Castor biogasoline via catalytic cracking over activated Ni–Zn/activated natural zeolite catalyst

IF 1.7 4区 化学 Q4 CHEMISTRY, PHYSICAL
Aman Santoso, Amalia Bella Saputri, Evilia Wahyuning, Sumari Sumari, Eli Hendrik Sanjaya, Muntholib Muntholib
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Abstract

Synthesizing biogasoline from castor oil was catalyzed by Activated Natural Zeolite (ANZ) catalyst modified Ni and Zn metals in batch-cracking reactor. The process was affected by the modified catalyst on variation of Ni:Zn ratio (1:1, 1:2, and 2:1) at the calcination temperature of 500 °C, and variation of the calcination temperature (500, 600, and 700 °C) At Ni–Zn (1:1). After characterizations and analysis, the higher the calcination temperature, the lower the acidity of the catalyst caused the resulting yield also decreases. The density of the product obtained ranged from 0.765–0.83 g/mL, the viscosity ranged from 1.42–1.95, the refractive index was 1.421–1.431, and the calorific value tested on the cracking product with Ni:Zn (1:1) (500 °C) Fraction I, Fraction II, and Fraction III were 0.9966 kcal/kg, 0.9068 kcal/kg, and 0.8755 kcal/kg, respectively. The results of FTIR and GC–MS showed that the composition of the catalytic cracking product was composed of C6–C14 hydrocarbons consisting of aldehydes, alkanes, alkenes, and carboxylic acids. The composition was dominated by biogasoline compounds (C5–C12).

Abstract Image

活化镍锌/活化天然沸石催化剂催化裂解蓖麻生物汽油
活性天然沸石(ANZ)催化剂改性镍和锌金属在间歇式裂解反应器中催化蓖麻油合成生物汽油。在煅烧温度为 500 °C、镍锌(1:1、1:2 和 2:1)和煅烧温度为 500、600 和 700 °C、镍锌(1:1)的条件下,改性催化剂对镍锌比的变化对工艺产生了影响。经过表征和分析,煅烧温度越高,催化剂的酸度越低,所产生的产率也越低。镍锌(1:1)(500 °C)馏分 I、馏分 II 和馏分 III 裂解产物的热值分别为 0.9966 千卡/千克、0.9068 千卡/千克和 0.8755 千卡/千克。傅立叶变换红外光谱(FTIR)和气相色谱-质谱(GC-MS)的结果表明,催化裂化产物的成分由 C6-C14 碳氢化合物组成,包括醛、烷、烯和羧酸。其中主要是生物汽油化合物(C5-C12)。
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来源期刊
CiteScore
3.30
自引率
5.60%
发文量
201
审稿时长
2.8 months
期刊介绍: Reaction Kinetics, Mechanisms and Catalysis is a medium for original contributions in the following fields: -kinetics of homogeneous reactions in gas, liquid and solid phase; -Homogeneous catalysis; -Heterogeneous catalysis; -Adsorption in heterogeneous catalysis; -Transport processes related to reaction kinetics and catalysis; -Preparation and study of catalysts; -Reactors and apparatus. Reaction Kinetics, Mechanisms and Catalysis was formerly published under the title Reaction Kinetics and Catalysis Letters.
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