CN1908140A - Aromatic sunflower oil - Google Patents
Aromatic sunflower oil Download PDFInfo
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- CN1908140A CN1908140A CN 200610069812 CN200610069812A CN1908140A CN 1908140 A CN1908140 A CN 1908140A CN 200610069812 CN200610069812 CN 200610069812 CN 200610069812 A CN200610069812 A CN 200610069812A CN 1908140 A CN1908140 A CN 1908140A
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- sunflower seed
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Abstract
the invention discloses a super fine sunflower seed oil in the edible oil manufacturing technological domain, which comprises the following steps: toasting; dewatering; hulling; rolling the model; evaporating the model; cooking the model; squeezing through large-size squeezer; removing phosphine wax; reserving; packing.
Description
One, technical field
The invention discloses a kind of edible vegetable oil, particularly a kind of aromatic sunflower oil of producing with oil sunflower seed belongs to the edible vegetable oil production technical field.
Two, background technology
Along with improving constantly of people's living standard, to the requirement of edible oil also towards high-level, the direction of many kinds develops, not only require to look good, smell good and taste good, and pay attention to the nutritional quality of edible oil more, so daily edible peanut oil, soya-bean oil, the vegetable seed wet goods does not satisfy people's needs far away, and China western part, the oily certain herbaceous plants with big flowers of a large amount of plantations in the northwestward, its oleaginousness height, domestic with in, the sunflower seed oil processing of small-sized oily factory is to produce without refining, the crude oil that contains a large amount of impurity is main, along with external salad oil technical equipment is introduced domestic, it is that the solvent extraction sunflower seeds of main component obtains crude oil that manufacturer generally adopts normal hexane, add acid again, add alkali, high temperature deodorization refining makes sunflower seed oil, but because when leaching system oil, added solvent such as normal hexane, the big bucket solvent of 6# wet goods, make the fragrance of oil product that change take place, natural perfume (or spice) is for losing; When the sunflower crude oil is carried out refining, to wherein added acid, material is learned in alkalization, not only can produce residual, contaminated product, harmful to human is health, and caused the loss of vitamin-E; Moreover the high temperature high vacuum that adopts of refining time decolouring, deodorization also can cause the loss of biologically active substance such as vitamin-E and fragrance, significantly reduced the nutritive ingredient in the oil, reduces the nutritive value of sunflower seed oil.
Three, summary of the invention
Purpose of the present invention is intended to overcome the deficiency of above-mentioned prior art, the aromatic sunflower oil that disclose a kind of nutrient health, looks good, smell good and taste good.
For achieving the above object, the technical solution used in the present invention is: a kind of aromatic sunflower oil, its special character are that it is raw material with the oil sunflower seed and processes according to following processing step successively;
(1), the removal of impurities of removing sand: oil sunflower seed is put into vibratory screening apparatus remove wherein impurity, remove wherein sandstone to obtain purified oil sunflower seed with specific-gravity stoner again;
(2), drying and dewatering: purified oil sunflower seed is carried out drying and dewatering, make its water content at 6%-8%;
(3), shelling: the oil sunflower seed behind the drying and dewatering is sent in the centrifugal decorticator, cot with oil sunflower seed under action of centrifugal force rushes open, seed benevolence and cot are separated, cot after the separation is drawn the phoenix machine and is siphoned away, the seed benevolence that is mixed with band shell seed is carried out filtering separation by vibratory screening apparatus, the band shell seed that wherein contains separated and it is returned in the decorticator and peel off, so repeatedly, the shell-containing rate in seed benevolence reaches below 5%;
(4), roll embryo: above-mentioned seed benevolence is put into softening kettle directly sprays into steam and regulate moisture content to 6-10%, treat that seed benevolence fully absorbs moisture and runs through after, it is sent in the tight roller flaker of hydraulic pressure rolls embryo, rolling the flake thickness degree is 0.3mm;
(5), steam embryo, fry embryo: the above-mentioned embryo that rolls is sent into the upper strata of five layers of steamer of open steam and insulation and is steamed embryo, steaming the embryo temperature and be 98-103 ℃, moisture content is 10-16%, steaming the embryo time is 35-45 minute, flow into successively then in two, three, four, five layers of steamer and fry embryo, through frying the embryo temperature of coming out behind the embryo is that 105-110 ℃, moisture content are 5-8%, it is reentered in the frying pan on the oil press zhai and account for the stir-fry seed benevolence of rolling embryo weight 5-15% and continue to fry embryo to wherein adding, the embryo temperature after the stir-fry is that 126-138 ℃, moisture content are 1-2%;
(6), large-scale oil press zhai squeezing: above-mentioned stir-fry embryo sent into squeezing obtains crude oil in the large-scale squeezing machine, the slag-containing rate of crude oil is 5-10%;
(7), anhydrously take off phosphine, take off cured: with the gained crude oil after plate-and-frame filter press filters, enter be equipped with that adjustable rotating speed stirs and the Oil Tank of spiral coil cooling tube in, under the stirring of 40r/min, be cooled to 30 ℃ with water cooling, to wherein adding the cured crystal seed that takes off that accounts for crude oil weight 3-7% flocculating aids and account for crude oil weight 0.2-1.0%, the adjusting mixing speed is 8-12r/min, continue to feed cooling water temperature to 6-12 ℃ and kept 8-12 hour, filter through pressure filter then and obtain the work in-process sunflower seed oil;
(8), storage, packing: the work in-process sunflower seed oil is through being pumped into basin or directly pouring in the PET bottle, and under the pressure of normal temperature, 100Pa to wherein feeding nitrogen preservation, be the aromatic sunflower oil finished product.
The positively effect that compared with the prior art the present invention has is that this sunflower seed oil adds the seed benevolence flavouring through frying in the process of producing, adopt low temperature to take off phosphine, take off cured lasting, except that helping the filter Ji, do not add other any solvent, can not produce pollution and residual, its aromatic flavour, as clear as crystal, golden yellow color, nutritious, oily but not greasy, go into that pot does not foam, over-emitting black exhaust not, suitablely cook, fry in shallow oil, explode, fry, its nutritional quality is good, looking good, smell good and taste good, is the choosing of the ideal of edible vegetable oil.
Contain a large amount of unsaturated fatty acidss in the sunflower seed oil that the present invention produces, wherein linolic acid is 29.9-72%, oleic acid is 29.3-60.0%, stearic acid is 1.7-3.9%, palmitinic acid is 4.6-6.8%, and rich in vitamin E, folic acid, iron, potassium, the nutritive ingredient of multiple needed by human such as zinc, wherein the content of vitamin-E is all higher than other vegetables oil, particularly linoleic content and balanced proportion, be suitable for the absorption of human body utilization, specific absorption can be tall and big by 96.5%, be higher than other vegetables oil far away, prevention of arterial is hardened, hypertension, the effect that coronary heart disease oil is certain, long-term edible, very useful to HUMAN HEALTH.
Four, embodiment
For understanding the present invention better, it is done further detailed elaboration below in conjunction with specific embodiment.
Aromatic sunflower oil of the present invention is that to plant in the oil sunflower seed of the oily certain herbaceous plants with big flowers of China western part, the northwestward be that raw material processes by a large amount of, at first oil sunflower seed is put into vibratory screening apparatus and removed wherein impurity, remove wherein sandstone to obtain clean pure oil sunflower seed with specific-gravity stoner again; Then the oil sunflower seed that obtains is carried out drying and dewatering, make its water content at 6%-8%; Again it is sent in the centrifugal decorticator and shell, cot with oil sunflower seed under action of centrifugal force rushes open, seed benevolence and cot are separated, cot after the separation is drawn the phoenix machine and is siphoned away, the seed benevolence that is mixed with band shell seed is carried out filtering separation by vibratory screening apparatus, the band shell seed that wherein contains separated and it is returned in the decorticator and peel off, so repeatedly, the shell-containing rate in seed benevolence reaches below 5%; Seed benevolence after the shelling is put into softening kettle directly spray into steam adjusting moisture content to 6-10%, after treating that seed benevolence fully absorbs moisture and runs through, it is sent in the tight roller flaker of hydraulic pressure roll embryo, rolling the flake thickness degree is 0.3mm, the embryo that rolls that obtains is sent into the upper strata of five layers of steamer of open steam and insulation and steamed embryo, steaming the embryo temperature is 98-103 ℃, moisture content is 10-16%, steaming the embryo time is 35-45 minute, flow into two of steamer then successively, three, four, fry embryo in five layers, be 105-110 ℃ through frying the embryo temperature of coming out behind the embryo, moisture content is 5-8%, to roll embryo again and send in the frying pan on the oil press zhai and to the seed benevolence flavouring that wherein adds after accounting for the frying of rolling embryo weight 5-15% and continue to fry embryo, the embryo temperature after the stir-fry is 126-138 ℃, moisture content is 1-2%; To roll embryo then sends in the large-scale squeezing machine squeezing and obtains the crude oil that slag-containing rate is 5-10%; Crude oil after filtering, plate-and-frame filter press is entered in the Oil Tank that adjustable rotating speed stirring and spiral coil cooling tube are housed, under the stirring of 40r/min, be cooled to 30 ℃ with water cooling, cured to wherein adding the perlite account for crude oil weight 3-7% and accounting for the plant that crude oil weight 0.2-1.0% deviate from, the adjusting mixing speed is 8-12r/min, continue to feed cooling water temperature to 6-12 ℃, stirred 8-12 hour, and obtained the work in-process sunflower seed oil after in pressure filter, filtering; At last with the work in-process sunflower seed oil through being pumped into basin or directly pouring in the PET bottle, and under the pressure of normal temperature, 100Pa to wherein feeding nitrogen, be the aromatic sunflower oil finished product; Its golden yellow color, gas perfume (or spice) is pleasant, and flavour is good to eat, and is nutritious; It is oxidized rotten in order to prevent oil product charging into nitrogen, keeps the freshness and the nutritive ingredient of oil product.
