Pipeline type gas-liquid two-phase flow mixer

A technology of gas-liquid two-phase flow and mixer, which is applied in the direction of fluid mixer, gas/steam and liquid mixing, mixer, etc., which can solve the problems of large local resistance of the mixer, large bubble size, high passing flow rate, etc. Achieve the effect of improving gas-liquid mass transfer efficiency and prolonging gas-liquid contact time

Pending Publication Date: 2022-01-07
SHANGHAI XINGHENG SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the large difference in density between gas and liquid, when using a pipeline static mixer to achieve the ideal mixing effect, a very high flow rate is required, which makes the local resistance of the mixer huge; at the same time, due to the existence of a large number of micro-void structures, it is easy to cause blockage. It is clogged and difficult to clean; while the mixing effect of the jet is concentrated in the vortex area before and after the throat, the gas-liquid contact mixing time is too short, and the bubble size is large, so the mixing effect is not good

Method used

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  • Pipeline type gas-liquid two-phase flow mixer
  • Pipeline type gas-liquid two-phase flow mixer
  • Pipeline type gas-liquid two-phase flow mixer

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Embodiment Construction

[0024] The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.

[0025] In describing the present invention, it should be understood that the terms "center", "longitudinal", "transverse", "length", "width", "thickness", "upper", "lower", "front", " The orientation or positional relationship indicated by "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc. is based on the orientation shown in the drawings Or positional relationship is only for the convenience of describing the present in...

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Abstract

The invention relates to the technical field of gas-liquid mixing, in particular to a pipeline type gas-liquid two-phase flow mixer which is characterized in that a main body of the pipeline type gas-liquid two-phase flow mixer is of an annular column structure, two ends of the pipeline type gas-liquid two-phase flow mixer are provided with a water inlet connector and a water outlet connector, and an intercepting pore plate, a plurality of intercepting pore extension pipes, a plurality of impact cavities and a set of impact cavity supports are arranged in an internal cylindrical water passing channel. Water flow is accelerated through the intercepting pore extension pipes and then jetted into an impact cavity, strong convection is formed in the impact cavity, the gas-liquid contact time is prolonged, the gas-liquid mass transfer efficiency is improved, gas-liquid sufficient mixing can be achieved in a short-distance pipeline, and the gas-liquid two-phase flow pipeline mixing device is particularly suitable for the gas-liquid two-phase flow pipeline mixing situation with the small gas-liquid ratio, the limited space, the small pipe diameter and the low flow.

Description

technical field [0001] The invention relates to the technical field of gas-liquid mixing, in particular to a pipeline type gas-liquid two-phase flow mixer. Background technique [0002] Gas-liquid mixed mass transfer is a very important process requirement for chemical industry, environmental protection, medicine and other industrial fields. Convective contact towers such as packed towers and sieve tray towers are very effective gas-liquid mixing equipment. However, in some fields, such as medical injection, micro-reactors, small instruments, etc., due to the very small installation space, pipe diameter and water flow rate, it is impossible to use the above-mentioned large-scale equipment for gas-liquid mixing and dissolution. [0003] For the above situation, in the prior art, the way of pipeline static mixer or jet is mostly used for mixing and mass transfer. Due to the large difference in density between gas and liquid, when using a pipeline static mixer to achieve the ...

Claims

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Application Information

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IPC IPC(8): B01F25/20B01F25/40B01F23/20
Inventor 王培
Owner SHANGHAI XINGHENG SCI & TECH
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