| 高效柔性污水处理生化反应器 |
Efficient Flexible Sewage Treatment Biochemical Reactor |
| 摘要 |
Abstract |
| 高效柔性污水处理生化反应器是一个具有器壁的容器，具有进水口，出水口，所述反应器中置有反应微生物，所述反应器器壁以面积计的十分之一以上由柔性材料制成，反应器器壁其余部分由刚性材料制成。 |
The efficient flexible sewage treatment biochemical reactor is a container with a wall and is provided with a water inlet and a water outlet, reactive microorganisms are arranged in the reactor, more than one tenth of the reactor wall in area is made of flexible materials, and the rest of the reactor wall is made of rigid materials. |
| 本反应器用于污水处理，器壁部分由柔性材料制成，便于做成可拆式、可移动式、可收缩式结构，使用方便，成本低、结构简单、不需要沉淀池，节省场地，处理速度快，效果好，电耗少，运行成本低。 |
The reactor is used for sewage treatment, the wall part of the reactor is made of a flexible material, so that the reactor can be conveniently made into a detachable, movable and retractable structure, and is convenient to use, low in cost, simple in structure, free of a sedimentation tank, capable of saving fields, high in processing speed, good in effect, low in power consumption and low in operation cost. |
| 权利要求书 |
Claims |
| 0001 . |
0001 . |
| 1 |
1 |
| 一种高效柔性污水处理生化反应器是一个具有器壁的容器，具有进水口，出水口，所述反应器中置有反应微生物，其特征是，所述反应器器壁以面积计的十分之一以上由柔性材料制成，反应器器壁其余部分由刚性材料制成。 |
An efficient flexible sewage treatment biochemical reactor is a container with a wall and is provided with a water inlet and a water outlet, reactive microorganisms are arranged in the reactor, characterized in that more than one tenth of the reactor wall in area is made of flexible materials, and the rest of the reactor wall is made of rigid materials. |
| 0002 . |
0002 . |
| 2 |
2 |
| 根据权利要求1所述的高效柔性污水处理生化反应器，其特征在于，所述反应器呈多面体、曲面体、多面体与曲面体的组合体、或不规则体。 |
The efficient flexible sewage treatment biochemical reactor according to claim 1, characterized in that the reactor is a polyhedron, a curved body, a combination of a polyhedron and a curved body, or an irregular body. |
| 0003 . |
0003 . |
| 3 |
3 |
| 根据权利要求2所述的高效柔性污水处理生化反应器，其特征在于，所述柔性材料为塑料薄膜和/或滤布。 |
The efficient flexible sewage treatment biochemical reactor according to claim 2, characterized in that the flexible material is a plastic film and/or a filter cloth. |
| 0004 . |
0004 . |
| 4 |
4 |
| 根据权利要求3所述的高效柔性污水处理生化反应器，其特征在于，所述塑料薄膜为聚乙烯薄膜、聚氯乙烯薄膜、或聚偏二氟乙烯薄膜。 |
The efficient flexible sewage treatment biochemical reactor according to claim 3, characterized in that the plastic film is a polyethylene film, a polyvinyl chloride film, or a polyvinylidene fluoride film. |
| 0005 . |
0005 . |
| 5 |
5 |
| 根据权利要求1或2或3或4所述的高效柔性污水处理生化反应器，其特征在于，所述反应器为上部敞口容器。 |
The efficient flexible sewage treatment biochemical reactor according to claim 1 or 2 or 3 or 4, characterized in that the reactor is an open-top container. |
| 0006 . |
0006 . |
| 6 |
6 |
| 根据权利要求1或2或3或4所述的高效柔性污水处理生化反应器，其特征在于，所述反应器为封闭容器。 |
The efficient flexible sewage treatment biochemical reactor according to claim 1 or 2 or 3 or 4, characterized in that it is a closed vessel. |
| 0007 . |
0007 . |
| 7 |
7 |
| 根据权利要求1或2或3或4所述的高效柔性污水处理生化反应器，其特征在于，所述反应器中置有微生物载体。 |
The efficient flexible sewage treatment biochemical reactor according to claim 1 or 2 or 3 or 4, characterized in that a microbial carrier is disposed in the reactor. |
| 0008 . |
0008 . |
| 8 |
8 |
| 根据权利要求1或2或3或4所述的高效柔性污水处理生化反应器，其特征在于，所述反应器具有反应器器壁支撑件； |
The efficient flexible sewage treatment biochemical reactor according to claim 1 or 2 or 3 or 4, characterized in that the reactor has a reactor wall support; |
| 所述反应器具有出泥口。 |
The reactor has a mud outlet. |
| 0009 . |
0009 . |
| 9 |
9 |
| 根据权利要求1或2或3或4所述的高效柔性污水处理生化反应器，其特征在于，所述反应器具有放置于反应器内的充氧装置。 |
The efficient flexible sewage treatment biochemical reactor according to claim 1 or 2 or 3 or 4, characterized in that the reactor has an oxygenating device placed in the reactor. |
| 0010 . |
0010 . |
| 10 |
10 |
| 根据权利要求1或2或3或4所述的高效柔性污水处理生化反应器，其特征在于，所述反应器具有放置于反应器外的充氧装置。 |
