CN204824845U - Chemical oscillation's small -size open reactor is participated in to enzyme - Google Patents
Chemical oscillation's small -size open reactor is participated in to enzyme Download PDFInfo
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- CN204824845U CN204824845U CN201520433949.0U CN201520433949U CN204824845U CN 204824845 U CN204824845 U CN 204824845U CN 201520433949 U CN201520433949 U CN 201520433949U CN 204824845 U CN204824845 U CN 204824845U
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- intermediate plate
- casing
- intermediate lamella
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Abstract
The utility model discloses a chemical oscillation's small -size open reactor is participated in to enzyme belongs to non - balance experiment technical field. The reactor includes box, reaction cabin, intermediate lamella and three coupling, and the horizontal fixed connection of intermediate lamella is on the inner wall of box, and the one end that processing responded the liquid pump hand -hole on the intermediate lamella is located the outside of box, two cavitys about the intermediate lamella becomes the internal partitioning of box, reaction cabin vertical fixation is at the upper surface of intermediate lamella and will react the liquid stream and portal and surround inside it completely, three coupling respectively with the box on the coupling connecting hole be connected, one of them coupling lies in the cavity of intermediate lamella below, a cavity that lies in the intermediate lamella top, last one lies in cavity of intermediate lamella top and runs through the reaction cabin simultaneously. The utility model discloses can effectually reduce the volume of reactor to can guarantee that feed liquor pipeline length is unanimous.
Description
Technical field
Utility model relates to the reactor of chemical oscillation experiment, is specifically related to the small size open type reactor that a kind of enzyme participates in chemical oscillation, belongs to Unbalanced Experiment device technique field.
Background technology
Open continuously stirring flowing tank reactor (CSTR) is the key part realizing chemical oscillation condition in experimental study.The fresh material constantly pumped into get rid of waste reaction solution in time, under the residence time makes system be in specific far from equilibrium state condition by adjustment, present unique space-time order phenomenon.For the Feedback mechanism in observation in experiment and specializes in chemistry oscillation system and Control factors provide simple and easy, effective experiment porch, it is the principal reaction device feeding back dynamics research in chemical oscillation system.
At present, existing experimental installation can solve the primary condition of such experiment and the realization of observation, make with glass for the conventional CSTR of specializes in chemistry vibration in laboratory, limit by complete processing, general volume is larger, cause chemical consumption in experimentation fast, be not suitable for the oscillatory reaction that the expensive biochemical reagents such as enzyme are participated in.Conventional CSTR takes an angle of 90 degrees four direction mode to lay water influent pipeline for preventing reaction solution pre-mixing in addition, and water influent pipeline length can be caused to occur the problem such as difference and complete processing complexity.
Utility model content
In view of this, the utility model provides the small size open type reactor that a kind of enzyme participates in chemical oscillation, effectively can reduce the volume of reactor, and can ensure that water influent pipeline length is consistent.
Enzyme participates in a small size open type reactor for chemical oscillation, comprises casing, reaction cabin, intermediate plate and three tube stubs;
Wherein, described casing is the container of open-top, and the outer wall of casing is provided with three tube stub connecting holes;
Described reaction cabin is cylinder type hollow housing and both ends open, and its one end is fixedly connected with the upper surface of intermediate plate, and the other end is for laying the plug of fixed electorde;
The profile of described intermediate plate is consistent with the orthographicprojection of the interior shape of casing, one side end face is processed with reaction solution and pumps into hole, described reaction solution pumps into hole extends to the middle part of intermediate plate perpendicular to this side end face after and passes forming reactions liquid taphole with 90 ° of angles from the upper surface of intermediate plate, described intermediate plate is also processed with the water hole running through its thickness direction;
Its integrated connection closes: described intermediate plate level is fixedly connected on the inwall of casing, intermediate plate is processed with the outside that one end that reaction solution pumps into hole is positioned at casing, the interior separation of casing is become upper and lower two cavitys by intermediate plate, described reaction cabin is vertically fixed on the upper surface of intermediate plate and reaction solution taphole is fully enclosed in its inside, described three tube stubs are connected with the tube stub connecting hole on casing respectively, one of them tube stub is positioned at the cavity below intermediate plate, a cavity be positioned at above intermediate plate, last is positioned at the cavity above intermediate plate and runs through reaction cabin simultaneously.
