CN218561380U - Rubber seed oil washing device - Google Patents

Rubber seed oil washing device Download PDF

Info

Publication number
CN218561380U
CN218561380U CN202220455108.XU CN202220455108U CN218561380U CN 218561380 U CN218561380 U CN 218561380U CN 202220455108 U CN202220455108 U CN 202220455108U CN 218561380 U CN218561380 U CN 218561380U
Authority
CN
China
Prior art keywords
oil
outlet
inlet
washing
stirring
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.)
Active
Application number
CN202220455108.XU
Other languages
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
Original Assignee
Suzhou Xuerong Wujiang Food Technology Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Suzhou Xuerong Wujiang Food Technology Co ltd filed Critical Suzhou Xuerong Wujiang Food Technology Co ltd
Application granted granted Critical
Publication of CN218561380U publication Critical patent/CN218561380U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • 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
    • 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
    • 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
    • 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

Landscapes

  • 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 rubber seed oil washing device includes: a water washing tank, a heater, a mixer, a flowmeter and a separator; wherein the water washing tank is provided with an oil inlet and an oil outlet, and the oil inlet is used for adding the rubber seed oil to be washed; the inlet of the heater is communicated with the oil outlet of the washing tank; the inlet of the mixer is communicated with the outlet of the heater; the flowmeter is provided with a water inlet and a water outlet, the water inlet is used for adding water, and the water outlet is communicated with the inlet of the mixer; the separating centrifuge is equipped with miscella import, emulsified oil export and crude oil export, and the export of miscella import intercommunication blender, the crude oil export is used for supplying the rubber seed oil after the washing to flow out, and the emulsified oil export is used for supplying the emulsified oil outflow that the washing produced. This washing device need not to subside, avoids producing a large amount of emulsified oil, and continuous washing is efficient moreover, and the cost is lower.

Description

Rubber seed oil washing device
Technical Field
The utility model relates to an oil refining field, in particular to rubber seed oil washing device.
Background
In the refining process of refined oil, included steps such as deacidification, washing, wherein the washing step is in order to clear away the soap that forms after the deacidification from oil, and current water washing device utilizes oil and soap self density difference mostly, and it makes its two subsides the separation to stew, and not only efficiency is lower, is settling the in-process moreover, very easily appears emulsification.
SUMMERY OF THE UTILITY MODEL
The utility model provides a rubber seed oil washing device, which aims to solve the problems mentioned in the background technology.
In order to achieve the above object, the utility model provides a rubber seed oil washing device, include:
the washing tank is provided with an oil inlet and an oil outlet, and the oil inlet is used for adding the rubber seed oil to be washed;
the inlet of the heater is communicated with the oil outlet of the washing tank;
a mixer, an inlet of the mixer being in communication with an outlet of the heater;
the flow meter is provided with a water inlet and a water outlet, the water inlet is used for adding water, and the water outlet is communicated with the inlet of the mixer;
the separating centrifuge is equipped with miscella import, emulsified oil export and crude oil export, miscella import intercommunication the export of blender, the crude oil export is used for supplying the rubber seed oil outflow after the washing, the emulsified oil export is used for supplying the emulsified oil outflow that the washing produced.
Optionally, still including dividing the oil tank, divide the import of oil tank with the export intercommunication of emulsified oil, it still is equipped with first export and second export to divide the oil tank, first export intercommunication the oil inlet of washing jar, the second export is used for supplying waste water outflow.
Optionally, a crude oil outlet of the separator is provided with a first pipeline and a second pipeline, the first pipeline is communicated with an oil inlet of the water washing tank, and the second pipeline is used for communicating to a next refining node.
Optionally, the washing tank has a vacuum cavity, be equipped with double-deck coil pipe and agitating unit in the vacuum cavity, double-deck coil pipe includes heating coil pipe and cooling coil, the washing tank still is equipped with filler and wastewater outlet, in vertical direction, wastewater outlet is located the below of oil-out.
Optionally, the stirring device includes a stirring shaft, at least a part of the stirring shaft extends into the vacuum cavity, at least one group of stirring paddles is arranged on the part of the stirring shaft located in the vacuum cavity, and a driving motor and a speed reducer are arranged on the part of the stirring shaft located outside the vacuum cavity.
Optionally, the double layer coil is disposed around the stirring shaft.
Optionally, 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 interval setting on the (mixing) shaft, double-deck coil pipe is around being located the centre the second stirring rake.
Optionally, the first stirring paddle, the second stirring paddle and the third stirring paddle are arranged at included angles with the cross section of the water washing tank.
Optionally, the projections of the first stirring paddle, the second stirring paddle and the third stirring paddle in the vertical direction form an included angle.
Optionally, the rubber seed oil washing device further comprises an oil transfer pump, an inlet of the oil transfer pump is communicated with an oil outlet of the washing tank, an outlet of the oil transfer pump is provided with a third pipeline, a fourth pipeline and a fifth pipeline, the third pipeline is communicated with an inlet of the heater, the fourth pipeline is used for being communicated to a next refining node, and the fifth pipeline is used for being communicated to a previous refining node.
The utility model provides a technical scheme, through setting up washing jar, can treat washing rubber seed oil and carry out prestore, save to a quantitative back, can utilize the heater to treat washing rubber seed oil and heat, can control the proportion of hot water and rubber seed oil through the flowmeter, then can be with the hot water and the rubber seed oil intensive mixing of certain proportion through the blender, then carry out centrifugal separation in the separating centrifuge, directly lead to next technology node with the crude oil after the separation, thereby realize continuous washing, the efficiency of washing has been improved, and pass through separating centrifuge centrifugal separation, avoid subsiding and produce a large amount of emulsified oil, the small part emulsified oil that produces in centrifugal process, also can separate with the crude oil through the centrifugation, discharge through the export of difference at last, not only water washing efficiency has been improved, also avoid producing a large amount of emulsified oil.
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 the rubber seed oil washing device of the present invention.
Reference numerals: 100-a water washing tank, 200-a heater, 300-a mixer, 400-a flow meter, 500-a separator, 510-a first pipeline, 520-a second pipeline, 600-an oil transfer pump, 610-a third pipeline, 620-a fourth pipeline, 630-a fifth pipeline, 700-a wastewater tank and 800-a fuel separation tank.
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 utility model provides a rubber seed oil washing device.
