def test_binplot_minimum(): "Bare minimum: binplot produces a result with no errors." # This test breaks on a lot of buildbots raise nose.SkipTest my_phases_alfe = [ 'LIQUID', 'FCC_A1', 'HCP_A3', 'AL5FE2', 'AL2FE', 'AL13FE4', 'AL5FE4' ] binplot(DBF_ALFE, ['AL', 'FE', 'VA'], my_phases_alfe, 'X(AL)', 300, 2000)
import matplotlib.pyplot as plt from pycalphad import Database, Model, binplot from pycalphad.core.utils import make_callable import pycalphad.variables as v db = Database('Fe-C_Fei_Brosh_2014_09.TDB') fig = binplot(db, ['FE', 'C', 'VA'], list(db.phases.keys()), 'X(C)', 300.0, 2000.0, P=1e10) plt.savefig('FeC.png')
def test_binplot_minimum(): "Bare minimum: binplot produces a result with no errors." # Purposefully dropping BCC_B2 here because it takes too long to compute # Future versions of binplot will address this and check for correctness my_phases_alfe = ['LIQUID', 'FCC_A1', 'HCP_A3', 'AL5FE2', 'AL2FE', 'AL13FE4', 'AL5FE4'] binplot(DBF_ALFE, ['AL', 'FE', 'VA'], my_phases_alfe, 'X(AL)', 300, 2000)
def fprime(x, a, b, c, d, e, f, g, h, i, j): return 10 * a * x**9 + 9 * b * x**8 + 8 * c * x**7 + 7 * d * x**6 + 6 * e * x**5 + 5 * f * x**4 + 4 * g * x**3 + 3 * h * x**2 + 2 * i * x + j # Cu-Ni (S. an Mey 1999) db_cuni = Database('CuNi_RWTH.tdb') my_phases_cuni = ['FCC_A1', 'LIQUID', 'BCC_A2', 'HCP_A3'] # Calculate Isobaric Binary Phase Diagram if not os.path.isfile('CuNi.png'): fig = plt.figure(figsize=(9, 6)) binplot(db_cuni, ['CU', 'NI', 'VA'], my_phases_cuni, { v.X('NI'): (0, 1, 0.01), v.T: (1300, 1800, 5), v.P: 101325 }, ax=fig.gca()) plt.savefig('CuNi.png', dpi=400, bbox_inches='tight') plt.close() # It is very common in CALPHAD modeling to directly examine the Gibbs energy surface of all the constituent phases in a system. # Below we show how the Gibbs energy of all phases may be calculated as a function of composition at a given temperature (1550 K). # Calculate Energy Surfaces of Binary Systems if not os.path.isfile('CuNi_energy.png'): legend_handles, colorlist = phase_legend(my_phases_cuni) fig = plt.figure(figsize=(9, 6)) ax = fig.gca() xref = np.linspace(-0.1, 1.1, 150)
from scipy.optimize import curve_fit, newton import os.path def func(x, a, b, c, d, e, f, g, h, i, j, k): return a*x**10 + b*x**9 + c*x**8 + d*x**7 + e*x**6 + f*x**5 + g*x**4 + h*x**3 + i*x**2 + j*x + k def fprime(x, a, b, c, d, e, f, g, h, i, j): return 10*a*x**9 + 9*b*x**8 + 8*c*x**7 + 7*d*x**6 + 6*e*x**5 + 5*f*x**4 + 4*g*x**3 + 3*h*x**2 + 2*i*x + j # Cu-Ni (S. an Mey 1999) db_cuni = Database('CuNi_RWTH.tdb') my_phases_cuni = ['FCC_A1', 'LIQUID', 'BCC_A2', 'HCP_A3'] # Calculate Isobaric Binary Phase Diagram if not os.path.isfile('CuNi.png'): fig = plt.figure(figsize=(9,6)) binplot(db_cuni, ['CU', 'NI', 'VA'] , my_phases_cuni, {v.X('NI'):(0,1,0.01), v.T: (1300, 1800, 5), v.P:101325}, ax=fig.gca()) plt.savefig('CuNi.png', dpi=400, bbox_inches='tight') plt.close() # It is very common in CALPHAD modeling to directly examine the Gibbs energy surface of all the constituent phases in a system. # Below we show how the Gibbs energy of all phases may be calculated as a function of composition at a given temperature (1550 K). # Calculate Energy Surfaces of Binary Systems if not os.path.isfile('CuNi_energy.png'): legend_handles, colorlist = phase_legend(my_phases_cuni) fig = plt.figure(figsize=(9,6)) ax = fig.gca() xref = np.linspace(-0.1,1.1,150) for name in my_phases_cuni:
def test_binplot_minimum(): "Bare minimum: binplot produces a result with no errors." # This test breaks on a lot of buildbots raise nose.SkipTest my_phases_alfe = ['LIQUID', 'FCC_A1', 'HCP_A3', 'AL5FE2', 'AL2FE', 'AL13FE4', 'AL5FE4'] binplot(DBF_ALFE, ['AL', 'FE', 'VA'], my_phases_alfe, 'X(AL)', 300, 2000)