CN201037140Y - Composite type grease continuous low temperature hydrated pot - Google Patents
Composite type grease continuous low temperature hydrated pot Download PDFInfo
- Publication number
- CN201037140Y CN201037140Y CNU2007200122396U CN200720012239U CN201037140Y CN 201037140 Y CN201037140 Y CN 201037140Y CN U2007200122396 U CNU2007200122396 U CN U2007200122396U CN 200720012239 U CN200720012239 U CN 200720012239U CN 201037140 Y CN201037140 Y CN 201037140Y
- Authority
- CN
- China
- Prior art keywords
- chamber
- pipe
- low temperature
- oil
- pot
- 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.)
- Expired - Fee Related
Links
Images
Abstract
The utility model relates to an oil processing device, in particular to a combined continuous low temperature oil hydration pot. The main body of the device is composed of a plurality of pot bodies 2 which are of different diameters and sheathed together. A hollow cavity of the middle pot body 2 is provided with a churn-dasher and a mixing chamber 4 of an oil-gas mixing device, and the other hollow cavities are provided with a precipitation chamber 5, an alkali refining chamber 7, a water-washing chamber 8 and a deposit chamber 9. The upper parts of the pot bodies outside each chamber are provided with an opening which are outwardly connected with a fluid guide pipe 10 or an oil pipe 5, and the lower parts of the pot bodies outside each chamber are connected with a residue collecting pot 12 through a discharging port 12. The utility model can perform multiple working procedures such as residue removal, degumming and deacidification continuously, and can be applied to high temperature oil hydration, thereby overcoming the disadvantages that the prior low temperature hydration art can not perform working procedures continuously and need to invert the pot intermittently. The combined continuous low temperature oil hydration pot provides an oil refining equipment device for the automation and routinization of oil hydration process, which is simple in structure, lower in cost and stable and reliable in work.
Description
Affiliated technical field
The utility model relates to a kind of fat and oil processing equipment, promptly a kind of composite type grease continuous low temperature hydrated pot.
Background technology
Grease after the grease hydration process mainly is meant and separates through slag liquid adds entry or steam, merges and dispel the process of the colloidal impurity in the oil, and what have also will extend to the alkali refining process and the water washing process of dispeling the acid value thing in the oil.Wherein, what add steam is the high-temperature water metallization processes, and what add water is low temperature hydrated technology.The high temperature aquation can be carried out continuously, and efficient is higher., the high temperature aquation needs a large amount of heat energy, and cost is higher, and can destroy greasy some nutritive substance, thereby should not adopt in food oils processing.Low temperature hydrated energy consumption is lower, the grease nutrient is more complete,, low temperature hydrated can only be intermittently of unit to carry out with the jar, can not be continuous between the not only different operations, and same operation can not be continuous, thereby expend a large amount of tank switching time and manpower and materials, seriously restricts the raising of working efficiency and quality product.
Summary of the invention
The purpose of this invention is to provide a kind of oil at low temperature hydration plant that can carry out continuously.
Above-mentioned purpose is realized by following technical scheme: develop a kind of composite type grease continuous low temperature hydrated pot, the main body of this equipment and tank body that be sleeved on together different by a plurality of diameters formed, the cavity that is positioned at the intermediary tank body is the mixing section that is provided with whipping appts and oily vapour mixing device, and the cavity that other tank bodies enclosed has settling pocket, alkali refining chamber, washing chamber and settling chamber from inside to outside successively; All there is opening each lower end, chamber, the open communication settling pocket under the mixing section, and other each lower ends, chamber connect the collection slag ladle by slag-drip opening respectively; The tank body top, the outside of settling pocket, alkali refining chamber and washing chamber all have opening and laterally adjacent cavities pick out thrust-augmenting nozzle, the outside, settling chamber tank body upper opening connects and stretches out a jar outer transition pipeline.
Whipping appts in the said mixing section is by the setting rotating shaft of the engine drive of tank deck, and stirring piece is housed in the rotating shaft.
Oily vapour mixing device in the said mixing section is to introduce oil pipe and water inlet pipe outward by jar, and oil pipe taps into oil pipe, and oil inlet pipe and water inlet pipe merge into the profit mixing tube that is access to mixing section.
Said oil pipe is connected the first tubulature and the oil inlet pipe of jar internal upper part respectively by control valve.
Slag-drip opening below said each tank body passes through scum pipe access set slag ladle separately, and the collection slag ladle is provided with the defeated pressure pipe of vapor pipe and input pressurized gas, and each vapor pipe all inserts equilibration tube, and equilibration tube upwards enters tank body, and extends a jar inner top space.
Said collection slag ladle bottom is provided with delivery pipe.
The outside of said settling chamber, the cavity that also has one deck tank body to surround is the separate chamber, one section of said oil inlet pipe connection profit mixing tube disconnects in the separate chamber, and an end of oil inlet pipe extends the bottom of separate chamber, and an end of profit mixing tube is positioned at the top of separate chamber.
The bottom of said separate chamber is provided with slag-drip opening, connects the collection slag ladle by scum pipe, and the delivery pipe of collection slag ladle inserts cake compressor.
In the outside of said outer tank body, be equipped with and the heating jacket that send heat pipe and circulation tube to communicate.
Adopt the composite type grease continuous low temperature hydrated pot of technique scheme, grease is after mixing section adds the steam stirring, colloidal impurity mixes back the separation with grease and precipitates discharge with steam, grease enters alkali refining chamber and washing chamber successively, comprehensive acid value thing is also discharged by wash-out, export self-cleaning oil at last, whole process does not need high temperature, tank switching intermittently, can carry out continuously, even can be extended down to slag liquid separation circuit in the past, thus overcome the shortcoming of existing oil at low temperature hydration technology, in addition, can also be competent at grease high-temperature water equalization, for realizing grease aquation automation technolo, it is a kind of simple in structure, with low cost that sequencing provides, the stable and reliable operation oil refining plant.
Description of drawings
Fig. 1 is the front view of first kind of embodiment;
Fig. 2 is the A-A sectional drawing of first kind of embodiment;
Fig. 3 is the front view of the parts oil vapour mixing tube of first kind of embodiment;
Fig. 4 is the vertical view of the parts oil vapour mixing tube of first kind of embodiment;
Fig. 5 is the parts water jet standpipe of first kind of embodiment or the front view of spray alkali pipe;
Fig. 6 is the parts water jet standpipe of first kind of embodiment or the vertical view of spray alkali pipe.
Fig. 7 is the front view of second kind of embodiment;
Fig. 8 is the cyclematics of second kind of embodiment;
Fig. 9 is the time variable control hardware chart of second kind of embodiment.
Among the figure as seen: oil pipe 1, tank body 2, oil inlet pipe 3, mixing section 4, transition pipeline 5, settling pocket 6, alkali refining chamber 7, washing chamber 8, settling chamber 9, thrust-augmenting nozzle 10, slag-drip opening 11, collection slag ladle 12, delivery pipe 13, valve 14, vapor pipe 15, scum pipe 16, defeated pressure pipe 17, equilibration tube 18, spreader plate 19, stirring piece 20, water jet standpipe 21, spray alkali pipe 22, first tubulature 23, profit mixing tube 24, rotating shaft 25, engine 26, water inlet pipe 27, buck inlet 28, trickle inlet 29, slag liquid separate chamber 30, cake compressor 31, recovery tube 32, a blob of slag 33, send heat pipe 34, heating jacket 35, circulation tube 36.
Embodiment
First kind of embodiment: shown in Fig. 1-6, this hydration tank is to be formed by surround cylindricality tank body 2 suits that five diameters do not wait, intermediary tank interior space is a mixing section 4, the rotating shaft 25 of a setting is equipped with in the inside, rotate under the drive of the motor 26 on tank body, by 20 work of the stirring piece in the rotating shaft 25.The outside of mixing section 4 has settling pocket 6, alkali refining chamber 7, washing chamber 8 and settling chamber 9 successively.Oil pipe 1 enters in the jar above tank body 2 outer, connects tubulature 23 just and oil inlet pipe 3 under the control of control valve respectively.Tubulature 23 just is provided with a plurality of perforates above above each tank body.Oil inlet pipe 3 merges into profit mixing tube 24 with water inlet pipe, enters mixing section 4.The top of three layers of tank body between middle tank body and outer tank body respectively has a through hole, each picks out a thrust-augmenting nozzle 10 laterally on the hole, each thrust-augmenting nozzle 10 respectively along alkali refining chamber 7, washing chamber 8, settling chamber stretch for 9 times, the top perforate of outermost layer tank body connects transition pipeline 5 and stretches out outside the jar.Other has buck inlet 28 and trickle inlet 29 to enter outside jar in the jar, forms circular water jet standpipe shown in Figure 4 25 and spray alkali pipe 26 respectively above washing chamber 8 and alkali refining chamber 7.A scum pipe 16 that valve is housed is all arranged at the bottom of each tank body, and each scum pipe 16 connects a collection slag ladle 12, and collection all is provided with delivery pipe 13 below the slag ladle 12.
During work, at first in jar, inject a certain amount of grease, and then close tubulature 23 just, from oil inlet pipe 3 fuel feeding in mixing section by first tubulature 23.The purpose of doing like this is to prevent that local pressure from crossing the havoc tank structure.Grease enters mixing section 4 jointly by oil gas mixing tube 24 and water, under the stirring of rotating shaft 25 and stirring piece 20, end opening through mixing section flows out, by spreader plate 19 minutes to around and enter settling pocket 6, colloidal impurity in the oil mixes the back with water sedimentation downwards because proportion is big, the up opening from settling pocket 6 tops of lighter grease enters thrust-augmenting nozzle 10, flows out upwards buoyance lift again from the bottom of alkali refining chamber 7, mix with the buck that sprays 22 ejections of alkali pipe simultaneously, dispel acid value thing and sinking in the oil.Grease through alkali refining enters washing chamber 8 by another thrust-augmenting nozzle again, and water jet standpipe 21 ejection water come grease is washed, and carry impurity.Grease through washing enters settling chamber 9 through another thrust-augmenting nozzle again, and residual impurity further precipitates, and purified grease enters transition pipeline 5 again, is transported to outside the jar.
As seen from the figure, slag-drip opening 11 is all arranged below each tank body, pick out scum pipe 16 respectively.Scum pipe 16 is provided with valve 14, regularly opens valve, makes impurity enter collection slag ladle 12.Above the collection slag ladle 12 vapor pipe 15 and defeated pressure pipe 17 are arranged, the gas of sweeping along in the impurity is pooled to equilibration tube 18 from vapor pipe 15 and sends back in the jar, when the dregs of fat reach a certain amount of in the collection slag ladle 12, opens valve, squeeze into high pressure gas by defeated pressure pipe 17, impurity is released delivery pipe 13.In a plurality of collection slag ladles, dregs of fat composition has nothing in common with each other, and the utilization that has that has is worth, and can collect and utilize, and waste treatment is done in the discharge that has.
As seen from the figure, when needs adopt the high-temperature water metallization processes,, thereby can avoid enterprise to repeat to purchase two cover hydration plants as long as in jar, provide steam by water inlet pipe 27.
Second kind of embodiment: as shown in Figure 7,9 outside has increased a slag liquid separate chamber 30 again in the settling chamber, oil inlet pipe 3 disconnects with profit mixing tube 24, and the opening end of oil inlet pipe 3 extends the bottom of slag liquid separate chamber 30 downwards, and the broken ends of fractured bone opening of profit mixing tube 24 is on the top of slag liquid separate chamber 30.Adopt this structure, can extend a procedure to the working range of this equipment forward, i.e. slag liquid separation circuit.Not separated grease is after the bottom enters, and the dregs of fat sink, and grease rises, and then enters hydration process.The dregs of fat that sink enter the collection slag ladle through scum pipe 16, enter cake compressor 31 again, and remaining grease is filtered off, and reclaim in recovery tube 32, and the dregs of fat are pressed into a blob of slag 33 row utilization again.
In addition, increase one deck heating jacket 35 again in the outside of slag liquid separate chamber 30, heating jacket 35 constitutes a heating plant by sending heat pipe 34 and circulation tube 36.During work, can suitably heat for a jar interior grease by circulatory mediators such as hot water, to improve greasy flowability.
The third embodiment:, thereby can be equipped with automatic control device or computer program control device owing to this hydration plant can be worked continuously.Fig. 8,9 has exemplified a kind of computer program figure and hardware chart, adopts this program control technology, can further improve efficiency of operation and the concise level of grease.
Claims (10)
1. composite type grease continuous low temperature hydrated pot, it is characterized in that: the main body of this equipment and tank body (2) that be sleeved on together different by a plurality of diameters formed, the cavity that is positioned at the intermediary tank body is the mixing section (4) that is provided with whipping appts and oily vapour mixing device, and the cavity that other tank bodies (2) are enclosed has settling pocket (6), alkali refining chamber (7), washing chamber (8) and settling chamber (9) from inside to outside successively; All there is opening each lower end, chamber, the open communication settling pocket (6) under the mixing section (4), and other each lower ends, chamber connect collection slag ladle (12) by slag-drip opening (11) respectively; Outside tank body (2) top of settling pocket (6), alkali refining chamber (7) and washing chamber (8) all have opening and laterally adjacent cavities pick out thrust-augmenting nozzle (6), settling chamber (9) outside tank body (2) upper opening connects and stretches out a jar outer transition pipeline (5).
2. composite type grease continuous low temperature hydrated pot according to claim 1 is characterized in that: the whipping appts in the said mixing section (4) is by the setting rotating shaft (25) of engine (26) drive of tank deck, and stirring piece (20) is housed in the rotating shaft (25).
3. composite type grease continuous low temperature hydrated pot according to claim 1, it is characterized in that: the oily vapour mixing device in the said mixing section (4) is to introduce oil pipe (1) and water inlet pipe (27) outward by jar, oil pipe (1) taps into oil pipe (3), and oil inlet pipe (3) and water inlet pipe (27) merge into the profit mixing tube (24) that is access to mixing section (4).
4. composite type grease continuous low temperature hydrated pot according to claim 3 is characterized in that: said oil pipe (1) is connected the first tubulature (23) and the oil inlet pipe (3) of jar internal upper part respectively by control valve.
5. composite type grease continuous low temperature hydrated pot according to claim 1, it is characterized in that: the slag-drip opening (11) below said each tank body (2) passes through scum pipe (16) access set slag ladle (12) separately, collection slag ladle (12) is provided with the defeated pressure pipe (17) of vapor pipe (15) and input pressurized gas, each vapor pipe (15) all inserts equilibration tube (18), equilibration tube (18) upwards enters tank body, and extends a jar inner top space.
6. composite type grease continuous low temperature hydrated pot according to claim 1 is characterized in that: said collection slag ladle (12) bottom is provided with delivery pipe (13).
7. composite type grease continuous low temperature hydrated pot according to claim 1, it is characterized in that: the outside of said settling chamber (9), the cavity that also has one deck tank body to surround is separate chamber (30), (30) extend the bottom of separate chamber (30) downwards to one end of the said oil inlet pipe (3) that is connected with oil pipe (1) along the separate chamber, and the oil-feed port of profit mixing tube (24) is positioned at the top of separate chamber (30).
8. composite type grease continuous low temperature hydrated pot according to claim 6 is characterized in that: the bottom of said separate chamber (10) is provided with slag-drip opening, and connects the collection slag ladle by scum pipe, and the delivery pipe of collection slag ladle inserts cake compressor (31).
9. composite type grease continuous low temperature hydrated pot according to claim 1 is characterized in that: in the outside of said outer tank body (2), be equipped with and the heating jacket (35) that send heat pipe (34) and circulation tube (36) to communicate.
10. composite type grease continuous low temperature hydrated pot according to claim 1 is characterized in that: this equipment also is provided with the computer program control device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200122396U CN201037140Y (en) | 2007-05-20 | 2007-05-20 | Composite type grease continuous low temperature hydrated pot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200122396U CN201037140Y (en) | 2007-05-20 | 2007-05-20 | Composite type grease continuous low temperature hydrated pot |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201037140Y true CN201037140Y (en) | 2008-03-19 |
Family
ID=39209652
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200122396U Expired - Fee Related CN201037140Y (en) | 2007-05-20 | 2007-05-20 | Composite type grease continuous low temperature hydrated pot |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201037140Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101054544B (en) * | 2007-05-25 | 2010-06-09 | 张建臣 | Composite type grease continuous low temperature hydrated pot |
-
2007
- 2007-05-20 CN CNU2007200122396U patent/CN201037140Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101054544B (en) * | 2007-05-25 | 2010-06-09 | 张建臣 | Composite type grease continuous low temperature hydrated pot |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202010687U (en) | Multifunctional machine apparatus for storage tank cleaning | |
| CN105499239B (en) | Oil storage tank Water Tank machine automatization clearing and retrieving system and method | |
| CN101054544B (en) | Composite type grease continuous low temperature hydrated pot | |
| CN201037140Y (en) | Composite type grease continuous low temperature hydrated pot | |
| CN202369562U (en) | Processing device for oil extraction and dephenolization for cottonseed | |
| CN201062256Y (en) | Grape jam juice double-circulating fermentation tank | |
| CN202237375U (en) | Multifunctional extracting and stirring device | |
| CN109939462A (en) | A kind of multistage spiral counterflow leaching equipment | |
| CN202070508U (en) | Special cleaning device for connecting rod of diesel engine | |
| CN214612391U (en) | Fermentation tank | |
| CN103060085B (en) | Total-immersion continuous differential countercurrent extractor | |
| CN210029308U (en) | Buffer tank for resin processing | |
| CN108998236A (en) | A kind of multistage conche for vegetable oil preparation | |
| CN115368968A (en) | Refined decoloration deodorization system of tea-seed oil | |
| CN212610501U (en) | Rapid deacidification and low-sulfur high-yield production system for producing fuel oil by using waste animal and vegetable oil | |
| CN201971813U (en) | Edible oil alkali refining device with oil residue recycling groove | |
| CN202199163U (en) | Continuous countercurrent extractor with suspension barrel | |
| CN105199844A (en) | Heating vibration type bleaching tower convenient to clean | |
| CN208333247U (en) | A kind of long defeated pipe network heat exchanger descaler in oil field | |
| CN113398872A (en) | Rectifying column kettle liquid nutrient content recovery system for producing soybean polysaccharide | |
| CN216934783U (en) | Steam recompression extraction device | |
| CN206219541U (en) | Edible oil material cooking tank | |
| CN218642695U (en) | Semi-continuous vegetable oil deodorization system | |
| CN110917649A (en) | Chinese-medicinal material active ingredient soaks extraction element | |
| CN218491518U (en) | Condensate recovery pretreatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHANG JIANCHEN; PATENTEE Free format text: FORMER OWNER: ZHANG JIANCHEN Effective date: 20080418 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| C53 | Correction of patent for invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Zhang Jianchen Inventor after: Zhang Jiaming Inventor before: Zhang Jianchen |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: ZHANG JIANCHEN TO: ZHANG JIANCHEN; ZHANG JIAMING |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20080418 Address after: Box 56102, Tongliao, the Inner Mongolia Autonomous Region 028000 Co-patentee after: Zhang Jiaming Patentee after: Zhang Jian Chen Address before: Box 56102, Tongliao, the Inner Mongolia Autonomous Region 028000 Patentee before: Zhang Jianchen |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080319 |