WO2017035924A1 - Device for integrating bag-breaking, screening and drying of household waste - Google Patents
Device for integrating bag-breaking, screening and drying of household waste Download PDFInfo
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- WO2017035924A1 WO2017035924A1 PCT/CN2015/092062 CN2015092062W WO2017035924A1 WO 2017035924 A1 WO2017035924 A1 WO 2017035924A1 CN 2015092062 W CN2015092062 W CN 2015092062W WO 2017035924 A1 WO2017035924 A1 WO 2017035924A1
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- screening
- drum
- drying
- bag
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- 238000012216 screening Methods 0.000 title claims abstract description 72
- 238000001035 drying Methods 0.000 title claims abstract description 42
- 239000010791 domestic waste Substances 0.000 title claims abstract description 12
- 238000007599 discharging Methods 0.000 claims abstract description 19
- 239000002699 waste material Substances 0.000 claims abstract description 10
- 239000010813 municipal solid waste Substances 0.000 claims description 61
- 238000005520 cutting process Methods 0.000 claims description 6
- 230000002093 peripheral effect Effects 0.000 claims description 6
- 238000009434 installation Methods 0.000 claims description 4
- 239000003638 chemical reducing agent Substances 0.000 claims description 3
- 230000003014 reinforcing effect Effects 0.000 claims description 3
- 238000005096 rolling process Methods 0.000 claims description 3
- 238000007873 sieving Methods 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims 1
- 238000002309 gasification Methods 0.000 abstract description 28
- 239000000463 material Substances 0.000 description 32
- 238000000034 method Methods 0.000 description 25
- 238000002485 combustion reaction Methods 0.000 description 13
- 239000007789 gas Substances 0.000 description 13
- 238000005516 engineering process Methods 0.000 description 9
- 239000002028 Biomass Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000011521 glass Substances 0.000 description 5
- 239000005416 organic matter Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000003546 flue gas Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000002956 ash Substances 0.000 description 3
- 239000011449 brick Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- -1 clothing Substances 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 229910010272 inorganic material Inorganic materials 0.000 description 2
- 239000011147 inorganic material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000010883 coal ash Substances 0.000 description 1
- 238000001599 direct drying Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000010806 kitchen waste Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/18—Drum screens
- B07B1/22—Revolving drums
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
Definitions
- the invention relates to the technical field of garbage disposal, in particular to a drum type device which is integrated with the domestic garbage gasification technology and which is used for breaking, sieving and drying the domestic garbage.
- Domestic garbage sorting is the separation of materials that can be recycled or used in the process of subsequent disposal. It is one of the important links and important operations in the garbage disposal project. Domestic garbage should be considered for technical, practical and economical while sorting and drying.
- the first method is to perform manual primary selection directly, followed by screening and manual sorting. This is a relatively low-level treatment method that is a relatively simple garbage sorting process in waste treatment plants.
- the second method is to first break the bagged garbage, and then perform screening and manual sorting.
- This method mainly refers to the garbage disposal of equipment in developed countries such as Europe and America. Foreign domestic garbage is collected in classified bags, while domestic garbage is collected in mixed bags. Therefore, the domestic garbage disposal method is not suitable for China's national conditions.
- the third way is to selectively break and sort the bulk materials in the garbage while the bagged garbage is broken, and then perform screening and manual sorting.
- Domestic garbage is mainly composed of perishable organic matter, coal ash, silt, pebbles, broken bricks, broken glass, waste plastics, clothing, paper, etc.
- the garbage has high water content and complex composition, and the structure changes greatly. It is extremely uneven, unlike the domestic garbage in Europe and America (the domestic garbage in Europe and America is generally strictly classified at the source, collected in classified bags).
- Biomass gasification is the process of converting biomass-forming hydrocarbons into combustible gases containing CO, H 2 , CH 4 under certain thermodynamic conditions.
- the gasification process requires the supply of air or oxygen to cause partial combustion of the feedstock.
- the difference between the gasification process and the common combustion process is that sufficient oxygen is supplied during the combustion process to fully burn the raw materials, and the purpose is to directly obtain heat.
- the products after combustion are non-reburnable flue gases such as carbon dioxide and water vapor; gasification process Only the portion of oxygen required for the thermochemical reaction is supplied, and energy is retained as much as possible in the combustible gas obtained after the reaction.
- the vaporized product is a combustible gas containing CO, H 2 , CH 4 and low molecular hydrocarbons.
- Biomass gasification includes drying, pyrolysis, oxidation, and reduction reactions.
- the organic components in the garbage are also biomass, so the organic components in the garbage can also be treated by gasification, which is the source of waste gasification technology.
- the garbage before the garbage gasification treatment, the garbage must be properly sorted and dried, and the inorganic materials such as moisture, dust, sand, pebbles, broken bricks, broken glass, and rust in the domestic garbage should be separated and separated as much as possible.
- perishable organic matter can be treated by fermentation.
- the object of the present invention is to provide a drum type domestic garbage breaking bag, screening and drying integrated equipment, which discharges organic matter and inorganic matter in domestic garbage from different discharge ports to achieve the purpose of garbage sorting and drying.
- a domestic waste sifting and drying integrated device which comprises a screening drum, a power device and a supporting device, wherein the screening drum is mounted on the supporting device and installed
- the discharge end of the rear screening drum is inclined downward by a certain angle, and the inclination angle with the horizontal plane is ⁇ , 3° ⁇ ⁇ ⁇ 10°
- the outer peripheral surface of the screening drum body is provided with a power gear, a power gear and a power device Connecting;
- the discharge end of the screening drum is connected to the gasifier through a burner;
- the higher end of the screening drum is a feeding end, the end is provided with a feeding hopper, and the inner chamber of the screening drum is from the feeding end
- the discharge end is divided into a first broken bag area, a first screening section, a second broken bag area, a second screening section, and a drying zone; wherein, the first broken bag area and the second broken bag area are on the wall Install n broken knives with the same vertical skew
- the supporting device comprises a front support frame at the feeding end of the screening drum and a rear support frame at the discharge end of the screening drum
- the front support frame and the rear support frame are all provided with support wheels, and the inlet and discharge ends of the screening drum are respectively placed on the corresponding support wheels.
- the power unit is a power motor.
- the screening drum is driven by a power gear, a speed reducer and a power motor, and the speed of the screening drum is m, 3 ⁇ m ⁇ 24.
