JP2021159064A - Konjac powder multienzyme hydrolysate and preparation method thereof - Google Patents
Konjac powder multienzyme hydrolysate and preparation method thereof Download PDFInfo
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- konjac
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- 229920002752 Konjac Polymers 0.000 title claims abstract description 108
- 235000010485 konjac Nutrition 0.000 title claims abstract description 107
- 239000000843 powder Substances 0.000 title claims abstract description 95
- 241001312219 Amorphophallus konjac Species 0.000 title claims abstract description 88
- 235000001206 Amorphophallus rivieri Nutrition 0.000 title claims abstract description 88
- 239000000252 konjac Substances 0.000 title claims abstract description 88
- 238000002360 preparation method Methods 0.000 title abstract description 4
- 239000000413 hydrolysate Substances 0.000 title abstract 4
- 230000002255 enzymatic effect Effects 0.000 claims abstract description 49
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 38
- 108090000790 Enzymes Proteins 0.000 claims abstract description 31
- 102000004190 Enzymes Human genes 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 239000002994 raw material Substances 0.000 claims abstract description 15
- 238000000034 method Methods 0.000 claims abstract description 9
- 238000000354 decomposition reaction Methods 0.000 claims description 53
- 229940088598 enzyme Drugs 0.000 claims description 30
- 238000004519 manufacturing process Methods 0.000 claims description 15
- 108010059892 Cellulase Proteins 0.000 claims description 13
- 229940106157 cellulase Drugs 0.000 claims description 13
- 238000000746 purification Methods 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 3
- 229920001542 oligosaccharide Polymers 0.000 abstract description 12
- 150000002482 oligosaccharides Chemical class 0.000 abstract description 12
- 239000000047 product Substances 0.000 description 30
- 241000700159 Rattus Species 0.000 description 21
- 239000008280 blood Substances 0.000 description 16
- 210000004369 blood Anatomy 0.000 description 16
- 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 11
- 239000008103 glucose Substances 0.000 description 11
- 230000000694 effects Effects 0.000 description 9
- 239000007857 degradation product Substances 0.000 description 8
- 206010012601 diabetes mellitus Diseases 0.000 description 8
- 235000000346 sugar Nutrition 0.000 description 8
- LUEWUZLMQUOBSB-FSKGGBMCSA-N (2s,3s,4s,5s,6r)-2-[(2r,3s,4r,5r,6s)-6-[(2r,3s,4r,5s,6s)-4,5-dihydroxy-2-(hydroxymethyl)-6-[(2r,4r,5s,6r)-4,5,6-trihydroxy-2-(hydroxymethyl)oxan-3-yl]oxyoxan-3-yl]oxy-4,5-dihydroxy-2-(hydroxymethyl)oxan-3-yl]oxy-6-(hydroxymethyl)oxane-3,4,5-triol 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]2[C@H](O[C@@H](OC3[C@H](O[C@@H](O)[C@@H](O)[C@H]3O)CO)[C@@H](O)[C@H]2O)CO)[C@H](O)[C@H]1O LUEWUZLMQUOBSB-FSKGGBMCSA-N 0.000 description 7
- 229920002581 Glucomannan Polymers 0.000 description 7
- 230000007515 enzymatic degradation Effects 0.000 description 7
- 229940046240 glucomannan Drugs 0.000 description 7
- 241000699666 Mus <mouse, genus> Species 0.000 description 6
- 241000699670 Mus sp. Species 0.000 description 6
- 150000004676 glycans Chemical class 0.000 description 6
- 229920001282 polysaccharide Polymers 0.000 description 6
- 239000005017 polysaccharide Substances 0.000 description 6
- 241001465754 Metazoa Species 0.000 description 5
- 230000035611 feeding Effects 0.000 description 5
- 238000010171 animal model Methods 0.000 description 4
- 230000037396 body weight Effects 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 230000002265 prevention Effects 0.000 description 4
- 208000008589 Obesity Diseases 0.000 description 3
- 210000000577 adipose tissue Anatomy 0.000 description 3
- 235000005911 diet Nutrition 0.000 description 3
- 230000037213 diet Effects 0.000 description 3
- 230000037406 food intake Effects 0.000 description 3
- 235000012631 food intake Nutrition 0.000 description 3
- 201000001421 hyperglycemia Diseases 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 235000020824 obesity Nutrition 0.000 description 3
- 206010036067 polydipsia Diseases 0.000 description 3
- 238000007619 statistical method Methods 0.000 description 3
- 150000008163 sugars Chemical class 0.000 description 3
- 208000024891 symptom Diseases 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000003110 anti-inflammatory effect Effects 0.000 description 2
- 238000009395 breeding Methods 0.000 description 2
- 230000001488 breeding effect Effects 0.000 description 2
- 239000000872 buffer Substances 0.000 description 2
- 230000007850 degeneration Effects 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 230000035622 drinking Effects 0.000 description 2
- 239000003651 drinking water Substances 0.000 description 2
- 235000020188 drinking water Nutrition 0.000 description 2
- 230000002496 gastric effect Effects 0.000 description 2
- 230000002440 hepatic effect Effects 0.000 description 2
- 210000003734 kidney Anatomy 0.000 description 2
- 150000002632 lipids Chemical class 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000001543 one-way ANOVA Methods 0.000 description 2
- 210000000056 organ Anatomy 0.000 description 2
- 239000001814 pectin Substances 0.000 description 2
- 229920001277 pectin Polymers 0.000 description 2
- 235000010987 pectin Nutrition 0.000 description 2
- 150000003254 radicals Chemical class 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 210000000582 semen Anatomy 0.000 description 2
- OESFSXYRSCBAQJ-UHFFFAOYSA-M sodium;3-carboxy-3,5-dihydroxy-5-oxopentanoate;2-hydroxypropane-1,2,3-tricarboxylic acid Chemical compound [Na+].OC(=O)CC(O)(C(O)=O)CC(O)=O.OC(=O)CC(O)(C(O)=O)CC([O-])=O OESFSXYRSCBAQJ-UHFFFAOYSA-M 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 210000004003 subcutaneous fat Anatomy 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 206010000060 Abdominal distension Diseases 0.000 description 1
- 206010002091 Anaesthesia Diseases 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 235000019750 Crude protein Nutrition 0.000 description 1
- AEMOLEFTQBMNLQ-YMDCURPLSA-N D-galactopyranuronic acid Chemical compound OC1O[C@H](C(O)=O)[C@H](O)[C@H](O)[C@H]1O AEMOLEFTQBMNLQ-YMDCURPLSA-N 0.000 description 1
- IAJILQKETJEXLJ-UHFFFAOYSA-N Galacturonsaeure Natural products O=CC(O)C(O)C(O)C(O)C(O)=O IAJILQKETJEXLJ-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
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 208000004880 Polyuria Diseases 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 210000001015 abdomen Anatomy 0.000 description 1
- 210000000683 abdominal cavity Anatomy 0.000 description 1
- 230000037005 anaesthesia Effects 0.000 description 1
- 210000005252 bulbus oculi Anatomy 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000007979 citrate buffer Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 235000021316 daily nutritional intake Nutrition 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000013872 defecation Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 235000013325 dietary fiber Nutrition 0.000 description 1
- 102000038379 digestive enzymes Human genes 0.000 description 1
- 108091007734 digestive enzymes Proteins 0.000 description 1
- 235000020776 essential amino acid Nutrition 0.000 description 1
- 239000003797 essential amino acid Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000013376 functional food Nutrition 0.000 description 1
- 210000002216 heart Anatomy 0.000 description 1
- 235000009200 high fat diet Nutrition 0.000 description 1
- 238000007602 hot air drying Methods 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000003859 lipid peroxidation Effects 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- XZWYZXLIPXDOLR-UHFFFAOYSA-N metformin Chemical compound CN(C)C(=N)NC(N)=N XZWYZXLIPXDOLR-UHFFFAOYSA-N 0.000 description 1
- 229960003105 metformin Drugs 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920005615 natural polymer Polymers 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 206010033675 panniculitis Diseases 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002504 physiological saline solution Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 235000019633 pungent taste Nutrition 0.000 description 1
- 238000011552 rat model Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000003307 slaughter Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 210000000952 spleen Anatomy 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 210000001519 tissue Anatomy 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 230000003442 weekly effect Effects 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
- 208000016261 weight loss Diseases 0.000 description 1
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- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/14—Preparation of compounds containing saccharide radicals produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase, e.g. by cellulase, hemicellulase
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- A23L33/125—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives containing carbohydrate syrups; containing sugars; containing sugar alcohols; containing starch hydrolysates
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Abstract
Description
本発明は機能性食品加工の技術分野に関し、特に、多酵素によるコンニャク精粉酵素分解物及びその製造方法に関する。 The present invention relates to the technical field of functional food processing, and more particularly to a konjac fine powder enzymatic decomposition product by a multienzyme and a method for producing the same.
