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Dynamic film separating method for processing sewage by using biological diatomite

A separation method and technology of diatomite, applied in the direction of sustainable biological treatment, biological water/sewage treatment, chemical instruments and methods, etc., can solve problems such as poor operation stability and complicated operation, and achieve long operation period and water permeability Large, good water permeability

Active Publication Date: 2012-05-23
华方水务(中国)有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the existing diatomite sewage treatment process has disadvantages such as complicated operation and poor operation stability.

Method used

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  • Dynamic film separating method for processing sewage by using biological diatomite
  • Dynamic film separating method for processing sewage by using biological diatomite
  • Dynamic film separating method for processing sewage by using biological diatomite

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] Such as figure 1 Shown, the specific implementation method of the independent unit operation of flat support biological diatomite dynamic membrane separation method is as follows:

[0034] Conditions of biological diatomaceous earth mixture in the sewage treatment process that needs to be separated:

[0035] The concentration of suspended solids (MLSS) in the biological diatomaceous earth mixture is 10-15g / L, not less than 10g / L;

[0036] The proportion of volatile suspended solids (MLVSS) in the mixed liquor is 30% to 40%, not more than 40%;

[0037] If the conditions cannot be fully met, diatomaceous earth needs to be supplemented to meet the above conditions.

[0038] The operation steps are as follows:

[0039] (1) First, select a stainless steel mesh (both 180 mesh to 200 mesh) flat support body, each flat support body 2m 2 , and 22 pieces of flat supports are assembled into a set of membrane modules, the design permeable flux of this module is 22×2×50L / m 2 .h...

Embodiment 2

[0048] Such as figure 2 As shown, the specific implementation method of the independent unit operation of the filter element support biological diatomite dynamic membrane separation method is as follows:

[0049] Conditions of biological diatomaceous earth mixture in the sewage treatment process that needs to be separated:

[0050] The concentration of suspended solids (MLSS) in the biological diatomaceous earth mixture is 10-15g / L, not less than 10g / L;

[0051] The proportion of volatile suspended solids (MLVSS) in the mixed liquor is 30% to 40%, not more than 40%;

[0052] If the conditions cannot be fully met, diatomaceous earth needs to be supplemented to meet the above conditions.

[0053] The operation steps are as follows:

[0054] (1) First select the stainless steel mesh (both 180 mesh to 200 mesh) filter element support body, each commercial finished filter element has a length of 0.8m, a regular hexagonal cross-section, a circumscribed circle diameter of 0.05m, ...

Embodiment 3

[0063] Such as image 3 As shown, the specific implementation method of the continuous flow operation of the multi-unit combined biological diatomite dynamic membrane separation method of the support body is as follows:

[0064] Conditions of biological diatomaceous earth mixture in the sewage treatment process that needs to be separated:

[0065] The concentration of suspended solids (MLSS) in the biological diatomaceous earth mixture is 10-15g / L, not less than 10g / L;

[0066] The proportion of volatile suspended solids (MLVSS) in the mixed liquor is 30% to 40%, not more than 40%;

[0067]If the conditions cannot be fully met, diatomaceous earth needs to be supplemented to meet the above conditions.

[0068] The operation steps are as follows:

[0069] (1) The biological diatomaceous earth dynamic membrane separation process runs continuously, and adopts multi-unit combination operation. Among them, one unit component is always in the cleaning state, and several other unit...

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Abstract

The present invention relates to a dynamic film separating method for processing sewage by using biological diatomite, which is a solid-liquid separating method using the biological diatomite as an automatic dynamic component and forming a dynamic film at the surface of a support body (stainless meshes or melon meshes ) with big holes. Compared with the prior art, on the basic of the sewage processing craftwork of biological diatomite, the solid-liquid separating method using the biological diatomite as an automatic dynamic component and forming a dynamic film at the surface of a support body(stainless meshes or melon meshes ) with big holes is used to obtain quality output water of which the suspended solid (SS)content or turbidity is low, and the quality output water is closed to the output quality of a membrane bioreactor (MBR). The present invention is suitable to the water processing technology by using the biological diatomite.

Description

technical field [0001] The invention relates to water treatment membrane technology, in particular to a dynamic membrane separation method for treating sewage with biological diatomite. Background technique [0002] In the 21st century, water treatment membrane separation technology has become more and more widely used. Dynamic membrane separation technology, which can achieve similar water quality to microfiltration technology, has become a hot spot in current membrane research due to its relatively low investment cost, easy control of membrane fouling, and low energy consumption. [0003] Dynamic membrane (Dynamic membrane) can also be called secondary membrane (second membrane), which refers to a new membrane formed on the surface of microfiltration membrane, ultrafiltration membrane or large-pore support by precoating agent or activated sludge (J.Lee , W.Y.Ahn, C.H.Lee. Comparison of the filtration characteristics between attached and suspended growth microorganisms in ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F1/44C02F3/10
CPCY02W10/10
Inventor 曹达文金伟董秉直范瑾初褚华强赵雅萍
Owner 华方水务(中国)有限公司