CN1793305A - Tech., for producing protoecological peanut oil and cake dregs - Google Patents
Tech., for producing protoecological peanut oil and cake dregs Download PDFInfo
- Publication number
- CN1793305A CN1793305A CN 200510045043 CN200510045043A CN1793305A CN 1793305 A CN1793305 A CN 1793305A CN 200510045043 CN200510045043 CN 200510045043 CN 200510045043 A CN200510045043 A CN 200510045043A CN 1793305 A CN1793305 A CN 1793305A
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- CN
- China
- Prior art keywords
- arachidis hypogaeae
- semen arachidis
- oil
- cake
- press
- 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.)
- Granted
Links
- 235000019483 Peanut oil Nutrition 0.000 title claims abstract description 14
- 239000000312 peanut oil Substances 0.000 title claims abstract description 14
- 239000003921 oil Substances 0.000 claims abstract description 22
- 235000019198 oils Nutrition 0.000 claims abstract description 22
- 238000001914 filtration Methods 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000001035 drying Methods 0.000 claims abstract description 9
- 238000004519 manufacturing process Methods 0.000 claims abstract description 8
- 235000010777 Arachis hypogaea Nutrition 0.000 claims abstract description 6
- 238000004140 cleaning Methods 0.000 claims abstract description 4
- 238000001816 cooling Methods 0.000 claims abstract description 4
- 210000000582 semen Anatomy 0.000 claims description 36
- 238000000034 method Methods 0.000 claims description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 239000010779 crude oil Substances 0.000 claims description 6
- 235000017060 Arachis glabrata Nutrition 0.000 claims description 5
- 241001553178 Arachis glabrata Species 0.000 claims description 5
- 235000018262 Arachis monticola Nutrition 0.000 claims description 5
- 235000020232 peanut Nutrition 0.000 claims description 5
- 102000004169 proteins and genes Human genes 0.000 claims description 5
- 108090000623 proteins and genes Proteins 0.000 claims description 5
- 238000013467 fragmentation Methods 0.000 claims description 4
- 238000006062 fragmentation reaction Methods 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 4
- 239000004575 stone Substances 0.000 claims description 4
- 230000002745 absorbent Effects 0.000 claims description 3
- 239000002250 absorbent Substances 0.000 claims description 3
- 235000013305 food Nutrition 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 239000012535 impurity Substances 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 230000008859 change Effects 0.000 abstract description 4
- 238000003825 pressing Methods 0.000 abstract description 4
- 238000007599 discharging Methods 0.000 abstract 2
- 235000003276 Apios tuberosa Nutrition 0.000 abstract 1
- 235000010744 Arachis villosulicarpa Nutrition 0.000 abstract 1
- 244000133018 Panax trifolius Species 0.000 abstract 1
- 235000021049 nutrient content Nutrition 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 5
- 239000004519 grease Substances 0.000 description 5
- 235000016709 nutrition Nutrition 0.000 description 5
- 230000035764 nutrition Effects 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000003801 milling Methods 0.000 description 4
- 235000015112 vegetable and seed oil Nutrition 0.000 description 3
- 239000008158 vegetable oil Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 150000004671 saturated fatty acids Chemical class 0.000 description 2
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 2
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 2
- 102000004895 Lipoproteins Human genes 0.000 description 1
- 108090001030 Lipoproteins Proteins 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000003053 toxin Substances 0.000 description 1
- 231100000765 toxin Toxicity 0.000 description 1
Images
Landscapes
- Fats And Perfumes (AREA)
- Seeds, Soups, And Other Foods (AREA)
- Edible Oils And Fats (AREA)
Abstract
The invention relates to native ecology groundnut oil and its cake manufacturing method. It includes the following steps: cleaning and classifying groundnut kernel; low temperature drying; discharging temperature is not more than 80 centigrade degree; cooling; peeling red peel; manual carefully chosen; smashing to 3mm-6mm grain; modulator; adding 3%-12% hot water with 60-80 centigrade degree; twice cold pressing; the discharging temperature is not more than 60 centigrade degree; residual oil content is not more than 60%; and twice filtering. The invention realizes low temperature pressing to make nutrient content not change.
Description
Technical field
The present invention relates to a kind of vegetable oil material production technology, specifically a kind of ecosystem peanut oil and grouts production technique.
Background technology
The vegetable oil production method that we use at present has two big classes, and a class is a milling process, and another kind of is lixiviation process.Milling process divides two kinds of hot moulding and cold press again, and in hot moulding technology, raw material steams fries the operation drop temperature all greater than 100 ℃ (＜grease is produced and processing technology〉work of how conquering east, the 91st page); In cold pressing process, the general simple helix oil press zhai that uses, press bore temperature in the working process and reach more than 120 ℃ (＜peanut processing technology〉Zhou Ruibao work the 62nd page), because of milling process temperature height, unsaturated fatty acids in the grease of being produced becomes saturated fatty acid, and protein solidifies sex change in the grouts; Residual in the grease of lixiviation process production and the grouts have solvent, and temperature reaches more than 100 ℃ in the precipitation operation, and the variation in the above-mentioned milling process also takes place for grease and grouts.
Vegetable oil lipoprotein Yin Gaowen changes nutrition, and particularly unsaturated fatty acids becomes saturated fatty acid, has reduced its nutrition and health care effect; Grouts Yin Gaowen protein solidifies sex change, can not further be processed into food again, can only use as animal-feed or fertilizer.
Summary of the invention
The objective of the invention is, a kind of peanut oil and grouts low-temperature cold pressing production technique are provided, make the nutrition in grease and the grouts keep ecosystem, human body is had more the nutrition and health care effect.
For achieving the above object, the present invention has adopted following technical scheme:
1. clean: the Semen arachidis hypogaeae raw material is removed impurity such as iron, stone through selection by winnowing;
2. classification: the Semen arachidis hypogaeae classification after will cleaning with grading machine, so that the processing of back operation;
3. dry: the Semen arachidis hypogaeae after the classification is dried in batches 80 ℃～100 ℃ of hot blast temperatures, 60 ℃～80 ℃ of Semen arachidis hypogaeae drop temperatures, drying time 25 minutes～40 minutes with low-temperature drier;
4. cooling: the Semen arachidis hypogaeae after will drying is sent into water cooler and is cooled to room temperature;
5. take off scarlet: cooled Semen arachidis hypogaeae is sent into peeling machine slough scarlet, and carry out the benevolence skin and separate;
6. selected: as to sort out with Semen arachidis hypogaeae and variable color Semen arachidis hypogaeae that manually will not slough scarlet;
7. broken: as the Semen arachidis hypogaeae after selected to be sent into crusher, be crushed to the small-particle of 3mm～6mm;
8. modified: the Semen arachidis hypogaeae to fragmentation in quality controling machine adds water 3%～12%, 60 ℃～80 ℃ of water temperatures, and keep 30 minutes～40 minutes absorbent times;
9. a cold press: the Semen arachidis hypogaeae input duplex oil press zhai after modified, carry out the cold press first time, the cake temperature of oil press zhai outlet is not more than 60 ℃, and the oleaginousness of cake is 11%～20%, and cake is broken in the oil press zhai exit;
10. secondary cold press: once press cake and import another group duplex oil press zhai, carry out the cold press second time, oil press zhai outlet cake temperature is not more than 60 ℃, and cake Residual oil content is not more than 6%, and secondary presses cake can further be processed into food such as peanut protein powder;
11. once filter: crude oil of a cold press gained and secondary cold press gained secondary crude oil are carried out the filtration first time with plate filter;
12. secondary filtration: with bag type filtering machine peanut oil is carried out the second time and filter, peanut oil gets product.
The present invention compared with prior art has following advantage:
1. because of using twice squeezing of duplex oil press zhai, realized the low temperature oil expression, guaranteed that the nutrition in peanut oil and the peanut cake does not change.
2. Semen arachidis hypogaeae takes off behind the scarlet selectedly, can find and remove the Semen arachidis hypogaeae of rotten variable color fully, has guaranteed no flavacin toxin in peanut oil and the grouts.
Description of drawings
Fig. 1 is a process flow sheet of the present invention.
Embodiment
Now in conjunction with the embodiments, the invention will be further described.
1. weigh: 500 kilograms of Semen arachidis hypogaeae raw materials;
2. clean: go the stone cleaner to remove impurity such as iron in the Semen arachidis hypogaeae, stone with proportion;
3. classification: the Semen arachidis hypogaeae after will cleaning with the ZD-4 grading machine is divided into three grades;
4. dry: the Semen arachidis hypogaeae after the classification is dried in batches 80 ℃ of drying machine hot blast temperatures, drying time 30 minutes, 60 ℃ of Semen arachidis hypogaeae drop temperatures with the MR-5 low-temperature drier;
5. cooling: the Semen arachidis hypogaeae after will drying is sent into the FL-15 water cooler and is cooled to room temperature;
6. take off scarlet: cooled Semen arachidis hypogaeae is sent into the ZHD-12 peeling machine slough scarlet, and carry out the benevolence skin and separate;
7. selected: as to sort out with Semen arachidis hypogaeae and variable color Semen arachidis hypogaeae that manually will not slough scarlet;
8. broken: as the Semen arachidis hypogaeae after selected to be sent into the DG-2-10 crusher, be crushed to the small-particle of 3mm～6mm;
9. modified: the Semen arachidis hypogaeae to fragmentation in the YP-II quality controling machine adds 25 kilograms in water, 70 ℃ of water temperatures, and keep 30 minutes absorbent times;
10. a cold press: the Semen arachidis hypogaeae input SSYZ-12/12 duplex oil press zhai after modified, carry out the cold press first time, 60 ℃ of the cake temperature of oil press zhai outlet, the oleaginousness of cake is 12%, cake is broken in the oil press zhai exit;
11. secondary cold press: once press cake and import another group SSYZ-12/12 duplex oil press zhai, carry out the cold press second time, 60 ℃ of oil press zhai outlet cake temperature, cake Residual oil content 5.8%, secondary presses cake and sends into the peanut protein powder job shop;
12. once filter: crude oil of a cold press gained and secondary cold press gained secondary crude oil are carried out the filtration first time with the BAMS450-25 plate filter;
13. secondary filtration: with the CL-1 bag type filtering machine peanut oil is carried out the second time and filter, peanut oil gets product.
Claims (1)
1. ecosystem peanut oil and grouts production technique is characterized in that:
(1). clean: the Semen arachidis hypogaeae raw material is removed impurity such as iron, stone through selection by winnowing;
(2). classification: the Semen arachidis hypogaeae classification after will cleaning with grading machine, so that the processing of back operation;
(3). drying: the Semen arachidis hypogaeae after the classification is dried in batches 80 ℃～100 ℃ of hot blast temperatures, 60 ℃～80 ℃ of Semen arachidis hypogaeae drop temperatures, drying time 25 minutes～40 minutes with low-temperature drier;
(4). cooling: the Semen arachidis hypogaeae after will drying is sent into water cooler and is cooled to room temperature;
(5). take off scarlet: cooled Semen arachidis hypogaeae is sent into peeling machine slough scarlet, and carry out the benevolence skin and separate;
(6). selected: as to sort out with Semen arachidis hypogaeae and variable color Semen arachidis hypogaeae that manually will not slough scarlet;
(7). fragmentation: the Semen arachidis hypogaeae after selected is sent into crusher, be crushed to the small-particle of 3mm～6mm;
(8). modified: the Semen arachidis hypogaeae to fragmentation in quality controling machine adds water 3%～12%, 60 ℃～80 ℃ of water temperatures, and keep 30～40 minutes absorbent times;
(9). once cold press: the Semen arachidis hypogaeae input duplex oil press zhai after modified, carry out the cold press first time, the cake temperature of oil press zhai outlet is not more than 60 ℃, and the oleaginousness of cake is 11%～20%, and cake is broken in the oil press zhai exit;
(10). the secondary cold press: once press cake and import another group duplex oil press zhai, carry out the cold press second time, oil press zhai outlet cake temperature is not more than 60 ℃, and cake Residual oil content is not more than 6%, and secondary presses cake can further be processed into food such as peanut protein powder;
(11). once filter: crude oil of a cold press gained and secondary cold press gained secondary crude oil are carried out the filtration first time with plate filter;
(12). secondary filtration: with bag type filtering machine peanut oil is carried out the second time and filter, peanut oil gets product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100450432A CN1313581C (en) | 2005-11-07 | 2005-11-07 | Tech., for producing protoecological peanut oil and cake dregs |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100450432A CN1313581C (en) | 2005-11-07 | 2005-11-07 | Tech., for producing protoecological peanut oil and cake dregs |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1793305A true CN1793305A (en) | 2006-06-28 |
| CN1313581C CN1313581C (en) | 2007-05-02 |
Family
ID=36804955
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100450432A Expired - Fee Related CN1313581C (en) | 2005-11-07 | 2005-11-07 | Tech., for producing protoecological peanut oil and cake dregs |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1313581C (en) |
Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101601430A (en) * | 2009-07-10 | 2009-12-16 | 山东天申生物蛋白有限公司 | Low temperature physically pressed virgin peanut oil |
| CN101095435B (en) * | 2007-07-23 | 2010-06-02 | 山东省高唐蓝山集团总公司 | Process for preparing peanut oil and peanut protein powder synchronously |
| CN101880594A (en) * | 2010-06-06 | 2010-11-10 | 山东省花生研究所 | Preparation method of high oleic acid virgin peanut oil |
| CN101560437B (en) * | 2009-05-25 | 2012-01-25 | 辽宁晟麦实业股份有限公司 | Method for preparing walnut oil |
| CN102492540A (en) * | 2011-11-24 | 2012-06-13 | 北京龙浩安达新技术有限公司 | Oil pressing and flour milling methods of cyperus esculentus |
| CN102669751A (en) * | 2012-06-20 | 2012-09-19 | 泗水慧丰花生食品有限公司 | Production process for hulled peanut kernels |
| CN103275805A (en) * | 2013-05-10 | 2013-09-04 | 沙学 | Preparation method for refining peanut oil from peanuts |
| CN103289813A (en) * | 2013-05-10 | 2013-09-11 | 沙学 | Preparation method of peanut oil |
| CN103289815A (en) * | 2013-05-10 | 2013-09-11 | 沙学 | Preparation process of refining peanut oil |
| CN103320212A (en) * | 2013-06-28 | 2013-09-25 | 山东省农业科学院农产品研究所 | Preparation method of aromatic cold-pressed peanut oil |
| CN103320213A (en) * | 2013-06-28 | 2013-09-25 | 山东省农业科学院农产品研究所 | Preparation method of cold-pressed peanut oil |
| CN103468394A (en) * | 2013-09-10 | 2013-12-25 | 滁州金恒油脂工业有限公司定远县金恒油厂 | Preparation method of creamy health-care peanut oil |
| CN104232293A (en) * | 2014-09-28 | 2014-12-24 | 蒋艳玲 | Peanut oil production process |
| CN104543373A (en) * | 2015-01-20 | 2015-04-29 | 青岛天祥食品集团有限公司 | Method for synchronously extracting peanut oil and performing high-value utilization to cakes |
| CN104673481A (en) * | 2013-12-01 | 2015-06-03 | 山东乐悠悠花生油科技有限公司 | Process method for grading peanut kernels and pressing peanut oil |
| CN104745297A (en) * | 2015-04-15 | 2015-07-01 | 滕州市皇宫顶基食品有限公司 | Production process of pressing peanut oil |
| CN105132132A (en) * | 2015-08-27 | 2015-12-09 | 成都市新津迎先粮油有限公司 | Preparation method of peanut oil |
| CN105331440A (en) * | 2015-10-22 | 2016-02-17 | 孙高雷 | Squeezing method for peanut oil |
| CN108913342A (en) * | 2018-08-04 | 2018-11-30 | 望江县振兴植物油厂（普通合伙） | A kind of preparation method of flavor ready-mixed oil |
| CN110257159A (en) * | 2019-06-21 | 2019-09-20 | 正阳新地食品工业有限公司 | A kind of cold press peanut oil processing method and its equipment |
| CN110951536A (en) * | 2019-11-22 | 2020-04-03 | 华南理工大学 | Cream-flavor peanut oil and preparation method thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1279153C (en) * | 2004-08-23 | 2006-10-11 | 隋利华 | Process for extracting peanut oil and producing peanut protein and products thereof |
-
2005
- 2005-11-07 CN CNB2005100450432A patent/CN1313581C/en not_active Expired - Fee Related
Cited By (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101095435B (en) * | 2007-07-23 | 2010-06-02 | 山东省高唐蓝山集团总公司 | Process for preparing peanut oil and peanut protein powder synchronously |
| CN101560437B (en) * | 2009-05-25 | 2012-01-25 | 辽宁晟麦实业股份有限公司 | Method for preparing walnut oil |
| CN101601430A (en) * | 2009-07-10 | 2009-12-16 | 山东天申生物蛋白有限公司 | Low temperature physically pressed virgin peanut oil |
| CN101880594A (en) * | 2010-06-06 | 2010-11-10 | 山东省花生研究所 | Preparation method of high oleic acid virgin peanut oil |
| CN102492540A (en) * | 2011-11-24 | 2012-06-13 | 北京龙浩安达新技术有限公司 | Oil pressing and flour milling methods of cyperus esculentus |
| CN102669751A (en) * | 2012-06-20 | 2012-09-19 | 泗水慧丰花生食品有限公司 | Production process for hulled peanut kernels |
| CN102669751B (en) * | 2012-06-20 | 2013-08-14 | 泗水慧丰花生食品有限公司 | Production process for hulled peanut kernels |
| CN103275805A (en) * | 2013-05-10 | 2013-09-04 | 沙学 | Preparation method for refining peanut oil from peanuts |
| CN103289813A (en) * | 2013-05-10 | 2013-09-11 | 沙学 | Preparation method of peanut oil |
| CN103289815A (en) * | 2013-05-10 | 2013-09-11 | 沙学 | Preparation process of refining peanut oil |
| CN103320212A (en) * | 2013-06-28 | 2013-09-25 | 山东省农业科学院农产品研究所 | Preparation method of aromatic cold-pressed peanut oil |
| CN103320213A (en) * | 2013-06-28 | 2013-09-25 | 山东省农业科学院农产品研究所 | Preparation method of cold-pressed peanut oil |
| CN103468394A (en) * | 2013-09-10 | 2013-12-25 | 滁州金恒油脂工业有限公司定远县金恒油厂 | Preparation method of creamy health-care peanut oil |
| CN104673481A (en) * | 2013-12-01 | 2015-06-03 | 山东乐悠悠花生油科技有限公司 | Process method for grading peanut kernels and pressing peanut oil |
| CN104232293A (en) * | 2014-09-28 | 2014-12-24 | 蒋艳玲 | Peanut oil production process |
| CN104543373A (en) * | 2015-01-20 | 2015-04-29 | 青岛天祥食品集团有限公司 | Method for synchronously extracting peanut oil and performing high-value utilization to cakes |
| CN104745297A (en) * | 2015-04-15 | 2015-07-01 | 滕州市皇宫顶基食品有限公司 | Production process of pressing peanut oil |
| CN105132132A (en) * | 2015-08-27 | 2015-12-09 | 成都市新津迎先粮油有限公司 | Preparation method of peanut oil |
| CN105331440A (en) * | 2015-10-22 | 2016-02-17 | 孙高雷 | Squeezing method for peanut oil |
| CN108913342A (en) * | 2018-08-04 | 2018-11-30 | 望江县振兴植物油厂（普通合伙） | A kind of preparation method of flavor ready-mixed oil |
| CN110257159A (en) * | 2019-06-21 | 2019-09-20 | 正阳新地食品工业有限公司 | A kind of cold press peanut oil processing method and its equipment |
| CN110951536A (en) * | 2019-11-22 | 2020-04-03 | 华南理工大学 | Cream-flavor peanut oil and preparation method thereof |
| CN110951536B (en) * | 2019-11-22 | 2021-10-26 | 华南理工大学 | Cream-flavor peanut oil and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1313581C (en) | 2007-05-02 |
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