def calc(self, p_bar, t_c):
"""
Расчет свойств нефти на основе набора корреляций McCain
расчитанные значения хранятся в соответствующих атрибутах класса
:param p_bar: давление, бар
:param t_c: температура, С
:return: 1 - если все свойства успешно были посчитаны
"""
super().calc(p_bar, t_c)
# подготовим внутренние переменные для расчетов
p_MPaa = uc.bar2MPa(self.p_bar)
pbcal_MPaa = uc.bar2MPa(self.pbcal_bar)
t_K = uc.c2k(self.t_c)
# найдем значение давления насыщения по Valko McCain
pb_MPaa = PVT.unf_pb_Valko_MPaa(self.rsb_m3m3, self.gamma_oil, self.gamma_gas, t_K)
self._pb_bar = uc.MPa2bar(pb_MPaa)
# TODO необходимо будет сделать калибровку при любом P,T любого свойства
if pbcal_MPaa > 0:
p_fact = pb_MPaa / pbcal_MPaa
# сдвигаем шкалу по давлению для расчета, если задана калибровка
p_MPaa = p_fact * p_MPaa
self._pb_bar = self._pb_bar/p_fact
# внутри rs есть проверка на давление насыщения
self._rs_m3m3 = PVT.unf_rs_Velarde_m3m3(p_MPaa, pb_MPaa, self.rsb_m3m3, self.gamma_oil, self.gamma_gas, t_K)
co_1MPa = PVT.unf_compressibility_oil_VB_1Mpa(self._rs_m3m3, t_K, self.gamma_oil, p_MPaa, self.gamma_gas)
self._compr_oil_1bar = uc.compr_1mpa_2_1bar(co_1MPa)
# внутри rho есть проверка на давление насыщения
self._rho_oil_kgm3 = PVT.unf_density_oil_Mccain(p_MPaa, pb_MPaa, co_1MPa, self._rs_m3m3, self.gamma_gas, t_K,
self.gamma_oil, self.gamma_gassp)
# оценим значение объемного коэффициента
# оценим значение объемного коэффициента при давлении насыщения
self._bob_m3m3 = PVT.unf_fvf_Mccain_m3m3_below(self.rho_oil_stkgm3, self.rsb_m3m3, self._rho_oil_kgm3,
self.gamma_gas)
if p_MPaa > pb_MPaa:
self._bo_m3m3 = PVT.unf_fvf_VB_m3m3_above(self._bob_m3m3, co_1MPa, pb_MPaa, p_MPaa)
else:
self._bo_m3m3 = PVT.unf_fvf_Mccain_m3m3_below(self.rho_oil_stkgm3, self._rs_m3m3, self._rho_oil_kgm3,
self.gamma_gas)
# проверим необходимость калибровки значения объемного коэффициента
if self.bobcal_m3m3 > 0:
b_fact = (self.bobcal_m3m3 - 1) / (self._bob_m3m3 - 1)
self._bo_m3m3 = b_fact * self._bo_m3m3
# оценим значение вязкости
self._mu_deadoil_cP = PVT.unf_deadoilviscosity_Beggs_cP(self.gamma_oil, t_K)
self._muob_cP = PVT.unf_saturatedoilviscosity_Beggs_cP(self._mu_deadoil_cP, self.rsb_m3m3)
self._mu_oil_cP = PVT.unf_oil_viscosity_Beggs_VB_cP(self._mu_deadoil_cP, self._rs_m3m3, p_MPaa, pb_MPaa)
if self.muobcal_cP > 0:
mu_fact = self.muobcal_cP / self._muob_cP
self._mu_oil_cP = mu_fact * self._mu_oil_cP
# gas
tpc_K = PVT.unf_pseudocritical_temperature_K(self.gamma_gas, self.y_h2s, self.y_co2, self.y_n2)
ppc_MPa = PVT.unf_pseudocritical_pressure_MPa(self.gamma_gas, self.y_h2s, self.y_co2, self.y_n2)
self._z = PVT.unf_zfactor_DAK(p_MPaa, t_K, ppc_MPa, tpc_K)
self._mu_gas_cP = PVT.unf_gasviscosity_Lee_cP(t_K, p_MPaa, self._z, self.gamma_gas)
self._bg_m3m3 = PVT.unf_gas_fvf_m3m3(t_K, p_MPaa, self._z)
self._compr_gas_1bar = uc.compr_1mpa_2_1bar(PVT.unf_compressibility_gas_Mattar_1MPa(p_MPaa, t_K,
ppc_MPa, tpc_K))
self._rho_gas_kgm3 = PVT.unf_gas_density_kgm3(t_K, p_MPaa, self.gamma_gas, self._z)
# water
# TODO НУЖНО ДОБАВИТЬ GWR
self._rho_wat_kgm3 = PVT.unf_density_brine_Spivey_kgm3(t_K, p_MPaa, self.s_ppm, self.par_wat)
self._compr_wat_1bar = uc.compr_1mpa_2_1bar(PVT.unf_compressibility_brine_Spivey_1MPa(t_K, p_MPaa, self.s_ppm,
self._z, self.par_wat))
self._bw_m3m3 = PVT.unf_fvf_brine_Spivey_m3m3(t_K, p_MPaa, self.s_ppm)
self._mu_wat_cP = PVT.unf_viscosity_brine_MaoDuan_cP(t_K, p_MPaa, self.s_ppm)
return 1
def calc(self, p_bar, t_c):
"""
Расчет свойств нефти на основе набора корреляций Standing
расчитанные значения хранятся в соответствующих атрибутах класса
:param p_bar: давление, бар
:param t_c: температура, С
:return: 1 - если все свойства успешно были посчитаны
"""
super().calc(p_bar, t_c)
# подготовим внутренние переменные для расчетов
p_MPaa = uc.bar2MPa(self.p_bar)
pbcal_MPaa = uc.bar2MPa(self.pbcal_bar)
t_K = uc.c2k(self.t_c)
# oil
# найдем значение давления насыщения по Standing
pb_MPaa = PVT.unf_pb_Standing_MPaa(self.rsb_m3m3, self.gamma_oil, self.gamma_gas, t_K)
self._pb_bar = uc.MPa2bar(pb_MPaa)
# TODO необходимо будет сделать калибровку при любом P,T любого свойства
if pbcal_MPaa > 0:
p_fact = pb_MPaa / pbcal_MPaa
# сдвигаем шкалу по давлению для расчета, если задана калибровка
p_MPaa = p_fact * p_MPaa
self._pb_bar = self._pb_bar / p_fact
# внутри rs есть проверка на давление насыщения
self._rs_m3m3 = PVT.unf_rs_Standing_m3m3(p_MPaa, pb_MPaa, self.rsb_m3m3, self.gamma_oil, self.gamma_gas, t_K)
co_1MPa = PVT.unf_compressibility_oil_VB_1Mpa(self._rs_m3m3, t_K, self.gamma_oil, p_MPaa, self.gamma_gas)
self._compr_oil_1bar = uc.compr_1mpa_2_1bar(co_1MPa)
# оценим значение объемного коэффициента
# оценим значение объемного коэффициента при давлении насыщения
self._bob_m3m3 = PVT.unf_fvf_Standing_m3m3_saturated(self.rsb_m3m3, self.gamma_gas, self.gamma_oil, t_K)
if p_MPaa > pb_MPaa:
self._bo_m3m3 = PVT.unf_fvf_VB_m3m3_above(self._bob_m3m3, co_1MPa, pb_MPaa, p_MPaa)
else:
self._bo_m3m3 = PVT.unf_fvf_Standing_m3m3_saturated(self._rs_m3m3, self.gamma_gas, self.gamma_oil, t_K)
# проверим необходимость калибровки значения объемного коэффициента
if self.bobcal_m3m3 > 0:
b_fact = (self.bobcal_m3m3 - 1) / (self._bob_m3m3 - 1)
self._bo_m3m3 = b_fact * self._bo_m3m3
self._rho_oil_kgm3 = PVT.unf_density_oil_Standing(p_MPaa, pb_MPaa, co_1MPa, self._rs_m3m3, self._bo_m3m3,
self.gamma_gas, self.gamma_oil)
# оценим значение вязкости
self._mu_dead_oil_cP = PVT.unf_deadoilviscosity_Beggs_cP(self.gamma_oil, t_K)
self._muob_cP = PVT.unf_saturatedoilviscosity_Beggs_cP(self._mu_dead_oil_cP, self.rsb_m3m3)
self._mu_oil_cP = PVT.unf_oil_viscosity_Beggs_VB_cP(self._mu_dead_oil_cP, self._rs_m3m3, p_MPaa, pb_MPaa)
if self.muobcal_cP > 0:
mu_fact = self.muobcal_cP / self._muob_cP
self._mu_oil_cP = mu_fact * self._mu_oil_cP
# определим термодинамические свойства нефти
self._heatcap_oil_jkgc = PVT.unf_heat_capacity_oil_Gambill_JkgC(self.gamma_oil, self.t_c)
self._thermal_conduct_oil_wmk = PVT.unf_thermal_conductivity_oil_Cragoe_WmK(self.gamma_oil, self.t_c)
# gas
tpc_K = PVT.unf_pseudocritical_temperature_K(self.gamma_gas, self.y_h2s, self.y_co2, self.y_n2)
ppc_MPa = PVT.unf_pseudocritical_pressure_MPa(self.gamma_gas, self.y_h2s, self.y_co2, self.y_n2)
self._z = PVT.unf_zfactor_DAK(p_MPaa, t_K, ppc_MPa, tpc_K)
self._mu_gas_cP = PVT.unf_gasviscosity_Lee_cP(t_K, p_MPaa, self._z, self.gamma_gas)
self._bg_m3m3 = PVT.unf_gas_fvf_m3m3(t_K, p_MPaa, self._z)
self._compr_gas_1bar = uc.compr_1mpa_2_1bar(PVT.unf_compressibility_gas_Mattar_1MPa(p_MPaa, t_K,
ppc_MPa, tpc_K))
self._rho_gas_kgm3 = PVT.unf_gas_density_kgm3(t_K, p_MPaa, self.gamma_gas, self._z)
# определим термодинамические свойства газа
self._heatcap_gas_jkgc = PVT.unf_heat_capacity_gas_Mahmood_Moshfeghian_JkgC(p_MPaa, t_K, self.gamma_gas)
self._thermal_conduct_gas_wmk = PVT.unf_thermal_conductivity_gas_methane_WmK(self.t_c)
# water
# TODO НУЖНО проверить GWR
self._rho_wat_kgm3 = PVT.unf_density_brine_Spivey_kgm3(t_K, p_MPaa, self.s_ppm, self.par_wat)
self._compr_wat_1bar = uc.compr_1mpa_2_1bar(PVT.unf_compressibility_brine_Spivey_1MPa(t_K, p_MPaa, self.s_ppm,
self._z, self.par_wat))
self._bw_m3m3 = PVT.unf_fvf_brine_Spivey_m3m3(t_K, p_MPaa, self.s_ppm)
self._mu_wat_cP = PVT.unf_viscosity_brine_MaoDuan_cP(t_K, p_MPaa, self.s_ppm)
self._rsw_m3m3 = PVT.unf_gwr_brine_Spivey_m3m3(self.s_ppm, self._z)
# определим термодинамические свойства воды
self._heatcap_wat_jkgc = PVT.unf_heat_capacity_water_IAPWS_JkgC(self.t_c)
self._thermal_conduct_wat_wmk = PVT.unf_thermal_conductivity_water_IAPWS_WmC(self.t_c)
self._thermal_expansion_wat_1c = PVT.unf_thermal_expansion_coefficient_water_IAPWS_1C(self.t_c)
# определим свойства системы
self._sigma_oil_gas_Nm = PVT.unf_surface_tension_go_Baker_Swerdloff_Nm(t_K, self.gamma_oil, p_MPaa)
self._sigma_wat_gas_Nm = PVT.unf_surface_tension_gw_Sutton_Nm(self.rho_wat_kgm3, self.rho_gas_kgm3, self.t_c)
return 1
def calc(self, p_bar, t_c):
self.p_bar = p_bar
self.t_c = t_c
self.t_k = uc.c2k(self.t_c)
self.p_mpa = uc.bar2MPa(self.p_bar)
self.t_res_k = uc.c2k(self.t_res_c)
if self.activate_rus_cor == 0: # нормальный расчет по UniflocVBA
# oil
# давление насыщения нефти
self.pb_mpa = self._calc_pb_MPaa(self.option.pb_cor_number)
self.pb_bar = uc.MPa2bar(self.pb_mpa)
pbcal_MPaa = uc.bar2MPa(self.pb_cal_bar)
if pbcal_MPaa > 0:
p_fact = self.pb_mpa / pbcal_MPaa
# сдвигаем шкалу по давлению для расчета, если задана калибровка
self.p_mpa = p_fact * self.p_mpa
self.pb_bar = self.pb_bar / p_fact
# газосодержание
self.rs_m3m3 = self._calc_rs_m3m3(self.option.rs_cor_number)
# коэффициент изотермической сжимаемости
if self.p_mpa >= self.pb_mpa:
self.compr_oil_1mpa = self._calc_compr_oil_1mpa(
self.option.compr_oil_cor_number)
else:
#self.compr_oil_1mpa = self._calc_compr_oil_below_pb_1mpa(self.option.compr_oil_below_pb_cor_number)
self.compr_oil_1mpa = 0
self.compr_oil_1bar = uc.compr_1mpa_2_1bar(self.compr_oil_1mpa)
# объемный коэффициент
self.b_oil_b_m3m3 = self._calc_b_oil_in_pb_m3m3(
self.option.b_oil_in_pb_cor_number)
if self.p_mpa > self.pb_mpa:
self.b_oil_m3m3 = self._calc_b_oil_above_pb_m3m3(
self.option.b_oil_above_pb_cor_number)
else:
self.b_oil_m3m3 = self._calc_b_oil_below_pb_m3m3(
self.option.b_oil_below_pb_cor_number)
if self.b_oil_b_cal_m3m3 > 0:
b_fact = (self.b_oil_b_cal_m3m3 - 1) / (self.b_oil_b_m3m3 - 1)
self.b_oil_m3m3 = b_fact * self.b_oil_m3m3
# плотность нефти
self.rho_oil_kgm3 = self._calc_rho_oil_kgm3(
self.option.rho_oil_cor_number)
# вязкость
self.mu_dead_oil_cp = self._calc_mu_dead_oil_cp(
self.option.mu_dead_oil_cor_number)
self.mu_oil_b_cP = self._calc_mu_oil_in_pb_cp(
self.option.mu_oil_pb_cor_number)
self.mu_oil_cp = self._calc_mu_oil_any_p_cp(
self.option.mu_oil_any_p_cor_number)
if self.mu_oil_b_cal_cp > 0:
mu_fact = self.mu_oil_b_cal_cp / self.mu_oil_b_cP
self.mu_oil_cp = mu_fact * self.mu_oil_cp
else: # расчет по Мищенко
if self.true_rsb_m3t:
self.rsb_m3t = self.rsb_m3m3 * 10**3 * 273 / 293 / (
self.gamma_oil * 1000)
else:
self.rsb_m3t = self.rsb_m3m3 / self.gamma_oil #c этой штукой расчет получше
self.pb_mpa = pvt_rus.calc_pb(self.pb_bar_for_rus_cor / 10,
self.gamma_oil * 1000, self.rsb_m3t,
self.t_res_k, self.t_k, self.y_ch4,
self.y_n2)
self.pb_bar = uc.MPa2bar(self.pb_mpa)
self.mt = pvt_rus.coef_mt(self.t_k, self.gamma_oil * 1000,
self.gamma_gas)
self.rp = pvt_rus.coef_rp(self.p_mpa, self.pb_mpa)
self.dt = pvt_rus.coef_dt(self.t_k, self.gamma_oil * 1000,
self.gamma_gas)
self.gas_liberated_m3t, self.gas_dissolved_m3t = pvt_rus.unf_calc_gas_liberated_and_dissolved(
self.t_k, self.gamma_oil * 1000, self.gamma_oil,
self.gamma_gas, self.p_mpa, self.pb_mpa, self.rsb_m3t,
False) #
self.gas_liberated_m3m3, self.rs_m3m3 = pvt_rus.unf_calc_gas_liberated_and_dissolved(
self.t_k, self.gamma_oil * 1000, self.gamma_oil,
self.gamma_gas, self.p_mpa, self.pb_mpa, self.rsb_m3t, True)
if self.p_mpa > self.pb_mpa:
if self.gas_dissolved_m3t_fixed != None and self.rs_m3m3_fixed != None:
self.gas_liberated_m3t, self.gas_dissolved_m3t = 0, self.gas_dissolved_m3t_fixed #73.23
self.gas_liberated_m3m3, self.rs_m3m3 = 0, self.rs_m3m3_fixed # 63.01
self.rho_gas_liberated_d = pvt_rus.rho_gas_liberated_relative(
self.p_mpa, self.pb_mpa, self.gamma_gas, self.gamma_oil,
self.t_k, self.rsb_m3t)
self.rho_gas_dissolved_relative_d = pvt_rus.unf_rho_gas_dissolved_relative(
self.rsb_m3t, self.gamma_oil, self.gamma_gas,
self.gas_liberated_m3t, self.gas_dissolved_m3t,
self.rho_gas_liberated_d, self.p_mpa, self.pb_mpa, self.t_k)
self.b_oil_m3m3 = pvt_rus.unf_b_oil_below_pb_m3m3(
self.t_k, self.p_mpa, self.gamma_oil, self.gamma_gas,
self.rho_gas_dissolved_relative_d, self.rho_gas_liberated_d,
self.gas_dissolved_m3t)
self.rho_oil_kgm3 = pvt_rus.unf_rho_oil_kgm3(
self.gamma_oil, self.rho_gas_dissolved_relative_d,
self.gas_dissolved_m3t, self.t_k, self.gamma_gas,
self.b_oil_m3m3)
self.mu_dead_oil_293_cp = pvt_rus.unf_mu_dead_oil_293_cp(
self.gamma_oil)
self.mu_dead_oil_t_cp = pvt_rus.unf_mu_dead_oil_t_cp(
self.mu_dead_oil_293_cp, self.t_k, self.gamma_oil)
self.mu_oil_below_pb_cp = pvt_rus.unf_mu_oil_below_pb_cp(
self.mu_dead_oil_t_cp, self.gas_dissolved_m3t, self.gamma_oil)
self.mu_oil_cp = self.mu_oil_below_pb_cp
self.sigma_oil_gas_nm = pvt_rus.unf_sigma_oil_gas_nm(
self.p_mpa, self.t_k, self.gamma_gas)
# теплоемкость
self.heatcap_oil_jkgc = self._calc_heatcap_oil_jkgc(
self.option.heatcap_oil_cor_number)
# теплопроводность
self.thermal_conduct_oil_wmk = self._calc_thermal_conduct_oil_wmk(
self.option.thermal_conduct_oil_cor_number)
# gas
self.tpc_k = self._calc_pseudocritical_temperature_k(
self.option.pseudocritical_temperature_cor_number)
self.ppc_mpa = self._calc_pseudocritical_pressure_mpa(
self.option.pseudocritical_pressure_cor_number)
self.z = self._calc_zfactor(self.option.z_cor_number)
self.mu_gas_cp = self._calc_mu_gas_cp(self.option.mu_gas_cor_number)
self.b_gas_m3m3 = self._calc_b_gas_m3m3(self.option.b_gas_cor_number)
self.compr_gas_1bar = self._calc_compr_gas_1bar(
self.option.compr_gas_cor_number)
self.rho_gas_kgm3 = self._calc_rho_gas_kgm3(
self.option.rho_gas_cor_number)
self.heatcap_gas_jkgc = self._calc_heatcap_gas_jkgc(
self.option.heatcap_gas_cor_number)
self.thermal_conduct_gas_wmk = self._calc_thermal_conduct_gas_wmk(
self.option.thermal_conduct_gas_cor_number)
# water
self.b_wat_m3m3 = self._calc_b_wat_m3m3(self.option.b_wat_cor_number)
self.rho_wat_kgm3 = self._calc_rho_wat_kgm3(
self.option.rho_wat_cor_number)
self.compr_wat_1bar = self._calc_compr_wat_1bar(
self.option.compr_gas_cor_number)
self.mu_wat_cp = self._calc_mu_wat_cp(self.option.mu_wat_cor_number)
self.rsw_m3m3 = self._calc_rs_wat_m3m3(self.option.rs_wat_cor_number)
self.heatcap_wat_jkgc = self._calc_heatcap_wat_jkgc(
self.option.heatcap_wat_cor_number)
self.thermal_conduct_wat_wmk = self._calc_thermal_conduct_wat_wmk(
self.option.thermal_conduct_wat_cor_number)
self.thermal_expansion_wat_1c = self._calc_thermal_expansion_wat_1c(
self.option.thermal_expansion_wat_cor_number)
# some system properties
self.sigma_oil_gas_Nm = self._calc_sigma_oil_gas_nm(
self.option.sigma_oil_gas_cor_number)
self.sigma_wat_gas_Nm = self._calc_sigma_wat_gas_nm(
self.option.sigma_wat_gas_cor_number)
def _calc_compr_wat_1bar(self, number_cor):
if number_cor == 0:
return uc.compr_1mpa_2_1bar(
PVT.unf_compressibility_brine_Spivey_1MPa(
self.t_k, self.p_mpa, self.s_ppm, self.z, self.par_wat))
def _calc_compr_gas_1bar(self, number_cor):
if number_cor == 0:
return uc.compr_1mpa_2_1bar(
PVT.unf_compressibility_gas_Mattar_1MPa(
self.p_mpa, self.t_k, self.ppc_mpa, self.tpc_k))
def calc(self, p_bar, t_c):
self.p_bar = p_bar
self.t_c = t_c
self.t_k = uc.c2k(self.t_c)
self.p_mpa = uc.bar2MPa(self.p_bar)
# oil
# давление насыщения нефти
self.pb_mpa = self._calc_pb_MPaa(self.option.pb_cor_number)
self.pb_bar = uc.MPa2bar(self.pb_mpa)
pbcal_MPaa = uc.bar2MPa(self.pb_cal_bar)
if pbcal_MPaa > 0:
p_fact = self.pb_mpa / pbcal_MPaa
# сдвигаем шкалу по давлению для расчета, если задана калибровка
self.p_mpa = p_fact * self.p_mpa
self.pb_bar = self.pb_bar / p_fact
# газосодержание
self.rs_m3m3 = self._calc_rs_m3m3(self.option.rs_cor_number)
# коэффициент изотермической сжимаемости
self.compr_oil_1mpa = self._calc_compr_oil_1mpa(
self.option.compr_oil_cor_number)
self.compr_oil_1bar = uc.compr_1mpa_2_1bar(self.compr_oil_1mpa)
# объемный коэффициент
self.b_oil_b_m3m3 = self._calc_b_oil_in_pb_m3m3(
self.option.b_oil_in_pb_cor_number)
if self.p_mpa > self.pb_mpa:
self.b_oil_m3m3 = self._calc_b_oil_above_pb_m3m3(
self.option.b_oil_above_pb_cor_number)
else:
self.b_oil_m3m3 = self._calc_b_oil_below_pb_m3m3(
self.option.b_oil_below_pb_cor_number)
if self.b_oil_b_cal_m3m3 > 0:
b_fact = (self.b_oil_b_cal_m3m3 - 1) / (self.b_oil_b_m3m3 - 1)
self.b_oil_m3m3 = b_fact * self.b_oil_m3m3
# плотность нефти
self.rho_oil_kgm3 = self._calc_rho_oil_kgm3(
self.option.rho_oil_cor_number)
# вязкость
self.mu_dead_oil_cp = self._calc_mu_dead_oil_cp(
self.option.mu_dead_oil_cor_number)
self.mu_oil_b_cP = self._calc_mu_oil_in_pb_cp(
self.option.mu_oil_pb_cor_number)
self.mu_oil_cp = self._calc_mu_oil_any_p_cp(
self.option.mu_oil_any_p_cor_number)
if self.mu_oil_b_cal_cp > 0:
mu_fact = self.mu_oil_b_cal_cp / self.mu_oil_b_cP
self.mu_oil_cp = mu_fact * self.mu_oil_cp
# теплоемкость
self.heatcap_oil_jkgc = self._calc_heatcap_oil_jkgc(
self.option.heatcap_oil_cor_number)
# теплопроводность
self.thermal_conduct_oil_wmk = self._calc_thermal_conduct_oil_wmk(
self.option.thermal_conduct_oil_cor_number)
# gas
self.tpc_k = self._calc_pseudocritical_temperature_k(
self.option.pseudocritical_temperature_cor_number)
self.ppc_mpa = self._calc_pseudocritical_pressure_mpa(
self.option.pseudocritical_pressure_cor_number)
self.z = self._calc_zfactor(self.option.z_cor_number)
self.mu_gas_cp = self._calc_mu_gas_cp(self.option.mu_gas_cor_number)
self.b_gas_m3m3 = self._calc_b_gas_m3m3(self.option.b_gas_cor_number)
self.compr_gas_1bar = self._calc_compr_gas_1bar(
self.option.compr_gas_cor_number)
self.rho_gas_kgm3 = self._calc_rho_gas_kgm3(
self.option.rho_gas_cor_number)
self.heatcap_gas_jkgc = self._calc_heatcap_gas_jkgc(
self.option.heatcap_gas_cor_number)
self.thermal_conduct_gas_wmk = self._calc_thermal_conduct_gas_wmk(
self.option.thermal_conduct_gas_cor_number)
# water
self.rho_wat_kgm3 = self._calc_rho_wat_kgm3(
self.option.rho_wat_cor_number)
self.compr_wat_1bar = self._calc_compr_wat_1bar(
self.option.compr_gas_cor_number)
self.b_wat_m3m3 = self._calc_b_wat_m3m3(self.option.b_wat_cor_number)
self.mu_wat_cp = self._calc_mu_wat_cp(self.option.mu_wat_cor_number)
self.rsw_m3m3 = self._calc_rs_wat_m3m3(self.option.rs_wat_cor_number)
self.heatcap_wat_jkgc = self._calc_heatcap_wat_jkgc(
self.option.heatcap_wat_cor_number)
self.thermal_conduct_wat_wmk = self._calc_thermal_conduct_wat_wmk(
self.option.thermal_conduct_wat_cor_number)
self.thermal_expansion_wat_1c = self._calc_thermal_expansion_wat_1c(
self.option.thermal_expansion_wat_cor_number)
# some system properties
self.sigma_oil_gas_Nm = self._calc_sigma_oil_gas_Nm(
self.option.sigma_oil_gas_cor_number)
self.sigma_wat_gas_Nm = self._calc_sigma_wat_gas_Nm(
self.option.sigma_wat_gas_cor_number)