CN211274624U - Soapstock oil foot pretreatment system - Google Patents
Soapstock oil foot pretreatment system Download PDFInfo
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- CN211274624U CN211274624U CN201921656057.1U CN201921656057U CN211274624U CN 211274624 U CN211274624 U CN 211274624U CN 201921656057 U CN201921656057 U CN 201921656057U CN 211274624 U CN211274624 U CN 211274624U
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- tank
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- vacuum condenser
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes
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Abstract
The utility model belongs to the technical field of the grease is made, concretely relates to system of soapstock oil foot preliminary treatment, including acetic acid jar, soapstock storage tank, modulation jar, heater, vacuum condenser and hot-water cylinder, acetic acid jar discharge gate and soapstock storage tank discharge gate all communicate several modulation jar feed inlet, modulation jar discharge gate intercommunication heater feed inlet, modulation jar tail gas export intercommunication vacuum condenser air inlet, modulation jar hot water import intercommunication hot-water cylinder delivery port, modulation jar steam inlet intercommunication steam conveying system export, modulation jar steam outlet intercommunication hot-water cylinder water inlet, the utility model discloses need not the reladling in the use, can continuous production.
Description
Technical Field
The utility model belongs to the technical field of the grease is made, concretely relates to system of soapstock oil foot preliminary treatment.
Background
Soapstock is leftover of edible oil processing production, and some byproducts can be used as production soap or processed into fatty acid as other product raw materials to improve the utilization rate of the product, the existing pretreatment mode of the soapstock oil foot is to use sulfuric acid and the soapstock oil foot to mix and heat up to form fatty acid.
Disclosure of Invention
An object of the utility model is to provide a system for soapstock oil foot preliminary treatment that need not the tank switching, can continuous production.
Based on the above-mentioned purpose, the utility model discloses take following technical scheme:
the system for pretreating the soapstock oil foot comprises an acetic acid tank, a soapstock storage tank, a modulation tank, a heater, a vacuum condenser and a hot water tank, wherein a discharge port of the acetic acid tank and a discharge port of the soapstock storage tank are communicated with a plurality of feed ports of the modulation tank, a discharge port of the modulation tank is communicated with the feed ports of the heater, a tail gas outlet of the modulation tank is communicated with an air inlet of the vacuum condenser, a hot water inlet of the modulation tank is communicated with a water outlet of the hot water tank, a steam inlet of the modulation tank is communicated with an outlet of a steam conveying system.
Further, the modulation jar including the modulation jar body, this modulation jar body top is equipped with modulation jar feed inlet, modulation jar tail gas export, modulation jar hot water import, is equipped with modulation jar discharge gate, modulation jar overcoat and establishes the steam jacket layer below, this jacket layer be one airtight in the cavity structure, jacket layer 306 one side is equipped with modulation jar steam inlet, the jacket layer opposite side is equipped with modulation jar steam outlet, the internal agitating unit that still is equipped with of modulation jar.
Further, first vacuum condenser include the first vacuum condenser jar of body, the internal first condenser pipe that is equipped with of first vacuum condenser jar, first condenser pipe one end opening stretches out the first vacuum condenser jar of body and is a vacuum condenser cooling water inlet, first condenser pipe other end opening stretches out the first vacuum condenser jar of body and is a vacuum condenser cooling water outlet, be equipped with first vacuum condenser air inlet, first vacuum condenser gas outlet and first vacuum condenser drain on the first vacuum condenser jar of body lateral wall.
Further, nigre storage tank discharge gate and modulation jar feed inlet between still be equipped with static mixer and high-efficient blender in proper order, this nigre storage tank discharge gate intercommunication static mixer feed inlet, the high-efficient blender feed inlet of static mixer discharge gate intercommunication, high-efficient blender discharge gate intercommunication modulation jar feed inlet, the high-efficient blender discharge gate still communicates static mixer feed inlet, be equipped with first valve and second valve between high-efficient blender discharge gate and the static mixer feed inlet, first valve is located high-efficient blender discharge gate department, the second valve is located between first valve and the static mixer feed inlet. The heater is also provided with a heater heat-conducting oil outlet and a heater heat-conducting oil inlet.
Further, the number of the modulation tanks is two.
The utility model discloses use acetic acid to replace traditional sulphuric acid, use acetic acid and soapstock oil foot to mix, produce glycerine and fatty acid to being furnished with two modulation jars, can continuous production, can be simultaneously to reaction process transported substance material, the modulation jar is equipped with and presss from both sides the cover, presss from both sides the cover and heats the modulation jar, avoids inside coking problem, but steam automatic control adjusts, the energy saving, and the technology suitability is strong, can subsequent defective work of cyclic processing.
