JPH0243469B2 - - Google Patents
Info
- Publication number
- JPH0243469B2 JPH0243469B2 JP61039375A JP3937586A JPH0243469B2 JP H0243469 B2 JPH0243469 B2 JP H0243469B2 JP 61039375 A JP61039375 A JP 61039375A JP 3937586 A JP3937586 A JP 3937586A JP H0243469 B2 JPH0243469 B2 JP H0243469B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- oil
- fats
- oils
- food
- 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
- 239000003921 oil Substances 0.000 claims description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 235000013305 food Nutrition 0.000 claims description 18
- 239000003925 fat Substances 0.000 claims description 17
- 238000010438 heat treatment Methods 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 9
- 239000000243 solution Substances 0.000 claims description 4
- 238000001704 evaporation Methods 0.000 claims description 3
- 230000008020 evaporation Effects 0.000 claims description 3
- 235000019198 oils Nutrition 0.000 description 20
- 235000019197 fats Nutrition 0.000 description 15
- 239000007864 aqueous solution Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 10
- 239000007787 solid Substances 0.000 description 10
- 239000000047 product Substances 0.000 description 8
- 239000002994 raw material Substances 0.000 description 8
- GVJHHUAWPYXKBD-UHFFFAOYSA-N d-alpha-tocopherol Natural products OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-UHFFFAOYSA-N 0.000 description 7
- 239000007788 liquid Substances 0.000 description 7
- 235000010384 tocopherol Nutrition 0.000 description 7
- 229960001295 tocopherol Drugs 0.000 description 7
- 229930003799 tocopherol Natural products 0.000 description 7
- 239000011732 tocopherol Substances 0.000 description 7
- GVJHHUAWPYXKBD-IEOSBIPESA-N α-tocopherol Chemical compound OC1=C(C)C(C)=C2O[C@@](CCC[C@H](C)CCC[C@H](C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-IEOSBIPESA-N 0.000 description 7
- 241000287828 Gallus gallus Species 0.000 description 6
- 238000009835 boiling Methods 0.000 description 6
- 235000013330 chicken meat Nutrition 0.000 description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- 235000013555 soy sauce Nutrition 0.000 description 6
- 238000001694 spray drying Methods 0.000 description 6
- 238000000855 fermentation Methods 0.000 description 5
- 230000004151 fermentation Effects 0.000 description 5
- 235000011194 food seasoning agent Nutrition 0.000 description 5
- 229920001353 Dextrin Polymers 0.000 description 4
- 239000004375 Dextrin Substances 0.000 description 4
- 235000019425 dextrin Nutrition 0.000 description 4
- 235000014347 soups Nutrition 0.000 description 4
- 235000013311 vegetables Nutrition 0.000 description 4
- 239000004278 EU approved seasoning Substances 0.000 description 3
- 241001465754 Metazoa Species 0.000 description 3
- 150000001413 amino acids Chemical class 0.000 description 3
- 210000000988 bone and bone Anatomy 0.000 description 3
- 238000002036 drum drying Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 238000004108 freeze drying Methods 0.000 description 3
- 235000014655 lactic acid Nutrition 0.000 description 3
- 239000004310 lactic acid Substances 0.000 description 3
- 241000234282 Allium Species 0.000 description 2
- 235000002732 Allium cepa var. cepa Nutrition 0.000 description 2
- 244000000626 Daucus carota Species 0.000 description 2
- 235000002767 Daucus carota Nutrition 0.000 description 2
- ZTHYODDOHIVTJV-UHFFFAOYSA-N Propyl gallate Chemical compound CCCOC(=O)C1=CC(O)=C(O)C(O)=C1 ZTHYODDOHIVTJV-UHFFFAOYSA-N 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 235000015203 fruit juice Nutrition 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 235000015277 pork Nutrition 0.000 description 2
- 235000021067 refined food Nutrition 0.000 description 2
- 235000015067 sauces Nutrition 0.000 description 2
- 239000008159 sesame oil Substances 0.000 description 2
- 235000011803 sesame oil Nutrition 0.000 description 2
- DJENHUUHOGXXCB-UHFFFAOYSA-N 2-butyl-6-methoxyphenol Chemical compound CCCCC1=CC=CC(OC)=C1O DJENHUUHOGXXCB-UHFFFAOYSA-N 0.000 description 1
- 240000002234 Allium sativum Species 0.000 description 1
- 240000007087 Apium graveolens Species 0.000 description 1
- 235000015849 Apium graveolens Dulce Group Nutrition 0.000 description 1
- 235000010591 Appio Nutrition 0.000 description 1
- 241000512259 Ascophyllum nodosum Species 0.000 description 1
- 240000006439 Aspergillus oryzae Species 0.000 description 1
- 235000002247 Aspergillus oryzae Nutrition 0.000 description 1
- 240000007124 Brassica oleracea Species 0.000 description 1
- 235000003899 Brassica oleracea var acephala Nutrition 0.000 description 1
- 235000011301 Brassica oleracea var capitata Nutrition 0.000 description 1
- 235000001169 Brassica oleracea var oleracea Nutrition 0.000 description 1
- 241000555825 Clupeidae Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 101710196208 Fibrinolytic enzyme Proteins 0.000 description 1
- 235000007688 Lycopersicon esculentum Nutrition 0.000 description 1
- 235000019502 Orange oil Nutrition 0.000 description 1
- 235000019482 Palm oil Nutrition 0.000 description 1
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- 240000003768 Solanum lycopersicum Species 0.000 description 1
- 235000009337 Spinacia oleracea Nutrition 0.000 description 1
- 244000300264 Spinacia oleracea Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 240000004668 Valerianella locusta Species 0.000 description 1
- 235000003560 Valerianella locusta Nutrition 0.000 description 1
- 239000006286 aqueous extract Substances 0.000 description 1
- 235000015278 beef Nutrition 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 239000002385 cottonseed oil Substances 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003527 fibrinolytic agent Substances 0.000 description 1
- 230000003480 fibrinolytic effect Effects 0.000 description 1
- 235000012041 food component Nutrition 0.000 description 1
- 239000005417 food ingredient Substances 0.000 description 1
- 235000004611 garlic Nutrition 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000010502 orange oil Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002540 palm oil Substances 0.000 description 1
- 239000000546 pharmaceutical excipient Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 235000013324 preserved food Nutrition 0.000 description 1
- 235000010388 propyl gallate Nutrition 0.000 description 1
- 239000000473 propyl gallate Substances 0.000 description 1
- 229940075579 propyl gallate Drugs 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 235000019512 sardine Nutrition 0.000 description 1
- 235000014102 seafood Nutrition 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 235000019871 vegetable fat Nutrition 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Freezing, Cooling And Drying Of Foods (AREA)
- General Preparation And Processing Of Foods (AREA)
- Seeds, Soups, And Other Foods (AREA)
- Formation And Processing Of Food Products (AREA)
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類、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
ている。[Prior art] Animal and vegetable soups, 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. must be made into powder or granules, and in this case spray drying, drum drying or freeze drying are applied.
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イ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(チエ
ンバー)やパイプに付着し、また、排気と共に微
粉となつて逸散し、収率が下落する欠点がある。
また噴霧乾燥法の場合は熱効率が悪く、通常30%
位である。 The most commonly used method, spray drying, involves atomizing an aqueous raw material solution through a rapidly rotating disk or high-pressure nozzle, contacting it with hot air to evaporate the water, and turning the solids into powder, which is then passed through a cyclone. The desired product can be obtained by collecting the product, but this method has the disadvantage that the product adheres to large drying chambers and pipes, and that it becomes fine powder and dissipates with the exhaust air, reducing yield. .
Additionally, spray drying has poor thermal efficiency, typically 30%
It is the rank.
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 solved the drawbacks of the above-mentioned conventional methods and efficiently produced water-soluble powdered foods with good flavor.
Moreover, various methods of manufacturing at low cost were investigated.
[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を加え、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
As a result of various studies, we found that by adding oil and fat to an aqueous food solution in a vacuum concentrator equipped with a stirrer, heating it while stirring and mixing, and applying a moderately strong vacuum, we can produce food in an extremely short time and with extremely high thermal efficiency. Furthermore, the present invention was completed by discovering that a water-soluble powdered food of excellent quality can be obtained with almost no loss of product.
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つて得られ
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, lactic acid fermentation, citric acid fermentation, etc. An example is an aqueous solution of the resulting flavor component.
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
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、ヘツト、チキンオイル等の動物性油
脂、大豆油、棉実油、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, the fats and oils used as a heat medium in the present invention include edible fats and oils such as animal fats and oils such as lard, het and chicken oil, and vegetable fats and oils 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エロー
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
ロピル等の適量を添加してもよい。 Furthermore, appropriate amounts of tocopherol, melanoidin, dibutylhydroxyltoluene, butylhydroxylanisole, propyl gallate, etc. may be added to prevent 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 reduced pressure concentrating 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つて一定
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2〜5倍(容積比)を用いる。 First, oil and fat and raw material aqueous solution are placed in a heating pot. The amount of oil and fat used varies depending on the water content of the raw material aqueous solution, but is usually 1 to 30 times (volume ratio), preferably 2 to 5 times (volume ratio) of the raw material aqueous solution.
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, amino acids, etc.
Excipients such as starch and dextrin may also 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、ほぼ一定の液温
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60〜120℃、減圧度200〜700mm
Hgの組み合わせを適用する。好ましくは温度90
℃、減圧度700mmHgで操作する。 Next, when the heating pot is heated under reduced pressure while stirring, the contents begin to boil, and the water evaporates while maintaining a nearly constant liquid temperature. Any combination of heating temperature and degree of depressurization may be used as long as the water evaporates, but the temperature should be 60 to 120℃ and the degree of decompression to be 200 to 700mm.
Apply a combination of Hg. Preferably temperature 90
Operate at ℃ and vacuum degree of 700 mmHg.
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 increased, the particles of the dried food obtained will become finer, and if these conditions are made gentler, the size of the particles 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
分離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 has been completed, so stop heating, take out the contents, and use a centrifuge to separate fats and oils while still warm (50 to 90°C) 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。 Incidentally, the powdered food obtained in this way contains some oil and fat, but this can be removed by washing with a harmless organic solvent (for example, n-hexane) if necessary.
[発明の効果]
まず、本発明によつ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溶性である。[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
は優れた製品であつて、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付着による損失がないの
で、目的の粉末食品の収率がよく、ほぼ定量的で
ある。 First of all, in the production method of the present invention, there is no loss due to adhesion to the drying can wall in the spray drying method, so the yield of the desired powdered food is good 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、設備投資面で優れている。ま
た本発明の製造方法における熱効率は非常によく
90%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。また、本発明の製造
方法の操作は簡単である。 Next, since the apparatus used in the present invention is simple as described above, conventional spray drying method, drum drying method,
Compared to the freeze-drying method, it is superior in terms of capital investment. Furthermore, the thermal efficiency of the manufacturing method of the present invention is very good.
90% or more, for example about 30% in spray drying method
It is far superior to %. Moreover, the operation of the manufacturing method of the present invention is simple.
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50Kgを、トコフエロール少量を含むチ
キンオイル120Kg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 amount of hot water, oil and fats and insoluble residues were removed, and the extract was concentrated to a solid content concentration of 30%. 50 kg of the liquid was mixed with 120 kg of chicken oil containing a small amount of tocopherol. In addition, when heating and stirring are continued while reducing the pressure to approximately 700 mmHg, the contents boil violently and lose water, and the water evaporation ends after about 2 hours.
この内容物を直ちに遠心分離機にかけ、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 are immediately centrifuged and the chicken oil is separated, resulting in powdered chicken bone soup.
Got 15Kg.
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、トコフエロール少量を含
むラード100Kgに加え、500mmHgの減圧下、約70
℃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。これを直ちに遠心分離
機にかけることにより、粉末醤油約15Kgを得た。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 100 kg of lard containing a small amount of tocopherol, and the mixture was heated to about 70 kg under a reduced pressure of 500 mmHg.
When heated to ℃ and stirred, water is completely lost after about 2 hours and a powder is precipitated. By immediately centrifuging this, approximately 15 kg of powdered soy sauce was obtained.
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%まで濃縮した液40Kg、固形分
40%のアミノ酸水溶液8Kg、濃口醤油5Kg、デキ
ストリン5Kgを撹拌、混合したものを、トコフエ
ロールおよびメラノイジン少量を添加したラード
1220Kg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, fats and oils and insoluble residues were removed, and the solid content was concentrated to 30%. 40 kg of liquid, solid content
Stir and mix 8 kg of 40% amino acid aqueous solution, 5 kg of dark soy sauce, and 5 kg of dextrin, and make lard with a small amount of tocopherol and melanoidin added.
When the contents are added to 1220 kg, heated to about 90°C under a reduced pressure of about 700 mmHg, and stirred, the water content evaporates while boiling violently, and the water evaporation ends after about 2 hours.
この内容物を約70℃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 cooling this content to about 70°C, it is centrifuged to separate the lard.
Obtained 22kg of delicious powdered seasoning.
実施例 4
鰯を熱垂で煮沸抽出し、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、
トコフエロール少量を添加したゴマ油100Kgに加
え、約400mmHgの減圧下、ゆるやかに撹拌しなが
ら80℃付近まで昇温してゆくと、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、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、顆粒
状の美味な調味料約25Kgを得た。Example 4 Sardines were extracted by boiling with hot water, insoluble matters and fats and oils were removed, and the liquid was concentrated to 30% solid content, 50 kg, solid content 40
Add 5 kg of dextrin to 10 kg of % amino acid aqueous solution and 5 kg of dark soy sauce, stir well and mix.
When adding 100 kg of sesame oil to which a small amount of tocopherol has been added and raising the temperature to around 80°C under a reduced pressure of approximately 400 mmHg while stirring gently, the contents will slowly boil and lose all moisture after approximately 3 hours. , precipitates large-grained solids. 60 contents
By cooling to below ℃ and centrifuging, approximately 25 kg of delicious granular seasoning was obtained.
実施例 5
乳酸醗酵液(固形分20%)の30Kgと、麹菌によ
るクエン酸醗酵物の抽出水溶液(固形分約40%)
の20Kgに砂糖10Kgを加え、よく混合した液を、ト
コフエロールを少量添加したコーンサラダ油80Kg
とオレンジ油1Kg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 20%) and aqueous extract solution of citric acid fermentation product using Aspergillus oryzae (solid content approximately 40%)
Add 10kg of sugar to 20kg of the liquid, mix well, and make 80kg of corn salad oil with a small amount of tocopherol added.
and 1 kg of orange oil and heated to approximately 80°C with stirring under reduced pressure of 700 mmHg or more.
The contents lose water while boiling vigorously. Once the boiling subsided, the contents were cooled to below 50°C and the oil was removed by centrifugation to obtain 24 kg of delicious powdered drink base.
実施例 6
細かく切りきざまれたキヤベツ、たまねぎ、に
んじん、もやし、ほうれん草等の混合物または単
体100Kgに、同量の水および繊維素分解酵素約0.1
%を加え、40℃付近で30分反応させた後遠心分離
機にかけ、得られる水溶液を、トコフエロール少
量を添加したラード200Kgに加え混合し、これを
約100℃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 To 100 kg of finely chopped cabbage, onions, carrots, bean sprouts, spinach, etc., or a mixture thereof, add the same amount of water and about 0.1 of a fibrinolytic enzyme.
% and reacted at around 40℃ for 30 minutes, then centrifuged.The resulting aqueous solution was added to 200kg of lard to which a small amount of tocopherol had been added, mixed, heated to about 100℃, and stirred under strong vacuum. 6 kg of water-soluble dried vegetable powder was obtained by removing water and removing fats and oils by centrifugation.
Claims (1)
溶性粉末食品の製造方法。 (1) 食品の水溶液と油脂を混合し、 (2) この混合液を加熱釜に入れ、減圧かつ撹拌下
に加熱して水分を蒸発させ、 (3) 水分の蒸発が完了した後、加熱を停止し、内
容物を遠心分離機にかけ、油脂を濾去し、残留
する水可溶性粉末食品を得る。[Claims] 1. A method for producing a water-soluble powdered food, which is characterized by operating according to the following steps. (1) Mix the aqueous food solution and fats and oils, (2) Place this mixture in a heating pot and heat under reduced pressure and stirring to evaporate the water. (3) After the water evaporation is complete, heat the mixture. Stop, centrifuge the contents, filter out the fat and oil, and obtain the remaining water-soluble powdered food.
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 JPS62198374A (en) | 1987-09-02 |
JPH0243469B2 true 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) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TW200815046A (en) * | 2006-06-22 | 2008-04-01 | Kaneka Corp | 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 |
JP6437727B2 (en) * | 2014-03-11 | 2018-12-12 | アサヒグループ食品株式会社 | Manufacturing method of granular soy sauce seasoning |
-
1986
- 1986-02-25 JP JP61039375A patent/JPS62198374A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS62198374A (en) | 1987-09-02 |
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