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1. 发明申请

WO2010139854A1 METHOD OF CARRYING OUT PYROLYSIS AND PYROLYSIS APPARATUS 审中-公开
标题翻译：实施热解和热解设备的方法
公开(公告)号：WO2010139854A1
公开(公告)日：2010-12-09
申请号：PCT/FI2010/050443
申请日：2010-06-01
申请人： UPM-KYMMENE CORPORATION , METSO POWER OY , JOKELA, Pekka , LEHTO, Jani
发明人： JOKELA, Pekka , LEHTO, Jani
IPC分类号： C10B49/22 , C10B53/02 , C10B49/16 , F23C10/00
CPC分类号： C10B49/22 , C10B49/10 , C10B49/16 , C10B53/00 , C10B53/02 , C10B55/10 , C10B57/10 , C10G1/02 , C10G9/32 , F23C10/002 , F23G2201/303 , F23G2203/501 , F23G2203/504 , F23G2206/10 , Y02E50/14
摘要： The invention relates to a method of carrying out pyrolysis process in a pyrolysis reactor (4) for solid fuel to produce pyrolysis oil. The method comprises supplying solid fuel into a drying zone in the pyrolysis reactor (4) for removing moisture containing gases, drying the solid fuel in the drying zone and extracting the moisture containing gases re- moved from the solid fuel out of the pyrolysis reactor (4), passing the dried solid fuel from the drying zone to the pyrolysis zone of the pyrolysis reactor (4), pyrolyzing the dried solid fuel for separating pyrolysis gases from the dried solid fuel and conducting the pyrolysis gases from the pyrolysis reactor (4) to a condenser (8) for producing pyrolysis oil.
摘要翻译：本发明涉及在用于固体燃料产生热解油的热解反应器（4）中进行热解过程的方法。该方法包括将固体燃料供应到热解反应器（4）的干燥区中，用于除去含湿气体，干燥干燥区中的固体燃料并将从固体燃料中排出的含水气体从热解反应器中提取出来 4），将干燥的固体燃料从干燥区传送到热解反应器（4）的热解区，热解干燥的固体燃料以从干燥的固体燃料中分离出热解气体并将热解气体从热解反应器（4）导入，到用于产生热解油的冷凝器（8）。

2. 发明申请

WO2012113979A1 TORREFACTION PROCESS INTEGRATED IN A FLUIDIZED BED REACTOR 审中-公开
标题翻译：集成在流化床反应器中的转矩过程
公开(公告)号：WO2012113979A1
公开(公告)日：2012-08-30
申请号：PCT/FI2012/050162
申请日：2012-02-20
申请人： METSO POWER OY , UPM-KYMMENE CORPORATION , LEHTO, Jani , JOKELA, Pekka
发明人： LEHTO, Jani , JOKELA, Pekka
IPC分类号： C10L9/08 , C10B49/04 , C10B49/22 , C10B53/02
CPC分类号： C10L9/083 , C10B49/04 , C10B49/22 , C10B53/02 , C10L5/447 , Y02E50/10 , Y02E50/14 , Y02E50/15 , Y02E50/30
摘要： The use of a fluidized bed boiler as a heat source for a torrefaction process is presented. The fluidized bed boiler (100, 150) comprises means (210, 106, 156) for heating heat transfer medium (112, 212), means (213, 302) for transferring the heat transfer medium to a torrefaction reactor (200, 300, 400, 500), and means (215, 313) for receiving heat transfer medium from the torrefaction reactor. Furthermore, a method for torrefying biomass (202) is presented. In the method, biomass is heated to a torrefaction temperature in a torrefaction reactor by means of heat transfer medium, and the biomass is kept at the torrefaction temperature for a retention time. Further in the method, the heat transfer medium (112, 212) is heated by a fluidized bed boiler (100, 150), the heat transfer medium (112, 212) is transferred from the fluidized bed boiler (100, 150) to the torrefaction reactor (200, 300, 400, 500), and the heat transfer medium is transferred from the torrefaction reactor to the fluidized bed boiler. Furthermore, a torrefaction system is presented, which comprises a torrefaction reactor (200, 300, 400, 500) for torrefying biomass (202) into biocoal (204), means for conveying biomass to the torrefaction reactor, and heat transfer medium (112, 212) for heating the biomass. The torrefaction system further comprises a fluidized bed boiler (100, 150) for heating the heat transfer medium, means (213, 302) for conveying the heat transfer medium from the fluidized bed boiler (100, 150) to the torrefaction reactor (200, 300, 400, 500), and means (215, 313) for conveying the heat transfer medium from the torrefaction reactor to the fluidized bed boiler (100, 150). Both in the method and in the system, torrefaction gas or bed material from the fluidized bed boiler may be used as the heat transfer medium.
摘要翻译：提出了使用流化床锅炉作为烘焙过程的热源。流化床锅炉（100,150）包括用于加热传热介质（112,212）的装置（210,106,156），用于将热传递介质传送到烘焙反应器（200,300）的装置（213,302） 400，500）和用于从烘焙反应器接收传热介质的装置（215,313）。此外，提出了一种用于烘焙生物质（202）的方法。在该方法中，通过传热介质将生物量加热到烘焙反应器中的烘焙温度，并将生物质保持在烘焙温度下保留时间。此外，在该方法中，传热介质（112,212）由流化床锅炉（100,150）加热，传热介质（112,212）从流化床锅炉（100,150）转移到烘焙反应器（200,300,400,500），并且传热介质从烘焙反应器转移到流化床锅炉。此外，提供了一种烘焙系统，其包括用于将生物质（202）焙烧成生物炭（204）的烘焙反应器（200,300,400,500），用于将生物质输送到烘焙反应器的装置和传热介质（112， 212）用于加热生物质。烘焙系统还包括用于加热传热介质的流化床锅炉（100,150），用于将热传递介质从流化床锅炉（100,150）输送到烘焙反应器（200,150）的装置（213,302） 300,400,500）和用于将热传递介质从焙烧反应器输送到流化床锅炉（100,150）的装置（215,313）。在方法和系统中，可以使用来自流化床锅炉的烘焙气体或床料作为传热介质。

3. 发明申请

WO2009135999A1 METHOD AND EQUIPMENT FOR TREATMENT OF BLACK LI QUOR AT PULP MILL 审中-公开
标题翻译：用于处理粉碎机中的黑色李子的方法和设备
公开(公告)号：WO2009135999A1
公开(公告)日：2009-11-12
申请号：PCT/FI2009/050362
申请日：2009-05-05
申请人： METSO POWER OY , LEHTO, Jani , KUUKKANEN, Kari , HONKOLA, Timo
发明人： LEHTO, Jani , KUUKKANEN, Kari , HONKOLA, Timo
IPC分类号： D21C11/04 , D21C11/12
CPC分类号： D21C11/04 , D21C11/06 , D21C11/12 , D21C11/125 , Y02P40/44 , Y02P70/24
摘要： The invention relates to a method and equipment for treatment of black liquor at a pulp mill in order to recover chemicals and energy contained therein. In the invention, the black liquor is pyrolyzed in a pyrolysis reactor (4), the formed gaseous components are forwarded for utilization and the solids are mixed with water, whereby the formed solids are returned to a lime burning kiln (1) and the sodium-hydroxide-containing liquid is returned to the pulp cooking process.
摘要翻译：本发明涉及在纸浆厂处理黑液以回收其中所含的化学物质和能量的方法和设备。在本发明中，黑液在热解反应器（4）中被热解，所形成的气体组分被转运用于使用，固体与水混合，由此将形成的固体返回到石灰燃烧窑（1）含氢氧化物的液体返回到纸浆蒸煮过程。

4. 发明申请

US20120073185A1 METHOD OF CARRYING OUT PYROLYSIS AND PYROLYSIS APPARATUS 有权
标题翻译：携带热解法和热解法的方法
公开(公告)号：US20120073185A1
公开(公告)日：2012-03-29
申请号：US13375351
申请日：2010-06-01
申请人： Pekka Jokela , Lehto Jani
发明人： Pekka Jokela , Lehto Jani
IPC分类号： C10L1/00 , C10L5/00
CPC分类号： C10B49/22 , C10B49/10 , C10B49/16 , C10B53/00 , C10B53/02 , C10B55/10 , C10B57/10 , C10G1/02 , C10G9/32 , F23C10/002 , F23G2201/303 , F23G2203/501 , F23G2203/504 , F23G2206/10 , Y02E50/14
摘要： The invention relates to a method of carrying out pyrolysis process in a pyrolysis reactor (4) for solid fuel to produce pyrolysis oil. The method comprises supplying solid fuel into a drying zone in the pyrolysis reactor (4) for removing moisture containing gases, drying the solid fuel in the drying zone and extracting the moisture containing gases re-moved from the solid fuel out of the pyrolysis reactor (4), passing the dried solid fuel from the drying zone to the pyrolysis zone of the pyrolysis reactor (4), pyrolyzing the dried solid fuel for separating pyrolysis gases from the dried solid fuel and conducting the pyrolysis gases from the pyrolysis reactor (4) to a condenser (8) for producing pyrolysis oil.
摘要翻译：本发明涉及在用于固体燃料的热解反应器（4）中进行热解过程以产生热解油的方法。该方法包括将固体燃料供应到热解反应器（4）中的干燥区中，用于除去含湿气体，干燥干燥区中的固体燃料并将从固体燃料中重新移出的含水气体从热解反应器中提取出来 4），将干燥的固体燃料从干燥区传送到热解反应器（4）的热解区，热解干燥的固体燃料以从干燥的固体燃料中分离热解气体并将热解气体从热解反应器（4）导入，到用于产生热解油的冷凝器（8）。

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