CN101618954A - Process system for processing municipal domestic waste by cement rotary kiln - Google Patents
Process system for processing municipal domestic waste by cement rotary kiln Download PDFInfo
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- CN101618954A CN101618954A CN200910065584A CN200910065584A CN101618954A CN 101618954 A CN101618954 A CN 101618954A CN 200910065584 A CN200910065584 A CN 200910065584A CN 200910065584 A CN200910065584 A CN 200910065584A CN 101618954 A CN101618954 A CN 101618954A
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- 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
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- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
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Abstract
The invention relates to a process system for processing municipal domestic waste by a cement rotary kiln. The domestic waste is processed by the following steps: manually separating, pre-dewatering and shattering the domestic waste; drying and burning the shattered domestic waste by an auxiliary burning furnace; enabling generated waste gas and released heat to enter a preheat decomposing system of the cement rotary kiln; and finishing the drying, preheating and partial burning functions of cement raw material, wherein burning ash enters the cement rotary kiln by a cement-decomposing kiln as a raw material to produce cement clinker. The invention fully utilizes facilities and places of the prior cement plants to save investments, processes harmful gas, does not need fuel consumption and has low processing cost and great handling capacity because of a high heat value of organic matter in the waste, solves the problem of secondary pollution, saves natural resources and non-renewable energy and reduces the influence of the waste on a burning system to the minimum.
Description
Technical field
The present invention relates to a kind of treatment of urban garbage technology, particularly relate to the process system that a kind of cement rotary kiln is handled domestic waste.
Background technology
How handling increasing domestic waste has become a great research topic of the world today.The traditional way that China handles domestic waste is a landfill method, and this method relatively is fit to a spot of domestic refuse in small city.The disadvantage of landfill is to take the land resources of a large amount of preciousnesses, and the refuse treatment cycle is long, causes percolate and volatilization gas polluted underground water, air and soil etc. easily.More novel processing mode is the burning electricity generation method, has that land occupation is few, the processing cycle is short, can realize significantly subtracting advantages such as appearance, recoverable energy.But waste incineration and generating electricity method treating refuse cost height is easy to generate toxic gas, and the disposal of the rubbish ash that produces after burning also is a very problem of trouble.External commonplace is to dispose domestic waste in Cement industry at present, and the inorganic components in the rubbish is as the raw material of producing cement, and organic composition can be used as secondary fuel.So both protect environment, saved resource again, had lot of advantages.Utilize domestic waste to produce cement, also should become our following main developing direction.
But the rubbish of China and external rubbish have very big difference on composition and collection mode, it is infeasible to indiscriminately imitate external method fully.The domestic city domestic refuse can not provide continual and steady energy for combustion processes because moisture height, calorific value are low, need to consume a large amount of auxiliary fuels, and these moisture enters the cement kiln preheating decomposition system with incineration flue gas, causes system jams easily; Domestic refuse complicated component, fluctuating range are big, cause the instability of firing system, and the part objectionable impurities is mingled in the incineration residue after burning, and also bring difficulty for the processing of incineration residue, and can produce harmful poisonous gas in burning; The size of rubbish differs, and brings disadvantageous effect to burning, saturating phenomenon occurs easily burning, and also can contain the very big particle of size in the incineration residue, enters the production that can influence cement clinker after the cement kiln system.Therefore, press for and work out the waste disposal method that is fit to a kind of China's actual conditions, reach the purpose of effective treating refuse.
Summary of the invention
Technical problem to be solved by this invention provides the process system that a kind of cement rotary kiln is handled domestic waste, solve the technical problem that faces in the garbage treatment process, particularly adopt some pretreatment technology and auxiliary mode of burning, reduce rubbish and drop into behind the cement kiln influence to cement clinker output and quality.
In order to reach the purpose that solves the problems of the technologies described above, the present invention has adopted following technical scheme:
A kind of cement kiln of the present invention is handled the domestic waste process system, comprising:
---the manual sorting, carry out the manual sorting with domestic waste and separate and to be not suitable for burning and residue is not suitable for the article of cement; Can be at transfer point through the manual sorting, sort out materials such as waste household appliances, furniture, concrete, iron and other metals of big part wherein and chloride PVC plastics, cable waste, rubbish after the letter sorting is transported to the cement mill with cram packer, also can sorts in the cement mill;
---pre-dehydration, domestic waste is dewatered, reach the reduction refuse moisture, increase the purpose of refuse thermal value; Dewatering can compress dehydration to domestic waste with the compression water extracter, also can use other effective ways, and technologies such as for example centrifuge dehydration, broken back leakage dehydration are dewatered;
---break process, the domestic waste after the dehydration is carried out break process, reduce the rubbish particle diameter, increase specific surface area, be convenient to burnout; Rubbish after breaking method can be to use reciprocating type shear breaker to dehydration carries out shearing-crushing, also can use other fragmentation or breaking method;
---auxiliary incinerator burns, to drying and burn through the domestic waste of dehydration, break process, cinder from refuse incineration enters the cement kiln system as raw material for producing cement chamotte by decomposing furnace, waste gas that waste incineration produces and the heat that discharges can enter the pre-heating system of cement kiln tail, finish oven dry, preheating and the part of cement slurry and burn.
What add incinerator in the cement producing line is feasible.At first, the equipment in the general cement firing system all has 15～20% scale-up factor in design, so that improve production line output.With the 5000t/d production line is example, the tertiary air total blast volume is the rich amount of hot blast that 450,000 m3/h (850 ℃) wherein have 70,000 m3/h, want preheating, oven dry to handle the domestic waste of 10t/h, probably need 5.7 ten thousand steres air quantity hourly, so original system can satisfy this system requirements; Secondly, in the cement precalcining system, the negative pressure in the tertiary-air pipe is-900Pa, and in three grades, level Four waste pipe its pressure at-3500Pa, maximum can reach-5000～-6000Pa, can guarantee the mobile unobstructed of flue gas.
Domestic waste amount of Chu Liing and needed exhaust gas volumn as required, the relevant parameter of design various device.For example, can design selection the physical dimension of auxiliary incinerator be Φ 4 * 16m, inlet/outlet pipe is Φ 2m, the cindery caliber of turnover material is Φ 800m.
The invention has the beneficial effects as follows: the present invention will be sent to the auxiliary incinerator of newly-designed rubbish through pretreated rubbish and burn, and then drop into cement kiln and produce cement clinker, thereby make domestic refuse obtain good treatment; Make full use of existing cement mill facility and place, reduced investment; The waste gas that waste incineration produces enters the cement pre-heating system, and obnoxious flavour obtains handling, and does not need newly-built emission-control equipment; Organism contains higher calorific value in the rubbish, and burning does not need to increase fuel consumption, and processing cost is low, and treatment capacity is big; Incinerator ash enters cement kiln at last as raw material production cement, has solved the secondary pollution problem; Natural resources and Nonrenewable energy resources have been saved; Rubbish through pre-treatment and auxiliary the burning after, the influence of firing system is dropped to minimum, reduce influence to cement clinker output and quality; Farthest realized " innoxious, minimizing, the resource utilization " of domestic waste.
Description of drawings
Fig. 1 is the domestic waste pretreatment technology schema of the embodiment of the invention.
Wherein: 1. cram packer, 2. rubbish stockyard, 3. grab bucket, 4. rubbish compression water extracter, 5. rotary conveyor, 6. threeway discharge valve, 7. reciprocating type shear breaker, 8. high angle belt conveyer machine, 9. leachate collection pond, 10. sump pump, 20. pretreated rubbish.
Fig. 2 is the auxiliary incineration process flow figure of the domestic waste of the embodiment of the invention.
Wherein: 11. high angle belt conveyer machines, 12. surge bunkers, 13. double-deck turnover panel lock feeding valves, 14. rubbish are assisted incinerator, 15. lock feeding valves, 16. bucket elevators, 17. decomposing furnace exhaust pipelines, 18. decomposing furnaces, 19. tertiary airs, 20. pretreated rubbish.
Fig. 3 is the auxiliary structural plan of incineration system in cement producing line of kiln tail that the present invention designs.
Wherein: 21. cloth grate plates, 22. air bubbles, 23. blanking pipelines, 24. blast pipes, 25. control gate valves, 31. one-level whirlwind tubes, 32. secondary whirlwind tubes, 33. 3 grades of whirlwind tubes, 34. Category Four cyclone tubes, 35. five-stage whirlwind tubes.
Fig. 4 is the sectional view of the auxiliary incineration system of the kiln tail that designs of the present invention.
Wherein: 26. preheating decomposition systems, 27. auxiliary incineration systems, 28. blanking pipelines, 29. exhaust pipelines, 30. burn exhaust pipeline, 33. 3 grades of whirlwind tubes, 34. Category Four cyclone tubes, 35. five-stage whirlwind tubes.
Embodiment
Specify the specific embodiment of the present invention below in conjunction with accompanying drawing, but the content that is not limited to enumerate in the embodiment.
A kind of cement rotary kiln of the present invention is handled the process system of domestic waste, the domestic refuse that manual sorting's process at first will disperse to collect is transported to transfer point, rubbish is transfer point process manual sorting, sort out waste household appliances, furniture, concrete, iron and other metals and the materials such as chloride PVC plastics, cable waste of big part wherein, the rubbish after the letter sorting is transported to the cement mill with cram packer.
Rubbish after the letter sorting at first will dewater in the cement mill and pre-treatment such as fragmentation.As shown in Figure 1, after cram packer enters factory, carry out weighing through the cement mill weighbridge earlier, the rubbish discharging platform is sailed in weighing cram packer 1 later into, and rubbish is discharged into rubbish stockyard 2.Control grab bucket 3 by the grab bucket watch-keeping cubicle rubbish put into trash compactor 4, rubbish compresses dehydration in compressor.Domestic refuse is after overdraft dehydration, and water ratio generally can be reduced to about 20% from 50%, and thermal value improves greatly.Rubbish after the dehydration is carried through rotary conveyor 5, enters reciprocating type shear breaker 7 by threeway discharge valve 6, carries out shearing-crushing work, reduces the particle diameter of rubbish.The shearing force of shear crusher utilization machinery is thick rubbish splitting and cut off, and increases the rubbish specific surface area, reduces particle diameter, improves the stability and the efficient of operations such as burning, thermolysis.The percolate in moisture that rubbish compresses out and rubbish stockyard enters leachate collection pond 9 together, after the capacity of collecting tank acquires a certain degree, by sump pump 10 percolate is squeezed into special sewage transport trolley and delivers to sewage work and handle.
Rubbish through dehydration and pre-treatment such as fragmentation after, enter auxiliary incineration system 27 and carry out burning disposal, the technical process that rubbish is assisted burning as shown in Figure 2.Delivered in high about 50 meters surge bunker 12 by high angle belt conveyer machine 11 through pretreated domestic waste 20, rubbish 20 evenly enters in the auxiliary incinerator 14 of domestic waste through double-deck turnover panel lock feeding valve 13 again.Domestic refuse 20 assists incinerator 14 to carry out sufficient heat exchange with the tertiary air 19 of tertiary-air pipe at rubbish, and rubbish is at first by hot-air seasoning, and the organic compound combustion in the rubbish decomposes, and discharges heat.Through after fully burning, wherein noncombustibles matter forms incineration residue to domestic refuse in incinerator, discharges incinerator by lock wind discharge valve 15.Enter in the auxiliary incinerator 14 through 25 fens two-way of control gate valve from the tertiary air in the tertiary-air pipe 19, carrying out heat exchange with material, finishing oven dry, preheating and the part of domestic refuse burns, send in the decomposing furnace exhaust pipeline 17 of kiln tail pre-heating system through gas exhaust duct, finish oven dry, preheating and the part of cement slurry again and burn function.On the in/out air tube road, also be provided with control gate valve 25, can split assisting incineration system to separate separately in case of necessity, and do not influence the normal operation of whole cement preheating decomposition system.Fig. 3 has shown the structural arrangement of auxiliary incineration system at cement producing line.Fig. 4 has shown the section layout drawing of auxiliary incineration system 27 in the preheating decomposition system 26 of cement kiln.
Handle the back domestic waste through auxiliary incineration system and become incineration residue, incineration residue is that bucket elevator 16 is sent in the decomposing furnace 18 in the cement precalcining system by handling equipment among Fig. 2, burn once more and decompose, enter cement kiln with raw material at last.Because the composition of waste incineration ash composition and clay is very close, therefore the part as cement raw material participates in firing of cement clinker.In the total system of the present invention's design, domestic waste has finally been realized the processing target of " innoxious, minimizing, resource utilization " basically.
For making material carry out heat exchange fully with hot blast in stove, which floor cloth grate plate 21 design has in the stove.According to coming material granularity and moisture situation, the comb hole dimension of cloth grate plate 21 varies in size.Cloth grate plate 21 is designed to the positive cone and the back taper of different angles, to enlarge heat exchange area and to prolong the residence time of material in stove.For the hot blast that makes equipment can adapt to 800 ℃～900 ℃ passes through, the grate plate material will be used high temperature steel, and the stove inner barrel also will have been built certain thickness refractory materials by laying bricks or stones and protected.In addition, for prevent material by the time with the comb hole plug, be provided with several air bubbles 22 at the different sites of body of heater, regularly or not timing suitably clear up.
A lock feeding valve 15 is set in the blanking pipeline 23, under the condition that guarantees tight lock wind, the material smoothness is fed in the stove equably, it is also like this to discharge cindery process.For guaranteeing that this system can the relatively independent works better that does not influence the firing system of cement, all establish control gate valve 25 in the blast pipe 24, controllable adjustable air intake and disconnect air intake at any time.
Fig. 4 has shown the section layout drawing of auxiliary incineration system 27 in the preheating decomposition system 26 of cement kiln.The waste gas that incinerator is discharged has two scheme arrangement: one, waste gas are delivered in the highly close decomposing furnace exhaust pipeline 17, and objectionable impurities can continue pyrolytic decomposition in decomposing furnace 18 in the waste gas, and the flying dust in the waste gas can further reclaim through whirlwind tube 31～35.Weak point is that the moisture of institute's carburation by evaporation also enters into preheating decomposition system 26 in the waste gas, may exert an influence to the heat exchange of raw material or because of the increase of moisture makes green powder attached on the tube wall, causes system's blanking pipeline 28 to stop up; Its two, lengthening burns exhaust pipeline 30, waste gas is directly guided in the exhaust pipeline 29 of one-level whirlwind tube 31 outlets, is discharged in the preheating decomposition system 27 by high-temperature blower, eliminates the disadvantageous effect of refuse moisture to precalcining system; Weak point is that flying dust in the waste gas and objectionable constituent reclaim and finished by the flare system of original production line, can cause the increase of ash amount, exhaust gas constituents complexity.Can adopt the scheme that relatively is fit to as the case may be.
Claims (2)
1, a kind of cement rotary kiln is handled the process system of domestic waste, it is characterized in that: cement kiln is handled the domestic waste process system and is comprised following process:
---the manual sorting, domestic waste is carried out the manual sorting, isolating is not suitable for burning is not suitable for producing the article of cement clinker with residue;
---pre-dehydration, domestic waste is dewatered, reach the reduction refuse moisture, increase the purpose of refuse thermal value;
---break process, the domestic waste after the dehydration is carried out break process, reduce the rubbish particle diameter, increase specific surface area;
---auxiliary incinerator (14) burns, to drying and burn through the domestic waste (20) of dehydration, break process, cinder from refuse incineration enters the cement kiln system as raw material for producing cement chamotte by decomposing furnace (18), waste gas that waste incineration produces and the heat that discharges can enter the preheating decomposition system (26) of cement kiln tail, finish oven dry, preheating and the part of cement slurry and burn.
2, handle the process system of domestic waste according to the described a kind of cement rotary kiln of claim 1, it is characterized in that: the rubbish after described break process method is to use reciprocating type shear breaker (7) to dehydration carries out shearing-crushing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN200910065584XA CN101618954B (en) | 2009-07-20 | 2009-07-20 | Process for processing municipal domestic waste by cement rotary kiln |
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| CN200910065584XA CN101618954B (en) | 2009-07-20 | 2009-07-20 | Process for processing municipal domestic waste by cement rotary kiln |
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| CN101618954A true CN101618954A (en) | 2010-01-06 |
| CN101618954B CN101618954B (en) | 2012-01-25 |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101793402A (en) * | 2010-03-25 | 2010-08-04 | 天津水泥工业设计研究院有限公司 | Method for processing domestic garbage riddlings and/or solid combustible wastes in cement kiln |
| CN102070308A (en) * | 2010-12-01 | 2011-05-25 | 中信重工机械股份有限公司 | Device technology configuration method for treating house refuses by using rotary cement kiln |
| CN103113030A (en) * | 2013-03-05 | 2013-05-22 | 郭文龙 | Method for treating household garbage by absorbing heat energy through raw meal nodules |
| CN103341300A (en) * | 2013-07-23 | 2013-10-09 | 郭涵 | Method for purifying waste incineration smoke by using novel dry process raw material vertical mill |
| CN101761928B (en) * | 2010-01-11 | 2014-01-15 | 中信重工机械股份有限公司 | Incineration treatment method for domestic refuse |
| CN104496134A (en) * | 2014-12-19 | 2015-04-08 | 北京金隅股份有限公司 | Method for treating sludge by using cement kiln, and cement kiln system for treating sludge |
| CN105669057A (en) * | 2016-01-15 | 2016-06-15 | 浙江环立环保科技有限公司 | Waste bag and active carbon treatment method |
| CN106871126A (en) * | 2017-01-04 | 2017-06-20 | 长沙汇聚环境技术有限公司 | A kind of processing method of house refuse low-temperature carbonization innoxious burning |
| CN106966618A (en) * | 2017-02-27 | 2017-07-21 | 西南科技大学 | A kind of method of cement kiln synergic processing house refuse |
| CN109731891A (en) * | 2019-03-06 | 2019-05-10 | 石磊 | A kind of refund up and down turns garbage dewatering device |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1313256A (en) * | 2000-03-15 | 2001-09-19 | 上海水泥厂 | Ecological cement prepared from industrial and city wastes |
| CN100548517C (en) * | 2006-06-22 | 2009-10-14 | 浙江大学 | A kind of comprehensive processing technique of domestic waste |
-
2009
- 2009-07-20 CN CN200910065584XA patent/CN101618954B/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101761928B (en) * | 2010-01-11 | 2014-01-15 | 中信重工机械股份有限公司 | Incineration treatment method for domestic refuse |
| CN101793402A (en) * | 2010-03-25 | 2010-08-04 | 天津水泥工业设计研究院有限公司 | Method for processing domestic garbage riddlings and/or solid combustible wastes in cement kiln |
| CN102070308A (en) * | 2010-12-01 | 2011-05-25 | 中信重工机械股份有限公司 | Device technology configuration method for treating house refuses by using rotary cement kiln |
| CN103113030A (en) * | 2013-03-05 | 2013-05-22 | 郭文龙 | Method for treating household garbage by absorbing heat energy through raw meal nodules |
| CN103341300A (en) * | 2013-07-23 | 2013-10-09 | 郭涵 | Method for purifying waste incineration smoke by using novel dry process raw material vertical mill |
| CN104496134A (en) * | 2014-12-19 | 2015-04-08 | 北京金隅股份有限公司 | Method for treating sludge by using cement kiln, and cement kiln system for treating sludge |
| CN105669057A (en) * | 2016-01-15 | 2016-06-15 | 浙江环立环保科技有限公司 | Waste bag and active carbon treatment method |
| CN106871126A (en) * | 2017-01-04 | 2017-06-20 | 长沙汇聚环境技术有限公司 | A kind of processing method of house refuse low-temperature carbonization innoxious burning |
| CN106966618A (en) * | 2017-02-27 | 2017-07-21 | 西南科技大学 | A kind of method of cement kiln synergic processing house refuse |
| CN109731891A (en) * | 2019-03-06 | 2019-05-10 | 石磊 | A kind of refund up and down turns garbage dewatering device |
| CN109731891B (en) * | 2019-03-06 | 2023-09-12 | 石磊 | Up-down rotary garbage dewatering device |
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| CN101618954B (en) | 2012-01-25 |
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