CN107754543A - Exhaust gas purification system - Google Patents
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- CN107754543A CN107754543A CN201711275276.0A CN201711275276A CN107754543A CN 107754543 A CN107754543 A CN 107754543A CN 201711275276 A CN201711275276 A CN 201711275276A CN 107754543 A CN107754543 A CN 107754543A
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- 238000000746 purification Methods 0.000 title claims abstract description 39
- 238000004062 sedimentation Methods 0.000 claims abstract description 55
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 238000001914 filtration Methods 0.000 claims abstract description 11
- 239000007789 gas Substances 0.000 claims description 42
- 229910000831 Steel Inorganic materials 0.000 claims description 20
- 238000005192 partition Methods 0.000 claims description 20
- 239000010959 steel Substances 0.000 claims description 20
- 239000004744 fabric Substances 0.000 claims description 13
- 239000002245 particle Substances 0.000 claims description 9
- 229920000742 Cotton Polymers 0.000 claims description 7
- 239000002351 wastewater Substances 0.000 claims description 7
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 6
- 239000003153 chemical reaction reagent Substances 0.000 claims description 6
- 239000010813 municipal solid waste Substances 0.000 claims description 6
- 239000004575 stone Substances 0.000 claims description 6
- 239000002912 waste gas Substances 0.000 claims description 6
- 239000011521 glass Substances 0.000 claims description 5
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 4
- 239000010865 sewage Substances 0.000 claims description 4
- 235000012255 calcium oxide Nutrition 0.000 claims description 3
- 239000000292 calcium oxide Substances 0.000 claims description 3
- 239000000571 coke Substances 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 6
- 238000000926 separation method Methods 0.000 abstract 1
- 239000008213 purified water Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000006870 function Effects 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003828 vacuum filtration Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 230000009931 harmful effect Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/60—Combinations of devices covered by groups B01D46/00 and B01D47/00
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Filtering Materials (AREA)
Abstract
本发明提供的废气净化系统,包括预处理过滤装置、第一真空过滤箱和第二真空过滤箱,同时还包括沉淀池,预处理过滤装置安装于废气进口处,第一真空过滤箱内设有水过滤处理装置,第二真空过滤箱内通有排气管,所述排气管上设有真空泵,沉淀池进水管与沉淀池连接处设置抽水泵;具有水、气分离效果好,净化效果好,净化效率高,净化成本低,应用范围广的特点。
The exhaust gas purification system provided by the present invention includes a pretreatment filter device, a first vacuum filter box and a second vacuum filter box, and also includes a sedimentation tank. The pretreatment filter device is installed at the exhaust gas inlet, and the first vacuum filter box is equipped with Water filtration treatment device, the second vacuum filter box is provided with an exhaust pipe, the exhaust pipe is provided with a vacuum pump, and a water pump is provided at the connection between the inlet pipe of the sedimentation tank and the sedimentation tank; it has good water and gas separation effect and good purification effect. Good, high purification efficiency, low purification cost and wide application range.
Description
技术领域technical field
本发明属于废气净化技术领域,具体涉及一种废气净化系统。The invention belongs to the technical field of exhaust gas purification, and in particular relates to an exhaust gas purification system.
背景技术Background technique
随着社会经济的发展,社会的工业化程度也在加深。与此同时,社会工业化进程所带来的大气污染问题也越来越引起人们的广泛关注。工业生产排放的废气,常对环境和人体健康产生有害影响,另一方面,企业的生存问题是废气大量排放所带来的必然结果,国家要求企业将其生产所产生的工业废气在排入大气前应采取净化措施处理,使之符合废气排放标准的要求,并对于不达标的废气排放企业进行了严厉的惩治。不论是出于保护环境,还是为了企业的可持续发展,废气净化都是当下一个急需解决的技术问题。With the development of social economy, the degree of industrialization of society is also deepening. At the same time, the problem of air pollution caused by the process of social industrialization has attracted more and more attention. The waste gas emitted by industrial production often has harmful effects on the environment and human health. On the other hand, the survival of enterprises is the inevitable result of the large amount of waste gas discharged. The state requires enterprises to discharge the industrial waste gas produced by their production into the atmosphere. Purification measures should be taken to make it meet the requirements of the exhaust gas emission standards, and severe punishments have been imposed on enterprises that fail to meet the emission standards. Whether it is for environmental protection or for the sustainable development of enterprises, exhaust gas purification is the next technical problem that needs to be solved urgently.
目前,废气净化系统采用的废气净化的基本方法有吸收法、吸附法、冷凝法、催化转化法及燃烧法等,其中水吸收法因成本低、需要的装置简单而应用范围较为广泛。但是现有技术中的采用水吸收法进行废气净化的系统存在由于净化水不能很好的循环利用,并且不能较好的与气体分离、干燥,继而造成净化水浪费,净化后的气体净化效果降低,最终造成整个废气净化系统的净化效果降低、净化效率降低和净化成本增高。At present, the basic methods of exhaust gas purification adopted by the exhaust gas purification system include absorption method, adsorption method, condensation method, catalytic conversion method and combustion method, etc. Among them, the water absorption method has a wide range of applications due to its low cost and simple required devices. However, in the prior art systems that use water absorption to purify exhaust gas, the purified water cannot be recycled well, and it cannot be separated and dried well from the gas, which in turn causes waste of purified water and reduces the purification effect of the purified gas. , Ultimately resulting in the reduction of the purification effect of the entire exhaust gas purification system, the reduction of purification efficiency and the increase of purification costs.
发明内容Contents of the invention
为了解决上述现有技术中存在的技术缺陷,本发明提供了一种能够实现净化水循环利用,同时充分分离和干燥净化水和气体,净化效果较好、净化效率较高,并且净化成本低的废气净化系统。In order to solve the technical defects in the above-mentioned prior art, the present invention provides a waste gas that can realize the recycling of purified water, fully separate and dry purified water and gas at the same time, have better purification effect, higher purification efficiency, and low purification cost. purification system.
本发明解决其技术问题是通过以下技术方案实现的:The present invention solves its technical problem and realizes through the following technical solutions:
废气净化系统,包括依次通过过滤管连通的预处理过滤装置、第一真空过滤箱和第二真空过滤箱,同时还包括沉淀池,所述第一真空过滤箱通过出水管将污水排入沉淀池,所述沉淀池通过进水管将沉淀后的净水输入第一真空过滤箱,所述预处理过滤装置安装于废气进口处,所述第一真空过滤箱内设有水过滤处理装置,所述第二真空过滤箱内通有排气管,所述排气管上设有真空泵,所述沉淀池的进水管与沉淀池连接处设置抽水泵。Exhaust gas purification system, including a pretreatment filtering device, a first vacuum filter box and a second vacuum filter box connected in sequence through a filter pipe, and also includes a sedimentation tank, and the first vacuum filter box discharges sewage into the sedimentation tank through an outlet pipe , the sedimentation tank enters the precipitated clean water into the first vacuum filter box through the water inlet pipe, the pretreatment filter device is installed at the exhaust gas inlet, the first vacuum filter box is provided with a water filter treatment device, and the There is an exhaust pipe in the second vacuum filter box, a vacuum pump is provided on the exhaust pipe, and a water pump is arranged at the connection between the inlet pipe of the sedimentation tank and the sedimentation tank.
作为进一步改进的技术方案,所述水过滤处理装置包括第一钢丝网和弯曲排气管道,所述第一钢丝网固定于第一真空过滤箱中,开有一个开孔,自所述预处理过滤装置通入第一真空过滤箱的过滤管穿过所述开孔后与下方的弯曲排气管道相接,所述第一钢丝网表面放置过滤布,所述弯曲排气管道表面设有若干微孔。As a further improved technical solution, the water filtration treatment device includes a first steel wire mesh and a curved exhaust pipe, the first steel wire mesh is fixed in the first vacuum filter box, and an opening is opened. The filter tube of the filter device leading into the first vacuum filter box passes through the opening and connects with the curved exhaust pipe below. The surface of the first steel mesh is placed with filter cloth, and the surface of the curved exhaust pipe is provided with several microporous.
作为进一步改进的技术方案,在所述第二真空过滤箱内的,所述过滤管的管口位置低于排气管的管口,同时所述排气管的管口设置为喇叭形。As a further improved technical solution, in the second vacuum filter box, the mouth of the filter pipe is lower than the mouth of the exhaust pipe, and the mouth of the exhaust pipe is set in a trumpet shape.
作为进一步改进的技术方案,所述真空泵采用排气多缸真空泵。As a further improved technical solution, the vacuum pump adopts an exhaust multi-cylinder vacuum pump.
作为进一步改进的技术方案,所述预处理过滤装置与第一真空过滤箱之间的过滤管上设有低压进度平衡表,所述排气管上同样设有低压进度平衡表,所述废气进口处和排气管上均设有调节阀,所述第一真空过滤箱一侧设有水位观测玻璃管。As a further improved technical solution, a low-pressure progress balance meter is provided on the filter pipe between the pretreatment filter device and the first vacuum filter box, and a low-pressure progress balance meter is also provided on the exhaust pipe. Adjusting valves are provided on the outlet and the exhaust pipe, and a water level observation glass tube is provided on one side of the first vacuum filter box.
作为进一步改进的技术方案,所述微孔的直径为0.5mm,所述微孔的间距为7-9mm。As a further improved technical solution, the diameter of the microholes is 0.5mm, and the distance between the microholes is 7-9mm.
作为进一步改进的技术方案,所述进水管通入第一真空过滤箱内的管口位于第一钢丝网之上。As a further improved technical solution, the mouth of the water inlet pipe leading into the first vacuum filter box is located above the first steel wire mesh.
作为进一步改进的技术方案,所述第一真空过滤箱和第二真空过滤箱底部均放置了坡度为30-35°的过滤石堆,同时还设置了拦污栅。As a further improved technical solution, filter stone piles with a slope of 30-35° are placed at the bottom of the first vacuum filter box and the second vacuum filter box, and trash racks are also installed.
作为进一步改进的技术方案,所述沉淀池依次分为各自设有调节阀的第一沉淀仓、第二沉淀仓和第三沉淀仓,自所述第一真空过滤箱通入的出水管中的废水通过出水管浸入第一沉淀仓底部,所述第一沉淀仓、第二沉淀仓和第三沉淀仓底部均设置了拦污栅和坡度为30-35°的过滤石堆,所述第一沉淀池与第二沉淀池之间由第一隔墙阻断,所述第一隔墙具有滤孔,所述滤孔呈倒三角形,所述第二沉淀池与第三沉淀池之间由第二隔墙阻断,所述第二隔墙具有楔形口,所述第一隔墙、第二隔墙均采用混凝土材料,所述滤孔、楔形口均采用钢质材料,所述第三沉淀仓中部设有水平的第二钢丝网,所述第二钢丝网表面覆有透水棉布,所述透水棉布上放有试剂,试剂由以下重量百分比的组分组成:生石灰40%、絮凝剂40%和焦炭20%。As a further improved technical solution, the sedimentation tank is divided into the first sedimentation bin, the second sedimentation bin and the third sedimentation bin each equipped with a regulating valve in turn, and the outlet pipe leading from the first vacuum filter box The waste water is immersed into the bottom of the first sedimentation bin through the outlet pipe, and the bottom of the first sedimentation bin, the second sedimentation bin and the third sedimentation bin are all equipped with trash racks and filter stone piles with a slope of 30-35°. The sedimentation tank and the second sedimentation tank are blocked by a first partition wall, the first partition wall has filter holes, and the filter holes are in an inverted triangle shape, and the second sedimentation tank and the third sedimentation tank are separated by a second partition wall. The second partition wall has a wedge-shaped opening, the first partition wall and the second partition wall are made of concrete materials, the filter holes and wedge-shaped openings are all made of steel materials, and the middle part of the third settling bin A horizontal second steel mesh is provided, and the surface of the second steel mesh is covered with a permeable cotton cloth, and a reagent is placed on the permeable cotton cloth, and the reagent is composed of the following components in weight percentage: quicklime 40%, flocculant 40% and coke 20%.