The efficient flexible sewage treatment biochemical reactor according to claim 1 or 2 or 3 or 4, characterized in that the reactor has an oxygenating device placed outside the reactor. |
| 说明书 |
Description |
| 高效柔性污水处理生化反应器 |
Efficient Flexible Sewage Treatment Biochemical Reactor |
| [0001] |
[0001] |
| 技术领域 |
TECHNICAL FIELD |
| [0002] |
[0002] |
| 本实用新型涉及一种污水处理生化反应器，尤其是一种高效柔性污水处理生化反应器，属于污水处理技术领域。 |
The utility model relates to a sewage treatment biochemical reactor, in particular to an efficient flexible sewage treatment biochemical reactor, and belongs to the technical field of sewage treatment. |
| [0003] |
[0003] |
| 背景技术 |
BACKGROUND OF THE INVENTION |
| [0004] |
[0004] |
| 目前，污水处理生化反应器大多为钢筋混凝土、钢结构等刚性材料构成的生化反应池，以及出水沉淀池，反应池中置有反应微生物，在好氧、兼氧处理反应池中还置有充氧装置。 |
At present, most sewage treatment biochemical reactors are biochemical reaction tanks formed by rigid materials such as reinforced concrete, steel structures and the like, and effluent sedimentation tanks, reaction microorganisms are placed in the reaction tanks, and oxygenating devices are placed in aerobic and facultative treatment reaction tanks. |
| 此类反应池的缺点是： |
The disadvantages of such reaction tanks are: |
| 占用较大的场地，成本较高，钢筋混凝土反应池和大型的钢结构反应池一旦建成以后，就无法移动； |
large sites are occupied, the cost is high, and the reinforced concrete reaction tank and the large steel structure reaction tank can not move once built; |
| 小型钢结构反应池在建成以后，移动也非常困难； |
the small steel structure reaction tank is difficult to move after being built; |
| 由于采用沉淀法来达到清水和微生物的分离，反应池中微生物的浓度通常只能维持在较低的水平，一般小于4000mg/L，池中被处理的污水需要较长的停留时间才能达到处理要求，因而现有的生化反应池不能实现污水的高效快速处理。 |
due to the fact that the precipitation method is used for separating clean water from microorganisms, the concentration of the microorganisms in the reaction tank can be generally maintained at a low level, generally less than 4000mg/L, the treated sewage in the reaction tank needs a long retention time to meet the treatment requirement, and therefore the existing biochemical reaction tank can not realize efficient and rapid treatment of the sewage. |
| [0005] |
[0005] |
| 实用新型内容 |
Summary of the Utility Model |
| [0006] |
[0006] |
| 本实用新型所要解决的技术问题是： |
The technical problem to be solved by the utility model is: |
| 克服现有污水处理生化反应池的缺点，提供一种高效柔性污水处理生化反应器。 |
The invention provides a efficient flexible sewage treatment biochemical reactor which overcomes the defects of the existing sewage treatment biochemical reaction tank. |
| [0007] |
[0007] |
| 本实用新型解决其技术问题的技术方案如下： |
The technical scheme for solving the technical problem of the utility model is as follows: |
| 一种高效柔性污水处理生化反应器是一个具有器壁的容器，具有进水口，出水口，所述反应器中置有反应微生物，其特征是，所述反应器器壁以面积计的十分之一以上由柔性材料制成，反应器器壁其余部分由刚性材料制成。 |
A efficient flexible sewage treatment biochemical reactor is a container with a wall and is provided with a water inlet and a water outlet, reactive microorganisms are arranged in the reactor, characterized in that more than one tenth of the reactor wall in area is made of flexible materials, and the rest of the reactor wall is made of rigid materials. |
| [0008] |
[0008] |
| 本实用新型进一步的技术方案如下： |
A further technical solution of the utility model is as follows: |
| [0009] |
[0009] |
| 1、 |
1、 |
| 所述反应器呈多面体、曲面体、多面体与曲面体的组合体、或不规则体； |
the reactor is a polyhedron, a curved body, a combination of the polyhedron and the curved body or an irregular body; |
| [0010] |
[0010] |
| 2、 |
2、 |
| 所述柔性材料为塑料薄膜和/或滤布； |
the flexible material is a plastic film and/or a filter cloth; |
| [0011] |
[0011] |
| 3、 |
3、 |
| 所述塑料薄膜为聚乙烯薄膜、聚氯乙烯薄膜、或聚偏二氟乙烯薄膜； |
the plastic film is a polyethylene film, a polyvinyl chloride film or a polyvinylidene fluoride film; |
| [0012] |
[0012] |
| 4、 |
4、 |
| 所述反应器为上部敞口容器； |
the reactor is an open-top container; |
| [0013] |
[0013] |
| 5、 |
5、 |
| 所述反应器为封闭容器； |
the reactor is a closed vessel; |
| [0014] |
[0014] |
| 6、 |
6、 |
| 所述反应器中置有微生物载体； |
