JPH05983B2 - - Google Patents
Info
- Publication number
- JPH05983B2 JPH05983B2 JP58205569A JP20556983A JPH05983B2 JP H05983 B2 JPH05983 B2 JP H05983B2 JP 58205569 A JP58205569 A JP 58205569A JP 20556983 A JP20556983 A JP 20556983A JP H05983 B2 JPH05983 B2 JP H05983B2
- Authority
- JP
- Japan
- Prior art keywords
- concentration
- broth
- salt
- reverse osmosis
- extract
- 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 - Lifetime
Links
- 239000000284 extract Substances 0.000 claims description 18
- 238000001223 reverse osmosis Methods 0.000 claims description 18
- 235000011194 food seasoning agent Nutrition 0.000 claims description 14
- 238000000909 electrodialysis Methods 0.000 claims description 13
- 239000007787 solid Substances 0.000 claims description 10
- 238000000354 decomposition reaction Methods 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 8
- 235000013372 meat Nutrition 0.000 claims description 8
- 239000012528 membrane Substances 0.000 claims description 8
- 239000003014 ion exchange membrane Substances 0.000 claims description 7
- 230000003204 osmotic effect Effects 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 241001465754 Metazoa Species 0.000 claims description 4
- 235000014102 seafood Nutrition 0.000 claims description 3
- 102000004190 Enzymes Human genes 0.000 claims description 2
- 108090000790 Enzymes Proteins 0.000 claims description 2
- 238000007738 vacuum evaporation Methods 0.000 claims 1
- 235000010633 broth Nutrition 0.000 description 28
- 235000002639 sodium chloride Nutrition 0.000 description 23
- 150000003839 salts Chemical class 0.000 description 20
- 235000018102 proteins Nutrition 0.000 description 8
- 102000004169 proteins and genes Human genes 0.000 description 8
- 108090000623 proteins and genes Proteins 0.000 description 8
- 235000019640 taste Nutrition 0.000 description 8
- 230000002255 enzymatic effect Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 239000012141 concentrate Substances 0.000 description 6
- 238000001704 evaporation Methods 0.000 description 6
- 239000000796 flavoring agent Substances 0.000 description 6
- 235000019634 flavors Nutrition 0.000 description 6
- 102000008186 Collagen Human genes 0.000 description 5
- 108010035532 Collagen Proteins 0.000 description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 5
- 229920001436 collagen Polymers 0.000 description 5
- 108090000765 processed proteins & peptides Proteins 0.000 description 5
- 108091005804 Peptidases Proteins 0.000 description 4
- 235000019658 bitter taste Nutrition 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 102000004196 processed proteins & peptides Human genes 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 238000010025 steaming Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000004278 EU approved seasoning Substances 0.000 description 3
- 102000035195 Peptidases Human genes 0.000 description 3
- 150000001413 amino acids Chemical class 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 239000011780 sodium chloride Substances 0.000 description 3
- 229920003934 Aciplex® Polymers 0.000 description 2
- 235000019606 astringent taste Nutrition 0.000 description 2
- 239000006103 coloring component Substances 0.000 description 2
- 238000005115 demineralization Methods 0.000 description 2
- 230000002328 demineralizing effect Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 239000010409 thin film Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 241000283153 Cetacea Species 0.000 description 1
- 241000238424 Crustacea Species 0.000 description 1
- 102000005593 Endopeptidases Human genes 0.000 description 1
- 108010059378 Endopeptidases Proteins 0.000 description 1
- 102000018389 Exopeptidases Human genes 0.000 description 1
- 108010091443 Exopeptidases Proteins 0.000 description 1
- 235000019733 Fish meal Nutrition 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 241001377695 Polygonum arenastrum Species 0.000 description 1
- 235000006386 Polygonum aviculare Nutrition 0.000 description 1
- 239000004365 Protease Substances 0.000 description 1
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 1
- 241000269851 Sarda sarda Species 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 235000021120 animal protein Nutrition 0.000 description 1
- 239000003011 anion exchange membrane Substances 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 235000015278 beef Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 150000001793 charged compounds Chemical class 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229940088598 enzyme Drugs 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000004467 fishmeal Substances 0.000 description 1
- 239000011346 highly viscous material Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 229940024999 proteolytic enzymes for treatment of wounds and ulcers Drugs 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 235000021067 refined food Nutrition 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000015170 shellfish Nutrition 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 235000019583 umami taste Nutrition 0.000 description 1
Landscapes
- Seasonings (AREA)
Description
【発明の詳細な説明】
本発明は動物、魚介類の肉の煮汁より呈味性に
優れ、渋味および塩分の少ない調味料又は調味料
素材を製造する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a seasoning or a seasoning material that has better taste than the broth of meat of animals, seafood, and has less astringency and salt.
最近インスタント食品の増加と食品の多様化に
伴つて多くの煮汁は濃縮されて天然調味料として
利用されつつある。しかし、現在天然調味料とし
て使用されている煮汁の種類はかなり限られてい
て、他の多くの種類の煮汁は飼料に利用されてい
るか、又は凝集沈澱法や活性汚泥法によつて有効
利用されないまま処理されているか、あるいはそ
のまま廃棄されて公害源の一つになつているかの
いずれかである。この様に煮汁の利用が限定され
ていた原因は
(1) 煮汁中のエキス成分濃度が低い場合蒸発法に
よる濃縮ではコストが高く採算性が悪い。 With the recent increase in the number of instant foods and the diversification of foods, many broths are being concentrated and used as natural seasonings. However, the types of broth currently used as natural seasonings are quite limited, and many other types of broth are used for feed or cannot be used effectively by coagulation-sedimentation or activated sludge methods. Either they are treated as they are, or they are disposed of and become a source of pollution. The reasons for this limited use of broth are: (1) When the concentration of extract components in broth is low, concentration by evaporation is expensive and unprofitable.
(2) 煮汁中の相対的塩分濃度が高く逆浸透による
濃縮法では塩分の浸透圧が高く高濃縮が難し
い。(2) The relative salt concentration in the broth is high, and the osmotic pressure of salt is high, making it difficult to achieve high concentration using reverse osmosis.
(3) 蒸煮条件が種々に異なるため煮汁中にコラー
ゲン及び熱水可溶性の蛋白質の溶出を生じてお
り蒸発法では濃縮中に粘度の増加、缶壁への焦
げ付き等を生じ濃縮が難しい。(3) Due to various steaming conditions, collagen and hot water-soluble proteins are eluted into the broth, and with the evaporation method, the viscosity increases during concentration and the can walls are scorched, making it difficult to concentrate.
(4) 煮汁中に比較的分子量の大きいペプチドが存
在する為、濃縮物に苦味を生じている。(4) The presence of relatively large molecular weight peptides in the broth gives the concentrate a bitter taste.
(5) 節等の製造においては天然の海水を使用して
いるためマグネシウム等のニガリ成分が存在
し、濃縮物に苦味を生じ、又塩分濃度が高くな
る。(5) Since natural seawater is used in the production of knotweed, bitter components such as magnesium are present, giving the concentrate a bitter taste and high salt concentration.
(6) 従来の製造法では、濃縮された最終製品の塩
分濃度が高くなり調味料としての汎用性に乏し
い。等、エキスとしての付加価値の低さ及び採
算性の低さに原因があつた。(6) With conventional production methods, the concentrated final product has a high salt concentration and lacks versatility as a seasoning. This was attributed to low added value as an extract and low profitability.
これらを経済的に濃縮させる方法としては、逆
浸透による濃縮が考えられるが相対的な塩分濃度
が高いため、固形分濃度30%程度とした場合でも
エキス成分濃縮としては10〜15%であり、又食品
の浸透圧の高さがこの濃縮に大きな障害となる。
更に微量に含まれるMg.Ca等のイオンが苦味成
分として残留濃縮される為、エキスとしての価値
を低下させている。又、コラーゲン及び熱水可溶
性蛋白質が含まれている為、最終濃縮に蒸発法に
よる濃縮を行なつた場合、粘度の上昇により焦
げ、缶壁への付着等を生じ、又食塩の析出により
スケーリングを生じる。 Concentration by reverse osmosis may be considered as a method to economically concentrate these, but because of the relative high salt concentration, even if the solid content concentration is about 30%, the concentration of extract components is 10 to 15%. Furthermore, the high osmotic pressure of foods poses a major obstacle to this concentration.
Furthermore, trace amounts of ions such as Mg.Ca remain and concentrate as bitter components, reducing its value as an extract. In addition, since it contains collagen and hot water-soluble proteins, if the final concentration is carried out by evaporation, the viscosity will increase, resulting in charring, adhesion to the can wall, etc., and the precipitation of salt will cause scaling. arise.
本発明はこのような欠点をなくし従来あまり問
題にされなかつた種々の肉類の煮汁より苦味、生
臭い臭気、塩分を除去し淡色、低粘度で透明感の
ある高級な調味エキスとして利用する方法であ
り、更に従来のビーフエキスおよびカツオエキス
を一層優れたものにするものであつて不溶性固形
分および油分を除去した肉類の蒸煮液あるいは煮
汁を蛋白分解酵素により酵素分解を行ない、その
分解液をイオン交換膜により電気透析し、透析液
を逆浸透膜により逆浸透させ、更に減圧蒸発濃縮
することを特徴とする調味エキスの製造方法であ
る。すなわち本発明の要旨は
(1)煮汁中に含有するコラーゲン、熱水可溶性の
蛋白質、高分子量のペプチド等の濁り及び一部の
着色成分等の高分子成分を酵素分解により、アミ
ノ酸等の呈味性低分子に分解し(2)次いで、イオン
交換膜電気透析法によつて煮汁中に含有する褐変
促進物質、Mg、Ca等の苦味成分及び食塩等の低
分子イオン成分を効率的に除去し、煮汁中に占め
る呈味成分の比率を高くした後に(3)逆浸透法によ
り効率的な濃縮を行ない、アミノ酸等の低級成分
を20%以上に濃縮し(4)更に減圧蒸発濃縮する事に
よりフレーバー、呈味性にすぐれた低塩エキスを
低コストにて製造することにある。 The present invention eliminates these drawbacks and is a method of removing bitterness, fishy odor, and salt from the broth of various meats, which have not been a problem in the past, and using it as a high-quality seasoning extract that is light in color, low in viscosity, and transparent. , which further improves the conventional beef extract and bonito extract, involves enzymatically decomposing the meat steaming liquid or broth from which insoluble solids and oil have been removed using a proteolytic enzyme, and then passing the decomposed liquid through an ion exchange membrane. This is a method for producing a seasoning extract, which is characterized in that electrodialysis is carried out, the dialysate is subjected to reverse osmosis using a reverse osmosis membrane, and further evaporation and concentration under reduced pressure are carried out. That is, the gist of the present invention is as follows: (1) The turbidity of collagen, hot water-soluble proteins, high-molecular weight peptides, etc. contained in the broth and the high-molecular components such as some coloring components are removed by enzymatic decomposition, and the flavoring components such as amino acids are removed. (2) Next, browning promoting substances, bitter components such as Mg and Ca, and low molecular ion components such as salt contained in the broth are efficiently removed by ion exchange membrane electrodialysis. After increasing the ratio of flavor components in the broth, (3) efficiently concentrating by reverse osmosis, lower components such as amino acids are concentrated to 20% or more, and (4) further evaporating under reduced pressure. To produce a low-salt extract with excellent flavor and taste at a low cost.
本発明にいう肉類とは、魚、貝、甲殻類、鳥、
鯨及びその他の獣の肉を言い、その蒸煮液又は煮
汁とはエキスを抽出するために、直接蒸煮あるい
は煮出したもののみならず、缶類、節類その他の
加工食品及びフイツシユミールを製造する際に副
生する蒸煮液、煮汁及びステイツクウオーターを
いうものである。 The meat referred to in the present invention includes fish, shellfish, crustaceans, birds,
Refers to the meat of whales and other animals, and its steaming liquid or broth refers to not only directly steamed or boiled meat to extract the extract, but also canned goods, joints, other processed foods, and when producing fish meal. This refers to by-products such as steaming liquid, boiling liquid, and state water.
これらの煮汁には、通常調味エキスには不適当
な成分である脂肪、不溶性蛋白質及び夾雑物が数
%含まれているので通常の方法によつて固液分離
を行ない、これらを除去しておく必要がある。 These broths usually contain several percent of fat, insoluble proteins, and impurities, which are ingredients unsuitable for seasoning extracts, so solid-liquid separation is performed in the usual manner to remove these. There is a need.
この際分離された油分は更に精製後、動物油と
してまた不溶性蛋白質はHAP(動物性蛋白質加水
分解調味料)の原料として利用する。 The oil separated at this time is further purified and used as animal oil, and the insoluble protein is used as a raw material for HAP (hydrolyzed animal protein seasoning).
前述の如く不溶性固形分および油脂分を除去し
た煮汁を蛋白分解酵素により酵素分解を行ない煮
汁中に含まれている巨大分子すなわちコラーゲ
ン、熱水可溶性の蛋白質、高分子量のペプチド及
び一部の着色成分を分解させる。分解液は苦味成
分の少ない淡色で透明感のある低粘度のエキスと
なる。この酵素分解されるものの苦味成分として
は高分子ペプチド、高粘性物質及び濁り成分とし
てはコラーゲン及び熱水可溶性の蛋白質があげら
れる。ここで使用する蛋白分解酵素は
Exopeptidase及びEndopeptidaseの両方の作用を
有するものが良く、活性の温度、PHについては限
定しない。酵素分解終了後分解液を酵素失活の温
度まで加熱した後更に電気透析を行ない金属イオ
ン等の褐変促進物質及び食塩等のイオン成分を除
去する。 As mentioned above, the broth from which insoluble solids and fats and oils have been removed is subjected to enzymatic decomposition using proteolytic enzymes to remove the macromolecules contained in the broth, including collagen, hot water-soluble proteins, high molecular weight peptides, and some coloring components. decompose. The decomposed liquid becomes a light-colored, transparent, and low-viscosity extract with little bitterness. Bitter components of the enzymatically decomposed substances include high-molecular peptides, highly viscous substances, and cloudy components include collagen and hot water-soluble proteins. The protease used here is
It is preferable to use a compound that has both exopeptidase and endopeptidase actions, and there are no limitations on the temperature and pH of the activity. After the enzymatic decomposition is completed, the decomposition solution is heated to a temperature that deactivates the enzyme, and then electrodialysis is performed to remove browning promoting substances such as metal ions and ionic components such as salt.
前記、酵素分解及び電気透析を行なう事によ
り、煮汁中の固形分濃度は1/2〜1/3に減少され、
又固形分の分子量の範囲は100〜3000位に揃い、
殆どが強い呈味性を示すエキス成分に限定されて
くる。この事により煮汁の浸透圧は1/2〜1/3にな
る為、次工程の浸透膜による高濃縮が可能とな
り、強い呈味性を示す濃縮エキスを得る事が出来
る。又低温での物理的な圧力濃縮が可能となる為
エキス中にフレーバー成分を保持する事が出来
る。 By performing the enzymatic decomposition and electrodialysis described above, the solid content concentration in the broth is reduced to 1/2 to 1/3,
In addition, the molecular weight range of the solid content is around 100 to 3000,
Most of them are limited to extract components that exhibit strong taste. This reduces the osmotic pressure of the broth to 1/2 to 1/3, making it possible to achieve high concentration using the osmotic membrane in the next step, making it possible to obtain a concentrated extract with a strong taste. Additionally, since physical pressure concentration at low temperatures is possible, flavor components can be retained in the extract.
