#通过一个字典定义一个汽轮机
import pandas as pd
from CoolProp.CoolProp import PropsSI
from collections import defaultdict
from datetime import datetime
class Turbine:
def __init__(self, params):
# 初始化汽轮机的属性
self.Zr = params.get("汽轮机再热次数")
self.CN = params.get("汽轮机缸体个数")
self.is_combined = params.get("汽轮机是否合缸")
self.HP = params.get("高加个数")
self.LP = params.get("低加个数")
self.NCG=params.get("超高压缸抽汽级数")
self.NG = params.get("高压缸抽汽级数")
self.NZ = params.get("中压缸抽汽级数")
self.NL = params.get("低压缸抽汽级数")
def __str__(self):
return (f"Turbine:\\n"
f"再热次数: {self.Zr}\\n"
f"缸体个数: {self.CN}\\n"
f"是否合缸: {'是' if self.is_combined else '否'}\\n"
f"高加个数: {self.HP}\\n"
f"低加个数: {self.LP}\\n"
f"超高压缸抽汽级数:{self.NCG}\\n"
f"高压缸抽汽级数: {self.NG}\\n"
f"中压缸抽汽级数: {self.NZ}\\n"
f"低压缸抽汽级数: {self.NL}")
# 示例字典
turbine_data = {
"汽轮机再热次数": 1,
"汽轮机缸体个数": 3,
"汽轮机是否合缸": True, # 可以是 True 或 False
"高加个数": 3,
"低加个数": 4,
"超高压缸抽汽级数":0,
"高压缸抽汽级数": 2,
"中压缸抽汽级数": 2,
"低压缸抽汽级数": 4,
}
# 创建Turbine实例
turbine = Turbine(turbine_data)
# 打印Turbine的属性
#print(turbine)
class Point:
def __init__(self, pressure, temperature, flow_rate=None):
self.pressure = pressure*1000000 # 压力 (MPa)
self.temperature = temperature+273.15 # 温度 (℃)
self.flow_rate = flow_rate # 流量 (t/h),可选
def calculate_enthalpy(self):
# 根据压力和温度计算焓值 kJ/kg
return PropsSI('H', 'P', self.pressure, 'T', self.temperature, 'Water')/1000
def calculate_entropy(self):
# 根据压力和温度计算熵值 kJ/kg.℃
return PropsSI('S', 'P', self.pressure, 'T', self.temperature, 'Water')/1000
def calculate_dryness_fraction(self):
# 根据压力和温度计算干度
P_sat = PropsSI('P', 'T', self.temperature, 'Q', 1, 'Water')
# 计算干度(湿度)
if P_sat > 0:
quality = 0.91
else:
quality = None # 饱和压力为0的情况,无法计算干度
#print("干度为:",quality)
return quality
# 初始化字典用于存储输入数据
qufu_1_measurementpoint = {}
class TurbineCylinder:
def __init__(self, inlet: Point, outlet: Point):
self.inlet = inlet # 进口工质状态点
self.outlet = outlet # 出口工质状态点
def calculate_efficiency(self):
# 计算出口等熵焓
outlet_isenthalpic_enthalpy = PropsSI('H', 'P', self.outlet.pressure, 'S', self.inlet.calculate_entropy()*1000,'Water')/1000
#print(outlet_isenthalpic_enthalpy)
# 根据公式计算汽轮机缸体内效率
efficiency = 100*(self.inlet.calculate_enthalpy() - self.outlet.calculate_enthalpy()) /(self.inlet.calculate_enthalpy() - outlet_isenthalpic_enthalpy)
return efficiency
class LowPressureTurbineCylinder(TurbineCylinder):
def calculate_efficiency(self):
# 计算进口蒸汽的焓
inlet_enthalpy = self.inlet.calculate_enthalpy()
# 计算出口蒸汽的焓
outlet_enthalpy = self.outlet.calculate_enthalpy()
# 计算出口蒸汽的干度
dryness_fraction = self.outlet.calculate_dryness_fraction()
# 计算出口等熵焓
outlet_isenthalpic_enthalpy = PropsSI(
'H', 'P', self.outlet.pressure, 'S', self.inlet.calculate_entropy() * 1000, 'Water'
) / 1000
#print("出口等熵焓",outlet_isenthalpic_enthalpy)
