CN202576178U - Sludge drying treatment device with low energy consumption - Google Patents

Sludge drying treatment device with low energy consumption Download PDF

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CN202576178U
CN202576178U CN201120528077.8U CN201120528077U CN202576178U CN 202576178 U CN202576178 U CN 202576178U CN 201120528077 U CN201120528077 U CN 201120528077U CN 202576178 U CN202576178 U CN 202576178U
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sludge
conveyor belt
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drying treatment
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黄超群
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    • YGENERAL 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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    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

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Abstract

本实用新型公开一种低能耗污泥干燥处理装置,包括干燥窑,所述干燥窑的上部设置有污泥斗,所述干燥窑的下部设置有污泥出口,所述干燥窑的下侧部设置有进风口,所述干燥窑的顶部设置有出风口,所述干燥窑的内部设置有多层网格状输送带,所述相邻的网格状输送带的运动方向相反,上一层的所述网格状输送带的污泥落入下一层的所述网格状输送带上。与现有技术相比,本实用新型提供的低能耗污泥干燥处理装置,热交换效率高,干燥污泥的产量高,可以降低能耗,且污泥不会堵塞设备,不会产生大量的细尘。

Figure 201120528077

The utility model discloses a low-energy sludge drying treatment device, which comprises a drying kiln, a sludge hopper is arranged on the upper part of the drying kiln, a sludge outlet is arranged on the lower part of the drying kiln, and a sludge outlet is arranged on the lower part of the drying kiln. An air inlet is provided, an air outlet is provided on the top of the drying kiln, and a multi-layer mesh conveyor belt is arranged inside the drying kiln, and the movement directions of the adjacent mesh conveyor belts are opposite, and the upper layer The sludge on the grid-like conveyor belt falls on the grid-like conveyor belt of the next layer. Compared with the prior art, the low-energy sludge drying treatment device provided by the utility model has high heat exchange efficiency, high output of dried sludge, can reduce energy consumption, and the sludge will not block the equipment and will not generate a large amount of fine dust.

Figure 201120528077

Description

一种低能耗污泥干燥处理装置A low-energy sludge drying treatment device

技术领域 technical field

本实用新型涉及污泥处理设备领域,确切地说是指一种低能耗污泥干燥处理装置。  The utility model relates to the field of sludge treatment equipment, in particular to a low-energy sludge drying treatment device. the

背景技术 Background technique

废水处理后产生的沉淀物、颗粒物和漂浮物等物质,统称为污泥。土地还原是我国目前污泥处理处置最主要的方法。随着污泥量不断增加,土地资源越来越紧缺,单纯的土地还原处理已不能满足需要,加之污泥含有多种有毒有害物质,不能直接作肥料或土壤改良剂,用土地还原处理又会留下新的环境问题。目前,无论是喷动式污泥干燥装置还是滚筒式干燥装置都不能普遍推广,其主要有以下缺点:  Substances such as sediment, particulate matter and floating matter produced after wastewater treatment are collectively referred to as sludge. Land reduction is currently the most important method for sludge treatment and disposal in my country. As the amount of sludge continues to increase, land resources are becoming more and more scarce. Simple land reduction treatment can no longer meet the needs. In addition, sludge contains a variety of toxic and harmful substances, which cannot be directly used as fertilizers or soil improvers. leaving new environmental problems. At present, neither the spraying sludge drying device nor the drum drying device can be widely promoted, and its main disadvantages are as follows:

1、热交换效率低,干燥污泥的产量低;  1. Low heat exchange efficiency and low output of dried sludge;

2、能耗高,系统阻力在7000Pa以上,每吨湿污泥(80%含水率)干燥到30%含水率需要耗电110度以上;  2. The energy consumption is high, the system resistance is above 7000Pa, and each ton of wet sludge (80% moisture content) needs to consume more than 110 degrees of electricity to dry to 30% moisture content;

3、在干燥过程中处于半干的污泥粘结力极强,造成设备堵塞影响产量,采用机械清扫设备磨损严重,影响设备使用寿命,维修量大;  3. During the drying process, the semi-dry sludge has a strong cohesive force, which causes equipment blockage and affects the output. Mechanical cleaning equipment is severely worn, which affects the service life of the equipment and requires a large amount of maintenance;

4、喷动式干燥由于流速高(喷动流速在39米/秒,烟气混合物上升流速在17米/秒),产生扬尘,系统需配备除尘设备,增加了设备投资。  4. Due to the high flow rate of the spray drying (the spray flow rate is 39 m/s, and the rising flow rate of the flue gas mixture is 17 m/s), dust is generated. The system needs to be equipped with dust removal equipment, which increases equipment investment. the

实用新型内容 Utility model content

针对上述缺陷,本实用新型解决的技术问题在于提供一种低能耗污泥干燥处理装置,热交换效率高,干燥污泥的产量高,可以降低能耗,且污泥不会堵 塞设备,不会产生大量的细尘。  In view of the above-mentioned defects, the technical problem solved by the utility model is to provide a low-energy sludge drying treatment device, which has high heat exchange efficiency, high output of dried sludge, can reduce energy consumption, and the sludge will not block the equipment, and will not Large amounts of fine dust are generated. the

为了解决以上的技术问题,本实用新型提供的低能耗污泥干燥处理装置,包括干燥窑,所述干燥窑的上部设置有污泥斗,所述干燥窑的下部设置有污泥出口,所述干燥窑的下侧部设置有进风口,所述干燥窑的顶部设置有出风口,所述干燥窑的内部设置有多层网格状输送带,所述相邻的网格状输送带的运动方向相反,上一层的所述网格状输送带的污泥落入下一层的所述网格状输送带上。  In order to solve the above technical problems, the low-energy sludge drying treatment device provided by the utility model includes a drying kiln, the upper part of the drying kiln is provided with a sludge bucket, and the lower part of the drying kiln is provided with a sludge outlet. The lower side of the drying kiln is provided with an air inlet, the top of the drying kiln is provided with an air outlet, and the inside of the drying kiln is provided with a multi-layer grid conveyor belt, and the movement of the adjacent grid conveyor belts The direction is opposite, and the sludge on the grid-like conveyor belt of the upper layer falls onto the grid-like conveyor belt of the next layer. the

优选地,所述污泥斗内设置有污泥分料机构,所述污泥分料机构包括两个旋转方向相反的转子,所述转子上设置有相互啮合的分料耙齿。  Preferably, a sludge distributing mechanism is provided in the sludge hopper, and the sludge distributing mechanism includes two rotors with opposite rotation directions, and the rotors are provided with distributing rakes meshing with each other. the

优选地,所述污泥斗的出料口处设置有污泥整平辊,所述污泥整平辊上设置有整平耙齿。  Preferably, a sludge leveling roller is provided at the outlet of the sludge hopper, and leveling rake teeth are arranged on the sludge leveling roller. the

优选地,所述网格状输送带的层数为2-30层。  Preferably, the number of layers of the mesh conveyor belt is 2-30 layers. the

优选地,所述网格状输送带的末端设置有污泥吹落气管,所述气管上设置有出气孔。  Preferably, a sludge blowing-off air pipe is provided at the end of the mesh conveyor belt, and an air outlet is provided on the air pipe. the

优选地,所述网格状输送带设置有托杆,所述托杆托住所述网格状输送带的上循环带。  Preferably, the grid-like conveyor belt is provided with a support rod, and the support rod supports the upper endless belt of the grid-like conveyor belt. the

优选地,所述网格状输送带设置有振杆,所述振杆托住所述网格状输送带的下循环带。  Preferably, the grid-like conveyor belt is provided with vibrating rods, and the vibration rods support the lower endless belt of the grid-like conveyor belt. the

优选地,所述干燥窑的下部为斗状结构,所述污泥出口处设置有干料输送机。  Preferably, the lower part of the drying kiln is a bucket-shaped structure, and a dry material conveyor is arranged at the sludge outlet. the

