CN104711125A - Special edible oil fatty acid layering tank - Google Patents
Special edible oil fatty acid layering tank Download PDFInfo
- Publication number
- CN104711125A CN104711125A CN201310675440.2A CN201310675440A CN104711125A CN 104711125 A CN104711125 A CN 104711125A CN 201310675440 A CN201310675440 A CN 201310675440A CN 104711125 A CN104711125 A CN 104711125A
- Authority
- CN
- China
- Prior art keywords
- fatty acid
- straight barrel
- edible oil
- tank
- pipe
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0211—Separation of non-miscible liquids by sedimentation with baffles
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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
- C11B13/00—Recovery of fats, fatty oils or fatty acids from waste materials
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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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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Fats And Perfumes (AREA)
Abstract
The invention discloses a special edible oil fatty acid layering tank. According to the principle that the specific gravity of the fatty acid is smaller than that of water, fatty acid is separated by using a sedimentation layering method, so that the effects of repeatedly utilizing water resources and recycling the fatty acid are achieved. The special edible oil fatty acid layering tank is characterized in that the lower end of a straight barrel of the tank is connected to a lower sealing head, and landing legs are arranged on the lower sealing head so as to support the weight of the whole tank; an inner conical disk and a baffle plate are arranged in the straight barrel and are used for blocking the straight barrel into a circulating channel; a hole is formed in the inner conical disk so as to facilitate sinking of heavy-phase substances in mixed liquid and floating of light-phase substances; a direct steam spray pipe with a downward open pore is arranged below the inner conical disk, the inner conical tank is heated by virtue of direct steam so as to ensure that the fatty acid is in liquid state, then the fatty liquid is output by an output pipe I and an output pipe II and recovered, water enters a circulating water tank from a drain pipe and is recycled, and wastewater is not generated; the pollution of wastewater to environments is improved; meanwhile, the economic benefits are improved by recycling the fatty acid.
Description
Technical field:
The product that the present invention relates to, is widely used in the technical field of vacuum in the deodorization of food oils engineering refining procedure edible oil, deacidification.
Background technology:
At present, the fats and oils processing enterprise of domestic various scale, edible oil deodorization in food oils refining procedure, deacidifying process utilize the difference of stink substance and fatty acid triglyceride volatility in grease, remove the process of stink substance under high temperature and high vacuum condition by water vapour.In order to produce high vacuum condition, general fats and oils processing enterprise adopts steam jet vacuum pump; Need a large amount of steam during steam jet vacuum pump work, what vacuum pump was extracted out from deodorizing tower is also high-temperature gas; Therefore a large amount of heats makes the Working environment of steam jet vacuum pump more and more higher.The volume Yin Wendu of air raises and increases, and high vacuum environment is affected; Therefore need to reduce envrionment temperature, make steam jet vacuum pump reach the effect producing high vacuum condition.General condenser is difficult to reach and is taken away by heat fast, and causes equipment to be lowered the temperature; Adopt dry condensate vacuum system containing lipid acid from dry condenser out mixing liquid, if be discharged into formation sewage in circulating water pool, to environment; Water resources can not reuse.
Summary of the invention:
Product involved by this project, for the problems referred to above, provides a kind of edible oil lipid acid specific hierarchical tank; Less than water according to the proportion of lipid acid, by the method separation of fatty acids of sedimentation layering; Thus reach the effect of recycling water resources, recovery lipid acid.
Edible oil lipid acid specific hierarchical tank, comprising: supporting leg, straight barrel, lower cover, lamina tecti, inner cone dish, output tube, No. two output tubes, dividing plate, liquid-inlet pipe, a visor, No. two visors, open steam jet pipe, discharging tubes.Straight barrel lower end is connected with lower cover by the mode of welding, and lower cover is provided with the weight that supporting leg supports whole equipment; Drain pipe is provided with below lower cover.Distance straight barrel lower end 300mm At The Height, is provided with an output tube, a visor; Distance 500mm place, straight barrel upper end, is provided with No. two output tubes, No. two visors; Straight barrel upper end is provided with lamina tecti, is bolted; Lamina tecti is provided with liquid-inlet pipe, blow-down pipe.Straight barrel inside is provided with inner cone dish, dividing plate, and the inner barrier of straight barrel is become circulation passage; Inner cone dish is provided with hole, and be convenient to heavy phase material in mixing liquid and sink, light phase material floats.The below of inner cone dish is provided with the downward open steam jet pipe of perforate, and because containing the higher lipid acid of zero pour in mixed solution, temperature is easy to solidify after reducing; Heated by open steam, make lipid acid remain on liquid state and be convenient to export.
Arranged by said structure, from dry condenser lipid acid out and the mixed solution of water, enter the circulation passage in cylindrical shell from liquid-inlet pipe; Lipid acid proportion is lighter than water, and lipid acid floats, and sinks under water.Due to the effect of open steam jet pipe steam, ensure that lipid acid is in liquid state, then reclaim after exporting through an output tube, No. two output tubes, water enters circulating water pool from discharging tube and recycles, and can not produce waste water; Improve the pollution of waste water to environment.Reclaim lipid acid simultaneously and improve economic benefit.
Accompanying drawing illustrates:
Below in conjunction with drawings and Examples, the present invention is further described, and Fig. 1 is edible oil lipid acid specific hierarchical jar structure schematic diagram.
