JPS585145A - Separation of germ from corn - Google Patents

Separation of germ from corn

Info

Publication number
JPS585145A
JPS585145A JP56100306A JP10030681A JPS585145A JP S585145 A JPS585145 A JP S585145A JP 56100306 A JP56100306 A JP 56100306A JP 10030681 A JP10030681 A JP 10030681A JP S585145 A JPS585145 A JP S585145A
Authority
JP
Japan
Prior art keywords
fermentation
germ
corn
germs
water
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.)
Pending
Application number
JP56100306A
Other languages
Japanese (ja)
Inventor
Shinya Matsumoto
松元 信也
Katsushi Kakihara
柿原 克史
Etsuko Nakajima
中嶋 悦子
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.)
Suntory Ltd
Original Assignee
Suntory 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 Suntory Ltd filed Critical Suntory Ltd
Priority to JP56100306A priority Critical patent/JPS585145A/en
Publication of JPS585145A publication Critical patent/JPS585145A/en
Pending legal-status Critical Current

Links

Landscapes

  • Cereal-Derived Products (AREA)

Abstract

PURPOSE:An aqueous suspension of corn meal is, without steaming, subjected to alcohol fermentation and germs floating on the surface of the fermentation mixture are collected by filtration, thus permitting the sepration of germs without treatment with high temperature and sulfurous acid. CONSTITUTION:Corn grains are crushed into particles of 1,680-420mu sizes and mixed with water at a weight ratio of 1/3.4-1/1.8 to form a suspension. Then, the suspension, without steaming, is subjected to fermentation by adding a saccharifying enzyme (mainly consisting one originating from Rhyzopus) and a yeast. The fermentation is effected at 25-35 deg.C and continued for 60hr, while germs are carried by the carbon dioxide evolved by the fermentation up to the surface and filtered off.

Description

【発明の詳細な説明】 本発明は全粒トウモロコシより胚芽部分を分離する方法
に関する。トウモロコシの胚芽は油分、蛋白質に富み、
サラダオイル、クツキングオイル等の食用油原料および
グルテン等の蛋白質原料として有用なものである。トウ
モロコシより胚芽全分離する従来法の殆んどは湿式粉砕
法によるものである。湿式粉砕法では全粒トウモロコシ
を水で浸漬する際殺菌や回収車内上等のため無水亜硫酸
を0.1〜0.3%程度添°加しなければならず、しか
も40℃以上に加温する必要があった。浸漬後は水管分
離し粉砕し再び水に懸濁させ比重差によって胚芽を分離
し、水洗、脱水、乾燥するものである。一方胚芽を分離
された残りの澱粉質は・更に磨砕され、粕等を分離した
後水洗等で精製されコーンスターチとするか、液化およ
びまたは糖化工程會経て水アメ、ブドウ糖、転化糖とす
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for separating the germ portion from whole corn. Corn germ is rich in oil and protein,
It is useful as a raw material for edible oils such as salad oil and cooking oil, and as a raw material for proteins such as gluten. Most of the conventional methods for completely separating the germ from corn are based on wet grinding. In the wet grinding method, when whole corn is soaked in water, it is necessary to add 0.1 to 0.3% of anhydrous sulfurous acid for sterilization and cleaning inside collection vehicles, and the corn must be heated to 40°C or higher. There was a need. After soaking, the germ is separated into water tubes, pulverized, suspended in water again, the germs are separated based on the difference in specific gravity, and then washed, dehydrated, and dried. On the other hand, the remaining starch from which the germ has been separated is further ground, and after separating the lees etc., it is purified by washing with water, etc. to make corn starch, or it is liquefied and/or saccharified to make starch syrup, glucose, and invert sugar. It is.

かかる従来法で分離された胚芽は高温下での大量の並値
aI!による処理等のため、胚芽よに見られる原料油即
ちコーンオイルは遊離脂肪酸が多いものでめる。更に従
来法は多量の水、勢および動力を必要とするものでめっ
た。本発明はかかる従来法とは全く異なる胚芽分離法を
提供するもので、全粒トウモロコシ粉砕物の水懸濁液を
無蒸煮のまま糖化酵素および酵母管加えアルコール発W
#金石わしめ、発酵液の上面に浮遊する胚芽會F取する
こと全特徴とするトウモロコシの胚芽分離法であるO 本発明における全粒トウモロコシ粉砕tIIIは微粉砕
しないことが必要で、好ましくは1680〜420μ程
度に粉砕されていればよい。かかる粉砕物を水と重量比
で1 : 3.4〜1:1.8程度の割合で混ぜ懸濁液
とすればよく、水にアルコール蒸留廃液を混合してもよ
く、水の全量を蒸留廃液にしてもよい。かかる懸濁液を
無蒸煮のまま糖化酵素および酵母を加えて25〜35℃
で発酵させる本のであるが、無蒸煮アルコール発酵法の
種々の態様について本発明者らilt既に開示している
。即ち糖化酵素剤としてリゾラプス起源のものを主体と
して使用することが好ましく、また発酵の最初の10時
間以内は酵母数を2 X 10’個/Wd以上に保つこ
とが好ましい。また細菌で汚染されている原料を使用す
る場合は無水亜硫酸を少量(320pPm以下)添加す
ればよい。かかる無蒸煮アルコール発酵において、胚芽
部分は発生する炭醗ガスによって運ばれ上面に浮遊して
くるので上面よりF取すればよいOF取する時期は発酵
中であればいつでもよいが取扱上発酵の前半の方が好ま
しいO本発明者らの開発した無蒸煮アルコール発酵法に
おいては発酵期間は90〜120時間であるので発酵開
始より60時間以前KP取するのが作業に適している。
The germs separated by this conventional method have a large amount of average aI at high temperatures! The raw material oil found in the germ, ie corn oil, has a high content of free fatty acids. Furthermore, conventional methods require large amounts of water, force, and power, making them difficult. The present invention provides a germ separation method that is completely different from such conventional methods, and involves adding a saccharifying enzyme and a yeast tube to an aqueous suspension of crushed whole corn grains without steaming, and evaporating the germs with alcohol.
#Kanaishi is a corn germ separation method characterized by collecting the germs floating on the upper surface of the fermentation liquid. The whole corn grinding tIII in the present invention is required not to be finely ground, and is preferably 1680 It is sufficient if it is crushed to about 420 μm. The pulverized product may be mixed with water at a weight ratio of about 1:3.4 to 1:1.8 to form a suspension.Alcoholic distillation waste liquid may be mixed with water, or the entire amount of water may be distilled. It may be used as waste liquid. Saccharifying enzyme and yeast were added to the suspension without steaming, and the mixture was heated at 25 to 35°C.
In this book, the present inventors have already disclosed various aspects of the non-cooking alcoholic fermentation method. That is, it is preferable to mainly use a saccharifying enzyme agent derived from Rhizolaps, and it is preferable to maintain the number of yeast at 2 x 10' cells/Wd or more within the first 10 hours of fermentation. Furthermore, when using raw materials contaminated with bacteria, a small amount (320 pPm or less) of anhydrous sulfite may be added. In such non-cooking alcoholic fermentation, the germ part is carried by the generated charcoal gas and floats to the top surface, so F can be removed from the top surface. OF can be removed at any time during fermentation, but for handling reasons, it is best to remove OF during the first half of fermentation. In the non-cooking alcoholic fermentation method developed by the present inventors, the fermentation period is 90 to 120 hours, so it is suitable for the operation to take KP 60 hours before the start of fermentation.

一方、全粒トウモロコシ粉砕物の水懸濁液を蒸煮してア
ルコール発rIIt−行う従来の発酵法では、加熱によ
る液化および糖化工程を受けているので胚芽は上面に浮
遊してくることなく、糖化粕、酵母等と一緒になってい
るので胚芽部分のみ分離することは困難である。
On the other hand, in the conventional fermentation method in which an aqueous suspension of ground whole corn grains is steamed to produce alcohol, the germ is liquefied and saccharified by heating, so the germ does not float to the top and is saccharified. Since it is mixed with lees, yeast, etc., it is difficult to separate only the germ part.

本発明法によって分離され九胚芽は必要に応じて水洗し
乾燥すればよく、従来の湿式粉砕で分離された胚芽と同
様コーン油ま九はグルテン製造原料とすることができる
。特に本発明によって分離された胚芽は細菌汚染の著し
い原料を使用しても亜硫酸濃度ti320ppm以下で
しか処理されていないので、従来法の亜硫酸濃度0.1
−0.3−での湿式粉砕によって見られる胚芽と比較し
て自然の11の状態である。従って本発明によって見ら
れる胚芽より見られるコーン油は抗酸化力が強く遊離脂
肪酸が少ないという特徴を有するものであり、食用油原
油としても秀れているものである。
The corn germ separated by the method of the present invention may be washed with water and dried if necessary, and the corn oil corn germ can be used as a raw material for gluten production, similar to the germ separated by conventional wet grinding. In particular, the germs separated by the present invention are processed only at a sulfite concentration of 320 ppm or less even if raw materials with significant bacterial contamination are used, whereas the sulfite concentration of the conventional method is 0.1.
11 condition compared to the germ seen by wet milling at -0.3-. Therefore, the corn oil obtained from the germ according to the present invention is characterized by strong antioxidant power and low free fatty acid content, and is excellent as an edible crude oil.

更に従来の湿式粉砕法の比重差による分離ては胚芽が完
全に分離されたかどうかあるいは澱粉質その他等を伴っ
ているかどうかは分離工程中では確認が困難であったが
、本発明方法では澱°粉部分は殆、んどアルコールに変
っており、皮等の不純物は酵母と共に沈降し、胚芽のみ
が上面に浮遊しているので完全に、しかも挾雑物を殆ん
ど含まずに分離できるという特徴を有する。従って分離
後の後処理が極めて容易であね更に収率よ〈分離できる
という効果?有する。また従来法の如く多量の水および
熱を使用しないというすぐれた効果を有するものである
。次に実施例によって詳細に説明する。なお、ここでい
う収率は次式で求め友もの実施例1゜ 全粒トウモロコシを下記粒度に粉砕した奄の2.4に、
、リゾラプス起源グルコアミラーゼ8.4単位(JIS
 K 7001−1972)/l原料、7i4.811
酒母(サツカロミセス・セレビシェ) 0.71を10
/容の檜に入れ撹拌混合後28℃にて112時間発酵せ
しめた。
Furthermore, in the conventional wet grinding method, it was difficult to confirm during the separation process whether the germ was completely separated or whether it contained starch or other substances, but with the method of the present invention, Most of the powder is converted to alcohol, impurities such as the skin settle down with the yeast, and only the germ floats on the top, so it can be completely separated with almost no impurities. Has characteristics. Therefore, post-treatment after separation is extremely easy, and the yield is even higher. have It also has the excellent effect of not using large amounts of water and heat unlike conventional methods. Next, a detailed explanation will be given using examples. In addition, the yield here is calculated using the following formula.
, Rhizolapus origin glucoamylase 8.4 units (JIS
K 7001-1972)/l raw material, 7i4.811
Sake mother (Satsucharomyces cerevisiae) 0.71 to 10
After stirring and mixing, the mixture was fermented at 28°C for 112 hours.

粒度 1680〜8411  69.0%840〜42
0μ  16.5嗟 420μ以下   14.5饅 JIS K 8801−1966による。
Particle size 1680~8411 69.0%840~42
0μ 16.5μ 420μ or less 14.5 according to JIS K 8801-1966.

発酵開始後24時間後に発酵液の上層に浮遊している胚
芽を網ですくい上げ水洗、乾燥し胚芽154.8p(水
分3チ)、収率7.55&をえた。一方発酵終了液の分
析結果は次の通りであった。
24 hours after the start of fermentation, the embryo floating in the upper layer of the fermentation liquid was scooped up with a net, washed with water, and dried to obtain 154.8 p of germ (3 g of moisture) and a yield of 7.55 ml. On the other hand, the analysis results of the fermentation-finished liquid were as follows.

pH4,9、TAC&酸) 3.1 、 フルコール1
4.2s。
pH 4.9, TAC & acid) 3.1, Flucol 1
4.2s.

FE(発酵歩合) 87.0 % 実施例2゜ 全粒トウモロコシを下記粒子に粉砕したもの3.0Kg
、リゾラプス起源ゲルコア之ラーゼ5.5単位/y原料
、水10.2/、酒母620m/を15/容の檜に入れ
撹拌混合後35℃で92時間発酵せしめた。
FE (fermentation ratio) 87.0% Example 2゜3.0kg of whole corn pulverized into the following particles
, 5.5 units/y of gelcoolase originating from Rhizolapus, 10.2 units/y of water, and 620 m/y of sake mash were placed in a 15/volume Japanese cypress, stirred and mixed, and then fermented at 35°C for 92 hours.

粒度 1680〜840μ ・30.0哄840〜42
0μ   34.11 420μ以下   35.9哄 発酵開始後48時間後に発酵液の上層部より胚芽部tF
別し、水洗後乾燥し胚芽186.1y(水分3%)、収
率7.4%fえた。一方発酵終了液の分析結果は次の通
りであった。
Particle size 1680~840μ ・30.0liters 840~42
0 μ 34.11 420 μ or less 35.9 48 hours after the start of fermentation, germ part tF is extracted from the upper layer of the fermentation liquid.
The germs were separated, washed with water, and dried to give an embryo of 186.1y (moisture content: 3%) and a yield of 7.4%f. On the other hand, the analysis results of the fermentation-finished liquid were as follows.

pH4,7、TA B、5、アルコール9,4−1FE
87.5Is 参考例1゜ 実施例1で得られた胚芽100yから圧搾−抽出法によ
妙原油48fを得た。この原油中の遊離脂肪酸含量はオ
レイン酸として1.5 %であった。
pH 4,7, TA B, 5, alcohol 9,4-1FE
87.5Is Reference Example 1 48f of Miao crude oil was obtained from 100y of the germ obtained in Example 1 by the compression-extraction method. The free fatty acid content in this crude oil was 1.5% as oleic acid.

参考例2゜ 実施例2で得られた胚芽100 f! jfc n−ヘ
キサン10(1/を加え、温度60℃程度に加温して1
2時間浸漬し、得られるきセラ(油脂と溶剤の混合溶液
)を採攻した。ミセラを取り除いた胚芽に新たにn−ヘ
キサンSodを加え、同様にして12時間浸漬した後、
ミセラを採取し、その油脂抽出操作を4回繰り返した。
Reference Example 2゜Embryo obtained in Example 2 100 f! Add jfc n-hexane 10 (1/), heat to about 60℃, and add 1/1
After immersion for 2 hours, the obtained sera (mixed solution of oil and fat and solvent) was sampled. N-hexane Sod was newly added to the embryo from which the micella had been removed, and after soaking in the same manner for 12 hours,
Micella was collected and the oil and fat extraction operation was repeated four times.

この油脂抽出操作によって得られたミセラ全量をジャケ
ット付蒸留罐に採り、窒素を吹込みつつ加熱温度90〜
100℃で2時間加熱して脱溶剤し、コーン原油51y
を得た。この原油の遊離脂肪酸含量はオレイン酸として
1.4チであった。
The entire amount of miscella obtained by this oil and fat extraction operation was taken into a jacketed distillation can, and heated to a temperature of 90 to 90°C while blowing nitrogen.
Heating at 100°C for 2 hours to remove the solvent, corn crude oil 51y
I got it. The free fatty acid content of this crude oil was 1.4 h as oleic acid.

mai人 サントリー株式会社 代理人 滝  川  敏  雄 −24コmai person Suntory Ltd. Agent Toshio Takikawa -24 pieces

Claims (1)

【特許請求の範囲】[Claims] 全粒トウモロコシ粉砕物の水懸濁液を無蒸煮のtt糖化
酵素および酵母を加えアルコール発酵金石わしめ、発酵
液の上面に浮遊する胚芽を戸取することを特徴とするト
ウモロコシの胚芽分離法。
A method for separating corn germ, which comprises adding non-cooked tt saccharifying enzyme and yeast to an aqueous suspension of ground whole grain corn, fermenting it with alcohol, and removing the germ floating on the top of the fermented liquid.
JP56100306A 1981-06-27 1981-06-27 Separation of germ from corn Pending JPS585145A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56100306A JPS585145A (en) 1981-06-27 1981-06-27 Separation of germ from corn

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56100306A JPS585145A (en) 1981-06-27 1981-06-27 Separation of germ from corn

Publications (1)

Publication Number Publication Date
JPS585145A true JPS585145A (en) 1983-01-12

Family

ID=14270478

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56100306A Pending JPS585145A (en) 1981-06-27 1981-06-27 Separation of germ from corn

Country Status (1)

Country Link
JP (1) JPS585145A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7618795B2 (en) 2003-06-25 2009-11-17 Novozymes A/S Starch process
US7688305B2 (en) 2003-11-25 2010-03-30 Kenji Nishi Information inputting tool, storage device, information inputting device, and information processing equipment
US7842484B2 (en) 2003-03-10 2010-11-30 Poet Research, Inc. Method for producing ethanol using raw starch
US7919289B2 (en) 2005-10-10 2011-04-05 Poet Research, Inc. Methods and systems for producing ethanol using raw starch and selecting plant material

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7842484B2 (en) 2003-03-10 2010-11-30 Poet Research, Inc. Method for producing ethanol using raw starch
US7919291B2 (en) 2003-03-10 2011-04-05 Poet Research, Inc. Method for producing ethanol using raw starch
US7618795B2 (en) 2003-06-25 2009-11-17 Novozymes A/S Starch process
US7998709B2 (en) 2003-06-25 2011-08-16 Novozymes A/S Process of producing a starch hydrolysate
US7688305B2 (en) 2003-11-25 2010-03-30 Kenji Nishi Information inputting tool, storage device, information inputting device, and information processing equipment
US7919289B2 (en) 2005-10-10 2011-04-05 Poet Research, Inc. Methods and systems for producing ethanol using raw starch and selecting plant material

Similar Documents

Publication Publication Date Title
US5013561A (en) Process for recovery of products from waxy barley
US4804545A (en) Production of beta-glucan, bran, protein, oil and maltose syrup from waxy barley
EP0192677B1 (en) Processes for recovery of products from waxy barley
JPS585145A (en) Separation of germ from corn
GB2094334A (en) Extracting oil, protein and flour from fresh coconut meat
JPS59205975A (en) Production of purified distilled liquor
CN113444578A (en) Extraction process of nannochloropsis oculata essential oil
Hassler Active Carbon: The Modern Purifier
CN107245369B (en) Method for producing vegetable oil without zearalenone by biological enzyme method
JPH0220225B2 (en)
US20040013768A1 (en) Method of obtaining ethyl alcohol or aqueous-alcoholic solution for preparation of vodka
JP3025822B2 (en) Method for clarifying soy sauce by centrifugation and method for recovering clarified soy sauce
JPS5955150A (en) Preparation of protein feed using residuary substances of mandarin as raw material
US2943983A (en) Process of obtaining concentrates of vitamins of the b12 group from waste liquors and residual products of industrial fermentation processes
JPH0530981A (en) Production of fat and oil extracted from yeast
JPH09163955A (en) Production of tomato flavor
JPS6023819B2 (en) Method for producing alcoholic fermented seasoning liquid using distillation waste liquid made from grains as raw material
US5013570A (en) Method of producing odorless ripe juice of houttuynia cordata
SU631524A1 (en) Method of obtaining vegetable oil from oil-containing fruit
SU697556A1 (en) Method of obtaining essential oil
CN113004971A (en) Method for preparing functional powdered oil by combining germination regulation and enzyme method
JPH0251587B2 (en)
CN113801750A (en) Mung bean flavor liquor rich in polypeptides and brewing method thereof
CN117063980A (en) Preparation method of cold-immersed aromatic pepper seasoning oil
JP5366114B2 (en) Triglyceride-producing yeast