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    • 85. 发明申请
    • BIOMASS FEED SYSTEM/PROCESS
    • 生物量进料系统/工艺
    • US20110174597A1
    • 2011-07-21
    • US12703492
    • 2010-02-10
    • ROBERT BARTEK
    • ROBERT BARTEK
    • B65G47/74
    • B01J3/02B65G53/04B65G53/66F23G5/027F23G5/444F23G2205/00F23G2205/14F23G2205/18F23G2205/20F23G2209/26F23G2900/55006F23K2201/505F23K2203/104
    • Disclosed is a process for conveying solid particulate biomass material to a reactor including: charging a quantity of solid particulate biomass material to a spool piece at a pressure P1; pressurizing the spool piece to a pressure P2, wherein P2 is greater than P1; conveying the solid particulate biomass material either directly to a reactor operated at or below P2 or first to a vibratory feeder and then to such reactor; isolating the spool piece from the vibratory feeder and or reactor and reducing the pressure in the spool piece to P1; and repeating these steps at least once. The vibratory feeder can include a bowl and an outlet spout extending tangentially from the bowl. Optionally, a hopper and a hopper-mounted solids conveyer, both resting on a mass measuring device, can be used to feed the solid particulate biomass material to the spool piece.
    • 公开了一种将固体颗粒生物质材料输送到反应器的方法,包括:在压力P1下将一定量的固体颗粒生物质材料装入卷筒件; 将卷筒片加压到P2,其中P2大于P1; 将固体颗粒生物质材料直接输送到在P2处或低于P2操作的反应器,或者首先传递到振动进料器,然后到达这种反应器; 将卷筒片与振动进料器和/或反应器隔离,并将卷筒片中的压力降低到P1; 并重复这些步骤至少一次。 振动进料器可以包括碗和从碗中切向延伸的出口喷口。 任选地,可以使用放在质量测量装置上的料斗和料斗安装的固体输送机将固体颗粒生物质材料供给到卷轴件。
    • 90. 发明申请
    • Treatment plant for refuse derived fuels
    • 垃圾衍生燃料的处理厂
    • US20030138748A1
    • 2003-07-24
    • US10203419
    • 2002-11-29
    • Clementino Cabrini
    • F23G007/08
    • F23G5/0276B01J3/006B01J3/02C10B49/06C10B53/00C10J3/66C10J2200/154C10J2300/1223C10K1/024C10K1/08F23G2202/101F23J2217/10F23J2217/50
    • Process for incinerating refuse derived fuels to obtain fuel gas therefrom by thermal cracking, comprising the following steps: subjecting the material to deaeration; advancing a bed of material within a vacuum environment insulated from the outside (thermal cracking chamber) and in which a temperature of between 400 DEG C. and 600 DEG C. is maintained by the countercurrent flow of hot gases which lap the material; feeding the material which has passed through the thermal cracking chamber to a reactor in order to be subjected to a temperature of between 1200 DEG C. and 1800 DEG C.; in proximity ot the entry end of said thermal cracking chamber, drawing off the gases generated by the thermal cracking together with the gases which have lapped the bed of material, in order to maintain the thermal cracking chamber under vacuum; feeding the drawn-off gases to the discharge conduit for the gases generated in the reactor; purifying and filtering the gases obtained in this manner for their use as fuel gases.
    • 用于焚烧垃圾衍生燃料以通过热裂解从其中获得燃料气的方法,包括以下步骤:对材料进行脱气; 在与外部绝热的真空环境(热裂解室)内推进材料床,其中温度在400摄氏度到600度之间的温度通过材料的热气流的逆流保持; 将已经通过热裂解室的材料进料到反应器中以进行1200℃至1800℃的温度; 在所述热裂解室的入口附近,将热裂解产生的气体与已经研磨材料床的气体一起排出,以便将热裂解室保持在真空状态; 将排出的气体输送到在反应器中产生的气体的排出管道; 净化和过滤以这种方式获得的气体用作燃料气体。