CN115990543A - A safe and efficient clean production method for reducing crushing and screening dust - Google Patents
A safe and efficient clean production method for reducing crushing and screening dust Download PDFInfo
- Publication number
- CN115990543A CN115990543A CN202310190439.4A CN202310190439A CN115990543A CN 115990543 A CN115990543 A CN 115990543A CN 202310190439 A CN202310190439 A CN 202310190439A CN 115990543 A CN115990543 A CN 115990543A
- Authority
- CN
- China
- Prior art keywords
- dust
- belt
- microporous membrane
- crusher
- production method
- 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
Images
Landscapes
- Disintegrating Or Milling (AREA)
Abstract
Description
技术领域technical field
本发明属于清洁生产领域,具体是一种安全高效降低破碎筛分粉尘的清洁生产方法。The invention belongs to the field of clean production, in particular to a clean production method for safely and efficiently reducing crushing and screening dust.
背景技术Background technique
工业的快速发展势必会造成一定的环境污染,煤矿、水泥、火电、化工等行业在生产过程中会产生大量的粉尘,不仅污染了工厂的作业环境,也威胁了工人的身体健康。对此,除尘器在工业生产环保方面发挥着十分重要的作用。同时,随着国民生活水平提高,人们对生活环境的要求随之提高,国家政策对颗粒物排放限值也不断提升,使得生产上对除尘器的要求也是越来越高,而传统除尘器在一定意义上已经不能满足现在实际的使用要求。The rapid development of industry will inevitably cause a certain amount of environmental pollution. Coal mines, cement, thermal power, chemical and other industries will produce a large amount of dust in the production process, which not only pollutes the working environment of the factory, but also threatens the health of workers. In this regard, dust collectors play a very important role in industrial production and environmental protection. At the same time, with the improvement of people's living standards, people's requirements for the living environment have also increased, and the national policy on the emission limit of particulate matter has also continued to increase, making the requirements for dust collectors in production more and more high. In a sense, it can no longer meet the actual use requirements now.
现有的破碎、筛分设备在破碎、出料和筛分的过程中,由于粉尘颗粒直径比较小,因此其会与石料分离,并漂浮在空气中,从而造成周围环境中的空气质量差,容易被吸入身体中并对工作人员的身体造成一定的损伤,现有的方法一般采用:1、风机将其引出工作环境,或者,2、喷洒水份抑制扬尘,但是引出工作环境的粉尘造成外部环境污染,粉尘排放量容易超标;同时两种方法均造成石料粉尘资源的浪费,从而导致其实用性较差。During the crushing, discharging and screening process of existing crushing and screening equipment, due to the relatively small diameter of dust particles, it will be separated from the stone and float in the air, resulting in poor air quality in the surrounding environment. It is easy to be sucked into the body and cause certain damage to the body of the staff. The existing methods generally adopt: 1. The fan leads it out of the working environment, or, 2. Spray water to suppress the dust, but the dust drawn out of the working environment causes external Environmental pollution, dust discharge is easy to exceed the standard; at the same time, both methods cause waste of stone dust resources, resulting in poor practicability.
发明内容Contents of the invention
本发明所要解决的技术问题是针对上述现有技术的不足提供一种安全高效降低破碎筛分粉尘的清洁生产方法,本安全高效降低破碎筛分粉尘的清洁生产方法流程简单、除尘效率高,实现了对粉尘排放量的有效控制,同时结合生产水进行造浆,使得收集的粉尘进入生产系统,提高对粉尘和水的利用率,节约资源及生产成本。The technical problem to be solved by the present invention is to provide a safe and efficient clean production method for reducing crushing and screening dust in view of the deficiencies of the above-mentioned prior art. The clean production method for safely and efficiently reducing crushing and screening dust has a simple process and high dust removal efficiency. In order to effectively control the dust emission, at the same time, it is combined with the production water to make slurry, so that the collected dust enters the production system, improves the utilization rate of dust and water, and saves resources and production costs.
