CN105879732A - Chemical-fluid mixing device - Google Patents
Chemical-fluid mixing device Download PDFInfo
- Publication number
- CN105879732A CN105879732A CN201610420087.7A CN201610420087A CN105879732A CN 105879732 A CN105879732 A CN 105879732A CN 201610420087 A CN201610420087 A CN 201610420087A CN 105879732 A CN105879732 A CN 105879732A
- Authority
- CN
- China
- Prior art keywords
- axis
- main pipeline
- chemical
- lateral
- mixing device
- 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.)
- Pending
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/311—Injector mixers in conduits or tubes through which the main component flows for mixing more than two components; Devices specially adapted for generating foam
Abstract
The invention discloses a chemical-fluid mixing device. The chemical-fluid mixing device comprises a main pipe and a branch pipe. The branch pipe extends into the main pipe, an included angle with 30 degrees to 40 degrees is formed between the axis of the extending end of the branch pipe and the axis of the main pipe, the section of axis, located at the tail end inside the main pipe, of the branch pipe is coincident with the axis of the main pipe, and propeller blades are arranged at an outlet of the branch pipe. According to the chemical-fluid mixing device, the pressure losses of the branch pipe are small, the spiral diffusion mixing mode is adopted, and the mixing effect is good; the chemical-fluid mixing device is reasonable is structural design, and has the advantages of being easy to manufacture, low in cost, high in efficiency and the like.
Description
Technical field
The present invention relates to technical field of chemical, particularly relate to a kind of chemical industry fluid mixer.
Background technology
In Chemical Manufacture, it is often necessary to two fluids shape industrial chemicals is pre-mixed, in prior art, the direct static mixing of general employing, but this hybrid mode, often mix uneven, cause mixed effect the best, be unfavorable for subsequent production.
Summary of the invention
The problem to be solved in the present invention is to overcome the deficiency in background technology, it is provided that a kind of chemical industry fluid mixer, this chemical industry fluid mixer, uses the hybrid mode of spiral diffusion, improves mixed effect.
For solving the problems referred to above, the present invention takes techniques below scheme:
A kind of chemical industry fluid mixer of the present invention, including main pipeline and lateral, described lateral stretches in main pipeline, the axis of the inserting end of described lateral becomes 30 °～45 ° of angles with the axis of main pipeline, described lateral is positioned at the axis of the end one section within main pipeline and the dead in line of main pipeline, and the exit of described lateral is provided with propeller blade.
Further, the extreme ends of described lateral is provided with support, and described propeller blade is rack-mount.
Compared with prior art, the invention has the beneficial effects as follows:
A kind of chemical industry fluid mixer of the present invention, two fluids shape industrial chemicals, lay respectively in main pipeline and lateral, lateral stretches into main pipeline, the axis of the inserting end of described lateral becomes 30 °～45 ° of angles with the axis of main pipeline, described lateral is positioned at the axis of the end one section within main pipeline and the dead in line of main pipeline, and the extreme ends at lateral is provided with support, is provided with propeller blade on support；When the industrial chemicals of a kind of flow-like flows into along lateral, 30 °～the angle of 45 °, guarantee that the industrial chemicals pressure loss of this flow-like is less, so that when end flows out along axis, drive propeller blade, flow-like stock dispersion is squeezed in the flow-like industrial chemicals of main pipeline by propeller blade, thus obtains uniform mixture.
A kind of chemical industry fluid mixer of the present invention, the lateral pressure loss is little, and the spiral diffusion hybrid mode of employing, mixed effect is good, and present configuration is reasonable in design, has easily manufacture, low cost, efficiency advantages of higher.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Fig. 2 is that the A of Fig. 1 is to schematic diagram.
Description of reference numerals: 1-main pipeline, 2-lateral, 3-propeller blade, 4-support.
Detailed description of the invention
As depicted in figs. 1 and 2, a kind of chemical industry fluid mixer of the present invention, including main pipeline 1 and lateral 2, described lateral 2 stretches in main pipeline 1, the axis of the inserting end of described lateral 2 becomes 30 °～45 ° of angles with the axis of main pipeline 1, described lateral 2 is positioned at the axis of the end one section within main pipeline 1 and the dead in line of main pipeline 1, and the exit of described lateral 2 is provided with propeller blade 3.
The extreme ends of described lateral 2 is provided with support 4, and described propeller blade 3 is arranged on support 4.
Compared with prior art, the invention has the beneficial effects as follows:
A kind of chemical industry fluid mixer of the present invention, two fluids shape industrial chemicals, lay respectively in main pipeline 1 and lateral 2, lateral 2 stretches into main pipeline 1, the axis of the inserting end of described lateral 2 becomes 30 °～45 ° of angles with the axis of main pipeline 1, described lateral 2 is positioned at the axis of the end one section within main pipeline 1 and the dead in line of main pipeline 1, and the extreme ends at lateral 2 is provided with support 4, is provided with propeller blade 3 on support 4；When the industrial chemicals of a kind of flow-like flows into along lateral 2,30 °～the angle of 45 °, guarantee that the industrial chemicals pressure loss of this flow-like is less, so that when end flows out along axis, drive propeller blade 3, flow-like stock dispersion is squeezed in the flow-like industrial chemicals of main pipeline 1 by propeller blade 3, thus obtains uniform mixture.
A kind of chemical industry fluid mixer of the present invention, the lateral pressure loss is little, and the spiral diffusion hybrid mode of employing, mixed effect is good, and present configuration is reasonable in design, has easily manufacture, low cost, efficiency advantages of higher.
It should be noted that, the foregoing is only the preferred embodiments of the present invention, be not limited to the present embodiment, all within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (2)
1. a chemical industry fluid mixer, including main pipeline (1) and lateral (2), it is characterized in that: described lateral (2) stretches in main pipeline (1), the axis of the inserting end of described lateral (2) becomes 30 °～45 ° of angles with the axis of main pipeline (1), described lateral (2) is positioned at the axis of the internal end one section of main pipeline (1) and the dead in line of main pipeline (1), and the exit of described lateral (2) is provided with propeller blade (3).
A kind of chemical industry fluid mixer the most according to claim 1, it is characterised in that: the extreme ends of described lateral (2) is provided with support (4), and described propeller blade (3) is arranged on support (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610420087.7A CN105879732A (en) | 2016-06-16 | 2016-06-16 | Chemical-fluid mixing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610420087.7A CN105879732A (en) | 2016-06-16 | 2016-06-16 | Chemical-fluid mixing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105879732A true CN105879732A (en) | 2016-08-24 |
Family
ID=56730675
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610420087.7A Pending CN105879732A (en) | 2016-06-16 | 2016-06-16 | Chemical-fluid mixing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105879732A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111153572A (en) * | 2020-01-13 | 2020-05-15 | 北京尚水清源水处理技术有限公司 | Anaerobic digestion sludge plate-frame dehydration pre-conditioning floc dynamic regulation reaction device and method |
| CN111655360A (en) * | 2017-11-06 | 2020-09-11 | 苏尔寿管理有限公司 | Improved mixer tube and process using same |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4498786A (en) * | 1980-11-15 | 1985-02-12 | Balcke-Durr Aktiengesellschaft | Apparatus for mixing at least two individual streams having different thermodynamic functions of state |
| CN201988343U (en) * | 2011-03-15 | 2011-09-28 | 天津力冠能源科技有限公司 | Ammonia gas and air Venturi mixer |
| CN103933858A (en) * | 2014-02-28 | 2014-07-23 | 东南大学 | Tangential double vortex SCR mixer |
| CN104645845A (en) * | 2015-03-18 | 2015-05-27 | 魏伯卿 | Large/small-drift diameter pipe phase mixing pipeline mixer |
| CN204672157U (en) * | 2015-05-30 | 2015-09-30 | 潍坊友容实业有限公司 | A kind of freshwater-seawater mixing device |
| CN205868039U (en) * | 2016-06-16 | 2017-01-11 | 无锡市翱宇特新科技发展有限公司 | Chemical industry fluid mixing arrangement |
-
2016
- 2016-06-16 CN CN201610420087.7A patent/CN105879732A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4498786A (en) * | 1980-11-15 | 1985-02-12 | Balcke-Durr Aktiengesellschaft | Apparatus for mixing at least two individual streams having different thermodynamic functions of state |
| CN201988343U (en) * | 2011-03-15 | 2011-09-28 | 天津力冠能源科技有限公司 | Ammonia gas and air Venturi mixer |
| CN103933858A (en) * | 2014-02-28 | 2014-07-23 | 东南大学 | Tangential double vortex SCR mixer |
| CN104645845A (en) * | 2015-03-18 | 2015-05-27 | 魏伯卿 | Large/small-drift diameter pipe phase mixing pipeline mixer |
| CN204672157U (en) * | 2015-05-30 | 2015-09-30 | 潍坊友容实业有限公司 | A kind of freshwater-seawater mixing device |
| CN205868039U (en) * | 2016-06-16 | 2017-01-11 | 无锡市翱宇特新科技发展有限公司 | Chemical industry fluid mixing arrangement |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111655360A (en) * | 2017-11-06 | 2020-09-11 | 苏尔寿管理有限公司 | Improved mixer tube and process using same |
| CN111655360B (en) * | 2017-11-06 | 2022-06-07 | 苏尔寿管理有限公司 | Improved mixer tube and process using same |
| US11752473B2 (en) | 2017-11-06 | 2023-09-12 | Sulzer Management Ag | Mixer duct and process of operation |
| CN111153572A (en) * | 2020-01-13 | 2020-05-15 | 北京尚水清源水处理技术有限公司 | Anaerobic digestion sludge plate-frame dehydration pre-conditioning floc dynamic regulation reaction device and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160824 |