CN203829688U - Liquid level adjusting crystallization kettle - Google Patents
Liquid level adjusting crystallization kettle Download PDFInfo
- Publication number
- CN203829688U CN203829688U CN201420191055.0U CN201420191055U CN203829688U CN 203829688 U CN203829688 U CN 203829688U CN 201420191055 U CN201420191055 U CN 201420191055U CN 203829688 U CN203829688 U CN 203829688U
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- China
- Prior art keywords
- baffle plate
- buoy
- bridge
- floating lever
- crystallization kettle
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model belongs to the field of acid plants and particularly relates to a liquid level adjusting crystallization kettle. The liquid level adjusting crystallization kettle comprises an evaporator, a crystallization kettle body, a flow guide funnel, a flow guide pipe, an exhaust pipe, a heat exchanger, a recirculating pipe, a circulating outflow pipe, a circulating pump, a base, a condensate water opening, a steam inlet, a screen cloth separator, a baffle A, a baffle B, a feed liquid inlet, a rotating wheel, an expansion pad A, an expansion pad B, a buoy A, a buoy B, a floating lever A, a floating lever B, a bar frame A, a bar frame B, a crystallization outlet and a steam outlet. The flow guide funnel is arranged on the crystallization kettle body. The flow guide pipe is arranged below the flow guide funnel. The evaporator is arranged on the flow guide funnel. One end of the exhaust pipe is connected with the evaporator, and the other end of the exhaust pipe is connected with the crystallization kettle body. The flow guide pipe, the baffle A, the baffle B, the rotating wheel, the expansion pad A, the expansion pad B, the buoy A, the buoy B, the floating lever A, the floating lever B, the bar frame A and the bar frame B are arranged in the crystallization kettle body.
Description
Technical field
The utility model belongs to pickler field, relates in particular to a kind of liquid level and regulates crystallization kettle.
[
background technology]
Industrial crystallization equipment mainly divides two kinds of cooled and vaporation-types, and the latter divides atmospheric evaporation formula and vacuum evaporation type according to evaporation operation pressure again.Because vacuum evaporation efficiency is higher, so vaporation-type crystallizer be take vacuum evaporation as main.The crystallization of specific objective product specifically selects the crystallizer of which kind of type mainly according to the solubility curve of target product, to determine.If the solubility with temperature of target product raises and enlarges markedly, can adopt cooling knot product device or evaporation knot product device, otherwise can only select evaporation type knot product device.
The cooling raio surface area of internal-circulation type crystallizer is less, and knot product speed is lower, is unsuitable for extensive crystallization operation.In addition, because the temperature of knot product wall is minimum, so solution degree of supersaturation is maximum. on wall, easily form brilliant dirt, affect heat transfer efficiency.Outer circulation type crystallizer is cooling by external heat exchanger, due to forced circulation, and solution high velocity stream over-heat-exchanger surface, less by the solution temperature difference of heat exchanger, heat-exchanger surface is difficult for formation product dirt, and exchange efficiency is higher, can long period continuous operation; But must select suitable circulating pump, in order to avoid the wearing and tearing of suspension product body are broken.Saturated solution is logical people from crystallizer bottom, crystallization in the mobile process that makes progress, the downward sedimentation of crystal of separating out.Because bottom flow velocity is higher, only have bulky grain crystal can be deposited to bottom and discharge.Employing chuck is cooling, and the volume of knot product device is less, is applicable to produce continuously on a small scale.
Crystallizing evaporator forms by tying product device main body, vaporization chamber and external heater.Solution is sent into vaporization chamber evaporation and concentration after outer loop heating, reaches hypersaturated state, by centre pipe, drops in crystalline growth groove.In knot product growths groove, the fluid crystallization mobile time that makes progress is constantly grown, and large particle crystal generation sedimentation, discharges product magma (mixture of crystal and solution is called magma) from bottom.Vaporization chamber is connected with vavuum pump, can carries out vacuum insulation evaporation.
Summary of the invention
The utility model provides a kind of liquid level to regulate crystallization kettle, to solve the problem of the crystallization kettle liquid level adjusting proposing in above-mentioned background technology.
