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Biodiesel synthesis from spent frying vegetable oils over heterogeneous inorganic catalysts

机译:在非均相无机催化剂上由油炸植物油中的生物柴油合成

摘要

Biodiesel derived from renewable plant seed oils and animal fats is a promising alternative to fossil diesel fuel. Commercially, triglyceride transesterification and free fatty acid esterification with short chain alcohols over soluble catalysts are crucial procedures for biodiesel synthesis. Such technologies are ecologically deplorable due to necessary removal of caustic catalysts from the product. Introducing separable solid heterogeneous catalysis systems has promoted less pronounced related operational problems. Even so, processing low quality feedstock over solid acid-base catalysis systems may add unavoidable processing cost. In this respect, the main goal of the research is to develop a new bi-functional heterogeneous catalytic system for biodiesel production from spent frying oils. K3PO4 was utilised in ethanolysis production of biodiesel from waste cooking oil in this dissertation. Biodiesel processing variables were optimised by following a two level-surface response coupled to central composite design methodology. The study suggested that leaching and catalyst agglomeration are the primary cause of catalyst deteriorations and product degradation. For the first time, aluminium and calcium phosphate-potassium ribbed bi-functional catalysts were synthesised for biodiesel processing. The catalysts were produced following dipping impregnation of γ-Al2O3 and seashell in aqueous solutions of K3PO4.The used seashell were used in raw and calcined forms respectively. Synthesised catalysts were comprehensively characterised and evaluated. Leaching of active species in the liquid phase was investigated over all synthesised catalysts. Results revealed that K3PO4 contents of 15,10and 25wt% on γ-Al2O3, calcined and raw seashell were the maximum synthesis ratios at which the resultant solids maintained their heterogeneous behaviour. Extensive ethanolysis reactions were carried out over pre-selected catalyst samples with secured heterogeneous behaviour in an attempt to select the most proficient and durable catalytic system for applications concerning biodiesel synthesis. Biodiesel processing parameters were optimised in an attempt to ensure the true chemical kinetic as a single rate determining step of the overall reaction. Catalyst characterisation coupled to biodiesel formation rate data collected, demonstrated that K3PO4/raw seashell catalyst was the most feasible, sustainable and active bi-functional catalysis system for biodiesel applications.
机译:源自可再生植物种子油和动物脂肪的生物柴油是化石柴油的有前途的替代品。在商业上,甘油三酸酯酯交换和在可溶性催化剂上与短链醇的游离脂肪酸酯化是生物柴油合成的关键步骤。由于必须从产物中除去苛性催化剂,因此这种技术在生态上是不利的。引入可分离的固体多相催化系统已经引起不太明显的相关操作问题。即使这样,通过固体酸碱催化系统处理低质量的原料仍可能增加不可避免的处理成本。在这方面,研究的主要目的是开发一种新的双功能多相催化系统,用于从废油炸油生产生物柴油。本文以K3PO4为原料,从废食用油中乙醇化生产生物柴油。通过遵循二级表面响应和中心复合材料设计方法来优化生物柴油的加工变量。研究表明,浸出和催化剂团聚是催化剂劣化和产物降解的主要原因。首次合成了铝和磷酸钙-钾带肋双功能催化剂,用于生物柴油加工。将γ-Al2O3和贝壳浸渍在K3PO4水溶液中制成催化剂,用过的贝壳分别以生料和煅烧形式使用。对合成的催化剂进行了全面的表征和评估。在所有合成的催化剂上研究了液相中活性物质的浸出。结果表明,煅烧和未加工的贝壳上,γ-Al2O3上的K3PO4含量分别为15,10和25wt%,是合成固体保持其异质性状的最大合成比。对具有固定多相行为的预选催化剂样品进行了广泛的乙醇分解反应,试图为生物柴油合成应用选择最有效和最持久的催化体系。优化生物柴油加工参数,以确保真正的化学动力学作为整个反应的单个速率确定步骤。催化剂特性与收集的生物柴油形成速率数据相结合,表明K3PO4 /生贝壳催化剂是生物柴油应用中最可行,可持续和活性最高的双功能催化系统。

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