CN102311871A - Sesame oil dehydration method and device - Google Patents
Sesame oil dehydration method and device Download PDFInfo
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- CN102311871A CN102311871A CN201110224949A CN201110224949A CN102311871A CN 102311871 A CN102311871 A CN 102311871A CN 201110224949 A CN201110224949 A CN 201110224949A CN 201110224949 A CN201110224949 A CN 201110224949A CN 102311871 A CN102311871 A CN 102311871A
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Abstract
The invention belongs to the field of edible oil dehydration, and provides a sesame oil dehydration device. The device provided by the invention comprises an adsorbent inlet, a sesame oil inlet, a reactor, a stirrer, a heater, a motor, a speed changer, a filter and a transfer pump, wherein the adsorbent inlet and the sesame oil inlet are arranged on the upper portion of the reactor; the stirrer and the heater are installed inside the reactor; the motor is installed on the top of the reactor; the stirrer is connected with the motor through the speed changer; and the filter communicates with the reactor through the transfer pump. According to the sesame oil dehydration device, a mixed solution of the sesame oil to be dehydrated and an adsorbent is heated and stirred by the heater and the stirrer, and the mixed solution is filtered and separated by the adoption of the filter to obtain the sesame oil, trace water of which is dehydrated. In addition, silica gel is used for dehydration to dry and absorb water, thus preventing the addition of original drying agent and peculiar smell of the product.
Description
Technical field
The invention belongs to edible oil lipid dehydration field, relate in particular to a kind of til dewatering and device.
Background technology
In the grease course of processing; A kind of low temperature pressing method of making oil is arranged, make oil expression fat just, because some heat-sensitive substances are arranged in the grease; Their existence is concerning the people of food oils; To health is useful, and has the moisture of trace to exist in the oil plant expressing process, can not carry out thermal dehydration again on the technology.The existence of minor amount of water can cause following problem, and the one, greasy freshness date short (the commodity shelf-lives is short), the 2nd, the poor transparency of grease finished product, the 3rd, crude oil causes filtering filter cake to be clamminess when filtering, and causes the difficulty of unloading cake.
In the oil plant course of processing, or a kind of sesame oil producing process, water is produced Oleum Sesami for method; High temperature is fried seed squeezing heavy fragrant peanut oil, because contain abundant fragrance matter in the grease, greasy concise heat can cause fragrance matter to run off; Therefore can not remove micro-moisture with the method for heating, more can not remove colloidal impurity, can only remove colloidal impurity with the cooling filter method with adding the method that water hydratable comes unstuck; And cooling filtering and removing colloidal impurity is not thorough yet; So quality product is not very stable,, can make the grease refining process quickness and high efficiency that becomes if solved the problem that flavor oil or pressed oil contain minor amount of water.
The sorbent material that uses in the adsorption dewatering at present is refining the forming of ore deposit soil of natural inorganic thing mostly, and they all have " native raw meat " flavor, can bring assorted flavor if be used for to grease in the adsorption dewatering process; Can make the local flavor variation of product; And now for above-mentioned special greasy dehydration, the one, lean on freezing and filtering, the 2nd, lean on natural sedimentation; These two kinds of method production efficiencys are too low, and not thorough.
Summary of the invention
The invention provides a kind of til dewatering and device, be intended to solve at present for special greasy dehydration, the freezing and filtering that is adopted, the dewatering of natural sedimentation; Production efficiency is too low, dehydration is not thorough; And the ore deposit that to be used for greasy adsorption dewatering sorbent material be the natural inorganic thing mostly soil is refining to form, and they all have " native raw meat " flavor, if; Can bring assorted flavor to grease, make the problem of product special flavour variation.
The object of the present invention is to provide a kind of til dewatering unit, this device comprises: sorbent material inlet, til inlet, reactor drum, whisking appliance, well heater, phonomoter, variator, filter, transferpump; Said sorbent material inlet enters the mouth with said til and is arranged on the top of said reactor drum; Said whisking appliance and said well heater are installed in the inside of said reactor drum; Said electric motor mount is at the top of said reactor drum; Said whisking appliance is connected with said phonomoter through said variator, and said filter is connected with said reactor drum through said transferpump.
Another object of the present invention is to provide a kind of til dewatering, this method may further comprise the steps:
With til to be drained off and silica type sorbent material injecting reactor, get both mixed solutions;
In reactor drum, the gained mixed solution is stirred, heats;
Mixed solution behind the filtering reaction obtains removing the sesame grease of minor amount of water.
Til dehydrated device provided by the invention is through adopting well heater, whisking appliance, the mixed solution of til to be drained off and silica type sorbent material is heated, stirs, and the application of filtration machine carries out filtering separation to mixed solution; Obtained removing the sesame grease of minor amount of water, to be used for can not be with the food oils complete processing of heating means dehydrations, perhaps after other greases are with hydration degum without the grease of heat drying; Use the principle of siccative adsorption dry; Accomplish removing of micro-moisture, and adopt the silica dehydrator adsorption dewatering, can prevent the adding of former siccative; Bring peculiar smell to product, influence the problem of product quality.
Description of drawings
Fig. 1 is the structural representation of the til dewatering unit that provides of the embodiment of the invention;
Fig. 2 is the schema of the til dewatering that provides of the embodiment of the invention.
Among the figure: 1, sorbent material inlet; 2, til inlet; 3, whisking appliance; 4, well heater; 5, reactor drum; 6, variator; 7, transferpump; 8, filter.
Embodiment
In order to make the object of the invention, technical scheme and advantage clearer,, the present invention is further specified below in conjunction with accompanying drawing and embodiment.Should be appreciated that specific embodiment described herein only in order to explanation the present invention, and be not used in the qualification invention.
Fig. 1 shows the structure of the til dewatering unit that the embodiment of the invention provides.For the ease of explanation, only show the part relevant with the present invention.
This device comprises: sorbent material inlet 1, til inlet 2, reactor drum 5, whisking appliance 3, well heater 4, phonomoter, variator 6, filter 8, transferpump 7; Sorbent material inlet 1 and til inlet 2 are arranged on the top of reactor drum 5; Whisking appliance 3 and well heater 4 are installed in the inside of reactor drum 5; Electric motor mount is at the top of reactor drum 5, and whisking appliance 3 is connected with phonomoter through variator 6, and filter 8 is connected with reactor drum 5 through transferpump 7.
As a preferred version of the embodiment of the invention, reactor drum 5 diameters are 1200 millimeters.
As a preferred version of the embodiment of the invention, filter 8 adopts plate and frame filter 8.
As a preferred version of the embodiment of the invention, the filtration medium that plate and frame filter 8 adopts is industrial all cloth.
Fig. 2 shows the realization flow of the til dewatering that the embodiment of the invention provides.
A kind of til dewatering, this method may further comprise the steps:
In step S201,, get both mixed solutions with til to be drained off and silica type sorbent material injecting reactor 5;
In step S202, in reactor drum 5, the gained mixed solution is stirred, heats;
In step S203, the mixed solution behind the filtering reaction obtains removing the sesame grease of minor amount of water.
In embodiments of the present invention, in reactor drum 5, the implementation method that the gained mixed solution is stirred, heats is:
Start the phonomoter of til dewatering unit, drive whisking appliance 3 and rotate, be set to 20～500rpm, mix liquid through variator 6 stirring velocitys;
Open the well heater 4 of til dewatering unit, Heating temperature is set to 40～70 degrees centigrade, the heating mixed solution.
In embodiments of the present invention, the mixed solution behind the filtering reaction, the implementation method that obtains removing the sesame grease of minor amount of water is:
Open transferpump 7, the grease that will contain sorbent material pumps in the filter 8 and filters, and obtains removing the sesame grease of minor amount of water.
Below in conjunction with accompanying drawing and specific embodiment application principle of the present invention is further described.
As shown in Figure 1, sorbent material inlet 1 and til inlet 2 are arranged in reactor drum 5 tops, and inside is well heater 4, and the top of reactor drum 5 is equipped with variator 6, and reactor drum 5 is connected with filter 8 through transferpump 7.
Grease to be drained off is placed a reactor drum 5, and reactor drum 5 is airtight, and whisking appliance 3, well heater 4 are installed in reactor drum 5; The compound siccative that takes off that adds silica gel; Be heated to 50～900 degrees centigrade the time, reacted 30～50 minutes, the grease that will contain silica gel after the end is squeezed into filter 8 and is filtered; The grease that obtains does not contain micro-moisture, and is as clear as crystal.
Be that example further specifies principle of work and process with the dehydration of moisture 0.2% til below.
Til to moisture 0.2% advances adsorption dewatering, and squeezing into diameter at grease to be drained off is in 1200 millimeters the reactor drum 5, the stirring velocity of reactor drum 5 be set to 200 circles/minute; Through well heater 4 reactor drum 5 temperature inside are controlled to be 50 degrees centigrade; Start whisking appliance 3, stirring reaction 25 minutes is after stirring; Open transferpump 7; Squeeze into flame filter press 8 to the grease that contains siccative and filter, filter 8 adopts industrial all cloth as filtration medium, obtains the sesame grease that dewaters at last.
The til dehydrated device that the embodiment of the invention provides is through adopting whisking appliance 3, well heater 4, the mixed solution of til to be drained off and silica type sorbent material is heated, stirs, and 8 pairs of mixed solutions of application of filtration machine carries out filtering separation; Obtained removing the sesame grease of minor amount of water, to be used for can not be with the food oils complete processing of heating means dehydrations, perhaps after other greases are with hydration degum without the grease of heat drying; Use the principle of siccative adsorption dry; Accomplish removing of micro-moisture, and adopt the silica dehydrator adsorption dewatering, can prevent the adding of former siccative; Bring peculiar smell to product, influence the problem of product quality.
The above is merely preferred embodiment of the present invention, not in order to restriction the present invention, all any modifications of within spirit of the present invention and principle, being done, is equal to and replaces and improvement etc., all should be included within protection scope of the present invention.
Claims (7)
1. a til dewatering unit is characterized in that, this device comprises: sorbent material inlet, til inlet, reactor drum, whisking appliance, well heater, phonomoter, variator, filter, transferpump;
Said sorbent material inlet enters the mouth with said til and is arranged on the top of said reactor drum; Said whisking appliance and said well heater are installed in the inside of said reactor drum; Said electric motor mount is at the top of said reactor drum; Said whisking appliance is connected with said phonomoter through said variator, and said filter is connected with said reactor drum through said transferpump.
2. device as claimed in claim 1 is characterized in that, said reactor diameter is 1200 millimeters.
3. device as claimed in claim 1 is characterized in that, said filter adopts the plate and frame filter.
4. device as claimed in claim 3 is characterized in that, the filtration medium that said plate and frame filter adopts is industrial all cloth.
5. a til dewatering is characterized in that, this method may further comprise the steps:
With til to be drained off and silica type sorbent material injecting reactor, get both mixed solutions;
In reactor drum, the gained mixed solution is stirred, heats;
Mixed solution behind the filtering reaction obtains removing the sesame grease of minor amount of water.
6. method as claimed in claim 5 is characterized in that, and is said in reactor drum, and the implementation method that the gained mixed solution is stirred, heats is:
Start the phonomoter of til dewatering unit, drive whisking appliance and rotate, be set to 20～500rpm, mix liquid through the variator stirring velocity;
Open the well heater of til dewatering unit, Heating temperature is set to 40～70 degrees centigrade, the heating mixed solution.
7. method as claimed in claim 5 is characterized in that, the mixed solution behind the said filtering reaction, and the implementation method that obtains removing the sesame grease of minor amount of water is:
Open transferpump, the grease that will contain sorbent material pumps in the filter and filters, and obtains removing the sesame grease of minor amount of water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110224949A CN102311871A (en) | 2011-08-08 | 2011-08-08 | Sesame oil dehydration method and device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110224949A CN102311871A (en) | 2011-08-08 | 2011-08-08 | Sesame oil dehydration method and device |
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| Publication Number | Publication Date |
|---|---|
| CN102311871A true CN102311871A (en) | 2012-01-11 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201110224949A Pending CN102311871A (en) | 2011-08-08 | 2011-08-08 | Sesame oil dehydration method and device |
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| CN (1) | CN102311871A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102787015A (en) * | 2012-08-17 | 2012-11-21 | 冯明华 | Normal-temperature dewatering and purifying method of rapeseed oil |
| CN103085306A (en) * | 2013-02-20 | 2013-05-08 | 朱杵养 | Vacuum environment-friendly oil pressing machine |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1160755A (en) * | 1996-03-21 | 1997-10-01 | 崔有志 | Preparation of refined orange oil |
| CN1400298A (en) * | 2002-04-16 | 2003-03-05 | 李大鹏 | Fruit kernel oil extracted from plant fruit kernel, its extraction method, medicinal composite and application |
| CN101574107A (en) * | 2009-05-25 | 2009-11-11 | 葛康年 | Refined sesame oil manufacture process |
| CN201506783U (en) * | 2009-09-28 | 2010-06-16 | 潍坊中业化学有限公司 | Refining castor oil dehydration device |
| CN101760296A (en) * | 2009-11-13 | 2010-06-30 | 段洪东 | Extraction method of volatile oil in wild green onion |
| CN101768511A (en) * | 2010-01-27 | 2010-07-07 | 卢玉胜 | Low-temperature refining method for tea seed oil and refining adsorbent |
-
2011
- 2011-08-08 CN CN201110224949A patent/CN102311871A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1160755A (en) * | 1996-03-21 | 1997-10-01 | 崔有志 | Preparation of refined orange oil |
| CN1400298A (en) * | 2002-04-16 | 2003-03-05 | 李大鹏 | Fruit kernel oil extracted from plant fruit kernel, its extraction method, medicinal composite and application |
| CN101574107A (en) * | 2009-05-25 | 2009-11-11 | 葛康年 | Refined sesame oil manufacture process |
| CN201506783U (en) * | 2009-09-28 | 2010-06-16 | 潍坊中业化学有限公司 | Refining castor oil dehydration device |
| CN101760296A (en) * | 2009-11-13 | 2010-06-30 | 段洪东 | Extraction method of volatile oil in wild green onion |
| CN101768511A (en) * | 2010-01-27 | 2010-07-07 | 卢玉胜 | Low-temperature refining method for tea seed oil and refining adsorbent |
Non-Patent Citations (3)
| Title |
|---|
| 《粮油工业志》 19940930 河南省粮油志编纂委员会 水代法 1-4 , 第1版 * |
| 刘洪章: "硅胶行业的现状和未来发展", 《2008全国无机硅化物行业协会年会论文集》 * |
| 河南省粮油志编纂委员会: "《粮油工业志》", 30 September 1994 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102787015A (en) * | 2012-08-17 | 2012-11-21 | 冯明华 | Normal-temperature dewatering and purifying method of rapeseed oil |
| CN103085306A (en) * | 2013-02-20 | 2013-05-08 | 朱杵养 | Vacuum environment-friendly oil pressing machine |
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Application publication date: 20120111 |