コンニャクは高い機能性と医学的価値を有している。現代の研究によれば、コンニャクの塊茎の主な化学成分は、グルコマンナン、デンプン、その他の多糖、粗蛋白、必須アミノ酸や、カリウム、カルシウム、マグネシウム、ナトリウム、鉄、マンガン、銅等の人体に必須の多種の微量元素である。 Konjac has high functionality and medical value. According to modern research, the main chemical constituents of konjac stalks are glucomannan, starch, other polysaccharides, crude proteins, essential amino acids, and the human body such as potassium, calcium, magnesium, sodium, iron, manganese, and copper. It is an essential trace element.
コンニャクのグルコマンナンは、デンプンやセルロースに続く豊富な再生可能天然高分子資源であり、生分解性と水溶性を有している。グルコマンナンは、分子量が大きく、最高の粘度を有する自然界の食物繊維であり、自身の体積の200倍もの水分子を吸着して粘性の溶液を形成可能なことから、満腹感を高めることが可能である。また、人体の消化酵素の影響を受けないため、熱量を発生することがない。つまり、グルコマンナンは周知の可溶性且つ多機能性の多糖であり、適度に分解することで機能がより強化されたコンニャクオリゴ糖を生成することも可能である。しかし、グルコマンナンは吸水膨張や溶解の速度が遅く、通常は2時間以上を要する。 Konjac glucomannan is a rich renewable natural polymer resource following starch and cellulose, and has biodegradability and water solubility. Glucomannan is a natural dietary fiber with a large molecular weight and the highest viscosity, and can adsorb 200 times as much water molecules as its own volume to form a viscous solution, which can enhance the feeling of fullness. Is. Moreover, since it is not affected by digestive enzymes of the human body, it does not generate calories. That is, glucomannan is a well-known soluble and multifunctional polysaccharide, and it is also possible to produce a konjac oligosaccharide having a more enhanced function by appropriately decomposing it. However, glucomannan has a slow rate of water absorption expansion and dissolution, and usually takes 2 hours or more.
現在、コンニャクのグルコマンナンの酵素分解には、次のような最適化を要する課題が存在する。(1)単一酵素による酵素分解のため酵素使用量が多く、酵素分解に過剰な時間を要する。また、コンニャク精粉の利用率が低い。(2)一部の酵素分解法では還元糖の検出を主な指標としており、還元糖の量の多さがオリゴ糖の含有量の多さを意味しない。反対に、可溶性固形物の含有量が同一であることを前提に、還元糖の含有量が多いほどオリゴ糖の含有量は少なくなる。よって、このような酵素分解技術の場合には、オリゴ糖を製造する意味がない。(3)一部の酵素分解法は実験室での研究にのみ応用可能であり、本格生産への導入が不可能である。(4)コンニャク精粉は吸水膨張との特性を有するため、分解しないまま食すると腹部膨満感が発生しやすく、一定の安全上のリスクが存在する。しかし、このような欠点は適度に分解することで解消され、且つ溶解速度を高めつつ、従来の機能特性を維持することも可能である。 Currently, the enzymatic degradation of konjac glucomannan presents the following issues that require optimization. (1) Since the enzyme is decomposed by a single enzyme, the amount of enzyme used is large, and the enzyme decomposition requires an excessive amount of time. In addition, the utilization rate of konjac fine powder is low. (2) In some enzymatic decomposition methods, the detection of reducing sugars is the main index, and a large amount of reducing sugars does not mean a large amount of oligosaccharides. On the contrary, on the premise that the contents of soluble solids are the same, the higher the content of reducing sugars, the lower the content of oligosaccharides. Therefore, in the case of such an enzymatic decomposition technique, there is no point in producing oligosaccharides. (3) Some enzymatic decomposition methods can be applied only to laboratory research and cannot be introduced into full-scale production. (4) Since konjac fine powder has a characteristic of water absorption and expansion, a feeling of abdominal bloating is likely to occur if it is eaten without decomposition, and there is a certain safety risk. However, such a defect can be eliminated by appropriately decomposing, and it is possible to maintain the conventional functional characteristics while increasing the dissolution rate.
本発明は、多酵素によるコンニャク精粉酵素分解物及びその製造方法を提供することを目的とする。これによれば、従来技術における酵素分解時間が長く、酵素分解が不完全であり、コンニャク精粉の利用率が低いといった欠点が解消され、一定の速溶性を持つ多糖及びオリゴ糖を含有する酵素分解産物が得られる。 An object of the present invention is to provide a polyenzymatic konjac fine powder enzymatic decomposition product and a method for producing the same. According to this, the drawbacks such as long enzymatic decomposition time, incomplete enzymatic decomposition, and low utilization rate of konjac fine powder in the prior art are eliminated, and an enzyme containing a polysaccharide and an oligosaccharide having a certain rapid solubility is eliminated. Degradation products are obtained.
上記の発明の目的を実現するために、本発明は以下の技術手段を提供する。 In order to realize the object of the above invention, the present invention provides the following technical means.
本発明は、多酵素によるコンニャク精粉酵素分解物の製造方法を提供する。当該製造方法は、(1)コンニャク精粉原料をアルコール中で精製することで、コンニャク湿潤精粉を取得するステップと、(2)コンニャク湿潤精粉をアルコール除去処理することで、精製コンニャク精粉を取得するステップと、(3)取得した精製コンニャク精粉と水及び酵素を混合して酵素分解を行うことで、多酵素によるコンニャク精粉酵素分解物を取得するステップ、を含む。 The present invention provides a method for producing a konjac fine powder enzymatic decomposition product using multiple enzymes. The production method is as follows: (1) Purifying the konjak refined raw material in alcohol to obtain konjak wet semen, and (2) Purifying the konjak moistened powder with alcohol removal treatment. (3) The step of obtaining the enzymatically decomposed konjak powder by multiple enzymes by mixing the obtained purified konjak powder with water and an enzyme and performing enzymatic decomposition is included.
好ましくは、前記ステップ(1)におけるアルコールの体積濃度は55〜75%とする。前記ステップ(1)におけるコンニャク精粉原料とアルコールとの固液比率は1g:3〜5mlとし、前記ステップ(1)における精製時間は1〜3hとする。また、前記ステップ(2)におけるアルコール除去処理の温度は50〜70℃とする。 Preferably, the volume concentration of alcohol in the step (1) is 55 to 75%. The solid-liquid ratio of the konjac refined powder raw material and alcohol in the step (1) is 1 g: 3 to 5 ml, and the purification time in the step (1) is 1 to 3 hours. The temperature of the alcohol removal treatment in the step (2) is 50 to 70 ° C.
好ましくは、前記ステップ(3)における精製コンニャク精粉と水との質量体積比は15〜30g:100mLとする。前記ステップ(3)における酵素は、グルコマンナナーゼ、セルラーゼ及びペクターゼを含む。前記グルコマンナナーゼの用量は精製コンニャク精粉に対し50〜70u/gとし、前記セルラーゼの用量は精製コンニャク精粉に対し40〜60u/gとし、前記ペクターゼは体系総質量の0.03〜0.05%を占める。前記酵素分解の温度は55〜65℃とし、酵素分解時間は2〜3hとする。 Preferably, the mass-volume ratio of the purified konjac fine powder to water in the step (3) is 15 to 30 g: 100 mL. The enzyme in step (3) includes glucomannanase, cellulase and pectase. The dose of the glucomannanase was 50 to 70 u / g with respect to the purified konjac refined powder, the dose of the cellulase was 40 to 60 u / g with respect to the purified konjac refined powder, and the pectase was 0.03 to 0. It accounts for 05%. The temperature of the enzymatic decomposition is 55 to 65 ° C., and the enzymatic decomposition time is 2 to 3 hours.
本発明は、更に、上記の製造方法で取得する多酵素によるコンニャク精粉酵素分解物を提供する。 The present invention further provides a konjac fine powder enzymatic decomposition product obtained by the above-mentioned production method.
本発明は、多酵素によるコンニャク精粉酵素分解物及びその製造方法を提供する。本方法により得られる酵素分解物中の機能成分(例えばオリゴ糖)の含有量は、精粉100gに対し5.69〜5.86gであり、糖含有量全体の39.33〜40.5%を占める。また、一定の速溶性を持つ多糖を更に含有する。当該製品は、肥満予防、血中脂質の低下、肝脂肪変性の予防といった作用を有する。また、血糖の低下、抗炎症、生体におけるフリーラジカル除去の向上といった作用を有し、糖尿病モデルラットの高血糖に対し改善作用を有する。 The present invention provides a konjac fine powder enzymatic decomposition product using multiple enzymes and a method for producing the same. The content of the functional component (for example, oligosaccharide) in the enzymatic decomposition product obtained by this method is 5.69 to 5.86 g with respect to 100 g of the refined powder, and 39.33 to 40.5% of the total sugar content. Occupy. In addition, it further contains a polysaccharide having a certain rapid solubility. The product has actions such as prevention of obesity, reduction of blood lipids, and prevention of hepatic fatty degeneration. In addition, it has effects such as lowering blood glucose, anti-inflammatory, and improving free radical removal in the living body, and has an improving effect on hyperglycemia in diabetic model rats.
本発明によれば、コンニャク精粉を原料とし、複合酵素を用いて酵素分解を行うことで、酵素分解過程が加速し、酵素分解効率が向上するとともに、酵素分解産物の品質が向上する。プロセスパラメータを最適化することで、使用酵素の選択、酵素用量、酵素分解時間等の生産プロセスパラメータが合理化され、且つ一定の速溶性を持つ多糖及びオリゴ糖を含有する酵素分解産物が得られる。 According to the present invention, by performing enzymatic decomposition using konjac refined powder as a raw material and using a complex enzyme, the enzymatic decomposition process is accelerated, the enzymatic decomposition efficiency is improved, and the quality of the enzymatic decomposition product is improved. By optimizing the process parameters, production process parameters such as selection of enzyme to be used, enzyme dose, and enzymatic decomposition time can be rationalized, and an enzymatic decomposition product containing a polysaccharide and an oligosaccharide having a certain rapid solubility can be obtained.
本発明は、以下のステップを含む多酵素によるコンニャク精粉酵素分解物の製造方法を提供する。 The present invention provides a method for producing a konjac fine powder enzymatic decomposition product by a multienzyme, which comprises the following steps.
(1)コンニャク精粉原料をアルコール中で精製することで、コンニャク湿潤精粉を取得する。 (1) Konjac wet fine powder is obtained by purifying the raw material of konjac fine powder in alcohol.
(2)コンニャク湿潤精粉をアルコール除去処理することで、精製コンニャク精粉を取得する。 (2) Purified konjak fine powder is obtained by treating the wet konjak fine powder with alcohol.
(3)取得した精製コンニャク精粉と水及び酵素を混合して酵素分解を行うことで、多酵素によるコンニャク精粉酵素分解物を取得する。 (3) The obtained purified konjak refined powder is mixed with water and an enzyme and enzymatically decomposed to obtain an enzymatically decomposed konjak refined powder by multiple enzymes.
本発明において、前記コンニャク精粉は、市販の高純度のコンニャク精粉とすることが好ましい。 In the present invention, the konjak refined powder is preferably a commercially available high-purity konjak refined powder.
本発明において、前記ステップ(1)のアルコールの体積濃度は55〜75%とすることが好ましく、より好ましくは60〜70%、更に好ましくは62〜68%とする。 In the present invention, the volume concentration of alcohol in step (1) is preferably 55 to 75%, more preferably 60 to 70%, and even more preferably 62 to 68%.
本発明において、前記ステップ(1)のコンニャク精粉原料とアルコールとの固液比率は1g:3〜5mlとすることが好ましく、より好ましくは1g:3.5〜4.5mlとする。 In the present invention, the solid-liquid ratio of the konjac refined powder raw material and alcohol in the step (1) is preferably 1 g: 3 to 5 ml, and more preferably 1 g: 3.5 to 4.5 ml.
本発明において、前記ステップ(1)の精製時間は1〜3hとすることが好ましく、より好ましくは1.5〜2.5hとする。 In the present invention, the purification time of the step (1) is preferably 1 to 3 hours, more preferably 1.5 to 2.5 hours.
本発明において、前記精製では、コンニャク精粉原料をアルコールと攪拌して均一に混合し、浸漬することが好ましい。 In the present invention, in the purification, it is preferable that the raw material of konjak refined powder is stirred with alcohol to be uniformly mixed and immersed.
本発明において、前記精製は、コンニャク精粉に含まれる生臭さ、辛味、SO2等を除去するためのものである。 In the present invention, the purification is for removing fishy odor, pungent taste, SO 2, etc. contained in konjac fine powder.
本発明において、前記アルコール除去処理は、熱風乾燥を手段として行うことが好ましい。 In the present invention, the alcohol removal treatment is preferably carried out by hot air drying as a means.
本発明において、前記アルコール除去処理の温度は50〜70℃とすることが好ましく、より好ましくは55〜65℃、更に好ましくは58〜62℃とする。 In the present invention, the temperature of the alcohol removal treatment is preferably 50 to 70 ° C, more preferably 55 to 65 ° C, and even more preferably 58 to 62 ° C.
本発明において、前記アルコール除去処理はアルコール臭を除去するためのものであって、アルコール臭を感じなくなることを基準とする。 In the present invention, the alcohol removal treatment is for removing the alcohol odor, and is based on the fact that the alcohol odor is no longer felt.
本発明において、前記ステップ(3)の精製コンニャク精粉と水との質量体積比は15〜30g:100mLとすることが好ましく、より好ましくは20〜25g:100mLとする。 In the present invention, the mass-volume ratio of the purified konjac fine powder in step (3) to water is preferably 15 to 30 g: 100 mL, and more preferably 20 to 25 g: 100 mL.
本発明において、前記ステップ(3)の酵素は、グルコマンナナーゼ、セルラーゼ及びペクターゼを含むことが好ましい。 In the present invention, the enzyme of step (3) preferably contains glucomannanase, cellulase and pectase.
本発明において、前記グルコマンナナーゼの用量は、精製コンニャク精粉に対し50〜70u/gとすることが好ましく、より好ましくは、精製コンニャク精粉に対し55〜65u/g、更に好ましくは、精製コンニャク精粉に対し60〜62u/gとする。前記セルラーゼの用量は、精製コンニャク精粉に対し40〜60u/gとすることが好ましく、より好ましくは、精製コンニャク精粉に対し45〜55u/g、更に好ましくは、精製コンニャク精粉に対し47〜52u/gとする。前記ペクターゼの用量は、体系総質量の0.03〜0.05%とすることが好ましく、より好ましくは、体系総質量の0.035〜0.04%とする。 In the present invention, the dose of the glucomannanase is preferably 50 to 70 u / g with respect to the purified konjac fine powder, more preferably 55 to 65 u / g with respect to the purified konjac fine powder, and further preferably the purified konjac. It is set to 60 to 62 u / g with respect to the refined powder. The dose of the cellulase is preferably 40 to 60 u / g with respect to the purified konjac powder, more preferably 45 to 55 u / g with respect to the purified konjac powder, and further preferably 47 with respect to the purified konjac powder. ~ 52u / g. The dose of the pectase is preferably 0.03 to 0.05% of the total mass of the system, and more preferably 0.035 to 0.04% of the total mass of the system.
本発明において、前記体系とは、精製コンニャク精粉、酵素及び水を混合して得られる混合物のことをいう。 In the present invention, the system refers to a mixture obtained by mixing purified konjac fine powder, an enzyme and water.
本発明において、前記酵素分解の温度は55〜65℃とすることが好ましく、より好ましくは58〜60℃とする。また、好ましくは、酵素分解時間は2〜3hとする。 In the present invention, the temperature of the enzymatic decomposition is preferably 55 to 65 ° C, more preferably 58 to 60 ° C. Further, preferably, the enzymatic decomposition time is set to 2 to 3 hours.
本発明における前記酵素分解の原理としては、酵素の特異性に基づいて、グルコマンナナーゼとセルラーゼを同時に使用することで、グルコマンナンを低重合度のコンニャク多糖及びコンニャクオリゴ糖に酵素分解する。また、ペクターゼがペクチンをガラクツロン酸に分解することで、コンニャク精粉の粒子構造が破壊されるため、その他の酵素の作用効果が向上する。 The principle of the enzymatic decomposition in the present invention is that glucomannan is enzymatically decomposed into konjac polysaccharide and konjac oligosaccharide having a low degree of polymerization by using glucomannanase and cellulase at the same time based on the specificity of the enzyme. In addition, pectin decomposes pectin into galacturonic acid, which destroys the particle structure of konjac fine powder, thereby improving the action and effect of other enzymes.
本発明は、更に、上記の製造方法で取得する多酵素によるコンニャク精粉酵素分解物を提供する。 The present invention further provides a konjac fine powder enzymatic decomposition product obtained by the above-mentioned production method.
以下に、実施例を組み合わせて、本発明で提供する技術手段につき詳細に説明するが、本発明の保護の範囲を限定するものと理解すべきではない。 Hereinafter, the technical means provided by the present invention will be described in detail in combination with examples, but it should not be understood as limiting the scope of protection of the present invention.
ステップ1:精製:コンニャク精粉原料を体積濃度55%のアルコール中で精製した。コンニャク精粉原料とアルコールとの固液比率は1g:3mlとし、1h精製することでコンニャク湿潤精粉を取得した。 Step 1: Purification: The konjac fine powder raw material was purified in alcohol having a volume concentration of 55%. The solid-liquid ratio of the konjak refined powder raw material to alcohol was 1 g: 3 ml, and the konjak wet fine powder was obtained by purifying for 1 hour.
ステップ2:アルコール除去:コンニャク湿潤精粉をアルコール除去処理した。アルコール除去温度は50℃とし、アルコール除去することで精製コンニャク精粉を取得した。 Step 2: Alcohol removal: Konjac wet powder was treated with alcohol removal. The alcohol removal temperature was set to 50 ° C., and the purified konjac fine powder was obtained by removing the alcohol.
ステップ3:酵素分解:精製コンニャク精粉を15g取って100mLの水を加え、更に、グルコマンナナーゼ、セルラーゼ及びペクターゼを加えて酵素分解を行った。グルコマンナナーゼの用量は精製コンニャク精粉に対し50u/g、セルラーゼの用量は精製コンニャク精粉に対し40u/gとした。また、ペクターゼの用量は体系総質量の0.03%とした。条件を55℃として2h酵素分解することで、多酵素によるコンニャク精粉酵素分解物を取得した。 Step 3: Enzymatic decomposition: 15 g of purified konjac fine powder was taken, 100 mL of water was added, and glucomannanase, cellulase and pectase were further added for enzymatic decomposition. The dose of glucomannanase was 50 u / g with respect to purified konjac fine powder, and the dose of cellulase was 40 u / g with respect to purified konjac fine powder. The dose of pectase was 0.03% of the total mass of the system. By enzymatically decomposing for 2 hours under the condition of 55 ° C., a konjac fine powder enzymatically decomposed product by multiple enzymes was obtained.
取得した酵素分解物中の機能成分(オリゴ糖)の含有量は、精粉100gに対し5.86gであり、糖含有量全体の40.5%を占めていた。 The content of the functional component (oligosaccharide) in the obtained enzymatic decomposition product was 5.86 g with respect to 100 g of the refined powder, accounting for 40.5% of the total sugar content.
ステップ1:精製:コンニャク精粉原料を体積濃度60%のアルコール中で精製した。コンニャク精粉原料とアルコールとの固液比率は1g:4mlとし、1.5h精製することでコンニャク湿潤精粉を取得した。 Step 1: Purification: The konjac fine powder raw material was purified in alcohol having a volume concentration of 60%. The solid-liquid ratio of the konjac fine powder raw material to alcohol was 1 g: 4 ml, and the konjak wet fine powder was obtained by purifying for 1.5 hours.
ステップ2:アルコール除去:コンニャク湿潤精粉をアルコール除去処理した。アルコール除去温度は65℃とし、アルコール除去することで精製コンニャク精粉を取得した。 Step 2: Alcohol removal: Konjac wet powder was treated with alcohol removal. The alcohol removal temperature was 65 ° C., and the purified konjac fine powder was obtained by removing the alcohol.
ステップ3:酵素分解:精製コンニャク精粉を25g取って100mLの水を加え、更に、グルコマンナナーゼ、セルラーゼ及びペクターゼを加えて酵素分解を行った。グルコマンナナーゼの用量は精製コンニャク精粉に対し60u/g、セルラーゼの用量は精製コンニャク精粉に対し50u/gとした。また、ペクターゼの用量は体系総質量の0.04%とした。条件を60℃として2.5h酵素分解することで、多酵素によるコンニャク精粉酵素分解物を取得した。 Step 3: Enzymatic decomposition: 25 g of purified konjac fine powder was taken, 100 mL of water was added, and glucomannanase, cellulase and pectase were further added for enzymatic decomposition. The dose of glucomannanase was 60 u / g with respect to purified konjac fine powder, and the dose of cellulase was 50 u / g with respect to purified konjac fine powder. The dose of pectase was 0.04% of the total mass of the system. By enzymatically decomposing for 2.5 hours under the condition of 60 ° C., a konjac fine powder enzymatic decomposition product by multiple enzymes was obtained.
取得した酵素分解物中の機能成分(オリゴ糖)の含有量は、精粉100gに対し5.78gであり、糖含有量全体の39.95%を占めていた。 The content of the functional component (oligosaccharide) in the obtained enzymatic decomposition product was 5.78 g with respect to 100 g of the refined powder, accounting for 39.95% of the total sugar content.
ステップ1:精製:コンニャク精粉原料を体積濃度75%のアルコール中で精製した。コンニャク精粉原料とアルコールとの固液比率は1g:5mlとし、3h精製することでコンニャク湿潤精粉を取得した。 Step 1: Purification: The konjac fine powder raw material was purified in alcohol having a volume concentration of 75%. The solid-liquid ratio of the konjak refined powder raw material to alcohol was 1 g: 5 ml, and the konjak wet fine powder was obtained by purifying for 3 hours.
ステップ2:アルコール除去:コンニャク湿潤精粉をアルコール除去処理した。アルコール除去温度は70℃とし、アルコール除去することで精製コンニャク精粉を取得した。 Step 2: Alcohol removal: Konjac wet powder was treated with alcohol removal. The alcohol removal temperature was set to 70 ° C., and the purified konjac fine powder was obtained by removing the alcohol.
ステップ3:酵素分解:精製コンニャク精粉を30g取って100mLの水を加え、更に、グルコマンナナーゼ、セルラーゼ及びペクターゼを加えて酵素分解を行った。グルコマンナナーゼの用量は精製コンニャク精粉に対し70u/g、セルラーゼの用量は精製コンニャク精粉に対し60u/gとした。また、ペクターゼの用量は体系総質量の0.05%とした。条件を65℃として3h酵素分解することで、多酵素によるコンニャク精粉酵素分解物を取得した。 Step 3: Enzymatic decomposition: 30 g of purified konjac fine powder was taken, 100 mL of water was added, and glucomannanase, cellulase and pectase were further added for enzymatic decomposition. The dose of glucomannanase was 70 u / g with respect to the purified konjac powder, and the dose of cellulase was 60 u / g with respect to the purified konjac powder. The dose of pectase was 0.05% of the total mass of the system. By enzymatically decomposing for 3 hours under the condition of 65 ° C., a konjac fine powder enzymatically decomposed product by multiple enzymes was obtained.
取得した酵素分解物中の機能成分(オリゴ糖)の含有量は、精粉100gに対し5.69gであり、糖含有量全体の39.33%を占めていた。 The content of the functional component (oligosaccharide) in the obtained enzymatic decomposition product was 5.69 g with respect to 100 g of the refined powder, accounting for 39.33% of the total sugar content.
実施例1〜3で製造した多酵素によるコンニャク精粉酵素分解物について動物実験を行った。 Animal experiments were carried out on the enzymatic decomposition products of konjac fine powder produced by the polyenzymes produced in Examples 1 to 3.
ステップ1:動物モデルの作製及び群分け
健康なメスのマウス50匹を選択し、一般飼料を2週間給餌したあと、ブランク対照群10匹(一般飼料を給餌)とモデル対照群40匹(高脂質飼料を給餌)の2群にランダムに分けた。次に、両群ともに制限なく飼料を与え、4週間飼育することでマウス肥満モデルを作製した。そして、モデル対照群を、10匹ずつ高脂質モデル群(高脂質飼料を給餌)、コンニャク精粉酵素分解物低投与量群(高脂質飼料を給餌し、且つ酵素分解物15mg・100g−1(BW)・d−1を胃内投与)、コンニャク精粉酵素分解物中投与量群(高脂質飼料を給餌し、且つ酵素分解物30mg・100g−1(BW)・d−1を胃内投与)、コンニャク精粉酵素分解物高投与量群(高脂質飼料を給餌し、且つ酵素分解物60mg・100g−1(BW)・d−1を胃内投与)の4群に任意に分けた。続いて、ブランク対照群のマウスには引き続き一般飼料を給餌した一方、高脂質モデル群及びコンニャク精粉酵素分解物低・中・高投与量群のマウスには引き続き高脂質飼料を給餌した。また、1か月連続でコンニャク精粉酵素分解物を胃内投与した。飼育温度は24〜27℃、相対湿度は45〜50%とし、昼夜比率11h:13hの断続照明を使用した。
Step 1: Preparation and grouping of animal models 50 healthy female mice were selected and fed with a general diet for 2 weeks, followed by 10 blank control groups (fed with a general diet) and 40 model control groups (high fat). The feed was randomly divided into two groups (feeding). Next, a mouse obesity model was prepared by feeding unlimited feeds in both groups and breeding them for 4 weeks. Then, the model control group was divided into a high-lipid model group (fed with a high-fat feed) and a low-dose group of enzyme-degraded konyaku fine powder (fed with a high-fat feed, and the enzymatic decomposition product was 15 mg / 100 g -1 (fed). BW) · d -1 was administered intragastrically), and the dose group in the enzyme degradation product of Konnaku semen (fed a high-lipid feed, and the enzymatic degradation product 30 mg · 100 g -1 (BW) · d -1 was intragastrically administered. ), And the enzyme-degraded product high-dose group (feeding a high-lipid feed and intragastrically administering the enzyme-degraded product 60 mg, 100 g -1 (BW), d -1). Subsequently, the mice in the blank control group were continuously fed with a general diet, while the mice in the high-fat model group and the low-, medium-, and high-dose groups of konjac fine powder enzyme decomposition products were continuously fed with a high-fat diet. In addition, the enzymatic decomposition product of konjac fine powder was intragastrically administered for 1 consecutive month. The breeding temperature was 24 to 27 ° C., the relative humidity was 45 to 50%, and intermittent lighting with a day / night ratio of 11h: 13h was used.
ステップ2:サンプル採集
給餌10週間後に各群のマウスを12h絶食させ、殺処理前に体重を測定した。そして、麻酔後に素早く眼球を摘出して採血し、頸椎脱臼により殺処理した。次に、肝臓、心臓、脾臓、腎臓、肺、腎周囲脂肪及び鼠蹊部皮下脂肪を素早く分離して、塩水で器官を洗浄してから濾紙で水を除去し、臓器及び組織の重量を測定した。
Step 2: Sample collection 10 weeks after feeding, mice in each group were fasted for 12 hours and weighed before slaughter. Then, after anesthesia, the eyeball was quickly removed, blood was collected, and the blood was killed by dislocation of the cervical spine. Next, the liver, heart, spleen, kidneys, lungs, perineal fat and subcutaneous fat in the inguinal region were quickly separated, the organs were washed with salt water, the water was removed with filter paper, and the weights of the organs and tissues were weighed. ..
ステップ3:指標の測定
実験期間中は、マウスの成長状態(マウスの毛色、摂食、排便及び活動)を毎日記録した。また、水曜日と木曜日にそれぞれマウスの1日当たりの摂食量と飲水量を測定した。つまり、水曜日と木曜日に飼料の総量と給水総量を測定し、木曜日と金曜日の同一時間に飼料の残量と水の残量を測定した(即ち、摂食量=飼料の総量−飼料の残量、飲水量=水の総量−水の残量)。また、毎週土曜日に体重を1回測定した。
Step 3: Measurement of indicators During the experimental period, mouse growth status (mouse coat color, feeding, defecation and activity) was recorded daily. In addition, the daily food intake and water intake of the mice were measured on Wednesday and Thursday, respectively. That is, the total amount of feed and the total amount of water supplied were measured on Wednesday and Thursday, and the remaining amount of feed and the remaining amount of water were measured at the same time on Thursday and Friday (that is, the amount of food intake = the total amount of feed-the remaining amount of feed). Drinking amount = total amount of water-remaining amount of water). In addition, the body weight was measured once every Saturday.
腹部を切開し、マウス体内の全ての脂肪(腎周囲の脂肪組織及び鼠蹊部の皮下脂肪組織を含む)を摘出して脂肪を測定し、式(1)に基づき脂肪指数を算出した。 The abdomen was incised, all the adipose tissue in the mouse body (including the adipose tissue around the kidney and the subcutaneous adipose tissue in the inguinal region) was removed, the fat was measured, and the fat index was calculated based on the formula (1).
脂肪指数/%=m1/m×100 (1) Fat index /% = m 1 / m x 100 (1)
式中、mはマウスの殺処理前の体重/g、m1はマウス体内の各脂肪組織の質量/gである。 In the formula, m is the body weight / g of the mouse before the killing treatment, and m 1 is the mass / g of each adipose tissue in the mouse body.
ステップ4:データ処理
ソフトウェアのSPSS20で統計分析を行い、平均値±標準偏差で表した。群間比較には一元配置分散分析を用いた。P<0.05は2つの群に有意差があることを示す。
Step 4: Statistical analysis was performed with the data processing software SPSS20 and expressed as mean ± standard deviation. One-way ANOVA was used for group-to-group comparison. P <0.05 indicates that there is a significant difference between the two groups.
表1から明らかなように、高脂質モデル群とコンニャク酵素分解物低・中・高投与量群の間には有意な差がみられた(P<0.05)。このことは、コンニャク酵素分解物がマウスの飲水量を一定程度減少させられることを意味する。なお、コンニャク酵素分解物高投与量群の効果が最も顕著であった。 As is clear from Table 1, there was a significant difference between the high-lipid model group and the low-, medium-, and high-dose groups of konjac enzymatic degradation products (P <0.05). This means that konjac enzymatic degradation products can reduce the amount of water consumed by mice to some extent. The effect of the high dose group of konjac enzymatic decomposition products was the most remarkable.
実施例1〜3で製造した多酵素によるコンニャク精粉酵素分解物について動物実験を行った。 Animal experiments were carried out on the enzymatic decomposition products of konjac fine powder produced by the polyenzymes produced in Examples 1 to 3.
ステップ1:糖尿病ラットモデルの作製
60匹の健康なメスのラットを1週間正常に飼育した。また、期間中は実験動物の飲水量と摂食量を定期的に測定した。1週間後に実験動物の体重と空腹時血糖値を測定して記録し、10匹ずつランダムに群分けした(正常対照群及び5つのモデル群)。モデル群のラットには、STZを含有するクエン酸−クエン酸ナトリウム緩衝液を腹腔注射して糖尿病を誘発した(予め冷却しておいたクエン酸塩緩衝液pH=4.5を用い、濃度1%でSTZを溶解したあと、0.22mol/Lの精密ろ過膜でろ過して除菌した。STZは活性を喪失しやすいため、素早く計量したあと錫箔で包んで遮光した。また、準備したものをその場で使用するようにし、常に氷浴内で待機させた)。注射するSTZの濃度は45mg/kg、注射量は2%とした。一方、正常群のラットには等体積のクエン酸−クエン酸ナトリウム緩衝液を腹腔注射した。また、STZの注射過程では、感染防止のためラットの腹腔の皮膚を消毒する必要があった。注射完了後、各群は引き続きこれまでの飲食を維持した。そして、24h後にラットの尾部から採血し、空腹時血糖値を測定した。血糖計及び血糖試験紙キットを用いてラットの空腹時血糖値を測定したところ、モデル群のラットの空腹時血糖値は>16.7mmol/Lであった(2〜3回繰り返し測定可能としたが、血糖値は安定していた)。且つ、多飲多尿や体重減少が症状として発生したため、モデル作製に成功したとみなした。
Step 1: Creating a diabetic rat model 60 healthy female rats were successfully bred for 1 week. In addition, during the period, the amount of water consumed and the amount of food consumed by the experimental animals were measured regularly. One week later, the body weight and fasting blood glucose level of the experimental animals were measured and recorded, and 10 animals were randomly grouped (normal control group and 5 model groups). Rats in the model group were intraperitoneally injected with STZ-containing citrate-sodium citrate buffer to induce diabetes (pre-cooled citrate buffer pH = 4.5 was used and a concentration of 1). After dissolving STZ in%, it was sterilized by filtering with a microfiltration membrane of 0.22 mol / L. Since STZ tends to lose its activity, it was quickly weighed and then wrapped in tin foil to shield it from light. Was used on the spot and was always kept waiting in the ice bath). The concentration of STZ to be injected was 45 mg / kg, and the injection amount was 2%. On the other hand, rats in the normal group were intraperitoneally injected with an equal volume of citrate-sodium citrate buffer. In addition, during the STZ injection process, it was necessary to disinfect the skin of the abdominal cavity of the rat to prevent infection. After the injection was completed, each group continued to maintain their previous eating and drinking. Then, 24 hours later, blood was collected from the tail of the rat, and the fasting blood glucose level was measured. When the fasting blood glucose level of the rats was measured using a glucose meter and a blood glucose test paper kit, the fasting blood glucose level of the rats in the model group was> 16.7 mmol / L (it was possible to measure repeatedly 2-3 times). However, the blood sugar level was stable). Moreover, since polydipsia and polyuria and weight loss occurred as symptoms, it was considered that the model was successfully created.
ステップ2:動物の群分け及び投薬
モデル作製に成功した糖尿病ラットを、コンニャク精粉酵素分解物高・中・低投与量群、ポジティブ投与群、糖尿病モデル群にそれぞれ群分け及び調整した。また、血糖値がモデル作製前と同一のラットを正常群とした。次に、6週間連続で胃内投与を行った。実験期間中、各群のラットには通常通り自由に飲水及び摂食させた。胃内投与の時間は毎日午後4時であった。また、各群のラットに対する胃内投与量については、コンニャク精粉酵素分解物高・中・低群がそれぞれ2.500g/(kg・d)、1.250g/(kg・d)、0.625g/(kg・d)、ポジティブ投与群が0.140g/(kg・d)であった。且つ、正常群及び高血糖モデル群には等量の生理食塩水を投与した。
Step 2: The diabetic rats that succeeded in grouping the animals and creating a dosing model were grouped and adjusted into a konjac fine powder enzyme decomposition product high / medium / low dose group, a positive administration group, and a diabetes model group, respectively. In addition, rats with the same blood glucose level as before model preparation were defined as the normal group. Next, intragastric administration was performed for 6 consecutive weeks. During the experiment, rats in each group were allowed to drink and feed freely as usual. The time of intragastric administration was 4 pm daily. Regarding the gastric dose to the rats in each group, 2.500 g / (kg · d), 1.250 g / (kg · d), and 0. It was 625 g / (kg · d) and 0.140 g / (kg · d) in the positive administration group. Moreover, an equal amount of physiological saline was administered to the normal group and the hyperglycemia model group.
ステップ3:指標の測定
ラットへの胃内投与期間中は、各群のラットの体重を毎週測定して記録した。結果はgで示し、各群のラットの体重の差を分析及び比較した。且つ、各群の実験ラットの空腹時血糖値を測定し、結果をmmol/Lで示すとともに、各群のラットの血糖値レベルの変化を分析及び比較した。また、実験動物の飲水量及び摂食量を測定して記録し、胃内投与期間中の各群のラットの飲水量及び摂食量の変化を分析した。
Step 3: Measurement of indicators During the period of intragastric administration to rats, the weight of rats in each group was measured and recorded weekly. The results are shown in g, and the difference in body weight of rats in each group was analyzed and compared. The fasting blood glucose level of the experimental rats in each group was measured, the results were shown in mmol / L, and the changes in the blood glucose level of the rats in each group were analyzed and compared. In addition, the amount of water and food intake of the experimental animals was measured and recorded, and changes in the amount of water and food intake of rats in each group during the gastric administration period were analyzed.
ステップ4:統計方法
ソフトウェアのSPSS20で統計分析を行い、平均値±標準偏差で表した。群間比較には一元配置分散分析を用いた。P<0.05は2つの群に有意差があることを示す。
Step 4: Statistical method Statistical analysis was performed with the software SPSS20 and expressed as mean ± standard deviation. One-way ANOVA was used for group-to-group comparison. P <0.05 indicates that there is a significant difference between the two groups.
表2から明らかなように、投与0日目において、モデル群の飲水量は正常群よりも顕著に上昇していた(p<0.01)。また、投与21日後に、ポジティブ投与群と各コンニャク酵素分解物投与量群の飲水量はそれぞれ異なる度合で減少していた。そして、投与42日目において、モデル群の飲水量は正常群との間に極めて顕著な有意差を示した(p<0.01)。また、ポジティブ投与群及び各コンニャク酵素分解物投与量群の飲水量は、モデル群との間に極めて顕著な有意差を示した(p<0.01)。且つ、コンニャク酵素分解物高・中投与量群の飲水量はポジティブ投与群との間に有意差がなかった。以上から明らかなように、コンニャク酵素分解物は糖尿病ラットの多飲症状を緩和可能であった。また、一定投与量のコンニャク酵素分解物は、糖尿病患者の多飲症状の緩和においてメトホルミンと類似の効果を有していた。 As is clear from Table 2, on day 0 of administration, the amount of water consumed in the model group was significantly higher than that in the normal group (p <0.01). In addition, 21 days after the administration, the amount of drinking water in the positive administration group and each konjac enzyme decomposition product dose group decreased to a different degree. Then, on the 42nd day of administration, the amount of water consumed by the model group showed a very significant difference from that of the normal group (p <0.01). In addition, the amount of water consumed by the positive administration group and each konjac enzymatic decomposition product dose group showed a very significant difference from the model group (p <0.01). Moreover, the amount of drinking water in the high / medium dose group of konjac enzymatic degradation product was not significantly different from that in the positive dose group. As is clear from the above, the konjac enzymatic degradation product was able to alleviate the polydipsia symptom of diabetic rats. In addition, a fixed dose of konjac enzymatic degradation product had an effect similar to that of metformin in alleviating polydipsia symptoms in diabetic patients.
以上の実施例から明らかなように、本発明は、多酵素によるコンニャク精粉酵素分解物の製造方法を提供する。動物(白ネズミ)実験の結果より、当該製品は、肥満予防、血中脂質の低下、肝脂肪変性の予防といった作用を有することがわかった。また、血糖の低下、脂質過酸化の低下、抗炎症、生体におけるフリーラジカル除去の向上といった作用を有し、糖尿病モデルラットの高血糖に対し改善作用を有することがわかった。 As is clear from the above examples, the present invention provides a method for producing a konjac fine powder enzymatic decomposition product using multiple enzymes. From the results of animal (white rat) experiments, it was found that the product has actions such as prevention of obesity, reduction of blood lipids, and prevention of hepatic fatty degeneration. It was also found that it has effects such as lowering blood glucose, lowering lipid peroxidation, anti-inflammatory, and improving free radical removal in the living body, and has an improving effect on hyperglycemia in diabetic model rats.
以上は本発明の好ましい実施例にすぎない。当業者であれば、本発明の原理を逸脱しないことを前提に、若干の改良及び補足が可能であり、これらの改良及び補足もまた本発明の保護の範囲とみなすべきである。 The above is only a preferable embodiment of the present invention. Those skilled in the art can make slight improvements and supplements on the premise that they do not deviate from the principles of the present invention, and these improvements and supplements should also be regarded as the scope of protection of the present invention.
Claims (4)
(1)コンニャク精粉原料をアルコール中で精製することで、コンニャク湿潤精粉を取得するステップと、
(2)前記コンニャク湿潤精粉をアルコール除去処理することで、精製コンニャク精粉を取得するステップと、
(3)取得した前記精製コンニャク精粉と水及び酵素を混合して酵素分解を行うことで、多酵素による前記コンニャク精粉酵素分解物を取得するステップ、を含むことを特徴とする方法。 It is a method for producing konjac fine powder enzymatic decomposition products by multiple enzymes.
(1) The step of obtaining konjac wet powder by purifying the raw material of konjac powder in alcohol, and
(2) A step of obtaining purified konjac fine powder by alcohol-removing the konjak wet fine powder, and
(3) A method comprising a step of obtaining the enzymatic decomposition product of the konjac fine powder by a multienzyme by mixing the obtained purified konjac fine powder with water and an enzyme and performing enzymatic decomposition.
前記ステップ(1)における前記コンニャク精粉原料と前記アルコールとの固液比率は1g:3〜5mlとし、
前記ステップ(1)における精製時間は1〜3hとし、
前記ステップ(2)における前記アルコール除去処理の温度は50〜70℃とすることを特徴とする請求項1に記載の製造方法。 The volume concentration of the alcohol in the step (1) was 55 to 75%.
The solid-liquid ratio of the konjak refined powder raw material and the alcohol in the step (1) was 1 g: 3 to 5 ml.
The purification time in the step (1) was set to 1 to 3 hours.
The production method according to claim 1, wherein the temperature of the alcohol removal treatment in the step (2) is 50 to 70 ° C.
前記ステップ(3)における前記酵素は、グルコマンナナーゼ、セルラーゼ及びペクターゼを含み、
前記グルコマンナナーゼの用量は前記精製コンニャク精粉に対し50〜70u/gとし、前記セルラーゼの用量は前記精製コンニャク精粉に対し40〜60u/gとし、前記ペクターゼは体系総質量の0.03〜0.05%を占め、
前記酵素分解の温度は55〜65℃とし、酵素分解時間は2〜3hとすることを特徴とする請求項1に記載の製造方法。 The mass-volume ratio of the purified konjac fine powder to the water in the step (3) was 15 to 30 g: 100 mL.
The enzyme in step (3) comprises glucomannanase, cellulase and pectase.
The dose of the glucomannanase is 50 to 70 u / g with respect to the purified konjac refined powder, the dose of the cellulase is 40 to 60 u / g with respect to the purified konjac refined powder, and the pectase is 0.03 to 0.03 to the total mass of the system. Occupies 0.05%
The production method according to claim 1, wherein the enzymatic decomposition temperature is 55 to 65 ° C., and the enzymatic decomposition time is 2 to 3 hours.
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JP2011254753A (en) * | 2010-06-09 | 2011-12-22 | Unitika Ltd | Method of producing monosaccharide |
WO2013051146A1 (en) * | 2011-10-07 | 2013-04-11 | 株式会社 荻野商店 | Method for producing depolymerized konjak glucomannan and depolymerized konjak glucomannan obtained thereby |
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JP2018113868A (en) * | 2017-01-16 | 2018-07-26 | 蒟蒻屋本舗株式会社 | Dripping suppressor and frozen food |
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JP4945132B2 (en) * | 2006-01-11 | 2012-06-06 | 蒟蒻屋本舗株式会社 | Manufacturing method of konjac fluid material |
CN103073656A (en) * | 2013-01-23 | 2013-05-01 | 湖北强森魔芋科技有限公司 | Method for processing konjac powder with wet method |
CN104560918A (en) * | 2014-12-25 | 2015-04-29 | 南阳师范学院 | Complex enzyme preparation for efficiently preparing mannose oligomer and application thereof |
CN108185294A (en) * | 2016-12-08 | 2018-06-22 | 陕西理工大学 | A kind of black rice konjaku complex enzyme hydrolysis liquid and preparation method thereof |
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JPH09176A (en) * | 1995-06-22 | 1997-01-07 | Nakano Vinegar Co Ltd | Pulverization of 'konjak' powder and production of 'konjak' or 'konjak'-containing food using the fine 'konjak' powder |
JP2008206404A (en) * | 2007-02-23 | 2008-09-11 | Shimizu Kagaku Kk | Method for producing quick-soluble konjak mannan |
JP2009060805A (en) * | 2007-09-04 | 2009-03-26 | Nippon Ecolonomix:Kk | New mannanase and dietary fiber food produced using the same |
JP2011254753A (en) * | 2010-06-09 | 2011-12-22 | Unitika Ltd | Method of producing monosaccharide |
WO2013051146A1 (en) * | 2011-10-07 | 2013-04-11 | 株式会社 荻野商店 | Method for producing depolymerized konjak glucomannan and depolymerized konjak glucomannan obtained thereby |
JP2016034244A (en) * | 2014-08-01 | 2016-03-17 | 蒟蒻屋本舗株式会社 | Usage of konjak fluid material |
JP2018113868A (en) * | 2017-01-16 | 2018-07-26 | 蒟蒻屋本舗株式会社 | Dripping suppressor and frozen food |
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