JPH0573373B2 - - Google Patents
Info
- Publication number
- JPH0573373B2 JPH0573373B2 JP59088939A JP8893984A JPH0573373B2 JP H0573373 B2 JPH0573373 B2 JP H0573373B2 JP 59088939 A JP59088939 A JP 59088939A JP 8893984 A JP8893984 A JP 8893984A JP H0573373 B2 JPH0573373 B2 JP H0573373B2
- Authority
- JP
- Japan
- Prior art keywords
- soy sauce
- vacuum
- temperature
- drying
- thin film
- 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
- 235000013555 soy sauce Nutrition 0.000 claims description 27
- 239000010409 thin film Substances 0.000 claims description 11
- 150000003839 salts Chemical class 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 8
- 238000001291 vacuum drying Methods 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000000654 additive Substances 0.000 description 6
- 238000001704 evaporation Methods 0.000 description 6
- 230000008020 evaporation Effects 0.000 description 6
- 239000012141 concentrate Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 239000011550 stock solution Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 238000004108 freeze drying Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000001694 spray drying Methods 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Landscapes
- Soy Sauces And Products Related Thereto (AREA)
- Seasonings (AREA)
Description
【発明の詳細な説明】
本発明は低塩粉末醤油の製造方法に関するもの
であつて、特に添加物がなく純粋な粉末醤油であ
つて、温水等に戻したときほぼ原料醤油と同等の
品質を保持するものを安価に提供できる製造方法
に係るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing low-salt powdered soy sauce, which is a pure powdered soy sauce without any additives, and which has almost the same quality as the raw soy sauce when reconstituted with hot water, etc. This relates to a manufacturing method that can provide a holding product at a low cost.
粉末醤油の製法には従来、凍結乾燥法、スプレ
ードライ法等があり、いずれも原料醤油を乾燥さ
せたものである。 Conventional methods for producing powdered soy sauce include freeze-drying and spray-drying, both of which involve drying raw soy sauce.
凍結乾燥法は低温で処理されるため、乾燥粉末
を水、温水に戻したとき、原料醤油の持つ品質と
ほぼ同等のものを再現できる。しかも添加物の混
らない純粋な粉末醤油ができる。但し、単位処理
当りの製造費用が高く、装置面積も広く必要とす
ることが、欠点である。 Since the freeze-drying method is processed at low temperatures, when the dried powder is returned to water or hot water, it is possible to reproduce the quality almost equivalent to that of the raw soy sauce. What's more, you can make pure powdered soy sauce without any additives. However, the disadvantages are that the manufacturing cost per unit treatment is high and the equipment requires a large area.
また、スプレードライ法は、製造費用は安い
が、原料醤油をそのまま噴霧し乾燥しようとする
と、乾燥塔内壁に付着し、取出しが困難となる、
一部製品にコゲが生ずる、比較的高温熱風を利用
するので風味成分が排気ガス中に移動し製品価値
を落す等の欠点があり、これらの欠点を克服する
ためにデキストリンを乾物比20%程度添加し乾燥
している。しかし、斯る添加剤の使用は近時の食
品に対する安全思想の高まりの上から好ましくな
いばかりでなく、水、温水に戻したとき原料醤油
と比較すると味、香、色等が劣るという欠点は免
れ得ないものであつた。 In addition, although the spray drying method has low production costs, if you spray the raw soy sauce as it is and try to dry it, it will stick to the inner wall of the drying tower and be difficult to remove.
There are drawbacks such as scorching on some products and the use of relatively high-temperature hot air, which causes flavor components to migrate into the exhaust gas and reduce product value. Add and dry. However, the use of such additives is not only undesirable due to the recent rise in food safety concerns, but also has the disadvantage that the taste, aroma, color, etc. are inferior to the raw soy sauce when reconstituted with cold or hot water. It was something that could not be avoided.
本発明はこのような従来製法の欠点を解消せん
としてなされたものであつて、先ず原料醤油を遠
心式薄膜真空濃縮装置において、低温下で瞬時に
濃縮し、析出した塩分を系外に除去し、しかる
後、これを真空乾燥装置で低温下で一気に乾燥す
るようにしたものである。これにより製造上添加
剤を混入せず純粋な粉末醤油であつて、温水で戻
したとき原料醤油の持つ味、香、色をほぼ再現で
きる優れた製品を、安い製造費用で製造できるも
のである。 The present invention was made to overcome the drawbacks of the conventional production method. First, raw soy sauce is instantaneously concentrated at low temperature in a centrifugal thin film vacuum concentrator, and precipitated salts are removed from the system. After that, this was dried all at once at a low temperature using a vacuum dryer. This makes it possible to produce an excellent product at a low manufacturing cost, which is a pure powdered soy sauce without any additives mixed in during manufacturing, and which can almost reproduce the taste, aroma, and color of the raw soy sauce when reconstituted with hot water. .
以下本発明を図示の実施例に基づいて具体的に
説明する。第1図は本発明の実施装置を骨格的に
示すものであつて、このものは遠心式薄膜真空濃
縮装置Aと真空乾燥装置Bを主体とするものであ
り、以下順を追つて説明する。先ず符号1は原液
供給タンクであつて、原液供給パイプ2により遠
心式薄膜真空濃縮装置Aと接続され、その間に原
液供給ポンプ3を設ける。 The present invention will be specifically described below based on illustrated embodiments. FIG. 1 schematically shows an apparatus for implementing the present invention, which is mainly composed of a centrifugal thin film vacuum concentration apparatus A and a vacuum drying apparatus B, which will be explained in sequence below. First, reference numeral 1 denotes a stock solution supply tank, which is connected to a centrifugal thin film vacuum concentrator A through a stock solution supply pipe 2, and a stock solution supply pump 3 is provided therebetween.
遠心式薄膜真空濃縮装置Aは真空容器5中に回
転する略円錐形ロータ6を設けたものであり、真
空容器5ひ真空ポンプ7を接続すると共にコンデ
ンサ8を設け、吸引した排気を気水分離して放出
する。また略円錐形ロータ6は内部をジヤケツト
構造とし、その中央部附近に蒸気等の加熱媒体の
供給部9を設け、外周部に集液溝10を形成し、
ここから機外にドレン回収チユーブ10を設け、
ここに真空ポンプ11を接続する。 The centrifugal thin film vacuum concentrator A is equipped with a rotating substantially conical rotor 6 in a vacuum container 5, and a vacuum pump 7 is connected to the vacuum container 5, and a condenser 8 is installed to separate air and water from the sucked exhaust gas. and release it. Further, the substantially conical rotor 6 has a jacket structure on the inside, a supply section 9 for a heating medium such as steam is provided near the center thereof, and a liquid collection groove 10 is formed on the outer periphery.
From here, a drain collection tube 10 is installed outside the machine,
A vacuum pump 11 is connected here.
またローラ外側の蒸発面6の中心部に前期原液
供給パイプ2の先を臨ませ、周縁部に濃縮液排出
チユープ12を設ける。 Further, the tip of the stock solution supply pipe 2 faces the center of the evaporation surface 6 on the outside of the roller, and a concentrated solution discharge tube 12 is provided at the peripheral edge.
尚、本発明においては濃縮を真空中で行ない低
温で蒸発させるものであるが、この際、蒸発に必
要な熱量の補給が必要であり、ここにおいて加熱
側の蒸気等の加熱媒体の温度を一定の温度に保つ
ことが望ましい。このため加熱媒体系内圧を制御
する構成を付加するのを可とする。 In the present invention, concentration is performed in a vacuum and evaporated at a low temperature, but at this time, it is necessary to replenish the amount of heat necessary for evaporation, and the temperature of the heating medium such as steam on the heating side is kept constant. It is desirable to maintain the temperature at For this reason, it is possible to add a configuration for controlling the internal pressure of the heating medium system.
次に真空乾燥装置Bは一例としてバンド型連続
真空乾燥装置を示すものである。符号35は真空
容器であつて真空ポンプ36を接続する。真空容
器35内にはエンドレスの平ベルト37を一対の
ロールにより張設し、ロールの一方を駆動してベ
ルト37を走行させる。駆動ロールには適宜市販
に供されている公知の変速機を附設し、ベルト3
7の走行速度を選択する構造とし得る。 Next, the vacuum drying device B is a band type continuous vacuum drying device as an example. Reference numeral 35 is a vacuum container to which a vacuum pump 36 is connected. An endless flat belt 37 is stretched in the vacuum container 35 by a pair of rolls, and one of the rolls is driven to run the belt 37. A known transmission that is commercially available is appropriately attached to the drive roll, and the belt 3
7 traveling speeds may be selected.
また、ベルト37には加熱用プレート38を一
定の長さに亘つて配設するものであつて、このも
のはベルト上の各部で異なつた温度条件での加熱
を行なうものであり、例えば第1ゾーンは蒸気、
第2ゾーンは温水を通すことが行なわれる。 Further, a heating plate 38 is disposed on the belt 37 over a certain length, and this plate heats each part of the belt under different temperature conditions. zone is steam,
The second zone is provided with hot water.
そして各加熱用プレート38に供給する蒸気、
温水等は適宜公知の温度調節装置を附設し、必要
温度に維持する構造とし得る。また、ベルト37
への濃縮液の供給部は一例として首振りノズルと
し、濃縮液をベルト上に均一に附着させ、ベルト
後端部には、バルブ39を具えた製品排出口40
を形成する。更に上記装置と共に次の装置を付加
する。即ち、遠心式薄膜真空濃縮装置Aと真空乾
燥装置Bとの間に過器41を設けると共にその
前後に濃縮液の供給用ポンプ42,43を設け
る。また、真空乾燥装置Bの製品排出口40の後
段には図示はしないが粉砕機、又はこれと共に造
粒機を設けるものである。 and steam supplied to each heating plate 38;
The hot water may be maintained at a required temperature by appropriately attaching a known temperature control device. Also, belt 37
The supply part of the concentrated liquid to the belt is, for example, an oscillating nozzle, so that the concentrated liquid is evenly deposited on the belt, and the rear end of the belt has a product discharge port 40 equipped with a valve 39.
form. Furthermore, the following devices are added in addition to the above devices. That is, a filter 41 is provided between the centrifugal thin film vacuum concentrator A and the vacuum dryer B, and pumps 42 and 43 for supplying concentrated liquid are provided before and after the filter. Further, although not shown, a pulverizer or a granulator is provided at a stage subsequent to the product discharge port 40 of the vacuum drying apparatus B, although not shown.
次に本発明方法の実施例を説明する。 Next, examples of the method of the present invention will be described.
先ず原料醤油(塩分濃度17%)を原料供給タン
ク1から遠心式薄膜真空濃縮装置Aに供給する。
同装置は加熱用蒸気温度100℃、真空容器真空度
約40メートル、蒸発温度40℃、ロータ回転数
800r.p.m、原料供給量300/Hの諸条件で運転
を行なう。原料液は略円錐形ロータ6の内面中心
部に供給され、回転により生ずる遠心力でロータ
内面を移動して薄膜状となり、約1秒程度で外周
部に集まり固定の濃縮液排出チユーブ12を経て
外部に取出される。この間、真空容器5内は減圧
状態が保たれ、蒸発面への短時間の滞留と減圧に
よる低温下での蒸発により、原料醤油の品質を全
量維持したまま濃縮ができる。これにより原料醤
油を3.3倍に濃縮し、塩分濃度56%の濃縮液を得
た。56%の塩分のうち25%は晶析し、30%の塩分
は濃縮液中に存在する。結晶塩はバンド型連続真
空乾燥装置Bに投入する前段階で過器41によ
り過し、系外へ取出した。次に30%の塩分を含
む濃縮液を、バンド型連続真空乾燥装置Bへ投入
する。 First, raw soy sauce (salt concentration 17%) is supplied from raw material supply tank 1 to centrifugal thin film vacuum concentrator A.
The device has a heating steam temperature of 100℃, a vacuum chamber vacuum level of approximately 40 meters, an evaporation temperature of 40℃, and a rotor rotation speed.
The operation is carried out under the following conditions: 800 rpm, raw material supply rate 300/hour. The raw material liquid is supplied to the center of the inner surface of the substantially conical rotor 6, moves along the inner surface of the rotor by the centrifugal force generated by rotation, becomes a thin film, collects on the outer periphery in about 1 second, and passes through the fixed concentrate discharge tube 12. taken outside. During this time, a reduced pressure state is maintained in the vacuum container 5, and by short-term residence on the evaporation surface and evaporation at low temperatures due to reduced pressure, it is possible to concentrate the raw material soy sauce while maintaining its quality in its entirety. As a result, the raw soy sauce was concentrated 3.3 times to obtain a concentrated solution with a salt concentration of 56%. Of the 56% salt, 25% crystallizes and 30% salt is present in the concentrate. The crystalline salt was filtered through a filter 41 before being introduced into the band-type continuous vacuum drying apparatus B, and was taken out of the system. Next, the concentrated liquid containing 30% salt is introduced into band type continuous vacuum drying apparatus B.
同装置は第1段加熱温度120℃、第2段加熱温
度60℃、真空度9トール、乾燥時間20分の諸条件
で運転を行なう。濃縮液はポンプ43を経由し、
首振りノズルから均一に送られ、ベルト37上に
薄膜上附着し、そして、ベルト上にて泡末化し間
接的に加熱乾燥されて6.3%WBの乾燥醤油を得
るものである。ここにおいても、加熱温度と蒸発
温度は必要な温度に調節可能であり低温での処理
が可能であり原料醤油の持つ品質を損うことがな
い。 The equipment is operated under the following conditions: first stage heating temperature 120°C, second stage heating temperature 60°C, degree of vacuum 9 Torr, and drying time 20 minutes. The concentrated liquid passes through the pump 43,
The soy sauce is uniformly sent from an oscillating nozzle, deposited on a belt 37 as a thin film, turned into foam on the belt, and indirectly heated and dried to obtain dry soy sauce with a WB of 6.3%. Here, too, the heating temperature and evaporation temperature can be adjusted to the required temperature, and processing at low temperatures is possible without impairing the quality of the raw material soy sauce.
このような製法によつて得られた低温粉末醤油
は、温水で戻すと直ちに溶解し、良好な溶解性を
示し、しかも味、香、色ともほぼ原料醤油と同等
のものであつた、。 The low-temperature powdered soy sauce obtained by such a manufacturing method immediately dissolved when reconstituted with hot water, exhibited good solubility, and was almost equivalent to the raw soy sauce in terms of taste, aroma, and color.
以上詳述したように本発明は乾燥工程の前に遠
心式薄膜真空濃縮装置を用いた濃縮工程を取入れ
たので、原料醤油の品質をほぼ全量維持しながら
濃縮が可能となり、添加剤のない濃縮醤油を容易
に乾燥し粉末化できるものである。 As detailed above, the present invention incorporates a concentration process using a centrifugal thin film vacuum concentrator before the drying process, making it possible to concentrate while maintaining almost all the quality of the raw soy sauce, and to concentrate without using additives. Soy sauce can be easily dried and powdered.
また、本発明は、乾燥工程の前に濃縮工程を設
けたのでランニングコストが低減でき、添加剤の
ない純粋な粉末醤油を安価に提供できるものであ
る。 Furthermore, since the present invention provides a concentration step before the drying step, running costs can be reduced, and pure powdered soy sauce without additives can be provided at low cost.
更にまた、本発明においては塩分含量を減少さ
せているので減塩粉末醤油として医療用に利用で
きる効果がある。 Furthermore, in the present invention, since the salt content is reduced, the soy sauce can be used for medical purposes as a low-salt powdered soy sauce.
第1図は本発明を実施する装置の一実施例を示
す説明図、第2図は本発明たる製造方法の一実施
例を示す説明図である。
1;原液供給タンク、A;遠心式薄膜真空濃縮
装置、B;真空乾燥機、41;過器。
FIG. 1 is an explanatory diagram showing an embodiment of an apparatus for implementing the present invention, and FIG. 2 is an explanatory diagram showing an embodiment of the manufacturing method of the present invention. 1: Stock solution supply tank, A: Centrifugal thin film vacuum concentrator, B: Vacuum dryer, 41: Filter.
Claims (1)
低温下で瞬時に濃縮し、析出した塩分を系外に除
去した後、濃縮液を真空乾燥装置において低温下
で乾燥することを特徴とする低塩粉末醤油の製造
方法。1. A low-salt powder characterized by instantaneously concentrating raw soy sauce at a low temperature in a centrifugal thin film vacuum concentrator, removing precipitated salts from the system, and then drying the concentrated liquid at a low temperature in a vacuum drying device. How to make soy sauce.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59088939A JPS60232074A (en) | 1984-05-02 | 1984-05-02 | Production of powdery soy |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59088939A JPS60232074A (en) | 1984-05-02 | 1984-05-02 | Production of powdery soy |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60232074A JPS60232074A (en) | 1985-11-18 |
JPH0573373B2 true JPH0573373B2 (en) | 1993-10-14 |
Family
ID=13956850
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59088939A Granted JPS60232074A (en) | 1984-05-02 | 1984-05-02 | Production of powdery soy |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60232074A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4603508B2 (en) * | 2006-05-29 | 2010-12-22 | ブレッシングフェバー株式会社 | Method for producing salty seasoning and salty seasoning |
US20100062140A1 (en) * | 2006-11-30 | 2010-03-11 | Misato Plaheat Mfg. Ltd. | Dry powder seasoning and manufacturing method and apparatus for the same |
US9808030B2 (en) | 2011-02-11 | 2017-11-07 | Grain Processing Corporation | Salt composition |
JP6674832B2 (en) * | 2016-04-18 | 2020-04-01 | キッコーマン株式会社 | Powdered soy sauce, seasoning composition, and method for producing powdered soy sauce |
-
1984
- 1984-05-02 JP JP59088939A patent/JPS60232074A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS60232074A (en) | 1985-11-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105152909B (en) | A kind of concentration, crystallization apparatus and technique for sodium gluconate production | |
RU2280990C2 (en) | Method and plant for evaporative concentration and crystallization of viscous lactose-containing aqueous liquid | |
JPH04272266A (en) | Method and device for continuous humidification of strip-like textile goods | |
US3892876A (en) | Process of preparing freeze-dried gelatin | |
CN106310704A (en) | Continuous single-effect vacuum evaporation crystallization system as well as application and technology | |
JPH0573373B2 (en) | ||
JP3380239B2 (en) | Method and apparatus for continuously producing hard candy material | |
CN208509983U (en) | Tea water-removing machine | |
KR100338837B1 (en) | Production of common salt from sea water | |
CN107751446A (en) | Saturated vapor formula tea water-removing machine | |
RU96122984A (en) | HIGH-CONCENTRATED, SOLID ACYCLIFUORFEN POWDERS AND METHODS FOR PRODUCING SOLID ACYFLUORFEN POWDERS IN DRY TYPE | |
JP3548963B2 (en) | Production of salt from seawater | |
CN101492747A (en) | Drying process of lactose production | |
US1478940A (en) | Process of preparing of dry and soluble extract of roasted coffee | |
US3257731A (en) | Process and equipment for the continuous lyophilization of liquid substances | |
US1596213A (en) | Method of drying and solidifying articles of food | |
US2326512A (en) | Desiccating apparatus | |
US2143256A (en) | Process for desiccating materials | |
RU2787188C1 (en) | Method for producing dry lactulose with crystal structure | |
JP3626717B2 (en) | Granulation drying system | |
US3882610A (en) | Freeze-drying process and apparatus | |
US765343A (en) | Process of evaporating liquids. | |
CN107047894A (en) | A kind of processing method of eucommia ulmoides male flower tea | |
HU177365B (en) | Process for continuous roasting basic cacaomass | |
KR920008078B1 (en) | Concentrating apparatus using underpressured vapor |