ALKYLATION OF PHENOL IN THE PRESENCE OF HOMOGENEOUS AND HETEROGENEOUS CATALYSTS

Phenol alkylation processes with both homogeneous and heterogeneous catalysts were studied. KU-2 was employed as a heterogeneous catalyst and sodium bisulfate (NaHSO_4) as a homogeneous catalyst during the reaction. In the presence of a NaHSO_4catalyst, alkylation reactions involving phenol and 1-methylcyclohexene were conducted. Kinetic parameters (temperature, duration, molar ratio of beginning components, amount of catalyst) were examined in relation to the process's selectivity and major product yield. At a temperature between 80 and 160°C, a reaction duration of 2 to 8 hours, a molar ratio of phenol to 1-methylcyclohexene between 1:2 and 3:1, and a catalyst amount between 5 and 15%, the alkylation reaction between phenol and 1-methylcyclohexene was investigated. The best conditions for the alkylation process were determined by the studies: temperature 140°C, reaction duration of 6 hours phenol:1-methylcyclohexene 1:1 mol/mol, and catalyst amount of 15% according to phenol taken. The process selectivity was 86.3% (based on the target product) and the target product's yield was 71.6% (based on the phenol taken) under the determined ideal conditions. Concurrently, alkylation processes between phenol and 1-methylcyclohexene were conducted with a KU-2 catalyst present. Kinetic parameters (temperature, duration, molar ratio of beginning components, amount of catalyst) were examined in relation to the process's selectivity and major product yield. At a temperature of 80–135°C, a reaction duration of 2–8 hours, a molar ratio of phenol to 1-methylcyclohexene with 1:2 and 3:1, and a catalyst amount between 5 and 20%, the alkylation reaction between phenol and 1-methylcyclohexene was investigated. According to the results of the investigations, the ideal parameters for the alkylation process were as follows: phenol: 1-methylcyclohexene 1:1 mol/mol, temperature 120°C, reaction duration 6 hours, and 10% catalyst, depending on the phenol used. The process's selectivity was 88.7% (based on the target product) and the target product's yield was 68.3% (based on the phenol extracted) under the ideal circumstances identified. Keywords: phenol, homogeneous catalysts, heterogeneous catalysts, alkylation, alkylphenols, green chemistry in catalysis.

Authors

Publication Details

Journal
PAHTEI-Procedings of Azerbaijan High Technical Educational Institutions
Published
2025-02-28
DOI
https://doi.org/10.36962/pahtei49022025-428
Primary Topic
Zeolite Catalysis and Synthesis
Type
article
Field-Weighted Citation Impact
0.00
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

ALKYLATION OF PHENOL IN THE PRESENCE OF HOMOGENEOUS AND HETEROGENEOUS CATALYSTS

Chingiz Rasulov Narmin Babayeva Narmin Babayeva
PAHTEI-Procedings of Azerbaijan High Technical Educational Institutions
Zeolite Catalysis and Synthesis
article

ALKYLATION OF PHENOL IN THE PRESENCE OF HOMOGENEOUS AND HETEROGENEOUS CATALYSTS

Chingiz Rasulov Narmin Babayeva Narmin Babayeva
article en

Abstract

Phenol alkylation processes with both homogeneous and heterogeneous catalysts were studied. KU-2 was employed as a heterogeneous catalyst and sodium bisulfate (NaHSO_4) as a homogeneous catalyst during the reaction. In the presence of a NaHSO_4catalyst, alkylation reactions involving phenol and 1-methylcyclohexene were conducted. Kinetic parameters (temperature, duration, molar ratio of beginning components, amount of catalyst) were examined in relation to the process's selectivity and major product yield. At a temperature between 80 and 160°C, a reaction duration of 2 to 8 hours, a molar ratio of phenol to 1-methylcyclohexene between 1:2 and 3:1, and a catalyst amount between 5 and 15%, the alkylation reaction between phenol and 1-methylcyclohexene was investigated. The best conditions for the alkylation process were determined by the studies: temperature 140°C, reaction duration of 6 hours phenol:1-methylcyclohexene 1:1 mol/mol, and catalyst amount of 15% according to phenol taken. The process selectivity was 86.3% (based on the target product) and the target product's yield was 71.6% (based on the phenol taken) under the determined ideal conditions. Concurrently, alkylation processes between phenol and 1-methylcyclohexene were conducted with a KU-2 catalyst present. Kinetic parameters (temperature, duration, molar ratio of beginning components, amount of catalyst) were examined in relation to the process's selectivity and major product yield. At a temperature of 80–135°C, a reaction duration of 2–8 hours, a molar ratio of phenol to 1-methylcyclohexene with 1:2 and 3:1, and a catalyst amount between 5 and 20%, the alkylation reaction between phenol and 1-methylcyclohexene was investigated. According to the results of the investigations, the ideal parameters for the alkylation process were as follows: phenol: 1-methylcyclohexene 1:1 mol/mol, temperature 120°C, reaction duration 6 hours, and 10% catalyst, depending on the phenol used. The process's selectivity was 88.7% (based on the target product) and the target product's yield was 68.3% (based on the phenol extracted) under the ideal circumstances identified. Keywords: phenol, homogeneous catalysts, heterogeneous catalysts, alkylation, alkylphenols, green chemistry in catalysis.

PAHTEI-Procedings of Azerbaijan High Technical Educational InstitutionsVol. 49(02)
Openalex Percentile: Top 85%
Zeolite Catalysis and Synthesis
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.