# 计算低压缸的缸效率
efficiency = 100 * (inlet_enthalpy - outlet_enthalpy * dryness_fraction) / (
inlet_enthalpy - outlet_isenthalpic_enthalpy)
return efficiency
class Heater:
def __init__(self, n, water_inlet: Point, water_outlet: Point,
steam_inlet: Point, steam_drain: Point,
n_minus_1_steam_drain: Point, N3):
self.n = n # 加热器编号
self.water_inlet = water_inlet # 水侧进口
self.water_outlet = water_outlet # 水侧出口
self.steam_inlet = steam_inlet # 汽侧进口
self.steam_drain = steam_drain # 汽侧疏水
self.n_minus_1_steam_drain = n_minus_1_steam_drain # n-1级加热器汽侧疏水
self.N3 = N3 # 参考的N3
def is_first_heater(self):
# 判断是否为首级加热器
return self.n == 1 or self.n == self.N3 + 1+1
def upper_difference(self):
# 加热器上端差
saturation_temp = PropsSI('T', 'P', self.steam_inlet.pressure, 'Q', 1, 'Water')
return saturation_temp - self.water_outlet.temperature
def lower_difference(self):
# 加热器下端差
return self.steam_drain.temperature - self.water_inlet.temperature
def temperature_rise(self):
# 加热器温升
return self.water_outlet.temperature - self.water_inlet.temperature
class Pump:
def __init__(self, inlet: Point, outlet1: Point, outlet2=None):
self.inlet = inlet # 水泵入口
self.outlet1 = outlet1 # 水泵出口1
self.outlet2 = outlet2 # 水泵出口2(可选)
def calculate_enthalpy_rise(self):
# 水泵焓升计算
return (self.outlet1.calculate_enthalpy() - self.inlet.calculate_enthalpy())
def calculate_efficiency(self, power_input, flow_rate):
# 水泵效率计算
# 效率 = 输出功 / 输入功
# 输出功 = 焓升 * 流量
# 输入功 = 电机功率
enthalpy_rise = self.calculate_enthalpy_rise()
output_power = enthalpy_rise * flow_rate/3.6
return output_power / power_input*100 if power_input > 0 else 0
"""
以曲阜热电厂1号机为例,进行演示
"""
# 以曲阜热电厂1号机为实例进行实例演示,三缸合缸机组
if __name__ == "__main__":
turbine_params = {
"汽轮机再热次数": 1,
"汽轮机缸体个数": 3,
"高加个数": 3,
"低加个数": 4,
"汽轮机是否合缸": True,
"超高压缸抽汽级数":0,
"高压缸抽汽级数": 2,
"中压缸抽汽级数": 2,
"低压缸抽汽级数": 4
}
qufu_1_turbine = Turbine(turbine_params)
#1 缸体参数
Case_inlet={}
Case_outlet={}
qufu_case={}
for i in range(1,qufu_1_turbine.CN+1):
Case_inlet[i]=Point(
pressure=float(input(f"请输入{i}号缸体进口压力,单位MPa:")),
temperature=float(input(f"请输入{i}号缸体进口温度,单位℃:"))
)
Case_outlet[i]=Point(
pressure=float(input(f"请输入{i}号缸体出口压力,单位MPa:")),
temperature=float(input(f"请输入{i}号缸体出口温度,单位℃:"))
)
qufu_case[i]=TurbineCylinder(Case_inlet[i], Case_outlet[i])
# 将数据存入字典
qufu_1_measurementpoint[f"{i}号缸体进口压力"] = Case_inlet[i].pressure
qufu_1_measurementpoint[f"{i}号缸体进口温度"] = Case_inlet[i].temperature
qufu_1_measurementpoint[f"{i}号缸体出口压力"] = Case_outlet[i].pressure
qufu_1_measurementpoint[f"{i}号缸体出口温度"] = Case_outlet[i].temperature
if i==qufu_1_turbine.CN:
qufu_case[3]=LowPressureTurbineCylinder(Case_inlet[i], Case_outlet[i])
# print(f"曲阜热电厂1号机高压缸的效率为{qufu_case[1].calculate_efficiency()}%")
# print(f"曲阜热电厂1号机中压缸的效率为{qufu_case[2].calculate_efficiency()}%")
# print(f"曲阜热电厂1号机低压缸的效率为{qufu_case[3].calculate_efficiency()}%")
#2抽汽