优选地,所述进风口通过进风管路与热风源连接,所述进风管路上设置有 风机。  Preferably, the air inlet is connected to a hot air source through an air inlet pipeline, and a blower fan is arranged on the air inlet pipeline. the

优选地,所述出风口通过出风管路与废气处理机构连接,所述出风口设置有脱水机构,所述出风管路上设置有风机。  Preferably, the air outlet is connected to the exhaust gas treatment mechanism through an air outlet pipeline, the air outlet is provided with a dehydration mechanism, and the air outlet pipeline is provided with a fan. the

本实用新型提供的低能耗污泥干燥处理装置,污泥通过污泥斗进入到干燥窑内的网格状输送带上,相邻的网格状输送带的运动方向相反,上一层的所述网格状输送带的污泥落入下一层的所述网格状输送带上,由于输送带是带有孔洞的网格状结构,热风通过下侧部的进风口进入,热风通过网格状输送带的孔洞从下往下运动,与含水量较高的污泥进行热交换,将污泥的水分烘干并将污泥干燥,最后带有水分的热风从干燥窑的顶部出风口流出。且由于热风流速低,经污泥层向上流动时不会带走扬尘,即有少量扬尘在经过湿污泥层时将由湿污泥吸附,使得热风的含尘量很少,能够达标排放。与现有技术相比,本实用新型提供的低能耗污泥干燥处理装置,热交换效率高,干燥污泥的产量高,可以降低能耗,且污泥不会堵塞设备,不会产生大量的细尘。  In the low-energy sludge drying treatment device provided by the utility model, the sludge enters the grid-shaped conveyor belt in the drying kiln through the sludge hopper, and the movement direction of the adjacent grid-shaped conveyor belt is opposite, and all the sludge on the upper layer The sludge on the grid conveyor belt falls onto the grid conveyor belt on the next layer. Since the conveyor belt has a grid structure with holes, the hot air enters through the air inlet on the lower side, and the hot air passes through the mesh. The holes of the lattice conveyor belt move from bottom to bottom, exchange heat with the sludge with high water content, dry the moisture of the sludge and dry the sludge, and finally the hot air with moisture comes out from the top air outlet of the drying kiln flow out. And because of the low flow rate of the hot air, it will not take away the dust when it flows upward through the sludge layer, that is, a small amount of dust will be absorbed by the wet sludge when it passes through the wet sludge layer, so that the dust content of the hot air is very small and can be discharged up to the standard. Compared with the prior art, the low-energy sludge drying treatment device provided by the utility model has high heat exchange efficiency, high output of dried sludge, can reduce energy consumption, and the sludge will not block the equipment and will not generate a large amount of fine dust. the

附图说明 Description of drawings

图1为本实用新型实施例1中低能耗污泥干燥处理装置的结构示意图;  Fig. 1 is the structure schematic diagram of low energy consumption sludge drying treatment device in embodiment 1 of the present utility model;

图2为本实用新型实施例2中低能耗污泥干燥处理装置的结构示意图;  Fig. 2 is a schematic structural view of a low-energy sludge drying treatment device in Example 2 of the utility model;

图3为本实用新型实施例3中低能耗污泥干燥处理装置的结构示意图。  Fig. 3 is a schematic structural diagram of a low-energy sludge drying treatment device in Example 3 of the present utility model. the

具体实施方式 Detailed ways

为了本领域的技术人员能够更好地理解本实用新型所提供的技术方案,下面结合具体实施例进行阐述。  In order for those skilled in the art to better understand the technical solutions provided by the utility model, the following will be described in conjunction with specific embodiments. the

实施例1  Example 1

请参见图1,该图为本实用新型实施例1中低能耗污泥干燥处理装置的结构示意图。  Please refer to Fig. 1, which is a schematic structural diagram of a low-energy sludge drying treatment device in Example 1 of the present utility model. the