As shown in fig. 1, fig. 1 is a schematic structural diagram of an embodiment of the water washing apparatus of the present invention, including: washing tank 100, heater 200, blender 300, flowmeter 400 and separating centrifuge 500, wherein, washing tank 100 has oil inlet and oil-out, the oil inlet is used for supplying treats that washing rubber seed oil adds, for example the oil inlet can communicate the deacidification technology of the refined technology of rubber seed oil, deacidification crude oil after the deacidification technology can directly flow to washing tank 100 through the oil inlet, prestore in washing tank 100, until storing unified washing after a ration again, improve the washing efficiency, save the cost. The inlet of the heater 200 is communicated with the oil outlet of the water washing tank 100, namely, after a certain amount of rubber seed oil to be washed is stored in the water washing tank 100, the water washing is started. Firstly, the rubber seed oil to be washed is conveyed to the heater 200 through the inlet of the heater 200, and the rubber seed oil to be washed is heated, wherein an oil pump or a valve can be arranged between the oil outlet of the washing tank 100 and the inlet of the heater 200 for control. The inlet of the mixer 300 is communicated with the outlet of the heater 200, so that the heated rubber seed oil to be washed flows from the outlet of the heater 200 to the inlet of the mixer 300, while the water inlet of the flow meter 400 is used for water supply, such as a hot water pump, a hot water tank or the like, and the outlet of the flow meter 400 is communicated with the inlet of the mixer 300, so that the hot water with the flow controlled by the flow meter 400 and the rubber seed oil to be washed heated by the heater 200 are merged at the inlet of the mixer 300 and are fully mixed in the mixer 300. Wherein the flow meter 400 can be a glass rotameter 400. And separating centrifuge 500 is equipped with the miscella import, the miscella import communicates with the export of blender 300, thereby water and the crude oil of waiting to wash rubber seed oil through the intensive mixing production, waste water and soap separate in getting into separating centrifuge 500 together, separating centrifuge 500 here can adopt butterfly centrifuge, after centrifugal separation, crude oil, waste water, emulsified oil and soap can produce the layering, the crude oil that is located the upper strata can directly flow from the crude oil export, and be located the waste water of lower floor, soap, and emulsified oil then discharges from the emulsified oil export, thereby can separate out crude oil.
In another embodiment, a heat insulation device, such as a heating wire, may be further provided on the pipe connecting the mixer 300 to the separator 500, or a branch pipe may be provided on the pipe between the mixer 300 and the separator 500 for connecting hot water, so that excessive temperature loss is avoided when oil and water flow between the two devices, thereby facilitating centrifugal separation in the separator 500.
Referring to fig. 1, in another embodiment, the rubber seed oil washing device further includes an oil distribution tank 800, an inlet of the oil distribution tank 800 is communicated with the emulsified oil outlet, the oil distribution tank 800 is further provided with a first outlet and a second outlet, the first outlet is communicated with an oil inlet of the washing tank 100, and the second outlet is used for flowing out waste water. It has been explained in the previous embodiment that the separator 500 finally separates the emulsified oil, the waste water, the soap from the crude oil, and discharges from the emulsified oil outlet, so the separated oil tank 800 is provided to collect the emulsified oil, the waste water and the soap, further the emulsified oil, the soap and the water are separated, as shown in fig. 1, the separated oil tank 800 includes the left oil outlet area and the right water outlet area, a baffle is provided between the oil outlet area and the water outlet area, the first outlet communicates with the left oil outlet area, the second outlet communicates with the right water outlet area, at first, the emulsified oil, the soap and the waste water enter the water outlet area from the inlet of the separated oil tank, because the emulsified oil and the waste water have different densities, the waste water is located in the lower layer, the emulsified oil is located in the upper layer, along with the rising of the liquid level, the emulsified oil located in the upper layer after crossing the liquid level baffle enters the left oil outlet area, and then discharges from the first outlet, and the waste water originally located in the lower layer can directly discharge in the second outlet.
In other embodiments, a return oil pump may be disposed at the first outlet, and the emulsified oil in the oil separating tank 800 is pumped back to the water washing tank 100 by the return oil pump for secondary water washing; and a wastewater pump can be arranged at the second outlet to pump wastewater back to the wastewater pool for uniform treatment.
With reference to fig. 1, in another embodiment, a first pipeline 510 and a second pipeline 520 are provided at a crude oil outlet of the separator 500, the first pipeline 510 is communicated with an oil inlet of the water washing tank 100, and the second pipeline 520 is used for communicating with a next refining node. For example, two pipelines are led out from the crude oil outlet of the separator 500, including the first pipeline 510 and the second pipeline 520, if the crude oil flowing out from the crude oil outlet is qualified in water washing, the crude oil directly flows to the next refining node (for example, a dewatering node) through the first pipeline 510, and if the crude oil flowing out from the crude oil outlet is unqualified in water washing, the crude oil can flow back to the water washing tank 100 through the second pipeline 520 to be subjected to the second water washing. In other embodiments, valves may be disposed in the first pipe 510 and the second pipe 520, respectively, for the convenience of the user.
In another embodiment, the water washing tank 100 has a vacuum cavity, a double-layer coil and a stirring device are arranged in the vacuum cavity, the double-layer coil comprises a heating coil and a cooling coil, the water washing tank 100 is further provided with a water filling port and a wastewater outlet, and the wastewater outlet is located below the oil outlet in the vertical direction. Specifically, the washing tank 100 is provided with a vacuum chamber inside, the oil inlet and the oil outlet are communicated with the vacuum chamber, the washing tank 100 is further provided with a water filling port for adding water for washing into the vacuum chamber, and the waste water outlet is provided below the oil outlet, for example, at the bottom of the washing tank 100. The inside double-deck coil pipe of washing jar 100, including one deck cooling coil and one deck heating coil, two-layer coil pipe encircle the inside wall setting of washing jar 100, and cooling coil has coolant liquid import and coolant liquid export, and heating coil has conduction oil import and conduction oil export, and wherein coolant liquid import, coolant liquid export, conduction oil import and conduction oil export all set up in the outside of washing jar 100, the user operation of being convenient for.
The stirring means extends downward from the upper portion of the water washing tank 100 for stirring. Therefore, the user can wash the water based on the water washing tank 100 in the embodiment alone, such as adding hot water from a water adding port, adding the rubber seed oil to be washed from an oil inlet, controlling the temperature by using the double-layer coil pipe, stirring by using the stirring device, after the stirring is sufficient, the wastewater and the soap are located below the water washing tank 100, the crude oil is located above, the wastewater and the soap are discharged by using a wastewater outlet below, and the crude oil after the water washing is discharged from oil outlet above. The water washing tank 100 can be used for intermittent water washing, is convenient to use when the treatment capacity is not large, and has less starting equipment and lower cost. Of course, when the treatment amount is large, continuous washing can be performed by the present washing tank 100, and in this case, the stirrer and the double-layer coil need not be opened, and the water supply port does not need to be filled with water.
In another embodiment, the stirring device comprises a stirring shaft, the stirring shaft at least partially extends into the vacuum cavity, at least one group of stirring paddles are arranged on the part of the stirring shaft located in the vacuum cavity, and a driving motor and a speed reducer are arranged on the part of the stirring shaft located outside the vacuum cavity. Wherein, inside the (mixing) shaft stretched into the vacuum cavity from the top of washing jar 100, the (mixing) shaft that is located the vacuum cavity was encircleed by double-deck coil pipe, is provided with driving motor and speed reducer on being located outside (mixing) shaft, drives the (mixing) shaft through driving motor and drives the stirring rake and rotate, through the speed of speed reducer control stirring, the user of being convenient for adjusts. And the stirring shaft is positioned in the middle of the double-layer coil pipe, so that heat transfer is facilitated through stirring, and small temperature difference of each position in the vacuum cavity is kept.
In another embodiment, the part that the (mixing) shaft is located the vacuum chamber is provided with first stirring rake, second stirring rake and third stirring rake, and three groups of stirring rakes distribute in upper portion, middle part and the lower part of vacuum chamber, first stirring rake the second stirring rake reaches the third stirring rake is in the interval sets up on the (mixing) shaft, double-deck coil pipe is around being located in the middle the second stirring rake, first stirring rake is located double-deck coil pipe top, the third stirring rake is located double-deck coil pipe below to oil and water that are located vacuum chamber upper portion, middle part or lower part all can be by intensive mixing, and carry out heat transfer with double-deck coil pipe 1, stir more abundant, also further guarantee whole less difference in temperature simultaneously.
In another embodiment, 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 water washing tank 100. 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, can do benefit to the flow that drives oil and water more when the stirring.
In another embodiment, the projections of the first stirring paddle, the second stirring paddle and the third stirring paddle 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 distribute the entire space, further improving the fluidity of the internal oil and water.
Referring to fig. 1, in another embodiment, the rubber seed oil washing apparatus further includes an oil transfer pump 600, an inlet of the oil transfer pump 600 is communicated with an oil outlet of the washing tank 100, an outlet of the oil transfer pump 600 is provided with a third pipeline 610, a fourth pipeline 620 and a fifth pipeline 630, the third pipeline 610 is communicated with an inlet of the heater 200, the fourth pipeline 620 is used for being communicated to a next refining node, and the fifth pipeline 630 is used for being communicated to a previous refining node. When continuous water washing is adopted, the heater 200 is accessed to water to be washed in the water washing tank 100 by using the third pipeline 610, and when intermittent water washing is adopted, if the water washing is qualified, crude oil is communicated to the next refining node through the fourth pipeline 620, if the water washing is qualified, or if a large amount of soap is left after the water washing, the crude oil can be communicated to the upper deacidification node through the fifth pipeline 630 to be deacidified again.
In another embodiment, a wastewater tank may be further disposed at a wastewater outlet of the water washing tank 100 to collect wastewater generated during intermittent water washing, and then the wastewater is uniformly recycled to a wastewater tank for treatment.
The utility model discloses technical scheme, through setting up washing jar 100, can treat washing rubber seed oil and carry out the prestore through setting up heater 200, flowmeter 400, blender 300, can treat washing rubber seed oil and heat earlier, still then through the proportion that can control hot water and rubber seed oil, and then can mix hot water and rubber seed oil of certain proportion in blender 300 fully, then carry out centrifugation in separating centrifuge 500, direct next technology node with crude oil leads to after the separation, thereby realize continuous washing, the efficiency of washing has been improved, and through separating centrifuge 500 centrifugation, avoid subsiding and produce a large amount of emulsified oil, the small part of emulsified oil that produces in centrifugal process, also can separate with crude oil through the centrifugation, discharge through the export of difference at last, not only improve efficiency, also avoid producing a large amount of emulsified oil. In addition, the rewashing tank 100 is provided with a water filling port, a stirring device and a double-layer coil, if the treatment capacity is small, the rewashing tank 100 can be independently utilized for intermittent water washing, if the treatment capacity is large, a continuous water washing mode can be selected, and multiple modes are convenient for users to select.

