JPH0159282B2 - - Google Patents
Info
- Publication number
- JPH0159282B2 JPH0159282B2 JP20458682A JP20458682A JPH0159282B2 JP H0159282 B2 JPH0159282 B2 JP H0159282B2 JP 20458682 A JP20458682 A JP 20458682A JP 20458682 A JP20458682 A JP 20458682A JP H0159282 B2 JPH0159282 B2 JP H0159282B2
- Authority
- JP
- Japan
- Prior art keywords
- carrageenan
- liquid
- gel
- thermal stability
- raw material
- 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
- 239000000679 carrageenan Substances 0.000 claims description 38
- 235000010418 carrageenan Nutrition 0.000 claims description 38
- 229920001525 carrageenan Polymers 0.000 claims description 38
- 229940113118 carrageenan Drugs 0.000 claims description 38
- UHVMMEOXYDMDKI-JKYCWFKZSA-L zinc;1-(5-cyanopyridin-2-yl)-3-[(1s,2s)-2-(6-fluoro-2-hydroxy-3-propanoylphenyl)cyclopropyl]urea;diacetate Chemical compound [Zn+2].CC([O-])=O.CC([O-])=O.CCC(=O)C1=CC=C(F)C([C@H]2[C@H](C2)NC(=O)NC=2N=CC(=CC=2)C#N)=C1O UHVMMEOXYDMDKI-JKYCWFKZSA-L 0.000 claims description 38
- 239000007788 liquid Substances 0.000 claims description 15
- 241000195493 Cryptophyta Species 0.000 claims description 11
- 239000002994 raw material Substances 0.000 claims description 10
- 239000000284 extract Substances 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims 2
- 239000000499 gel Substances 0.000 description 17
- 238000000034 method Methods 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 239000005909 Kieselgur Substances 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 238000000605 extraction Methods 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 238000013112 stability test Methods 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate group Chemical group S(=O)(=O)([O-])[O-] QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- -1 hydrogen ions Chemical class 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- 241000206572 Rhodophyta Species 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000001103 potassium chloride Substances 0.000 description 2
- 235000011164 potassium chloride Nutrition 0.000 description 2
- 159000000001 potassium salts Chemical class 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- WZYRMLAWNVOIEX-BGPJRJDNSA-N 3,6-anhydro-D-galactose Chemical group O=C[C@H](O)[C@H]1OC[C@@H](O)[C@@H]1O WZYRMLAWNVOIEX-BGPJRJDNSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 241000206575 Chondrus crispus Species 0.000 description 1
- 241001428166 Eucheuma Species 0.000 description 1
- 241000940372 Eucheuma denticulatum Species 0.000 description 1
- 241001467355 Gigartina Species 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
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical class OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 150000001860 citric acid derivatives Chemical class 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- VZCYOOQTPOCHFL-OWOJBTEDSA-L fumarate(2-) Chemical class [O-]C(=O)\C=C\C([O-])=O VZCYOOQTPOCHFL-OWOJBTEDSA-L 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 150000003891 oxalate salts Chemical class 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000035807 sensation Effects 0.000 description 1
- 230000001953 sensory effect Effects 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 150000003892 tartrate salts Chemical class 0.000 description 1
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
Description
本発明は、熱安定性が良好で、かつゲルの食感
が改良されたカラギーナンの効率的な製造法に関
する。
カラギーナンは紅藻類例えばコンドラス・クリ
スパス(Chondrus Crispus)、ギカルテイナ・ス
テラタ(Gigartina Stellatta)、ユーキユーマ・
コトニ(Eucheuma Ccttonii)、ユーキユーマ・
スピノサム(Eucheuma Spinosum)等を中性な
いし弱アルカリ性の熱水で抽出することにより得
られる硫酸化ガラクタンである。これには硫酸基
及び3,6―アンヒドロ―D―ガラクトース単位
の含有量が異なる数種のものがあるが、一般に
は、κ,λ,ιに大別され、それぞれ特異なゲル
化能力及びミルク反応性を有しており、これを利
用して食品工業、化粧品工業をはじめとして広範
な分野で使用されている。
カラギーナンはその熱安定性が他の多糖類に比
して著しく劣り、例えば空気中に100℃の温度で
1〜4時間放置すると、変色ないし炭化が起こ
り、それに伴いカラギーナンに要求される粘度、
ゲル強度等の物理的諸性質も著しく低下する。こ
の変化は、さらに低温例えば60〜80℃の温度でさ
えも10〜100時間の間に認められ、より高温例え
ば130〜150℃では極めて短時間すなわち5〜50分
の間に同様な変化が進行する。このことはカラギ
ーナンを使用するに到るまでの諸工程、例えば殺
菌工程後における熱負荷による品質劣化が著し
く、使用するまでの諸特性の経時的劣化が避けら
れないことを意味している。業界においてはこれ
らの現象を見越して、カラギーナンを必要量以上
に添加する等の方法により、この問題を回避して
いるのが現状であるが、製造費の増加や劣化状況
把握のための物性値の測定頻度の増加という煩わ
しさを余儀なくされている。
本発明者らは、カラギーナンの有するこの熱不
安定性について研究を重ねた結果、不安定性がカ
ラギーナンのガラクタン骨格に結合した硫酸基に
対するカチオンの化学的不均一性にあり、これが
硫酸基の不安定性を導き、ひいてはカラギーナン
を不安定にしていることを知見した。さらに本発
明者らの研究によれば、従来より実施されている
PH5.0〜8.0の温水で抽出する方法で製造されるカ
ラギーナンは、その抽出液の示すPH値に応じて構
成する硫酸基のカウンタ―カチオンとしての水素
イオンを有する構造を不均一に含有しており、こ
の不均一性が製造されたカラギーナンの熱安定性
を著しく悪化させる原因となつていることが明ら
かになつた。そしてこの不均一を解決するには、
液のPHを9.0以上とすることが有効であり、こ
の方法により製造されるカラギーナンは熱安定性
が極めて良好であることを確認した。
この研究結果から、PH9.0以上の温水で原料藻
を抽出することにより、製造されるカラギーナン
の熱安定性は賦与されるであろうことは容易に推
察できる。しかしこの方法はカラギーナンの抽出
効率が極めて低く、しかも過が非常に困難であ
るため、経済性の点から工業的生産方法としては
好ましくない。その原因はPH9.0以上では原料藻
の膨潤度が低く、カラギーナンの抽出効率が低く
なること、したがつて原料藻の未抽出残が多く、
またアルカリ土類金属塩の一部が不溶化し、この
両者が共存状態で過に付されると、過負荷が
過大となることが挙げられる。
本発明は、原料藻からPH5.0〜8.0でカラギーナ
ンを抽出し、抽出液を過し、液をPH9.0〜
12.0として再度過したのち脱水することを特徴
とする、カラギーナンの製造法である。
本発明方法はPH5.0〜8.0において原料藻を抽出
したのち過し、次いで液のPHを9.0〜12.0と
する点が製造効率の面からの大きな特色を成して
いる。すなわちPH5.0〜8.0で原料藻を抽出するこ
とによりカラギーナンの抽出効率の低下は完全に
回避され、続く過においても困難さを生じな
い。次に液のPHを9.0〜12.0とすると、アルカ
リ土類金属塩の一部が不溶化するために過工程
を必要とするが、原料藻の未抽出残は予め除去さ
れているので、過負荷は著しく軽減される。
本発明を実施するに際しては、まず原料藻から
PH5.0〜8.0でカラギーナンを抽出する。原料藻と
しては前記の紅藻類が挙げられる。抽出法として
は、例えば原料藻を水に浸漬し、酸又はアルカリ
でPH5.0〜8.0としたのち加熱する方法が用いられ
る。加熱温度は70〜100℃が好ましい。加熱時間
は2〜8時間である。
次いで抽出液を過し、液のPHを9.0〜12.0
として再び過する。液のPHが9.0より低いと、
得られるカラギーナンの熱安定性が劣り、またPH
が12.0より高いとカラギーナンの物理的性質が劣
化し、また原料藻に含まれる色素が変色して、カ
ラギーナンの品質が著しく低下する。液のPHを
調整するための塩基としては、例えば下記のもの
が用いられる。ナトリウム、カルシウム、マグネ
シウム、カリウム等の水酸化物、炭酸塩、酢酸
塩、くえん酸塩、修酸塩、酒石酸塩、フマル酸
塩、アジピン酸塩、燐酸塩、アンモニア、アミン
等並びにこれらの2種以上の混合物。水酸化物と
炭酸塩の併用は特に好ましい。
こうして得られた液を必要に応じて濃縮した
のち、脱水して乾燥すると、カラギーナンが得ら
れる。
脱水法としては、例えば水混和性有機溶剤を加
えてカラギーナンを沈殿させる方法、液をゲル
化させたのち加圧する方法などが用いられる。水
混和性有機溶剤としてはメタノール、エタノー
ル、イソプロパノール、アセトン等が好ましい。
脱水工程を経ることにより、過剰のアルカリを除
去することができる。脱水後、常法により乾燥す
ると、PH7.8〜9.5のカラギーナンが得れる。
本発明方法により製造されるカラギーナンは熱
安定性に優れ、物理的諸特性の経時的変化が少な
い。また意外にも、製品のゲル性状が、特にカツ
パカラギーナンにおいて著しく改良される。従来
の方法で製造されるカツパカラギーナンで調製さ
れるゲルは著しく脆く、食用に供された時に、い
わゆるパサパサ感があり、不快感を与える。この
傾向は塩化カリウム等のカリウム塩を添加した時
に特に顕著である。
これに対し、本発明方法により製造されたカツ
パカラギーナンから調整されるゲルは脆さが解消
され、塩化カリウム等のカリウム塩を添加した時
にも不快感を与えない。このことはネオカードメ
ータ(飯尾電機社製)、レオメーター(不動工業
社製)等のゲル性状評価機器による各種の測定値
からも証明される。例えばゲル破断に到るまでの
ゲル表面の変位が、本発明方法により製造される
カラギーナンで調製されたゲルの方が従来の方法
によりなる製品のゲルより大きい点からも、脆
さ、パサパサ感が解消されていることが明らかで
ある。
実施例1〜5及び比較例1
ユーキユーマ・コトニ6Kgを水洗したのち100
の水に浸漬し、塩酸又は水酸化カリウムでPH
7.1としたのち80℃に加熱して抽出した。3時間
後、抽出液に珪藻土を1Kg加えて過し、液90
を得た。この液に第1A表に示すカリウム固
体を加え、第1A表中の2段目PH欄に示すPHに調
節したのち、珪藻土を300g加えて再び過した。
得られた液1重量部に対し、2重量部のイソプ
ロパノールを加えてカツパカラギーナンを沈殿さ
せたのち、80℃で30分間乾燥して乾燥カツパカラ
ギーナンを得た。これを次に示す試験に供した。
熱安定性試験80℃の空気中に放置して所定時
間熱処理を行う。この熱処理の前後に1.5%溶
液の75℃における粘度及びゲル強度を測定し
た。また150℃の空気中での炭化に到るまでの
時間を測定した。
保存安定性試験:30℃、湿度60%の空気調整
室に200及び400日間放置し、粘度及びゲル強度
の変化を測定した。
ゲルの食感:1.5%の溶液を冷却してゲル化
させ、試食官能試験を行い、またネオカードメ
ーターにより破断に到るまでのゲル表面の変位
量を測定した(プランジヤー径5.6mm)。その結
果を第1A表及び1B表に示す。
比較例1に比べて本発明方法により得られるカ
ツパカラギーナンが熱安定性、保存安定性及びゲ
ル食感において優れていることが知られる。
The present invention relates to an efficient method for producing carrageenan with good thermal stability and improved gel texture. Carrageenan is derived from red algae such as Chondrus crispus, Gigartina Stellatta, Euchyuma
Eucheuma Ccttonii
It is a sulfated galactan obtained by extracting spinosum (Eucheuma Spinosum) etc. with neutral to weakly alkaline hot water. There are several types of these with different contents of sulfate groups and 3,6-anhydro-D-galactose units, but they are generally classified into κ, λ, and ι, each with a unique gelling ability and It has reactivity and is used in a wide range of fields including the food industry and the cosmetics industry. Carrageenan is significantly inferior in thermal stability compared to other polysaccharides; for example, if it is left in the air at a temperature of 100°C for 1 to 4 hours, it will change color or carbonize, resulting in a decrease in the viscosity required for carrageenan.
