CN106746473A - For the dry belt drying system of sludge from wastewater treatment plant and drying means - Google Patents
For the dry belt drying system of sludge from wastewater treatment plant and drying means Download PDFInfo
- Publication number
- CN106746473A CN106746473A CN201710194815.1A CN201710194815A CN106746473A CN 106746473 A CN106746473 A CN 106746473A CN 201710194815 A CN201710194815 A CN 201710194815A CN 106746473 A CN106746473 A CN 106746473A
- Authority
- CN
- China
- Prior art keywords
- sludge
- drying
- conveyer
- cage
- belt
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000001035 drying Methods 0.000 title claims abstract description 93
- 239000010802 sludge Substances 0.000 title claims abstract description 73
- 238000004065 wastewater treatment Methods 0.000 title claims 12
- 230000007246 mechanism Effects 0.000 claims abstract description 64
- 239000003638 chemical reducing agent Substances 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 claims 2
- 238000013019 agitation Methods 0.000 claims 1
- 239000010865 sewage Substances 0.000 abstract description 10
- 239000006185 dispersion Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000003756 stirring Methods 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 6
- 230000032258 transport Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000009827 uniform distribution Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000009826 distribution Methods 0.000 description 1
- 238000010981 drying operation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/001—Runoff or storm water
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
- Drying Of Solid Materials (AREA)
Abstract
本发明涉及用于城市污水处理厂污泥干燥的带式干燥系统,包括将污泥搅拌并从低处输送至高处的绞笼输送机构,将绞笼输送机构输出的污泥均匀分布的分散机构,将分散机构输出的污泥传送的干燥输送带机构,位于干燥输送带机构末端的集料斗,装有抽风装置的干燥间;绞笼输送机构、分散机构、干燥输送带机构、集料斗均位于干燥间内。还涉及用于城市污水处理厂污泥干燥的带式干燥方法。本发明提高干空气利用率和干燥效率,减少干燥过程中的臭味,实现低能耗和环境保护的效果,属于污泥干燥技术领域。
The invention relates to a belt-type drying system for sludge drying in urban sewage treatment plants, including a twisted cage conveying mechanism for stirring the sludge and transporting it from a low place to a high place, and a dispersion mechanism for evenly distributing the sludge output by the twisted cage conveying mechanism , the drying conveyor belt mechanism that conveys the sludge output by the dispersing mechanism, the collecting hopper at the end of the drying conveyor belt mechanism, and the drying room equipped with an exhaust device; In the drying room. It also relates to a belt drying method for sludge drying in urban sewage treatment plants. The invention improves the dry air utilization rate and drying efficiency, reduces the odor in the drying process, realizes the effects of low energy consumption and environmental protection, and belongs to the technical field of sludge drying.
Description
技术领域technical field
本发明涉及污泥干燥技术,具体涉及一种用于城市污水处理厂污泥干燥的带式干燥系统和干燥方法。The invention relates to sludge drying technology, in particular to a belt drying system and drying method for sludge drying in urban sewage treatment plants.
背景技术Background technique
污泥是污水处理的二次产物,随着工业的发展,污泥量不断增加。未经处理的污泥具有体积大、含水率高的特点,不仅会占用大量土地,而且会对土壤、地下水带来二次污染,因而需要对污泥进行进一步处理。在污泥焚烧、填埋和资源化利用等处置方式中,均对污泥含水率有一定要求,含水率在50%以下才能进行焚烧处理,含水率在60%以下才能达到填埋标准,污泥干燥是降低其含水率的关键环节之一。经干燥后的污泥,含水率降低,体积减小,便于运输、储存和利用。Sludge is a secondary product of sewage treatment. With the development of industry, the amount of sludge is increasing. Untreated sludge has the characteristics of large volume and high water content, which not only occupies a large amount of land, but also causes secondary pollution to soil and groundwater, so further treatment of sludge is required. In the disposal methods of sludge incineration, landfill, and resource utilization, there are certain requirements for the moisture content of sludge. The incineration treatment can only be carried out if the moisture content is below 50%, and the landfill standard can only be reached if the moisture content is below 60%. Mud drying is one of the key links to reduce its moisture content. The dried sludge has lower water content and smaller volume, which is convenient for transportation, storage and utilization.
