首页> 外文会议>European biomass conference and exhibition;ETA-Florence Renewable Energies >NEW LANTHANA-ALUMINA PROMOTED CATALYST FOR TAR CONVERSION IN SEWAGE SLUDGE GASIFICATION: CATALYTIC REFORMING VS. THERMAL PROCESS USING TOLUENE AS TAR MODEL COMPOUND
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NEW LANTHANA-ALUMINA PROMOTED CATALYST FOR TAR CONVERSION IN SEWAGE SLUDGE GASIFICATION: CATALYTIC REFORMING VS. THERMAL PROCESS USING TOLUENE AS TAR MODEL COMPOUND

机译:用于污水污泥气化中焦油转化的新型Lanthana-Aluminum促进型催化剂:催化重整与VS。以甲苯为焦油模型化合物的热过程

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摘要

In this work, new nickel lanthana promoted catalyst was synthesized, tested and compared with thermalrntar conversion process. An alternative analysis method implemented allows taking measure of product distributionrnand tar conversion estimation in continuous way by GC-mass spectrometry, overcoming the problems ascribed to therndiscontinuous method proposed by the Technical Specification CEN/TS 15439. The catalyst synthesized showed totalrntoluene conversion without by-products (tar) at 500℃ when was submitted to a sludge gasification simulated gasrnstream using toluene as a model tar compound in a concentration of 25 g·m~(-3). Catalyst was tested in a long-termrnexperiment up to 110 h at 700℃, showing total toluene conversion without by-products presence (tar), whichrndemonstrate that this catalyst could be implemented in a bench scale gasifier to be tested in real conditions.
机译:在这项工作中,合成,测试了新的镍镧系助催化剂,并将其与热转化工艺进行了比较。实施的另一种分析方法可以通过气相色谱-质谱法连续测量产物分布和焦油转化率,从而克服了技术规范CEN / TS 15439提出的不连续方法带来的问题。合成的催化剂显示出甲苯总转化率,而没有副产物浓度为25 g·m〜(-3)的甲苯作为模型焦油化合物,在500℃的温度下进入污泥气化模拟气流。该催化剂在700℃下进行了长达110h的长期实验测试,结果表明甲苯总转化率没有副产物的存在(焦油),这表明该催化剂可以在台式气化炉中实施以在实际条件下进行测试。

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