a microbial carrier is arranged in the reactor; |
| [0015] |
[0015] |
| 7、 |
7、 |
| 所述反应器具有反应器器壁支撑件； |
the reactor having a reactor wall support; |
| 所述反应器具有出泥口； |
the reactor is provided with a mud outlet; |
| [0016] |
[0016] |
| 8、 |
8、 |
| 所述反应器具有放置于反应器内的充氧装置，直接对反应器内的水充氧； |
the reactor is provided with an oxygenating device placed in the reactor, and water in the reactor is directly oxygenated; |
| [0017] |
[0017] |
| 9、 |
9、 |
| 所述反应器具有放置于反应器外的充氧装置，利用充氧装置的增压作用将充氧后的水输入反应器，使得反应器的结构简单，安装操作方便。 |
The reactor is provided with an oxygenating device arranged outside the reactor, and oxygenated water is input into the reactor by utilizing the pressurization effect of the oxygenating device, so that the reactor is simple in structure and convenient to install and operate. |
| [0018] |
[0018] |
| 需要说明的是，本实用新型的反应器器壁由柔性材料和刚性材料两部分按面积比例构成，是对反应器器壁构造的限定。 |
It should be noted that the reactor wall of the present utility model is composed of two parts- a flexible material and a rigid material with an area ratio, which defines the structure of the reactor wall. |
| [0019] |
[0019] |
| 本实用新型的有益效果如下： |
The utility model has the following beneficial effects: |
| [0020] |
[0020] |
| 1、 |
1、 |
| 柔性材料(包括滤布)成本低廉，因此，用柔性材料(包括滤布)制成的反应器成本很低； |
the cost of the flexible material (comprising the filter cloth) is low, so that the cost of the reactor made of the flexible material (comprising the filter cloth) is very low; |
| 柔性材料(包括滤布)制成的反应器便于做成可拆式、可移动式、可收缩式结构，便于清洗并恢复过滤功能，使用方便。 |
A reactor made of a flexible material (comprising filter cloth) is convenient to make into a detachable, movable and retractable structure, is convenient to clean and restore a filtering function, and is convenient to use. |
| 适合在多种场合使用，尤其适用于河流、湖泊等受污染的水体的净化处理。 |
The method is suitable for being used in various occasions, and is particularly suitable for purifying polluted water bodies such as rivers and lakes. |
| [0021] |
[0021] |
| 2、 |
2、 |
| 本实用新型反应器采用滤布过滤，可以将绝大部分微生物截留在反应器内，不存在活性污泥流失的问题，出水的悬浮物浓度很低。 |
The reactor of the utility model adopts filter cloth to filter, so that most microorganisms can be trapped in the reactor, the problem of loss of activated sludge does not exist, and the concentration of suspended matters in effluent is very low. |
| 同时，该反应器内的微生物浓度可以比常规生化处理器高出2 - 3倍，甚至更高，因此，其处理污染物的速度比常规处理方法快一倍以上； |
meanwhile, the concentration of microorganisms in the reactor can be 2-3 times higher than that of a conventional biochemical processor or even higher, so that the speed of treating pollutants by the reactor is more than one time faster than that of a conventional treatment method; |
| 由于该反应器中不存在硝化细菌流失的问题，因此，硝化细菌可以维持较高的浓度，从而利于氨氮的去除。 |
due to the fact that the problem of loss of nitrifying bacteria does not exist in the reactor, the nitrifying bacteria can maintain a high concentration, and therefore removal of ammonia nitrogen is facilitated. |
| 同时，该装置具有粘附、过滤蓝藻的功能，有利于富营养化水体的净化处理。 |
meanwhile, the device has the functions of adhering and filtering blue algae and is beneficial to purification treatment of eutrophic water. |
| [0022] |
[0022] |
| 因此，本实用新型反应器成本低、结构简单、不需要沉淀池，节省场地，处理速度快，效果好，电耗少，运行成本低。 |
therefore, the reactor of the utility model has the advantages of low cost, simple structure, no need of a sedimentation tank, site saving, high processing speed, good effect, low power consumption and low operation cost. |
| [0023] |
[0023] |
| 附图说明 |
BRIEF DESCRIPTION OF THE DRAWINGS |
| [0024] |
[0024] |
| 图1为本实用新型实施例1的结构示意图。 |
Figure 1 is a structural schematic diagram of embodiment 1 of the present utility model. |
| [0025] |
[0025] |
| 图2为本实用新型实施例2的结构示意图。 |
Figure 2 is a structural schematic diagram of embodiment 2 of the present utility model. |
| [0026] |
[0026] |
| 图3为本实用新型实施例3的结构示意图。 |
Figure 3 is a structural schematic diagram of embodiment 3 of the present utility model. |
| [0027] |
[0027] |
