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JPH0732689B2 - Seasoning manufacturing method - Google Patents
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JPH0732689B2 - Seasoning manufacturing method - Google Patents

Seasoning manufacturing method

Info

Publication number
JPH0732689B2
JPH0732689B2 JP61126953A JP12695386A JPH0732689B2 JP H0732689 B2 JPH0732689 B2 JP H0732689B2 JP 61126953 A JP61126953 A JP 61126953A JP 12695386 A JP12695386 A JP 12695386A JP H0732689 B2 JPH0732689 B2 JP H0732689B2
Authority
JP
Japan
Prior art keywords
carbon dioxide
pressure
spices
dioxide gas
liquefied carbon
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 - Fee Related
Application number
JP61126953A
Other languages
Japanese (ja)
Other versions
JPS62282565A (en
Inventor
清仁 平出
幸雄 石黒
隆志 岡崎
康明 松原
正彦 吉田
麻理 鵜飼
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.)
Kagome Co Ltd
Original Assignee
Kagome Co Ltd
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 Kagome Co Ltd filed Critical Kagome Co Ltd
Priority to JP61126953A priority Critical patent/JPH0732689B2/en
Publication of JPS62282565A publication Critical patent/JPS62282565A/en
Publication of JPH0732689B2 publication Critical patent/JPH0732689B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Seasonings (AREA)

Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は調味料の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION <Field of Industrial Application> The present invention relates to a method for producing a seasoning.

家庭内での色々な料理に香辛料類が広く利用されてい
る。香辛料類は、それぞれ独特の香味を持ち、料理を引
き立てるのに重要である。
Spices are widely used in various dishes at home. Spices have their own unique flavors and are important for complementing food.

本発明は、香辛料類本来の香味を有し、家庭内で使用す
るに便利な調味料の製造方法に関するものである。
The present invention relates to a method for producing a seasoning which has the original flavor of spices and is convenient to use at home.

<従来の技術、その問題点> 従来、家庭内で使用する香辛料類には、生のままの物、
乾燥物、粉砕物、抽出液、抽出液を他の素材で被覆乃至
吸着した物等、種々の形態の物がある。
<Conventional technology and its problems> Conventional spices used at home include raw spices,
There are various forms such as a dried product, a pulverized product, an extract, and a product obtained by coating or adsorbing the extract with another material.

ところが、生のままの物は家庭内での保存や使用に実際
問題として不適当な場合が多く、乾燥物や粉砕物は流通
段階や家庭内での保存中にその本来の香味成分が酸化劣
化し、料理によってはこれら固形の香辛料類がその外観
や食感を損なってしまうという問題点がある。また、抽
出液やこれを他の素材で被覆乃至吸着した物は、概して
水蒸気蒸留や有機溶剤によるその抽出の際に本来の香味
が失われており、香味が余りにも強烈すぎて家庭では使
用し辛いという問題点がある。
However, raw materials are often unsuitable as a practical problem for storage and use at home, and dried and crushed products have their original flavor component oxidatively deteriorated during the distribution stage or during storage at home. However, depending on the dish, there is a problem that these solid spices impair the appearance and texture. In addition, the extract or the product obtained by coating or adsorbing it with other materials generally loses the original flavor during steam distillation or extraction with an organic solvent, and the flavor is too intense to use at home. There is a problem that it is painful.

<発明が解決しようとする問題点、その解決手段> 本発明は叙上の如き従来の問題点を解決する改良された
調味料の製造方法を提供するものである。
<Problems to be Solved by the Invention and Means for Solving the Problems> The present invention provides an improved method for producing a seasoning which solves the above-mentioned conventional problems.

ところで近年、抽出溶剤としての液化炭酸ガスが注目さ
れている。液化炭酸ガスは、有機成分に対する抽出効果
があり、低温操作ができるために抽出物へ悪影響を及ぼ
さず、抽出操作後におけるその完全除去が容易で、しか
も毒性がないために食品へ使用しても危険性がない等、
多くの利点を有するところから、そのままの状態で或は
超臨界状態で、食品関係の香味成分抽出にもその活用が
注目されている(特公昭45−8624号、特公昭48−44864
号、特公昭51−36344号、特開昭59−232064号、特開昭6
0−120957号)。
By the way, in recent years, liquefied carbon dioxide gas as an extraction solvent has attracted attention. Liquefied carbon dioxide has an extraction effect on organic components, does not adversely affect the extract because it can be operated at low temperature, can be easily completely removed after the extraction operation, and is not toxic even when used in foods. There is no danger, etc.
Because of its many advantages, its utilization is also attracting attention for the extraction of flavor components related to foods as they are or in a supercritical state (Japanese Examined Patent Publication Nos. 45-8624 and 48-44864).
JP-B-51-36344, JP-A-59-232064, JP-A-6
0-120957).

そこで本発明者らは、液化炭酸ガスによる抽出に着目し
て、香辛料類本来の香味を有する家庭内での使用に便利
な調味料を得るべく研究した結果、装置面及び操作面で
の制約が少ないそのままの状態での液化炭酸ガスを用い
る香辛料類を所定条件下で抽出し、その抽出液を乳化し
て、更に粘稠にすると、正しく合目的的な調味料が得ら
れることを見出した。
Therefore, the present inventors focused their attention on extraction with liquefied carbon dioxide gas, and as a result of research to obtain a seasoning that has the original flavor of spices and that is convenient for use in the home, the results show that there are restrictions in terms of equipment and operation. It has been found that when spices using liquefied carbon dioxide gas in a small amount as they are are extracted under predetermined conditions, and the extract is emulsified and made more viscous, a correct and purposeful seasoning can be obtained.

すなわち本発明は、下記の第1工程、第2工程及び第3
工程を経ることを特徴とする調味料の製造方法に係る。
That is, the present invention includes the following first step, second step and third step.
The present invention relates to a method for producing a seasoning, which is characterized by undergoing steps.

第1工程:耐圧容器に香辛料類及びドライアイスを装入
した後、該耐圧容器に液化炭酸ガスを送入して、5〜30
℃の温度及び40〜75kg/cm2の圧力下で抽出する工程 第2工程:耐圧容器から液化炭酸ガスを気化させて排気
した後、香辛料類の抽出残渣を取り出して、抽出液を得
る工程 第3工程:抽出液に水及び乳化剤を加えて乳化した後、
更に糊料を加えて粘稠にする工程 本発明の第1工程では、耐圧容器に香辛料類及びドライ
アイスを装入した後、該耐圧容器に液化炭酸ガスを送入
して、5〜30℃の温度及び40〜75kg/cm2の圧力下で抽出
する。通常、香辛料類は網容器に充填しておき、該網容
器と共に耐圧容器に装入する。またドライアイスは予め
耐圧容器に装入しておき、その上から上記の網容器を装
入する。本発明では、炭酸ガスを液化状態のままで使用
し、超臨界状態(過臨界状態)にはしない。炭酸ガスを
数百kg/cm2の高圧下で超臨界状態にすると、その抽出作
用が高まることは知られているが、このような超臨界状
態を実現しようとすると、装置が大型化し、また高価に
なり、その操作も厄介になる。本発明では、装置を小型
化し、また安価にして、その操作を簡単にするために、
液化炭酸ガスをそのまま使用する。しかし、単に液化炭
酸ガスを耐圧容器に送入すると、その内部で気化し易
く、気化した炭酸ガスそれ自体には抽出作用が殆どな
い。ドライアイスは、耐圧容器に送入した液化炭酸ガス
の温度を下げ、また該ドライアイスから気化した炭酸ガ
スが耐圧容器内の圧力を高めるので、かかる温度低下及
び圧力上昇の双方を活用して、耐圧容器へ送入した液化
炭酸ガスが気化してしまうのを防止するために用いる。
耐圧容器内の温度を5〜30℃に維持し、また圧力を40〜
75kg/cm2に維持すれば、該耐圧容器に送入した液化炭酸
ガスが気化してしまうのを防止できるので、ドライアイ
スはかかる温度及び圧力を維持するに足る量を耐圧容器
に装入しておけばよく、その量は、周囲の温度、耐圧容
器の内容積及びこれに送入する液化炭酸ガスの量等によ
っても影響されるが、通常、送入する液化炭酸ガスの15
重量%程度相当量とすれば充分である。
First step: After charging spices and dry ice into a pressure vessel, liquefied carbon dioxide gas is fed into the pressure vessel, and the pressure is increased to 5 to 30%.
Step of extracting at a temperature of ℃ and a pressure of 40 to 75 kg / cm 2 Step 2: Step of vaporizing liquefied carbon dioxide from the pressure vessel and exhausting it, and then removing the extraction residue of spices to obtain an extract Step 3: After adding water and an emulsifier to the extract to emulsify it,
In the first step of the present invention, the pressure-resistant container is charged with spices and dry ice, and then liquefied carbon dioxide gas is fed into the pressure-resistant container to make it 5 to 30 ° C. to the extraction under pressure of a temperature and 40~75kg / cm 2. Usually, the spices are filled in a mesh container, and the sponge is placed in a pressure container together with the mesh container. Further, dry ice is charged in a pressure resistant container in advance, and the above net container is charged from above. In the present invention, carbon dioxide gas is used in a liquefied state without being brought into a supercritical state (supercritical state). It is known that when carbon dioxide gas is brought into a supercritical state under a high pressure of several hundred kg / cm 2 , its extraction action is enhanced, but when trying to realize such a supercritical state, the device becomes large and It becomes expensive and difficult to operate. In the present invention, in order to make the device compact and inexpensive and to simplify its operation,
Liquefied carbon dioxide is used as it is. However, when liquefied carbon dioxide gas is simply fed into the pressure resistant container, it is easily vaporized inside, and the vaporized carbon dioxide gas itself has almost no extraction action. Dry ice lowers the temperature of the liquefied carbon dioxide gas fed into the pressure vessel, and since carbon dioxide gas vaporized from the dry ice increases the pressure in the pressure vessel, both the temperature decrease and the pressure increase are utilized, It is used to prevent the liquefied carbon dioxide gas sent into the pressure vessel from being vaporized.
Maintain the temperature in the pressure vessel at 5 ~ 30 ℃, and the pressure at 40 ~
If it is maintained at 75 kg / cm 2 , it is possible to prevent the liquefied carbon dioxide gas sent to the pressure vessel from being vaporized, so dry ice should be charged to the pressure vessel in an amount sufficient to maintain the temperature and pressure applied. The amount of liquefied carbon dioxide gas to be fed is usually 15 although it is affected by the ambient temperature, the internal volume of the pressure vessel and the amount of liquefied carbon dioxide gas fed into it.
It suffices if the amount is equivalent to about wt%.

