CN201614321U - New pulse water distribution UASB water treatment device - Google Patents
New pulse water distribution UASB water treatment device Download PDFInfo
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- CN201614321U CN201614321U CN2009201070631U CN200920107063U CN201614321U CN 201614321 U CN201614321 U CN 201614321U CN 2009201070631 U CN2009201070631 U CN 2009201070631U CN 200920107063 U CN200920107063 U CN 200920107063U CN 201614321 U CN201614321 U CN 201614321U
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract
新型脉冲布水UASB水处理方法与装置,涉及一种废水处理设备技术。本实用新型是为解决UASB反应器内容易出现的布水不均、堵塞及短流等现象而提出的改进装置,采用脉冲布水器和新型布水装置相结合的方法提供均匀布水,促进反应器内泥水混合;新型布水装置含布水托架和紧密排列的布水板,水流通过布水板之间的缝隙折流进入反应器;在三相分离器的气室设置回流挡板,有助于气室混合液回流,防止堵塞,利于气体释放和收集。本实用新型投资少,水处理效率高,可有效回收沼气资源,还具有运行稳定,便于操作管理等优点。
A novel pulse water distribution UASB water treatment method and device relates to a waste water treatment equipment technology. The utility model is an improved device proposed to solve the phenomenon of uneven water distribution, blockage and short flow that easily occur in the UASB reactor. The mud and water are mixed in the reactor; the new water distribution device includes a water distribution bracket and closely arranged water distribution plates, and the water flow enters the reactor through the gap between the water distribution plates; a backflow baffle is set in the air chamber of the three-phase separator , which is helpful for the backflow of the mixed liquid in the gas chamber, prevents clogging, and facilitates the release and collection of gas. The utility model has the advantages of less investment, high water treatment efficiency, effective recovery of biogas resources, stable operation, and convenient operation and management.
Description
技术领域technical field
本实用新型涉及一种废水处理设备,具体是一种脉冲布水UASB的水处理方法和装置。The utility model relates to a waste water treatment device, in particular to a water treatment method and device of a pulse water distribution UASB.
背景技术Background technique
厌氧生物处理利用厌氧性微生物的代谢,在毋需提供外源能量的条件下,以被还原有机物作为受氢体,同时产生有能源价值的甲烷气体。不仅适用于高浓度有机废水,进水BOD最高浓度可达数万毫克升,也可适用于低浓度有机废水,如城市污水等。在全社会提倡循环经济,关注工业废弃物实施资源化再生利用的今天,厌氧生物处理显然是能够使污水资源化的优选工艺。升流式厌氧污泥床(UASB)工艺由于具有厌氧过滤及厌氧活性污泥法的双重特点,作为能够将污水中的污染物转化成再生清洁能源——沼气的一项技术。对于不同含固量污水的适应性也强,且其结构、运行操作维护管理相对简单,造价也相对较低,正日益受到污水处理业界的重视,得到广泛的欢迎和应用。Anaerobic biological treatment uses the metabolism of anaerobic microorganisms to use the reduced organic matter as a hydrogen acceptor without providing external energy, and at the same time produce methane gas with energy value. It is not only suitable for high-concentration organic wastewater, the highest concentration of BOD in the influent can reach tens of thousands of milliliters, but also suitable for low-concentration organic wastewater, such as urban sewage. Today, when the whole society advocates circular economy and pays attention to the recycling of industrial waste, anaerobic biological treatment is obviously the preferred process for recycling sewage. Upflow Anaerobic Sludge Blanket (UASB) process is a technology that can convert pollutants in sewage into renewable clean energy—biogas because of its dual characteristics of anaerobic filtration and anaerobic activated sludge process. It also has strong adaptability to sewage with different solid content, and its structure, operation, operation, maintenance and management are relatively simple, and its cost is relatively low. It is increasingly valued by the sewage treatment industry and widely welcomed and applied.
然而,UASB在实际运行过程中仍然存在着一些问题。UASB内的水流流态较为复杂,由于产气的结果,反应器内形成一股上升的气流,带动部分泥水混合液作向上运动,与此同时,这股气、水流周围的介质则向下运动,造成逆向混合,这种流态造成了水的短流,在远离这股上升气、水流的地方则容易形成死角。因而,UASB系统的稳定运行需要设置合理的进水和布水方式,实际工程中UASB容易出现布水不均匀和堵塞等问题。However, there are still some problems in the actual operation of UASB. The water flow in UASB is relatively complicated. As a result of gas production, a rising air flow is formed in the reactor, which drives part of the mud-water mixture to move upward. At the same time, the medium around the gas and water flow moves downward. , resulting in reverse mixing, this flow state has caused a short flow of water, and it is easy to form a dead angle in a place far away from this rising air and water flow. Therefore, the stable operation of the UASB system requires reasonable water intake and water distribution methods. In actual projects, UASB is prone to problems such as uneven water distribution and blockage.