| 图4为本实用新型实施例4的结构示意图。 |
Figure 4 is a structural schematic diagram of embodiment 4 of the present utility model. |
| [0028] |
[0028] |
| 图5为本实用新型实施例5的结构示意图。 |
Fig. 5 is a structural schematic diagram of embodiment 5 of the present utility model. |
| [0029] |
[0029] |
| 图6为本实用新型实施例6的结构示意图。 |
Figure 6 is a structural schematic diagram of embodiment 6 of the present utility model. |
| [0030] |
[0030] |
| 具体实施方式 |
DETAILED DESCRIPTION OF THE INVENTION |
| [0031] |
[0031] |
| 下面参照附图并结合实施例对本实用新型作进一步详细描述。 |
The present utility model will be described in further detail with reference to the accompanying drawings and examples. |
| 但是本实用新型不限于所给出的例子。 |
However, the utility model is not limited to the examples given. |
| [0032] |
[0032] |
| 实施例1 |
Example 1 |
| [0033] |
[0033] |
| 本实施例的高效柔性生化反应器基本结构如图1所示，适用于好氧、兼氧生化处理，反应器为封闭容器1，容积为50m3。 |
The basic structure of the efficient flexible biochemical reactor of the embodiment is shown in figure 1 and is suitable for aerobic and facultative biochemical treatment, the reactor is a closed container 1, and the volume is 50m3. |
| 反应器呈曲面体，例如球体、类球体、或圆柱体等。 |
The reactor is a curved body, such as a sphere, spheroid, or cylinder. |
| 反应器器壁全部由膜厚度为0.05mm的聚乙烯薄膜柔性材料11制成。 |
The reactor walls are all made of a flexible material 11 of polyethylene film with a film thickness 0.05mm. |
| 本实施例所选用的柔性材料以不透水、具有一定强度的塑料薄膜为优选材料。 |
The flexible material selected for this embodiment is preferably a water impermeable, strong plastic film. |
| 图中3为反应器进水口，5为放置于反应器外的充氧装置，4为充氧装置进气口，8为出水口，7为出泥口，在一般处理过程中，出泥口是关闭的，需要排泥时，采用压力泵喷射微生物载体，使载体上的微生物脱落进入水中，然后用泵将污泥泵入河道两侧的绿地，6为反应器器壁钢结构支撑件，本实施例中的支撑件为固定在河道中的支撑杆，通过绳索61与反应器柔性材料11制成的器壁上的挂耳62固定连接，23为置于反应器中的微生物载体--球径为5cm的多面空心塑料球。 |
In the figure, 3 is a water inlet of a reactor, 5 is an oxygenating device placed outside the reactor, 4 is an air inlet of the oxygenating device, 8 is a water outlet, and 7 is a mud outlet. In a common treatment process, the mud outlet is closed, and when mud discharge is needed, a pressure pump is used to spray a microorganism carrier so that microorganisms on the carrier fall off into water, and then the sludge is pumped into green lands on two sides of a river channel by a pump; 6 is a steel structure support member of a reactor wall, the support member in the embodiment is . |
| 待处理湖泊水经充氧装置充氧后由进水口3进入反应器。 |
lake water to be treated enters the reactor from the water inlet 3 after being oxygenated by the oxygenating device. |
| [0034] |
[0034] |
| 反应器中的微生物浓度可达到12000 - 13000mg/L。 |
The concentration of microorganisms in the reactor can reach 12000-13000mg/L. |
| [0035] |
[0035] |
| 将该反应器用于某湖泊水体的处理，充氧装置的功率为1.5Kw，其处理水量为45吨/小时，进水在容器内累计停留时间为1.1小时，其进水水质均值如下所示： |
The reactor is used for treating a lake water body, the power of the oxygenating device is 1.5Kw, the treatment water amount is 45 tons/hour, the accumulated retention time of inlet water in a container is 1.1 hours, and the average inlet water quality is as follows: |
| [0036] |
[0036] |
| COD |
COD |
| BOD5 |
BOD5 |
| 氨氮 |
ammonia nitrogen |
| 动植物油 |
Animal and plant oil |
| 总磷 |
Total Phosphorus |
| 50 |
50 |
| 8mg/l |
8mg/l |
| 24 |
24 |
| 9 mg/l |
9 mg/l |
| 5 |
5 |
| 23 mg/l |
23 mg/l |
| 12 |
12 |
| 6 mg/l |
6 mg/l |
| .00 |
.00 |
| 89 mg/l |
89 mg/l |
| [0037] |
[0037] |
| 经处理后，其出水水质均值浓度如下： |
After treatment, the effluent water quality average concentration is as follows: |
| [0038] |
[0038] |
| COD |
COD |
| BOD5 |
BOD5 |
| 氨氮 |
ammonia nitrogen |
| 动植物油 |
Animal and plant oil |
| 总磷 |
Total Phosphorus |
| 25 |
25 |
| 0mg/l |
0mg/l |
| 5 |
5 |
| 30 mg/l |
30 mg/l |
| .00 |
.00 |
| 842 mg/l |
842 mg/l |
| .00 |
.00 |
| 15 mg/l |
15 mg/l |
| .00 |
.00 |
| 18 mg/l |
18 mg/l |
| [0039] |
[0039] |
| 以上湖泊水进水水质浓度超过《地表水环境质量标准》（GB3838-2002）中的Ⅴ类水水质标准，经处理后，测得出水口处的水质指标达到《地表水环境质量标准》（GB3838-2002）中的Ⅳ类水水质标准。 |
