WO2009104311A1 - 固形燃料及び固形燃料の製造方法 - Google Patents
固形燃料及び固形燃料の製造方法 Download PDFInfo
- Publication number
- WO2009104311A1 WO2009104311A1 PCT/JP2008/069952 JP2008069952W WO2009104311A1 WO 2009104311 A1 WO2009104311 A1 WO 2009104311A1 JP 2008069952 W JP2008069952 W JP 2008069952W WO 2009104311 A1 WO2009104311 A1 WO 2009104311A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- solid fuel
- beer
- beer lees
- heating
- fuel
- Prior art date
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Definitions
- ⁇ Koji known as a solid fuel, is used as a fuel for cooking or warming, and is an important fuel source in stone pots and wood stoves for baking pizza and bread.
- the raw wood used as the raw material for firewood contains nearly 50% of moisture, and it is necessary to dry the moisture to around 15% in order to burn it as firewood.
- burning soot that is not sufficiently dry there is a problem that a lot of tar or soot is generated.
- the standard management only the management to the extent that the length of the trees is divided is made, the quality is non-uniform, and the variation of each firewood is very large, so it is difficult to adjust the heating and the like.
- sawdust is processed into a bowl-shaped molded body as a raw material and used as a fuel.
- These are characterized in that moisture is controlled during processing and that a molded product of the same size can be produced industrially, and therefore, when used as a bag, it is easy to make adjustments such as heating and reducing.
- sawdust made from sawdust is a recycled product, sawdust is originally made from raw wood. Therefore, it is a resource that can be obtained only after cutting trees useful for CO 2 reduction.
- the volatile components unique to living trees generate unpleasant smoke that can be seen by the eyes.
- the hopper portion 20 is formed in a drawn shape whose diameter dimension gradually decreases toward the lower side, and is connected to a charging port 11a formed in the housing main body 11 of the stirring molding portion 10.
- the housing body 11 of the agitation molding unit 10 is formed in a cylindrical shape, and a hemispherical tip housing 12 is fastened to one end of the housing body 11 in the horizontal direction (X-axis direction). It is fixed via a bolt 13.
- a rotor 14 is rotatably accommodated in the tip housing 12, and an outer blade 14a having a twist angle is formed on the outer surface of the rotor 14.
- the outer blade 14 a of the rotor 14 is twisted in the opposite direction with respect to the inner blade 12 a of the tip housing 12.
- the rotating shaft 14b of the rotor 14 extends in the X-axis direction and is rotationally driven by a driving force transmitted from the motor 40 illustrated in FIG.
- the drive mechanism of the rotor 14 will be described later.
- the screw shaft 16a of the tip screw 16 is arranged coaxially with the rotating shaft 14b of the rotor 14, and the rotor 14 and the tip screw 16 rotate integrally by the driving force transmitted from the motor 40.
- R1-R2 is preferably 0.3 to 0.5 mm, more preferably 0.3 mm.
- a heating cylinder 17 is provided concentrically with the sleeve 15. The heat generating cylinder 17 generates heat by heat transferred from a heat source (not shown).
- the gear box 30 contains a first gear 31 and a second gear train 32 that engages with the first gear 31.
- the second gear train 32 is connected to the rotation shaft 14 b of the rotor 14, and the rotor 14 rotates in accordance with the rotation operation of the second gear train 32.
- the supply speed of the beer koji to the housing body 11 is preferably 100 kg / h or more, more preferably 130 kg / h or more. This is because when the supply speed is 100 kg / h or less, the heating time of the solid fuel located inside the sleeve 15 becomes long, and the surface of the solid fuel is carbonized.
- rate of beer lees can be suitably changed according to the apparatus structure of a manufacturing apparatus from a viewpoint that the surface of a solid fuel is not carbonized.
- the amount of transfer per rotation of the rotor 14 can be increased.
- the amount of beer lees supplied from the tip housing 12 to the sleeve 15 can be limited.
- the heating temperature of the sleeve 15 can be appropriately changed according to the device configuration of the solid fuel production device. In this case, it is possible to visually identify the occurrence of cracks in the solid fuel and the occurrence of a thin skin-like burn on the surface. Therefore, the optimum heating temperature can be experimentally derived by adjusting the heating temperature of the sleeve 15 while visually observing the surface of the solid fuel discharged from the sleeve 15.
- the flash points of the example and the comparative example were 217 ° C. and 246 ° C., respectively, and it was found that the flash point was lower than that of the comparative example and the ignition was easy.
- the IMO burning rate experiment was measured at the Safety Engineering Laboratory, Sumika Analysis Center, Ehime Works.
- the test conditions were a temperature of 27 ° C. and a humidity of 84%.
- the following criteria were adopted for the judgment method. That is, when the combustion speed is 2.0 mm / sec or more, the combustion risk is evaluated as high, and when the combustion speed is higher than 0 mm / sec and lower than 2.0 mm / sec, the combustion risk is high. Was evaluated as medium, and when the combustion speed was 0 mm / sec, the combustion risk was evaluated as small. Also, a test piece is deposited on a heat insulating plate (thickness 10 mm, thermal conductivity 0.1 W / m ⁇ K or less at 0 ° C.
