CN1253379C - Gas float and deposition equipment for separating solid and liquid - Google Patents
Gas float and deposition equipment for separating solid and liquid Download PDFInfo
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- CN1253379C CN1253379C CN 200410043895 CN200410043895A CN1253379C CN 1253379 C CN1253379 C CN 1253379C CN 200410043895 CN200410043895 CN 200410043895 CN 200410043895 A CN200410043895 A CN 200410043895A CN 1253379 C CN1253379 C CN 1253379C
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- 239000007788 liquid Substances 0.000 title claims abstract description 8
- 230000008021 deposition Effects 0.000 title 1
- 239000007787 solid Substances 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 131
- 238000005188 flotation Methods 0.000 claims abstract description 39
- 238000004062 sedimentation Methods 0.000 claims abstract description 26
- 238000000926 separation method Methods 0.000 claims abstract description 24
- 238000004891 communication Methods 0.000 claims abstract description 11
- 238000001556 precipitation Methods 0.000 claims abstract description 9
- 238000009826 distribution Methods 0.000 claims description 18
- 239000002893 slag Substances 0.000 claims description 13
- 239000013049 sediment Substances 0.000 claims description 10
- 238000005189 flocculation Methods 0.000 claims description 8
- 230000016615 flocculation Effects 0.000 claims description 8
- 238000005192 partition Methods 0.000 claims description 8
- 238000003860 storage Methods 0.000 claims description 5
- 238000000746 purification Methods 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 5
- 239000012535 impurity Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 241000195493 Cryptophyta Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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Abstract
气浮与沉淀固液分离装置,它涉及一种能切换运行的气浮与沉淀两种水处理工艺的净化水质的装置。本发明接触区挡板(5)的中下部开有通水孔(34),在通水孔(34)的接触区挡板(5)上设有连通阀(17),分离区(31)处的外壳(30)内的下部设有穿孔集水管(12),穿孔集水管(12)的外端穿过外壳(30)与气浮出水阀(9)的一端固定连接,气浮出水阀(9)的另一端连接有气浮出水管(13),穿孔花墙(20)的上部开有通孔(33)。本发明在接触区挡板(5)上开有通水孔(34)并设置了连通阀(17),在分离区(31)内设置了穿孔集水管(12),将穿孔花墙(20)的通孔(33)开在穿孔花墙(20)的上部,兼顾了气浮与沉淀两者的要求。本发明具有结构合理、操作方便、水质净化效果可达最佳效果的优点。
The utility model relates to an air flotation and sedimentation solid-liquid separation device, which relates to a water purification device capable of switching two water treatment processes of air flotation and sedimentation. The middle and lower part of the contact area baffle plate (5) of the present invention has a water hole (34), and a communication valve (17) is provided on the contact area baffle plate (5) of the water hole (34), and the separation area (31) The lower part of the shell (30) at the bottom is provided with a perforated water collection pipe (12), and the outer end of the perforated water collection pipe (12) passes through the shell (30) and is fixedly connected with one end of the air flotation water outlet valve (9), and the air flotation comes out The other end of the water valve (9) is connected with an air flotation outlet pipe (13), and the top of the perforated flower wall (20) has a through hole (33). The present invention has a water hole (34) on the baffle plate (5) in the contact area and is provided with a connecting valve (17), and a perforated water collection pipe (12) is provided in the separation area (31), and the perforated flower wall (20) The through hole (33) is opened on the top of the perforated flower wall (20), taking into account both the requirements of air flotation and precipitation. The invention has the advantages of reasonable structure, convenient operation and optimal water purification effect.
Description
技术领域technical field
本发明涉及一种能切换运行的气浮与沉淀两种水处理工艺的净化水质的装置,特别是制造生活和生产用水,以及污水处理等领域的固液分离装置。The invention relates to a water purification device capable of switching two water treatment processes of air flotation and sedimentation, in particular to a solid-liquid separation device in the fields of domestic and production water and sewage treatment.
背景技术Background technique
中国专利号为ZL92104174.8,名称为“侧向流斜板浮沉固液分离装置”的发明专利。这种装置对于处理低温低浊及高藻类水质原水,有一定的效果;对高浊度原水的处理也有较好的适应性。但通过生产实践证明仍存在严重影响水处理效果的问题;其一、设计的主导思想是兼顾气浮与沉淀两者设备的要求,实际上既没有很好满足气浮也没有很好满足沉淀的净水效果,其二、接触区挡板因兼顾气浮与沉淀两种工艺要求,而设置较矮,这样没能很好地满足气浮时溶气水与待处理水间充分混合接触形成絮凝体而凝聚的要求;同时,由于接触区挡板的设置阻碍了沉淀配水,易造成已形成良好的絮凝体破碎,影响处理效果,其三、为兼顾气浮与沉淀,设置穿孔花墙与集水槽集出水装置,气浮与沉淀共用,穿孔花墙开孔位于中部,而气浮要求底部集水,沉淀要求顶部集水,设在中部对二者都不满足,造成运行时无论气浮还是沉淀,出水中都挟带较多的絮凝体,影响沉淀与气浮的净水效果。The Chinese patent number is ZL92104174.8, which is an invention patent named "Floating and sinking solid-liquid separation device of lateral flow inclined plate". This device has a certain effect on the treatment of low-temperature, low-turbidity and high-algae water quality raw water; it also has good adaptability to the treatment of high-turbidity raw water. However, the production practice proves that there are still problems that seriously affect the water treatment effect; first, the leading idea of the design is to take into account the requirements of both air flotation and sedimentation equipment, and in fact neither air flotation nor sedimentation can be well satisfied Water purification effect, second, the baffle in the contact area is set relatively short because of the two technological requirements of air flotation and sedimentation, which fails to meet the full mixing and contact between dissolved air water and water to be treated during air flotation to form flocculation At the same time, because the setting of the baffle in the contact area hinders the sedimentation and water distribution, it is easy to cause the well-formed flocs to break and affect the treatment effect. Third, in order to take into account both air flotation and sedimentation, a perforated flower wall and a water collection tank are installed. The water collection and discharge device is shared by air flotation and sedimentation. The perforated flower wall opening is located in the middle, while air flotation requires water collection at the bottom and sedimentation requires water collection at the top. Setting it in the middle does not satisfy both, resulting in no matter whether it is air flotation or sedimentation during operation. There are more flocs in the effluent, which affects the water purification effect of sedimentation and air flotation.
发明内容:Invention content:
本发明的目的是提供一种气浮与沉淀固液分离装置,它具有结构合理、操作方便、水质净化效果可达到最佳状态的特点。本发明由隔板1、配水挡板2、溶气水管3、释放器4,接触区挡板5、斜板组件6、穿孔排泥管7、阻流板8、气浮出水阀9、刮泥机10、沉淀出水阀11、穿孔集水管12、气浮出水管13、沉淀排泥阀14、沉淀出水管15、排渣槽16、连通阀17、阀门手轮18、连杆19、穿孔花墙20、集水槽21、回流水泵22、空压机23、储气罐24、溶气罐25、管道26、总集水槽27、刮渣机28、外壳30组成,接触区挡板5固定在外壳30内,接触区挡板5左侧的外壳30内形成絮凝池29,接触区挡板5右侧的外壳30内形成分离区31,隔板1固定在絮凝池29处的外壳30内,配水挡板2固定在隔板1两侧的外壳30内,配水挡板2的下端与外壳30的内底之间设有过水通道32,接触区挡板5与相邻的配水挡板2之间形成接触区35,阻流板8固定在分离区31的外壳30的内底上,斜板组件6固定在阻流板8的上部,斜板组件6右侧的外壳30内固定有穿孔花墙20,穿孔花墙20上部的左侧固定有排渣槽16,穿孔花墙20与外壳30之间的上部设有集水槽21,集水槽21右侧的外壳30的上部固定有总集水槽27,总集水槽27的下部连接有沉淀出水阀11,沉淀出水阀11的下端连接有沉淀出水管15,外壳30的上开口处设有刮渣机28,外壳30下部的一侧设有排泥管7,排泥管7的内端与外壳30的内部相连通,排泥管7的外端连接有沉淀排泥阀14,分离区31的外壳30内的下部设有刮泥机10,溶气水管3的一端与溶气罐25的出口固定连接,溶气水管3的另一端设在接触区35内配水挡板2与接触区挡板5之间的下部并固定有释放器4,接触区挡板5的中下部开有通水孔34,在通水孔34处的接触区挡板5上设有连通阀17,连通阀17上设有连杆19,连杆19的外端固定有阀门手轮18,分离区31处的外壳30内的下部设有穿孔集水管12,穿孔集水管12的外端穿过外壳30与气浮出水阀9的一端固定连接,气浮出水阀9的另一端连接有气浮出水管13,穿孔花墙20的上部开有通孔33。本发明的接触区挡板5比已有技术挡板的高度加高了近三分之一,很好地满足了气浮时溶气水与待处理水间充分混合接触形成絮凝体而凝聚的要求;在接触区挡板5上开有通水孔34并设置了连通阀17,在分离区31内设置了穿孔集水管12,将穿孔花墙20的通孔33开在穿孔花墙20的上部,兼顾了气浮与沉淀两者的要求。本发明具有结构合理、操作方便、水质净化效果可达最佳效果的优点。The object of the present invention is to provide an air flotation and sedimentation solid-liquid separation device, which has the characteristics of reasonable structure, convenient operation and optimal water purification effect. The present invention consists of a
附图说明:Description of drawings:
图1是本发明的俯视结构示意图,图2是图1的A-A剖视图,图3是接触区挡板5与连通阀17的结构示意图,图4是已有气浮与沉淀固液分离装置的结构示意图。Fig. 1 is a schematic view of the top view of the present invention, Fig. 2 is a sectional view of A-A of Fig. 1, Fig. 3 is a schematic view of the structure of the contact
具体实施方式:Detailed ways:
具体实施方式一:(参见图1-图3)本实施方式由隔板1、配水挡板2、溶气水管3、释放器4,接触区挡板5、斜板组件6、穿孔排泥管7、阻流板8、气浮出水阀9、刮泥机10、沉淀出水阀11、穿孔集水管12、气浮出水管13、沉淀排泥阀14、沉淀出水管15、排渣槽16、连通阀17、阀门手轮18、连杆19、穿孔花墙20、集水槽21、回流水泵22、空压机23、储气罐24、溶气罐25、管道26、总集水槽27、刮渣机28、外壳30组成,接触区挡板5固定在外壳30内,接触区挡板5左侧的外壳30内形成絮凝池29,接触区挡板5右侧的外壳30内形成分离区31,隔板1固定在絮凝池29处的外壳30内,配水挡板2固定在隔板1两侧的外壳30内,配水挡板2的下端与外壳30的内底之间设有过水通道32,接触区挡板5与相邻的配水挡板2之间形成接触区35,阻流板8固定在分离区31的外壳30的内底上,斜板组件6固定在阻流板8的上部,斜板组件6右侧的外壳30内固定有穿孔花墙20,穿孔花墙20上部的左侧固定有排渣槽16,穿孔花墙20与外壳30之间的上部设有集水槽21,集水槽21右侧的外壳30的上部固定有总集水槽27,总集水槽27的下部连接有沉淀出水阀11,沉淀出水阀11的下端连接有沉淀出水管15,外壳30的上开口处设有刮渣机28,外壳30下部的一侧设有排泥管7,排泥管7的内端与外壳30的内部相连通,排泥管7的外端连接有沉淀排泥阀14,分离区31的外壳30内的下部设有刮泥机10,回流水泵22的出口端与管道26的一端固定连接,管道26的另一端与溶气罐25的进水端固定连接,空压机23的输出端与储气罐24的入口端相连接,储气罐24的出口端与溶气罐25的进气端相连接,溶气水管3的一端与溶气罐25的出口固定连接,溶气水管3的另一端设在接触区35内配水挡板2与接触区挡板5之间的下部并固定有释放器4,接触区挡板5的中下部开有通水孔34,在通水孔34处的接触区挡板5上设有连通阀17,连通阀17上设有连杆19,连杆19的外端固定有阀门手轮18,分离区31处的外壳30内的下部设有穿孔集水管12,穿孔集水管12的外端穿过外壳30与气浮出水阀9的一端固定连接,气浮出水阀9的另一端连接有气浮出水管13,穿孔花墙20的上部开有通孔33。Specific embodiment one: (see Figure 1-Figure 3) This embodiment consists of a
具体实施方式二:(参见图1)本实施方式与具体实施方式一的不同点在于,溶气水管3由两根组成,两根溶气水管3平行设置。其它组成和连接关系与Embodiment 2: (see FIG. 1 ) The difference between this embodiment and
具体实施方式一相同。The specific embodiment one is the same.
工作原理:在原水浊度较低及低温低浊、高藻、高色时,切换到气浮工艺运行。Working principle: When the raw water has low turbidity, low temperature, low turbidity, high algae, and high color, switch to the air flotation process.
(一)打开沉淀排泥阀14、启动刮泥机10,进行刮排泥,同时关闭沉淀出水阀11,停止出水。(二)根据排泥水质确定沉淀污泥排净后,关闭接触区挡板5上的连通阀17,启动回流水泵22、空压机23,待溶气压力达到时,通过压力溶气水管3及释放器4向接触区35即由接触区挡板5与配水挡板2之间构成的区域内通入压力溶气水,打开气浮出水阀9,关闭沉淀排泥阀14,停止排泥。(三)水流经接触区35即由接触区挡板5与配水挡板2构成的区域向上,越过接触区挡板5进入分离区31,再流经斜板组件6,实现水中杂质颗粒上浮分离后,倾斜偏向出水端向下流入穿孔集水管12内,构成出水。(1) Open the sediment discharge valve 14, start the
在原水浊度较高时,则切换至沉淀工艺运行。When the raw water turbidity is high, switch to the sedimentation process to run.
(一)关闭气浮出水阀9,同时启动刮渣机28,刮去水面浮渣。(二)打开接触区挡板5上的连通阀17。(三)打开沉淀出水阀11。(四)絮凝后的水流经接触区挡板5下部的连通阀17,进入斜板组件6,在其内进行沉淀分离,絮凝体杂质沉入底部,净化后水流入穿孔花墙20上部所开的通孔33,进入集水槽21,最后形成沉淀出水。(1) Close the air flotation
本发明的组件中如外壳、挡板、穿孔花墙、阻流板等部件可制成砼大型结构,也可用钢板、塑料等材料制做成中小型的结构。Parts such as shell, baffle plate, perforated flower wall, baffle plate and the like can be made into concrete large-scale structure in the assembly of the present invention, also available steel plate, plastics and other materials are made into medium and small-sized structure.
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CN101580314B (en) * | 2009-05-21 | 2014-02-26 | 广州市市政工程设计研究院 | Method for removing algae by air flotation and sedimentation solid-liquid separation |
CN101941765A (en) * | 2010-07-23 | 2011-01-12 | 东北电力大学 | Flotation and sedimentation solid-liquid separation device |
CN103332806A (en) * | 2013-06-24 | 2013-10-02 | 宜兴市全洲水工设备厂 | Automatic water processing system |
CN103570159A (en) * | 2013-11-14 | 2014-02-12 | 常州大学 | Device for treating high-concentration ammonia nitrogen in coal chemical wastewater in vortex mixing dispersion way by using surfactant |
CN107364936A (en) * | 2016-05-13 | 2017-11-21 | 江苏瑞盛水处理有限公司 | Efficient degreasing skimmer device |
CN105923680B (en) * | 2016-06-16 | 2019-10-25 | 广州市市政工程设计研究总院有限公司 | Downward and upward flow inclined plate air flotation-sedimentation solid-liquid separation device |
CN109502799A (en) * | 2017-09-15 | 2019-03-22 | 桑炎彬 | A kind of innoxious technology of waste water control and its technique |
CN107986511A (en) * | 2017-12-31 | 2018-05-04 | 广州市市政工程设计研究总院 | Water process air supporting and sedimentation solid-liquid separation device and processing method |
CN109205747A (en) * | 2018-10-26 | 2019-01-15 | 江门市新会区猫淘鹰贸易有限公司 | A kind of water process coagulation system |
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