CN203052677U - Sludge magnetizing pyrolysis and combustion integration machine - Google Patents
Sludge magnetizing pyrolysis and combustion integration machine Download PDFInfo
- Publication number
- CN203052677U CN203052677U CN 201220731861 CN201220731861U CN203052677U CN 203052677 U CN203052677 U CN 203052677U CN 201220731861 CN201220731861 CN 201220731861 CN 201220731861 U CN201220731861 U CN 201220731861U CN 203052677 U CN203052677 U CN 203052677U
- Authority
- CN
- China
- Prior art keywords
- pyrolysis
- cylinder
- rotary kiln
- mud
- inner barrel
- 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.)
- Withdrawn - After Issue
Links
Images
Landscapes
- Gasification And Melting Of Waste (AREA)
- Incineration Of Waste (AREA)
Abstract
The utility model relates to a sludge magnetizing pyrolysis and combustion integration machine. The sludge magnetizing pyrolysis and combustion integration machine is characterized by comprising a rotary kiln cylinder arranged horizontally and provided with a feed inlet and a discharge outlet, wherein an inner cylinder is arranged in the rotary kiln cylinder in a penetrating mode, a gap cavity allowing sludge to be transferred from the feed inlet to the discharge outlet is formed between the rotary kiln cylinder and the inner cylinder, and a through hole enabling the gap cavity to be communicated with the inner cavity of the inner cylinder is formed at the end, close to the discharge outlet of the rotary kiln cylinder, of the inner cylinder. The sludge magnetizing pyrolysis and combustion integration machine has the advantages that heat loss is reduced and the using rate of heat is improved due to the integration of internal heat and external heat combination and waste heat utilization; system technology plane arrangement is compact, an independent secondary combustion chamber does not need to be arranged behind the sludge magnetizing pyrolysis and combustion integration machine, the using area of land is reduced, and investment cost is greatly reduced; and the integration design enables system configuration to be reasonable, simple and clear, operation is simple, the number of personnel needed is small, and therefore labor cost and maintenance cost are reduced.
Description
Technical field:
The utility model relates to a kind of mud magnetization pyrolysis, burning integral machine.
Background technology:
High temperature anhydration and incineration method and the pyrolysismethod of sludge treatment equipment employing at present adopt dryer that mud is dried pretreated UTILIZATION OF VESIDUAL HEAT IN form more.Mud after the oven dry enters in the stove again and burns or pyrolysis, from the stove or the high-temperature flue gas of dual firing chamber, produces high temperature air and enter the mud dryer again mud is carried out prebake after waste heat boiler produces steam (or conduction oil) or heat exchanger heat exchange.
Mud is dried pretreated some mud dryer exist drying efficiency low, fluctuation of service, the life-span is low, the cost height, particularly be difficult to problems such as maximization, and the steam that mud oven dry back produces also needs the condensation dehydration, there are drawbacks such as secondary pollution in addle and the foul smell of generation.The bootstrap system of mud dryer, waste heat boiler (or heat exchanger) formation also takies a large amount of plant areas simultaneously, increases infrastructure investment.System flow is long, and pipeline is many, and heat loss is big, has reduced UTILIZATION OF VESIDUAL HEAT IN efficient, has increased maintenance difficulties and cost.
Summary of the invention:
The purpose of this utility model is to provide a kind of mud magnetization pyrolysis, burning integral machine, and this mud magnetizes pyrolysis, the burning integral machine is not only simple in structure, reasonable in design, and is conducive to solve problems such as UTILIZATION OF VESIDUAL HEAT IN efficient is low.
The utility model is achieved through the following technical solutions:
The utility model mud magnetization pyrolysis, burning integral machine, it is characterized in that: comprise a horizontally set and have the cylinder of rotary kiln of charging and discharging mouth, be equipped with an inner barrel in the described cylinder of rotary kiln, be formed with between cylinder of rotary kiln and the inner barrel in order to mud and be sent to the spatia of discharging opening from charging aperture, described inner barrel is provided with the port of spatia and inner barrel intracavity inter-connection near the discharge port end of cylinder of rotary kiln.
Be connected to switch-plate from charging aperture toward discharge port end with the intermittent weld of helix mode on the above-mentioned cylinder of rotary kiln internal face.
Above-mentioned feed inlet end is provided with feed arrangement, and described feed arrangement material-pulling device pneumatic for adopting, Driven by Hydraulic Cylinder perhaps is made of conveying worm and feed hopper.
Above-mentioned feed inlet end also is provided with magnetization active oxygen input port.
Above-mentioned inner barrel is provided with the combustor that stretches in the inner barrel near the discharging oral-lateral.
Above-mentioned inner barrel is connected with the flue gas cleaner import near the gas discharge outlet that the charging oral-lateral is provided with, and the flue gas cleaner outlet is connected with air-introduced machine.
Operation principle of the present utility model: mud delivers into cylinder of rotary kiln through feed arrangement, along with cylinder of rotary kiln constantly rotates, through the switch-plate effect on the cylinder of rotary kiln inwall, the spatia of mud in cylinder of rotary kiln constantly turns over, preceding sending, drying and stage casing pyrolytic gasification, finally by becoming the ash section to form lime-ash, discharge through the discharging opening deslagging device.The flue gas aspect, behind the utility model system magnetization pyrolysis mud, the flue gas that contains fuel gas that produces enters in the inner barrel from the inner barrel port by spatia, under the effect of inner barrel internal combustion machine supplemental heat source, fuel gas and harmful substance are at high temperature by completing combustion with destroy by fire, inner barrel outer wall from the port to the gas discharge outlet also heats mud, thereby reaches the purpose of UTILIZATION OF VESIDUAL HEAT IN; Through purifications such as exhaust purifiers, qualified discharge is to atmosphere after treatment through the flue gas after the heat exchange.
The utlity model has following advantage:
1, it is less to be subject to some independent mud drying system disposal ability, burn usually or the pyrolysis processing disposal system be difficult to maximize, the utility model has thoroughly solved this problem;
2, system process horizontal layout compactness need not arrange independently secondary combustion chamber again after mud magnetizes pyrolysis, burning integral machine, the factory building usable floor area is little, has reduced land use area, greatly reduces investment cost;
3, the integrated mode of the compound UTILIZATION OF VESIDUAL HEAT IN of inside and outside heat has reduced the loss of heat, has improved heat utilization ratio;
4, integrated design makes system configuration rationally, concisely, and simple to operate, staffing is few, thereby reduces cost of labor and maintenance cost.
Description of drawings:
Fig. 1 is organigram of the present utility model.
The specific embodiment:
The utility model modified form pyrolyzing sludge apparatus sewage sludge magnetization pyrolysis, burning integral machine, comprise a horizontally set and have charging and discharging mouth 1,2 cylinder of rotary kiln 3, be equipped with an inner barrel 4 in the described cylinder of rotary kiln 3, be formed with between cylinder of rotary kiln and the inner barrel in order to mud and be sent to the spatia 5 of discharging opening from charging aperture, described inner barrel is provided with the port 6 of spatia and inner barrel intracavity inter-connection near the discharge port end of cylinder of rotary kiln.
Be connected to switch-plate from charging aperture toward discharge port end with the intermittent weld of helix mode on the above-mentioned cylinder of rotary kiln internal face.This switch-plate not only plays the effect of feeding and stirring, also plays the effect that increases heat exchange efficiency simultaneously.
For the ease of charging, above-mentioned feed inlet end is provided with feed arrangement, and described feed arrangement material-pulling device pneumatic for adopting, Driven by Hydraulic Cylinder perhaps is made of conveying worm 8 and feed hopper 9.
Discharging opening is provided with deslagging device, and this deslagging device can be that spiral is slagged tap, and planet is slagged tap, hydropneumatic flashboard various ways such as slag tap.
Above-mentioned feed inlet end also is provided with magnetization active oxygen input port 10.Micro-magnetic air by this magnetization active oxygen input port self-magnetization in the future air air supply device is sent in the cylinder, make and keep in the spatia 5 under anoxic and 300 ℃ of-400 ℃ of states, make the mud organic substance matter of continuous feed that the chain reaction of aquation, gasification, inorganic ash scorification etc. continuously take place.
For further burning is from the fuel gas of spatia 5 discharges, above-mentioned inner barrel is provided with the combustor 11 that stretches in the inner barrel near the discharging oral-lateral.
For cleaning of off-gas, above-mentioned inner barrel is connected with flue gas cleaner 13 imports near the gas discharge outlet 12 that the charging oral-lateral is provided with, and the flue gas cleaner outlet is connected with air-introduced machine 14.Wherein flue gas cleaner plays effects such as smoke abatement, deodorizing.
Operation principle of the present utility model: mud delivers into cylinder of rotary kiln through feed arrangement, along with cylinder of rotary kiln constantly rotates, through the switch-plate effect on the cylinder of rotary kiln inwall, the spatia of mud in cylinder of rotary kiln constantly turns over, preceding sending, drying and stage casing pyrolytic gasification, finally by becoming the ash section to form lime-ash, discharge through the discharging opening deslagging device.The flue gas aspect, behind the utility model system pyrolysis mud, the flue gas that contains fuel gas that produces enters in the inner barrel from the inner barrel port by spatia, under the effect of inner barrel internal combustion machine supplemental heat source, fuel gas and harmful substance are at high temperature by completing combustion with destroy by fire, inner barrel outer wall from the port to the gas discharge outlet also heats mud, thereby reaches the purpose of UTILIZATION OF VESIDUAL HEAT IN and resource; Through purifications such as exhaust purifiers, qualified discharge is to atmosphere after treatment through the flue gas after the heat exchange.
The utlity model has following advantage:
1, it is less to be subject to some independent mud drying system disposal ability, burn usually or the pyrolysis processing disposal system be difficult to maximize, the utility model has thoroughly solved this problem;
2, system process horizontal layout compactness need not arrange independently secondary combustion chamber again after mud magnetizes pyrolysis, burning integral machine, the factory building usable floor area is little, has reduced land use area, greatly reduces investment cost;
3, the integrated mode of the compound UTILIZATION OF VESIDUAL HEAT IN of inside and outside heat has reduced the loss of heat, has improved heat utilization ratio;
4, integrated design makes system configuration rationally, concisely, and simple to operate, staffing is few, thereby reduces cost of labor and maintenance cost.
The above only is preferred embodiment of the present utility model, and all equalizations of doing according to the utility model claim change and modify, and all should belong to covering scope of the present utility model.
Claims (6)
1. a mud magnetizes pyrolysis, burning integral machine, it is characterized in that: comprise a horizontally set and have the cylinder of rotary kiln of charging and discharging mouth, be equipped with an inner barrel in the described cylinder of rotary kiln, be formed with between cylinder of rotary kiln and the inner barrel in order to mud and be sent to the spatia of discharging opening from charging aperture, described inner barrel is provided with the port of spatia and inner barrel intracavity inter-connection near the discharge port end of cylinder of rotary kiln.
2. mud magnetization pyrolysis according to claim 1, burning integral machine is characterized in that: be connected to switch-plate from charging aperture toward discharge port end with the intermittent weld of helix mode on the described cylinder of rotary kiln internal face.
3. mud according to claim 1 and 2 magnetizes pyrolysis, burning integral machine, it is characterized in that: described feed inlet end is provided with feed arrangement, described feed arrangement material-pulling device pneumatic for adopting, Driven by Hydraulic Cylinder perhaps is made of conveying worm and feed hopper.
4. mud according to claim 3 magnetizes pyrolysis, burning integral machine, it is characterized in that: described feed inlet end also is provided with magnetization active oxygen input port.
5. according to claim 1,2 or 4 described mud magnetization pyrolysis, burning integral machine, it is characterized in that: described inner barrel is provided with the combustor that stretches in the inner barrel near the discharging oral-lateral.
6. mud according to claim 5 magnetizes pyrolysis, burning integral machine, it is characterized in that: described inner barrel is connected with the flue gas cleaner import near the gas discharge outlet that the charging oral-lateral is provided with, and the flue gas cleaner outlet is connected with air-introduced machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220731861 CN203052677U (en) | 2012-12-27 | 2012-12-27 | Sludge magnetizing pyrolysis and combustion integration machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220731861 CN203052677U (en) | 2012-12-27 | 2012-12-27 | Sludge magnetizing pyrolysis and combustion integration machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203052677U true CN203052677U (en) | 2013-07-10 |
Family
ID=48735624
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220731861 Withdrawn - After Issue CN203052677U (en) | 2012-12-27 | 2012-12-27 | Sludge magnetizing pyrolysis and combustion integration machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203052677U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102997250A (en) * | 2012-12-27 | 2013-03-27 | 福建庄讯环保科技有限公司 | Sludge magnetizing pyrolysis and incineration technological process and integrated machine thereof |
| CN113970100A (en) * | 2020-07-22 | 2022-01-25 | 中冶长天国际工程有限责任公司 | Hazardous waste pyrolysis incineration system and hazardous waste pyrolysis incineration method |
-
2012
- 2012-12-27 CN CN 201220731861 patent/CN203052677U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102997250A (en) * | 2012-12-27 | 2013-03-27 | 福建庄讯环保科技有限公司 | Sludge magnetizing pyrolysis and incineration technological process and integrated machine thereof |
| WO2014101324A1 (en) * | 2012-12-27 | 2014-07-03 | Lin Xiumei | Sludge magnetic pyrolysis, exhaust gas incineration process, and integrated machine therefor |
| CN102997250B (en) * | 2012-12-27 | 2015-05-20 | 林秀梅 | Sludge magnetizing pyrolysis and incineration technological process and integrated machine thereof |
| CN113970100A (en) * | 2020-07-22 | 2022-01-25 | 中冶长天国际工程有限责任公司 | Hazardous waste pyrolysis incineration system and hazardous waste pyrolysis incineration method |
| CN113970100B (en) * | 2020-07-22 | 2023-06-23 | 中冶长天国际工程有限责任公司 | Hazardous waste pyrolysis incineration system and hazardous waste pyrolysis incineration method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102997250B (en) | Sludge magnetizing pyrolysis and incineration technological process and integrated machine thereof | |
| CN102840587B (en) | Compound method and system for directly recovering heat inside and outside rotary kiln | |
| CN105333439A (en) | Second-level high-temperature gasification incineration system for rubbish | |
| CN203052677U (en) | Sludge magnetizing pyrolysis and combustion integration machine | |
| CN101373070B (en) | Heat decomposition gas processing method and apparatus of carbonization processing system containing water | |
| CN112460598B (en) | Multi-section coupling system and process for garbage pyrolysis furnace and coal-fired boiler | |
| CN105066136A (en) | Combined incineration device for rotary furnace fire grate | |
| CN203116031U (en) | System incinerating sludge through smoke waste heat of garbage-incinerating electricity generation | |
| CN102205343B (en) | Integrated processing system for domestic waste and sewage of new countryside small cities, and integrated processing method thereof | |
| CN104501172B (en) | Organic solid waste gasification treatment device | |
| KR101613968B1 (en) | steam generating system having ultra high temperature sludge drying apparatus | |
| CN201096352Y (en) | Gas-solid mixing combustion purifying and heat distribution system | |
| CN203731462U (en) | Biomass fuel integrated cyclone combustion boiler | |
| CN205599653U (en) | Household garbage treating device and machineshop car | |
| CN106468434B (en) | Rubbish row sieves the mixed combustion pyrolysis installation of whirlwind | |
| CN203642160U (en) | Steam boiler for burning herb residues | |
| CN203869051U (en) | Wet-type short-flue high-pressure air inducing incinerator | |
| CN103121786B (en) | Integrated condensation dehydration and waste heat utilization sludge treatment device and technological process | |
| CN108036327B (en) | Small-size energy-conserving high-efficient domestic waste incineration disposal system | |
| CN219140779U (en) | System for cement kiln is handled solid waste in coordination | |
| CN110779019A (en) | Domestic waste anaerobic sectional type pyrolysis furnace | |
| CN205174375U (en) | Small -size domestic waste incineration disposal system | |
| CN110822448A (en) | Sludge blending combustion system for dry-type slag extractor | |
| CN104006389A (en) | Rubbish thermal decomposition and gasification incineration method and system | |
| CN219607103U (en) | Integrated smoke-free environment-friendly boiler for waste incineration continuous kiln |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: LIN JIANNAN Effective date: 20130822 Owner name: LIN XIUMEI Free format text: FORMER OWNER: FUJIAN ZONSEN ENVIRONMENTAL TECHNOLOGY CO., LTD. Effective date: 20130822 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20130822 Address after: 350003, 4 floor, No. 1, 5 environmental protection road, Gulou District, Fujian, Fuzhou, 401 Patentee after: Lin Xiumei Patentee after: Lin Jiannan Address before: 350003, 4 floor, No. 1, 5 environmental protection road, Gulou District, Fujian, Fuzhou, 401 Patentee before: Fujian Zonsen Environmental Protection Technology Co., Ltd. |
|
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Fujian Zonsen Environmental Protection Technology Co., Ltd. Assignor: Lin Xiumei| Lin Jiannan Contract record no.: 2014350000084 Denomination of utility model: Sludge magnetizing pyrolysis and combustion integration machine Granted publication date: 20130710 License type: Exclusive License Record date: 20140715 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20130710 Effective date of abandoning: 20150520 |
|
| RGAV | Abandon patent right to avoid regrant |