Physical properties such as gel strength are also significantly reduced. This change is observed over a period of 10 to 100 hours even at lower temperatures, e.g., 60 to 80 degrees Celsius, and a similar change occurs within an extremely short period of time, i.e., 5 to 50 minutes, at higher temperatures, e.g., 130 to 150 degrees Celsius. do. This means that carrageenan undergoes significant quality deterioration due to heat load during various steps before it is used, such as after the sterilization step, and that deterioration of various properties over time is unavoidable before use. In anticipation of these phenomena, the industry is currently avoiding this problem by adding carrageenan in excess of the required amount, but this increases production costs and increases the need for physical property values to understand the state of deterioration. The company is forced to go through the trouble of having to measure more frequently. As a result of repeated research on the thermal instability of carrageenan, the present inventors found that the instability lies in the chemical heterogeneity of the cations with respect to the sulfate groups bonded to the galactan skeleton of carrageenan, and that this causes the instability of the sulfate groups. It was discovered that the carrageenan was destabilized. Furthermore, according to the research conducted by the present inventors,
Carrageenan, which is produced by extraction with hot water with a pH of 5.0 to 8.0, contains a heterogeneous structure with hydrogen ions as counter cations of the sulfate group, depending on the pH value of the extract. It has become clear that this non-uniformity is the cause of significantly deteriorating the thermal stability of the produced carrageenan. And to resolve this heterogeneity,
It was confirmed that it is effective to adjust the pH of the liquid to 9.0 or higher, and that the carrageenan produced by this method has extremely good thermal stability. From the results of this study, it can be easily inferred that thermal stability will be imparted to the produced carrageenan by extracting the raw material algae with hot water with a pH of 9.0 or higher. However, this method has extremely low extraction efficiency of carrageenan and is very difficult to filter, so it is not preferred as an industrial production method from the economic point of view. The reason for this is that when the pH is above 9.0, the degree of swelling of the raw material algae is low, and the extraction efficiency of carrageenan is low.
Further, if a part of the alkaline earth metal salt becomes insolubilized and the two are applied together in a coexisting state, overload may become excessive. The present invention extracts carrageenan from raw algae at a pH of 5.0 to 8.0, filters the extract, and converts the liquid to a pH of 9.0 to 8.0.
This is a method for producing carrageenan, which is characterized by passing it through again as 12.0 and then dehydrating it. A major feature of the method of the present invention in terms of production efficiency is that the raw material algae is extracted and filtered at a pH of 5.0 to 8.0, and then the pH of the liquid is adjusted to 9.0 to 12.0. That is, by extracting raw material algae at pH 5.0 to 8.0, a decrease in the extraction efficiency of carrageenan can be completely avoided, and no difficulty will arise in the subsequent steps. Next, when the pH of the liquid is set to 9.0 to 12.0, an over-step is required to insolubilize some of the alkaline earth metal salts, but since the unextracted residue of the raw material algae has been removed in advance, overloading is not possible. significantly reduced. When carrying out the present invention, first the raw material algae is
Extract carrageenan at PH5.0-8.0. Examples of raw material algae include the above-mentioned red algae. As an extraction method, for example, a method is used in which the raw material algae is immersed in water, the pH is adjusted to 5.0 to 8.0 with acid or alkali, and then heated. The heating temperature is preferably 70 to 100°C. Heating time is 2 to 8 hours. Next, filter the extract and adjust the pH of the liquid to 9.0 to 12.0.
As will pass again. If the pH of the liquid is lower than 9.0,
The resulting carrageenan has poor thermal stability and PH
If it is higher than 12.0, the physical properties of carrageenan will deteriorate, and the pigments contained in the raw material algae will change color, resulting in a significant decrease in the quality of carrageenan. For example, the following bases are used to adjust the pH of the liquid. Hydroxides, carbonates, acetates, citrates, oxalates, tartrates, fumarates, adipates, phosphates, ammonia, amines, etc. of sodium, calcium, magnesium, potassium, etc., and two types thereof A mixture of the above. A combination of hydroxide and carbonate is particularly preferred. Carrageenan is obtained by concentrating the thus obtained liquid as necessary, dehydrating it, and drying it. As the dehydration method, for example, a method in which carrageenan is precipitated by adding a water-miscible organic solvent, a method in which the liquid is gelled and then pressurized, etc. are used. Preferred water-miscible organic solvents include methanol, ethanol, isopropanol, and acetone.
Excess alkali can be removed through a dehydration step. After dehydration, carrageenan with a pH of 7.8 to 9.5 can be obtained by drying using a conventional method. Carrageenan produced by the method of the present invention has excellent thermal stability and shows little change in physical properties over time. Also surprisingly, the gel properties of the product are significantly improved, especially in Katupa carrageenan. Gels prepared using Katupa carrageenan produced by conventional methods are extremely brittle and have a so-called dry feeling when eaten, giving an unpleasant sensation. This tendency is particularly noticeable when potassium salts such as potassium chloride are added. On the other hand, the gel prepared from Katupa carrageenan produced by the method of the present invention has no brittleness and does not cause discomfort even when potassium salts such as potassium chloride are added. This is also evidenced by various measured values using gel property evaluation instruments such as a Neocard meter (manufactured by Iio Electric Co., Ltd.) and a rheometer (manufactured by Fudo Kogyo Co., Ltd.). For example, gels prepared with carrageenan produced by the method of the present invention have a larger displacement on the gel surface before gel rupture than gels produced by conventional methods, and therefore have less brittleness and dryness. It is clear that it has been resolved. Examples 1 to 5 and Comparative Example 1 After washing 6 kg of Yukiyuma kotoni with water,
Soak in water and PH with hydrochloric acid or potassium hydroxide
After adjusting the temperature to 7.1, it was heated to 80°C and extracted. After 3 hours, add 1 kg of diatomaceous earth to the extract and filter.
I got it. The potassium solid shown in Table 1A was added to this liquid to adjust the pH to the pH shown in the second column of Table 1A, and then 300 g of diatomaceous earth was added and filtered again.
2 parts by weight of isopropanol was added to 1 part by weight of the obtained liquid to precipitate Katupa carrageenan, which was then dried at 80° C. for 30 minutes to obtain dried Katupa carrageenan. This was subjected to the following test. Thermal stability test: Leave in air at 80°C and heat-treat for a specified period of time. The viscosity and gel strength of the 1.5% solution at 75°C were measured before and after this heat treatment. In addition, the time required to reach carbonization in air at 150°C was measured. Storage stability test: The samples were left in an air-controlled room at 30°C and 60% humidity for 200 and 400 days, and changes in viscosity and gel strength were measured. Gel texture: A 1.5% solution was cooled to gel, and a tasting sensory test was conducted, and the amount of displacement of the gel surface until breakage was measured using a Neo Card meter (plunger diameter: 5.6 mm). The results are shown in Tables 1A and 1B. It is known that the Katupa carrageenan obtained by the method of the present invention is superior in thermal stability, storage stability, and gel texture as compared to Comparative Example 1.
【表】【table】
【表】
比較例 2
ユーキユーマ・コトニ6Kgを水洗したのち100
の水に浸漬し、水酸化カリウムでPH10.2とな
し、80℃で加熱抽出した。3時間後、抽出液に珪
藻土を1.3Kg加えて過したところ、流速が急激
に低下し、15の液しか得られなかつた。
実施例6〜10及び比較例 3
ユーキユーマ・スピノサム6.2Kgを水洗したの
ち100の水に浸漬し、塩酸又は水酸化カルシウ
ムでPH7.3としたのち80℃に加熱抽出した。3時
間後、抽出液に珪藻土を1Kg加えて過し、液
91を得た。次いで液にアルカリ固体を加えて
第2A表中の2段目PH欄に示すPHに調節したのち
珪藻土を300g加えて再び過した。得られた
液1重量部に対して2重量部のイソプロパノール
を加えてイオタカラギーナンを沈殿させ、これを
80℃で30分間乾燥して乾燥イオタカラギーナンを
得た。これを用いて実施例1と同様にして熱安定
性試験及び保存安定性試験を行つた。ただしゲル
強度は測定しなかつた。その結果を第2A表及び
2B表に示す。比較例に比して本発明方法により
得られるイオタカラギーナンが熱安定性及び保存
安定性において優れていることが知られている。[Table] Comparative example 2 After washing 6 kg of Yukiyuma kotoni with water,
The mixture was soaked in water, adjusted to pH 10.2 with potassium hydroxide, and extracted by heating at 80°C. After 3 hours, 1.3 kg of diatomaceous earth was added to the extract and filtered, but the flow rate suddenly decreased and only 15 liquids were obtained. Examples 6 to 10 and Comparative Example 3 After washing 6.2 kg of Euchyuma spinosum with water, it was immersed in 100 ml of water, adjusted to pH 7.3 with hydrochloric acid or calcium hydroxide, and then heated and extracted at 80°C. After 3 hours, add 1 kg of diatomaceous earth to the extract and filter it.
Got 91. Next, an alkaline solid was added to the liquid to adjust the pH to the pH shown in the second column of Table 2A, and 300 g of diatomaceous earth was added and filtered again. Add 2 parts by weight of isopropanol to 1 part by weight of the obtained liquid to precipitate iota carrageenan.
Dry iota carrageenan was obtained by drying at 80°C for 30 minutes. Using this, a thermal stability test and a storage stability test were conducted in the same manner as in Example 1. However, gel strength was not measured. The results are shown in Table 2A and
Shown in Table 2B. It is known that iota carrageenan obtained by the method of the present invention is superior in thermal stability and storage stability as compared to comparative examples.
【表】【table】
【表】【table】
Claims (1)
し、抽出液を過し、液をPH9.0〜12.0として
再度過したのち脱水することを特徴とする、カ
ラギーナンの製造法。1. A method for producing carrageenan, which comprises extracting carrageenan from raw material algae at a pH of 5.0 to 8.0, filtering the extract, filtering the liquid again at a pH of 9.0 to 12.0, and then dehydrating it.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20458682A JPS5996102A (en) | 1982-11-24 | 1982-11-24 | Production of carrageenan |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20458682A JPS5996102A (en) | 1982-11-24 | 1982-11-24 | Production of carrageenan |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5996102A JPS5996102A (en) | 1984-06-02 |
| JPH0159282B2 true JPH0159282B2 (en) | 1989-12-15 |
Family
ID=16492913
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20458682A Granted JPS5996102A (en) | 1982-11-24 | 1982-11-24 | Production of carrageenan |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5996102A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62151558A (en) * | 1985-12-25 | 1987-07-06 | Mitsubishi Heavy Ind Ltd | Member having corrosion resistant alloy film |
| JPH0662682B2 (en) * | 1985-12-27 | 1994-08-17 | 三菱レイヨン株式会社 | Carrageenan production method |
| FR2664279B1 (en) * | 1990-07-06 | 1994-05-13 | Sanofi | PROCESS FOR OBTAINING KAPPA CARRAGHENANES. |
-
1982
- 1982-11-24 JP JP20458682A patent/JPS5996102A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5996102A (en) | 1984-06-02 |
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