- the purpose of pretreatment is to achieve the technical classification of waste, to improve the utilization of various resources as much as possible, and to provide suitable material status for the subsequent processing of various materials.
- the working principle of the household garbage breaking bag and screening equipment of this scheme is: when the bagged domestic garbage enters the drum from the feeding port, the water and ash in the garbage are broken after the bag breaking knife in the broken bag area is broken for the first time. Smaller inorganic components such as granules, pebbles and broken glass are screened out in the first sieve section; and the bag-breaking knives in the sieve segment connection zone are used to break the partially unbroken garbage again, which is bulky. The inorganic matter is sieved out in the second sieve section, and the organic matter continues to advance in the drum, and is discharged after being properly dried by the biomass gasification and combustion device.
- Garbage gasification has higher requirements on the humidity of the material. It can be said that the dryer the material, the better the gasification effect. Drying means that a certain amount of heat energy is transferred to the moisture contained in the material per unit time. These wet fractions are heated and vaporized, separated from the materials, and the materials that lose moisture are collected, and the vaporized moisture is discharged into the atmosphere. It is the process of drying.
- the material consumes more energy for drying, and the heating method for material drying is divided into direct drying and indirect drying. Drying is done by heat.
- the heat is usually generated by the combustion of the material.
- the heat generated by the combustion is present in the hot gas. There are two types of heat utilization:
- Indirect use The heat of the hot gas is passed through a heat exchanger and transmitted to a certain medium, such as the drum wall, to heat the wet material in the drum through the wall of the drum. In this way, the hot gas is not in contact with the dried wet material, and the heat is partially utilized. Indirect use has more heat loss, generally between 30-70%.
- direct or indirect heating has different thermal efficiency losses.
- the heat source exhaust gas directly becomes a medium, and its thermal efficiency is close to the combustion efficiency itself.
- the biomass gas produced by combustion of biomass gasifier is above 200 °C. This is a high-temperature fluid that transfers heat from the heat generated by combustion to the waste with high water content. Generally, the thermal efficiency of gas hot gas Between 70% and 90%.
- the main body of the drying device of the present embodiment is a cylindrical body which is slightly inclined and can be rotated.
- the wet material moves from the higher end to the lower end by the gravity and the lifting plate by the slow rotation of the cylinder, and the wet material is in effective contact with the hot air or the heated wall in the cylinder.
- the dried, dried material is discharged from the lower end of the rear end.
- the drum is equipped with a lifting plate, so that the material is continuously picked up and sprinkled during the rotation process of the cylinder to make it fully contact with the hot air flow to improve the drying efficiency and move the wet material forward.
- the present invention is an equipment matched with the domestic garbage gasification treatment technology, which breaks the bag and sieves the garbage. And using the heat generated by the original dry garbage gasification to dry the garbage with high humidity, this integrated equipment has practical significance.
- Figure 1 is a schematic view of the overall structure of the present invention.
- Figure 2 is a schematic cross-sectional view of Figure 1.
- Figure 3 is a schematic view of the process flow of the present invention.
- Figure 4 is a schematic view showing the inclination angle of the screening drum of the present invention.
- Figure 5 is a schematic view showing the movement direction of the screening drum of the present invention.
- the domestic waste sifting and drying integrated device includes a screening roller and a power.
- the device and the supporting device wherein the screening roller is mounted on the supporting device, the supporting device is composed of a front supporting frame 4 at the feeding end of the screening roller and a rear supporting frame 12 at the discharging end of the screening roller, the front supporting frame 4 and the rear Supporting frame 12 is provided with supporting wheels, and the feeding and discharging ends of the screening drum are respectively placed on the corresponding supporting wheels;
- the discharging end of the screening drum after installation is inclined downward by a certain angle, and the inclination angle with the horizontal plane is ⁇ , 3° ⁇ ⁇ ⁇ 10°;
- a power gear 9 is arranged on the outer peripheral surface of the screening drum body, and the power gear 9 is connected with the power device;
- the power device of the present scheme is the power motor 10, and the screening roller is driven by the power
- the discharge end of the screening drum is connected to the gasifier 16 through a burner 15; the higher end of the screening drum is a feeding end, and the end is provided with a feeding hopper 1 and the inner chamber of the screening drum is fed from the feeding
- the end to the discharge end are sequentially divided into a first bag breaking zone 2, a first screen segment 6, a second bag breaking zone 7, a second screen segment 8, and a drying zone 11; wherein, the first bag breaking zone 2 and The inner wall of the second bag-breaking area 7 is provided with n vertical broken knives 3, 3 ⁇ n ⁇ 20, and the broken knives 3 are 50-150 mm high and 30-100 mm wide, and the cutting edge is curved.
- the skew angle of the blade is the same as the inclination angle ⁇ of the drum, and the cutting edge faces the direction of the garbage rolling;
- the inner surface of the screen cylinder is alternately installed in the axial direction and the circumferential direction to install a special arc-shaped bag cutter And lifting board.
- the bag-breaking knife is installed in the broken bag area, and the lifting plate is installed in the drying zone of the rear section, and is made of plate with high strength and hardness, and both are radial radiant installation.
- the lifting plate is combined with the spinning cylinder to rotate the animal material to facilitate the drying of the material.
- a plurality of small circular holes are distributed on the wall of the first sieve segment 6 and the second sieve segment 8 , and the diameter of the small hole of the first sieve segment 6 is d1. It is used to screen inorganic lime soil, pebbles, broken bricks, broken glass, etc.; the diameter of the small hole of the second sieve segment 8 is d2, d2>d1, Used to screen for perishable organics and coarser inorganics. It is also possible to add one or more sieve sections having larger sieve openings as needed. After the raw garbage is sent into the sieve drum, the rotation of the sieve cylinder moves forward and breaks the bag inside the sieve cylinder and the screening is carried out immediately.
- the dust, crushed sand, broken glass and porcelain fragments scattered in the garbage are mainly used.
- the inorganic material is subjected to the screening process by the first screen section. After the first sieve segmentation, the garbage reduction is obvious, and some of the garbage will not be broken, and will be further broken in the second broken bag area. With the completion of the second bag breaking process, the material enters the second sieve section and continues to be screened.
- the second sieve section of the sieved material is a perishable organic substance mainly composed of kitchen waste and a part of coarse inorganic matter. . It is also possible to increase the size of the sieve section with a larger aperture as needed.
