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- SUBROUTINE FricPressDrop(iloc)
-
-
-
- !! Record of revisions
- !! Date Programmer Discription of change
- !! ------ ------------ -----------------------
- !! 1396/07/23 Sheikh Original code
- !!
-
-
-
- USE FricPressDropVars
- USE CMudPropertiesVariables
- USE Fluid_Flow_Startup_Vars
- USE CError
-
- IMPLICIT NONE
-
- INTEGER :: iloc
- REAL :: TauZero
- TauZero = 12.0
- !ActiveRheologyModel = Herschel_Bulkley_RheologyModel
-
- ! 0 = Power Law , 1 = Bingham Plastic , 2 = Newtonian
- !TotFricPressLoss = 0.0
-
- FlowEl(iloc)%alpha = 1 ! assume that all elements have annulus geometry
- FlowEl(iloc)%dPdLfric = 0.0
- FlowEl(iloc)%f = 0.0
- FlowEl(iloc)%FlowRate = ABS(FlowEl(iloc)%FlowRate)
-
-
-
- IF ((FlowEl(iloc)%FlowRate >= PressFlowrateTolerance) &
- .AND. (FlowEl(iloc)%MaterialType /= 1) & ! not gas kick
- .AND. (ABS(FlowEl(iloc)%Length) >= PressLengthTolerance) &
- .AND. (FlowEl(iloc)%MaterialType /= 4)) THEN ! not air
-
- IF (FlowEl(iloc)%Id==0) THEN
- FlowEl(iloc)%alpha = 0
- END IF
-
- FlowEl(iloc)%muPlastic = FlowEl(iloc)%Theta600 - FlowEl(iloc)%Theta300 ! cp
- FlowEl(iloc)%YieldP = 2.0 * FlowEl(iloc)%Theta300 - FlowEl(iloc)%Theta600 ! lbf/100ft**2
- FlowEl(iloc)%nIndex = 3.32 * log10(FlowEl(iloc)%Theta600 / FlowEl(iloc)%Theta300)
- FlowEl(iloc)%kIndex = 510.0 * FlowEl(iloc)%Theta300 / (511.0**FlowEl(iloc)%nIndex) ! rabete fv2
- IF (MudProperties%ActiveRheologyModel == Herschel_Bulkley_RheologyModel .AND. FlowEl(iloc)%alpha == 0) THEN
- FlowEl(iloc)%kIndex = 1.066 * FlowEl(iloc)%Theta300 / (511.0**FlowEl(iloc)%nIndex)
- ELSE IF (MudProperties%ActiveRheologyModel == Herschel_Bulkley_RheologyModel .AND. FlowEl(iloc)%alpha == 1) THEN
- FlowEl(iloc)%nIndex = 3.32 * log10((FlowEl(iloc)%Theta600 - TauZero) / (FlowEl(iloc)%Theta300 - TauZero))
- FlowEl(iloc)%kIndex = 1.066 * (FlowEl(iloc)%Theta300 - TauZero) / (511.0**FlowEl(iloc)%nIndex)
- END IF
-
-
-
-
- ! Calculating velocity
- FlowEl(iloc)%vel = 0.408 * FlowEl(iloc)%FlowRate / (FlowEl(iloc)%Od**2 - FlowEl(iloc)%Id**2) ! velocity in ft/s
- !FlowEl(iloc)%vel = 24.51 * FlowEl(iloc)%FlowRate / (FlowEl(iloc)%Od**2 - FlowEl(iloc)%Id**2) ! velocity in ft/min
-
- !IF (FlowModel == Bingham_RheologyModel) THEN ! Bingham Plastic
- ! FlowEl(iloc)%Gf = (2. + FlowEl(iloc)%alpha) / 2.
- !ELSE IF (FlowModel == PowerLow_RheologyModel) THEN
- ! FlowEl(iloc)%Gf = ((3. - FlowEl(iloc)%alpha) * FlowEl(iloc)%nIndex + 1.) / FlowEl(iloc)%nIndex / (4. - FlowEl(iloc)%alpha) * (2. + FlowEl(iloc)%alpha) / 2.
- !END IF
-
- !FlowEl(iloc)%gammaW = 1.6 * FlowEl(iloc)%Gf * FlowEl(iloc)%vel / FlowEl(iloc)%Dhyd
-
- !IF (FlowModel == Bingham_RheologyModel) THEN ! Bingham Plastic
- ! FlowEl(iloc)%tauW = 1.067 * ((4. - FlowEl(iloc)%alpha) / (3. - FlowEl(iloc)%alpha) * FlowEl(iloc)%YieldP + FlowEl(iloc)%muPlastic * FlowEl(iloc)%gammaW)
- ! !FlowEl(iloc)%tauW = 1.067*(FlowEl(iloc)%YieldP+FlowEl(iloc)%muPlastic*FlowEl(iloc)%gammaW)
- !ELSE IF (FlowModel == PowerLow_RheologyModel) THEN ! Power law
- ! FlowEl(iloc)%tauW = 1.067 * FlowEl(iloc)%kIndex * FlowEl(iloc)%gammaW**FlowEl(iloc)%nIndex
- !END IF
-
- ! Calculating effective or apparent viscosity
- IF (MudProperties%ActiveRheologyModel == Bingham_RheologyModel) THEN ! Bingham Plastic
- FlowEl(iloc)%mueff = FlowEl(iloc)%muPlastic + 5. * FlowEl(iloc)%YieldP * FlowEl(iloc)%Dhyd / FlowEl(iloc)%vel
- !write(*,*) 'pointer1' , FlowEl(iloc)%muPlastic , FlowEl(iloc)%YieldP , FlowEl(iloc)%Dhyd , FlowEl(iloc)%vel
- ELSE IF (MudProperties%ActiveRheologyModel == PowerLaw_RheologyModel .OR. MudProperties%ActiveRheologyModel == Herschel_Bulkley_RheologyModel) THEN ! Power Law
- FlowEl(iloc)%Gf = ((3. - FlowEl(iloc)%alpha) * FlowEl(iloc)%nIndex + 1.0) / FlowEl(iloc)%nIndex / (4.0 - FlowEl(iloc)%alpha) * (2.0 + FlowEl(iloc)%alpha) / 2.0
- FlowEl(iloc)%mueff = (FlowEl(iloc)%kIndex) / (1. + FlowEl(iloc)%alpha / 2.) * ((96. * FlowEl(iloc)%vel / FlowEl(iloc)%Dhyd)**(FlowEl(iloc)%nIndex - 1)) * FlowEl(iloc)%Gf**FlowEl(iloc)%nIndex
- !write(*,*) 'pointer2' , FlowEl(iloc)%kIndex ,FlowEl(iloc)%alpha , FlowEl(iloc)%vel ,FlowEl(iloc)%Dhyd,FlowEl(iloc)%nIndex ,FlowEl(iloc)%Gf ,FlowEl(iloc)%nIndex
- END IF
-
- FlowEl(iloc)%gammaW = 96.0 * FlowEl(iloc)%Gf * FlowEl(iloc)%vel / FlowEl(iloc)%Dhyd
-
- FlowEl(iloc)%tauW = ((4.0 - FlowEl(iloc)%alpha) / (3.0 - FlowEl(iloc)%alpha))**FlowEl(iloc)%nIndex * TauZero + FlowEl(iloc)%kIndex * FlowEl(iloc)%gammaW**FlowEl(iloc)%nIndex
-
-
- ! Calculating Reynolds number
- IF (FlowEl(iloc)%Od == FlowEl(iloc)%Dhyd) THEN
- FlowEl(iloc)%GenRe = 928. * FlowEl(iloc)%density * FlowEl(iloc)%vel * FlowEl(iloc)%Dhyd / FlowEl(iloc)%mueff
- ELSE
- FlowEl(iloc)%GenRe = 757. * FlowEl(iloc)%density * FlowEl(iloc)%vel * FlowEl(iloc)%Dhyd / FlowEl(iloc)%mueff
- END IF
-
- !FlowEl(iloc)%GenRe = 2997 * FlowEl(iloc)%density * FlowEl(iloc)%vel**2 / 19.36 / FlowEl(iloc)%tauW
-
- ! Calculating friction factor
- IF (MudProperties%ActiveRheologyModel == Bingham_RheologyModel) THEN ! Bingham Plastic
- IF (FlowEl(iloc)%GenRe <= 2000.0) THEN ! laminar regime
- FlowEl(iloc)%f = 16.0 / FlowEl(iloc)%GenRe
- ELSE IF (FlowEl(iloc)%GenRe >= 4000.0) THEN ! turbulent regime