本发明的有益效果为:The beneficial effects of the present invention are:
(1)采用两个真空过滤箱,一个用作进行水过滤,一个用作在水过滤后对净化好的气体进行干燥,如此便能够较好的使得净化水和气体分离,保证了净化后排放出的气体具有较好的净化效果,同时也减少了净化水的消耗和浪费,降低了净化成本;(1) Two vacuum filter boxes are used, one is used for water filtration, and the other is used for drying the purified gas after water filtration, so that the purified water and gas can be separated better, ensuring the discharge after purification The gas produced has a better purification effect, and at the same time reduces the consumption and waste of purified water, and reduces the cost of purification;
(2)设置了沉淀池,对使用后、受污染的净化水进行沉淀,最终得到干净的净化水,再次加入第一真空过滤箱中进行净化过滤,能够实现净化水的循环利用,不仅能解决地方缺水的问题,节约了资源,同时还提高了净化的效率;(2) Set up a sedimentation tank to settle the polluted purified water after use, and finally get clean purified water, which is added to the first vacuum filter box for purification and filtration, which can realize the recycling of purified water, and can not only solve the problem of The problem of local water shortage saves resources and improves the efficiency of purification;
(3)结构简单,使用方便,应用范围广,具有良好的应用前景和商业前景。(3) The structure is simple, the use is convenient, the application range is wide, and it has good application prospects and commercial prospects.
附图说明Description of drawings
图1是本发明的平面结构示意图;Fig. 1 is a schematic plan view of the present invention;
图2是本发明公开的排气多缸真空泵机构示意图;Fig. 2 is a schematic diagram of the exhaust multi-cylinder vacuum pump mechanism disclosed by the present invention;
附图标记:1、预处理过滤装置;11、大颗粒过滤网;12、沉淀杯;2、第一真空过滤箱;21、水过滤处理装置;211、第一钢丝网;2111、开孔;2112、滤布;212、弯曲排气管道;2121、微孔;3、第二真空过滤箱;31、排气管;32、真空泵;4、沉淀池;41、出水管;42、进水管;43、抽水泵;44、第一沉淀仓;45、第二沉淀仓;46、第三沉淀仓;461、第二钢丝网;462、透水棉布;47、第一隔墙;471、滤孔;48、第二隔墙;481、楔形口;5、低压进度平衡表;6、调节阀;7、水位观测玻璃管;8、过滤石堆;9、拦污栅;10、过滤管;13、废气入口;14、排污管道。Reference signs: 1. Pretreatment filter device; 11. Large particle filter; 12. Sedimentation cup; 2. First vacuum filter box; 21. Water filtration treatment device; 211. First steel wire mesh; 2111. Opening; 2112, filter cloth; 212, curved exhaust pipe; 2121, microporous; 3, the second vacuum filter box; 31, exhaust pipe; 32, vacuum pump; 4, sedimentation tank; 41, outlet pipe; 42, water inlet pipe; 43, water pump; 44, first sedimentation bin; 45, second sedimentation bin; 46, third sedimentation bin; 461, second steel wire mesh; 462, permeable cotton cloth; 47, first partition wall; 471, filter hole; 48. Second partition wall; 481. Wedge-shaped opening; 5. Low-pressure progress balance meter; 6. Regulating valve; 7. Glass tube for water level observation; 8. Filter stone pile; 9. Trash rack; 10. Filter pipe; 13. Exhaust gas inlet; 14. Sewage pipe.
具体实施方式Detailed ways
下面结合图1和发明的原理对本发明的具体实施方式进行进一步的阐述,以下具体实施方式例只是描述性的,不是限定性的,不能以此限定本发明的保护范围。The specific implementation of the present invention will be further elaborated below in conjunction with FIG. 1 and the principle of the invention. The following specific implementation examples are only descriptive, not restrictive, and cannot limit the protection scope of the present invention.
实施例Example
如图1所示,待处理的废气从废气入口13处,经过预处理过滤装置1,大颗粒过滤网1111将首先把废气中的大颗过滤掉,在大颗粒过滤网11的前端设置有沉淀杯12,其目的是为了盛装经大颗粒过滤网11滤出的废气中的大颗粒。As shown in Figure 1, the exhaust gas to be treated passes through the pretreatment filter device 1 from the exhaust gas inlet 13, and the large particle filter screen 1111 will first filter out the large particles in the exhaust gas, and the front end of the large particle filter screen 11 is provided with a sediment The purpose of cup 12 is to contain the large particles in the exhaust gas filtered out by the large particle filter screen 11.
本实施例中,从第一真空过滤箱2中的滤布2112及钢丝网上的开孔2111穿过的过滤管10浸入水中并与弯曲排气管道212相接,需要说明的是,第一真空过滤箱2中的水位高度不超过第一钢丝网211。为了增大废气和水的接触面积,弯曲排气管道212呈盘旋状盘叠,其盘旋的圈数根据靠近废气入口13处的低压进度平衡表5来确定;同时,弯曲排气管道212表面每间隔7-9mm布置一个微孔2121,微孔2121的直径为0.5mm,废气从过微孔2121中排出,进入水中。In this embodiment, the filter pipe 10 passing through the filter cloth 2112 in the first vacuum filter box 2 and the opening 2111 on the wire mesh is immersed in water and connected with the curved exhaust pipe 212. It should be noted that the first vacuum The water level in the filter box 2 does not exceed the first wire mesh 211 . In order to increase the contact area between exhaust gas and water, the curved exhaust pipe 212 is stacked in a spiral shape, and the number of circles is determined according to the low-pressure schedule balance table 5 near the exhaust gas inlet 13; at the same time, the surface of the curved exhaust pipe 212 is A microhole 2121 is arranged at an interval of 7-9mm, and the diameter of the microhole 2121 is 0.5mm. The exhaust gas is discharged through the microhole 2121 and enters the water.
在整个废气净化过程中,真空泵32保持工作状态,如图2所示,本实施例中的真空泵32采用排气多缸真空泵32。需要说明的是,排气多缸真空泵32的气压大小根据进出口处的低压进度平衡表5来具体确定。经第一真空过滤箱2净化后的气体在排气多缸真空泵32的作用下穿过滤布2112被吸出,继而进入第二真空过滤箱3。需要说明的是,滤布2112具有控制气体湿度和进一步净化气体的作用。During the whole waste gas purification process, the vacuum pump 32 keeps working. As shown in FIG. 2 , the vacuum pump 32 in this embodiment adopts an exhaust multi-cylinder vacuum pump 32 . It should be noted that the air pressure of the exhaust multi-cylinder vacuum pump 32 is specifically determined according to the low pressure schedule balance table 5 at the inlet and outlet. The gas purified by the first vacuum filter box 2 is sucked out through the filter cloth 2112 under the action of the exhaust multi-cylinder vacuum pump 32 , and then enters the second vacuum filter box 3 . It should be noted that the filter cloth 2112 has the functions of controlling the humidity of the gas and further purifying the gas.
本实施例中的连通第一真空过滤箱2和第二真空过滤箱3的过滤管10,其置于第一真空过滤箱2内的管口距离水面距离至少30cm,如此设置,是因为在管口距离水面30cm以上时,能够防止水被吸进过滤管10。在实施例实施时,即便有水被真空泵32吸入第二真空过滤箱3,在经第二真空过滤箱3净化后,气体也能够和水分离,再通过排气管31排出。为了提高净化后的气体排放效率,本实施例中,在第二真空过滤箱3内,过滤管10的管口位置低于排气管31的管口位置,同时排气管31的管口设置为喇叭形。The filter pipe 10 that communicates with the first vacuum filter box 2 and the second vacuum filter box 3 in the present embodiment, it is placed in the pipe mouth in the first vacuum filter box 2 and is at least 30cm away from the water surface, so it is set because in the tube When the mouth is more than 30cm away from the water surface, water can be prevented from being sucked into the filter tube 10. When the embodiment is implemented, even if water is sucked into the second vacuum filter box 3 by the vacuum pump 32 , the gas can be separated from the water after being purified by the second vacuum filter box 3 , and then discharged through the exhaust pipe 31 . In order to improve the gas discharge efficiency after purification, in the present embodiment, in the second vacuum filter box 3, the nozzle position of the filter pipe 10 is lower than the nozzle position of the exhaust pipe 31, and the nozzle position of the exhaust pipe 31 is set at the same time Trumpet shaped.
