CFD Simulations of Vapour-Liquid Separator in LNG Process
In natural gas processing, vapour-liquid separation (VLS) is one of the commonly used unit operations. In this paper, a series of Computational Fluid Dynamics (CFD) simulations were conducted on an industrial scale VLS. Initially, simulations were carried out to evaluate the performance of inlet...
| Main Authors: | , , , , , |
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| Format: | Conference Paper |
| Published: |
2019
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| Online Access: | http://hdl.handle.net/20.500.11937/76967 |
| _version_ | 1848763794129420288 |
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| author | Mahadika Priyambodo, Muhammad Dary Sun, Biao Bhatelia, Tejas Utikar, Ranjeet Pareek, Vishnu Byfield, Geoffrey |
| author_facet | Mahadika Priyambodo, Muhammad Dary Sun, Biao Bhatelia, Tejas Utikar, Ranjeet Pareek, Vishnu Byfield, Geoffrey |
| author_sort | Mahadika Priyambodo, Muhammad Dary |
| building | Curtin Institutional Repository |
| collection | Online Access |
| description | In natural gas processing, vapour-liquid separation (VLS) is one of the commonly used unit
operations. In this paper, a series of Computational Fluid Dynamics (CFD) simulations were
conducted on an industrial scale VLS. Initially, simulations were carried out to evaluate the
performance of inlet diverter by studying the effect of inlet Reynolds number on the crosssectional
variance of velocity. It was found that the flow was highly symmetrical and evenly
distributed with a variance nearly zero at a very low Reynolds number (Re = 1000), but as the
inlet Reynolds number increased, the variance increased to 0.03 and the flow was highly
dominated towards the wall. To simulate the Knitmesh, porous media was used with inertial
and viscous resistance calculated and validated using previously published experimental data
(Rahimi and Abbaspour 2008).
When a full scale VLS was simulated, it was found that at industrially relevant condition the
effect of inlet diverter was significant on the Knitted mesh mist eliminator performance and
approx. 88% of it was subject to velocities above the prescribed terminal velocity and would
lead to poor vapor liquid separation. Without any hardware change to mitigate this
underperformance, it would be required to drop the capacity of the VLS by at least 5 times. On
the other hand, if two layers of mist pads with 75% size of full mesh pad was used, 26% recovery
in performance can be achieved.
The model proposed in this work provides the basis for future development of parametric study
on various configurations of mesh pad that can ultimately improve the capacity and
performance of the VLS. |
| first_indexed | 2025-11-14T11:09:07Z |
| format | Conference Paper |
| id | curtin-20.500.11937-76967 |
| institution | Curtin University Malaysia |
| institution_category | Local University |
| last_indexed | 2025-11-14T11:09:07Z |
| publishDate | 2019 |
| recordtype | eprints |
| repository_type | Digital Repository |
| spelling | curtin-20.500.11937-769672025-04-28T03:14:29Z CFD Simulations of Vapour-Liquid Separator in LNG Process Mahadika Priyambodo, Muhammad Dary Sun, Biao Bhatelia, Tejas Utikar, Ranjeet Pareek, Vishnu Byfield, Geoffrey In natural gas processing, vapour-liquid separation (VLS) is one of the commonly used unit operations. In this paper, a series of Computational Fluid Dynamics (CFD) simulations were conducted on an industrial scale VLS. Initially, simulations were carried out to evaluate the performance of inlet diverter by studying the effect of inlet Reynolds number on the crosssectional variance of velocity. It was found that the flow was highly symmetrical and evenly distributed with a variance nearly zero at a very low Reynolds number (Re = 1000), but as the inlet Reynolds number increased, the variance increased to 0.03 and the flow was highly dominated towards the wall. To simulate the Knitmesh, porous media was used with inertial and viscous resistance calculated and validated using previously published experimental data (Rahimi and Abbaspour 2008). When a full scale VLS was simulated, it was found that at industrially relevant condition the effect of inlet diverter was significant on the Knitted mesh mist eliminator performance and approx. 88% of it was subject to velocities above the prescribed terminal velocity and would lead to poor vapor liquid separation. Without any hardware change to mitigate this underperformance, it would be required to drop the capacity of the VLS by at least 5 times. On the other hand, if two layers of mist pads with 75% size of full mesh pad was used, 26% recovery in performance can be achieved. The model proposed in this work provides the basis for future development of parametric study on various configurations of mesh pad that can ultimately improve the capacity and performance of the VLS. 2019 Conference Paper http://hdl.handle.net/20.500.11937/76967 restricted |
| spellingShingle | Mahadika Priyambodo, Muhammad Dary Sun, Biao Bhatelia, Tejas Utikar, Ranjeet Pareek, Vishnu Byfield, Geoffrey CFD Simulations of Vapour-Liquid Separator in LNG Process |
| title | CFD Simulations of Vapour-Liquid Separator in LNG
Process |
| title_full | CFD Simulations of Vapour-Liquid Separator in LNG
Process |
| title_fullStr | CFD Simulations of Vapour-Liquid Separator in LNG
Process |
| title_full_unstemmed | CFD Simulations of Vapour-Liquid Separator in LNG
Process |
| title_short | CFD Simulations of Vapour-Liquid Separator in LNG
Process |
| title_sort | cfd simulations of vapour-liquid separator in lng
process |
| url | http://hdl.handle.net/20.500.11937/76967 |