LAPSE:2023.36044
Published Article

LAPSE:2023.36044
Biowax Production from the Hydrotreatment of Refined Palm Oil (RPO)
June 9, 2023
Abstract
In this study, conditions were determined to obtain a solid wax with a waxy ester content of more than 25% from the hydrotreating of palm oil. The experiments were conducted in a pilot-scale fixed-bed reactor. The influence of temperature, liquid hourly space velocity (LHSV), and pressure on the conversion of triglycerides were evaluated using a nickel molybdenum catalyst (NiMo/Al2O3). The variables were evaluated between 240 and 260 °C, 1 and 2 h−1 and 41 and 55 bar, respectively. Based on these results, the best conditions were T:240−260 °C; P: 90 bar; LHSV: 1.5 h−1; hydrogen/oil ratio 472 LN/L with a conversion around 60 wt%; and a selectivity towards waxy esters of 40 wt%. These conditions were then validated with a second catalyst (NiMoB/Al2O3), yielding a triglyceride conversion of about 60 wt% and a waxy ester concentration of around 30 wt%.
In this study, conditions were determined to obtain a solid wax with a waxy ester content of more than 25% from the hydrotreating of palm oil. The experiments were conducted in a pilot-scale fixed-bed reactor. The influence of temperature, liquid hourly space velocity (LHSV), and pressure on the conversion of triglycerides were evaluated using a nickel molybdenum catalyst (NiMo/Al2O3). The variables were evaluated between 240 and 260 °C, 1 and 2 h−1 and 41 and 55 bar, respectively. Based on these results, the best conditions were T:240−260 °C; P: 90 bar; LHSV: 1.5 h−1; hydrogen/oil ratio 472 LN/L with a conversion around 60 wt%; and a selectivity towards waxy esters of 40 wt%. These conditions were then validated with a second catalyst (NiMoB/Al2O3), yielding a triglyceride conversion of about 60 wt% and a waxy ester concentration of around 30 wt%.
Record ID
Keywords
biowax, hydrotreatment, refined palm oil
Suggested Citation
Olarte G, Garzón L, Sarmiento J, López-Giraldo LJ, Vivas-Báez JC. Biowax Production from the Hydrotreatment of Refined Palm Oil (RPO). (2023). LAPSE:2023.36044
Author Affiliations
Olarte G: Food Science & Technology Research Center (CICTA), Universidad Industrial de Santander, Carrera 27, Calle 9, Bucaramanga 680002, Colombia [ORCID]
Garzón L: Colombian Petroleum Institute, Km 7 Vía Piedecuesta, Piedecuesta 681017, Colombia
Sarmiento J: Colombian Petroleum Institute, Km 7 Vía Piedecuesta, Piedecuesta 681017, Colombia
López-Giraldo LJ: Food Science & Technology Research Center (CICTA), Universidad Industrial de Santander, Carrera 27, Calle 9, Bucaramanga 680002, Colombia [ORCID]
Vivas-Báez JC: Colombian Petroleum Institute, Km 7 Vía Piedecuesta, Piedecuesta 681017, Colombia [ORCID]
Garzón L: Colombian Petroleum Institute, Km 7 Vía Piedecuesta, Piedecuesta 681017, Colombia
Sarmiento J: Colombian Petroleum Institute, Km 7 Vía Piedecuesta, Piedecuesta 681017, Colombia
López-Giraldo LJ: Food Science & Technology Research Center (CICTA), Universidad Industrial de Santander, Carrera 27, Calle 9, Bucaramanga 680002, Colombia [ORCID]
Vivas-Báez JC: Colombian Petroleum Institute, Km 7 Vía Piedecuesta, Piedecuesta 681017, Colombia [ORCID]
Journal Name
Processes
Volume
11
Issue
5
First Page
1372
Year
2023
Publication Date
2023-05-01
ISSN
2227-9717
Version Comments
Original Submission
Other Meta
PII: pr11051372, Publication Type: Journal Article
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LAPSE:2023.36044
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https://doi.org/10.3390/pr11051372
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[v1] (Original Submission)
Jun 9, 2023
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Jun 9, 2023
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Record Owner
Calvin Tsay
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