实用新型内容Utility model content
本实用新型的目的是针对传统UASB反应器的缺陷,提出一种新型脉冲布水UASB水处理方法与装置,该实用新型采用脉冲布水器提供脉冲进水,并采用新型布水装置与其相配合,一方面为反应器提供了均匀的脉冲水流,间歇性提供上升水流和污泥下沉时间,促进泥水混合,另一方面解决了布水堵塞的问题;并且在三相分离器的气室设置回流挡板,促进气室混合液回流,防止堵塞,利于气体释放和收集。The purpose of this utility model is to propose a new pulse water distribution UASB water treatment method and device for the defects of traditional UASB reactors. The utility model uses a pulse water distributor to provide pulse water intake, and a new water distribution device to cooperate with it , On the one hand, it provides uniform pulsed water flow for the reactor, intermittently provides rising water flow and sludge sinking time, promotes mud-water mixing, and on the other hand solves the problem of water blockage; and the air chamber of the three-phase separator is set The backflow baffle promotes the backflow of the mixed liquid in the gas chamber, prevents clogging, and facilitates the release and collection of gas.
本实用新型通过以下方案实现:该装置包括脉冲布水器1、新型布水装置2、UASB反应器3和三相分离器4;其特征在于,该三相分离器4设置气室回流挡板,该新型布水装置2由布水托架9和紧密排列的布水板10组成,该布水板10倾斜放置于布水托架9之上,与布水托架9构成布水室;水流通过布水板10之间的缝隙折流进入反应器内;新型布水装置2为圆形、方形或矩形,含两组或两组以上布水板,布水板呈环形、回形或直线型排列。The utility model is realized through the following scheme: the device includes a
一种采用上述装置的新型脉冲布水UASB水处理方法,其特征在于,进水由脉冲布水器1提供脉冲水流,经新型布水装置2进入反应器内;新型布水装置2的特别设计使水流和反应器内的污泥层5充分接触反应并可有效防止堵塞问题;泥水反应后产生的气泡携带污水混合物经悬浮层6进入三相分离器,气泡碰到回流挡板时散开,进入气室7,经气室7顶部的导管导出;气室7中的污水混合液经三相分离器4的回流挡板回流至悬浮层6;污水中的污泥相互絮凝积聚在重力作用下下沉;污水混合液进入沉淀区8沉淀出水;该方法由脉冲布水器提供脉冲进水方式,为反应器提供间歇式的上升水流和污泥下沉时间,促进泥水混合;新型布水装置在提供均匀进水的同时,可以有效防止堵塞问题;布水室为进水的均匀分布提供了条件;三相分离器设置气室回流挡板,可以将积聚在气室的污泥回流至悬浮层,防止气室堵塞,利于气体释放和收集。A new pulse water distribution UASB water treatment method using the above-mentioned device, characterized in that the incoming water is provided with pulse water flow by the
本实用新型克服了传统UASB反应器内的短流和死角现象,采用脉冲进水方式和新型布水装置相结合的方法提供均匀布水,促进反应器内泥水混合,三相分离器的回流挡板有助于气室混合液回流,防止堵塞,利于气体释放和收集。本实用新型投资少,水处理效率高,可有效回收沼气资源,还具有运行稳定,便于操作管理等优点。The utility model overcomes the short flow and dead angle phenomenon in the traditional UASB reactor, adopts the method of combining the pulse water inlet mode and the new water distribution device to provide uniform water distribution, promote the mixing of mud and water in the reactor, and the backflow block of the three-phase separator The plate helps the gas chamber mixture to flow back, prevents clogging, and facilitates gas release and collection. The utility model has the advantages of less investment, high water treatment efficiency, effective recovery of biogas resources, stable operation, and convenient operation and management.
附图说明Description of drawings
图1为本实用新型装置示意图。Fig. 1 is the schematic diagram of the utility model device.
图中:1-脉冲布水器,2-新型布水装置,3-UASB反应器,4-三相分离器,5-污泥层,6-悬浮层,7-气室,8-沉淀区。In the figure: 1-pulse water distributor, 2-new water distribution device, 3-UASB reactor, 4-three-phase separator, 5-sludge layer, 6-suspension layer, 7-air chamber, 8-sedimentation area .
图2为本实用新型提供的新型布水装置剖面图和平面图。Fig. 2 is a sectional view and a plan view of the new water distribution device provided by the utility model.
图中,9-布水托架,10-布水板。Among the figure, 9-water distribution bracket, 10-water distribution plate.
图3为本实用新型提供的新型布水装置俯视图。Fig. 3 is a top view of the new water distribution device provided by the utility model.
图中,10-布水板。Among the figure, 10-water distribution board.
具体实施方式Detailed ways
下面结合附图,对本实用新型的原理和工作过程作进一步的说明。Below in conjunction with accompanying drawing, the principle of the utility model and working process are further described.
如图1所示,进水由脉冲布水器1提供脉冲水流,经新型布水装置2进入反应器内;脉冲进水方式可为反应器提供间歇式的上升水流和污泥下沉时间,促进泥水混合;新型布水装置2中布水板10的倾斜设置可有效防止堵塞问题,使得进水经布水板折流进入反应器,产生斜向的水流,引起反应器内的污泥层5扰动混合,并与进水充分接触反应;由布水托架9和布水板10构成的布水室可缓解单点进水冲击,为进水的均匀分布提供了条件;脉冲进水方式与新型布水装置2相结合使得进水水流分布均匀,避免了短流和死角;泥水反应后产生的气泡携带污水混合物经悬浮层6进入三相分离器4,气泡碰到回流挡板时散开,进入气室7,经气室7顶部的导管导出;气室7中的污水混合液经三相分离器4的回流挡板回流至悬浮层6,可以防止气室堵塞,利于气体释放和收集;污水中的污泥相互絮凝积聚在重力作用下下沉;污水混合液进入沉淀区8沉淀出水。As shown in Figure 1, the water inflow is provided by the
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102815784A (en) * | 2012-08-29 | 2012-12-12 | 深圳清华大学研究院 | Aerobic three-phase separator and application method thereof in sewage treatment |
| CN102992482A (en) * | 2012-12-31 | 2013-03-27 | 浙江水美环保工程有限公司 | Low concentration organic wastewater anaerobic reactor |
| CN104692523A (en) * | 2013-12-04 | 2015-06-10 | 林凤俊 | UASB reactor |
| CN108946936A (en) * | 2018-08-23 | 2018-12-07 | 重庆怡灏园林工程有限公司 | The UASB reactor of tape pulse water distribution |
| CN109160604A (en) * | 2018-10-25 | 2019-01-08 | 青岛理工大学 | Combined type three-phase separator |
-
2009
- 2009-05-22 CN CN2009201070631U patent/CN201614321U/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102815784A (en) * | 2012-08-29 | 2012-12-12 | 深圳清华大学研究院 | Aerobic three-phase separator and application method thereof in sewage treatment |
| CN102815784B (en) * | 2012-08-29 | 2014-06-25 | 深圳清华大学研究院 | Aerobic three-phase separator and application method thereof in sewage treatment |
| CN102992482A (en) * | 2012-12-31 | 2013-03-27 | 浙江水美环保工程有限公司 | Low concentration organic wastewater anaerobic reactor |
| CN104692523A (en) * | 2013-12-04 | 2015-06-10 | 林凤俊 | UASB reactor |
| CN108946936A (en) * | 2018-08-23 | 2018-12-07 | 重庆怡灏园林工程有限公司 | The UASB reactor of tape pulse water distribution |
| CN108946936B (en) * | 2018-08-23 | 2024-02-02 | 怡灏环境技术有限公司 | UASB reactor with pulse water distribution |
| CN109160604A (en) * | 2018-10-25 | 2019-01-08 | 青岛理工大学 | Combined type three-phase separator |
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| CB03 | Change of inventor or designer information |
Inventor after: Chen Futai Inventor after: Fan Zhenghong Inventor before: Chen Futai Inventor before: Fan Zhenghong Inventor before: Du Jiedi Inventor before: Zheng Xiankai |
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Address after: 100085 C building, Ka Wah building, No. 9, 3rd Street, Beijing, Haidian District, C404 Patentee after: BEIJING GO HIGHER ENVIRONMENT CO., LTD. Address before: 100085 C building, Ka Wah building, No. 9, 3rd Street, Beijing, Haidian District, C404 Patentee before: Beijing Qingda Guohua Environmental Protection Technology Co., Ltd. |
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Granted publication date: 20101027 |
