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Preparation of biodiesel from oil palm industrial waste using sulphated heterogeneous catalyst

机译:使用硫酸化非均相催化剂从油棕工业废料中制备生物柴油

摘要

The use of waste, particularly in the biodiesel industry has gained great potential in countering higher feedstock cost. In the present work, methyl ester was prepared from waste sources, palm fatty acid distillate (PFAD) and decanter cake oil (Dc-oil) via solid acid catalysts (SO42-/TiO2-SiO2 and NiSO4/SiO2). In line with the costing related matter, silica from rice husk ash (RHA), an agricultural waste, is used as a support for all the catalysts. The SO42-/TiO2-SiO2 and NiSO4/SiO2 catalysts were prepared by wet impregnation method. The obtained results showed that, both prepared catalysts lay in acidic form as tested using Hammett indicators. Both of the catalysts possessed mesoporous structures which were ideal catalyst for biodiesel production. PFAD was successfully esterified using SO42-/TiO2-SiO2 (calcined at 500 ºC) under the optimal conditions of 2.97 wt.% catalyst amount, 5.85:1 methanol to PFAD molar ratio and reaction time of 3.12 h to produce 93.3% methyl ester. Similarly, 93% methyl ester was achieved using NiSO4/SiO2 (calcined at 300 ºC) under the optimal conditions of 15 wt.% catalyst amount, 5:1 methanol to PFAD molar ratio and 7 h of methanol refluxing process. As for Dc-oil, SO42-/TiO2-SiO2 was used to transesterify the oil at optimal conditions of 5 wt.% catalyst amount , 9:1 methanol Dc-oil molar ratio for 5 h response time, producing 60.7% methyl esters. Similarly, 71% methyl esters was achieved using NiSO4/SiO2 under the optimal conditions of 11 wt.% catalyst amount, 15:1 methanol to oil molar ratio for 9 h reaction time. The prepared SO42-/TiO2-SiO2 catalyst for the esterification of PFAD was found to be reused up to two times with more than 90% methyl esters produced. On other hand, NiSO4/SiO2 catalyst for the esterification of PFAD can be reused once only with methyl esters produced about 90%. Besides that, the findings also revealed SO42-/TiO2-SiO2 had better catalytic activity in esterification of PFAD and transesterification of Dc-oil compared to NiSO4/SiO2. The investigated solid acid catalysts, SO42-/TiO2-SiO2 and NiSO4/SiO2 were found applicable for esterification and transesterification of high FFA feedstock especially from waste feedstock.
机译:废物的利用,特别是在生物柴油行业中的利用,在应对较高的原料成本方面具有巨大的潜力。在本工作中,甲酯是通过固体酸催化剂(SO42- / TiO2-SiO2和NiSO4 / SiO2)由废料,棕榈脂肪酸馏出物(PFAD)和倾析饼油(Dc-油)制备的。与成本核算相关的是,来自农业废料的稻壳灰(RHA)中的二氧化硅被用作所有催化剂的载体。采用湿法浸渍法制备了SO42- / TiO2-SiO2和NiSO4 / SiO2催化剂。获得的结果表明,两种制备的催化剂如使用哈米特指示剂测试的那样呈酸性形式。两种催化剂均具有介孔结构,这是生物柴油生产的理想催化剂。使用SO42- / TiO2-SiO2(在500℃下煅烧),在催化剂量2.97 wt。%,甲醇与PFAD摩尔比为5.85:1和反应时间3.12 h的最佳条件下成功酯化了PFAD,得到93.3%的甲酯。同样,使用NiSO4 / SiO2(在300ºC下煅烧),在催化剂量为15%(重量),甲醇与PFAD的摩尔比为5:1和甲醇回流过程为7小时的最佳条件下,可获得93%的甲酯。对于Dc-油,在催化剂量为5%(重量),甲醇Dc-油摩尔比为9:1的最佳条件下,使用SO42- / TiO2-SiO2对油进行酯交换反应,反应时间为5小时,产生60.7%的甲酯。同样,使用NiSO4 / SiO2在最佳催化剂量为11%(重量),甲醇与油的摩尔比为15:1的最佳条件下反应9小时可获得71%的甲酯。发现所制备的用于PFAD酯化的SO42- / TiO2-SiO2催化剂可重复使用两次,生产的甲酯超过90%。另一方面,用于PFAD酯化的NiSO4 / SiO2催化剂只能与产生约90%的甲酯一起重复使用一次。除此之外,研究结果还表明,与NiSO4 / SiO2相比,SO42- / TiO2-SiO2在PFAD酯化和Dc-油的酯交换反应中具有更好的催化活性。发现所研究的固体酸催化剂SO42- / TiO2-SiO2和NiSO4 / SiO2适用于高FFA原料的酯化和酯交换,特别是废料。

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    Nurul Hajar Embong;

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  • 年度 2016
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