The technical problem that the utility model solves realizes by the following technical solutions: the utility model provides a kind of liquid level to regulate crystallization kettle, it is characterized in that: comprise evaporimeter, crystallization kettle, water conservancy diversion bucket, mozzle, blast pipe, heat exchanger, recirculation pipe, circulation effuser, circulating pump, base, the condensation mouth of a river, steam inlet, screen separators, baffle plate A, baffle plate B, feed liquid entrance, runner, expansion pad A, expansion pad B, buoy A, buoy B, floating lever A, floating lever B, bridge A, bridge B, crystallization outlet, steam (vapor) outlet, described water conservancy diversion bucket is on described crystallization kettle, described mozzle is below described water conservancy diversion bucket, described evaporimeter is on described water conservancy diversion bucket, one end of described blast pipe connects described evaporimeter, the other end of described blast pipe connects described crystallization kettle, described blast pipe is on the side of described water conservancy diversion bucket, described crystallization outlet is on the side of described crystallization kettle, described crystallization outlet is below described blast pipe, one end of described recirculation pipe connects described evaporimeter, and the other end of described recirculation pipe connects described heat exchanger, the described condensation mouth of a river, steam inlet is on described heat exchanger, described steam inlet is on the described condensation mouth of a river, described circulation effuser is below described recirculation pipe, described feed liquid entrance is on described circulation effuser, one end of described circulation effuser connects described crystallization kettle, the other end of described circulation effuser connects described heat exchanger, described base is below described heat exchanger, described circulating pump is on described base, described circulating pump is on the side of described circulation effuser, described circulating pump connects described circulation effuser, described steam (vapor) outlet is on described evaporimeter, described screen separators is on the top of described evaporimeter, described mozzle, baffle plate A, baffle plate B, runner, expansion pad A, expansion pad B, buoy A, buoy B, floating lever A, floating lever B, bridge A, bridge B is in the inside of described crystallization kettle, described baffle plate A, baffle plate B, bridge A, bridge B is in the bottom of described crystallization kettle, described baffle plate A, baffle plate B connects described mozzle, described bridge A, bridge B is at described baffle plate A, between baffle plate B, described buoy A, buoy B is on the side of described mozzle, and described buoy A is at described water conservancy diversion bucket, between baffle plate B, described buoy B is at described water conservancy diversion bucket, between baffle plate A, described runner, expansion pad A, expansion pad B is in the inside of described mozzle, and described runner, on the top of described mozzle, has long tooth on described runner, short tooth, described expansion pad A, expansion pad B is below described runner, and described expansion pad A is on described baffle plate A, described expansion pad B on described baffle plate B, described floating lever A, floating lever B is on the side of described mozzle, and one end of described floating lever A connects described buoy A, and the other end of described floating lever A connects described bridge A, and one end of described floating lever B connects described buoy B, and the other end of described floating lever B connects described bridge B.
The length of described short tooth is half of length of described long tooth.
Described baffle plate A, baffle plate B etc. are large, and described expansion pad A, expansion pad B etc. are large, and described buoy A, buoy B etc. are large, and described floating lever A, floating lever B are isometric, and described bridge A, bridge B are isometric.
The beneficial effects of the utility model are:
1 buoy moves with the height change of liquid level, and buoy drives motion bar that bridge is moved, and liquid level declines, and buoy declines, and when bridge is closed, dope subsidence velocity is accelerated, and etc. liquid level, rises, and buoy rises, and bridge opens, and dope subsidence velocity slows down.
2 runners, with the short tooth of long tooth, can be controlled dope subsidence velocity and flow by rotation.
3 expansion pads are according to the solid content convergent-divergent of dope, also liquid level in adjustable crystallization kettle.
4 bridges are moved and can be contacted expansion pad by folding, also can control the use of expansion pad.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is described further:
In figure: 1-evaporimeter, 2-crystallization kettle, 3-water conservancy diversion bucket, 4-mozzle, 5-blast pipe, 6-heat exchanger, 7-recirculation pipe, 8-circulation effuser, 9-circulating pump, 10-base, the 11-condensation mouth of a river, 12-steam inlet, 13-screen separators, 14-baffle plate A, 15-baffle plate B, 16-feed liquid entrance, 17-runner, the long tooth of 18-, the short tooth of 19-, 20-expansion pad A, 21-expansion pad B, 22-buoy A, 23-buoy B, 24-floating lever A, 25-floating lever B, 26-bridge A, 27-bridge B, 28-crystallization outlet, 29-steam (vapor) outlet.