本实施例中,第一真空过滤箱2底部通过出水管41连通沉淀池4,沉淀池4依次分为各自设有调节阀6的第一沉淀仓44、第二沉淀仓45和第三沉淀仓46,自第一真空过滤箱2通入的出水管41中的废水通过排水管浸入第一沉淀仓44底部,所述第一沉淀仓44、第二沉淀仓45和第三沉淀仓46底部均设置了拦污栅9和坡度为30-35°的过滤石堆8,所述第一沉淀池4与第二沉淀池4之间由第一隔墙47阻断,所述第一隔墙47具有滤孔471,所述滤孔471呈倒三角形,所述第二沉淀池4与第三沉淀池4之间由第二隔墙48阻断,所述第二隔墙48具有楔形口481,所述第一隔墙47、第二隔墙48均采用混凝土材料,所述滤孔471、楔形口481均采用钢质材料。需要说明的是,沉淀池4的大小根据废气的排气量来确定。进入第一沉淀仓44的出水管41浸入水中,如此能够增大真空过滤箱中水的阻力。本实施例中在沉淀仓的底部还设置了排污管道14,目的是为了过滤废水中的杂质,防止大的杂质的堵塞。滤孔471具有测流量和过滤的作用,在第一沉淀仓44经过沉淀后的废水经过滤孔471进入第二沉淀仓45。楔型口具有引流和加氧的作用,第二沉淀仓45中的废水经过楔型口流入第三沉淀仓46中。第三沉淀仓46中部设有水平的第二钢丝网461,第二钢丝网461上表面覆又透水棉布462,透水棉布462上放有试剂,试剂由生石灰40%、絮凝剂40%和焦炭20%的重量百分比组分组成,其目的是为了中和废水中的化学物质,实现综合净化。第三沉淀池4仓中的水经过抽水泵43又重新进入真空过滤箱,抽水泵43的功率根据废气量的大小来确定。本实施例中,进水管42通入第一真空过滤箱2内的管口位于钢丝网之上,其目的是自动冲洗滤布2112。In this embodiment, the bottom of the first vacuum filter box 2 is connected to the sedimentation tank 4 through the outlet pipe 41, and the sedimentation tank 4 is divided into a first sedimentation bin 44, a second sedimentation bin 45, and a third sedimentation bin that are each provided with a regulating valve 6 in turn. 46, the waste water in the outlet pipe 41 leading from the first vacuum filter box 2 is immersed into the bottom of the first settling bin 44 through the drain pipe, and the bottoms of the first settling bin 44, the second settling bin 45 and the third settling bin 46 are all A trash rack 9 and a filter stone pile 8 with a slope of 30-35° are set, and the first sedimentation tank 4 and the second sedimentation tank 4 are blocked by a first partition wall 47, and the first partition wall 47 There is a filter hole 471, the filter hole 471 is an inverted triangle, the second sedimentation tank 4 and the third sedimentation tank 4 are blocked by a second partition wall 48, and the second partition wall 48 has a wedge-shaped mouth 481, Both the first partition wall 47 and the second partition wall 48 are made of concrete, and the filter hole 471 and the wedge-shaped opening 481 are made of steel. It should be noted that the size of the sedimentation tank 4 is determined according to the exhaust gas volume. The outlet pipe 41 entering the first settling bin 44 is immersed in water, which can increase the resistance of the water in the vacuum filter box. In this embodiment, a sewage discharge pipe 14 is also provided at the bottom of the sedimentation bin, the purpose of which is to filter impurities in the waste water and prevent blockage of large impurities. The filter hole 471 has the functions of measuring flow rate and filtering, and the waste water after sedimentation in the first settling bin 44 enters the second settling bin 45 through the filter hole 471 . The wedge-shaped mouth has the functions of drainage and oxygenation, and the waste water in the second sedimentation bin 45 flows into the third sedimentation bin 46 through the wedge-shaped mouth. The middle part of the third settling bin 46 is provided with a horizontal second steel wire mesh 461. The upper surface of the second steel wire mesh 461 is covered with a water-permeable cotton cloth 462. A reagent is placed on the water-permeable cotton cloth 462. The reagent consists of 40% quicklime, 40% flocculant and 20% coke. % by weight component composition, its purpose is to neutralize the chemical substances in the wastewater and realize comprehensive purification. The water in the third settling tank 4 storehouse re-enters the vacuum filter box through the water pump 43, and the power of the water pump 43 is determined according to the amount of waste gas. In this embodiment, the mouth of the water inlet pipe 42 leading into the first vacuum filter box 2 is located above the steel wire mesh, and its purpose is to automatically flush the filter cloth 2112 .