本発明の第2工程では、耐圧容器から液化炭酸ガスを気
化させて排気した後、香辛料類の抽出残渣を取り出し
て、抽出液を得る。耐圧容器に取付けたバルブを開い
て、耐圧容器内の圧力を下げると、耐圧容器内の液化炭
酸ガスは気化し、自動的に耐圧容器外へ排気される。か
くして液化炭酸ガスを気化させて排気した後、耐圧容器
から通常は網容器と共に香辛料類の抽出残渣を取り出す
と、耐圧容器内には抽出液だけが残る。
In the second step of the present invention, after the liquefied carbon dioxide gas is vaporized from the pressure container and exhausted, the extraction residue of the spices is taken out to obtain an extraction liquid. When the pressure inside the pressure vessel is lowered by opening the valve attached to the pressure vessel, the liquefied carbon dioxide gas inside the pressure vessel is vaporized and automatically discharged outside the pressure vessel. Thus, after the liquefied carbon dioxide gas is vaporized and exhausted, when the extraction residue of the spices is taken out from the pressure resistant container together with the net container, only the extract remains in the pressure resistant container.

本発明の第3工程では、抽出液に水及び乳化剤を加えて
乳化した後、更に糊料を加えて粘稠にする。かくして、
所望通りの調味料を得る。
In the third step of the present invention, water and an emulsifier are added to the extract to emulsify it, and then a paste is further added to make it viscous. Thus,
Get the seasoning as desired.

第1図は本発明において抽出状態を略示する縦断面図で
ある。蓋体1の開閉可能な耐圧容器2の内部に網容器3
が装入されており、網容器3の内部には香辛料類Aが充
填されていて、網容器3よりも下方における耐圧容器2
の底部には図示しないドライアイスが装入されている。
蓋体1にはバルブ4,5を介してボンベ6が配管接続され
ており、ボンベ6の内部には液化炭酸ガスBが封入され
ている。蓋体1には圧力計7と、バルブ8を備える排出
管9とが取付けられており、耐圧容器2の底部にはバル
ブ10を備える取出管11が取付けられている。
FIG. 1 is a vertical sectional view schematically showing an extraction state in the present invention. A mesh container 3 is provided inside the pressure-resistant container 2 of the lid 1 which can be opened and closed.
Is charged, the spices A are filled in the inside of the mesh container 3, and the pressure-resistant container 2 below the mesh container 3 is filled.
Dry ice (not shown) is charged at the bottom of the.
A cylinder 6 is connected to the lid body 1 through valves 4 and 5, and a liquefied carbon dioxide gas B is sealed inside the cylinder 6. A pressure gauge 7 and a discharge pipe 9 having a valve 8 are attached to the lid body 1, and an ejection pipe 11 having a valve 10 is attached to the bottom of the pressure resistant container 2.

図示した状態で、バルブ4,5,8,10の操作により、ボンベ
6から液化炭酸ガスBを耐圧容器2内へ送入して、液化
炭酸ガスBと香辛料類Aとを接触させ、香辛料類Aの香
味成分を液化炭酸ガスBへ抽出する。抽出操作は、操作
温度との関係で圧力計7の指示値を確認しつつ、5〜30
℃の温度及び40〜75kg/cm2の圧力下で行なうが、液化炭
酸ガスBを耐圧容器2の内部へ送入する一方で排出管9
から気化した炭酸ガスを排出するという連続抽出でもよ
いし、又は一旦液化炭酸ガスBを耐圧容器2の内部へほ
ぼ満注して一定時間経過後に満注した液化炭酸ガスBの
全量を気化させて排出管9から排気するという操作を繰
り返すバッチ抽出でもよい。
In the illustrated state, the valves 4, 5, 8 and 10 are operated to feed the liquefied carbon dioxide B from the cylinder 6 into the pressure resistant container 2 to bring the liquefied carbon dioxide B and the spices A into contact with each other. The flavor component of A is extracted into liquefied carbon dioxide gas B. For the extraction operation, while checking the indicated value of the pressure gauge 7 in relation to the operation temperature,
It is carried out at a temperature of ℃ and a pressure of 40 to 75 kg / cm 2 , but the liquefied carbon dioxide gas B is fed into the pressure vessel 2 while the discharge pipe 9
Continuous extraction may be performed in which vaporized carbon dioxide gas is discharged from the tank, or once the liquefied carbon dioxide gas B is almost completely injected into the pressure vessel 2 and after a lapse of a certain time, the entire amount of the liquefied carbon dioxide gas B is vaporized. Batch extraction that repeats the operation of exhausting from the discharge pipe 9 may be used.

かくして炭酸ガスを排気後、蓋体1を開いて、香辛料類
Aの抽出残渣を網容器3と共に取り出すと、耐圧容器2
の底部に抽出液を得る。この抽出液に、充分に攪拌乃至
混練しつつ水及び乳化剤を加えて、乳化液とする。最後
に、上記乳化液に糊料を均一分散乃至溶解して全体を粘
稠にし、目的の調味料を得る。
Thus, after exhausting the carbon dioxide gas, the lid 1 is opened, and the extraction residue of the spices A is taken out together with the net container 3.
Obtain the extract at the bottom of the. Water and an emulsifier are added to this extract while being sufficiently stirred or kneaded to obtain an emulsion. Finally, the paste is uniformly dispersed or dissolved in the above emulsion to make the whole viscous, and the desired seasoning is obtained.

本発明において、香辛料類は単品でも又は混合品でもよ
く、その形態は生のままの物でもよいが、抽出効率の点
で乾燥粉砕物が好ましい。
In the present invention, the spices may be a single product or a mixed product, and the form thereof may be a raw product, but a dry pulverized product is preferable from the viewpoint of extraction efficiency.

また抽出は、その途中で耐圧容器に振動を加えたり、或
は耐圧容器を転倒させて行なうのが好ましい。排出管か
ら系外へ排気した炭酸ガスを回収して再使用に供するこ
とができることはいうまでもない。
Further, it is preferable to perform the extraction by applying vibration to the pressure-resistant container during the extraction or by inverting the pressure-resistant container. It goes without saying that the carbon dioxide gas exhausted from the exhaust pipe to the outside of the system can be recovered and reused.

更に抽出液を乳化液にするとき、攪拌や混合でもよい
が、できるだけ少量の水及び乳化剤を使用して、例えば
乳鉢と乳棒とで混練するのが好ましい。使用する乳化剤
は、シュガーエステル、グリセリン脂肪酸エステル、プ
ロピレングリコール脂肪酸エステル、ソルビタン脂肪酸
エステル、レシチン等、食品用のものであれば特に制限
はないが、合目的的にβ−サイクロデキストリンが最も
好適である。
Further, when the extract is made into an emulsion, it may be stirred or mixed, but it is preferable to use as little water and an emulsifier as possible, for example, kneading with a mortar and a pestle. The emulsifier used is not particularly limited as long as it is a food product such as sugar ester, glycerin fatty acid ester, propylene glycol fatty acid ester, sorbitan fatty acid ester and lecithin, but β-cyclodextrin is most suitable for purpose. .

そして乳化液に糊料を均一分散乃至溶解するとき、予め
糊料を水に均一化しておいたものを使用するのが好まし
い。使用する糊料は、天然物でも又は人工物でもよく、
トラガントガム、グアーガム、キサンタンガム等のガム
類、小麦粉や片栗粉等の澱粉類、ペクチン、カラギーナ
ン、CMC等、食品用のものであれば特に制限はない。香
辛料類の種類や製品用途との関係でも異なるが、通常、
全体を粘稠にした最終形態で、抽出液が50〜500倍程度
に希釈されたものとするのが好ましい。
When the paste is uniformly dispersed or dissolved in the emulsion, it is preferable to use the paste which has been homogenized in water beforehand. The glue used may be natural or artificial,
There is no particular limitation as long as it is for foods, such as gums such as tragacanth gum, guar gum and xanthan gum, starches such as wheat flour and starch starch, pectin, carrageenan, CMC and the like. Although it depends on the type of spice and the product application, it is usually
It is preferable that the extract is in a final form in which the whole is viscous, and the extract is diluted about 50 to 500 times.

液化炭酸ガスによる抽出液を乳化液とし、更に糊料で均
一な粘稠物とすることによって、香辛料類本来の香味成
分が活用された、適切濃度で該香味成分を含有する長期
間に亘って安定な、したがって家庭内で使用するに便利
な調味料を製造することができる。
By using the liquid extract of liquefied carbon dioxide as an emulsion and further making it a viscous material with a paste, the original flavor components of spices were utilized, and the flavor components were contained at appropriate concentrations over a long period of time. It is possible to produce seasonings that are stable and therefore convenient for domestic use.

<実施例> 第1図に略示した縦断面図にしたがい、前述したバッチ
抽出で、以下の条件下に抽出した。
<Example> According to the longitudinal sectional view schematically shown in FIG. 1, the batch extraction described above was performed under the following conditions.

香辛料類:粒度60〜120メッシュに調整した乾燥粉砕物
で、トウガラシ20g+ショウガ40g+クロコショウ20g+
ベイリーブス10g+タイム10gの混合品 耐圧容器:内容2のステンレス製耐圧容器 網容器:内容0.5で200メッシュのステンレス製網容器 液化炭酸ガス:各回で1.3kgを送入 ドライアイス:各回で0.2kgを装入 抽出:各回で30分間の抽出を合計15回行ない、各回で5
分毎に耐圧容器を転倒した かくして抽出した後、耐圧容器から抽出液を取出し、そ
の2gを自動乳鉢に採り、水0.5ml及びβ−サイクロデキ
ストリン1.6g(商品名セルデックスCH−30を使用、日本
食品化工社製、β−サイクロデキストリンを約20重量%
含有)を加えて、5分間混練し、乳化液とした。
Spices: Dry crushed product with particle size of 60-120 mesh, 20 g of capsicum + 40 g of ginger + 20 g of black pepper +
Mixture of Bay Reeves 10g + thyme 10g Pressure container: Stainless steel pressure container with content 2 Net container: 200 mesh stainless steel mesh container with content 0.5 Liquefied carbon dioxide gas: 1.3kg each time Dry ice: 0.2kg each time Charge Extraction: Extraction for 30 minutes is performed 15 times each time, 5 times each time.
After extracting by inverting the pressure vessel every minute, extract the extract from the pressure vessel, place 2 g of it in an automatic mortar, and add 0.5 ml of water and 1.6 g of β-cyclodextrin (trade name Celdex CH-30, About 20% by weight of β-cyclodextrin manufactured by Nippon Shokuhin Kako Co., Ltd.
Contained) and kneaded for 5 minutes to obtain an emulsion.

そして上記乳化液0.5gに、予め水100mlに小麦粉6gを徐
加して均一分散させたものを加熱し冷却した糊料を均一
混合し、全体を粘稠にした調味料を得た。
Then, to 0.5 g of the above emulsion, 6 g of flour was gradually added to 100 ml of water in advance and uniformly dispersed, and the paste which was heated and cooled was uniformly mixed to obtain a seasoning having an overall viscosity.

得られた調味料は、その香味及び外観ともに所望通りの
優れたものであり、密封後に加熱殺菌して冷却したもの
を6か月放置しても全く変化がなかった。
The seasoning thus obtained was excellent in both flavor and appearance as desired, and there was no change even when the product was heat-sterilized after being sealed and cooled, and allowed to stand for 6 months.

<発明の効果> 以上説明した通りであるから、本発明には、香辛料類本
来の香味を有し、料理の外観を損なうことがない、家庭
内で使用するに便利な調味料を製造することができると
いう効果がある。
<Effects of the Invention> As described above, according to the present invention, it is possible to produce a seasoning that has the original flavor of spices and that does not impair the appearance of dishes and that is convenient to use at home. There is an effect that can be.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明において抽出状態を略示する縦断面図で
ある。 1……蓋体、2……耐圧容器、3……網容器、 4,5,8,10……バルブ、6……ボンベ、 7……圧力計、9……排出管、11……取出管、 A……香辛料類、B……液化炭酸ガス
FIG. 1 is a vertical sectional view schematically showing an extraction state in the present invention. 1 ... Lid, 2 ... Pressure-resistant container, 3 ... Mesh container, 4,5,8,10 ... Valve, 6 ... Cylinder, 7 ... Pressure gauge, 9 ... Discharge pipe, 11 ... Ejection Tube, A ... Spices, B ... Liquefied carbon dioxide

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】下記の第1工程、第2工程及び第3工程を
経ることを特徴とする調味料の製造方法。 第1工程:耐圧容器に香辛料類及びドライアイスを装入
した後、該耐圧容器に液化炭酸ガスを送入して、5〜30
℃の温度及び40〜75kg/cm2の圧力下で抽出する工程 第2工程:耐圧容器から液化炭酸ガスを気化させて排気
した後、香辛料類の抽出残渣を取り出して、抽出液を得
る工程 第3工程:抽出液に水及び乳化剤を加えて乳化した後、
更に糊料を加えて粘稠にする工程
1. A method for producing a seasoning, which comprises the following first step, second step and third step. First step: After charging spices and dry ice into a pressure vessel, liquefied carbon dioxide gas is fed into the pressure vessel, and the pressure is increased to 5 to 30%.
Step of extracting at a temperature of ℃ and a pressure of 40 to 75 kg / cm 2 Step 2: Step of vaporizing liquefied carbon dioxide from the pressure vessel and exhausting it, and then removing the extraction residue of spices to obtain an extract Step 3: After adding water and an emulsifier to the extract to emulsify it,
The process of adding a paste to make it more viscous
【請求項2】乳化剤がβ−サイクロデキストリンである
特許請求の範囲第1項記載の調味料の製造方法。
2. The method for producing a seasoning according to claim 1, wherein the emulsifier is β-cyclodextrin.
JP61126953A 1986-05-30 1986-05-30 Seasoning manufacturing method Expired - Fee Related JPH0732689B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61126953A JPH0732689B2 (en) 1986-05-30 1986-05-30 Seasoning manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61126953A JPH0732689B2 (en) 1986-05-30 1986-05-30 Seasoning manufacturing method

Publications (2)

Publication Number Publication Date
JPS62282565A JPS62282565A (en) 1987-12-08
JPH0732689B2 true JPH0732689B2 (en) 1995-04-12

Family

ID=14947981

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61126953A Expired - Fee Related JPH0732689B2 (en) 1986-05-30 1986-05-30 Seasoning manufacturing method

Country Status (1)

Country Link
JP (1) JPH0732689B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0732687B2 (en) * 1988-05-09 1995-04-12 カゴメ株式会社 How to extract spicy ingredients from spicy spices

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5296774A (en) * 1976-02-09 1977-08-13 Teijin Ltd Oil in water type emulsified food
DE2931395A1 (en) * 1979-08-02 1981-02-26 Henkel Kgaa METHOD FOR PRODUCING SPICE EXTRACTS
JPS58869A (en) * 1981-06-26 1983-01-06 Lion Corp Powdery spice composition

Also Published As

Publication number Publication date
JPS62282565A (en) 1987-12-08

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