Embodiment:
The present embodiment comprises evaporimeter 1, crystallization kettle 2, water conservancy diversion bucket 3, mozzle 4, blast pipe 5, heat exchanger 6, recirculation pipe 7, circulation effuser 8, circulating pump 9, base 10, the condensation mouth of a river 11, steam inlet 12, screen separators 13, baffle plate A14, baffle plate B15, feed liquid entrance 16, runner 17, expansion pad A20, expansion pad B21, buoy A22, buoy B23, floating lever A24, floating lever B25, bridge A26, bridge B27, crystallization outlet 28, steam (vapor) outlet 29, water conservancy diversion bucket 3 is on crystallization kettle 2, and mozzle 4 is below water conservancy diversion bucket 3, and evaporimeter 1 is on water conservancy diversion bucket 3, one end of blast pipe 5 connects evaporimeter 1, the other end of blast pipe 5 connects crystallization kettle 2, and blast pipe 5 is on the side of water conservancy diversion bucket 3, and crystallization exports 28 sides at crystallization kettle 2, crystallization outlet 28 is below blast pipe 5, one end of recirculation pipe 7 connects evaporimeter 1, and the other end of recirculation pipe 7 connects heat exchanger 6, the condensation mouth of a river 11, steam inlet 12 is on heat exchanger 6, steam inlet 12 is on the condensation mouth of a river 11, circulation effuser 8 is below recirculation pipe 7, feed liquid entrance 16 is on circulation effuser 8, one end of circulation effuser 8 connects crystallization kettle 2, the other end of circulation effuser 8 connects heat exchanger 6, base 10 is below heat exchanger 6, circulating pump 9 is on base 10, circulating pump 9 is on the side of circulation effuser 8, and circulating pump 9 connects circulation effuser 8, and steam (vapor) outlet 29 is on evaporimeter 1, screen separators 13 is on the top of evaporimeter 1, mozzle 4, baffle plate A14, baffle plate B15, runner 17, expansion pad A20, expansion pad B21, buoy A22, buoy B23, floating lever A24, floating lever B25, bridge A26, bridge B27 is in the inside of crystallization kettle 2, baffle plate A14, baffle plate B15, bridge A26, bridge B 27 is in the bottom of crystallization kettle 2, baffle plate A14, baffle plate B15 connects mozzle 4, bridge A26, bridge B27 is at baffle plate A14, between baffle plate B15, buoy A22, buoy B23 is on the side of mozzle 4, and buoy A22 is at water conservancy diversion bucket 3, between baffle plate B15, buoy B23 is at water conservancy diversion bucket 3, between baffle plate A14, runner 17, expansion pad A20, expansion pad B21 is in the inside of mozzle 4, and runner 17, on the top of mozzle 4, has long tooth 18 on runner 17, short tooth 19, expansion pad A20, expansion pad B21 is below runner 17, and expansion pad A20 is on baffle plate A14, expansion pad B21 on baffle plate B15, floating lever A24, floating lever B25 is on the side of mozzle 4, and one end of floating lever A24 connects buoy A22, and the other end of floating lever A24 connects bridge A26, and one end of floating lever B25 connects buoy B23, and the other end of floating lever B25 connects bridge B27.
The length of short tooth 19 is half of length of long tooth 18.
Baffle plate A14, baffle plate B15 etc. are large, and expansion pad A20, expansion pad B21 etc. are large, and buoy A22, buoy B23 etc. are large, and floating lever A24, floating lever B25 are isometric, and bridge A26, bridge B27 are isometric.
Utilize technical scheme described in the utility model, or those skilled in the art being under the inspiration of technical solutions of the utility model, designs similar technical scheme, and reaching above-mentioned technique effect, is all to fall into protection domain of the present utility model.
Claims (3)
1. liquid level regulates a crystallization kettle, it is characterized in that: comprise evaporimeter, crystallization kettle, water conservancy diversion bucket, mozzle, blast pipe, heat exchanger, recirculation pipe, circulation effuser, circulating pump, base, the condensation mouth of a river, steam inlet, screen separators, baffle plate A, baffle plate B, feed liquid entrance, runner, expansion pad A, expansion pad B, buoy A, buoy B, floating lever A, floating lever B, bridge A, bridge B, crystallization outlet, steam (vapor) outlet, described water conservancy diversion bucket is on described crystallization kettle, described mozzle is below described water conservancy diversion bucket, described evaporimeter is on described water conservancy diversion bucket, one end of described blast pipe connects described evaporimeter, the other end of described blast pipe connects described crystallization kettle, described blast pipe is on the side of described water conservancy diversion bucket, described crystallization outlet is on the side of described crystallization kettle, described crystallization outlet is below described blast pipe, one end of described recirculation pipe connects described evaporimeter, and the other end of described recirculation pipe connects described heat exchanger, the described condensation mouth of a river, steam inlet is on described heat exchanger, described steam inlet is on the described condensation mouth of a river, described circulation effuser is below described recirculation pipe, described feed liquid entrance is on described circulation effuser, one end of described circulation effuser connects described crystallization kettle, the other end of described circulation effuser connects described heat exchanger, described base is below described heat exchanger, described circulating pump is on described base, described circulating pump is on the side of described circulation effuser, described circulating pump connects described circulation effuser, described steam (vapor) outlet is on described evaporimeter, described screen separators is on the top of described evaporimeter, described mozzle, baffle plate A, baffle plate B, runner, expansion pad A, expansion pad B, buoy A, buoy B, floating lever A, floating lever B, bridge A, bridge B is in the inside of described crystallization kettle, described baffle plate A, baffle plate B, bridge A, bridge B is in the bottom of described crystallization kettle, described baffle plate A, baffle plate B connects described mozzle, described bridge A, bridge B is at described baffle plate A, between baffle plate B, described buoy A, buoy B is on the side of described mozzle, and described buoy A is at described water conservancy diversion bucket, between baffle plate B, described buoy B is at described water conservancy diversion bucket, between baffle plate A, described runner, expansion pad A, expansion pad B is in the inside of described mozzle, and described runner, on the top of described mozzle, has long tooth on described runner, short tooth, described expansion pad A, expansion pad B is below described runner, and described expansion pad A is on described baffle plate A, described expansion pad B on described baffle plate B, described floating lever A, floating lever B is on the side of described mozzle, and one end of described floating lever A connects described buoy A, and the other end of described floating lever A connects described bridge A, and one end of described floating lever B connects described buoy B, and the other end of described floating lever B connects described bridge B.
2. a kind of liquid level according to claim 1 regulates crystallization kettle, it is characterized in that: the length of described short tooth is half of length of described long tooth.
3. a kind of liquid level according to claim 1 regulates crystallization kettle, it is characterized in that: described baffle plate A, baffle plate B etc. are large, described expansion pad A, expansion pad B etc. are large, and described buoy A, buoy B etc. are large, described floating lever A, floating lever B are isometric, and described bridge A, bridge B are isometric.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420191055.0U CN203829688U (en) | 2014-04-18 | 2014-04-18 | Liquid level adjusting crystallization kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420191055.0U CN203829688U (en) | 2014-04-18 | 2014-04-18 | Liquid level adjusting crystallization kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203829688U true CN203829688U (en) | 2014-09-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420191055.0U Expired - Fee Related CN203829688U (en) | 2014-04-18 | 2014-04-18 | Liquid level adjusting crystallization kettle |
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| Country | Link |
|---|---|
| CN (1) | CN203829688U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109173329A (en) * | 2018-10-31 | 2019-01-11 | 浙江新和成股份有限公司 | Device for evaporative crystallization |
-
2014
- 2014-04-18 CN CN201420191055.0U patent/CN203829688U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109173329A (en) * | 2018-10-31 | 2019-01-11 | 浙江新和成股份有限公司 | Device for evaporative crystallization |
| CN109173329B (en) * | 2018-10-31 | 2023-08-29 | 浙江新和成股份有限公司 | Device for evaporative crystallization |
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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: 20140917 Termination date: 20150418 |
|
| EXPY | Termination of patent right or utility model |