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-   -   error in run (https://www.cfd-online.com/Forums/converge/241630-error-run.html)

farnaz.rezaei March 9, 2022 13:25

error in run
 
Hi

when I want to run in converge v3 there is some error than I cant fixed it
I need help

Error is:
= BAD TERMINATION OF ONE OF YOUR APPLICATION PROCESSES

= RANK 2 PID 7608 RUNNING AT DESKTOP-TATL411H

= EXIT STATUS: -1073741515 (c00001135)

jetcheve March 9, 2022 16:22

Quote:

Originally Posted by farnaz.rezaei (Post 823863)
Hi

when I want to run in converge v3 there is some error than I cant fixed it
I need help

Error is:
= BAD TERMINATION OF ONE OF YOUR APPLICATION PROCESSES

= RANK 2 PID 7608 RUNNING AT DESKTOP-TATL411H

= EXIT STATUS: -1073741515 (c00001135)

Hi, Farnaz!

Unfortunately this error message by itself is impossible to troubleshoot with additional information Could you provide more information? What version are you using? What are you trying to do? When does this error occur? Is there more information that is given such as a warning or a more detailed error message?

Thanks!

- John

farnaz.rezaei March 10, 2022 02:01

Hi

I use version 3.0.17
when I want run converge this massage appear in run page and then stop running and write finished.
I am running one-cycle, four stroke of a motored DI engine and fuel is diesel2.
my case setup has no error and validate all.
as the ‘‘baseline simulations,” the flow field solution was implemented using the Re-Normalization Group (RNG) Reynolds Averaged Navier–Stokes (RANS) k–e turbulence model. The primary and secondary breakup of the injected fuel were modeled using the Kelvin–Helmholtz and Rayleigh–Taylor (KH–RT) models.

jetcheve March 10, 2022 13:17

Quote:

Originally Posted by farnaz.rezaei (Post 823884)
Hi

I use version 3.0.17
when I want run converge this massage appear in run page and then stop running and write finished.
I am running one-cycle, four stroke of a motored DI engine and fuel is diesel2.
my case setup has no error and validate all.
as the ‘‘baseline simulations,” the flow field solution was implemented using the Re-Normalization Group (RNG) Reynolds Averaged Navier–Stokes (RANS) k–e turbulence model. The primary and secondary breakup of the injected fuel were modeled using the Kelvin–Helmholtz and Rayleigh–Taylor (KH–RT) models.

Farnaz -

First, I would try updating your solver to the latest version in case this is a known issue that we have fixed already.

Next, if you could tell me if there are any errors or warnings and when the crash occurs that would be helpful. Unfortunately the error message you've provided doesn't tell us much without more context.

- John


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