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A linear model for LNG transport via existing pipeline and re-gasification terminals

  • Majed M. A. Munasser , Sabla Y. Alnouri EMAIL logo and Abdelbaki Benamor
Published/Copyright: August 25, 2025
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Abstract

This paper presents a linear programming (LP) model for optimizing the transportation of liquefied natural gas (LNG) through existing regasification terminals and Europe’s cross-border pipeline network. While pipelines offer fixed, efficient, and direct transport over land, LNG shipping provides flexibility and scalability, particularly for regions lacking pipeline connectivity. The model is demonstrated through five different case studies. Each case involves the identification of optimal LNG supply strategies from Qatar to the European Union under Russian gas disruption scenarios of 25 %, 50 %, and 75 % (equivalent to 34, 68, and 102 MTPA, respectively). The results show that the model prioritizes deliveries to destinations with available regasification capacity and low transport costs, with key importers including Turkey, Italy, Spain, and northern corridor countries. Annual network costs range from $8.1–8.8 billion for a 25 % disruption to $21–24 billion for a 75 % disruption, with liquefaction as the largest cost component. Strategic supply routes via southern, northern, and Baltic corridors were identified to enhance EU energy security, though fully replacing Russian gas would require contract adjustments and infrastructure agreements within the EU. The findings highlight the importance of integrating LNG shipping with pipeline capacity and fostering partnerships with intermediary countries.


Corresponding author: Sabla Y. Alnouri, Gas Processing Centre, College of Engineering, Qatar University, P.O. Box 2713, Doha, Qatar, E-mail:

  1. Research ethics: Not applicable.

  2. Informed consent: Not applicable.

  3. Author contributions: All authors have accepted responsibility for the entire content of this manuscript and approved its submission. M.M performed statistical and computational analyses, developed the LP model, gathered and processed the data, wrote an initial draft of the manuscript and contributed to the results and discussion sections. S.A. developed the research idea, designed the study, assisted in the development of the LP model, ensured technical accuracy and supervised the overall project. Moreover, S.A. contributed to data analysis, the interpretation and visualization of the results, in addition to editing and finalizing the manuscript. A. B. assisted in literature review, manuscript formatting, contributed to editing and finalizing the manuscript, and provided critical revisions to enhance the intellectual content of the paper.

  4. Use of Large Language Models, AI and Machine Learning Tools: None declared.

  5. Conflict of interest: The authors state no conflict of interest.

  6. Research funding: None declared.

  7. Data availability: Not applicable.

Nomenclature

R i,j

NG revenue made by exporting country i to importing country j

R i,k

NG revenue made by exporting country i to intermediate country k

R k,j

NG revenue made by intermediate country k to importing country j

C i,j

NG cost incurred by exporting country i to importing country j

C i,k

NG cost incurred by exporting country i to intermediate country k

C k,j

NG cost incurred by intermediate country k to importing country j

F LNG i,j

LNG flowrate from exporting country i to importing country j

F LNG i,k

LNG flowrate from exporting country i to intermediate country k

F LNG k,j

LNG flowrate from intermediate country k to importing country j

F PIPE i,j

flowrate of NG via pipeline from exporting country i to importing country j

F PIPE i,k

flowrate of NG via pipeline from exporting country i to intermediate country k

F PIPE k,j

flowrate of NG via pipeline from intermediate country k to importing country j

F i LNG Export Capacity

total LNG export capacity of country i

F j PIPE Import Capacity

total pipe capacity of country j

C RG,CAPEX

Regasification capital cost

C RG,OPEX

Regasification operating cost

C LIQ

LNG liquefaction cost

C STR

LNG storage cost

C SHIP

LNG shipping cost

C PIPE

Pipe maintenance cost

(θ)

Fraction

F NG-Base

Total LNG exports from base country

GC j Exist

Existing gasification capacity of country j

GC j Expand

Expanded gasification capacity of country j

GC k Exist

Existing gasification capacity of country k

GC k Expand

Expanded gasification capacity of country k

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Received: 2025-01-26
Accepted: 2025-08-11
Published Online: 2025-08-25

© 2025 Walter de Gruyter GmbH, Berlin/Boston

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