Claims (10)

1. The rubber seed oil washing device is characterized by comprising:
the washing tank is provided with an oil inlet and an oil outlet, and the oil inlet is used for adding the rubber seed oil to be washed;
the inlet of the heater is communicated with the oil outlet of the water washing tank;
a mixer, an inlet of the mixer being in communication with an outlet of the heater;
the flow meter is provided with a water inlet and a water outlet, the water inlet is used for adding water, and the water outlet is communicated with the inlet of the mixer;
the separating centrifuge is equipped with miscella import, emulsified oil export and crude oil export, miscella import intercommunication the export of blender, the crude oil export is used for supplying the rubber seed oil outflow after the washing, the emulsified oil export is used for supplying the emulsified oil outflow that the washing produced.
2. The rubber seed oil washing device of claim 1, further comprising an oil separation tank, wherein an inlet of the oil separation tank is communicated with the emulsified oil outlet, the oil separation tank is further provided with a first outlet and a second outlet, the first outlet is communicated with an oil inlet of the washing tank, and the second outlet is used for outflow of wastewater.
3. The rubber seed oil washing device of claim 1, wherein a crude oil outlet of the separator is provided with a first pipeline and a second pipeline, the first pipeline is communicated with an oil inlet of the washing tank, and the second pipeline is communicated with a next refining node.
4. The rubber seed oil washing device of claim 1, wherein the washing tank is provided with a vacuum cavity, a double-layer coil and a stirring device are arranged in the vacuum cavity, the double-layer coil comprises a heating coil and a cooling coil, the washing tank is further provided with a water filling port and a waste water outlet, and the waste water outlet is located below the oil outlet in the vertical direction.
5. The rubber seed oil washing device of claim 4, wherein the stirring device comprises a stirring shaft, the stirring shaft at least partially extends into the vacuum cavity, at least one group of stirring paddles are arranged on the part of the stirring shaft located in the vacuum cavity, and a driving motor and a speed reducer are arranged on the part of the stirring shaft located outside the vacuum cavity.
6. The rubber seed oil washing device of claim 5, wherein the double-layer coil is arranged around the stirring shaft.
7. The rubber seed oil washing device of claim 6, wherein the at least one group of stirring paddles comprises a first stirring paddle, a second stirring paddle and a third stirring paddle, the first stirring paddle, the second stirring paddle and the third stirring paddle are arranged on the stirring shaft at intervals, and the double-layer coil pipe surrounds the second stirring paddle in the middle.
8. The rubber seed oil washing device of claim 7, wherein the first stirring paddle, the second stirring paddle and the third stirring paddle are arranged to form included angles with the cross section of the washing tank.
9. The rubber seed oil washing device of claim 7, wherein the projections of the first stirring paddle, the second stirring paddle and the third stirring paddle in the vertical direction form included angles.
10. The rubber seed oil washing device of any one of claims 1-9, further comprising an oil transfer pump, wherein an inlet of the oil transfer pump is communicated with an oil outlet of the washing tank, an outlet of the oil transfer pump is provided with a third pipeline, a fourth pipeline and a fifth pipeline, the third pipeline is communicated with an inlet of the heater, the fourth pipeline is used for being communicated to a next refining node, and the fifth pipeline is used for being communicated to a previous refining node.
CN202220455108.XU 2021-04-19 2022-03-02 Rubber seed oil washing device Active CN218561380U (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

Publications (1)

Publication Number Publication Date
CN218561380U true CN218561380U (en) 2023-03-03

Family

ID=82693195

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

Family Applications Before (6)

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

Family Applications After (2)

Application Number Title Priority Date Filing Date
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

Country Status (1)

Country Link
CN (9) CN217149083U (en)

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

Also Published As

Publication number Publication date
CN217265588U (en) 2022-08-23
CN217265592U (en) 2022-08-23
CN115216362B (en) 2024-03-01
CN218339771U (en) 2023-01-20
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

Similar Documents

Publication Publication Date Title
CN218561380U (en) Rubber seed oil washing device
CN102353133A (en) Quick-heating electrical heating water boiling device
CN205948856U (en) Cooling system of mediation cauldron
CN204569873U (en) One vegetable oil continuous refining washing waste water reuse and online adding set
CN106938151A (en) A kind of oily-water seperating equipment with temperature sensor
CN207401438U (en) A kind of mixing arrangement for being used to produce motor vehicle antifreeze fluid
CN207786421U (en) A kind of mixed stirring device of concrete additive production
CN202195576U (en) Instant-heating type electric water heating device
CN100404443C (en) Oil-containing sludge treating process
CN101559339B (en) Fuel emulsification continuous type automatic production device and fuel emulsification method
CN210001613U (en) tank liquid oil-water separation system
CN201632250U (en) Slurry bed reactor
CN102888283B (en) Multi-frequency ultrasonic radiation overflow groove continuous biodiesel production device
CN212128067U (en) A agitating unit in advance for coal tar dehydration
US2762682A (en) Method and reactor for continuously reacting liquids while adding or removing heat
CN211920963U (en) Chemical industry environmental protection oil-water separator
CN219752108U (en) Compact oil sludge separation system
CN109749853A (en) A kind of device by soap stock continuous production acidification oil and by-product sodium sulfate crystal
CN209237380U (en) It is a kind of with gas from the fine chemicals distillation still of backflow functionality
CN217312811U (en) Effectual emulsification agitated kettle of homogeneity
CN207062202U (en) Energy-saving production device of emulsified pitch
CN214716028U (en) Soap lye tank dosing unit for pitch production
CN214714492U (en) Automatic refining device of pressure vessel
CN215250691U (en) Non-transgenic low-reverse-resistance frying-resistant soybean oil production device
CN212246940U (en) Efficient continuous grease washing equipment

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant