CN1436478A - Production process and apparatus for granular composite plant protein crystal - Google Patents
Production process and apparatus for granular composite plant protein crystal Download PDFInfo
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- CN1436478A CN1436478A CN 02139881 CN02139881A CN1436478A CN 1436478 A CN1436478 A CN 1436478A CN 02139881 CN02139881 CN 02139881 CN 02139881 A CN02139881 A CN 02139881A CN 1436478 A CN1436478 A CN 1436478A
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Abstract
The present invention is production process and apparatus for granular composite plant protein crystal. Grain and bean materials are produced into the granular composite plant protein crystal through the process of lixiviation, synchronous extraction with gel liquid, isoelectric acid precipitation to obtain concentrated protein milk, nitrogen foaming, spraying to pellelize and centrifugal spray drying. The production apparatus includes adjustable continuous foam generator and connected spray pelletizing and drying tower. The present invention has the advantages of no acid and alkali used, no heavy metal contamination, reasonable utilization of protein resource, amino acid complementation resulting in high nutrient value, etc. The said technology of the present invention may be used also in producing various tea, Chinese medicine, fruit and vegetable products.
Description
Technical field:
The present invention relates to the extracting method and the device of food processing field vegetable protein, particularly brilliant manufacture method of graininess compound plant protein and device thereof.
Background technology:
In food industry, the rational exploitation and utilization of raw material resources, improve the nutritive value of vegetable protein and the extraction of vegetable protein and the technology of preparing of pellets of vegetable protein is the important topic that receives much concern always.
Existing technology status is: be the food-processing industry of raw material with cereal, beans such as rice, broad bean, mung bean, peas at present, as the enterprise that makes monosodium glutamate, maltose, bean vermicelli, the processing method that adopts is still mostly uses earlier starch, again from processing " byproduct ", extract albumen for example poor, rice slag and the powder process tail water from sugar, traditional handicraft mainly as animal and fowl fodder, rather than " synchronously " directly extracts starch, these two kinds of important nutrient of protein, cause originally to can be used as edible protein resource and fail rationally to be utilized, this is a big defective.Secondly, processing is extracted vegetable protein and is adopted used chemical industry soda acid in " alkali is carried, acid sink " technology, even food industry allows use, but because of it can not natural degradation, tool contains a certain amount of heavy metal---lead etc., in machining process, also the heavy metal accumulation of lead and so on might be brought in the finished product, cause the product heavy metals exceeding standard and pollute.
Summary of the invention:
The objective of the invention is to overcome the prior art defective, a kind of directly " synchronously " extraction, separating starch and vegetable protein from cereal, bean material are provided, and avoid using the heavy metal accumulation that chemistry is sour, alkali may bring and polluting, study, developed the method and the device thereof that carry out limiting amino acid complementation, its nutritive value of composite raising and manufacturing graininess compound plant protein crystalline substance with 2-4 kind plant albumen.
Technical solution of the present invention is brilliant manufacture method of a kind of graininess compound plant protein and device thereof.
The manufacture method of graininess compound plant protein crystalline substance is a kind of with various types of grain, the albumin milk of bean material after the immersion of basic ion type leaching liquor, defibrination, slagging-off, adverse current " synchronously " are extracted separating starch, " wait electricity, flocculation, sedimentation " through acid ion type coagulation liquid again, high speed centrifugation separates the dense breast of vegetable protein that obtains, transfer pH value, through sterilization, homogeneous, fill nitrogen foaming, form the dense newborn expanding foam solution of albumen, through the granulation of foam centrifugal spray drying, composite making do not contain cholesterol, the brilliant particle of quickly dissolving compound plant protein.The characteristics of its method are:
(1) directly make raw material with cereal, beans, adopt alkali to put forward technology, " synchronously " extracts starch and vegetable protein.
(2) alkali is carried the alkali extracting solution in the technology, but adopts the little molecule basic ion of the pure natural type leaching liquor of natural degradation.
(3) the dense newborn expanding foam solution of albumen is the vegetable protein milk that extracts from cereal, bean material " synchronously ", the dense breast of albumen that obtains with the acid ion type coagulation liquid " isoelectric precipitation " of being furnished with minute quantity food acids and flocculant fills with nitrogen gas foaming, makes it to become the dense newborn expanding foam solution of vegetable protein.
(4) adopt reverse counterflow to the spray prilling, this technology be the dense newborn expanding foam solution of cereal, bean albumen respectively from the dry following current of the top centrifugal atomizing of foam centrifugal spray drying granulation tower downwards and with double flowing nozzle from the below upwards two rightabouts carry out adverse current to the spray granulation.
The manufacturing installation of graininess compound plant protein crystalline substance is a foam centrifugal spray drying prilling granulator, and it is mainly connected with foam centrifugal spray drying granulation tower by adjustable continuous foam generator and constitutes, and it is characterized in that:
(1) foam maker is that adjustable foam recurs device, and it comprises the profile of tooth rotating disk foaming machine of the adjustable gaps between the adjustable mixed jet of gas-liquid flow and rotating speed and rotating disk and stator.
(2) spray drying tower comprises an air dewetting drying, hot-air system that the clean temperature of handling is adjustable and adverse current to spray granulating and drying and the dry again structure of low temperature fluid bed, it is by the foam centrifugal atomizer and the hot blast radome fairing of cat head, with the gas-liquid double flowing nozzle formation of tower bottom.
(3) the dual antiseized protection structure of spray-drying inner wall of tower, it is made of inner wall of tower antiadhesion barrier and generation ring inner wall of tower vertical current clean dried secondary low temperature hot blast kuppe.
Description of drawings:
The brilliant manufacturing installation structural representation of Fig. 1 graininess compound plant protein.
The specific embodiment:
Structure specific embodiment of the present invention further specifies as follows referring to accompanying drawing: the brilliant manufacture method of graininess compound plant protein of the present invention is with cereal, raw materials such as beans, defibrination after basic ion type leaching liquor soaks, slagging-off is with after starch " synchronously " separates, albumin milk flocculates through acid ion type coagulation liquid again, sedimentation, high speed centrifugation separates the dense breast of acquisition vegetable protein, transfer pH value to neutral, through sterilization, homogeneous fills the nitrogen foaming and forms the dense newborn expanding foam solution of albumen, spray-dried then and fluidisation is drying-granulating again, the last composite brilliant particle of quickly dissolving compound plant protein of making, its method is:
(1) directly make raw material with cereal, beans, adopt alkali to put forward technology, " synchronously " extracts starch and vegetable protein.
(2) but alkali is carried the little molecule basic ion of the pure natural type leaching liquor that alkali extract in the technology adopts natural degradation.
(3) the dense newborn expanding foam solution of albumen is the vegetable protein milk that extracts with cereal, bean material " synchronously ", with the dense breast of albumen that the acid ion type coagulation liquid " isoelectric precipitation " of being furnished with a small amount of food acids and flocculant obtains, fill again with nitrogen gas foaming and make it to become the dense newborn expanding foam solution of vegetable protein.
(4) adopt reverse counterflow to the spray prilling, promptly the dense newborn expanding foam solution of vegetable protein respectively from the top centrifugal atomizing of foam centrifugal spray drying granulation tower dry and with double flowing nozzle from the below upwards two rightabouts carry out adverse current to the spray granulation.
The concrete enforcement of the present invention is to select for use rice and beans as the raw material of making graininess compound plant protein crystalline substance.
Calculate through with AAS differential technique (AASD) essential amino acid between various plants albumen being carried out complementation, select the compound prescription of five groups of paddy, beans or oilseed plant albumen, the proportioning of formula material is:
(1) long-grained nonglutinous rice albumen: soybean protein=1: 1.5
(2) long-grained nonglutinous rice albumen: pea protein=1: 1.2
(3) long-grained nonglutinous rice albumen: mung bean protein=1: 0.73
(4) long-grained nonglutinous rice albumen: broad bean albumen: soybean protein=1: 1.1: 0.8
(5) long-grained nonglutinous rice albumen: broad bean albumen: soybean protein=1: 0.7: 0.5: 0.4.
Protein after above-mentioned prescription is compound, its limiting amino acid content, ratio are all recommended pattern near WHO/FAO, are the higher complete proteins of nutritive value.According to raw material variety, price and cost, can from above five groups prescription, select 1～2 group again and do preferred compound plant protein prescription use.
Be the unified calculation data, this prescription is system's " composition table of foods " listed essential amino acid data computation of writing according to Chinese Academy Of Preventive Medicine Research Institute Of Nutrition And Food Hygiene and getting all, in fact vegetable protein is because raw material variety, the place of production difference of selecting for use, its crude protein content and essential amino acids content also are not quite similar, the extract that in addition extracts albumen and extraction, separating technology are different, and eight kinds of contents of essential amino acids in the gained vegetable protein, ratio also have discrepancy.Therefore, in suitability for industrialized production, should add the vegetable protein that technology makes and detect the measured data that obtains by of the present invention with the raw material in the selected place of production, the prescription that preferably obtains by recipe calculation method of the present invention be as the criterion.
The inventive method adopts " it is heavy that alkali is proposed acid " but technology is produced the little molecule basic ion of All Pure Nature type leaching liquor and the acid ion type coagulation liquid that the employed soda acid of vegetable protein is natural degradation, and without chemical industry acid, alkali, to avoid bringing the heavy metal pollution problem in the finished product.What use is to be base-material with basic ion water and acid ion water, the acid ion type coagulation liquid that is mixed with basic ion type leaching liquor and prepares with the food acids and the edible flocculant of minute quantity.By infiltration, dissolution is strong, the little molecule basic ion of All Pure Nature type leaching liquor that can natural degradation is to cereal, beans continuous dipping, counter-flow extraction and " synchronously, extract and separate " protein and starch, and this is a kind of novel technique different with prior art safety.
The starch slurry that separates is sent into powder process, making maltose and monosodium glutamate brewing room, still can use the existing processes technical equipment, is processed into bean vermicelli or makes the rice maltose or make the rice starch syrup; The albumin milk that separates, transfer pH value to isoelectric points of proteins flocculation, sedimentation with acid ion type coagulation liquid again, high speed centrifugation is isolated the dense breast of albumen, the dense breast of albumen transfers pH value to neutral, after heat sterilization homogeneous, the foaming, use centrifugal atomizer, high pressure nozzle or double flowing nozzle carry out spray-drying, make the vegetable protein powder, formula material as the instant compound plant protein crystalline substance of graininess, also can be re-dubbed the compound plant protein nutrition fortifier, in food industry series compound plant protein nourishing reinforced food, use.
The manufacturing installation of graininess compound plant protein crystalline substance of the present invention is a foam centrifugal spray drying prilling granulator.
It mainly connects foam centrifugal spray drying granulation tower B by adjustable continuous foam generator A through connecting pipe [4] and constitutes, referring to accompanying drawing 1, foam maker A is an adjustable continuous foam generator, it comprises the profile of tooth rotating disk foaming machine [3] of the adjustable gaps joint between the adjustable mixed jet [2] of gas-liquid flow and rotating speed and rotating disk and stator, foaming machine [3] connects a control flow [1], regulates gas-liquid flow and the rotating speed of foaming machine [3] and the gap between profile of tooth rotating disk and stator by control flow [1].Adjustable continuous foam generator A one side has liquor inlet [21] and nitrogen inlet [22], and opposite side has expanding foam solution outlet [20], charges into nitrogen by the dense feed liquid of vegetable protein through foam maker and forms the albumen dope and fill the nitrogen expanding foam solution.
Foam centrifugal spray drying granulation tower B is by connecting cylindrical cavity [12] in the barrel-shaped body of the tower of circular cone [14] with one heart, inner chamber [12] top connects the hot blast radome fairing, the hot blast radome fairing comprises a hot blast radome fairing [9] and secondary hot-air kuppe [5], hot blast radome fairing one side once dry-heat air inlet [10] input through hot blast of clean dried of dehumidification treatments, opposite side has clean dried low temperature secondary hot-air inlet [6], inlet is sent into the clean dried secondary hot-air through dehumidification treatments thus, cat head hot blast radome fairing center is connected with centrifugal atomizer [7] by the connection seat [8] of conical connection holes, or connects composition exchange draw bail fast with high pressure nozzle or double flowing nozzle.Centrifugal atomizer [7] connects with the expanding foam solution outlet [20] of foam maker A via connecting pipe [4].
Between body of the tower [14] and the inner chamber [12] cloth bag filter chamber [13] is arranged, filter cloth bag by several and form cloth bag filter chamber [13], on the annular top surface of body of the tower [14] and inner chamber [12] connection place exhaust outlet [19] is arranged, on the central axis at the circular cone tube middle part that body of the tower [14] is following section double flowing nozzle [17] is installed, body of the tower [14] lower end cone ports one side has dry-heat air inlet [15], send into clean removal moisture drying hot blast thus, opposite side has particle outlet [16].Double flowing nozzle [17] connects with the expanding foam solution outlet [20] of foam maker through connecting pipe, or the inlet L of double flowing nozzle
1Connect the air inlet L of double flowing nozzle with the liquor inlet [22] or the binder liquid stream of foam maker
2Connect with the dried compressed air of the oil removing that dewaters.
In sum, foam centrifugal spray drying granulation tower B contains following special construction:
A. adverse current is to spray granulation and the dry again structure of fluid bed, it is made up of foam centrifugal atomizer [7] and hot blast radome fairing [9], secondary wind kuppe [5] and the tower bottom gas-liquid double flowing nozzle of cat head, it forms upper and lower and to adverse current the foam droplet of spray and the clean dried hot blast of reverse convection current is contacted, make the foam droplet rapidly bonded pelleting form distinctive spherical hollow micro capsule particle, and fully dry.
B. the dual antiseized protection structure of spray-drying inner wall of tower; it is made up of inner wall of tower [12] antiadhesion barrier [18] and the vertical current clean dried secondary low temperature hot blast kuppe that produces ring Ta Bi chamber; the vertical current hot blast of ring tower wall inner chamber is that hot blast radome fairing [9], [5] by cat head produce, it can prevent foam material liquid and not the micro-capsule adhesion of bone dry assemble on inner wall of tower [12].Dual antiseized structure prevents that effectively foam material liquid and micro-capsule from upward boning at inwall [12].
C. cat head guarantees that by the interchangeable draw bail of connection seat [8] formation of taper connection holes cat head can connect with centrifugal atomizer [7] or with high pressure nozzle or with the double flowing nozzle exchange flexibly and easily through the connection seat [8] of taper connection holes.Form the high-pressure spray-drying tower respectively, or double-current spray dryer.The feed liquid spray-drying that can be suitable for different rerum naturas like this is assembled into the multifunctional spray drying tower of can a tower using more.
The advantage of this device is to connect flexibly and easily.Thereby centrifugal atomizer or high pressure nozzle or double flowing nozzle obtain multiple function, can prevent effectively that foam material liquid from boning on the spray-drying inner wall of tower, can eliminate race powder phenomenon simultaneously by the fully dry atomizing microcapsule granule that foams, obtain the dried particles of distinctive spherical hollow micro capsule.
Foam centrifugal spray drying prilling granulator is a kind of multi-functional equipment, can be with adjustable continuous foam generator foaming the become foaming protein liquid of the dense breast of compound plant protein by inflated with nitrogen, send into centrifugal atomizer and double flowing nozzle, with up and down to the spray the mode mist projection granulating, the inflated with nitrogen albumen hollow micro capsule of the foam droplet of last spray after with the hot-air preliminarily dried is further adhered to one another, is gathered into the compound plant protein crystal grain of larger particles.Also the albumen after high-pressure homogeneous can be adopted high-pressure fog, centrifugal atomizing or double-current mode of spraying by dense breast, in the vertical thermal air-flow, directly make droplet be dried to the compound plant protein powder.
But the key problem in technology of this multifunctional foam centrifugal spray drying prilling granulator is supporting continuous foam generator and tower wall clean dried low temperature secondary wind and the antiadhesion barrier dado structure of handling through air dewetting that inflated with nitrogen, gas-liquid mixed adjustable nozzle are arranged, to reduce and to prevent that feed liquid and powder from gluing wall; The hot blast radome fairing that cat head is installed can make hot blast vertically send in the tower, reduces the generation of turbulent flow and eddy current, makes globular protein hollow foam droplet be dried to the albumen hollow micro capsule rapidly; The dense newborn expanding foam solution of albumen of the double-current method nozzle of spraying ejection or edible gluing are made agent solution from bottom to top, make the further adhesion and aggregation drying of hollow micro capsule become the compound plant protein crystalline substance of big crystal grain, and its largest particles particle diameter can reach about 500 microns sometimes.The compound plant protein particle of this gathering granulating by the capillary suction-operated, is easy to dissolving in water.
This device is designed to the pattern that the cat head atomizer can exchange, the high pressure nozzle that it is identical with centrifugal atomizer taper cover for seat or the taper cover for seat of double flowing nozzle can very make things convenient for and change the outfit efficiently in the centrifugal type atomizer taper cover for seat of cat head, repack high pressure or double-current spraying system into, the multifunctional spray drying tower that this equipment is really become have multiple pattern spray-drying function.Not needing also to can be used for the Chinese herbal medicine of the spray-drying of instant powder grain material or different rerum naturas to extract the spray drying granulation of concentrate or plant, fruits and vegetables inspissated juice.
This device has designed and the direct continuous cloth bag filter chamber of tower wall outer tube wall, its maximum characteristics are to utilize the heat conducting heat of tower wall, heating and insulation cloth bag filter chamber, making cloth bag filtration indoor temperature remain at air draft contains more than the dew-point temperature of humid air, prevent to contain moisture dewfall on cloth bag filter chamber inwall and filtration cloth bag of humid air, the micro mist that air draft is carried can not met wet bonding and be caused air draft not smooth in cloth bag, influence spray drying tower and advance, the normal operation of exhaust system.Can come off voluntarily after micro mist gathering in the filtration cloth bag reaches certain thickness, or shake off to get back in the tower, continue to participate in granulation and circulate with shaking device.After particle diameter reaches requirement, then cut down discharge, pack after cooling, the screening by side sealing discharging at the bottom of the tower.
The technological process of the brilliant manufacture method specific embodiment of graininess compound plant protein is as follows:
Embodiment 1, the manufacture method of broad bean albumen powder
Broad bean → check, impurity elimination → heating go out enzyme, classification, decortication → temperature soak → defibrination → basic ion type leaching liquor continuous flow upstream lixiviate → screenings separation → broad bean slurries → albumen, starch " synchronously " separation → broad bean albumin milk acid ion type coagulates
↓
The poly-liquid flocculation of broad bean starch slurry (system starch and bean vermicelli), sedimentation → high speed centrifugation separation → albumen underflow → accent pH value are to neutrality → heating, homogeneous → spray-drying → broad bean albumen powder.
2, the manufacture method of long-grained nonglutinous rice albumen powder
Long-grained nonglutinous rice (or cracking rice) → check impurity elimination → immersion → defibrination → screenings separation → Rice ﹠ peanut milk → Continuous Countercurrent Extraction rice gluten → starch, protein milk " synchronously " separation → albumin milk → flocculation, sedimentation → high speed centrifugation separation → rice gluten be dense ↓ extremely neutrality → sterilization of rice starch slurry (processing maltose or starch syrup) breast → accent pH value, homogeneous → spray-drying → rice gluten powder.
3, the brilliant manufacture method of the instant compound plant protein of graininess
The paddy bean food raw material of industry-→ the check impurity elimination-→ the continuous temperature of formula material basic ion type soak soaks-→ defibrination-→ Continuous Countercurrent Extraction-→ screenings separates-→ starch, protein milk " synchronously " separation-→ protein emulsion
↓ ↓
Granulated slag starch slurry (respectively in order to powder process or as making maltose, starch syrup material)-→ acid ion type coagulation liquid transfer the isoelectric point flocculating setting-→ high speed centrifugation separates or static separation-→ the dense breast of compound plant protein → accents pH value to neutral-→ further take off raw meat → sterilization-→ homogeneous foaming → foam centrifugal spray drying ↑ filling with inert gas granulation and fluidisation drier-→ the finished product screening-→ the instant compound plant protein of graininess is brilliant-→ quality inspection-→ fill the nitrogen-charging fresh-keeping inner wrapping-→ fill large package encapsulation and cartoning-→ stock inspects by random samples-→ the certified products sale that comes into the market.
Semi-finished product in the technological process---vegetable protein emulsion can be used as the raw material of preparation " compound plant protein milk "; The dense breast of vegetable protein does not require instant " compound plant protein nutrition fortifier " as being processed into, then available multi-functional special equipment of the present invention, adopt high pressure or centrifugal spray drying mode directly to be processed into the vegetable protein powder, also available 2～4 kinds of plant albumen powder grain prescriptions are made powder shape compound plant protein nutrition fortifier.
The invention has the advantages that:
What (1) this method manufacturing obtained is that the dried particles that a kind of distinctive spherical hollow micro capsule is agglomerated into can be fast water-soluble.
(2) use the acid of degradable pure natural small molecular ion type, alkali lye in the process for making,, avoid the heavy metal accumulation and the pollution to product that may cause without the chemical industry soda acid.
(3) directly use cereal, bean material, rather than produce food plant albumen, can make full use of raw material resources with their " byproduct ".
(4) vegetable protein and starch extract synchronously, can make the edible protein and the starch of high-quality, kill two birds with one stone.
(5) adopt reverse counterflow to spray drying-granulating method, the work efficiency height, effective.
(6) apparatus of the present invention possess multi-functionally, can be suitable for centrifugal spray drying prilling method, high-pressure spray-drying prilling method and double-current spray drying granulation process.
Claims (2)
1, brilliant manufacture method of a kind of particle compound plant protein and device thereof, its method is a kind of with various types of grain, the albumin milk of bean material after the immersion of basic ion type leaching liquor, defibrination, slagging-off, adverse current " synchronously " are extracted separating starch, " wait electricity, flocculation, precipitation " through acid ion type coagulation liquid again, high speed centrifugation separates the dense breast of albumen that obtains, transfer pH value, sterilization, homogeneous, fill the nitrogen foaming, form the dense newborn expanding foam solution of albumen, through the granulation of foam centrifugal spray drying, composite making do not contain cholesterol, the brilliant particle of quickly dissolving compound plant protein.Its method feature is:
(1) directly make raw material with cereal, beans, adopt alkali to put forward technology, " synchronously " extracts starch and vegetable protein;
(2) alkali is carried the alkali extracting solution in the technology, but adopts the little molecule basic ion of the pure natural type leaching liquor of natural degradation;
(3) the dense newborn expanding foam solution of albumen is the vegetable protein milk that extracts from cereal, bean material " synchronously ", the dense breast of albumen that obtains with the acid ion type coagulation liquid " isoelectric precipitation " of being furnished with minute quantity food acids and flocculant fills with nitrogen gas foaming, makes it to become the dense newborn expanding foam solution of vegetable protein.
(4) adopt reverse counterflow to the spray prilling, this technology be the dense newborn expanding foam solution of cereal, bean albumen respectively from the dry following current of the top centrifugal atomizing of foam centrifugal spray drying granulation tower downwards and with double flowing nozzle from the below upwards two rightabouts carry out adverse current to the spray granulation.
2, the brilliant manufacturing installation of a kind of graininess compound plant protein, it is a kind of foam centrifugal spray drying prilling granulator, it mainly is made of adjustable continuous foam generator and the connection of spray drying granulation tower, it is characterized in that:
(1) foam maker is adjustable continuous foam generator.It comprises the profile of tooth rotating disk foaming machine of the adjustable gaps between the adjustable mixing nozzle of gas-liquid flow and rotating speed and rotating disk and stator.
(2) spray drying tower comprises an air dewetting drying, hot-air system that the clean temperature of handling is adjustable and adverse current to spray granulating and drying and the dry again structure of low temperature fluid bed, it is by the foam centrifugal atomizer and the hot blast radome fairing of cat head, with the gas-liquid double flowing nozzle formation of tower bottom.
(3) the dual antiseized protection structure of spray-drying inner wall of tower, it is made of inner wall of tower antiadhesion barrier and the vertical current clean dried secondary low temperature hot blast kuppe that produces the ring inner wall of tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02139881 CN1268222C (en) | 2002-12-27 | 2002-12-27 | Production process and apparatus for granular composite plant protein crystal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02139881 CN1268222C (en) | 2002-12-27 | 2002-12-27 | Production process and apparatus for granular composite plant protein crystal |
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| CN1436478A true CN1436478A (en) | 2003-08-20 |
| CN1268222C CN1268222C (en) | 2006-08-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 02139881 Expired - Fee Related CN1268222C (en) | 2002-12-27 | 2002-12-27 | Production process and apparatus for granular composite plant protein crystal |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101805033B (en) * | 2009-02-17 | 2013-07-17 | 张志勇 | Automatic separation system and method for protein in liquid |
| CN103393103A (en) * | 2013-07-10 | 2013-11-20 | 南京财经大学 | Rice bran selenoprotein and soyabean protein compound capsule |
| CN106539094A (en) * | 2016-09-23 | 2017-03-29 | 上海浦力膜制剂辅料有限公司 | A kind of preparation method of Instant protein powder |
| CN108178455A (en) * | 2018-01-31 | 2018-06-19 | 河南桑达能源环保有限公司 | A kind of sewage multi-stage processing equipment |
| CN110522039A (en) * | 2019-08-28 | 2019-12-03 | 苏州恒瑞健康科技有限公司 | A kind of high protein composite nutrition powder and preparation method thereof |
-
2002
- 2002-12-27 CN CN 02139881 patent/CN1268222C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101805033B (en) * | 2009-02-17 | 2013-07-17 | 张志勇 | Automatic separation system and method for protein in liquid |
| CN103393103A (en) * | 2013-07-10 | 2013-11-20 | 南京财经大学 | Rice bran selenoprotein and soyabean protein compound capsule |
| CN103393103B (en) * | 2013-07-10 | 2015-04-29 | 南京财经大学 | Rice bran selenoprotein and soyabean protein compound capsule |
| CN106539094A (en) * | 2016-09-23 | 2017-03-29 | 上海浦力膜制剂辅料有限公司 | A kind of preparation method of Instant protein powder |
| CN107897938A (en) * | 2016-09-23 | 2018-04-13 | 上海浦力膜制剂辅料有限公司 | A kind of preparation method of Instant protein powder |
| CN108178455A (en) * | 2018-01-31 | 2018-06-19 | 河南桑达能源环保有限公司 | A kind of sewage multi-stage processing equipment |
| CN108178455B (en) * | 2018-01-31 | 2021-04-09 | 河南桑达能源环保有限公司 | Sewage multi-stage treatment equipment |
| CN110522039A (en) * | 2019-08-28 | 2019-12-03 | 苏州恒瑞健康科技有限公司 | A kind of high protein composite nutrition powder and preparation method thereof |
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| Publication number | Publication date |
|---|---|
| CN1268222C (en) | 2006-08-09 |
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