- the outer peripheral surface of the screening drum is provided with a plurality of radial reinforcing hoops 5; the bottom of the discharging end of the screening drum is provided with a discharging port 14, the end of the discharging end is provided with a temperature controlling plate 13, and the temperature regulating plate 13 is fixed at the discharging end
- the outer portion is connected to the burner 15 through a conical cylinder; the temperature control plate 13 is provided with a plurality of temperature control holes. Preventing the flame of the burner from directly spraying on the garbage, the experiment shows that the hot air temperature entering the drying cylinder through the small hole of the temperature control plate is generally about 85 °C, which is good for the drying of the garbage.
- the processing technology of the above device is:
- the rotary cylinder dryer is basically preheated, and the wet material is continuously and uniformly placed from the feeding device, and the finished product is discharged from the discharge port at the rear end.
- the normal ash generated by the gasification process can be directly sprinkled into the land. If the heavy metal of the ash residue exceeds the standard, it is treated with sanitary landfill or cement.
- the integrated machine of this program is aimed at the current status of domestic garbage of Chinese residents, and it is of great help to the garbage gasification treatment.
- the integrated bag breaking, screening and drying equipment has a simple structure, convenient manufacturing and maintenance, strong adjustment ability, suitable for different processing scales, and is advantageous for popularization and application.
- the sieve cylinder of the scheme has large diameter, low rotation speed, stable operation and low noise. It integrates bag breaking, crushing, sieving and drying into one, adapts to high water content garbage, has high screening efficiency, obvious screening effect, and simplifies the pretreatment process route.
- the main technical parameters of the bag breaking, screening and drying integrated device are as follows: treatment scale 3t/h: sieve cylinder length 8m, diameter ⁇ 1000mm, quality 1t; screen cylinder speed 6r / min or so (frequency control); screen hole diameter ⁇ 22mm (first screen segment), ⁇ 70mm (second screen segment); installation tilt angle 5 °; sieve cylinder motor power 5KW; noise ⁇ 80dB; Screening efficiency ⁇ 70mm sieve pass rate ⁇ 80% (refers to perishable organic matter and coarse inorganic matter), ⁇ 22mm sieve hole pass rate ⁇ 70% (referring to inorganic matter); bag breaking efficiency ⁇ 90%.
- the material of the first sieve section accounts for about 30% of the total mass of the material, the material of the second sieve section accounts for about 15%, the material of the sieved material accounts for about 50%, and some of the water evaporates, and the whole is close to the garbage component. .
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- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
A device for integrating bag-breaking, screening and drying of household waste comprises a screening drum, a power unit and a support device. The screening drum is mounted on the support device, has a discharging end tilted downward by a certain angle, and is provided with power gears (9) on an outer circumferential surface thereof. The power gears (9) are connected to the power unit. The discharging end of the screening drum is connected to a gasification furnace (16) via a burner (15). An internal cavity of the screening drum is sequentially divided into a first bag-breaking region (2), a first screening section (6), a second bag-breaking region (7), a second screening section (8) and a drying region (11) from a feeding end to the discharging end. The first bag-breaking region (2) and second bag-breaking region (7) are provided with n shredding knives (3) on internal walls thereof. Several small circular holes distribute on the drum walls of the first screening section (6) and second screening section (8). The device performs bag-breaking and screening on waste, and utilizes the heat generated by gasification of dry waste for drying waste having a higher humidity, thus enabling actual practicability.
Description
本发明涉及垃圾处理技术领域,尤其是指一种与生活垃圾气化技术配合使用的生活垃圾破袋、筛分、烘干为一体的滚筒式装置。The invention relates to the technical field of garbage disposal, in particular to a drum type device which is integrated with the domestic garbage gasification technology and which is used for breaking, sieving and drying the domestic garbage.
一、生活垃圾分选First, the domestic garbage sorting
人类活动必然会产生垃圾,目前生活垃圾的处理已经成为一个社会问题。生活垃圾处理工程中一个重要的环节是垃圾的预处理,主要是垃圾的分选和干燥。Human activities will inevitably produce garbage, and the treatment of domestic garbage has become a social problem. An important part of the domestic waste treatment project is the pretreatment of garbage, mainly the sorting and drying of garbage.
生活垃圾分选是把垃圾中可回收利用或不利于后续处置工艺要求的物料分离出来,是垃圾处理工程中的重要环节和重要操作之一。生活垃圾分选、干燥的同时应考虑技术性、实用性和经济性。Domestic garbage sorting is the separation of materials that can be recycled or used in the process of subsequent disposal. It is one of the important links and important operations in the garbage disposal project. Domestic garbage should be considered for technical, practical and economical while sorting and drying.
目前生活垃圾分选处理工艺主要有以下三种:At present, there are three main types of domestic waste sorting processes:
第一种方式为直接进行人工初选,然后进行筛选和人工分选。这是一种比较低级的处理方式是垃圾处理厂一种比较简陋的垃圾分选工艺方式。The first method is to perform manual primary selection directly, followed by screening and manual sorting. This is a relatively low-level treatment method that is a relatively simple garbage sorting process in waste treatment plants.
第二种方式为先对袋装垃圾进行破袋,再进行筛分和人工分选。该方式主要是参照欧、美等发达国家的设备进行垃圾处理。国外生活垃圾是分类袋装收集,而我国生活垃圾是混合袋装收集,因此国外的生活垃圾处理方式并不适合我国的国情。The second method is to first break the bagged garbage, and then perform screening and manual sorting. This method mainly refers to the garbage disposal of equipment in developed countries such as Europe and America. Foreign domestic garbage is collected in classified bags, while domestic garbage is collected in mixed bags. Therefore, the domestic garbage disposal method is not suitable for China's national conditions.
第三种方式是在对袋装垃圾进行破袋的同时,对垃圾中的大块物料进行选择性破碎和分选,再进行筛分和人工分选。The third way is to selectively break and sort the bulk materials in the garbage while the bagged garbage is broken, and then perform screening and manual sorting.
我国生活垃圾主要由易腐有机物、煤灰、泥沙、小石子、碎砖块、碎玻璃、废旧塑料类、衣物类、纸类等成分构成,垃圾的含水量高且成分复杂,结构变化大又极不均匀,不同于欧美的生活垃圾(欧美的生活垃圾一般在源头经过严格分类,采用分类袋装收集)。Domestic garbage is mainly composed of perishable organic matter, coal ash, silt, pebbles, broken bricks, broken glass, waste plastics, clothing, paper, etc. The garbage has high water content and complex composition, and the structure changes greatly. It is extremely uneven, unlike the domestic garbage in Europe and America (the domestic garbage in Europe and America is generally strictly classified at the source, collected in classified bags).
二、生活垃圾气化原理及其预处理Second, the principle of domestic garbage gasification and its pretreatment
现在人类的生活垃圾处理技术呈现多样化的趋势,其中生物质气化技术用于生活垃圾的处理正在逐步走向实用化,其对人类环境保护的功能前景无限。Nowadays, human waste treatment technology is showing a diversified trend. The treatment of biomass gasification technology for domestic garbage is gradually becoming practical, and its functional prospects for human environmental protection are infinite.
生物质气化是在一定的热力学条件下,将组成生物质的碳氢化合物转化为含CO、H2、CH4等可燃气体的过程。为了提供反应的热力学条件,气化过程需要供给空气或氧气,使原料发生部分燃烧。气化过程和常见的燃烧过程的区别是燃烧过程中供给充足的氧气,使原料充分燃烧,目的是直接获取热量,燃烧后的产物是二氧化碳和水蒸气等不可再燃烧的烟气;气化过程只供给热化学反应所需的那部分氧气,而尽可能将能量保留在反应后得到的可
燃气体中,气化后的产物是含CO、H2、CH4和低分子烃类的可燃气体。生物质气化包括干燥、热解、氧化和还原反应。Biomass gasification is the process of converting biomass-forming hydrocarbons into combustible gases containing CO, H 2 , CH 4 under certain thermodynamic conditions. In order to provide the thermodynamic conditions of the reaction, the gasification process requires the supply of air or oxygen to cause partial combustion of the feedstock. The difference between the gasification process and the common combustion process is that sufficient oxygen is supplied during the combustion process to fully burn the raw materials, and the purpose is to directly obtain heat. The products after combustion are non-reburnable flue gases such as carbon dioxide and water vapor; gasification process Only the portion of oxygen required for the thermochemical reaction is supplied, and energy is retained as much as possible in the combustible gas obtained after the reaction. The vaporized product is a combustible gas containing CO, H 2 , CH 4 and low molecular hydrocarbons. Biomass gasification includes drying, pyrolysis, oxidation, and reduction reactions.
垃圾中的有机成分也属于生物质,因此垃圾中的有机成分也能用气化方法来处理,这就是垃圾气化处理技术的来源。The organic components in the garbage are also biomass, so the organic components in the garbage can also be treated by gasification, which is the source of waste gasification technology.
但垃圾气化处理前必须对垃圾进行适当的分选和干燥,将生活垃圾中的水分、灰尘、沙子、小石子、碎砖块、碎玻璃、锈蚀物等无机物尽可能分离分选出来另行填埋处理,易腐有机物可以选择采用发酵方法处理。However, before the garbage gasification treatment, the garbage must be properly sorted and dried, and the inorganic materials such as moisture, dust, sand, pebbles, broken bricks, broken glass, and rust in the domestic garbage should be separated and separated as much as possible. For landfill treatment, perishable organic matter can be treated by fermentation.
考虑到我国垃圾组成的复杂性,针对我国城市生活垃圾混合包装、混合收集的现状,从气化处理的角度出发,提高生活垃圾分选工艺的效果和效率,简化后续处理工艺路线,降低投资和运行成本是气化处理技术应用之前提。Considering the complexity of China's garbage composition, aiming at the current situation of mixed packaging and mixed collection of urban domestic garbage in China, from the perspective of gasification treatment, improve the effect and efficiency of domestic waste sorting process, simplify the subsequent processing route, reduce investment and Operating costs are raised before the application of gasification technology.
针对生活垃圾气化处理工艺的要求,迫切需要开发出适合我国国情的专用破袋、筛分、烘干设备,该设备对袋装垃圾进行破袋的同时,再进行筛分和初步烘干。分选出的含塑料等有机成分的垃圾再进行适当的人工分选,分别采用发酵技术和气化技术处理。这种垃圾破袋、筛分、烘干一体机在目前国内外还未见开发。In response to the requirements of the domestic waste gasification treatment process, it is urgent to develop a special bag breaking, screening and drying equipment suitable for China's national conditions. The equipment is used for bagging and bagging, and then screening and preliminary drying. The sorted garbage containing organic components such as plastics is subjected to appropriate manual sorting, and respectively treated by fermentation technology and gasification technology. This kind of garbage bag breaking, screening and drying machine has not been developed at home and abroad.
发明内容Summary of the invention
本发明的目的提供一种滚筒式生活垃圾破袋、筛分、烘干一体式装备,将生活垃圾中的有机物和无机物由不同的出料口排出,达到垃圾分选和烘干的目的。The object of the present invention is to provide a drum type domestic garbage breaking bag, screening and drying integrated equipment, which discharges organic matter and inorganic matter in domestic garbage from different discharge ports to achieve the purpose of garbage sorting and drying.
为实现上述目的,本发明所提供的技术方案为:一种生活垃圾破筛烘一体式装置,它包括有筛分滚筒、动力装置、支撑装置,其中,筛分滚筒安装在支撑装置上,安装后的筛分滚筒出料端向下倾斜一定的角度,其与水平面的倾斜角为α,3°≤α≤10°;筛分滚筒筒身外周面上设有动力齿轮,动力齿轮与动力装置连接;筛分滚筒出料端通过燃烧机与气化炉相连接;所述的筛分滚筒较高的一端为进料端,该端设有进料斗,筛分滚筒内腔从进料端至出料端依次分为第一破袋区、第一筛分段、第二破袋区、第二筛分段、烘干区;其中,第一破袋区和第二破袋区内壁上安装n把竖直的偏斜角相同的碎碎刀,3≤n≤20,碎碎刀高50~150mm,宽30~100mm,刃口呈弧形,且有一定的偏斜度,刀片的偏斜角与滚筒的倾斜角α相同,且刃口迎着垃圾滚动的方向;第一筛分段和第二筛分段筒壁上分布有若干个小圆孔,第一筛分段的小孔直径为d1,第二筛分段的小孔直径为d2,d2>d1,筛分滚筒外周面上设有若干径向加强箍;筛分滚筒出料端底部设有出料口,出料端端部设有控温板控温板固定在出料端端部,其外侧通过一圆锥形筒与燃烧机相连接;控温板板面上均布有若干控温孔。In order to achieve the above object, the technical solution provided by the present invention is: a domestic waste sifting and drying integrated device, which comprises a screening drum, a power device and a supporting device, wherein the screening drum is mounted on the supporting device and installed The discharge end of the rear screening drum is inclined downward by a certain angle, and the inclination angle with the horizontal plane is α, 3° ≤ α ≤ 10°; the outer peripheral surface of the screening drum body is provided with a power gear, a power gear and a power device Connecting; the discharge end of the screening drum is connected to the gasifier through a burner; the higher end of the screening drum is a feeding end, the end is provided with a feeding hopper, and the inner chamber of the screening drum is from the feeding end The discharge end is divided into a first broken bag area, a first screening section, a second broken bag area, a second screening section, and a drying zone; wherein, the first broken bag area and the second broken bag area are on the wall Install n broken knives with the same vertical skew angle, 3≤n≤20, broken knives 50-150mm high, 30-100mm wide, the cutting edge is curved, and has a certain degree of skewness, the blade The skew angle is the same as the tilt angle α of the drum, and the cutting edge faces the direction of the garbage rolling; the first screen segment and the first Screen section cylinder wall distributed plurality of small circular holes, the hole diameter of the first screen section is d1, The diameter of the small hole of the second sieve section is d2, d2>d1, The outer peripheral surface of the screening drum is provided with a plurality of radial reinforcing hoops; the bottom of the discharging end of the screening drum is provided with a discharging port, and the end of the discharging end is provided with a temperature controlling plate and a temperature regulating plate is fixed at the end of the discharging end, and the outer side thereof The utility model is connected to the burner through a conical cylinder; a plurality of temperature control holes are arranged on the surface of the temperature control plate.
