CN204767554U - Crystallizer - Google Patents

Crystallizer Download PDF

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Publication number
CN204767554U
CN204767554U CN201520347851.3U CN201520347851U CN204767554U CN 204767554 U CN204767554 U CN 204767554U CN 201520347851 U CN201520347851 U CN 201520347851U CN 204767554 U CN204767554 U CN 204767554U
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CN
China
Prior art keywords
casing
rotating shaft
cooling
crystallizer
communicated
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
Application number
CN201520347851.3U
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Chinese (zh)
Inventor
徐堃
顾汉章
戴红梅
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JIANGSU HAN KUANG BIOLOGICAL ENGINEERING Co Ltd
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JIANGSU HAN KUANG BIOLOGICAL ENGINEERING Co Ltd
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Priority to CN201520347851.3U priority Critical patent/CN204767554U/en
Application granted granted Critical
Publication of CN204767554U publication Critical patent/CN204767554U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model relates to a crystallizer belongs to fractional crystallization technical field. This crystallizer includes frame, motor, pivot and casing, and the casing is fixed in the frame, and the pivot runs through the casing setting, and the motor is close to the setting of pivot one end and is used for driving the pivot rotation, and the outside parcel of casing has the cover of clamp, and the casing inner wall is equipped with at least one and presss from both sides the hollow cooling slab of cover intercommunication, and hollow cooling slab is perpendicular with the casing inner wall, is equipped with agitating unit in the pivot. Through pressing from both sides cover and hollow jointly use of cooling off the slab, make material and a large amount of cooling surfaces fully contact, the cooling is rapidly to the all space of crystallization built -in have the cooling surface nearby, do not have the cooling dead angle, make the crystallization of material very even.

Description

A kind of crystallizer
Technical field
The utility model relates to a kind of crystallizer, belongs to fractional crystallization technical field.
Background technology
A kind of trough-shaped container of crystallizer, wall is provided with chuck or device built with coiled pipe, in order to solution in heating or cooling bath.Crystallization tank can be used as crystallizing evaporator or cooler crystallizer.For improving crystal production intensity, agitator can be set up in groove.Crystallization tank can be used for continued operation or intermittently operated.The crystal that intermittently operated obtains is comparatively large, but crystal is easily linked to be druse, entrainment mother liquor, affects product purity.This mold structure is simple, and production intensity is lower, is applicable to the production of be pilot (as chemical reagent and biochemical reagents etc.).The type of crystallizer 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 (i.e. the mixture of mother liquor and crystal) circulation crystallization device by the type of flow; Continuous crystalizer and periodic crystallisation device can be divided by mode of operation.
The crystallizer of current domestic application is owing to adopting chuck cooling, and crystallization, first from still wall, makes crystalline thing first tie at still wall, can form thick crystalline thing, greatly affect heat transfer efficiency time serious on still wall.Though the method by improving speed of agitator reduces the problem of crystalline thing knot wall on still wall, but paddle is generally difficult to accomplish that scraping wall stirs, under a lot of situation, crystallization is also subject to the restriction of speed of agitator, speed of agitator is too fast, size of microcrystal can be made greatly to reduce, affect next step filtration washing operation.Crystallization kettle is often better near external refrigeration still wall crystallization effect, and the material crystallization at close still center is very slow, and cause crystal grain uneven, overall crystallization rate is very slow.In addition, higher for material concentration, the crystallization kettle that crystalline solid is more, often discharge is not thorough, and partially crystallizable solid can remain in row in still and not go out, and affects output and energy consumption.
Utility model content
The technical problems to be solved in the utility model is, not enough for prior art, proposes a kind of crystallizer of good cooling results.
The utility model is the technical scheme solving the problems of the technologies described above proposition: a kind of crystallizer, comprise frame, motor, rotating shaft and housing, described casing is fixed in frame, described rotating shaft runs through casing and arranges, described motor arranges near rotating shaft one end and is used for drive shaft rotation, described hull outside is enclosed with chuck, described casing inner wall is provided with at least one hollow cooling plate be communicated with described chuck, described hollow cooling plate is vertical with described casing inner wall, and described rotating shaft is provided with agitating device.
The improvement of technique scheme is: described frame is also provided with cooling water tank, and described cooling water tank to be communicated with described chuck by pipeline and to form loop, is provided with water pump in described cooling water tank.
The improvement of technique scheme is: described agitating device and described hollow cooling sheet contacts, described agitating device is screw propulsion shape.
The improvement of technique scheme is: described casing one end is communicated with feed pipe, and described feed pipe is provided with inlet valve.
The improvement of technique scheme is: described casing is communicated with discharge nozzle away from one end of feed pipe, and described discharge nozzle is communicated with material collecting barrel.
The improvement of technique scheme is: be shaft end seal between described rotating shaft two ends and housing.
The improvement of technique scheme is: described motor is connected with described rotating shaft by shaft coupling.
The improvement of technique scheme is: be also provided with gearbox between described motor and rotating shaft.
The improvement of technique scheme is: described frame bottom is also provided with feet, and described feet is enclosed with rubber.
The utility model adopts the beneficial effect of technique scheme to be: (1) is by the conbined usage of chuck and hollow cooling plate, material is fully contacted with a large amount of cooling surfaces, cooling rapidly, and space intervals all in crystallizer has cooling surface nearby, without cooling dead angle, make the crystallization of material very even; (2) due to agitating device and described hollow cooling sheet contacts, wall effect clearly can be played, prevent from forming crystallizing layer at hollow cooling plate, cooling effectiveness is improved greatly; (3) because agitating device is screw propulsion shape, also gearbox is provided with between motor and rotating shaft, entered from one end by the material of crystallization, and slowly pushed ahead to other end overflow discharge by full of twists and turns, material is fully contacted with a large amount of cooling surfaces, rapid cooling, can control arbitrarily speed of agitator and crystallization rate, obtain desirable crystal particle diameter; (4) because feet is enclosed with rubber, good damping effect.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the utility model is described in further detail:
Fig. 1 is the structural representation of the utility model embodiment crystallizer.
Number in the figure is schematically as follows: 1-frame; 2-motor; 3-gearbox; 4-chuck; 5-inlet valve; 6-agitating device; The hollow cooling plate of 7-; 8-rotating shaft; 9-discharge nozzle; 10-material collecting barrel; 11-cooling water tank; 12-feet.
Detailed description of the invention
Embodiment one
The crystallizer of the present embodiment comprises frame 1, motor 2, rotating shaft 8 and housing, casing is fixed in frame 1, and casing one end is communicated with feed pipe, and feed pipe is provided with inlet valve 5, casing is communicated with discharge nozzle 9 away from one end of feed pipe, and discharge nozzle 9 is communicated with material collecting barrel 10.Rotating shaft 8 runs through casing and arranges, and is shaft end seal between rotating shaft 8 two ends and housing.Motor 2 is arranged near rotating shaft 8 one end, motor 2 is connected with rotating shaft 8 by shaft coupling, motor 2 rotates for drive shaft 8, hull outside is enclosed with chuck 4, casing inner wall is interval with the hollow cooling plate 7 be communicated with chuck 4, and hollow cooling plate 7 is vertical with casing inner wall, and rotating shaft 8 is provided with agitating device 6, agitating device 6 contacts with hollow cooling plate 7, and agitating device 6 is screw propulsion shape.Frame 1 is also provided with cooling water tank 11, and cooling water tank 11 to be communicated with chuck 4 by pipeline and to form loop, is provided with water pump in cooling water tank 11.Frame 1 bottom is also provided with feet 12, and feet 12 is enclosed with rubber.
During crystallizer work, motor 2 starts, and drives rotating shaft 8 to rotate, pump working in cooling water tank 11, sent in chuck 4 and hollow cooling plate 7 by pipeline by cooling water and form circulation, meanwhile, inlet valve 5 is opened, entered from one end by the material of crystallization, and be stirred device 6 full of twists and turns slowly push ahead other end overflow discharge, material is fully contacted with a large amount of cooling surfaces, cools rapidly, obtain crystal, the material after crystallization enters material collecting barrel 10 by discharge nozzle 9.
Embodiment two
The crystallizer of the present embodiment is roughly the same with the crystallizer of embodiment one, and difference is also to be provided with gearbox 3 between motor 2 and rotating shaft 8.
During crystallizer work, the rotating speed of rotating shaft 8 can be controlled by gearbox 3, thus control material crystallization rate, obtain desirable crystal particle diameter.
The utility model is not limited to above-described embodiment.All employings are equal to the technical scheme of replacing and being formed, and all drop on the protection domain of the utility model requirement.

Claims (9)

1. a crystallizer, comprise frame, motor, rotating shaft and housing, it is characterized in that: described casing is fixed in frame, described rotating shaft runs through casing and arranges, described motor arranges near rotating shaft one end and is used for drive shaft rotation, and described hull outside is enclosed with chuck, and described casing inner wall is provided with at least one hollow cooling plate be communicated with described chuck, described hollow cooling plate is vertical with described casing inner wall, and described rotating shaft is provided with agitating device.
2. crystallizer according to claim 1 is characterized in that: described frame is also provided with cooling water tank, and described cooling water tank to be communicated with described chuck by pipeline and to form loop, is provided with water pump in described cooling water tank.
3. crystallizer according to claim 2 is characterized in that: described agitating device and described hollow cooling sheet contacts, described agitating device is screw propulsion shape.
4. crystallizer according to claim 3 is characterized in that: described casing one end is communicated with feed pipe, and described feed pipe is provided with inlet valve.
5. crystallizer according to claim 4 is characterized in that: described casing is communicated with discharge nozzle away from one end of feed pipe, and described discharge nozzle is communicated with material collecting barrel.
6. crystallizer according to claim 5 is characterized in that: be shaft end seal between described rotating shaft two ends and housing.
7. crystallizer according to claim 6 is characterized in that: described motor is connected with described rotating shaft by shaft coupling.
8. crystallizer according to claim 7 is characterized in that: be also provided with gearbox between described motor and rotating shaft.
9. crystallizer according to claim 8 is characterized in that: described frame bottom is also provided with feet, and described feet is enclosed with rubber.
CN201520347851.3U 2015-05-27 2015-05-27 Crystallizer Expired - Fee Related CN204767554U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520347851.3U CN204767554U (en) 2015-05-27 2015-05-27 Crystallizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520347851.3U CN204767554U (en) 2015-05-27 2015-05-27 Crystallizer

Publications (1)

Publication Number Publication Date
CN204767554U true CN204767554U (en) 2015-11-18

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520347851.3U Expired - Fee Related CN204767554U (en) 2015-05-27 2015-05-27 Crystallizer

Country Status (1)

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CN (1) CN204767554U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106237650A (en) * 2016-08-20 2016-12-21 姜向前 A kind of batch (-type) quickly cools down crystallization in motion tank
CN108339289A (en) * 2018-04-20 2018-07-31 上海涛川能源科技有限公司 A kind of the centrifugation rotation crystallizer and recovery tower of high efficiente callback carbon dioxide
CN115304081A (en) * 2022-09-14 2022-11-08 优利德(江苏)化工有限公司 Preparation method and device of electronic-grade potassium hydroxide

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106237650A (en) * 2016-08-20 2016-12-21 姜向前 A kind of batch (-type) quickly cools down crystallization in motion tank
CN108339289A (en) * 2018-04-20 2018-07-31 上海涛川能源科技有限公司 A kind of the centrifugation rotation crystallizer and recovery tower of high efficiente callback carbon dioxide
CN115304081A (en) * 2022-09-14 2022-11-08 优利德(江苏)化工有限公司 Preparation method and device of electronic-grade potassium hydroxide
CN115304081B (en) * 2022-09-14 2024-03-01 优利德(江苏)化工有限公司 Preparation method and device of electronic-grade potassium hydroxide

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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: 20151118

Termination date: 20180527

CF01 Termination of patent right due to non-payment of annual fee