Influence of loading on the heat transfer rate and specific water consumption of detached loosed fresh palm fruits during vertical mini-batch sterilization

This study presents the effect of loading on the heat transfer rate and specific water consumption of detached loosed fresh palm fruits during sterilization. Sterilization is an integral process of palm oil extraction that con- sumes a lot of water. However, most industrial research in the past focused on fresh fruit bunch (FFB) sterili- zation dynamics. At the same time, the medium- and small-scale industries sterilize already detached loosed fresh palm fruits (LFPF) that have been removed from the spikelet as purchased from aggregators. Therefore, the process data generated from the sterilization of FFB might not be optimal for sterilizing LFPF. This study, therefore, investigates the transient response of variation in LFPF loading of the sterilization chamber to steam injection during steam sterilization of LFPF at 3 ± 0.5 bars using a vertical, single-peak LFPF sterilizer that combines the boiler and sterilizer in a single unit. The LFPF were loaded at mass intervals of 0.2 kg ranging from 0.2 kg to 2 kg. The vapour temperature dynamics, heat transfer rate, steam energy utilization efficiency and specific water consumption parameters were studied. The average vapour temperature varied from 100 ◦C to 130 ◦C for the LFPF mass range of 0.2 to 2 kg at steam injection temperature of 140 ◦C and pressure of 3 ± 0.5 bars. This temperature range matched the saturated vapour temperature of pure water at 1.0––2.8 bars absolutepressure but slightly lower than the saturated vapour temperature of 133.54 ◦C for pure steam at 3 bars. The percentage of steam energy utilization effectiveness is inversely related to the steam mass flow rate. While energy effectiveness increased with loading mass, the steam mass flow rate decreased with increased LFPF mass. Thevalue of the heat transfer rate ranged between 1.7––55.4 W, while the specific heat transfer rate ranged between8.5–––41.8 W/kg. The average specific water consumption ranged from 0.014 to 0.09 kg-water/kg-LFPF, with an average value of 0.031 kg-water/kg-LFPF. This value is lower than 0.112–––0.5 kg-water/kg-FFB, with an average value of 0.256 kg-water/kg-FFB for conventional FFB steam sterilization. This represents an 87.9%reduction in water consumption in conventional FFB steam sterilization. An empirical model deduced for specific heat transfer rate and water consumption for steam sterilization of LFPF at 3 ± 0.5 bars and vapour temperature range of 100––130 ◦C showed a high coefficient of determination above 99%.

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Journal
Journal of King Saud University - Engineering Sciences
Published
2025-12-01
DOI
https://doi.org/10.1007/s44444-025-00074-y
Primary Topic
Food Drying and Modeling
Type
article
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article

Influence of loading on the heat transfer rate and specific water consumption of detached loosed fresh palm fruits during vertical mini-batch sterilization

Godwin Usoh, Macmanus Chinenye Ndukwu, Leonard Akuwueke, Mathew I. Ibeh et al.
Journal of King Saud University - Engineering Sciences
Food Drying and Modeling
article

Influence of loading on the heat transfer rate and specific water consumption of detached loosed fresh palm fruits during vertical mini-batch sterilization

Godwin Usoh, Macmanus Chinenye Ndukwu, Leonard Akuwueke, Mathew I. Ibeh, Fidelis I. Abam, Linus Oriaku, Godwin Akpan, Chinedu. M. Nkuma
article en

Abstract

This study presents the effect of loading on the heat transfer rate and specific water consumption of detached loosed fresh palm fruits during sterilization. Sterilization is an integral process of palm oil extraction that con- sumes a lot of water. However, most industrial research in the past focused on fresh fruit bunch (FFB) sterili- zation dynamics. At the same time, the medium- and small-scale industries sterilize already detached loosed fresh palm fruits (LFPF) that have been removed from the spikelet as purchased from aggregators. Therefore, the process data generated from the sterilization of FFB might not be optimal for sterilizing LFPF. This study, therefore, investigates the transient response of variation in LFPF loading of the sterilization chamber to steam injection during steam sterilization of LFPF at 3 ± 0.5 bars using a vertical, single-peak LFPF sterilizer that combines the boiler and sterilizer in a single unit. The LFPF were loaded at mass intervals of 0.2 kg ranging from 0.2 kg to 2 kg. The vapour temperature dynamics, heat transfer rate, steam energy utilization efficiency and specific water consumption parameters were studied. The average vapour temperature varied from 100 ◦C to 130 ◦C for the LFPF mass range of 0.2 to 2 kg at steam injection temperature of 140 ◦C and pressure of 3 ± 0.5 bars. This temperature range matched the saturated vapour temperature of pure water at 1.0––2.8 bars absolutepressure but slightly lower than the saturated vapour temperature of 133.54 ◦C for pure steam at 3 bars. The percentage of steam energy utilization effectiveness is inversely related to the steam mass flow rate. While energy effectiveness increased with loading mass, the steam mass flow rate decreased with increased LFPF mass. Thevalue of the heat transfer rate ranged between 1.7––55.4 W, while the specific heat transfer rate ranged between8.5–––41.8 W/kg. The average specific water consumption ranged from 0.014 to 0.09 kg-water/kg-LFPF, with an average value of 0.031 kg-water/kg-LFPF. This value is lower than 0.112–––0.5 kg-water/kg-FFB, with an average value of 0.256 kg-water/kg-FFB for conventional FFB steam sterilization. This represents an 87.9%reduction in water consumption in conventional FFB steam sterilization. An empirical model deduced for specific heat transfer rate and water consumption for steam sterilization of LFPF at 3 ± 0.5 bars and vapour temperature range of 100––130 ◦C showed a high coefficient of determination above 99%.

Journal of King Saud University - Engineering SciencesVol. 37(8)
Akwa Ibom State University (NG), National Root Crops Research Institute (NG), University of Calabar (NG), Michael Okpara University of Agriculture (NG)
Openalex Percentile: Top 56%
Food Drying and Modeling
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