CN101828089A - 间接加热干燥装置、被干燥物的间接加热干燥方法、以及固态燃料的制造方法及制造装置 - Google Patents
间接加热干燥装置、被干燥物的间接加热干燥方法、以及固态燃料的制造方法及制造装置 Download PDFInfo
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- F26B11/04—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis
- F26B11/0445—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis having conductive heating arrangements, e.g. heated drum wall
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- 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
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- 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
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- Drying Of Solid Materials (AREA)
Abstract
Description
比较例1 | 实施例1 | |
干燥工序的方式 | 干燥机一台(以往) | 干燥机串联两台(本发明) |
载气流入方式 | 对流 | 前段:并流后段:对流 |
干燥机入口部的状态 | 高露点、低产品温度、低气体温度,因此产生附着气体温度:大约140℃气体露点:大约125℃产品温度:大约135℃ | 前段:低露点、高气体温度,因此不产生附着气体温度:大约210℃气体露点:大约80℃产品温度:135℃后段:高产品温度、高气体温度,因此不产生附着气体温度:大约210℃气体露点:大约110℃产品温度:215℃ |
集尘机的方式 | 湿式洗涤器气体温度:大约140℃气体露点:大约125℃收集粉尘作为浆料回收,因此需要再处理 | 前段、后段:干式袋式集尘器前段:气体温度:大约210℃气体露点:大约140℃后段:气体温度:大约210℃气体露点:大约110℃收集粉尘返回干燥机,制成产品 |
比较例1 | 实施例1 | |
产品的含液率 | 使用一台干燥机进行恒速干燥与减速干燥,因此存在产生短路的现象,在大约2~1wt%WB变动 | 后段为减速干燥区间专用的干燥机,因此稳定在大约1wt%WB |
干燥机尺寸导热面积 | φ3800×33mL导热面积大约2200m2 | 前段:φ3050×20mL导热面积:大约1100m2后段:φ3050×20mL导热面积:大约600m2 |
载气流量 | 大约9800Nm3/h | 前段:大约4800Nm3/h后段:大约3900Nm3/h |
气体加热器蒸汽量 | 大约1300kg/h | 前段:大约550kg/h后段:大约500kg/h |
Claims (7)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2007269278A JP4979538B2 (ja) | 2007-10-16 | 2007-10-16 | 間接加熱乾燥装置、被乾燥物の間接加熱乾燥方法、ならびに固形燃料の製造方法および製造装置 |
JP2007-269278 | 2007-10-16 | ||
PCT/JP2008/064907 WO2009050939A1 (ja) | 2007-10-16 | 2008-08-21 | 間接加熱乾燥装置、被乾燥物の間接加熱乾燥方法、ならびに固形燃料の製造方法および製造装置 |
Publications (2)
Publication Number | Publication Date |
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CN101828089A true CN101828089A (zh) | 2010-09-08 |
CN101828089B CN101828089B (zh) | 2012-07-04 |
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CN2008801117655A Active CN101828089B (zh) | 2007-10-16 | 2008-08-21 | 间接加热干燥装置、被干燥物的间接加热干燥方法、以及固态燃料的制造方法及制造装置 |
Country Status (6)
Country | Link |
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US (1) | US8580000B2 (zh) |
JP (1) | JP4979538B2 (zh) |
CN (1) | CN101828089B (zh) |
AU (1) | AU2008313118B2 (zh) |
DE (1) | DE112008002740B4 (zh) |
WO (1) | WO2009050939A1 (zh) |
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CN104276415A (zh) * | 2014-09-15 | 2015-01-14 | 常州利普金属制品有限公司 | 粉体表面改性机 |
CN104603565A (zh) * | 2012-09-11 | 2015-05-06 | 月岛机械株式会社 | 间接加热型旋转干燥机 |
CN104781625A (zh) * | 2012-11-16 | 2015-07-15 | 株式会社神户制钢所 | 粒状物的间接加热干燥方法、改性煤的制造方法、间接加热型干燥装置以及改性煤制造装置 |
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CN108387069A (zh) * | 2017-01-24 | 2018-08-10 | 李柱先 | 褐煤干燥系统及褐煤干燥方法 |
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US20110041393A1 (en) | 2011-02-24 |
CN101828089B (zh) | 2012-07-04 |
WO2009050939A1 (ja) | 2009-04-23 |
AU2008313118B2 (en) | 2011-03-31 |
JP2009097783A (ja) | 2009-05-07 |
JP4979538B2 (ja) | 2012-07-18 |
DE112008002740T5 (de) | 2010-08-26 |
US8580000B2 (en) | 2013-11-12 |
AU2008313118A1 (en) | 2009-04-23 |
DE112008002740B4 (de) | 2019-02-21 |
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