CN204084385U - A kind of pretreatment system utilizing cement rotary kiln to carry out waste incineration - Google Patents
A kind of pretreatment system utilizing cement rotary kiln to carry out waste incineration Download PDFInfo
- Publication number
- CN204084385U CN204084385U CN201420558191.9U CN201420558191U CN204084385U CN 204084385 U CN204084385 U CN 204084385U CN 201420558191 U CN201420558191 U CN 201420558191U CN 204084385 U CN204084385 U CN 204084385U
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- China
- Prior art keywords
- machine
- rotary kiln
- cement rotary
- waste incineration
- carry out
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- 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.)
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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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
Abstract
The utility model discloses a kind of pretreatment system utilizing cement rotary kiln to carry out waste incineration, comprise the weighing unit, bag breaker, elementary drying machine, one-level screening machine, secondary screening machine and the divisional processing system that connect successively; Described divisional processing system comprises treatment system A and treatment system B; Described treatment system A comprises the picking device be connected with one-level screening machine and the cutting machine be connected with picking device, cutting mill, disintegrating machine and magnetic separator A; Described treatment system B comprises the winnowing machine, pulverizer and the drying machine that is connected with pulverizer that are connected with secondary screening machine.The utility model carries out pretreatment to the rubbish utilizing cement rotary kiln to burn, and rubbish is at utmost recycled and the rubbish burned is the combustible of low water content, high heating value, and resource recovery is high, economize energy, clean environment firendly, system stability.
Description
Technical field
The utility model relates to burning city domestic garbage preprocessing technical field, specifically refers to a kind of pretreatment system utilizing cement rotary kiln to carry out waste incineration.
Background technology
The fast development of urbanization, causes the increase rapidly of domestic waste total amount, and adopt cement rotary kiln to burn away the refuse, gas can be recycled, and slag body can be used as the raw material producing cement; And cement rotary kiln burn wide adaptability, furnace type structure is simple, fault is few, can long-time continuous run.
But China's domestic waste mainly contains kitchen excess, stationery, vegetation class, Plastic, rubber-like, metal species, sandstone class etc., do not classify when collecting, so complicated component, size differ, water content is high, when utilizing rotary kiln to burn, easily cause the wasting of resources, the thermal efficiency low, burn insufficient, produce the situations such as pernicious gas such as bioxin.For overcoming the above problems, and improving the recovery utilization rate of dissimilar rubbish, needing to arrange a set of pretreatment system before utilizing cement rotary furnace to carry out waste incineration, Rational Classification is carried out to rubbish and effectively controls water content.
Utility model content
The purpose of this utility model is to provide that a kind of resource recovery is high, energy utilization rate is high, the cement rotary kiln that utilizes of clean environment firendly carries out the pretreatment system of waste incineration, and this system architecture is compact, and equipment is simple, can long-time continuous run.
The utility model is achieved through the following technical solutions: a kind of pretreatment system utilizing cement rotary kiln to carry out waste incineration, comprises the weighing unit, bag breaker, elementary drying machine, one-level screening machine, secondary screening machine and the divisional processing system that connect successively; Described divisional processing system comprises treatment system A and treatment system B; Described treatment system A comprises the picking device be connected with one-level screening machine and the cutting machine be connected with picking device, cutting mill, disintegrating machine, magnetic separator A; Described treatment system B comprises the winnowing machine, pulverizer and the drying machine that is connected with pulverizer that are connected with secondary screening machine;
Domestic waste is discharged into bag breaker bale broken on weighing unit, the rubbish of dispersion is transported to screening machine after elementary drying machine drying, classify by the particle size of article, enter divisional processing system: particle diameter large article is classified by artificial hand selection, plastics, rubber enter cutting machine cutting, paper, woodwork enter cutting mill and pulverize, category of glass goods enter disintegrating machine and pulverize, metallic article enters magnetic separator and is separated by magnetic metal, all sorted rubbish enters corresponding collection box, waits pending; The article that particle diameter is less enter in corresponding winnowing machine after the screening of secondary screening machine, the kitchen waste compost process that selection by winnowing goes out, metal, sandstone enter magnetic separator and are separated by magnetic metal, and the flammable lightweight things such as paper, plastics, textile wait for that after pulverizer pulverizing, drying machine drying entering rotary kiln burns.
Because the operation principles such as the drying machine in system, screening machine, cutting machine, disintegrating machine, pulverizer, winnowing machine, magnetic separator all belong to techniques well known, and improvement of the present utility model does not lie in the said equipment, therefore repeat no more respective structure and operation principle.
Further, the top distribution spray equipment of described bag breaker inside, two sides arrange conical tooth to inwall, and inwall is fixed with axle between both sides, axle are arranged the thin tooth of gear shape.
Rubbish enters bag breaker, bale broken and spray course synchronization: refuse bag is bored after tooth or the thin tooth of gear type tear, and rubbish scatter, and the spray equipment of bag breaker inner tip continues to spray fungicidal wash downwards, plays the effect of control dust, sterilizing.
Further, described treatment system B comprises at least one winnowing machine.Winnowing machine quantity is preferably two, winnowing machine A and winnowing machine B; Described winnowing machine A and winnowing machine B is in parallel.
Because the operation principle of winnowing machine requires that article particle diameter is close, according to article gravity, heavy thing, lightweight thing effectively could be separated, so through the sorting of secondary screening machine, according to particle size range by article delivery in the winnowing machine of correspondence.In native system, the article of particle diameter 30-200mm enter in winnowing machine A, and the article that particle diameter is less than 30mm enter in winnowing machine B.In treatment system B, the function of winnowing machine is identical, is only configured according to the scope of article particle diameter and the running parameter of winnowing machine, so the arrangement mode of pneumatic separation device is in parallel, quantity adjusts according to actual conditions.
Further, connect with pipeline between described equipment, in pipeline, be provided with conveyer belt.
Be the routine techniques in this area due to pipeline and conveyer belt, and improvement of the present utility model does not lie in this, and those skilled in the art can draw setting and the course of work of pipeline and conveyer belt by basic general knowledge yet, therefore it not illustrated in detail.
Further, ventilation unit, dust arrester is also comprised.
Because the operation principles such as the ventilation unit in system, dust arrester all belong to techniques well known, and improvement of the present utility model does not lie in the said equipment, therefore repeats no more respective structure and operation principle.
Further, described drying machine B is preferably pneumatic drier, and drying machine B bottom sets into gas port, and drying machine B top sets out gas port.
The utility model compared with prior art, has the following advantages and beneficial effect:
(1) refuse classification control water content, making to enter the rubbish that cement rotary kiln burns is the small particle diameter combustible that water content is lower, has not only ensured the stability of burning but also the calorific value improving burning, thus has reduced the use of postcombustion, economize energy, reduces costs; Meanwhile, the generation controlling the pernicious gases such as bioxin is beneficial to, clean environment firendly.
(2) system layout is reasonable, farthest improves the recycling of all kinds of rubbish.
(3) whole system compact conformation, floor space is little, and equipment composition is simple, is convenient to adjustment and maintenance, can long-time continuous run.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the internal structure schematic diagram of bag breaker.
Wherein: 1-spray equipment, 2-conical tooth, the thin tooth of 3-gear shape, 4-axle.
Detailed description of the invention
Below in conjunction with embodiment, the utility model is described in further detail, but embodiment of the present utility model is not limited thereto.
Embodiment 1:
The utility model is a kind of pretreatment system utilizing cement rotary kiln to carry out waste incineration, as shown in Figure 1, rubbish is discharged in bag breaker from weighing unit, refuse bag is bored after tooth or the thin tooth of gear type tear, rubbish scatter, elementary drying machine is entered by the conveyer belt in pipeline, be transported to one-level screening machine after simple dehydration drying again and carry out one-level screening, the large piece article that particle diameter is greater than 200mm enters treatment system A, is transported to picking device and carries out artificial separation: plastics, rubber are deposited to collection box A after entering cutting machine cutting; Paper, woodwork enter after cutting mill is pulverized to be deposited to collection box B; Category of glass goods enter after disintegrating machine is pulverized to be deposited to collection box C; After metal species goods enter magnetic separator A, magnetic metal is deposited to collection box D, and nonmagnetic metal is deposited to collection box E; Sandstone, brick and tile etc. are deposited to collection box F; Dangerous material, poisonous and harmful article are deposited to collection box G; Other article storages are to collection box Z.The rubbish that particle diameter is less than 200mm is transported to secondary screening machine from one-level screening machine and carries out secondary screening, and enter treatment system B, particle diameter is that the article delivery of 30-200mm is to sorting again in winnowing machine A; The small article that particle diameter is less than 30mm is delivered to sorting again in winnowing machine B: the organic matters such as kitchen excess are deposited to collection box H compost treatment after Anaerobic Digestion; After metal, sandstone etc. enter magnetic separator B, magnetic metal is deposited to collection box D, and nonmagnetic metal is deposited to collection box E, and sandstone etc. are deposited to collection box F; Made of paper, the lightweight combustible such as plastics, textile is ground into through pulverizer the small particle diameter material that particle diameter is less than 30mm, is delivered to rotary kiln again and carries out burning disposal after refuse moisture being controlled to 15%-25% by drying machine.
Embodiment 2:
The utility model sets up spray equipment 1 in bag-breaking machine, rubbish is discharged in bag breaker from weighing unit, spray process and bale broken process are carried out simultaneously, refuse bag is bored after tooth or the thin tooth of gear type tear, rubbish scatter, the spraying disinfectant of bag breaker upper end spray equipment 1 consistent, floating dust diffusion in minimizing bale broken process also carries out sterilizing to the rubbish of dispersion, and the rubbish after dispersion sterilization enters the drying of elementary drying machine simple dehydration by the conveyer belt in pipeline.Other parts of the present embodiment are identical with embodiment 1, therefore repeat no more.
The above; it is only preferred embodiment of the present utility model; not do any pro forma restriction to the utility model, every any simple modification, equivalent variations done above embodiment according to technical spirit of the present utility model, all falls within protection domain of the present utility model.
Claims (7)
1. utilize cement rotary kiln to carry out a pretreatment system for waste incineration, it is characterized in that: comprise the weighing unit, bag breaker, elementary drying machine, one-level screening machine, secondary screening machine and the divisional processing system that connect successively; Described divisional processing system comprises treatment system A and treatment system B; Described treatment system A comprises the picking device be connected with one-level screening machine and the cutting machine be connected with picking device, cutting mill, disintegrating machine, magnetic separator A; Described treatment system B comprises the winnowing machine, pulverizer and the drying machine that is connected with pulverizer that are connected with secondary screening machine.
2. the pretreatment system utilizing cement rotary kiln to carry out waste incineration according to claim 1, it is characterized in that: top distribution spray equipment (1) of described bag breaker inside, inwall two sides are arranged conical tooth (2), be fixed with axle (4) between inwall both sides, axle (4) arranged the thin tooth of gear shape (3).
3. the pretreatment system utilizing cement rotary kiln to carry out waste incineration according to claim 1, is characterized in that: described treatment system B comprises at least one winnowing machine.
4. the cement rotary kiln that utilizes according to claim 1 or 3 carries out the pretreatment system of waste incineration, it is characterized in that: described winnowing machine quantity is two, winnowing machine A and winnowing machine B; Described winnowing machine A and winnowing machine B is in parallel.
5. the pretreatment system utilizing cement rotary kiln to carry out waste incineration according to claim 1, is characterized in that: connect with pipeline between described equipment, be provided with conveyer belt in pipeline.
6. utilize cement rotary kiln to carry out the pretreatment system of waste incineration according to claim 1 or 5, it is characterized in that: also comprise ventilation unit, dust arrester.
7. the pretreatment system utilizing cement rotary kiln to carry out waste incineration according to claim 1, is characterized in that: described drying machine is pneumatic drier, and drying machine bottom sets into gas port, and drying machine top sets out gas port.
Priority Applications (1)
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CN201420558191.9U CN204084385U (en) | 2014-09-26 | 2014-09-26 | A kind of pretreatment system utilizing cement rotary kiln to carry out waste incineration |
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CN201420558191.9U CN204084385U (en) | 2014-09-26 | 2014-09-26 | A kind of pretreatment system utilizing cement rotary kiln to carry out waste incineration |
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CN204084385U true CN204084385U (en) | 2015-01-07 |
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CN201420558191.9U Expired - Fee Related CN204084385U (en) | 2014-09-26 | 2014-09-26 | A kind of pretreatment system utilizing cement rotary kiln to carry out waste incineration |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107796007A (en) * | 2017-10-26 | 2018-03-13 | 杜荷昌 | It is a kind of that rubbish is produced into waste gas progress combustion power generation equipment |
CN112207115A (en) * | 2020-09-22 | 2021-01-12 | 武汉科技大学 | Process for cooperatively treating medical waste by utilizing low-temperature pyrolysis dechlorination upgrading coupling cement kiln of hot flue gas |
CN112592219A (en) * | 2020-12-28 | 2021-04-02 | 华中科技大学 | Aerobic composting system |
-
2014
- 2014-09-26 CN CN201420558191.9U patent/CN204084385U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107796007A (en) * | 2017-10-26 | 2018-03-13 | 杜荷昌 | It is a kind of that rubbish is produced into waste gas progress combustion power generation equipment |
CN112207115A (en) * | 2020-09-22 | 2021-01-12 | 武汉科技大学 | Process for cooperatively treating medical waste by utilizing low-temperature pyrolysis dechlorination upgrading coupling cement kiln of hot flue gas |
CN112592219A (en) * | 2020-12-28 | 2021-04-02 | 华中科技大学 | Aerobic composting system |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150107 Termination date: 20190926 |
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CF01 | Termination of patent right due to non-payment of annual fee |