目前,市场上已有的带式干燥机虽可以达到降低污泥含水率的效果,但存在加料不均匀,干空气利用率低,干燥效率低等缺点。At present, although the existing belt dryers on the market can achieve the effect of reducing the moisture content of sludge, they have disadvantages such as uneven feeding, low utilization rate of dry air, and low drying efficiency.
发明内容Contents of the invention
针对现有技术中存在的技术问题,本发明的目的是:提供一种布料均匀、干燥效率高、能耗低的用于城市污水处理厂污泥干燥的带式干燥系统和干燥方法。In view of the technical problems existing in the prior art, the purpose of the present invention is to provide a belt drying system and drying method for drying sludge in urban sewage treatment plants with uniform distribution, high drying efficiency and low energy consumption.
为了达到上述目的,本发明采用如下技术方案:In order to achieve the above object, the present invention adopts following technical scheme:
用于城市污水处理厂污泥干燥的带式干燥系统,包括将污泥搅拌并从低处输送至高处的绞笼输送机构,将绞笼输送机构输出的污泥均匀分布的分散机构,将分散机构输出的污泥传送的干燥输送带机构,位于干燥输送带机构末端的集料斗,装有抽风装置的干燥间;绞笼输送机构、分散机构、干燥输送带机构、集料斗均位于干燥间内。The belt drying system used for sludge drying in urban sewage treatment plants includes a twisted cage conveying mechanism that stirs the sludge and transports it from a low place to a high place, and a dispersion mechanism that evenly distributes the sludge output by the twisted cage conveying mechanism. The drying conveyor belt mechanism for conveying the sludge output by the mechanism, the collecting hopper at the end of the drying conveyor belt mechanism, and the drying room equipped with an exhaust device; the twisted cage conveying mechanism, the dispersion mechanism, the drying conveyor belt mechanism, and the collecting hopper are all located in the drying room .
作为一种优选,干燥输送带机构包括多组干燥输送带单元,每组干燥输送带单元均包括一条与水平方向倾斜的传送带,各传送带相互平行且在一个竖直平面内从上往下依次排列,上方传送带的末端位于相邻下侧传送带的首段上方;传送带之间围成空气环流的空间。As a preference, the drying conveyor belt mechanism includes multiple groups of drying conveyor belt units, each group of drying conveyor belt units includes a conveyor belt inclined to the horizontal direction, and the conveyor belts are parallel to each other and arranged in sequence from top to bottom in a vertical plane , the end of the upper conveyor belt is located above the first section of the adjacent lower conveyor belt; a space for air circulation is enclosed between the conveyor belts.
作为一种优选,每组干燥输送带单元均包括一条传送带、两个驱动轮、多个支撑辊轮、两块挡板和调整传送带高低位置的可调支撑架;驱动轮位于传送带的首端和末端,支撑辊轮位于两个驱动轮之间,传送带成环形缠绕在两个驱动轮之间且中间由支撑辊轮支撑,用于安装支撑辊轮的挡板位于传送带的两侧。As a kind of preference, each group of drying conveyer belt unit all comprises a conveyer belt, two driving wheels, a plurality of supporting rollers, two baffles and the adjustable supporting frame of adjusting conveyer belt height position; At the end, the support roller is located between the two driving wheels, the conveyor belt is looped between the two driving wheels and supported by the support roller in the middle, and the baffles for installing the support roller are located on both sides of the conveyor belt.
作为一种优选,位于最上方的传送带为第一段传送带,它的首端的位置低于末端的位置,它的首段位于分散机构的正下方。As a preference, the uppermost conveyor belt is the first conveyor belt, the position of its head end is lower than that of the end, and its head end is located directly below the dispersing mechanism.
作为一种优选,绞笼输送机构包括电机减速机、绞笼输送机、绞笼机架、进料口、出料口;电机减速机与绞笼输送机相接驱动绞笼输送机运行,绞笼输送机通过绞笼机架安装在干燥间内;进料口位于绞笼输送机的下端上侧,出料口位于绞笼输送机的上端下侧。As a preference, the twisted cage conveying mechanism includes a motor reducer, a twisted cage conveyor, a twisted cage frame, a feed inlet, and a discharge port; the motor reducer is connected with the twisted cage conveyor to drive the twisted cage conveyor to run, and the twisted cage conveyor is The cage conveyor is installed in the drying room through the twisted cage frame; the feed inlet is located on the upper side of the lower end of the twisted cage conveyor, and the discharge port is located on the lower side of the upper end of the twisted cage conveyor.
作为一种优选,分散机构包括从上往下依次设置的下料斗、分散器、布料器,分散机构通过分散机构机架安装在干燥间内;分散器内设有将污泥挤压成饼状的挤压构件。As a preference, the dispersing mechanism includes a lower hopper, a disperser, and a distributor arranged sequentially from top to bottom, and the dispersing mechanism is installed in the drying room through the frame of the dispersing mechanism; extrusion components.
作为一种优选,干燥间设有进风口和出风口,进风口位于干燥间的一侧的下端,出风口位于干燥间的另一侧的上端,出风口装有抽风装置。As a preference, the drying room is provided with an air inlet and an air outlet, the air inlet is located at the lower end of one side of the drying room, the air outlet is located at the upper end of the other side of the drying room, and the air outlet is equipped with a draft device.
作为一种优选,在俯视方向上,传送带与绞笼输送机构倾斜设置,两者的交点位于分散机构。As a preference, in a plan view direction, the conveyor belt and the cage conveying mechanism are arranged obliquely, and the intersection of the two is located at the dispersing mechanism.
用于城市污水处理厂污泥干燥的带式干燥方法,采用用于城市污水处理厂污泥干燥的带式干燥系统,污泥由绞笼输送机构从低处向高处输送至分散机构,分散机构将污泥压成饼状,均匀分布的饼状污泥由干燥输送带机构缓慢输送至集料斗的过程中被常温对流风干。The belt drying method used for sludge drying in urban sewage treatment plants adopts the belt drying system for sludge drying in urban sewage treatment plants. The mechanism presses the sludge into a cake shape, and the evenly distributed cake-shaped sludge is slowly transported to the collecting hopper by the drying conveyor belt mechanism and is air-dried at room temperature by convection.
作为一种优选,污泥由干燥输送带机构输送的过程中,依次经过多条排列在同一竖直面上的传送带,相邻传送带之间围成空气环流的空间,加大了空气的局部环流,提高污泥干燥效率。As a preference, in the process of conveying the sludge by the drying conveyor belt mechanism, it passes through several conveyor belts arranged on the same vertical plane in turn, and the space for air circulation is formed between adjacent conveyor belts, which increases the local circulation of air , Improve sludge drying efficiency.
本发明的原理是:污泥由绞笼输送机构提升,由分散机构压紧和均布,由干燥输送带机构提供一段较长的输送路径,并在输送的过程中在干燥室内低温对流烘干,最终由集料斗收集。The principle of the present invention is: the sludge is lifted by the twisted cage conveying mechanism, compacted and evenly distributed by the dispersing mechanism, a long conveying path is provided by the drying conveyor belt mechanism, and it is dried in the drying chamber by low-temperature convection during the conveying process. , and finally collected by the collection hopper.
总的说来,本发明具有如下优点:Generally speaking, the present invention has following advantages:
(1)布料均匀:待干燥的污泥通过分散机构,经挤压构件后,呈泥饼状,再通过布料器送至传送带,污泥层厚度均匀,达到均匀布料的效果,增加了干燥的均匀度,提高污泥干燥效率。(1) Uniform distribution: The sludge to be dried passes through the dispersing mechanism, and after being extruded by the components, it is in the shape of a mud cake, and then sent to the conveyor belt through the distributor. The thickness of the sludge layer is uniform, achieving the effect of uniform distribution and increasing the drying time. Uniformity, improve sludge drying efficiency.
(2)能耗低:较之于传统的带式高温干燥,低温干燥大幅度减少能耗,达到节能减排的要求,采用多层传送带垂直分布的方式,加大了空气的局部环流,提高空气利用效率,增强其干燥效果。(2) Low energy consumption: Compared with the traditional belt-type high-temperature drying, low-temperature drying greatly reduces energy consumption and meets the requirements of energy saving and emission reduction. The vertical distribution of multi-layer conveyor belts is adopted to increase the local circulation of air and improve Air utilization efficiency enhances its drying effect.
(3)环保:污泥在传统高温干燥操作下,会产生大量臭气,严重影响环境。若不对臭气进行收集处理,会造成二次污染;对其进行处理,又会提高运行成本。而在污泥低温干燥过程中,臭气产生量少,避免了臭气对环境的影响。(3) Environmental protection: Under the traditional high-temperature drying operation, sludge will produce a large amount of odor, which seriously affects the environment. If the odor is not collected and treated, it will cause secondary pollution; if it is treated, it will increase the operating cost. In the low-temperature drying process of sludge, the amount of odor generated is small, which avoids the impact of odor on the environment.
(4)传送带竖向布置,一方面在保证较长输送路线的情况下可节省占地空间,另一方面污泥在层间自然落料传送相当于翻料,有利于污泥干燥,此外还可在传送带间增大空气环流,提升干燥效率。(4) The conveyor belt is vertically arranged. On the one hand, it can save space while ensuring a long conveying route. On the other hand, the sludge is naturally dropped and transported between layers, which is equivalent to turning the material, which is conducive to sludge drying. Increased air circulation between conveyor belts improves drying efficiency.
附图说明Description of drawings
图1是用于城市污水处理厂污泥干燥的带式干燥系统的示意图。Figure 1 is a schematic diagram of a belt drying system for sludge drying in urban sewage treatment plants.
图2是绞笼输送机构、分散机构、干燥输送带机构的俯视图。Fig. 2 is a top view of the twisted cage conveying mechanism, the dispersing mechanism, and the drying conveyor belt mechanism.
图3是支撑辊轮的结构示意图。Fig. 3 is a structural schematic diagram of the support roller.
其中,1是进风口,2是进料口,3是电机减速机,4是绞笼输送机,5-1是绞笼机架,5-2是分散机构机架,6是出料口,7是下料斗,8是分散器,9是挤压构件,10是布料器,11是驱动轮,12是第一段传送带,13为第二段传送带,14为第三段传送带,15为集料斗,16为出风口,17为挡板,18为支撑辊轮,19为可调支撑架,20为辊轮轴,21为卡销。α为传送带与绞笼输送机构在俯视方向上的夹角,β为传送带的倾角。Among them, 1 is the air inlet, 2 is the feed port, 3 is the motor reducer, 4 is the twisted cage conveyor, 5-1 is the twisted cage frame, 5-2 is the dispersion mechanism frame, 6 is the discharge port, 7 is the lower hopper, 8 is the disperser, 9 is the extruding member, 10 is the distributor, 11 is the driving wheel, 12 is the first section of the conveyor belt, 13 is the second section of the conveyor belt, 14 is the third section of the conveyor belt, 15 is the collector Hopper, 16 is an air outlet, 17 is a baffle plate, 18 is a support roller, 19 is an adjustable support frame, 20 is a roller shaft, and 21 is a bayonet pin. α is the angle between the conveyor belt and the twisted cage conveying mechanism in the top view direction, and β is the inclination angle of the conveyor belt.
具体实施方式detailed description
下面来对本发明做进一步详细的说明。The present invention will be described in further detail below.
用于城市污水处理厂污泥干燥的带式干燥系统,包括将污泥搅拌并从低处输送至高处的绞笼输送机构,将绞笼输送机构输出的污泥均匀分布的分散机构,将分散机构输出的污泥传送的干燥输送带机构,位于干燥输送带机构末端的集料斗,装有抽风装置的干燥间;绞笼输送机构、分散机构、干燥输送带机构、集料斗均位于干燥间内。在俯视方向上,传送带与绞笼输送机构倾斜设置,倾角为α,两者的交点位于分散机构。The belt drying system used for sludge drying in urban sewage treatment plants includes a twisted cage conveying mechanism that stirs the sludge and transports it from a low place to a high place, and a dispersion mechanism that evenly distributes the sludge output by the twisted cage conveying mechanism. The drying conveyor belt mechanism for conveying the sludge output by the mechanism, the collecting hopper at the end of the drying conveyor belt mechanism, and the drying room equipped with an exhaust device; the twisted cage conveying mechanism, the dispersion mechanism, the drying conveyor belt mechanism, and the collecting hopper are all located in the drying room . In the direction of looking down, the conveyor belt and the twisted cage conveying mechanism are arranged obliquely, the inclination angle is α, and the intersection point of the two is located in the dispersion mechanism.