本实用新型提供的低能耗污泥干燥处理装置,包括干燥窑1,干燥窑1的上部设置有污泥斗4,干燥窑1的下部设置有污泥出口,干燥窑1的下侧部设置有进风口11,干燥窑1的顶部设置有出风口,干燥窑1的内部设置有5层网格状输送带7,相邻的网格状输送带7的运动方向相反,上一层的网格状输送带7的污泥落入下一层的网格状输送带7上。  The low energy consumption sludge drying treatment device provided by the utility model comprises a drying kiln 1, the upper part of the drying kiln 1 is provided with a sludge bucket 4, the lower part of the drying kiln 1 is provided with a sludge outlet, and the lower part of the drying kiln 1 is provided with a The air inlet 11, the top of the drying kiln 1 is provided with an air outlet, and the inside of the drying kiln 1 is provided with 5 layers of grid-shaped conveyor belts 7, the movement direction of the adjacent grid-shaped conveyor belts 7 is opposite, and the grid of the upper layer The sludge on the grid-shaped conveyor belt 7 falls on the grid-shaped conveyor belt 7 of the next layer. the

污泥斗4内设置有污泥分料机构5,污泥分料机构包括两个旋转方向相反的转子,转子上设置有相互啮合的分料耙齿。污泥分料机构5将污泥均匀铺设在网格状输送带上。  A sludge distributing mechanism 5 is arranged inside the sludge hopper 4, and the sludge distributing mechanism includes two rotors with opposite rotation directions, and mutually meshing distributing rake teeth are arranged on the rotors. The sludge distributing mechanism 5 spreads the sludge evenly on the grid conveyor belt. the

污泥斗4的出料口处设置有污泥整平辊6,污泥整平辊6上设置有整平耙齿,整平耙齿将铺设在网格状输送带7的污泥均匀耙成细条状,既有利于热风吹入,又有利于增加污泥的表面积,提高热交换效率。  A sludge leveling roller 6 is arranged at the outlet of the sludge hopper 4, and the sludge leveling roller 6 is provided with leveling rake teeth, which evenly rake the sludge laid on the mesh conveyor belt 7 Formed into thin strips, it is not only conducive to the blowing of hot air, but also conducive to increasing the surface area of the sludge and improving the heat exchange efficiency. the

网格状输送带7的末端设置有污泥吹落气管10,气管10上设置有出气孔,污泥吹落气管10可以通过气压将附着在网格状输送带7上的污泥吹落,防止污泥粘结网格状输送带7上。  The end of the mesh conveyor belt 7 is provided with a sludge blowing off air pipe 10, and the air pipe 10 is provided with an air outlet, and the sludge blowing off air pipe 10 can blow off the sludge attached to the mesh conveyor belt 7 by air pressure, Prevent sludge from adhering to the mesh conveyor belt 7. the

网格状输送带7设置有托杆8,托杆8托住网格状输送带7的上循环带,可以防止网格状输送带7的上循环带下垂。  Grid conveyor belt 7 is provided with support bar 8, and support bar 8 supports the upper loop belt of grid conveyor belt 7, can prevent the upper loop belt of grid conveyor belt 7 from sagging. the

网格状输送带7设置有方形振杆9,方形振杆9托住网格状输送带7的下循环带,既可以托住网格状输送带7的下循环带,又可以使网格状输送带7的下循环带产生自振动,进一步振下粘在网格状输送带7上的污泥。  The grid conveyor belt 7 is provided with a square vibrating rod 9, and the square vibrating rod 9 supports the lower circulation belt of the grid conveyor belt 7, which can hold the lower circulation belt of the grid conveyor belt 7 and make the grid The lower circulation belt of grid-shaped conveyor belt 7 produces self-vibration, and further vibrates the sludge stuck on grid-shaped conveyor belt 7. the

干燥窑1的下部为斗状结构,污泥出口处设置有干料输送机16,有利于干燥污泥的输送。  The lower part of the drying kiln 1 is a bucket-shaped structure, and a dry material conveyor 16 is arranged at the sludge outlet, which is beneficial to the conveyance of the dried sludge. the

进风口11通过进风管路与热风源13连接,风机12设置在进风管路上。出风口通过出风管路与废气处理机构15连接,出风口设置有脱水机构14。  The air inlet 11 is connected with the hot air source 13 through the air inlet pipeline, and the fan 12 is arranged on the air inlet pipeline. The air outlet is connected to the waste gas treatment mechanism 15 through the air outlet pipeline, and the air outlet is provided with a dehydration mechanism 14 . the

本实用新型提供的低能耗污泥干燥处理装置,污泥在污泥池2通过湿料输送机3进入污泥斗4,再通过污泥斗4进入到干燥窑内的网格状输送带7上,相邻的网格状输送带7的运动方向相反,上一层的所述网格状输送带7的污泥落入下一层的所述网格状输送带7上,由于输送带是带有孔洞的网格状结构,热风通过下侧部的进风口11进入,热风通过网格状输送带7的孔洞从下往下运动,与含水量较高的污泥进行热交换,将污泥的水分烘干并将污泥干燥,最后带有水分的热风从干燥窑的顶部出风口流出。且由于热风流速低,经污泥层向上流动时不会带走扬尘,即有少量扬尘在经过湿污泥层时将由湿污泥吸附,使得热风的含尘量很少,能够达标排放。  In the low-energy sludge drying treatment device provided by the utility model, the sludge enters the sludge bucket 4 through the wet material conveyor 3 in the sludge pool 2, and then enters the grid-shaped conveyor belt 7 in the drying kiln through the sludge bucket 4 Above, the moving direction of the adjacent grid-shaped conveyor belt 7 is opposite, and the sludge of the grid-shaped conveyor belt 7 on the upper layer falls on the grid-shaped conveyor belt 7 of the next layer, because the conveyor belt It is a grid-like structure with holes. The hot air enters through the air inlet 11 on the lower side, and the hot air moves from bottom to bottom through the holes of the grid-like conveyor belt 7 to exchange heat with the sludge with high water content. The moisture of the sludge is dried and the sludge is dried, and finally the hot air with moisture flows out from the top air outlet of the drying kiln. And because of the low flow rate of the hot air, it will not take away the dust when it flows upward through the sludge layer, that is, a small amount of dust will be absorbed by the wet sludge when it passes through the wet sludge layer, so that the dust content of the hot air is very small and can be discharged up to the standard. the

与现有技术相比,本实用新型提供的低能耗污泥干燥处理装置,热交换效率高,干燥污泥的产量高,可以降低能耗,且污泥不会堵塞设备,不会产生大量的细尘,具体而言,具有以下优点:  Compared with the prior art, the low-energy sludge drying treatment device provided by the utility model has high heat exchange efficiency, high output of dried sludge, can reduce energy consumption, and the sludge will not block the equipment and will not generate a large amount of Fine dust, specifically, has the following advantages:

1、高效节能技术适用于膏糊状、滤饼等物料的直接快速干燥。  1. The high-efficiency and energy-saving technology is suitable for direct and rapid drying of paste, filter cake and other materials. the

2、密闭性好,干化过程中不增加氧含量,几乎与烟道气含氧量相同,消除了污泥在干化过程中爆燃的可能性。  2. The airtightness is good, the oxygen content is not increased during the drying process, which is almost the same as the oxygen content of the flue gas, eliminating the possibility of sludge deflagration during the drying process. the

3、不会粘结设备,可采用聚四氟乙稀、钢网带或其他耐高温非金属材料网带不易粘结且有喷吹风及拍打网格状输送带,使得粘在网格状输送带上的污 泥快速脱落。  3. It will not stick to the equipment. It can use polytetrafluoroethylene, steel mesh belt or other high temperature resistant non-metallic material. The sludge on the belt falls off quickly. the