为实现上述技术目的,本发明采取的技术方案为:For realizing above-mentioned technical purpose, the technical scheme that the present invention takes is:
一种安全高效降低破碎筛分粉尘的清洁生产方法,包括:颚式破碎机、圆锥破碎机和振动筛工作产生的粉尘由吸尘罩和管道吸至除尘器内,同时颚式破碎机和圆锥破碎机工作后的破碎产品落至第一带式运输机的皮带上扬起的粉尘也由吸尘罩和管道吸至除尘器内;进入除尘器中的粉尘在自身重力作用下沉降并从除尘器的排污口下落至集矿池内;集矿池的上层溢流水经自流进入蓄水池,集矿池的底部矿浆积累至一定程度后,将蓄水池内的水输送至集矿池内从而对矿浆冲洗并造浆,随后矿浆自流进入中转池,将中转池内的矿浆输送至生产系统。A safe and efficient clean production method for reducing crushing and screening dust, including: the dust generated by jaw crushers, cone crushers and vibrating screens is sucked into the dust collector by dust suction hoods and pipes, while jaw crushers and cone crushers are After the crusher works, the broken products fall on the belt of the first belt conveyor, and the dust raised is also sucked into the dust collector by the dust suction cover and the pipeline; the dust entering the dust collector settles under its own gravity and is discharged from the dust collector The sewage outlet falls into the ore collection pool; the upper overflow water of the ore collection pool enters the storage tank by gravity, and after the bottom of the ore collection pool has accumulated to a certain extent, the water in the storage tank is transported to the ore collection pool to wash and clean the slurry. Slurry is made, and then the pulp flows into the transfer tank by itself, and the pulp in the transfer tank is transported to the production system.
作为本发明进一步改进的技术方案,所述除尘器为微孔膜过滤除尘器,进入微孔膜过滤除尘器中大颗粒的粉尘在自身重力作用下沉降到微孔膜过滤除尘器的下箱体内;小颗粒的粉尘随气流进入微孔膜过滤除尘器的微孔膜,在压强差作用下,含尘气流在微孔膜上过滤,过滤干净的空气通过微孔膜过滤除尘器的出风口排出,粉尘截留在微孔膜上,当微孔膜表面的粉尘积聚到一定的厚度时,粉尘靠自身重力作用脱落至下箱体,粘在微孔膜上的粉尘由压缩空气喷吹脱落至下箱体,下箱体内粉尘均从下箱体底部的排污口排出,粉尘落入集矿池内沉淀,集矿池的上层溢流水经自流进入蓄水池,集矿池的底部矿浆积累至一定程度后,通过泵将蓄水池内的水输送至集矿池内从而对矿浆冲洗并造浆,随后矿浆通过管道自流进入中转池,再通过泵将中转池内的矿浆输送至生产系统。As a further improved technical solution of the present invention, the dust collector is a microporous membrane filter dust collector, and the large particle dust entering the microporous membrane filter dust collector settles into the lower box of the microporous membrane filter dust collector under the action of its own gravity ;Small particles of dust enter the microporous membrane of the microporous membrane filter dust collector with the airflow. Under the action of the pressure difference, the dusty airflow is filtered on the microporous membrane, and the filtered clean air is discharged through the air outlet of the microporous membrane filter dust collector. , the dust is trapped on the microporous membrane. When the dust on the surface of the microporous membrane accumulates to a certain thickness, the dust will fall off to the lower box by its own gravity, and the dust stuck on the microporous membrane will be blown off by the compressed air to the lower box. The dust in the box body and the lower box is discharged from the sewage outlet at the bottom of the lower box body, and the dust falls into the ore collection pool for sedimentation. Finally, pump the water in the reservoir to the ore collection pool to flush and make pulp, then the pulp flows into the transfer pool through the pipeline, and then the pulp in the transfer pool is transported to the production system through the pump.
作为本发明进一步改进的技术方案,所述颚式破碎机的排料口通过第一带式运输机与振动筛的进料口连通,所述振动筛的粗颗粒出料口通过第二带式运输机与圆锥破碎机的进料口连通,所述圆锥破碎机的排料口通过第一带式运输机与振动筛的进料口连通。As a further improved technical solution of the present invention, the discharge port of the jaw crusher communicates with the feed port of the vibrating screen through the first belt conveyor, and the coarse particle discharge port of the vibrating screen passes through the second belt conveyor. It communicates with the feed port of the cone crusher, and the discharge port of the cone crusher communicates with the feed port of the vibrating screen through the first belt conveyor.
作为本发明进一步改进的技术方案,所述颚式破碎机的破碎腔外壳上连通有吸尘罩,所述颚式破碎机的排料口连通有吸尘罩,且颚式破碎机排料口处的吸尘罩罩在第一带式运输机的皮带上。As a further improved technical solution of the present invention, the crushing cavity shell of the jaw crusher is connected with a dust suction hood, the discharge port of the jaw crusher is connected with a dust suction hood, and the discharge port of the jaw crusher is The suction hood at is covered on the belt of the first belt conveyor.
作为本发明进一步改进的技术方案,所述圆锥破碎机的进料口上方设有吸尘罩,所述圆锥破碎机的排料口连通有吸尘罩,且圆锥破碎机排料口处的吸尘罩罩在第一带式运输机的皮带上。As a further improved technical solution of the present invention, a dust suction hood is provided above the feed port of the cone crusher, a dust suction hood is connected to the discharge port of the cone crusher, and the suction at the discharge port of the cone crusher is The dust cover covers the belt of the first belt conveyor.
作为本发明进一步改进的技术方案,所述圆锥破碎机的进料口四周设有封闭箱体,封闭箱体与吸尘罩密封连通,所述封闭箱体上还设置有观察口,所述观察口的四周设有橡胶垫,所述观察口通过合页铰接有盖板,所述盖板与橡胶垫密封盖合。As a further improved technical solution of the present invention, a closed box is provided around the feed port of the cone crusher, and the closed box is sealed and communicated with the dust collection hood. The closed box is also provided with an observation port. A rubber pad is provided around the mouth, and the observation port is hinged with a cover plate through a hinge, and the cover plate is sealed and closed with the rubber pad.
作为本发明进一步改进的技术方案,所述颚式破碎机排料口密封连通的吸尘罩与圆锥破碎机排料口密封连通的吸尘罩为一体结构,该一体结构与第一带式运输机上的皮带通过皮带边皮密封滑动连接。As a further improved technical solution of the present invention, the dust suction hood sealed and connected to the discharge port of the jaw crusher and the dust suction hood sealed and connected to the discharge port of the cone crusher are integrally structured, and the integrated structure is integrated with the first belt conveyor The belt on the belt is connected by a belt skin seal sliding connection.
作为本发明进一步改进的技术方案,所述颚式破碎机排料口密封连通的吸尘罩与颚式破碎机的排料口淌槽的角度为50~70°,所述圆锥破碎机排料口密封连通的吸尘罩与圆锥破碎机的排料口淌槽的角度为50~70°。As a further improved technical solution of the present invention, the angle between the suction hood that is sealed and communicated with the discharge port of the jaw crusher and the discharge channel of the jaw crusher is 50-70°, and the discharge port of the cone crusher The angle between the dust suction hood that is sealed and communicated with the discharge port of the cone crusher is 50-70°.
作为本发明进一步改进的技术方案,所述振动筛采用全封闭振动筛,所述振动筛的全封闭振动筛密封连通有吸尘罩。As a further improved technical solution of the present invention, the vibrating screen adopts a fully enclosed vibrating screen, and the fully enclosed vibrating screen of the vibrating screen is sealed and communicated with a dust collection cover.
作为本发明进一步改进的技术方案,所述集矿池的底部与水平面具有一定倾角,所述集矿池的底部出料口与中转池进料口具有高度差,从而使矿浆经管道自流进入中转池,所述中转池进料口下端设有过滤网。As a further improved technical solution of the present invention, the bottom of the ore collection pool has a certain inclination angle to the horizontal plane, and there is a height difference between the outlet of the bottom of the ore collection pool and the feed port of the transfer pool, so that the ore pulp flows into the transfer tank by itself through the pipeline. pool, the lower end of the feed port of the transfer pool is provided with a filter.
本发明的有益效果为:The beneficial effects of the present invention are:
本发明颚式破碎机、圆锥破碎机及振动筛进料端实现全封闭状态,能有效避免粉尘外逸,同时在进料端设置观察口,随时关注进料情况;本发明颚式破碎机、圆锥破碎机及振动筛在工作过程中产生的粉尘由吸尘罩和管道输送至除尘器,圆锥破碎机的进料口四周设有封闭箱体,圆锥破碎机的封闭箱体与吸尘罩密封连通,从而将进料口与给料皮带头附近的粉尘通过吸尘罩输送至除尘器,有效收集粉尘;将第一带式运输机上方的吸尘罩与破碎机排料口淌槽的角度控制在50~70°范围内,不仅能防止角度过小时吸入皮带上的粗颗粒物料,还能避免角度过大时粉尘吸收率低的问题;第一带式运输机上方的吸尘罩与皮带之间采用皮带边皮进行密封滑动连接,能很好地使其成为一个封闭整体,同时也不影响皮带的正常运行;流程简单、使用寿命长,收尘效率高,且总收尘效率可达到99.9~99.99%;通过微孔膜高效过滤除尘器对粉尘收集,进入除尘器中较大颗粒的粉尘由于气流速度减慢,在自身重力作用下沉降到除尘器下箱体内,较小颗粒的粉尘随气流进入微孔膜滤料,在压强差作用下,含尘气流在微孔膜上过滤,粉尘截留在微孔膜上,而过滤干净的空气通过出风口排出,实现了对粉尘排放量的有效控制,当微孔膜表面的粉尘积聚到一定的厚度时,绝大部分粉尘靠自身重力作用脱落下来至下箱体,粘在微孔膜上的粉尘由压缩空气喷吹脱落至下箱体,下箱体内粉尘均从排污口排至集矿池;集矿池设为斜坡式储存物料,有利于粉尘的收集及生产水的冲洗,且集矿池出料口与中转池进料口设有一定高度差,便于矿浆自流进入中转池内,同时避免管道堵塞;中转池进料口下端设有过滤网,过滤一些杂质物质,以免堵塞管道,有利于系统的正常运行;集矿池内上层溢流水进入蓄水池,蓄水池内生产水用于冲洗落入集矿池内粉尘,实现生产水的循环使用,同时集矿池内形成的矿浆最终进入生产系统,进行选别,有效提高粉尘的利用率,实现资源综合利用。The feeding end of the jaw crusher, cone crusher and vibrating screen of the present invention realizes a fully closed state, which can effectively prevent dust from escaping. At the same time, an observation port is set at the feeding end to pay attention to the feeding situation at any time; The dust generated by the cone crusher and the vibrating screen is transported to the dust collector by the dust hood and the pipeline. There is a closed box around the feed port of the cone crusher, and the closed box of the cone crusher is sealed with the dust hood. Connected, so that the dust near the feed inlet and the feed belt head is transported to the dust collector through the dust suction hood to effectively collect dust; the angle between the dust suction hood above the first belt conveyor and the discharge groove of the crusher is controlled. In the range of 50-70°, it can not only prevent the coarse particle material on the belt from being sucked into the belt when the angle is too small, but also avoid the problem of low dust absorption rate when the angle is too large; between the dust suction hood above the first belt conveyor and the belt The belt side skin is used for sealed sliding connection, which can make it a closed whole without affecting the normal operation of the belt; the process is simple, the service life is long, the dust collection efficiency is high, and the total dust collection efficiency can reach 99.9~ 99.99%; the dust is collected by the high-efficiency filter dust collector through the microporous membrane. The dust with larger particles entering the dust collector will settle into the lower box of the dust collector under the action of its own gravity due to the slowing down of the airflow velocity, and the dust with smaller particles will flow with the airflow. Enter the microporous membrane filter material, under the action of pressure difference, the dust-laden airflow is filtered on the microporous membrane, the dust is trapped on the microporous membrane, and the filtered clean air is discharged through the air outlet, which realizes the effective control of dust emission , when the dust on the surface of the microporous membrane accumulates to a certain thickness, most of the dust will fall off to the lower box by its own gravity, and the dust stuck on the microporous membrane will be blown off by compressed air to the lower box, and then The dust in the box is discharged from the sewage outlet to the collection pool; the collection pool is set up as a slope to store materials, which is conducive to the collection of dust and the flushing of production water, and the discharge port of the collection pool and the feed port of the transfer pool are provided with certain The difference in height facilitates the self-flow of ore pulp into the transfer tank and avoids pipeline blockage; the lower end of the feed port of the transfer tank is equipped with a filter to filter some impurities so as not to block the pipeline, which is conducive to the normal operation of the system; the upper overflow water in the collection tank enters the storage tank The production water in the water tank and the storage tank is used to wash the dust falling into the mining pool to realize the recycling of the production water. At the same time, the ore pulp formed in the mining pool finally enters the production system for sorting, effectively improving the utilization rate of dust and realizing resource utilization. Comprehensive utilization.
附图说明Description of drawings
图1为本发明安全高效降低破碎筛分粉尘的清洁生产装置的结构示意图;Fig. 1 is the structural representation of the clean production device of the present invention that reduces crushing and screening dust safely and efficiently;
图2为本发明安全高效降低破碎筛分粉尘的清洁生产装置的破碎厂房结构示意图;Fig. 2 is a schematic diagram of the crushing plant structure of the clean production device for safely and efficiently reducing crushing and screening dust of the present invention;
图3为本发明安全高效降低破碎筛分粉尘的清洁生产装置的观察口结构示意图;Fig. 3 is a schematic view of the structure of the observation port of the clean production device for safely and efficiently reducing crushing and screening dust of the present invention;
图4为本发明安全高效降低破碎筛分粉尘的清洁生产装置的除尘器区域结构示意图;Fig. 4 is a schematic diagram of the structure of the dust collector area of the clean production device for safely and efficiently reducing crushing and screening dust of the present invention;
其中,1、颚式破碎机;2、圆锥破碎机;3、振动筛;4、除尘器;5、集矿池;6、蓄水池;7、中转池;8、粗颗粒返回箱;9、观察口;10、淌槽;11、吸尘罩;12、皮带边皮;13封闭箱体;14、合页;15、盖板;16、橡胶垫;17、进风口;18、出风口;19、上箱体;20、下箱体;21、排污口;22、第一带式运输机;23、第二带式运输机;24、管道。Among them, 1. Jaw crusher; 2. Cone crusher; 3. Vibrating screen; 4. Dust collector; , observation port; 10, drip groove; 11, vacuum cover; 12, belt edge; 13 closed box; 14, hinge; 15, cover plate; 16, rubber pad; 17, air inlet; 18, air outlet ; 19, the upper box; 20, the lower box; 21, the sewage outlet; 22, the first belt conveyor; 23, the second belt conveyor; 24, the pipeline.
具体实施方式Detailed ways
下面根据附图对本发明的具体实施方式作出进一步说明:The specific embodiment of the present invention is described further below according to accompanying drawing:
如图1所示,本实施例提供一种安全高效降低破碎筛分粉尘的清洁生产装置,包括颚式破碎机1、圆锥破碎机2、振动筛3、除尘器4、集矿池5、蓄水池6和中转池7;所述颚式破碎机1、圆锥破碎机2和振动筛3处均设置有吸尘罩11,多个吸尘罩11分别通过管道24与除尘器4的进风口17连接;所述除尘器4置于集矿池5上方;所述蓄水池6位于集矿池5一侧从而保证集矿池5的上层溢流水进入蓄水池6内,所述集矿池5的底部出料口通过管道24与中转池7连接;所述蓄水池6通过泵和管道24与集矿池5连接,集矿池5与蓄水池6内水循环使用;所述中转池7内矿浆用于通过管道24和泵进入生产系统。As shown in Figure 1, this embodiment provides a safe and efficient clean production device for reducing crushing and screening dust, including a
具体地,如图1所示,所述颚式破碎机1的排料口通过第一带式运输机22与振动筛3的进料口连通,所述振动筛3的粗颗粒出料口(也即粗颗粒返回箱8)通过第二带式运输机23与圆锥破碎机2的进料口连通,所述圆锥破碎机2的排料口通过第一带式运输机22与振动筛3的进料口连通。Specifically, as shown in Figure 1, the discharge port of the
如图2所示,所述颚式破碎机1处的多个吸尘罩11分别置于颚式破碎机1的破碎腔以及粉尘落料至第一带式运输机22处,即,所述颚式破碎机1的破碎腔外壳上连通有吸尘罩11,所述颚式破碎机1的排料口连通有吸尘罩11,且颚式破碎机1排料口处的吸尘罩11罩在第一带式运输机22的皮带上。As shown in Figure 2, the plurality of
如图2所示,所述圆锥破碎机2处的多个吸尘罩11分别置于进料口上方以及粉尘落料至第一带式运输机22处;即,所述圆锥破碎机2的进料口上方设有吸尘罩11,具体地,其中,圆锥破碎机2的进料口四周以及第二带式运输机23的给料皮带头部的外部均罩有封闭箱体13,封闭箱体13与圆锥破碎机2的外壳密封固定连接,封闭箱体13与吸尘罩11密封连通,所述封闭箱体13上还设置有观察口9,如图3所示,所述观察口9的四周设有橡胶垫16,所述观察口9通过合页14铰接有盖板15(采用钢板),所述盖板15与橡胶垫16密封盖合;所述圆锥破碎机2的排料口连通有吸尘罩11,且圆锥破碎机2排料口处的吸尘罩11罩在第一带式运输机22的皮带上。As shown in Figure 2, a plurality of
所述颚式破碎机1排料口密封连通的吸尘罩11与圆锥破碎机2排料口密封连通的吸尘罩11为一体结构,该一体结构与第一带式运输机22上的皮带通过皮带边皮12密封滑动连接。The
如图2所示,所述颚式破碎机1排料口密封连通的吸尘罩11与颚式破碎机1的排料口淌槽10的角度为50~70°,所述圆锥破碎机2排料口密封连通的吸尘罩11与圆锥破碎机2的排料口淌槽10的角度为50~70°。As shown in Figure 2, the angle between the
所述振动筛3采用全封闭振动筛3,所述振动筛3的全封闭振动筛3的上箱体密封连通有吸尘罩11。The vibrating
所述除尘器4为DZF4-2.0型微孔膜高效过滤除尘器,由除尘器进风口17、过滤系统、出风口18、清灰系统、上箱体19、下箱体20及卸灰装置等组成。如图4所示,所述除尘器4底部设有排污口21,排污口21上连接有排污阀,排污口21置于集矿池5上方从而使得除尘器4内的粉尘从排污口21排出至集矿池5。The dust collector 4 is a DZF4-2.0 microporous membrane high-efficiency filter dust collector, which consists of a dust
所述集矿池5的底部与水平面具有一定倾角,所述集矿池5的底部出料口与中转池7进料口具有高度差,从而使集矿池5内的矿浆经管道24自流进入中转池7,所述中转池7进料口下端设有过滤网。The bottom of the
本实施例的颚式破碎机1、圆锥破碎机2和振动筛3的进料端外部均罩有封闭箱体13,以防进料端处的粉尘进入生产环境中,封闭箱体13上设置观察口9,如图3所示,封闭箱体13上还设置有观察口9,所述观察口9的四周设有橡胶垫,所述观察口9通过合页14铰接有盖板15,为达到更好的封闭效果,橡胶垫置于封闭箱体13与盖板15之间,所述盖板15与观察口9通过橡胶垫密封盖合。The
本实施例的颚式破碎机1和圆锥破碎机2产品由第一带式运输机22运输至振动筛3,筛上产品经粗颗粒返回箱8至第二带式运输机23,并由第二带式运输机23运输至圆锥破碎机2进行再次破碎,筛下产品由第三带式运输机转运至第四带式运输机进入粉矿仓进行后续作业。The products of
在除尘过程中,颚式破碎机1的破碎腔、圆锥破碎机2进料口及振动筛3工作产生的内部粉尘由吸尘罩11联通管道24吸至除尘器4内,同时颚式破碎机1和圆锥破碎机2工作后的破碎产品落至第一带式运输机22的皮带上扬起的粉尘也由吸尘罩11联通管道24吸至除尘器4内。进入除尘器4中较大颗粒的粉尘由于气流速度减慢,在自身重力作用下沉降到除尘器4下箱体20内;较小颗粒的粉尘随气流进入微孔膜滤料,在压强差作用下,含尘气流在微孔膜上过滤,粉尘截留在微孔膜上,而过滤干净的空气通过上箱体19、出风口18排出。当微孔膜表面的粉尘积聚到一定的厚度时,绝大部分粉尘靠自身重力作用脱落下来,粘在微孔膜上的粉尘由压缩空气喷吹脱落至下箱体20,下箱体20内粉尘均从排污口21排出。粉尘落入集矿池5沉淀,集矿池5的上层溢流水经自流可以进入蓄水池6,用于后续造浆使用,底部矿浆积累至一定程度后,通过泵将蓄水池6内的生产水输送集矿池5内,从而用生产水进行冲洗并造浆,随后矿浆通过管道24自流进入中转池7,再通过泵打至生产系统,提高对粉尘和生产水的利用率,节约资源及生产成本。During the dust removal process, the internal dust generated by the crushing cavity of the
本实施例还提供一种安全高效降低破碎筛分粉尘的清洁生产方法,包括:颚式破碎机1、圆锥破碎机2和振动筛3工作产生的粉尘由吸尘罩11和管道24吸至微孔膜过滤除尘器内,同时颚式破碎机1和圆锥破碎机2工作后的破碎产品落至第一带式运输机22的皮带上扬起的粉尘也由吸尘罩11和管道24吸至微孔膜过滤除尘器内;进入微孔膜过滤除尘器中大颗粒的粉尘在自身重力作用下沉降到微孔膜过滤除尘器的下箱体20内;小颗粒的粉尘随气流进入微孔膜过滤除尘器的微孔膜,在压强差作用下,含尘气流在微孔膜上过滤,过滤干净的空气通过微孔膜过滤除尘器的出风口18排出,粉尘截留在微孔膜上,当微孔膜表面的粉尘积聚到一定的厚度时,粉尘靠自身重力作用脱落至下箱体20,粘在微孔膜上的粉尘由压缩空气喷吹脱落至下箱体20,下箱体20内粉尘均从下箱体20底部的排污口21排出,粉尘落入集矿池5内沉淀,集矿池5的上层溢流水经自流进入蓄水池6,集矿池5的底部矿浆积累至一定程度后,通过泵将蓄水池6内的水输送至集矿池5内从而对矿浆冲洗并造浆,随后矿浆通过管道自流进入中转池7,再通过泵将中转池7内的矿浆输送至生产系统。This embodiment also provides a safe and efficient clean production method for reducing crushing and screening dust, including: the dust generated by the
通过工艺提升改造,本安全高效降低破碎筛分粉尘的清洁生产方装置运行情况良好,除尘效率提高到99.5%,排放口颗粒物浓度小于特别排放限值10mg/m3,重金属排放量下降20%以上,满足了政府环保对破碎筛分废气排放口颗粒物浓度必须低于《铅锌工业污染物排放标准(GB25466-2010)修订单》特别排放限值,重金属排放量要比之前下降15%的要求。此外,系统中收集的粉尘全部重新进入生产系统,每年能回收原矿450吨,大大提高了粉尘的利用率,保护环境的同时实现资源综合利用。Through process upgrading and transformation, the safe and efficient clean production equipment for reducing crushing and screening dust is in good condition, the dust removal efficiency is increased to 99.5%, the concentration of particulate matter at the discharge port is less than the special discharge limit of 10mg/m 3 , and the discharge of heavy metals is reduced by more than 20%. , to meet the requirements of the government's environmental protection that the concentration of particulate matter at the exhaust outlet of crushing and screening must be lower than the special discharge limit of the "Lead and Zinc Industrial Pollutant Discharge Standard (GB25466-2010) Revised Sheet", and the heavy metal discharge should be 15% lower than before. In addition, all the dust collected in the system re-enters the production system, and 450 tons of raw ore can be recovered each year, which greatly improves the utilization rate of dust and realizes comprehensive utilization of resources while protecting the environment.
本发明的保护范围包括但不限于以上实施方式,本发明的保护范围以权利要求书为准,任何对本技术做出的本领域的技术人员容易想到的替换、变形、改进均落入本发明的保护范围。The scope of protection of the present invention includes but is not limited to the above embodiments. The scope of protection of the present invention is based on the claims. Any replacement, deformation, and improvement that are easily conceived by those skilled in the art for this technology fall within the scope of the present invention. protected range.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310190439.4A CN115990543A (en) | 2023-03-02 | 2023-03-02 | A safe and efficient clean production method for reducing crushing and screening dust |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310190439.4A CN115990543A (en) | 2023-03-02 | 2023-03-02 | A safe and efficient clean production method for reducing crushing and screening dust |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN115990543A true CN115990543A (en) | 2023-04-21 |
Family
ID=85995173
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202310190439.4A Pending CN115990543A (en) | 2023-03-02 | 2023-03-02 | A safe and efficient clean production method for reducing crushing and screening dust |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN115990543A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN120586552A (en) * | 2025-08-08 | 2025-09-05 | 云南凯瑞特工程机械设备有限公司 | A centralized dust removal system for crawler mobile crushing and screening stations |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104128347A (en) * | 2014-07-10 | 2014-11-05 | 侯计文 | Method and system for dust disposal during ore processing |
| CN105169866A (en) * | 2015-08-31 | 2015-12-23 | 北京大学 | Microporous ceramic dedusting method used for treatment of high-temperature flue gas in desulfuration of chlorine leaching residues |
| CN207805795U (en) * | 2017-12-29 | 2018-09-04 | 邝贤语 | A kind of waterpower separator |
| CN109011993A (en) * | 2018-08-31 | 2018-12-18 | 贺州市骏鑫矿产品有限责任公司 | A kind of potassium feldspar dust recoverying and utilizing method |
| CN211190536U (en) * | 2019-12-09 | 2020-08-07 | 安徽海螺建材设计研究院有限责任公司 | Crushing system of siliceous raw materials in mine |
| CN214320525U (en) * | 2020-12-18 | 2021-10-01 | 新巴尔虎右旗荣达矿业有限责任公司 | Grinding and floating system construction accident ore drawing pool |
| CN214634408U (en) * | 2021-03-19 | 2021-11-09 | 云南驰宏锌锗股份有限公司 | Concentrate pond suitable for dehydration of high fine particle fraction concentrate |
| CN214972795U (en) * | 2021-04-21 | 2021-12-03 | 潍坊理工学院 | Wet type cyclone dust collector |
| CN218222811U (en) * | 2022-09-21 | 2023-01-06 | 王洪洋 | Solid waste material non ferrous metal ore recovery production line |
-
2023
- 2023-03-02 CN CN202310190439.4A patent/CN115990543A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104128347A (en) * | 2014-07-10 | 2014-11-05 | 侯计文 | Method and system for dust disposal during ore processing |
| CN105169866A (en) * | 2015-08-31 | 2015-12-23 | 北京大学 | Microporous ceramic dedusting method used for treatment of high-temperature flue gas in desulfuration of chlorine leaching residues |
| CN207805795U (en) * | 2017-12-29 | 2018-09-04 | 邝贤语 | A kind of waterpower separator |
| CN109011993A (en) * | 2018-08-31 | 2018-12-18 | 贺州市骏鑫矿产品有限责任公司 | A kind of potassium feldspar dust recoverying and utilizing method |
| CN211190536U (en) * | 2019-12-09 | 2020-08-07 | 安徽海螺建材设计研究院有限责任公司 | Crushing system of siliceous raw materials in mine |
| CN214320525U (en) * | 2020-12-18 | 2021-10-01 | 新巴尔虎右旗荣达矿业有限责任公司 | Grinding and floating system construction accident ore drawing pool |
| CN214634408U (en) * | 2021-03-19 | 2021-11-09 | 云南驰宏锌锗股份有限公司 | Concentrate pond suitable for dehydration of high fine particle fraction concentrate |
| CN214972795U (en) * | 2021-04-21 | 2021-12-03 | 潍坊理工学院 | Wet type cyclone dust collector |
| CN218222811U (en) * | 2022-09-21 | 2023-01-06 | 王洪洋 | Solid waste material non ferrous metal ore recovery production line |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN120586552A (en) * | 2025-08-08 | 2025-09-05 | 云南凯瑞特工程机械设备有限公司 | A centralized dust removal system for crawler mobile crushing and screening stations |
| CN120586552B (en) * | 2025-08-08 | 2025-11-14 | 云南凯瑞特工程机械设备有限公司 | A centralized dust removal system for tracked mobile crushing and screening stations |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103463886B (en) | Environment-friendly dust removal device | |
| CN115990543A (en) | A safe and efficient clean production method for reducing crushing and screening dust | |
| CN112047509A (en) | A processing system for copper mine mining and sorting waste water | |
| CN219441984U (en) | Safe and efficient clean production device for reducing crushing and screening dust | |
| CN216970918U (en) | Furfural production raw material conveying and dedusting device | |
| CN211874541U (en) | Anchor spouts quick-witted dust device with flat bag collector | |
| CN213569774U (en) | Special sand-water separation spiral lifting device | |
| CN214817843U (en) | Combined type granule recovery unit | |
| CN212396821U (en) | A variety of metal ore beneficiation equipment with dust removal function | |
| CN211492934U (en) | Sorting equipment for large-substance kitchen waste | |
| CN201711288U (en) | Sulfuric acid catalyst sieving machine | |
| CN203494871U (en) | Ball grinder tail gas dedusting and purifying device | |
| CN210455960U (en) | Be used for cement jar material loading dust removal recovery unit | |
| CN113291711A (en) | Furfural production raw material conveying and dust removing device and raw material purifying and conveying method | |
| CN208436503U (en) | Cassava slurry desanding trash discharging apparatus | |
| CN209173624U (en) | A local spray dedusting device for metal and nonmetal mine beneficiation plant | |
| CN207253849U (en) | The sieve energy-efficient mud and water separating equipment of filtering type is dropped down in a kind of bucket storehouse | |
| CN214132630U (en) | Renewable sand classification recycling device | |
| CN219023648U (en) | Spraying dust device for concrete production | |
| CN206372567U (en) | A kind of glass powder reclaiming device of glass production device | |
| CN220531124U (en) | A kind of mine ventilation dust collector | |
| CN212417428U (en) | Special dust pelletizing system of slay | |
| CN207641942U (en) | Blast furnace ore tank regional water clean and reuse utilizes system | |
| CN210786714U (en) | A dust collector for broken system of water glass waste sand | |
| CN212524510U (en) | Dust collector of slag mill |
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 | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20230421 |