JPS62198374A - Production of powder food - Google Patents

Production of powder food

Info

Publication number
JPS62198374A
JPS62198374A JP61039375A JP3937586A JPS62198374A JP S62198374 A JPS62198374 A JP S62198374A JP 61039375 A JP61039375 A JP 61039375A JP 3937586 A JP3937586 A JP 3937586A JP S62198374 A JPS62198374 A JP S62198374A
Authority
JP
Japan
Prior art keywords
oil
food
water
heating
aqueous 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.)
Granted
Application number
JP61039375A
Other languages
Japanese (ja)
Other versions
JPH0243469B2 (en
Inventor
Takuya Kishimoto
卓也 岸本
Masahiko Nishimura
正彦 西村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SANBEESU FOOD KK
Arkray Inc
Original Assignee
SANBEESU FOOD KK
Arkray Inc
Kyoto Daiichi Kagaku KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SANBEESU FOOD KK, Arkray Inc, Kyoto Daiichi Kagaku KK filed Critical SANBEESU FOOD KK
Priority to JP61039375A priority Critical patent/JPS62198374A/en
Publication of JPS62198374A publication Critical patent/JPS62198374A/en
Publication of JPH0243469B2 publication Critical patent/JPH0243469B2/ja
Granted legal-status Critical Current

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  • Seeds, Soups, And Other Foods (AREA)
  • Formation And Processing Of Food Products (AREA)
  • Freezing, Cooling And Drying Of Foods (AREA)
  • General Preparation And Processing Of Foods (AREA)

Abstract

PURPOSE:Aqueous solution of food are dehydrated by heating it in oil to make a water-soluble powder food of good quality keeping the nutrients and savor of the original food in an very short time in high heat efficiency. CONSTITUTION:Animal or vegetable soup, vegetable essence, liquid seasoning, fruit juice and aqueous solution of various foods is charged in a heating pot or kettle together with oil and dehydrated by heating it while stirring under reduced pressure. After completion of dehydration, the oil is centrifuged to collect the powder food.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は水可溶性の粉末食品の製造方法に係り、その製
造方法は食品の水溶液を油脂中で加熱して脱水させるこ
とを特徴とする。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing a water-soluble powdered food, which is characterized by heating an aqueous solution of the food in fats and oils to dehydrate it.

[従来技術] 動物性および植物性のスープ頚、醤油やソース等の調味
料、果汁、乳酸醗酵生産物等は、通常水溶液状態で飲食
されるが、これを加工食品あるいはインスタント食品等
に用いる場合は粉末または顆粒状にする必要があり、こ
の場合は噴霧乾燥法、ドラム乾燥法あるいは凍結乾燥法
が適用されてい最もよく使われている噴霧乾燥法の場合
は、原料の水溶液を゛高速回転ディスクまたは高圧ノズ
ルを通して霧状にし、これを熱風と接触させることによ
り水分を蒸発させ、固形分を粉末状にし、サイクロンに
捕集することにより目的の製品が得られるが、この方法
では製品が大きな乾燥室(チェンバーχやパイプに付着
し、また、排気と共に微粉となって逸散し、収率が下落
する欠点がある。
[Prior art] Animal and vegetable soup bases, seasonings such as soy sauce and sauces, fruit juices, lactic acid fermentation products, etc. are usually consumed in the form of aqueous solutions, but when used in processed foods or instant foods, etc. In this case, spray drying, drum drying, or freeze drying methods are applied.In the spray drying method, which is the most commonly used method, an aqueous solution of the raw material is transferred to a high-speed rotating disk. Alternatively, the desired product can be obtained by atomizing it through a high-pressure nozzle and contacting it with hot air to evaporate the moisture, turning the solids into powder, and collecting it in a cyclone. It has the disadvantage that it adheres to the chamber (chamber χ) and pipes, and also becomes a fine powder and dissipates with the exhaust gas, resulting in a decrease in yield.