4、逆流干造,且平铺污泥小于5mm,根据产量可做多层网格状输送带结构,使得污泥接触面积大,干燥时热烟气与污泥接触时间长,热交换效率高、产量高。  4. Countercurrent drying, and the flat sludge is less than 5mm. According to the output, it can be made into a multi-layer mesh conveyor belt structure, so that the sludge contact area is large, the hot flue gas and the sludge contact for a long time during drying, and the heat exchange efficiency is high. ,High Yield. the

5、逆流干造,采用污泥分料机构和污泥整平辊使污泥平铺均匀分布,相当于滤袋除尘,不产生扬尘,排放干净。  5. Countercurrent dry manufacturing, the sludge distribution mechanism and sludge leveling roller are used to spread the sludge evenly, which is equivalent to filter bag dust removal, does not generate dust, and discharges cleanly. the

6、系统阻力小(小于2000Pa)能耗低,比传统的喷动干燥要降低70%的能耗。  6. The system resistance is small (less than 2000Pa) and the energy consumption is low, which is 70% lower than the traditional spray drying. the

7、本低能耗干燥机设计紧凑,体积小,投资低。  7. This low energy consumption dryer has compact design, small volume and low investment. the

8、当用户干燥量大而用地有限时,装置可以向空中发展,占地面积小。  8. When the user has a large amount of drying and the land is limited, the device can be developed in the air, and the occupied area is small. the

9、采用以废治废的方式对污泥进行干燥,不但降低污泥干化处理成本,同时利用锅炉烟气废热,将含水率80%左右的湿污泥干化成15-30%的干污泥,然后采用输送装置送入锅炉中进行燃烧,将污泥中热值转化为热能资源进行有效利用,实现以废治废回收热能的目的。  9. The method of waste treatment is used to dry the sludge, which not only reduces the cost of sludge drying treatment, but also uses the waste heat of boiler flue gas to dry the wet sludge with a moisture content of about 80% into 15-30% dry sewage The sludge is then sent to the boiler by a conveying device for combustion, and the calorific value in the sludge is converted into thermal energy resources for effective use, so as to realize the purpose of waste treatment and waste recovery of heat energy. the

10、干燥后的污泥送入锅炉经高温燃烧后,完全分解成无害物质,实现了最终无害化处理,防止二次污染。  10. After the dried sludge is sent to the boiler for high-temperature combustion, it will be completely decomposed into harmless substances, realizing the final harmless treatment and preventing secondary pollution. the

11、实现了低碳排放,减少温室气体的产生。  11. Realized low-carbon emissions and reduced greenhouse gas production. the

12、有效的回收了污泥内的可燃物(生活污泥低位热值1500Kcal/Kg以上,印染污泥低位热值1800Kcal/Kg以上,造纸污泥低位热值2000Kcal/Kg以上,饮料食品行业的废水污泥都有很高的热值)真正实现了以废治废、变废为宝的环境治理理念。  12. Effective recovery of combustibles in the sludge (the low calorific value of domestic sludge is more than 1500Kcal/Kg, the lower calorific value of printing and dyeing sludge is more than 1800Kcal/Kg, the lower calorific value of papermaking sludge is more than 2000Kcal/Kg, the beverage and food industry Wastewater sludge has a high calorific value) has truly realized the environmental management concept of treating waste and turning waste into treasure. the

实施例2  Example 2

请参见图2,该图为本实用新型实施例2中低能耗污泥干燥处理装置的结构示意图。进风口11通过进风管路与热风源13连接。出风口通过出风管路与废气处理机构15连接,出风口设置有脱水机构14,风机12设置在出风管路上。  Please refer to Fig. 2, which is a schematic structural diagram of a low-energy sludge drying treatment device in Example 2 of the present utility model. The air inlet 11 is connected with the hot air source 13 through an air inlet pipeline. The air outlet is connected to the waste gas treatment mechanism 15 through the air outlet pipeline, the air outlet is provided with a dehydration mechanism 14, and the fan 12 is arranged on the air outlet pipeline. the

