KR20040036933A - Process for Producing Powdery Soybean Protein Material - Google Patents
Process for Producing Powdery Soybean Protein Material Download PDFInfo
- Publication number
- KR20040036933A KR20040036933A KR10-2004-7003302A KR20047003302A KR20040036933A KR 20040036933 A KR20040036933 A KR 20040036933A KR 20047003302 A KR20047003302 A KR 20047003302A KR 20040036933 A KR20040036933 A KR 20040036933A
- Authority
- KR
- South Korea
- Prior art keywords
- soy protein
- powder
- powdered
- dextrin
- protein material
- Prior art date
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- 108010073771 Soybean Proteins Proteins 0.000 title claims abstract description 128
- 239000000463 material Substances 0.000 title claims abstract description 45
- 238000000034 method Methods 0.000 title claims description 16
- 235000019710 soybean protein Nutrition 0.000 title claims description 9
- 229940001941 soy protein Drugs 0.000 claims abstract description 119
- 239000000843 powder Substances 0.000 claims abstract description 80
- 229920001353 Dextrin Polymers 0.000 claims abstract description 54
- 239000004375 Dextrin Substances 0.000 claims abstract description 54
- 235000019425 dextrin Nutrition 0.000 claims abstract description 54
- 238000004519 manufacturing process Methods 0.000 claims abstract description 27
- 235000013305 food Nutrition 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims description 23
- 239000007921 spray Substances 0.000 claims description 20
- 235000021110 pickles Nutrition 0.000 claims description 16
- 238000005507 spraying Methods 0.000 claims description 13
- 239000003995 emulsifying agent Substances 0.000 claims description 10
- 241000251468 Actinopterygii Species 0.000 claims description 6
- 235000013361 beverage Nutrition 0.000 claims description 6
- 238000012545 processing Methods 0.000 claims description 6
- 235000013322 soy milk Nutrition 0.000 claims description 6
- 229920002245 Dextrose equivalent Polymers 0.000 claims description 4
- 239000008280 blood Substances 0.000 claims description 4
- 210000004369 blood Anatomy 0.000 claims description 4
- 235000013372 meat Nutrition 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 44
- 239000012460 protein solution Substances 0.000 abstract description 10
- 238000013019 agitation Methods 0.000 abstract description 5
- 239000003921 oil Substances 0.000 description 14
- 235000019198 oils Nutrition 0.000 description 14
- 239000000546 pharmaceutical excipient Substances 0.000 description 14
- 239000003925 fat Substances 0.000 description 11
- 235000019197 fats Nutrition 0.000 description 11
- 238000003756 stirring Methods 0.000 description 11
- 235000010469 Glycine max Nutrition 0.000 description 8
- 244000068988 Glycine max Species 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- 239000000243 solution Substances 0.000 description 8
- 238000007664 blowing Methods 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 7
- 238000011156 evaluation Methods 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- -1 protease Chemical compound 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 229920002472 Starch Polymers 0.000 description 6
- 238000001694 spray drying Methods 0.000 description 6
- 239000008107 starch Substances 0.000 description 6
- 235000019698 starch Nutrition 0.000 description 6
- 235000000346 sugar Nutrition 0.000 description 6
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 5
- 239000000787 lecithin Substances 0.000 description 5
- 235000010445 lecithin Nutrition 0.000 description 5
- 229940067606 lecithin Drugs 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 238000004090 dissolution Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 235000014113 dietary fatty acids Nutrition 0.000 description 3
- 239000000194 fatty acid Substances 0.000 description 3
- 229930195729 fatty acid Natural products 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 235000004252 protein component Nutrition 0.000 description 3
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- 235000019482 Palm oil Nutrition 0.000 description 2
- 108091005804 Peptidases Proteins 0.000 description 2
- 239000004365 Protease Substances 0.000 description 2
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- 235000013622 meat product Nutrition 0.000 description 2
- DNIAPMSPPWPWGF-UHFFFAOYSA-N monopropylene glycol Natural products CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 2
- 239000002540 palm oil Substances 0.000 description 2
- 235000018102 proteins Nutrition 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 150000008163 sugars Chemical class 0.000 description 2
- QCVGEOXPDFCNHA-UHFFFAOYSA-N 5,5-dimethyl-2,4-dioxo-1,3-oxazolidine-3-carboxamide Chemical compound CC1(C)OC(=O)N(C(N)=O)C1=O QCVGEOXPDFCNHA-UHFFFAOYSA-N 0.000 description 1
- GUBGYTABKSRVRQ-XLOQQCSPSA-N Alpha-Lactose Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@H](O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-XLOQQCSPSA-N 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- 240000000731 Fagus sylvatica Species 0.000 description 1
- 235000010099 Fagus sylvatica Nutrition 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerol Natural products OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 238000007696 Kjeldahl method Methods 0.000 description 1
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 235000019774 Rice Bran oil Nutrition 0.000 description 1
- 235000019485 Safflower oil Nutrition 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001341 alkaline earth metal compounds Chemical class 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 235000014121 butter Nutrition 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000005687 corn oil Nutrition 0.000 description 1
- 239000002285 corn oil Substances 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 239000002385 cottonseed oil Substances 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 235000014103 egg white Nutrition 0.000 description 1
- 210000000969 egg white Anatomy 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000021323 fish oil Nutrition 0.000 description 1
- 235000013332 fish product Nutrition 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000008101 lactose Substances 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 235000020991 processed meat Nutrition 0.000 description 1
- 238000013441 quality evaluation Methods 0.000 description 1
- 239000008165 rice bran oil Substances 0.000 description 1
- 235000005713 safflower oil Nutrition 0.000 description 1
- 239000003813 safflower oil Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 235000013580 sausages Nutrition 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000003760 tallow Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
- A23J3/00—Working-up of proteins for foodstuffs
- A23J3/14—Vegetable proteins
- A23J3/16—Vegetable proteins from soybean
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/52—Adding ingredients
- A23L2/66—Proteins
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P10/00—Shaping or working of foodstuffs characterised by the products
- A23P10/30—Encapsulation of particles, e.g. foodstuff additives
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P10/00—Shaping or working of foodstuffs characterised by the products
- A23P10/40—Shaping or working of foodstuffs characterised by the products free-flowing powder or instant powder, i.e. powder which is reconstituted rapidly when liquid is added
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Nutrition Science (AREA)
- Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Meat, Egg Or Seafood Products (AREA)
- Beans For Foods Or Fodder (AREA)
- Jellies, Jams, And Syrups (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
- General Preparation And Processing Of Foods (AREA)
Abstract
본 발명은 제조 규모에 있어서 강력한 교반없이 약한 교반하에서도 쉽게 물에 분산시키며, 식품에 요구되는 충분한 겔 형성성을 겸비한 분말상 대두 단백 소재를 제공하는 것이다.SUMMARY OF THE INVENTION The present invention provides a powdered soy protein material that is easily dispersed in water even under mild agitation without strong agitation on a production scale and has sufficient gel formability required for food.
대두 단백 분말의 제조 공정에 있어서, 대두 단백 용액을 분무 건조하여 일단 분말화한 후, 이 대두 단백 분말 100 중량부에 대하여 DE치 10 내지 25의 덱스트린 0.5 내지 3 중량부를 부형액으로서 더 분무하고 부착시킴으로써 얻어진 분말상 대두 단백 소재가 충분한 겔 형성성을 유지하면서도 약한 교반에서도 우수한 수분산성을 갖는다는 사실을 알게 되어, 본 발명을 완성하기에 이르렀다.In the manufacturing process of soy protein powder, the soy protein solution is spray-dried and once powdered, and then 0.5-3 parts by weight of DE values 10-25 dextrins are further sprayed and adhered to 100 parts by weight of the soy protein powder. The powdery soy protein material obtained by the present invention was found to have excellent water dispersibility even under mild agitation while maintaining sufficient gel formability, thus completing the present invention.
Description
대두 단백 분말을 사용하여 식품을 제조 가공할 때에는 물에 용해, 분산시켜 취급하는 경우가 많다. 이 때, 특히 대두 단백 분말에서의 가용성 단백질 함량의 비율(NSI: 질소 수용성 계수로 표시할 수 있음)이 높을수록 덩어리(내부에 물이 침투하지 않고, 분체 표면만이 물에 습윤되고, 큰 입자가 형성된 상태)가 생기기 쉬우며, 이 대두 단백 분말을 완전히 분산, 용해하기 위해서는 상당한 시간을 필요로 한다. 또한, 물에 용해시 분말 날림이 많아 작업상 취급이 어렵다는 문제가 있었다.When food is manufactured and processed using soy protein powder, it is often dissolved and dispersed in water and handled. At this time, especially, the higher the ratio of the soluble protein content in the soy protein powder (which can be expressed by NSI: nitrogen solubility coefficient), the mass (water does not penetrate inside, only the powder surface is wetted with water, Is easily formed, and a considerable time is required to completely disperse and dissolve the soy protein powder. In addition, there is a problem that handling is difficult in handling a lot of powder when dissolving in water.
이러한 문제를 해결하는 수단으로서, 예를 들면 일본 특허 공개 2000-102352호 공보(JP)에서는 대두 단백 분말에 유지 및 유화제를 첨가하는 방법이, 또한 일본 특허 공개 (평)8-154593호 공보(JP)에서는 대두 단백을 수계하에서 프로테아제에 의해 가수분해하여 유지 및 유화제를 첨가하는 방법이 개시되어 있다. 그러나, 이들 방법은 비이커 규모로 용해시키는 경우, 또는 제조 규모에 있어서도 용해에분말 믹서, 마일더, 고압 균질기 등의 강력한 교반ㆍ유화 장치를 사용할 수 있는 경우라면 유효하지만, 제조 규모에 있어서 이러한 장치를 갖지 않고, 프로펠라 교반과 같은 간편한 교반 장치밖에 없는 경우에는 여전히 신속하게 분산시키기가 어렵고, 덩어리가 생기기 쉬워 작업상 문제가 남아 있었다. 이와 같이 어떠한 제조 설비에 있어서도 어려움없이 분산시킬 수 있는 적용 범위가 넓은 분말상 대두 단백 소재는 아직 얻지 못하였다.As a means to solve this problem, for example, Japanese Patent Application Laid-Open No. 2000-102352 (JP) discloses a method of adding a fat or oil and an emulsifier to soy protein powder, and also Japanese Patent Application Laid-Open No. 8-154593 (JP). ) Discloses a method in which soy protein is hydrolyzed by a protease in an aqueous system to add a fat or oil and an emulsifier. However, these methods are effective when dissolving on a beaker scale or when a strong stirring / emulsifying device such as a powder mixer, a milder, or a high pressure homogenizer can be used for dissolution even on a manufacturing scale. In the case of having a simple stirring device such as propeller agitation, it was still difficult to disperse quickly and agglomerates tended to remain in operation. As such, a powdery soy protein material having a wide range of application that can be dispersed without difficulty in any manufacturing facility has not yet been obtained.
한편, 동일한 목적으로 일본 특허 공개 (평)9-275911호 공보(JP)에서는 분말상 대두 단백 소재를 제조할 때, 대두 단백 용액을 분무 건조하기 전에 대두 단백 용액에 전분 부분 가수분해물(덱스트린)을 대두 단백 용액의 고형분 100 중량부에 대하여 2 내지 40 중량부 첨가 용해하고, 그 후 분무 건조에 의해 분말상 대두 단백 소재를 얻는 방법이 개시되어 있다. 그러나, 이 방법은 대두 단백 용액을 분말화하기 전에 덱스트린을 혼합 용해시킨다는 점에서 본 발명과는 덱스트린의 첨가 공정이 상이하다. 또한, 이 방법에 따르면 충분한 수분산성을 얻기 위해 덱스트린의 첨가량을 늘릴 필요가 있기 때문에 얻어지는 분말상 대두 단백 소재 중의 단백 성분의 구성 비율이 저하되고, 식품 가공에 있어서 분말상 대두 단백 소재의 가장 중요한 기능인 겔 형성성에 영향을 미치는 경우가 있었다.On the other hand, Japanese Patent Application Laid-Open No. 9-275911 (JP) discloses that when preparing a powdered soy protein material, starch partial hydrolyzate (dextrin) is added to the soy protein solution before spray drying the soy protein solution. The method of adding 2-40 weight part of melt | dissolution with respect to 100 weight part of solid content of a protein solution, and obtaining a powdery soy protein material by spray drying after that is disclosed. However, this method differs from the present invention in that the dextrin is added to the process by mixing and dissolving dextrin before powdering the soy protein solution. In addition, according to this method, it is necessary to increase the amount of dextrin added to obtain sufficient water dispersibility, so that the composition ratio of the protein component in the powdered soy protein material is lowered, and gel formation is the most important function of the powdered soy protein material in food processing. There was a case of affecting sex.
본 발명은 제조 규모에 있어서 강력한 교반을 행하지 않고 약한 교반 조건하에서도 우수한 수분산성을 발휘하고, 대두 단백에 요구되는 충분한 겔 형성성을 겸비한 분말상 대두 단백 소재를 제공하는 것이다.SUMMARY OF THE INVENTION The present invention provides a powdered soy protein material which exhibits excellent water dispersibility even under mild stirring conditions without producing strong agitation at the production scale and has sufficient gel formability required for soy protein.
본 발명은 강력한 교반기를 사용하지 않아도 덩어리가 생기지 않고, 수분산성이 우수한 분말상 대두 단백 소재의 제조 방법에 관한 것이다.The present invention relates to a method for producing a powdered soy protein material excellent in water dispersibility without forming agglomerates without using a powerful stirrer.
본 발명자들은 상기 과제를 해결하기 위해 예의 연구한 결과, 대두 단백 분말의 제조 공정에 있어서 대두 단백 용액을 분무 건조하여 일단 분말화한 후, 이 대두 단백 분말에 대하여 특정한 DE치를 갖는 덱스트린 용액을 분무, 부착시킴으로써 얻어진 분말상 대두 단백 소재가 충분한 겔 형성성을 유지하면서도 약한 교반에서도 우수한 수분산성을 갖는다는 사실을 알게 되어, 본 발명을 완성하기에 이르렀다.MEANS TO SOLVE THE PROBLEM As a result of earnestly researching in order to solve the said subject, as a result of spray-drying a soy protein solution in the manufacturing process of soy protein powder, it is made into powder once, and then spraying the dextrin solution which has a specific DE value with respect to this soy protein powder, It has been found that the powdered soy protein material obtained by adhesion has excellent water dispersibility even under mild stirring while maintaining sufficient gel formability, thus completing the present invention.
즉, 본 발명은That is, the present invention
(1) 대두 단백 분말에 대하여 DE치(Dextrose Equivalent) 10 내지 25의 덱스트린을 분무하는 것을 특징으로 하는 분말상 대두 단백 소재의 제조 방법.(1) A method for producing a powdered soy protein material, characterized by spraying a dextrin having a DE value (Dextrose Equivalent) of 10 to 25 to soy protein powder.
(2) 상기 (1)에 있어서, 덱스트린의 분무량이 대두 단백 분말 100 중량부에 대하여 0.5 내지 3 중량부인 제조 방법.(2) The production method according to (1), wherein the spray amount of dextrin is 0.5 to 3 parts by weight based on 100 parts by weight of soy protein powder.
(3) 상기 (1) 또는 (2)에 있어서, 대두 단백 분말 100 중량부에 대하여 유지 0.1 내지 0.3 중량부를 분무하거나, 또는 유지 0.1 내지 0.3 중량부 및 유지 분무 중량의 1/2 중량 이하의 유화제를 분무하는 제조 방법.(3) The emulsifier according to the above (1) or (2), which is sprayed with 0.1 to 0.3 parts by weight of fat or oil, or 0.1 to 0.3 parts by weight of fat or oil and 1/2 weight or less of the weight of fat or oil spray based on 100 parts by weight of soy protein powder. Method of spraying.
(4) 상기 (1) 내지 (3) 중 어느 한 항에 있어서, 대두 단백 분말이 분리 대두 단백, 전지 또는 탈지 두유 분말 또는 농축 대두 단백인 제조 방법.(4) The production method according to any one of (1) to (3), wherein the soy protein powder is separated soy protein, whole or skim soy milk powder, or concentrated soy protein.
(5) 상기 (1) 내지 (4) 중 어느 한 항에 기재된 제조 방법에 의해 얻어진 분말상 대두 단백 소재.(5) The powdered soy protein material obtained by the manufacturing method in any one of said (1)-(4).
(6) 상기 (5)에 기재된 분말상 대두 단백 소재를 사용한 축육 가공 제품 또는 수산 가공 제품.(6) Meat processed products or fish processed products using the powdered soy protein material according to the above (5).
(7) 상기 (5)에 기재된 분말상 대두 단백 소재를 사용한 축육 가공 제품의 피클액.(7) The pickle liquid of the processed meat product using the powdered soy protein material as described in said (5).
(8) 상기 (5)에 기재된 분말상 대두 단백 소재를 사용한 분말 음료 또는 액체 음료.(8) Powdered beverage or liquid beverage using the powdered soy protein material as described in said (5).
(9) 상기 (5)에 기재된 분말상 대두 단백 소재를 사용한 프라이 조리 식품의 옷.(9) Clothes of fried foods using the powdered soy protein material according to the above (5).
(10) 상기 (5)에 기재된 분말상 대두 단백 소재를 사용한 교자류의 피(皮).등을 제공한다.(10) Provided are blood of gyoza using the powdered soy protein material according to (5) above.
<발명을 실시하기 위한 최선의 형태>Best Mode for Carrying Out the Invention
본 발명은 대두 단백 분말에 대하여 특정한 DE치를 갖는 덱스트린을 분무하고, 대두 단백 분말 표면에 덱스트린을 부착시키는 데 그 특징이 있다. 그 분무 방법이나 사용하는 장치의 종류, 분무 후의 건조 방법에 대해서는 특별히 한정되지는 않는다. 바람직한 양태로서는 유동층 건조기 등(예를 들면 플로우 코터 등)과 같이 밀폐계의 유동층 내에서 대두 단백 분말을 풍압에 의해 유동시키면서, 이 분말에 대하여 덱스트린을 용해시킨 부형액을 안개상으로 분무시켜 부착시키고, 동시에 유동층 내의 가열에 의해 상기 분말의 건조까지 행하는 방법을 들 수 있다. 또한, 부형액이란 대두 단백 분말에 분무하여 부착시키는 용액을 말하며, 결합제액, 결착액이라고도 부를 수 있다.The present invention is characterized by spraying dextrin having a specific DE value to soy protein powder and attaching dextrin to the surface of soy protein powder. It does not specifically limit about the spraying method, the kind of apparatus to be used, and the drying method after spraying. In a preferred embodiment, the soy protein powder is flown by air pressure in a closed fluidized bed, such as a fluidized bed dryer (e.g., a flow coater), and the excipient in which dextrin is dissolved is sprayed onto the powder in the form of a mist and attached. And the method of performing the drying of the powder by heating in a fluidized bed at the same time. In addition, excipient means the solution which sprays and adheres to soy protein powder, and can also be called binder liquid and binder liquid.
즉, 덱스트린을 대두 단백 분말의 표면에만 부착시킴으로써 소량의 덱스트린첨가량으로도 덱스트린의 수화성에 의해 수분산성을 높일 수 있다. 또한, 분말상대두 단백 소재 중의 대두 단백의 구성비를 거의 낮추지 않기 때문에 대두 단백의 중요한 기능인 겔 형성성에의 영향도 매우 적다. 한편, 예를 들면 덱스트린을 대두 단백 용액에 혼합 용해시키고 나서 상기 용액을 분무 건조기 등으로 분무 건조하는 방법에서는 대두 단백과 덱스트린 분자가 용액 중에 균일하게 분산된 상태에서 분말화되는 것이라고 여겨지며, 반드시 대두 단백 분말의 표면을 주체로 덱스트린이 부착된 상태가 되는 것은 아니므로 수분산성을 높이기 위해 본 발명의 방법보다도 다량의 덱스트린을 첨가하는 것이 필요하다. 이 경우, 분말상 대두 단백 소재 중의 대두 단백의 구성비가 떨어지기 때문에 대두 단백의 겔 형성성을 저하시킬 가능성이 있어 식품 가공상 바람직하지 않다. 또한, 대두 단백 분말에 단순히 덱스트린 분말을 혼합하는 것만으로는 대두 단백 분말 표면에 덱스트린 분말이 부착되지 않기 때문에 수분산성은 개선되지 않는다.That is, by adhering dextrin only to the surface of soy protein powder, the water dispersibility can be improved by the hydration of dextrin even with a small amount of dextrin addition. In addition, since the composition ratio of soy protein in powdered soy protein material is hardly lowered, the influence on gel formation, which is an important function of soy protein, is also very small. On the other hand, for example, in the method of mixing and dissolving dextrin in a soy protein solution and then spray-drying the solution with a spray dryer or the like, it is considered that the soy protein and dextrin molecules are powdered in a uniformly dispersed state in a solution, and soy protein Since dextrin is not mainly attached to the surface of the powder, it is necessary to add a larger amount of dextrin than the method of the present invention to increase water dispersibility. In this case, since the composition ratio of the soy protein in powdered soy protein material falls, there exists a possibility that the gel formation property of soy protein may fall, and it is unpreferable for food processing. Also, simply mixing the dextrin powder with the soy protein powder does not improve the water dispersibility because the dextrin powder does not adhere to the surface of the soy protein powder.
본 발명에서 사용하는 "대두 단백 분말"로서는, 예를 들면 대두나 탈지 대두 등의 대두 원료를 물로 추출하고, 산 침전시켜 분리하여 중화한 후, 분무 건조 등에 의해 분말화된 분리 대두 단백을 적용할 수 있다. 이 경우, 물 추출은 수성 용매를 대두 원료에 첨가하여 교반 등으로 슬러리상을 만들고, 불용성 분획(비지)을 원심 분리, 여과 분별 등의 방법에 의해 분리, 제거하여 두유를 얻는다. 이어서, 이 두유에 산류(염산, 황산 등의 무기산 또는 그 밖의 유기산과의 병용 등)를 첨가하여 단백성 침전 분획(카드)를 분취한다. 이 카드에 알칼리류(수산화나트륨, 수산화칼슘 등)를 첨가하여 중화하여 "대두 단백 용액"을 얻는다. 중화 후에 통상 가열 살균 등을 행하고, 이 용액을 분무 건조기 등을 이용한 분무 건조 등의 수단에 의해 건조하여 대두 단백 분말인 분리 대두 단백을 제조할 수 있다. 이 때, 예를 들면 카드에 가열 처리를 행하거나, 대두 단백 용액에 프로테아제 등의 산소나 산에 의한 부분적인 가수분해를 실시하거나, 염화마그네슘 등의 알칼리 토금속 화합물 등을 첨가하는 등의 원하는 가공 처리를 행할 수도 있다. 또한, 다른 대두 단백 분말로서는 전지/탈지 두유 분말, 농축 대두 단백 등도 사용할 수 있다.As the "soy protein powder" used in the present invention, soybean raw materials such as soybean or skim soybean are extracted with water, acid precipitated, separated and neutralized, and then powdered soybean protein powdered by spray drying or the like can be applied. Can be. In this case, water extraction adds an aqueous solvent to the soybean raw material to form a slurry phase by stirring or the like, and the insoluble fraction (beech) is separated and removed by a method such as centrifugation or filtration fractionation to obtain soymilk. Subsequently, acids (in combination with inorganic acids such as hydrochloric acid and sulfuric acid or other organic acids, etc.) are added to the soy milk to separate the proteinaceous precipitate fraction (card). Alkali (sodium hydroxide, calcium hydroxide, etc.) is added to the card and neutralized to obtain a "soy protein solution". After neutralization, heat sterilization or the like is usually carried out, and the solution can be dried by means such as spray drying using a spray dryer or the like to produce a soybean protein powder that is soybean protein powder. At this time, for example, desired processing such as heat treatment to the card, partial hydrolysis by oxygen or acid such as protease, or addition of alkaline earth metal compounds such as magnesium chloride, etc. to the soy protein solution. You can also do As other soy protein powders, battery / degreasing soy milk powder, concentrated soy protein, and the like can also be used.
덱스트린이란 전분을 화학적 또는 효소적 방법에 의해 저분자화한 전분 부분 가수분해물이다. DE치(Dextrose Equivalent)란 덱스트린의 구성 단위인 글루코스 잔기의 장쇄의 지표가 되는 것이며, 덱스트린 중의 환원당의 함유량(%)을 나타내는 값이다. 이 값이 클수록 덱스트린의 장쇄는 짧아진다.Dextrin is a starch partial hydrolyzate in which starch is low molecularized by chemical or enzymatic methods. DE value (Dextrose Equivalent) is an index of the long chain of glucose residue which is a structural unit of dextrin, and is a value which shows content (%) of reducing sugar in dextrin. The larger this value, the shorter the long chain of dextrin.
본 발명에 사용하는 덱스트린으로서는 DE치가 10 내지 25인 것이 바람직하고, 16 내지 20인 것이 보다 바람직하며, 17 내지 19인 것이 가장 바람직하다.As dextrin used for this invention, it is preferable that DE value is 10-25, It is more preferable that it is 16-20, It is most preferable that it is 17-19.
DE치가 지나치게 작으면 물성이 전분에 가까워지기 때문에, 예를 들면 대두 단백 분말에 덱스트린을 부형액으로서 분무하는 경우에는 부형액의 점도가 지나치게 높아지고, 분무를 행하기 어려워지는 경향이 있다. 또한, 물에의 분산성도 나빠지며, 피클액으로서 사용했을 경우, 피클액의 점도 자체도 상승하기 때문에 햄 제조시 육 조직으로의 피클액의 침투성이 저해되고, 햄의 식감 등의 품질이 저하되는 경향이 있다. 따라서, 덱스트린 대신에 전분을 사용해도 동일한 경향을 보인다.If the DE value is too small, since the physical properties are close to starch, for example, when dextrin is sprayed on soy protein powder as an excipient, the viscosity of the excipient is too high, and it is difficult to spray. In addition, the dispersibility in water also worsens, and when used as a pickle liquid, the viscosity of the pickle liquid also increases, so that the permeability of the pickle liquid into the ham tissue during ham production is impaired, and the quality of the ham texture and the like is deteriorated. There is a tendency. Therefore, the use of starch instead of dextrins shows the same trend.
또한, DE가 지나치게 높으면 물성이 소당류에 가까워지기 때문에, 예를 들면 유동층 건조기에 있어서 대두 단백 분말에 대하여 상기 덱스트린을 부형액으로서분무하면 부형액이 가열에 의해 갈변되어 분말상 대두 단백 소재 자체의 색조가 변화되는 경향이 있다. 따라서, 덱스트린 대신에 설탕, 락토오스, 포도당 등의 소당류를 사용해도 동일한 경향을 보인다.In addition, if DE is too high, the physical properties are close to the small sugars. For example, when the dextrin is sprayed as an excipient with respect to soy protein powder in a fluidized bed dryer, the excipient is browned by heating, and the color of the powdered soy protein material itself is changed. Tends to change. Therefore, the use of small sugars such as sugar, lactose, glucose and the like instead of dextrin shows the same tendency.
특정한 글루코스쇄 길이(DE 10 내지 25)를 갖는 덱스트린은 대두 단백 분말의 수분산성에 특히 우수한 특성을 갖는 것이다.Dextrins with a particular glucose chain length (DE 10-25) are those which have particularly good properties for the water dispersibility of soy protein powders.
대두 단백 분말 100 중량부에 대한 상기 덱스트린의 분무량은 수분산성이 발휘되는 데 충분한 양 이상으로서, 대두 단백의 겔 형성성을 저하시키지 않는 상한치 이하인 것이 바람직하다. 특히, 0.5 내지 3 중량부가 바람직하고, 0.8 내지 2 중량부가 보다 바람직하며, 1 내지 1.7 중량부가 가장 바람직하다. 분무량이 지나치게 적으면 대두 단백 분말에 부착되는 덱스트린의 양이 부족하기 때문에 수분산성이 발휘되기 어렵다. 또한, 분무량이 지나치게 많으면 수분산성은 높지만, 제품 중의 대두 단백의 구성 비율이 저하되기 때문에 대두 단백의 중요한 기능인 겔 형성성이 저하되어 햄 등의 식품 가공품에 대하여 충분한 기능이 발휘되기 어렵다.The spray amount of the said dextrin with respect to 100 weight part of soy protein powder is more than an amount sufficient for water dispersibility, and it is preferable that it is below an upper limit which does not reduce the gel formation property of soy protein. In particular, 0.5-3 weight part is preferable, 0.8-2 weight part is more preferable, and 1-1.7 weight part is the most preferable. If the spray amount is too small, the water dispersion is hardly exhibited because the amount of dextrin adhered to the soy protein powder is insufficient. In addition, when the spray amount is too large, the water dispersibility is high, but since the composition ratio of soy protein in the product is lowered, the gel formability, which is an important function of the soy protein, is lowered, so that a sufficient function is hardly exerted on food products such as ham.
본 발명은 덱스트린과 함께 유지 또는 유지 및 유화제를 분무함으로써 분말상 대두 단백 소재 용해시의 분말 날림을 억제하고, 습윤성을 신속히 할 수 있다. 즉, 덱스트린에 의한 수분산성의 개선과 협조하여 우수한 용해 특성을 갖는 분말상 대두 단백 소재를 얻을 수 있는 것이다. 분무는 덱스트린과 동시에 또는 덱스트린의 분무 전후에 행하는 것이 바람직하다.The present invention can suppress powder blowing at the time of dissolving the powdered soy protein material by spraying a fat or oil and an emulsifier with the dextrin, and can quickly improve wettability. That is, in cooperation with the improvement of the water dispersibility by dextrin, it is possible to obtain a powdered soy protein material having excellent dissolution properties. Spraying is preferably performed simultaneously with or before or after spraying of dextrin.
본 발명에서 사용하는 유지는 용도에 따라 팜유, 야자유, 대두유, 면실유, 옥수수유, 홍화유, 쌀겨유 등의 식물성 유지, 우지, 돈지, 어유, 그 밖의 동물유등의 동물성 유지 또는 효모 등의 미생물에 의한 유지, 또는 이들의 분별, 경화 또는 에스테르 교환 유지 등을 사용할 수 있다.The fats and oils used in the present invention may be produced by microorganisms such as vegetable oils such as palm oil, palm oil, soybean oil, cottonseed oil, corn oil, safflower oil, rice bran oil, animal fats and oils such as tallow, lard, fish oil, and other animal oils. Fats and oils, or fractions thereof, curing or transesterified oils and the like can be used.
분무하는 유지의 양은 덱스트린의 분무량에 따른 양으로 하는 것이 적당하다. 즉, 대두 단백 분말 100 중량부에 대하여 0.1 내지 0.3 중량부가 바람직하고, 0.15 내지 0.25 중량부가 보다 바람직하다. 이 범위보다 적으면 분말 날림이 발생하기 쉽고, 습윤성도 느려지기 쉽다. 반대로 지나치게 많으면 습윤성이 지나치게 빨라져 대두 단백 분말로부터 유래하는 블록킹이 발생하기 쉬워진다.The amount of the oil or fat to be sprayed is suitably set in accordance with the amount of dextrin sprayed. That is, 0.1-0.3 weight part is preferable with respect to 100 weight part of soy protein powder, and 0.15-0.25 weight part is more preferable. If it is less than this range, powder blowing is easy to occur, and wettability tends to become slow. On the contrary, when too much, wettability will become too fast and the blocking derived from soy protein powder will occur easily.
본 발명에서 사용하는 유화제는 용도에 따라 레시틴, 글리세린 지방산 에스테르, 소르비탄 지방산 에스테르, 프로필렌글리콜 지방산 에스테르, 당 에스테르 등 각종 계면활성제를 사용할 수 있다. 분무하는 유화제의 양도 덱스트린의 분무량에 따른 양으로 하는 것이 바람직하고, 대두 단백 분말에 분무하는 유지 중량의 1/2 이하가 적당하며, 1/10 이상 2/5 이하가 보다 바람직하다. 유화제의 양이 지나치게 많으면 유화제의 풍미가 강해지고, 유화제의 양이 지나치게 적으면 유지가 갖는 분말 날림 억제나 습윤성 개선의 기능을 높이는 효과가 발휘되기 어렵다.The emulsifiers used in the present invention may be various surfactants such as lecithin, glycerin fatty acid esters, sorbitan fatty acid esters, propylene glycol fatty acid esters and sugar esters. It is preferable to make the quantity of the emulsifier sprayed into the quantity according to the spray amount of dextrin, and 1/2 or less of the holding weight sprayed on soy protein powder is suitable, and 1/10 or more and 2/5 or less are more preferable. When the amount of the emulsifier is too large, the flavor of the emulsifier is strong, and when the amount of the emulsifier is too small, it is difficult to exert the effect of improving the function of suppressing powder blowing and improving wettability of oil or fat.
본 발명의 제조 방법에 의해 얻어진 분말상 대두 단백 소재는 대두 단백 소재의 NSI가 80 이상으로 비교적 높은 경우에 있어서도, 제조 규모에서의 약한 교반하에서도 냉수로 쉽게 분산시켜 높은 겔 형성성을 유지하다. 따라서, 이러한 분말상 대두 단백 소재는 이들 특성을 살린 각종 식품(예를 들면 햄, 소시지 등의 축육 가공 제품, 어묵, 구멍뚫린 어묵, 어육 햄버그 등의 수산 가공 제품 등)으로의 이용이 바람직하다. 특히, 햄 제조에 사용되는 피클액으로의 사용은 피클액의 제조시 작업성을 개선하고, 햄에 양호한 식감을 제공하기 때문에 가장 바람직한 이용 양태 중 하나이다.The powdered soy protein material obtained by the production method of the present invention is easily dispersed in cold water even under mild stirring at the production scale to maintain high gel formation even when the NSI of the soy protein material is relatively high. Therefore, the powdered soy protein material is preferably used for various foods utilizing these characteristics (for example, meat products such as ham and sausage, fish paste, perforated fish paste, fish products such as fish hamburg and the like). In particular, use as a pickle liquid used in ham production is one of the most preferred modes of use because it improves workability in the production of pickle liquid and provides a good texture to the ham.
또한, 수분산성이 우수하고, 덩어리가 생기지 않는 특성을 이용하여 단백 분말 등의 분말 음료, 대두 단백이 들어간 액체 음료, 프라이 조리 식품의 옷으로서의 버터 믹스, 교자류(교자, 만두, 찐 만두 등)의 피 반죽, 제과ㆍ제빵류의 반죽 등으로의 사용도 가능하다. 또한, 우유 등의 물 이외의 가식성 액체에 분산시켜 사용할 수도 있다.In addition, it is excellent in water dispersibility and does not form lumps, so it is a powdered beverage such as protein powder, a liquid beverage containing soy protein, a butter mix as clothes for fried foods, gyoza (gyoza, dumplings, steamed dumplings, etc.). It can also be used as dough for blood, dough for confectionery and bakery. Moreover, it can also be used disperse | distributing to edible liquids other than water, such as milk.
이하, 본 발명의 실시예를 나타내지만, 본 발명이 이들에 의해 그 기술 범위가 한정되는 것은 아니다.Hereinafter, although the Example of this invention is shown, this technical scope is not limited by these.
<실시예 1><Example 1>
탈지 대두 박편 10 kg을 물 100 kg에 분산시키고, 호모 믹서(도꾸슈 기까 고교(주) 제조)로 교반하면서 50 ℃에서 30 분간 단백 성분을 추출한 후, 원심 분리기를 이용하여 불용물을 제거하여 얻은 두유에 pH 4.5가 될 때까지 염산을 첨가하고, 산 침전 분획을 원심 분리기에 의해 회수하였다. 이 산 침전 분획(고형분 4 kg)을 물 40 kg에 분산시키고, 수산화나트륨을 더 첨가하여 pH 7.0으로 중화하여 대두 단백 용액을 얻고, 이것을 140 ℃에서 60 초간 가열 살균하고, 분무 건조기를 이용하여 분무 건조하여 분리 대두 단백인 대두 단백 분말 4.0 kg을 얻었다. 이 대두 단백 분말의 NSI는 93이었다.10 kg of defatted soybean flakes were dispersed in 100 kg of water, extracted with protein components at 50 ° C. for 30 minutes while stirring with a homomixer (manufactured by Tokushu Kika Kogyo Co., Ltd.), and then obtained by removing insoluble matters using a centrifuge. Hydrochloric acid was added to soymilk until pH 4.5, and the acid precipitate fractions were recovered by centrifuge. This acid precipitate fraction (4 kg of solid) was dispersed in 40 kg of water, and further added sodium hydroxide to neutralize to pH 7.0 to obtain a soy protein solution, which was heated and sterilized at 140 ° C. for 60 seconds and sprayed using a spray dryer. It dried and obtained 4.0 kg of soy protein powder which is a separated soy protein. NSI of this soy protein powder was 93.
또한, NSI는 정법에 의해 분리 대두 단백에 10 배량의 물을 첨가하여 프로펠라 교반하고, 여과지(NO.5) 투과액 중의 질소를 켈달법으로 측정하고, 동일한 방법으로 분리 대두 단백의 총 질소량에서 차감하여 백분율로 나타내었다.In addition, NSI added 10 times the amount of water to the separated soy protein by the conventional method, stirred the propeller, measured the nitrogen in the filter paper (NO.5) permeate by the Kjeldahl method, and subtracted from the total nitrogen content of the isolated soy protein by the same method. As a percentage.
이어서, 70 ℃의 끓인 물 600 g에 호모 믹서를 사용하여 DE치 18의 덱스트린 (산와 덴분(주) 제조 "산덱 185N") 60 g(대두 단백 분말에 대하여 1.5 중량%), 레시틴(트루 레시틴 고교(주) 제조 "SLP 화이트") 2.4 g(대두 단백 분말에 대하여 0.06 중량%)을 교반 혼합한 후, 대두 백교유 7.2 g(대두 단백 분말에 대하여 0.18 %)을 첨가하여 부형액을 제조하였다. 이어서, 유동층 건조기인 플로우 코터(오까와라 세이사꾸쇼(주) 제조) 내에서 대두 단백 분말을 풍압에 의해 유동시키면서 부형액을 대두 단백 분말에 대하여 분무하고, 이 덱스트린, 대두 백교유 및 레시틴을 대두 단백 분말에 부착시킴과 동시에 그에 따라 습윤된 분말을 가열 건조시켜 분말상 대두 단백 소재 3.8 kg을 얻었다.Then, 600 g of boiled water at 70 ° C. using a homo mixer, 60 g of dextrin having a DE value of 18 (" Sandek 185N " manufactured by Sanwa Denbun Co., Ltd.) (1.5 wt% based on soy protein powder), lecithin (true lecithin high school) 2.4 g (0.06 wt% based on soy protein powder) was prepared by stirring and mixing 2.4 g (0.18% based on soy protein powder). Subsequently, the excipient is sprayed on the soy protein powder while the soy protein powder is flowed by wind pressure in a flow coater (manufactured by Okawara Seisakusho Co., Ltd.), which is a fluidized bed dryer, and the dextrin, soybean white oil and lecithin are soybean. The wet powder was then dried by adhering to the protein powder to obtain 3.8 kg of powdered soy protein material.
<실시예 2, 비교예 1, 2, 3><Example 2, Comparative Examples 1, 2, 3>
실시예 1과 동일한 제조 방법으로 부형액 성분으로서 덱스트린만을 첨가한 것(실시예 2), 레시틴과 대두 백교유만을 첨가한 것(비교예 1), 아무것도 첨가하지 않은 끓인 물만 넣은 것(비교예 2)을 사용하여 각각 분말상 대두 단백 소재를 제조하였다. 또한, 대두 단백 분말에 부형액을 분무하는 대신에 대두 단백 분말에 실시예 2와 동일한 양의 덱스트린 분말을 단순히 혼합하기만한 것을 비교예 3으로 하였다.In the same manufacturing method as Example 1, only dextrin was added as an excipient component (Example 2), only lecithin and soy bean white oil were added (Comparative Example 1), and nothing but boiled water was added (Comparative Example 2). Powdered soy protein material was prepared using In addition, instead of spraying the excipients to the soy protein powder, Comparative Example 3 was to simply mix the same amount of dextrin powder to the soy protein powder as in Example 2.
이어서, 100 kg 규모의 용해 탱크에서 실시예 1, 2 및 비교예 1, 2에서 얻어진 분말상 대두 단백 소재 3 kg에 건조 난백 2 kg, 카제인 나트륨 1 kg, 식염 2kg, 설탕 3 kg, 조미료 2 kg 및 물(수온 5 ℃) 50 ℓ를 첨가하고, 저속으로 프로펠라 교반(회전수 300 rpm)하여 로스햄용 피클액 63 kg을 제조하였다.Then, in a 100 kg scale dissolution tank, 3 kg of powdered soy protein material obtained in Examples 1 and 2 and Comparative Examples 1 and 2, 2 kg of dry egg white, 1 kg of casein sodium, 2 kg of salt, 3 kg of sugar, 2 kg of seasoning and 50 L of water (water temperature 5 degreeC) was added, and 63 kg of pickles for Rosham were manufactured by propeller stirring at low speed (300 rpm).
각 분말상 대두 단백 소재의 수분산성, 분말 날림, 습윤성에 대하여 평가하였다. 수분산성에 대해서는 첨가시 덩어리 발생이 없고, 신속하게 분산되는 가의 여부를 관찰하였다(이후, 동일한 평가 방법으로 함). 분말 날림에 대해서는 첨가시 공중으로의 분말의 비산 상태를 관찰하였다. 습윤성에 대해서는 분말이 물에 튕겨 수면에 떠오르지 않고 신속하게 용해되는 가를 관찰하였다. 또한, 각 피클액을 사용하여 제조한 로스햄에 대하여 5명의 패널에 의해 햄의 경도, 색조, 풍미에 대하여 품질 평가를 행하였다(이후, 동일한 평가 방법으로 함). 그 결과를 하기 표 1에 기재하였다.The water dispersibility, powder blowing, and wettability of each powdery soy protein were evaluated. As for water dispersibility, it was observed that there was no lump at the time of addition and dispersed rapidly (the same evaluation method thereafter). For powder blowing, the scattering state of the powder into the air at the time of addition was observed. For wettability, it was observed whether the powder dissolves quickly and does not float on the water. In addition, quality evaluation of the hardness, color tone, and flavor of ham was carried out by five panelists about Rosham manufactured using each pickle liquid (hereinafter, the same evaluation method). The results are shown in Table 1 below.
실시예 1의 제품은 제조 규모에서의 약한 교반 상태에 있어서도 덩어리가 생기지 않고, 수분산성이 매우 우수하였다. 또한, 분말 날림에 대해서도 분말이 비산되지 않고 작업성이 우수하였다. 또한, 습윤성에 대해서도 분말이 튕기지 않고 신속하게 물에 침투하는 우수한 것이었다. 실시예 2는 실시예 1과 동일하게 수분산성은 양호하며, 분말 날림 억제 및 습윤성에 대해서도 실시예 1보다 약간 떨어지기는 하지만, 덱스트린의 분무 효과가 높아 품질상의 문제는 없었다. 비교예 1 및 비교예 2는 덱스트린 무첨가 때문에 수분산성이 나쁘고, 분말이 덩어리져서 매우 용해되기 어려운 상태가 되어 버렸다. 비교예 3은 단순히 분말을 혼합했을 뿐이기 때문에 모든 평가가 좋지 못하였다.The product of Example 1 did not produce agglomerates even in a weak stirring state at the production scale, and was excellent in water dispersibility. In addition, the powder was not scattered with respect to powder blowing, and the workability was excellent. In addition, the wettability was excellent in that the powder penetrated into the water quickly without splashing. Example 2 has good water dispersibility as in Example 1, and slightly lower than Example 1 in terms of powder blowing suppression and wettability, but the spray effect of dextrin is high and there is no quality problem. Comparative Examples 1 and 2 had poor water dispersibility due to no addition of dextrin, and the powder became agglomerated and very difficult to dissolve. In Comparative Example 3, all the evaluations were not good because only the powder was mixed.
<실시예 3><Example 3>
분말상 대두 단백 소재의 수분산성을 개선하는 덱스트린의 DE치의 최적치를 조사하였다.The optimum value of DE value of dextrin to improve water dispersibility of powdered soy protein material was investigated.
실시예 1과 동일하게 대두 단백 분말을 얻었다. 이어서, 실시예 1의 덱스트린을 각종 DE치(5 내지 30)를 갖는 덱스트린으로 치환하여 부형액을 분무하고, 마찬가지로 분말상 대두 단백 소재를 제조한 후, 피클액을 제조하여 로스햄을 제조하였다(테스트 No.1 내지 5). 각 피클액 제조시의 수분산성, 분무시의 부형액의 점성, 분말상 대두 단백 소재의 색조, 로스햄의 품질에 대하여 평가하였다. 부형액의 점성에 대해서는 부형액의 플로우 코터로의 송액 효율, 즉 유속의 안정성 유무나 유속의 저하 유무에 대하여 관찰하였다. 색조에 대해서는 분무 가열에 의해 분말상 대두 단백 소재의 열에 의한 갈변이 발생하였는 지의 여부를 관찰하였다. 결과를 하기 표 2에 기재하였다.Soy protein powder was obtained in the same manner as in Example 1. Subsequently, the dextrin of Example 1 was replaced with dextrin having various DE values (5 to 30) to spray the excipient solution, and similarly a powdered soy protein material was prepared, followed by pickle liquid to prepare Rosham (test). No. 1 to 5). The water dispersibility at the time of manufacturing each pickle liquid, the viscosity of the excipient liquid at the time of spraying, the color tone of the powdered soy protein material, and the quality of Rosham were evaluated. The viscosity of the excipient was observed for the efficiency of feeding the liquid to the flow coater, that is, whether the flow rate was stable or not. About the color tone, it was observed whether browning by heat of the powdery soy protein material occurred by spray heating. The results are shown in Table 2 below.
DE치가 지나치게 낮으면 No.1의 결과대로 약한 교반 상태에서의 수분에 대한 분산성이 저하되는 경향이 있고, 전분에 가까운 물성이 되기 때문에 부형액의 점도가 높아지며, 플로우 코터에서의 분무 속도가 늦어져 분무 효율이 저하됨과 동시에 가열 시간이 길어지기 때문에 가열 과다에 의한 NSI의 저하가 발생하고, 겔 형성성이 저하되는 경향이 있었다. 또한, No.1의 제품으로부터 햄의 제조에 사용하는 피클액을 제조했더니, 피클액의 점도가 높기 때문에 햄 제조의 작업성에 지장을 초래하였다. 반대로 DE치가 지나치게 높아지면 No.5의 결과대로 분말상 대두 단백 소재의 색조가 갈변되는 경향이 있었다. 그 원인은 불명확하지만, 플로우 코터 내에서의 가열에 의해 DE치가 낮은 덱스트린이 갈변을 일으켰을 가능성이 있다. No.2 내지 4의 평가는 양호하고, No.3의 평가는 가장 우수하였다.If the DE value is too low, the dispersibility with respect to moisture in a weakly stirred state tends to be lowered as a result of No. 1, and the viscosity of the excipient becomes high because it becomes a physical property close to starch, and the spray rate in the flow coater is slow. As a result, the spraying efficiency was lowered and the heating time was longer, so that the NSI was lowered due to excessive heating, and the gel formability tended to be lowered. Moreover, when pickle liquid used for manufacturing ham was produced from the product of No. 1, since the viscosity of pickle liquid was high, the workability of ham manufacture was impaired. On the contrary, when the DE value became too high, the color tone of the powdered soy protein material tended to brown as the result of No. 5. The cause is unclear, but there is a possibility that dextrin having a low DE value caused browning by heating in the flow coater. The evaluation of Nos. 2 to 4 was good, and the evaluation of No. 3 was the best.
<실시예 4><Example 4>
대두 단백의 수분산성을 개선하는 덱스트린의 최적 분무량을 조사하였다.The optimal spray amount of dextrin to improve the water dispersibility of soy protein was investigated.
실시예 1과 동일하게 대두 단백 분말을 얻었다. 또한, 실시예 1의 DE치 18의 덱스트린의 양을 바꾸어 첨가량으로서 8 g(대두 단백 분말에 대하여 0.2 중량%)인 것을 No.6, 28 g(대두 단백 분말에 대하여 0.7 중량%)인 것을 No.7, 60 g(대두 단백 분말에 대하여 1.5 중량%)인 것을 No.8, 72 g(대두 단백 분말에 대하여 1.8 중량%)인 것을 No.9, 140 g(대두 단백 분말에 대하여 3.5 중량%)인 것을 No.10으로서 각각 부형액을 분무하여 분말상 대두 단백 소재를 제조한 후, 피클액을 제조하여 로스햄을 제조하였다. 얻어진 각 제품에 대하여 피클액 제조시의 수분산성, 겔 형성성 및 로스햄의 풍미를 평가하였다. 또한, 겔 형성성에 대해서는 각 분말상 대두 단백 소재의 12 %(w/w) 용액을 가열하고, 냉각 후의 겔의 경도를 지표로 하였다.Soy protein powder was obtained in the same manner as in Example 1. Further, the amount of dextrin having a DE value of 18 in Example 1 was changed to 8 g (0.2 wt% based on soy protein powder) and 6, 28 g (0.7 wt% based on soy protein powder) as No. .7, 60 g (1.5 wt% based on soy protein powder) No.8, 72 g (1.8 wt% based on soy protein powder) No.9, 140 g (3.5 wt% based on soy protein powder) No. 10 was sprayed into the excipient solution to prepare a powdered soy protein material, and then pickle liquor was prepared to produce Rossham. About each obtained product, the water dispersibility, gel formation property, and the flavor of Rosham at the time of pickle liquid preparation were evaluated. In addition, about gel formation property, the 12% (w / w) solution of each powdery soybean protein material was heated, and the hardness of the gel after cooling was made into the index.
No.6의 결과대로 덱스트린의 분무량이 지나치게 적으면 덱스트린의 효과가 없어지고, 수분산성이 저하되는 경향이 있었다. 반대로 No.10의 결과대로 덱스트린이 지나치게 많으면 수분산성은 문제가 없지만, 단백 성분의 구성 비율이 상대적으로 저하되기 때문에 겔 형성성의 저하가 보였다. 결과적으로 No.6과 10은 모두 총평으로서 보통 이상이었지만, No.7 내지 9의 평가가 높고, 특히 No.8이 우수하였다.As a result of No. 6, when the spray amount of dextrin was too small, the effect of dextrin was lost and there existed a tendency for water dispersibility to fall. On the contrary, if there is too much dextrin as a result of No. 10, there is no problem in water dispersibility, but since the composition ratio of the protein component is relatively reduced, the gel formation property was seen to fall. As a result, although No. 6 and 10 were more than ordinary as a general evaluation, evaluation of No. 7-9 was high, especially No. 8 was excellent.
이상 설명한 바와 같이 본원 발명의 제조 방법에 의해 얻어진 분말상 대두단백 소재는 제조 규모에 있어서 강력한 교반 장치없이 약한 교반하에서도 냉수로 쉽게 분산시키는 효과, 높은 겔 형성성을 발휘하는 효과를 가지며, 다양한 제조 환경에 대응할 수 있는 것이다. 이러한 분말상 대두 단백 소재는 이들 특성을 살린 식품(예를 들면 축육 제품, 수산 가공 제품, 분말 음료, 액체 음료, 프라이 조리 식품의 옷, 교자류의 피 등) 등으로의 이용이 바람직하며, 햄 제조에 사용되는 피클액으로의 사용은 가장 바람직한 이용 양태 중 하나이다.As described above, the powdered soybean protein material obtained by the production method of the present invention has the effect of easily dispersing with cold water even under mild stirring in a production scale and exhibiting high gel formability in various production environments. It can respond to. Such powdered soy protein material is preferably used for foods utilizing these characteristics (e.g. meat products, fish processed products, powdered drinks, liquid drinks, clothes of fried foods, blood of gyoza, etc.), and ham production. Use as a pickle liquid for use is one of the most preferred modes of use.
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JP2005287506A (en) * | 2004-03-08 | 2005-10-20 | Fuji Oil Co Ltd | Powdery composition for protein-containing acid food and drink |
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CN101522047B (en) * | 2006-11-27 | 2012-07-18 | 不二制油株式会社 | Antiswelling agent for starch food |
US8124157B2 (en) | 2006-12-14 | 2012-02-28 | Fuji Oil Company, Limited | Noodles and noodle skins comprising soybean protein composition and the method of making same |
JP5190738B2 (en) | 2007-02-01 | 2013-04-24 | ハウス食品株式会社 | Soy mixed powder |
MY156854A (en) * | 2007-12-27 | 2016-04-15 | Fuji Oil Holdings Inc | Novel soybean protein material and method for producing the same |
CN102639002B (en) * | 2010-02-03 | 2013-10-02 | 不二制油株式会社 | Powdery soybean protein material |
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CN103262941B (en) * | 2013-05-14 | 2014-07-02 | 华南理工大学 | Isoflavone aglycone-enriched soybean protein and preparation method thereof |
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