JP2009159913A - Induction-heating apparatus for bioethanol production process - Google Patents
Induction-heating apparatus for bioethanol production process Download PDFInfo
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- JP2009159913A JP2009159913A JP2008002271A JP2008002271A JP2009159913A JP 2009159913 A JP2009159913 A JP 2009159913A JP 2008002271 A JP2008002271 A JP 2008002271A JP 2008002271 A JP2008002271 A JP 2008002271A JP 2009159913 A JP2009159913 A JP 2009159913A
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- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/12—Bioreactors or fermenters specially adapted for specific uses for producing fuels or solvents
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- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M47/00—Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
- C12M47/12—Purification
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Abstract
Description
本発明は、バイオエタノール製造プロセスに用いる誘導加熱装置に関するものである。 The present invention relates to an induction heating apparatus used in a bioethanol production process.
最近、環境問題や原油依存脱却の点から、砂糖キビやトウモロコシ、廃木材などを原料とするバイオエタノールの利用が進められている。図4はこのようなバイオエタノールを製造する一般的な工程を示すもので、砂糖キビ、甜菜、小麦やコーン等の穀物あるいは木の先端部、枝、根っ子や廃木材などの原料を細分し、細分した原料を蒸煮し、それに酵素を加えて所定の温度(約75℃)に加熱して糖化する。 In recent years, bioethanol using sugar millet, corn, waste wood, etc. as a raw material has been promoted from the viewpoint of environmental problems and the escape from crude oil dependence. FIG. 4 shows a general process for producing such bioethanol, and subdivides raw materials such as sugar millet, sugar beet, grains such as wheat and corn, or tree tips, branches, roots and waste wood. Then, the subdivided raw material is cooked, an enzyme is added thereto, and the mixture is heated to a predetermined temperature (about 75 ° C.) for saccharification.
その後、所定の温度(約30℃)に冷却し、酵母を加えその温度に保持して発酵させる。発酵後、100℃以上に加熱蒸留してエタノールが作成される。なお、砂糖キビや甜菜を原料とする場合には、その原料を搾って糖蜜を作り、その糖蜜を約30℃に保持して発酵させ、そのあと遠心分離機で酵母を取り出し、その残りを100℃以上に加熱蒸留してエタノールを作成する場合もある。 Then, it cools to predetermined | prescribed temperature (about 30 degreeC), yeast is added, it is made to maintain at that temperature, and it ferments. After fermentation, ethanol is produced by heating to 100 ° C or higher. In addition, when sugar millet or sugar beet is used as a raw material, the raw material is squeezed to make molasses, the molasses is kept at about 30 ° C. and fermented, and then the yeast is taken out with a centrifuge and the rest is taken as 100 In some cases, ethanol is produced by distillation by heating to a temperature higher than C.
このように、バイオエタノールの製造においては、加熱、冷却、発酵温度保持、加熱が繰り替えされ、これらを実行するために熱交換器やボイラーが用いられている。ボイラーの燃料としては、化石燃料(主に重油)あるいは木屑やバイオエタノール精製工程で出る粕(例えば砂糖キビの搾り粕)が使用されている。 Thus, in the production of bioethanol, heating, cooling, fermentation temperature retention, and heating are repeated, and a heat exchanger and a boiler are used to perform these. As fuel for the boiler, fossil fuel (mainly heavy oil) or wood chips and firewood produced in the bioethanol refining process (for example, sugar milled rice cake) are used.
しかし、このような熱交換器やボイラーの使用では、熱の損失が多く効率良く熱を利用することが困難であり、また、化石燃料とする場合には周囲の環境を汚染する恐れがあり、木屑やバイオエタノール精製工程で出る粕をボイラーの燃料とする場合にはバイオエタノール精製する原料の無駄使いとなるといった問題があった。 However, with the use of such heat exchangers and boilers, it is difficult to use heat efficiently because there is a lot of heat loss, and there is a risk of contaminating the surrounding environment when using fossil fuel, In the case where wood waste or firewood produced in the bioethanol purification process is used as boiler fuel, there is a problem that the raw material for bioethanol purification is wasted.
本発明が解決しようとする課題は、バイオエタノールの製造に際し、エネルギーの利用効率を高くするとともに、原料の無駄使いや周囲の環境の汚染を抑制できるようにし、斯かる問題を解消する点にある。 The problem to be solved by the present invention is to increase the efficiency of energy use in the production of bioethanol, to suppress wasteful use of raw materials and contamination of the surrounding environment, and to solve such problems. .
本発明は、鉄心と、前記鉄心に巻回された誘導コイルと、前記誘導コイルに巻回され、前記誘導コイルの交流励磁電流より発熱する貫通孔が形成された導電性加熱パイプとを有し、前記導電性加熱パイプの貫通孔内にバイオエタノールを精製する原料を注入して前記原料を所定の温度に加熱保温してなることを特徴とする。 The present invention includes an iron core, an induction coil wound around the iron core, and a conductive heating pipe wound around the induction coil and formed with a through hole that generates heat from an AC excitation current of the induction coil. The raw material for purifying bioethanol is injected into the through hole of the conductive heating pipe, and the raw material is heated and kept at a predetermined temperature.
本発明では、バイオエタノールの製造に際し、バイオエタノール精製する原料の加熱や保温を熱効率がほぼ100%に近い誘導加熱で行うので省エネルギーを図ることができる。また、熱源は電気であることからクリーンであり、熱交換器やボイラーを使用する場合のような原料の無駄使いや周囲の環境の汚染の発生を抑制することができる。さらに、誘導加熱は温度管理がしやすいため加熱温度の変更や所定の温度を維持することが簡単かつ迅速にできる。 In the present invention, in the production of bioethanol, it is possible to save energy since the raw material to be purified by bioethanol is heated and kept warm by induction heating with a thermal efficiency of nearly 100%. Further, since the heat source is electricity, it is clean, and wasteful use of raw materials and contamination of the surrounding environment as in the case of using a heat exchanger or a boiler can be suppressed. Furthermore, since induction heating is easy to manage the temperature, it is possible to easily and quickly change the heating temperature and maintain a predetermined temperature.
バイオエタノールの製造に際し、エネルギーの利用効率を高くするとともに、原料の無駄使いや周囲の環境の汚染を抑制できるようにする目的を、誘導加熱されるパイプ内にバイオエタノール精製する原料を注入し、その原料の加熱や保温を行うことにより実現した。 In the production of bioethanol, in order to increase the efficiency of energy use and to suppress wasteful use of raw materials and contamination of the surrounding environment, the raw material for bioethanol purification is injected into a pipe that is heated by induction, This was achieved by heating and keeping the raw material.
以下、本発明に係る実施例について図1を参照して説明する。図1は実施例に係るバイオエタノール製造プロセス用誘導加熱装置の上面図(a)と側面図(b)、図2は誘導加熱部の構成を示す部分断面図、図3は結線図である。図1ないし図3において、1は三脚鉄心、2は三脚の脚鉄心にそれぞれ巻回された誘導コイル、3は各誘導コイルの外周に巻回された導電性加熱パイプである。 An embodiment according to the present invention will be described below with reference to FIG. FIG. 1 is a top view (a) and a side view (b) of an induction heating apparatus for a bioethanol production process according to an embodiment, FIG. 2 is a partial sectional view showing the configuration of an induction heating unit, and FIG. 3 is a connection diagram. 1 to 3, 1 is a tripod iron core, 2 is an induction coil wound around each of the tripod leg iron cores, and 3 is a conductive heating pipe wound around the outer periphery of each induction coil.
三脚鉄心1のそれぞれは上部と下部のヨーク鉄心1a、1bに固定金具4により固定されており閉磁路構成とされている。各誘導コイル2の端部は端子台11の端子(UX、VY、WZ)に接続されており、この実施例では各誘導コイル2は三相の交流電流により励磁できるようにされている。各誘導コイル2が交流電流で励磁されると鉄心1に交番磁束が発生し、その磁束により導電性加熱パイプ3に電流が誘起し、その電流で導電性加熱パイプ3はジュール発熱する。導電性加熱パイプ3の温度は各誘導コイル2に印加する交流電圧を制御することにより簡単に調整することができる。
Each of the tripod iron cores 1 is fixed to the upper and lower yoke iron cores 1a and 1b by a
誘導コイル2の外周に巻回された各導電性加熱パイプ3の両端にはフランジが形成され、このフランジに連結用のパイプを適宜連結する。図示例では、一端部の誘導コイル2の外周に巻回された導電性加熱パイプ3の一端は、注入パイプ5に連結され、他端は中央部の誘導コイル2の外周に巻回された導電性加熱パイプ3の一端とパイプ6で連結され、中央部の誘導コイル2の外周に巻回された導電性加熱パイプ3の他端は、他端部の誘導コイル2の外周に巻回された導電性加熱パイプ3の一端とパイプ7で連結され、他端部の誘導コイル2の外周に巻回された導電性加熱パイプ3の他端は開口している。導電性加熱パイプ3の適宜位置に、バイオエタノール精製時に発生する粕を取出す弁8が設けられている。
A flange is formed at both ends of each
図1は、図4に示すバイオエタノール精製する原料を糖化する場合に使用する誘導加熱装置を示している。この場合、注入パイプ5に枝別れした分岐パイプ9が連結され、分岐パイプ9の一方はバイオエタノール精製する原料を、他方は酵素をそれぞれ注入するパイプ10、11に連結されている。
FIG. 1 shows an induction heating apparatus used when the raw material to be purified by bioethanol shown in FIG. 4 is saccharified. In this case, the
このように構成した誘導加熱装置は、バイオエタノール精製する原料と酵素とを注入パイプ5を経て、各導電性加熱パイプ3内に送り込み糖化に必要な温度に加熱保温する。糖化後、弁8を開き残り粕を取出し、糖化された原料を導電性加熱パイプ3の他端の開口から送り出す。送り出された原料は冷却機で所定の温度(発酵に適する温度)に冷却し、発酵工程へ移送し、発酵後温度を上げて蒸留してバイオエタノール抽出する。
The induction heating apparatus configured as described above feeds the raw material for bioethanol purification and the enzyme through the
なお、図1はバイオエタノール精製する原料を糖化する場合に使用する誘導加熱装置を示すものであるが、本例の誘導加熱装置は、発酵、蒸留工程においても使用することができる。また、誘導加熱装置に冷却機能を負荷すれば、一貫してバイオエタノールを精製することができる。 FIG. 1 shows an induction heating apparatus used when saccharifying a raw material to be purified by bioethanol, but the induction heating apparatus of this example can also be used in fermentation and distillation processes. Moreover, if a cooling function is loaded on the induction heating device, bioethanol can be purified consistently.
以上の実施例では、三脚の脚鉄心のそれぞれに誘導コイルと導電性加熱パイプを巻回して誘導加熱装置を構成しているが、一脚の脚鉄心に誘導コイルと導電性加熱パイプを巻回して誘導加熱装置を構成してもよい。 In the above embodiments, the induction heating device is configured by winding the induction coil and the conductive heating pipe around each of the tripod leg iron cores. However, the induction coil and the conductive heating pipe are wound around the monopod leg iron core. An induction heating device may be configured.
1 鉄心
2 誘導コイル
3 導電性加熱パイプ
4 固定金具
5,6,7
パイプ
8 排出弁
11 端子台
1 Iron Core 2
Pipe 8
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JP2013053760A (en) * | 2011-09-01 | 2013-03-21 | Tokuden Co Ltd | Superheated steam generating device |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH01233474A (en) * | 1988-03-14 | 1989-09-19 | Ricoh Co Ltd | Electrophotographic process |
WO1998029685A1 (en) * | 1996-12-26 | 1998-07-09 | Kabushiki Kaisha Seta Giken | Superheated steam generator |
JP2003202158A (en) * | 2002-01-04 | 2003-07-18 | Shizuo Minagawa | System for heating or warming liquid or fluid material instantly or in very short time period by electromagnetic induction heating system |
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Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH01233474A (en) * | 1988-03-14 | 1989-09-19 | Ricoh Co Ltd | Electrophotographic process |
WO1998029685A1 (en) * | 1996-12-26 | 1998-07-09 | Kabushiki Kaisha Seta Giken | Superheated steam generator |
JP2003202158A (en) * | 2002-01-04 | 2003-07-18 | Shizuo Minagawa | System for heating or warming liquid or fluid material instantly or in very short time period by electromagnetic induction heating system |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013053760A (en) * | 2011-09-01 | 2013-03-21 | Tokuden Co Ltd | Superheated steam generating device |
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