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Reducing the CO2 footprint at an LNG asset with replicate trains using operational data-driven analysis. A case study on end flash vessels

Published online by Cambridge University Press:  08 January 2025

Rakesh Paleja
Affiliation:
Shell Research Limited, London, SE1 7LZ, UK.
Ekhorutomwen Osemwinyen
Affiliation:
NLNG Plant Complex, Bonny Island, Rivers State, Nigeria
Matthew Jones
Affiliation:
Shell Global Solutions International BV, Amsterdam, 1031 HW, The Netherlands
John Ayoola
Affiliation:
NLNG Plant Complex, Bonny Island, Rivers State, Nigeria
Raghuraman Pitchumani
Affiliation:
Shell International Exploration and Production Inc., Houston, TX 77079, USA
Philip Jonathan*
Affiliation:
Shell Research Limited, London, SE1 7LZ, UK. Department of Mathematics and Statistics, Lancaster University, Lancaster, LA1 4YF, UK
*
Corresponding author: Philip Jonathan; Emails: philip.jonathan@shell.com; p.jonathan@lancaster.ac.uk

Abstract

A liquefied natural gas (LNG) facility often incorporates replicate liquefaction trains. The performance of equivalent units across trains, designed using common numerical models, might be expected to be similar. In this article, we discuss statistical analysis of real plant data to validate this assumption. Analysis of operational data for end flash vessels from a pair of replicate trains at an LNG facility indicates that one train produces 2.8%–6.4% more end flash gas than the other. We then develop statistical models for train operation, facilitating reduced flaring and hence a reduction of up to 45% in CO2 equivalent flaring emissions, noting that flaring emissions for a typical LNG facility account for ~4%–8% of the overall facility emissions. We recommend that operational data-driven models be considered generally to improve the performance of LNG facilities and reduce their CO2 footprint, particularly when replica units are present.

Information

Type
Translational Article
Creative Commons
Creative Common License - CCCreative Common License - BY
This is an Open Access article, distributed under the terms of the Creative Commons Attribution licence (http://creativecommons.org/licenses/by/4.0), which permits unrestricted re-use, distribution and reproduction, provided the original article is properly cited.
Copyright
© Shell Information Technology International Ltd., London SE1 7NA, United Kingdom., 2025. Published by Cambridge University Press
Figure 0

Figure 1. Schematic of the cold section of LNG train. The end flash vessel shown in blue produces end flash gas, used as fuel gas for the facility.

Figure 1

Figure 2. Schematic of two replicate trains, Train 1 and Train 2, feeding EFG to FG pool besides BOG from LNG tank LBOB from tank in the loading vessel (also shown in blue). When the FG pool has excess FG it is released and flared through the flare valve.

Figure 2

Figure 3. Scatter plots of Q3, T3, P4, and Q5 across trains Tr1, Tr2 of operational data sampled at 5-minute intervals for the year 2019. Values for time points satisfying the filter conditions in Equation 1 are shown in green. All other time points are shown in blue. Values of Q3 and Q5 have been normalized using a common factor so that the global maximum value of Q5 is 100 T/d.

Figure 3

Figure 4. Histograms of filtered Q51 (blue) and Q52 (red) data per annum, for years 2015–2019. Panel titles indicate the number of observations n retained after filtering. Vertical lines and annotated text give mean values of filtered data. Values of Q5 have been normalized using a common factor so that the global maximum value is 100 T/d.

Figure 4

Figure 5. Histograms of full unfiltered data for Q51 (blue) and Q52 (red) per annum, for years 2015–2019. Panel titles indicate the number of observations n retained after filtering. Vertical lines and annotated text give mean values of filtered data. Values of Q5 have been normalized using a common factor so that the global maximum value is 100 T/d.

Figure 5

Table 1. Independent two-sample t-test for population mean difference $ {\overline{\mathrm{Q}5}}_1 $ - $ {\overline{\mathrm{Q}5}}_2 $ per annum. Null hypothesis rejected for each year since LCL > 0. Note that the critical value $ {t}_{\mathrm{crit},\nu }(0.95) $ at infinite sample size is adopted as a good approximation, since $ n>1000 $ throughout

Figure 6

Figure 6. Adjusted response values for Q5 with respect to Q3, T3, and P4 for U1 (blue circles) and U2 (red circles). Corresponding adjusted fit functions $ g $ are shown as black lines.

Figure 7

Figure 7. Flare valve opening, ranging from High, Medium to Low for Period 1 (left) and Period 2 (right) as a function of a mean of T3 and a sum of Q3 from Tr1 and Tr2. In Period 1, simultaneous and equal reductions were made, first for T3 and subsequently if necessary for Q3, for both trains at the point of flare onset. In Period 2, T31 and then Q31 (if necessary) were reduced first, followed (if necessary) by T32 and Q32. Polygons show domains of mean T3 and total Q3 corresponding to low risk of High and Medium flare opening.

Figure 8

Table A1: Summary statistics of samples of filtered Q5 values for train Tr1 over years 2015 to 2019. Values have been normalized using a common factor so that the global maximum value (over both trains and all years) is 100 T/d

Figure 9

Table A2: Summary statistics of filtered Q5 values for train Tr2 over years 2015 to 2019. Values have been normalized using a common factor so that the global maximum value (over both trains and all years) is 100 T/d

Figure 10

Table B1: Welch’s t-test for population mean difference $ {\overline{\mathrm{Q}5}}_1 $ - $ {\overline{\mathrm{Q}5}}_2 $ per annum, assuming unequal population variances. Null hypothesis rejected for each year since LCL > 0. Note that the critical value $ {t}_{\mathrm{crit},\nu }(0.95) $ at infinite sample size is adopted as a good approximation, since $ n>1000 $ throughout

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