干燥间设有进风口和出风口,进风口位于干燥间的一侧的下端,出风口位于干燥间的另一侧的上端,出风口装有抽风装置。本实施例的抽风装置为抽风机。The drying room is provided with an air inlet and an air outlet, the air inlet is located at the lower end of one side of the drying room, the air outlet is located at the upper end of the other side of the drying room, and the air outlet is equipped with an exhaust device. The exhaust device of this embodiment is an exhaust fan.
绞笼输送机构包括电机减速机、绞笼输送机、绞笼机架、进料口、出料口。电机减速机与绞笼输送机通过轴连接,从而驱动绞笼输送机运行。绞笼输送机通过绞笼机架安装在干燥间内,绞笼机架设置在绞笼输送机的1/3与2/3处,作为绞笼输送机的支撑体。进料口位于绞笼输送机的下端起始端的上侧,出料口位于绞笼输送机的上端终止端的下侧,出料方向向下。绞笼输送机是现有的设备,作用是将污泥从低处运送至高处,且将污泥螺旋搅拌,均匀混合。The twisted cage conveying mechanism includes a motor reducer, a twisted cage conveyor, a twisted cage frame, a material inlet, and a material outlet. The motor reducer is connected with the twisted cage conveyor through a shaft to drive the twisted cage conveyor to run. The twisted cage conveyor is installed in the drying room through the twisted cage frame, and the twisted cage frame is set at 1/3 and 2/3 of the twisted cage conveyor as the support body of the twisted cage conveyor. The feed inlet is located on the upper side of the lower starting end of the twisted cage conveyor, the discharge outlet is located on the lower side of the upper end of the twisted cage conveyor, and the discharging direction is downward. The twisted cage conveyor is an existing equipment, and its function is to transport the sludge from a low place to a high place, and to agitate the sludge in a spiral and mix it evenly.
分散机构包括从上往下依次设置的下料斗、分散器、布料器,分散机构通过分散机构机架安装在干燥间内;分散器内设有将污泥挤压成饼状的挤压构件。下料斗设置在绞笼输送机的出料口的正下方,以接住绞笼输送机的出料。本实施例的挤压构件为成对的挤压辊,布料器为下端开口较窄的锥形斗。The dispersing mechanism includes a lower hopper, a disperser, and a distributor arranged in sequence from top to bottom. The dispersing mechanism is installed in the drying room through the dispersing mechanism frame; the dispersing device is equipped with an extruding member that squeezes the sludge into a cake shape. The lower hopper is arranged directly below the discharge port of the twisted cage conveyor to catch the discharge of the twisted cage conveyor. The extruding member in this embodiment is a pair of extruding rollers, and the distributor is a tapered bucket with a narrower opening at the lower end.
干燥输送带机构包括三组干燥输送带单元。每组干燥输送带单元均包括一条传送带、两个驱动轮、多个支撑辊轮、两块挡板和调整传送带高低位置的可调支撑架;驱动轮位于传送带的首端和末端,多个支撑辊轮位于两个驱动轮之间相互平行、并列设置,传送带成环形缠绕在两个驱动轮之间且中间由支撑辊轮支撑,用于安装支撑辊轮的挡板位于传送带的两侧。三条传送带相互平行(倾角为β)且在一个竖直平面内从上往下依次排列,上方传送带的末端位于相邻下侧传送带的首段上方(即第一段传送带的末端位于第二段传送带的首端的正上方,第二段传送带的末端位于第三段传送带的首端的正上方,在垂直方向上,形成了多层交错均匀分布的传送带系统);传送带之间围成空气环流的空间。位于最上方的传送带为第一段传送带,它的首端的位置低于末端的位置,它的首段位于布料器的正下方。传送带由驱动轮带动缓慢运行。The drying conveyor mechanism consists of three sets of drying conveyor units. Each group of dry conveyor belt units includes a conveyor belt, two driving wheels, multiple supporting rollers, two baffles and an adjustable support frame for adjusting the height of the conveyor belt; the driving wheels are located at the head and end of the conveyor belt, and multiple supports The rollers are located between the two driving wheels parallel to each other and arranged side by side. The conveyor belt is looped between the two driving wheels and supported by the support rollers in the middle. The baffles for installing the support rollers are located on both sides of the conveyor belt. The three conveyor belts are parallel to each other (the inclination angle is β) and are arranged sequentially from top to bottom in a vertical plane. The end of the second section of the conveyor belt is located directly above the head end of the third section of the conveyor belt. In the vertical direction, a multi-layer staggered and evenly distributed conveyor belt system is formed); the space between the conveyor belts is surrounded by air circulation. The top conveyor belt is the first conveyor belt, its head end is lower than the end, and its head end is directly below the distributor. The conveyor belt is driven by the driving wheel to run slowly.
