CN220317724U - Refining device - Google Patents
Refining device Download PDFInfo
- Publication number
- CN220317724U CN220317724U CN202321840948.9U CN202321840948U CN220317724U CN 220317724 U CN220317724 U CN 220317724U CN 202321840948 U CN202321840948 U CN 202321840948U CN 220317724 U CN220317724 U CN 220317724U
- Authority
- CN
- China
- Prior art keywords
- tank
- crude oil
- phosphoric acid
- refining
- clay
- 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.)
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- 238000007670 refining Methods 0.000 title claims abstract description 39
- 238000002156 mixing Methods 0.000 claims abstract description 24
- 238000006243 chemical reaction Methods 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000006260 foam Substances 0.000 claims abstract description 8
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 96
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 48
- 239000004927 clay Substances 0.000 claims description 45
- 239000000428 dust Substances 0.000 claims description 19
- 239000002699 waste material Substances 0.000 claims description 11
- 239000008258 liquid foam Substances 0.000 claims description 8
- 238000003466 welding Methods 0.000 claims description 6
- 239000010779 crude oil Substances 0.000 abstract description 55
- 239000008157 edible vegetable oil Substances 0.000 abstract description 6
- 239000000049 pigment Substances 0.000 abstract description 5
- 238000004332 deodorization Methods 0.000 abstract description 2
- 239000002932 luster Substances 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 22
- 235000019198 oils Nutrition 0.000 description 22
- 238000007599 discharging Methods 0.000 description 6
- 235000015112 vegetable and seed oil Nutrition 0.000 description 5
- 239000008158 vegetable oil Substances 0.000 description 5
- 239000004519 grease Substances 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 235000013311 vegetables Nutrition 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 150000003904 phospholipids Chemical class 0.000 description 3
- 239000000084 colloidal system Substances 0.000 description 2
- 238000004042 decolorization Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- QBKSWRVVCFFDOT-UHFFFAOYSA-N gossypol Chemical compound CC(C)C1=C(O)C(O)=C(C=O)C2=C(O)C(C=3C(O)=C4C(C=O)=C(O)C(O)=C(C4=CC=3C)C(C)C)=C(C)C=C21 QBKSWRVVCFFDOT-UHFFFAOYSA-N 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 1
- QHOPXUFELLHKAS-UHFFFAOYSA-N Thespesin Natural products CC(C)c1c(O)c(O)c2C(O)Oc3c(c(C)cc1c23)-c1c2OC(O)c3c(O)c(O)c(C(C)C)c(cc1C)c23 QHOPXUFELLHKAS-UHFFFAOYSA-N 0.000 description 1
- 238000009874 alkali refining Methods 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229930000755 gossypol Natural products 0.000 description 1
- 229950005277 gossypol Drugs 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000000787 lecithin Substances 0.000 description 1
- 229940067606 lecithin Drugs 0.000 description 1
- 235000010445 lecithin Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- -1 mucus Substances 0.000 description 1
- 210000003097 mucus Anatomy 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Fats And Perfumes (AREA)
Abstract
The utility model provides a refining device, which relates to the technical field of edible oil refining and comprises a bottom plate and a refining mechanism, wherein a supporting frame is welded at the top end of the bottom plate, an operating table is welded at the other end of the supporting frame, a crude oil tank is arranged at one side of the operating table, a water pump is connected with the bottom end of the crude oil tank through bolts, and the refining mechanism is arranged at one side of the crude oil tank. The collocation setting of carclazyte blending tank, carclazyte premixing tank and decoloration jar can carry out the reaction with carclazyte and crude oil after fully mixing, can get rid of various pigment in the crude oil effectively, make the crude oil become more clear transparent, the foam catcher can handle floater and the foam on the surface of crude oil, promote the color and luster of crude oil, the peculiar smell that exists in the crude oil also can be got rid of effectively to the decoloration jar simultaneously, increase the mellow degree of crude oil, multiple refining treatment can be effectual carry out deacidification, decoloration and deodorization to the crude oil and handle, the purity of crude oil has been improved effectively.
Description
Technical Field
The utility model relates to the technical field of edible oil refining, in particular to a refining device.
Background
The oil is obtained by freshly squeezing a plurality of grease-enriched plants, and a large amount of harmful and useless impurities such as gossypol, protein, phospholipid, mucus, water and the like which are unfavorable for eating, storage, industrial production and the like exist in the oil, and the impurities not only affect the edible value and safe storage of the grease, but also bring difficulty to deep processing, so that a refining device is needed.
Through retrieval, the patent number is CN113736559A, which provides a refining system for vegetable squeezed edible oil, and relates to the technical field of edible oil refining; the refining system comprises a shell, a shell cover, a motor, a filter plate, a first groove, a fourth groove and a first column; the motor rotates, the filter plate rotates to stir vegetable oil in the shell, alkali refining materials in the vegetable oil are fully mixed with the vegetable oil, the filter plate filters vegetable residues in the vegetable oil, the filter plate contacts with a second plate on the first plate, the second plate scrapes the vegetable residues adhered to the surface of the filter plate, and when the filter plate and the first plate reach a state parallel to each other, the vegetable residues scraped by the second plate enter the collecting bin, so that the quality of the vegetable oil is improved; when the motor drives the filter plate to rotate along the inner wall of the shell, the first column is contacted with the lower end of the inner part of the shell, and the first column rotates, so that the friction force between the filter plate and the shell is reduced to a certain extent, the service life of the filter plate is prolonged to a certain extent, and when the motor is used, phospholipid substances in edible oil can be effectively removed, the purity of the edible oil is improved, but in practice, the odor and the heterochromatic treatment of fresh pressed oil are not carried out, the crude oil treated by the device has deeper and opaque color and other problems, and meanwhile, more odor, froth and impurities possibly exist, and the purification degree is not high.
Thus we provide a refining apparatus.
Disclosure of Invention
The present utility model aims to provide a refining apparatus which solves the problems set forth in the background art.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a refining device, includes bottom plate and refining mechanism, the top welding of bottom plate has the support frame, the top welding of support frame has the operation panel, one side of operation panel is provided with the crude oil jar, the bottom bolted connection of crude oil jar has the water pump, one side of crude oil jar is provided with the refining mechanism, the port buckle of water pump is connected with the oil pipe, the other end buckle of oil pipe is connected with phosphoric acid mixer.
Preferably, the refining mechanism comprises an oil delivery pipe, a phosphoric acid mixer, a phosphoric acid bin, a phosphoric acid reaction tank, a clay mixing tank, a clay premixing tank, a clay feeding port, a discharging machine, a pulse dust collector, a waste port, a decoloring tank, a liquid foam catcher, a filter plate and an oil outlet.
Preferably, a phosphoric acid bin is welded at the top end of the phosphoric acid mixer, and a phosphoric acid reaction tank is welded at the bottom end of the phosphoric acid mixer.
Preferably, a clay mixing tank is arranged on one side of the phosphoric acid reaction tank, a clay premixing tank is welded at the top end of the clay mixing tank, and a clay feeding port is welded at the top end of the clay premixing tank.
Preferably, a discharging machine is connected with a port of the clay mixing tank in a threaded manner, a pulse dust collector is connected with the lower side of the clay mixing tank through a pipeline, and a waste port is fixedly connected to one side of the pulse dust collector.
Preferably, a decolorizing tank is connected above the pulse dust collector through a pipeline, and a liquid foam catcher is welded at the top end of the decolorizing tank.
Preferably, a filter is arranged on one side of the pulse dust collector, a filter plate is inserted in the filter, and an oil outlet is arranged at a port of the filter.
Compared with the prior art, the utility model has the beneficial effects that:
according to the refining device, through the arrangement of an oil conveying pipe, a phosphoric acid mixer, a phosphoric acid bin, a phosphoric acid reaction tank, a carclazyte mixing tank, a carclazyte premixing tank, a carclazyte feeding port, a discharging machine, a pulse dust remover, a waste material port, a decoloring tank, a liquid foam catcher, a filter plate and an oil outlet, crude oil and phosphoric acid can be fully mixed and reacted, deacidification treatment of the crude oil is facilitated, and the contents of phosphoric acid and lecithin in the crude oil are effectively reduced.
The collocation setting of carclazyte blending tank, carclazyte premixing tank and decoloration jar can carry out the reaction with carclazyte and crude oil after fully mixing, can get rid of various pigment in the crude oil effectively, make the crude oil become more clear transparent, the foam catcher can handle floater and the foam on the surface of crude oil, promote the color and luster of crude oil, the peculiar smell that exists in the crude oil also can be got rid of effectively to the decoloration jar simultaneously, increase the mellow degree of crude oil, multiple refining treatment can be effectual carry out deacidification, decoloration and deodorization to the crude oil and handle, the purity of crude oil has been improved effectively.
Drawings
FIG. 1 is a schematic diagram of the front structure of the present utility model;
FIG. 2 is a right side view of the present utility model;
FIG. 3 is a schematic view of the left side view of the present utility model;
FIG. 4 is a schematic diagram of the filter and filter plate of the present utility model.
Reference numerals in the drawings: 1. a bottom plate; 2. a support frame; 3. an operation table; 4. a crude oil tank; 5. a water pump; 6. a refining mechanism; 601. an oil delivery pipe; 602. a phosphoric acid mixer; 603. a phosphoric acid bin; 604. a phosphoric acid reaction tank; 605. a clay mixing tank; 606. a clay premixing tank; 607. a clay feeding port; 608. a discharging machine; 609. a pulse dust collector; 610. a waste port; 611. a decoloring tank; 612. a liquid foam catcher; 613. a filter; 614. a filter plate; 615. an oil outlet.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Referring to fig. 1-4, the present utility model provides a technical solution: the utility model provides a refining device, includes bottom plate 1 and refining mechanism 6, and the top welding of bottom plate 1 has support frame 2, and the top welding of support frame 2 has operation panel 3, and one side of operation panel 3 is provided with crude oil tank 4, and the bottom bolted connection of crude oil tank 4 has water pump 5, and one side of crude oil tank 4 is provided with refining mechanism 6, and the port buckle of water pump 5 is connected with oil pipe 601, and the other end buckle of oil pipe 601 is connected with phosphoric acid mixer 602.
Further, the refining mechanism 6 comprises an oil delivery pipe 601, a phosphoric acid mixer 602, a phosphoric acid bin 603, a phosphoric acid reaction tank 604, a clay mixing tank 605, a clay premixing tank 606, a clay feeding port 607, a discharging machine 608, a pulse dust collector 609, a waste port 610, a decoloring tank 611, a foam catcher 612, a filter 613, a filter plate 614 and an oil outlet 615, and an agitating rod in the phosphoric acid mixer 602 can be used for fully mixing input crude oil and phosphoric acid, so that subsequent refining treatment is facilitated.
Further, a phosphoric acid bin 603 is welded at the top end of the phosphoric acid mixer 602, a phosphoric acid reaction tank 604 is welded at the bottom end of the phosphoric acid mixer 602, a water pump 5 for providing a pump pressure is connected at the bottom ends of the phosphoric acid reaction tank 604 and the crude oil tank 4, the phosphoric acid reaction tank 604 provides proper reaction conditions for crude oil and phosphoric acid, and the crude oil and phosphoric acid are fully reacted, so that phospholipid colloid and non-hydratable colloid in the oil are removed.
Further, a clay mixing tank 605 is arranged on one side of the phosphoric acid reaction tank 604, a clay premixing tank 606 is welded at the top end of the clay mixing tank 605, a clay feeding port 607 is welded at the top end of the clay premixing tank 606, pigment in oil is adsorbed by clay after clay and crude oil in the clay mixing tank 605 are fully mixed, and meanwhile, impurities in the oil can be adsorbed, so that the color of grease is improved, and the quality of the grease is improved.
Further, a discharging machine 608 is connected to a port of the clay mixing tank 605 in a threaded manner, a pulse dust collector 609 is connected to the lower portion of the clay mixing tank 605 through a pipeline, a waste material port 610 is fixedly connected to one side of the pulse dust collector 609, clay in crude oil can be separated through high-frequency pulses by the pulse dust collector 609, clay is discharged from the waste material port 610, and the crude oil continues to enter refining.
Further, a decolorizing tank 611 is connected above the pulse dust collector 609 through a pipeline, a liquid foam catcher 612 is welded at the top end of the decolorizing tank 611, the activated carbon in the decolorizing tank 611 is used for adsorbing residual pigment of crude oil, further decolorizing treatment is completed, the color of the crude oil becomes pure, a silk screen in the liquid foam catcher 612 can remove liquid foam on the surface of the crude oil through filtering the crude oil, and the purity of refined oil is increased.
Further, a filter 613 is arranged on one side of the pulse dust collector 609, a filter plate 614 is inserted in the filter 613, an oil outlet 615 is arranged at a port of the filter 613, and the filter plate 614 in the filter 613 filters peculiar smell and possible particulate matters.
Working principle: firstly, a refining device is moved to a working position, firstly, unrefined crude oil is added into a crude oil tank 4 from an oil inlet, phosphoric acid is added into a phosphoric acid bin 603, a clay is added into a clay feeding port 607, secondly, an operation table 3 controls the device to start working, a water pump 5 at the bottom end of the crude oil tank 4 and a phosphoric acid reaction tank 604 provides pressure so as to facilitate subsequent operation, thirdly, crude oil and phosphoric acid are fully mixed in a phosphoric acid mixer 602, then the crude oil and phosphoric acid are injected into the phosphoric acid reaction tank 604 for deacidification treatment, fourthly, the deacidified crude oil and clay are fully reacted in the clay mixing tank 605 after being mixed in advance by a clay premixing tank 606, pigment in the crude oil is adsorbed by clay, decolorization treatment of the crude oil is realized, the processed crude oil is injected into a pulse dust remover 609 for treatment, sediment generated after the clay and deacidification in the crude oil are removed, the waste material is discharged from a waste material port 610, and the crude oil is injected into an active carbon bleaching tank 611 for further decolorization treatment, and a filter is further carried out by a filter screen 612 for foam filter, and a filter plate is used for realizing the filter of foam removal of the crude oil, and finally, the filter is finished.
Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (7)
1. A refining apparatus, characterized in that: including bottom plate (1) and refining mechanism (6), the top welding of bottom plate (1) has support frame (2), the top welding of support frame (2) has operation panel (3), one side of operation panel (3) is provided with oil tank (4), the bottom bolted connection of oil tank (4) has water pump (5), one side of oil tank (4) is provided with refining mechanism (6), the port buckle of water pump (5) is connected with oil pipe (601), the other end buckle of oil pipe (601) is connected with phosphoric acid mixer (602).
2. A refining apparatus as claimed in claim 1, characterized in that the refining means (6) comprise an oil delivery pipe (601), a phosphoric acid mixer (602), a phosphoric acid bin (603), a phosphoric acid reaction tank (604), a clay mixing tank (605), a clay premixing tank (606), a clay feeding port (607), a discharger (608), a pulse dust collector (609), a waste port (610), a decolorizing tank (611), a foam catcher (612), a filter (613), a filter plate (614) and an oil outlet (615).
3. A refining apparatus as claimed in claim 1, characterized in that the top end of the phosphoric acid mixer (602) is welded with a phosphoric acid bin (603), and the bottom end of the phosphoric acid mixer (602) is welded with a phosphoric acid reaction tank (604).
4. A refining apparatus as claimed in claim 3, characterized in that a clay mixing tank (605) is arranged on one side of the phosphoric acid reaction tank (604), a clay premixing tank (606) is welded on top of the clay mixing tank (605), and a clay feeding port (607) is welded on top of the clay premixing tank (606).
5. The refining device according to claim 4, characterized in that a discharge machine (608) is connected to a port of the clay mixing tank (605) in a threaded manner, a pulse dust collector (609) is connected to the lower portion of the clay mixing tank (605) through a pipeline, and a waste port (610) is fixedly connected to one side of the pulse dust collector (609).
6. A refining apparatus as claimed in claim 5, characterized in that the upper part of the pulse dust collector (609) is connected with a decolorizing tank (611) through a pipeline, and a liquid foam catcher (612) is welded at the top end of the decolorizing tank (611).
7. The refining device according to claim 5, characterized in that a filter (613) is arranged on one side of the pulse dust collector (609), a filter plate (614) is inserted in the filter (613), and an oil outlet (615) is arranged at a port of the filter (613).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321840948.9U CN220317724U (en) | 2023-07-13 | 2023-07-13 | Refining device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321840948.9U CN220317724U (en) | 2023-07-13 | 2023-07-13 | Refining device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220317724U true CN220317724U (en) | 2024-01-09 |
Family
ID=89425306
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321840948.9U Active CN220317724U (en) | 2023-07-13 | 2023-07-13 | Refining device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220317724U (en) |
-
2023
- 2023-07-13 CN CN202321840948.9U patent/CN220317724U/en active Active
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| GR01 | Patent grant | ||
| GR01 | Patent grant |