CN200949096Y - Wax remover for sunflower oil - Google Patents
Wax remover for sunflower oil Download PDFInfo
- Publication number
- CN200949096Y CN200949096Y CNU2006200915302U CN200620091530U CN200949096Y CN 200949096 Y CN200949096 Y CN 200949096Y CN U2006200915302 U CNU2006200915302 U CN U2006200915302U CN 200620091530 U CN200620091530 U CN 200620091530U CN 200949096 Y CN200949096 Y CN 200949096Y
- Authority
- CN
- China
- Prior art keywords
- sunflower oil
- water
- tank body
- pipe
- cooling tube
- 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
- 235000019486 Sunflower oil Nutrition 0.000 title claims abstract description 19
- 239000002600 sunflower oil Substances 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 46
- 238000001816 cooling Methods 0.000 claims abstract description 43
- 239000002826 coolant Substances 0.000 claims abstract description 3
- 238000004018 waxing Methods 0.000 claims description 12
- 239000000446 fuel Substances 0.000 claims description 5
- 230000000630 rising effect Effects 0.000 claims description 5
- 239000003921 oil Substances 0.000 abstract description 18
- 235000019198 oils Nutrition 0.000 abstract description 18
- 238000003756 stirring Methods 0.000 abstract description 6
- 238000002425 crystallisation Methods 0.000 abstract description 3
- 230000008025 crystallization Effects 0.000 abstract description 2
- 239000013078 crystal Substances 0.000 abstract 2
- 238000005057 refrigeration Methods 0.000 abstract 1
- 230000003068 static effect Effects 0.000 abstract 1
- 239000001993 wax Substances 0.000 description 15
- 238000000034 method Methods 0.000 description 5
- 239000004519 grease Substances 0.000 description 4
- 230000002035 prolonged effect Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 241000549173 Celastrus scandens Species 0.000 description 1
- 241000628997 Flos Species 0.000 description 1
- 241000208818 Helianthus Species 0.000 description 1
- 235000003222 Helianthus annuus Nutrition 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 239000008157 edible vegetable oil Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 235000008935 nutritious Nutrition 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
Images
Classifications
-
- 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
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model relates to a mechanical device, namely a sunflower oil wax remover. The existing sunflower oil wax remover is provided with a tank body, double water-cooling walls are arranged on the periphery of the tank body, sunflower oil is cooled through water cooling to be dewaxed, the tank body needs to be stirred during operation, a crystal growing tank needs to be added, and the sunflower oil wax remover is complex in structure, high in power consumption and low in efficiency. For this reason, develop a new-type sunflower oil wax remover, this kind of wax remover also has a jar body (1), also is equipped with oil inlet (2) and oil discharge outlet (6) on jar body (1), and the institute is different: the cooling pipe (3) communicated with the coolant circulating system is arranged in the tank body (1), the internal water cooling area is enlarged, even refrigeration can be realized without stirring, the sunflower oil is cooled in a relatively static state, wax crystallization is facilitated, a stirrer, a crystal growing tank and a stirring power device are omitted, the operation quality is obviously improved, and the cost is obviously reduced.
Description
Technical field the utility model relates to a kind of mechanism, promptly a kind of de-waxing apparatus for sunflower oil.
The background technology Trisun Oil R 80 is the grease that extracts from the real the inside of the son of Sunflower Receptacle, and is nutritious, give off a strong fragrance, and be high-quality edible oil and important industrial raw material., a large amount of waxs is contained in Trisun Oil R 80 the inside, deposits in the process wax and separates out and be floss, influences greasy impression and quality, therefore needs to remove.At present, dispel wax and adopt method of cooling more, promptly use a cooling tank, around the tank body is double-deck water wall, and Trisun Oil R 80 is put into jar, and makes the water cycle in the water wall, so that the heat in the oil is taken away, wax is crystallizable separating out after the Trisun Oil R 80 cooling, by filtering wax is separated, as the raw material of various wax works again., there are many shortcomings in this wax apparatus that removes.For example: tank skin and width between centers are far away, and cooling rate is very fast on every side, and the centre is but very slow, inside and outside inequality.Particularly outer wax can hinder the carrying out of heat exchange attached on the tank skin, thereby has prolonged the time of dewaxing.In order to improve refrigerative efficient, in jar, installed agitator additional, make a jar interior oil tanker stream contact water wall by stirring, make the oil body uniform decrease in temperature, like this, can improve cooling rate, can prevent tank skin extension wax again., this stirring has also brought many drawbacks, needs consume electric power on the one hand, increase mixing component and power set, stirring is stirred grease on the other hand, is unfavorable for that the wax crystalline forms, grease after the cooling also need be deposited for some time under the immobilized state, prolonged to account for a jar time.In order to improve the utilization ratio of cooling tank, also to increase a maturator on the next door of cooling tank, cooled grease is poured into and is carried out crystallisation process in the maturator.This mode needs two jars, and structure and technological process be more complicated all, has increased the extraction difficulty of Trisun Oil R 80.
The summary of the invention the purpose of this utility model provides a kind of compact construction, and is easy and simple to handle, cost and all lower de-waxing apparatus for sunflower oil of power consumption.
Above-mentioned purpose is realized by following technical scheme: develop a kind of de-waxing apparatus for sunflower oil, this Wax remover also has the tank body of a hollow, also be provided with oil-in and fuel outlet on the tank body, different is: be provided with the cooling tube that is connected with coolant circulating system in the said tank body.
It is medium with water that said cooling tube is one, and reciprocating disk around spiral tube, an end of spiral tube is a water inlet pipe, the other end is a return water pipe, water inlet pipe and return water pipe and water pump and water source constitute water-flow circuit.
Said cooling tube is different by two above spiral shells footpaths, and the spiral tube suit in parallel that communicates with same water inlet pipe and same return water pipe forms.
Adopt the de-waxing apparatus for sunflower oil of such scheme, strengthened inner water-cooled area, need not stir also and can evenly freeze, Trisun Oil R 80 can lowered the temperature under the immobilized state relatively, and wax also crystallization is simultaneously separated out, thereby has omitted agitator and power set, and omitted a crystallizer, simplify the structure and technological process, reduced cost and power consumption, have considerable market outlook.
Description of drawings embodiment of the present utility model and concrete structure are provided by the following drawings:
Fig. 1 is the front view of first kind of embodiment;
Fig. 2 is the vertical view of first kind of embodiment;
Fig. 3 is the partial view of second kind of embodiment;
Fig. 4 is the partial view of the 4th kind of embodiment.
Fig. 5 is the partial view of the 5th kind of embodiment.
Among the figure as seen: tank body 1, oil-in 2, cooling tube 3, water inlet pipe 4, return water pipe 5, fuel outlet 6, support 7, middle level cooling tube 8, internal layer cooling tube 9, double-deck water wall 10.
Embodiment is introduced five kinds of embodiment below in conjunction with accompanying drawing:
First kind of embodiment: as shown in Figure 1, 2, this Wax remover also is a thin and tall hollow vessel 1, and there is oil-in 2 upper end, and there is fuel outlet 6 lower end, is supported by support 7 below.Its improvements are: be provided with in tank body 1 the inside one group of reciprocating disk around spiral helicine cooling tube 3, can feed various liquid refrigerants in the cooling tube 3, the most frequently used is cold water, cold water passes through the micro pump pump circulation by the water source, enter from the water inlet pipe 4 of cooling tube 3 upper ends, emit from the return water pipe 5 of lower end.During work, Trisun Oil R 80 is sent in the jar from oil-in 2, switched on the pump that it is cooling water circulation to make, thereby the Trisun Oil R 80 heat is taken away.After the Trisun Oil R 80 cooling, wax wherein is crystallizable separating out, and evenly is suspended in the oil.Then, open fuel outlet 6, in jar the pressurization or from end by negative pressure oily sucking-off, enter strainer oil leached, wax is separated.Higher at wax content, or oil can adopt the measure of twice paraffin removal when having relatively high expectations.Promptly the oil that first jar emitted is sent in second jar, perhaps sends back in first jar, and further growing the grain is gone and filtered.
Second kind of embodiment: height, lift angle and the number of cooling tube 3 in jar will determine according to the volume of tank body 1, and in general, 100mm's cooling range that every section pipe is born is advisable to be no more than on every side.As shown in Figure 3, this cooling tube is to form promptly outer cooling tube 3 by the spiral tube suit that does not wait in three groups of spiral shell footpaths, middle level cooling tube 8, internal layer cooling tube 9 is formed, and water inlet pipe 3 and rising pipe 5 communicate with the two ends of three spiral tubes respectively, are parallel-connection structure between three spiral tubes.
The third embodiment: cooling tube also is to be formed by the spiral tube suit that does not wait in three groups of spiral shell footpaths, promptly by outer cooling tube 3, middle level cooling tube 8, internal layer cooling tube 9 is formed, three groups of cooling tubes are to be coiled to form by a branching pipe, water inlet pipe 3 and rising pipe 5 communicate with the top of the first layer spiral tube and the end of the 3rd helical layer pipe respectively, are end to end cascaded structure between three spiral tubes.
The 4th kind of embodiment: as shown in Figure 4, the refrigerating unit of this Wax remover has also kept the double-deck water wall 10 of original tank body except the spiral tube of jar the inside, also claim chuck, water wall 10 both can communicate with spiral tube, also can circulate separately, both cooperate, and can improve cooling efficiency.
The 5th kind of embodiment: as shown in Figure 5, the cooling tube 3 of jar the inside is the standpipe of some Zhi Shuli, and standpipe can link to each other respectively at two ends, also can be end to end, but the individual layer setting, but also multilayer setting, every standpipe all is connected with water inlet pipe and return water pipe, and its principle of work is identical with precedent.
Claims (7)
1. a de-waxing apparatus for sunflower oil also has a tank body (1), also is provided with oil-in (2) and fuel outlet (6) on the tank body (1), it is characterized in that: be provided with the cooling tube (3) that is connected with coolant circulating system in the said tank body (1).
2. de-waxing apparatus for sunflower oil according to claim 1, it is characterized in that: said cooling tube (3) be a reciprocating disk around spiral tube, one end of spiral tube is water inlet pipe (4), and the other end is return water pipe (5), and water inlet pipe (4) and return water pipe (5) constitute water-flow circuit with water pump and water source.
3. de-waxing apparatus for sunflower oil according to claim 1 is characterized in that: said cooling tube (3) is different by two-layer above spiral shell footpath, and the spiral tube that communicates with same water inlet pipe (4) and same return water pipe (5) suit in parallel forms.
4. de-waxing apparatus for sunflower oil according to claim 1, it is characterized in that: the said cooling tube (3) that constitutes by the different spiral tube in two-layer above spiral shell footpath, each helical layer pipe is end to end, water inlet pipe (4) joins with the top of the first layer spiral tube, and return water pipe (5) joins with the end of last helical layer pipe.
5. de-waxing apparatus for sunflower oil according to claim 1 is characterized in that: the said tank body (1) that cooling tube (3) are housed, its tank skin is double-deck water wall (10), the cavity of water wall (10) and the shared water inlet pipe of cooling tube (3) (4) and rising pipe (5).
6. de-waxing apparatus for sunflower oil according to claim 1, it is characterized in that: the said tank body (1) that cooling tube (3) are housed, its tank skin is double-deck water wall (10), and the cavity of water wall (10) is connected to water inlet pipe (4) and rising pipe (5), constitutes the independently recycle system.
7. de-waxing apparatus for sunflower oil according to claim 1 is characterized in that: the cooling tube (3) of said tank body (1) the inside is the standpipe of some Zhi Shuli, and each standpipe all is connected with water inlet pipe (4) and rising pipe (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006200915302U CN200949096Y (en) | 2006-06-09 | 2006-06-09 | Wax remover for sunflower oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006200915302U CN200949096Y (en) | 2006-06-09 | 2006-06-09 | Wax remover for sunflower oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200949096Y true CN200949096Y (en) | 2007-09-19 |
Family
ID=38891641
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2006200915302U Expired - Fee Related CN200949096Y (en) | 2006-06-09 | 2006-06-09 | Wax remover for sunflower oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200949096Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104709621A (en) * | 2015-03-17 | 2015-06-17 | 张建臣 | Liquid laminar flow processor |
| CN104826356A (en) * | 2015-03-17 | 2015-08-12 | 张建臣 | Liquid laminar-flow crystallizer |
-
2006
- 2006-06-09 CN CNU2006200915302U patent/CN200949096Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104709621A (en) * | 2015-03-17 | 2015-06-17 | 张建臣 | Liquid laminar flow processor |
| CN104826356A (en) * | 2015-03-17 | 2015-08-12 | 张建臣 | Liquid laminar-flow crystallizer |
| CN104826356B (en) * | 2015-03-17 | 2016-05-18 | 张建臣 | Liquid laminar flow crystallizer |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US8203014B2 (en) | Fractionation processes and devices for oils and fats | |
| CN1197637C (en) | Freeze concentration for aqueous solutions | |
| CN102021107B (en) | Total-reflux white spirit freezing and filtering device and method thereof | |
| DK2464717T3 (en) | Device and method of fermentation | |
| CN210559482U (en) | Freezing crystallization sodium sulfate removal device | |
| CN2794513Y (en) | Dripping pill machine | |
| CN200949096Y (en) | Wax remover for sunflower oil | |
| CN101129206B (en) | Device for separating ice and crystal | |
| CN203170321U (en) | Reaction kettle | |
| CN101077140B (en) | Crystal diabetin manufacturing technique on vertical type continuous crystallizer | |
| CN101092588A (en) | Wax remover for sunflower oil | |
| CN201168456Y (en) | Low-temperature grease crystallizing tank | |
| EA017783B1 (en) | Plant for water purification | |
| CN207775186U (en) | Energy-efficient fat crystals maturator | |
| CN212881137U (en) | Vertical wall-scraping type continuous crystallization device | |
| CN2915834Y (en) | Crystallizer for salt cake separation using freeze method | |
| EP3096852B1 (en) | A modular sub-unit for a suspension crystallization system and a suspension crystallization process using said modular sub-unit | |
| CN209846131U (en) | A stirring filter equipment for honey purification | |
| CN203128523U (en) | Fish oil refining device | |
| CN205235452U (en) | Crystallization kettle | |
| RU2505593C1 (en) | Method of purifying vegetable oil | |
| Anuar et al. | Effect of stirring rate and freezing time on the percentage of recovery of residual oil from palm oil mill effluent via a stirred freeze crystallizer | |
| CN101054544A (en) | Combined type grease continuous low-temperature hydration tank | |
| CN211394333U (en) | Azo-bis-isobutyronitrile integrated dissolution and crystallization production device | |
| CN219001209U (en) | Cooling device for pill dropping machine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070919 Termination date: 20100609 |