JP2009050195A - Method and facility for producing ethanol - Google Patents

Method and facility for producing ethanol Download PDF

Info

Publication number
JP2009050195A
JP2009050195A JP2007219305A JP2007219305A JP2009050195A JP 2009050195 A JP2009050195 A JP 2009050195A JP 2007219305 A JP2007219305 A JP 2007219305A JP 2007219305 A JP2007219305 A JP 2007219305A JP 2009050195 A JP2009050195 A JP 2009050195A
Authority
JP
Japan
Prior art keywords
rice
ethanol
washing
ethanol production
power generation
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
JP2007219305A
Other languages
Japanese (ja)
Other versions
JP5257570B2 (en
Inventor
Takeshi Fukumori
武 福森
Shigeharu Kanemoto
繁晴 金本
Hidenori Mizuno
英則 水野
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.)
Satake Engineering Co Ltd
Satake Corp
Original Assignee
Satake Engineering Co Ltd
Satake Corp
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 Satake Engineering Co Ltd, Satake Corp filed Critical Satake Engineering Co Ltd
Priority to JP2007219305A priority Critical patent/JP5257570B2/en
Publication of JP2009050195A publication Critical patent/JP2009050195A/en
Application granted granted Critical
Publication of JP5257570B2 publication Critical patent/JP5257570B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing ethanol, which enables raw material procurement continuously and steadily in commercially producing ethanol in our country and utilizes carbon dioxide as a byproduct in ethanol production. <P>SOLUTION: The method includes the step of producing ethanol through liquefaction/saccharification by inoculating Aspergillus oryzae into rice washed water recovered in the treatment step for obtaining non-wash rice in a rice-polishing plant and concurrently through alcoholic fermentation by yeast addition, and the step of producing a functional food by extracting functional ingredients from a byproduct such as rice bran recovered in the rice-polishing plant by utilizing ethanol or carbon dioxide produced in the ethanol production step. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、バイオマス資源を利用したエタノールの製造方法及びその製造施設に関する。特に、精米工場における無洗化処理工程からの副産物(いわゆる、研ぎ汁)を利用して、自動車用ガソリンの代替用などのバイオエタノールを製造する方法に関する。 The present invention relates to a method for producing ethanol using biomass resources and a production facility thereof. In particular, the present invention relates to a method for producing bioethanol, such as a substitute for gasoline for automobiles, by using a by-product (so-called sharpened soup) from a washing process in a rice mill.

各種生物学的材料からエタノールを製造する方法は周知であり、例えば、出発原料として、トウモロコシ等デンプン質が容易に糖化され得る材料を用い、この出発原料に醸造イースト菌等を添加してデンプン質を糖化・発酵処理し、次いで、発酵液を蒸留処理して水を分離するとエタノールが得られる。この際、副産物として二酸化炭素及び残渣物が生じるが、該二酸化炭素を単に大気に逃がすのではなく、再利用して工業用メタノール、アセチレン及びベンゼンを合成して有効活用する一方、残渣物については、動物飼料の補足物又は肥料として再利用する技術がある(特許文献1参照)。 Methods for producing ethanol from various biological materials are well known. For example, as a starting material, a material such as corn that can easily saccharify starch can be used. When saccharification / fermentation treatment is performed, and then the fermentation broth is subjected to distillation treatment to separate water, ethanol is obtained. At this time, carbon dioxide and residue are produced as by-products, but the carbon dioxide is not simply released to the atmosphere, but reused to synthesize and effectively use industrial methanol, acetylene and benzene. There is a technique of reusing as a supplement or fertilizer for animal feed (see Patent Document 1).

上記出発原料に着目すると、わが国で作付けされている食用の穀物(米、小麦、大豆、サトウキビ等)を出発原料としてエタノールを製造することは、原料コストが非常に高いことと、残渣物から得られる動物飼料や植物肥料等が循環資源として再利用できるものの、ただ同然で取引されているために付加価値が低いという理由により、採算が合わず非現実的であった。したがって、出発原料としては、高価なデンプン質含有穀物を使用するのではなく、廃木材等のセルロース系廃棄物を用いると、経済的にも安く生産することができる。 Focusing on the above starting materials, producing ethanol from edible grains (rice, wheat, soybeans, sugarcane, etc.) planted in Japan is very expensive and can be obtained from residues. Although animal feeds and plant fertilizers can be reused as recyclable resources, they are unprofitable and unrealistic because they are traded as they are and their added value is low. Therefore, if cellulosic waste such as waste wood is used as a starting material instead of expensive starch-containing grains, it can be economically produced.

しかしながら、上記廃木材等のセルロース系廃棄物を用いることについても、現在、研究開発段階であり、また、わが国で商業的なエタノール生産を行うにあたって継続的・恒常的に原料調達が可能であるか等の問題点がある。
特表昭56−501311号公報
However, the use of cellulosic waste such as waste wood is currently in the research and development stage, and is it possible to procure raw materials continuously and constantly for commercial ethanol production in Japan? There are problems such as.
JP-T 56-501311

本発明は上記問題点にかんがみ、わが国で商業的なエタノール生産を行うにあたって継続的・恒常的に原料調達が可能であり、かつ、エタノール生産における副産物である二酸化炭素を有効活用するとともに、副産物である残渣物から付加価値の高い食品素材を製造することが可能なエタノールの生産方法及びその製造施設を提供することを技術的課題とする。 In view of the above problems, the present invention can continuously and constantly procure raw materials for commercial ethanol production in Japan, and can effectively use carbon dioxide, which is a by-product in ethanol production, as a by-product. It is a technical problem to provide an ethanol production method and a production facility thereof capable of producing a food material with high added value from a certain residue.

上記課題を解決するため本発明は、精米工場における無洗米化処理工程で回収される研ぎ汁に麹菌を接種して液化・糖化させるとともに、酵母を添加してアルコール発酵させてエタノールを生産するエタノール製造工程と、前記精米工場で回収される米糠等の副産物に、前記エタノール製造工程で生産されたエタノール又は二酸化炭素を利用して機能性成分を抽出する機能性食品製造工程と、を備えるという技術的手段を講じた。 In order to solve the above-mentioned problems, the present invention is an ethanol that inoculates koji mold collected in the washing-free rice treatment process in a rice mill and liquefies and saccharifies it, and also adds yeast to produce alcohol by alcohol fermentation. Technology that includes a production process and a functional food production process for extracting functional components using ethanol or carbon dioxide produced in the ethanol production process as a by-product such as rice bran recovered in the rice mill Took appropriate measures.

また、前記精米工場の精米工程で生じた米糠などの外皮を利用してガス化発電を行うガス化発電工程を備えるとよい。 Moreover, it is good to provide the gasification electric power generation process which performs gasification electric power generation using hulls, such as a rice bran produced in the rice polishing process of the said rice mill.

そして、前記ガス化発電工程で発電した電気を前記精米工程、無洗米化処理工程、エタノール製造工程及び機能性食品製造工程にそれぞれ送電するとともに、前記ガス化発電工程で生じた排熱を、前記エタノール製造工程で使用する熱源に利用するとよい。 And while transmitting electricity generated in the gasification power generation process to the rice milling process, washing-free rice treatment process, ethanol production process and functional food production process, respectively, the waste heat generated in the gasification power generation process, It may be used as a heat source used in the ethanol production process.

本発明のエタノールの製造方法によれば、精米工場における無洗米化処理工程で回収される研ぎ汁を用いてエタノールを製造することができるので、近年の無洗米の急速な需要拡大により継続的、かつ、恒常的に、しかも安価に原料調達が可能となる。また、研ぎ汁は多数のデンプン粒子を含有するものであり、廃木材等のセルロース系廃棄物と比較しても容易に液化・糖化するため、不純物が少なく高濃度のエタノールを製造することが可能となる。また、研ぎ汁は液状であるために加水分解処理や粉砕処理が不要となる。さらに、精米工場で回収される米糠等の副産物とエタノール製造工程で生産されたエタノール又は二酸化炭素とを利用して、機能性成分を抽出して付加価値の高い食品素材を製造することが可能であり、エタノールを生産する際の採算性が飛躍的に向上する。 According to the method for producing ethanol of the present invention, ethanol can be produced using the sharpened juice collected in the washing-free rice treatment step in the rice mill, so that the demand for washing-free rice has increased rapidly in recent years. In addition, raw materials can be procured constantly and inexpensively. In addition, sharpening juice contains a large number of starch particles, and it is easily liquefied and saccharified compared to cellulosic waste such as waste wood, so it is possible to produce high-concentration ethanol with less impurities. It becomes. Further, since the sharpening juice is in a liquid state, hydrolysis and pulverization are not required. Furthermore, by using by-products such as rice bran recovered at the rice mill and ethanol or carbon dioxide produced in the ethanol production process, it is possible to extract functional ingredients and produce food materials with high added value. Yes, the profitability when producing ethanol is dramatically improved.