The aromatic sunflower oil that the foregoing description the makes content of wherein main unsaturated fatty acids after testing is respectively: oleic acid 24.29%, linolic acid 63.7.%, stearic acid 4.59%, palmitinic acid 5.49%, and contain vitamin-E and the mineral substance that enriches needed by human, its AOM value (needed time when the greasy peroxide value of per 1000 grams reaches 100 milligramequivalents under the mal-condition of setting) is 11 hours, be 2 times of the sunflower seed oil produced of common process, has stronger resistance of oxidation, be of high nutritive value, helping HUMAN HEALTH, is a kind of edible vegetable oil of health-nutrition.
Claims (1)
1, a kind of aromatic sunflower oil is characterized in that: it is raw material with the oil sunflower seed and processes by following processing step successively;
(1), the removal of impurities of removing sand: oil sunflower seed is put into vibratory screening apparatus remove wherein impurity, remove wherein sandstone to obtain purified oil sunflower seed with specific-gravity stoner again;
(2), drying and dewatering: purified oil sunflower seed is carried out drying and dewatering, make its water content at 6%-8%;
(3), shelling: the oil sunflower seed behind the drying and dewatering is sent in the centrifugal decorticator, cot with oil sunflower seed under action of centrifugal force rushes open, seed benevolence and cot are separated, cot after the separation is drawn the phoenix machine and is siphoned away, the seed benevolence that is mixed with band shell seed is carried out filtering separation by vibratory screening apparatus, the band shell seed that wherein contains separated and it is returned in the decorticator and peel off, so repeatedly, the shell-containing rate in seed benevolence reaches below 5%;
(4), roll embryo: above-mentioned seed benevolence is sent into sprayed into steam in the softening kettle and regulate moisture content to 6-10%, treat that seed benevolence fully absorbs moisture and runs through after, it is sent in the tight roller flaker of hydraulic pressure rolls embryo, rolling the flake thickness degree is 0.3mm;
(5), steam embryo, fry embryo: will roll embryo and send into the upper strata of five layers of steamer of open steam and insulation and steam embryo, steaming the embryo temperature and be 98-103 ℃, moisture content is 10-16%, steaming the embryo time is 35-45 minute, flow into successively then in two, three, four, five layers of steamer and fry embryo, through frying the embryo temperature of coming out behind the embryo is that 105-110 ℃, moisture content are 5-8%, it is reentered in the frying pan on the oil press zhai and to wherein add account for the frying of rolling embryo weight 5-15% after seed benevolence continue to fry embryo, the embryo temperature after the stir-fry is that 126-138 ℃, moisture content are 1-2%;
(6), large-scale oil press zhai squeezing: above-mentioned stir-fry embryo sent into squeezing obtains crude oil in the large-scale squeezing machine, the slag-containing rate of crude oil is 5-10%;
(7), anhydrously take off phosphine, take off cured: with the gained crude oil after plate-and-frame filter press filters, enter be equipped with that adjustable rotating speed stirs and the Oil Tank of spiral coil cooling tube in, under the stirring of 40r/min, be cooled to 30 ℃ with water cooling, take off cured crystal seed to wherein adding the flocculating aids that accounts for crude oil weight 3-7% and accounting for crude oil weight 0.2-1.0%, the adjusting mixing speed is 8-12r/min, continue to feed cooling water temperature to 6-12 ℃ and kept 8-12 hour, filter through pressure filter then and obtain the work in-process sunflower seed oil;
(8), storage, packing: the work in-process sunflower seed oil is through being pumped into basin or directly pouring in the PET bottle, and under the pressure of normal temperature, 100Pa to wherein feeding nitrogen preservation, be the aromatic sunflower oil finished product.
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CNB2006100698127A CN100535093C (en) | 2006-08-04 | 2006-08-04 | Aromatic sunflower oil |
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Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101880591A (en) * | 2010-06-13 | 2010-11-10 | 中山大学 | Application of housefly maggots as oil material insects |
CN102002432A (en) * | 2010-11-29 | 2011-04-06 | 新疆泰昆集团股份有限公司 | Deep processing method of oil sunflower seeds |
CN102899159A (en) * | 2012-09-29 | 2013-01-30 | 奇台县博峰伟业有限责任公司 | Pure physical squeezing technology for sunflower seed oil |
CN103181418A (en) * | 2011-12-30 | 2013-07-03 | 丰益(上海)生物技术研发中心有限公司 | Method for mixedly squeezing edible oil |
CN104782795A (en) * | 2015-05-11 | 2015-07-22 | 查孝柱 | Organic sunflower seed oil and production process thereof |
CN104946377A (en) * | 2015-05-30 | 2015-09-30 | 益海(昌吉)粮油工业有限公司 | Squeezing method of strong aroma sunflower seed oil |
CN105132130A (en) * | 2015-08-20 | 2015-12-09 | 成都市新津迎先粮油有限公司 | Seed stir-frying method for rapeseed oil |
CN105265603A (en) * | 2014-07-11 | 2016-01-27 | 马井芳 | Edible oil and preparation method thereof |
CN105542945A (en) * | 2015-12-17 | 2016-05-04 | 安徽嘉旗粮油工程技术有限公司 | Rich-aroma sunflower seed oil production method |
CN105707288A (en) * | 2016-02-03 | 2016-06-29 | 桐城市放牛娃家庭农场有限公司 | Refining method for sunflower seed oil capable of nourishing spleen and stomach |
CN105838497A (en) * | 2016-04-13 | 2016-08-10 | 许昌维尔康植物油有限公司 | Method for preparing hot-molding pressed vegetable oil |
CN106635398A (en) * | 2017-02-20 | 2017-05-10 | 宁夏吴忠市苏酥清真粮油工贸有限公司 | Pressing processing technology of sunflower seed oil |
CN110218608A (en) * | 2019-07-01 | 2019-09-10 | 佳格投资(中国)有限公司 | A kind of pretreating process obtaining the good squeezing sunflower oil of safety, nutrition, organoleptic quality |
-
2006
- 2006-08-04 CN CNB2006100698127A patent/CN100535093C/en active Active
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101880591A (en) * | 2010-06-13 | 2010-11-10 | 中山大学 | Application of housefly maggots as oil material insects |
CN102002432A (en) * | 2010-11-29 | 2011-04-06 | 新疆泰昆集团股份有限公司 | Deep processing method of oil sunflower seeds |
CN102002432B (en) * | 2010-11-29 | 2013-02-27 | 新疆泰昆集团股份有限公司 | Deep processing method of oil sunflower seeds |
CN103181418A (en) * | 2011-12-30 | 2013-07-03 | 丰益(上海)生物技术研发中心有限公司 | Method for mixedly squeezing edible oil |
CN103181418B (en) * | 2011-12-30 | 2015-06-17 | 丰益(上海)生物技术研发中心有限公司 | Method for mixedly squeezing edible oil |
CN102899159A (en) * | 2012-09-29 | 2013-01-30 | 奇台县博峰伟业有限责任公司 | Pure physical squeezing technology for sunflower seed oil |
CN105265603A (en) * | 2014-07-11 | 2016-01-27 | 马井芳 | Edible oil and preparation method thereof |
CN104782795A (en) * | 2015-05-11 | 2015-07-22 | 查孝柱 | Organic sunflower seed oil and production process thereof |
CN104946377A (en) * | 2015-05-30 | 2015-09-30 | 益海(昌吉)粮油工业有限公司 | Squeezing method of strong aroma sunflower seed oil |
CN105132130A (en) * | 2015-08-20 | 2015-12-09 | 成都市新津迎先粮油有限公司 | Seed stir-frying method for rapeseed oil |
CN105542945A (en) * | 2015-12-17 | 2016-05-04 | 安徽嘉旗粮油工程技术有限公司 | Rich-aroma sunflower seed oil production method |
CN105707288A (en) * | 2016-02-03 | 2016-06-29 | 桐城市放牛娃家庭农场有限公司 | Refining method for sunflower seed oil capable of nourishing spleen and stomach |
CN105838497A (en) * | 2016-04-13 | 2016-08-10 | 许昌维尔康植物油有限公司 | Method for preparing hot-molding pressed vegetable oil |
CN106635398A (en) * | 2017-02-20 | 2017-05-10 | 宁夏吴忠市苏酥清真粮油工贸有限公司 | Pressing processing technology of sunflower seed oil |
CN110218608A (en) * | 2019-07-01 | 2019-09-10 | 佳格投资(中国)有限公司 | A kind of pretreating process obtaining the good squeezing sunflower oil of safety, nutrition, organoleptic quality |
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