The inlet water quality concentration of the lake above exceeds the class V water quality standard in the Surface Water Environment Quality Standard (GB3838-2002), and after treatment, the measured water quality index at the outlet reaches the class IV water quality standard in the Surface Water Environment Quality Standard (GB3838-2002). |
| [0040] |
[0040] |
| 实施例2 |
Example 2 |
| [0041] |
[0041] |
| 本实施例的高效柔性生化反应器基本结构如图2所示，适用于好氧、兼氧生化处理，反应器为敞口容器1，容积为10m3。 |
The basic structure of the efficient flexible biochemical reactor of the embodiment is shown in figure 2 and is suitable for aerobic and facultative biochemical treatment, the reactor is an open container 1, and the volume is 10m3. |
| 反应器呈多面体，例如矩形体。 |
The reactor is polyhedral, e.g. rectangular. |
| 占反应器器壁80 %面积的部分由钢筋混凝土刚性材料12制成，占反应器器壁19 %面积的部分由膜厚度为0.08mm的聚氯乙烯薄膜柔性材料11制成，反应器器壁其余部分由滤孔目数为800的涤纶滤布13制成。 |
A portion accounting for 80% of the area of the reactor wall is made of a reinforced concrete rigid material 12, a portion accounting for 19% of the area of the reactor wall is made of a polyvinyl chloride film flexible material 11 having a film thickness of 0.08mm, and the rest of the reactor wall is made of a polyester filter cloth 13 having a mesh number of filter holes of 800. |
| 本实施例所选用的柔性材料以不透水、具有一定强度的塑料薄膜为优选材料。 |
The flexible material selected for this embodiment is preferably a water impermeable, strong plastic film. |
| 聚氯乙烯薄膜和钢筋混凝土之间采用胶粘密封连接，聚氯乙烯薄膜与涤纶滤布之间采用胶粘或缝合密封连接。 |
the polyvinyl chloride film is hermetically connected with the reinforced concrete through gluing, and the polyvinyl chloride film is hermetically connected with the polyester filter cloth through gluing or sewing. |
| 柔性材料和刚性材料的密封连接也可以采用嵌槽压条或整体浇筑。 |
The sealed connection of the flexible material and the rigid material may also be made using a caulking bead or integrally cast. |
| 图中，3为进水口，4为充氧装置进气口，5为放置于反应器内的充氧装置，直接对反应器内的水充氧，7为出泥口，其作用同实施例1，6为反应器敞口处环形钢结构支撑件，21为置于反应器中的颗粒状微生物载体，22为置于反应器中的纤维状微生物载体。 |
In the figure, 3 is a water inlet, 4 is an air inlet of an oxygenating device, 5 is an oxygenating device placed in a reactor to directly oxygenate water in the reactor, 7 is a mud outlet, and the functions thereof are the same as those Examples 1 and 6 are annular steel structure supports at the opening of the reactor, 21 is a granular microbial carrier placed in the reactor, and 22 is a fibrous microbial carrier placed in the reactor. |
| 滤布兼有出水口功能，处理过的水经滤布过滤排出。 |
The filter cloth has a water outlet function, and the treated water is filtered and discharged through the filter cloth. |
| [0042] |
[0042] |
| 反应器中的微生物浓度可达到8000 - 9000mg/L。 |
The concentration of microorganisms in the reactor can reach 8000-9000mg/L. |
| 处理污水时，用抽水装置通过进水口3将待处理污水输进容器1。 |
In the treatment of sewage, the sewage to be treated is conveyed into the container 1 through the water inlet 3 by a pumping device. |
| [0043] |
[0043] |
| 将该反应器用于某黑臭河流的污水处理，其进水水量为3.0吨/小时，停留时间为3.30小时，其进水水质均值如下所示： |
The reactor is used for sewage treatment of a black and odorous river, the inflow water quantity is 3.0 ton/hour, the retention time is 3.30 hours, and the average inflow water quality is as follows: |
| [0044] |
[0044] |
| COD |
COD |
| BOD5 |
BOD5 |
| 氨氮 |
ammonia nitrogen |
| 动植物油 |
Animal and plant oil |
| 总磷 |
Total Phosphorus |
| 181 |
181 |
| 2mg/l |
2mg/l |
| 87 |
87 |
| 5 mg/l |
5 mg/l |
| 35 |
35 |
| 2 mg/l |
2 mg/l |
| 12 |
12 |
| 6 mg/l |
6 mg/l |
| 2 |
2 |
| 3 mg/l |
3 mg/l |
| [0045] |
[0045] |
| 经处理后，其出水水质均值浓度如下： |
After treatment, the effluent water quality average concentration is as follows: |
| [0046] |
[0046] |
| COD |
COD |
| BOD5 |
BOD5 |
| 氨氮 |
ammonia nitrogen |
| 动植物油 |
Animal and plant oil |
| 总磷 |
Total Phosphorus |
| 45 |
45 |
| 0mg/l |
0mg/l |
| 8 |
8 |
| 1 mg/l |
1 mg/l |
| 3 |
3 |
| 2 mg/l |
2 mg/l |
| .00 |
.00 |
| 15 mg/l |
15 mg/l |
| .00 |
.00 |
| 34 mg/l |
34 mg/l |
| [0047] |
[0047] |
| 以上出水水质指标达到《城镇污水处理厂污染物排放标准》（GB18918-2002）中的一级A标准，接近《地表水环境质量标准》（GB3838-2002）中的Ⅴ类水质标准。 |
The effluent quality meets the first level of A criteria specified in Discharge Standard of Pollutants for Municipal sewage Treatment Plant (GB18918-2002) and approaches the V criteria specified in Environmental Quality Standard for Surface Water (GB3838-2002). |
| [0048] |
[0048] |
| 实施例3 |
Example 3 |
| [0049] |
[0049] |
| 本实施例的高效柔性生化反应器基本结构如图3所示，适用于好氧、兼氧生化处理，反应器为封闭容器1，容积为100m3。 |
The basic structure of the efficient flexible biochemical reactor of the embodiment is shown in Fig. 3 and is suitable for aerobic and facultative biochemical treatment, the reactor is a closed container 1 and the volume is 100m3. |
| 反应器呈不规则体。 |
The reactor was irregular. |
| 反应器器壁全部由滤孔目数为325的丙纶滤布13制成。 |
The reactor walls are all made of polypropylene filter cloth 13 with 325 mesh. |
| 24为置于反应器中的絮状微生物载体。 |
24 is a flocculent microbial carrier placed in the reactor. |
| 图中其余标号同实施例2。 |
The rest of the figures are numbered as in Example 2. |
| 滤布兼有出水口功能，处理过的水经滤布过滤排出。 |
The filter cloth has a water outlet function, and the treated water is filtered and discharged through the filter cloth. |
| [0050] |
[0050] |
| 反应器中的微生物浓度达到11000 - 12000mg/L。 |
The microbial concentration in the reactor reached 11000-12000mg/L. |
| [0051] |
[0051] |
| 将该反应器用于某劣Ⅴ类水体的处理，其进水水量为100吨/小时，停留时间为1.0小时，其进水水质均值如下所示： |
when the reactor is used for treating a certain type V water body, the inflow water quantity is 100 tons/hour, the retention time is 1.0 hours, and the average inflow water quality is as follows: |
| [0052] |
[0052] |
| COD |
COD |
| BOD5 |
BOD5 |
| SS |
SS |
| 氨氮 |
ammonia nitrogen |
| 石油类 |
Petroleum |
| 总磷 |
Total Phosphorus |
| 55 |
55 |
| 0mg/l |
0mg/l |
| 21 |
21 |
| 5 mg/l |
5 mg/l |
| 32 |
32 |
| 0 mg/l |
0 mg/l |
| 5 |
5 |
| 2 mg/l |
2 mg/l |
| 2 |
2 |
| 6 mg/l |
6 mg/l |
| .00 |
.00 |
| 37mg/l |
37mg/l |
| [0053] |
[0053] |
| 以上水质指标超出《地表水环境质量标准》（GB3838-2002）中的Ⅴ类水质标准。 |
The above water quality indexes exceed the Grade V water quality standard in Surface Water Environmental Quality Standard (GB3838-2002). |
| [0054] |
[0054] |
| 经处理后，其出水水质均值浓度如下： |
After treatment, the effluent water quality average concentration is as follows: |
| [0055] |
[0055] |
| COD |
COD |
| BOD5 |
BOD5 |
| SS |
SS |
| 氨氮 |
ammonia nitrogen |
| 石油类 |
Petroleum |
| 总磷 |
Total Phosphorus |
| 24 |
24 |
| 0mg/l |
0mg/l |
| 4 |
4 |
| 3 mg/l |
3 mg/l |
| 4 |
4 |
| 20mg/l |
20mg/l |
| .00 |
.00 |
| 78 mg/l |
78 mg/l |
| .00 |
.00 |
| 03 mg/l |
03 mg/l |
| .00 |
.00 |
| 07mg/l |
07mg/l |
| [0056] |
[0056] |
| 以上COD 、BOD5出水水质指标达到《地表水环境质量标准》（GB3838-2002）中的Ⅳ类水质标准，氨氮、石油类、总磷指标达到Ⅱ类水质标准。 |
The effluent quality indexes of COD and BOD5 above reach class IV water quality standard in Surface Water Environment Quality Standard (GB3838-2002), and the indexes of ammonia nitrogen, petroleum and total phosphorus reach class II water quality standard. |
| [0057] |
[0057] |
| 实施例4 |
Example 4 |
| [0058] |
[0058] |
| 本实施例的高效柔性生化反应器基本结构如图4所示，适用于好氧、兼氧生化处理，反应器为封闭容器1，容积为20m3。 |
The basic structure of the efficient flexible biochemical reactor of the embodiment is shown in Fig. 4 and is suitable for aerobic and facultative biochemical treatment, the reactor is a closed container 1, and the volume is 20m3. |
| 反应器呈多面体与曲面体的组合体，例如矩形体与球体或类球体的组合体。 |
The reactor is a combination of polyhedrons and curved bodies, such as a combination of rectangular bodies and spheres or spheroids. |
| 占反应器器壁50 %面积的部分由膜厚度为0.2mm聚偏二氟乙烯薄膜柔性材料11制成，反应器器壁其余部分由滤孔目数为500的涤纶滤布13制成。 |
The part accounting for 50% of the area of the reactor wall is made of a flexible material 11 with a membrane thickness of 0.2mm polyvinylidene fluoride membrane, and the rest of the reactor wall is made of a polyester filter cloth 13 with 500 mesh number of filter holes. |
| 本实施例所选用的柔性材料以不透水、具有一定强度的塑料薄膜为优选材料。 |
The flexible material selected for this embodiment is preferably a water impermeable, strong plastic film. |
| 聚偏二氟乙烯薄膜与涤纶滤布之间采用胶粘或缝合密封连接。 |
and the polyvinylidene fluoride film and the polyester filter cloth are sealed and connected by gluing or sewing. |
| 图中其余标号同实施例2。 |
The rest of the figures are numbered as in Example 2. |
| 滤布兼有出水口功能，处理过的水经滤布过滤排出。 |
The filter cloth has a water outlet function, and the treated water is filtered and discharged through the filter cloth. |
| [0059] |
[0059] |
| 反应器中的微生物浓度达到9000 - 10000mg/L。 |
The microbial concentration in the reactor reached 9000-10000mg/L. |
| [0060] |
[0060] |
| 将该反应器用于某湖泊水体的处理，其进水水量为20吨/小时，停留时间为1.0小时，其进水水质均值如下所示： |
The reactor is used for treating a lake water body, the water inflow amount is 20 tons/hour, the retention time is 1.0 hours, and the average water inflow quality is as follows: |
| [0061] |
[0061] |
| COD |
COD |
| BOD5 |
BOD5 |
| SS |
SS |
| 氨氮 |
ammonia nitrogen |
| 石油类 |
Petroleum |
| 总磷 |
Total Phosphorus |
| 65 |
65 |
| 1mg/l |
1mg/l |
| 27 |
27 |
| 3 mg/l |
3 mg/l |
| 33 |
33 |
| 9 mg/l |
9 mg/l |
| 4 |
4 |
| 9 mg/l |
9 mg/l |
| 3 |
3 |
| 8mg/l |
8mg/l |
| .00 |
.00 |
| 83mg/l |
83mg/l |
| [0062] |
[0062] |
| 以上水质指标超出《地表水环境质量标准》（GB3838-2002）中的Ⅴ类水质标准。 |
The above water quality indexes exceed the Grade V water quality standard in Surface Water Environmental Quality Standard (GB3838-2002). |
| [0063] |
[0063] |
| 经处理后，其出水水质均值浓度如下： |
After treatment, the effluent water quality average concentration is as follows: |
| [0064] |
[0064] |
| COD |
COD |
| BOD5 |
BOD5 |
| SS |
SS |
| 氨氮 |
ammonia nitrogen |
| 石油类 |
Petroleum |
| 总磷 |
Total Phosphorus |
| 23 |
23 |
| 4mg/l |
4mg/l |
| 5 |
5 |
| 7 mg/l |
7 mg/l |
| 6 |
6 |
| 9mg/l |
9mg/l |
| .00 |
.00 |
| 88 mg/l |
88 mg/l |
| .00 |
.00 |
| 06 mg/l |
06 mg/l |
| .00 |
.00 |
| 15mg/l |
15mg/l |
| [0065] |
[0065] |
| 以上COD 、BOD5出水水质指标达到《地表水环境质量标准》（GB3838-2002）中的Ⅳ类水质标准，氨氮、石油类、总磷指标达到Ⅱ类水质标准。 |
The effluent quality indexes of COD and BOD5 above reach class IV water quality standard in Surface Water Environment Quality Standard (GB3838-2002), and the indexes of ammonia nitrogen, petroleum and total phosphorus reach class II water quality standard. |
| [0066] |
[0066] |
| 实施例5 |
Example 5 |
| [0067] |
[0067] |
| 本实施例的高效柔性生化反应器基本结构如图5所示，适用于好氧、兼氧生化处理，反应器为封闭容器1，容积为20m3。 |
The basic structure of the efficient flexible biochemical reactor of the embodiment is shown in Fig. 5 and is suitable for aerobic and facultative biochemical treatment, the reactor is a closed container 1, and the volume is 20m3. |
| 多面体与曲面体的组合体，例如矩形体与圆柱体的组合体。 |
A combination of a polyhedron and a curved body, such as a rectangle and a cylinder. |
| 占反应器器壁20 %面积的部分由钢筋混凝土刚性材料12制成，反应器器壁其余部分由滤孔目数为625的丙纶滤布13制成。 |
A portion occupying 20% of the area of the reactor wall is made of a reinforced concrete rigid material 12, and the remaining portion of the reactor wall is made of a polypropylene filter cloth 13 having a mesh number of filter holes of 625. |
| 丙纶滤布和钢筋混凝土之间采用整体浇筑密封连接。 |
and the polypropylene fiber filter cloth and the reinforced concrete are connected in a sealing manner by integral pouring. |
| 柔性材料和刚性材料的密封连接也可以采用嵌槽压条或胶粘。 |
The sealed connection of the flexible material and the rigid material may also be made using a caulking bead or glue. |
| 图中其余标号同实施例2。 |
The rest of the figures are numbered as in Example 2. |
| 滤布兼有出水口功能，处理过的水经滤布过滤排出。 |
The filter cloth has a water outlet function, and the treated water is filtered and discharged through the filter cloth. |
| [0068] |
[0068] |
| 反应器中的微生物浓度达到9000 - 10000mg/L。 |
The microbial concentration in the reactor reached 9000-10000mg/L. |
| [0069] |
[0069] |
| 该反应器用于某湖泊水体的处理，其进水水量为13吨/小时，停留时间为1.54小时，其进水水质均值如下所示： |
The reactor is used for treating a lake water body, the water inflow amount is 13 tons/hour, the retention time is 1.54 hours, and the average water inflow quality is as follows: |
| [0070] |
[0070] |
| COD |
COD |
| BOD5 |
BOD5 |
| 氨氮 |
ammonia nitrogen |
| 石油类 |
Petroleum |
| 总磷 |
Total Phosphorus |
| 56 |
56 |
| 2mg/l |
2mg/l |
| 23 |
23 |
| 1 mg/l |
1 mg/l |
| 5 |
5 |
| 7 mg/l |
7 mg/l |
| 2 |
2 |
| 9 mg/l |
9 mg/l |
| .00 |
.00 |
| 44mg/l |
44mg/l |
| [0071] |
[0071] |
| 以上水质指标超出《地表水环境质量标准》（GB3838-2002）中的Ⅴ类水质标准。 |
The above water quality indexes exceed the Grade V water quality standard in Surface Water Environmental Quality Standard (GB3838-2002). |
| [0072] |
[0072] |
| 经处理后，其出水水质均值浓度如下： |
After treatment, the effluent water quality average concentration is as follows: |
| [0073] |
[0073] |
| COD |
COD |
| BOD5 |
BOD5 |
| 氨氮 |
ammonia nitrogen |
| 石油类 |
Petroleum |
| 总磷 |
Total Phosphorus |
| 12 |
12 |
| 9mg/l |
9mg/l |
| 2 |
2 |
| 3mg/l |
3mg/l |
| .00 |
.00 |
| 28 mg/l |
28 mg/l |
| .00 |
.00 |
| 03 mg/l |
03 mg/l |
| .00 |
.00 |
| 09mg/l |
09mg/l |
| [0074] |
[0074] |
| 出水水质指标达到《地表水环境质量标准》（GB3838-2002）中的Ⅱ类水水质标准。 |
The quality index of the effluent water meets the class II water quality standard in Surface Water Environmental Quality Standard (GB3838-2002). |
| [0075] |
[0075] |
| 实施例6 |
Example 6 |
| [0076] |
[0076] |
| 本实施例的高效柔性生化反应器基本结构如图6所示，适用于厌氧生化处理，反应器为封闭容器1，容积为50m3。 |
The basic structure of the efficient flexible biochemical reactor of this embodiment is shown in Fig. 6, which is suitable for anaerobic biochemical treatment, and the reactor is a closed vessel 1 with a volume of 50m3. |
| 反应器呈不规则体。 |
The reactor was irregular. |
| 反应器器壁全部由滤孔目数为325的丙纶滤布13制成。 |
The reactor walls are all made of polypropylene filter cloth 13 with 325 mesh. |
| 图中3为进水口，7为出泥口，作用同实施例1，24为置于反应器中的絮状微生物载体。 |
Fig. 3 shows a water inlet and Fig. 7 shows a sludge outlet for the same purpose as in Examples 1 and 24 for a flocculent microorganism carrier placed in a reactor. |
| 滤布兼有出水口功能，经厌氧处理过的水经滤布过滤排出反应器。 |
The filter cloth has a water outlet function, and the anaerobic treated water is filtered by the filter cloth and discharged out of the reactor. |
| [0077] |
[0077] |
| 反应器中的微生物浓度达到20000 - 25000mg/L。 |
The microbial concentration in the reactor reached 20000-25000mg/L. |
| [0078] |
[0078] |
| 将该反应器用于某劣Ⅴ类水体的处理，其进水水量为25吨/小时，停留时间为2.0小时，其进水水质均值如下所示： |
when the reactor is used for treating a certain type V water body, the water inflow amount is 25 tons/hour, the retention time is 2.0 hours, and the average water inflow quality is as follows: |
| [0079] |
[0079] |
| COD |
COD |
| BOD5 |
BOD5 |
| 255 |
255 |
| 0mg/l |
0mg/l |
| 130 |
130 |
| 8 mg/l |
8 mg/l |
| [0080] |
[0080] |
| 以上水质指标严重超出《地表水环境质量标准》（GB3838-2002）中的Ⅴ类水质标准。 |
The above water quality indexes seriously exceed the Grade V water quality standard in Surface Water Environmental Quality Standard (GB3838-2002). |
| [0081] |
[0081] |
| 经处理后，其出水水质均值浓度如下： |
After treatment, the effluent water quality average concentration is as follows: |
| [0082] |
[0082] |
| COD |
COD |
| BOD5 |
BOD5 |
| 84 |
84 |
| 0mg/l |
0mg/l |
| 43 |
43 |
| 1 mg/l |
1 mg/l |
| [0083] |
[0083] |
| 经过所述反应器处理后，其COD、BOD5的去除率大于60 %，处理效果良好。 |
After the reactor treatment, the removal rate of COD and BOD5 is more than 60%, and the treatment effect is good. |
| [0084] |
[0084] |
| 本实用新型的高效柔性生化反应器若出现微生物絮体或悬浮物堵塞滤布的情况，则可以采用清水冲洗即可恢复过滤功能。 |
according to the efficient flexible biochemical reactor, if the filter cloth is blocked by microbial flocs or suspended solids, the filter function can be recovered by flushing with clear water. |
| [0085] |
[0085] |
| 除上述实施例外，本实用新型还可以有其他实施方式。 |
In addition to the above embodiments, other embodiments of the present utility model are possible. |
| 凡采用等同替换或等效变换形成的技术方案，均落在本实用新型要求的保护范围。 |
Any technical solution formed by equivalent substitution or equivalent transformation falls within the scope of protection claimed in the present utility model. |