HYBRID POWER GENERATION SYSTEM USING SOLAR ENERGY AND BIOENERGY
    6.
    发明申请
    HYBRID POWER GENERATION SYSTEM USING SOLAR ENERGY AND BIOENERGY 审中-公开
    混合发电系统采用太阳能和生物能源

    公开(公告)号:US20170030226A1

    公开(公告)日:2017-02-02

    申请号:US15289992

    申请日:2016-10-11

    IPC分类号: F01K3/18 H02K7/18 F01D15/10

    摘要: A hybrid power generation system using solar energy and bioenergy, including a solar thermal boiler system, a biomass boiler system, and a turbogenerator system. The solar thermal boiler system includes a trough solar collector, a heat collector, an oil circulating pump, a storage tank for storing heat transfer oil, a solar thermal heater, a solar thermal evaporator, a main pipe transporting saturated steam, and an auxiliary boiler. Heat transfer oil output from a solar light field of the solar thermal boiler system is transmitted through and transfers heat to the solar thermal evaporator and the solar thermal heater, and the heat transfer oil returns to the storage tank for storing heat transfer oil. The heat transfer oil in the storage tank is pumped to the solar light field via the oil circulating pump.

    摘要翻译: 使用太阳能和生物能源的混合发电系统,包括太阳能热水锅炉系统,生物质锅炉系统和涡轮发电机系统。 太阳能热水锅炉系统包括槽式太阳能收集器,集热器,油循环泵,用于储存传热油的储罐,太阳能热加热器,太阳能热蒸发器,输送饱和蒸汽的主管和辅助锅炉 。 由太阳能热水锅炉系统的太阳光场输出的传热油通过太阳热能蒸发器和太阳能热能加热器传递并传递热量,传热油返回储存储存传热油的储罐。 储油罐中的传热油通过油循环泵泵送到太阳光场。

    METHOD FOR MODIFYING BIO-OIL DERIVED FROM BIOMASS PYROLYSIS
    9.
    发明申请
    METHOD FOR MODIFYING BIO-OIL DERIVED FROM BIOMASS PYROLYSIS 有权
    用于修饰生物量热解生物油的方法

    公开(公告)号:US20160060539A1

    公开(公告)日:2016-03-03

    申请号:US14935429

    申请日:2015-11-08

    IPC分类号: C10G3/00 B01D17/04

    摘要: A method for modifying bio-oil derived from biomass pyrolysis, the method including: 1) adding an inorganic salt and an organic demulsifier to a bio-oil; oscillating or stirring the resulting mixture, and resting the resulting mixture, to yield a lower layer being an aqueous solution and an upper layer being the bio-oil, and collecting the bio-oil; 2) employing a zeolite molecular sieve-loaded clay as a catalyst, and aging the catalyst using pure steam, to yield a modified catalyst; and 3) adding the modified catalyst obtained in 2) to a conventional catalytic cracking reactor, injecting the bio-oil obtained in 1) to the conventional catalytic cracking reactor using a piston pump, and allowing the bio-oil to react under a weight hourly space velocity (WHSV) of between 6 and 15 h−1, a temperature of between 380 and 700° C., and a pressure between 0.1 and 0.8 megapascal.

    摘要翻译: 一种改性生物质热解生物油的方法,所述方法包括:1)向生物油中加入无机盐和有机破乳剂; 振荡或搅拌所得混合物,并静置所得混合物,得到作为生物油的水溶液和上层的下层,并收集生物油; 2)使用沸石分子筛负载的粘土作为催化剂,并使用纯蒸汽使催化剂老化,得到改性的催化剂; 和3)将常规催化裂解反应器中的2)中得到的改性催化剂加入到常规催化裂化反应器中,使用活塞泵将1)中得到的生物油注入到生物油中, 在6和15h-1之间的空间速度(WHSV),温度在380和700℃之间,压力在0.1和0.8兆帕之间。

    Method for preparing liquid hydrocarbons from syngas
    10.
    发明授权
    Method for preparing liquid hydrocarbons from syngas 有权
    从合成气制备液态烃的方法

    公开(公告)号:US09255225B2

    公开(公告)日:2016-02-09

    申请号:US14569774

    申请日:2014-12-14

    摘要: A method for preparing a liquid hydrocarbon from syngas. The method includes: 1) mixing crude syngas from a biomass gasifier and a hydrogen-rich gas to yield a mixed gas; 2) dehydrating and decarbonizing the mixed gas for removal of moisture, carbon dioxide, and impurities, to yield a fine syngas; 3) introducing the fine syngas to a Fischer-Tropsch synthesis device in the presence of a catalyst, controlling a reaction temperature of the Fischer-Tropsch synthesis at between 150 and 300° C. and a reaction pressure of between 2 and 4 MPa (A), to yield a liquid hydrocarbon and water which is discharged out of the Fischer-Tropsch synthesis device; and 4) returning 70-95 vol. % of exhaust gases from the Fischer-Tropsch synthesis device to step 3) to mix with the fine syngas, and introducing the resulting mixed gas to the Fischer-Tropsch synthesis device.

    摘要翻译: 从合成气制备液态烃的方法。 该方法包括:1)从生物质气化炉和富氢气体混合粗合成气,得到混合气体; 2)将混合气体脱水脱碳以除去水分,二氧化碳和杂质,产生细小的合成气; 3)在催化剂存在下将细合成气引入费 - 托合成装置中,在150-300℃之间控制费 - 托合成的反应温度和2-4MPa的反应压力(A ),以产生从费 - 托合成装置排出的液体烃和水; 和4)返回70-95卷。 从费 - 托合成装置到步骤3)的废气的%)与细合成气混合,并将所得混合气体引入费 - 托合成装置。