さらに、前記精米工場の精米工程で生じた米糠などの外皮を利用してガス化発電を行うガス化発電工程を備え、該ガス化発電工程で発電した電気を前記精米工程、無洗米化処理工程、エタノール製造工程及び機能性食品製造工程にそれぞれ送電するとともに、前記ガス化発電工程で生じた排熱を、前記エタノール製造工程で使用する熱源に利用して、外皮を循環資源として利用することができる。 Furthermore, it comprises a gasification power generation process that performs gasification power generation using an outer skin such as rice bran produced in the rice milling process of the rice mill, and the electricity generated in the gasification power generation process is converted into the rice milling process and the washing-free rice processing process. In addition to transmitting power to the ethanol production process and the functional food production process, the waste heat generated in the gasification power generation process can be used as a heat source to be used in the ethanol production process, and the outer skin can be used as a circulation resource. it can.

本発明のエタノールの製造方法は、出発原料として精米工場における無洗化処理工程からの研ぎ汁が用いられる。本発明者らは、炊飯時に研ぐ必要のない無洗化処理米が、近年、急速に需要拡大されていることにより、その副産物である研ぎ汁が継続的、かつ、恒常的に、しかも安価に原料調達が可能であることを見出した。また、研ぎ汁は多数のデンプン粒子を含有するものであり、廃木材等のセルロース系廃棄物と比較しても容易に液化・糖化するため、不純物が少なく高濃度のエタノールを製造することが可能であることを見出した。 In the method for producing ethanol of the present invention, sharpening juice from a non-washing process in a rice mill is used as a starting material. The inventors of the present invention have made rapid progress in demand for washing-free treated rice that does not need to be sharpened during rice cooking. It was found that raw materials can be procured. In addition, sharpening juice contains a large number of starch particles, and it is easily liquefied and saccharified compared to cellulosic waste such as waste wood, so it is possible to produce high-concentration ethanol with less impurities. I found out.

以下、本発明の実施の形態を図面を参照して説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図1は本発明のエタノールの製造方法の工程を示すブロック図であり、図1を参照しながら本発明のエタノールの製造方法を説明する。 FIG. 1 is a block diagram showing the steps of the method for producing ethanol of the present invention. The method for producing ethanol of the present invention will be described with reference to FIG.

図1の工程1は、大規模穀物乾燥調製貯蔵施設であり、荷受された高水分の籾を、粗選、乾燥、貯留を行った後、籾摺機1に供給される。籾摺機1により原料籾が籾摺・精製されると、玄米は工程2の精米工場に出荷され、副産物となる籾殻は工程6のガス化発電設備に供給される。工程2の精米工場で使用される精米機2は、研削式精米機、摩擦式精米機、ブラシロールによる研磨式精米機、湿式摩擦式精米機など各種精米機を使用することができる。また、湿式摩擦式精米機を扱わない場合、精米機2の前工程に、玄米に対して2%重量の水を添加後、常温で5分間テンパリングを行う加水工程を設けるとよい。 Step 1 in FIG. 1 is a large-scale grain drying preparation storage facility, and after the coarsely picked, dried, and stored high-moisture rice cake received is supplied to the huller 1. When the raw rice cake is crushed and refined by the rice huller 1, the brown rice is shipped to the rice mill in step 2, and the rice husk as a by-product is supplied to the gasification power generation facility in step 6. Various rice milling machines such as a grinding rice mill, a friction rice mill, a polishing rice mill using a brush roll, and a wet friction rice mill can be used as the rice mill 2 used in the rice mill in step 2. Moreover, when not handling a wet friction type | formula rice mill, it is good to provide the watering process which performs tempering for 5 minutes at normal temperature after adding 2% weight water with respect to brown rice in the front process of the rice mill 2.

ブラシロールによる研磨式精米機を用いた場合、ブラシロールの仕様としては、ブラシ素材がSUS304,ひねり線、線径が0.6mm、ブラシ長が25mmのものを使用するとよい。これにより、通常の突起部を有する摩擦式精穀ロールに比べて、胚乳回収率が向上し、砕米発生率が減少することが分かった(下表参照)。

Figure 2009050195
When a polishing type rice mill using a brush roll is used, the brush roll should be made of SUS304, a twisted wire, a wire diameter of 0.6 mm, and a brush length of 25 mm. As a result, it was found that the endosperm recovery rate was improved and the broken rice generation rate was reduced as compared with a friction type cereal roll having a normal protrusion (see the table below).
Figure 2009050195

そして、前記精米機2の副産物となる糠及び胚芽は工程4に供給され、精品となる白米は、ロータリシフタ又は色彩選別機からなる精選機3を経て無洗米製造装置4に供給される。そして、該無洗米製造装置4の副産物となる研ぎ汁は、まず、麹菌が投入されている発酵タンク5Aに供給されて液化され、次いで、発酵タンク5Bに供給されて糖化が行われる。発酵タンク5A,5Bでは、アミラーゼを分泌する麹菌が研ぎ汁のデンプン質を溶かして液化・糖化が行われて糖化液が作成される。この製法に限らず、特殊な酵母を用いて、麹菌によりデンプン質を糖化する工程を省略することも可能である。また、精選機3により精選された微砕粒を研ぎ汁に混合して処理することも可能である。次に、この糖化液は、工程3の酵母菌が投入されている発酵タンク6に供給されてアルコール発酵が行われる。 Then, the rice bran and germ as by-products of the rice mill 2 are supplied to the step 4, and the white rice as the refined product is supplied to the washing-free rice production apparatus 4 through the refiner 3 comprising a rotary shifter or a color sorter. Then, the sharpening soup that is a by-product of the washing-free rice production apparatus 4 is first supplied to the fermentation tank 5A in which koji molds are introduced and liquefied, and then supplied to the fermentation tank 5B for saccharification. In the fermentation tanks 5A and 5B, the koji mold that secretes amylase dissolves the starch of the sharpened juice and is liquefied and saccharified to produce a saccharified solution. Not only this manufacturing method but also using a special yeast, it is possible to omit the step of saccharifying starch with gonococcus. Moreover, it is also possible to mix and process the finely pulverized granule selected by the refiner 3 with the sharpening juice. Next, this saccharified solution is supplied to the fermentation tank 6 in which the yeast of step 3 is introduced, and alcohol fermentation is performed.

発酵タンク6では、酵母が糖化されたデンプン質を発酵してアルコールを生ずる働きをする。発酵タンク6Bから取り出されたエキスは、エタノール含有アルコールであり、次の蒸留装置7に供給される。蒸留装置7では、加熱蒸気を利用することによって、エタノール含有アルコールを熱して蒸留処理を行い、高濃度のエタノールが得られ、工業用エタノール、燃料用エタノールとして提供される。 In the fermentation tank 6, the yeast functions to ferment the saccharified starch and produce alcohol. The extract taken out from the fermentation tank 6 </ b> B is ethanol-containing alcohol and is supplied to the next distillation apparatus 7. In the distillation apparatus 7, by using heated steam, the ethanol-containing alcohol is heated to perform a distillation treatment to obtain high-concentration ethanol, which is provided as industrial ethanol and fuel ethanol.

図1の工程4は、前記工程2の精米機2で生じた副産物から付加価値の高い健康食品等を製造するための機能性食品製造工程を示す。 Step 4 in FIG. 1 shows a functional food production process for producing high-value-added health foods and the like from the by-products produced in the rice milling machine 2 in the above-mentioned process 2.

該機能性食品製造工程では、精米機2から取り分けた糠及び胚芽がそれぞれ油回収機8A,8Bに供給される。該油回収機8A,8Bは圧搾式の搾油機でよく、米糠油や胚芽油を得ることができる。次に、搾油された米糠油、胚芽油及びそれらの搾り粕(かす)はそれぞれの精油装置9A,9Bに供給される。精油装置9A,9Bには、二酸化炭素が送給されており、該二酸化炭素の性状としては、液体状態又は超臨界状態のものを使用することができる。この二酸化炭素は脱脂用抽出溶剤と使用するもので、n-ヘキサンを使用しないので、無害であり、また、食品中に灯油様の臭いが付着することもない。脱脂用抽出溶媒としては、これらに限定されることなく、例えば、前記エタノール製造工程で得られたエタノールを使用することもできる。 In the functional food manufacturing process, the rice bran and germ separated from the rice mill 2 are supplied to the oil recovery machines 8A and 8B, respectively. The oil recovery machines 8A and 8B may be compression type oil presses, and can obtain rice bran oil or germ oil. Next, the squeezed rice bran oil, germ oil, and those squeezed straws are supplied to the respective essential oil devices 9A and 9B. Carbon dioxide is supplied to the essential oil devices 9A and 9B. As the properties of the carbon dioxide, those in a liquid state or a supercritical state can be used. This carbon dioxide is used as an extraction solvent for degreasing and does not use n-hexane, so it is harmless and no kerosene-like odor is attached to the food. The extraction solvent for degreasing is not limited to these, and for example, ethanol obtained in the ethanol production process can also be used.

