CN103271219A - Psophocarpus tetragonolobus protein powder processing technology - Google Patents
Psophocarpus tetragonolobus protein powder processing technology Download PDFInfo
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- CN103271219A CN103271219A CN2013100993734A CN201310099373A CN103271219A CN 103271219 A CN103271219 A CN 103271219A CN 2013100993734 A CN2013100993734 A CN 2013100993734A CN 201310099373 A CN201310099373 A CN 201310099373A CN 103271219 A CN103271219 A CN 103271219A
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Abstract
The invention discloses a Psophocarpus tetragonolobus protein powder processing technology. The technology comprises the following steps: breaking halves of Psophocarpus tetragonolobus seeds, peeling, grinding, adjusting the pH value of the obtained slurry by using sodium hydroxide, carrying out pressure filtration, adjusting the pH value of the obtained filtrate by using an acidic solution, stirring, allowing the obtained filtrate to stand, and centrifuging to obtain crude protein powder; mixing 60-100 parts by weight of the crude protein powder, 10-15 parts of honey, 10-20 parts of white granulated sugar and 5-10 parts of maltose, adding water, stirring, and carrying out vacuum degassing treatment; and carrying out spray drying. The addition of some ingredients to the obtained crude protein powder according to the nutrition demands of humans enriches the nutritional components of the protein powder of Psophocarpus tetragonolobus.
Description
Technical field:
The present invention relates to technical field of pharmaceuticals, specifically is a kind of processing technology of albumen powder of goa bean.
Background technology:
Goa bean, another name winged bean, four jiaos of beans, carambola beans belong to the pulse family Papillionoideae, and life in 1 year or perennial liana originate in the torrid zone.Goa bean is tied English on the ground, underground long potato (piece root), and complete stool is rich in proteins,vitamins,and minerals.According to surveying and determination, mature seed (beans) protein content is 32%-42%, and young pod protein content (with dry weight basis) is 15%, piece radixin matter content (with dry weight basis) is 25%, belongs to quality plant protein, pure natural, easily digesting and assimilating, is the high high-protein food of a kind of nutritive value; Fat content 15.0%～20.4%, unsaturated fatty acid content is abundant in the oil content, and unsaturated fatty acid content accounts for 70% of total oil content, obvious health-care efficacy; Carbohydrate content 28.0%～31.6%, and be rich in V.And Vo.Present many countries particularly African those lack the poor and backward country of protein resource, fall over each other it is developed as high protein grain new resources, are called as " green gold ".
Current urbanite is to the pursuit of nutrition, and various differently flavoured protein can satisfy the demand of different people, and have a large amount of consumption markets.Again because the protein content height of goa bean, and the process progress of domestic albumen powder processing for goa bean is slow, and the processing technology of the albumen powder of a kind of goa bean of the present invention can be optimized the exploitation of goa bean protein resource, enriches the albumen powder nutritional labeling of goa bean.
Summary of the invention:
The object of the invention is to overcome deficiency of the prior art, and the blank at existing goa bean Protein Extraction technology provides a kind of technology reasonable, simple to operate, the processing technology of the albumen powder of nutritious a kind of goa bean.
For solving the problems of the technologies described above, the present invention by the following technical solutions: a kind of processing technology of albumen powder of goa bean may further comprise the steps:
(1) preliminary treatment: the goa bean seed of maturation is cleaned, and is that broken lobe is removed the peel behind 0.1% soaking with sodium hydroxide, 6～7h of 8～9 with pH value;
(2) defibrination separates: will remove the peel goa bean and put into refining equipment, and add water, solid-liquid ratio is 1:5～1:15 (m:v), defibrination, with 0.1% NaOH slurries being transferred to the pH value is 9～11, at 25～35 ℃ of insulation 4h, by 200～300 purpose filter pressure filtrations, get filtrate;
(3) extract the crude protein powder: with 0.15% acid liquid filtrate being transferred to the pH value is 3.8～4.2, behind the stirring 10min, leaves standstill 30min, centrifugal, gets the crude protein powder;
(4) with 10～20 parts of 10～15 parts of 60～100 parts in crude protein powder, honey, white granulated sugars, 5～10 parts of the maltose of weight portion, mix, add water and stir, solid-liquid ratio is 1:3～1:5 (m:v), at 25～35 ℃ of insulation 4h, gets mixed liquor;
(5) be to carry out vacuum outgas under the 0.0907-0.0933MPa to handle with step (4) gained mixed liquor at 70-80 ℃, negative pressure of vacuum; Spray-drying gets final product again.
Advantage of the present invention is as follows:
1, the present invention has added some batchings according to people's nutritional need in obtaining the crude protein powder, has enriched the albumen powder nutritional labeling of goa bean.
2, this method is handled goa bean through decortication, avoids the loss of goa bean nutrient protein composition.
3, the present invention adopts vacuum outgas to handle, and has overcome the special beany flavor of goa bean in the traditional handicraft albumen powder manufacturing process.
The specific embodiment:
Below further specify essentiality content of the present invention with embodiments of the invention, but do not limit the present invention with this.
Embodiment 1
10kg is removed the peel goa bean put into refining equipment, add water, solid-liquid ratio is 1:10 (m:v), defibrination, and with 0.1% NaOH slurries being transferred to the pH value is 10, at 35 ℃ of insulation 4h, by 300 purpose filter pressure filtrations, gets filtrate; With 0.15% acid liquid filtrate being transferred to the pH value is 4.0, stir 10min after, leave standstill 30min, be that the centrifuge of 4000rpm is centrifugal with rotating speed, the time is 20min, gets the crude protein powder; 10 parts of 10 parts of 80 parts in crude protein powder, honey, white granulated sugars, 5 parts of maltose with weight portion, mix, add water and stir, solid-liquid ratio is 1:3 (m:v), at 35 ℃ of insulation 4h, get mixed liquor: be to carry out vacuum outgas under the 0.0933MPa to handle with the gained mixed liquor at 80 ℃, negative pressure of vacuum at last; Spray-drying gets final product again.
Embodiment 2
10kg is removed the peel goa bean put into refining equipment, add water, solid-liquid ratio is 1:10 (m:v), defibrination, and with 0.1% NaOH slurries being transferred to the pH value is 10, at 35 ℃ of insulation 4h, by 300 purpose filter pressure filtrations, gets filtrate; With 0.15% acid liquid filtrate being transferred to the pH value is 4.0, stir 10min after, leave standstill 30min, be that the centrifuge of 4000rpm is centrifugal with rotating speed, the time is 20min, gets the crude protein powder; 10 parts of 10 parts of 60 parts in crude protein powder, honey, white granulated sugars, 5 parts of maltose with weight portion, mix, add water and stir, solid-liquid ratio is 1:3 (m:v), at 35 ℃ of insulation 4h, get mixed liquor: be to carry out vacuum outgas under the 0.0933MPa to handle with the gained mixed liquor at 80 ℃, negative pressure of vacuum at last; Spray-drying gets final product again.
Embodiment 3
10kg is removed the peel goa bean put into refining equipment, add water, solid-liquid ratio is 1:10 (m:v), defibrination, and with 0.1% NaOH slurries being transferred to the pH value is 10, at 35 ℃ of insulation 4h, by 300 purpose filter pressure filtrations, gets filtrate; With 0.15% acid liquid filtrate being transferred to the pH value is 4.0, stir 10min after, leave standstill 30min, be that the centrifuge of 4000rpm is centrifugal with rotating speed, the time is 20min, gets the crude protein powder; 10 parts of 13 parts of 80 parts in crude protein powder, honey, white granulated sugars, 5 parts of maltose with weight portion, mix, add water and stir, solid-liquid ratio is 1:3 (m:v), at 35 ℃ of insulation 4h, get mixed liquor: be to carry out vacuum outgas under the 0.0933MPa to handle with the gained mixed liquor at 80 ℃, negative pressure of vacuum at last; Spray-drying gets final product again.
Embodiment 4
10kg is removed the peel goa bean put into refining equipment, add water, solid-liquid ratio is 1:10 (m:v), defibrination, and with 0.1% NaOH slurries being transferred to the pH value is 10, at 35 ℃ of insulation 4h, by 300 purpose filter pressure filtrations, gets filtrate; With 0.15% acid liquid filtrate being transferred to the pH value is 4.0, stir 10min after, leave standstill 30min, be that the centrifuge of 4000rpm is centrifugal with rotating speed, the time is 20min, gets the crude protein powder; 13 parts of 10 parts of 80 parts in crude protein powder, honey, white granulated sugars, 5 parts of maltose with weight portion, mix, add water and stir, solid-liquid ratio is 1:3 (m:v), at 35 ℃ of insulation 4h, get mixed liquor: be to carry out vacuum outgas under the 0.0933MPa to handle with the gained mixed liquor at 80 ℃, negative pressure of vacuum at last; Spray-drying gets final product again.
Embodiment 5
10kg is removed the peel goa bean put into refining equipment, add water, solid-liquid ratio is 1:10 (m:v), defibrination, and with 0.1% NaOH slurries being transferred to the pH value is 10, at 35 ℃ of insulation 4h, by 300 purpose filter pressure filtrations, gets filtrate; With 0.15% acid liquid filtrate being transferred to the pH value is 4.0, stir 10min after, leave standstill 30min, be that the centrifuge of 4000rpm is centrifugal with rotating speed, the time is 20min, gets the crude protein powder; 10 parts of 10 parts of 80 parts in crude protein powder, honey, white granulated sugars, 8 parts of maltose with weight portion, mix, add water and stir, solid-liquid ratio is 1:3 (m:v), at 35 ℃ of insulation 4h, get mixed liquor: be to carry out vacuum outgas under the 0.0933MPa to handle with the gained mixed liquor at 80 ℃, negative pressure of vacuum at last; Spray-drying gets final product again.
Claims (2)
1. the processing technology of the albumen powder of a goa bean is characterized in that, this method may further comprise the steps:
(1) preliminary treatment: the goa bean seed of maturation is cleaned, and is that broken lobe is removed the peel behind 0.1% soaking with sodium hydroxide, 6～7h of 8～9 with pH value;
(2) defibrination separates: will remove the peel goa bean and put into refining equipment, and add water, solid-liquid ratio is 1:5～1:15 (m:v), defibrination, with 0.1% NaOH slurries being transferred to the pH value is 9～11, at 25～35 ℃ of insulation 4h, by 200～300 purpose filter pressure filtrations, get filtrate;
(3) extract the crude protein powder: with 0.15% acid liquid filtrate being transferred to the pH value is 3.8～4.2, behind the stirring 10min, leaves standstill 30min, centrifugal, gets the crude protein powder;
(4) with 10～20 parts of 10～15 parts of 60～100 parts in crude protein powder, honey, white granulated sugars, 5～10 parts of the maltose of weight portion, mix, add water and stir, solid-liquid ratio is 1:3～1:5 (m:v), at 25～35 ℃ of insulation 4h, gets mixed liquor;
(5) be to carry out vacuum outgas under the 0.0907-0.0933MPa to handle with step (4) gained mixed liquor at 70-80 ℃, negative pressure of vacuum; Spray-drying gets final product again.
2. the processing technology of the albumen powder of a kind of goa bean according to claim 1 is characterized in that: centrifugal rotation speed is 4000rpm in the described step (4), and the time is 20min.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN2013100993734A CN103271219A (en) | 2013-03-26 | 2013-03-26 | Psophocarpus tetragonolobus protein powder processing technology |
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| CN2013100993734A CN103271219A (en) | 2013-03-26 | 2013-03-26 | Psophocarpus tetragonolobus protein powder processing technology |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20180028414A1 (en) * | 2016-07-27 | 2018-02-01 | Tokiwa Corporation | Method for producing solid powder cosmetic material and solid powder cosmetic material |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1981592A (en) * | 2005-12-16 | 2007-06-20 | 刘辉 | Functional snacks |
| CN100411543C (en) * | 2005-12-31 | 2008-08-20 | 北京康比特体育科技股份有限公司 | Protein rod |
| CN102406133A (en) * | 2011-11-29 | 2012-04-11 | 湖南农业大学 | Technology for producing winged bean protein peptide nutrient powder |
-
2013
- 2013-03-26 CN CN2013100993734A patent/CN103271219A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1981592A (en) * | 2005-12-16 | 2007-06-20 | 刘辉 | Functional snacks |
| CN100411543C (en) * | 2005-12-31 | 2008-08-20 | 北京康比特体育科技股份有限公司 | Protein rod |
| CN102406133A (en) * | 2011-11-29 | 2012-04-11 | 湖南农业大学 | Technology for producing winged bean protein peptide nutrient powder |
Non-Patent Citations (1)
| Title |
|---|
| 李白玉等: "四棱豆蛋白质提取工艺研究", 《食品与机械》 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20180028414A1 (en) * | 2016-07-27 | 2018-02-01 | Tokiwa Corporation | Method for producing solid powder cosmetic material and solid powder cosmetic material |
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Application publication date: 20130904 |