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Re: applying heat load in BHE and varying input T? I guess you should remove the inactive cell at DHE input and use GENER to inject your variable fluid rate history by assigning the injection enthalpy corresponding to your desired inlet T vs time.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 3 days ago
- TOUGH2
- Reported - view
Re: applying heat load in BHE and varying input T? Dear Hanna, I understood you want to apply a heat load to your entire BHE. But you applied the heat load by just injecting heat into the BHE inlet (eleme A1000).…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 10 days ago
- TOUGH2
- Reported - view
Re: CHEMP block for diesel and gasoline? Mikey, as diesel fuel and gasoline are complex HC mixtures, if you want to simulate approximately their thermodynamic behaviour you might use a pseudo-component approach as customary made in the O&G…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 mth ago
- TMVOC
- Reported - view
Re: Pressure vs CO2 DG Jose, if you are using T2Well, it would probably mean that domain belongs to a wellbore section for which you want the calculation of wellbore heat exchange using the analytical formulation by Ramey.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 mth ago
- TOUGH2
- Reported - view
Re: Pressure reporting: Tgh2-ECO2M Apologize for the typo: I used T2Well-ECO2M (not ECOM). A.
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 mth ago
- TOUGH2
- Reported - view
Re: Efficient time stepping with great variability in pumping/shutin period durations Yannick, I would try using the actual pumping history with MOP(12) =2. In this way you should at least replicate the cumulative production during each time step.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 mth ago
- TOUGH3
- Reported - view
Re: Pressure reporting: Tgh2-ECO2M Godarzi, I need to clarify my previous post. The ECOM version I used is V.2 by Lehua Pan which can simulate H2O-CO2-NaCl mixtures up to 300°C. It seems it is not able to accept the ECO2N style INCON…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 mth ago
- TOUGH2
- Reported - view
Re: Pressure reporting: Tgh2-ECO2M Hi Godarzi. I tried your input file with T2Well-ECO2M, of course with no wellbore flow. The P vs log(radius) at 1 year is shown below. In your input file I noticed that you have omitted the phase…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 mth ago
- TOUGH2
- Reported - view
Re: Relative permeability curves in tough2 Dear Emad, I would try with the VG model for the water phase and the Corey model for the gas phase using the set of parameters listed below. The two figures show a reasonable match of your data.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 mth ago
- 1
- TOUGH2
- Reported - view
Re: How to create meshes with local grid refinements Dear Alejandro, As suggested by Stefano, VORO2MESH can build full 3D unstructured grids conforming to the IFDM used by TOUGH2/3. The possible refinement of 2D cartesian grids for TOUGH2 was…
Attachment
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 mth ago
- Pre & Post Processors
- Reported - view
Re: Radioactive chain decay Hi Kaveh, I would remind that if one is interested to an isotope decay chain only, but not to model water-rock equilibria with TOUGHREACT, a generic isotope decay chain or even multiple chains could…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 mth ago
- TOUGHREACT
- Reported - view
Re: JT Heat exchange in the cell containing well (using ECO2N) Dear Godarzi, if I properly understood your question, in T2Well-ECO2N (as in all TOUGH2/3 simulators) there are no specific options to model JT effects.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 4 mths ago
- TOUGH2
- Reported - view
Re: Can TOUGH3 model temperature below zero degree? As reminded by Christine, TOUGH2/3 cannot handle T below the triple point of water, as 0.01°C is the lower limit for the old IFC67 and the new IAPWS-IF97 correlations for the properties of water and…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 4 mths ago
- TOUGH3
- Reported - view
Re: TMVOC initial conditions Convergence Failure Dear Mostafa, you have specified 3-phase conditions for the CLAY zone with SO=0.1, which is a bit strange if you want to simulate first a steady-state before the NAPL spill.…
Attachment
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 4 mths ago
- TMVOC
- Reported - view
Re: TMVOC initial conditions Convergence Failure Dear Mostafa, It is a bit hard to comment about the convergence problem you mention without running the model. Could you share the Petrasim file? If you can, my email is alf_batt@yahoo.com .…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 5 mths ago
- 1
- TMVOC
- Reported - view
Re: how to cancel or minimize VOC volatilization Dear Ziming, if you want to reduce the evaporation of VOCs from the NAPL phase, you may consider to reduce their vapor pressure which is computed either by the Wagner or Antoine eqs (eqs. 4.3.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 7 mths ago
- TMVOC
- Reported - view
Re: Pore Compressibility in ECO2M For 'initial pressure' I do mean the P of each element at the beginning of a simulation run. If you need a steady state run and you activate the pore compressibility (>0.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 7 mths ago
- 1
- TOUGH2
- Reported - view
Re: Pore Compressibility in ECO2M Dear Nur, pore compressibility changes the rock porosity as function of pressure change occurring in time since the start of simulation with respect to the initial pressure.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 7 mths ago
- TOUGH2
- Reported - view
Re: T2Well constant fluid properties and EOS1 relationship? Dear Hannah, if I understood properly your question, you would like to have a variable P boundary, with P varying in time according to some constraint specific of your simulated problem.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 9 mths ago
- TOUGH2
- Reported - view
Re: T2Well constant fluid properties and EOS1 relationship? Dear Hanna, fluid properties will be computed according to local conditions by the EOS (EOS1 in your case) in all grid elements, either belonging to reservoir or wellbore.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 9 mths ago
- 1
- TOUGH2
- Reported - view
Re: T2Well constant fluid properties and EOS1 relationship? Dear Hanna, the parameters listed under ROCKS block are related to wellbore discretization elements, not to the fluid flowing within the wellbore. Fluid properties are computed according to the…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 9 mths ago
- 2
- TOUGH2
- Reported - view
Re: Code: modify the Biodegradation module in TMVOC Dear Guiyao, biodegradation capabilities were added to TMVOC V.1.0 (Pruess and Battistelli, 2002) in a version called TMVOCBio, which was not distributed at the time.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 10 mths ago
- TMVOC
- Reported - view
Re: bugs or misunderstanding? Dear Jian, about your comments related to T2VOC: 1) simply at the time the density of aqueous phase was not added to the printout. Of course it is not a bug: adding Daq printout would be very easy.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 11 mths ago
- T2VOC
- Reported - view
Re: Constant gas production rate Dear Ozawa, requiring a constant NCG production rate when a multicomponent mixture is present might not be physical. But going to your question from a purely modeling point of view: 1.…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 yr ago
- TOUGH2
- Reported - view
Re: EOS7 - Brine Definition & Tracing flow of brines I think you have to consider the intrinsic limitations of EOS7 approach to model a brine of variable salinity. Strong evaporation processes may increase the brine fraction Xb over 1,…
- Alfredo Battistelli
- Reservoir Engineer
- Alfredo_b
- 1 yr ago
- TOUGH2
- Reported - view

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Alfredo Battistelli

Alfredo_b

Reservoir Engineer

Italy

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