added a CLI option to adjust output verbosity
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1 changed files with 23 additions and 12 deletions
35
coal.py
35
coal.py
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@ -1,15 +1,25 @@
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from functools import reduce
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import argparse
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import logging
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import cantera as ct
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import argparse
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logger = logging.getLogger()
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stream_handler = logging.StreamHandler()
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logger.addHandler(stream_handler)
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parser = argparse.ArgumentParser(description='Calculate Thermodynamic States of the Coal fired Boiler')
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parser.add_argument('--hhv', action='store_true', help='Higher heating value is used')
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parser.add_argument('-v', '--verbose', action='store_true', help='Verbose output')
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args = parser.parse_args()
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is_HHV = vars(args)['hhv']
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is_verbose = vars(args)['verbose']
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if is_verbose:
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logger.setLevel(logging.INFO)
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else:
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logger.setLevel(logging.WARNING)
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stdT = 298.15 # Temperature at standard state, K
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@ -72,7 +82,7 @@ airs = [
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]
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for i, air in enumerate(airs):
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print("air {}, T = {}, mass flow rate = {}".format(i+1, air.T, air.mass))
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logger.info("air {}, T = {}, mass flow rate = {}".format(i+1, air.T, air.mass))
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airmix = reduce(lambda a, b: a+b, airs)
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print("Total Air flow rate = ", airmix.mass)
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@ -128,18 +138,19 @@ Discrepency in Enthalpy of Formation for H2O is due to phase difference
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value above is for vapor and otherwise is for liquid water
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'''
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print(hf_product_coefs("CO2", "C"))
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print(hf_product_coefs("H2O", "H"))
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print(hf_product_coefs("SO2", "S"))
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logger.info("hf(CO2) / W(C) = {}".format(hf_product_coefs("CO2", "C")))
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logger.info("hf(H2O) / W(H) = {}".format(hf_product_coefs("H2O", "H")))
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logger.info("hf(SO2) / W(S) = {}".format(hf_product_coefs("SO2", "S")))
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sum_product_hf = (
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hf_product_coefs("CO2", "C") * coal.elemental_mass_fraction('C')
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+ hf_product_coefs("H2O", "H") * coal.elemental_mass_fraction('H')
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+ hf_product_coefs("SO2", "S") * coal.elemental_mass_fraction('S'))
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print("Sum(Hf_product), kJ/kg = ", sum_product_hf)
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sum_coal_hf = - coalHV + sum_product_hf
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print("Sum(Hf_reactant), kJ/kg = ", sum_coal_hf)
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logger.info("Sum(Hf_product), kJ/kg = {}".format(sum_product_hf))
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logger.info("Sum(Hf_reactant), kJ/kg = {}".format(sum_coal_hf))
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"""#############################################################################
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@ -150,11 +161,11 @@ Coal Enthalpy at 348.15 K = \Delta H_f + (H(348.15) - H(298.15))
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gr = ct.Solution('graphite.cti')
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gr.TP = coalT, ct.one_atm
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coal_preheat_enthalpy = gr.enthalpy_mass / 1000. # kJ/kg
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print("Coal preheat H , kJ/kg = ", coal_preheat_enthalpy)
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coal_enthalpy = sum_coal_hf + coal_preheat_enthalpy
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print("Coal enthalpy , kJ/kg = ", coal_enthalpy)
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print("Dummy Coal H , kJ/kg = ", coal.enthalpy_mass/1000.)
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logger.info("Coal preheat H , kJ/kg = ", coal_preheat_enthalpy)
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logger.info("Coal enthalpy , kJ/kg = ", coal_enthalpy)
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logger.info("Dummy Coal H , kJ/kg = ", coal.enthalpy_mass/1000.)
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"""#############################################################################
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@ -165,7 +176,7 @@ Therefore only difference between real coal enthalpy and dummy gas coal is
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#############################################################################"""
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enthalpy_added_after_mixing = (coal_enthalpy*1000 - coal.enthalpy_mass) * fuelMfr # J
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print("enthalpy to add later = ", enthalpy_added_after_mixing)
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logger.info("enthalpy to add later = ", enthalpy_added_after_mixing)
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################################################################################
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