前記精油装置9A,9Bでは、米糠油及び胚芽油が得られ、これらは血液中のコレステロールを減少させるというγ-オリザノールが含有した健康食品、医薬品、化粧品、食品用油として提供される。一方、二酸化炭素により脱脂された搾り粕(かす)のうち、脱脂糠は微粉砕機10に、脱脂胚芽は機能性成分抽出機11にそれぞれ供給される。前記微粉砕機10により粉砕された脱脂糠は、配合飼料を主に、漬物等の食品用粉末、肥料等として提供される。機能性成分抽出機11に供給された脱脂胚芽は、酵素処理、エタノール抽出等によりγ-アミノ酪酸、フィチン酸、イノシトール、ビタミンB1といった機能性成分を抽出し、濃縮・乾燥・粉末化処理を経て、健康食品として提供される。 In the essential oil devices 9A and 9B, rice bran oil and germ oil are obtained, and these are provided as health foods, pharmaceuticals, cosmetics and food oils containing γ-oryzanol, which reduces cholesterol in the blood. On the other hand, among the pomace degreased with carbon dioxide, the degreased koji is supplied to the pulverizer 10 and the degreased germ is supplied to the functional component extractor 11. The defatted lees pulverized by the fine pulverizer 10 are provided mainly as a mixed feed, as food powder such as pickles, fertilizer and the like. The defatted germ supplied to the functional component extractor 11 extracts functional components such as γ-aminobutyric acid, phytic acid, inositol, and vitamin B1 by enzymatic treatment, ethanol extraction, etc., and undergoes concentration, drying, and powdering treatment. Provided as a health food.

図1の工程5は、前記発酵タンク5A,5B及び6の副産物である二酸化炭素を回収し、前記工程4に供給して再利用するための炭酸ガス回収・再利用装置である。エタノールを製造する際に発生する二酸化炭素を、単に大気に逃がさずに再利用する技術として、化学薬品に転換する方法及び石油化学製品の生産に転換する方法は公知であるが、機能性食品製造工程で使用することは知られていない。 Step 5 in FIG. 1 is a carbon dioxide recovery / reuse device for recovering carbon dioxide, which is a byproduct of the fermentation tanks 5A, 5B, and 6, and supplying it to the step 4 for reuse. Methods for converting carbon dioxide generated when ethanol is produced into chemicals and petrochemical products are known as technologies for simply reusing carbon dioxide without letting it escape to the atmosphere. It is not known for use in the process.

図1の工程6は、前記籾摺機1の副産物である籾殻を回収し、ガス化発電機12の燃料として用いるガス化発電工程である。該ガス化発電機12は前記工程1乃至工程5の電気をまかなうことが可能であり、また、発電に伴い発生する排熱は、前記エタノール製造工程の蒸留装置7において使用する熱源に利用することができ、籾殻を循環資源として再利用することができる。 Step 6 in FIG. 1 is a gasification power generation step in which rice husks, which are by-products of the rice huller 1, are recovered and used as fuel for the gasification generator 12. The gasification generator 12 can cover the electricity of the steps 1 to 5, and the exhaust heat generated by the power generation is used as a heat source used in the distillation apparatus 7 in the ethanol production step. The rice husk can be reused as a recycling resource.

図2は本発明のエタノールの製造施設に適用される穀物乾燥調製施設の概略図である。穀物乾燥調製施設は、収穫された高水分の生籾を受け入れる荷受ホッパ13と、藁屑等の夾雑物を除去する粗選機14と、粗選された生籾を計量する計量機16と、生籾を一時貯蔵する貯蔵タンク19と、籾を乾燥する乾燥機22とにより主要部が構成される。符号26は間隙サイロであって、乾燥開始直後の籾をテンパリングするもので、籾が設定水分に乾燥されるまでは前記乾燥機22と該間隙サイロ26との間を循環しながらの乾燥が行われる。符号25は間隙サイロ26に併設された貯留サイロであって、籾が設定水分にまで乾燥された後に該貯留サイロ25に貯留されることになる。 FIG. 2 is a schematic view of a grain drying preparation facility applied to the ethanol production facility of the present invention. The grain drying preparation facility includes a receiving hopper 13 that receives the harvested high moisture ginger, a roughing machine 14 that removes impurities such as sawdust, a weighing machine 16 that measures the coarsely picked ginger, A main part is composed of a storage tank 19 for temporarily storing the ginger and a dryer 22 for drying the ginger. Reference numeral 26 denotes a gap silo that tempers the soot immediately after the start of drying, and drying is performed while circulating between the dryer 22 and the gap silo 26 until the soot is dried to the set moisture. Is called. Reference numeral 25 denotes a storage silo provided alongside the gap silo 26 and is stored in the storage silo 25 after the soot is dried to the set moisture.

設定水分まで乾燥された籾は、搬出用コンベア27、切換弁28により貯留サイロ25から取り出され、籾摺調製工程に搬送される。籾摺調製工程には、前述の籾摺機1と揺動式の穀粒選別機29とが設けられている。籾摺機1に籾が供給されると、籾殻と玄米とに分離され、副産物となる籾殻は前記ガス化発電工程に供給される。一方、籾摺機1により摺り落とされた玄米と籾との混合物は揺動式選別機29に供給され、該揺動式選別機29において玄米と、籾と、籾と玄米の混合物とに選別される。選別後の玄米は次工程の精米機2に供給されるが、籾は籾摺機1に返還されて再籾摺りが行われ、混合物は揺動式選別機29に返還されて再選別が行われることになる。 The soot dried to the set moisture is taken out of the storage silo 25 by the carry-out conveyor 27 and the switching valve 28 and is transported to the hull preparation process. In the hulling preparation process, the hulling machine 1 described above and the swinging grain sorter 29 are provided. When rice bran is supplied to the rice huller 1, the rice husk is separated into rice husk and brown rice, and the rice husk as a by-product is supplied to the gasification power generation process. On the other hand, the mixture of brown rice and rice bran that has been scraped off by the rice huller 1 is supplied to a swinging sorter 29, which sorts it into brown rice, rice bran, and a mixture of rice bran and brown rice. Is done. The unpolished rice after the sorting is supplied to the rice mill 2 in the next process, but the rice bran is returned to the rice grinder 1 and re-milled, and the mixture is returned to the swinging sorter 29 and re-sorted. It will be.

精米機2に供給された玄米は白米と糠・胚芽とに分離され、副産物の糠・胚芽が前記機能性食品製造工程に供給され、白米は次工程に至る。白米は、ロータリシフタ又は色彩選別機からなる精選機3を経て無洗米製造装置4に供給される。そして、該無洗米製造装置4の副産物となる研ぎ汁は、前記エタノール製造工程に供給されることになる。 The brown rice supplied to the rice mill 2 is separated into white rice and koji / germ, and the by-product koji / germ is supplied to the functional food manufacturing process, and the white rice reaches the next process. The white rice is supplied to the non-washed rice production apparatus 4 through a selection machine 3 composed of a rotary shifter or a color sorter. And the sharpening soup which becomes a by-product of this washing-free rice manufacturing apparatus 4 will be supplied to the said ethanol manufacturing process.

図1の穀物調製加工工程1及び精米工程2において、原料籾55トンを籾摺、精米を行うと、精白米40トン、糠2.9トン、胚芽1.3トンが得られた。精選機3にて得られる微細粒は0.2トンであり、無洗米製造装置4にて排出される研ぎ汁1リットル中に含まれる米デンプン量は約2%であり、40トンの精白米を無洗化処理して得られた研ぎ汁から生じる米デンプン量は0.8トンである。この微細粒と研ぎ汁とを合わせた米デンプン量1トンが液化・糖化・発酵・蒸留処理されることになる。 In the grain preparation processing step 1 and the rice polishing step 2 in FIG. 1, when 55 tons of raw rice koji was milled and polished, 40 tons of polished rice, 2.9 tons of rice bran, and 1.3 tons of germ were obtained. The fine grain obtained by the clarifier 3 is 0.2 tons, the amount of rice starch contained in 1 liter of the polishing juice discharged from the washing-free rice production apparatus 4 is about 2%, and 40 tons of polished rice is not used. The amount of rice starch produced from the sharpening juice obtained by washing is 0.8 ton. One ton of rice starch, which is a combination of this fine grain and sharpening juice, is liquefied, saccharified, fermented and distilled.

エタノール製造工程2で得られたエタノールは、0.425キロリットル、工程5で回収された二酸化炭素は、0.325トンであった。機能性食品製造工程4において、糠2.9トン及び胚芽1.3トンを搾油・脱脂・精製処理を行うと、米糠油・胚芽油0.5トン、機能性成分0.3トン、食品用粉末3.7トンが得られた。 The ethanol obtained in the ethanol production process 2 was 0.425 kiloliters, and the carbon dioxide recovered in the process 5 was 0.325 tons. In functional food production process 4, 2.9 tons of cocoons and 1.3 tons of germs were subjected to oil extraction / defatting / refining treatment to obtain 0.5 tons of rice bran oil / germ oil, 0.3 tons of functional ingredients, and 3.7 tons of food powder.

機能性成分の粉末100グラムあたりの成分含有量は表2のようになった。

Figure 2009050195
The component content per 100 grams of powder of the functional component is as shown in Table 2.
Figure 2009050195

本発明のエタノールの製造方法の工程を示すブロック図である。It is a block diagram which shows the process of the manufacturing method of ethanol of this invention. 本発明のエタノールの製造施設に適用される穀物乾燥調製施設の概略図である。It is the schematic of the grain drying preparation facility applied to the ethanol manufacturing facility of this invention.

