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CATALYTIC PYROLYSIS PROCESS AND PYROLYSIS PRODUCTS SO FORMED

机译:如此形成的催化热解过程和热解产物

摘要

Biomass material is pyrolyzed in the absence of air O H and solvent (e.g. HO) at 500°C or above in a reactor containing (i) a catalyst which as charged is a rehydrated calcined calcium containing layered dihydroxide comprised of particles having an average particle size in the range of about 40 to about 400 microns (preferably in the range of about 50 to about 150 microns) which optionally is in a pre agglomerized form and (ii) a particulate fluidizable heat transfer medium preferably sand; and condensing and isolating pyrolysis oil produced and collecting and isolating non condensable gases separately from the condensed isolated liquid pyrolysis oil product. Pyrolysis oil obtained directly from the pyrolysis has a total acid number less than 70 mg/KOH/g; and a weight percentage of O removal of 72 wt% or more as determined by a described test procedure and as calculated using an expression given in the text.
机译:在含有(i)催化剂的反应器中,在没有空气OH和溶剂(例如HO)的情况下,在没有空气OH和溶剂的情况下,将生物质材料热解,该反应器包含(i)催化剂,该催化剂是由平均粒径的颗粒组成的复水煅烧含钙层状二氢氧化物在约40至约400微米的范围内(优选在约50至约150微米的范围内),其任选地是预附聚的形式,和(ii)颗粒状可流化的传热介质,优选为沙;产生的冷凝和分离的热解油,以及与冷凝的分离的液体热解油产物分开收集和分离的不可冷凝气体。直接从热解获得的热解油的总酸值小于70 mg / KOH / g;通过所述测试程序确定并使用本文给出的表达式计算出的O去除的重量百分比为72重量%以上。

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