工作过程如下:待干燥的污泥由进料口送入绞笼输送机中,在电机减速机的驱动下,绞笼输送机将污泥沿着机身从低处斜向上运输,污泥在绞笼输送机中被螺旋搅拌,混合均匀,经出料口送至分散机构的下料斗中,沿下料斗进入分散器的挤压构件处,经挤压构件处理后,待干燥的污泥呈饼状,由分散器下端的布料器将污泥均匀传送至传送带上。污泥从第一段传送带传送至第二段传送带,再到第三段传送带,干燥空气从进风口进入,由抽风装置带动干燥空气向上缓慢运动,最后由出风口排出。污泥在传送带上与干燥空气进行气湿交换。污泥传送到第三段传送带末端时,自动滑落到集料斗中。传送带竖向布置,相邻传送带之间围成空气环流的空间,加大了空气的局部环流,提高污泥干燥效率。The working process is as follows: the sludge to be dried is sent into the twisted cage conveyor from the feed port, driven by the motor reducer, the twisted cage conveyor transports the sludge obliquely upward along the body from the bottom, and the sludge is The twisted cage conveyor is screw-stirred, mixed evenly, sent to the lower hopper of the dispersing mechanism through the discharge port, and enters the extruding member of the disperser along the lower hopper. After being processed by the extruding member, the sludge to be dried is Cake shape, the sludge is evenly sent to the conveyor belt by the distributor at the lower end of the disperser. The sludge is conveyed from the first section of conveyor belt to the second section of conveyor belt, and then to the third section of conveyor belt. Dry air enters from the air inlet, driven by the exhaust device to move upward slowly, and finally discharged from the air outlet. The sludge is exchanged with dry air on the conveyor belt. When the sludge is transferred to the end of the third conveyor belt, it will automatically slide down into the collecting hopper. The conveyor belts are vertically arranged, and the air circulation space is enclosed between adjacent conveyor belts, which increases the local circulation of the air and improves the sludge drying efficiency.
上述实施例为本发明较佳的实施方式,但本发明的实施方式并不受上述实施例的限制,其他的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。The above-mentioned embodiment is a preferred embodiment of the present invention, but the embodiment of the present invention is not limited by the above-mentioned embodiment, and any other changes, modifications, substitutions, combinations, Simplifications should be equivalent replacement methods, and all are included in the protection scope of the present invention.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710194815.1A CN106746473A (en) | 2017-03-29 | 2017-03-29 | For the dry belt drying system of sludge from wastewater treatment plant and drying means |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710194815.1A CN106746473A (en) | 2017-03-29 | 2017-03-29 | For the dry belt drying system of sludge from wastewater treatment plant and drying means |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106746473A true CN106746473A (en) | 2017-05-31 |
Family
ID=58966553
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710194815.1A Pending CN106746473A (en) | 2017-03-29 | 2017-03-29 | For the dry belt drying system of sludge from wastewater treatment plant and drying means |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106746473A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108218185A (en) * | 2017-12-28 | 2018-06-29 | 山东九择环保设备有限公司 | Oiliness sludge treater |
CN113562951A (en) * | 2020-04-29 | 2021-10-29 | 上海三航奔腾海洋工程有限公司 | High-efficient sludge dewatering treatment facility |
CN114292004A (en) * | 2021-09-09 | 2022-04-08 | 大连青乌环保科技有限公司 | Sludge treatment system and sludge treatment method |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20090126563A (en) * | 2008-06-04 | 2009-12-09 | 주식회사 세트이엔지 | Low Temperature Sludge Drying Equipment Using Recovered Heat |
CN105948431A (en) * | 2016-06-24 | 2016-09-21 | 广州凯能电器科技有限公司 | Sludge drying full-automatic production line |
CN205933567U (en) * | 2016-06-24 | 2017-02-08 | 广州凯能电器科技有限公司 | Sludge drying device |
CN106495429A (en) * | 2017-01-07 | 2017-03-15 | 天津五洲同创空调制冷设备有限公司 | A kind of drying sludge air source heat pump system and its sludge drier |
-
2017
- 2017-03-29 CN CN201710194815.1A patent/CN106746473A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20090126563A (en) * | 2008-06-04 | 2009-12-09 | 주식회사 세트이엔지 | Low Temperature Sludge Drying Equipment Using Recovered Heat |
CN105948431A (en) * | 2016-06-24 | 2016-09-21 | 广州凯能电器科技有限公司 | Sludge drying full-automatic production line |
CN205933567U (en) * | 2016-06-24 | 2017-02-08 | 广州凯能电器科技有限公司 | Sludge drying device |
CN106495429A (en) * | 2017-01-07 | 2017-03-15 | 天津五洲同创空调制冷设备有限公司 | A kind of drying sludge air source heat pump system and its sludge drier |
Non-Patent Citations (1)
Title |
---|
孙秀云等: "《固体废物处理处置》", 28 February 2015, 北京航空航天大学出版社 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108218185A (en) * | 2017-12-28 | 2018-06-29 | 山东九择环保设备有限公司 | Oiliness sludge treater |
CN113562951A (en) * | 2020-04-29 | 2021-10-29 | 上海三航奔腾海洋工程有限公司 | High-efficient sludge dewatering treatment facility |
CN114292004A (en) * | 2021-09-09 | 2022-04-08 | 大连青乌环保科技有限公司 | Sludge treatment system and sludge treatment method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN113979754B (en) | Ceramic powder making technology for energy saving and emission reduction | |
CN108311395A (en) | A kind of aging rubbish drying sorting integration apparatus | |
WO2023035588A1 (en) | Efficient energy-saving mud drying apparatus | |
CN105669266B (en) | Self-discharging tray type three-dimensional fermentation system | |
CN106746473A (en) | For the dry belt drying system of sludge from wastewater treatment plant and drying means | |
CN206767916U (en) | The belt drying system dried for sludge from wastewater treatment plant | |
CN208230053U (en) | A kind of civil engineering work waste treatment device | |
CN106807270A (en) | For the dry front end decentralized system of sludge of sewage treatment plant and process for dispersing | |
CN203577859U (en) | Double-roller dispersing device | |
CN218078111U (en) | A breaker for bituminous concrete retrieves and recycles | |
CN105905530B (en) | An aquatic plant dehydration treatment system | |
CN116839329A (en) | Dregs of a decoction steam tubulation drying device | |
CN210340668U (en) | Silt and waste slurry drying production line | |
CN204672135U (en) | A kind of limestone desulfurizer production line | |
CN211938384U (en) | Mechanical system for realizing solid-liquid separation of waste vegetables by applying biochemical wall breaking technology | |
CN204638342U (en) | Impurity screening device in timber | |
CN208434622U (en) | High tower grain drier and its multistage lifting mechanism | |
CN113105087A (en) | A normal temperature ventilation type sludge deep dewatering and drying method and device | |
CN222583581U (en) | Mushroom desiccator | |
CN111303924B (en) | Automatic material collection type pyrolysis and distillation device and automatic material collection method for pyrolysis and distillation | |
CN206666350U (en) | The combination unit of dewatered sludge | |
CN106810036A (en) | A kind of coal slime, drying sludge device for improving quality and technique | |
CN219713807U (en) | Household garbage drying system utilizing cement kiln waste gas | |
CN111994648A (en) | Large screening equipment feeding device | |
CN115245851B (en) | A kind of unloading device for microalgae phosphorus accumulation to produce phosphate rock |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170531 |
|
RJ01 | Rejection of invention patent application after publication |