Lars Hov Odsæter

Dr. Lars Hov Odsæter

orcid

Research Focus & Metrics

Academic Career Length

12Years (2015-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

View All Publications
1 January 2019 in Computer Methods in Applied Mechanics and Engineering
Verified
Journal Article
Open access
LOLars Hov Odsæter
Lars Hov Odsæter
TKTrond Kvamsdal
Trond Kvamsdal
MLMats G. Larson
Mats G. Larson

1 March 2017 in Computer Methods in Applied Mechanics and Engineering
Verified
Journal Article
Open access
LOLars Hov Odsæter
Lars Hov Odsæter
MWMary F. Wheeler
Mary F. Wheeler
TKTrond Kvamsdal
Trond Kvamsdal
MLMats G. Larson
Mats G. Larson
A conservative flux postprocessing algorithm is presented for both steady-state and dynamic flow models. The postprocessed flux is shown to have the same convergence order as the original flux. An arbitrary flux approximation is projected into a conservative subspace by adding a piecewise constant correction that is minimized in a weighted $L^2$ norm. The application of a weighted norm appears to yield better results for heterogeneous media than the standard $L^2$ norm which has been considered in earlier works. We also study the effect of different flux calculations on the domain boundary. In particular we consider the continuous Galerkin finite element method for solving Darcy flow and couple it with a discontinuous Galerkin finite element method for an advective transport problem.Comment: 34 pages, 17 figures, 11 table

21 September 2015 in Transport in Porous Media
Verified
Journal Article
Open access
PDF file
LOLars Hov Odsæter
Lars Hov Odsæter
CBCarl Fredrik Berg
Carl Fredrik Berg
ARAlf Birger Rustad
Alf Birger Rustad
Steady-state upscaling of relative permeability is studied for a range of reservoir models. Both rate-dependent upscaling and upscaling in the capillary and viscous limits are considered. In particular, we study fluvial depositional systems, which represent a large and important class of reservoirs. Numerical examples show that steady-state upscaling is rate dependent, in accordance with previous work. In this respect we introduce a scale-dependent capillary number to estimate the balance between viscous and capillary forces. The difference between the limit solutions can be large, and we show that the intermediate flow rates can span several orders of magnitude. This substantiate the need for rate-dependent steady-state upscaling in a range of flow scenarios. We demonstrate that steady-state upscaling converges from the capillary to the viscous limit solution as the flow rate increases, and we identify a simple synthetic model where the convergence fails to be monotone. Two different sets of boundary conditions were tested, but had only minor effects on the presented reservoir models. Finally, we demonstrate the applicability of steady-state upscaling by performing dynamic flow simulation at the reservoir scale, both on fine-scaled and on upscaled models. The considered model is viscous dominated for realistic flow rates, and the simulation results indicate that viscous limit upscaling is appropriate.

6 August 2021 in Energies
Verified
Journal Article
Open access
PDF file
LOLars Hov Odsæter
Lars Hov Odsæter
HSHans Skarsvåg
Hans Skarsvåg
EAEskil Aursand
Eskil Aursand
FUFederico Ustolin
Federico Ustolin
GRGunhild A. Reigstad
Gunhild A. Reigstad
Nicola PaltrinieriNicola Paltrinieri
Nicola Paltrinieri
Liquid hydrogen (LH2) spills share many of the characteristics of liquefied natural gas (LNG) spills. LNG spills on water sometimes result in localized vapor explosions known as rapid phase transitions (RPTs), and are a concern in the LNG industry. LH2 RPT is not well understood, and its relevance to hydrogen safety is to be determined. Based on established theory from LNG research, we present a theoretical assessment of an accidental spill of a cryogen on water, including models for pool spreading, RPT triggering, and consequence quantification. The triggering model is built upon film-boiling theory, and predicts that the mechanism for RPT is a collapse of the gas film separating the two liquids (cryogen and water). The consequence model is based on thermodynamical analysis of the physical processes following a film-boiling collapse, and is able to predict peak pressure and energy yield. The models are applied both to LNG and LH2, and the results reveal that (i) an LNG pool will be larger than an LH2 pool given similar sized constant rate spills, (ii) triggering of an LH2 RPT event as a consequence of a spill on water is very unlikely or even impossible, and (iii) the consequences of a hypothetical LH2 RPT are small compared to LNG RPT. Hence, we conclude that LH2 RPT seems to be an issue of only minor concern.

26 October 2020 in Greenhouse Gases: Science and Technology
Verified
Journal Article
Open access
PDF file
SMSvend Tollak Munkejord
Svend Tollak Munkejord
MHMorten Hammer
Morten Hammer
ÅEÅsmund Ervik
Åsmund Ervik
LOLars Hov Odsæter
Lars Hov Odsæter
HLHalvor Lund
Halvor Lund
We present a model framework for dynamic simulation of the flow of CO 2 and other components in an injection well coupled with a near‐well reservoir. With a partitioned approach, we employ numerical methods adapted to the governing equations in each domain. In both well and reservoir, accurate thermodynamics are used. This model can be used for various design and operational considerations for CO 2 ‐injection wells, that is, the quantification of pressure and temperature transients, and phase composition, including the appearance of a water‐rich phase. We study cases where the flow in the well and the near‐well reservoir is dynamically coupled. The rock properties are seen to strongly affect the well dynamics, both regarding magnitude and transient evolution of the bottom‐hole pressure. We consider a variation of this case where water is co‐injected with CO 2 , showing that this is a potential method to mitigate salt precipitation. We also consider intermittent injection, representing the case of direct injection from ships transporting CO 2 . Finally, we observe that in the present cases, a coupled model (as opposed to a well‐only model) is necessary in order to capture the dynamics in the well during injection. © 2020 Society of Chemical Industry and John Wiley & Sons, Ltd.