CN208406278U - A kind of high-efficiency filtration systems of cold pressing rapeseed oil - Google Patents
A kind of high-efficiency filtration systems of cold pressing rapeseed oil Download PDFInfo
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- CN208406278U CN208406278U CN201820943820.8U CN201820943820U CN208406278U CN 208406278 U CN208406278 U CN 208406278U CN 201820943820 U CN201820943820 U CN 201820943820U CN 208406278 U CN208406278 U CN 208406278U
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- strainer
- filter
- oil tank
- cold pressing
- filter cylinder
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- 238000001914 filtration Methods 0.000 title claims abstract description 45
- 235000019484 Rapeseed oil Nutrition 0.000 title claims abstract description 24
- 238000003825 pressing Methods 0.000 title claims abstract description 16
- 239000003921 oil Substances 0.000 claims abstract description 27
- 235000019198 oils Nutrition 0.000 claims abstract description 27
- 239000003208 petroleum Substances 0.000 claims abstract description 21
- 239000000341 volatile oil Substances 0.000 claims abstract description 14
- 238000011010 flushing procedure Methods 0.000 claims abstract description 13
- 239000002893 slag Substances 0.000 claims description 10
- 210000002421 cell wall Anatomy 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims 1
- 235000019197 fats Nutrition 0.000 description 13
- 239000012535 impurity Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 4
- GVJHHUAWPYXKBD-UHFFFAOYSA-N (±)-α-Tocopherol Chemical group OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-UHFFFAOYSA-N 0.000 description 2
- 210000004204 blood vessel Anatomy 0.000 description 2
- 239000008157 edible vegetable oil Substances 0.000 description 2
- 240000000467 Carum carvi Species 0.000 description 1
- 235000005747 Carum carvi Nutrition 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 1
- 229930003427 Vitamin E Natural products 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- WHGYBXFWUBPSRW-FOUAGVGXSA-N beta-cyclodextrin Chemical compound OC[C@H]([C@H]([C@@H]([C@H]1O)O)O[C@H]2O[C@@H]([C@@H](O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O3)[C@H](O)[C@H]2O)CO)O[C@@H]1O[C@H]1[C@H](O)[C@@H](O)[C@@H]3O[C@@H]1CO WHGYBXFWUBPSRW-FOUAGVGXSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 210000004556 brain Anatomy 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- WIGCFUFOHFEKBI-UHFFFAOYSA-N gamma-tocopherol Natural products CC(C)CCCC(C)CCCC(C)CCCC1CCC2C(C)C(O)C(C)C(C)C2O1 WIGCFUFOHFEKBI-UHFFFAOYSA-N 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 235000020778 linoleic acid Nutrition 0.000 description 1
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 210000005036 nerve Anatomy 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000010499 rapseed oil Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009758 senescence Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 239000011709 vitamin E Substances 0.000 description 1
- 229940046009 vitamin E Drugs 0.000 description 1
- 235000019165 vitamin E Nutrition 0.000 description 1
Landscapes
- Fats And Perfumes (AREA)
- Filtration Of Liquid (AREA)
Abstract
The utility model discloses a kind of high-efficiency filtration systems of cold pressing rapeseed oil, including first squeezing oil tank, filter device and essential oil tank, first level filtering device and two-stage filter include filter cylinder, strainer, telescopic rod and reciprocating mechanism, the inside of filter cylinder is arranged in strainer, flushing device is provided with below strainer, top is provided with slag-draining device, and first squeezing oil tank is connect by the first petroleum pipeline with oil inlet pipe, and essential oil tank is connect by the second petroleum pipeline with the flowline of two-stage filter bottom.The utility model carries out movement back and forth by reciprocating mechanism driving filter cylinder, carries out high pressure to strainer by flushing device and washes away, the dregs of fat for being deposited in strainer upper surface are rushed to open, and are suspended in the upper surface of strainer, are at this moment excluded these dregs of fat by slag-draining device.The utility model rate of filtration is fast, and filter efficiency is high, and the dregs of fat are cleaned out, conveniently, has significant economic value and social value.
Description
Technical field
The utility model relates to edible oil processing technique fields, and in particular to a kind of high efficiency filter of cold pressing rapeseed oil
System.
Background technique
Rapeseed oil is exactly the rape oil that we are commonly called as, and is called caraway oil, is with the crucifer rape i.e. seed of rape
Press the liquid of resulting transparent or semitransparent shape.The battalion such as the unsaturated fatty acids such as linoleic acid contained by rapeseed oil and vitamin E
Form point can be absorbed by organisms well, have effects that certain softening blood vessel to human body, delay senescence, in addition, due to squeezing
The raw material of oil is the seed of plant, can generally contain certain seed phosphatide, development of the seed phosphatide to blood vessel, nerve, brain
It plays an important role.In the production process of cold press rapeseed oil, cold pressing technique, no refinery practice, maximum limit are used
Various fat-soluble nutrients ingredients in the peculiar flavour and oil of grease are saved to degree, therefore cold pressing rapeseed oil is a kind of green
Color, free of contamination edible oil.
Using cold pressing process squeeze out come rapeseed oil in containing rap oil seedcake slag and some other impurity, these impurity
It will affect quality and the holding time of rapeseed oil, therefore need the slag in rapeseed oil after rape oil-pressing using filter device
Dregs and other impurities remove, and existing filter device is usually that strainer is being arranged inside, and rapeseed oil is input in filter device,
Impurities are removed by the filtration of strainer after standing a period of time, so that it is preferably oily to obtain quality, but time-consuming,
Filter efficiency is low, effect is bad, and during the filtration process, the dregs of fat are easily deposited on strainer, influences the rate of filtration, reduces filtering effect
Rate, dregs of fat cleaning are inconvenient.Therefore, it is fast to develop a kind of rate of filtration, filter efficiency is high, and the dregs of fat are cleaned out, easily
The high-efficiency filtration systems of cold pressing rapeseed oil are desirabilities.
Utility model content
The purpose of this utility model is to provide a kind of rate of filtration is fast, filter efficiency is high, and the dregs of fat are cleaned out, easily
The high-efficiency filtration systems of cold pressing rapeseed oil.
The purpose of this utility model is achieved in that the utility model includes first squeezing oil tank, filter device and essential oil tank,
Filter device includes shell and setting in the intracorporal first level filtering device of shell and two-stage filter, and first level filtering device setting exists
The top of two-stage filter, first level filtering device and two-stage filter include filter cylinder, strainer, telescopic rod and reciprocating machine
The inside of filter cylinder is arranged in structure, strainer, and flushing device is provided with below strainer, and top is provided with slag-draining device, and telescopic rod is set
It sets between filter cylinder and shell, reciprocating mechanism is mounted on the outside of shell, the outer wall transmission of reciprocating mechanism and filter cylinder
Connection, the bottom of filter cylinder are provided with flowline, and oil inlet pipe is provided at the top of shell, and oil inlet pipe passes through the first petroleum pipeline and first squeezing
Oil tank connection, essential oil tank are connect by the second petroleum pipeline with the flowline of two-stage filter bottom.
Further, reciprocating mechanism includes drive rod, rotary table, idler wheel, cam mechanism, fixed block and reset spring,
The diameter of rotary table is greater than the diameter of drive rod, and drive rod is connected to the side of rotary table with one heart, and idler wheel is connected to the other side of rotary table,
The wheel rim of idler wheel is against on the cam of cam mechanism, and fixed block movable set is on drive rod, and one end of fixed block and shell
Outer wall connection, the other end processing it is fluted, reset spring is installed in the space between drive rod and the cell wall of groove, reset
The extension end of spring is against on the end face of rotary table.
Further, the sieve meshes diameter of first level filtering device is greater than the sieve meshes diameter of two-stage filter.
Further, strainer is horizontally disposed or is obliquely installed.
Further, flushing device includes that high-pressure nozzle, third petroleum pipeline and high-pressure pump, high-pressure nozzle are placed under strainer
Side, and the nozzle of high-pressure nozzle is connected between high-pressure nozzle and essential oil tank by third petroleum pipeline towards the lower surface of strainer, it is high
Press pump is arranged on third petroleum pipeline, and the third petroleum pipeline between filter cylinder and shell is bellows.
Further, slag-draining device includes scum pipe, deslagging pump and dregs of fat tank, and the slag absorbing end of scum pipe is arranged on strainer
On the cartridge sidewall of side, slag output end is placed in the top of dregs of fat tank, and the row on scum pipe, between filter cylinder and shell is arranged in deslagging pump
Slag pipe is bellows.
The utility model drives first level filtering device and second level mistake in the filter process of rapeseed oil, by reciprocating mechanism
The movement of device progress back and forth is filtered, accelerates the filter process of rapeseed oil, improves filter efficiency, deslagging is provided with above strainer
Device, lower section are provided with flushing device, after filtration carries out a period of time, carry out high pressure punching to strainer by flushing device
Brush, the dregs of fat for being deposited in strainer upper surface are rushed to open, and are suspended in the upper surface of strainer, at this moment by slag-draining device by these dregs of fat
It excludes.The utility model rate of filtration is fast, and filter efficiency is high, and the dregs of fat are cleaned out, conveniently, has significant economic value and society
It can be worth.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
In figure: 1- first squeezing oil tank, 2- filter device, 3- essential oil tank, the first petroleum pipeline of 4-, the second petroleum pipeline of 5-, 6- shell,
7- oil inlet pipe, 8- filter cylinder, 9- strainer, 10- telescopic rod, 11- reciprocating mechanism, 12- flushing device, 13- slag-draining device, 14-
Drive rod, 15- flowline, 16- rotary table, 17- idler wheel, 18- cam mechanism, 19- fixed block, 20- reset spring, 21- high pressure spray
Head, 22- third petroleum pipeline, 23- high-pressure pump, 24- scum pipe, 25- deslagging pump, 26- dregs of fat tank.
Specific embodiment
The utility model will be further described below with reference to the accompanying drawings, but is not subject in any way to the utility model
Limitation instructs made any changes and modifications based on the utility model, belongs to the protection scope of the utility model.
As shown in Figure 1, the utility model includes first squeezing oil tank 1, filter device 2 and essential oil tank 3, filter device 2 includes shell
Body 6 and the first level filtering device and two-stage filter being arranged in shell 6, first level filtering device are arranged in two-stage filter
Top, first level filtering device and two-stage filter include filter cylinder 8, strainer 9, telescopic rod 10 and reciprocating mechanism 11, filter
The inside of filter cylinder 8 is arranged in net 9, and the lower section of strainer 9 is provided with flushing device 12, and top is provided with slag-draining device 13, telescopic rod
10 are arranged between filter cylinder 8 and shell 6, and reciprocating mechanism 11 is mounted on the outside of shell 6, the driving of reciprocating mechanism 11
The outer wall of bar 14 and filter cylinder 8 is sequentially connected, and the bottom of filter cylinder 8 is provided with flowline 15, and the top of shell 6 is provided with oil inlet pipe 7,
Flowmeter and control valve can be set on oil inlet pipe 7, according to the processing capacity of filter device 2, control enters oil mass therein, into
Oil pipe 7 is connect by the first petroleum pipeline 4 with first squeezing oil tank 1, and essential oil tank 3 passes through the second petroleum pipeline 5 and two-stage filter bottom
Flowline 15 connect.
Reciprocating mechanism 11 includes drive rod 14, rotary table 16, idler wheel 17, cam mechanism 18 and fixed block 19, rotary table 16
Diameter be greater than the diameter of drive rod 14, drive rod 14 is connected to the side of rotary table 16 with one heart, and idler wheel 17 is connected to rotary table 16
The other side, the wheel rim of idler wheel 17 are against on the cam of cam mechanism 18, and 19 movable set of fixed block is fixed on drive rod 14
One end of block 19 is connect with the outer wall of shell 6, and other end processing is fluted, is pacified in the space between drive rod 14 and groove cell wall
Equipped with reset spring 20, the extension end of reset spring 20 is against on the end face of rotary table 16, is connected with motor on cam mechanism 18, is opened
After opening motor, motor band moving cam is rotated, and in combination with the effect of reset spring 20, drive rod 14 is driven to move reciprocatingly, from
And achieve the purpose that move back and forth first level filtering device and two-stage filter.
In order to filter the dregs of fat and impurity in rapeseed oil step by step, first level filtering device is initial filter device, two-stage filter
For fine filtering device, therefore the sieve meshes diameter of first level filtering device is greater than the sieve meshes diameter of two-stage filter.
Strainer 9 is horizontally disposed or is obliquely installed, when being obliquely installed, for the ease of deslagging, the slag absorbing end of scum pipe 24
Lowest point on strainer 9 should be set.
Flushing device 12 includes high-pressure nozzle 21, third petroleum pipeline 22 and high-pressure pump 23, and high-pressure nozzle 21 is placed in strainer 9
Lower section, and the nozzle of high-pressure nozzle 21 passes through third oil transportation towards the lower surface of strainer 9 between high-pressure nozzle 21 and essential oil tank 3
Pipe 22 is connected to, and high-pressure pump 23 is arranged on third petroleum pipeline 22, and the third petroleum pipeline 22 between filter cylinder 8 and shell 6 is soft to stretch
Oil pump in essential oil tank 3 at high-pressure nozzle 21, is carried out high pressure to the lower surface of strainer 9 and washed away by pipe, high-pressure pump 23, strainer 9
The dregs and impurity of upper surface accumulation are washed from the upper surface of strainer 9, are suspended in the top of strainer 9.
Slag-draining device 13 includes scum pipe 24, deslagging pump 25 and dregs of fat tank 26, and the slag absorbing end of scum pipe 24 is arranged in strainer 9
On 8 side wall of filter cylinder of top, slag output end is placed in the top of dregs of fat tank 26, and deslagging pump 25 is arranged on scum pipe 24, filter cylinder 8 and shell
Scum pipe 24 between body 6 is bellows, and strainer 9 is washed away by flushing device 12, and dregs and impurity are washed from strainer 9
Upper surface when being suspended in the top of strainer 9, is opened deslagging pump 25, dregs and impurity is siphoned away, to achieve the purpose that deslagging.
The working process of the utility model is as follows: the rapeseed oil of first squeezing is input to the top of filter device 2 from first squeezing oil tank 1
The filtering of first level filtering device and two-stage filter is successively passed through in portion, and during the filtration process, by reciprocating mechanism 11
It drives first level filtering device and two-stage filter to move reciprocatingly, to accelerate the speed of filtering, improves the efficiency of filtering, when
Filtration carry out a period of time after, combined by flushing device 12 and slag-draining device 13, will be deposited in the dregs on strainer 9 and
Impurity excludes, and avoids the blocking of 9 mesh of strainer, prevents the reduction of filter efficiency, and scour medium used in flushing device 12 is
The essential oil that filtering is completed will not impact the quality of filtered oil in scour process.
Claims (6)
1. a kind of high-efficiency filtration systems of cold pressing rapeseed oil, including first squeezing oil tank (1), filter device (2) and essential oil tank
(3), it is characterised in that: the filter device (2) includes the first level filtering device and two of shell (6) and setting in shell (6)
The top of two-stage filter, first level filtering device and secondary filtration dress is arranged in grade filter device, the first level filtering device
It sets including filter cylinder (8), strainer (9), telescopic rod (10) and reciprocating mechanism (11), the strainer (9) is arranged in filter cylinder (8)
Inside is provided with flushing device (12) below strainer (9), and top is provided with slag-draining device (13), and the telescopic rod (10) sets
It sets between filter cylinder (8) and shell (6), the reciprocating mechanism (11) is mounted on the outside of shell (6), reciprocating mechanism
(11) it is sequentially connected with the outer wall of filter cylinder (8), the bottom of the filter cylinder (8) is provided with flowline (15), the top of the shell (6)
Portion is provided with oil inlet pipe (7), and the oil inlet pipe (7) is connect by the first petroleum pipeline (4) with first squeezing oil tank (1), the essential oil tank
(3) it is connect by the second petroleum pipeline (5) with the flowline (15) of two-stage filter bottom.
2. a kind of high-efficiency filtration systems of cold pressing rapeseed oil according to claim 1, it is characterised in that: described reciprocal
Movement mechanism (11) includes drive rod (14), rotary table (16), idler wheel (17), cam mechanism (18) and fixed block (19), the circle
The diameter of platform (16) is greater than the diameter of drive rod (14), and the drive rod (14) is connected to the side of rotary table (16), idler wheel with one heart
(17) it is connected to the other side of rotary table (16), the wheel rim of the idler wheel (17) is against on the cam of cam mechanism (18), described solid
Block (19) movable set is determined on drive rod (14), and one end of fixed block (19) is connect with the outer wall of shell (6), the other end adds
Work is fluted, is equipped with reset spring (20) in the space between the drive rod (14) and groove cell wall, reset spring (20)
Extension end be against on the end face of rotary table (16).
3. a kind of high-efficiency filtration systems of cold pressing rapeseed oil according to claim 1, it is characterised in that: the level-one
The sieve meshes diameter of filter device is greater than the sieve meshes diameter of two-stage filter.
4. a kind of high-efficiency filtration systems of cold pressing rapeseed oil according to claim 1, it is characterised in that: the strainer
It (9) is to be horizontally disposed with or be obliquely installed.
5. a kind of high-efficiency filtration systems of cold pressing rapeseed oil according to claim 1, it is characterised in that: described to wash away
Device (12) includes high-pressure nozzle (21), third petroleum pipeline (22) and high-pressure pump (23), and high-pressure nozzle (21) is placed in strainer (9)
Lower section, and the nozzle of high-pressure nozzle (21) is towards the lower surface of strainer (9), between the high-pressure nozzle (21) and essential oil tank (3)
It is connected to by third petroleum pipeline (22), the high-pressure pump (23) is arranged on third petroleum pipeline (22).
6. a kind of high-efficiency filtration systems of cold pressing rapeseed oil according to claim 1, it is characterised in that: the deslagging
Device (13) includes scum pipe (24), deslagging pump (25) and dregs of fat tank (26), and the slag absorbing end setting of the scum pipe (24) is being filtered
On filter cylinder (8) side wall above net (9), slag output end is placed in the top of dregs of fat tank (26), and the deslagging pump (25) is arranged in deslagging
It manages on (24).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820943820.8U CN208406278U (en) | 2018-06-19 | 2018-06-19 | A kind of high-efficiency filtration systems of cold pressing rapeseed oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820943820.8U CN208406278U (en) | 2018-06-19 | 2018-06-19 | A kind of high-efficiency filtration systems of cold pressing rapeseed oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208406278U true CN208406278U (en) | 2019-01-22 |
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|---|---|---|---|
| CN201820943820.8U Active CN208406278U (en) | 2018-06-19 | 2018-06-19 | A kind of high-efficiency filtration systems of cold pressing rapeseed oil |
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| CN (1) | CN208406278U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109758815A (en) * | 2019-03-28 | 2019-05-17 | 曹月英 | One vegetable oil oil plant separation equipment |
| CN112933733A (en) * | 2021-02-06 | 2021-06-11 | 天津市浩宇助剂有限公司 | Reciprocating type sewage treatment plant for industrial waste water of environmental protection |
| CN113528232A (en) * | 2021-08-05 | 2021-10-22 | 方燕青 | Preparation method of camellia oil |
| CN114797268A (en) * | 2021-11-19 | 2022-07-29 | 河南省淇花食用油有限公司 | Residue filter equipment of edible vegetable oil production usefulness |
-
2018
- 2018-06-19 CN CN201820943820.8U patent/CN208406278U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109758815A (en) * | 2019-03-28 | 2019-05-17 | 曹月英 | One vegetable oil oil plant separation equipment |
| CN109758815B (en) * | 2019-03-28 | 2021-04-20 | 山东创优生物科技有限公司 | Vegetable oil material splitter |
| CN112933733A (en) * | 2021-02-06 | 2021-06-11 | 天津市浩宇助剂有限公司 | Reciprocating type sewage treatment plant for industrial waste water of environmental protection |
| CN112933733B (en) * | 2021-02-06 | 2022-11-18 | 湖南伍玖环保科技发展有限公司 | Reciprocating type sewage treatment plant for industrial waste water of environmental protection |
| CN113528232A (en) * | 2021-08-05 | 2021-10-22 | 方燕青 | Preparation method of camellia oil |
| CN113528232B (en) * | 2021-08-05 | 2024-03-15 | 贵州省多野农林科技有限公司 | Preparation method of camellia oil |
| CN114797268A (en) * | 2021-11-19 | 2022-07-29 | 河南省淇花食用油有限公司 | Residue filter equipment of edible vegetable oil production usefulness |
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|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 655700 Qujing City, Yunnan province Shizong Danfeng County Street Fengxiang Light Industrial Park Patentee after: Yunnan Derui Oil Co., Ltd Address before: 655700 Qujing City, Yunnan province Shizong Danfeng County Street Fengxiang Light Industrial Park Patentee before: SHIZONGDE OIL AND FAT Co.,Ltd. |
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| CP01 | Change in the name or title of a patent holder |