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Chlorine dioxide generator

A chlorine dioxide and generator technology, applied in chlorine dioxide, chlorine oxide and other directions, can solve the problems of increasing operation difficulty and equipment cost, destroying the flow status of chlorine dioxide, affecting the conversion rate of chlorine dioxide, etc., and achieving a good industrial Application prospect, saving user investment, not limited by raw materials

Inactive Publication Date: 2019-12-27
SICHUAN QILI LVYUAN WATER TREATMENT TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the aeration process is also very difficult to operate in actual operation: if the aeration is too small, it will not have the effect of mixing and dilution, on the one hand, it will affect the chemical reaction effect, on the other hand, it will cause the concentration of chlorine dioxide in the gas phase to be too high Large, prone to explosion; and when the aeration is too large, the "flooding" phenomenon occurs in the reactor, so that the aeration not only fails to achieve its due effect, but also destroys the flow of the liquid in the chlorine dioxide generator. Affect the conversion rate of chlorine dioxide
Moreover, the existing technology also includes operations such as stirring in order to react uniformly and fully. At the same time, because the reactor is a gas-liquid two-phase, in order to make the chlorine dioxide mixture flow out, the working pressure of the water injector is ≥ 0.8MPa, and these operations have increased. Practical difficulty and equipment cost

Method used

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  • Chlorine dioxide generator

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0087] Embodiment 1 of the present invention provides a kind of chlorine dioxide generator, as figure 1 As shown, it includes a feed device, a reaction device and a discharge device; the feed device, the reaction device and the discharge device are connected in sequence.

[0088] The feeding device includes a tee 1 , a connecting pipe 2 , a feeding elbow 3 , and a first reducing pipe 4 .

[0089] The tee includes a first feed port 101, a second feed port 102, and an outlet;

[0090] The outlet of the tee 1 is connected to the upper end of the connecting pipe 2; the lower end of the connecting pipe 2 is connected to the upper end of the feed elbow 3; the first reducing pipe 4 is connected to the lower end of the feed elbow 3; The outlet diameter of the tee 1 is smaller than the inlet diameter of the first pipe 5 .

[0091] The reaction device comprises a reaction unit A, a first reaction unit B and a second reaction unit B; the reaction unit A comprises a first pipeline 5 and...

Embodiment 2

[0098] Embodiment 2 of the present invention provides a kind of chlorine dioxide generator as described in embodiment 1, described tee, connecting pipe, feed elbow, elbow, discharge elbow, the first reducing pipe, The materials of the second reducing pipe, the first pipe, the first elbow and the pipe are all PVC.

[0099] The outlet diameter of the tee 1 is 2 / 3 smaller than the inlet diameter of the first pipe 5 .

[0100] The pipe has a diameter of 125 mm and a length of 1800 mm.

[0101] The horizontal gradient of the pipeline from the inlet to the outlet is 11%.

[0102] The inlet diameter of the outlet elbow 14 is 2 / 3 smaller than the outlet diameter of the third pipeline 11 .

[0103] This example also provides a method for using the chlorine dioxide generator, and the steps are as follows:

[0104] Step 1: Connect the discharge elbow 14 with the injector;

[0105]Step 2: After adding the raw material A solution and the raw material B solution through the first feed p...

Embodiment 3

[0110] Embodiment 3 of the present invention provides a kind of chlorine dioxide generator, and it is similar to embodiment 2, and difference is that the outlet diameter of described tee 1 is 1 / 2 smaller than the inlet diameter of pipeline; The inlet diameter of the elbow is 1 / 2 smaller than the inlet diameter of the pipe.

[0111] According to the test method described in Example 2, the chlorine dioxide conversion rate is 97%.

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Abstract

According to a chlorine dioxide generator provided by the invention, a tubular reactor is adopted, and a reaction solution flows and turns at a certain speed in a pipeline by controlling the flow direction of the reaction solution and the parameters of a reaction tube, so that sufficient stirring is realized, and the reaction is uniform. Chlorine dioxide conversion rate tests show that the chlorine dioxide generator provided by the invention can enable the chlorine dioxide conversion rate to be greater than or equal to 95%, which is much higher than the national performance requirements on thechlorine dioxide generator. The chlorine dioxide generator provided by the invention is in a liquid phase and does not contain a gas phase, chlorine dioxide is not easy to decompose and explode, no leakage risk exists, and the safety of the reaction process is high; and a mixed liquid can flow out by adopting a water ejector with a lower vacuum degree, so that the energy consumption is reduced. In addition, the chlorine dioxide generator provided by the invention is stable and reliable in operation and stable in chlorine dioxide yield; the manufacturing cost is low, the structure is simple, and the industrial application prospect is good.

Description

technical field [0001] The invention relates to the field of disinfection and sterilization, in particular to a chlorine dioxide generator. Background technique [0002] Chlorine dioxide is an internationally recognized safe and non-toxic green disinfectant. Due to its strong selective oxidation ability and broad-spectrum and high-efficiency bactericidal ability, it has been used for pulp and fiber bleaching and drinking water disinfection. , food processing, preservation, waste water treatment, medical disinfection and sterilization, bleaching, water injection oil recovery, oil well deblocking and control of biological pollution and many other aspects. [0003] The current prior art generally uses reactors or multi-stage reactors in series to prepare chlorine dioxide, but because the reactor is in gas-liquid two-phase during the preparation process, chlorine dioxide is an unstable gas, and its volume in the space is greater than 10% there is a risk of explosion. Therefore...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B11/02
CPCC01B11/024C01B11/025C01B11/026C01B11/027
Inventor 穆超银
Owner SICHUAN QILI LVYUAN WATER TREATMENT TECH CO LTD
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