实施例3  Example 3

请参见图3,该图为本实用新型实施例3中低能耗污泥干燥处理装置的结构示意图。进风口11通过进风管路与热风源13连接,风机12设置在进风管路上。出风口通过出风管路与废气处理机构15连接,出风口设置有脱水机构14,风机12设置在出风管路上。  Please refer to FIG. 3 , which is a schematic structural diagram of a low-energy sludge drying treatment device in Embodiment 3 of the present utility model. The air inlet 11 is connected with the hot air source 13 through the air inlet pipeline, and the fan 12 is arranged on the air inlet pipeline. The air outlet is connected to the waste gas treatment mechanism 15 through the air outlet pipeline, the air outlet is provided with a dehydration mechanism 14, and the fan 12 is arranged on the air outlet pipeline. the

对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本实用新型。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本实用新型的精神或范围的情况下,在其它实施例中实现。因此,本实用新型将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。  The above description of the disclosed embodiments enables those skilled in the art to realize or use the utility model. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention will not be limited to these embodiments shown herein, but will conform to the widest scope consistent with the principles and novel features disclosed herein. the

Claims (10)

1.一种低能耗污泥干燥处理装置,其特征在于,包括干燥窑,所述干燥窑的上部设置有污泥斗,所述干燥窑的下部设置有污泥出口,所述干燥窑的下侧部设置有进风口,所述干燥窑的顶部设置有出风口,所述干燥窑的内部设置有多层网格状输送带,所述相邻的网格状输送带的运动方向相反,上一层的所述网格状输送带的污泥落入下一层的所述网格状输送带上。 1. A low-energy sludge drying treatment device, characterized in that it comprises a drying kiln, the top of the drying kiln is provided with a sludge bucket, the bottom of the drying kiln is provided with a sludge outlet, and the bottom of the drying kiln The side is provided with an air inlet, and the top of the drying kiln is provided with an air outlet. The inside of the drying kiln is provided with a multi-layer mesh conveyor belt, and the moving directions of the adjacent mesh conveyor belts are opposite. The sludge of the mesh conveyor belt of one layer falls onto the mesh conveyor belt of the next layer. 2.根据权利要求1所述的低能耗污泥干燥处理装置,其特征在于,所述污泥斗内设置有污泥分料机构,所述污泥分料机构包括两个旋转方向相反的转子,所述转子上设置有相互啮合的分料耙齿。 2. The low-energy sludge drying treatment device according to claim 1, wherein a sludge distribution mechanism is arranged in the sludge hopper, and the sludge distribution mechanism includes two rotors with opposite rotation directions , the rotor is provided with intermeshing distribution rake teeth. 3.根据权利要求1所述的低能耗污泥干燥处理装置,其特征在于,所述污泥斗的出料口处设置有污泥整平辊,所述污泥整平辊上设置有整平耙齿。 3. The low-energy sludge drying treatment device according to claim 1, wherein a sludge leveling roller is arranged at the outlet of the sludge hopper, and a leveling roller is arranged on the sludge leveling roller. Flat tines. 4.根据权利要求1所述的低能耗污泥干燥处理装置,其特征在于,所述网格状输送带的层数为2-30层。 4. The low-energy sludge drying treatment device according to claim 1, characterized in that, the number of layers of the mesh conveyor belt is 2-30 layers. 5.根据权利要求1所述的低能耗污泥干燥处理装置,其特征在于,所述网格状输送带的末端设置有污泥吹落气管,所述气管上设置有出气孔。 5 . The low-energy sludge drying treatment device according to claim 1 , characterized in that, the end of the grid-shaped conveyor belt is provided with a sludge blow-off air pipe, and the air pipe is provided with an air outlet. 5 . 6.根据权利要求1所述的低能耗污泥干燥处理装置,其特征在于,所述网格状输送带设置有托杆,所述托杆托住所述网格状输送带的上循环带。 6. The low-energy sludge drying treatment device according to claim 1, characterized in that, the grid-shaped conveyor belt is provided with a support rod, and the support rod supports the upper circulation belt of the grid-shaped conveyor belt. 7.根据权利要求1所述的低能耗污泥干燥处理装置,其特征在于,所述网格状输送带设置有振杆,所述振杆托住所述网格状输送带的下循环带。 7. The low-energy sludge drying treatment device according to claim 1, characterized in that, the grid-shaped conveyor belt is provided with vibrating rods, and the vibrating rods support the lower circulation belt of the grid-shaped conveyor belt. 8.根据权利要求1所述的低能耗污泥干燥处理装置,其特征在于,所述干燥窑的下部为斗状结构,所述污泥出口处设置有干料输送机。  8. The low-energy sludge drying treatment device according to claim 1, characterized in that, the lower part of the drying kiln is a bucket-shaped structure, and a dry material conveyor is arranged at the sludge outlet. the 9.根据权利要求1所述的低能耗污泥干燥处理装置,其特征在于,所述进风口通过进风管路与热风源连接,所述进风管路上设置有风机。 9. The low-energy sludge drying treatment device according to claim 1, wherein the air inlet is connected to a hot air source through an air inlet pipeline, and a fan is arranged on the air inlet pipeline. 10.根据权利要求1所述的低能耗污泥干燥处理装置,其特征在于,所述出风口通过出风管路与废气处理机构连接,所述出风口设置有脱水机构,所述出风管路上设置有风机。  10. The low-energy sludge drying treatment device according to claim 1, characterized in that, the air outlet is connected to the exhaust gas treatment mechanism through an air outlet pipeline, the air outlet is provided with a dehydration mechanism, and the air outlet pipe There is a fan on the road. the
CN201120528077.8U 2011-12-15 2011-12-15 Sludge drying treatment device with low energy consumption Expired - Lifetime CN202576178U (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103964671A (en) * 2013-01-25 2014-08-06 宝山钢铁股份有限公司 Sludge drying apparatus and method for drying sludge by using sludge drying apparatus
TWI616407B (en) * 2017-01-25 2018-03-01 辰灝股份有限公司 organic sludge combustion equipment
CN109626792A (en) * 2019-02-18 2019-04-16 韩国综合技术有限公司 Sludge dewatering and drying unit
CN110156296A (en) * 2018-02-11 2019-08-23 北京市水利规划设计研究院 Mud drying device and sludge drying method
CN110551549A (en) * 2019-09-10 2019-12-10 浙江富春江环保热电股份有限公司 Device and method for preparing sludge-biomass particle fuel rod
CN110567266A (en) * 2019-09-16 2019-12-13 谢樱 Novel thermal desorption device
CN111875202A (en) * 2020-09-08 2020-11-03 湖南大湘农环境科技股份有限公司 A circulating rake type sewage fermentation treatment equipment

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103964671A (en) * 2013-01-25 2014-08-06 宝山钢铁股份有限公司 Sludge drying apparatus and method for drying sludge by using sludge drying apparatus
CN103964671B (en) * 2013-01-25 2015-12-09 宝山钢铁股份有限公司 A kind of mud drying device and utilize the method for this device dewatered sludge
TWI616407B (en) * 2017-01-25 2018-03-01 辰灝股份有限公司 organic sludge combustion equipment
CN110156296A (en) * 2018-02-11 2019-08-23 北京市水利规划设计研究院 Mud drying device and sludge drying method
CN109626792A (en) * 2019-02-18 2019-04-16 韩国综合技术有限公司 Sludge dewatering and drying unit
CN110551549A (en) * 2019-09-10 2019-12-10 浙江富春江环保热电股份有限公司 Device and method for preparing sludge-biomass particle fuel rod
CN110567266A (en) * 2019-09-16 2019-12-13 谢樱 Novel thermal desorption device
CN110567266B (en) * 2019-09-16 2024-04-26 谢樱 Novel thermal analysis device
CN111875202A (en) * 2020-09-08 2020-11-03 湖南大湘农环境科技股份有限公司 A circulating rake type sewage fermentation treatment equipment

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