As shown in Figure 1: supporting leg 1, backplate 2, inner cone dish 3, output tube 4, No. two output tubes 5, dividing plate 6, blow-down pipe 7, lamina tecti 8, liquid-inlet pipe 9, bolt 10, separator channels 11, No. two visors 12, straight barrel 13, visor 14, lower cover 15, spray orifice 16, open steam jet pipe 17, a discharging tube 18.
Embodiment:
Product involved by this project, as shown in Figure 1, straight barrel 13 lower end is connected with lower cover 15 by the mode of welding, and lower cover 15 is provided with the weight that supporting leg 1 supports whole equipment; Drain pipe 18 is provided with below lower cover 15.Distance straight barrel lower end 300mm At The Height, is provided with an output tube 4, visor 14; Distance 500mm place, straight barrel upper end, is provided with No. two output tubes 5, No. two visors 12; Straight barrel 13 upper end is provided with lamina tecti 8, is connected by bolt 10; Lamina tecti 8 is provided with liquid-inlet pipe 9, blow-down pipe 7.Straight barrel 13 inside is provided with inner cone dish 3, dividing plate 6, and dividing plate 6 is provided with separator channels 11; The inner barrier of straight barrel is become circulation passage; Inner cone dish 3 is provided with hole, and be convenient to heavy phase material in mixing liquid and sink, light phase material floats.The below of inner cone dish 3 is provided with open steam jet pipe 17, and open steam jet pipe 17 is provided with the spray orifice 16 that Open Side Down.From dry condenser lipid acid out and the mixed solution of water, enter the circulation passage in straight barrel 13 from liquid-inlet pipe 9; Lipid acid proportion is lighter than water, and lipid acid floats, and sinks under water.Due to the effect of open steam jet pipe steam, ensure that lipid acid is in liquid state, lipid acid has just started to export through an output tube 4; Rear recovery is exported from No. two output tubes 5 after liquid level reduces; Water enters circulating water pool from discharging tube 18 and recycles.
Claims (4)
1. edible oil lipid acid specific hierarchical tank, comprising: supporting leg (1), straight barrel (13), lower cover (15), lamina tecti (8), inner cone dish (3), output tube (4), No. two output tubes (5), dividing plate (6), liquid-inlet pipe (9), visor (14), No. two visors (12), open steam jet pipe (17), discharging tube (18); It is characterized in that: described straight barrel (13) lower end is connected with lower cover (15), is provided with drain pipe below lower cover, upper end is provided with lamina tecti (8) and is connected by bolt (10); Described lower cover (15) is provided with the weight that supporting leg (1) supports whole equipment; Straight barrel (13) inside is provided with inner cone dish (3), dividing plate (6), and the inner barrier of straight barrel (13) is become circulation passage; Described inner cone dish (3) is provided with hole, and the below of inner cone dish (3) is provided with the downward open steam jet pipe (17) of perforate.
2. edible oil lipid acid specific hierarchical tank according to claim 1, it is characterized in that: described inner cone dish (3) has open steam jet pipe (17), open steam jet pipe (17) is provided with the spray orifice (16) that Open Side Down.
3. edible oil lipid acid specific hierarchical tank according to claim 1, is characterized in that: described straight barrel (13) distance lower end 300mm At The Height, is provided with an output tube (4), a visor (14); Distance 500mm place, straight barrel (13) upper end, is provided with No. two output tubes (5), No. two visors (12).
4. edible oil lipid acid specific hierarchical tank according to claim 1, is characterized in that: described lamina tecti (8) is provided with liquid-inlet pipe (9), blow-down pipe (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310675440.2A CN104711125A (en) | 2013-12-13 | 2013-12-13 | Special edible oil fatty acid layering tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310675440.2A CN104711125A (en) | 2013-12-13 | 2013-12-13 | Special edible oil fatty acid layering tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104711125A true CN104711125A (en) | 2015-06-17 |
Family
ID=53410845
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310675440.2A Pending CN104711125A (en) | 2013-12-13 | 2013-12-13 | Special edible oil fatty acid layering tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104711125A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107537429A (en) * | 2017-10-13 | 2018-01-05 | 安徽天意环保科技有限公司 | Pre-process ester exchange reaction system |
| CN107597042A (en) * | 2017-10-13 | 2018-01-19 | 安徽天意环保科技有限公司 | The production system of surfactant |
| CN107617399A (en) * | 2017-10-13 | 2018-01-23 | 安徽天意环保科技有限公司 | The pretreatment unit of surfactant |
| CN111473916A (en) * | 2020-04-10 | 2020-07-31 | 中国石油化工股份有限公司 | Monitoring method for crystallizer corrosion leakage condition |
-
2013
- 2013-12-13 CN CN201310675440.2A patent/CN104711125A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107537429A (en) * | 2017-10-13 | 2018-01-05 | 安徽天意环保科技有限公司 | Pre-process ester exchange reaction system |
| CN107597042A (en) * | 2017-10-13 | 2018-01-19 | 安徽天意环保科技有限公司 | The production system of surfactant |
| CN107617399A (en) * | 2017-10-13 | 2018-01-23 | 安徽天意环保科技有限公司 | The pretreatment unit of surfactant |
| CN111473916A (en) * | 2020-04-10 | 2020-07-31 | 中国石油化工股份有限公司 | Monitoring method for crystallizer corrosion leakage condition |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20150617 |