JPS59156247A - Equipment for making formulated fine coconut milk - Google Patents

Equipment for making formulated fine coconut milk

Info

Publication number
JPS59156247A
JPS59156247A JP58033175A JP3317583A JPS59156247A JP S59156247 A JPS59156247 A JP S59156247A JP 58033175 A JP58033175 A JP 58033175A JP 3317583 A JP3317583 A JP 3317583A JP S59156247 A JPS59156247 A JP S59156247A
Authority
JP
Japan
Prior art keywords
tank
milk
coconut milk
crude
mixing
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
JP58033175A
Other languages
Japanese (ja)
Other versions
JPS6036742B2 (en
Inventor
Akemasa Miyake
三宅 明正
Yasutoku Yasuda
安田 泰徳
Atsushi Yanaka
惇 谷中
Katsutoshi Tsuboi
坪井 勝利
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP58033175A priority Critical patent/JPS6036742B2/en
Publication of JPS59156247A publication Critical patent/JPS59156247A/en
Publication of JPS6036742B2 publication Critical patent/JPS6036742B2/en
Expired legal-status Critical Current

Links

Abstract

PURPOSE:The titled equipment in which the nonvolatile components in crude coconut milk are dispersed into very fine particles and auxiliary additives such as stabilizers or flavors are added to effect sterilization, deodorization and stabilization, thus giving a formulated coconut milk suitable for high-class beverage. CONSTITUTION:Frozen crude coconut milk is thawed in the thawer 1 and sent from the tank 3 to the receive tank equipped with a mixing mechanism and diluted with hot water at 60-70 deg.C from the tank 7. The resultant milk is passed through static mixer 11, homogenizer 13 to the deaerator 15 where gases, air and volatile substances are removed. Stabilizers and flavors are combined in the mixing tank 19 together with auxiliary agents mixed with water. The formulated emulsion is sent into the steril-deodorizer 43 where it is heated by means of boiler 25 at 130-140 deg.C. The volatile odors are removed in the vacuum deaerator 44. The resultant emulsion is sent through homogenizer 45, cooled in heat exchanger 47, then transferred into the germfree tank 48 and sent to the filling machine 48.

Description

【発明の詳細な説明】 この発明は、調整ファインココナツミルクの製造゛装置
に関するものであり、特に内方において原産されるココ
ナツから得られた粗ココナンミルクを源科として高級飲
料用として部品価値の高い調整ファインココナツミルク
を工業的m俣で製造できる装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for producing adjusted fine coconut milk, and in particular, it uses coarse coconut milk obtained from coconuts originating in India as a source material to produce fine coconut milk with component value for high-grade beverages. The present invention relates to an apparatus capable of producing fine coconut milk with a high concentration on an industrial scale.

ココナツの口実を細砕圧さくすることによって得られた
絞り汁を冷凍したものは「狙ココナツミルク」として知
られており、調整ミルクの原料として、種々秀れた特性
をそなえているにも拘らず、高級飲料分野におけるオリ
用はほとんどされていないのが現状である。これにはい
ろいろなノ京因かあるがその内大きなものとしては、製
造工程中に粒度の大きい沈殿が生じて所謂ミジン現象が
発生したり油分が分離するために均一な乳濁孜を得るこ
とができないこと、および租ココナツミルク製造工程中
空気との接触によってできた酸化物等の不純物による揮
発性不快臭気を除(ことが困難なため、高級飲料に不適
であること等が挙げられる。
The frozen juice obtained by crushing and compressing coconut is known as ``target coconut milk,'' and although it has various excellent properties as a raw material for modified milk. At present, it is hardly used in the high-end beverage field. There are various reasons for this, but the major ones are the formation of large-grained precipitates during the manufacturing process, which causes the so-called mijin phenomenon, and the separation of oil to obtain a uniform emulsion. It is difficult to remove volatile unpleasant odors caused by impurities such as oxides produced by contact with air during the production process of coconut milk, making it unsuitable for high-end beverages.

この発明は粗ココナツミルクの本来発生する原料特性を
充分に活しながらも、かつ、上記した様な工程上の諸問
題を除いて、高級飲料に適した調整ココナツミルクを製
造することのできる装置を提供することを目的とするも
のである。
This invention is an apparatus that can produce adjusted coconut milk suitable for high-grade beverages while fully utilizing the raw material properties of crude coconut milk and eliminating the process problems described above. The purpose is to provide the following.

即ちこの発明にあろては、租ココナツミルク中の不揮発
成分を微細粒子状に分散させるとともに、安定剤や調味
料などの助剤を添加し、更に殺閑、脱臭左よぴ安定化を
図るものである。
That is, in this invention, the non-volatile components in the coconut milk are dispersed in the form of fine particles, and auxiliary agents such as stabilizers and seasonings are added to further stabilize the milk by killing it, deodorizing it, and so on. It is.

以下冷付の図面に基いて更に詳細にこの発明の調整ファ
インココナツミルクの製造装置について説明する。
The apparatus for producing adjusted fine coconut milk of the present invention will be described in more detail below with reference to the cooling drawings.

前記したように、この発明はココナツの口実をa(?f
=圧さくしてカスと分離することにより得られた絞り汁
を冷凍した「粗ココナツミ・ルク」を累材とするもので
ある。したがってまず、この冷凍粗ココナツミルクを解
凍する必要かある。そこで、これをまず解凍器(又は冷
蔵庫)1へ送り込んでやる。そして解凍が済むと解凍器
とパイプで接続されている貯蔵タンク3へ送り込む。こ
の貯蔵タンク6は更にポンプP1を升してミキシング1
幾構つきのレシーブタンク5にパイプ接続されている。
As mentioned above, this invention makes coconut pretext a(?f
= Crude coconut milk is made by freezing the squeezed juice obtained by crushing and separating it from the dregs. Therefore, first of all, it is necessary to thaw this frozen crude coconut milk. Therefore, first send this to the defroster (or refrigerator) 1. Once thawed, it is sent to a storage tank 3 connected to the thawing machine through a pipe. This storage tank 6 is further equipped with a pump P1 for mixing 1.
It is connected to a receiving tank 5 with several pipes.

したがって、貯蔵タンク乙に収容された解凍された祖コ
コナツミ5ルクはポンプP1によりレシーブタンク5に
移送される。そして、このレシーブタンク5に温湯を供
給して租ココナツミルク・を希釈化する必要があるが、
この温湯(60〜b貯蔵タンク7からポンプP2を介し
てパイプ給送される。レシーブタンク5の下流側は更に
ポンプP6を介してスタティックミキサー11とパイプ
接続されている。このスタティックミキサー11にて、
上記温湯で希釈化された粗ココナツミルクを充分に攪拌
する。スタティックミキサー11はその下流側で例えば
200〜50.0 kg /cm2程度の 。
Accordingly, the thawed coconut milk 5 stored in the storage tank B is transferred to the receiving tank 5 by the pump P1. Then, it is necessary to supply hot water to this receiving tank 5 to dilute the coconut milk.
This hot water (60~b) is pipe-fed from the storage tank 7 via a pump P2. The downstream side of the receiving tank 5 is further connected via a pipe to a static mixer 11 via a pump P6. ,
Thoroughly stir the crude coconut milk diluted with the warm water. The static mixer 11 has, for example, about 200 to 50.0 kg/cm2 on its downstream side.

高圧で均質化処理して瓶細粒化するホモゲナイザ−13
にパイプ接続されている。そして、ホモゲナイザ−13
はポンプP4を介して脱気槽15にパイプ接続されてい
る。ホモゲナイザ−13によって均質化処理されて乳濁
液となったココナツミルクは、脱気′)lVJ15vC
強制移送されるが、この脱気槽15には、真空ポンプ等
の減圧・脱気装置17が接続されており、乳濁液を減圧
脱気処理し、ガス、空気及び揮発性物質を除去する。脱
気槽15の下流側は、ポンプP5を介してミキシングタ
ンク19にパイプ接続されている。このミキシングタン
ク19は、上記減圧脱気処理された乳濁液と安定剤や調
味料を適温の水と混和した助剤とを混合するものである
。ところで、この助剤をミキシングタンク19に給送す
る機構としては次の通りである。即ち、ミキシングタン
ク21には例えばバクガ糖を、ミキシングタンク23に
は例えば脱脂粉乳を入れ、これら両ミキシングタンク2
3には、ボイラー25の熱で昇温させられた蓄湯槽27
内の温湯を給送せしめる様にパイプ接続されている。
Homogenizer 13 that homogenizes at high pressure to make the bottle fine particles
is connected to the pipe. And homogenizer-13
is pipe-connected to the deaeration tank 15 via a pump P4. The coconut milk that has been homogenized into an emulsion by the homogenizer 13 is deaerated')lVJ15vC
This deaeration tank 15 is connected to a depressurization/deaeration device 17 such as a vacuum pump, and the emulsion is degassed under reduced pressure to remove gas, air, and volatile substances. . The downstream side of the deaeration tank 15 is pipe-connected to a mixing tank 19 via a pump P5. This mixing tank 19 is for mixing the emulsion which has been subjected to the vacuum degassing treatment and an auxiliary agent made by mixing stabilizers and seasonings with water at an appropriate temperature. By the way, the mechanism for feeding this auxiliary agent to the mixing tank 19 is as follows. That is, the mixing tank 21 is filled with, for example, Bakuga sugar, and the mixing tank 23 is filled with, for example, skim milk powder.
3, a hot water storage tank 27 heated by the heat of the boiler 25;
Pipes are connected to supply hot water inside.

両ミキシングタンク2’1.23で夫々バクガ糖、脱脂
粉乳を温湯で混合する。そして、両ミキシングタンク2
1.23の下流側にパイプ接続されているホモゲナイザ
−29にバクガ穂液、脱脂粉乳液を送り込み、両液を混
合均質化させた調合液をつくる。このホモゲナイザ−2
9の下流側には上記調合液を一担収容するレジ2プタン
ク31が接続されており、更にその下流側はポンプP6
を介して前記ミキシングタンク19に接続されている。
Mix Bakuga sugar and skim milk powder with warm water in both mixing tanks 2'1.23. And both mixing tanks 2
1. Pipe-connected to the homogenizer 29 on the downstream side of the machine 23, feed the cornflower liquid and skimmed milk powder, and mix and homogenize the two liquids to create a blended liquid. This homogenizer-2
A register tank 31 for storing the above-mentioned mixed liquid is connected to the downstream side of the pump P6, and a pump P6 is connected to the downstream side thereof.
It is connected to the mixing tank 19 via.

このミキシングタンク19には、前記した様に均質化処
理された乳濁液が送り込まれているので、このミキシン
グタ/り19で乳濁液と助剤たる均質化処理された調合
液とを混合させる。ここで調合61み乳濁液はミキシン
グタンク19の下流にパイプ接続されている殺菌脱臭機
43へと送り込まれる。この56.菌脱臭磯43は前記
ボイラー25か接続されており、このボイラー25によ
って殺菌脱臭機46内の調合済み乳濁液を例えば160
〜140”Cの所属の温度で加熱殺閑する。この加熱収
繭処理の際揮発性の臭気がでるが、この臭気を除去する
ために、殺菌脱臭機46に減圧脱気装置44を伺設して
おいてやる。
Since the emulsion that has been homogenized as described above is sent to this mixing tank 19, the emulsion is mixed with the homogenized blended liquid as an auxiliary agent in this mixing tank 19. let Here, the emulsion prepared 61 is sent to a sterilizing and deodorizing machine 43 which is pipe-connected downstream of the mixing tank 19. This 56. The bacteria deodorizing iso 43 is connected to the boiler 25, and the prepared emulsion in the sterilizing and deodorizing machine 46 is, for example, 160
Heat and sterilize at a temperature of ~140"C. Volatile odor is emitted during this heating and cocoon treatment, but in order to remove this odor, a vacuum deaerator 44 is installed in the sterilizer and deodorizer 46. I'll leave it to you.

殺菌脱臭機46で枚重脱臭された調合済み乳濁液は、更
にその下流1則にパイプ接続されているホモゲナイザ−
45に送り込まれ、調合済み乳濁液を均質化処理する。
The prepared emulsion that has been heavily deodorized by the sterilizing and deodorizing machine 46 is further passed through a homogenizer that is connected to a pipe downstream of the emulsion.
45 to homogenize the prepared emulsion.

ホモゲナイザ−45の下流側には熱交換?547がパイ
プ接続されており、ここで、加熱された調合液が混入さ
れて、温度が上昇した乳濁液を冷却させる。黙交侠器4
7の下流側には、無菌貯蔵タンク48がパイプ接続され
ており、冷却された乳濁液たるココナツミルク液を焦眉
状態で貯留する。この貯蔵タンク48は更に充填機49
へとパイプ接続されており、この充*槻49でココナツ
ミルク液はテトラパックやびん等に詰められて出荷され
るのである。
Is there a heat exchanger downstream of the homogenizer 45? 547 is piped into which the heated formulation is mixed to cool the emulsion which has risen in temperature. Mokukyokai 4
A sterile storage tank 48 is pipe-connected to the downstream side of the tank 7, and stores the cooled coconut milk liquid as an emulsion in a hot state. This storage tank 48 is further equipped with a filling machine 49.
The coconut milk liquid is packed into tetra packs, bottles, etc. and shipped via this pipe.

この様にこの発明によれば、イ且ココナツミルクを原料
として、高級飲料用として部品価値の高いファインココ
ナンミルクを工業力規模で生産することかnJ能と7よ
った。
As described above, according to the present invention, it is possible to produce, on an industrial scale, fine coconan milk, which has a high component value and is used for high-grade beverages, using coconut milk as a raw material.

【図面の簡単な説明】[Brief explanation of the drawing]

添付の図面はこの発明の調整ファインココナツミルクの
製造表置を模式的に示した説明図である。 1・・・解凍器       3・・・貯蔵タンク5・
・・レシーブタンク  7・・・貯蔵タンク11・・ス
タティックミキサー 13.29.45・・・ホモゲツーイザー15・・・脱
気槽      17・・・減圧脱気装置19.21.
23・・・ミキシングタンク25・・・ボイラー   
  27・・・蓄湯遭61・・レシーブタンク   4
6川殺菌説臭磯47・・・熱交換磯     48・・
・無菌貯蔵タンク49・・・充填機 特許出願人  安  1) 泰  徳 特許出願代理人 弁理士 ′R原一部
The accompanying drawings are explanatory drawings schematically showing the production layout of the adjusted fine coconut milk of the present invention. 1... Thaw device 3... Storage tank 5.
...Receive tank 7...Storage tank 11...Static mixer 13.29.45...Homogetsuizer 15...Degassing tank 17...Reducing pressure deaerator 19.21.
23...Mixing tank 25...Boiler
27... Hot water storage accident 61... Receive tank 4
6 River Sterilization Theory Odor Rock 47...Heat Exchange Rock 48...
・Sterile storage tank 49...Filling machine patent applicant Yasun 1) Yasunori Patent application agent Patent attorney 'R Harabetsu

Claims (1)

【特許請求の範囲】 冷凍化ココナツを解凍する解凍器(1)と、該解凍され
た粗ココナツミルを貯蔵する貯蔵タンク(3)と該ココ
ナツミルクを温湯と混合希釈化して収容するレシーブタ
ンク(5)と上記希釈化された粗ミルク液を攪拌するス
タティックミキサー(11)と該攪拌済み粗ミルク液を
均質化処理する第1のホモグナイザ−(16)と均質化
処理された租ミルク液中のガス分を除去する脱気槽(1
5)とガス分が除去されたミルク液を助剤と混合するミ
キシングタンク(19)と、調合済ミルク液を一担貯留
するストレージタンク(41)と調合済ミルク液を殺菌
し、且つ臭気を除去する殺菌脱臭機(46)と、殺菌脱
臭街調合ミルク液を均質化処理ずる第2のホモナイザー
(45)と、均質化処理された調合ミルク液を冷却させ
る冷却器(47)と、冷却された均質化調合ミルク液を
収容する無菌タンク(48)と該ミルク液を所定の容器
(《充填する充填機(49)とからなり、且つこれらは
上記記載の順序にバイブ接続されており、 上記レシーブタンク(5)には更に貯湯タンク(7)K
バイブ接続されており、 前記脱気槽(15)には減圧脱気装置(17)が接続さ
れており、 前記ミキシングタンク(19)には更に均質化処理され
た助剤が収容されているレシーブタンク(31)が接続
されており、 更に上記部材記載の順序に梢製過程中の粗ココナツミル
ク液を移送させるためのポンプCP)からなる ことを特徴とする調整ファインココナンミルクの製造装
置。
[Scope of Claims] A thawing device (1) for thawing frozen coconut, a storage tank (3) for storing the thawed crude coconut mill, and a receiving tank (3) for storing the coconut milk diluted by mixing it with warm water. 5), a static mixer (11) for stirring the diluted crude milk liquid, a first homogenizer (16) for homogenizing the agitated crude milk liquid, and a first homogenizer (16) for homogenizing the agitated crude milk liquid; Deaeration tank (1
5), a mixing tank (19) for mixing the milk liquid from which gas has been removed with an auxiliary agent, a storage tank (41) for storing the mixed milk liquid, and a storage tank (41) for sterilizing the mixed milk liquid and eliminating odors. A sterilizing and deodorizing machine (46) for removing sterilized and deodorized milk, a second homogenizer (45) for homogenizing the sterilized and deodorized mixed milk, and a cooler (47) for cooling the homogenized mixed milk. It consists of a sterile tank (48) that accommodates the homogenized milk solution, and a filling machine (49) that fills the milk solution into a predetermined container, and these are connected to the vibrator in the order described above. The receiving tank (5) also has a hot water storage tank (7) K.
A vibrator is connected to the degassing tank (15), a vacuum degassing device (17) is connected to the degassing tank (15), and the mixing tank (19) further includes a receiver containing a homogenized auxiliary agent. An apparatus for producing adjusted fine coconan milk, which is connected to a tank (31) and further comprises a pump (CP) for transferring the crude coconut milk liquid during the coconut milk production process in the order described above.
JP58033175A 1983-02-28 1983-02-28 Adjusted fine coconut milk production equipment Expired JPS6036742B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58033175A JPS6036742B2 (en) 1983-02-28 1983-02-28 Adjusted fine coconut milk production equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58033175A JPS6036742B2 (en) 1983-02-28 1983-02-28 Adjusted fine coconut milk production equipment

Publications (2)

Publication Number Publication Date
JPS59156247A true JPS59156247A (en) 1984-09-05
JPS6036742B2 JPS6036742B2 (en) 1985-08-22

Family

ID=12379178

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58033175A Expired JPS6036742B2 (en) 1983-02-28 1983-02-28 Adjusted fine coconut milk production equipment

Country Status (1)

Country Link
JP (1) JPS6036742B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008057762A1 (en) * 2006-11-01 2008-05-15 Pepsico, Inc. Beverage manufacture using a static mixer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008057762A1 (en) * 2006-11-01 2008-05-15 Pepsico, Inc. Beverage manufacture using a static mixer

Also Published As

Publication number Publication date
JPS6036742B2 (en) 1985-08-22

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