Further, the material of described casing, reaction cabin and intermediate plate adopts acrylic glass.
Further, the profile of described casing and inner chamber are rectangle.
Principle of work: first water-bath is opened during use, thermostat(t)ed water enters the cavity below intermediate plate by tube stub, then enter the cavity above intermediate plate by the water hole on intermediate plate, the tube stub finally by top is discharged, and reaction cabin is remained on a constant temp by thermostat(t)ed water; Pump into hole from the reaction solution of intermediate plate subsequently and pump into reaction solution, reaction solution enters reaction cabin inside by reaction solution taphole, reaction solution stirs through magnetic stir bar in reaction zone and reacts, and the electrode of insertion collects signal, and waste liquid flows out casing naturally by the tube stub of access reaction cabin.
Beneficial effect:
1, the material of the utility model reactor all have employed acrylic glass, relative to adopt glass material home built reactor can Scaling to the limit of processing units, therefore the utility model significantly can reduce the volume of reactor.
2, traditional reactor limits by glassware processing and experiment condition, and four passages on reactor point to four direction respectively, will some need to lengthen from the pipeline that pump picks out, and is difficult to ensure that water influent pipeline length is consistent; Reaction solution of the present utility model pumps into hole all in the same side of intermediate plate, and the pipeline picked out from pump does not need to do prolongation process, therefore, it is possible to ensure that water influent pipeline length is consistent.
3, the utility model significantly reduces reactor size by replacing reactor manufactured materials and internal structure design, makes reaction occur in less space under the prerequisite not introducing negative impact, is more suitable for the reaction system of reaction substrate containing enzyme.Because reaction system can not work under the high temperature conditions, so use acrylic material instead to manufacture reactor, make reactor be easier to processing than conventional reactor, body structure is more strong.Have modified the feed liquor direction of reaction solution simultaneously, significantly reduce the difference in length between water influent pipeline compared with conventional reactor, promote the precision of feed liquor system.
Accompanying drawing explanation
Fig. 1 is one-piece construction schematic diagram of the present utility model.
Fig. 2 is the vertical view of Fig. 1.
Fig. 3 is the structural representation of the utility model intermediate plate;
Fig. 4 is running status schematic diagram of the present utility model.
Wherein, 1-casing, 2-reaction cabin, 3-intermediate plate, 4-tube stub I, 5-tube stub II, 6-tube stub III, 7-reaction solution pump into hole, 8-reaction solution taphole, 9-water hole.
Embodiment
To develop simultaneously embodiment below in conjunction with accompanying drawing, the utility model is described in detail.
As shown in Figure 1, the utility model provides the small size open type reactor that a kind of enzyme participates in chemical oscillation, comprises casing 1, reaction cabin 2, intermediate plate 3, tube stub I 4, tube stub II 5 and tube stub III 6;
Wherein, described casing 1 is the rectangular vessel of open-top, and the size of its length, width and height is 70mm, and the outer wall of casing is provided with tube stub I 4, tube stub II 5 and tube stub III 6 connecting hole;
Described reaction cabin 2 is cylinder type hollow housing and both ends open, and its one end is fixedly connected with the upper surface of intermediate plate 3, and the other end is for laying the plug of fixed electorde;
As shown in Figures 2 and 3, the described profile of intermediate plate 3 is consistent with the orthographicprojection of the interior shape of casing, the thickness of intermediate plate 3 is 6mm, one side end face is processed with reaction solution and pumps into hole 7, its aperture is 2mm, described reaction solution pumps into hole 7 extends to the middle part of intermediate plate 3 perpendicular to this side end face after and passes forming reactions liquid taphole 8 with 90 ° of angles from the upper surface of intermediate plate 3, described intermediate plate 3 is also processed with the water hole 9 running through its thickness direction;
Its integrated connection closes: described intermediate plate 3 level is fixedly connected on the inwall of casing 1, intermediate plate 3 is processed with the outside that one end that reaction solution pumps into hole 7 is positioned at casing, the interior separation of casing is become upper and lower two cavitys by intermediate plate 3, described reaction cabin 2 is vertically fixed on the upper surface of intermediate plate 3 and reaction solution taphole 8 is fully enclosed in its inside, described tube stub I 4, tube stub II 5 and tube stub III 6 are connected with the tube stub connecting hole on casing 1 respectively, tube stub II 5 is positioned at the cavity below intermediate plate 3, tube stub I 4 is positioned at the cavity above intermediate plate, tube stub III 6 is positioned at the cavity above intermediate plate and runs through reaction cabin 2 simultaneously.
The material of described casing 1, reaction cabin 2 and intermediate plate 3 adopts acrylic glass.
Principle of work: as shown in Figure 4, first water-bath is opened during use, thermostat(t)ed water enters the cavity below intermediate plate 3 by tube stub II 5, then the cavity above intermediate plate is entered by the water hole 9 on intermediate plate 3, discharge finally by tube stub I 4, reaction cabin 2 is remained on a constant temp by thermostat(t)ed water; Pump into hole 7 from the reaction solution of intermediate plate 3 subsequently and pump into reaction solution, it is inner that reaction solution enters reaction cabin 2 by reaction solution taphole 8, reaction solution stirs through magnetic stir bar in reaction zone and reacts, and the electrode of insertion collects signal, and waste liquid flows out casing 1 naturally by tube stub III 6.
In sum, these are only preferred embodiment of the present utility model, be not intended to limit protection domain of the present utility model.All within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (3)
1. enzyme participates in the small size open type reactor of chemical oscillation, it is characterized in that, comprises casing (1), reaction cabin (2), intermediate plate (3) and three tube stubs;
Wherein, the container that described casing (1) is open-top, the outer wall of casing is provided with three tube stub connecting holes;
Described reaction cabin (2) is for cylinder type hollow housing and both ends open;
The profile of described intermediate plate (3) is consistent with the orthographicprojection of the interior shape of casing, one side end face is processed with reaction solution and pumps into hole (7), described reaction solution pumps into hole (7) extends to the middle part of intermediate plate (3) perpendicular to this side end face after and passes forming reactions liquid taphole (8) with 90 ° of angles from the upper surface of intermediate plate (3), described intermediate plate (3) is also processed with the water hole (9) running through its thickness direction;
Its integrated connection closes: described intermediate plate (3) level is fixedly connected on the inwall of casing (1), intermediate plate (3) is processed with the outside that one end that reaction solution pumps into hole (7) is positioned at casing, the interior separation of casing is become upper and lower two cavitys by intermediate plate (3), described reaction cabin (2) is vertically fixed on the upper surface of intermediate plate (3) and reaction solution taphole (8) is fully enclosed in its inside, described three tube stubs are connected with the tube stub connecting hole on casing (1) respectively, one of them tube stub is positioned at the cavity of intermediate plate (3) below, a cavity be positioned at above intermediate plate, last is positioned at the cavity above intermediate plate and runs through reaction cabin (2) simultaneously.
2. a kind of enzyme as claimed in claim 1 participates in the small size open type reactor of chemical oscillation, it is characterized in that, the material of described casing (1), reaction cabin (2) and intermediate plate (3) adopts acrylic glass.
3. a kind of enzyme as claimed in claim 1 participates in the small size open type reactor of chemical oscillation, and it is characterized in that, profile and the inner chamber of described casing (1) are rectangle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520433949.0U CN204824845U (en) | 2015-06-23 | 2015-06-23 | Chemical oscillation's small -size open reactor is participated in to enzyme |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520433949.0U CN204824845U (en) | 2015-06-23 | 2015-06-23 | Chemical oscillation's small -size open reactor is participated in to enzyme |
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| Publication Number | Publication Date |
|---|---|
| CN204824845U true CN204824845U (en) | 2015-12-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520433949.0U Expired - Fee Related CN204824845U (en) | 2015-06-23 | 2015-06-23 | Chemical oscillation's small -size open reactor is participated in to enzyme |
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| CN (1) | CN204824845U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110121549A (en) * | 2016-07-29 | 2019-08-13 | 朱诺治疗学股份有限公司 | Bioreactor console |
-
2015
- 2015-06-23 CN CN201520433949.0U patent/CN204824845U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110121549A (en) * | 2016-07-29 | 2019-08-13 | 朱诺治疗学股份有限公司 | Bioreactor console |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151202 Termination date: 20190623 |