THERMOCHEMICAL CONVERSION OF BIOMASS
    1.
    发明申请
    THERMOCHEMICAL CONVERSION OF BIOMASS 审中-公开
    生物质热化学转化

    公开(公告)号:WO2010149138A2

    公开(公告)日:2010-12-29

    申请号:PCT/DE2010000706

    申请日:2010-06-22

    Inventor: WILLNER THOMAS

    Abstract: The invention relates to a method for producing crude oil from biomass by direct liquefaction under atmospheric pressure, involving the following steps: introducing dried biomass into a reactor containing heavy oil to form a sump oil phase consisting of biomass and heavy oil; maintaining the temperature of the sump oil phase at a predetermined reaction temperature; condensing and collecting the volatile reaction products; and isolating and collecting the crude oil. Said method is characterized in that the heavy oil phase has at least 5 wt.% organically bound oxygen.

    Abstract translation: 一种用于通过在大气压下直接液化原油生产的生物质的方法,包括以下步骤:包含在重油反应器用于形成由生物质和重质油池的油相的组供给干燥的生物质; 回火贮槽油相至预定的反应温度; 冷凝和收集所述挥发性反应产物; 和分离和收集原油,其特征在于,所述重油相包含至少5重量%的有机结合的氧。

    BIOREFINERY METHOD
    2.
    发明申请
    BIOREFINERY METHOD 审中-公开
    生物炼制方法

    公开(公告)号:WO2010149137A2

    公开(公告)日:2010-12-29

    申请号:PCT/DE2010000705

    申请日:2010-06-22

    Inventor: WILLNER THOMAS

    Abstract: The invention relates to a method for producing a petrochemical product from biomass, involving the following steps: dewatering and drying biomass; producing crude oil by the direct liquefaction of the dried biomass; hydrogenating the crude oil into hydrocarbons; and refining the hydrocarbons into a petrochemical product. Said method is characterized in that the hydrogen used for hydrogenating the crude oil is obtained from the wastewater accumulated during the dewatering and drying of the biomass and/or during the direct liquefaction and from the residue accumulated during the direct liquefaction.

    Abstract translation: 一种从生物质制备石油化学产品,包括脱水和生物质的干燥步骤过程; 由干燥的生物质的直接液化生产原油; 氢化原油烃; 和精炼烃石油化学产品,其特征在于,用于原油的加氢的氢从回收的生物量的脱水和干燥和/或在直接液化流出物获得和在直接液化残渣获得。

    TREATMENT OF RECYCLING GAS FOR DIRECT THERMOCHEMICAL CONVERSION OF HIGH MOLECULAR WEIGHT ORGANIC SUBSTANCES INTO LOW VISCOSITY LIQUID RAW MATERIALS, COMBUSTIBLES AND FUELS
    5.
    发明申请
    TREATMENT OF RECYCLING GAS FOR DIRECT THERMOCHEMICAL CONVERSION OF HIGH MOLECULAR WEIGHT ORGANIC SUBSTANCES INTO LOW VISCOSITY LIQUID RAW MATERIALS, COMBUSTIBLES AND FUELS 审中-公开
    有机物质在分子高液态低ROH和燃料气路中气体处理直接热化学转化

    公开(公告)号:WO2009130046A3

    公开(公告)日:2010-01-14

    申请号:PCT/EP2009003023

    申请日:2009-04-24

    Abstract: The invention relates to a method for the direct thermochemical conversion of high molecular weight organic starting products into low molecular weight organic products that are liquid with a low viscosity at ambient temperature and can be combusted. Said method consists of the following steps: (1) the starting product, at least one reducing gas and slow-evaporating product fractions are provided in a reactor, (2) the provided starting material is rapidly heated to a reaction temperature, (3) said starting material is converted using the temperature, the reducing effect of the gas and autocatalytical effects of the product fractions in vaporous reaction products and reaction gas, (4) the reaction gas is separated by means of condensation by evacuating the condensed reaction products, said separated reaction gas comprising a mixture of hydrogen, methane and other hydrocarbons and carbon monoxide and carbon dioxide. Said claimed method is characterised by other additional steps: (5) the separated reaction gas is conditioned by discharging at least one part of the gas mixture and optionally, introducing hydrogen, said conditioning followed by (6) re-injecting the conditioned reaction gas into the reactor for simultaneously producing a hydrating, reducing and stripping effect for converting the starting material. According to the invention, the amount of active gas fractions and its part in the total flow of the reaction gas can be modified in an advantageous manner, thus increasing the effectiveness of the method and leading to an improvement of the target product quality and yield with total lower production costs. The invention also relates to a method for carrying out the claimed method.

    Abstract translation: 本发明涉及一种用于高分子量有机起始原料在低分子量的有机物,其存在在室温下为低粘度的流体,并且可燃的直接热化学转化的方法,包括以下步骤:(1)提供起始原料,至少一种还原在反应器中气体和低挥发性的产物馏分 ,(2)所提供的原料的冲击加热至反应温度,(3)服用以蒸气反应产物和反应气体产物组分的气体和自催化效应的还原作用的温度的优点的原料的转化,(4)通过冷凝并除去的分离反应气体 冷凝的反应产物,其中包括氢,甲烷和其他烃的混合物以及一氧化碳和二氧化碳,其特征在于,作为进一步的横移被分离的反应气体 由气体混合物的至少一部分的放电的装置和任选的另外的氢气入口的装置,随后(6)再循环调节反应气体到反应器中用于同时生产一种氢化的ensschritte分离的反应气体的(5)调节,减少和对转化剥离效果 离析物被提供。 根据本发明的方法,有效的气体成分和它们的反应气体的总流量的比例的量因此可以以有利的方式修改,从而导致增加了过程的效率,以及到目标产品的质量和产量的降低整体工艺成本的改进。 本发明还涉及一种用于实施本发明方法的装置。

    THERMOCHEMISCHE UMWANDLUNG VON BIOMASSE
    9.
    发明申请

    公开(公告)号:WO2010149138A3

    公开(公告)日:2010-12-29

    申请号:PCT/DE2010/000706

    申请日:2010-06-22

    Inventor: WILLNER, Thomas

    Abstract: Verfahren zur Herstellung von Rohöl aus Biomasse durch Direktverflüssigung unter Atmosphärendruck, mit den Schritten: Zuführen von getrockneter Biomasse in einen Schweröl enthaltenden Reaktor zum Ausbilden einer aus Biomasse und Schweröl bestehenden Sumpfölphase; Temperieren der Sumpfölphase auf eine vorbestimmte Reaktionstemperatur; Kondensieren und Auffangen der flüchtigen Reaktionsprodukte; und Abscheiden und Auffangen des Rohöls, dadurch gekennzeichnet, dass die Schwerölphase wenigstens 5 Gew.-% organisch gebundenen Sauerstoff aufweist.

    VERFAHREN ZUR BIORAFFINERIE
    10.
    发明申请

    公开(公告)号:WO2010149137A3

    公开(公告)日:2010-12-29

    申请号:PCT/DE2010/000705

    申请日:2010-06-22

    Inventor: WILLNER, Thomas

    Abstract: Verfahren zur Herstellung eines petrochemischen Produkts aus Biomasse, mit den Schritten: Entwässern und Trocknen von Biomasse; Erzeugen von Rohöl mittels Direktverflüssigung der getrockneten Biomasse; Hydrieren des Rohöls zu Kohlenwasserstoffen; und Raffinieren der Kohlenwasserstoffe zum petrochemischen Produkt, dadurch gekennzeichnet, dass der für das Hydrieren des Rohöls verwendete Wasserstoff aus dem beim Entwässern und Trocknen der Biomasse und/oder bei der Direktverflüssigung anfallenden Abwasser und dem bei der Direktverflüssigung anfallenden Rückstand gewonnen wird.

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