JPS58162242A - Preparation of raw bean jam - Google Patents

Preparation of raw bean jam

Info

Publication number
JPS58162242A
JPS58162242A JP57041765A JP4176582A JPS58162242A JP S58162242 A JPS58162242 A JP S58162242A JP 57041765 A JP57041765 A JP 57041765A JP 4176582 A JP4176582 A JP 4176582A JP S58162242 A JPS58162242 A JP S58162242A
Authority
JP
Japan
Prior art keywords
water
bean jam
machine
bean
bean paste
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
JP57041765A
Other languages
Japanese (ja)
Other versions
JPS5940419B2 (en
Inventor
Hiroshi Nishimoto
洋 西本
Hitoshi Takei
武井 仁
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.)
Sanyu Co Ltd
Original Assignee
Sanyu 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 Sanyu Co Ltd filed Critical Sanyu Co Ltd
Priority to JP57041765A priority Critical patent/JPS5940419B2/en
Publication of JPS58162242A publication Critical patent/JPS58162242A/en
Publication of JPS5940419B2 publication Critical patent/JPS5940419B2/en
Expired legal-status Critical Current

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  • Confectionery (AREA)

Abstract

PURPOSE:To reduce the amount of water to be used for water treatment and to improve operation efficiency, by removing high-temperature water contained in bean jam material from the bean jam material prepared by a machine for preparing bean jam, separating it into bean jam juice and residuary substances of bean skin, subjecting the bean jam juice to water treatment and drying in the sun. CONSTITUTION:A bean jam material prepared by the machine 2 for preparing bean jam is sent to the water extracting machine 8 so that high-temperature water contained in it is removed. In the operation, a small amount of water is dropped from the shower 10 so that the clogging of the wire netting 9 is prevented. The bean jam material from which water is removed is introduced into the machine 3 for separating and screening residuary substances of bean skin, treated with water from the shower 12, bean jam juice is eluted to the outside of the wire netting 11, the residuary substances are left inside it and discharged. The separated bean jam juice is cooled and washed with water from a great number of the equipped nozzles 13, introduced into the water treatment machine 6 of the screening machine type, impurities attached to the surfaces of soybean jam particles are further washed and released while being treated with water of the shower 14 and rotated, it is purified into high-quality bean jam particles, stored by the storage tank 15 and dehydrated by a dehydrator to give a product.

Description

【発明の詳細な説明】 従来より知られる一般的な生能の製造工程は、第1図に
示す如く豆煮釜(1)にて煮上げた煮熟豆を製餡機(2
)において摺潰して餡材料とし、この餡材料をまづ分離
篩別機(3))に送って灰滓と結社とに分離し、しかる
のち結社を加水沈澱槽(タ)に貯留して水晒し処理を行
い、厳終的に沈澱した餡粒子を上澄液を除去して脱水機
(j)により脱水することにより最終的な製品とする。
DETAILED DESCRIPTION OF THE INVENTION As shown in FIG. 1, the conventionally known general production process for raw beans is to boil boiled beans in a bean boiler (1) and then transfer them to a bean paste making machine (2).
), the bean paste material is first sent to a separator and sieve (3) to separate it into ash and aggregates, and then the aggregates are stored in a water-adding sedimentation tank (ta) to remove water. After the bleaching process, the final product is obtained by removing the supernatant liquid from the precipitated bean paste particles and dehydrating them in a dehydrator (j).

ところでとの生略製造法においては、分離篩別機((9
)によって灰滓と分離した結社から餡粒子を分離する工
程が、結社を沈澱槽(4’)内に貯留し、該槽内に連続
的に水を注入することによって餡粒子を沈降させるもの
であるため、餡粒子が上澄液と共に流出することが多く
、また餡粒子の自然沈降を待つために作業能率が悪いと
いう問題、更には水晒し処理として沈澱槽内に注入され
る水の使用量も多大となるという問題を有していた。
By the way, in the raw production method mentioned above, a separating sieve machine ((9
) The step of separating the bean paste particles from the ash that has been separated from the ash involves storing the coagulation in a sedimentation tank (4') and settling the bean paste particles by continuously injecting water into the tank. As a result, the bean paste particles often flow out together with the supernatant liquid, and there is also the problem of poor work efficiency as the bean paste particles wait for natural settling.Furthermore, the amount of water used in the settling tank for water exposure treatment is reduced. There was also a problem in that the amount of energy required was also large.

このため最近では、第一図に示す如く分離篩別機(3)
によって灰滓から分離された結社を水晒し処理する工程
として、結社を上方からシャワー水が加えられ乍ら回転
する筒型の晒し装N(6)内に通過させ、更に該晒し装
置(6)を通った結社を内側に晒し用水流ノズルを備え
た橋形の流路(7)内に水と共に流動させることにより
、結社から餡粒子を分離させる水晒し処理を連続的に行
い、作業能率を向上させるようにした方法が提唱された
(実公昭36−3乙305号)。
For this reason, recently, a separating sieve machine (3) is used as shown in Figure 1.
As a process of bleaching the collage separated from the ash dregs with water, the collage is passed through a rotating cylindrical bleaching device N (6) to which shower water is added from above, and then further exposed to the bleaching device (6). By making the passed-through flow together with water in a bridge-shaped flow channel (7) equipped with a water flow nozzle for bleaching inside, a water-bleaching process that separates the bean paste particles from the knots is performed continuously, improving work efficiency. A method was proposed to improve the quality of water (Utokoko No. 305, No. 305, 36-3).

しかし乍らこの方法においては、灰滓と分離された餡粒
子の水晒し処理が連続的に行えるため生産卵率を向上し
得るという利点を有するもの\、この水晒し処理を連続
的に行うということは、究局的に結社に常時水流を加え
て橋形流路内を水と共に流動させる過程において餡粒子
を分離するという晒し作用を与えるため、水晒し処理に
要する水の使用量は第1図に示す従来法と同様に依然と
して多く、使用水の節減を図るという面から見えば未だ
解決されるべき問題点を含んでいると言える。
However, this method has the advantage that the egg production rate can be improved because the bean paste particles separated from the ash can be continuously exposed to water. This is because, in the end, the process of constantly applying a water flow to the knot and allowing it to flow together with the water in the bridge-shaped channel provides a bleaching effect that separates the bean paste particles, so the amount of water required for the water bleaching process is As with the conventional method shown in the figure, there are still many problems, and from the perspective of reducing water usage, it can be said that there are still problems that need to be solved.

本発明は、これらの従来法における水晒し処理に使用さ
れる水の使用量を大幅に節減し、併せて作業能率の向上
を期待し得る生詰製造法の提供を目的としたものである
The present invention aims to provide a fresh packing manufacturing method that can significantly reduce the amount of water used in the water bleaching treatment in these conventional methods and can also be expected to improve work efficiency.

本発明者らは従来の生詰製造法における結社の水晒し処
理が大量の水を使用することになる原因を検討した結果
、従来の製造法における斯る原因が第7図及び第2図に
示す製餡機(−)より得られた餡材料を次の工程として
分離篩別機(3)によって灰滓と結社とに篩別処理する
ことに基因しているという結論を得た。即ち従来の製法
のように製餡機(2)から得られた餡材料を次の処理と
してまず分離篩別機(3)によって灰滓と結社とに分離
すると、分離篩別機(3)に送られた餡材料は@餡機(
2)から出た直後で高温の水分を多分に含んでいるため
に、この高温水分が分離篩別機(3)から結社と共にそ
のまま多量に流出して、抽出された結社と一体となって
次の工程としての晒し処理に移送されること\なる。勿
論制汗と共に流出した前記の水分は高い温度を有し、そ
の量も多くかつ汚れている。しかし乍らこの段階でこの
余分な水分のみを結社中の必要とされる餡粒子と分離さ
せることはできないので、以後の水晒しの過程において
前記水分の冷却と、餡粒子から汚れを除去しなければな
らず、そのために例えば第2図の製法のように筒型の晒
し装置(6)を複数段配置すると共に、流路(7)を長
く設定して冷却に要する時間と洗浄に要する時間とを多
くしなければならず、当然のこと乍ら晒し用水の使用量
が増大する結果となる。
The inventors of the present invention investigated the causes of the use of a large amount of water in the water-bleaching treatment of the knots in the conventional raw production method, and found that such causes in the conventional production method are shown in Figures 7 and 2. It was concluded that this is due to the fact that the bean paste material obtained from the bean paste making machine (-) shown in the figure is sieved into ash dregs and ash in the next step using a separation sieve machine (3). That is, as in the conventional manufacturing method, the bean paste material obtained from the bean paste making machine (2) is first separated into ash and cake by the separator and sieve machine (3) as the next process. The sent bean paste materials are sent to the @anko machine (
Since it contains a large amount of high-temperature moisture immediately after exiting from 2), a large amount of this high-temperature moisture flows out from the separating sieve machine (3) along with the aggregates, and together with the extracted aggregates, it is passed on to the next product. It will be transferred to the bleaching process as a process. Of course, the water that flows out with the antiperspirant has a high temperature, is large in amount, and is dirty. However, at this stage, it is not possible to separate this excess moisture from the required bean paste particles in the dough, so in the subsequent water-bleaching process, the moisture must be cooled and dirt must be removed from the bean paste particles. Therefore, for example, as in the manufacturing method shown in Fig. 2, cylindrical bleaching devices (6) are arranged in multiple stages, and the flow path (7) is set long to reduce the time required for cooling and cleaning. This naturally results in an increase in the amount of bleaching water used.

本発明に係る生詰製造法においては、結社から餡粒子を
分離するための水晒し処理が能率的に行えるようにする
ため、製餡機から得られた餡材料から分離篩別機によっ
て灰滓と結社とを分離する前の工程において、まず該餡
材料中に含まれる大量の高温水分の大半を除去排出せし
め、しかるのちこの不要水分の除去された状態の餡材料
を分離篩別機に送って灰滓と純度の高い結社とに分離す
ることにより、結社の冷却作用と結社からの餡粒子の分
離作用とが比較的少量の晒し用水によって行えるように
したことを特徴とするものである。
In the raw filling manufacturing method according to the present invention, in order to efficiently carry out the water bleaching treatment to separate the bean paste particles from the aggregate, the bean paste material obtained from the bean paste making machine is separated by a separating sieve machine. In the process before separating the paste from the paste, first, most of the large amount of high-temperature water contained in the paste material is removed and discharged, and then the paste material from which unnecessary water has been removed is sent to a separation sieve machine. By separating the ash dregs and high-purity coagulation, the cooling effect of the coagulation and the separation of bean paste particles from the coagulation can be performed using a relatively small amount of bleaching water.

次に本発明に係る生詰製造法を第3図以下に示す実施例
に基いて詳記すれば、第3図において製餡機(2)によ
って得られた餡材料をまず水分抽出機(,1’)に供給
し、該水分抽出機(、r)によって製餡機(コ)から出
た直後の高温状態の餡材料中に含まれる高温水分を除去
する。この水分抽出機(r)としては、例えばメツシュ
の小さい金網(り)によって形成された筒形の回転篩別
機の如きものであればよい。また篩別機型以外のものと
しては例えば遠心分離器型のものであってもよい。第3
図の回転篩分機型の水分抽出機(Ir)内に導入された
餡材料は製餡機(2)内において加工される段階で水分
と豆との比率が約3=1程度の割合であるため、抽出機
(rlが低速で回転されると大半の高温水分が金網(q
)を通して排出される。その際金網(9)の目詰りを防
止するため、抽出機(Ir)の上部に設けたシャワー型
注水器(/のから小量の水を降水させる。抽出1−m 
(J−)は傾斜角を有しているために内部の餡材料は水
分が抽出された状態で下方に流動し、灰滓分離篩別機(
3)内に導入される。この篩別機(3)は従来の製法に
用いられるものと同様にメツシュの粗い金網(//)?
有した回転する筒状体からなり、上部にシャワー型注水
器(12)が設けられている。前記餡材料は該分離篩別
機(3)内においてシャワー水を受けることにより、鮎
汁が金網(ll)外に溶出して灰滓は内部に残留する。
Next, the raw filling manufacturing method according to the present invention will be described in detail based on the examples shown in Figure 3 and below. In Figure 3, the bean paste material obtained by the bean paste making machine (2) is first 1'), and the high-temperature water contained in the bean paste material in a high temperature state immediately after coming out of the bean paste making machine (k) is removed by the water extractor (r). The water extractor (r) may be a cylindrical rotary sieve formed of a small wire mesh, for example. In addition to the sieving machine type, for example, a centrifugal separator type may be used. Third
The bean paste material introduced into the rotary sieve-type moisture extraction machine (Ir) shown in the figure has a ratio of water to beans of about 3 = 1 when it is processed in the bean paste making machine (2). Therefore, when the extractor (rl) is rotated at low speed, most of the high temperature moisture is transferred to the wire mesh (q
) is discharged through. At that time, in order to prevent clogging of the wire mesh (9), a small amount of water is rained down from the shower type water pourer (/) installed at the top of the extractor (Ir).Extraction 1-m
(J-) has an inclination angle, so the filling material inside flows downward with moisture extracted, and the ash slag separation sieve machine (
3) be introduced within. This sieving machine (3) has a coarse wire mesh (//) similar to those used in conventional manufacturing methods.
It consists of a rotating cylindrical body with a shower type water injector (12) installed at the top. When the bean paste material receives shower water in the separator (3), the sweetfish juice is eluted out of the wire gauze (11) and the ash remains inside.

該篩別機(jは傾斜しているために内部に残留した灰滓
は機端から排出される。
Since the sieving machine (j) is inclined, the ash remaining inside is discharged from the end of the machine.

分離された結社は篩別機(3)の下面に配置された橋形
の流路(7)を通って篩別機型の晒し機(6)に送られ
る。第1図に示すように流路(7)は内側に多数の晒し
用水流ノズル(/3)が設けられており、結社はこの流
路(7)内を流下する間に該ノズル(/3)から流出す
る水によって冷却と洗浄作用を受け、不純物の溶出と餡
粒子の分離即ち水晒し工程が促がされる。
The separated aggregates are sent to a sieving machine-type bleaching machine (6) through a bridge-shaped channel (7) arranged on the underside of the sieving machine (3). As shown in Fig. 1, the flow path (7) is provided with a large number of bleaching water nozzles (/3) inside, and while the association flows down this flow path (7), the nozzles (/3) ) is subjected to cooling and cleaning effects by the water flowing out from the container, which promotes the elution of impurities and the separation of bean paste particles, that is, the water exposure process.

流路(7)を流下した結社は、前記の篩別機型晒し機(
6)内において上方の注水器(lりからのシャワー水を
受は乍ら回転されることにより餡粒子の表面に付着した
不純物の洗浄剥離作用が更に促がされ、良質の餡粒子と
して精製されたのち貯留槽(tS)に貯留され、しかる
のち脱水機により脱水されて製品となる。
The tissue flowing down the flow path (7) is processed by the sieving machine type bleaching machine (
6) The shower water from the upper water pourer is rotated while the water is being rotated, which further promotes the cleaning and peeling action of impurities attached to the surface of the bean paste particles and refines them into high-quality bean paste particles. It is then stored in a storage tank (tS) and then dehydrated by a dehydrator to become a product.

以上に述べた如く本発明に係る生詰製造法は、製餡機(
2)から送出された餡材料をまず分離篩別機(3)によ
って灰滓と結社とに分離する前処理として水分抽出機(
、r)に送って該餡材料に含まれている大半の高温水分
を除去するため、次の工程において餡材料から分離篩別
機(3)により灰滓と結社とを分離した際に高温水分を
含まない餡汁を得ることができる。このように多量の高
温水分を含まない状態の餡材料から餡汁を得る場合と、
従来のように多量の高温水分を含む状態の餡材料から結
社を得る場合とでは、当然のこと乍ら餡材料の温度は同
じであっても単位容量においては大幅な相違を有するこ
と\なる。従って高温水分を含まない容量の少ない餡材
料から得られる結社は以後の水晒しの工程において結社
のみを冷却するだけの量の晒し用水でたりることになり
、従って晒し用水の使用量を従来の製法による場合に比
較して半分以下程度に低減することができる。
As described above, the raw filling manufacturing method according to the present invention is based on the bean paste making machine (
The bean paste material sent out from 2) is first separated into ash and ash by a separation sieve (3).
, r) to remove most of the high-temperature moisture contained in the bean paste material. It is possible to obtain bean soup that does not contain In this way, when obtaining bean paste from bean paste material that does not contain a large amount of high-temperature water,
Naturally, when obtaining a dough from an bean paste material that contains a large amount of high-temperature moisture as in the past, there is a large difference in unit volume even if the temperature of the bean paste material is the same. Therefore, the amount of bleaching water used to cool only the knots in the subsequent water-bleaching process for the knots obtained from a filling material with a small capacity that does not contain high-temperature moisture is reduced compared to the conventional method. This can be reduced to about half or less compared to when using the manufacturing method.

勿論分離篩別機(3)から得られた餡汁が高温水分を含
まないということは、冷却水の使用量を節減し得るとい
う利点の外、冷却に要する時間を短縮でき、その結果処
理工程中における有害菌の繁殖を防止できることになる
。また結社の冷却が急速に行われるので、餡汁から餡粒
子を分離するための水晒し処理に要する時間を短縮でき
ると共に設備を縮減でき、作業能率の大幅な向上を期待
できるという効果を有する。
Of course, the fact that the bean paste obtained from the separating and sieving machine (3) does not contain high-temperature water has the advantage of reducing the amount of cooling water used, as well as shortening the time required for cooling, and as a result, the processing process This will prevent the growth of harmful bacteria inside. In addition, since the dough is rapidly cooled, it is possible to shorten the time required for the water exposure treatment to separate the bean paste particles from the bean paste soup, and also to reduce the amount of equipment required, which has the effect that a significant improvement in work efficiency can be expected.

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

第1図及び第2図はいずれも従来における生詰製造法の
工程図、第3図は本発明に係る生詰製造法の工程図、第
7図は本発明の製造法における水晒し工程に用いられる
結線流路の斜視図である。 図において、 (1):豆煮釜、(2):製餡機、(3):分離篩別機
、(ゲ):沈澱槽、(j):脱水機、(6):篩形晒し
装置、(7):流路、(ざ):水分抽出機、(lの(/
2) (/+) :シャワー型注水器、(/3) :晒
し用水流ノズル、(/!;) :貯留槽。 特許出願人 株式会社サンユー
Figures 1 and 2 are process diagrams for the conventional raw filling manufacturing method, Figure 3 is a process diagram for the raw packaging manufacturing method according to the present invention, and Figure 7 is a process diagram for the soaking process in the manufacturing method of the present invention. FIG. 3 is a perspective view of a used connection flow path. In the figure, (1): Bean boiling pot, (2): Bean paste making machine, (3): Separation and sieving machine, (GE): Sedimentation tank, (J): Dehydrator, (6): Sieve-shaped bleaching device , (7): Channel, (za): Water extractor, (l's (/
2) (/+): Shower type water injector, (/3): Water nozzle for bleaching, (/!;): Storage tank. Patent applicant: Sanyu Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] L  mtia機にて製造された鮎材料からまず水分抽
出装置を介して含有高温水分を取除き、しかるのちこの
萬温水分を除去した餡材料から分離篩別機を介して結社
と灰滓とを分離し、この分離された結社を水晒し処理す
ることを特徴とした生詰製造法。
First, the high-temperature moisture contained in the sweetfish material produced in the L mtia machine is removed through a moisture extraction device, and then the sweet paste and ash are separated from the bean paste material from which the moisture has been removed through a separation sieve. A method for producing fresh ingredients characterized by separating the aggregates and exposing the separated aggregates to water.
JP57041765A 1982-03-18 1982-03-18 Raw “An” manufacturing method Expired JPS5940419B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57041765A JPS5940419B2 (en) 1982-03-18 1982-03-18 Raw “An” manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57041765A JPS5940419B2 (en) 1982-03-18 1982-03-18 Raw “An” manufacturing method

Publications (2)

Publication Number Publication Date
JPS58162242A true JPS58162242A (en) 1983-09-26
JPS5940419B2 JPS5940419B2 (en) 1984-09-29

Family

ID=12617493

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57041765A Expired JPS5940419B2 (en) 1982-03-18 1982-03-18 Raw “An” manufacturing method

Country Status (1)

Country Link
JP (1) JPS5940419B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6833152B2 (en) * 2001-10-31 2004-12-21 Yugenkaisha Sakai Soybean jam

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6833152B2 (en) * 2001-10-31 2004-12-21 Yugenkaisha Sakai Soybean jam

Also Published As

Publication number Publication date
JPS5940419B2 (en) 1984-09-29

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