CN101054544A - Combined type grease continuous low-temperature hydration tank - Google Patents
Combined type grease continuous low-temperature hydration tank Download PDFInfo
- Publication number
- CN101054544A CN101054544A CN 200710107698 CN200710107698A CN101054544A CN 101054544 A CN101054544 A CN 101054544A CN 200710107698 CN200710107698 CN 200710107698 CN 200710107698 A CN200710107698 A CN 200710107698A CN 101054544 A CN101054544 A CN 101054544A
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- Prior art keywords
- chamber
- pipe
- tank body
- oil
- low temperature
- Prior art date
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- Granted
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- 239000004519 grease Substances 0.000 title claims abstract description 38
- 230000036571 hydration Effects 0.000 title abstract description 11
- 238000006703 hydration reaction Methods 0.000 title abstract description 11
- 239000002893 slag Substances 0.000 claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 238000009874 alkali refining Methods 0.000 claims abstract description 13
- 238000005406 washing Methods 0.000 claims abstract description 13
- 238000003756 stirring Methods 0.000 claims abstract description 8
- 239000002131 composite material Substances 0.000 claims description 14
- 238000011067 equilibration Methods 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 6
- 230000007704 transition Effects 0.000 claims description 5
- 238000004590 computer program Methods 0.000 claims description 3
- 238000004891 communication Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 10
- 238000005516 engineering process Methods 0.000 abstract description 6
- 238000007670 refining Methods 0.000 abstract description 2
- 230000007547 defect Effects 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 28
- 239000012535 impurity Substances 0.000 description 8
- 239000007788 liquid Substances 0.000 description 8
- 239000003513 alkali Substances 0.000 description 5
- 239000007921 spray Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000001465 metallisation Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- UPLPHRJJTCUQAY-WIRWPRASSA-N 2,3-thioepoxy madol Chemical compound C([C@@H]1CC2)[C@@H]3S[C@@H]3C[C@]1(C)[C@@H]1[C@@H]2[C@@H]2CC[C@](C)(O)[C@@]2(C)CC1 UPLPHRJJTCUQAY-WIRWPRASSA-N 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000012163 sequencing technique Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Lubricants (AREA)
Abstract
The invention relates to grease processing equipment, in particular to a combined grease continuous low-temperature hydration tank. The main body of the equipment is composed of a plurality of tank bodies 2 which have different diameters and are sleeved together, the cavity of the middle tank body 2 is a mixing chamber 4 provided with a stirring device and an oil-gas mixing device, other cavities are sequentially provided with a settling chamber 5, an alkali refining chamber 7, a water washing chamber 8 and a settling chamber 9, the upper part of each outdoor tank body is provided with an opening which is outwards connected with a guide pipe 10 or an oil conveying pipe 5, and the lower end of each outdoor tank body is respectively connected with a slag collecting tank 12 through a slag discharge port 11. Can continuously carry out a plurality of procedures such as deslagging, degumming, deacidification and the like, and can be used for high-temperature hydration operation of the grease. Therefore, the defects that the existing low-temperature hydration technology can not be continuously carried out and intermittent tank pouring is needed are overcome, and the oil refining equipment with simple structure, low cost and stable and reliable work is provided for realizing automation and programming of the oil hydration technology.
Description
Affiliated technical field
The present invention 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 low temperature hydrated equipment of combined fat 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 connection 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 cylindrical tank 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 |
|---|---|---|---|
| CN2007101076987A CN101054544B (en) | 2007-05-25 | 2007-05-25 | Composite type grease continuous low temperature hydrated pot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007101076987A CN101054544B (en) | 2007-05-25 | 2007-05-25 | Composite type grease continuous low temperature hydrated pot |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101054544A true CN101054544A (en) | 2007-10-17 |
| CN101054544B CN101054544B (en) | 2010-06-09 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2007101076987A Expired - Fee Related CN101054544B (en) | 2007-05-25 | 2007-05-25 | Composite type grease continuous low temperature hydrated pot |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101054544B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101185466B (en) * | 2007-12-18 | 2010-09-29 | 杨孟君 | Alkalization, decolorizing and deodorization integration pan for camellia oil precision machining |
| CN102293263A (en) * | 2011-07-29 | 2011-12-28 | 甘肃陇新综合商贸有限公司 | Physical low-temperature cold pressing production technology of refined walnut oil |
| CN107245375A (en) * | 2017-07-21 | 2017-10-13 | 成都市新兴粮油有限公司 | Rapeseed oil aquation Degumming method |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1042140C (en) * | 1992-05-03 | 1999-02-17 | 浙江轻工机械厂 | Method and equipment for continuous hydration degum of vegetable oil |
| CN201037140Y (en) * | 2007-05-20 | 2008-03-19 | 张建臣 | Combined type grease continuous low-temperature hydration tank |
-
2007
- 2007-05-25 CN CN2007101076987A patent/CN101054544B/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101185466B (en) * | 2007-12-18 | 2010-09-29 | 杨孟君 | Alkalization, decolorizing and deodorization integration pan for camellia oil precision machining |
| CN102293263A (en) * | 2011-07-29 | 2011-12-28 | 甘肃陇新综合商贸有限公司 | Physical low-temperature cold pressing production technology of refined walnut oil |
| CN107245375A (en) * | 2017-07-21 | 2017-10-13 | 成都市新兴粮油有限公司 | Rapeseed oil aquation Degumming method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101054544B (en) | 2010-06-09 |
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Granted publication date: 20100609 Termination date: 20160525 |