本实施例中,第一真空过滤箱2一侧设有水位观测玻璃管7,水位观测玻璃管7能够直观反映第一真空过滤箱2内水位的变化。In this embodiment, a water level observation glass tube 7 is provided on one side of the first vacuum filtration box 2 , and the water level observation glass tube 7 can intuitively reflect the change of the water level in the first vacuum filtration box 2 .
本发明的规模可以根据具体的应用对象而定,经过发明人的长期研究和试验,本发明的所述的技术方案不仅适用于工厂,化肥厂,印刷厂,制药厂等大型企业,对于商场,餐馆,家庭等公共场所同样也适用,应用前景十分广阔。The scale of the present invention can be determined according to the specific application object. Through the long-term research and experiment of the inventor, the described technical scheme of the present invention is not only applicable to large enterprises such as factories, chemical fertilizer plants, printing plants, and pharmaceutical factories. For shopping malls, Public places such as restaurants and families are also applicable, and the application prospect is very broad.
以上所述仅是本发明的优选具体实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention, it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the present invention, some improvements and modifications can also be made, these improvements and modifications It should also be regarded as the protection scope of the present invention.
Claims (10)
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Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003078028A1 (en) * | 2002-03-19 | 2003-09-25 | Bum-Hong Kim | Waste gas purifier |
| CN2616280Y (en) * | 2003-04-18 | 2004-05-19 | 溧阳市溧竹环境工程有限公司 | Efficient wet desulfurizing dust-removing apparatus |
| CN2675231Y (en) * | 2004-02-18 | 2005-02-02 | 单国良 | Combined type flue desulfurizing and dust-removing purifier |
| CN102863079A (en) * | 2012-10-25 | 2013-01-09 | 河北嘉诚环境工程有限公司 | Improved aeration settling tank |
| CN203577543U (en) * | 2013-10-14 | 2014-05-07 | 中国华能集团清洁能源技术研究院有限公司 | Smoke cooling and dedusting device capable of reducing PM2.5 (Particulate Matter) discharge for coal-fired power plant |
| CN105833627A (en) * | 2016-06-01 | 2016-08-10 | 中冶长天国际工程有限责任公司 | Water bath deduster, dedusting method and quicklime slaking and dedusting device |
| CN105833625A (en) * | 2015-01-14 | 2016-08-10 | 李俊德 | Gas filtering cylinder structure |
| CN205850419U (en) * | 2016-07-22 | 2017-01-04 | 上海海洋大学 | A kind of gas-liquid separation device being applied to solid-phase extracting instrument |
| CN106492610A (en) * | 2016-11-20 | 2017-03-15 | 杨朴 | A kind of water bath dust-removing desulfurization and dirt mud processing method |
-
2017
- 2017-12-06 CN CN201711275276.0A patent/CN107754543A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003078028A1 (en) * | 2002-03-19 | 2003-09-25 | Bum-Hong Kim | Waste gas purifier |
| CN2616280Y (en) * | 2003-04-18 | 2004-05-19 | 溧阳市溧竹环境工程有限公司 | Efficient wet desulfurizing dust-removing apparatus |
| CN2675231Y (en) * | 2004-02-18 | 2005-02-02 | 单国良 | Combined type flue desulfurizing and dust-removing purifier |
| CN102863079A (en) * | 2012-10-25 | 2013-01-09 | 河北嘉诚环境工程有限公司 | Improved aeration settling tank |
| CN203577543U (en) * | 2013-10-14 | 2014-05-07 | 中国华能集团清洁能源技术研究院有限公司 | Smoke cooling and dedusting device capable of reducing PM2.5 (Particulate Matter) discharge for coal-fired power plant |
| CN105833625A (en) * | 2015-01-14 | 2016-08-10 | 李俊德 | Gas filtering cylinder structure |
| CN105833627A (en) * | 2016-06-01 | 2016-08-10 | 中冶长天国际工程有限责任公司 | Water bath deduster, dedusting method and quicklime slaking and dedusting device |
| CN205850419U (en) * | 2016-07-22 | 2017-01-04 | 上海海洋大学 | A kind of gas-liquid separation device being applied to solid-phase extracting instrument |
| CN106492610A (en) * | 2016-11-20 | 2017-03-15 | 杨朴 | A kind of water bath dust-removing desulfurization and dirt mud processing method |
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Application publication date: 20180306 |