN105013802 A CN 105013802A CN 201510466201 A CN201510466201 A CN 201510466201A CN 105013802 A CN105013802 A CN 105013802A
- Authority
- CN
- China
- Prior art keywords
- organic solid
- unit
- carbonization
- heat exchanger
- machine
- 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.)
- Pending
Links
Abstract
The invention discloses an organic solid waste high-temperature carbonization and drying system with a waste heat utilization device. The organic solid waste high-temperature carbonization and drying system comprises a carbonization machine, a drying machine, a heat exchanger, a hot air unit, an air return unit, a dehumidifier and a tail gas processing device, wherein the carbonization machine is connected with the drying machine through a spiral conveyor; a distributor and a spiral discharger are arranged in the drying machine; the hot air unit is installed at the bottom of the drying machine; the air return unit is installed on the top of the drying machine; the carbonization machine is sequentially connected with the heat exchanger and the hot air unit through high-temperature gas ducts; the air return unit is sequentially connected with the dehumidifier, the tail gas processing device and the heat exchanger through air return pipes. Compared with the prior art, the organic solid waste high-temperature carbonization and drying system has the advantages that a great cost advantage is achieved, the physicochemical properties of materials are not changed at the drying temperature within 70 DEG C, and the value of the materials can be maintained; air is recycled after being dehumidified, so that the energy saving effect is more remarkable; moreover, no gas is exhausted, and secondary pollution is avoided.
Description
Technical field
The present invention relates to bootstrap system, particularly relate to a kind of organic solid castoff high temperature carbonization and the anhydration system with residual heat using device.
Background technology
Constantly produce a large amount of solid waste in modern society's production, life, wherein have quite a few to contain higher moisture.Organic solid waste is a kind of recoverable " waste material ", but the higher moisture bottleneck restricting organic solid castoff often and recycle.Present stage, general dry technology mainly contained high-temperature steam paddle-dryer, solar energy drying room, fire coal or air dry cylinder, mechanism filter-pressing etc.Above-mentioned various technology path has its respective feature, causes there is different applicabilities.Paddle-dryer produces a large amount of fine solid particles and there is larger potential safety hazard in dry run; Solar energy drying room need huge floor space and the cycle longer, also can be limited by local solar radiation; Coal-fired or air dry cylinder then will be equipped with comparatively complicated, huge follow-up exhaust treatment system, otherwise there is the discharge risk of foul gas and the pollution factor such as sulfur dioxide, oxynitrides; Mechanism filter-pressing is then because of the physicochemical property limit value of organic solid castoff, and dehydrating effect does not often reach requirement.
Summary of the invention
The present invention is to solve above-mentioned deficiency, provides a kind of organic solid castoff high temperature carbonization and the anhydration system with residual heat using device.
Above-mentioned purpose of the present invention is realized by following technical scheme: a kind of organic solid castoff high temperature carbonization and anhydration system with residual heat using device, comprise carbonizer, desiccation machine, heat exchanger, hot blast unit, return air unit, dehumidifier and exhaust gas processing device, described carbonizer connects desiccation machine by screw input feeder, is provided with distributing device and spiral discharging device in desiccation machine; Described hot blast unit is arranged on bottom desiccation machine, return air unit is arranged on desiccation machine top, described carbonizer connects heat exchanger and hot blast unit successively by high-temperature gas conduit, and described return air unit connects dehumidifier, exhaust gas processing device and heat exchanger successively by return air duct.
Operation principle of the present invention: carbonizer waste heat exports to after heat exchanger heat exchange through high-temperature gas conduit, and Cryogenic air heats by heat energy, then it is inner to introduce desiccation machine through hot blast unit, heat material, after material is heated, moisture diffusion is in hot blast; Hot blast is derived to enter in dehumidifier by return air unit and is carried out dehumidifying, dewatering, and the air after dehydration enters in heat exchanger through exhaust gas processing device and heats, and after heating, then it is inner to introduce desiccation machine by hot blast unit.And so forth, constantly take away the moisture in material, thus make material be reduced to setting moisture content from high-moisture.
The present invention be by the carbonizer course of work produce high-temperature tail gas and carry out heat exchange and change heating, after heating, heated material and air in fixing space, after moisture enters air, through dehumidifier, water is converted into liquid state by gaseous state, thus reaches the object of material mummification.
Present invention utilizes the waste heat that carbonizer produces, reach the target of energy-saving and emission-reduction; Mummification temperature controls, within 70 DEG C, effectively to maintain organic physicochemical property, and avoids the generation of foul gas; Air recycling after dehumidifying, reduces energy consumption further; The aqueous water produced is distilled water, non-secondary pollution.
The present invention's advantage is compared with prior art: compared with the charing of the present invention and traditional organic solid castoff and anhydration system, have great cost advantage; Mummification temperature within 70 DEG C, does not change the physicochemical property of material, and the value of material is retained; Air reciprocation cycle after dehumidifying utilizes, and energy-saving effect is more obvious, and discharges without gas, avoids the generation of secondary pollution.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is described in further detail.
As shown in Figure 1, a kind of organic solid castoff high temperature carbonization and anhydration system with residual heat using device, comprise carbonizer 1, desiccation machine 2, heat exchanger 3, hot blast unit 9, return air unit 7, dehumidifier 5 and exhaust gas processing device 4, described carbonizer 1 connects desiccation machine 2 by screw input feeder 12, is provided with distributing device 6 and spiral discharging device 11 in desiccation machine 2; Described hot blast unit 9 is arranged on bottom desiccation machine 2, return air unit 7 is arranged on desiccation machine 2 top, described carbonizer 1 connects heat exchanger 3 and hot blast unit 9 successively by high-temperature gas conduit 2, and described return air unit 7 connects dehumidifier 5, exhaust gas processing device 4 and heat exchanger 3 successively by return air duct 13.
Operation principle of the present invention: carbonizer 1 waste heat exports to after heat exchanger 3 heat exchange through high-temperature gas conduit 2, and Cryogenic air heats by heat energy, then it is inner to introduce desiccation machine 8 through hot blast unit 9, heat material, after material is heated, moisture diffusion is in hot blast; Hot blast is derived to enter in dehumidifier 5 by return air unit 7 and is carried out dehumidifying, dewatering, and the air after dehydration enters in heat exchanger 3 through exhaust gas processing device 4 and heats, and after heating, then introduces desiccation machine inside by hot blast unit 9.And so forth, constantly take away the moisture in material, thus make material be reduced to setting moisture content from high-moisture.
The invention belongs to the category of using waste heat from tail gas regeneration, power plant, cement plant using waste heat from tail gas regeneration know well by the public.But high temperature carbonization system waste heat being carried out organic solid castoff drying technique, to be applied to organic solid castoff process field be then new trial, and be considered to a kind of up-and-coming organic solid waste mummification mode, also the popularization for organic solid castoff high temperature carbonization treatment technology is provided support.
During organic solid castoff high temperature carbonization system cloud gray model, unit organic solid castoff will produce 300m
3left and right tail gas, exhaust temperature can reach 250-350 DEG C, and the heat of this gas is no less than 300kw.h.
The tail gas that current carbonization system produces after running directly discharges after the modes such as Water spray are lowered the temperature, and first can cause the waste of heat energy, and if the waste water produced after Water spray deal with improperly and also easily cause secondary sludge; There is the problems such as energy consumption is high, secondary pollution problem serious, material physical and chemical properties change more in traditional organic solid castoff mummification mode.
The present invention enters heat-exchanger rig by after carbonization system exhaust collection, this heat energy is used for the heating of air, makes air themperature be heated to 50-70 DEG C.Air after heating enters in dry cavity and contacts with material, and material moisture through diffusing into by the air that heats, thus reaches the moisture object of reduction material, and ensure that material physicochemical property does not change.
Air containing moisture enters dehumidifier by return air, is divided by vaporous water to carry out condensation and become liquid state, and aqueous water carries out water conservancy diversion by pipeline; Air heat energy after dehumidifying is retained, and imports in mummification cavity utilize through blower fan circulation.And so forth, according to need of production, the moisture of organic solid castoff can be reduced to less than 15%.
Adopt high temperature carbonization of the present invention and anhydration system, under the condition of use do not used or significantly reduce other energy, greatly reduce the energy consumption needed for organic solid castoff drying process, and alleviate and avoid difficulty and the cost of carbonization system rear end vent gas treatment.
Adopt high temperature carbonization of the present invention and anhydration system, within 70 DEG C, temperature section carries out mummification, and material properties does not change, and the value of material is retained, and heated air reciprocation cycle utilizes not outer row, avoids the problem of secondary pollution as stench.
Adopt high temperature carbonization of the present invention and anhydration system effectively supplementing as carbonizer system, provide strong support by for carbonizer system in the extensive use of organic solid castoff process field.
The foregoing is only embodiments of the invention; not thereby the scope of the claims of the present invention is limited; every utilize description of the present invention and accompanying drawing content to do equivalent structure or equivalent flow process conversion; or be directly or indirectly used in other relevant technical fields, be all in like manner included in scope of patent protection of the present invention.
Claims (1)
1. one kind has organic solid castoff high temperature carbonization and the anhydration system of residual heat using device, it is characterized in that: comprise carbonizer, desiccation machine, heat exchanger, hot blast unit, return air unit, dehumidifier and exhaust gas processing device, described carbonizer connects desiccation machine by screw input feeder, is provided with distributing device and spiral discharging device in desiccation machine; Described hot blast unit is arranged on bottom desiccation machine, return air unit is arranged on desiccation machine top, described carbonizer connects heat exchanger and hot blast unit successively by high-temperature gas conduit, and described return air unit connects dehumidifier, exhaust gas processing device and heat exchanger successively by return air duct.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510466201.5A CN105013802A (en) | 2015-08-03 | 2015-08-03 | Organic solid waste high-temperature carbonization and drying system with waste heat utilization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510466201.5A CN105013802A (en) | 2015-08-03 | 2015-08-03 | Organic solid waste high-temperature carbonization and drying system with waste heat utilization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105013802A true CN105013802A (en) | 2015-11-04 |
Family
ID=54404306
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510466201.5A Pending CN105013802A (en) | 2015-08-03 | 2015-08-03 | Organic solid waste high-temperature carbonization and drying system with waste heat utilization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105013802A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112486084A (en) * | 2020-11-03 | 2021-03-12 | 江门绿润环保科技有限公司 | Remote control method and system for low-temperature drying machine |
| CN113751464A (en) * | 2021-08-27 | 2021-12-07 | 田园牧歌生态环境科技(江苏)有限公司 | Solid waste organic matter processing system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102476907A (en) * | 2010-11-25 | 2012-05-30 | 溧阳正昌干燥设备有限公司 | Equipment and method of high-efficiency high-speed environmentally-friendly energy-saving sludge treatment system |
| KR101211375B1 (en) * | 2010-10-21 | 2012-12-13 | 한국에너지기술연구원 | A Waste Heat Recovery System For Tenter Exhaust Fumes |
| CN103911168A (en) * | 2014-04-09 | 2014-07-09 | 江苏河海科技工程集团有限公司 | Integral rapid carbonizing treatment technology for municipal waste |
| CN203999502U (en) * | 2014-07-07 | 2014-12-10 | 江门绿润环保科技有限公司 | A kind of organic solid castoff mummification charing integrated system |
| CN203999497U (en) * | 2014-07-15 | 2014-12-10 | 江门绿润环保科技有限公司 | A kind of organic solid castoff high temperature carbonization system |
| CN104229797A (en) * | 2013-06-08 | 2014-12-24 | 中国科学院工程热物理研究所 | Pyrolysis-activation-combustion-gasification integrated furnace, garbage landfill coordinating treatment system and activated carbon preparation method |
