CN204601766U - Impurity multiple stage filtration system in a kind of production technology of walnut oil - Google Patents
Impurity multiple stage filtration system in a kind of production technology of walnut oil Download PDFInfo
- Publication number
- CN204601766U CN204601766U CN201520318410.0U CN201520318410U CN204601766U CN 204601766 U CN204601766 U CN 204601766U CN 201520318410 U CN201520318410 U CN 201520318410U CN 204601766 U CN204601766 U CN 204601766U
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- filter
- feed bin
- primary
- walnut oil
- secondary filter
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- Food-Manufacturing Devices (AREA)
Abstract
The utility model discloses the impurity multiple stage filtration system in a kind of production technology of walnut oil, feed pipe connects the bottom of point feed bin, the top of feed bin is divided evenly to be provided with primary filter, the endoporus of primary filter aims at the installing hole at point feed bin top, and the top of primary filter is by top closure press seal; Be positioned at a point feed bin top and be provided with secondary filter, all primary filters are positioned at secondary filter inside, and the top of secondary filter is by top closure press seal; Divide feed bin and secondary filter to be positioned at fluid and collect inside, storehouse, fluid collects the tube connector being provided with bottom storehouse and being communicated with fine filter; Described fine filter is provided with micro porous filtration sieve and liquid level peephole, is provided with discharge nozzle bottom fine filter.The purpose of this utility model is by designing a set of multiple stage filtration system, makes walnut oil reach the standard of ultrahigh quality oil.
Description
Technical field
The present invention relates to a kind of walnut oil refining device field, particularly relate to the impurity multiple stage filtration system in a kind of production technology of walnut oil.
Background technology
Walnut oil is through China Preventive Medicial Science Institute, national grain oil inspection Spot detection: unsaturated fatty acid content accounts for more than 90%, aliphatic acid composition palmitic acid acid 5.1%, stearic acid 2%, oleic acid 18.1%, linoleic acid 65.4%, leukotrienes 9.4%, vitamin E2 2.84mg/100g, calcium 1.6mg/100g, iron 0.4mg/100g, its physical and chemical index and sanitary index all meet the requirement of edible oil technical standard.The nutritive value of every 500ml walnut oil is 6 times of peanut, 8.5 times of soybean, 10 times of meat, 12 times of egg, 25 times of milk, has unique nourishing, nutrition, health-care effect, is described as precious high-grade nutrient health care oil.
Walnut is a kind of senior pollution-free food, the multiple unsaturated acids up to about 90% is rich in the walnut oil of walnut oil cold press, wherein linoleic acid content is more, for 3 to 4 times of common rapeseed oil content, linoleic acid is the aliphatic acid of needed by human, as lacked required aliphatic acid, all systems of human body all there will be exception.But human body self can not synthesize linoleic acid, must lean on and absorb from food, and general edible vegetable oil can not supply the linoleic acid of human body normal need.
Walnut oil, in leaching process, needs to carry out cleaning impurity to it, makes it reach high quality oils.
Summary of the invention
The object of the invention is, by designing a set of multiple stage filtration system, to make walnut oil reach the standard of ultrahigh quality oil.
For realizing above technical purpose, the technical solution adopted in the utility model: the impurity multiple stage filtration system in a kind of production technology of walnut oil, is characterized in that it comprises feed pipe (1), divides feed bin (3), primary filter (2), secondary filter (4), top closure (5), fluid to collect storehouse (6), tube connector (7), fine filter (8); Feed pipe (1) connects the bottom of point feed bin (3), the top of feed bin (3) is divided evenly to be provided with primary filter (2), the endoporus of primary filter (2) aims at the installing hole at point feed bin (3) top, and the top of primary filter (2) is by top closure (5) press seal; Be positioned at a point feed bin (3) top and be provided with secondary filter (4), it is inner that all primary filters (2) are positioned at secondary filter (4), and the top of secondary filter (4) is by top closure (5) press seal; Divide feed bin (3) and secondary filter (4) to be positioned at fluid and collect inside, storehouse (6), fluid collects bottom, storehouse (6) and is provided with the tube connector (7) be communicated with fine filter (8); Described fine filter (8) is provided with micro porous filtration sieve (82) and liquid level peephole (81), and fine filter (8) bottom is provided with discharge nozzle (9).
The area of described micro porous filtration sieve (82) is 5-20 times of tube connector (7) cross-sectional area.
Beneficial effect of the present invention: classified filtering can be carried out to impurity by three-level filter device, thus better can realize filter effect.This system another one advantage is that impurity can not drop out in beneath through hole when more renew cartridge.Described fine filter is provided with and liquid level peephole, just can determine whether to need to change micro porous filtration sieve by the height observing fluid liquid level in liquid level peephole.Native system structure is simple, and manufacturing cost is lower.
Accompanying drawing explanation
Fig. 1 is the structural representation of native system.
Detailed description of the invention
In order to make those skilled in the art understand technical scheme of the present invention better, describe the present invention below in conjunction with accompanying drawing, the description of this part is only exemplary and explanatory, should not have any restriction to protection scope of the present invention.
Referring to Fig. 1, structural relation of the present utility model is: it comprises feed pipe 1, divides feed bin 3, primary filter 2, secondary filter 4, top closure 5, fluid to collect storehouse 6, tube connector 7, fine filter 8; Feed pipe 1 connects the bottom of point feed bin 3, and the top of point feed bin 3 is evenly provided with primary filter 2, and the endoporus of primary filter 2 aims at the installing hole at point feed bin 3 top, and the top of primary filter 2 is by top closure 5 press seal; Be positioned at point feed bin 3 top and be provided with secondary filter 4, it is inner that all primary filters 2 are positioned at secondary filter 4, and the top of secondary filter 4 is by top closure 5 press seal; Divide feed bin 3 and secondary filter 4 to be positioned at fluid and collect inside, storehouse 6, fluid collects the tube connector 7 being provided with bottom storehouse 6 and being communicated with fine filter 8; Described fine filter 8 is provided with micro porous filtration sieve 82 and liquid level peephole 81, is provided with discharge nozzle 9 bottom fine filter 8, and the area of described micro porous filtration sieve 82 is 5-20 times of tube connector 7 cross-sectional area.
Operation principle of the present utility model: the walnut oil with impurity enters into point feed bin 3 by feed pipe 1, divide the walnut oil in feed bin 3 to carry out first time by primary filter 2 to filter, carry out second time from primary filter 2 walnut oil out through secondary filter 4 to filter, walnut oil through filtering for the second time enters fluid and collects storehouse 6, the walnut oil that fluid collects in storehouse 6 enters into fine filter 8 by tube connector 7, and micro porous filtration is sieved 82 pairs of walnut oils and carried out last filtration together.After micro porous filtration sieve 82 uses a period of time, the sieve aperture of micro porous filtration sieve 82 is easily blocked, judge that 82 blocked degree are sieved in micro porous filtration by the height of the liquid level position observing liquid level peephole 81, judge that micro porous filtration sieve 82 is the need of replacing further.
Claims (2)
1. the impurity multiple stage filtration system in production technology of walnut oil, is characterized in that it comprises feed pipe (1), divides feed bin (3), primary filter (2), secondary filter (4), top closure (5), fluid to collect storehouse (6), tube connector (7), fine filter (8); Feed pipe (1) connects the bottom of point feed bin (3), the top of feed bin (3) is divided evenly to be provided with primary filter (2), the endoporus of primary filter (2) aims at the installing hole at point feed bin (3) top, and the top of primary filter (2) is by top closure (5) press seal; Be positioned at a point feed bin (3) top and be provided with secondary filter (4), it is inner that all primary filters (2) are positioned at secondary filter (4), and the top of secondary filter (4) is by top closure (5) press seal; Divide feed bin (3) and secondary filter (4) to be positioned at fluid and collect inside, storehouse (6), fluid collects bottom, storehouse (6) and is provided with the tube connector (7) be communicated with fine filter (8); Described fine filter (8) is provided with micro porous filtration sieve (82) and liquid level peephole (81), and fine filter (8) bottom is provided with discharge nozzle (9).
2. the impurity multiple stage filtration system in a kind of production technology of walnut oil according to claim 1, is characterized in that the area of micro porous filtration sieve (82) is 5-20 times of tube connector (7) cross-sectional area.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520318410.0U CN204601766U (en) | 2015-05-18 | 2015-05-18 | Impurity multiple stage filtration system in a kind of production technology of walnut oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520318410.0U CN204601766U (en) | 2015-05-18 | 2015-05-18 | Impurity multiple stage filtration system in a kind of production technology of walnut oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204601766U true CN204601766U (en) | 2015-09-02 |
Family
ID=53954357
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520318410.0U Expired - Fee Related CN204601766U (en) | 2015-05-18 | 2015-05-18 | Impurity multiple stage filtration system in a kind of production technology of walnut oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204601766U (en) |
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2015
- 2015-05-18 CN CN201520318410.0U patent/CN204601766U/en not_active Expired - Fee Related
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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: 20150902 Termination date: 20160518 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |