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    • 3. 发明申请
    • PROCESS FOR THE EXTRACTION OF LIPIDS AND SUGARS FROM ALGAL BIOMASS
    • 从ALGAL BIOMASS提取脂肪和糖的方法
    • WO2015075630A1
    • 2015-05-28
    • PCT/IB2014/066130
    • 2014-11-18
    • ENI S.P.A.
    • MASSETTI, FeliciaCAPUANO, FedericoMEDICI, RobertoMIGLIO, Roberta
    • C11C1/10C12N1/12C12P19/00
    • C11B1/10C12N1/02C12N1/12C13K1/00C13K13/002C13K13/007Y02E50/13
    • Process for the extraction of lipids and sugars from algal biomass, which comprises: - producing an aqueous suspension of algal biomass; - bringing the pH of said aqueous suspension of algal biomass to a value higher than or equal to 10, preferably ranging from 10.2 to 12, obtaining an aqueous suspension of algal biomass at basic pH; - adding at least one anionic flocculant to said aqueous suspension of algal biomass at basic pH obtaining a concentrated algal biomass; - recovering said concentrated algal biomass; -subjecting said concentrated algal biomass to extraction of the lipids obtaining: (i) an organic phase comprising lipids; (ii) a semi-solid phase comprising a residue of said algal biomass; - subjecting said semi-solid phase (ii) to hydrolysis obtaining sugars. The lipids thus obtained can be advantageously used in the production of biodiesel or green diesel which can be used as such, or in a mixture with other fuels for motor vehicles. The sugars thus obtained can be advantageously used as carbon sources in fermentation processes for the production of lipids and also for the production of alcohols (e.g., ethanol, butanol). Said alcohols can be advantageously used as biofuels for motor vehicles or as components that can be added to fuels for motor vehicles.
    • 从藻类生物质中提取脂质和糖的方法,其包括: - 产生藻类生物质的水悬浮液; - 将藻类生物质的所述水性悬浮液的pH值提高到高于或等于10,优选为10.2至12的值,得到碱性pH下的藻类生物质的水悬浮液; - 在碱性pH下向藻类生物质的所述水性悬浮液中加入至少一种阴离子絮凝剂,得到浓缩藻类生物质; - 回收所述浓缩藻类生物质; - 将所述浓缩的藻类生物质引入所述脂质的提取中,获得:(i)包含脂质的有机相; (ii)包含所述藻类生物质的残余物的半固相; - 对所述半固相(ii)进行水解获得糖。 由此获得的脂质可以有利地用于生产生物柴油或绿色柴油,其可以原样使用,或与用于机动车辆的其它燃料的混合物。 由此获得的糖可有利地用作用于生产脂质的发酵方法中的碳源,也可用于生产醇(例如乙醇,丁醇)。 所述醇可以有利地用作机动车辆的生物燃料或作为机动车辆燃料的组分。
    • 4. 发明申请
    • WASTE SLUDGE INCINERATOR USING PYROLYSIS AND GASIFICATION, AND RELATIVE PROCESS
    • 使用溶解和气化的废弃物焚烧炉及相关工艺
    • WO2015049659A1
    • 2015-04-09
    • PCT/IB2014/065021
    • 2014-10-02
    • ENI S.P.A.
    • MASSETTI, FeliciaPISTELLI, Maria IlariaPINTI, Medardo
    • C02F11/10C10J3/00F23G5/00F23G5/027F23G5/04F23G5/20F23G5/46
    • F23G7/001C02F11/06C02F11/10C10J3/005C10J3/60C10J2200/158C10J2300/1246F23G5/006F23G5/027F23G5/0273F23G5/04F23G5/20F23G5/44F23G5/46F23G2201/101F23G2201/302F23G2201/303F23G2201/40F23G2203/211F23G2206/10F23G2209/12F23G2900/50001F23G2900/50201F23G2900/50204F23G2900/52001F23G2900/52002F23G2900/54402Y02W10/40
    • The present invention relates to reaction equipment for the treatment of organic and/or inorganic waste of refineries or petrochemical plants comprising: • - a drying and pyrolysis device (4) which rotates around its longitudinal, tilted rotation axis (A), • - a gasification device (6) which rotates around its longitudinal, horizontal rotation axis (B), • - a combustion device (14) comprising a burner (13) having a longitudinal horizontal axis (C), • - at least one settling chamber (15) for the collection of intermediate solid residues and the accumulation of intermediate gaseous reaction products, • - at least one outlet duct of the gaseous end-products (16), at least one outlet duct of the solid end-products (7), and at least one inlet duct of the feedstock (2) • - said combustion device (14), drying and pyrolysis device (4), gasification device (6) are physically separated and positioned on three different levels, • - the longitudinal rotation axis (A) of the drying and pyrolysis device (4) is tilted with respect to both the longitudinal rotation axis (B) of the gasification device (6) and also with respect to the longitudinal axis (C) of the combustion device (14), • - the longitudinal rotation axis (B) of the gasification device (6) is parallel to the longitudinal axis (C) of the combustion device (14), • - the combustion device (14) is in fluid communication with the drying and pyrolysis device (4), • - the drying and pyrolysis device (4) comprises, in its interior, a first indirect heat exchange device (3) in which the combustion fumes coming from the combustion device (14) flow, • - at least one settling chamber (15) in fluid communication with said drying and pyrolysis device (4) and with said gasification device (6) and with said combustion device (14), • - conveying means (5) are positioned in the settling chamber (15) and put the drying and pyrolysis device (4) in fluid communication with the gasification device, • - it comprises a second heat exchange device (12) in fluid communication with the first indirect heat exchange device (3) and the combustion device (14), • - it comprises means for the suction of the intermediate gaseous reaction products, said means being positioned in the settling chamber (15).
    • 本发明涉及用于处理炼油厂或石油化工厂的有机和/或无机废物的反应设备,包括: - 围绕其纵向倾斜旋转轴线(A)旋转的干燥和热解装置(4), - - 一种燃烧装置(14),包括具有纵向水平轴线(C)的燃烧器(13), - 至少一个沉降室(15) ),用于收集中间固体残余物和中间气体反应产物的积聚, - 至少一个气体终产物(16)的出口管道,至少一个固体终产物(7)的出口管道,和 原料(2)的至少一个入口管道•所述燃烧装置(14),干燥和热解装置(4),气化装置(6)被物理地分离并定位在三个不同的水平上, - 纵向旋转轴线 A)干燥a d热解装置(4)相对于气化装置(6)的纵向旋转轴线(B)倾斜并且相对于燃烧装置(14)的纵向轴线(C)倾斜, - 纵向旋转 气化装置(6)的轴线(B)平行于燃烧装置(14)的纵向轴线(C); - 燃烧装置(14)与干燥和热解装置(4)流体连通, - 干燥和热解装置(4)在其内部包括第一间接热交换装置(3),其中来自燃烧装置(14)的燃烧烟雾流动; - 至少一个沉降室(15) 与所述干燥和热解装置(4)和所述气化装置(6)和所述燃烧装置(14)流体连通,•输送装置(5)定位在沉降室(15)中,并将干燥和 与气化装置流体连通的热解装置(4), - 它包括 与所述第一间接热交换装置(3)和所述燃烧装置(14)流体连通的第二热交换装置(12), - 其包括用于吸入中间气体反应产物的装置,所述装置位于 沉降室(15)。