-
2015
- 2015-08-03 CN CN201510466201.5A patent/CN105013802A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101211375B1 (en) * | 2010-10-21 | 2012-12-13 | 한국에너지기술연구원 | A Waste Heat Recovery System For Tenter Exhaust Fumes |
| CN102476907A (en) * | 2010-11-25 | 2012-05-30 | 溧阳正昌干燥设备有限公司 | Equipment and method of high-efficiency high-speed environmentally-friendly energy-saving sludge treatment system |
| CN104229797A (en) * | 2013-06-08 | 2014-12-24 | 中国科学院工程热物理研究所 | Pyrolysis-activation-combustion-gasification integrated furnace, garbage landfill coordinating treatment system and activated carbon preparation method |
| CN103911168A (en) * | 2014-04-09 | 2014-07-09 | 江苏河海科技工程集团有限公司 | Integral rapid carbonizing treatment technology for municipal waste |
| CN203999502U (en) * | 2014-07-07 | 2014-12-10 | 江门绿润环保科技有限公司 | A kind of organic solid castoff mummification charing integrated system |
| CN203999497U (en) * | 2014-07-15 | 2014-12-10 | 江门绿润环保科技有限公司 | A kind of organic solid castoff high temperature carbonization system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112486084A (en) * | 2020-11-03 | 2021-03-12 | 江门绿润环保科技有限公司 | Remote control method and system for low-temperature drying machine |
| CN113751464A (en) * | 2021-08-27 | 2021-12-07 | 田园牧歌生态环境科技(江苏)有限公司 | Solid waste organic matter processing system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101857350B (en) | Device for indirectly drying and utilizing sludge by cement kiln waste gas and process method thereof | |
| CN203487024U (en) | Heat pump low temperature sludge drying treatment system | |
| CN103644709A (en) | Superheated steam drying device and method | |
| CN207435292U (en) | A kind of coupled electricity-generation system using smoke residual heat to dry sludge | |
| CN100520261C (en) | Method of utilizing exhausted steam afterheat from plaster tablet drying machine | |
| CN105254147A (en) | Triple utilization device and method for exhaust steam waste heat produced during superheat steam drying of sludge | |
| CN103697668A (en) | Heated air circulation double drum type dryer with high temperature heat pump | |
| CN203629203U (en) | Superheat steam drying device | |
| CN103524013A (en) | Wet sludge treatment method and equipment thereof | |
| CN103148692B (en) | Vertical briquette dryer | |
| CN204041130U (en) | The brown coal drying power generation system of Water Sproading in a kind of coal | |
| CN104150732A (en) | Two-stage sludge drying system | |
| CN103242876A (en) | Drying or low-temperature dry distillation method and device of brown coal or low-metamorphic candle coal | |
| CN103438678B (en) | Efficient energy-saving pulp dewatering and drying equipment | |
| CN205133368U (en) | Triple devices that utilize of mud superheated steam drying exhaust steam waste heat | |
| CN104197684B (en) | Can the superheat steam drying brown coal system of Water Sproading and process thereof | |
| CN103333703B (en) | Drying or low-temperature destructive distillation method and device of brown coal or low-deterioration long flame coal | |
| CN105013802A (en) | Organic solid waste high-temperature carbonization and drying system with waste heat utilization device | |
| CN204918333U (en) | Part energy recuperation sludge drying system | |
| CN103940208B (en) | Plasterboard industrial exhaust heat drying system | |
| CN103822439B (en) | One utilizes surplus heat of power plant to carry out pre-dried system and method to brown coal | |
| CN103588379A (en) | Vertical sludge dryer | |
| CN107218797A (en) | A kind of drying device and its application | |
| CN104710094A (en) | Printing and dyeing sludge drying method and apparatus thereof | |
| CN104197692A (en) | Drying system and method for mercury catalyst production tail gas recycling |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20180125 Address after: 529152 Guangdong Province, Jiangmen City Xinhui District Industrial Park first Applicant after: Jiangmen Green Run Carbonization Technology Co., Ltd. Address before: 529000 Guangdong City, Jiangmen province Yingbin Road, Pengjiang District, No. six, layer 118 Applicant before: JIANGMEN LYURUN ENVIRONMENTAL PROTECTION SCIENCE & TECHNOLOGY CO., LTD. |
|
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20151104 |