CN202802843U - Sediment type liquid dividing tank - Google Patents
Sediment type liquid dividing tank Download PDFInfo
- Publication number
- CN202802843U CN202802843U CN 201220297210 CN201220297210U CN202802843U CN 202802843 U CN202802843 U CN 202802843U CN 201220297210 CN201220297210 CN 201220297210 CN 201220297210 U CN201220297210 U CN 201220297210U CN 202802843 U CN202802843 U CN 202802843U
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- liquid outlet
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- tank body
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Abstract
The utility model discloses a sediment type liquid dividing tank. The sediment type liquid dividing tank comprises a tank body, a liquid inlet pipe, an upper liquid outlet, a lower liquid outlet and an exhaustion hole, wherein a partition wall and a top partition board are arranged crossly between an upper level of the tank body and a lower level of the tank body; an upper level of cavity body is communicated with a vertical separation tube in a lower level of cavity body by a horizontal tube; the bottom of each level of tank body is provided with hoppers and is connected with bottom pumping units with pump bodies by hoppers; the lower part of each level of tank body is provided with an outlet to be connected with an outer conveying tube; and the upper liquid outlet is positioned on the upper part of the final level of the tank body; and the lower liquid outlet is positioned among each level of cavity body of the tank body. The liquid dividing tank is precipitated in multiple levels, and mixed liquid is high in steady flow, so that the sedimentation condition of the bottom of the tank is reduced, and the tank is compact in structure and used for running water type separation of the mixed solution which can be layered in a sediment mode; and therefore, the sediment type liquid dividing tank is high in working efficiency.
Description
One, technical field
The utility model relates to a kind of liquid separating appts, is specially a kind of precipitating type separating box.
Two, background technology
Produce in the technique of cottonseed kernel protein at lixiviation process, first-selected to behind the cottonseed employing organic solvent lixiviate grease, obtain cottonseed kernel protein thereby adopt methyl alcohol to carry out dephenolize to cotton dregs.Wherein after the methyl alcohol dephenolize, need to separate mixed solution, in order to obtain organic solvent and methanol solution, be cycled to used in the processing of follow-up material.
Because immiscible property and the laminarity of organic solvent and methanol solution all are the separation of carrying out mixed solution with the precipitation method in cottonseed kernel protein technique usually.But the long period is wanted in the layering of common settling tank technology current stabilization, the one, need casing very large, the equipment of large volume not only cost increases but also needs larger installing space, and the 2nd, owing to be mixed with the solid impurity particle in the mother liquor, solution needs often to stop work cleaning in device bottom, has a strong impact on the production work efficiency.
Need especially the layering of a kind of energy High-rate sedimentation in the production practices, build is compact, and the cleaning frequency of stopping work is low, the separating box that the production work efficiency is high.
Three, summary of the invention
The purpose of this utility model is after a kind of dephenolize workshop section in cottonseed extraction production cottonseed kernel protein process will be provided, and mixed liquor is carried out the efficiency compact high liquid distributing device of fractional precipitation.
A kind of precipitating type separating box of the utility model, comprise casing, feed tube, the outlet of upper liquid, the outlet of lower liquid, steam vent, described casing is divided into multistage, be staggeredly equipped with partition wall and roof spacer between higher level and the subordinate, and the upper level cavity communicates with vertical separator tube in the next stage cavity by horizontal tube; The bottom of casings at different levels is designed to respectively funnel, and by this funnel with pump with the bottom of the pump housing pipe link to each other; Lower box at different levels set out mouth and link to each other with outer carrier pipe; Described upper liquid outlet is positioned at the top of casing afterbody, and lower liquid outlet lays respectively at the middle part of casing cavitys at different levels, and converges outside casing.
This precipitating type separating box multi stage precipitation, take full advantage of cabinet space, the mixed liquor current stabilization is fast, compact conformation, and the bottom arranges and pumps mechanism, particle impurity can be returned pump to the section of being filtered dry of dephenolizing process, has greatly alleviated bottom alluvial situation, the cleaning frequency reduces greatly, and the precipitate and separate work efficiency is higher.
Four, description of drawings
Fig. 1 is the cross-sectional view of this precipitating type separating box.
Five, the specific embodiment
Such as Fig. 1, this precipitating type separating box comprises casing 1, feed tube 6, upper liquid outlet 12, lower liquid outlet 4, steam vent 10, casing 1 is three grades, be staggeredly equipped with partition wall 3 and roof spacer 7 between higher level and the subordinate, and the upper level cavity communicates with vertical separator tube 8 in the next stage cavity by horizontal tube 5; The bottom of casings 1 at different levels is designed to respectively only have a side to the slope funnel 13 of downward-extension, and by funnel 13 with pump pipe with the bottom of the pump housing 10 and 11 link to each other; Lower box at different levels set out mouthfuls 14 and link to each other with outer carrier pipe 2; Described upper liquid outlet 12 is positioned at the top of casing 1 third level, and lower liquid outlet 4 lays respectively at the middle part of casing 1 cavitys at different levels, and converges outside casing 1.
After the mixing mother liquor enters first order cavity from feed tube 6, under the effect of partition wall 3 and dividing plate 7 by current stabilization step by step, in this process, organic solvent and part methyl alcohol enter vertical separator tube 8 in the next stage cavity by horizontal tube 5, carry out gravitational separation, the methyl alcohol that enters next stage reduces step by step, and organic solvent is concentrated to compile in the third level, and is transfused to preorder lixiviate workshop section by upper liquid outlet 12 and recycles.Methyl alcohol in the casings 1 at different levels flows out from lower liquid outlet 4, and converges outside casing 1 and be collected.The outlet 14 of lower box at different levels links to each other with outer carrier pipe 2, the mixing material that does not separate fully is conveyed into evaporation section carries out circulating and evaporating.Ramp type funnel 13 is pumped pipe 11 and is filtered dry into the dregs of rice through the section of being filtered dry that the pump housing 10 pressurizations are recycled to dephenolizing process sending into the bottom after the granule foreign precipitation.Alleviated bottom alluvial situation, the cleaning frequency reduces.Ramp type funnel 13 is more convenient for from a side pipeline and cleaning maintenance, the corresponding reduction of task difficulty being installed.
Claims (3)
1. precipitating type separating box, comprise casing (1), feed tube (6), upper liquid outlet (12), the outlet of lower liquid (4), steam vent (10), it is characterized in that described casing (1) is divided into multistage, be staggeredly equipped with partition wall (3) and roof spacer (7) between higher level and the subordinate, and the upper level cavity communicates with vertical separator tube (8) in the next stage cavity by horizontal tube (5); The bottom of casings at different levels (1) is designed to respectively funnel (13), and by this funnel (13) with pump pipe (11) with the bottom of the pump housing (10) and link to each other; Lower box at different levels set out mouthful (14) and link to each other with outer carrier pipe (2); Described upper liquid outlet (12) is positioned at the top of casing (1) afterbody, and lower liquid outlet (4) lays respectively at the middle part of casing (1) cavitys at different levels, and converges outside casing (1).
2. precipitating type separating box as claimed in claim 1 is characterized in that described casing (1) is three grades.
3. precipitating type separating box as claimed in claim 1 or 2 is characterized in that described funnel (13) is for to only have a side to the slope funnel of downward-extension.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220297210 CN202802843U (en) | 2012-06-12 | 2012-06-12 | Sediment type liquid dividing tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220297210 CN202802843U (en) | 2012-06-12 | 2012-06-12 | Sediment type liquid dividing tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202802843U true CN202802843U (en) | 2013-03-20 |
Family
ID=47861790
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220297210 Expired - Fee Related CN202802843U (en) | 2012-06-12 | 2012-06-12 | Sediment type liquid dividing tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202802843U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422433A (en) * | 2016-09-23 | 2017-02-22 | 苏州市浒墅关化工添加剂有限公司 | Solvent-based dinonyl-naphthalenesulfonic acid barium layered continuous sedimentation tank |
| CN113853245A (en) * | 2019-09-19 | 2021-12-28 | 株式会社Lg化学 | Neutralization/water separation tank for esterification product and neutralization/water separation method for esterification product |
-
2012
- 2012-06-12 CN CN 201220297210 patent/CN202802843U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422433A (en) * | 2016-09-23 | 2017-02-22 | 苏州市浒墅关化工添加剂有限公司 | Solvent-based dinonyl-naphthalenesulfonic acid barium layered continuous sedimentation tank |
| CN113853245A (en) * | 2019-09-19 | 2021-12-28 | 株式会社Lg化学 | Neutralization/water separation tank for esterification product and neutralization/water separation method for esterification product |
| EP3943480A1 (en) * | 2019-09-19 | 2022-01-26 | Lg Chem, Ltd. | Neutralization/water separation tank for esterification product and method for neutralization/water separation of esterification product |
| EP3943480A4 (en) * | 2019-09-19 | 2022-04-20 | Lg Chem, Ltd. | Neutralization/water separation tank for esterification product and method for neutralization/water separation of esterification product |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: Xinjiang Zhenqi Bio-technology Co.,Ltd. Document name: Notification to Pay the Fees |
|
| 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: 20130320 Termination date: 20170612 |