November 7, 2020 at 11:17 amveeraSubscriber
for my problem , inlet temperature is more than inlet temperature , i am using pressure based approach , transient conditions, density is ideal gas
even i monitored velocity also , it is very very low , so i cant sure about kinetic energy , and any other factor my temperature is more than inlet temperatureNovember 9, 2020 at 1:36 pmKarthik RAdministratorHello,nHow are you calculating this inlet temperature? Please provide the necessary screenshots so we are able to understand this better? nAlso, what is the boundary condition at your inlet? What are the boundary conditions at the adjoining wall?nThank you.nKarthiknNovember 10, 2020 at 4:52 amNovember 10, 2020 at 12:07 pmRobAnsys EmployeePlot temperature, pressure and flow field so we can see what's going on. How well converged is the solution? nNovember 25, 2020 at 10:06 amveeraSubscriberThat is well converged one sir , but I need to update one , I run simulation both the cases as pressure based approach and density based approach , nfor steady case approach , temperature is not existing the inlet temperature ..there its finenin transient approach , if i use constant inlet with pressure based approach .. temperature is not more than inlet temperature nbut when i use variable pressure boundary at inlet ..its more than inlet temperature for the both pressure and density based approachesnso please help me to resolve this issuesnnNovember 25, 2020 at 10:18 amRobAnsys EmployeeWhat variable pressure? How much warmer does the domain get? Remember as gas compresses it'll heat up. Assuming you're modelling with ideal gas. nNovember 25, 2020 at 11:11 amNovember 25, 2020 at 4:24 pmRobAnsys EmployeeFlow enters the domain and doesn't leave. It's an ideal gas. Domain is adiabatic. If the pressure increases, what should the temperature do? nNovember 25, 2020 at 4:56 pmDrAmineAnsys EmployeeHot hotnNovember 26, 2020 at 6:09 amveeraSubscriberbut in steady case , this not the case wright , why only in transient pressure variable at inletnNovember 26, 2020 at 6:11 amveeraSubscriberthank you , rob sir np = rho * R * T neven temperature also i used to give variable temperaturenNovember 26, 2020 at 7:01 amveeraSubscriberso i gave p and T as input so , with that ideal equations are calculated , or what is the case sir nNovember 26, 2020 at 9:07 amDrAmineAnsys EmployeeHi,be patient when raising a question. While raising a question: provide all necessary information. Can you now summarize the whole problem in a single message?nNovember 26, 2020 at 11:25 amveeraSubscriberyes , DrAminenGENERAL : Pressure based approach , TRANSIENT conditionsnMATERIAL: H2O (ideal gas law)nINLET: TWO INLET : VARYING PRESSURE BASED INLET CONDTIONS AND TEMPERATURE (EXPERIMENATL RESULTS)nnOUTLET : CLOSED (wall adiabatic)nWALL : ADIABATIC AND HEAT FLUX = 0nnabove mentioned is basic setup for my problem , when i am running this setup , withinin few seconds i am getting average temperature inside the domain volume is more than inlet temperature what i am specified at variable temperature inletneven i approach the same setup with density based approach , I am getting same error (average temperature inside the domain more than inlet specified)nNovember 26, 2020 at 11:32 amRobAnsys EmployeePlease plot the volume average temperature on the same graph as the inlet temperature against time. Also post the convergence plot. Going back to my earlier question, why shouldn't the domain get warmer as you compress the gas?nNovember 27, 2020 at 5:58 amNovember 27, 2020 at 11:58 amDrAmineAnsys Employee@veera, @Rob, asked for '..Please plot the volume average temperature on the same graph as the inlet temperature against time.'
we not compressing the fluid , we plotted Mach number also . that is very very less convergence plothttps://us.v-cdn.net/6032193/uploads/NILKTRM4JW3I/image.pnghttps://forum.ansys.com/discussion/comment/98545#Comment_98545nViewing 16 reply threads
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