CN205145659U - Quick solution crystallizer - Google Patents
Quick solution crystallizer Download PDFInfo
- Publication number
- CN205145659U CN205145659U CN201520958565.0U CN201520958565U CN205145659U CN 205145659 U CN205145659 U CN 205145659U CN 201520958565 U CN201520958565 U CN 201520958565U CN 205145659 U CN205145659 U CN 205145659U
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- China
- Prior art keywords
- crystallizing tank
- crystallizer
- drain pipe
- crystallization
- shaft
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Abstract
The utility model discloses a quick solution crystallizer, including inlet pipe, crystallizer, high -order liquid alarm, cooler, (mixing) shaft, heater, filter screen, drain pipe, pump, back flow, level gauge and thermometer, the crystallizer top be equipped with the inlet pipe, crystallizer upper portion inner wall is equipped with high -order liquid alarm, crystallizer side wall mounting transparency glass plate, the crystallizer inner wall is equipped with the cooler, be equipped with the (mixing) shaft in the crystallizer, install rotating vane on the (mixing) shaft, crystallization tank bottom end inner wall is equipped with the heater, crystallization tank bottom end and drain pipe intercommunication, the drain pipe is equipped with the filter screen with the crystallizer junction, be equipped with the pump on the drain pipe, back flow one end is connected with the drain pipe, the back flow other end with be connected, be equipped with the thermometer on the crystallizer, you are equipped with the level gauge crystallizer. The utility model discloses increase the speed of solution crystallization, increase the speed of crystallization and the crystal purity that the crystallization goes out, simple structure, convenient to use does benefit to the popularization.
Description
Technical field
The utility model relates to a kind of chemical industry equipment, specifically a kind of fast solutions crystallizer.
Background technology
Chemical industry equipment comprises in all chemical machinery Dou Shi chemical plants of chemical industry equipment the instrument realizing Chemical Manufacture and adopt.The normal operation of chemical products production process, the control of product quality and output and guarantee, be unable to do without adaptation and the normal operation of various chemical industry equipment.The apolegamy of chemical industry equipment must pass through and calculates the detail of whole chemical process, design, processes, manufactures and match, and adapt to required for Chemical Manufacture.Wherein solution crystallization device is the important component part of chemical industry equipment.The type of existing solution crystallization device is a lot, and the method obtaining hypersaturated state by solution can divide crystallizing evaporator and cooler crystallizer; Can decomposition mother solution circulation crystallization device and magma circulation crystallization device by the type of flow; Continuous crystalizer and periodic crystallisation device can be divided by mode of operation.But the general crystalline rate of existing solution crystallization device is slow, and operating efficiency is low.
Utility model content
The purpose of this utility model is to provide a kind of fast solutions crystallizer, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
A kind of fast solutions crystallizer, comprise feed pipe, crystallizing tank, high-order level alarm device, cooler, shaft, heater, filter screen, drain pipe, pump, return duct, liquid level gauge and thermometer, described crystallizing tank top is provided with feed pipe, crystallizing tank upper inside wall is provided with high-order level alarm device, crystallizing tank sidewall installs transparency glass plate, crystallizing tank inwall is provided with cooler, shaft is provided with in crystallizing tank, shaft installs rotating vane, crystallizing tank bottom inwall is provided with heater, crystallizing tank bottom is communicated with drain pipe, drain pipe and crystallizing tank junction are provided with filter screen, drain pipe is provided with pump, return duct one end is connected with drain pipe, the return duct other end be connected, crystallizing tank is provided with thermometer, crystallizing tank you be provided with liquid level gauge.
As further program of the utility model: described feed pipe is provided with control valve.
As the utility model further scheme: described crystallizing tank top is provided with evaporation apertures.