- Table 7 shows data of the examples, where the vertical axis indicates the component amount and the horizontal axis indicates time.
- Table 8 shows data of the comparative example, where the vertical axis indicates the component amount and the horizontal axis indicates time.
Abstract
Description
(変形例)
上述のビール粕とともに、コーヒー豆の焙煎粕、役目の終えた酒造用樽(酒樽、ワイン樽、ウィスキー樽、等)を粉砕した粒子、果汁の絞り粕(りんご、みかん等)、ビール醸造後のホップ粕を攪拌成形部10に装入して、固形燃料に香り付けを行ってもよい。
(実施例)
実施例を示して本発明を具体的に説明する。
引火点については、消防法危険物確認試験実施マニュアルに準じて行った。具体的には、引火点測定器具としてセタ密閉式の測定器具を使用した。試験は、(株)住化分析センター 愛媛事業所 安全工学研究室で行った。実施例の試験条件は、その温度が26℃、その湿度が58%、その気圧が1008hPa、その試験実施日が2008年8月27日であった。比較例の試験条件は、その温度が24℃、その湿度が51%、その気圧が1010hPa、その試験実施日が2008年8月25日であった。実施例の試験結果を表1に示し、比較例の試験結果を表2に示した。
発熱量については、JIS M 8814マニュアルに準じて行った。試験は、(株)住化分析センター 愛媛事業所 安全工学研究室で行った。試験条件は、温度が22℃、湿度が78%、気圧が1007hPaであった。実施例の試験結果を表3に示し、比較例の試験結果を表4に示した。
IMO燃焼速度は、(株)住化分析センター 愛媛事業所 安全工学研究室で行った。試験条件は、温度が27℃、湿度が84%であった。判定方法については、下記の基準を採用した。すなわち、燃焼速度が2.0mm/sec以上である場合には、燃焼危険性を大と評価し、燃焼速度が0mm/secよりも大きく2.0mm/secよりも小さい場合には、燃焼危険性を中と評価し、燃焼速度が0mm/secである場合には、燃焼危険性を小と評価した。また、断熱板(厚さ10mm、0℃における熱伝導率0.1W/m・K以下)上に、試験片を全長250mm、幅20mm、高さ10mmのプリズム型に堆積させ、その一端を液化石油ガスの着火器具を用いて着火した。そして、反応域が120mm進んだ後、そこからさらに100mm燃焼が進行する時間を測定した。試験は、実施例及び比較例ともに、6回繰り返した。実施例の試験結果を表5に示し、比較例の試験結果を表6に示す。
(揮発成分について)
実施例及び比較例の固形燃料をJIS K 7217の燃焼装置で燃焼させ、燃焼時に発生したガスをテドラーバックに捕集し、この捕集したガスをガスクロマトグラフ法(GC/TCD)で測定した。燃焼ガス発生装置として杉山元医理器製のPCT-1を使用した。温度は750℃に設定した。支燃ガスとして空気を使用した。支燃ガス供給量は0.5(L/min)に設定した。ガスクロマトグラフとして島津製作所のGC-14Bを使用した。その分析結果を表7及び表8に示す。表7は実施例のデータであり、縦軸は成分量、横軸は時間を示している。表8は比較例のデータであり、縦軸は成分量、横軸は時間を示している。
11 ハウジング本体
12 先端ハウジング
13 締結ボルト
14 ロータ
15 スリーブ
16 先端スクリュー
Claims (2)
- 炭化しないように加熱処理されたビール粕の粒子を含む固形燃料。
- ビール粕を攪拌しながら加熱する第1のステップと、
前記第1のステップで攪拌されたビール粕を加熱しながら固形燃料の形状に圧縮成形する第2のステップとを含み、
前記第2のステップにおいて、前記ビール粕を炭化させないように加熱することを特徴とする固形燃料の製造方法。
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2009519076A JP4465411B2 (ja) | 2008-02-18 | 2008-10-31 | 固形燃料の製造装置及び製造方法 |
US12/918,018 US20100325946A1 (en) | 2008-02-18 | 2008-10-31 | Solid fuel and method of producing solid fuel |
CN2008801273032A CN101970620A (zh) | 2008-02-18 | 2008-10-31 | 固体燃料及固体燃料的制造方法 |
EP08872724A EP2258816A4 (en) | 2008-02-18 | 2008-10-31 | SOLID FUEL AND METHOD FOR PRODUCING SOLID FUEL |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2008-035984 | 2008-02-18 | ||
JP2008035984 | 2008-02-18 |
Publications (1)
Publication Number | Publication Date |
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WO2009104311A1 true WO2009104311A1 (ja) | 2009-08-27 |
Family
ID=40985205
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2008/069952 WO2009104311A1 (ja) | 2008-02-18 | 2008-10-31 | 固形燃料及び固形燃料の製造方法 |
Country Status (5)
Country | Link |
---|---|
US (1) | US20100325946A1 (ja) |
EP (1) | EP2258816A4 (ja) |
JP (1) | JP4465411B2 (ja) |
CN (1) | CN101970620A (ja) |
WO (1) | WO2009104311A1 (ja) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102191100A (zh) * | 2010-04-09 | 2011-09-21 | 神华集团有限责任公司 | 一种生物质型煤 |
JP5530042B1 (ja) * | 2014-01-08 | 2014-06-25 | 新日鉄住金エンジニアリング株式会社 | 炭化物の製造方法及び炭化物の製造システム |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102041125A (zh) * | 2011-01-17 | 2011-05-04 | 泸州品创科技有限公司 | 燃料棒及其制备方法 |
CN102206527B (zh) * | 2011-05-04 | 2013-08-21 | 邹属民 | 一种生物质燃料及其制备方法 |
RU2634645C2 (ru) * | 2014-11-19 | 2017-11-02 | Татьяна Евгеньевна Белькова | Способ и устройство для сушки дров |
CN106957771A (zh) * | 2017-05-19 | 2017-07-18 | 贵州省仁怀市茅台镇郑氏酒业有限公司 | 酱香型白酒的酿造工艺 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2000033496A (ja) | 1998-07-21 | 2000-02-02 | Asahi Breweries Ltd | ビール粕炭化用成型装置 |
JP2001241848A (ja) * | 2000-02-28 | 2001-09-07 | Asahi Breweries Ltd | ビール粕の乾燥処理システム |
JP2005140484A (ja) * | 2003-11-04 | 2005-06-02 | Yasunobu Yoshida | 循環式廃棄物の乾燥及び微粉化燃料システムの方法とその装置 |
Family Cites Families (8)
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DE3346378A1 (de) * | 1983-12-19 | 1985-04-04 | Manger, Karlheinz | Receyclingverfahren: hochdruckgepresste weinhefe (naturprodukt) unter entziehung der feuchtigkeit zu verwenden als alternativbrennstoff zu kohle,- brikett und oel |
US4863488A (en) * | 1986-06-13 | 1989-09-05 | Ube Industries, Ltd. | Solid fuels |
JPH08163977A (ja) * | 1994-12-15 | 1996-06-25 | Kitagawa Iron Works Co Ltd | 残飯などの有機物分解用担材 |
AT404253B (de) * | 1996-11-20 | 1998-10-27 | Steirerbrau Ag | Verfahren zum thermischen verwerten von biertrebern |
JP2001009317A (ja) * | 1999-07-02 | 2001-01-16 | Yamamoto Co Ltd | 粉砕装置 |
JP3954769B2 (ja) * | 2000-02-28 | 2007-08-08 | アサヒビール株式会社 | ビール粕の炭化処理システム |
JP2002180064A (ja) * | 2000-12-14 | 2002-06-26 | Takeji Motai | 人工炭及びその製造法 |
JP4288079B2 (ja) * | 2003-01-21 | 2009-07-01 | 株式会社北川鉄工所 | 圧縮微粉砕装置 |
-
2008
- 2008-10-31 US US12/918,018 patent/US20100325946A1/en not_active Abandoned
- 2008-10-31 WO PCT/JP2008/069952 patent/WO2009104311A1/ja active Application Filing
- 2008-10-31 EP EP08872724A patent/EP2258816A4/en not_active Withdrawn
- 2008-10-31 JP JP2009519076A patent/JP4465411B2/ja not_active Expired - Fee Related
- 2008-10-31 CN CN2008801273032A patent/CN101970620A/zh active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2000033496A (ja) | 1998-07-21 | 2000-02-02 | Asahi Breweries Ltd | ビール粕炭化用成型装置 |
JP2001241848A (ja) * | 2000-02-28 | 2001-09-07 | Asahi Breweries Ltd | ビール粕の乾燥処理システム |
JP2005140484A (ja) * | 2003-11-04 | 2005-06-02 | Yasunobu Yoshida | 循環式廃棄物の乾燥及び微粉化燃料システムの方法とその装置 |
Non-Patent Citations (2)
Title |
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SEARCH ON THE INTERNET, 30 October 2008 (2008-10-30), Retrieved from the Internet <URL:http://www..japan-hp.com/ksd_hako.html> |
See also references of EP2258816A4 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102191100A (zh) * | 2010-04-09 | 2011-09-21 | 神华集团有限责任公司 | 一种生物质型煤 |
JP5530042B1 (ja) * | 2014-01-08 | 2014-06-25 | 新日鉄住金エンジニアリング株式会社 | 炭化物の製造方法及び炭化物の製造システム |
Also Published As
Publication number | Publication date |
---|---|
CN101970620A (zh) | 2011-02-09 |
EP2258816A4 (en) | 2012-01-25 |
JP4465411B2 (ja) | 2010-05-19 |
JPWO2009104311A1 (ja) | 2011-06-16 |
US20100325946A1 (en) | 2010-12-30 |
EP2258816A1 (en) | 2010-12-08 |
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