- FlowEl(iloc)%a = 0.0791
- FlowEl(iloc)%b = 0.25
- FlowEl(iloc)%f = FlowEl(iloc)%a / FlowEl(iloc)%GenRe**FlowEl(iloc)%b
- ELSE !! transition from laminar to turbulent regime
- FlowEl(iloc)%a = 0.0791
- FlowEl(iloc)%b = 0.25
- FlowEl(iloc)%f = (4000.0 - FlowEl(iloc)%GenRe) / 2000.0 * 16. / FlowEl(iloc)%GenRe &
- + (FlowEl(iloc)%GenRe - 2000.0) / 2000.0 * FlowEl(iloc)%a / FlowEl(iloc)%GenRe**FlowEl(iloc)%b
- END IF
-
- ELSE IF (MudProperties%ActiveRheologyModel == PowerLaw_RheologyModel) THEN ! Power law
- FlowEl(iloc)%ReCritLam = 3470. - 1370. * FlowEl(iloc)%nIndex
- FlowEl(iloc)%ReCritTurb = 4270. - 1370. * FlowEl(iloc)%nIndex
-
- IF (FlowEl(iloc)%GenRe <= FlowEl(iloc)%ReCritLam) THEN ! laminar regime
- FlowEl(iloc)%f = 16.0 / FlowEl(iloc)%GenRe / (1 - 0.184 * FlowEl(iloc)%alpha)
- ELSE IF (FlowEl(iloc)%GenRe >= FlowEl(iloc)%ReCritTurb) THEN ! turbulent regime
- FlowEl(iloc)%a = (log10(FlowEl(iloc)%nIndex) + 3.93) / 50.
- FlowEl(iloc)%b = (1.75 - log10(FlowEl(iloc)%nIndex)) / 7.
- FlowEl(iloc)%f = FlowEl(iloc)%a / FlowEl(iloc)%GenRe**FlowEl(iloc)%b
- ELSE
- FlowEl(iloc)%a = (log10(FlowEl(iloc)%nIndex) + 3.93) / 50.
- FlowEl(iloc)%b = (1.75 - log10(FlowEl(iloc)%nIndex)) / 7.
- FlowEl(iloc)%f = (FlowEl(iloc)%ReCritTurb - FlowEl(iloc)%GenRe) / 800.0 * 16. / FlowEl(iloc)%GenRe &
- + (FlowEl(iloc)%GenRe - FlowEl(iloc)%ReCritLam) / 800.0 * FlowEl(iloc)%a / FlowEl(iloc)%GenRe**FlowEl(iloc)%b
- END IF
-
- END IF
-
- !WRITE (*,*) 'fric press drop', iloc
- !WRITE (*,*) 'Length', ABS(REAL(FlowEl(iloc)%Length))
- !WRITE (*,*) 'FlowRate', FlowEl(iloc)%FlowRate
- !WRITE (*,*) 'Theta600 , Theta300', FlowEl(iloc)%Theta600 , FlowEl(iloc)%Theta300
- !WRITE (*,*) 'Dhyd', FlowEl(iloc)%Dhyd
- !WRITE (*,*) 'GenRe', FlowEl(iloc)%GenRe
- !WRITE (*,*) 'f', FlowEl(iloc)%f
-
-
-
-
- END IF
-
- ! Frictional pressure loss gradient calculation
- ! FlowEl(iloc)%dPdLfric = 1.076 * FlowEl(iloc)%f * FlowEl(iloc)%vel**2 * FlowEl(iloc)%density / 10**5 / FlowEl(iloc)%Dhyd
- FlowEl(iloc)%dPdLfric = FlowEl(iloc)%f * (FlowEl(iloc)%vel)**2 * FlowEl(iloc)%density / 25.81 / FlowEl(iloc)%Dhyd
- FlowEl(iloc)%FricPressLoss = FlowEl(iloc)%dPdLfric * ABS(REAL(FlowEl(iloc)%Length))
-
- IF (FlowEl(iloc)%FrictionDirection == -1) THEN
- FlowEl(iloc)%FlowRate = - FlowEl(iloc)%FlowRate
- FlowEl(iloc)%dPdLfric = - FlowEl(iloc)%dPdLfric
- FlowEl(iloc)%FricPressLoss = - FlowEl(iloc)%FricPressLoss
- END IF
-
-
-
- !END DO
-
-
- END SUBROUTINE FricPressDrop
-
-
- SUBROUTINE PartialDerivativeFricToFlowRate(iloc)
-
- USE FricPressDropVars
- USE CMudPropertiesVariables
- USE Fluid_Flow_Startup_Vars
- USE KickVariables
- USE CError
-
-
- IMPLICIT NONE
-
- INTEGER :: iloc
-
- FlowEl(iloc)%FricToQPartialDiff = 0.0
- !FlowEl(iloc)%FlowRate = ABS(FlowEl(iloc)%FlowRate)
-
-
- IF ((ABS(FlowEl(iloc)%FlowRate) >= PressFlowrateTolerance) &
- .AND. (FlowEl(iloc)%MaterialType /= 1) & ! not gas kick
- .AND. (ABS(FlowEl(iloc)%Length) >= PressLengthTolerance) &
- .AND. (FlowEl(iloc)%MaterialType /= 4)) THEN ! not air
-
- IF (MudProperties%ActiveRheologyModel == PowerLaw_RheologyModel) THEN ! Power law
- !IF (FlowEl(iloc)%Flowrate == 0.0) THEN
- ! FlowEl(iloc)%Flowrate = 10.0
- ! CALL FricPressDrop(iloc)
- !END IF
- IF (FlowEl(iloc)%GenRe <= FlowEl(iloc)%ReCritLam) THEN ! laminar flow
- FlowEl(iloc)%FricToQPartialDiff = FlowEl(iloc)%FricPressLoss / FlowEl(iloc)%FlowRate * FlowEl(iloc)%nIndex
-
- ELSE IF (FlowEl(iloc)%GenRe >= FlowEl(iloc)%ReCritTurb) THEN ! turbulent flow
- FlowEl(iloc)%FricToQPartialDiff = FlowEl(iloc)%FricPressLoss / FlowEl(iloc)%FlowRate &
- * (2. - FlowEl(iloc)%b * (2. - FlowEl(iloc)%nIndex))
-
- ELSE ! transition from laminar to turbulent
- FlowEl(iloc)%FricToQPartialDiff = FlowEl(iloc)%FricPressLoss / FlowEl(iloc)%FlowRate &
- * (2. + (2. - FlowEl(iloc)%nIndex) &
- * ((FlowEl(iloc)%a * FlowEl(iloc)%GenRe**(1. - FlowEl(iloc)%b) - 16.) / 800. / FlowEl(iloc)%f - 1.))
- END IF
-
- ELSE IF (MudProperties%ActiveRheologyModel == Bingham_RheologyModel) THEN ! Bingham Plastic
- IF (FlowEl(iloc)%GenRe <= 2000.0 .OR. FlowEl(iloc)%f == 0.0) THEN ! laminar flow if f = 0.0, we have no flow in first time flowing
- FlowEl(iloc)%FricToQPartialDiff = (16. * FlowEl(iloc)%muPlastic * REAL(FlowEl(iloc)%Length) * 2.224 * (10.)**(-3)) &
- / (25.81 * 928. * (1 - 0.184 * FlowEl(iloc)%alpha) * FlowEl(iloc)%Dhyd**2 * FlowEl(iloc)%Area)
-
- ELSE IF (FlowEl(iloc)%GenRe >= 4000.0) THEN ! turbulent flow
- FlowEl(iloc)%FricToQPartialDiff = FlowEl(iloc)%FricPressLoss / FlowEl(iloc)%FlowRate &
- * (2. - FlowEl(iloc)%b * (2. - FlowEl(iloc)%muPlastic / FlowEl(iloc)%mueff))
-
- ELSE ! transition from laminar to turbulent
- FlowEl(iloc)%FricToQPartialDiff = FlowEl(iloc)%FricPressLoss / FlowEl(iloc)%FlowRate &
- * (2. + (2. - FlowEl(iloc)%muPlastic / FlowEl(iloc)%mueff) &
- * ((FlowEl(iloc)%a * FlowEl(iloc)%GenRe**(1. - FlowEl(iloc)%b) - 16.) / 2000. / FlowEl(iloc)%f - 1.))
- END IF
- END IF
- END IF
-
-
- IF (FlowEl(iloc)%FricToQPartialDiff < 0.0) THEN
- !WRITE (*,*) ' iloc, Re, FricPressLoss, FricToQPartialDiff' , iloc, FlowEl(iloc)%GenRe, FlowEl(iloc)%FricPressLoss, FlowEl(iloc)%FricToQPartialDiff
- !CALL ERRORSTOP('Error in Calculating FricToQPartialDiff')
- END IF
-
- END SUBROUTINE PartialDerivativeFricToFlowRate
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