CN204352868U - The multistage hybrid reaction tank of a kind of miscella - Google Patents
The multistage hybrid reaction tank of a kind of miscella Download PDFInfo
- Publication number
- CN204352868U CN204352868U CN201420808833.6U CN201420808833U CN204352868U CN 204352868 U CN204352868 U CN 204352868U CN 201420808833 U CN201420808833 U CN 201420808833U CN 204352868 U CN204352868 U CN 204352868U
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- reative cell
- miscella
- reaction
- reaction room
- order reaction
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Abstract
The multistage hybrid reaction tank of a kind of miscella, belongs to fat and oil processing equipment technical field, for improving reaction efficiency, reducing mixing finished product oil colours pool, improving miscella refining rate.Its technical scheme is: connect 1-5 order reaction room in its tank body from bottom to top, and shaft through reative cell at different levels, the shaft in reative cell at different levels is separately installed with one group of stirring wing, the dividing plate between adjacent two-stage reaction room has flash mouth vertically downward.The utility model arranges Pyatyi reative cell, material is indoor after the abundant stirring reaction of stirring wing at every order reaction, enter last layer reative cell from flash mouth and continue reaction, achieve the abundant reaction of miscella soda acid and soap stock to the abundant absorption of pigment, improve the utilization rate of alkali, reduce the neutral oil loss adding alkali in a large number and cause, avoid pigment in miscella and directly enter in mixing product oil without abundant absorption.The utility model improves reaction efficiency, reduces mixing finished product oil colours pool, improves miscella refining rate.
Description
Technical field
The utility model relates to soda acid hybrid reaction agitator tank in a kind of miscella refining technique, belongs to fat and oil processing equipment technical field.
Background technology
In Foodgrain and oilseed production, the reaction of miscella alkali refining after stirring reaction a period of time, directly enters centrifuge and carry out oily soap separation in the retort of a sealing.Problem is both ways deposited: first in course of reaction at present in retort, control inaccurate to the time of acid-base reaction in stirring reaction process, make the absorption of the soap stock of formation to pigment insufficient, cause partial pigment not have time enough to be adsorbed by soap stock, result makes mixing finished product oil colours pool heavier; Secondly, in order to reduce finished product oil colours pool, can strengthen alkali charge, the alkali institute saponification that this can cause part neutral oil to be added into, causes miscella refining rate to reduce.The problem of above two aspects reduces quality and the refining yield of miscella, in order to improve the quality of products and economic benefit, is necessary to improve existing retort, more effectively to control course of reaction.
Utility model content
Technical problem to be solved in the utility model is to provide the multistage hybrid reaction tank of a kind of miscella, this multistage hybrid reaction tank can realize effective control of acid-base reaction time, soap stock is made to have time enough adsorpting pigment, reduce mixing finished product cast of oil, decrease the addition of alkali simultaneously, improve the utilization rate adding alkali in miscella, reduce neutral oil by the probability of excess base saponification, significantly improve the efficiency of miscella reaction and the refining yield of product oil.
The technical scheme solved the problems of the technologies described above is:
The multistage hybrid reaction tank of a kind of miscella, it comprises tank body, first order reaction room, second order reaction room, third-order reaction room, fourth-order reaction room, Pyatyi reative cell, fire-proof motor, reductor, shaft, stirring wing, first order reaction room, second order reaction room, third-order reaction room, fourth-order reaction room, Pyatyi reative cell is connected from bottom to top in tank body, by baffle for separating between reative cell at different levels, fire-proof motor and reductor are installed above tank body, fire-proof motor is connected with reductor, the output shaft of reductor is connected with shaft upper end, shaft is vertically downward through reative cell at different levels, shaft in reative cell at different levels is separately installed with one group of stirring wing, charging aperture is arranged at the bottom of first order reaction room, dividing plate between adjacent two-stage reaction room there is flash mouth, there is discharging opening on the top of reative cell at different levels respectively.
The multistage hybrid reaction tank of above-mentioned miscella, the charging aperture place of described first order reaction room is provided with delivery pump.
The multistage hybrid reaction tank of above-mentioned miscella, the discharging opening of described reative cell at different levels diagonally distributes with the flash mouth entering this grade.
The multistage hybrid reaction tank of above-mentioned miscella, the sidewall of described reative cell at different levels is provided with visor.
The beneficial effects of the utility model are:
The utility model arranges Pyatyi reative cell, material is indoor after the abundant stirring reaction of stirring wing at every order reaction, under the spiral effect of stirring wing generation and the pressure of inlet feed, enter last layer reative cell from flash mouth and continue reaction, achieve the abundant reaction of miscella soda acid and soap stock to the abundant absorption of pigment, improve the utilization rate of alkali, reduce the neutral oil loss adding alkali in a large number and cause, avoid pigment in miscella and directly enter in mixing product oil without abundant absorption.The utility model improves reaction efficiency, to reduction mixing finished product oil colours pool, improves miscella refining rate and has remarkable result.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure, mark is as follows: tank body 1, first order reaction room 2, second order reaction room 3, third-order reaction room 4, fourth-order reaction room 5, Pyatyi reative cell 6, dividing plate 7, charging aperture 8, discharging opening 9, flash mouth 10, fire-proof motor 11, reductor 12, shaft 13, stirring wing 14.
Detailed description of the invention
The utility model comprises tank body 1, fire-proof motor 11, reductor 12, shaft 13, stirring wing 14.
Show in figure, be divided into first order reaction room 2, second order reaction room 3, third-order reaction room 4, fourth-order reaction room 5, Pyatyi reative cell 6 1--5 order reaction room altogether in tank body 1 from bottom to top, between reative cell at different levels, have dividing plate 7 separately.
Show in figure, fire-proof motor 11 and reductor 12 are installed above tank body 1, fire-proof motor 11 is connected with reductor 12, the output shaft of reductor 12 is connected with shaft 13 upper end, shaft 13 through reative cell at different levels, the shaft 13 in reative cell at different levels is separately installed with one group of stirring wing 14 vertically downward.
Show in figure, have charging aperture 8 in the bottom of first order reaction room 2, have discharging opening 9 on the top of reative cell at different levels, the dividing plate 7 between adjacent two-stage reaction room has flash mouth 10.Material enters from the charging aperture 8 of first order reaction room 2, second order reaction room is entered again from the flash mouth 10 between first order reaction room 2 and second order reaction room 3, material in the middle of second order reaction room 3 enters third-order reaction room 4 from the flash mouth 10 between second order reaction room 3 and third-order reaction room 4, the like, the charging aperture of the reative cells at different levels of second order reaction room more than 3 is the flash mouth 10 on underlay screen 7.
Show in figure, the top of reative cell at different levels also has discharging opening 9, and the discharging opening 9 of reative cell at different levels diagonally distributes with the flash mouth 10 entering this grade, enters next stage reative cell after fully reacting to make material in reative cell at different levels again, avoids reaction insufficient.
Show in figure, the charging aperture place of first order reaction room 2 is provided with delivery pump, for convey materials in tank body 1.
Show in figure, the sidewall of reative cell at different levels is provided with visor, be used for observing liquid level and response situation.
Every first order reaction room volume of an embodiment of the present utility model is fixed as 0.5 cube.
The course of work of the present utility model is as follows:
Miscella adds after alkali mixes, first order reaction room 2 is entered from charging aperture 8, under the stirring of stirring wing 14, carry out first order reaction, along with material constantly enters from charging aperture 8, the miscella reacted enters second order reaction room 3 from flash mouth 10, under the effect of the stirring wing 14 simultaneously in second order reaction room 3, carry out second level reaction, the like, the time of reacting as required and the total amount of material, select suitable discharging opening 9 discharging, complete the acid-base reaction in miscella.
Claims (4)
1. the multistage hybrid reaction tank of miscella, is characterized in that: it comprises tank body (1), first order reaction room (2), second order reaction room (3), third-order reaction room (4), fourth-order reaction room (5), Pyatyi reative cell (6), fire-proof motor (11), reductor (12), shaft (13), stirring wing (14), first order reaction room (2), second order reaction room (3), third-order reaction room (4), fourth-order reaction room (5), Pyatyi reative cell (6) is connected from bottom to top in tank body (1), separated by dividing plate (7) between reative cell at different levels, tank body (1) top is provided with fire-proof motor (11) and reductor (12), fire-proof motor (11) is connected with reductor (12), the output shaft of reductor (12) is connected with shaft (13) upper end, shaft (13) is vertically downward through reative cell at different levels, shaft (13) in reative cell at different levels is separately installed with one group of stirring wing (14), charging aperture (8) is arranged at the bottom of first order reaction room (2), dividing plate (7) between adjacent two-stage reaction room has flash mouth (10), and discharging opening (9) is arranged respectively at the top of reative cell at different levels.
2. the multistage hybrid reaction tank of miscella according to claim 1, is characterized in that: charging aperture (8) place of described first order reaction room (2) is provided with delivery pump.
3. the multistage hybrid reaction tank of miscella according to claim 1 and 2, is characterized in that: the discharging opening (9) of described reative cell at different levels and the flash mouth (10) entering this grade diagonally distribute.
4. the multistage hybrid reaction tank of miscella according to claim 3, is characterized in that: the sidewall of described reative cell at different levels is provided with visor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420808833.6U CN204352868U (en) | 2014-12-19 | 2014-12-19 | The multistage hybrid reaction tank of a kind of miscella |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420808833.6U CN204352868U (en) | 2014-12-19 | 2014-12-19 | The multistage hybrid reaction tank of a kind of miscella |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204352868U true CN204352868U (en) | 2015-05-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420808833.6U Expired - Fee Related CN204352868U (en) | 2014-12-19 | 2014-12-19 | The multistage hybrid reaction tank of a kind of miscella |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204352868U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107626253A (en) * | 2017-09-25 | 2018-01-26 | 天能电池集团有限公司 | A kind of continuous paste mixing machine |
| CN116328695A (en) * | 2023-05-26 | 2023-06-27 | 东营市赫邦化工有限公司 | Improved generation epoxy chloropropane saponification tower |
-
2014
- 2014-12-19 CN CN201420808833.6U patent/CN204352868U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107626253A (en) * | 2017-09-25 | 2018-01-26 | 天能电池集团有限公司 | A kind of continuous paste mixing machine |
| CN107626253B (en) * | 2017-09-25 | 2023-11-21 | 天能电池集团股份有限公司 | Continuous paste mixing machine |
| CN116328695A (en) * | 2023-05-26 | 2023-06-27 | 东营市赫邦化工有限公司 | Improved generation epoxy chloropropane saponification tower |
| CN116328695B (en) * | 2023-05-26 | 2023-07-21 | 东营市赫邦化工有限公司 | Improved generation epoxy chloropropane saponification tower |
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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: 20150527 Termination date: 20171219 |