Compared with prior art, the beneficial effects of the utility model are: in the utility model control valve control feed pipe, saturated solution enters, when the too much alarm of solution in crystallizing tank, solution is avoided to overflow, the crystallization situation seen timely in crystallizing tank can be known by transparency glass plate, saturated solution is at the effect borehole cooling crystallize out of cooler, under the stirring of shaft and rotating vane, accelerate the heat exchange of solution in crystallizing tank simultaneously, increase the speed of solution crystallization, when after solution crystallize out, by pump and drain pipe, solution in crystallizing tank is discharged, the crystal floccule of separating out is stayed in crystallizing tank under the stop of filter screen, heater is again to the mixture heating evaporation stayed in crystallizing tank, volatilize moisture wherein, the crystal purity that the speed of increase crystallization and crystallization go out, the solution that drain pipe is discharged is got back in feed pipe by return duct and is continued crystallization, also can directly discharge, thermometer detects temperature in crystallizing tank at any time, the number of solution in crystallizing tank monitored at any time by liquid level gauge, evaporation apertures is beneficial to evaporation, accelerate crystalline rate, structure is simple, easy to use, be beneficial to popularization.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of fast solutions crystallizer.
In figure: 1, feed pipe, 2, control valve, 3, crystallizing tank, 4, high-order level alarm device, 5, transparency glass plate, 6, cooler, 7, shaft, 8, rotating vane, 9, heater, 10, filter screen, 11, drain pipe, 12, pump, 13, return duct, 14, liquid level gauge, 15, evaporation apertures, 16, thermometer.
Detailed description of the invention
Be described in more detail below in conjunction with the technical scheme of detailed description of the invention to this patent.
Refer to Fig. 1, a kind of fast solutions crystallizer, comprise feed pipe 1, crystallizing tank 3, high-order level alarm device 4, cooler 6, shaft 7, heater 9, filter screen 10, drain pipe 11, pump 12, return duct 13, liquid level gauge 14 and thermometer 16, described crystallizing tank 3 top is provided with feed pipe 1, feed pipe 1 is provided with control valve 2, control valve 2 controls entering of saturated solution in feed pipe 1, crystallizing tank 3 upper inside wall is provided with high-order level alarm device 4, when the too much alarm of solution in crystallizing tank 3, solution is avoided to overflow, crystallizing tank 3 sidewall installs transparency glass plate 5, the crystallization situation seen timely in crystallizing tank 3 can be known by transparency glass plate 5, crystallizing tank 3 inwall is provided with cooler 6, shaft 7 is provided with in crystallizing tank 3, shaft 7 is installed rotating vane 8, shaft 7 is connected with external motor, saturated solution is at the effect borehole cooling crystallize out of cooler 6, under the stirring of shaft 7 and rotating vane 8, accelerate the heat exchange of solution in crystallizing tank 3 simultaneously, increase the speed of solution crystallization, crystallizing tank 3 bottom inwall is provided with heater 9, crystallizing tank 3 bottom is communicated with drain pipe 11, drain pipe 11 and crystallizing tank 3 junction are provided with filter screen 10, drain pipe 11 is provided with pump 12, return duct 13 one end is connected with drain pipe 11, return duct 13 other end is connected with 1, when after solution crystallize out, by pump 12 and drain pipe 11, solution in crystallizing tank 3 is discharged, the crystal floccule of separating out is stayed in crystallizing tank 3 under the stop of filter screen 10, heater 9 is again to the mixture heating evaporation stayed in crystallizing tank 3, volatilize moisture wherein, the crystal purity that the speed of increase crystallization and crystallization go out, the solution that drain pipe 11 is discharged is got back in feed pipe 1 by return duct 13 and is continued crystallization, also can directly discharge, crystallizing tank 3 is provided with thermometer 16, thermometer 16 detects temperature in crystallizing tank 3 at any time, crystallizing tank 3 you be provided with liquid level gauge 14, the number of solution in crystallizing tank 3 monitored at any time by liquid level gauge 14, crystallizing tank 3 top is provided with evaporation apertures 15, evaporation apertures 15 is beneficial to evaporation, accelerate crystalline rate.
Operation principle of the present utility model is: in the utility model control valve control feed pipe, saturated solution enters, when the too much alarm of solution in crystallizing tank, solution is avoided to overflow, the crystallization situation seen timely in crystallizing tank can be known by transparency glass plate, saturated solution is at the effect borehole cooling crystallize out of cooler, under the stirring of shaft and rotating vane, accelerate the heat exchange of solution in crystallizing tank simultaneously, increase the speed of solution crystallization, when after solution crystallize out, by pump and drain pipe, solution in crystallizing tank is discharged, the crystal floccule of separating out is stayed in crystallizing tank under the stop of filter screen, heater is again to the mixture heating evaporation stayed in crystallizing tank, volatilize moisture wherein, the crystal purity that the speed of increase crystallization and crystallization go out, the solution that drain pipe is discharged is got back in feed pipe by return duct and is continued crystallization, also can directly discharge, thermometer detects temperature in crystallizing tank at any time, the number of solution in crystallizing tank monitored at any time by liquid level gauge, evaporation apertures is beneficial to evaporation, accelerate crystalline rate.
Above the better embodiment of this patent is explained in detail, but this patent is not limited to above-mentioned embodiment, in the ken that one skilled in the relevant art possesses, can also makes a variety of changes under the prerequisite not departing from this patent aim.
Claims (3)
1. a fast solutions crystallizer, comprise feed pipe, crystallizing tank, high-order level alarm device, cooler, shaft, heater, filter screen, drain pipe, pump, return duct, liquid level gauge and thermometer, it is characterized in that, described crystallizing tank top is provided with feed pipe, crystallizing tank upper inside wall is provided with high-order level alarm device, crystallizing tank sidewall installs transparency glass plate, crystallizing tank inwall is provided with cooler, shaft is provided with in crystallizing tank, shaft installs rotating vane, crystallizing tank bottom inwall is provided with heater, crystallizing tank bottom is communicated with drain pipe, drain pipe and crystallizing tank junction are provided with filter screen, drain pipe is provided with pump, return duct one end is connected with drain pipe, the return duct other end be connected, crystallizing tank is provided with thermometer, crystallizing tank you be provided with liquid level gauge.
2. a kind of fast solutions crystallizer according to claim 1, it is characterized in that, described feed pipe is provided with control valve.
3. a kind of fast solutions crystallizer according to claim 1, is characterized in that, described crystallizing tank top is provided with evaporation apertures.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520958565.0U CN205145659U (en) | 2015-11-27 | 2015-11-27 | Quick solution crystallizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520958565.0U CN205145659U (en) | 2015-11-27 | 2015-11-27 | Quick solution crystallizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205145659U true CN205145659U (en) | 2016-04-13 |
Family
ID=55681403
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520958565.0U Expired - Fee Related CN205145659U (en) | 2015-11-27 | 2015-11-27 | Quick solution crystallizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205145659U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106730977A (en) * | 2016-12-13 | 2017-05-31 | 顾马飞 | A kind of syrup solution quick solidification apparatus |
| CN107126724A (en) * | 2017-06-01 | 2017-09-05 | 杨露萍 | A kind of chemical engineering experiment efficient crystallization device |
| CN113638394A (en) * | 2021-09-10 | 2021-11-12 | 连云港徐圩城建工程有限公司 | Coastal beach salinized soil improvement device and improvement method |
-
2015
- 2015-11-27 CN CN201520958565.0U patent/CN205145659U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106730977A (en) * | 2016-12-13 | 2017-05-31 | 顾马飞 | A kind of syrup solution quick solidification apparatus |
| CN107126724A (en) * | 2017-06-01 | 2017-09-05 | 杨露萍 | A kind of chemical engineering experiment efficient crystallization device |
| CN113638394A (en) * | 2021-09-10 | 2021-11-12 | 连云港徐圩城建工程有限公司 | Coastal beach salinized soil improvement device and improvement 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: 20160413 Termination date: 20161127 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |