Dear T2Well users; Looking for a tool to design CO2 injection aiming at CCS. T2Well-ECO2N software is new to me, I wonder if it is only a 1D simulator? Do you have good experience with modelling near well effect of CO2 injection (for example in depleted reservoirs or else)? Is there any existing code coupling a T2Well module with Tough2 where the entire suite of EOS including EOS2 or EOS7C functioning in a 3D setting? I very much looking forward to and appreciate your possible response.
T2Well-ECO2N allows simulating the coupled wellbore-reservoir flow. Of course, while 1D flow is modeled along the wellbore, the reservoir can be discretised as usually made for standard TOUGH2 simulations, including 3D cartesian or unstructured grids.
T2Well-ECO2N is perfectly suitable for modeling near wellbore processes in full transient conditions.
When you mention depleted reservoirs what are you referring to? You cannot model CO2 injection in depleted natural gas reservoirs with T2Well-ECO2N, as it handles only H2O-NaCl-CO2 mixtures.
As far as I know T2Well was already coupled at LBNL also to ECO2M, EOS3, and an enhanced version of EOS8. I have worked with T2Well coupled to EWASG and EOS2H, the latter a version of EOS2 which is able to model steam-like supercritical conditions.
Coupling T2Well to one of the standard TOUGH2 EOS modules, such as EOS7C, is rather simple once you have access to both source codes.
Thank you Alfredo,
Your words made me to dig up a bit more. But still, I am in search for a non-isothermal Tough-based coupled well & reservoir modelling solution to model brine (or water+ NaCl)+Co2(all phases)+HC gases (at least CH4) including partitioning of CO2 in both gaseous and aqueous phases together with salt precipitation. I would rather avoid ToughReact if possible. I appreciate your further comment on this topic. A summary of what I could capture in Tough documentations regarding this topic follows:
EOS7C handles Brine, CH4-CO2 mixtures, CO2 in only non-condensable form, no phase transitions and no solid precipitation, 2 phases (G+Aq) and 5 components (W+Br+NCG+Tracer+CH4)
ECO2N handles H2O-NaCl-CO2 mixtures, CO2 in only non-condensable form, no phase transitions but solid appearance/disappearance, no HC gases, 3 phases (G+Aq+S) and 3 components (W+NaCl+CO2), P:1000 bar, T: 10-300’C
ECO2M handles H2O-NaCl-CO2 mixtures, CO2 in both gas and liquid phases, phase transitions and solid appearance/disappearance, no HC gases, 3 phases (G+Aq+S) and 3 components (W+NaCl+CO2), P: 600bar, T:10-110’C
I am aiming at using depleted gas field for CCS application. Is it right to say that a suitable EOS could be a step away from ECO2M due to the lack of CH4? I am not sure if there any ongoing EOS improvement to look for in the near future or it might be better idea to look for a Tough based simulation with something else; like Real Gas Brine (Moridis / Freeman??)?. Also important to see whether T2Well couplable to ECO2M as easy as ECO2N?
To help you decide whether you need ECO2M versus ECO2N, below is the phase diagram of CO2. If your problem will not cross the saturation line (shown in black) or get near the critical point (the end of the saturation line at about 31 C and 74 Bar), then ECO2N will work for you. But it does not have CH4, so that may be a deal breaker. If you opt for EOS7C, then you can have CH4, but no salt precipitation, and you still need to not cross the saturation line or get close to the critical point. The only EOS coupled to T2Well that is available to the public is ECO2N, but Alfredo may be able to point you to the people who have created other versions for their own use on particular projects, and they might be willing to share them with you. I am not so familiar with Real Gas Brine, but according to the user's guide, you can have CO2, CH4, and salt that can precipitate. CO2 is described as a "condensable" gas, but there does not appear to be a provision for more than two fluid phases (aqueous and gas), so it may be that you cannot cross the saturation line there either. I don't see any mention of a wellbore simulator in Real Gas Brine, but it does include an option for non-Darcian turbulent flow, which you might find reasonable to represent wellbore flow.
Thank you Christine and Alfredo;
for useful advises and pointing out rational behind the EOS’s constraints. I hope that I will be able to come in contact with people aiming at similar applications, including the ones that might have coupled ECO2M.
However, With cold- but deep injection and heterogenous anticline structure, I expect entering the P/T envelope around critical point is inevitable. We have also to include a supercritical phase, whether dealt with as a “dense unique phase” or a liquid within an extended physio/thermodynamic property envelope. I have to peruse further what you indicated on RGB, regarding handling of CO2 phases. From the manual you get the impression that CO2 partitioning finds place properly??
The other thing that I try to find out is the scalability and simulation efficiency when you undertake a storage project of huge dimension that should be modelled and run for at least 10 decades. Here, it might come the question of using Though2, Tough+ or other alternative able to use effectively 10s/100s of cpu cores in parallel. I appreciate any reference or advice on that front as well.
ECO2M has been already coupled to a new, 3-phase flow version of T2well coded by Lehua Pan. It can handle all the phase combinations of H2O-NaCl-CO2 mixtures, including halite precipitation. But it cannot handle CH4.
If you really need 3-phase flow with multicomponent inorganic and organic fluid mixtures, I think the only code of TOUGH family able to do that is TOGA by Lehua Pan. Its distribution by LBNL started in 2020.
But TOGA should be coupled to the new 3-phase version of T2Well for coupled wellbore-reservoir flow simulations.
T2Well implements a full transient approach for wellbore flow which is in particular suitable for simulating the wellbore transients at injection startup or shut-in. For long term field-wide simulations of CCS with multiple wells, T2Well might increase the simulation time because of tiny time steps required for solving strong wellbore transients.
Years ago I coded wellbore flow equations in a TOUGH2 version assuming wellbore flow was steady-state within each time step. The solution was not so accurare as that of T2Well for injection start-up, but was satisfactory when modeling longterm injection with slow transients.
That version is coupled to the TMGAS EOS which can handle mixtures of inorganic gases and HCs (C1-C10, BTEX, +pseudo-components for C10+).
The non aqueous mixture can be in gas, liquid or supercritical conditions, but only two-phase brine - non-aqueos phase equilbrium can be simulated. That is only one NAq phase can be present at the same time in one grid element.
We run injection of CO2-rich mixtures in gas reservoirs and saline aquifers and of sour or acid gas mixtures in undersaturated oil reservoirs (see Battistelli et al., 2010; Castelletto et al. 2013 IJGGC; Battistelli et al., 2011 TiPM).
This year I'll probably work on the coupling of TMGAS to T2Well. A 3-phase version of TMGAS was always considered, but never developed...
TOGA does handle three-phase flow, and when I asked Lehua about the possibility of using it for CO2 in liquid, gaseous, and supercritical phases (like ECO2M), he said that formally it should work, but that he has not tested it.
Regarding your other question about running in parallel, TOUGH3 and TOUGH+ can be run in parallel, but the current version of TOGA is not designed to do that.
Thank you both for important additional information.
I feel that I have now some clue about the capabilities of the codes. Your input have been very helpful. I will definitely have to learn more and follow further development of, not least- your well flow module. It is particularly interesting at the stage when we will estimate large dimension storage and need speedy cpu with less transient around the sinks/sources. My prime aim now is to be able to model the near wellbore phenomenon when dry CO2 is injected into very saline aquifer or deep depleted HC formation. This will also mean estimating water vaporization and resulting salt precipitation (reduced injectivity) under transient condition and frequent shut-in events, which is expected in such projects.
Thanks again to both of you.
if you are interested primarily to simulate fast transients at well start-up or shut-in, then you definetely have to use T2Well.
For pure CO2 injection in saline aquifers with T<100°C and single fase flow within the wellbore, T2Well-ECO2N, already distributed by LBNL, can do the job.
T2Well-ECO2M can also simulate 3-phase flow (including the wellbore) and T up to 300°C. I think it is still a research code not yet distributed by LBNL. A search on the TOUGH web site can confirm that.
We are working with T2Well-ECO2M evaluating the code capabilities for CO2 sequestration in saline aquifers. Some results with a slightly modified code version are documented by Strpić et al. (2020). "Modeling of transient multiphase flow in a CO2 injection well with the wellbore-reservoir coupled simulator T2Well-ECO2M". GET2020, 1st Geoscience & Engineering in Energy Transition Conference.
As previously mentioned, when other components are involved (such as other inorganic gases or hydrocarbons), no rediliy available tools seems to be available within the official LBNL TOUGH2/3 family of codes.
I suggest to have a look to Shabani and Vilcaez (2018) for an EOS module for mixtures of CO2-CH4-H2S-N2 (Comp. & Geosc.) and to Loeve et al. (2014), GHGT-12, for an EOS module which includes the handling of CO2-CH4 3-phase mixtures.