この電気透析法を更に説明すると、イオン交換
膜電気透析装置において、電気透析槽は多数のイ
オン交換膜と陰イオン交換膜を交互に配列して一
室おきに脱塩室と濃縮室を構成したものより成
り、その両端に電極室が設けられている。煮汁は
脱塩室を、希薄食塩水(通常1〜4%)は濃縮室
と電極室を、それぞれ循環流通させながら両極間
に直流電圧をかけると、煮汁中の無機塩や食塩は
陽イオン、陰イオンとして各々膜を透過移動す
る。その結果、脱塩室の煮汁は塩濃度が低下して
脱塩され、濃縮室においては塩濃度が上昇して食
塩等の塩が濃縮される。 To further explain this electrodialysis method, in an ion-exchange membrane electrodialysis device, the electrodialysis tank has a large number of ion-exchange membranes and anion-exchange membranes arranged alternately to form a demineralization chamber and a concentration chamber in every other chamber. It is made of metal, and electrode chambers are provided at both ends. When the broth is circulated through the demineralization chamber, and the diluted saline solution (usually 1-4%) is circulated through the concentration chamber and electrode chamber, and a DC voltage is applied between the two electrodes, the inorganic salts and common salt in the broth become cations, Each migrates through the membrane as an anion. As a result, the salt concentration of the broth in the desalination chamber decreases and is desalted, and in the concentration chamber the salt concentration increases and salts such as common salt are concentrated.
ここにいう電気透析に使用することの出来るイ
オン交換膜については、セレミオン(登録商標)
CMV、セレミオンAMV(旭硝子株式会社)、ア
シプレツクスCK−1、アシプレツクスCA−2
(旭化成工業株式会社製品)、等の一般市販品が利
用でき、またこれらの膜を組み込んだ電気透析装
置も各イオン交換膜メーカーで製作しているので
利用できる。 Regarding ion exchange membranes that can be used for electrodialysis, Selemion (registered trademark)
CMV, Selemion AMV (Asahi Glass Co., Ltd.), Aciplex CK-1, Aciplex CA-2
(Asahi Kasei Kogyo Co., Ltd. product), etc. can be used, and electrodialysis devices incorporating these membranes are also manufactured by various ion exchange membrane manufacturers, so they can be used.
この様に酵素分解及び電気透析により精製され
た煮汁を、逆浸透膜により固形分濃度20%程度ま
で逆浸透させ濃縮を行なう。この場合、前記工程
の酵素分解及び電気透析により高分子成分及び食
塩を除去している為、固形分中に占める呈味成分
(旨味成分)の比率が80%以上となつており、こ
れら高分子成分及び食塩を除去せずに逆浸透を行
なつた時と比較すると、呈味成分の濃縮率は約3
倍となり、逆浸透による濃縮を非常に効率的に行
なう為、エネルギーコストを低減させる事が出来
る。 The broth thus purified by enzymatic decomposition and electrodialysis is concentrated by reverse osmosis through a reverse osmosis membrane to a solid content concentration of about 20%. In this case, since the polymer components and salt are removed by enzymatic decomposition and electrodialysis in the above steps, the ratio of taste components (umami components) in the solid content is 80% or more, and these polymer components Compared to performing reverse osmosis without removing ingredients and salt, the concentration rate of flavor ingredients is approximately 3
Since concentration by reverse osmosis is performed very efficiently, energy costs can be reduced.
ここで逆浸透法について説明すると。 Let me explain about reverse osmosis here.
逆浸透法(Reverse Osmosis)とは「溶媒は
通すが溶質を通さない」という性質を持つた半透
膜を用いて、溶液にその浸透圧以上の圧力をかけ
て、溶媒のみ透過させることによつて、溶液を濃
縮すると同時に溶媒を得る方法をいう。 Reverse osmosis is a method that uses a semipermeable membrane that allows the solvent to pass through but not the solute, and applies a pressure higher than the osmotic pressure to the solution, allowing only the solvent to pass through. This refers to a method of concentrating a solution and simultaneously obtaining a solvent.
本発明に於いては溶質としてはアミノ酸及び低
分子ペプチド等、溶媒としては水となる。ここに
いう逆浸透に使用することの出来る逆浸透膜は、
PBIL逆浸透巻きTL−195,198(帝人エンジニア
リング株式会社)等の一般市販品が利用できる
が、NaCl排除率90%以上のものが望ましい。 In the present invention, the solute is an amino acid, a low molecular weight peptide, etc., and the solvent is water. The reverse osmosis membranes that can be used for reverse osmosis are:
General commercial products such as PBIL reverse osmosis roll TL-195, 198 (Teijin Engineering Ltd.) can be used, but those with a NaCl removal rate of 90% or higher are preferable.
逆浸透により固形分20%程度に迄濃縮された煮
汁を、薄膜式蒸発機等により低温減圧濃縮を行な
う事により、フレーバーの変質や褐色を防止しな
がら、固形分50%以上の強い呈味性を示すエキス
を得る事が出来る。 By concentrating the broth that has been concentrated to a solid content of approximately 20% through reverse osmosis and using a thin-film evaporator at low temperature and reduced pressure, it is possible to prevent flavor deterioration and browning while producing a strong taste with a solid content of over 50%. It is possible to obtain an extract that shows.
本法に於いてフレーバーの変質や褐色を防止し
うるのは、酵素分解により高粘性及び焦げ附着等
の原因となる高分子物質を除去し、電気透析によ
り濃縮中に析出する食塩分を除去した事にある。
すなわち、煮汁の粘度低下を行なう事により低温
における減圧濃縮が可能となつた為である。又、
逆浸透による濃縮率が向上し、蒸発による濃縮量
が激減する為ランニングコストは従来法に比して
格段に低いものとなる。この様に本発明によれ
ば、従来飼料に利用又は廃棄されていた様な煮汁
より呈味性に優れ、渋味及び塩分の少ない高品質
の調味料又は調味料素材を低コスト、省エネルギ
ーで製造する事が出来、国家経済的にも非常に有
益である。 In this method, flavor deterioration and browning can be prevented by removing high molecular substances that cause high viscosity and burnt adhesion by enzymatic decomposition, and by removing salt that precipitates during concentration by electrodialysis. It's true.
That is, by reducing the viscosity of the broth, it became possible to concentrate it under reduced pressure at low temperatures. or,
Since the concentration rate by reverse osmosis is improved and the amount of concentration due to evaporation is drastically reduced, running costs are significantly lower than that of conventional methods. As described above, according to the present invention, high-quality seasonings or seasoning materials with better taste, less astringency, and less salt can be produced at low cost and with energy savings, compared to the broth that was conventionally used for feed or discarded. It is very beneficial for the national economy.
(実施例)
あらかじめ不溶性蛋白質および夾雑物を濾過に
より除去した動物または魚介類の肉の煮汁1Kgを
加熱器に入れ、蛋白分解酵素を約1g添加したの
ち、温度50℃前後に2時間保ち、続いて約90℃で
約15分間加熱した。得られた淡色で透明感のある
低濃度のエキスを脱塩室に入れて電気解析を行
い、塩分濃度を低下させた後、逆浸透を行い、さ
らに、薄膜式蒸発器によつて低温減圧濃縮をおこ
なつた。(Example) 1 kg of animal or seafood meat broth from which insoluble proteins and impurities have been removed by filtration is placed in a heater, approximately 1 g of proteolytic enzyme is added, the temperature is maintained at around 50°C for 2 hours, and then heated. and heated at about 90°C for about 15 minutes. The resulting light-colored, transparent, and low-concentration extract is placed in a desalting chamber for electrical analysis to reduce the salt concentration, followed by reverse osmosis, and then low-temperature vacuum concentration using a thin-film evaporator. I did this.
得られた濃縮エキス600gは、強い呈味性を示
し、食塩が低濃度まで除去されているので、調味
料あるいは調味素材として好適に使用することが
できる。 600 g of the obtained concentrated extract has a strong taste and salt has been removed to a low concentration, so it can be suitably used as a seasoning or a seasoning material.
Claims (1)
介類の肉の煮汁を酵素分解を行ない、その分解液
をイオン交換膜により電気透析し、透析液を浸透
膜により逆浸透を行ない、更に減圧蒸発濃縮する
ことを特徴とする調味エキスの製造方法。1 Enzyme decomposition of animal or seafood meat broth from which insoluble solids and oil have been removed, electrodialysis of the decomposed liquid using an ion exchange membrane, reverse osmosis of the dialysate using an osmotic membrane, and further vacuum evaporation concentration. A method for producing a seasoning extract.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58205569A JPS6098959A (en) | 1983-10-31 | 1983-10-31 | Preparation of seasoning extract |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58205569A JPS6098959A (en) | 1983-10-31 | 1983-10-31 | Preparation of seasoning extract |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6098959A JPS6098959A (en) | 1985-06-01 |
JPH05983B2 true JPH05983B2 (en) | 1993-01-07 |
Family
ID=16509060
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58205569A Granted JPS6098959A (en) | 1983-10-31 | 1983-10-31 | Preparation of seasoning extract |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6098959A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0657122B2 (en) * | 1988-01-20 | 1994-08-03 | 株式会社ハチテイ | Method for producing natural seasoning using effluent during food processing |
EP0574586B1 (en) * | 1991-11-12 | 1997-01-22 | Kyowa Hakko Kogyo Co., Ltd. | Process for producing food and drink |
-
1983
- 1983-10-31 JP JP58205569A patent/JPS6098959A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6098959A (en) | 1985-06-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4091003A (en) | Fish protein isolate | |
US5049397A (en) | Degradation product of total protein | |
EP0247500B1 (en) | Process for producing a seasoning agent, and foods containing the same | |
AU2005320344A1 (en) | Process for producing a low fat, concentrated meat broth from meat by-products | |
US1992462A (en) | Manufacture of flavoring materials | |
JPS6027359A (en) | Production of seasoning extract | |
JPH05983B2 (en) | ||
LIN et al. | Desalting and recovery of flavour compounds from salted shrimp processing waste water by membrane processes | |
US3978234A (en) | Protein composition | |
JP3108346B2 (en) | Treatment method of fish broth extract | |
JP3347822B2 (en) | Extraction and purification method of quinic acid | |
JPH0254070B2 (en) | ||
JPH03175949A (en) | Preparation of natural seasoning from stick water using membrane process | |
JP3171831B2 (en) | Acid seasonings | |
JP2557015B2 (en) | Method for producing fish and shellfish extract | |
JPH05984B2 (en) | ||
JPH10327796A (en) | Production of seasoning | |
JP3649310B2 (en) | Animal seasoning | |
JPH0453498B2 (en) | ||
JPH11196815A (en) | Production of fish soy sauce | |
JPS645589B2 (en) | ||
JPH0718256A (en) | Method for treating coffee grounds | |
JPS61216657A (en) | Method of providing food with taste of good body | |
JP2889937B2 (en) | Salty seasoning | |
CA1173693A (en) | Process for enhancing the viscosity of milk protein |