CN202284200U - Alkali refining tank for oil - Google Patents
Alkali refining tank for oil Download PDFInfo
- Publication number
- CN202284200U CN202284200U CN2011203972628U CN201120397262U CN202284200U CN 202284200 U CN202284200 U CN 202284200U CN 2011203972628 U CN2011203972628 U CN 2011203972628U CN 201120397262 U CN201120397262 U CN 201120397262U CN 202284200 U CN202284200 U CN 202284200U
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- CN
- China
- Prior art keywords
- tank body
- tank
- oil
- alkali
- alkali refining
- 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
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Abstract
The utility model discloses an alkali refining tank for oil, and belongs to an alkali refining tank device for preparing wheat germ oil. The tank comprises a tank body in which a stirring device is arranged. The stirring device comprises a stirring rod. Stirring blades on the upper and middle parts of the stirring rod are flat paddle type stirring blades, and stirring blades on the lower part of the stirring rod are spiral stirring blades. A hot air inlet/outlet is formed in the top end of the tank body. The stirring device is improved and started in alkali liquor addition and temperature raising processes, so that the non-uniform and local saponification of alkali liquor is prevented, the oil is fully mixed with alkali, and a free fatty acid is fully reacted with the alkali at the same time. In addition, the hot air inlet/outlet is formed, so that foreign materials in the tank can be blown out of the tank when the tank is washed, and the tank can be dried as quickly as possible. The alkali refining tank is high in production efficiency and energy saving, and the requirements of large-scale wheat germ oil production enterprises are met.
Description
Technical field
The utility model relates to the alkali refining tank arrangement in a kind of wheatgerm oil refining process, and a kind of specifically oil alkali refining jar belongs to the grain and oil processing technique field.
Background technology
The oil alkali refining jar is a production unit important in the wheatgerm oil refining process, and traditional alkali refining jar mainly is made up of tank body, heating coil, whipping appts and transmission rig etc.This equipment all is to be used for industrial-scale production, and size is bigger, and all about 2～3 tons, the tank body volume is more than 3 cubic metres for every jar charging capacity.For bigger alkali refining jar, add in the alkali lye process, inhomogeneously cause that to add alkali inhomogeneous if stir, alkali lye is too concentrated, local saponification phenomenon will occur, causes oily soap not easily separated, influences refining effect.The whipping appts of oil alkali refining jar can not well satisfy production requirement at present.
The utility model content
The purpose of the utility model is to provide a kind of oil alkali refining jar, and this alkali refining jar has improved the stirring facility, prevents that effectively alkali lye is inhomogeneous.
The technical scheme that its technical problem of the utility model solution is taked is: a kind of oil alkali refining jar, comprise tank body, and it is characterized in that; The top of said tank body is provided with the oil plant import; The tank body bottom is provided with drain, and the outside of tank body is provided with heating coil, and tank interior is provided with the stirring facility; Said heating coil is provided with heating agent import and heating agent outlet; Said stirring facility comprises agitator arm, and agitator arm links to each other with motor and stretches in the tank body, is distributed with three groups of agitating vanes on the agitator arm from top to bottom, and the agitating vane at top and middle part is flat oar formula agitating vane, and the agitating vane of bottom is spiral agitating vane.
The top of said tank body is provided with a warm air and imports and exports.
The top of said tank body is provided with a TM.
Described tank body top is column part, and the bottom is the conical head part, and the ratios of column part and conical head part is between 1.0～1.8, and tank body back cut diameter and tank body ratios are between 0.4～0.7.
Described tank body places on the support.
The volume of said tank body is 3000 liters.
Compared with prior art, the utlity model has following outstanding beneficial effect:
1, improved the stirring facility, be distributed with three groups of agitating vanes on the agitator arm from top to bottom, the agitating vane at top and middle part is flat oar formula agitating vane; The agitating vane of bottom is spiral agitating vane; Effectively guarantee to add the uniformity coefficient that stirs in the alkali lye process,, prevent the local saponification of the inhomogeneous generation of alkali lye when under a lot of situation of oil plant, adding alkali for bigger alkali refining jar; Make oily alkali thorough mixing simultaneously, free fatty acids and alkali fully react.
2, be provided with warm air on the top of tank body and import and export, when cleaning tank body, can feed warm air and make that foreign material are blown outside the jar in the jar, make jar dry as early as possible.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Among the figure: 1 tank body, 2 oil plant imports, 3 heating agent imports, 4 flat oar formula agitating vanes, 5 supports, the outlet of 6 heating agents, 7 drains, 8 warm airs are imported and exported, 9 TMs, 10 heating coils, 11 motors, 12 spiral agitating vanes.
Embodiment
Below in conjunction with Figure of description and embodiment the utility model is done further description:
As shown in Figure 1.A kind of oil alkali refining jar comprises tank body 1, and the top of said tank body 1 is provided with oil plant import 2, and tank body 1 bottom is provided with drain 7, and the outside of tank body 1 is provided with heating coil 10, and tank body 1 inside is provided with the stirring facility; Said heating coil 10 is provided with heating agent import 3 and heating agent outlet 6; Said stirring facility comprises agitator arm; Agitator arm links to each other with motor 11 and stretches in the tank body 1; Be distributed with three groups of agitating vanes on the agitator arm from top to bottom, the agitating vane at top and middle part is flat oar formula agitating vane 4, and the agitating vane of bottom is spiral agitating vane 12.
The top of said tank body 1 is provided with a warm air and imports and exports 8.When cleaning tank body 1, can feed warm air and make that foreign material are blown outside the jar in the jar, make jar dry as early as possible.
The top of said tank body 1 is provided with a TM 9.TM 9 is used to observe tank body 1 temperature, is convenient to timely control.
Described tank body 1 top is column part, and the bottom is the conical head part, and the ratios of column part and conical head part is between 1.0～1.8, and tank body back cut diameter and tank body ratios are between 0.4～0.7.
Described tank body 1 places on the support 5.
The volume of said tank body 1 is 3000 liters.
The working process of the utility model is: with the wheatgerm crude oil that refines, add the tank body 1 from oil plant import 2, open thermal source; Heating medium flows into from heating agent import 3, and heating agent outlet 6 is flowed out, and material in the tank body 1 is heated; Open the stirring facility, stirring velocity is 60～70r/min, closes thermal source after treating about oily temperature rise to 30 ℃; The alkali lye for preparing is added in the oil fast, add alkali and finish, stirring velocity is transferred to 30～35r/min.When tiny neat soap occurs, open thermal source, with about oily temperature rise to 65 ℃, close the stirring facility then, insulation deposition about 4 hours is emitted Chinese honey locust.Wash then, decolouring, deodorization obtain refining oil.
Stir facility and in adding alkali lye and temperature-rise period, launch, prevent the local saponification of the inhomogeneous generation of alkali lye, make oily alkali thorough mixing simultaneously, free fatty acids and alkali fully react.Warm air is imported and exported 8 and behind purge tank, is fed warm air, will blow out outside the jar attached to wheatgerm oil on the tank skin and water emulsion.
Embodiment 1:
A kind of oil alkali refining jar structure above is said, and the ratios of tank body 1 column part and conical head part is 1.5, and tank body 1 back cut diameter and tank body 1 ratios are 0.5.
Embodiment 2:
A kind of oil alkali refining jar structure is with embodiment 1, and the ratios of tank body 1 column part and conical head part is 1.3, and tank body 1 back cut diameter and tank body 1 ratios are 0.4.
Embodiment 3:
A kind of oil alkali refining jar structure is with embodiment 1, and the ratios of tank body 1 column part and conical head part is 1.7, and tank body 1 back cut diameter and tank body 1 ratios are 0.6.
The above; Some principles of the utility model just explain through diagrams; This specification sheets be not be to the utility model be confined to shown in described concrete structure and the scope of application; So every the modify and equivalent that might be utilized all belongs to the claim that the utility model is applied for.
Except that the said technical characterictic of specification sheets, all the other technical characterictics are those skilled in the art's known technology.
Claims (6)
1. an oil alkali refining jar comprises tank body, it is characterized in that, the top of said tank body is provided with the oil plant import, and the tank body bottom is provided with drain, and the outside of tank body is provided with heating coil, and tank interior is provided with the stirring facility; Said heating coil is provided with heating agent import and heating agent outlet; Said stirring facility comprises agitator arm, and agitator arm links to each other with motor and stretches in the tank body, is distributed with three groups of agitating vanes on the agitator arm from top to bottom, and the agitating vane at top and middle part is flat oar formula agitating vane, and the agitating vane of bottom is spiral agitating vane.
2. a kind of oil alkali refining jar according to claim 1 is characterized in that, the top of said tank body is provided with a warm air and imports and exports.
3. a kind of oil alkali refining jar according to claim 1 and 2 is characterized in that the top of said tank body is provided with a TM.
4. a kind of oil alkali refining jar according to claim 3; It is characterized in that described tank body top is column part, the bottom is the conical head part; The ratios of column part and conical head part is between 1.0～1.8, and tank body back cut diameter and tank body ratios are between 0.4～0.7.
5. a kind of oil alkali refining jar according to claim 1 is characterized in that described tank body places on the support.
6. a kind of oil alkali refining jar according to claim 1 is characterized in that the volume of said tank body is 3000 liters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203972628U CN202284200U (en) | 2011-10-18 | 2011-10-18 | Alkali refining tank for oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203972628U CN202284200U (en) | 2011-10-18 | 2011-10-18 | Alkali refining tank for oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202284200U true CN202284200U (en) | 2012-06-27 |
Family
ID=46295728
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203972628U Expired - Fee Related CN202284200U (en) | 2011-10-18 | 2011-10-18 | Alkali refining tank for oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202284200U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108998212A (en) * | 2018-08-24 | 2018-12-14 | 铜陵瑞璞牡丹产业发展有限公司 | Guarantee the production line of peony seed oil quality |
| CN109012285A (en) * | 2018-08-27 | 2018-12-18 | 北京艺轩吉装饰工程有限公司 | A kind of mobile decorative engineering mixed stirring device |
| CN110205199A (en) * | 2019-06-05 | 2019-09-06 | 湖北双明粮棉油股份有限公司 | A kind of circulating multi-cavity alkali-refining pot of turbulent flow |
-
2011
- 2011-10-18 CN CN2011203972628U patent/CN202284200U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108998212A (en) * | 2018-08-24 | 2018-12-14 | 铜陵瑞璞牡丹产业发展有限公司 | Guarantee the production line of peony seed oil quality |
| CN109012285A (en) * | 2018-08-27 | 2018-12-18 | 北京艺轩吉装饰工程有限公司 | A kind of mobile decorative engineering mixed stirring device |
| CN110205199A (en) * | 2019-06-05 | 2019-09-06 | 湖北双明粮棉油股份有限公司 | A kind of circulating multi-cavity alkali-refining pot of turbulent flow |
| CN110205199B (en) * | 2019-06-05 | 2022-04-12 | 湖北双明粮棉油股份有限公司 | Turbulent circulation type multi-cavity alkali refining pot |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120627 Termination date: 20121018 |