CN204973854U - Chemical reaction system - Google Patents
Chemical reaction system Download PDFInfo
- Publication number
- CN204973854U CN204973854U CN201520772249.4U CN201520772249U CN204973854U CN 204973854 U CN204973854 U CN 204973854U CN 201520772249 U CN201520772249 U CN 201520772249U CN 204973854 U CN204973854 U CN 204973854U
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- blender
- reaction tube
- liquid
- spiral
- reaction
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Abstract
The utility model discloses a chemical reaction system, including blender and spiral reaction tube, two inlets of blender are respectively through first micro - feed liquor ware of tube coupling and second trace feed liquor ware, and the liquid outlet of blender passes through the pipeline to be connected with the inlet of spiral reaction tube, just are provided with the vortex pipe on the continuous pipeline of blender and spiral reaction tube, it disturbs stream block to be provided with the round on the inner wall of vortex pipe, the spiral reaction tube sets up the inside at the temperature control box. The utility model discloses a blender and vortex pipe carry out twice mixture to the reaction liquid, can promote the mixability and the mixing efficiency of liquid to guarantee two kinds of liquid and follow the shunting and trigger living reaction in the spiral reaction tube, improve the reaction yield, because the whole pipe wall area of spiral reaction tube is big, so the temperature control box can carry out the control by temperature change to reaction liquid in the spiral reaction tube fast to realize high -efficient control by temperature change.
Description
Technical field
The utility model belongs to technical field of chemical reaction devices, relates in particular to a kind of chemical reaction system.
Background technology
When carrying out chemical reaction between different liquids, its mixing efficiency and mixability directly affect reaction efficiency between different liquids and reaction yield, and the mixability therefore improved between differential responses liquid is most important; Simultaneous reactions temperature is also related to reaction efficiency and reaction yield, and the reaction temperature therefore how more effectively controlling reactant is also very important.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, provides a kind of chemical reaction system, and the utility model can make different reaction liquids efficiently mix, and control effectively to reaction temperature simultaneously.
The utility model is achieved through the following technical solutions:
A kind of chemical reaction system, comprises blender and spiral reaction tube;
The inside of described blender is hollow cavity, blender comprises two inlets and a liquid outlet, inlet is connected with hollow cavity with liquid outlet, two inlets of blender connect the first micro-liquid inlet device and the second micro-liquid inlet device respectively by pipeline, the liquid outlet of blender is connected with the inlet of spiral reaction tube by pipeline, and the pipeline be connected with spiral reaction tube at blender is provided with disturbed flow pipe, the inwall of described disturbed flow pipe is provided with a circle flow-disturbing block;
Described spiral reaction tube is spirality pipe structure, and its two ends are respectively arranged with inlet and liquid outlet, and spiral reaction tube is arranged on the inside of temperature control box.
In technique scheme, the inside of described blender is T-shaped hollow cavity.
In technique scheme, flow-disturbing block evenly equidistantly distributes along the inwall of disturbed flow pipe.
During use, the flow of the first micro-liquid inlet device and the second micro-liquid inlet device is set in advance according to the ratio requirement of reaction, open the first micro-liquid inlet device and the second micro-liquid inlet device passes into two kinds of reaction liquids in blender, two kinds of reaction liquids mix for the first time in the T-shaped hollow cavity of blender; Then liquid stream is through disturbed flow pipe, and under the flow-disturbing effect of the flow-disturbing block of disturbed flow pipe, liquid mixes again; After twice mixing, liquid enters spiral reaction tube, sets the reaction temperature needed for spiral response liquid in pipe by temperature control box, thus makes liquid complete reaction in spiral reaction tube.The utility model carries out twice mixing by blender and disturbed flow pipe to reaction liquid, can promote mixability and the mixing efficiency of liquid, thus ensures that two kinds of liquid carry out touching from tap reacting in spiral reaction tube, improves reaction yield.Due to spiral reaction tube integral tube wall area large (heat transference efficiency is higher), so temperature control box can carry out temperature control to reaction liquid in spiral reaction tube fast, thus realize high efficiency temperature controlled.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the perspective view of the disturbed flow pipe in the utility model.
Fig. 3 is the side view of the disturbed flow pipe shown in Fig. 2.
Wherein: 1 is blender, 2 is disturbed flow pipe, and 3 is spiral reaction tube, and 4 is temperature control box, and 5 is the first micro-liquid inlet device, and 6 is the second micro-liquid inlet device, and 2-1 is flow-disturbing block.
Detailed description of the invention
The technical solution of the utility model is further illustrated below in conjunction with specific embodiment.
As shown in Figure 1, a kind of chemical reaction system involved by the utility model, comprises blender 1 and spiral reaction tube 3,
The inside of described blender is T-shaped hollow cavity, blender 1 comprises two inlets and a liquid outlet, inlet is connected with T-shaped hollow cavity with liquid outlet, two inlets of blender connect the first micro-liquid inlet device 5 and the second micro-liquid inlet device 6 respectively by pipeline, the liquid outlet of blender is connected by the inlet of pipeline with spiral reaction tube 3, and (namely the liquid outlet of blender is connected with one end of disturbed flow pipe 2 to be provided with disturbed flow pipe 2 on the pipeline that blender is connected with spiral reaction tube, the other end of disturbed flow pipe 2 is connected with the inlet of spiral reaction tube 3), as shown in Figures 2 and 3, the inwall of described disturbed flow pipe 2 is provided with a circle flow-disturbing block 2-1, flow-disturbing block 2-1 evenly equidistantly distributes along the inwall of disturbed flow pipe, when liquid stream is through disturbed flow pipe 2, flow-disturbing block 2-1 can produce flow-disturbing effect to liquid thus promote the mixing of liquid,
Described spiral reaction tube 3 is spirality pipe structure, its two ends are respectively arranged with inlet and liquid outlet, spiral reaction tube 3 is arranged on the inside of temperature control box 4, the reaction temperature of liquid in spiral reaction tube 3 can be controlled by temperature control box, the time (i.e. the reaction time of reaction liquid) that reaction liquid flows through spiral reaction tube can be set by the spiral number of turns increasing or reduce spiral reaction tube;
During use, the flow of the first micro-liquid inlet device 5 and the second micro-liquid inlet device 6 is set in advance according to the ratio requirement of reaction, open the first micro-liquid inlet device 5 and the second micro-liquid inlet device 6 passes into two kinds of reaction liquids in blender 1, two kinds of reaction liquids mix for the first time in the T-shaped hollow cavity of blender 1; Then liquid stream is through disturbed flow pipe 2, and under the flow-disturbing effect of the flow-disturbing block 2-1 of disturbed flow pipe 2, liquid mixes again; After twice mixing, liquid enters spiral reaction tube 3, sets the reaction temperature needed for spiral response liquid in pipe by temperature control box, thus makes liquid complete reaction in spiral reaction tube 3.
Above exemplary description is done to the utility model; should be noted that; when not departing from core of the present utility model, any simple distortion, amendment or other those skilled in the art can not spend the equivalent replacement of creative work all to fall into protection domain of the present utility model.
Claims (3)
1. a chemical reaction system, is characterized in that: comprise blender and spiral reaction tube;
The inside of described blender is hollow cavity, blender comprises two inlets and a liquid outlet, inlet is connected with hollow cavity with liquid outlet, two inlets of blender connect the first micro-liquid inlet device and the second micro-liquid inlet device respectively by pipeline, the liquid outlet of blender is connected with the inlet of spiral reaction tube by pipeline, and the pipeline be connected with spiral reaction tube at blender is provided with disturbed flow pipe, the inwall of described disturbed flow pipe is provided with a circle flow-disturbing block;
Described spiral reaction tube is spirality pipe structure, and its two ends are respectively arranged with inlet and liquid outlet, and spiral reaction tube is arranged on the inside of temperature control box.
2. a kind of chemical reaction system according to claim 1, is characterized in that: the inside of described blender is T-shaped hollow cavity.
3. a kind of chemical reaction system according to claim 1, is characterized in that: described flow-disturbing block evenly equidistantly distributes along the inwall of disturbed flow pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520772249.4U CN204973854U (en) | 2015-09-30 | 2015-09-30 | Chemical reaction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520772249.4U CN204973854U (en) | 2015-09-30 | 2015-09-30 | Chemical reaction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204973854U true CN204973854U (en) | 2016-01-20 |
Family
ID=55108274
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520772249.4U Expired - Fee Related CN204973854U (en) | 2015-09-30 | 2015-09-30 | Chemical reaction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204973854U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106390883A (en) * | 2016-10-31 | 2017-02-15 | 山东豪迈化工技术有限公司 | Microfluidic reactor |
| CN107670594A (en) * | 2017-11-10 | 2018-02-09 | 大丰鑫源达化工有限公司 | A kind of device of continous way speed up gas and liquid reaction |
| CN109695442A (en) * | 2017-12-05 | 2019-04-30 | 安徽省睿斯达石油有限公司 | One kind is allied the communists the spiral pressure break liquid mixing system of formula |
| CN110043802A (en) * | 2019-03-15 | 2019-07-23 | 中国煤层气集团有限公司 | Duct type gasification installation |
| CN112113822A (en) * | 2019-06-21 | 2020-12-22 | 深圳迈瑞生物医疗电子股份有限公司 | Biological sample dyeing device, push piece dyeing machine and biological sample dyeing method |
-
2015
- 2015-09-30 CN CN201520772249.4U patent/CN204973854U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106390883A (en) * | 2016-10-31 | 2017-02-15 | 山东豪迈化工技术有限公司 | Microfluidic reactor |
| CN107670594A (en) * | 2017-11-10 | 2018-02-09 | 大丰鑫源达化工有限公司 | A kind of device of continous way speed up gas and liquid reaction |
| CN109695442A (en) * | 2017-12-05 | 2019-04-30 | 安徽省睿斯达石油有限公司 | One kind is allied the communists the spiral pressure break liquid mixing system of formula |
| CN110043802A (en) * | 2019-03-15 | 2019-07-23 | 中国煤层气集团有限公司 | Duct type gasification installation |
| CN110043802B (en) * | 2019-03-15 | 2021-11-30 | 中国煤层气集团有限公司 | Pipeline type gasification device |
| CN112113822A (en) * | 2019-06-21 | 2020-12-22 | 深圳迈瑞生物医疗电子股份有限公司 | Biological sample dyeing device, push piece dyeing machine and biological sample dyeing method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160120 Termination date: 20160930 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |