CN115245193B - Method for producing corn whole meal by cooperation of bacterial enzymes - Google Patents
Method for producing corn whole meal by cooperation of bacterial enzymes Download PDFInfo
- Publication number
- CN115245193B CN115245193B CN202210013195.8A CN202210013195A CN115245193B CN 115245193 B CN115245193 B CN 115245193B CN 202210013195 A CN202210013195 A CN 202210013195A CN 115245193 B CN115245193 B CN 115245193B
- Authority
- CN
- China
- Prior art keywords
- fermentation
- corn
- corn flour
- starch
- whole
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 240000008042 Zea mays Species 0.000 title claims abstract description 155
- 235000002017 Zea mays subsp mays Nutrition 0.000 title claims abstract description 155
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 title claims abstract description 154
- 235000005822 corn Nutrition 0.000 title claims abstract description 154
- 102000004190 Enzymes Human genes 0.000 title claims abstract description 32
- 108090000790 Enzymes Proteins 0.000 title claims abstract description 32
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 230000001580 bacterial effect Effects 0.000 title claims abstract description 16
- 235000012054 meals Nutrition 0.000 title claims 3
- 235000013312 flour Nutrition 0.000 claims abstract description 95
- 238000001125 extrusion Methods 0.000 claims abstract description 16
- 238000002360 preparation method Methods 0.000 claims abstract description 16
- 239000000843 powder Substances 0.000 claims abstract description 10
- 239000002994 raw material Substances 0.000 claims abstract description 9
- 241000186660 Lactobacillus Species 0.000 claims abstract description 5
- 229940039696 lactobacillus Drugs 0.000 claims abstract description 5
- 238000000855 fermentation Methods 0.000 claims description 127
- 230000004151 fermentation Effects 0.000 claims description 103
- 229940088598 enzyme Drugs 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 27
- 239000007788 liquid Substances 0.000 claims description 25
- 238000000034 method Methods 0.000 claims description 23
- 239000007787 solid Substances 0.000 claims description 22
- 230000001007 puffing effect Effects 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 15
- 108010059892 Cellulase Proteins 0.000 claims description 14
- 229940106157 cellulase Drugs 0.000 claims description 14
- 238000005406 washing Methods 0.000 claims description 10
- 238000001035 drying Methods 0.000 claims description 7
- 238000007670 refining Methods 0.000 claims description 7
- 230000002195 synergetic effect Effects 0.000 claims description 7
- 230000018044 dehydration Effects 0.000 claims description 6
- 238000006297 dehydration reaction Methods 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 6
- 229940059442 hemicellulase Drugs 0.000 claims description 5
- 108010002430 hemicellulase Proteins 0.000 claims description 5
- 239000007921 spray Substances 0.000 claims description 5
- 235000013339 cereals Nutrition 0.000 claims description 3
- 238000004537 pulping Methods 0.000 claims description 3
- 238000001704 evaporation Methods 0.000 claims description 2
- 230000008020 evaporation Effects 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- 239000011343 solid material Substances 0.000 claims description 2
- 239000002054 inoculum Substances 0.000 claims 1
- 238000003801 milling Methods 0.000 claims 1
- 229920002472 Starch Polymers 0.000 abstract description 29
- 235000019698 starch Nutrition 0.000 abstract description 29
- 239000008107 starch Substances 0.000 abstract description 29
- 235000018102 proteins Nutrition 0.000 abstract description 11
- 102000004169 proteins and genes Human genes 0.000 abstract description 11
- 108090000623 proteins and genes Proteins 0.000 abstract description 11
- 235000013305 food Nutrition 0.000 abstract description 10
- 238000012545 processing Methods 0.000 abstract description 10
- 239000000835 fiber Substances 0.000 abstract description 7
- 235000016709 nutrition Nutrition 0.000 abstract description 5
- 108010068370 Glutens Proteins 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract description 3
- 235000021312 gluten Nutrition 0.000 abstract 1
- 238000002513 implantation Methods 0.000 abstract 1
- 239000004615 ingredient Substances 0.000 abstract 1
- 238000005215 recombination Methods 0.000 abstract 1
- 230000006798 recombination Effects 0.000 abstract 1
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 74
- 241000894006 Bacteria Species 0.000 description 42
- 235000014655 lactic acid Nutrition 0.000 description 37
- 239000004310 lactic acid Substances 0.000 description 37
- 238000000265 homogenisation Methods 0.000 description 20
- 229920000856 Amylose Polymers 0.000 description 15
- 229920000294 Resistant starch Polymers 0.000 description 11
- 235000021254 resistant starch Nutrition 0.000 description 11
- 230000008569 process Effects 0.000 description 10
- 238000012360 testing method Methods 0.000 description 10
- 229920000945 Amylopectin Polymers 0.000 description 9
- 241000196324 Embryophyta Species 0.000 description 9
- 238000004140 cleaning Methods 0.000 description 9
- 235000019629 palatability Nutrition 0.000 description 9
- 229920002678 cellulose Polymers 0.000 description 7
- 239000001913 cellulose Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- 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 6
- 239000008280 blood Substances 0.000 description 6
- 210000004369 blood Anatomy 0.000 description 6
- 239000008103 glucose Substances 0.000 description 6
- 238000000227 grinding Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 239000006872 mrs medium Substances 0.000 description 6
- 235000015097 nutrients Nutrition 0.000 description 6
- 240000006024 Lactobacillus plantarum Species 0.000 description 5
- 235000013965 Lactobacillus plantarum Nutrition 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 230000002641 glycemic effect Effects 0.000 description 5
- 229940072205 lactobacillus plantarum Drugs 0.000 description 5
- 108090000344 1,4-alpha-Glucan Branching Enzyme Proteins 0.000 description 4
- 102000003925 1,4-alpha-Glucan Branching Enzyme Human genes 0.000 description 4
- 241000699670 Mus sp. Species 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 4
- 108090000637 alpha-Amylases Proteins 0.000 description 4
- 238000011081 inoculation Methods 0.000 description 4
- 230000000813 microbial effect Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 208000001072 type 2 diabetes mellitus Diseases 0.000 description 4
- 229920002261 Corn starch Polymers 0.000 description 3
- 206010022489 Insulin Resistance Diseases 0.000 description 3
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 3
- 241000209140 Triticum Species 0.000 description 3
- 235000021307 Triticum Nutrition 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000008120 corn starch Substances 0.000 description 3
- 229940079919 digestives enzyme preparation Drugs 0.000 description 3
- 235000019197 fats Nutrition 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 229920002521 macromolecule Polymers 0.000 description 3
- 239000002609 medium Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- GVJHHUAWPYXKBD-UHFFFAOYSA-N (±)-α-Tocopherol Chemical compound OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-UHFFFAOYSA-N 0.000 description 2
- 102000002322 Egg Proteins Human genes 0.000 description 2
- 108010000912 Egg Proteins Proteins 0.000 description 2
- 229920001503 Glucan Polymers 0.000 description 2
- 208000008589 Obesity Diseases 0.000 description 2
- 108091005804 Peptidases Proteins 0.000 description 2
- 239000004365 Protease Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 235000010980 cellulose Nutrition 0.000 description 2
- 210000001072 colon Anatomy 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 235000013325 dietary fiber Nutrition 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 230000037406 food intake Effects 0.000 description 2
- 239000001963 growth medium Substances 0.000 description 2
- 239000010903 husk Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 230000035764 nutrition Effects 0.000 description 2
- 235000020824 obesity Nutrition 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- 239000000523 sample Substances 0.000 description 2
- 230000001953 sensory effect Effects 0.000 description 2
- OWEGMIWEEQEYGQ-UHFFFAOYSA-N 100676-05-9 Natural products OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(OC2C(OC(O)C(O)C2O)CO)O1 OWEGMIWEEQEYGQ-UHFFFAOYSA-N 0.000 description 1
- 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
- 239000004382 Amylase Substances 0.000 description 1
- 108010065511 Amylases Proteins 0.000 description 1
- 102000013142 Amylases Human genes 0.000 description 1
- 229920001685 Amylomaize Polymers 0.000 description 1
- 244000025254 Cannabis sativa Species 0.000 description 1
- 108010084185 Cellulases Proteins 0.000 description 1
- 102000005575 Cellulases Human genes 0.000 description 1
- 206010009944 Colon cancer Diseases 0.000 description 1
- 208000001333 Colorectal Neoplasms Diseases 0.000 description 1
- 102000051366 Glycosyltransferases Human genes 0.000 description 1
- 108700023372 Glycosyltransferases Proteins 0.000 description 1
- 238000007696 Kjeldahl method Methods 0.000 description 1
- GUBGYTABKSRVRQ-PICCSMPSSA-N Maltose Natural products O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 description 1
- 208000001132 Osteoporosis Diseases 0.000 description 1
- 108090000284 Pepsin A Proteins 0.000 description 1
- 102000057297 Pepsin A Human genes 0.000 description 1
- 102000035195 Peptidases Human genes 0.000 description 1
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 1
- 238000000944 Soxhlet extraction Methods 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 102000004357 Transferases Human genes 0.000 description 1
- 108090000992 Transferases Proteins 0.000 description 1
- 229930003270 Vitamin B Natural products 0.000 description 1
- 229930003427 Vitamin E Natural products 0.000 description 1
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 description 1
- 238000005903 acid hydrolysis reaction Methods 0.000 description 1
- 230000006518 acidic stress Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 235000019418 amylase Nutrition 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000008429 bread Nutrition 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 206010012601 diabetes mellitus Diseases 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 235000014103 egg white Nutrition 0.000 description 1
- 210000000969 egg white Anatomy 0.000 description 1
- 210000002969 egg yolk Anatomy 0.000 description 1
- 235000013345 egg yolk Nutrition 0.000 description 1
- 235000013601 eggs Nutrition 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000012041 food component Nutrition 0.000 description 1
- 235000012631 food intake Nutrition 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- WIGCFUFOHFEKBI-UHFFFAOYSA-N gamma-tocopherol Natural products CC(C)CCCC(C)CCCC(C)CCCC1CCC2C(C)C(O)C(C)C(C)C2O1 WIGCFUFOHFEKBI-UHFFFAOYSA-N 0.000 description 1
- 108010061330 glucan 1,4-alpha-maltohydrolase Proteins 0.000 description 1
- 108700014210 glycosyltransferase activity proteins Proteins 0.000 description 1
- 230000007407 health benefit Effects 0.000 description 1
- 208000019622 heart disease Diseases 0.000 description 1
- 238000000338 in vitro Methods 0.000 description 1
- 239000003262 industrial enzyme Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000007413 intestinal health Effects 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 150000002605 large molecules Chemical class 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 238000009630 liquid culture Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 235000009973 maize Nutrition 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000021049 nutrient content Nutrition 0.000 description 1
- 229940111202 pepsin Drugs 0.000 description 1
- 230000001766 physiological effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000001243 protein synthesis Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000036186 satiety Effects 0.000 description 1
- 235000019627 satiety Nutrition 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 210000000813 small intestine Anatomy 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000035882 stress Effects 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000014616 translation Effects 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 235000019156 vitamin B Nutrition 0.000 description 1
- 239000011720 vitamin B Substances 0.000 description 1
- 235000019165 vitamin E Nutrition 0.000 description 1
- 229940046009 vitamin E Drugs 0.000 description 1
- 239000011709 vitamin E Substances 0.000 description 1
- 235000012794 white bread Nutrition 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
- A23L7/10—Cereal-derived products
- A23L7/104—Fermentation of farinaceous cereal or cereal material; Addition of enzymes or microorganisms
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/20—Reducing nutritive value; Dietetic products with reduced nutritive value
- A23L33/21—Addition of substantially indigestible substances, e.g. dietary fibres
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
- A23L7/10—Cereal-derived products
- A23L7/161—Puffed cereals, e.g. popcorn or puffed rice
- A23L7/165—Preparation of puffed cereals involving preparation of meal or dough as an intermediate step
- A23L7/17—Preparation of puffed cereals involving preparation of meal or dough as an intermediate step by extrusion
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
- A23L7/10—Cereal-derived products
- A23L7/161—Puffed cereals, e.g. popcorn or puffed rice
- A23L7/191—After-treatment of puffed cereals, e.g. coating or salting
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Mycology (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Cereal-Derived Products (AREA)
Abstract
Description
技术领域Technical Field
本发明涉及食品加工技术领域,特别是涉及一种菌酶协同生产玉米全粉的方法。The invention relates to the technical field of food processing, in particular to a method for producing whole corn flour in a bacterial and enzyme-assisted manner.
背景技术Background technique
玉米为一年生禾本科植物,又名苞谷、玉蜀黍、棒子等,是重要的粮食作物和重要的饲料来源,也是全世界总产量最高的粮食作物,而且营养丰富。干玉米籽粒中含有蛋白、脂肪、淀粉,还含有丰富的膳食纤维、维生素B、维生素E,以及人体所必需的微量元素。玉米因其丰富的营养成分及浓郁香味广受消费者青睐,拥有较大市场。Corn is an annual grass plant, also known as corn, maize, and corn. It is an important food crop and an important source of feed. It is also the food crop with the highest total output in the world and is rich in nutrition. Dry corn kernels contain protein, fat, starch, as well as rich dietary fiber, vitamin B, vitamin E, and trace elements necessary for the human body. Corn is widely favored by consumers for its rich nutrients and strong aroma, and has a large market.
虽然玉米作为粗粮具有诸多优点,日益受到追捧,但是受其自身特性的限制,无法赋予玉米粉面团优良的加工特性:由于玉米蛋白中缺少面筋蛋白,因此由玉米粉直接制成的面团无法形成网状结构,得到的玉米面团的可塑性较差;另外,玉米粉中的淀粉与蛋白质之间包裹过于紧密,淀粉得不到较好的吸水膨胀,因此玉米面团的黏弹性较差;这也造成了玉米粉的食用口感粗糙,这在很大程度上限制了玉米粉在主食加工方面的应用。Although corn has many advantages as a coarse grain and is increasingly sought after, it is limited by its own characteristics and cannot give corn flour dough excellent processing characteristics: due to the lack of gluten protein in corn protein, the dough made directly from corn flour cannot form a network structure, and the resulting corn dough has poor plasticity; in addition, the starch and protein in corn flour are wrapped too tightly, and the starch cannot absorb water and expand well, so the viscoelasticity of the corn dough is poor; this also makes the corn flour have a rough taste, which greatly limits the application of corn flour in staple food processing.
而且,目前玉米面粉的主要的加工方式是将成熟玉米籽粒干法脱皮脱胚后进行干法粉碎得到的粮食初级加工产品玉米粉,或者将玉米脱皮脱胚脱除角质、只保留淀粉部分磨制较细的玉米面粉。但由于这些方法中均采用剥皮和脱胚等前处理工序,工艺繁琐、原料浪费,并且制得产品存在粘弹性低、口感粗硬、适口性较差等问题。Moreover, the main processing method of corn flour at present is to dry-peel and degerminate mature corn kernels and then dry-grind them to obtain corn flour, a primary processed product of grain, or to peel and degerminate corn kernels, remove hornyness, and only retain the starch part to grind finer corn flour. However, since these methods all use pre-treatment processes such as peeling and degerming, the process is cumbersome, the raw materials are wasted, and the obtained products have problems such as low viscoelasticity, rough taste, and poor palatability.
发明内容Summary of the invention
本发明的目的是提供一种菌酶协同生产玉米全粉的方法,以解决上述现有技术存在的问题,本发明主要针对玉米粉不含面筋蛋白,且淀粉包裹蛋白质过于紧密,所制产品存在粘弹性、延展性、持水性差等问题,通过酶制剂和乳酸菌的植入结合挤压膨化技术,并以未经过脱皮脱胚的玉米全籽粒为原料,实现了玉米中淀粉、蛋白、纤维的质构重组,保持了玉米全部营养成分,赋予玉米粉优质的质构特性。The purpose of the present invention is to provide a method for producing whole corn flour by using bacteria and enzymes to solve the problems existing in the above-mentioned prior art. The present invention mainly aims at the problems that corn flour does not contain gluten protein, starch wraps protein too tightly, and the prepared product has poor viscoelasticity, ductility, and water holding capacity. By implanting enzyme preparations and lactic acid bacteria in combination with extrusion puffing technology, and using whole corn kernels that have not been peeled or degermed as raw materials, the texture reconstruction of starch, protein, and fiber in corn is achieved, all the nutrients of corn are maintained, and the corn flour is endowed with high-quality texture characteristics.
为实现上述目的,本发明提供了如下方案:To achieve the above object, the present invention provides the following solutions:
本发明提供一种菌酶协同生产玉米全粉的方法,包括以下步骤:The present invention provides a method for producing whole corn flour by bacterial enzyme synergism, comprising the following steps:
以玉米全籽粒为原料,经挤压膨化后破碎、厌氧发酵、洗涤、磨浆、均质、脱水干燥,得到所述玉米全粉。The whole corn kernels are used as raw materials, and the whole corn flour is obtained by extruding and puffing, crushing, anaerobic fermentation, washing, grinding, homogenization, dehydration and drying.
进一步地,所述挤压膨化的条件为:含水量16-24wt%,温度100-180℃,螺杆转速为324-486r/min,物料投速162-378r/min。Furthermore, the extrusion puffing conditions are: water content 16-24wt%, temperature 100-180°C, screw speed 324-486r/min, material feeding speed 162-378r/min.
挤压膨化过程中,将玉米粉进行对辊儿挤压,通过腔体内部的高温高压环境让玉米粉发生膨胀,使玉米粉变成无数细致多孔的海绵体,比表面积增加,玉米粉孔径增大,这样使得乳酸菌与玉米粉发酵的作用面积增大,乳酸菌群量产生加快,缩短到达发酵pH要求的时间,膨化过程中粉体表面形成的微孔结构也有利于营养物质的流出,促进了乳酸菌的产菌速率。由于玉米淀粉含量比例高,在60%左右,并且淀粉是大分子,包裹在淀粉的维生素,矿物质很难全部释放出来,使制得的玉米口感较差,营养成分释放不出来,营养价值很低。通过挤压膨化对玉米粉进行预处理,使得淀粉与包裹在其周围的各种物质进行分离,同时,高温高压的环境也对玉米粉起到了杀菌的作用,这为下一步减少发酵时间,避免杂菌的产生几率提供了保障,提升了玉米全粉的营养价值。During the extrusion and puffing process, the corn flour is extruded by rollers, and the high temperature and high pressure environment inside the cavity makes the corn flour expand, turning the corn flour into countless fine and porous sponges, increasing the specific surface area and the pore size of the corn flour. This increases the fermentation area of lactic acid bacteria and corn flour, accelerates the production of lactic acid bacteria, and shortens the time to reach the pH requirement of fermentation. The microporous structure formed on the surface of the powder during the puffing process is also conducive to the outflow of nutrients and promotes the production rate of lactic acid bacteria. Due to the high proportion of corn starch content, about 60%, and starch is a large molecule, it is difficult to release all the vitamins and minerals wrapped in starch, so that the prepared corn has a poor taste, the nutrients cannot be released, and the nutritional value is very low. The corn flour is pretreated by extrusion and puffing, so that the starch is separated from the various substances wrapped around it. At the same time, the high temperature and high pressure environment also has a sterilizing effect on the corn flour, which provides a guarantee for reducing the fermentation time and avoiding the probability of the production of miscellaneous bacteria in the next step, and improves the nutritional value of the whole corn flour.
同时,挤压膨化也保证了玉米全籽粒在不脱皮脱胚脱角质的情况下,经后续发酵处理和磨浆工艺后得到的玉米全粉的适口性和可加工性,同时由于未经脱皮脱胚脱角质处理,使得纤维素利用率得以提升。挤压膨化的物料含水量、套筒温度、螺杆转速、物料投速对玉米粉糊化度、吸水性指数、水溶性指数质构特性、流变特性以及保留玉米片中的纤维不受损失等都有较大影响,膨化温度过高,或者含水量过低,都会使纤维在膨化过程中分解流失,从而影响玉米粉中纤维利用率,膨化温度过低则不能对玉米皮起到较好的软化作用,从而影响后续步骤,进而影响玉米粉的适口性和可加工性。At the same time, extrusion puffing also ensures the palatability and processability of the whole corn flour obtained after subsequent fermentation and pulping process without peeling, germining and horny removal of whole corn kernels. At the same time, due to the lack of peeling, germining and horny removal, the cellulose utilization rate is improved. The moisture content of the extruded material, the sleeve temperature, the screw speed, and the material feeding speed have a great influence on the gelatinization degree, water absorption index, water solubility index texture characteristics, rheological properties, and the retention of fiber in corn flakes. If the puffing temperature is too high or the moisture content is too low, the fiber will be decomposed and lost during the puffing process, thereby affecting the fiber utilization rate in the corn flour. If the puffing temperature is too low, the corn husk cannot be softened well, thereby affecting the subsequent steps, and then affecting the palatability and processability of the corn flour.
进一步地,所述破碎为将挤压膨化后的玉米粉破碎至60-100目;Furthermore, the crushing is to crush the extruded and puffed corn flour into 60-100 meshes;
所述厌氧发酵包括以下步骤:经破碎后的物料按照接种量0.01-0.02%接种乳酸菌后进行厌氧发酵,发酵温度为36-38℃,发酵时间为14-16h。优选的,发酵结束时,发酵液pH值为4-5。The anaerobic fermentation comprises the following steps: the crushed material is inoculated with lactic acid bacteria at an inoculation rate of 0.01-0.02%, and then anaerobic fermentation is performed at a fermentation temperature of 36-38°C and a fermentation time of 14-16 hours. Preferably, at the end of the fermentation, the pH value of the fermentation liquid is 4-5.
利用微生物发酵的方法可以提高玉米粉的适口性和加工特性。乳酸菌发酵是利用菌种对玉米粉进行发酵,这些微生物中含有丰富的酶系,这些酶的联合作用能够破坏淀粉、纤维素和蛋白质等大分子物质的紧密结构,改变玉米粉中淀粉、蛋白质、纤维素等大分子物质的结构,改变玉米粉的组成。经发酵后玉米粉中的淀粉含量有所提升,其它相对含量有所降低(以粗纤维和灰分为主),蛋白质含量的降低说明了微生物破坏了包裹在淀粉周围的蛋白质分子,纯化了淀粉分子。并且发酵玉米中直链淀粉含量增加,乳酸菌的发酵作用使得部分支链淀粉的侧链水解,因而以支链淀粉为主的大分子淀粉区平均分子量变小,而以直链淀粉为主的小分子淀粉区平均分子量变大,支链淀粉的相对含量降低。此外发酵改性玉米粉,使玉米蛋白Zein的结构趋于稳定,这也增加了玉米面团的稳定性。外源的添加酶系,如蛋白酶和纤维素酶等,能够更加有效的改善玉米粉的性质。最终,发酵玉米粉表现为较好的韧性和黏度,从而改善了其加工性能,如适口性、耐咀嚼以及拉伸性能等。The palatability and processing characteristics of corn flour can be improved by using microbial fermentation. Lactic acid bacteria fermentation is to ferment corn flour with bacteria. These microorganisms contain rich enzyme systems. The combined action of these enzymes can destroy the tight structure of macromolecular substances such as starch, cellulose and protein, change the structure of macromolecular substances such as starch, protein, cellulose and so on in corn flour, and change the composition of corn flour. After fermentation, the starch content in corn flour has increased, and the relative content of other substances has decreased (mainly crude fiber and ash). The decrease in protein content indicates that microorganisms have destroyed the protein molecules wrapped around starch and purified the starch molecules. In addition, the content of amylose in fermented corn increases, and the fermentation of lactic acid bacteria hydrolyzes the side chains of some amylopectin. Therefore, the average molecular weight of the macromolecular starch region dominated by amylopectin decreases, while the average molecular weight of the small molecular starch region dominated by amylose increases, and the relative content of amylopectin decreases. In addition, fermentation and modification of corn flour stabilizes the structure of corn protein Zein, which also increases the stability of corn dough. Exogenous addition of enzyme systems, such as proteases and cellulases, can more effectively improve the properties of corn flour. Finally, fermented corn flour exhibited better toughness and viscosity, thereby improving its processing properties, such as palatability, chewiness, and tensile properties.
进一步地,所述洗涤包括:将厌氧发酵产物经固液分离后,使用高压喷雾水对固体物料进行洗涤至pH值至6.8~7.2。Furthermore, the washing comprises: after solid-liquid separation of the anaerobic fermentation product, washing the solid material with high-pressure spray water until the pH value reaches 6.8 to 7.2.
进一步地,所述磨浆包括:将经过洗涤的固体发酵粉料和水混合得到磨浆料,磨浆料同时进行锉磨和齿磨至固体发酵粉料粒径为120-140目,水和固体发酵粉料的质量比为(2-4):1。Furthermore, the refining comprises: mixing the washed solid fermentation powder and water to obtain a refining material, and simultaneously filing and grinding the refining material until the particle size of the solid fermentation powder is 120-140 meshes, and the mass ratio of water to solid fermentation powder is (2-4):1.
对经过乳酸菌发酵后的固体发酵粉料进行锉磨和齿磨混合处理,锉磨时间长、耗能多,二者结合能够减少磨浆次数,节省能源。The solid fermented powder after lactic acid bacteria fermentation is subjected to a mixed treatment of filing and tooth grinding. Filing takes a long time and consumes a lot of energy. The combination of the two can reduce the number of grinding times and save energy.
进一步地,所述均质压力为15~20Mpa,3~5min/次,均质3-8次;所述脱水干燥采用过滤后闪蒸。Furthermore, the homogenization pressure is 15-20 MPa, 3-5 min/time, and the homogenization is 3-8 times; the dehydration and drying adopts flash evaporation after filtration.
进一步地,所述厌氧发酵过程中加入酶制剂。Furthermore, an enzyme preparation is added during the anaerobic fermentation process.
进一步地,所述酶制剂的加入时间为发酵终止前110-130min;所述酶制剂为纤维素酶和/或半纤维素酶。Furthermore, the enzyme preparation is added 110-130 minutes before the end of fermentation; and the enzyme preparation is cellulase and/or hemicellulase.
尽管乳酸菌发酵能够改善玉米粉结构,使制得的玉米粉的加工性能和适口性得到改善,但是单纯的乳酸菌发酵不能充分降解玉米中的淀粉和纤维素等物质,加之本发明在进行发酵前未对玉米皮进行去除,从而导致乳酸菌发酵对玉米粉的加工性能和适口性改善效果有限,经过单纯乳酸菌发酵后的玉米粉仍然不能达到和小麦粉相媲美的弹性、韧性、成团性和咀嚼性。因此,在本发明的技术方案中,在乳酸菌厌氧发酵后期加入了酶制剂,一方面酶制剂能够对乳酸菌不能充分分解的淀粉和纤维素进行进一步的降解处理,提升发酵玉米粉的性能,另一方面,酶制剂对纤维素等的降解又为乳酸菌提供了新的发酵底物,使乳酸菌在厌氧发酵后期的发酵活性增强,二者产生协同作用,使乳酸菌的厌氧发酵效率得以显著提升,从而克服现有技术中使用单一的乳酸菌得到的玉米粉无法媲美小麦粉的技术问题。酶制剂的加入时间同样是基于促使二者发挥最大的协同效果而进行的考虑,酶制剂加入的时间过早,则过早的参与玉米的发酵降解过程,对于发酵后期难降解的物质作用力不足,同时和乳酸菌的协同效果也显著减弱,酶制剂加入的时间过晚,则酶制剂和乳酸菌之间协同效果的发挥空间较小,不利于发酵效率的提升。Although lactic acid bacteria fermentation can improve the structure of corn flour, so that the processing performance and palatability of the obtained corn flour are improved, simple lactic acid bacteria fermentation cannot fully degrade substances such as starch and cellulose in corn, and the present invention does not remove corn husk before fermentation, which leads to limited improvement of processing performance and palatability of corn flour by lactic acid bacteria fermentation, and corn flour after simple lactic acid bacteria fermentation still cannot achieve elasticity, toughness, agglomeration and chewiness comparable to wheat flour. Therefore, in the technical scheme of the present invention, an enzyme preparation is added in the late stage of lactic acid bacteria anaerobic fermentation. On the one hand, the enzyme preparation can further degrade starch and cellulose that lactic acid bacteria cannot fully decompose, thereby improving the performance of fermented corn flour. On the other hand, the degradation of cellulose by the enzyme preparation provides new fermentation substrates for lactic acid bacteria, so that the fermentation activity of lactic acid bacteria in the late stage of anaerobic fermentation is enhanced, and the two produce a synergistic effect, so that the anaerobic fermentation efficiency of lactic acid bacteria is significantly improved, thereby overcoming the technical problem that corn flour obtained by using a single lactic acid bacteria in the prior art cannot be comparable to wheat flour. The time of adding the enzyme preparation is also based on the consideration of promoting the maximum synergistic effect between the two. If the enzyme preparation is added too early, it will participate in the fermentation and degradation process of corn too early, and will not have enough effect on the difficult-to-degrade substances in the later stage of fermentation. At the same time, the synergistic effect with lactic acid bacteria will be significantly weakened. If the enzyme preparation is added too late, the synergistic effect between the enzyme preparation and lactic acid bacteria will have little room to play, which is not conducive to improving the fermentation efficiency.
同时,乳酸菌发酵时间较长且较难控制,目前现有技术中至少需要发酵24h,如何采用有效的手段控制发酵过程缩短发酵时间,是实现工业规模生产玉米全粉的关键。本发明在发酵过程中加入酶制剂,使二者产生协同作用,提高了发酵效率,缩短了发酵时间,提高了发酵终止pH,避免了pH过低所引起的风味不佳的问题。At the same time, the lactic acid bacteria fermentation time is long and difficult to control. At present, the prior art requires at least 24 hours of fermentation. How to use effective means to control the fermentation process and shorten the fermentation time is the key to achieving industrial-scale production of whole corn flour. The present invention adds enzyme preparations during the fermentation process, so that the two produce a synergistic effect, improve the fermentation efficiency, shorten the fermentation time, increase the fermentation termination pH, and avoid the problem of poor flavor caused by too low pH.
本发明还提供一种上述的菌酶协同生产玉米全粉的方法生产得到的玉米全粉。The present invention also provides whole corn flour produced by the method for producing whole corn flour by cooperating with bacteria and enzymes.
本发明还提供一种上述的玉米全粉加工的产品,所述产品用于控制糖尿病或肥胖。The present invention also provides a product processed from the whole corn flour, which is used for controlling diabetes or obesity.
玉米淀粉由两种葡萄糖聚合物—直链淀粉和支链淀粉组成,其中直链淀粉含量约25%左右。直链淀粉与支链淀粉的比例对于玉米淀粉健康益处和最终质量具有决定性影响。高直链淀粉中抗性淀粉含量更高。抗性淀粉是在小肠中不能被消化吸收,但进食2小时后可到达结肠并被结肠中的微生物菌群发酵,继而发挥有益的生理作用的淀粉,被视为膳食纤维的组成成分之一。抗性淀粉在促进肠健康状况以及预防结肠直肠癌、Ⅱ型糖尿病、肥胖、心脏病以及骨质疏松症等疾病中具有重要作用,并且抗性淀粉可以增加饱腹感而减少食物摄入,对于肥胖人群具有重要作用。大部分经过加工的含淀粉的食物中均含有少量抗性淀粉,但一般使用常规小麦粉或玉米粉的食物如面包中抗性淀粉的含量小于1%,通过本发明处理之后,玉米全粉中直链淀粉含量可达到约48-73%,抗性淀粉含量可达到约33-65%,具有有效控制体重的生理功效。Corn starch is composed of two glucose polymers, amylose and amylopectin, of which the amylose content is about 25%. The ratio of amylose to amylopectin has a decisive influence on the health benefits and final quality of corn starch. The resistant starch content is higher in high-amylose starch. Resistant starch is a starch that cannot be digested and absorbed in the small intestine, but can reach the colon and be fermented by the microbial flora in the colon 2 hours after eating, and then play a beneficial physiological role. It is regarded as one of the components of dietary fiber. Resistant starch plays an important role in promoting intestinal health and preventing diseases such as colorectal cancer, type 2 diabetes, obesity, heart disease and osteoporosis. In addition, resistant starch can increase satiety and reduce food intake, which is important for obese people. Most processed starch-containing foods contain a small amount of resistant starch, but the content of resistant starch in foods such as bread that generally use conventional wheat flour or corn flour is less than 1%. After being processed by the present invention, the amylose content in whole corn flour can reach about 48-73%, and the resistant starch content can reach about 33-65%, which has the physiological effect of effectively controlling weight.
本发明公开了以下技术效果:The present invention discloses the following technical effects:
本发明的生产方法通过植入酶制剂和乳酸菌,改良玉米粉的加工特性和适口性,并且应用挤压膨化技术,对玉米粉进行预处理,大大缩短了微生物发酵的时间,减少了发酵过程中杂菌产生的几率,提高了工业生产效率;通过挤压膨化和微生物发酵相结合可以保留玉米全粉中的全部营养物质,面粉的加工性能好,营养丰富。The production method of the invention improves the processing characteristics and palatability of corn flour by implanting enzyme preparations and lactic acid bacteria, and pretreats the corn flour by applying extrusion puffing technology, thereby greatly shortening the time of microbial fermentation, reducing the probability of miscellaneous bacteria generation during the fermentation process, and improving industrial production efficiency; all nutrients in the whole corn flour can be retained by combining extrusion puffing with microbial fermentation, and the flour has good processing performance and rich nutrition.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required for use in the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying creative work.
图1为发酵过程pH变化对比图。Figure 1 is a comparison chart of pH changes during the fermentation process.
具体实施方式Detailed ways
现详细说明本发明的多种示例性实施方式,该详细说明不应认为是对本发明的限制,而应理解为是对本发明的某些方面、特性和实施方案的更详细的描述。Various exemplary embodiments of the present invention will now be described in detail. This detailed description should not be considered as limiting the present invention, but should be understood as a more detailed description of certain aspects, features, and embodiments of the present invention.
应理解本发明中所述的术语仅仅是为描述特别的实施方式,并非用于限制本发明。另外,对于本发明中的数值范围,应理解为还具体公开了该范围的上限和下限之间的每个中间值。在任何陈述值或陈述范围内的中间值以及任何其他陈述值或在所述范围内的中间值之间的每个较小的范围也包括在本发明内。这些较小范围的上限和下限可独立地包括或排除在范围内。It should be understood that the terms described in the present invention are only for describing a particular embodiment and are not intended to limit the present invention. In addition, for the numerical range in the present invention, it should be understood that each intermediate value between the upper and lower limits of the scope is also specifically disclosed. Each smaller range between the intermediate value in any stated value or stated range and any other stated value or intermediate value in the described range is also included in the present invention. The upper and lower limits of these smaller ranges can be independently included or excluded in the scope.
除非另有说明,否则本文使用的所有技术和科学术语具有本发明所述领域的常规技术人员通常理解的相同含义。虽然本发明仅描述了优选的方法和材料,但是在本发明的实施或测试中也可以使用与本文所述相似或等同的任何方法和材料。本说明书中提到的所有文献通过引用并入,用以公开和描述与所述文献相关的方法和/或材料。在与任何并入的文献冲突时,以本说明书的内容为准。Unless otherwise indicated, all technical and scientific terms used herein have the same meanings as commonly understood by those skilled in the art. Although the present invention describes only preferred methods and materials, any methods and materials similar or equivalent to those described herein may also be used in the implementation or testing of the present invention. All documents mentioned in this specification are incorporated by reference to disclose and describe methods and/or materials related to the documents. In the event of a conflict with any incorporated document, the content of this specification shall prevail.
