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51. 发明申请

WO01062873A1 SHAFT-MELT GASIFIER AND A METHOD FOR THERMAL TREATMENT AND PROCESSING OF WASTE MATERIALS 审中-公开
标题翻译： BAY熔解了热处理和废物处置的碳水化合物和方法
公开(公告)号：WO01062873A1
公开(公告)日：2001-08-30
申请号：PCT/DE2001/000401
申请日：2001-01-31
IPC分类号： C10J3/16 , C10J3/26
CPC分类号： C10J3/26 , C10J3/16 , C10J2200/152 , C10J2300/0946 , C10J2300/0959
摘要： The invention relates to a method for thermal treatment and processing of waste materials of various types, consistency and composition, such as pollutant-loaded waste wood, old tyres, industrial/commercial waste, domestic waste and bulk waste and a shaft-melt gasifier for carrying out said method. The above is achieved, whereby the waste material is introduced into the high temperature zone (H), directly after burning in the shaft-melt gasifier. The organic components contained in the waste material react with oxygen here. The reaction products are sucked into the furnace along with the residual waste materials in a co-current flow. The incompletely combusted organic components of the waste materials undergo a pyrolytic decomposition. Pyrolytic coke is formed, which is burned with oxygen in the reducing/cracking zone (Z) and the raw gas sucked off between the zones (11) and (7).
摘要翻译：本发明涉及一种用于热处理和各种，一致性废料回收和组合物作为污染废木材，废轮胎，工业/商业废物，家庭和笨重，以及用于执行该方法的轴熔融气化炉的方法。这是通过废料实现在轴熔融气化炉的燃烧后直接引入高温区H. 这里，包含在废料的有机成分与氧气发生反应。反应产物被吸入与剩余的废料中的DC电力到炉。废物物质的未完全燃烧的有机成分都受到了热分解。它形成在与氧的还原/裂化区Z燃烧热解焦炭，并且这些区11和图7之间的原料气体被吸入关闭。

52. 发明申请

WO00058421A1 METHOD AND DEVICE FOR PRODUCING ENERGY OR METHANOL 审中-公开
标题翻译：方法和设备生产的节能或甲醇
公开(公告)号：WO00058421A1
公开(公告)日：2000-10-05
申请号：PCT/EP2000/002517
申请日：2000-03-22
IPC分类号： C07C29/151 , C10J3/00 , C10J3/04 , C10J3/16
CPC分类号： C10J3/04 , C07C29/1518 , C10J3/00 , C10J2300/1646 , C10J2300/1665 , C10J2300/1693 , C10K1/024 , Y02E50/18 , Y02P20/145 , Y10S123/12 , C07C31/04
摘要： The invention relates to a method for producing energy, comprising the following steps: 1) Burning of fuel in an internal combustion engine (12), thereby producing mechanical energy and a waste gas containing carbon dioxide and water vapour; 2) Reduction of the carbon dioxide and water vapour waste gas components in an environment (28) containing organic material into a synthesis gas which contains carbon monoxide and hydrogen; 3) Feeding the synthesis gas which was produced in step 2 to the internal combustion engine. In order to produce methanol, a methanol synthesis (44) is introduced between steps 2 and 3 of the inventive method.
摘要翻译：一种用于产生电力的步骤包括如下步骤：在内燃发动机（12 1）中燃烧燃料），以产生机械能和二氧化碳和水，2）减少排气成分的二氧化碳和水在含有机物区域的废气包含水蒸汽的（28）含有一氧化碳和氢，3）将在步骤2中在所述内燃发动机产生的合成气的合成气。以制造甲醇，甲醇合成（44）插入在本发明方法的步骤2和3之间。

53. 发明申请

WO99037738A1 A METHOD FOR PROCESSING SOLID MUNICIPAL WASTE 审中-公开
标题翻译：一种处理固体废物的方法
公开(公告)号：WO99037738A1
公开(公告)日：1999-07-29
申请号：PCT/FI1999/000045
申请日：1999-01-22
IPC分类号： F23G5/027 , C10J3/16 , C10J3/02
CPC分类号： C10J3/16 , C10J2300/0946 , C10J2300/0956 , C10J2300/0993 , C10J2300/1807 , Y02E20/12
摘要： The invention pertains to methods to process combustible solid municipal wastes (SMW), primarily highly humid ones, by means of pyrolysis and gasification of their organic part so as to produce liquid hydrocarbon products of pyrolysis and fuel gas, which are used for energy generation. The method can be used for environmentally friendly processing/disposal of poorly combustible wastes. SMW is charged in a gasifier reactor type of a shaft kiln, possibly together with a solid incombustible material, countercurrently to an oxygen-containing gasifying agent and combustible components of SMW are gasified. Smoke gases are introduced in the gasifying agent. The maximum temperature in the reactor is controlled within 800 to 1300 DEG C through variation of at least one of the following parameters, the mass fraction of oxygen in the gasifying agent a, and the mass fraction of incombustibles in the processed SMW b, and the mass fraction of combustibles in processed SMW c, while the ratio A = ab/c is maintained within 0.022 to 0.1.
摘要翻译：本发明涉及通过其有机部分的热分解和气化处理可燃性固体城市废物（SMW）的方法，主要是高度湿润的废物，以产生用于能量产生的热解和燃料气体的液体烃产物。该方法可用于环境友好的易燃易燃废物处理/处理。 SMW在气窑反应器类型的竖窑中，可能与固体不可燃材料一起，与含氧气化剂逆流，并将SMW的可燃组分气化。烟气引入气化剂中。反应器中的最高温度通过改变以下参数中的至少一个，气化剂a中的氧的质量分数和加工的SMW b中的不可燃物的质量分数来控制在800-1300℃，在加工的SMW c中可燃物的质量分数，而A = ab / c的比率保持在0.022至0.1之间。

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