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Flocculation reactor

A reactor and flocculation technology, applied in the direction of flocculation/sedimentation water/sewage treatment, chemical instruments and methods, separation methods, etc., can solve the problems of long reaction time, decrease of flocculation effect, increase of large particle breakage, etc., to improve flocculation effect , reduced energy consumption and response time, rapid growth reduction effects

Inactive Publication Date: 2011-09-07
BEIJING JIAOTONG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, due to the large fluctuations in the velocity gradient of this type of flocculation reactor, the change trend is wavy or broken-line, which causes the velocity gradient of the existing flocculation reactor to be very large at the turning or the water passing section. Velocity gradient is very small in straight pipe section or at the place with larger cross-section
Especially in the late stage of the flocculation reaction, when the size of the particles is large, the breakage of large particles will undoubtedly increase at the corner with a large velocity gradient or at the small cross-section of the water, which will eventually lead to a decline in the flocculation effect.
This brings high energy consumption and long reaction time of existing flocculation reactors

Method used

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Embodiment Construction

[0017] In order to make the above objects, features and advantages of the present invention more comprehensible, the present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments.

[0018] refer to figure 1 , figure 1 It is a top view of an embodiment of the flocculation reactor of the present invention. The flocculation reactor of the present invention includes a water inlet 1, a water outlet 2, and a reactor body between the water inlet 1 and the water outlet 2. The reactor body includes a continuous flow groove 3, and the width of the flow groove 3 is along the length of the water inlet. 1 to outlet 2 gradually increase. The launder 3 is bounded by two launder walls 4 . A flow tank 3 with continuously variable width is used to realize continuous variation of the gradient of water flow velocity in the flocculation reactor.

[0019] Due to the gradual increase of the width of the launder, the gradient ...

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Abstract

The invention discloses a flocculation reactor, comprising a water inlet, a water outlet and a reactor body arranged between the water inlet and the water outlet, wherein the reactor body comprises a spiral sluice with width continuously changed; and the spiral sluice is used for ensuring the velocity of the flow in the flocculation reactor to continuously change in a gradient manner and gradually decrease. The flocculation reactor designed in the invention conforms to the requirement of coagulation kinetics for gradient change of velocity, can not only meet the requirement of rapid growth ofthe grains but also reduce breakage of the large scale grains, and reduces the energy consumption and the reaction time while improving the flocculation effect.

Description

technical field [0001] The invention relates to a water treatment device, in particular to a flocculation reactor of a spiral flow tank with continuously changing velocity gradient. Background technique [0002] The flocculation process is a process in which floc particles grow gradually. The velocity gradient plays two opposite roles in the flocculation reactor. A larger velocity gradient corresponds to a greater collision frequency and thus promotes the growth of particles. At the same time, an increase in the velocity gradient also increases the probability of breaking large-scale particles. [0003] Existing flocculation reactors, such as reciprocating flocculation reactors, rotary flocculation reactors, and folded plate flocculation reactors, all use different structures of flocculation reactors to change the flow rate and direction of water flow to achieve flocculation effects. However, due to the large fluctuations in the velocity gradient of this type of flocculatio...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D21/01C02F1/52
Inventor 赵宗升年跃刚
Owner BEIJING JIAOTONG UNIV
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