符号の説明Explanation of symbols

1 籾摺機
2 精米機
3 精選機
4 無洗米製造装置
5 発酵タンク
6 発酵タンク
7 蒸留装置
8 油回収機
9 精油装置
10 微粉砕機
11 機能性成分抽出機
12 ガス化発電機
13 荷受ホッパ
14 粗選機
15 揚穀機
16 計量機
17 揚穀機
18 搬入用コンベア
19 貯蔵タンク
20 排出用コンベア
21 揚穀機
22 乾燥機
23 揚穀機
24 搬入用コンベア
25 貯留サイロ
26 間隙サイロ
27 搬出用コンベア
28 切換弁
29 揺動選別機
DESCRIPTION OF SYMBOLS 1 Rice huller 2 Rice mill 3 Refiner 4 Wash-free rice production apparatus 5 Fermentation tank 6 Fermentation tank 7 Distillation apparatus 8 Oil recovery machine 9 Oil refiner 10 Fine grinder 11 Functional component extractor 12 Gasification generator 13 Load receiving hopper 14 Coarse selection machine 15 Graining machine 16 Weighing machine 17 Graining machine 18 Carry-in conveyor 19 Storage tank 20 Discharge conveyor 21 Graining machine 22 Dryer 23 Graining machine 24 Carry-in conveyor 25 Storage silo 26 Gap silo 27 Carry-out conveyor 28 Switching valve 29 Oscillating sorter

Claims (4)

精米工場における無洗米化処理工程で回収される研ぎ汁に麹菌を接種して液化・糖化させるとともに、酵母を添加してアルコール発酵させてエタノールを生産するエタノール製造工程と、
前記精米工場で回収される米糠等の副産物に、前記エタノール製造工程で生産されたエタノール又は二酸化炭素を利用して機能性成分を抽出する機能性食品製造工程と、
を備えたことを特徴とするエタノールの製造方法。
An ethanol production process for inoculating the koji mold collected in the washing-free rice treatment process in the rice mill and liquefying and saccharifying it, adding yeast and fermenting alcohol to produce ethanol,
A functional food production process for extracting functional components using ethanol or carbon dioxide produced in the ethanol production process as a by-product such as rice bran recovered at the rice mill,
A method for producing ethanol, comprising:
前記精米工場の精米工程で生じた米糠などの外皮を利用してガス化発電を行うガス化発電工程を備えてなる請求項1のエタノールの製造方法。   The method for producing ethanol according to claim 1, further comprising a gasification power generation step of performing gasification power generation using a hull such as rice bran produced in the rice milling process of the rice mill. 前記ガス化発電工程で発電した電気を前記精米工程、無洗米化処理工程、エタノール製造工程及び機能性食品製造工程にそれぞれ送電するとともに、前記ガス化発電工程で生じた排熱を、前記エタノール製造工程で使用する熱源に利用してなる請求項2記載のエタノールの製造方法。   The electricity generated in the gasification power generation process is transmitted to the rice milling process, the washing-free rice treatment process, the ethanol production process, and the functional food production process, respectively, and the waste heat generated in the gasification power generation process is transmitted to the ethanol production process. The method for producing ethanol according to claim 2, wherein the method is used as a heat source used in the process. 荷受された玄米を、粗選・精選を行った後、精米に加工し、さらに無洗米化処理を行って無洗米に仕上げる精米工場内に、
前記無洗米化処理によって生じる研ぎ汁に麹菌を接種して液化・糖化させるとともに、酵母を添加してアルコール発酵させた後、蒸留処理するエタノール製造装置と、
前記精米及び無洗米から取り分けた米糠などの外皮を圧搾し、圧搾後の搾り粕(かす)を脱脂処理して機能性成分を抽出する機能性食品製造装置と、
を備えたことを特徴とするエタノールの製造施設。
In the milled rice mill, the unpolished rice that has been received is subjected to coarse selection and selection, then processed into polished rice, and then subjected to washing-free rice processing to finish washing-free rice.
An ethanol production device that inoculates the koji mold produced by the non-washing rice treatment and liquefies and saccharifies it, and after adding yeast and alcoholic fermentation, an ethanol production apparatus for distillation treatment;
A functional food production apparatus that squeezes the hulls such as rice bran separated from the polished rice and non-washed rice, and degreases the squeezed rice bran after squeezing to extract functional components;
An ethanol production facility comprising:
JP2007219305A 2007-08-27 2007-08-27 Ethanol production method and production facility Expired - Fee Related JP5257570B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2007219305A JP5257570B2 (en) 2007-08-27 2007-08-27 Ethanol production method and production facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2007219305A JP5257570B2 (en) 2007-08-27 2007-08-27 Ethanol production method and production facility

Publications (2)

Publication Number Publication Date
JP2009050195A true JP2009050195A (en) 2009-03-12
JP5257570B2 JP5257570B2 (en) 2013-08-07

Family

ID=40501869

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2007219305A Expired - Fee Related JP5257570B2 (en) 2007-08-27 2007-08-27 Ethanol production method and production facility

Country Status (1)

Country Link
JP (1) JP5257570B2 (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10276753A (en) * 1997-02-10 1998-10-20 Tax Adm Agency Production of liquors from uncooked raw material
JP2002059118A (en) * 2000-08-23 2002-02-26 Nobuyuki Hayashi Method of pressure hydrothermally decomposing plant based biomass and system therefor
JP2002255784A (en) * 2001-03-02 2002-09-11 Oriza Yuka Kk Composition for beautiful skin
JP2002265377A (en) * 2001-03-14 2002-09-18 Oriza Yuka Kk Physiologically active composition derived from rice bran
JP2007044689A (en) * 2005-07-15 2007-02-22 Yasuo Morikawa Method for producing methane gas using ligneous biomass, and method for producing electricity utilizing the method
US20070094930A1 (en) * 2005-11-01 2007-05-03 Prm Energy Systems, Inc. Particulate waste product gasification system and method
JP2007325564A (en) * 2006-06-09 2007-12-20 Satake Corp Method and facility for producing ethanol

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10276753A (en) * 1997-02-10 1998-10-20 Tax Adm Agency Production of liquors from uncooked raw material
JP2002059118A (en) * 2000-08-23 2002-02-26 Nobuyuki Hayashi Method of pressure hydrothermally decomposing plant based biomass and system therefor
JP2002255784A (en) * 2001-03-02 2002-09-11 Oriza Yuka Kk Composition for beautiful skin
JP2002265377A (en) * 2001-03-14 2002-09-18 Oriza Yuka Kk Physiologically active composition derived from rice bran
JP2007044689A (en) * 2005-07-15 2007-02-22 Yasuo Morikawa Method for producing methane gas using ligneous biomass, and method for producing electricity utilizing the method
US20070094930A1 (en) * 2005-11-01 2007-05-03 Prm Energy Systems, Inc. Particulate waste product gasification system and method
JP2007325564A (en) * 2006-06-09 2007-12-20 Satake Corp Method and facility for producing ethanol

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
JPN6012064956; 桝谷英樹: 'アミラーゼ・マルターゼおよび酵母のバイオリアクターを用いたデンプンからのエタノール生成とその教材化' 化学と教育 Vol.51(9), 2003, p.557-559 *

Also Published As

Publication number Publication date
JP5257570B2 (en) 2013-08-07

Similar Documents

Publication Publication Date Title
Veljković et al. Biodiesel production from corn oil: A review
US9567612B2 (en) Corn degerming ethanol fermentation processes
Jin et al. Integrated processing of plant-derived waste to produce value-added products based on the biorefinery concept
US8080274B2 (en) Dry corn mill as a biomass factory
US8449728B2 (en) System for production of ethanol and co-products with fractionation of feedstock and solvent washing of fermentation product
US20070099278A1 (en) Production of biodiesel from combination of corn (maize) and other feed stocks
AU731717B2 (en) A method of utilizing vegetal biomass, and a screw press to carry out said method
US20070014905A1 (en) Starchy material processed to produce one or more products comprising starch, ethanol, sugar syrup, oil, protein, fiber, gluten meal, and mixtures thereof
Cheng et al. Economics of plant oil recovery: A review
CN101795578A (en) The dry classification of corn separates
WO2019079491A1 (en) Method of and system for producing a syrup with the highest concentration using a dry mill process
US20140273140A1 (en) Simultaneous Food And Fuel Corn Refining
CN101080483A (en) Integrated corn processing
US20140273138A1 (en) Simultaneous Food And Fuel Corn Refining
CN101565187B (en) Aroma type spirit distiller grain comprehensive utilization method
JP4911426B2 (en) Ethanol production method and production facility
Agrawal et al. Recycling potential of brewer's spent grains for circular biorefineries
JP6002550B2 (en) Ethanol production facility and residue reduction method
CN100343218C (en) Method for extracting omega 6 polyunsaturated fatty acid from plant seeds
JP5257570B2 (en) Ethanol production method and production facility
RU2162103C1 (en) Method of production of ethyl alcohol from grain stock
RU2443781C1 (en) Method for production of ethyl alcohol from grain raw material
Huda Increased Oil Recovery from Distillers Dried Grains with Solubles and Whole Stillage
Du Toit Triticale grain fermentation for production of bio ethanol and animal feed
Singh et al. Process and engineering effects on DDGS products–Present and future

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20100716

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20121212

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20130123

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20130327

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20130409

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20160502

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 5257570

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees