CN1250082A - Oil material extruding and puffing technology and apparatus - Google Patents
Oil material extruding and puffing technology and apparatus Download PDFInfo
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- CN1250082A CN1250082A CN 99123044 CN99123044A CN1250082A CN 1250082 A CN1250082 A CN 1250082A CN 99123044 CN99123044 CN 99123044 CN 99123044 A CN99123044 A CN 99123044A CN 1250082 A CN1250082 A CN 1250082A
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- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
- Edible Oils And Fats (AREA)
Abstract
The main technological feature of the present invention is that oil raw material is first crushed, then extruded and puffed, and finally lixiviated. Compared with available oil material extruding and puffing process or traditional oil making pre-treatment,the said technological process has no crushing, softening, rolling, steaming, pre-pressing steps and relevant equipment. The apparatus uses axially opened thimble with automatically controlled temperature. The lixiviator and other apparatus have optimized parameters and thus have high production capacity and oil extracting rate.
Description
The invention belongs to lixiviation process and produce oil plant extruding puffing processing technique field in the greasy preprocessing process.
In recent years, domestic have many utility model patents to relate to this technology.932434053), the oil plant extruder patent (patent No.: 94212300X), the self-cleaning type oil plant extruder patent (patent No.: 942118405) etc. as the bulking machine patent (patent No.:.Before its oil plant enters extruder, still need and carry out fragmentation, soften, roll embryo, steam operations such as frying (or oven dry), pre-press for extracting juice.Pertinent data report and computer search result all show, also do not find domestic use oil plant extruding and puffing technology, make original equipment leaching ability increase by 50% research or achievement report.Relate to the oil plant extruder of the U.S. Anderson company that the mainly contains production of this technology abroad, we have carried out examination on the spot to it.Its in Jinzhou, ground such as 93 farms, Heilungkiang, the farm of advancing use the result to show that make former leacher leaching ability increase at 50% o'clock, dregs of rice Residual oil is about 1.5%.And the fragmentation of before oil plant (mainly being soybean) enters extruder, still needing, soften, roll embryo, steam operation and equipment such as stir-fry.Patent-improved soyabean processing patent (the patent No.: EP0341020 that relates to this technology abroad, applicant: The French Oil Mill Machinery Company, inventor: Upchurch, Ray), this patent is saved softening, roll embryo, pressing technology and equipment in advance of traditional immersion oil preprocessing process, has increased pulverizing and extruding-puffing technique and equipment.During the extruding puffing soybean, the material particular diameter that enters bulking machine is 0.254mm～0.508mm, and band pressure hot steam is directly injected material between screw rod and the sleeve, adds thermal material.The material of discharging from nib is column, its diameter, and length is 12.71～25.4mm, and each operation of all the other technological processs (take off as soybean oven dry, cleaning, fragmentation, peeling, leaching, precipitation, steaming etc.) is identical with the traditional technology process.This patent is not pointed out the parameters optimization of oil plant (soybean) extruding-puffing technique, and corresponding effect, the degree that reduces as the residual oil content of the raising degree of the leaching ability of former leaching plant and the dregs of rice etc.According to relevant bibliographical information (Herman Rittner Conditioning ofOil-Bearing Materials for Solvent Extraction by Extrusion.JAOCS1984, Vol.64, No.7:1200-1203).In traditional soybean oil leaching process, use the soybean extruding-puffing treatment process, can make original equipment leaching ability improve nearly 100%.
The object of the present invention is to provide a kind of lixiviation process to produce oil plant (as soybean, maize etc.) extruding-puffing technique and extrusion pressing puffing apparatus thereof in the grease preprocessing process.When its support equipment is done corresponding improvement, adopt the extruding puffing optimal parameters, can make the leaching ability of former leacher and the throughput of original system all improve 60%～150%, dregs of rice residual oil content≤1%, simultaneously, save that present oil plant extruding-puffing technique needs or the oil plant that the oily preprocessing process of tradition system adopts fragmentation, soften, roll embryo, steam operation and equipment such as frying (or oven dry), pre-press for extracting juice.
Technology contents of the present invention
It is characterized in that oil plant-soybean, maize etc., moisture is ground into the particle that particle diameter is 0.6mm-1.0mm less than 14%, enters extrusion pressing puffing apparatus (seeing accompanying drawing) from feeding mouth 1, and the material after expanded is extruded from nib 5, is cooled to 50 ℃-55 ℃, enters leacher.The compass screen surface alive at the solvent oil flow of leacher, the sieve end is long-pending, the rotating speed of leacher etc. should be aligned.Simultaneously, the throughput of wet dregs of rice precipitation and parts such as drying plant, miscella evaporation and stripping apparatus, solvent condenses and cooling apparatus should be done corresponding improvement.The sleeve 2 of extrusion pressing puffing apparatus is axial opposite opened.Sleeve 2 closures, locking during work, when checking screw rod 3 grades parts or cleaning are inner in addition, template of dismantling 4 and fastening piece 6, sleeve 2 along the outwards rotation of A, B point, separate sleeve respectively vertically.The outside surface of sleeve 2 is by band pressure hot steam or electrically heated, by water coolant or force air cooling.The warm self controllable adjusting of tube.Screw rod 3, sleeve 2 combine by more piece.Oil plant extruding puffing optimal parameters scope of the present invention is: the temperature of sleeve 2 is 55 ℃-105 ℃, self controllable adjusting, and the rotating speed of screw rod 3 is that 180r/min-300r/min is adjustable, the aperture of nib 4 is that Φ 4-Φ 20 is adjustable.The moisture of oil plant and pulverizing back particle diameter are as described above.Use oil plant extruding puffing immersion oil preprocessing process of the present invention to be: oil plant (as soybean, maize etc., its moisture is less than 14%), (particle diameter is 0.6mm-1.0mm for → cleaning (impurity elimination, remove stone, de-iron etc.) → pulverize.As when requiring defilming soybean (other oil plants do not have this requirement), then soybean needs broken (4～6 lobe), and peeling is then pulverized again, and particle diameter is the same.) → extruding puffing → cooling (to 50 ℃-55 ℃) → enter leacher (leacher and support equipment all should be done corresponding improvement by aforementioned requirement).Be the technological process identical such as precipitation, drying of evaporation, stripping and the wet cypress of mixing oil then with traditional technology.
The present invention compared with prior art has following advantage:
1. the present invention points out that not in extruder cavity material directly injects the hot steam of band pressure, adds thermal material.The outside surface of sleeve 2 is by band pressure hot steam or electrically heated, by water coolant or force air cooling, the warm self controllable adjusting of tube.By the material that is extruded between sleeve 2 heating or cooling cover 2 internal surfaces and screw rod 3 outside surfaces.Present domestic and international oil plant extruder is that the EP0341020 patent all is hot steams that material is injected band pressure between screw rod and sleeve as the oil plant extruder and the patent No. of home-made oil plant extruder, Andersoan company, adds thermal material.And the sleeve temperature can not be regulated in automatic control.
2. after the present invention pointed out to treat that expanded oil plant is pulverized, particle diameter was 0.60mm-1.0mm.The patent No. is that particle diameter was 0.254mm-0.508mm after the oil plant (soybean) of EP0341020 patent was pulverized.
3. the present invention has pointed out the parameters optimization scope of oil plant extruding-puffing technique, and advantage.Its parameter is: the oil plant powder particle diameter is 0.60-1.0mm, and water content is less than 14%, and the rotating speed of screw rod 3 is that 180r/min-300r/min is adjustable, and the temperature of sleeve 2 is 55 ℃-105 ℃, self controllable adjusting, and the aperture of nib 5 is that Φ 4～Φ 20 is adjustable.When leacher and support equipment are done aforementioned improved, adopt above-mentioned parameters optimization.Its advantage is: can make former leacher leaching ability and original system throughput all increase 60%-150%, dregs of rice residual oil content is less than 1%.Oil plant extruding-puffing technique and extruder (patent No. is patent and other the oil plant extruder about patent and Anderson company of EP0341020 as the aforementioned) thereof all do not relate to these contents both at home and abroad at present.The present invention simultaneously cancels the fragmentation adopted in the needed or traditional oil plant preprocessing process of present oil plant extruder, softens, rolls embryo, steams operation and equipment such as frying (or oven dry), pre-press for extracting juice.Pulverizing, extruding-puffing technique and equipment have been increased.
Description of drawings: Figure of description is for implementing extrusion pressing puffing apparatus of the present invention.
The embodiment of the invention:, the invention process is described further below in conjunction with accompanying drawing.Accompanying drawing is for implementing oil plant extrusion pressing puffing apparatus of the present invention, the rotating speed of screw rod 3 is that 180r/min-300r/min is adjustable, through the oil plant (particle diameter is 0.60mm-1.0mm) after oven dry, cleaning, the pulverizing, water content is less than 14%) from feeding mouth 1 feeding extrusion pressing puffing apparatus, oil plant rotates with screw rod 3, simultaneously in the extrusion chamber that the internal surface of the outside surface of screw rod 3 and sleeve 2 constitutes, oil plant is carried to template 4 from feeding mouth 1 in the mistake that is extruded, shears, stirs becomes.The outside surface of band pressure hot steam or electrically heated sleeve 2, or by the outside surface of water coolant or force air cooling cover 2, by the oil plant in sleeve 2 heating or the cooling extrusion chamber, the warm self controllable conciliation of tube, the temperature of sleeve 2 is 55 ℃-105 ℃.The aperture of the nib 5 of template 4 is that φ 4-φ 20 is adjustable.The sleeve of extrusion pressing puffing apparatus is axial opposite opened.Check screw rod 3 grades in addition when parts or cleaning sleeve 2 inwalls and screw rod 3 outside surfaces, template of dismantling 4 and fastening piece 6, sleeve 2 along the outwards rotation of A, B point, separate sleeve respectively vertically.Sleeve 2 closures, locking during work.The oil plant that is extruded is extruded from nib 5, forms the porous columnar structure, is cooled to 50 ℃-55 ℃ then, is admitted to leacher.Each technology of follow-up oil plant leaching process is identical with traditional technology.
The present invention also processes applicable to the extruding puffing of Semen Brassicae campestris, peanut, sunflower seeds, cottonseed, rice bran etc. and pre-pressed cake thereof.
Claims (3)
1. an extruding puffing complete processing and extrusion pressing puffing apparatus thereof that is used for leaching the oil plant preprocessing process of legal system oil, it is characterized in that oil plant-soybean, maize etc., moisture＜14%, be ground into the particle of particle diameter 0.6～1.0mm, after expanded, directly enter leacher, save present oil plant and enter the fragmentation adopted in needed or traditional oil plant preprocessing process before the extruder, soften, roll embryo, steam (oven dry), operation and the equipment such as press for extracting juice in advance fried; Leacher and support equipment are done corresponding improvement; The self controllable adjusting of temperature of the sleeve of extrusion pressing puffing apparatus (2) is 55 ℃～105 ℃, and the rotating speed of screw rod (3) is that 180r/min～300r/min is adjustable, and the aperture of the nib (5) on the template (4) is that Φ 4～Φ 20 can wither.
2. extrusion pressing puffing apparatus according to claim 1, it is characterized in that its sleeve (2) is axial opposite opened, closed, the locking of sleeve during work (2), check when screw rod (3) waits other parts or cleaning inner, template of dismantling (4) and fastening piece (6), sleeve (2) outwards rotates along A, B point respectively, and sleeve (2) is separated vertically; The outside surface of sleeve (2) is by band pressure hot steam or electrically heated, by water coolant or force air cooling, the warm self controllable adjusting of tube; Screw rod (3) and sleeve (2) are the more piece built-up type, and the aperture of the rotating speed of screw rod (3) and nib (5) is all adjustable.
3. oil plant extruding-puffing technique according to claim 1, leacher and support equipment thereof need be done corresponding improvement, solvent oil flow, the compass screen surface alive at the sieve end as leacher is long-pending, rotating speed etc. should be aligned, and the throughput of wet dregs of rice precipitation and parts such as drying plant, miscella evaporation and stripping apparatus, solvent condenses and cooling apparatus is done corresponding increase.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99123044 CN1250082A (en) | 1999-10-30 | 1999-10-30 | Oil material extruding and puffing technology and apparatus |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99123044 CN1250082A (en) | 1999-10-30 | 1999-10-30 | Oil material extruding and puffing technology and apparatus |
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| CN1250082A true CN1250082A (en) | 2000-04-12 |
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| CN 99123044 Pending CN1250082A (en) | 1999-10-30 | 1999-10-30 | Oil material extruding and puffing technology and apparatus |
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100408659C (en) * | 2006-07-07 | 2008-08-06 | 白长军 | Method of making mixed oil using cotton seed puffing impregnation process |
| CN102174344A (en) * | 2011-03-17 | 2011-09-07 | 朱文鑫 | Pretreatment method suitable for extracting one-time oil pressed cake |
| CN102295985A (en) * | 2011-07-30 | 2011-12-28 | 河南工业大学 | Wet sesame residue expansion granulation drying leaching and oil extraction process |
| CN102676289A (en) * | 2012-06-04 | 2012-09-19 | 山东省农业科学院农产品研究所 | Method for low temperature cold pressing of peanut oil |
| CN102703206A (en) * | 2012-06-19 | 2012-10-03 | 东北农业大学 | Method for extracting fragrant sunflower seed oil |
| CN103614234A (en) * | 2013-12-12 | 2014-03-05 | 酉阳县康友粮油有限公司 | Rapeseed pre-pressing technology |
| CN105996102A (en) * | 2016-07-14 | 2016-10-12 | 天津市真如果食品工业有限公司 | Expanded food extruder |
| CN107043650A (en) * | 2017-06-01 | 2017-08-15 | 湖北恒贸茶油有限公司 | Seed device is steamed in the extruding for producing tea oil |
| CN110343565A (en) * | 2019-08-21 | 2019-10-18 | 嘉里粮油（营口）有限公司 | A kind of expansion extraction oil technique, edible fat production technique and device |
| CN112175712A (en) * | 2019-07-03 | 2021-01-05 | 上海谷励智能设备有限公司 | Ultrasonic wall-breaking screw device for vegetable oil |
| CN115678668A (en) * | 2022-10-24 | 2023-02-03 | 安徽华安食品有限公司 | Rapeseed oil leaching processing wet meal desolventizing device and implementation method |
| CN116159843A (en) * | 2023-01-10 | 2023-05-26 | 江苏丰尚油脂工程技术有限公司 | Oil byproduct processing equipment and processing method |
-
1999
- 1999-10-30 CN CN 99123044 patent/CN1250082A/en active Pending
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100408659C (en) * | 2006-07-07 | 2008-08-06 | 白长军 | Method of making mixed oil using cotton seed puffing impregnation process |
| CN102174344A (en) * | 2011-03-17 | 2011-09-07 | 朱文鑫 | Pretreatment method suitable for extracting one-time oil pressed cake |
| CN102295985A (en) * | 2011-07-30 | 2011-12-28 | 河南工业大学 | Wet sesame residue expansion granulation drying leaching and oil extraction process |
| CN102676289A (en) * | 2012-06-04 | 2012-09-19 | 山东省农业科学院农产品研究所 | Method for low temperature cold pressing of peanut oil |
| CN102703206A (en) * | 2012-06-19 | 2012-10-03 | 东北农业大学 | Method for extracting fragrant sunflower seed oil |
| CN103614234A (en) * | 2013-12-12 | 2014-03-05 | 酉阳县康友粮油有限公司 | Rapeseed pre-pressing technology |
| CN105996102A (en) * | 2016-07-14 | 2016-10-12 | 天津市真如果食品工业有限公司 | Expanded food extruder |
| CN107043650A (en) * | 2017-06-01 | 2017-08-15 | 湖北恒贸茶油有限公司 | Seed device is steamed in the extruding for producing tea oil |
| CN112175712A (en) * | 2019-07-03 | 2021-01-05 | 上海谷励智能设备有限公司 | Ultrasonic wall-breaking screw device for vegetable oil |
| CN110343565A (en) * | 2019-08-21 | 2019-10-18 | 嘉里粮油（营口）有限公司 | A kind of expansion extraction oil technique, edible fat production technique and device |
| CN115678668A (en) * | 2022-10-24 | 2023-02-03 | 安徽华安食品有限公司 | Rapeseed oil leaching processing wet meal desolventizing device and implementation method |
| CN115678668B (en) * | 2022-10-24 | 2024-01-02 | 安徽华安食品有限公司 | Wet meal desolventizing device for rapeseed oil leaching processing and implementation method |
| CN116159843A (en) * | 2023-01-10 | 2023-05-26 | 江苏丰尚油脂工程技术有限公司 | Oil byproduct processing equipment and processing method |
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