JPH045420B2 - - Google Patents

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Publication number
JPH045420B2
JPH045420B2 JP58023866A JP2386683A JPH045420B2 JP H045420 B2 JPH045420 B2 JP H045420B2 JP 58023866 A JP58023866 A JP 58023866A JP 2386683 A JP2386683 A JP 2386683A JP H045420 B2 JPH045420 B2 JP H045420B2
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Japan
Prior art keywords
granules
raw material
water
seasoning
metal salt
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Expired - Lifetime
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JP58023866A
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Japanese (ja)
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JPS59151850A (en
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Priority to JP58023866A priority Critical patent/JPS59151850A/en
Publication of JPS59151850A publication Critical patent/JPS59151850A/en
Publication of JPH045420B2 publication Critical patent/JPH045420B2/ja
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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、粒状食品の製造方法に関する。 従来、粒状食品の製法としては、ゼラチン・ペ
クチンなどのゼリー化剤を流動原料に添加して粒
状にゲル化させる方法の他、アルギン酸塩ないし
低メトキシルペクチンの単独又は混合物(以下、
代表例としてアルギン酸塩をもつて説明する。)
と多価金属塩とによる不溶性ゲル状皮膜形成反応
を利用して流動原料の粒を被覆してゲル化させる
方法が知られている。しかして、この皮膜形成法
は、さらに、特公昭45−29422号のようにアルギ
ン酸塩を添加した原料を多価金属塩溶液の中に滴
下する方法と、特公昭48−16133号のように多価
金属塩を添加した原料をアルギン酸塩溶液の中に
滴下する方法とに大別できる。しかしながら、こ
の皮膜形成法は、粒状ゲル化物を簡単に得ること
ができるという利点があるものの、前者の方法で
は、アルギン酸塩によるソフトゲル状の粒体(以
下、たんに、「ソフトゲル」と略す)が得られて
も時間の経過につれて内部までゼリー様に固まつ
てハードゲル化してしまうことを阻止し得ず、ま
た後者の方法では、未反応の多価金属塩が原料中
に残存し異味を呈するようになるので、いずれに
してもこれら従来法によつて製する粒状食品は食
味・食感上の問題がある。 本発明者は、先に、皮膜形成法により粒状食品
を製造するに際し、上記前者の方法を改良した発
明をしたが(特願昭57−141702号(特公昭61−
25343号))、さらに考究の結果、この発明におい
ても調味成分の吸収が不十分であり粒状食品の食
味・食感の向上のためには若干の改良の余地があ
ることに気付いた。すなわち本発明は特願昭57−
141702号の発明にさらに改良を加えたもので、食
味・食感が良好な粒状食品の製造方法を提供する
ことを目的とするものである。 しかして本発明は、アルギン酸塩・低メトキシ
ルペクチンの単独又は混合物と共にクエン酸塩を
添加してある流動状原料を多価金属塩溶液中に滴
下して上記原料の表面にゲル状皮膜を形成した粒
体を得、これを清水中に浸漬して水晒しをした
後、さらに調味液中に浸漬して調味成分を粒体内
に吸収させることを特徴とする粒状食品の製造方
法である。 本発明においては、流動状原料として、清水に
必要に応じ、グルコース・庶糖などの糖類、ガム
質・ゼラチン・寒天・果実ペクチン質などの粘稠
性原料を加えてもよいが、アルギン酸塩・低メト
キシルペクチンの単独又は混合物と、クエン酸塩
(1価の金属塩を示す。好ましくはクエン酸ナト
リウムがよい。)とは、併用添加しておく必要が
ある。 ここでクエン酸塩を添加する理由は、これを添
加しないで製した流動状原料では、多価金属塩溶
液中に滴下して粒体を形成すると、その粒体はハ
ードゲル化して、次に水晒した調味液への浸漬を
行つても食感のソフトなゲルに戻らないばかりで
なく、水晒しや調味液浸漬の際、膨潤したり収縮
したりする作用が起きないので、粒体内へ調味成
分を十分に吸収させることができないからであ
る。クエン酸塩の使用量は、流動状原料全量に対
して0.02〜1.5%(重量%をいう。以下同じ。)好
ましくは0.1〜1.0%であることが望ましい。クエ
ン酸塩の添加量が0.02%未満であると、多価金属
塩溶液でのゲル化に当つてハードゲル化が生じや
すいと同時に、粒体内への調味成分の吸収が不十
分となりやすく、一方、1.5%を越えると最終製
品の長期保存中に粒体が相互に融着して形が崩壊
することがあるので注意することが望ましい。 この流動状原料は、粒状とするために、粘度は
2000C・P(センチポアズ)から10000C.Pくらい
に、好ましくは5000C・Pから8000C・Pくらい
に調整するのがよく、粒形を球状に整えるにはキ
サンタンガムの使用が特に好適である。また、流
動状原料全量に対し、糖類を5〜35%添加する
と、流動状原料の比重が大きくなり、粒体が多価
金属塩溶液中に沈下しきれいな粒体を形成しやす
くなるので、上記範囲内で糖類を添加することが
好ましい。 アルギン酸塩・低メトキシルペクチンの単独又
は混合物の使用量は、流動状原料全量に対して、
0.3〜1.5%、好ましくは0.4〜0.7%とするのがよ
い。 以上に述べた原料のほかに、卵黄・全卵などの
蛋白性原料や大豆油・ひまわり油などの油脂原料
を流動状原料として使用することができる。尚、
蛋白性原料と油脂原料を併用するときは、流動状
原料全体を乳化状態にしておくことが好ましい。 次に、このように調整した流動状原料を適宜の
方法により、直径4〜10m/mの小粒状にして多
価金属塩、好ましくは塩化カルシウム又は乳酸カ
ルシウムなどの0.5〜4.0%水溶液、好ましくは2.0
%水溶液中に滴下する。そうすると、流動状原料
の粒の表面がアルギン酸カルシウムなどの不溶性
ゲル皮膜で被覆され、1〜5分間くらい浸漬して
おくと浸漬液から取り出す際にくずれにくい粒体
が形成される。多価金属塩溶液中に浸漬する時間
があまり長くなると粒体が固くなつてしまう、す
なわち皮膜内部までゼリー様に固まつてハードゲ
ル化してしまうので、注意を要する。 次に、粒体を多価金属塩溶液からとり出し、水
洗の上、清水中に浸漬して水晒しを行う。水晒し
を続けているうちに、清水が粒体内にだんだん吸
収され、粒体は浸漬前の1.1〜2.0倍容に膨潤す
る。そして粒体の表面に亀裂などを生ずることな
く、その中心まで均一でやわらかく、水晒し前よ
りももつとやわらかいソフトゲルとなる。ここで
粒体が膨潤する原理については定かでないが、流
動状原料中にクエン酸塩を添加したときのみ粒体
が膨潤することから、クエン酸塩が粒体の吸水性
を促進させる触媒的役割を果しているものと推察
される。水晒しは、用いた流動状原料の組成にも
よるが、1時間以上行うことが望ましい。水晒し
が1時間未満であると粒体の吸水が不十分で粒体
が膨潤しないので、注意することが望ましい。 最後に、水晒しによつて得たソフトゲルの粒体
を調味液中に浸漬して調味成分を粒体内に吸収さ
せる。調味液としては特に種類を問わず、例えば
食酢・液状コーヒー・紅茶・液状の各種ソース・
果汁・酒類・食塩水・糖液など粒体の味付けの目
的に応じて使用することができる。しかして調味
液の調味成分の濃度は、粒体内に調味成分が吸収
されやすくするために通常の調味液の濃度より高
くしておくことが望ましい。調味液への浸漬を続
けているうちに、粒体内に調味成分が吸収される
と同時に、粒体が若干収縮する。ここで粒体が収
縮するのは調味液中の調味成分の浸透圧作用によ
るものである。調味液中への浸漬時間は、調味成
分の濃度にもよるが、1時間以上行うことが好ま
しい。浸漬が1時間未満であると、調味成分を粒
体内に十分に吸収させることができないので注意
することが望ましい。 調味液中への浸漬が終了した粒体は、調味液中
からとり出し、製品とする。得られる粒状食品
は、所要に応じ加熱殺菌することができる。そし
て、加熱殺菌は、粒体を調味液中に浸漬している
間に行つてもよいが、また液を混じた状態で加熱
する方が、対流を生じ加熱が均一に行われるので
好結果が得られる。 以上述べたように本発明によれば、流動状原料
中にクエン酸塩を添加するので、多価金属塩中に
滴下させて粒体を形成させると、ソフトゲルが得
られるが、このソフトゲルからなる粒体を水晒し
をすれば、クエン酸塩の作用により粒体が水を吸
収して膨潤し、ハードゲル化の進行が止まり、そ
ればかりか水晒し前よりももつとやわらかい粒体
が得られる。さらにこの粒体を調味液中に浸漬す
ることにより、調味成分を十分に粒体内に吸収さ
せることができる。 したがつて、本発明によれば食味・食感が良好
な粒状食品を確実に製造することができる。 試験例 (1) 試験区 アルギン酸ナトリウム 0.5g キサンタンガム 0.4 含水性結晶グルコース 12.0 クエン酸ナトリウム 0.5 清 水 47.6 卵 黄 5.0 サラダ油 34.0 合 計 100g を原料として、常法により乳化させて粘度
6000C・Pの流動状原料を得る。この流動状原
料を直径5m/mの小粒状にして2%塩化カル
シウム水溶液中に滴下して、この水溶液中に2
分間静置後、とり出し粒体を得た。 得られた粒体を静水中に10時間静置して水晒
しを行つた後、さらに粒体100部に対して10%
食塩水50部を加えて10時間静置して調味液浸漬
を行ない粒状食品を得た。 (2) 対照区 アルギン酸ナトリウム 0.5g キサンタンガム 0.4 含水性結晶グルコース 12.0 清 水 48.1 卵 黄 5.0 サラダ油 34.0 合 計 100g を原料とし、他の条件は試験区と同じ方法で対
照品を試作した。 上記テスト品と対照品について、各別に水晒
終了直後の粒体の体積の膨潤度及び調味液浸漬
終了直後の粒体の体積の収縮度を測定した。ま
た粒体内への食塩の吸収状態を知るためテスト
品と対照品の粒体の食塩濃度を測定したところ
表−1の結果が得られた。
The present invention relates to a method for producing granular foods. Conventionally, methods for producing granular foods include adding gelatinizing agents such as gelatin and pectin to fluid raw materials to gel them into granular forms, as well as adding alginate or low methoxyl pectin alone or as a mixture (hereinafter referred to as
This will be explained using alginate as a representative example. )
A method is known in which particles of a fluid raw material are coated and gelled using an insoluble gel-like film formation reaction between a polyvalent metal salt and a polyvalent metal salt. Therefore, this film forming method is further divided into a method in which a raw material to which alginate is added is dropped into a polyvalent metal salt solution as in Japanese Patent Publication No. 45-29422, and a method in which a raw material to which alginate is added is dropped into a polyvalent metal salt solution, as in Japanese Patent Publication No. 48-16133. This method can be roughly divided into two methods: a method in which a raw material to which a valent metal salt has been added is dropped into an alginate solution. However, although this film formation method has the advantage of being able to easily obtain granular gelled products, the former method produces soft gel-like granules (hereinafter simply referred to as "soft gel") made of alginate. ), it cannot prevent the inside from solidifying like a jelly and turning into a hard gel over time, and in the latter method, unreacted polyvalent metal salts remain in the raw materials, causing off-flavors. In any case, granular foods produced by these conventional methods have problems in terms of taste and texture. The present inventor previously made an invention that improved the above-mentioned former method when producing granular foods by a film forming method (Japanese Patent Application No. 141702/1983 (Japanese Patent Application No. 141702/1983).
No. 25343)), and as a result of further study, it was discovered that even in this invention, absorption of seasoning ingredients was insufficient, and there was room for some improvement in improving the taste and texture of granular foods. That is, the present invention was filed in Japanese Patent Application No. 57-
This invention is a further improvement on the invention of No. 141702, and its purpose is to provide a method for producing granular foods with good taste and texture. Therefore, in the present invention, a fluid raw material to which citrate is added together with alginate and low methoxyl pectin alone or in combination is dropped into a polyvalent metal salt solution to form a gel-like film on the surface of the raw material. This is a method for producing a granular food product, which comprises obtaining granules, immersing them in clean water for bleaching, and then further immersing them in a seasoning liquid to absorb seasoning components into the granules. In the present invention, as a fluid raw material, sugars such as glucose and sucrose, and viscous raw materials such as gum, gelatin, agar, and fruit pectin may be added to fresh water as needed, but alginate and low It is necessary to add methoxyl pectin alone or as a mixture and citrate (representing a monovalent metal salt, preferably sodium citrate). The reason for adding citrate here is that when a fluid raw material made without the addition of citrate is dropped into a polyvalent metal salt solution to form granules, the granules turn into a hard gel, and then water Not only does the texture not return to a soft gel even when immersed in a seasoning solution, but also the swelling and shrinking effects do not occur when exposed to water or immersed in a seasoning solution, so the seasoning is absorbed into the granules. This is because the ingredients cannot be absorbed sufficiently. The amount of citrate to be used is preferably 0.02 to 1.5% (in weight %, the same applies hereinafter), preferably 0.1 to 1.0%, based on the total amount of the fluid raw material. If the amount of citrate added is less than 0.02%, hard gelation tends to occur during gelation with a polyvalent metal salt solution, and at the same time, absorption of seasoning components into the granules tends to be insufficient. If the content exceeds 1.5%, the particles may fuse together and lose their shape during long-term storage of the final product, so care should be taken. This fluid raw material is made into granules, so the viscosity is
It is best to adjust the temperature from 2000 C.P (centipoise) to about 10000 C.P, preferably from 5000 C.P to about 8000 C.P, and it is particularly suitable to use xanthan gum to make the grain shape spherical. In addition, if 5 to 35% of sugars are added to the total amount of fluid raw materials, the specific gravity of the fluid raw materials will increase, and the granules will sink into the polyvalent metal salt solution, making it easier to form clean granules. It is preferable to add sugars within this range. The amount of alginate/low methoxyl pectin to be used alone or as a mixture is based on the total amount of fluid raw materials.
The content is preferably 0.3 to 1.5%, preferably 0.4 to 0.7%. In addition to the raw materials mentioned above, protein raw materials such as egg yolks and whole eggs, and oil and fat raw materials such as soybean oil and sunflower oil can be used as fluid raw materials. still,
When a proteinaceous raw material and an oil or fat raw material are used together, it is preferable to keep the entire fluid raw material in an emulsified state. Next, the fluid raw material prepared in this way is made into small particles with a diameter of 4 to 10 m/m by an appropriate method to form a 0.5 to 4.0% aqueous solution of a polyvalent metal salt, preferably calcium chloride or calcium lactate, preferably 2.0
% aqueous solution. Then, the surface of the particles of the fluid raw material is coated with an insoluble gel film such as calcium alginate, and if the particles are immersed for about 1 to 5 minutes, granules that do not easily collapse when taken out from the immersion liquid are formed. If the granules are immersed in the polyvalent metal salt solution for too long, they will become hard, i.e., the inside of the film will solidify like a jelly and become a hard gel, so care must be taken. Next, the granules are taken out from the polyvalent metal salt solution, washed with water, and then immersed in clean water to be exposed to water. As the water exposure continues, clean water is gradually absorbed into the granules, and the granules swell to 1.1 to 2.0 times the volume before soaking. The granules do not have any cracks on their surface, and are uniform and soft down to the center, becoming a soft gel that is even softer than before being exposed to water. The principle behind the swelling of the granules is not clear, but since the granules swell only when citrate is added to the fluid raw material, citrate plays a catalytic role in promoting the water absorption of the granules. It is presumed that this is the case. Although it depends on the composition of the fluid raw material used, it is desirable that the water exposure be carried out for one hour or more. If the exposure time is less than 1 hour, water absorption of the granules will be insufficient and the granules will not swell, so care should be taken. Finally, the soft gel granules obtained by bleaching with water are immersed in a seasoning liquid to absorb seasoning ingredients into the granules. Seasoning liquids can be of any type, such as vinegar, liquid coffee, black tea, various liquid sauces, etc.
It can be used depending on the purpose of flavoring the granules, such as fruit juice, alcoholic beverages, salt solutions, and sugar solutions. Therefore, it is desirable that the concentration of the seasoning components in the seasoning liquid be higher than that of a normal seasoning liquid in order to facilitate absorption of the seasoning components into the granules. As the granules continue to be immersed in the seasoning liquid, the seasoning components are absorbed into the granules, and at the same time, the granules shrink slightly. The shrinkage of the granules here is due to the osmotic pressure action of the seasoning components in the seasoning liquid. The immersion time in the seasoning liquid depends on the concentration of the seasoning components, but is preferably 1 hour or more. If the immersion time is less than 1 hour, the seasoning components cannot be sufficiently absorbed into the granules, so it is desirable to be careful. The granules that have been immersed in the seasoning liquid are taken out from the seasoning liquid and used as a product. The resulting granular food can be heat sterilized as required. Heat sterilization can be carried out while the granules are immersed in the seasoning liquid, but it is better to heat the granules while they are mixed with the liquid, as convection occurs and heating is done evenly, resulting in better results. can get. As described above, according to the present invention, since citrate is added to the fluid raw material, a soft gel can be obtained by dropping it into a polyvalent metal salt to form granules. When the granules made of the granules are exposed to water, the granules absorb water and swell due to the action of citrate, and the progress of hard gelation is stopped, and the granules are softer than before being exposed to water. It will be done. Furthermore, by immersing the granules in a seasoning liquid, the seasoning components can be sufficiently absorbed into the granules. Therefore, according to the present invention, granular foods with good taste and texture can be reliably produced. Test example (1) Test area Sodium alginate 0.5g Xanthan gum 0.4 Hydrous crystalline glucose 12.0 Sodium citrate 0.5 Clear water 47.6 Egg yolk 5.0 Salad oil 34.0 Using a total of 100g as raw materials, emulsify using a conventional method to determine the viscosity.
Obtain fluid raw material of 6000C/P. This fluid raw material was made into small particles with a diameter of 5 m/m and was dropped into a 2% calcium chloride aqueous solution.
After standing still for a minute, it was taken out to obtain granules. After leaving the obtained granules in still water for 10 hours and exposing them to water, further add 10% to 100 parts of granules.
Fifty parts of saline solution was added and the mixture was allowed to stand for 10 hours for seasoning liquid immersion to obtain a granular food. (2) Control group A control product was prototyped using 100 g of sodium alginate 0.5 g, xanthan gum 0.4, hydrous crystalline glucose 12.0, fresh water 48.1, egg yolk 5.0, salad oil 34.0 (total) as raw materials, and using the same method as the test group with other conditions. For the above test products and control products, the degree of swelling of the volume of the granules immediately after exposure to water and the degree of shrinkage of the volume of the granules immediately after completion of immersion in the seasoning liquid were measured separately. In addition, in order to know the state of absorption of salt into the granules, the salt concentration of the granules of the test product and the control product was measured, and the results shown in Table 1 were obtained.

【表】 尚、表中、膨潤度とは、水晒前の粒体の体積と
比較した場合の体積の増加率をいう。また収縮
度とは調味液浸漬前の粒体の体積と比較した場
合の体積の収縮率をいう。 実施例 1 粒状マヨネーズの製法 (イ) 流動状原料の配合と調整 アルギン酸ナトリウム 0.5Kg キサンタンガム 0.3 含水結晶グルコース 11.2 クエン酸ナトリウム 0.1 食 塩 0.3 清 水 48.5 卵 黄 4.0 サラダ油 30.0 オイルマスタード 0.1 合 計 95Kg 上記原料を使用し、オンレータ内に清水を投
入し、ついで加熱撹拌しながら粉状原料(アル
ギン酸ナトリウム、キサンタンガム、含水結晶
グルコース、クエン酸ナトリウム)を加えて、
ペーストに仕上げた後、このペーストを冷却す
る。 上記ペーストをミキサー内に投入し撹拌しな
がら、先ず、卵黄を投入し、次いで、サラダ油
とオイルマスタードを注加して流動状原料を得
る。 (ロ) 多価金属塩溶液の調整 清水98.0Kgに塩化カルシウム2.0Kgを加えて
溶解させ2.0%塩化カルシウム水溶液を得る。 (ハ) 調味液の配合と調整 食 塩 10Kg 砂 糖 10 グルタミン酸ソーダ 2 酸度8%の食酢 45 清 水 33 合 計 100Kg 上記配合により、調味液を得る。 (ニ) 粒体の形成 上記流動状原料を上記多価金属塩溶液に常法
どおり滴下し、2分後にとり出して粒体を集め
アミの上で水洗する。粒体はやや偏平状であつ
た。 (ホ) 水晒し この粒体を清水中に投入し、10時間水晒し
後、とり出す。粒体は投入前にくらべ略3割体
積が膨潤し、球状となつた。 (ヘ) 調味液浸漬 粒体100部と調味液50部とをタンク中に投入
し、24時間静置の後、とり出したところ、粒体
のマヨネーズが得られた。粒体は投入前にくら
べ略2割体積が収縮したが球状であつた。 実施例 2 粒状コーヒーゼリーの製法 (イ) 流動状原料の配合と調整 低メトキシルペクチン 0.5Kg キサンタンガム 0.4 庶 糖 3.0 クエン酸ナトリウム 0.1 清 水 36.0 合 計 40Kg 上記配合により各原料を溶解し脱気してお
く、 (ロ) 多価金属塩溶液の調整 清水49Kgに塩化カルシウム1Kgを加えて溶解
させ2%塩化カルシウム水溶液を得る。 (ハ) 調味液(コーヒー抽出液)の調整 挽いたコーヒーの粉末10Kgを常法のとおり抽
出し70の抽出液を得る。この濃度は、通常飲
料の略2倍であり、RI3.5、PH4.8であつた。 (ニ) 粒体の形成 上記流動状原料を4m/m目のオリフイスを
通して2%塩化カルシウム水溶液中に滴下し
て、2分後にとり出して粒体を集めアミの上で
水洗する。 (ホ) 水晒し 粒体を清水中に投入し、5時間水晒し後、と
り出す粒体は投入前にくらべて略6割体積が膨
潤し、球状となつた。 (ヘ) 調味液浸漬 粒体100部と上記コーヒー抽出液100部をタン
ク内に投入し90℃で30分間加熱後、冷却し、3
時間放置したところ、やわらかな粒状コーヒー
ゼリーが得られた。粒体は投入前にくらべ、略
0.5割体積が収縮したが球状であつた。
[Table] In the table, the degree of swelling refers to the rate of increase in volume when compared to the volume of the granules before exposure to water. Further, the degree of shrinkage refers to the shrinkage rate of the volume when compared with the volume of the granules before immersion in the seasoning liquid. Example 1 Manufacturing method of granular mayonnaise (a) Combination and adjustment of fluid raw materials Sodium alginate 0.5Kg Xanthan gum 0.3 Hydrous crystalline glucose 11.2 Sodium citrate 0.1 Salt 0.3 Clear water 48.5 Egg yolk 4.0 Salad oil 30.0 Oil mustard 0.1 Total 95Kg Above raw materials Using a water bottle, pour fresh water into the onlet, then add the powdered raw materials (sodium alginate, xanthan gum, hydrated crystalline glucose, sodium citrate) while heating and stirring.
After finishing the paste, the paste is cooled. While putting the above paste into a mixer and stirring, first add egg yolk, then add salad oil and oil mustard to obtain a fluid raw material. (b) Preparation of polyvalent metal salt solution Add 2.0 kg of calcium chloride to 98.0 kg of fresh water and dissolve it to obtain a 2.0% calcium chloride aqueous solution. (c) Mixing and adjusting the seasoning liquid Salt 10Kg Sugar 10 Sodium glutamate 2 Vinegar with an acidity of 8% 45 Fresh water 33 Total 100Kg A seasoning liquid is obtained by the above combination. (d) Formation of granules The above fluid raw material is added dropwise to the above polyvalent metal salt solution in a conventional manner, and after 2 minutes it is taken out and the granules are collected and washed with water on a rack. The grains were slightly oblate. (E) Water exposure The granules are placed in clean water, soaked for 10 hours, and then taken out. The granules swelled by approximately 30% in volume compared to before being added, and became spherical. (f) Seasoning liquid immersion 100 parts of the granules and 50 parts of the seasoning liquid were put into a tank, and after standing still for 24 hours, they were taken out, and a granular mayonnaise was obtained. The volume of the granules shrunk by about 20% compared to before they were added, but they remained spherical. Example 2 Manufacturing method of granular coffee jelly (a) Combination and adjustment of fluid raw materials Low methoxyl pectin 0.5Kg Xanthan gum 0.4 Sucrose 3.0 Sodium citrate 0.1 Clear water 36.0 Total 40Kg Each raw material was dissolved and degassed according to the above composition. (b) Preparation of polyvalent metal salt solution Add 1 kg of calcium chloride to 49 kg of clear water and dissolve to obtain a 2% calcium chloride aqueous solution. (c) Adjustment of seasoning liquid (coffee extract) Extract 10 kg of ground coffee powder in the usual manner to obtain 70 extracts. This concentration was approximately twice that of a regular drink, with an RI of 3.5 and a PH of 4.8. (d) Formation of granules The above fluidized raw material is dropped into a 2% aqueous calcium chloride solution through a 4 m/m orifice, taken out after 2 minutes, and the granules are collected and washed with water on a rack. (e) Water exposure The granules were put into clean water and after being exposed to water for 5 hours, the granules taken out swelled by about 60% in volume compared to before being added, and became spherical. (f) Seasoning liquid immersion: Put 100 parts of the granules and 100 parts of the above coffee extract into a tank, heat at 90°C for 30 minutes, cool, and
After leaving it for a while, soft granular coffee jelly was obtained. The granules are compared before being added.
Although the volume shrank by 0.50%, it remained spherical.

Claims (1)

【特許請求の範囲】 1 アルギン酸塩・低メトキシルペクチンの単独
又は混合物と共にクエン酸塩を添加してある流動
状原料を多価金属塩溶液中に滴下して上記原料の
表面にゲル状皮膜を形成した粒体を得、これを清
水中に浸漬して水晒しをした後、さらに調味液中
に浸漬して調味成分を粒体内に吸収させることを
特徴とする粒状食品の製造方法。 2 流動状原料に糖類を5〜35%添加してある特
許請求の範囲第1項記載の粒状食品の製造方法。
[Claims] 1. A fluid raw material to which citrate is added together with alginate and low methoxyl pectin alone or in combination is dropped into a polyvalent metal salt solution to form a gel-like film on the surface of the raw material. A method for producing a granular food product, which comprises obtaining granules, immersing them in clean water to expose them to water, and then further immersing them in a seasoning liquid to absorb seasoning ingredients into the granules. 2. The method for producing a granular food according to claim 1, wherein 5 to 35% of sugars are added to the fluid raw material.
JP58023866A 1983-02-17 1983-02-17 Preparation of granular food Granted JPS59151850A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58023866A JPS59151850A (en) 1983-02-17 1983-02-17 Preparation of granular food

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58023866A JPS59151850A (en) 1983-02-17 1983-02-17 Preparation of granular food

Publications (2)

Publication Number Publication Date
JPS59151850A JPS59151850A (en) 1984-08-30
JPH045420B2 true JPH045420B2 (en) 1992-01-31

Family

ID=12122359

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58023866A Granted JPS59151850A (en) 1983-02-17 1983-02-17 Preparation of granular food

Country Status (1)

Country Link
JP (1) JPS59151850A (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5814183B2 (en) * 1978-08-31 1983-03-17 キユーピー株式会社 Method for producing spherical food

Also Published As

Publication number Publication date
JPS59151850A (en) 1984-08-30

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