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614 | # Applied Python PRISM
# (PRISM) PaRametrIc System Model
#
# Written by Charlie Taylor <cet@appliedpython.com>
# Oct,21 2005
import sys
import numpy
from math import *
from prism.MassItem import MassItem
from prism.fortran import tank_eles
from prism.props import Materials
from prism.Summary import Summary
from prism.pov import POV_Items, POV_Basics
from prism.utils.Goal import Goal
# comments from the ELES tank routine
#C INPUT
#C makeCompositeTank - Make Composite Tank (0=No, 1=Yes)
#C KALMOD-CALCULATION MODE (0=INPUT RCYLTD, 1=INPUT RINSID)
#C SY - design strength (psi)
#C E - material elastic modulus (psi)
#C RHO - tank material density (lbm/in^3)
#C TMING - minimum gauge (in)
#C VFREE-total volume Usabel Volume (ullage plus propellant)
# (does NOT include Residual Propellant)
#C ELL-ellipse ratio
#C RCYLTD-ratio of cylindrical section length to diameter
#C (MAY BE INPUT OR OUTPUT)
#C ptank-pressure in tank
#C SF-safety factor
#C CXW-tank weight multiplier (welds, bosses, etc.)
#C ITHCYL-tank wall thickness flag(0=variable thickness,1=constant)
#C KACQUI-kind of acquisition device flag(0=none,1=transverse collapsin
#C Alum. bladder,2=full bonded rolling diaphram(BRD) Al,3=half
#C BRD Al,4=full BRD stainless steel,5=half BRD ss,6=capillary
#C device, 7=elastomeric bladder, 8=Titanium Bladder)
#C INPEX-input expulsion efficiency flag(0=calculate eff,1=input)
#C EXPEFI-input expulsion efficiency
#C TBLAD-bladder thickness(in)(0<KACQUI<6, or =7,8)
#C TBOND-bond thickness(in)(1<KACQUI<6 or =7,8)
#C TTRSPC-transverse collapsing bladder initial space distance(in)
#C (KACQUI=1 or 7)
#C RHOBND-density of bonding material (lbm/in**3)(1<KACQUI<6 or =7,8)
#C RHOACQ-density of acquisition device(lbm/in**3)(KACQUI=6 or 7)
acq_dict = {0:'no acq. device',1:'transverse collapsing Alum. bladder',
2:'full bonded rolling diaphram(BRD) Al',3:'half BRD Al',
4:'full BRD stainless steel',5:'half BRD ss',6:'capillary device',
7:'elastomeric transverse bladder (dP=0)',
8:'Titanium transverse collapsing'}
ith_dict = {0:'variable thickness',1:'constant thickness'}
exp_dict = {0:'calculate expulsion eff',1:'input expulsion eff'}
class Tank( MassItem ):
def __init__(self, name="tank", mass_lbm=0.0,
makeCompositeTank=0,kalmod=0, matlName="Ti", Cp_eff=0.15, # Cp Ti=.125, Al=.2, Monel=.1
tMinGaugeUser=0.0,
vfree=1000.0,ell=1.414,rcyltd=2.0,ptank=350.0,
sf=1.5,cxw=1.25, NumExtraBaffles=0,
ithcyl=1,kacqui=0,inpex=0,expefi=0.99, Number=1,
inpTblad=1, tblad=0.030,tbond=0.030,ttrspc=0.010,
rhobnd=0.04,rhoacq=0.28,tliner=0.0,rholiner=0.1,
hasCommonDome=0, deltaPCommonDome=100.0, sf_CommonDome=1.5, matlCommonDome='Ti',
maxVolFrac_CommonDome=0.75):
# if common dome is imput, then tliner and rholiner will be modified to approximate the
# mass and volume required for the common dome.
#
# BE SURE TO CHECK MINIMUM VOLUME OF ZERO CYLINDER CONCAVE DOMES
# The max volume side of the dome may be limited by the ellipse ratio
# the variable "maxVolFrac_CommonDome" reflects the volume split.
# The concave dome volume must be less than or equal to maxVolFrac_CommonDome * vfree
MassItem.__init__(self, name, type="inert", mass_lbm=mass_lbm)
self.makeCompositeTank = makeCompositeTank
self.kalmod = kalmod
self.matlName = matlName
self.rho, self.sy, self.e, self.tming = Materials.getMatlProps(matlName)
self.Cp_eff = Cp_eff # effective Cp of all tank materials combined
if tMinGaugeUser> self.tming:
self.tming = tMinGaugeUser
self.Number = Number # each tank has vfree
self.vfree = vfree
self.ell = ell
self.rcyltd = rcyltd
self.ptank = ptank
self.sf = sf
self.cxw = cxw
self.ithcyl = ithcyl
self.kacqui = kacqui
self.NumExtraBaffles = NumExtraBaffles
self.inpex = inpex
self.expefi = expefi
self.inpTblad = inpTblad
if self.kacqui in [7,8] and not inpTblad:
print 'WARNING... inpTblad should be equal to 1 for kacqu=7 or 8'
self.inpTblad = 1
self.tblad = tblad
self.tbond = tbond
self.ttrspc = ttrspc
self.rhobnd = rhobnd
self.rhoacq = rhoacq
self.tliner = tliner
self.rholiner = rholiner
self.hasCommonDome = hasCommonDome
self.deltaPCommonDome = deltaPCommonDome
self.sf_CommonDome = sf_CommonDome
self.matlCommonDome = matlCommonDome
self.rho_cd, self.sy_cd, self.e_cd, self.tming_cd = Materials.getMatlProps(matlCommonDome)
self.maxVolFrac_CommonDome = maxVolFrac_CommonDome
self.reCalc()
def getPOV_Item(self):
if hasattr( self, 'texture'):
texture = self.texture
else:
texture = POV_Basics.Texture( colorName="Gray50" )
s = POV_Items.CSE_Tank( radius=self.OR, ellRatio=self.ell, cylLen=self.cyl, texture=texture)
return s
def setToLcyl(self, Lcyl=0.5):
t3 = 4.*pi/3./self.ell
t2 = Lcyl*pi
# do a couple of iterations to get vtank
for i in range(3):
self.reCalc()
# assume there is always a positive root
poly = numpy.poly1d([t3,t2,0.,-self.vtank])
roots = numpy.roots( poly )
#print poly
#print roots
R = roots[0]
for r in roots[1:]:
if r>R: R=r
#print 'Radius =',R
D = 2.0 * R
self.rcyltd = Lcyl / D
self.reCalc()
def setToMaxID(self, IDmax=100.0, rcyltdMin=0.0):
self.rcyltd = rcyltdMin
self.reCalc()
Rmax = IDmax / 2.0
if self.rinsid > Rmax:
Vd = 4.*pi*Rmax**3/3./self.ell
L = (self.vtank-Vd)/pi/Rmax**2
self.rcyltd = max(rcyltdMin,L/Rmax/2.0)
self.reCalc()
def setToMaxOD(self, ODmax=100.0, rcyltdMin=0.0):
self.rcyltd = rcyltdMin
self.reCalc()
if self.OD > ODmax:
# assume the OD will converge pretty quickly
for i in range(10):
Rest = ODmax / 2.0 - (self.OR - self.rinsid)
Vd = 4.*pi*Rest**3/3./self.ell
L = (self.vtank-Vd)/pi/Rest**2
self.rcyltd = max(rcyltdMin,L/Rest/2.0)
self.reCalc()
def setToMaxOH(self, Hgoal=25.0):
self.rcyltd = 0.0
self.reCalc()
if self.OH < Hgoal:
lodMin = 0.0
lodMax = sqrt(self.vfree/Hgoal)
for i in range(6):
self.rcyltd = lodMax
self.reCalc()
if self.OH < Hgoal:
lodMax *= 1.2
else:
break
def testHt( lod ):
self.rcyltd = lod
self.reCalc()
return self.OH
G = Goal(goalVal=Hgoal, minX=lodMin, maxX=lodMax,
funcOfX=testHt, tolerance=1.0E-5, maxLoops=40, failValue=self.vfree)
lod, ierror = G()
self.rcyltd = lod
self.reCalc()
def solveVolumeForOD(self, ODgoal=10.0):
self.reCalc()
if self.OD > ODgoal:
Vmax = self.vfree
Vmin = (ODgoal/self.OD)**(3.) * self.vfree / 2.0
else:
Vmin = self.vfree
Vmax = (ODgoal/self.OD)**(3.) * self.vfree * 2.0
def testVol( vol ):
self.vfree = vol
self.reCalc()
return self.OD
G = Goal(goalVal=ODgoal, minX=Vmin, maxX=Vmax,
funcOfX=testVol, tolerance=1.0E-5, maxLoops=40, failValue=self.vfree)
vol, ierror = G()
self.vfree = vol
self.reCalc()
def setToLength(self, L=100.0):
self.rcyltd = 0.0
self.reCalc()
# only try to make it L long by adding cylinder length
if self.hinsid < L:
V = self.vtank
e = self.ell
rmax = (V*e*3./4./pi)**(1./3.)
rmin = sqrt( V/pi/L )
for i in range(40):
r = (rmin+rmax)/2.0
Lcyl = L - 2.0*r/e
Vtest = 4.*pi*r**3/3./e + pi*r**2*Lcyl
if Vtest>V:
rmax = r
else:
rmin = r
self.rcyltd = max(0.0,Lcyl/r/2.0)
self.reCalc()
def reCalc(self):
default_cxw = 1.0
kacqui = self.kacqui
if self.kacqui in [7]:
kacqui = 1
if self.kacqui in [8]:
kacqui = 2 # like Al BRD
self.VolLimit_cd = self.maxVolFrac_CommonDome * self.vfree
if self.hasCommonDome:
rinsid_cd,hinsid_cd,cyl_cd,wacqui_cd,\
vacqui_cd,dpacq_cd,pullag_cd,vresid_cd,\
vtank_cd,thkcyl_cd, self.thkCommonDome, thkBladOut_cd,wliner_cd,wtank_cd= \
tank_eles.csetnk(0,self.kalmod,
self.sy_cd,self.e_cd,self.rho_cd,self.tming_cd,self.vfree,
self.ell,self.rcyltd,self.deltaPCommonDome, self.sf_CommonDome,default_cxw,
self.ithcyl,kacqui,self.inpex,self.expefi,
self.inpTblad,self.tblad,self.tbond,self.ttrspc,
self.rhobnd,self.rhoacq,self.tliner,self.rholiner)
SACYL=2.*pi*rinsid_cd*cyl_cd
if self.ell <= 1.:
SAENDS=4.*pi*rinsid_cd**2
else:
ECC=sqrt(1.-(1./self.ell)**2)
SAENDS=2.*pi*rinsid_cd**2 + pi*(rinsid_cd/self.ell)**2/ECC*log((1.+ECC)/(1.-ECC))
# calc minimum volume in concave domes
self.VolCommonDomeEllipse = 4.*pi*rinsid_cd**3/self.ell/3.
if self.VolLimit_cd < self.VolCommonDomeEllipse:
vfree_eff = self.vfree + ( self.VolCommonDomeEllipse - self.VolLimit_cd )
else:
vfree_eff = self.vfree
self.VolCommonDomeMatl = SAENDS * self.thkCommonDome / 2.0
self.WtCommonDome = self.VolCommonDomeMatl * self.rho_cd
# estimate surface area ratio with and w/o common dome
SAwo = SACYL + SAENDS
SAwith = SACYL + SAENDS * 2.0
# the effective thickness will get the matl volume correct
# includes the volume of the common dome and the liner
tliner_eff = self.tliner * SAwith / SAwo + self.VolCommonDomeMatl/SAwo
# the effective density will get the matl mass of the liner ONLY correct
# includes additional mass of liner due to extra surface area of common dome
volMatlEff = tliner_eff * SAwo
rholiner_eff = wliner_cd * SAwith / SAwo / volMatlEff
else:
tliner_eff = self.tliner
rholiner_eff = self.rholiner
self.WtCommonDome = 0.0
self.VolCommonDomeEllipse = 0.0
vfree_eff = self.vfree
self.rinsid,self.hinsid,self.cyl,self.wacqui,\
self.vacqui,self.dpacq,self.pullag,self.vresid,\
self.vtank,self.thkcyl,self.thkend,self.thkBladOut,self.wliner,self.wtank= \
tank_eles.csetnk(self.makeCompositeTank,self.kalmod, # <== call to tank_eles
self.sy,self.e,self.rho,self.tming,vfree_eff,
self.ell,self.rcyltd,self.ptank,self.sf,default_cxw,
self.ithcyl,kacqui,self.inpex,self.expefi,
self.inpTblad,self.tblad,self.tbond,self.ttrspc,
self.rhobnd,self.rhoacq,tliner_eff,rholiner_eff)
if self.kacqui==7: # user defined bladder (elastomeric)
self.dpacq = 0.0
self.wacqui = self.wacqui * self.rhoacq * self.tblad / self.thkBladOut / 0.1
self.vacqui = self.vacqui * self.tblad / self.thkBladOut
self.thkBladOut = self.tblad
if self.kacqui==8: # Titanium Bladder
self.dpacq = 2.0 * self.dpacq # estimate Ti is 4x Al
self.wacqui = self.wacqui * 0.16 * self.tblad / self.thkBladOut / 0.1
self.vacqui = self.vacqui * self.tblad / self.thkBladOut
#self.thkBladOut = self.tblad
self.dinsid = 2.0*self.rinsid
self.pov_h = self.cyl + self.dinsid/self.ell
self.pov_w = self.dinsid
self.pov_d = self.dinsid
self.Across = pi * self.rinsid**2
ECC=sqrt(1.-(1./self.ell)**2)
HEADCO=pi/2.
if self.ell>1.0:
HEADCO=(pi/4.)*(1.+log((1.+ECC)/(1.-ECC))/(2.*ECC*self.ell**2))
HSA = HEADCO*self.dinsid**2
self.SAinsid = pi*self.dinsid*self.cyl + 2.*HSA
if self.NumExtraBaffles > 0:
self.WtExtraBaffles = pi * self.rinsid**2 * self.tming * self.rho * self.NumExtraBaffles
else:
self.WtExtraBaffles = 0.0
self.mass_lbm = (self.wtank + self.wacqui ) * self.cxw + self.WtExtraBaffles + self.WtCommonDome
if self.thkcyl <= self.tming:
self.Pburst = self.tming * self.sy / self.rinsid
else:
self.Pburst = self.sf * self.ptank
self.OD = 2.0* (self.rinsid + self.thkcyl + self.thkBladOut + self.tliner)
self.OR = self.OD / 2.0
self.OH = self.hinsid + 2.0* ( self.thkend + self.thkBladOut + self.tliner)
# if more than one tank, increase mass to reflect that
self.mass_lbm *= self.Number
try:
self.PVoverW = self.ptank*self.vtank*self.Number/self.mass_lbm
self.PburstVoverW = self.Pburst*self.vtank*self.Number/self.mass_lbm
except:
self.PVoverW = 0.0
self.PburstVoverW = 0.0
def minGaugeStr(self, t):
if t<= self.tming:
return 'Min Gauge'
else:
return ''
def buildSummary(self):
summ = Summary( summName='Cylindrical/Spherical/Elliptical Tank',
componentName=self.name, mass_lbm=self.mass_lbm, type=self.type)
if self.makeCompositeTank:
summ.addAssumption('Composite Tank Algorithm')
else:
summ.addAssumption('Metal Tank Algorithm')
summ.addAssumption('Structural Material : ' + self.matlName )
if self.hasCommonDome:
summ.addAssumption('Includes Common Dome of "%s"'%self.matlCommonDome)
summ.addAssumption('Limiting Common Dome Volume = %g cuin'%self.VolCommonDomeEllipse)
summ.addAssumption('Required Common Dome Volume = %g cuin'%self.VolLimit_cd)
if self.VolLimit_cd >= self.VolCommonDomeEllipse:
summ.addAssumption('(MEETS VOLUME REQUIREMENT, Required > Limiting)')
else:
summ.addAssumption('(WARNING... DOES NOT MEET VOLUME REQUIREMENT)')
deltaVol = self.VolCommonDomeEllipse - self.VolLimit_cd
summ.addAssumption('(INCREASED TOTAL VOLUME BY %g cuin TO MEET REQUIREMENT)'%deltaVol)
if self.NumExtraBaffles > 0:
summ.addAssumption("%i Extra Baffles are added to tank"%self.NumExtraBaffles)
if self.kacqui in [1,2,3,4,5,7,8]:
if self.inpTblad:
summ.addAssumption('Bladder Thickness is input at %.3f in'%self.tblad)
else:
summ.addAssumption('Bladder Thickness is calculated at %.3f in'%self.tblad)
summ.addAssumption('kalmod = ' + str( self.kalmod ) )
if self.Number>1:
summ.addAssumption( 'Mass is for %i Tanks total'%self.Number )
# add inputs
summ.addInput('vfree', self.vfree, 'cuin', '%g')
summ.addInput('vfreeTotal', self.vfree*self.Number, 'cuin', '%g')
if self.hasCommonDome:
summ.addInput('maxVolFrac_CommonDome', self.maxVolFrac_CommonDome, '', '%g')
summ.addInput('deltaPCommonDome', self.deltaPCommonDome, 'psia', '%g')
summ.addInput('ell', self.ell, '', '%g')
summ.addInput('rcyltd', self.rcyltd, '', '%g')
summ.addInput('ptank', self.ptank, 'psia', '%g')
summ.addInput('sf', self.sf, '', '%g')
summ.addInput('cxw', self.cxw, '', '%g')
summ.addInput('ithcyl', self.ithcyl, '', '%g')
summ.addInput('kacqui', self.kacqui, acq_dict[self.kacqui], '%s')
summ.addInput('inpex', self.inpex, '', '%g')
summ.addInput('expefi', self.expefi, '', '%g')
summ.addInput('tblad', self.tblad, 'in', '%.3f')
summ.addInput('tbond', self.tbond, 'in', '%.3f')
summ.addInput('ttrspc', self.ttrspc, 'in', '%.3f')
summ.addInput('rhobnd', self.rhobnd, 'lbm/cuin', '%g')
summ.addInput('rhoacq', self.rhoacq, 'lbm/cuin', '%g')
summ.addInput('tliner', self.tliner, 'in', '%.3f')
summ.addInput('rholiner', self.rholiner, 'lbm/cuin', '%g')
# add outputs
summ.addOutput( 'rinsid', self.rinsid, 'in', '%.3f' )
summ.addOutput( 'dinsid', self.dinsid, 'in', '%.3f' )
summ.addOutput( 'OR', self.OR, 'in', '%.3f' )
summ.addOutput( 'OD', self.OD, 'in', '%.3f' )
summ.addOutput( 'OH', self.OH, 'in', '%.3f' )
summ.addOutput( 'hinsid', self.hinsid, 'in', '%.3f' )
summ.addOutput( 'SAinsid', self.SAinsid, 'sqin', '%.3f' )
summ.addOutput( 'cyl', self.cyl, 'in', '%.3f' )
summ.addOutput( 'wacqui', self.wacqui, 'lbm', '%.3f' )
summ.addOutput( 'vacqui', self.vacqui, 'cuin', '%g' )
summ.addOutput( 'dpacq', self.dpacq, 'psig', '%g' )
summ.addOutput( 'pullag', self.pullag, 'psia', '%g' )
summ.addOutput( 'vresid', self.vresid, 'cuin', '%g' )
summ.addOutput( 'vtank', self.vtank, 'cuin', '%g' )
summ.addOutput( 'tming', self.tming, 'in', '%.3f' )
if self.thkcyl <= self.tming:
summ.addOutput( 'thkcyl', self.thkcyl, 'in (use tming)', '%.3f' )
else:
summ.addOutput( 'thkcyl', self.thkcyl, 'in', '%.3f' )
if self.thkend <= self.tming:
summ.addOutput( 'thkend', self.thkend, 'in (use tming)', '%.3f' )
else:
summ.addOutput( 'thkend', self.thkend, 'in', '%.3f' )
summ.addOutput( 'thkBladOut', self.thkBladOut, 'in', '%.3f' )
if self.NumExtraBaffles > 0:
summ.addOutput( 'WtExtraBaffles', self.WtExtraBaffles, 'lbm', '%.3f' )
if self.hasCommonDome:
summ.addOutput( 'thkCommonDome', self.thkCommonDome, 'in', '%.3f' )
summ.addOutput( 'WtCommonDome', self.WtCommonDome, 'lbm', '%.3f' )
if self.wliner > 0.0:
summ.addOutput( 'wliner', self.wliner, 'lbm', '%.3f' )
summ.addOutput( 'wtank(+liner)', self.wtank, 'lbm', '%.3f' )
else:
summ.addOutput( 'wtank', self.wtank, 'lbm', '%.3f' )
summ.addOutput( 'rho', self.rho, 'lbm/cuin', '%g' )
if not self.makeCompositeTank:
summ.addOutput( 'sy', self.sy, 'psi', '%g' )
summ.addOutput( 'e', self.e, 'psi', '%g' )
summ.addOutput( 'PmeopVoverW', self.PVoverW, 'lbf-in/lbm', '%g' )
summ.addOutput( 'Pburst(est.)', self.Pburst, 'psia', '%.1f' )
summ.addOutput( 'PburstVoverW', self.PburstVoverW, 'lbf-in/lbm', '%g' )
return summ
if __name__ == "__main__": #self test
print "Actual FFC Prop Tank =", 3.703,"lbm"
print "Calculated = ",
oxFFC = Tank(name="FFC Propellant Tank", mass_lbm=3.703,
makeCompositeTank=1, kalmod=0,
matlName="grEpox", vfree=486.0,ell=1.767,rcyltd=1.445,
ptank=1400.0,sf=1.5,cxw=1.5,
ithcyl=1,kacqui=1,inpex=1,expefi=0.98,
tblad=0.030,tbond=0.030,ttrspc=0.010,
rhobnd=0.04,rhoacq=0.098,tliner=0.03,rholiner=0.098)
print oxFFC.getMassStr()
print
print oxFFC.getSummary()
print '===================================================================='
print "Actual Mars PMD Prop Tank =", 8.5,"lbm (PSI SN 80353-1)"
print "Calculated Mars = ",
pmd = Tank(name="Mars Observer Propellant Tank", mass_lbm=8.5,
makeCompositeTank=0, kalmod=0,
matlName="Ti", vfree=3490.0,ell=1.0,rcyltd=0.0, # input vfree=3490 cuin to get 3575 total
ptank=400.0,sf=1.5,cxw=1.07, NumExtraBaffles=3,
ithcyl=1,kacqui=6,inpex=1,expefi=0.98,
tblad=0.0,tbond=0.0,ttrspc=0.0,rhoacq=0.16)
print pmd.getMassStr()
print
print pmd.getSummary()
print '===================================================================='
print "Spherical Prop Tank =", 12.04,"lbm w/o diaphram or PK baffles (PSI SN 80274-1)"
print "Calculated Mass = ",
pmd = Tank(name="PSI 80274-1 Tank", mass_lbm=12.04, tMinGaugeUser=0.035,
makeCompositeTank=0, kalmod=0,
matlName="Ti", vfree=3660.0,ell=1.0,rcyltd=0.0,
ptank=377.0,sf=1.5,cxw=1.32, NumExtraBaffles=3,
ithcyl=1,kacqui=6,inpex=1,expefi=0.98,
tblad=0.0,tbond=0.0,ttrspc=0.0,rhoacq=0.16)
print pmd.getMassStr()
print
print pmd.getSummary()
print '===================================================================='
print "Actual FFC He Tank=",3.157,"lbm (single tank)"
print "Calculated =",
HeFFC = Tank(name="FFC Helium Tank", mass_lbm=3.157,
makeCompositeTank=1, kalmod=0, Number=1,
matlName="grEpox", vfree=160.0, ell=1.764,rcyltd=1.142,
ptank=10000.0,sf=2.0,cxw=1.25,
ithcyl=1,kacqui=0,inpex=0,
inpTblad=0, tblad=0.030,tbond=0.030,ttrspc=0.010,
rhobnd=0.04,rhoacq=0.1,tliner=0.04,rholiner=0.1)
print HeFFC.getMassStr()
print
print HeFFC.getSummary()
sys.exit()
HeFFC.setToMaxID( IDmax=4.0)
print
print HeFFC.getSummary()
HeFFC.setToMaxOD( ODmax=4.0)
print
print HeFFC.getSummary()
if 0:
HeFFC.setToLcyl( 7.0 )
#HeFFC.setToLength( L=10.0)
print
print HeFFC.getSummary()
print '===================================================================='
print "Common Dome Prop Tank WITHOUT CommonDome Option="
cdtank = Tank(name="FFC Propellant Tank", mass_lbm=3.703,
makeCompositeTank=1, kalmod=0,
matlName="grEpox", vfree=486.0,ell=1.767,rcyltd=1.445,
ptank=1400.0,sf=1.5,cxw=1.5,
ithcyl=1,kacqui=1,inpex=1,expefi=0.98,
tblad=0.030,tbond=0.030,ttrspc=0.010,
rhobnd=0.04,rhoacq=0.098,tliner=0.03,rholiner=0.098,
hasCommonDome=0, deltaPCommonDome=100.0, sf_CommonDome=1.5, matlCommonDome='Ti')
print
print cdtank.getSummary()
print "Common Dome Prop Tank ="
cdtank = Tank(name="FFC Propellant Tank", mass_lbm=3.703,
makeCompositeTank=1, kalmod=0,
matlName="grEpox", vfree=486.0,ell=1.767,rcyltd=1.445,
ptank=1400.0,sf=1.5,cxw=1.5,
ithcyl=1,kacqui=1,inpex=1,expefi=0.98,
tblad=0.030,tbond=0.030,ttrspc=0.010,
rhobnd=0.04,rhoacq=0.098,tliner=0.03,rholiner=0.098,
hasCommonDome=1, deltaPCommonDome=100.0, sf_CommonDome=1.5, matlCommonDome='Ti',
maxVolFrac_CommonDome=0.15)
#cdtank.setToMaxOH(Hgoal=15.0)
print
print cdtank.getSummary()
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