また噴霧乾燥法の場合は熱効率が悪く、通常30%位で
ある。
Furthermore, in the case of spray drying, the thermal efficiency is poor, usually around 30%.

ドラム乾燥法は設備費に対して生産効率が悪く、償却費
が高くつくことが大きい欠点である。
The drum drying method has a major disadvantage in that production efficiency is low relative to equipment costs, and depreciation costs are high.

凍結乾燥法はエネルギーを大量に消費し、乾燥経費が高
く、また設備費が極めて高いために償却費が高くつく欠
点がある。
The freeze-drying method consumes a large amount of energy, has high drying costs, and has the drawbacks of high depreciation costs due to extremely high equipment costs.

[発明が解決しようとする問題点] 本発明者等は、上記の従来方法の欠点を解消し、風味の
よい水可溶性の粉末食品を効率よく、しかも安価に製造
する方法について種々検討した。
[Problems to be Solved by the Invention] The present inventors have investigated various methods for solving the drawbacks of the above-mentioned conventional methods and efficiently and inexpensively producing water-soluble powdered foods with good flavor.

[問題点を解消するための手段] 本発明者等は、かかる従来法の難点に鑑み、種々検討し
た結果、食品の水溶液を撹拌機付き真空濃縮釜の中の油
脂に加え、撹拌混合しながら加熱し、適度の強さの真空
をかけることにより、極めて短時間に、また極めて熱効
率よく、更に殆ど製品を損失することなく、優れた品質
の水可溶性粉末食品が得られることを見出して本発明を
完成した。
[Means for Solving the Problems] In view of the drawbacks of the conventional method, the present inventors conducted various studies, and as a result, added an aqueous solution of food to oil and fat in a vacuum concentrator equipped with a stirrer, and while stirring and mixing. The present invention was based on the discovery that by heating and applying a moderately strong vacuum, a water-soluble powdered food of excellent quality can be obtained in an extremely short time, with extremely high thermal efficiency, and with almost no loss of product. completed.

以下に本発明を説明する。The present invention will be explained below.

まず、本発明において原料に該当する食品の水溶液(以
下これを「原料水溶液」という)としては、牛、豚、鶏
、魚介等を水で煮沸して得られる動物性スープ、トマト
、たまねぎ、にんにく、にんじん、セロリ、こんぶ等か
ら同様にして得られる植物性スープ、繊維素分解酵素に
よって得られる植物性のエキス、醤油、ソース等の液体
調味料、果汁、乳酸醗酵やクエン酸醗酵等から得られる
呈味成分の水溶液が挙げられる。
First, food aqueous solutions that correspond to raw materials in the present invention (hereinafter referred to as "raw material aqueous solutions") include animal soup obtained by boiling beef, pork, chicken, seafood, etc. in water, tomatoes, onions, garlic, etc. , vegetable soups obtained in the same way from carrots, celery, kelp, etc., vegetable extracts obtained by fibrinolytic enzymes, liquid seasonings such as soy sauce and sauces, fruit juices, obtained from lactic acid fermentation, citric acid fermentation, etc. Examples include aqueous solutions of taste components.

これらの各原料水溶液は、それぞれ単独で使用してもよ
いが、任意に混合して用いてもよい。
Each of these raw material aqueous solutions may be used alone, or may be used in arbitrary combination.

そして、これらの原料水溶液は、必要に応じて才濾過し
、実質的に不溶物を除去して用いる。
These raw material aqueous solutions are filtered as necessary to substantially remove insoluble matter before use.

次に、本発明で熱媒体として用いる油脂としては、ラー
ド、ヘット、チキンオイル等の動物性油脂、大豆油、綿
実油、パーム油、ゴマ油等の植物性油脂などの食用油脂
が挙げられる。
Next, examples of the fats and oils used as a heat medium in the present invention include animal fats and oils such as lard, het oil, and chicken oil, and edible fats and oils such as vegetable oils and fats such as soybean oil, cottonseed oil, palm oil, and sesame oil.

そして、これらはそれぞれ単独で用いてもよく、任意に
混合してもよい。
Each of these may be used alone or may be arbitrarily mixed.

更に、油脂の酸化防止のためにトコフェロール、メラノ
イジン、ジブチルヒドロキシルトルエン、ブチルヒドロ
キシルアニソール、没食子酸プロ七ル等の適量を添加し
てもよい。
Furthermore, appropriate amounts of tocopherol, melanoidin, dibutylhydroxyltoluene, butylhydroxylanisole, pro7yl gallate, etc. may be added to prevent the oxidation of fats and oils.

更に、本発明を実施するには、撹拌機を有する加熱釜、
これと連結する減圧濃縮装置(真空ポンプ、水蒸気凝縮
器等)および粉末製品を油脂から分離するための遠心分
離機が用いられる。
Furthermore, in order to carry out the present invention, a heating pot having a stirrer,
A vacuum concentration device (vacuum pump, steam condenser, etc.) connected thereto and a centrifugal separator for separating the powder product from fats and oils are used.

更に詳しくは、本発明は次のとおり実施される。More specifically, the invention is implemented as follows.

まず、油脂と原料水溶液を加熱釜に入れる。油脂の使用
量は原料水溶液の水分含量によって一定しないが、通常
には原料水溶液の1〜30倍(容積比)、好ましくは2
〜5f”(容積比)を用いる。
First, oil and fat and raw material aqueous solution are placed in a heating pot. Although the amount of oil and fat used varies depending on the water content of the raw material aqueous solution, it is usually 1 to 30 times the raw material aqueous solution (volume ratio), preferably 2
~5f'' (volume ratio) is used.

この際、食塩、砂糖、アミノ酸等の調味料や、澱粉、デ
キストリン等の賦形剤を添加してもよい。
At this time, seasonings such as salt, sugar, and amino acids, and excipients such as starch and dextrin may be added.

次に、加熱釜を撹拌しながら減圧下で加熱してゆくと、
内容物は沸騰を開始し、はぼ一定の液温を保ちながら水
分が蒸発してゆく、加熱温度と減圧度は、水が蒸発しさ
えすればどんな組み合わせでもよいが、温度60〜12
0℃、減圧度200〜700mmHgの組み合わせを適
用する。好ましくは温度90℃、減圧度700 m m
 Hgで繰作する。
Next, as the heating pot is heated under reduced pressure while stirring,
The contents begin to boil, and the water evaporates while maintaining a constant liquid temperature.Any combination of heating temperature and degree of decompression can be used as long as the water evaporates, but at a temperature of 60 to 12
A combination of 0°C and reduced pressure of 200 to 700 mmHg is applied. Preferably the temperature is 90°C and the degree of vacuum is 700 mm.
Repeat with Hg.

この際、撹拌および減圧度を強くすると、得られる乾燥
食品の粒子は細かくなり、これらの条件をゆるやかにす
ると、粒子の大きさは粗大となり、顆粒状に仕上げるこ
とも可能である。
At this time, if the degree of stirring and vacuum is strengthened, the particles of the dried food obtained will become finer, and if these conditions are made gentler, the particle size will become coarser and it is also possible to finish it in the form of granules.

上記の様に加熱脱水を続けてゆくと、やがて内容物の沸
騰が静まり、温度が上昇し始める。これは脱水が完了し
た証拠であるので、加熱を停止し、内容物を取り出し、
温時(50〜90℃)に遠心分i4機を用いて油脂を分
離し、目的とする粉末食品を得る。
As the heating and dehydration continues as described above, the boiling of the contents eventually subsides and the temperature begins to rise. This is proof that dehydration is complete, so stop heating, remove the contents,
At a warm temperature (50 to 90°C), fats and oils are separated using a centrifugal separator i4 to obtain the desired powdered food.

尚、この様にして得られる粉末食品は若干の油脂を含有
しているが、必要に応じて無害な有機溶媒(例えばn−
ヘキサン)で洗浄して除去することができる。
The powdered food obtained in this way contains some oil and fat, but if necessary, a harmless organic solvent (e.g. n-
It can be removed by washing with (hexane).

[発明の効果] まず、本発明によって得られる粉末食品は、その原料食
品成分の本来の風味を良好に保持しており、その成分自
体は水に可容性である。
[Effects of the Invention] First, the powdered food obtained by the present invention retains the original flavor of its raw food ingredients well, and the ingredients themselves are soluble in water.

この様な点において本発明で得られる粉末食品は優れた
製品であって、加工食品用およびインスタント食品用に
極めて適している。
In these respects, the powdered food obtained by the present invention is an excellent product, and is extremely suitable for processed foods and instant foods.

次に、本発明の製造方法は次の利点を有する。Next, the manufacturing method of the present invention has the following advantages.

まず第一に、本発明の製造方法では、噴霧乾燥法におけ
る乾燥缶壁へのけ着による損失がないので、目的の粉末
食品の収率がよく、はぼ定量的である。
First of all, in the production method of the present invention, there is no loss due to adhesion to the wall of the drying can in the spray drying method, so the yield of the desired powdered food is high and almost quantitative.

次に、本発明で用いる装置は前述のとおり簡単であるの
で、従来の噴霧乾燥法、ドラム乾燥法、凍結乾燥法に比
し、設備投資面て優れている。また本発明の製造方法に
おける熱効率は非常によく9026以上であり、例えば
噴霧乾燥法における約30%に比し遥かに優れている。
Next, since the apparatus used in the present invention is simple as described above, it is superior in terms of equipment investment compared to conventional spray drying methods, drum drying methods, and freeze drying methods. Further, the thermal efficiency in the production method of the present invention is very good, 9026 or higher, which is far superior to, for example, about 30% in the spray drying method.

また、本発明の製造方法の操作は簡単である。Furthermore, the manufacturing method of the present invention is easy to operate.

以上述べた様に、本発明の製造方法は、優れた水可溶性
粉末食品を提供する極めて有利な製造方法である。
As described above, the production method of the present invention is an extremely advantageous production method that provides an excellent water-soluble powdered food.

[実施例] 実施例 1 鶏骨を約3倍量の熱水で抽出し、油脂および不溶性残渣
を除去した抽出液を固形分濃度30%まで濃縮した液5
0Kgを、トコフェロール少量を含むチキンオイル12
0Kgに加え、約700mmHgに減圧しながら加熱、
撹拌を続けると、内容物は激しく沸騰しながら水分を失
い、約2時間後に水分の蒸発は終わる。
[Example] Example 1 Chicken bones were extracted with about 3 times the volume of hot water, and the extract obtained by removing fats and oils and insoluble residues was concentrated to a solid content concentration of 30%. Liquid 5
0Kg of chicken oil containing a small amount of tocopherol 12
In addition to 0Kg, heat while reducing the pressure to about 700mmHg.
As stirring continues, the contents lose water while boiling vigorously, and evaporation of water stops after about 2 hours.

この内容物を直ちに遠心分M機にかけ、チキンオイルを
分離することにより、鶏骨スープの粉末15Kgを得た
The contents were immediately applied to a centrifuge M machine to separate chicken oil, thereby obtaining 15 kg of chicken bone soup powder.

実施例 2 濃口醤油30Kgと固形分濃度30%のデキストリン水
溶液20Kgの混合物を、トコフェロール少量を含むラ
ードloOKgに加え、500mmHgの減圧下、約7
0℃に加熱、撹拌すると、約2時間後に水分を完全に失
い、粉末を析出する。
Example 2 A mixture of 30 kg of dark soy sauce and 20 kg of dextrin aqueous solution with a solid content concentration of 30% was added to loOKg of lard containing a small amount of tocopherol, and the mixture was heated under a reduced pressure of 500 mmHg to about 7 kg.
When heated to 0°C and stirred, water is completely lost after about 2 hours, and a powder is precipitated.

これを直ちに遠心分離機にかけることにより一5粉末醤
油約15Kgを得た。
This was immediately centrifuged to obtain about 15 kg of 15 powdered soy sauce.

実施例 3 豚骨を熱水で抽出し、油脂および不溶性残渣を除去し、
固形分30?6まで濃縮した液40Kg、固形分40%
のアミノ酸水溶液8Kg−[口醤油5Kg、デキストリ
ン5Kgを撹拌、混合したものを、トコフェロールおよ
びメラノイジン少量を添加したラード120Kgに加え
、約700mmHgの減圧下、約90℃に加熱、撹拌す
ると、内容物は激しく沸騰しながら水分を蒸発し、約2
時間後に水分の蒸発は終わる。
Example 3 Pork bones were extracted with hot water to remove fats and oils and insoluble residues,
40 kg of liquid concentrated to solid content 30-6, solid content 40%
A mixture of 8 kg of an amino acid aqueous solution, 5 kg of soy sauce, and 5 kg of dextrin was added to 120 kg of lard to which a small amount of tocopherol and melanoidin had been added, and when the mixture was heated to approximately 90°C under a reduced pressure of approximately 700 mmHg and stirred, the contents were Evaporate the water while boiling vigorously, and boil for about 2
After some time, the moisture will stop evaporating.

この内容物を約70°Cに冷却した後に、これを遠心分
離機にかけ、ラードを分離することにより、美味な粉末
調味料22Kgを得た。
After the contents were cooled to about 70°C, they were centrifuged to separate the lard, yielding 22 kg of a delicious powdered seasoning.

実施例 4 鰯を熱水で煮沸抽出し、不溶物および油脂を除去し、固
形分30%まで濃縮した液50Kg、固形分40%のア
ミノ酸水溶液10Kg、濃口醤油5Kgに、デキストリ
ン5Kgを加え、よく撹拌混合したものを、トコフェロ
ール少量を添加したゴマ油100Kgに加え、約400
mmHgの減圧下、ゆるやかに撹拌しなから80’C付
近まで昇温しでゆくと、内容物はゆるやかに沸騰しなが
ら、約3時間後水分を完全に失い1粒子の大きい固形物
を析出する。内容物を60℃以下に冷却し、遠心分離す
ることにより、!i粒状の美味な調味料約25Kgを得
た。
Example 4 Sardines were extracted by boiling in hot water, insoluble materials and fats and oils were removed, and dextrin (5 kg) was added to 50 kg of the liquid concentrated to 30% solids, 10 kg of an aqueous amino acid solution with a solid content of 40%, and 5 kg of dark soy sauce. Add the stirred mixture to 100 kg of sesame oil containing a small amount of tocopherol, and add about 400 kg of sesame oil to which a small amount of tocopherol has been added.
When the temperature is raised to around 80'C under a reduced pressure of mmHg and with gentle stirring, the contents will boil slowly and after about 3 hours completely lose moisture and precipitate one large particle of solid matter. . By cooling the contents to below 60°C and centrifuging,! Approximately 25 kg of delicious seasoning in the form of i-granules was obtained.

実施例 5 乳酸醗酵液(固形分209≦)の30Kgと、麹菌によ
るクエン酸醗酵物の抽出水溶液(固形公約40%)の2
0Kgに砂1!10Kgを加え、よく混合した液を、ト
コフェロールを少量添加したコーンサラダ油80Kgと
オレンジ油IKgとの混合物に加え、700mmHg以
上の減圧下、撹拌しながら約80℃に加熱すると、内容
物は激しく沸騰しながら水分を失う、沸騰がおさまれば
内容物を50℃以下に冷却し、油分を遠心分離により除
去して美味な粉末状のドリンクベース24Kgを得た。
Example 5 30 kg of lactic acid fermentation liquid (solid content 209≦) and 2 pieces of aqueous solution of citric acid fermentation product extracted by Aspergillus oryzae (solid content 40%)
Add 1 to 10 kg of sand to 0 kg, mix well, add to a mixture of 80 kg of corn salad oil to which a small amount of tocopherol has been added, and I kg of orange oil, and heat to approximately 80°C with stirring under reduced pressure of 700 mmHg or more. The contents lost water while boiling violently. Once the boiling subsided, the contents were cooled to below 50°C and the oil was removed by centrifugation, yielding 24 kg of a delicious powdered drink base.

実施例 6 細かく切りきざまれなキャベツ、たまねぎ、にんじん、
もやし、はうれんそう等の混合物または箪#100Kg
に、同量の水および繊維素分解酵素的0.1%を加え、
40℃け近で30分反応さ・せな液を、トコフェロール
少量を添加したラード200Kgに加え混合し、これを
約100’Cに加熱、撹拌しながら強い減圧下で水分を
除去し、油脂を遠心分離により除去することにより、水
溶性乾燥野菜粉末6Kgを得た。
Example 6 Finely chopped cabbage, onions, carrots,
Mixture of bean sprouts, spinach, etc. or container #100Kg
Add the same amount of water and 0.1% fibrinolytic enzyme to
React for 30 minutes at around 40°C. Add and mix the Sena liquid to 200kg of lard to which a small amount of tocopherol has been added. Heat this to about 100'C, remove water under strong vacuum while stirring, and centrifuge the fats and oils. By removing by separation, 6 kg of water-soluble dried vegetable powder was obtained.

Claims (1)

【特許請求の範囲】[Claims] 食品の水溶液を油脂中で加熱して脱水させることを特徴
とする水可溶性粉末食品の製造方法。
A method for producing a water-soluble powdered food, which comprises heating an aqueous food solution in oil and fat to dehydrate it.
JP61039375A 1986-02-25 1986-02-25 Production of powder food Granted JPS62198374A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61039375A JPS62198374A (en) 1986-02-25 1986-02-25 Production of powder food

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61039375A JPS62198374A (en) 1986-02-25 1986-02-25 Production of powder food

Publications (2)

Publication Number Publication Date
JPS62198374A true JPS62198374A (en) 1987-09-02
JPH0243469B2 JPH0243469B2 (en) 1990-09-28

Family

ID=12551287

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61039375A Granted JPS62198374A (en) 1986-02-25 1986-02-25 Production of powder food

Country Status (1)

Country Link
JP (1) JPS62198374A (en)

Cited By (3)

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JP2009149584A (en) * 2007-12-21 2009-07-09 Kaneka Corp Reduced coenzyme q10-containing particulate composition and its manufacturing method
JP5140585B2 (en) * 2006-06-22 2013-02-06 株式会社カネカ Reduced coenzyme Q10-containing composition and method for producing the same
JP2015171325A (en) * 2014-03-11 2015-10-01 天野実業株式会社 Granular soy sauce seasoning and production method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5140585B2 (en) * 2006-06-22 2013-02-06 株式会社カネカ Reduced coenzyme Q10-containing composition and method for producing the same
US9295656B2 (en) 2006-06-22 2016-03-29 Kaneka Corporation Composition containing reduced coenzyme Q10 and production method thereof
US9981899B2 (en) 2006-06-22 2018-05-29 Kaneka Corporation Composition containing reduced coenzyme Q10 and production method thereof
JP2009149584A (en) * 2007-12-21 2009-07-09 Kaneka Corp Reduced coenzyme q10-containing particulate composition and its manufacturing method
JP2015171325A (en) * 2014-03-11 2015-10-01 天野実業株式会社 Granular soy sauce seasoning and production method thereof

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