CN218339771U - Reaction tank - Google Patents

Reaction tank Download PDF

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Publication number
CN218339771U
CN218339771U CN202220440686.6U CN202220440686U CN218339771U CN 218339771 U CN218339771 U CN 218339771U CN 202220440686 U CN202220440686 U CN 202220440686U CN 218339771 U CN218339771 U CN 218339771U
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China
Prior art keywords
coil
oil
coil pipe
inlet
outlet
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Active
Application number
CN202220440686.6U
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Chinese (zh)
Inventor
陈宏伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Suzhou Xuerong Wujiang Food Technology Co ltd
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Suzhou Xuerong Wujiang Food Technology Co ltd
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    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B3/00Refining fats or fatty oils
    • C11B3/02Refining fats or fatty oils by chemical reaction
    • C11B3/06Refining fats or fatty oils by chemical reaction with bases
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B3/00Refining fats or fatty oils
    • C11B3/001Refining fats or fatty oils by a combination of two or more of the means hereafter
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B3/00Refining fats or fatty oils
    • C11B3/008Refining fats or fatty oils by filtration, e.g. including ultra filtration, dialysis
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B3/00Refining fats or fatty oils
    • C11B3/10Refining fats or fatty oils by adsorption
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B3/00Refining fats or fatty oils
    • C11B3/16Refining fats or fatty oils by mechanical means
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/54Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • 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 reaction tank, include: the tank body is provided with a vacuum cavity, and an oil inlet and an oil outlet which are communicated with the vacuum cavity; the temperature control system comprises at least one layer of coil pipe, the at least one layer of coil pipe is arranged in the vacuum cavity, the coil pipe is provided with an inlet and an outlet which are positioned outside the vacuum cavity, and the inlet and the outlet are used for supplying water vapor or condensed water to circularly flow in the coil pipe so as to heat or cool substances in the tank body; and the stirring device is arranged in the vacuum cavity and used for stirring the substances in the tank body. The utility model discloses a temperature control system includes the one deck coil pipe at least, and the coil pipe is used for intercommunication vapor or comdenstion water to oil to the internal portion of jar heats or cools down, and vapor and comdenstion water are compared in heating oil, can not pollute the internal oil production of jar.

Description

Reaction tank
Technical Field
The utility model relates to an oil refining field, in particular to retort.
Background
In the refining process of refined oil, including treatment process such as decoloration, dehydration, generally can go on in the jar body when carrying out decoloration or dehydration to need to maintain jar proper temperature of body, set up the oil circuit pipeline in jar body mostly now, and then heat up cooperation and cooling to the jar body through the temperature of control conduction oil. In addition, in the links of storage of finished oil, saponin and the like, the tank body is mostly used, and the tank body is matched with heat conduction oil and an oil way pipeline to maintain the proper temperature in the tank body. For the temperature control mode through the heat conduction oil and the oil way pipeline, the oil leakage condition exists after long-time use, and if the refined oil is edible oil, huge pollution is undoubtedly caused to the edible oil.
SUMMERY OF THE UTILITY MODEL
The utility model provides a reaction tank, which aims at solving the problem mentioned in the background technology.
In order to achieve the above object, the utility model provides a reaction tank, include:
the tank body is provided with a vacuum cavity, and an oil inlet and an oil outlet which are communicated with the vacuum cavity;
the temperature control system comprises at least one layer of coil pipe, the at least one layer of coil pipe is arranged in the vacuum cavity, the coil pipe is provided with an inlet and an outlet which are positioned outside the vacuum cavity, and the inlet and the outlet are used for supplying water vapor or condensed water to circularly flow in the coil pipe so as to heat or cool substances in the tank body;
and the stirring device is arranged in the vacuum cavity and used for stirring the substances in the tank body.
In the embodiment of this application, temperature control system includes first coil pipe and second coil pipe, the import of first coil pipe is used for supplying water vapour to flow in, the export of first coil pipe is used for supplying water vapour to flow out, the import of second coil pipe is used for supplying the condensate water to flow in, the export of second coil pipe is used for supplying the condensate water to flow out.
In an embodiment of the present application, the first coil and the second coil are toroidal coils.
In an embodiment of the present application, the first coil pipe and the second coil pipe are spaced apart from an inner side wall of the tank body.
In this application embodiment, agitating unit includes the (mixing) shaft, the (mixing) shaft at least part stretches into the vacuum cavity, the (mixing) shaft is located part in the vacuum cavity is equipped with at least a set of stirring rake, the (mixing) shaft is located the outside part of vacuum cavity is equipped with driving motor and speed reducer.
In an embodiment of the application, the coil surrounds the stirring shaft.
In this application embodiment, at least a set of stirring rake includes first stirring rake, second stirring rake and third stirring rake, first stirring rake the second stirring rake reaches the third stirring rake is in the interval sets up on the (mixing) shaft, the coil pipe is around being located in the middle of the second stirring rake.
In the embodiment of the present application, the paddle surfaces of the first stirring paddle, the second stirring paddle and the third stirring paddle are all disposed at an included angle with the cross section of the reaction tank.
In this application embodiment, the projection of first stirring rake, second stirring rake reaches the third stirring rake in vertical direction becomes the contained angle setting.
In this application embodiment, the top of the jar body is equipped with the intercommunication the vacuum tube of vacuum cavity to and at least one sight glass, the lateral wall of the jar body still is equipped with the heat preservation.
The utility model discloses a temperature control system includes the one deck coil pipe at least, and the coil pipe is used for intercommunication vapor or comdenstion water to oil to the internal portion of jar heats or cools down, and vapor and comdenstion water are compared in heating oil, can not pollute the internal oil production of jar.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings needed to be used in the description of the embodiments or the prior art 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 view of an embodiment of a reaction tank of the present invention;
figure 2 is a top view of the reaction tank shown in the bitmap 1.
Reference numerals: 100-tank, 110-first coil, 111-steam inlet, 112-steam outlet, 120-second coil. 121-a condensed water inlet, 122-a condensed water outlet, 130 a stirring device, 131-a stirring shaft, 132-a first stirring paddle, 133-a second stirring paddle, 134-a third stirring paddle, 135-a driving motor, 136-a speed reducer, 140-a vacuum tube, 150-a sight glass, 160-a manhole, 170-an oil inlet, 180-an oil outlet and 190-a vacuum cavity.
The realization, the functional characteristics and the advantages of the utility model are further explained by combining the embodiment and referring to the attached drawings.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by a person skilled in the art without making creative efforts belong to the protection scope of the present invention.
It should be noted that, if directional indications (such as up, down, left, right, front, back, 8230; \8230;) are provided in the embodiments of the present invention, the directional indications are only used to explain the relative position relationship between the components, the motion situation, etc. in a specific posture (as shown in the attached drawings), and if the specific posture is changed, the directional indications are correspondingly changed.
In addition, if there is a description relating to "first", "second", etc. in the embodiments of the present invention, the description of "first", "second", etc. is for descriptive purposes only and is not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one of the feature. In addition, the technical solutions in the embodiments may be combined with each other, but it must be based on the realization of those skilled in the art, and when the technical solutions are contradictory to each other or cannot be realized, such a combination should not be considered to exist, and is not within the protection scope of the present invention.
As shown in fig. 1, in the embodiment of the present application, there is provided a reaction tank including: the tank body 100 is provided with a vacuum cavity 190 and an oil inlet 170 and an oil outlet 180 which are communicated with the vacuum cavity 190;
the temperature control system comprises at least one layer of coil pipe, the at least one layer of coil pipe is arranged in the vacuum cavity 190, the coil pipe is provided with an inlet and an outlet which are positioned outside the vacuum cavity 190, and the inlet and the outlet are used for supplying water vapor or condensed water to circulate in the coil pipe so as to heat or cool the substances in the tank body 100;
and a stirring device 130 provided in the vacuum chamber 190 for stirring the material in the tank 100.
As shown in fig. 1, in the embodiment of the present application, the tank 100 is substantially cylindrical, the interior of the tank 100 is hollow to form a vacuum cavity 190, and the outer side wall of the tank 100 is provided with an oil inlet 170 and an oil outlet 180, wherein the oil inlet 170 is disposed at an upper position of the tank 100, and the oil outlet 180 is disposed at a bottom of the tank 100. The reaction tank in the application can be used for multiple purposes, such as decolorization treatment for refining rubber seed oil, wherein the oil inlet 170 and the oil outlet 180 are used for allowing the rubber seed oil to be decolorized to flow in and out; for another example, the oil inlet 170 and the oil outlet 180 can be used for dewatering treatment, and the rubber seed oil to be dewatered flows in and out at the time; and for example, the oil inlet 170 and the oil outlet 180 are used for the inflow and outflow of the product oil, and so on.
A temperature control system is arranged in the vacuum cavity 190, the temperature control system comprises at least one layer of coil, namely, the coil can be a single-layer coil or a multilayer coil, and the inlet and the outlet of each coil are both positioned on the outer side of the tank body 100, so that condensed water or vapor can be conveniently guided in and out. For example, in one embodiment, only a single layer of coil is provided, and when the oil in the tank 100 needs to be heated, the inlet of the coil is connected to a steam source, so that steam enters from the inlet of the coil and flows out from the outlet, and circulates in the coil by using the steam, thereby heating the oil in the tank 100. When the oil in the tank body 100 needs to be cooled, the inlet of the coil pipe is connected with a condensed water source, so that condensed water enters from the inlet of the coil pipe and flows out from the outlet, and the condensed water circularly flows in the coil pipe, so that the oil in the tank body 100 is cooled.
For example, in another embodiment, as shown in fig. 1, the temperature control system may be provided with two layers of coils, including a first coil 110 and a second coil 120, when two layers of coils are provided, one layer of coils may be used for heating, and the other layer of coils may be used for cooling, for example, the first coil 110 is a heating coil, the second coil 120 is a cooling coil, the inlet of the first coil 110 is a steam inlet 111 for connecting with a steam source, and the outlet of the first coil 110 is a steam outlet 112; the inlet of the second coil 120 is a condensed water inlet 121 for communicating with a condensed water source, and the outlet of the second coil 120 is a condensed water outlet 122. Through setting temperature control system to two-layer coil pipe, separate control intensification or cooling respectively to when the temperature of the needs in to jar body 100 is adjusted, can quick response.
Referring to fig. 1, in an embodiment of the present application, the first coil 110 and the second coil 120 are annular coils. As shown in fig. 1, the first coil 110 and the second coil 120 are substantially circular and helical.
Referring to fig. 1, in another embodiment of the present application, the first coil 110 and the second coil 120 are spaced apart from the inner sidewall of the tank 100. For example, the diameters of the first coil pipe 110 and the second coil pipe 120 may be set to be smaller than the inner diameter of the tank body 100, and then the first coil pipe 110 and the second coil pipe 120 have a certain distance from the inner side wall of the tank body 100, so that the outer surfaces of the coil pipes can be in full contact with rubber seed oil in the tank body 100, and the temperature regulation effect can be improved.
With continued reference to fig. 1, a stirring device 130 is further disposed in the vacuum chamber 190, and the stirring device 130 can stir the oil in the vacuum chamber 190. For example, when the reaction tank is used for dehydration, the rubber seed oil to be dehydrated can be stirred by the stirring device 130 to increase the dehydration rate. For another example, when the reaction tank is used for washing, the rubber seed oil to be washed may be stirred by the stirring device 130 to improve the washing effect.
As shown in fig. 1, in the embodiment of the present application, the stirring device 130 includes a stirring shaft 131, the stirring shaft 131 at least partially extends into the vacuum cavity 190, at least one set of stirring paddles is disposed on a portion of the stirring shaft 131 located in the vacuum cavity 190, and a driving motor 135 and a speed reducer 136 are disposed on a portion of the stirring shaft 131 located outside the vacuum cavity 190. Wherein, (mixing) shaft 131 stretches into inside vacuum chamber 190 from retort's top, and the (mixing) shaft 131 that is located vacuum chamber 190 is surrounded by the coil pipe, is provided with driving motor 135 and speed reducer 136 on being located outside (mixing) shaft 131, drives (mixing) shaft 131 through driving motor 135 and drives the stirring rake and rotate, controls the speed of stirring through speed reducer 136, and the user of being convenient for adjusts. And the stirring shaft 131 is located in the middle of the coil to facilitate heat transfer by stirring to maintain a small temperature difference at various locations within the vacuum chamber 190.
Referring to fig. 1, in another embodiment, a portion of the stirring shaft 131 located in the vacuum chamber 190 is provided with a first stirring paddle 132, a second stirring paddle 133 and a third stirring paddle 134, three groups of stirring paddles are distributed on the upper portion, the middle portion and the lower portion of the vacuum chamber 190, the first stirring paddle 132, the second stirring paddle 133 and the third stirring paddle 134 are arranged on the stirring shaft 131 at intervals, the coil surrounds the second stirring paddle 133 located in the middle, the first stirring paddle 132 is located above the coil, and the third stirring paddle 134 is located below the coil, so that oil or water located in the upper portion, the middle portion or the lower portion of the vacuum chamber 190 can be fully stirred and can perform heat transfer with the coil, the stirring is more sufficient, and a smaller temperature difference in the tank 100 is further ensured.
Referring to fig. 2, in another embodiment, the first stirring paddle 132, the second stirring paddle 133 and the third stirring paddle 134 are disposed at an included angle with the cross section of the reaction tank. Specifically, the direction of three stirring rake can incline upwards, perhaps the slope is downwards, and the incline direction of three stirring rake can be the same moreover, also can be different, through setting the stirring rake to have certain inclination, is favorable to driving the flow of oil and water when the stirring.
Referring to fig. 1, in another embodiment, the projections of the first stirring paddle 132, the second stirring paddle 133 and the third stirring paddle 134 in the vertical direction form an included angle. That is, in the vertical direction, the three paddles are staggered with each other so that the paddles can be distributed in the entire space, further improving the fluidity of the oil and water inside the tank body 100.
In another embodiment of the present application, as shown in fig. 2, a vacuum tube 140 is provided on the top of the can 100 to communicate with the vacuum chamber 190, and at least one sight glass 150. The vacuum pipe 140 is located at the top of the tank 100, and the vacuum pipe 140 can be used to vacuumize the tank 100, so that when the reaction tank is used for storing product oil or soapstock oil, air in the tank 100 can be pumped out to prevent the oil in the tank 100 from being oxidized, and the oil can be stored stably. In the embodiment shown in fig. 2, four viewing mirrors 150 are provided, and the four viewing mirrors 150 are spaced apart from each other, so that the operator can observe the inside of the vacuum chamber 190 through the viewing mirrors 150, and the operator can know the processing condition inside the vacuum chamber 190 conveniently. It should be noted that the number of the mirrors 150 is not limited, and the user can set the number according to the requirement.
As shown in fig. 1, in another embodiment, an insulating layer may be further disposed on an outer side of the tank 100, and the insulating layer wraps the tank 100, so that heat loss of the tank 100 may be prevented, and thus the reaction tank may maintain a stable temperature for a long time.
In another embodiment, as shown in fig. 1, a manhole 160 may be provided on an outer side wall of the tank body 100, and a worker may enter the inside of the tank body 100 through the manhole 160, so that when a fault occurs in the tank body 100, the maintenance may be performed using the manhole 160.
The utility model discloses a temperature control system includes the one deck coil pipe at least, and the coil pipe is used for intercommunication vapor or comdenstion water to oil to the internal portion of jar heats or cools down, and vapor and comdenstion water are compared in heating oil, can not produce the pollution to the oil in the jar body 100.
The above only is the preferred embodiment of the present invention, not limiting the scope of the present invention, all the equivalent structure changes made by the contents of the specification and the drawings under the inventive concept of the present invention, or the direct/indirect application in other related technical fields are included in the patent protection scope of the present invention.

Claims (7)

1. A reaction tank, comprising:
the tank body is provided with a vacuum cavity, and an oil inlet and an oil outlet which are communicated with the vacuum cavity;
the temperature control system comprises at least one layer of coil pipe, the at least one layer of coil pipe is arranged in the vacuum cavity, the coil pipe is provided with an inlet and an outlet which are positioned outside the vacuum cavity, and the inlet and the outlet are used for supplying water vapor or condensed water to circularly flow in the coil pipe so as to heat or cool substances in the tank body;
agitating unit locates in the vacuum chamber, it is right to be used for the internal material of jar stirs, agitating unit includes the (mixing) shaft, the (mixing) shaft at least part stretches into the vacuum chamber, the (mixing) shaft is located the outside part of vacuum chamber is equipped with driving motor and speed reducer, the (mixing) shaft is located part in the vacuum chamber is equipped with first stirring rake, second stirring rake and third stirring rake, first stirring rake the second stirring rake reaches the third stirring rake is in the interval sets up on the (mixing) shaft, the coil pipe is around being located the centre the second stirring rake.
2. The retort of claim 1, wherein the temperature control system comprises a first coil and a second coil, wherein an inlet of the first coil is for inflow of water vapor, an outlet of the first coil is for outflow of water vapor, an inlet of the second coil is for inflow of condensed water, and an outlet of the second coil is for outflow of condensed water.
3. The retort of claim 2, wherein the first coil and the second coil are toroidal coils.
4. The retort of claim 2, wherein the first coil and the second coil are spaced apart from an interior side wall of the canister body.
5. The reactor tank of claim 1, wherein the paddle surfaces of the first, second and third paddles are disposed at an angle to the cross-section of the reactor tank.
6. The retort of claim 1, wherein the first, second and third paddles are angled in vertical projection.
7. A reaction tank as claimed in any one of claims 1 to 6, wherein a vacuum tube is provided on the top of the tank body for communicating with the vacuum chamber, and at least one sight glass, and the tank body is further provided with an insulating layer on the outer side wall.
CN202220440686.6U 2021-04-19 2022-03-02 Reaction tank Active CN218339771U (en)

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

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CN218339771U true CN218339771U (en) 2023-01-20

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Family Applications (9)

Application Number Title Priority Date Filing Date
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
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

Family Applications After (6)

Application Number Title Priority Date Filing Date
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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Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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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Publication number Publication date
CN217265588U (en) 2022-08-23
CN217265592U (en) 2022-08-23
CN218561380U (en) 2023-03-03
CN115216362B (en) 2024-03-01
CN217230646U (en) 2022-08-19
CN217149083U (en) 2022-08-09
CN115216362A (en) 2022-10-21
CN217377806U (en) 2022-09-06
CN217265590U (en) 2022-08-23

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