CN217265590U - Rubber seed oil deacidification device - Google Patents
Rubber seed oil deacidification device Download PDFInfo
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- CN217265590U CN217265590U CN202220468791.0U CN202220468791U CN217265590U CN 217265590 U CN217265590 U CN 217265590U CN 202220468791 U CN202220468791 U CN 202220468791U CN 217265590 U CN217265590 U CN 217265590U
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/02—Refining fats or fatty oils by chemical reaction
- C11B3/06—Refining fats or fatty oils by chemical reaction with bases
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/001—Refining fats or fatty oils by a combination of two or more of the means hereafter
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/008—Refining fats or fatty oils by filtration, e.g. including ultra filtration, dialysis
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/10—Refining fats or fatty oils by adsorption
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/16—Refining fats or fatty oils by mechanical means
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
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- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Drying Of Solid Materials (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Cleaning By Liquid Or Steam (AREA)
Abstract
The utility model discloses a rubber seed oil deacidification device, include: the system comprises a proportioning pump, a heater, a mixer, a pressure stabilizing reactor and at least one separator; the rubber seed oil to be processed and the alkaline substance solution can be proportioned according to a preset proportion through a proportioning pump, the rubber seed oil to be processed can be heated by a heater, then mixed with the alkaline substance solution in a mixer, and then enter a pressure stabilizing reactor for deacidification reaction, and enter a separator for oil-soap separation after deacidification; the utility model discloses technical scheme can control the proportion of rubber seed oil and alkaline solution through setting up the ratio of joining in marriage the pump earlier, can heat rubber seed oil through the heater, can mix the two fully through the blender, then carry out the deacidification reaction in getting into the steady voltage reactor again, has improved the deacidification rate, sets up the separating centrifuge and can make the oil soap separation more complete.
Description
Technical Field
The utility model relates to an oil refining field, in particular to rubber seed oil deacidification device.
Background
In the refining process of refined oil, the deacidification process is mostly included, especially for the refining of rubber seed oil, the deacidification rate and the separation degree of oil soap directly influence the refining effect of the rubber seed oil, and the deacidification rate of the existing deacidification equipment is lower, and the separation of the oil soap after deacidification is not complete enough.
SUMMERY OF THE UTILITY MODEL
The utility model provides a rubber seed oil deacidification device aims at solving the problem that mentions in the above-mentioned background art.
In order to achieve the above object, the utility model provides a rubber seed oil deacidification device, include:
the proportioning pump is provided with a first inlet, a second inlet, a first outlet and a second outlet, the first inlet is used for adding an alkaline substance solution, the second inlet is used for adding the rubber seed oil to be processed, the first outlet is used for flowing out the alkaline substance solution, and the second outlet is used for flowing out the rubber seed oil;
the inlet of the heater is communicated with the second outlet;
a mixer having an inlet in communication with the first outlet and the heater outlet, respectively;
the inlet of the pressure stabilizing reactor is communicated with the outlet of the mixer;
the separator is provided with a separator inlet, a nigre outlet and a crude oil outlet, the separator inlet is communicated with the pressure stabilizing reactor outlet, the nigre outlet is used for the nigre produced by deacidification of the rubber seed oil to be processed to flow out, and the crude oil outlet is used for the crude oil produced by deacidification of the rubber seed oil to be processed to flow out.
Optionally, the rubber seed oil deacidification device still includes:
the inlet of the intermediate oil storage tank is communicated with the crude oil outlet;
the oil transfer pump has the oil transfer pump import, first oil transfer pump export and second oil transfer pump export, the oil transfer pump import intercommunication the export of middle oil storage tank, first oil transfer pump export is used for the intercommunication the second import, the second oil transfer pump export is used for supplying after the deacidification is qualified the rubber seed oil discharges.
Optionally, the rubber seed oil deacidification device further comprises an alkali liquor tank and an oil tank;
the alkali liquor tank is used for containing the alkaline substance solution, and an outlet of the alkali liquor tank is communicated with the first inlet;
the oil tank is used for containing the rubber seed oil to be processed, the outlet of the first oil delivery pump is communicated with the inlet of the oil tank, and the outlet of the oil tank is communicated with the second inlet.
Optionally, the rubber seed oil deacidification device further comprises:
the first filter is arranged between the lye tank and the proportioning pump, an inlet of the first filter is communicated with an outlet of the lye tank, and an outlet of the first filter is communicated with the first inlet;
and the second filter is arranged between the oil tank and the proportioning pump, the inlet of the second filter is communicated with the outlet of the oil tank, and the outlet of the second filter is communicated with the second inlet.
Optionally, rubber seed oil deacidification device still includes clear oil skimming case, clear oil skimming case is located the separating centrifuge with between the middle oil storage tank, the import intercommunication of clear oil skimming case the crude oil export, the export intercommunication of clear oil skimming case the import of middle oil storage tank.
Optionally, the rubber seed oil deacidification device further comprises a soapstock tank, and an inlet of the soapstock tank is communicated with the soapstock outlet.
Optionally, the rubber seed oil deacidification device further comprises a soapstock pump and an oil removing pot, wherein an inlet of the soapstock pump is communicated with an outlet of the soapstock tank, and an outlet of the soapstock pump is used for being communicated with the oil removing pot.
Optionally, rubber seed oil deacidification device still includes the waste oil bucket, the import of waste oil bucket with the second export the steady voltage reactor export and whole crude oil export intercommunication.
Optionally, the rubber seed oil deacidification device further comprises a hot water tank and a high-level water tank, the hot water tank is provided with heating equipment, a water outlet of the hot water tank is communicated with a water inlet of the high-level water tank, and a water outlet of the high-level water tank is communicated with all inlets of the separator.
Optionally, the rubber seed oil deacidification device further comprises a steam distributor, wherein the steam distributor is provided with a steam outlet, and the steam outlet is communicated with the separator inlet of all the separators.
The technical scheme of the utility model, through setting up than joining in marriage pump, heater, blender and steady voltage reactor, can realize joining in marriage alkaline material solution and waiting to process rubber seed oil according to the predetermined proportion, heating, after intensive mixing, reentrant steady voltage reactor carries out the deacidification reaction, has improved the deacidification rate; then deacidified and separated in a separator to separate oil and soap, so that the oil and soap are separated more completely.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the embodiments or the prior art descriptions will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the structures shown in the drawings without creative efforts.
Fig. 1 is a schematic structural diagram of an embodiment of a rubber seed oil deacidification apparatus of the present invention;
reference numerals: 100-proportioning pump, 110-lye tank, 120-oil tank, 130-heater, 140-mixer, 150-pressure stabilizing reactor, 160-steam distributor, 170-separator, 180-high level water tank, 190-hot water tank, 200-waste oil tank, 210-soapstock tank, 220-soapstock pump, 230-clear oil skimmer, 240-intermediate oil storage tank and 250-oil transfer pump.
The objects, features and advantages of the present invention will be further described with reference to the accompanying drawings.
Detailed Description
The utility model provides a rubber seed oil deacidification device.
As shown in fig. 1, the deacidification apparatus according to an embodiment of the present invention includes a proportioning pump 100, a heater 130, a mixer 140, a pressure-stabilizing reactor 150, and at least one separator 170. The proportioning pump 100 is provided with a first inlet, a second inlet, a first outlet and a second outlet, wherein the first inlet is used for adding an alkaline substance solution, the second inlet is used for adding rubber seed oil to be processed, the first outlet is used for flowing out the alkaline substance solution, and the second outlet is used for flowing out the rubber seed oil; the inlet of the heater 130 is communicated with the second outlet; a mixer 140, an inlet of the mixer 140 being in communication with the first outlet and an outlet of the heater 130, respectively; a pressure stabilizing reactor 150, wherein the inlet of the pressure stabilizing reactor 150 is communicated with the outlet of the mixer 140; the separator 170 is provided with a separator inlet, a nigre outlet and a crude oil outlet, the separator inlet is communicated with the outlet of the pressure stabilizing reactor 150, the nigre outlet is used for the nigre produced by deacidification of the rubber seed oil to be processed to flow out, and the crude oil outlet is used for the crude oil produced by deacidification of the rubber seed oil to be processed to flow out.
Taking the example that the alkaline substance solution adopts a sodium hydroxide aqueous solution and/or a potassium hydroxide aqueous solution, after the proportioning pump 100 is set according to the preset proportion parameters, the alkaline substance solution and the rubber seed oil to be processed respectively flow out from the first outlet and the second outlet according to the preset proportion. The heater 130 is located behind the proportioning pump 100, the mixer 140 is located behind the heater 130, the inlet of the mixer 140 is respectively communicated with the first outlet and the outlet of the heater 130, namely, the rubber seed oil to be processed flowing out of the second outlet is led to the heater 130 for heating, and flows to the inlet of the mixer 140 from the outlet of the heater 130 after being heated, and the alkaline substance solution flows out of the first outlet of the proportioning pump 100 and is directly communicated to the inlet of the mixer 140 without passing through the heater 130, so that the alkaline substance solution and the heated rubber seed oil to be processed meet at the inlet of the mixer 140 and are fully mixed in the mixer 140. Wherein the mixer 140 may be a butterfly mixer or other type of mixer. After the alkaline substance solution and the rubber seed oil to be processed are mixed by the mixer 140, the mixture enters the pressure stabilizing reactor 150 from the outlet of the mixer 140, and the deacidification reaction is carried out in the pressure stabilizing reactor 150. The mixing proportion of the rubber seed oil to be processed and the alkaline substance solution is controlled by the proportioning pump 100, the rubber seed oil to be processed is heated by the heater 130 and then is uniformly mixed with the alkaline substance solution in the mixer 140, the uniformly mixed solution is led to the pressure stabilizing reactor 150, and the mixed solution of the nigre and the deacidified crude oil is obtained after reaction, wherein the soapstock is heated by the heater 130 and then enters the mixer 140 for mixing, so that the deacidification speed can be increased, the reaction time can be shortened, the pressure and the temperature during the deacidification reaction can be ensured by arranging the pressure stabilizing reactor 150, and the deacidification rate is increased.
In the embodiment of the present application, taking three separators 170 as an example, inlets of the three separators 170 are all communicated with an outlet of the pressure stabilizing reactor 150, so that the deacidified soapstock and the deacidified crude oil enter the separator 170 from the inlet of the separator 170 to perform oil-soap separation. The separator 170 is preferably a tubular centrifuge, in this embodiment, the three separators 170 all adopt tubular centrifuges, and the reacted deacidified crude oil and soapstock mixed solution flows into the three separators 170 under the control of the pressure stabilizing reactor 150 to separate deacidified crude oil from soapstock; it should be noted that in the present embodiment, three first separators 170 are provided, and in other embodiments, there may be one, two or more first separators 170, and the number of the first separators 170 is not limited in the present technical solution, and in other embodiments, the three first separators 170 may be separators with different models partially or completely.
With continued reference to fig. 1, in another embodiment, the rubber seed oil deacidification apparatus further comprises: middle oil storage tank 240 and petroleum pump 250, middle oil storage tank 240 are located after the separating centrifuge 170, and petroleum pump 250 is located after middle oil tank 120, wherein, the import of middle oil storage tank 240 and the crude oil export intercommunication of separating centrifuge 170, and petroleum pump 250 has the import of petroleum pump, first petroleum pump export and second petroleum pump export, and the import intercommunication of petroleum pump 250 the export of middle oil storage tank 240, first petroleum pump export is used for the intercommunication the second import, second petroleum pump export is used for supplying after the deacidification is qualified rubber seed oil discharges. Therefore, the deacidified crude oil separated by the oil soap flows out of the separator 170 from the crude oil outlet, firstly enters the intermediate oil storage tank 240, and is stored in the intermediate oil storage tank 240, if the deacidified crude oil is qualified after once deacidification and oil soap separation, the deacidified crude oil can directly pass through the outlet of the second oil delivery pump of the oil delivery pump 250 to the inlet of the next process equipment, such as a water washing device, so that the deacidification process and the next process (water washing) can be continuously carried out, and the refining efficiency is improved; if after once deacidifying, discover that the deacidification crude oil quality in middle oil storage tank 240 is unqualified, then can be directly lead to the second import of joining in marriage pump 100 with the deacidification crude oil in oil storage tank 120 through the first oil delivery pump export of oil delivery pump 250, carry out the secondary deacidification, after the deacidification crude oil in oil storage tank 120 is qualified, export next technology through the second oil delivery pump export, consequently, both can select continuous deacidification, improve the efficiency of whole process flow, can select secondary deacidification again, even cubic deacidification, in order to improve the deacidification rate.
With continued reference to fig. 1, in another embodiment, the rubber seed oil deacidification apparatus further comprises: a lye tank 110 and an oil tank 120; wherein the lye tank 110 is used for containing alkaline solution, and the outlet of the lye tank 110 is communicated with the first inlet of the proportioning pump 100; the oil tank 120 is used for containing rubber seed oil to be processed, an inlet of the oil tank 120 is communicated with an outlet of the first oil transfer pump 250, and an outlet of the oil tank 120 is communicated with the second inlet.
With continued reference to fig. 1, in another embodiment, the rubber seed oil deacidification apparatus further comprises: a first filter and a second filter, wherein the first filter is arranged between the lye tank 110 and the proportioning pump 100, the inlet of the first filter is communicated with the outlet of the lye tank 110, and the outlet of the first filter is communicated with the first inlet of the proportioning pump 100; the second filter is arranged between the oil tank 120 and the proportioning pump 100, the inlet of the second filter is communicated with the outlet of the oil tank 120, and the outlet of the second filter is communicated with the second inlet of the proportioning pump 100. The first inlet and the second inlet of the proportioning pump 100 are respectively provided with a filter, so that when the alkaline substance solution and the rubber seed oil to be processed enter the proportioning pump 100, the alkaline substance solution and the rubber seed oil to be processed are filtered, large-particle impurities in the alkaline substance solution are filtered, and the subsequent equipment is prevented from being blocked.
With continued reference to fig. 1, in another embodiment, the rubber seed oil deacidification apparatus further comprises: the clear oil skimmer box 230 is positioned between the separator 170 and the intermediate oil storage tank 240, the inlet of the clear oil skimmer box 230 is communicated with the crude oil outlet of the separator 170, and the outlet of the clear oil skimmer box 230 is communicated with the inlet of the intermediate oil storage tank 240. Wherein, when being equipped with a plurality of separating centrifuge 170, the crude oil export of a plurality of separating centrifuge 170 all communicates the import of clear oil skimmer box 230, when the oil soap separation, can produce the oil foam in the separating centrifuge 170, consequently, the deacidification crude oil that flows out from the crude oil export, at first get into in the clear oil skimmer box 230, goes out the oil foam in the oil deacidification crude oil, then in the middle oil storage tank 240 of getting into to can directly attack next process and use, perhaps carry out the secondary deacidification.
With continued reference to fig. 1, in another embodiment, the rubber seed oil deacidification apparatus further comprises a soapstock tank 210 and a deoiling pot, wherein the inlet of the soapstock tank 210 is communicated with the soapstock outlet, and the soapstock outlets of all separators 170 are communicated with the soapstock tank 210, so that the uniform recycling function can be achieved. In other embodiments, the soapstock pump 220 may be disposed at an outlet of the soapstock tank 210, and an inlet of the soapstock pump 220 is communicated with an outlet of the soapstock tank 210, and an outlet of the soapstock pump 220 is used for being communicated with the oil-removing pot, so that all soapstocks after oil and soap separation are firstly collected by the soapstock tank 210 and then directly conveyed to the oil-removing pot for treatment, and the treatment is more convenient and efficient.
With continued reference to fig. 1, in another embodiment, the rubber seed oil deacidification apparatus further comprises a waste oil tank 200, wherein an inlet of the waste oil tank 200 is communicated with the second outlet of the proportioning pump, the outlet of the pressure stabilizing reactor 150 and the crude oil outlet of the entire separator 170 for collecting waste oil.
With continued reference to fig. 1, in another embodiment, the rubber seed oil deacidification apparatus further includes a hot water tank 190 and a high-level water tank 180, wherein a water inlet of the hot water tank 190 is used for communicating city water or other water sources, a heating device is disposed inside the hot water tank 190, a water outlet of the hot water tank 190 is communicated with a water inlet of the high-level water tank 180, for example, after the city water enters the hot water tank 190, the city water is heated to a set temperature by the heating device and then enters the high-level water tank 180, and a water outlet of the high-level water tank 180 is communicated with inlets of all the separators 170, so that the hot water heated to the set temperature can enter the separators 170 together with the alkaline solution and the rubber seed oil to be processed, and soapstock after deacidification can be dissolved in water under the action of the hot water, while crude oil cannot be dissolved in water, so that oil and soap separation can be accelerated.
With continued reference to fig. 1, in another embodiment, the rubber seed oil deacidification apparatus further comprises a steam distributor 160, wherein the steam outlet of the steam distributor 160 is communicated with the inlets of all the separators 170, so that the steam distributed by the steam distributor 160 can be fed into the separator 170 from the inlet of the separator 170 together with the alkaline substance and the rubber seeds to be processed for oil soap separation, and the oil soap separation rate is further increased under the action of the steam.
The technical proposal of the utility model is that the setting is adopted, the pump 100, the heater 130, the mixer 140 and the pressure stabilizing reactor 150 are arranged, the alkaline substance solution and the rubber seed oil to be processed are arranged according to a certain proportion, and after heating and full mixing, the mixture enters the pressure stabilizing reactor 150 for deacidification reaction, thus improving the deacidification rate; then deacidified and sent to a separator 170 for oil and soap separation, so that the oil and soap separation is more complete; by arranging the steam distributor 160, the hot water tank 190 and the high-level water tank 180, the soap separation speed is improved, and the oil and soap separation is more thorough; through setting up middle oil storage tank 240, petroleum pump 250, not only can realize continuous deacidification, improve deacidification efficiency, can realize intermittent type formula deacidification again, improve the deacidification rate.
Claims (10)
1. The utility model provides a rubber seed oil deacidification device which characterized in that includes:
the specific mixing pump is provided with a first inlet, a second inlet, a first outlet and a second outlet, wherein the first inlet is used for adding an alkaline substance solution, the second inlet is used for adding the rubber seed oil to be processed, the first outlet is used for allowing the alkaline substance solution to flow out, and the second outlet is used for allowing the rubber seed oil to flow out;
the inlet of the heater is communicated with the second outlet;
a mixer having an inlet in communication with the first outlet and the heater outlet, respectively;
the inlet of the pressure stabilizing reactor is communicated with the outlet of the mixer;
the separator is provided with a separator inlet, a soapstock outlet and a crude oil outlet, the separator inlet is communicated with the pressure stabilizing reactor outlet, the soapstock outlet is used for flowing out of the soapstock generated by deacidification of the rubber seed oil to be processed, and the crude oil outlet is used for flowing out of the crude oil obtained after deacidification of the rubber seed oil to be processed.
2. The rubber seed oil deacidification apparatus according to claim 1, further comprising:
the inlet of the intermediate oil storage tank is communicated with the crude oil outlet;
the oil transfer pump is provided with an oil transfer pump inlet, a first oil transfer pump outlet and a second oil transfer pump outlet, the oil transfer pump inlet is communicated with the outlet of the intermediate oil storage tank, the first oil transfer pump outlet is used for communicating the second inlet, and the second oil transfer pump outlet is used for discharging the qualified rubber seed oil after deacidification.
3. The deacidification apparatus for rubber seed oil according to claim 2, further comprising an alkali liquor tank and an oil tank;
the alkali liquor tank is used for containing the alkaline substance solution, and an outlet of the alkali liquor tank is communicated with the first inlet;
the oil tank is used for containing the rubber seed oil to be processed, the outlet of the first oil delivery pump is communicated with the inlet of the oil tank, and the outlet of the oil tank is communicated with the second inlet.
4. The rubber seed oil deacidification apparatus according to claim 3, further comprising:
the first filter is arranged between the lye tank and the proportioning pump, an inlet of the first filter is communicated with an outlet of the lye tank, and an outlet of the first filter is communicated with the first inlet;
and the second filter is arranged between the oil tank and the proportioning pump, the inlet of the second filter is communicated with the outlet of the oil tank, and the outlet of the second filter is communicated with the second inlet.
5. The rubber seed oil deacidification device according to claim 2, further comprising a clear oil skimming tank, wherein the clear oil skimming tank is positioned between the separator and the intermediate oil storage tank, an inlet of the clear oil skimming tank is communicated with the crude oil outlet, and an outlet of the clear oil skimming tank is communicated with an inlet of the intermediate oil storage tank.
6. The rubber seed oil deacidification apparatus in accordance with claim 1, further comprising a soapstock tank, wherein an inlet of said soapstock tank is in communication with said soapstock outlet.
7. The rubber seed oil deacidification device according to claim 6, further comprising a soapstock pump and a deoiling pot, wherein an inlet of the soapstock pump is communicated with an outlet of the soapstock tank, and an outlet of the soapstock pump is communicated with the deoiling pot.
8. The rubber seed oil deacidification apparatus according to any one of claims 1 to 7, further comprising a waste oil tank, wherein an inlet of said waste oil tank is in communication with said second outlet, said pressure stabilization reactor outlet, and all of said crude oil outlets.
9. The rubber seed oil deacidification device according to any one of claims 1 to 7, further comprising a hot water tank and a high-level water tank, wherein the hot water tank is provided with a heating device, a water outlet of the hot water tank is communicated with a water inlet of the high-level water tank, and a water outlet of the high-level water tank is communicated with all the separator inlets.
10. The rubber seed oil deacidification apparatus defined in any one of claims 1-7, further comprising a steam distributor having a steam outlet in communication with the separator inlet of all of the separators.
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2021104212216 | 2021-04-19 | ||
| CN202110421221 | 2021-04-19 | ||
| CN202110426259 | 2021-04-20 | ||
| CN2021104262592 | 2021-04-20 | ||
| CN202110432808 | 2021-04-21 | ||
| CN2021104328087 | 2021-04-21 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217265590U true CN217265590U (en) | 2022-08-23 |
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| CN202220454110.5U Active CN217149083U (en) | 2021-04-19 | 2022-03-02 | Deodorization tank |
| CN202220442794.7U Active CN217377806U (en) | 2021-04-19 | 2022-03-02 | Continuous dewatering device of rubber seed oil |
| CN202220440686.6U Active CN218339771U (en) | 2021-04-19 | 2022-03-02 | Reaction tank |
| CN202220440688.5U Active CN217230646U (en) | 2021-04-19 | 2022-03-02 | Rubber seed oil deodorizing device |
| CN202220468791.0U Active CN217265590U (en) | 2021-04-19 | 2022-03-02 | Rubber seed oil deacidification device |
| CN202220454243.2U Active CN217265592U (en) | 2021-04-19 | 2022-03-02 | Rubber seed oil dewatering device |
| CN202220455108.XU Active CN218561380U (en) | 2021-04-19 | 2022-03-02 | Rubber seed oil washing device |
| CN202220442753.8U Active CN217265588U (en) | 2021-04-19 | 2022-03-02 | Rubber seed oil decoloration device |
| CN202210408685.8A Active CN115216362B (en) | 2021-04-19 | 2022-04-19 | Rubber seed oil and preparation method and application thereof |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202220454110.5U Active CN217149083U (en) | 2021-04-19 | 2022-03-02 | Deodorization tank |
| CN202220442794.7U Active CN217377806U (en) | 2021-04-19 | 2022-03-02 | Continuous dewatering device of rubber seed oil |
| CN202220440686.6U Active CN218339771U (en) | 2021-04-19 | 2022-03-02 | Reaction tank |
| CN202220440688.5U Active CN217230646U (en) | 2021-04-19 | 2022-03-02 | Rubber seed oil deodorizing device |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202220454243.2U Active CN217265592U (en) | 2021-04-19 | 2022-03-02 | Rubber seed oil dewatering device |
| CN202220455108.XU Active CN218561380U (en) | 2021-04-19 | 2022-03-02 | Rubber seed oil washing device |
| CN202220442753.8U Active CN217265588U (en) | 2021-04-19 | 2022-03-02 | Rubber seed oil decoloration device |
| CN202210408685.8A Active CN115216362B (en) | 2021-04-19 | 2022-04-19 | Rubber seed oil and preparation method and application thereof |
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|---|---|---|---|---|
| CN101319167B (en) * | 2008-06-13 | 2010-12-01 | 合肥工业大学 | High-acid value rice bran oil esterification depickling process |
| CN101475874A (en) * | 2009-01-21 | 2009-07-08 | 云南绿宝百瑞替代产业有限公司 | Method for acid stripping and refining of rubber seed crude oil packing thin film |
| CN101705147B (en) * | 2009-11-19 | 2012-06-27 | 中国农业科学院油料作物研究所 | Lipin deacidifying method |
| CN102559381A (en) * | 2011-12-27 | 2012-07-11 | 海南大学 | Physical deacidification method of rubber seed oil with high acid value |
| CN104877757B (en) * | 2015-06-05 | 2018-02-16 | 武汉轻工大学 | Peracid value rice bran oil synchronization depickling dewaxing technique |
| CN105132156A (en) * | 2015-08-28 | 2015-12-09 | 成都市新津迎先粮油有限公司 | Method for refining rape-seed raw oil |
| CN105131030A (en) * | 2015-09-07 | 2015-12-09 | 云南省化工研究院 | Method for preparing phosphate ester from rubber seed oil with high acid value |
| CN106854492A (en) * | 2017-02-07 | 2017-06-16 | 西双版纳华坤生物科技有限责任公司 | A kind of high acid value, the method for thermally labile grease physical deacidification deodorization and its device |
| CN108624399B (en) * | 2018-05-04 | 2022-02-22 | 海南侯臣生物科技有限公司 | Preparation process of refined rubber seed oil |
| CN109337760A (en) * | 2018-11-15 | 2019-02-15 | 绩溪瀚徽农业开发有限公司 | A kind of refining vegetable oil and preparation method thereof |
| CN109456829A (en) * | 2018-11-22 | 2019-03-12 | 西南林业大学 | A kind of preparation method of rubber seed oil |
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| CN115216362B (en) | 2024-03-01 |
| CN218339771U (en) | 2023-01-20 |
| CN217230646U (en) | 2022-08-19 |
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| CN217377806U (en) | 2022-09-06 |
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