Drawings
FIG. 1 is a schematic diagram of the system of the present invention;
FIG. 2 is a schematic diagram of a brewing canister;
FIG. 3 is a schematic structural view of a heater;
fig. 4 is a schematic structural view of the first vacuum condenser.
Detailed Description
The system for pretreating the soapstock oil foot as shown in fig. 1-4 comprises an acetic acid tank 1, a soapstock storage tank 2, a modulation tank 3, a heater 4, a vacuum condenser 5 and a hot water tank 6, wherein a discharge port 101 of the acetic acid tank and a discharge port 201 of the soapstock storage tank are both communicated with a plurality of modulation tank feed ports 301, the number of the modulation tanks 3 is two, a discharge port 302 of the modulation tank is communicated with a heater feed port 401, a tail gas outlet 303 of the modulation tank is communicated with an air inlet 501 of the vacuum condenser, a hot water inlet 304 of the modulation tank is communicated with a water outlet 601 of the hot water tank, a steam inlet 307 of the modulation tank is communicated with an outlet 701 of a steam conveying system.
The brewing tank 3 comprises a brewing tank body 305, a brewing tank feeding port 301, a brewing tank tail gas outlet 303 and a brewing tank hot water inlet 304 are arranged at the top of the upper portion of the brewing tank body 305, a brewing tank discharging port 302 is arranged below the brewing tank body, a steam jacket layer 306 is sleeved outside the brewing tank 3, the jacket layer 306 is of a sealed cavity structure, a brewing tank steam inlet 307 is arranged on one side of the jacket layer 306, a brewing tank steam outlet 308 is arranged on the other side of the jacket layer 306, and a stirring device 309 is further arranged in the brewing tank body 305.
The first vacuum condenser 5 comprises a first vacuum condenser tank 503, a first condenser pipe 504 is arranged in the first vacuum condenser tank 503, one end opening of the first condenser pipe 504 extends out of the first vacuum condenser tank 503 and is a first vacuum condenser cooling water inlet 505, the other end opening of the first condenser pipe 504 extends out of the first vacuum condenser tank 503 and is a first vacuum condenser cooling water outlet 506, a first vacuum condenser air inlet 501, a first vacuum condenser air outlet 502 and a first vacuum condenser vent 507 are arranged on the side wall of the first vacuum condenser tank 503, and the first vacuum condenser cooling water inlet 505 and the first vacuum condenser cooling water outlet 506 are communicated with a water cooling tower to cool gas in the first vacuum condenser 5.
Still be equipped with static mixer 8 and high-efficient blender 9 between nigre storage tank discharge gate 201 and the retort feed inlet 301 in proper order, this nigre storage tank discharge gate 201 communicates static mixer feed inlet 801, static mixer discharge gate 802 communicates high-efficient blender feed inlet 901, high-efficient blender discharge gate 902 communicates retort feed inlet 301, high-efficient blender discharge gate 902 still communicates static mixer feed inlet 801, be equipped with first valve 10 and second valve 5 between high-efficient blender discharge gate 902 and the static mixer feed inlet 801, first valve 10 is located high-efficient blender discharge gate 902 department, second valve 5 is located between first valve 10 and the static mixer feed inlet 801. The heater 4 is also provided with a heater heat-conducting oil outlet 403 and a heater heat-conducting oil inlet 404.
When the device is used, firstly, the acetic acid aqueous solution in the acetic acid tank 1 and the soapstock aqueous solution in the soapstock storage tank 2 are fed into the modulation tank 3 from the modulation tank feeding port 301, the acetic acid aqueous solution and the soapstock aqueous solution are fully mixed and heated in the modulation tank 3, the mixed solution enters the heater 4 from the modulation tank discharging port 302 for further heating, the heated mixed solution enters the next reaction section, wherein in the stirring process of the modulation tank 3, the hot water tank 6 can also feed hot water into the modulation tank hot water inlet 304, the hot water enters from the hot water tank 6 to the modulation tank hot water inlet 304, the steam conveying system 7 can heat steam and feed the steam from the modulation tank steam inlet 307 into the jacket layer 306, the modulation tank steam outlet 308 is arranged on the other side of the jacket layer 306 and feeds the hot water into the hot water tank 6, and in the use process, two modulation tanks 3 can feed to the next reaction section. The utility model discloses not only can be applicable to the preliminary treatment that nigre and acetic acid reaction generated fatty acid, also be applicable to the preliminary treatment that nigre and sulphuric acid reaction generated fatty acid simultaneously, use the carbomorphism that the acetic acid reaction can effectively prevent to produce between sulphuric acid and the nigre, improve product quality.
Claims (6)
1. The system for pretreating the soapstock oil foot is characterized by comprising an acetic acid tank, a soapstock storage tank, a modulating tank, a heater, a vacuum condenser and a hot water tank, wherein a discharging port of the acetic acid tank and a discharging port of the soapstock storage tank are communicated with a plurality of feeding ports of the modulating tank, a discharging port of the modulating tank is communicated with a feeding port of the heater, a tail gas outlet of the modulating tank is communicated with an air inlet of the vacuum condenser, a hot water inlet of the modulating tank is communicated with a water outlet of the hot water tank, a steam inlet of the modulating tank is communicated with an outlet of a steam conveying system, and.
2. The system for pretreating soapstock oil foot according to claim 1, wherein the brewing tank comprises a brewing tank body, a brewing tank feed inlet, a brewing tank tail gas outlet and a brewing tank hot water inlet are formed in the top of the brewing tank body, a brewing tank discharge port is formed in the lower portion of the brewing tank body, a steam jacket layer is sleeved outside the brewing tank and is of a closed cavity structure, a brewing tank steam inlet is formed in one side of the jacket layer 306, a brewing tank steam outlet is formed in the other side of the jacket layer, and a stirring device is further arranged in the brewing tank body.
3. The soapstock oil foot pretreatment system according to claim 1, wherein the vacuum condenser comprises a vacuum condenser tank, a first condenser pipe is arranged in the vacuum condenser tank, one end of the first condenser pipe extends out of the vacuum condenser tank and is a cooling water inlet of the vacuum condenser, the other end of the first condenser pipe extends out of the vacuum condenser tank and is a cooling water outlet of the vacuum condenser, and a vacuum condenser air inlet, a vacuum condenser air outlet and a vacuum condenser vent are arranged on the side wall of the vacuum condenser tank.
4. The system of claim 1, wherein a static mixer and a high-efficiency mixer are sequentially arranged between the soapstock storage tank discharge port and the feed port of the modulation tank, the soapstock storage tank discharge port is communicated with the feed port of the static mixer, the static mixer discharge port is communicated with the feed port of the high-efficiency mixer, the feed port of the modulation tank is communicated with the feed port of the high-efficiency mixer, the feed port of the static mixer is communicated with the feed port of the high-efficiency mixer, a first valve and a second valve are arranged between the feed port of the high-efficiency mixer and the feed port of the static mixer, the first valve is arranged at the feed port of the high-efficiency mixer, and the second valve is arranged between the first valve and the feed port of the static mixer.
5. The system of claim 1, wherein the heater further comprises a heater oil outlet and a heater oil inlet.
6. The soapstock oil foot pretreatment system of claim 1, wherein there are two modulation tanks.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921656057.1U CN211274624U (en) | 2019-09-30 | 2019-09-30 | Soapstock oil foot pretreatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921656057.1U CN211274624U (en) | 2019-09-30 | 2019-09-30 | Soapstock oil foot pretreatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211274624U true CN211274624U (en) | 2020-08-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921656057.1U Active CN211274624U (en) | 2019-09-30 | 2019-09-30 | Soapstock oil foot pretreatment system |
Country Status (1)
| Country | Link |
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| CN (1) | CN211274624U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114317123A (en) * | 2021-02-05 | 2022-04-12 | 广西森洲生物技术有限公司 | Soapstock oil foot acidification reaction system and technology |
-
2019
- 2019-09-30 CN CN201921656057.1U patent/CN211274624U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114317123A (en) * | 2021-02-05 | 2022-04-12 | 广西森洲生物技术有限公司 | Soapstock oil foot acidification reaction system and technology |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230720 Address after: 530022 room 1401, 14th floor, Huasen building, 2 Yulan Road, Qingxiu District, Nanning City, Guangxi Zhuang Autonomous Region Patentee after: Guangxi senzhou Biotechnology Co.,Ltd. Patentee after: Beihai senzhou Biotechnology Co.,Ltd. Address before: 530022 room 1401, 14th floor, Huasen building, 2 Yulan Road, Qingxiu District, Nanning City, Guangxi Zhuang Autonomous Region Patentee before: Guangxi senzhou Biotechnology Co.,Ltd. |
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| TR01 | Transfer of patent right |