在不背离本发明的范围或精神的情况下,可对本发明说明书的具体实施方式做多种改进和变化,这对本领域技术人员而言是显而易见的。由本发明的说明书得到的其他实施方式对技术人员而言是显而易见得的。本发明说明书和实施例仅是示例性的。It will be apparent to those skilled in the art that various modifications and variations may be made to the specific embodiments of the present invention description without departing from the scope or spirit of the present invention. Other embodiments derived from the present invention description will be apparent to those skilled in the art. The present invention description and examples are exemplary only.
关于本文中所使用的“包含”、“包括”、“具有”、“含有”等等,均为开放性的用语,即意指包含但不限于。The words “include,” “including,” “have,” “contain,” etc. used in this document are open-ended terms, meaning including but not limited to.
实施例1Example 1
一种菌酶协同生产玉米全粉的方法,包括以下步骤:A method for producing whole corn flour by bacterial enzyme synergism comprises the following steps:
(1)清粮:以市售玉米粒为原料,将玉米除杂、除石、清洗处理。(1) Cleaning corn: Using commercially available corn kernels as raw materials, the corn is cleaned of impurities, stones and cleaning.
(2)挤压膨化:玉米清粮后,晾晒,控制玉米水分含量20wt%,采用双螺杆挤压膨化机(天津泰斯特)对玉米全籽粒进行挤压膨化,控制挤压膨化温度140℃,螺杆转速为486r/min,物料投速270r/min。(2) Extrusion and puffing: After cleaning the corn, dry it in the sun and control the moisture content of the corn to 20wt%. Use a twin-screw extruder (Tianjin Test) to extrude and puff the whole corn kernels. The extrusion temperature is controlled at 140℃, the screw speed is 486r/min, and the material feeding speed is 270r/min.
(3)破碎:将挤压膨化后的玉米粉输送到破碎机中,破除程度80目。(3) Crushing: The extruded corn flour is conveyed to the crusher and crushed to 80 mesh.
(4)发酵:破碎后的玉米粉加入到恒温密闭发酵罐中,控制玉米粉干性物和水的质量比为1:2;然后进行厌氧发酵,在发酵罐中按照接种量0.01%接种乳酸菌(植物乳杆菌,通过商购途径获得)进行发酵,发酵温度控制在36℃,密闭厌氧14h,在发酵终止前110min加入植物纤维素酶(纤维素酶和半纤维素酶等比例混合物),加入量为玉米粉干性物质量的1%;终止发酵,此时pH值保持在4.5;发酵物过滤后,固液分离,得到固体发酵产物和液体发酵产物,液体发酵产物返回发酵罐中,作为发酵母液继续进行厌氧发酵,重复利用。(4) Fermentation: The crushed corn flour is added to a constant temperature sealed fermentation tank, and the mass ratio of corn flour dry matter to water is controlled to be 1:2; then anaerobic fermentation is carried out, and lactic acid bacteria (Lactobacillus plantarum, obtained through commercial channels) is inoculated in the fermentation tank at an inoculation rate of 0.01% for fermentation, and the fermentation temperature is controlled at 36°C, and the sealed anaerobic fermentation is carried out for 14 hours. Plant cellulase (a mixture of cellulase and hemicellulase in equal proportions) is added 110 minutes before the end of fermentation, and the added amount is 1% of the mass of the corn flour dry matter; the fermentation is terminated, and the pH value is maintained at 4.5; after the fermentation product is filtered, the solid and liquid are separated to obtain a solid fermentation product and a liquid fermentation product, and the liquid fermentation product is returned to the fermentation tank and used as a yeast liquid to continue anaerobic fermentation and reuse.
(5)洗涤:用高压喷雾凉水洗涤步骤(4)所得固体发酵产物,至pH值6.8,然后干燥。(5) Washing: Wash the solid fermentation product obtained in step (4) with high-pressure spray cold water to a pH value of 6.8, and then dry.
(6)磨浆:按照固体质量和水的质量比为1:2,将经过步骤(5)处理的发酵产物和水进行混合后,使用混体浆机(锉磨机和齿形磨浆机一体机)进行磨浆处理1h,此时玉米粉粒径为120目。(6) Refining: The fermentation product treated in step (5) is mixed with water in a solid mass to water ratio of 1:2, and then refined for 1 hour using a mixed pulper (a file grinder and a toothed pulper in one). At this time, the corn flour particle size is 120 mesh.
(7)高压均质:经过步骤(6)处理后的产物进行高压均质,高压均质条件为15Mpa,高压均质次数3次,每次高压均质时间3min。(7) High-pressure homogenization: The product after treatment in step (6) was subjected to high-pressure homogenization at a condition of 15 MPa, 3 times of high-pressure homogenization, and each time of high-pressure homogenization for 3 minutes.
(8)脱水、干燥:将经过步骤(7)高压均质处理的浆料采用板框过滤器,除去水,然后在170℃条件下闪蒸5s,得到产物玉米全粉。(8) Dehydration and drying: The slurry subjected to the high pressure homogenization treatment in step (7) is filtered through a plate and frame filter to remove water, and then flash evaporated at 170° C. for 5 seconds to obtain the product corn flour.
实施例2Example 2
与实施例1的不同之处仅在于,在步骤(4)厌氧发酵过程中,未加入植物纤维素酶。The only difference from Example 1 is that during the anaerobic fermentation in step (4), plant cellulase was not added.
实施例3Example 3
与实施例1的不同之处仅在于,将步骤(6)的混体浆机更换为锉磨机。The only difference from Example 1 is that the mixed pulp machine in step (6) is replaced by a rasp grinder.
实施例4Example 4
与实施例1的不同之处仅在于,将步骤(6)的混体浆机更换为齿形磨浆机。The only difference from Example 1 is that the mixed pulper in step (6) is replaced by a toothed pulper.
实施例5Example 5
与实施例1的不同之处仅在于,将步骤(6)的混体磨浆过程更换为先锉磨机磨浆0.5h,然后齿形磨浆机至玉米粒径为120目。The only difference from Example 1 is that the mixed pulping process in step (6) is replaced by first grinding with a file grinder for 0.5 h and then grinding with a tooth grinder until the corn particle size is 120 mesh.
实施例6Example 6
与实施例1的不同之处仅在于,步骤(4)中,植物纤维素酶的加入时机为厌氧发酵开始时。The only difference from Example 1 is that in step (4), the plant cellulase is added at the beginning of anaerobic fermentation.
实施例7Example 7
与实施例1的不同之处仅在于,厌氧发酵过程中,植物纤维素酶的加入时机为发酵终止前60min。The only difference from Example 1 is that during the anaerobic fermentation process, the plant cellulase is added 60 minutes before the end of the fermentation.
实施例8Example 8
与实施例1的不同之处仅在于,将纤维素酶更换为质量比为1:1的纤维素酶和胃蛋白酶。The only difference from Example 1 is that the cellulase is replaced with cellulase and pepsin in a mass ratio of 1:1.
对实施例2和实施例8发酵过程中pH变化情况进行记录,结果如图1所示。从图中可以看出,24h以内随着时间的增加,发酵pH呈现不断下降的趋势,单独采用乳酸菌发酵的pH下降趋势较为缓慢,联合使用纤维素酶和蛋白酶提前了酸度下降时间,可以缩短发酵时间,提高玉米粉适口性和可加工性。The pH changes during the fermentation process of Example 2 and Example 8 were recorded, and the results are shown in Figure 1. As can be seen from the figure, within 24 hours, the fermentation pH shows a downward trend with the increase of time. The pH decline trend of lactic acid bacteria fermentation alone is relatively slow. The combined use of cellulase and protease advances the acidity decline time, shortens the fermentation time, and improves the palatability and processability of corn flour.
实施例9Example 9
与实施例1的不同之处仅在于,厌氧发酵所使用的植物乳杆菌在投加前进行驯化,具体步骤如下:The only difference from Example 1 is that the plant lactobacillus used in the anaerobic fermentation is domesticated before addition, and the specific steps are as follows:
(1)分别配制MRS固体培养基和MRS液体培养基;(1) Prepare MRS solid culture medium and MRS liquid culture medium respectively;
(2)向100mL MRS培养基中添加不同量的乳酸,得到乳酸浓度分别为5g/L、10 g/L、15 g/L的酸性MRS培养基。(2) Different amounts of lactic acid were added to 100 mL of MRS medium to obtain acidic MRS medium with lactic acid concentrations of 5 g/L, 10 g/L, and 15 g/L, respectively.
(3)将植物乳杆菌从冰箱中取出,活化后在固体MRS培养基中划线分离,挑取单菌菌落接种于100mL MRS液体培养基中,37℃恒温厌氧培养24h后,按照2%的菌液量接种于浓度为5g/L酸性MRS培养基中,37℃恒温厌氧培养至生长稳定后,再按照2%的菌液量接种于浓度为10g/L酸性MRS培养基中,37℃恒温厌氧培养至生长稳定后,再按照2%的菌液量接种于浓度为15g/L酸性MRS培养基中,37℃恒温厌氧培养至生长稳定,然后转入按照2%的菌液量接种于添加有液体发酵产物(实施例1步骤(4)中提及的液体发酵产物)的MRS液体培养基中(液体发酵产物和MRS液体培养基的混合体积比为2:2),37℃恒温厌氧培养至生长稳定得到经过驯化的植物乳杆菌。(3) The plant lactobacillus was taken out of the refrigerator, activated and separated by streaking in a solid MRS medium, a single bacterial colony was picked and inoculated into 100 mL of MRS liquid medium, and cultured anaerobically at 37°C for 24 h. Then, 2% of the bacterial liquid was inoculated into an acidic MRS medium with a concentration of 5 g/L, and cultured anaerobically at 37°C until the growth was stable. Then, 2% of the bacterial liquid was inoculated into an acidic MRS medium with a concentration of 10 g/L, and cultured anaerobically at 37°C until the growth was stable. Then, 2% of the bacterial liquid was inoculated into an acidic MRS medium with a concentration of 15 g/L, and cultured anaerobically at 37°C until the growth was stable. Then, 2% of the bacterial liquid was inoculated into an MRS liquid medium supplemented with a liquid fermentation product (the liquid fermentation product mentioned in step (4) of Example 1) (the mixed volume ratio of the liquid fermentation product to the MRS liquid medium was 2:2), and cultured anaerobically at 37°C until the growth was stable to obtain domesticated plant lactobacillus.
在使用乳酸菌对玉米粉进行发酵过程中,伴随着乳酸菌厌氧产酸的过程使得发酵环境的不断酸化,从而使发酵环境逐渐偏离了乳酸菌的最适发酵环境,当乳酸菌处于酸胁迫环境下时,会影响乳酸菌吸收营养物质和蛋白质合成过程,同时也会产生某些应激反应,产生影响玉米口感和可加工性能的不利效果,这也是单独使用乳酸菌对玉米进行发酵不理想的又一重要原因。为解决该技术问题,在进行乳酸菌厌氧发酵前,对其进行驯化处理,提升乳酸菌的耐酸性能,促使乳酸菌保持较高的发酵活力,提高厌氧发酵效率和玉米粉的性能。In the process of using lactic acid bacteria to ferment corn flour, the fermentation environment is continuously acidified as the lactic acid bacteria produce acid anaerobicly, which gradually deviates from the optimal fermentation environment for lactic acid bacteria. When lactic acid bacteria are in an acid stress environment, it will affect the lactic acid bacteria's absorption of nutrients and protein synthesis process, and will also produce certain stress reactions, which will have an adverse effect on the taste and processability of corn. This is another important reason why it is not ideal to ferment corn with lactic acid bacteria alone. In order to solve this technical problem, before the lactic acid bacteria are anaerobic fermented, they are tamed to improve the acid resistance of the lactic acid bacteria, prompt the lactic acid bacteria to maintain a high fermentation activity, and improve the anaerobic fermentation efficiency and the performance of corn flour.
实施例10Example 10
一种菌酶协同生产玉米全粉的方法,包括以下步骤:A method for producing whole corn flour by bacterial enzyme synergism comprises the following steps:
(1)清粮:以市售玉米粒为原料,将玉米除杂、除石、清洗处理。(1) Cleaning corn: Using commercially available corn kernels as raw materials, the corn is cleaned of impurities, stones and cleaning.
(2)挤压膨化:玉米清粮后,晾晒,控制玉米水分含量22wt%,采用双螺杆挤压膨化机(天津泰斯特)对玉米全籽粒进行挤压膨化,控制挤压膨化温度150℃,螺杆转速为486r/min,物料投速270r/min。(2) Extrusion and puffing: After cleaning the corn, dry it in the sun and control the moisture content of the corn to 22 wt%. Use a twin-screw extruder (Tianjin Test) to extrude and puff the whole corn kernels. The extrusion temperature is controlled at 150 °C, the screw speed is 486 r/min, and the material feeding speed is 270 r/min.
(3)破碎:将挤压膨化后的玉米粉输送到破碎机中,破除程度70目。(3) Crushing: The extruded corn flour is conveyed to the crusher and crushed to 70 mesh.
(4)发酵:破碎后的玉米粉加入到恒温密闭发酵罐中,控制玉米粉干性物和水的质量比为1:3;然后进行厌氧发酵,在发酵罐中按照接种量0.015%接种乳酸菌(植物乳杆菌)进行发酵,发酵温度控制在37℃,密闭厌氧15h,在发酵终止前120min加入分离植物纤维素酶(纤维素酶和半纤维素酶等比例混合物),加入量为玉米粉干性物质量的1%;终止发酵,此时pH值保持在4.6;发酵物过滤后,固液分离,得到固体发酵产物和液体发酵产物,液体发酵产物返回发酵罐中,作为发酵母液继续进行厌氧发酵,重复利用。(4) Fermentation: The crushed corn flour is added to a constant temperature sealed fermentation tank, and the mass ratio of corn flour dry matter to water is controlled to be 1:3; then anaerobic fermentation is carried out, and lactic acid bacteria (Lactobacillus plantarum) are inoculated in the fermentation tank at an inoculation rate of 0.015% for fermentation. The fermentation temperature is controlled at 37°C, and the sealed anaerobic fermentation is carried out for 15 hours. 120 minutes before the end of the fermentation, isolated plant cellulase (a mixture of cellulase and hemicellulase in equal proportions) is added, and the added amount is 1% of the mass of the corn flour dry matter; the fermentation is terminated, and the pH value is maintained at 4.6; after the fermentation product is filtered, the solid and liquid are separated to obtain solid fermentation products and liquid fermentation products, and the liquid fermentation product is returned to the fermentation tank and used as the yeast liquid to continue anaerobic fermentation and reuse.
(5)洗涤:用高压喷雾凉水洗涤步骤(4)所得固体发酵产物,至pH值7.2,然后干燥。(5) Washing: Wash the solid fermentation product obtained in step (4) with high-pressure spray cold water to a pH value of 7.2, and then dry.
(6)磨浆:按照固体质量和水的质量比为1:3,将经过步骤(5)处理的发酵产物和水进行混合后,使用混体浆机(锉磨机和齿形磨浆机一体机)进行磨浆处理1h,此时玉米粉粒径为130目。(6) Refining: The fermentation product treated in step (5) is mixed with water at a solid mass to water ratio of 1:3, and then refined for 1 h using a mixed pulper (a file grinder and a toothed pulper in one). At this time, the corn flour particle size is 130 mesh.
(7)高压均质:经过步骤(6)处理后的产物进行高压均质,高压均质条件为17Mpa,高压均质次数4次,每次高压均质时间4min。(7) High-pressure homogenization: The product after treatment in step (6) was subjected to high-pressure homogenization. The high-pressure homogenization condition was 17 MPa, the high-pressure homogenization was repeated 4 times, and the high-pressure homogenization time was 4 min each time.
(8)脱水、干燥:将经过步骤(7)高压均质处理的浆料采用板框过滤器,除去水,然后在170℃条件下闪蒸5s,得到产物玉米全粉。(8) Dehydration and drying: The slurry subjected to the high pressure homogenization treatment in step (7) is filtered through a plate and frame filter to remove water, and then flash evaporated at 170° C. for 5 seconds to obtain the product corn flour.
实施例11Embodiment 11
一种菌酶协同生产玉米全粉的方法,包括以下步骤:A method for producing whole corn flour by bacterial enzyme synergism comprises the following steps:
(1)清粮:以市售玉米粒为原料,将玉米除杂、除石、清洗处理。(1) Cleaning corn: Using commercially available corn kernels as raw materials, the corn is cleaned of impurities, stones and cleaning.
(2)挤压膨化:玉米清粮后,晾晒,控制玉米水分含量24wt%,采用双螺杆挤压膨化机(天津泰斯特)对玉米全籽粒进行挤压膨化,控制挤压膨化温度160℃,螺杆转速为486r/min,物料投速270r/min。(2) Extrusion and puffing: After cleaning the corn, dry it in the sun and control the moisture content of the corn to 24 wt%. Use a twin-screw extruder (Tianjin Test) to extrude and puff the whole corn kernels. The extrusion temperature is controlled at 160 °C, the screw speed is 486 r/min, and the material feeding speed is 270 r/min.
(3)破碎:将挤压膨化后的玉米粉输送到破碎机中,破除程度80目。(3) Crushing: The extruded corn flour is conveyed to the crusher and crushed to 80 mesh.
(4)发酵:破碎后的玉米粉加入到恒温密闭发酵罐中,控制玉米粉干性物和水的质量比为1:4;然后进行厌氧发酵,在发酵罐中按照接种量0.02%接种乳酸菌(植物乳杆菌)进行发酵,发酵温度控制在38℃,密闭厌氧16h,在发酵终止前130min加入分离植物纤维素酶(纤维素酶和半纤维素酶等比例混合物),加入量为玉米粉干性物质量的1%;终止发酵,此时pH值保持在4.7;发酵物过滤后,固液分离,得到固体发酵产物和液体发酵产物,液体发酵产物返回发酵罐中,作为发酵母液继续进行厌氧发酵,重复利用。(4) Fermentation: The crushed corn flour is added to a constant temperature sealed fermentation tank, and the mass ratio of corn flour dry matter to water is controlled to be 1:4; then anaerobic fermentation is carried out, and lactic acid bacteria (Lactobacillus plantarum) are inoculated in the fermentation tank at an inoculation rate of 0.02% for fermentation. The fermentation temperature is controlled at 38°C, and the sealed anaerobic fermentation is carried out for 16 hours. 130 minutes before the end of the fermentation, isolated plant cellulase (a mixture of cellulase and hemicellulase in equal proportions) is added, and the amount added is 1% of the mass of the corn flour dry matter; the fermentation is terminated, and the pH value is maintained at 4.7; after the fermentation product is filtered, the solid and liquid are separated to obtain solid fermentation products and liquid fermentation products, and the liquid fermentation product is returned to the fermentation tank and used as the yeast liquid to continue anaerobic fermentation and reuse.
(5)洗涤:用高压喷雾凉水洗涤步骤(4)所得固体发酵产物,至pH值7.2,然后干燥。(5) Washing: Wash the solid fermentation product obtained in step (4) with high-pressure spray cold water to a pH value of 7.2, and then dry.
(6)磨浆:按照固体质量和水的质量比为1: 4,将经过步骤(5)处理的发酵产物和水进行混合后,使用混体浆机(锉磨机和齿形磨浆机一体机)进行磨浆处理1h,此时玉米粉粒径为140目。(6) Refining: The fermentation product treated in step (5) is mixed with water at a solid mass to water ratio of 1:4, and then refined for 1 h using a mixed pulper (a file grinder and a toothed pulper in one). At this time, the corn flour particle size is 140 mesh.
(7)高压均质:经过步骤(6)处理后的产物进行高压均质,高压均质条件为20Mpa,高压均质次数5次,每次高压均质时间5min。(7) High-pressure homogenization: The product after treatment in step (6) was subjected to high-pressure homogenization. The high-pressure homogenization condition was 20 MPa, the high-pressure homogenization times were 5 times, and the high-pressure homogenization time was 5 min each time.
(8)脱水、干燥:将经过步骤(7)高压均质处理的浆料采用板框过滤器,除去水,然后在170℃条件下闪蒸5s,得到产物玉米全粉。(8) Dehydration and drying: The slurry subjected to the high pressure homogenization treatment in step (7) is filtered through a plate and frame filter to remove water, and then flash evaporated at 170° C. for 5 seconds to obtain the product corn flour.
实施例12Example 12
与实施例9的不同之处仅在于,在步骤(5)洗涤至pH值7.2后,按照1%的加入量在固体发酵产物加入淀粉分支酶,30℃孵育30min,然后再加入1%麦芽糖淀粉酶,50℃处理40min,然后再进行干燥。The only difference from Example 9 is that after washing to a pH value of 7.2 in step (5), starch branching enzyme is added to the solid fermentation product at an amount of 1%, incubated at 30°C for 30 min, and then 1% maltogenic amylase is added, treated at 50°C for 40 min, and then dried.
淀粉分支酶,糖基转移酶之一,具有转移酶活性,即将α-1,4-葡聚糖直链供体(直链淀粉和支链淀粉的直链区)切开并通过α-1,6糖苷键的形成使切下短链连于受体链上(原链或其他链)。该酶反应不但产生分支,而且非还原端可供α-1,4-葡聚糖链进一步延伸。通过淀粉分支酶能够水解淀粉中直链淀粉簇之间的片段的连接,从而产生直链淀粉簇,同时,分支酶将支化的侧链连接到直链淀粉上,从而产生支化的直链淀粉,然后继续采用麦芽糖淀粉酶处理产物,将长的侧链切断为短的侧链,并将葡萄糖转移到侧链上,提高淀粉中直链淀粉的支化程度,支化程度的增加可以使淀粉的水解更缓慢,避免糖尿病人摄食后短时间血糖急剧升高,并且,水解变缓慢可以使得其能够持续地供应能量,使血糖更平稳。Starch branching enzyme, one of the glycosyltransferases, has transferase activity, that is, it cuts the α-1,4-glucan linear donor (the linear region of amylose and amylopectin) and connects the cut short chain to the acceptor chain (original chain or other chain) through the formation of α-1,6 glycosidic bonds. This enzyme reaction not only produces branches, but also the non-reducing end can be used for further extension of the α-1,4-glucan chain. The starch branching enzyme can hydrolyze the connection between the fragments of the amylose clusters in the starch to produce amylose clusters. At the same time, the branching enzyme connects the branched side chains to the amylose to produce branched amylose. Then, the product is treated with maltose amylase to cut the long side chains into short side chains and transfer glucose to the side chains to increase the branching degree of amylose in the starch. The increase in the degree of branching can make the hydrolysis of starch slower, avoiding the rapid increase of blood sugar in diabetics in a short time after ingestion. In addition, the slow hydrolysis can enable it to continuously supply energy and make blood sugar more stable.
实施例13Example 13
与实施例1的不同之处在于,在接种植物乳杆菌的同时,还接种1%普鲁兰酶产生菌,并将发酵温度提高至39℃。The difference from Example 1 is that, while inoculating Lactobacillus plantarum, 1% of pullulanase-producing bacteria is also inoculated, and the fermentation temperature is increased to 39°C.
实施例14Embodiment 14
与实施例12的不同之处在于,在接种植物乳杆菌的同时,还接种1%普鲁兰酶产生菌,并将发酵温度提高至39℃。The difference from Example 12 is that, while inoculating Lactobacillus plantarum, 1% pullulanase-producing bacteria was also inoculated, and the fermentation temperature was increased to 39°C.
普鲁兰酶是一种重要的工业用酶,将普鲁兰酶与其他酶协同作用,可以大规模地提高淀粉的利用率和生产效率,其可专一水解支链淀粉分支点中的α-1,6-糖苷键,形成直链淀粉,提高抗性淀粉含量。Pullulanase is an important industrial enzyme. The synergistic effect of pullulanase with other enzymes can greatly improve the utilization rate and production efficiency of starch. It can specifically hydrolyze the α-1,6-glycosidic bonds in the branch points of amylopectin to form amylose and increase the content of resistant starch.
试验例1Test Example 1
对实施例1-14(标记为样品1-14)和市场购买的未经过发酵的去皮玉米粉(标记为样品15)进行性能验证实验,对比技术效果;具体过程如下:A performance verification experiment was conducted on Examples 1-14 (marked as Samples 1-14) and unfermented peeled corn flour purchased from the market (marked as Sample 15) to compare the technical effects; the specific process is as follows:
1.1玉米粉基本营养成分测定1.1 Determination of basic nutritional components of corn flour
以市售玉米粒为原料,除去石子和坏粒,进行研磨、过筛,对玉米粉的蛋白质含量(GB/T5009.5—2016凯氏定氮法测定)、脂肪(GB/T 14772-2008索氏抽提法测定)、淀粉含量(GB/T5009.9-2016酸解法测定),纤维素含量(GB/T5009.88-2014酶重量法测定)、灰分(GB/T5009.4—2016灼烧法测定)、直链淀粉含量(采用双波长法)、抗性淀粉含量(采用Megazyme抗性淀粉试剂盒法)进行测量,结果如表1。Commercially available corn kernels were used as raw materials, stones and bad kernels were removed, and the corn flour was ground and sieved. The protein content (determined by GB/T5009.5-2016 Kjeldahl method), fat (determined by GB/T 14772-2008 Soxhlet extraction method), starch content (determined by GB/T5009.9-2016 acid hydrolysis method), cellulose content (determined by GB/T5009.88-2014 enzyme weight method), ash (determined by GB/T5009.4-2016 burning method), amylose content (determined by dual wavelength method), and resistant starch content (determined by Megazyme resistant starch kit method) of the corn flour were measured. The results are shown in Table 1.
1.2全玉米蛋糕的制作1.2 Preparation of whole corn cake
将样品1-15制备全玉米蛋糕,具体制备工艺:Samples 1-15 were used to prepare whole corn cakes, and the specific preparation process was as follows:
a取玉米粉200g、烘焙油90mL、鸡蛋100g、白砂糖90g;a Take 200g corn flour, 90mL baking oil, 100g eggs, and 90g white sugar;
b将烘焙油、蛋黄搅拌混匀,打至乳白色细泡为止;b. Stir the baking oil and egg yolk until they are milky white and fine bubbles;
c蛋清与白砂糖一起打发;c. Beat the egg white and sugar together;
d将玉米粉加入步骤b中混匀,调成糊状;d. Add corn flour into step b and mix well to make a paste;
e将步骤c物料分3次加入步骤d中混匀,调成糊状;e. Add the material from step c to step d in three portions and mix well to form a paste;
f蛋糕杯预先刷底油以防粘连, 将e产物加入蛋糕杯中;f. Brush the cake cup with oil in advance to prevent sticking, add product e into the cake cup;
g烤箱 180℃预热5分钟,上火150℃,下火160℃烤制17分钟。g Preheat the oven to 180℃ for 5 minutes, bake at 150℃ on top and 160℃ on bottom for 17 minutes.
用质构仪分别对玉米粉制作的全玉米蛋糕的硬度、弹性、回复性和阻嚼性进行比较,质构仪检测参数:测试距离10mm,测试速度0.5mm/s,触发点载荷7g,探头类型P/20,测试次数为2次,结果见表2。The hardness, elasticity, resilience and chewiness of the whole corn cake made of corn flour were compared using a texture analyzer. The testing parameters of the texture analyzer were as follows: test distance 10 mm, test speed 0.5 mm/s, trigger point load 7 g, probe type P/20, and test times 2. The results are shown in Table 2.
1.3感官评价1.3 Sensory evaluation
邀请20 个志愿者(男女各10人)从气味、色泽、味道和口感4个角度对玉米粉制作的全玉米蛋糕进行打分,满分10分,将4项指标进行加权得分,用以下公式计算:Invite 20 volunteers (10 men and 10 women) to rate the whole corn cake made of corn flour from four perspectives: smell, color, taste and mouthfeel. The full score is 10 points. The four indicators are weighted and calculated using the following formula:
总分=气味×0.1+色泽×0.2+味道×0.3+口感×0.4。Total score = smell × 0.1 + color × 0.2 + taste × 0.3 + mouthfeel × 0.4.
统计结果记录于表3。The statistical results are recorded in Table 3.
表1玉米粉营养物质含量Table 1 Nutrient content of corn flour
注:蛋白质、脂肪、淀粉、纤维和灰分的百分比含量基于玉米粉,直链淀粉和抗性淀粉的百分比含量基于淀粉。Note: The percentages of protein, fat, starch, fiber and ash are based on corn flour, while the percentages of amylose and resistant starch are based on starch.
表2全玉米蛋糕质构结果Table 2 Whole corn cake texture results
表3全玉米蛋糕感官评价结果Table 3 Sensory evaluation results of whole corn cake
1.4全玉米蛋糕的血糖指数1.4 Glycemic Index of Whole Corn Cake
血糖指数也称血糖生成指数,是指与食物如葡萄糖或白面包摄入后血糖浓度的变化程度相比,含糖食物使血糖水平相对升高的相对能力。The glycemic index, also known as the glycemic index, refers to the relative ability of sugary foods to raise blood sugar levels compared to the change in blood sugar concentration after the intake of foods such as glucose or white bread.
计算公式如下:GI=(含有50g碳水化合物某食物的2小时血糖应答/50g葡萄糖的2小时血糖应答)×100%。The calculation formula is as follows: GI = (2-hour blood glucose response to a food containing 50g of carbohydrates/2-hour blood glucose response to 50g of glucose) × 100%.
对蛋糕样品的血糖指数(GI)进行体外测量,结果如表4。The glycemic index (GI) of the cake samples was measured in vitro and the results are shown in Table 4.
表4 血糖指数Table 4 Glycemic Index
用本发明实施例1-15生产的玉米粉和市购支链淀粉饲喂小鼠,观察小鼠的胰岛素抗性,试验表明,从12-16周起,饲喂支链淀粉的小鼠开始产生不可逆的胰岛素抗性,而饲喂本发明玉米粉的小鼠则不产生胰岛素抗性。Mice were fed with corn flour produced by Examples 1-15 of the present invention and commercially available amylopectin, and the insulin resistance of the mice was observed. The test showed that from 12 to 16 weeks, the mice fed with amylopectin began to develop irreversible insulin resistance, while the mice fed with corn flour of the present invention did not develop insulin resistance.
以上所述的实施例仅是对本发明的优选方式进行描述,并非对本发明的范围进行限定,在不脱离本发明设计精神的前提下,本领域普通技术人员对本发明的技术方案做出的各种变形和改进,均应落入本发明权利要求书确定的保护范围内。The embodiments described above are only descriptions of the preferred modes of the present invention, and are not intended to limit the scope of the present invention. Without departing from the design spirit of the present invention, various modifications and improvements made to the technical solutions of the present invention by ordinary technicians in this field should all fall within the protection scope determined by the claims of the present invention.
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210013195.8A CN115245193B (en) | 2022-01-07 | 2022-01-07 | Method for producing corn whole meal by cooperation of bacterial enzymes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210013195.8A CN115245193B (en) | 2022-01-07 | 2022-01-07 | Method for producing corn whole meal by cooperation of bacterial enzymes |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115245193A CN115245193A (en) | 2022-10-28 |
CN115245193B true CN115245193B (en) | 2024-06-25 |
Family
ID=83698478
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210013195.8A Active CN115245193B (en) | 2022-01-07 | 2022-01-07 | Method for producing corn whole meal by cooperation of bacterial enzymes |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115245193B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115299556B (en) * | 2022-01-07 | 2024-02-09 | 齐齐哈尔大学 | Production method of full-nutrition corn base material powder |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115299556A (en) * | 2022-01-07 | 2022-11-08 | 齐齐哈尔大学 | A kind of production method of full nutrition corn base powder |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100825674B1 (en) * | 2006-10-02 | 2008-04-29 | 김승건 | Fine Rice Flour Composition, Process for its Preparation, Rice Bread Using Micro Wet Rice Flour Composition and Process for Producing the Same. |
JP2010514910A (en) * | 2007-01-02 | 2010-05-06 | ベータテック ホプフェンプロドゥクテ ゲーエムベーハー | Method for producing starch |
CN101156665A (en) * | 2007-11-26 | 2008-04-09 | 曲建波 | Method for producing corn wheaten flour |
CN110839823A (en) * | 2019-11-20 | 2020-02-28 | 齐齐哈尔大学 | Corn noodles and preparation method thereof |
-
2022
- 2022-01-07 CN CN202210013195.8A patent/CN115245193B/en active Active
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115299556A (en) * | 2022-01-07 | 2022-11-08 | 齐齐哈尔大学 | A kind of production method of full nutrition corn base powder |
Also Published As
Publication number | Publication date |
---|---|
CN115245193A (en) | 2022-10-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101103287B1 (en) | Method for producing fermented product using natural products and food or pharmaceutical product containing fermented product produced by the method | |
CN115624186B (en) | High-protein low-GI composite grain composition and preparation method and application thereof | |
CN101156691A (en) | A kind of production method and product thereof of high active corn bran dietary fiber | |
CN108391692A (en) | A kind of production method of high microsteping beans short paste work goods | |
CN111789225A (en) | Low-GI non-fried extruded instant noodles and preparation method thereof | |
CN110150636A (en) | Resistant miscellaneous grain starch prepared by biological fermentation and method for preparing rice flour | |
CN101156667A (en) | Production method of enzymatic corn noodles | |
CN115245193B (en) | Method for producing corn whole meal by cooperation of bacterial enzymes | |
CN103844194B (en) | A kind of preparation method of low albumen whole-wheat nutritional noodles | |
CN104544433A (en) | Preparation method for highland barley fiber and cereal drink | |
KR102134219B1 (en) | Manufacturing method for cake and macaron manufactured by the same | |
CN1879500A (en) | A method for preparing glutinous maize fermented flour and application thereof | |
CN115299556B (en) | Production method of full-nutrition corn base material powder | |
CN1117797A (en) | Instant noodles made from maize meal and processing method thereof | |
CN112655733A (en) | Preparation method of germinated brown rice bread with high GABA content and high protein | |
CN107794160B (en) | Cereal protein liquid and preparation method thereof | |
CN112544882A (en) | Highland barley puffed food and preparation method thereof | |
CN102342422A (en) | Method for producing glutinous rice dumplings without being mixed in soup | |
CN101803744B (en) | Processing method for preparing dietary fiber substitute by utilizing bean vermicelli leftovers | |
CN116515923A (en) | Production technology of rice bran fiber polysaccharide for prolonging shelf life of quick-frozen rice dumplings | |
CN111728134B (en) | High-cellulose high-nutrition fermented corn noodles and preparation method thereof | |
KR20180135678A (en) | Manufacturing method of squid Gijungdduck with enzymatic squid hydrolysate | |
JP4432849B2 (en) | Bread production method | |
CN106261493A (en) | A kind of corn powder and preparation method thereof | |
CN113354747A (en) | Preparation method of corn resistant starch |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |