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1.发明公开CONVERSION OF BIOMASS, ORGANIC WASTE AND CARBON DIOXIDE INTO SYNTHETIC HYDROCARBONS 审中-公开生物质，有机废弃物和二氧化碳转化为合成烃
公开(公告)号：EP3237585A1
公开(公告)日：2017-11-01
申请号：EP15871395.8
申请日：2015-12-22
IPC分类号： C10L1/04 , C01B3/34 , C07C1/04 , C10G1/00 , C10G2/00 , C10G50/00 , C12M1/00 , C12M1/107 , C12P3/00 , C12P5/02 , D21C1/02 , D21C1/10 , C02F11/04
CPC分类号： C10G2/34 , C10G2/32 , C12M21/04 , C12M21/12 , C12M23/58 , C12M43/00 , C12P3/00 , C12P5/023 , Y02E50/343 , Y02P30/30
摘要： A process and system for producing a synthetic hydrocarbon having a desired H/C ratio is disclosed. Organic material is biochemically digested in a two stage biodigester for separately producing a hydrogen containing biogas substantially free of methane in a first stage and a methane containing biogas in a second stage. The methane containing biogas is reformed in a first reformer to generate hydrogen gas and carbon monoxide gas, which are then combined in a mixer with the hydrogen containing biogas into a syngas in amounts to achieve in the syngas an overall H/C ratio substantially equal to the desired H/C ratio. The syngas is reacted with a catalyst in a second reformer, a Fischer-Tropsch (FT) reactor, to produce the hydrocarbon. Using a two stage biodigester allows for the generation of separate hydrogen and methane streams, a more economical generation of the FT syngas and reduced fouling of the FT catalyst.
摘要翻译： 公开了生产具有所需H / C比的合成烃的方法和系统。 在两级生物消化器中生物化学消化有机物质，用于在第一阶段分别生产基本上不含甲烷的含氢生物气和在第二阶段生产含甲烷的生物气。 含甲烷的沼气在第一重整器中重整以产生氢气和一氧化碳气体，然后在混合器中将含氢沼气混合成合成气，合成气的量达到合成气的总H / C比基本等于 所需的H / C比。 合成气在第二重整器，费托（FT）反应器中与催化剂反应以产生烃。 使用两级生物消化器允许产生分离的氢气和甲烷流，FT合成气的更经济的生成和FT催化剂的减少的污染。
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公开(公告)号：EP2833986A1
公开(公告)日：2015-02-11
申请号：EP13772219.5
申请日：2013-04-05
IPC分类号： B01D29/82
CPC分类号： B01D33/009 , B01D29/46 , B01D29/828 , B30B1/00 , B30B9/12 , B30B9/16 , B30B9/26 , B30B11/24
摘要： Disclosed is a solid/liquid separation apparatus including an extruder press combined with a solid/fluid separation module for separating fluid from a mass of solids compressed by the extruder at elevated pressures. The extruder includes two or more extruder screws with flighting intercalated at least along a part of the extruder barrel. The separation module forms a continuation of the barrel, receives the pressurized mass and at least a portion of the twin screws, and includes a filter pack consisting of a filter plate and a backer plate. The filter plate has a throughgoing filter slot extending away from a core opening and into the filter plate for directing fluid away from the core opening. The backer plate has a core opening shaped and sized equal to the barrel and defines a passage for guiding fluid collected in the filter slot to an exterior of the filter pack.
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公开(公告)号：EP2736615A1
公开(公告)日：2014-06-04
申请号：EP12817499.2
申请日：2012-07-20
IPC分类号： B01D1/26
摘要： A process for separation of solid and liquid components in a distillation whole stillage utilizing airless spray drying is disclosed, which is more efficient and economical than conventional processes. In the process, distillation whole stillage resulting from distillation of fermented biomass is first subjected to an evaporation step for separating the whole stillage into a condensate and a concentrate including water, dissolved solids and suspended solids. The concentrate is then subjected to airless steam spray drying for converting the concentrate into dried solids, steam and vapors. All steam and vapors resulting from the airless steam spray drying step are then redirected as energy source to a processing step upstream of the airless spray drying step. At least some of the steam generated in the airless spray drying step is airless steam.
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