JPS61227760A - Production of food extender - Google Patents
Production of food extenderInfo
- Publication number
- JPS61227760A JPS61227760A JP60067988A JP6798885A JPS61227760A JP S61227760 A JPS61227760 A JP S61227760A JP 60067988 A JP60067988 A JP 60067988A JP 6798885 A JP6798885 A JP 6798885A JP S61227760 A JPS61227760 A JP S61227760A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- raw material
- dehydrated
- raw materials
- bones
- 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.)
- Granted
Links
Landscapes
- Meat, Egg Or Seafood Products (AREA)
Abstract
Description
【発明の詳細な説明】 (イ) 産業上の利用分野 この発明は食品増m剤の製造法に関する。[Detailed description of the invention] (b) Industrial application field This invention relates to a method for producing a food thickener.
(ロ) 従来の技術及びその問題点
従来、動物・魚介類の内臓・骨等を加工してペースト状
の食品増量剤を製造するには、上記原料を直接グライン
ダー等にて摺り潰して製造されていた。(b) Conventional technology and its problems Conventionally, in order to manufacture paste-like food extenders by processing the internal organs, bones, etc. of animals and seafood, the above raw materials were directly ground using a grinder, etc. was.
(ハ) 発明解決しようとする問題点
しかしながら、原料には、水分、油分、蛋白質、特にゼ
ラチン質等粘性物質が含まれているため、摩擦熱が発生
して高水分下での加熱を受けて製品が熱変性をおこし、
また、原料中の細菌がそのまま製品に移行して、この製
品をハンバーグ・ソーセージ等に増量剤として使用した
場合、腐敗が早く日持ちが悪いという欠点があった。(c) Problems to be solved by the invention However, since the raw materials contain moisture, oil, protein, and especially viscous substances such as gelatin, frictional heat is generated and the problem is caused by heating under high moisture conditions. The product undergoes heat denaturation,
In addition, the bacteria in the raw materials transfer directly to the product, and when this product is used as a filler for hamburgers, sausages, etc., it has the disadvantage that it spoils quickly and has a short shelf life.
(ニ) 問題点を解決するための手段
この発明では、原料の動物・魚介類の内臓・骨等を、所
定温度に保持した加熱油中に浸漬すると共に、初段階で
は軽度の減圧、次段階では強度の減圧の二段階減圧条件
下で、原料中の水分を蒸発脱水し、引き続き減圧条件下
で脱水処理後の原料の脱油処理を行い、脱水、脱油処理
後の原料を、グラインダー等にて温潤することを特徴と
する食品増量剤の製造法を提供せんとするものである。(d) Means for solving the problem In this invention, raw materials such as internal organs, bones, etc. of animals, seafood, etc. are immersed in heated oil maintained at a predetermined temperature, and at the same time, the pressure is slightly reduced in the first stage, and then in the next stage. Then, water in the raw material is evaporated and dehydrated under two-step conditions of strong vacuum, and then the raw material after dehydration is deoiled under reduced pressure conditions, and the raw material after dehydration and oil removal is transferred to a grinder etc It is an object of the present invention to provide a method for producing a food extender characterized by being warm and moist.
(ホ) 作 用
この発明では、原料を所定温度の加熱油を熱媒体として
原料を加熱すると共に、初期の軽度の減圧により、原料
中の水溶性蛋白質・炭水化物・ビタミン類等の栄養素を
熱凝固及び安定化し、次段階の強度の減圧により原料中
の水分を蒸発脱水し、引続き減圧条件下での脱油処理に
より、常圧下での脱油時とは異なり、常圧に戻す際に原
料組織中に加熱油が大気圧により圧入される以前に脱油
を行うため、脱油処理後の含油量が少ない。以上のよう
に脱水・脱油処理された原料は、蛋白質等の粘性物質が
熱凝固及び脱水されて固形化しているため破砕されやす
く、ブライインダー等による描潰に際し、摩擦熱の発生
が僅少であり、また、原料に残留した加熱油がmW4剤
として作用して、更に摩擦熱の発生を抑制して、原料の
熱変性を防止し、しかも、加熱脱水により原料中の細菌
が死滅して、増量剤として使用した際の腐敗が発生しに
くく日持ちがよい。(E) Function In this invention, the raw materials are heated using heating oil at a predetermined temperature as a heating medium, and nutrients such as water-soluble proteins, carbohydrates, and vitamins in the raw materials are thermally coagulated by a slight initial pressure reduction. The moisture in the raw material is then evaporated and dehydrated by intense vacuum in the next step, and then the raw material structure is removed when the pressure is returned to normal pressure, unlike deoiling under normal pressure. Since the oil is removed before the heated oil is pressurized into the tank under atmospheric pressure, the oil content after the oil removal process is small. Raw materials that have been dehydrated and deoiled as described above are easily crushed because the viscous substances such as proteins are solidified by thermal coagulation and dehydration, and when being crushed with a blinder etc., the generation of frictional heat is minimal. In addition, the heated oil remaining in the raw material acts as a mW4 agent, further suppressing the generation of frictional heat and preventing thermal denaturation of the raw material.Moreover, the bacteria in the raw material are killed by heating and dehydration. When used as a bulking agent, it is less prone to spoilage and has a long shelf life.
(へ) 効 果
この発明によれば、加熱油を熱媒体とした二段階減圧、
脱水処理及び減圧条件下での脱油処理により、各種栄養
素を失うことなく、原料を脱水乾燥させ、原料中のm菌
を死滅させることにより、描潰時の発熱を抑制して原料
の熱変性を防止し、増量剤としての製品の保存性を高め
、また、同製品をハンバーグ、ソーセージ等に添加した
際の保存性を高めるという効果がある。(f) Effects According to this invention, two-stage decompression using heated oil as a heat medium;
Through dehydration treatment and deoiling treatment under reduced pressure conditions, the raw material is dehydrated and dried without losing various nutrients, and by killing microorganisms in the raw material, heat generation during drawing is suppressed and heat denaturation of the raw material is achieved. It has the effect of preventing this, increasing the shelf life of the product as a bulking agent, and increasing the shelf life of the product when added to hamburgers, sausages, etc.
(ト) 実施例
この発明の実施例を詳細に説明すれば、原料の動物・魚
介類の内臓・骨等を、一定のサイズに切断しておき、一
方、容量的4.5mのクツカー中に動物油・植物油・鉱
物油及び動植物油脂の単−油又は混合油を約900kg
投入し所定温度(60〜120℃の間)に加熱しておく
。(G) Example To explain the example of this invention in detail, the internal organs, bones, etc. of animals and seafood as raw materials are cut into a certain size, and on the other hand, they are placed in a cutter with a capacity of 4.5 m. Approximately 900 kg of animal oil, vegetable oil, mineral oil, and single or mixed animal and vegetable fats and oils
Pour it in and heat it to a predetermined temperature (between 60 and 120°C).
次いで、加熱油中に原料を浸漬し、クツカーを閉蓋して
、加熱油の温度を保持しながら原料の加熱油への浸漬か
ら約30分間、10〜20mmH9の軽度の減圧を行い
、次いで740〜750mmhlの強度の減圧を行う。Next, the raw material is immersed in the heated oil, the lid of the cutter is closed, and a slight pressure reduction of 10 to 20 mmH9 is performed for about 30 minutes after the raw material is immersed in the heated oil while maintaining the temperature of the heated oil. Perform a strong vacuum of ~750 mmhl.
かかる減圧処理は、初段階の軽度の減圧により、原料中
の水溶性蛋白質、糖類、ビタミン類等各種栄養素を熱凝
固及び安定化せしめ、次段階の強度の減圧時に、各種栄
養素が流口、分解することを防止するものであり、次段
階強度の減圧により、原料中の水分を蒸発脱水するもの
である。また、加熱油を熱媒体とすることにより原料は
組織の内外から加熱され、強度の減圧と相俟って、比較
的低温でしかも短時間で脱水処理が完了し、各種栄養素
は分解等により失われることなく原料中に残存するもの
である。また、脱水処理に引続いての減圧条件下での脱
油処理では、常圧下での脱油処理と異なり、常圧に戻す
際加熱油が大気圧により原料中に圧入される以前に脱油
処理が行われるので、残油率を低くすることができる。In this depressurization process, various nutrients such as water-soluble proteins, sugars, and vitamins in the raw materials are thermally coagulated and stabilized by a mild decompression in the first stage, and in the next stage of strong depressurization, various nutrients are released into the flow outlet and decomposed. The water in the raw materials is evaporated and dehydrated by the next step of intense vacuum. In addition, by using heated oil as a heat medium, the raw material is heated from the inside and outside of the tissue, and combined with strong vacuum, the dehydration process is completed at a relatively low temperature and in a short time, and various nutrients are lost due to decomposition etc. It remains in the raw material without being degraded. In addition, in deoiling treatment under reduced pressure conditions following dehydration treatment, unlike deoiling treatment under normal pressure, oil is removed before the heated oil is injected into the raw material by atmospheric pressure when returning to normal pressure. Since the treatment is performed, the residual oil percentage can be lowered.
かくして、脱水・脱油処理された原料を、グラインダー
等により描潰して、製品としてのペースト状の食品増量
剤となるものであるが、原料はすでに脱水処理されて破
砕しやすくなっており、更に原料に残留した加熱油が潤
滑剤として作用して発熱が抑制され熱変性を防止してい
る。In this way, the dehydrated and oil-depleted raw material is crushed using a grinder or the like to become a paste-like food extender product, but the raw material has already been dehydrated and is easily crushed. The heating oil remaining in the raw material acts as a lubricant, suppressing heat generation and preventing thermal denaturation.
なお、製品の残油率を更に下げる必要があるときは、ノ
ルマルヘキサン等の有機溶媒を用いて、製品中の油分を
溶解抽出して残油率を低下させることも可能である。Note that if it is necessary to further reduce the residual oil percentage of the product, it is also possible to dissolve and extract the oil in the product using an organic solvent such as n-hexane to reduce the residual oil percentage.
かくして得られた食品増量剤は、原料に含まれていた各
種栄養素を保全したまま、脱水乾燥状態のペースト状で
あり、脱水処理中に細菌が死滅しているので、食品増量
剤として保存中はもちろん、ハンバーグ・ソーセージ等
の練り製品に添加した場合も細菌数が少ないので、腐敗
が遅く日持ちのよい練り製品を作ることができる。The food extender obtained in this way is in the form of a dehydrated and dried paste while preserving the various nutrients contained in the raw materials.Since the bacteria are killed during the dehydration process, it is safe to use as a food extender during storage. Of course, when it is added to pasted products such as hamburgers and sausages, the number of bacteria is small, so it is possible to make paste products that are slow to spoil and have a long shelf life.
Claims (1)
持した加熱油中に浸漬すると共に、初段階では軽度の減
圧、次段階では強度の減圧の二段階減圧条件下で、原料
中の水分を蒸発脱水し、引き続き減圧条件下で脱水処理
後の原料の脱油処理を行い、脱水、脱油処理後の原料を
、グラインダー等にて擂潰することを特徴とする食品増
量剤の製造法。1) The internal organs, bones, etc. of animals and seafood used as raw materials are immersed in heated oil maintained at a predetermined temperature, and the raw materials are immersed in heated oil maintained at a predetermined temperature, and under two-step depressurization conditions: a mild decompression in the first stage, and a strong decompression in the second stage. A food bulking agent characterized by evaporating and dehydrating the water contained therein, then deoiling the dehydrated raw material under reduced pressure conditions, and grinding the dehydrated and deoiled raw material using a grinder or the like. manufacturing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60067988A JPH069480B2 (en) | 1985-03-30 | 1985-03-30 | Food extender manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60067988A JPH069480B2 (en) | 1985-03-30 | 1985-03-30 | Food extender manufacturing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61227760A true JPS61227760A (en) | 1986-10-09 |
JPH069480B2 JPH069480B2 (en) | 1994-02-09 |
Family
ID=13360862
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60067988A Expired - Lifetime JPH069480B2 (en) | 1985-03-30 | 1985-03-30 | Food extender manufacturing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH069480B2 (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4833060A (en) * | 1971-08-30 | 1973-05-07 | ||
JPS59132872A (en) * | 1983-01-19 | 1984-07-31 | Shuzo Nakazono | Solubilization of thermally coagulated protein source |
JPS59166060A (en) * | 1983-03-09 | 1984-09-19 | Tanpaku Shigen Kaihatsu Kk | Method for treating lever and gut of animal, fish, shellfish and poultry |
-
1985
- 1985-03-30 JP JP60067988A patent/JPH069480B2/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4833060A (en) * | 1971-08-30 | 1973-05-07 | ||
JPS59132872A (en) * | 1983-01-19 | 1984-07-31 | Shuzo Nakazono | Solubilization of thermally coagulated protein source |
JPS59166060A (en) * | 1983-03-09 | 1984-09-19 | Tanpaku Shigen Kaihatsu Kk | Method for treating lever and gut of animal, fish, shellfish and poultry |
Also Published As
Publication number | Publication date |
---|---|
JPH069480B2 (en) | 1994-02-09 |
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