JPS6228676B2 - - Google Patents
Info
- Publication number
- JPS6228676B2 JPS6228676B2 JP54120709A JP12070979A JPS6228676B2 JP S6228676 B2 JPS6228676 B2 JP S6228676B2 JP 54120709 A JP54120709 A JP 54120709A JP 12070979 A JP12070979 A JP 12070979A JP S6228676 B2 JPS6228676 B2 JP S6228676B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- acetic acid
- alcohol
- vinegar
- solution
- 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.)
- Expired
Links
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 117
- 239000007788 liquid Substances 0.000 claims description 49
- 238000000855 fermentation Methods 0.000 claims description 45
- 230000004151 fermentation Effects 0.000 claims description 45
- 239000000243 solution Substances 0.000 claims description 36
- 235000021419 vinegar Nutrition 0.000 claims description 34
- 239000000052 vinegar Substances 0.000 claims description 33
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 29
- 241000894006 Bacteria Species 0.000 claims description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 16
- 230000001580 bacterial effect Effects 0.000 claims description 16
- 239000007787 solid Substances 0.000 claims description 15
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 claims description 14
- 235000013922 glutamic acid Nutrition 0.000 claims description 14
- 239000004220 glutamic acid Substances 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 230000001476 alcoholic effect Effects 0.000 claims description 11
- 239000002994 raw material Substances 0.000 claims description 11
- 239000000126 substance Substances 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 229910052757 nitrogen Inorganic materials 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 7
- 150000003839 salts Chemical class 0.000 claims description 7
- 239000011573 trace mineral Substances 0.000 claims description 7
- 235000013619 trace mineral Nutrition 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 6
- 235000016709 nutrition Nutrition 0.000 claims description 6
- 230000032683 aging Effects 0.000 claims description 5
- 238000003860 storage Methods 0.000 claims description 4
- 125000000218 acetic acid group Chemical class C(C)(=O)* 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 claims 1
- 235000013339 cereals Nutrition 0.000 description 26
- 235000019441 ethanol Nutrition 0.000 description 25
- WHUUTDBJXJRKMK-VKHMYHEASA-N L-glutamic acid Chemical compound OC(=O)[C@@H](N)CCC(O)=O WHUUTDBJXJRKMK-VKHMYHEASA-N 0.000 description 17
- 241000209094 Oryza Species 0.000 description 9
- 235000007164 Oryza sativa Nutrition 0.000 description 9
- 239000000796 flavoring agent Substances 0.000 description 9
- 235000019634 flavors Nutrition 0.000 description 9
- 235000009566 rice Nutrition 0.000 description 9
- 238000012258 culturing Methods 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 238000012360 testing method Methods 0.000 description 5
- USFZMSVCRYTOJT-UHFFFAOYSA-N Ammonium acetate Chemical compound N.CC(O)=O USFZMSVCRYTOJT-UHFFFAOYSA-N 0.000 description 4
- 239000005695 Ammonium acetate Substances 0.000 description 4
- 239000004382 Amylase Substances 0.000 description 4
- 102000013142 Amylases Human genes 0.000 description 4
- 108010065511 Amylases Proteins 0.000 description 4
- 241000186146 Brevibacterium Species 0.000 description 4
- 229940043376 ammonium acetate Drugs 0.000 description 4
- 235000019257 ammonium acetate Nutrition 0.000 description 4
- 235000019418 amylase Nutrition 0.000 description 4
- 229930195712 glutamate Natural products 0.000 description 4
- 230000001953 sensory effect Effects 0.000 description 4
- 241000186226 Corynebacterium glutamicum Species 0.000 description 3
- 240000005979 Hordeum vulgare Species 0.000 description 3
- 235000007340 Hordeum vulgare Nutrition 0.000 description 3
- 238000005273 aeration Methods 0.000 description 3
- 238000012136 culture method Methods 0.000 description 3
- 235000013312 flour Nutrition 0.000 description 3
- YBJHBAHKTGYVGT-ZKWXMUAHSA-N (+)-Biotin Chemical compound N1C(=O)N[C@@H]2[C@H](CCCCC(=O)O)SC[C@@H]21 YBJHBAHKTGYVGT-ZKWXMUAHSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- 240000006439 Aspergillus oryzae Species 0.000 description 2
- 235000002247 Aspergillus oryzae Nutrition 0.000 description 2
- 239000005909 Kieselgur Substances 0.000 description 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- GXCLVBGFBYZDAG-UHFFFAOYSA-N N-[2-(1H-indol-3-yl)ethyl]-N-methylprop-2-en-1-amine Chemical compound CN(CCC1=CNC2=C1C=CC=C2)CC=C GXCLVBGFBYZDAG-UHFFFAOYSA-N 0.000 description 2
- 108091005804 Peptidases Proteins 0.000 description 2
- 239000004365 Protease Substances 0.000 description 2
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- -1 ammonium ions Chemical group 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000002431 foraging effect Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000011550 stock solution Substances 0.000 description 2
- DEXFNLNNUZKHNO-UHFFFAOYSA-N 6-[3-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperidin-1-yl]-3-oxopropyl]-3H-1,3-benzoxazol-2-one Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1CCN(CC1)C(CCC1=CC2=C(NC(O2)=O)C=C1)=O DEXFNLNNUZKHNO-UHFFFAOYSA-N 0.000 description 1
- 239000001888 Peptone Substances 0.000 description 1
- 108010080698 Peptones Proteins 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 235000020958 biotin Nutrition 0.000 description 1
- 239000011616 biotin Substances 0.000 description 1
- 229960002685 biotin Drugs 0.000 description 1
- 229940041514 candida albicans extract Drugs 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 235000013877 carbamide Nutrition 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000004925 denaturation Methods 0.000 description 1
- 230000036425 denaturation Effects 0.000 description 1
- ZPWVASYFFYYZEW-UHFFFAOYSA-L dipotassium hydrogen phosphate Chemical compound [K+].[K+].OP([O-])([O-])=O ZPWVASYFFYYZEW-UHFFFAOYSA-L 0.000 description 1
- 229910000396 dipotassium phosphate Inorganic materials 0.000 description 1
- 235000019797 dipotassium phosphate Nutrition 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 125000001477 organic nitrogen group Chemical group 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- LWIHDJKSTIGBAC-UHFFFAOYSA-K potassium phosphate Substances [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- DPJRMOMPQZCRJU-UHFFFAOYSA-M thiamine hydrochloride Chemical compound Cl.[Cl-].CC1=C(CCO)SC=[N+]1CC1=CN=C(C)N=C1N DPJRMOMPQZCRJU-UHFFFAOYSA-M 0.000 description 1
- 239000011691 vitamin B1 Substances 0.000 description 1
- 239000012138 yeast extract Substances 0.000 description 1
Landscapes
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Description
本発明は穀類を原料とする食酢の製造法、特に
品質の安定した風味の優れた食酢を製造する方法
に関する。
すなわち、本発明は穀類の糖化液をアルコール
発酵させるか、または穀類の糖化液にアルコール
を添加することにより得たアルコール含有液に種
酢および必要に応じて栄養物質、アルコールまた
はアルコール含有液、水などを加えて酢酸発酵を
行なわせ、この酢酸発酵液またはこれより菌体な
どの固形物を除去した液に窒素源、および必要に
応じて無機塩、微量要素などを加え、これにグル
タミン酸生産菌を接種し培養して得られた培養液
またはこれより菌体などの固形物を除去した液、
もしくはこれらに酢酸発酵液またはこれより菌体
などの固形物を除去して得た液を添加混合した混
合液を熟成貯蔵することを特徴とする穀類を原料
とした食酢の製造法であつて、その目的は品質の
安定した呈味性の高い食酢を製造する方法を提供
することにある。
従来、穀類を原料とする食酢の製造における仕
込液の調製には、例えば米、麦などの穀類の糖化
液をアルコール発酵させるか、または糖化液にア
ルコールを添加することにより得たアルコール含
有液、種酢および必要に応じて酒精、栄養物質、
水などが用いられている。これら穀類を原料とし
て得たアルコール含有液は、酢酸菌に栄養分を与
えると共に食酢に特有の香味成分を生成する原料
としての役目を果している。しかし充分な香味を
持つ食酢を得るためには相当多量の原料を必要と
し、多量の原料穀類を使用すると、原料に由来す
る各種無機質、脂質、難分解性の炭水化物、蛋白
質などの影響により食酢の品質が非常に不安定に
なるので、現在一般にはこれら米、麦などの穀類
の使用量を一定量に止めなければならず、充分な
香味を持つ食酢が得られていないのが現状であ
る。
本発明者らは、このような事情にかんがみ、穀
類を原料として品質が安定し、かつ香味の優れた
食酢を製造する方法について種々研究した結果、
先に穀類の糖化液をアルコール発酵させるか、ま
たは穀類の糖化液にアルコールを添加することに
より得たアルコール含有液を用いて仕込液を調製
し、この仕込液を酢酸発酵させて穀類を原料とす
る食酢を製造するに当り、穀類の糖化液に窒素源
及び必要に応じて無機塩、微量要素などを加えた
液体培地にグルタミン酸生産菌を接種して培養し
た培養液またはこれより菌体を除去した液を、上
記の仕込液ないし酢酸発酵中の発酵液に加えて酢
酸発酵を行なわせることを特徴とする穀類を原料
とする食酢の製造法(特願昭53−153671号)、お
よび穀類の糖化液に窒素源および必要に応じて無
機塩、微量要素などを加えた液体培地にグルタミ
ン酸生産菌を接種し、培養して得られたグルタミ
ン酸含有培養液に、糖分を追加添加または添加す
ることなしに、アルコール発酵性酵母を加えてア
ルコール発酵させるか、または上記グルタミン酸
含有培養液にアルコールを加えることによりアル
コールおよびグルタミン酸含有液を得、これに種
酢および必要に応じて酒精、栄養物質、水などを
加えて酢酸発酵を行なわせることを特徴とする穀
類を原料とする食酢の製造法(特願昭53−154217
号)を発明した。
その後、さらに研究を続けた結果、穀類の糖化
液をアルコール発酵させるか、または穀類の糖化
液にアルコールを添加することにより得たアルコ
ール含有液に種酢および必要に応じて栄養物質、
アルコールまたはアルコール含有液、水などを加
えて酢酸発酵を行なわせ、この酢酸発酵液または
これより菌体などの固形物を除去した液に窒素
源、および必要に応じて無機塩、微量要素などを
加え、これにグルタミン酸生産菌を接種し培養し
て得られた培養液またはこれより菌体などの固形
物を除去した液、もしくはこれらに酢酸発酵液ま
たはこれより菌体などの固形物を除去して得た液
を添加混合した混合液を熟成貯蔵して食酢を製造
すると、グルタミン酸生産菌により生成された成
分が、酢酸発酵により生成した酢酸、その他の成
分と混合醸成され、さらに熟成貯蔵中に酢酸、そ
の他の成分と混和醸成されて優れた香味を有する
品質の安定した食酢が得られることを発見した。
本発明はこの発見に基づいて完成されたものであ
る。
以下本発明について具体的に説明する。
本発明に用いられる穀類の具体例としては、通
常、穀類を原料として食酢を製造するのに用いら
れる米、麦などが挙げられ、さらにこれから調製
した米粉、麦粉なども用いることができる。
穀類の糖化は、常法に従つて行なうことがで
き、例えば穀類に蒸煮などの変性処理を行なつた
後、粗製又は精製したアミラーゼ剤および必要に
応じてプロテアーゼ剤を加えて糖化を行なつても
よく、また変性処理した穀類自体を黄麹菌等のア
ミラーゼ生産菌を用いて製麹し、得られた麹に水
を加えて糖化を行なわせ糖化液を製造してもよ
い。
この穀類の糖化液を常法に従いアルコール発酵
させて得たアルコール発酵液または該糖化液にア
ルコールを添加した液をアルコール含有液として
酢酸発酵の仕込調製に用いる。酢酸発酵の仕込液
は前記のアルコール含有液に種酢および必要に応
じてアルコールまたはアルコール含有液、酢酸菌
の栄養物質、水、その他を混和して調製する。
本発明において酢酸発酵は、従来の食酢醸造で
用いられるすべての方法(例えば表面培養法、深
部培養法など)を用いて行なうことができる。
そして酢酸発酵終了後は、そのままグルタミン
酸生産菌の培養に使用しても良いが、適当な手段
で菌体などの固形物(酢酸菌菌体およびその他の
固形物質)を除去した後、使用した方が望まし
い。
この酢酸発酵液に加える窒素源としては、例え
ばアンモニア、硫酸アンモニウム、酢酸アンモニ
ウム、尿素、ペプトン、肉エキス、酵母エキス、
コーンスチープリカーなどの無機態および有機態
の窒素源が適宜用いられるが、特に酢酸アンモニ
ウムを用いた場合はアンモニウムイオン消費後、
陰イオン残基が食酢の品質に影響を及ぼすことが
なく最も好適である。窒素源の濃度は0.05〜0.30
%(窒素換算)とするのが適当である。また無機
塩や微量要素などは加えても加えなくてもよい
が、無機塩としては例えば硫酸マグネシウムやリ
ン酸二カリウムなどが、また微量要素としては例
えばビオチンやビタミンB1などが好適に用いら
れる。
本発明において使用されるグルタミン酸生産菌
としては、通常グルタミン酸発酵に使用されてい
る菌株で酢酸資化能を有するものであれば、菌の
属、種を問わず、いずれでも用いることができる
が、例えばブレビバクテリウム・ラクトフアーメ
ンタムATCC13655、ブレビバクテリウム・ラク
トフアーメンタムATCC13869、ミクロコツカ
ス・グルタミクスATCC13032、コリネバクテリ
ウム・グルタミクムATCC21543などが好適に用
いられる。
グルタミン酸生産菌の培養は、培養温度27〜37
℃、PH6〜8の範囲で、通常12〜48時間、振盪ま
たは通気撹拌培養で行なわれる。培養中、必要で
あればPHをアンモニア水またはアンモニアガスを
フイードして6〜8に保ち、培養終了時にアンモ
ニウムイオンが残存しないようにするため、培養
中適当な時期にアンモニア水またはアンモニアガ
スのフイードを中止する。
このようにしてグルタミン酸生産菌の培養を終
了した培養液は、そのまままたは適当な手段で例
えば遠心分離または過によつて菌体などの固形
物を除去した後、必要に応じて殺菌(例えば加熱
殺菌)して、熟成貯蔵を行なつて製品としても良
いが、グルタミン酸生産菌の培養の結果として酢
酸濃度が減少した場合には、酢酸発酵液またはこ
れより菌体などの固形物を除去した液を添加、混
合して酢酸濃度を適当な値に調整した後、熟成貯
蔵を行なう。なお、この場合、酢酸発酵液として
は、上記と異なる酢酸発酵液を用いることもでき
るが、上記と同じ酢酸発酵液を用いるのが好まし
い。
本発明によりグルタミン酸生産菌の生成した成
分がグルタミン酸発酵中および熟成貯蔵中に酢酸
その他の成分と混和醸成されて優れた香味を有す
る食酢を得ることができることを官能検査の結果
を示して説明すると次の如くである。
すなわち、後記実施例1に記載の方法に従つて
製造した米酢(試料A)と酢酸発酵液にグルタミ
ン酸生産菌ブレビバクテリウム・ラクトフアーメ
ンタムATCC13869を培養しない以外は実施例1
に記載したと同様に糖化、アルコール発酵、酢酸
発酵および熟成貯蔵を行なつて得た醸造酢(試料
B)について、酢に関して習熟したパネル20名に
より3点試験法(例えば昭和38年7月20日、財団
法人日本科学技術連盟発行、日科技連官能検査委
員会編著「工業における官能検査ハンドブツク」
第492頁参照)を用いて官能検査を行なつたとこ
ろ、第1表に示す様な結果を得た。
The present invention relates to a method for producing vinegar using grains as a raw material, and particularly to a method for producing vinegar with stable quality and excellent flavor. That is, the present invention involves adding seed vinegar and optionally nutritional substances, alcohol or an alcohol-containing liquid, and water to an alcohol-containing liquid obtained by alcoholic fermentation of a saccharified liquid of cereals or by adding alcohol to a saccharified liquid of cereals. A nitrogen source and, if necessary, inorganic salts, trace elements, etc. are added to this acetic acid fermentation solution or a solution from which solid matter such as bacterial cells has been removed, and glutamate-producing bacteria are added to this solution. The culture solution obtained by inoculating and culturing or the solution from which solid matter such as bacterial bodies has been removed,
Alternatively, a method for producing vinegar using grains as a raw material, which comprises adding and mixing an acetic acid fermentation liquid or a liquid obtained by removing solid matter such as bacterial cells therefrom, and storing the mixed liquid for aging, The purpose is to provide a method for producing vinegar with stable quality and high taste. Conventionally, in the preparation of a charging liquid in the production of vinegar using grains as raw materials, for example, an alcohol-containing liquid obtained by alcoholic fermentation of a saccharified liquid of grains such as rice or barley, or by adding alcohol to a saccharified liquid; Seed vinegar and optionally alcoholic spirit, nutritional substances,
Water is used. The alcohol-containing liquid obtained from these grains serves as a raw material that not only provides nutrients to acetic acid bacteria but also produces flavor components specific to vinegar. However, in order to obtain vinegar with sufficient flavor, a considerable amount of raw materials are required, and when a large amount of grain is used, the vinegar is affected by various minerals, lipids, persistent carbohydrates, proteins, etc. derived from the raw materials. Since the quality is extremely unstable, it is generally necessary to limit the amount of these grains such as rice and wheat to a certain level, and the current situation is that vinegar with sufficient flavor cannot be obtained. In view of these circumstances, the present inventors conducted various research on methods for producing vinegar with stable quality and excellent flavor using grains as raw materials.
First, a stock solution is prepared using an alcohol-containing solution obtained by alcoholic fermentation of a saccharified grain solution or by adding alcohol to a saccharified solution of grains, and this stock solution is fermented with acetic acid to make grains into raw materials. To produce vinegar, glutamate-producing bacteria are inoculated into a liquid medium prepared by adding a nitrogen source and, if necessary, inorganic salts, trace elements, etc. to a saccharified grain solution. A method for producing vinegar using grains as a raw material (Japanese Patent Application No. 153,671/1989), characterized in that the resulting liquid is added to the above-mentioned charging solution or fermentation solution during acetic acid fermentation to carry out acetic acid fermentation, and Glutamic acid-producing bacteria are inoculated into a liquid medium prepared by adding a nitrogen source and, if necessary, inorganic salts, trace elements, etc. to the saccharified solution, and sugar is added or not added to the resulting glutamic acid-containing culture solution. A liquid containing alcohol and glutamic acid is obtained by adding alcohol-fermenting yeast and performing alcoholic fermentation, or by adding alcohol to the above-mentioned glutamic acid-containing culture liquid, and adding vinegar seeds and optionally alcoholic substances, nutritional substances, water, etc. A method for producing vinegar using grains as a raw material, characterized by adding acetic acid fermentation to
No.) was invented. Subsequently, as a result of further research, it was found that the alcohol-containing liquid obtained by alcoholic fermentation of the saccharified grain solution or the addition of alcohol to the saccharified grain solution was added with seed vinegar and nutritional substances as necessary.
Alcohol or an alcohol-containing liquid, water, etc. are added to carry out acetic acid fermentation, and a nitrogen source and, if necessary, inorganic salts, trace elements, etc. In addition, a culture solution obtained by inoculating and culturing glutamic acid-producing bacteria, or a solution obtained by removing solid matter such as bacterial cells from this, or an acetic acid fermentation solution or a solution obtained by removing solid matter such as bacterial cells from this. When vinegar is produced by aging and storing the mixture obtained by adding and mixing the liquid obtained by adding and mixing, the components produced by glutamic acid-producing bacteria are mixed and brewed with acetic acid produced by acetic acid fermentation and other components, and further during aging and storage. It has been discovered that vinegar of stable quality and excellent flavor can be obtained by mixing and brewing with acetic acid and other ingredients.
The present invention was completed based on this discovery. The present invention will be specifically explained below. Specific examples of grains used in the present invention include rice, barley, etc., which are usually used to produce vinegar from grains, and rice flour, barley flour, etc. prepared from these grains can also be used. Saccharification of grains can be carried out according to a conventional method, for example, after subjecting the grains to a denaturation treatment such as steaming, saccharification is carried out by adding a crude or purified amylase agent and, if necessary, a protease agent. Alternatively, the denatured grain itself may be made into koji using amylase-producing bacteria such as Aspergillus oryzae, and water may be added to the resulting koji to perform saccharification to produce a saccharified liquid. The alcoholic fermentation liquid obtained by alcohol fermentation of this saccharified cereal liquid according to a conventional method, or the liquid obtained by adding alcohol to the saccharified liquid, is used as an alcohol-containing liquid for preparation of acetic acid fermentation. A charging solution for acetic acid fermentation is prepared by mixing the above-mentioned alcohol-containing solution with seed vinegar and, if necessary, alcohol or an alcohol-containing solution, nutritional substances for acetic acid bacteria, water, and others. In the present invention, acetic acid fermentation can be carried out using all methods used in conventional vinegar brewing (eg, surface culture method, deep culture method, etc.). After the acetic acid fermentation is completed, it may be used as is for culturing glutamic acid producing bacteria, but it is better to use it after removing solid substances such as bacterial cells (acetic acid bacteria cells and other solid substances) by appropriate means. is desirable. Examples of nitrogen sources added to this acetic acid fermentation solution include ammonia, ammonium sulfate, ammonium acetate, urea, peptone, meat extract, yeast extract,
Inorganic and organic nitrogen sources such as corn steep liquor are used as appropriate, but especially when ammonium acetate is used, after consumption of ammonium ions,
Anionic residues are most preferred because they do not affect the quality of vinegar. The concentration of nitrogen source is 0.05-0.30
% (in terms of nitrogen) is appropriate. In addition, inorganic salts and trace elements may or may not be added, but examples of inorganic salts such as magnesium sulfate and dipotassium phosphate, and trace elements such as biotin and vitamin B1 are preferably used. . As the glutamic acid-producing bacteria used in the present invention, any strain that is normally used for glutamic acid fermentation and has the ability to assimilate acetic acid can be used, regardless of the genus or species of the bacteria. For example, Brevibacterium lactofamentum ATCC 13655, Brevibacterium lactofamentum ATCC 13869, Micrococcus glutamicus ATCC 13032, Corynebacterium glutamicum ATCC 21543, etc. are preferably used. Cultivation of glutamate-producing bacteria is performed at a culture temperature of 27 to 37
℃ and pH range of 6 to 8, usually for 12 to 48 hours, with shaking or aeration. During culturing, if necessary, feed ammonia water or ammonia gas to keep the pH at 6 to 8. To prevent ammonium ions from remaining at the end of culturing, feed ammonia water or ammonia gas at appropriate times during culturing. cancel. The culture solution that has been cultivated for glutamate-producing bacteria in this way may be used as is or after solid matter such as bacterial cells is removed by centrifugation or filtration, if necessary, it may be sterilized (e.g., heat sterilized). ) and then aged and stored to produce a product. However, if the acetic acid concentration decreases as a result of culturing glutamic acid-producing bacteria, use the acetic acid fermentation liquid or a liquid from which solids such as bacterial bodies have been removed. After adding and mixing to adjust the acetic acid concentration to an appropriate value, the mixture is aged and stored. In this case, as the acetic acid fermentation liquid, an acetic acid fermentation liquid different from the above can be used, but it is preferable to use the same acetic acid fermentation liquid as above. The present invention shows that the components produced by glutamic acid-producing bacteria can be mixed with acetic acid and other components during glutamic acid fermentation and aging storage to obtain vinegar with excellent flavor. This will be explained by showing the results of a sensory test. It's like this. That is, Example 1 except that the glutamic acid producing bacterium Brevibacterium lactofamentum ATCC13869 was not cultured in the rice vinegar (sample A) and acetic acid fermentation liquid produced according to the method described in Example 1 below.
The brewed vinegar (sample B) obtained by saccharification, alcohol fermentation, acetic acid fermentation, and aging storage in the same manner as described in 1. "Sensory Testing Handbook in Industry" published by the Japan Federation of Science and Technology Foundation, edited by the Japan Federation of Science and Technology Sensory Testing Committee
When a sensory test was carried out using the following method (see page 492), the results shown in Table 1 were obtained.
【表】
上記試験の結果から、本発明によつて得られる
食酢は、従来の穀類を原料とする醸造酢の香味よ
り一段と優れた香りおよび風味を有する食酢であ
ることが明らかに認められる。
次に本発明の実施例を示す。
実施例 1
精白された米50Kgを水に浸漬後、通常の方法に
より蒸煮し、冷却した蒸米に麹菌を接種して30
℃、湿度95%で3日間製麹して米麹65Kgを得た。
この65Kgの米麹と水200を300の容器に入れて
混合し、加温して60℃で40時間糖化し、糖化終了
後、圧搾して200の糖化液を得た。この糖化液
200に前培養しておいた酒母40を加え、20℃
でアルコール発酵を10日間行ない、発酵終了後
200の香味良好な酒精発酵液を得た。
この酒精発酵液200と95%酒精12および水
188を混合し、加温して40℃となし、これに種
酢350を加え、800容木桶にて保温しながら静
置して60日間酢酸発酵を行なわせた。この発酵液
に珪藻土を加えて過して菌体を除き、清澄な酢
酸発酵液720を得た。
このようにして得た酢酸発酵液をアンモニアガ
スと酢酸アンモニウムでPHを7とした後、1500
ジヤーフアーメンターに入れ、ブレビバクテリウ
ム・ラクトフアーメンタムATCC13869を接種し
て31.5℃で48時間通気撹拌培養した。培養を終了
した培養液は遠心分離機にかけて菌体を除去した
後、加熱殺菌を行ない培養液650を得た。この
培養液に深部培養法で製造し菌体などの固形物を
除去した酢酸発酵液150を混合して60日間熟成
貯蔵して食酢720を得た。
実施例 2
小麦粉5Kgに水45を加えて加熱タンクに入れ
た。これに液化型アミラーゼ0.1Kgを加え、加熱
蒸煮を100℃で120分間行ない、冷却後、これに糖
化型アミラーゼ0.1Kgおよびプロテアーゼ0.01Kg
を加え、良く混合して65℃で70時間糖化を行なつ
た。糖化終了後、圧搾して糖化液40を得た。
この糖化液40に95%エチルアルコール10と
水50を混合し、加温して40℃となし、これを
200容の木桶に入れ、種酢80を加えて保温
し、60日間静置して酢酸発酵を行なわせた。この
発酵液に珪藻土を加え過して菌体などの固形物
を除き、清澄な酢酸発酵液150を得た。
このようにして得た酢酸発酵液を80分取し、
アンモニアガスと酢酸アンモニウムでPHを7とし
た後、200ジヤーフアーメンターに入れ、ミク
ロコツカス・グルタミクスATCC13032を接種
し、30℃で48時間通気撹拌培養した。培養を終了
した培養液を遠心分離機にかけて菌体などの固形
物を除去した後、加熱殺菌を行ない、培養液70
を得た。
この培養液を前記の酢酸発酵終了液70に混合
して60日間熟成貯蔵して食酢120を得た。[Table] From the results of the above test, it is clearly recognized that the vinegar obtained by the present invention has a flavor and aroma that are even better than those of conventional vinegars brewed from grains. Next, examples of the present invention will be shown. Example 1 After soaking 50kg of polished rice in water, it was steamed using the usual method, and the cooled steamed rice was inoculated with Aspergillus oryzae for 30 minutes.
Koji was made for 3 days at ℃ and 95% humidity to obtain 65 kg of rice malt.
This 65Kg of rice malt and 200ml of water were mixed in a 300ml container, heated and saccharified at 60°C for 40 hours, and after the saccharification was completed, it was squeezed to obtain a 200ml saccharified liquid. This saccharified liquid
Add pre-cultured sake mash 40 to 200 and heat at 20℃.
After 10 days of alcoholic fermentation,
200 alcoholic fermented liquor with good flavor was obtained. This alcohol fermented liquid 200% and 95% alcohol 12% and water
188 was mixed and heated to 40°C, 350% of seed vinegar was added thereto, and the mixture was left to stand in an 800-volume wooden vat while keeping warm for 60 days to carry out acetic acid fermentation. Diatomaceous earth was added to this fermentation liquid and the bacterial cells were removed by filtering to obtain a clear acetic acid fermentation liquid 720. After adjusting the pH of the acetic acid fermentation liquid thus obtained to 7 with ammonia gas and ammonium acetate,
Brevibacterium lactofarmentum ATCC13869 was inoculated into a jar and cultured with aeration at 31.5°C for 48 hours. After the culture was completed, the culture solution was centrifuged to remove bacterial cells, and then heated and sterilized to obtain culture solution 650. This culture solution was mixed with acetic acid fermentation solution 150 produced by a deep culture method and from which solid matter such as bacterial cells had been removed, and the mixture was aged and stored for 60 days to obtain vinegar 720. Example 2 5 kg of flour was added with 45 kg of water and placed in a heating tank. Add 0.1 kg of liquefied amylase to this, heat and steam at 100℃ for 120 minutes, and after cooling, add 0.1 kg of saccharified amylase and 0.01 kg of protease.
was added, mixed well, and saccharified at 65°C for 70 hours. After the saccharification was completed, saccharified liquid 40 was obtained by squeezing. Mix 40 parts of this saccharified liquid with 10 parts of 95% ethyl alcohol and 50 parts of water, heat it to 40℃, and then
The mixture was placed in a 200-volume wooden vat, 80% of seed vinegar was added to keep it warm, and left to stand for 60 days to allow acetic acid fermentation. Diatomaceous earth was added to this fermentation liquid and filtered to remove solid matter such as bacterial cells, to obtain a clear acetic acid fermentation liquid 150. The acetic acid fermentation liquid obtained in this way was collected for 80 minutes,
After adjusting the pH to 7 with ammonia gas and ammonium acetate, the mixture was placed in a 200 jar fermenter, inoculated with Micrococcus glutamicus ATCC 13032, and cultured with aeration at 30°C for 48 hours. After the culture has been completed, the culture solution is centrifuged to remove solid matter such as bacterial cells, and then heat sterilized to reduce the culture solution to 70%.
I got it. This culture solution was mixed with the acetic acid fermentation finished solution 70 and stored for aging for 60 days to obtain vinegar 120.
Claims (1)
たは穀類の糖化液にアルコールを添加することに
より得たアルコール含有液に種酢および必要に応
じて栄養物質、アルコールまたはアルコール含有
液、水などを加えて酢酸発酵を行なわせ、この酢
酸発酵液またはこれより菌体などの固形物を除去
した液に窒素源、および必要に応じて無機塩、微
量要素などを加え、これにグルタミン酸生産菌を
接種し培養して得られた培養液またはこれより菌
体などの固形物を除去した液、もしくはこれらに
酢酸発酵液またはこれより菌体などの固形物を除
去して得た液を添加混合した混合液を熟成貯蔵す
ることを特徴とする穀類を原料とした食酢の製造
法。1. Add seed vinegar and optionally nutritional substances, alcohol or an alcohol-containing liquid, water, etc. to the alcohol-containing liquid obtained by alcoholic fermentation of the saccharified liquid of grains or by adding alcohol to the saccharified liquid of grains. Acetic acid fermentation is carried out, and a nitrogen source and, if necessary, inorganic salts and trace elements are added to this acetic acid fermentation liquid or a liquid from which solid matter such as bacterial cells has been removed, and glutamic acid-producing bacteria are inoculated and cultured. The culture solution obtained by this process or a solution from which solid matter such as bacterial bodies has been removed, or a mixed solution obtained by adding and mixing an acetic acid fermentation solution or a solution obtained by removing solid matter such as bacterial bodies from these. A method for producing vinegar using grains as raw materials, which is characterized by aging and storage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12070979A JPS5645186A (en) | 1979-09-21 | 1979-09-21 | Production of vinegar using grains as starting material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12070979A JPS5645186A (en) | 1979-09-21 | 1979-09-21 | Production of vinegar using grains as starting material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5645186A JPS5645186A (en) | 1981-04-24 |
| JPS6228676B2 true JPS6228676B2 (en) | 1987-06-22 |
Family
ID=14793042
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12070979A Granted JPS5645186A (en) | 1979-09-21 | 1979-09-21 | Production of vinegar using grains as starting material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5645186A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107916208A (en) * | 2017-12-07 | 2018-04-17 | 山西三盟实业发展有限公司 | A kind of lentinan zymotic fluid and its process for solid state fermentation for improving immunity |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5019645B2 (en) * | 2009-04-13 | 2012-09-05 | 福山黒酢株式会社 | Vinegar and method for producing the same |
| CN107858258B (en) * | 2018-01-02 | 2021-01-01 | 山西梁汾金龙鱼醋业有限公司 | Preparation method of succinic acid-rich mature vinegar and succinic acid-rich mature vinegar |
-
1979
- 1979-09-21 JP JP12070979A patent/JPS5645186A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107916208A (en) * | 2017-12-07 | 2018-04-17 | 山西三盟实业发展有限公司 | A kind of lentinan zymotic fluid and its process for solid state fermentation for improving immunity |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5645186A (en) | 1981-04-24 |
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