CN205164688U - Gas, liquid phase material mixing duct for reation kettle - Google Patents
Gas, liquid phase material mixing duct for reation kettle Download PDFInfo
- Publication number
- CN205164688U CN205164688U CN201521035537.8U CN201521035537U CN205164688U CN 205164688 U CN205164688 U CN 205164688U CN 201521035537 U CN201521035537 U CN 201521035537U CN 205164688 U CN205164688 U CN 205164688U
- Authority
- CN
- China
- Prior art keywords
- liquid phase
- liquid
- gas
- stop piece
- utility
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a gas, liquid phase material mixing duct for reation kettle, including liquid phase entry, liquid phase export and body, liquid phase entry and liquid phase export are located the both sides of body respectively, the gaseous phase entry has been offered on the lateral wall of body near liquid phase entry tip, the inside slope separation blade that is equipped with of body. Through the utility model discloses, gaseous phase material and liquid phase material are direct not to need the dedicated blender of reload at pipe -line blending, and the investment of having saved the production line has improved the mixing quality of material simultaneously.
Description
Technical field
The utility model relates to chemical reaction still field, specifically, relates to a kind of reactor gas, liquid mixing of materials pipeline.
Background technology
In Chemical Manufacture, if when the heterogeneous reaction mixing of materials in reactor is insufficient, the yield of product can be caused lower, and quality is also poor, also causes a large amount of wastes of raw material simultaneously, increase production cost.Traditional solution is numbered-up mixers before reactor, material enters reactor after first mixing in a mixer again, but the production line investment of adopting in this way is high, complex structure, install loaded down with trivial details, and add the mixing of materials time, production efficiency reduces greatly.
Utility model content
The purpose of this utility model is to provide that a kind of structure is simple, with low cost, production efficiency is high and mictoplasm measured reactor gas, liquid mixing of materials pipeline.
Reactor gas, liquid mixing of materials pipeline, comprises liquid phase entrance, liquid-phase outlet and body, and described liquid phase entrance and described liquid-phase outlet lay respectively at the both sides of body; Described body offers gas phase entrance on the sidewall of liquid phase arrival end; Evenly be provided with some upper stop pieces on the upside of described tubular body, be evenly provided with some lower stop pieces on the downside of described tubular body, described upper stop piece and described lower stop piece interval on flow direction is arranged.
As a kind of improved procedure, described upper stop piece and flow direction form 45-90 degree inclination angle, and described lower stop piece and flow direction form the inclination angle of 90-135 degree.
The beneficial effect that the utility model is carried is: (1) gas, liquid mixing of materials is carried out in body, does not need the blender that new clothes are special, saves the investment of production line; (2) owing to offering baffle plate in body, the flow direction is changed thus adds the length that liquid passes through, extend the incorporation time of gaseous phase materials and liquid phase material, mixing quality is good; (3) catch forms inclination angle in body, thus makes liquid form collision in body, further increases mixing quality.
Accompanying drawing explanation
Fig. 1 is the main pseudosection of the reactor gas, liquid mixing of materials pipeline that the utility model provides;
Fig. 2 is graphics of the present utility model;
In figure: 1-liquid phase entrance, 2-liquid-phase outlet, 3-gas phase entrance, 4-body, 5-lower stop piece, 6-upper stop piece.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
The utility model provides reactor gas, liquid mixing of materials pipeline, comprises liquid phase entrance 1, liquid-phase outlet 2 and body 4, and described liquid phase entrance 1 and described liquid-phase outlet 2 lay respectively at the both sides of body 4; Described body 4 offers gas phase entrance 3 on the sidewall of described liquid phase entrance 1 end; Described body 4 upper inside is evenly provided with some upper stop pieces 6, described body 4 inner lower is evenly provided with some lower stop pieces 5, described upper stop piece 6 and described lower stop piece 5 interval on flow direction is arranged, and described upper stop piece 6 forms 45-90 degree inclination angle with flow direction, described lower stop piece 5 and flow direction form the inclination angle of 90-135 degree
In the present embodiment, liquid phase material flows into from liquid phase entrance 1, and gaseous phase materials flows into from gas phase entrance 3, and both flow out from liquid-phase outlet 2 after mixing in body 4; Offer lower stop piece 5 and the upper stop piece 6 of inclination in body 4, liquid forms mixing power through lower stop piece 5 and upper stop piece 6 acting in conjunction after liquid phase entrance 1 flows into, and further increases mixed effect simultaneously.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (2)
1. reactor gas, liquid mixing of materials pipeline, comprises liquid phase entrance, liquid-phase outlet and body, and described liquid phase entrance and described liquid-phase outlet lay respectively at the both sides of described body, and described body offers gas phase entrance on the sidewall of liquid phase inlet end portion; It is characterized in that: be evenly provided with some upper stop pieces on the upside of described tubular body, be evenly provided with some lower stop pieces on the downside of described tubular body, described upper stop piece and described lower stop piece interval on flow direction is arranged.
2. reactor gas, liquid mixing of materials pipeline as claimed in claim 1, it is characterized in that: described upper stop piece and flow direction form 45-90 degree inclination angle, described lower stop piece and flow direction form the inclination angle of 90-135 degree.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521035537.8U CN205164688U (en) | 2015-12-10 | 2015-12-10 | Gas, liquid phase material mixing duct for reation kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521035537.8U CN205164688U (en) | 2015-12-10 | 2015-12-10 | Gas, liquid phase material mixing duct for reation kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205164688U true CN205164688U (en) | 2016-04-20 |
Family
ID=55728727
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521035537.8U Expired - Fee Related CN205164688U (en) | 2015-12-10 | 2015-12-10 | Gas, liquid phase material mixing duct for reation kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205164688U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112439330A (en) * | 2019-08-30 | 2021-03-05 | 宁波方太厨具有限公司 | Micro-nano bubble generating device and cleaning machine applying same |
| CN114471428A (en) * | 2022-01-26 | 2022-05-13 | 浙江长江搅拌设备有限公司 | Gas dispersion device |
-
2015
- 2015-12-10 CN CN201521035537.8U patent/CN205164688U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112439330A (en) * | 2019-08-30 | 2021-03-05 | 宁波方太厨具有限公司 | Micro-nano bubble generating device and cleaning machine applying same |
| CN112439330B (en) * | 2019-08-30 | 2022-10-21 | 宁波方太厨具有限公司 | Micro-nano bubble generating device and cleaning machine applying same |
| CN114471428A (en) * | 2022-01-26 | 2022-05-13 | 浙江长江搅拌设备有限公司 | Gas dispersion device |
| CN114471428B (en) * | 2022-01-26 | 2024-01-30 | 浙江长江搅拌设备有限公司 | Gas dispersing device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205164688U (en) | Gas, liquid phase material mixing duct for reation kettle | |
| CN205988681U (en) | A kind of Liqiud-gas mixing device of built-in spiral deflector | |
| CN204159333U (en) | A kind of water pump type still external circulating device | |
| CN205965548U (en) | A blending tank for gas -liquid two -phase reaction | |
| CN203458993U (en) | Medicament mixer | |
| CN204220147U (en) | A kind of chemical industry efficient uniform heating mixing agitator | |
| CN205146085U (en) | Be used for solid -liquid mixture agitator | |
| CN202762430U (en) | Defoaming agent reactor | |
| CN205182572U (en) | Chemical industry reation kettle of mixer of crouching ushers to seat | |
| CN203253439U (en) | Modified starch wet process production reaction device | |
| CN204365159U (en) | There is the blender of fixed blade | |
| CN202226895U (en) | Novel rare earth extraction tank unit system device | |
| CN206295924U (en) | A kind of reactor vacuum feeder | |
| CN105413590A (en) | Butane catalytic oxidation reaction device | |
| CN204247146U (en) | Directly can access the liquid mixer of fluid pipeline | |
| CN205109588U (en) | Graphite chlorine distributor | |
| CN204395799U (en) | Prepare the slurry agitating device of cool skin | |
| CN205164681U (en) | Novel reaction of butane catalytic oxidation device | |
| CN205761152U (en) | A kind of nitration reaction still | |
| CN204824183U (en) | Anti -oxidant expandable graphite's preparation system | |
| CN205146190U (en) | Ammoniation reaction ware | |
| CN203227459U (en) | Mixing structure for smears | |
| CN207287375U (en) | Butane air gas mixed distribution device | |
| CN203208927U (en) | Dynamic mixer | |
| CN202647773U (en) | Eccentric multi-mixing static gas mixer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 262737 Lingang Industrial Park, Binhai Economic Development Zone, Weifang, Shandong Patentee after: Agricultural Chemical Co.,Ltd. Weifang run Address before: 262737 Lingang Industrial Zone, Binhai Economic and Technological Development Zone, Weifang, Shandong Patentee before: WEIFANG HAILIAN CHEMICAL ENGINEERING CO.,LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160420 Termination date: 20211210 |