JPS601852B2 - A method for producing sugar solution used as a raw material for beer, etc., and protein used as food from rice or milo. - Google Patents
A method for producing sugar solution used as a raw material for beer, etc., and protein used as food from rice or milo.Info
- Publication number
- JPS601852B2 JPS601852B2 JP54078547A JP7854779A JPS601852B2 JP S601852 B2 JPS601852 B2 JP S601852B2 JP 54078547 A JP54078547 A JP 54078547A JP 7854779 A JP7854779 A JP 7854779A JP S601852 B2 JPS601852 B2 JP S601852B2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- rice
- liquid
- milo
- protein
- 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
Links
- 239000002994 raw material Substances 0.000 title claims description 24
- 235000007164 Oryza sativa Nutrition 0.000 title claims description 13
- 108090000623 proteins and genes Proteins 0.000 title claims description 13
- 102000004169 proteins and genes Human genes 0.000 title claims description 13
- 235000009566 rice Nutrition 0.000 title claims description 13
- 238000004519 manufacturing process Methods 0.000 title claims description 12
- 240000006394 Sorghum bicolor Species 0.000 title claims description 10
- 235000011684 Sorghum saccharatum Nutrition 0.000 title claims description 10
- 235000009430 Thespesia populnea Nutrition 0.000 title claims description 10
- 235000013405 beer Nutrition 0.000 title claims description 10
- 235000013305 food Nutrition 0.000 title claims description 6
- 240000007594 Oryza sativa Species 0.000 title claims 3
- 239000007788 liquid Substances 0.000 claims description 19
- 238000002791 soaking Methods 0.000 claims description 14
- 229920002472 Starch Polymers 0.000 claims description 12
- 239000000839 emulsion Substances 0.000 claims description 12
- 238000000227 grinding Methods 0.000 claims description 12
- 235000019698 starch Nutrition 0.000 claims description 12
- 239000008107 starch Substances 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 11
- 239000002351 wastewater Substances 0.000 claims description 9
- 239000007787 solid Substances 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 4
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims description 4
- 238000000855 fermentation Methods 0.000 claims description 3
- 230000004151 fermentation Effects 0.000 claims description 3
- 239000004310 lactic acid Substances 0.000 claims description 2
- 235000014655 lactic acid Nutrition 0.000 claims description 2
- 210000004072 lung Anatomy 0.000 claims description 2
- 238000005498 polishing Methods 0.000 claims 2
- 230000008961 swelling Effects 0.000 claims 1
- 241000209094 Oryza Species 0.000 description 10
- 235000018102 proteins Nutrition 0.000 description 10
- 239000000243 solution Substances 0.000 description 6
- 239000011362 coarse particle Substances 0.000 description 5
- 238000003801 milling Methods 0.000 description 4
- 239000002562 thickening agent Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 235000013339 cereals Nutrition 0.000 description 3
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- UKLNMMHNWFDKNT-UHFFFAOYSA-M sodium chlorite Chemical compound [Na+].[O-]Cl=O UKLNMMHNWFDKNT-UHFFFAOYSA-M 0.000 description 2
- 229960002218 sodium chlorite Drugs 0.000 description 2
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 2
- 230000002087 whitening effect Effects 0.000 description 2
- 108010082495 Dietary Plant Proteins Proteins 0.000 description 1
- 241000287828 Gallus gallus Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 244000062793 Sorghum vulgare Species 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 235000021329 brown rice Nutrition 0.000 description 1
- QBWCMBCROVPCKQ-UHFFFAOYSA-N chlorous acid Chemical compound OCl=O QBWCMBCROVPCKQ-UHFFFAOYSA-N 0.000 description 1
- 229940077239 chlorous acid Drugs 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 230000003544 deproteinization Effects 0.000 description 1
- 235000021245 dietary protein Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000019713 millet Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 235000008935 nutritious Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- 235000015096 spirit Nutrition 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 229920001864 tannin Polymers 0.000 description 1
- 239000001648 tannin Substances 0.000 description 1
- 235000018553 tannin Nutrition 0.000 description 1
- 239000011882 ultra-fine particle Substances 0.000 description 1
- 235000021419 vinegar Nutrition 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
Landscapes
- Fodder In General (AREA)
- Jellies, Jams, And Syrups (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Description
【発明の詳細な説明】
この発明はビール等の原料に用いる糖液および食糧とし
て用いる蛋白質を米あるいはマィロより製造する方法に
関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a sugar solution used as a raw material for beer and the like and a protein used as food from rice or milo.
従来、ビールの原料として必要な糖液は、細米を蒸し、
これを糖化させて使用しており、その際できる粕には良
質の蛋白質が多量に含有されているのにも拘ず、単に飼
料として利用されているに過ぎないもので、含有蛋白質
は廃棄処分同然に取り扱われていた。Traditionally, the sugar solution needed as a raw material for beer was produced by steaming fine rice.
This is used after being saccharified, and although the resulting lees contain a large amount of high-quality protein, it is merely used as feed, and the protein content is disposed of as waste. It was treated the same way.
この発明はこのような点に着目してなされたもので、米
あるいはマィロより糠液を製造し、これをビール等の糠
液原料として使用するとともに、糠液製造の際に除去し
た蛋白は食糧として利用し、また製造工程中において排
出される廃水の一部は原料の米あるいはマィロの精白の
際に出る糠と混合して飼料として利用し、さらに廃水の
残部は製造工程へ返戻して再利用し、廃水公害が発生す
る恐れなく製造できるようにする製造法を提供しようと
するものである。This invention was made with attention to these points, and involves producing bran from rice or milo, using this as a bran raw material for beer, etc., and using the protein removed during the bran production as a food source. In addition, a portion of the wastewater discharged during the manufacturing process is mixed with the rice or bran produced during milling of the raw material and used as feed, and the remainder of the wastewater is returned to the manufacturing process and recycled. The aim is to provide a manufacturing method that enables production without the risk of wastewater pollution.
次にこの発明の実施例を図に示す工程図によりながら説
明する。Next, an embodiment of the present invention will be described with reference to process diagrams shown in the drawings.
１は精白機で、原料の玄米あるし、は玄穀マィロを精白
して糠を取り去り、浸債槽２へ送る。1 is a milling machine that mills brown rice and millet grains as raw materials, removes the bran, and sends it to the soaking tank 2.
精白により得られる糠は原料の全量の約２０％重量にも
達し、回収して後述する浸漬液等の廃水と混合し飼料と
する。浸債槽２では原料を、徴量の亜塩素酸ソーダを弱
酸性液とした溶液に浸潰して殺菌するとともに、４尊○
〜４７０の温度にて１幼時間内外、カウンターターレン
ト方式にて浸糟する。原料にマィロを使用した場合は、
ここでタンニンを除去しかつ脱色をする。そして浸債終
了後、膨潤した原料を取出して磨砕装置３へ送り、水を
加えながら磨砕したのち、液体サイクロン４およびシッ
クナー５に順次送って粗粒と澱粉乳液と腕芽とに分離し
、粗粒はさらに次の磨砕装置６で磨砕したのち、再度液
体サイクロン７およびシックナー８に順次送って粗粒と
澱粉乳液と肺芽とに分離し、残った粗粒はさらに次の磨
砕装置９で磨砕したのち、再再度液体サイクロン１０お
よびシックナー１１に順次送って粗粒を分離し「分離し
た粗粒は前段の磨砕装置６へ返戻する操作を繰返して、
粗粒を完全に澱粉乳液にする。上記の操作によって分離
された腕芽は回収して別途に利用する。このようにして
磨砕および分離された澱粉乳液は、２００メツシ程度の
節１２に通し、時間の経過とともに膨潤した澱粉乳液中
の粗繊縦を除去したのちタンク１３に収容する。除去し
た細繊維はグラインダー磨砕機１４で磨砕して極超微粒
子にし、液体サイクロン１５を通して磨砕工程へ返す。
タンク１３に収容された澱粉乳液は液体サイクロン１６
で澱粉乳液中に極少量存在するグリッッおよび砂を分離
し、その後、濃縮機１７で濃縮し、水分は浸債槽２およ
び磨砕工程へ返して再利用する。また上記のグリッッは
磨砕工程へ返す。そして濃縮した澱粉乳液はＰＨを６位
に保持しながら液化酵素を加えて加熱装置１８で加熱し
たのち、液化タンク１９に滞溜させて液化させ、その後
、液化タンク１９より出して再度加熱装置２０で加熱す
るが、原料に米を使用した場合は１１０００位に、また
マイロを使用した場合は１１０ｏｏ〜１２０００に加熱
し、その後、何れの場合も９０ｏｏ位までに冷却し、さ
らに酵素を加えて液化タンク２１に再度入れ嫌溜させて
さらに液化を促進させる。液化液はその後、デカンター
２２に送り液と固形物とに分離し、液は清澄機２３で清
澄化し糖液として回収し、ビール、蒸溜酒、醸造酢など
の糖液原料として使用する。またデカンタ−２２により
分離された固形物は清澄機２３により除去された固形物
と混合して加熱装置２４へ送り、高温の熱水にて溶解し
、その後タンク２５に入れて滞溜させたのち、脱水機２
６で脱水し乾燥して蛋白質として回収し、脱水した水分
はデカン夕−２２および清澄機２３により除去された固
形物に混入する。回収した蛋白質は食糧として利用し、
特に米蛋白は植物性蛋白としてすぐれ、栄養食として、
また工業原料として利用できる。一方浸濃終了後、浸債
槽２より排出される浸債液は一部を磨砕工程へ返して利
用し、残部および磨砕工程等において排出された廃水の
一部とを醗酵槽２７に収容し、温度４５ｑｏ〜４７℃、
ＰＨ５〜６に保持しながら乳酸酸髪蓬させたのち、蒸発
燐で濃緒し、この濃縮液と精白機１により排出される原
料の糠とを混合し乾燥して飼料とする。The bran obtained by milling accounts for about 20% of the total amount of raw materials, and is collected and mixed with waste water such as soaking liquid, which will be described later, to make feed. In soaking tank 2, the raw materials are sterilized by soaking them in a weakly acidic solution of sodium chlorite.
Soak for 1 hour at a temperature of ˜470° C. in a counterculture method. If you use Milo as a raw material,
Here tannins are removed and the color is bleached. After soaking, the swollen raw material is taken out and sent to the grinding device 3, where it is ground while adding water, and then sequentially sent to the liquid cyclone 4 and thickener 5, where it is separated into coarse grains, starch emulsion, and arm buds. After the coarse particles are further ground in the next grinding device 6, they are sequentially sent to the liquid cyclone 7 and thickener 8 to be separated into coarse particles, starch emulsion, and lung buds, and the remaining coarse particles are sent to the next grinding device. After being ground in the grinding device 9, the particles are sent to the liquid cyclone 10 and the thickener 11 again to separate coarse particles, and the separated coarse particles are returned to the previous grinding device 6.
Completely convert coarse grains into starch emulsion. The arm buds separated by the above procedure are collected and used separately. The starch emulsion thus ground and separated is passed through a node 12 of about 200 mesh to remove coarse fibers in the starch emulsion that swell over time, and then stored in a tank 13. The removed fine fibers are ground into ultra-fine particles by a grinder 14 and returned to the grinding process through a hydrocyclone 15.
The starch emulsion stored in the tank 13 is transferred to the liquid cyclone 16
Grit and sand present in a very small amount in the starch emulsion are separated, and then concentrated in a concentrator 17, and the water is returned to the soaking tank 2 and the grinding process for reuse. The above grits are also returned to the grinding process. The concentrated starch emulsion is then heated in the heating device 18 with the addition of a liquefaction enzyme while maintaining the pH at 6th position, and then retained in the liquefaction tank 19 and liquefied. However, if rice is used as the raw material, it is heated to about 11,000 degrees Celsius, and if Milo is used, it is heated to about 110 to 12,000 degrees Celsius.After that, in either case, it is cooled to about 90 degrees Celsius, and then enzymes are added and liquefied. The liquid is put into the tank 21 again and stored to further promote liquefaction. The liquefied liquid is then sent to a decanter 22 where it is separated into a feed liquid and solid matter, and the liquid is clarified by a clarifier 23 and recovered as a sugar solution, which is used as a raw material for sugar solutions such as beer, distilled spirits, and brewed vinegar. In addition, the solids separated by the decanter 22 are mixed with the solids removed by the clarifier 23, sent to the heating device 24, dissolved in high-temperature hot water, and then put into the tank 25 where they are allowed to stagnate. , dehydrator 2
The protein is dehydrated and dried in Step 6 and recovered as protein, and the dehydrated water is mixed into the solids removed by the decanter 22 and clarifier 23. The recovered protein is used as food,
In particular, rice protein is an excellent vegetable protein and is used as a nutritional food.
It can also be used as an industrial raw material. On the other hand, after the completion of soaking, a part of the soaking liquid discharged from the soaking tank 2 is returned to the grinding process for use, and the remaining part and a part of the wastewater discharged during the grinding process etc. are sent to the fermentation tank 27. accommodated at a temperature of 45qo to 47°C,
After being soaked in lactic acid while maintaining the pH at 5 to 6, it is concentrated with evaporated phosphorus, and this concentrated liquid is mixed with the raw material bran discharged from the whitening machine 1 and dried to form feed.
なお浸債槽２において殺菌のために使用された徴量の亜
塩素酸ソーダは浸債中にほとんどが亜塩素酸に分解され
、また除蛋白と脱色に消費される結果、外部へ排出され
ることはない。In addition, most of the collected sodium chlorite used for sterilization in the soaking tank 2 is decomposed into chlorous acid during the soaking process, and is also consumed for deproteinization and decolorization, which is then discharged to the outside. Never.
なお亜硫酸ソーダを加えて還元させるときは完全に消滅
させることが可能である。以上説明したようにこの発明
によると、米あるいはマィロを原料とし、これよりビー
ル等に用いる糠液を製造するとともに、糖液製造の際に
原料に含有している蛋白質を除去するので、ビール等の
糠液原料として用いられる米あるいはマィロより食糧と
しての蛋白質を有効に回収できることになり、糠液原料
としての米あるいはマィロの価値を著しく高めることが
でき、延し、てはビール等のコストダウンをはかれると
ともに、省資源化に寄与できる。Note that when adding sodium sulfite for reduction, it is possible to completely eliminate it. As explained above, according to the present invention, rice or milo is used as a raw material to produce bran liquid used for beer, etc., and since the protein contained in the raw material is removed during the production of sugar solution, beer etc. Food protein can be effectively recovered from rice or milo, which is used as a raw material for bran, and the value of rice or milo as a raw material for bran can be significantly increased, which in turn can reduce the cost of beer, etc. It can also contribute to resource conservation.
しかも糖液は、澱粉乳液として回収されるので、ビール
等の糠液原料として直ちに使用でき、非常に好都合であ
るとともに、取扱いも容易である。Moreover, since the sugar solution is recovered as a starch emulsion, it can be used immediately as a raw material for bran liquid for beer, etc., which is very convenient and easy to handle.
また回収した蛋白質は、栄養価の高い蛋白質として各方
向に有効に利用できる。In addition, the recovered protein can be effectively used in various ways as a highly nutritious protein.
そして製造工程中において排出される廃水はその一部を
原料の米あるいはマィロの精白の際にできる糠と混合し
て飼料とし、廃水の残部は製造工程へ返戻して再利用す
るので、廃水公害が発生することなく製造できる効果が
ある。Part of the wastewater discharged during the manufacturing process is mixed with the raw material rice or bran produced during milling and used as feed, and the rest of the wastewater is returned to the manufacturing process and reused, resulting in no wastewater pollution. This has the effect of allowing manufacturing to be carried out without the occurrence of.
図はこの発明の実施例を示す工程図である。
１・・・・・・精白機、２・・…・浸債槽、３，６．９
・・・・・・磨砕装置、４，７，１０・・…・液体サイ
クロン、５，８，１１……シックナー、１８，２０……
加熱装置、１９，２１・…・・液化タンク、２２・・・
・・・ナカンター、２６・・・・・・脱水機、２７・・
…・酉醗酵槽。The figure is a process diagram showing an embodiment of this invention. 1... Whitening machine, 2... Bond soaking tank, 3, 6.9
...... Grinding device, 4,7,10... Liquid cyclone, 5,8,11... Thickener, 18,20...
Heating device, 19, 21... Liquefaction tank, 22...
...Nakanter, 26...Dehydrator, 27...
...・Rooster fermentation tank.
Claims (1)
浸漬して膨潤させ、膨潤後、浸漬液より取出して磨砕し
澱粉乳液にするとともに、この澱粉乳液中より肺芽を分
離し、その後、この澱粉乳液を加熱して液化したのち、
この液化液を液と固形物とに分離し、液は糖液として回
収し、また固形物はさらに脱水および乾燥して蛋白質と
して回収する一方、上記工程において排出される浸漬液
等の廃水の一部は適度の温度に保持しながら乳酸醗酵さ
せたのち濃縮し、この濃縮液と上記原料の精白の際にで
きた糠とを混合し乾燥して飼料とし、また上記廃水の残
部は上記工程において浸漬、磨砕等の際に再利用するこ
とを特徴とするビール等の原料に用いる糖液および食糧
として用いる蛋白質を米あるいはマイロより製造する方
法。1 Rice or milo is used as a raw material. After polishing the raw material, it is soaked and swollen. After swelling, it is taken out from the soaking liquid and ground to make a starch emulsion. The lung buds are separated from this starch emulsion, and then this After heating the starch emulsion and liquefying it,
This liquefied liquid is separated into liquid and solids, the liquid is recovered as a sugar solution, and the solids are further dehydrated and dried to be recovered as protein. The remaining part is subjected to lactic acid fermentation while maintaining at an appropriate temperature, and then concentrated. This concentrated liquid is mixed with the bran produced during the polishing of the above raw materials and dried to be used as feed, and the remainder of the above waste water is used in the above process. A method for producing a sugar solution used as a raw material for beer and the like and a protein used as food from rice or milo, which is characterized by reuse during soaking, grinding, etc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54078547A JPS601852B2 (en) | 1979-06-20 | 1979-06-20 | A method for producing sugar solution used as a raw material for beer, etc., and protein used as food from rice or milo. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54078547A JPS601852B2 (en) | 1979-06-20 | 1979-06-20 | A method for producing sugar solution used as a raw material for beer, etc., and protein used as food from rice or milo. |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS561880A JPS561880A (en) | 1981-01-10 |
| JPS601852B2 true JPS601852B2 (en) | 1985-01-17 |
Family
ID=13664935
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54078547A Expired JPS601852B2 (en) | 1979-06-20 | 1979-06-20 | A method for producing sugar solution used as a raw material for beer, etc., and protein used as food from rice or milo. |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS601852B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6285639U (en) * | 1985-11-15 | 1987-06-01 | ||
| JPH04106225A (en) * | 1990-08-27 | 1992-04-08 | Iida Tekko:Kk | Clamping bucket and its fitting method |
| JPH0428371Y2 (en) * | 1986-06-28 | 1992-07-09 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2024484B1 (en) * | 2006-05-19 | 2014-05-14 | Heineken Supply Chain B.V. | Continuous method for the production of a yeast fermented beverage |
| LT2027245T (en) * | 2006-05-19 | 2018-11-12 | Heineken Supply Chain B.V. | A method of producing a mash extract and an apparatus for performing such method |
-
1979
- 1979-06-20 JP JP54078547A patent/JPS601852B2/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6285639U (en) * | 1985-11-15 | 1987-06-01 | ||
| JPH0428371Y2 (en) * | 1986-06-28 | 1992-07-09 | ||
| JPH04106225A (en) * | 1990-08-27 | 1992-04-08 | Iida Tekko:Kk | Clamping bucket and its fitting method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS561880A (en) | 1981-01-10 |
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