所述的支撑装置由位于筛分滚筒进料端的前支撑架和位于筛分滚筒出料端的后支撑架
构成,前支撑架、后支撑架上均设有支撑轮,筛分滚筒进、出料端分别置于相应的支撑轮上。The supporting device comprises a front support frame at the feeding end of the screening drum and a rear support frame at the discharge end of the screening drum
The front support frame and the rear support frame are all provided with support wheels, and the inlet and discharge ends of the screening drum are respectively placed on the corresponding support wheels.
所述的动力装置为动力电机。The power unit is a power motor.
所述的筛分滚筒由动力齿轮、减速机和动力电机带动,筛分滚筒转速为m,3≤m≤24。The screening drum is driven by a power gear, a speed reducer and a power motor, and the speed of the screening drum is m, 3≤m≤24.
在生活垃圾气化处理工艺中,预处理的目的是为了实现对垃圾的技术性分类,尽可能提高各类资源利用率,并为各种物料的后序处理工艺提供适合的物料状态。本方案的生活垃圾破袋、筛分装备的工作原理是:当袋装生活垃圾由进料口进入滚筒内,经过破袋区的破袋刀第一次破袋后,垃圾中的水分、灰粒、小石子和碎玻璃等体积较小的无机物成分在第一筛分段筛出;再经过筛分段连接区的破袋刀将部分未破袋的垃圾再次进行破袋,体积较大的无机物在第二筛分段筛出,有机物继续在滚筒内前行,经生物质气化及燃烧装置适当烘干后排出。In the domestic waste gasification treatment process, the purpose of pretreatment is to achieve the technical classification of waste, to improve the utilization of various resources as much as possible, and to provide suitable material status for the subsequent processing of various materials. The working principle of the household garbage breaking bag and screening equipment of this scheme is: when the bagged domestic garbage enters the drum from the feeding port, the water and ash in the garbage are broken after the bag breaking knife in the broken bag area is broken for the first time. Smaller inorganic components such as granules, pebbles and broken glass are screened out in the first sieve section; and the bag-breaking knives in the sieve segment connection zone are used to break the partially unbroken garbage again, which is bulky. The inorganic matter is sieved out in the second sieve section, and the organic matter continues to advance in the drum, and is discharged after being properly dried by the biomass gasification and combustion device.
垃圾气化对物料的湿度有较高的要求,可以说物料越干燥气化效果越好。干燥意味着在单位时间里将一定数量的热能传给物料所含的湿分,这些湿分受热后汽化,与物料分离,失去湿分的物料收集起来,汽化的湿分排入大气中,这就是干化的工艺过程。Garbage gasification has higher requirements on the humidity of the material. It can be said that the dryer the material, the better the gasification effect. Drying means that a certain amount of heat energy is transferred to the moisture contained in the material per unit time. These wet fractions are heated and vaporized, separated from the materials, and the materials that lose moisture are collected, and the vaporized moisture is discharged into the atmosphere. It is the process of drying.
物料干燥消耗的能源较多,物料干化的加热方式分直接干化和间接干化。干化是依靠热量来完成的,热量一般都是物料燃烧产生,燃烧产生的热量存在于热气中,这部分热量的利用形式有两类:The material consumes more energy for drying, and the heating method for material drying is divided into direct drying and indirect drying. Drying is done by heat. The heat is usually generated by the combustion of the material. The heat generated by the combustion is present in the hot gas. There are two types of heat utilization:
①直接利用:将高温热气直接引入干燥器,通过气体与湿物料的接触、对流进行换热。这种做法的特点是热量利用的效率高。1 direct use: direct high-temperature hot gas into the dryer, through the contact of gas and wet materials, convection heat exchange. This approach is characterized by high efficiency of heat utilization.
②间接利用:将高温热气的热量通过热交换器,传给某种介质,如滚筒壁,通过滚筒壁将滚筒内的湿物料加热。这种方式热气与被干化的湿物料没有接触,热量被部分利用。间接利用存在较多的热损失,一般来说在30-70%之间。2 Indirect use: The heat of the hot gas is passed through a heat exchanger and transmitted to a certain medium, such as the drum wall, to heat the wet material in the drum through the wall of the drum. In this way, the hot gas is not in contact with the dried wet material, and the heat is partially utilized. Indirect use has more heat loss, generally between 30-70%.
对垃圾干燥来说,直接或间接加热具有不同的热效率损失。直接加热形式中热源尾气直接成为介质,其热效率接近燃烧效率本身。For waste drying, direct or indirect heating has different thermal efficiency losses. In the direct heating form, the heat source exhaust gas directly becomes a medium, and its thermal efficiency is close to the combustion efficiency itself.
生物质气化炉燃气燃烧后产生的尾气温度在200℃以上,这是一种高温流体,将热量从燃烧所产生的热气转移到含水率较高的垃圾中,一般来说,燃气热气的热效率介于70%-90%之间。The biomass gas produced by combustion of biomass gasifier is above 200 °C. This is a high-temperature fluid that transfers heat from the heat generated by combustion to the waste with high water content. Generally, the thermal efficiency of gas hot gas Between 70% and 90%.
本方案的烘干装置主体是略带倾斜并能回转的圆筒体。在干燥过程中,湿物料借助于圆筒的缓慢的转动,在重力和扬料板的作用下从较高一端向较低一端移动,湿物料与通过筒内的热风或加热壁面进行有效地接触而被干燥,干燥后的物料从后端下部排出。一般滚筒内装有扬料板,使物料在筒体回转过程中不断抄起又洒下,使其充分与热气流接触,以提高干燥效率并使湿物料向前移动。The main body of the drying device of the present embodiment is a cylindrical body which is slightly inclined and can be rotated. During the drying process, the wet material moves from the higher end to the lower end by the gravity and the lifting plate by the slow rotation of the cylinder, and the wet material is in effective contact with the hot air or the heated wall in the cylinder. The dried, dried material is discharged from the lower end of the rear end. Generally, the drum is equipped with a lifting plate, so that the material is continuously picked up and sprinkled during the rotation process of the cylinder to make it fully contact with the hot air flow to improve the drying efficiency and move the wet material forward.
综上所述,本发明是一种与生活垃圾气化处理技术配套的装备,将垃圾破袋、筛分,
并利用原有的干燥垃圾气化产生的热能烘干湿度较大的垃圾,这种一体化装备具有实际意义。In summary, the present invention is an equipment matched with the domestic garbage gasification treatment technology, which breaks the bag and sieves the garbage.
And using the heat generated by the original dry garbage gasification to dry the garbage with high humidity, this integrated equipment has practical significance.
图1为本发明的整体结构示意图。Figure 1 is a schematic view of the overall structure of the present invention.
图2为图1的剖面示意图。Figure 2 is a schematic cross-sectional view of Figure 1.
图3为本发明的工艺流程示意图。Figure 3 is a schematic view of the process flow of the present invention.
图4为本发明的筛分滚筒倾斜角度示意图。Figure 4 is a schematic view showing the inclination angle of the screening drum of the present invention.
图5为本发明的筛分滚筒运动方向示意图。Figure 5 is a schematic view showing the movement direction of the screening drum of the present invention.
下面结合所有附图对本发明作进一步说明,本发明的较佳实施例为:参见附图1至附图5,本实施例所述的生活垃圾破筛烘一体式装置包括有筛分滚筒、动力装置、支撑装置,其中,筛分滚筒安装在支撑装置上,支撑装置由位于筛分滚筒进料端的前支撑架4和位于筛分滚筒出料端的后支撑架12构成,前支撑架4、后支撑架12上均设有支撑轮,筛分滚筒进、出料端分别置于相应的支撑轮上;安装后的筛分滚筒出料端向下倾斜一定的角度,其与水平面的倾斜角为α,3°≤α≤10°;筛分滚筒筒身外周面上设有动力齿轮9,动力齿轮9与动力装置连接;本方案的动力装置为动力电机10,筛分滚筒由动力齿轮9、减速机和动力电机10带动,筛分滚筒转速为m,3≤m≤24。筛分滚筒出料端通过燃烧机15与气化炉16相连接;所述的筛分滚筒较高的一端为进料端,该端设有进料斗1,筛分滚筒内腔从进料端至出料端依次分为第一破袋区2、第一筛分段6、第二破袋区7、第二筛分段8、烘干区11;其中,第一破袋区2和第二破袋区7内壁上安装n把竖直的偏斜角相同的碎碎刀3,3≤n≤20,碎碎刀3高50~150mm,宽30~100mm,刃口呈弧形,且有一定的偏斜度,刀片的偏斜角与滚筒的倾斜角α相同,且刃口迎着垃圾滚动的方向;筛筒内表面在轴向和圆周方向交错地安装特制的弧状破袋刀和扬料板。破袋刀安装在破袋区,扬料板安装在后段的烘干区,都是用强度和硬度较高的板材制成,且均为向心辐射式安装。扬料板结合筛筒自身旋转带动物料扬升,便于物料烘干。第一筛分段6和第二筛分段8筒壁上分布有若干个小圆孔,第一筛分段6的小孔直径为d1,用来筛分无机灰土、小石子、碎砖头、碎玻璃等;第二筛分段8的小孔直径为d2,d2>d1,用来筛分易腐有机物和较粗大的无机物。根据需要,还可以增加一至多个筛孔更大的破筛段。原生垃圾送入筛筒后,通过筛筒的旋转在筛筒内部向前移动破袋和筛分随即进行,散存在垃圾中的以灰土、碎砂石、碎玻璃和瓷物碎片等为主的无机物便由第一筛分段完成其筛分过程。经过第一筛分段筛分后,垃圾减量化明显,且还会有部分垃圾未破烂,在第二破袋区会进一步破碎。随着二次破袋过程的完成,物料便进入第二筛分段继续进行筛分,第二筛分段的筛下物是以厨余物为主的易腐有机物和部分较粗大的无机物。
根据需要,还可以增加孔径更大的筛分段。筛分滚筒外周面上设有若干径向加强箍5;筛分滚筒出料端底部设有出料口14,出料端端部设有控温板13,控温板13固定在出料端端部,其外侧通过一圆锥形筒与燃烧机15相连接;控温板13板面上均布有若干控温孔。防止燃烧机的火焰直接喷射在垃圾上发生燃烧,实验表明,经过控温板的小孔进入烘干筒的热风温度一般为85℃左右,利于垃圾的烘干。The present invention will be further described with reference to the accompanying drawings. The preferred embodiment of the present invention is as follows: Referring to FIG. 1 to FIG. 5, the domestic waste sifting and drying integrated device according to the embodiment includes a screening roller and a power. The device and the supporting device, wherein the screening roller is mounted on the supporting device, the supporting device is composed of a front supporting frame 4 at the feeding end of the screening roller and a rear supporting frame 12 at the discharging end of the screening roller, the front supporting frame 4 and the rear Supporting frame 12 is provided with supporting wheels, and the feeding and discharging ends of the screening drum are respectively placed on the corresponding supporting wheels; the discharging end of the screening drum after installation is inclined downward by a certain angle, and the inclination angle with the horizontal plane is α, 3° ≤ α ≤ 10°; a power gear 9 is arranged on the outer peripheral surface of the screening drum body, and the power gear 9 is connected with the power device; the power device of the present scheme is the power motor 10, and the screening roller is driven by the power gear 9, The speed reducer and the power motor 10 drive, and the speed of the screening drum is m, 3 ≤ m ≤ 24. The discharge end of the screening drum is connected to the gasifier 16 through a burner 15; the higher end of the screening drum is a feeding end, and the end is provided with a feeding hopper 1 and the inner chamber of the screening drum is fed from the feeding The end to the discharge end are sequentially divided into a first bag breaking zone 2, a first screen segment 6, a second bag breaking zone 7, a second screen segment 8, and a drying zone 11; wherein, the first bag breaking zone 2 and The inner wall of the second bag-breaking area 7 is provided with n vertical broken knives 3, 3 ≤ n ≤ 20, and the broken knives 3 are 50-150 mm high and 30-100 mm wide, and the cutting edge is curved. And there is a certain degree of skewness, the skew angle of the blade is the same as the inclination angle α of the drum, and the cutting edge faces the direction of the garbage rolling; the inner surface of the screen cylinder is alternately installed in the axial direction and the circumferential direction to install a special arc-shaped bag cutter And lifting board. The bag-breaking knife is installed in the broken bag area, and the lifting plate is installed in the drying zone of the rear section, and is made of plate with high strength and hardness, and both are radial radiant installation. The lifting plate is combined with the spinning cylinder to rotate the animal material to facilitate the drying of the material. a plurality of small circular holes are distributed on the wall of the first sieve segment 6 and the second sieve segment 8 , and the diameter of the small hole of the first sieve segment 6 is d1. It is used to screen inorganic lime soil, pebbles, broken bricks, broken glass, etc.; the diameter of the small hole of the second sieve segment 8 is d2, d2>d1, Used to screen for perishable organics and coarser inorganics. It is also possible to add one or more sieve sections having larger sieve openings as needed. After the raw garbage is sent into the sieve drum, the rotation of the sieve cylinder moves forward and breaks the bag inside the sieve cylinder and the screening is carried out immediately. The dust, crushed sand, broken glass and porcelain fragments scattered in the garbage are mainly used. The inorganic material is subjected to the screening process by the first screen section. After the first sieve segmentation, the garbage reduction is obvious, and some of the garbage will not be broken, and will be further broken in the second broken bag area. With the completion of the second bag breaking process, the material enters the second sieve section and continues to be screened. The second sieve section of the sieved material is a perishable organic substance mainly composed of kitchen waste and a part of coarse inorganic matter. . It is also possible to increase the size of the sieve section with a larger aperture as needed. The outer peripheral surface of the screening drum is provided with a plurality of radial reinforcing hoops 5; the bottom of the discharging end of the screening drum is provided with a discharging port 14, the end of the discharging end is provided with a temperature controlling plate 13, and the temperature regulating plate 13 is fixed at the discharging end The outer portion is connected to the burner 15 through a conical cylinder; the temperature control plate 13 is provided with a plurality of temperature control holes. Preventing the flame of the burner from directly spraying on the garbage, the experiment shows that the hot air temperature entering the drying cylinder through the small hole of the temperature control plate is generally about 85 °C, which is good for the drying of the garbage.
上述装置的处理工艺为:The processing technology of the above device is:
1)、先准备好气化料,并将之置入气化炉内并适当压料。1) Prepare the gasification material first, and place it in the gasifier and press it properly.
2)、开启烟气助烧功能,将电子点火棒放入气化炉内将物料点着火,产生的烟气导入助烧装置助烧掉。2) Turn on the flue gas to help the burning function, put the electronic ignition rod into the gasifier to ignite the material, and the generated flue gas is introduced into the combustion-assisting device to help burn it.
3)、气化过程正常以后,关闭烟气助烧功能,将气化燃烧装置一起推向滚筒后端的烘干区热能入口。注意调整燃烧机二次进风量的大小,氧气供应量为实际需求量的110%左右,即为过氧燃烧,以减少燃气燃烧产生二次污染。开启旋转圆筒烘干机的旋转电机,让圆筒转动起来。3) After the gasification process is normal, the flue gas assisting function is turned off, and the gasification combustion device is pushed together to the heat energy inlet of the drying zone at the rear end of the drum. Pay attention to adjusting the amount of secondary air intake of the burner. The oxygen supply is about 110% of the actual demand, which is peroxygen combustion to reduce secondary pollution caused by gas combustion. Turn on the rotating motor of the rotating cylinder dryer to rotate the cylinder.
4)、气化炉正常使用5分钟以后,旋转圆筒烘干机基本预热完毕,从进料装置持续、均匀地放入湿物料,成品从后端的出料口排出。4) After the gasifier is used for 5 minutes, the rotary cylinder dryer is basically preheated, and the wet material is continuously and uniformly placed from the feeding device, and the finished product is discharged from the discharge port at the rear end.
5)、停止垃圾破袋、筛分和烘干工作,应先停止进料,然后停止气化炉的使用。5) Stop the garbage bag breaking, screening and drying work, stop the feeding first, and then stop the use of the gasifier.
6)、气化过程产生的正常灰渣可以直接撒入土地,如果灰渣重金属超标,则进行卫生填埋或送水泥窖处理。6) The normal ash generated by the gasification process can be directly sprinkled into the land. If the heavy metal of the ash residue exceeds the standard, it is treated with sanitary landfill or cement.
本方案的一体机针对目前中国居民的生活垃圾现状开发,对垃圾气化处理有极大的帮助。The integrated machine of this program is aimed at the current status of domestic garbage of Chinese residents, and it is of great help to the garbage gasification treatment.
采用一体化破袋、筛分、烘干设备结构简单,制造维修方便,调节能力强,适合不同的处理规模,利于推广应用。The integrated bag breaking, screening and drying equipment has a simple structure, convenient manufacturing and maintenance, strong adjustment ability, suitable for different processing scales, and is advantageous for popularization and application.
本方案的筛筒直径较大、转速低、运转平稳、噪声小。且集破袋、破碎、筛分、烘干为一体,适应高含水率垃圾,其筛分效率高、筛分效果明显,简化预处理工艺路线。The sieve cylinder of the scheme has large diameter, low rotation speed, stable operation and low noise. It integrates bag breaking, crushing, sieving and drying into one, adapts to high water content garbage, has high screening efficiency, obvious screening effect, and simplifies the pretreatment process route.
举例。用于乡、镇、村级别单位规模的生活垃圾集中预处理时,其破袋、筛分、烘干一体装置的主要技术参数如下:处理规模3t/h:筛筒长度8m,直径Φ1000mm,质量1t;筛筒转速6r/min左右(变频控制);筛孔直径Φ22mm(第一筛分段),Φ70mm(第二筛分段);安装倾角5°;筛筒电机功率5KW;噪声≤80dB;筛分效率Φ70mm筛孔通过率≥80%(指易腐有机物和粗大无机物),Φ22mm筛孔通过率≥70%(指无机物);破袋效率≥90%。第一筛分段的物料占物料总质量的30%左右,第二筛分段的物料占15%左右,筛上物的物料占50%左右,另有部分水分蒸发,总体与垃圾组分接近。
For example. For the centralized pretreatment of domestic garbage at the township, town and village level, the main technical parameters of the bag breaking, screening and drying integrated device are as follows: treatment scale 3t/h: sieve cylinder length 8m, diameter Φ1000mm, quality 1t; screen cylinder speed 6r / min or so (frequency control); screen hole diameter Φ22mm (first screen segment), Φ70mm (second screen segment); installation tilt angle 5 °; sieve cylinder motor power 5KW; noise ≤ 80dB; Screening efficiency Φ70mm sieve pass rate ≥80% (refers to perishable organic matter and coarse inorganic matter), Φ22mm sieve hole pass rate ≥70% (referring to inorganic matter); bag breaking efficiency ≥90%. The material of the first sieve section accounts for about 30% of the total mass of the material, the material of the second sieve section accounts for about 15%, the material of the sieved material accounts for about 50%, and some of the water evaporates, and the whole is close to the garbage component. .
Claims (4)
- 一种生活垃圾破筛烘一体式装置,其特征在于:它包括有筛分滚筒、动力装置、支撑装置,其中,筛分滚筒安装在支撑装置上,安装后的筛分滚筒出料端向下倾斜一定的角度,其与水平面的倾斜角为α,3°≤α≤10°;筛分滚筒筒身外周面上设有动力齿轮(9),动力齿轮(9)与动力装置连接;筛分滚筒出料端通过燃烧机(15)与气化炉(16)相连接;所述的筛分滚筒较高的一端为进料端,该端设有进料斗(1),筛分滚筒内腔从进料端至出料端依次分为第一破袋区(2)、第一筛分段(6)、第二破袋区(7)、第二筛分段(8)、烘干区(11);其中,第一破袋区(2)和第二破袋区(7)内壁上安装n把竖直的偏斜角相同的碎碎刀(3),3≤n≤20,碎碎刀(3)高50~150mm,宽30~100mm,刃口呈弧形,且有一定的偏斜度,刀片的偏斜角与滚筒的倾斜角α相同,且刃口迎着垃圾滚动的方向;第一筛分段(6)和第二筛分段(8)筒壁上分布有若干个小圆孔,第一筛分段(6)的小孔直径为d1,第二筛分段(8)的小孔直径为d2,d2>d1,筛分滚筒外周面上设有若干径向加强箍(5);筛分滚筒出料端底部设有出料口(14),出料端端部设有控温板(13),控温板(13)固定在出料端端部,其外侧通过一圆锥形筒与燃烧机(15)相连接;控温板(13)板面上均布有若干控温孔。The utility model relates to a domestic waste sifting and drying integrated device, which is characterized in that it comprises a screening roller, a power device and a supporting device, wherein the screening roller is mounted on the supporting device, and the discharging end of the screening roller after installation is downward Tilting at a certain angle, the inclination angle with the horizontal plane is α, 3° ≤ α ≤ 10°; the outer peripheral surface of the screening drum body is provided with a power gear (9), and the power gear (9) is connected with the power device; The discharge end of the drum is connected to the gasifier (16) through a burner (15); the higher end of the sieve drum is a feed end, and the end is provided with a feed hopper (1), which is inside the sieve drum The cavity is divided into a first broken bag area (2), a first screening section (6), a second broken bag section (7), a second screening section (8), and drying from the feeding end to the discharging end. Zone (11); wherein, the inner wall of the first bag breaking zone (2) and the second bag breaking zone (7) are provided with n vertical knives (3) having the same skew angle, 3 ≤ n ≤ 20, The broken knife (3) is 50-150mm high and 30-100mm wide. The cutting edge is curved and has a certain degree of skewness. The skew angle of the blade is the same as the tilt angle α of the drum, and the cutting edge meets the garbage rolling. Direction; first screen segment (6) and Two screen section (8) with a cylinder wall a number of small circular profile, a first sieving section (6) The pore diameter is d1, The diameter of the small hole of the second sieve section (8) is d2, d2>d1, The outer peripheral surface of the screening drum is provided with a plurality of radial reinforcing hoops (5); the bottom of the discharging end of the screening drum is provided with a discharging port (14), and the end of the discharging end is provided with a temperature controlling plate (13), and the temperature controlling plate (13) fixed at the end of the discharge end, the outer side of which is connected to the burner (15) through a conical cylinder; the temperature control plate (13) is provided with a plurality of temperature control holes on the surface.
- 根据权利要求1所述的一种生活垃圾破筛烘一体式装置,其特征在于:支撑装置由位于筛分滚筒进料端的前支撑架(4)和位于筛分滚筒出料端的后支撑架(12)构成,前支撑架(4)、后支撑架(12)上均设有支撑轮,筛分滚筒进、出料端分别置于相应的支撑轮上。A domestic waste screen-drying integrated device according to claim 1, wherein the supporting device comprises a front support frame (4) at the feeding end of the screening drum and a rear support frame at the discharge end of the screening drum ( 12) The front support frame (4) and the rear support frame (12) are respectively provided with support wheels, and the inlet and discharge ends of the screening drum are respectively placed on the corresponding support wheels.
- 根据权利要求1所述的一种生活垃圾破筛烘一体式装置,其特征在于:动力装置为动力电机(10)。A domestic waste screen-drying integrated device according to claim 1, wherein the power unit is a power motor (10).
- 根据权利要求1所述的一种生活垃圾破筛烘一体式装置,其特征在于:筛分滚筒由动力齿轮(9)、减速机和动力电机(10)带动,筛分滚筒转速为m,3≤m≤24。 The integrated waste screen drying and drying device according to claim 1, wherein the screening drum is driven by a power gear (9), a speed reducer and a power motor (10), and the speed of the screening drum is m, 3 ≤m≤24.
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