Extraction={}
for i in range(1,qufu_1_turbine.NCG+qufu_1_turbine.NG+qufu_1_turbine.NZ+qufu_1_turbine.NL+1):
Extraction[i]=Point(
pressure=float(input(f"请输入{i}段抽汽压力,单位MPa: ")),
temperature=float(input(f"请输入{i}段抽汽温度,单位℃: "))
)
qufu_1_measurementpoint[f"{i}段抽汽压力"] = Extraction[i].pressure
qufu_1_measurementpoint[f"{i}段抽汽温度"] = Extraction[i].temperature
from collections import defaultdict
# 初始化字典
HP_water_inlet = {}
HP_water_outlet = {}
HP_steam_inlet = {}
HP_steam_drain = defaultdict(lambda: Point(pressure=0, temperature=0)) # 使用 defaultdict
HP_heater = {}
#3高压加热器输入数据并初始化加热器
for i in range(1, qufu_1_turbine.HP + 1):
# 输入水侧进口参数
HP_water_inlet[i] = Point(
pressure=float(input(f"请输入{i}号高加水侧进口压力,单位MPa: ")),
temperature=float(input(f"请输入{i}号高加水侧进口温度,单位℃: "))
)
# 输入水侧出口参数
HP_water_outlet[i] = Point(
pressure=float(input(f"请输入{i}号高加水侧出口压力,单位MPa: ")),
temperature=float(input(f"请输入{i}号高加水侧出口温度,单位℃: "))
)
# 输入汽侧进口参数
HP_steam_inlet[i] = Point(
pressure=float(input(f"请输入{i}号高加汽侧进口压力,单位MPa: ")),
temperature=float(input(f"请输入{i}号高加汽侧进口温度,单位℃: "))
)
# 输入汽侧疏水参数
HP_steam_drain[i] = Point(
pressure=float(input(f"请输入{i}号高加汽侧疏水压力,单位MPa: ")),
temperature=float(input(f"请输入{i}号高加汽侧疏水温度,单位℃: "))
)
# 将数据存入字典
qufu_1_measurementpoint[f"{i}号高加水侧进口压力"] = HP_water_inlet[i].pressure
qufu_1_measurementpoint[f"{i}号高加水侧进口温度"] = HP_water_inlet[i].temperature
qufu_1_measurementpoint[f"{i}号高加水侧出口压力"] = HP_water_outlet[i].pressure
qufu_1_measurementpoint[f"{i}号高加水侧出口温度"] = HP_water_outlet[i].temperature
qufu_1_measurementpoint[f"{i}号高加汽侧进口压力"] = HP_steam_inlet[i].pressure
qufu_1_measurementpoint[f"{i}号高加汽侧进口温度"] = HP_steam_inlet[i].temperature
qufu_1_measurementpoint[f"{i}号高加汽侧疏水压力"] = HP_steam_drain[i].pressure
qufu_1_measurementpoint[f"{i}号高加汽侧疏水温度"] = HP_steam_drain[i].temperature
# 创建加热器实例
if i == 1:
# 首级加热器没有上一级疏水点
HP_heater[i] = Heater(
n=i,
water_inlet=HP_water_inlet[i],
water_outlet=HP_water_outlet[i],
steam_inlet=HP_steam_inlet[i],
steam_drain=HP_steam_drain[i],
n_minus_1_steam_drain=None, # 首级加热器没有上一级疏水点
N3=qufu_1_turbine.HP
)
elif i >= 2:
# 非首级加热器,使用上一级疏水点
HP_heater[i] = Heater(
n=i,
water_inlet=HP_water_inlet[i],
water_outlet=HP_water_outlet[i],
steam_inlet=HP_steam_inlet[i],
steam_drain=HP_steam_drain[i],
n_minus_1_steam_drain=HP_steam_drain[i - 1], # 使用上一级疏水点
N3=qufu_1_turbine.HP
)
# print(f"{i}号高加是否为首级加热器:", HP_heater[i].is_first_heater())
#
# print(f"{i}号高加上端差:", HP_heater[i].upper_difference(), "K")
# print(f"{i}号高加下端差:", HP_heater[i].lower_difference(), "K")
# print(f"{i}号高加温升:", HP_heater[i].temperature_rise(), "K")
# 3低压加热器输入数据并初始化加热器
# 初始化字典
LP_water_inlet = {}
LP_water_outlet = {}
LP_steam_inlet = {}
LP_steam_drain = defaultdict(lambda: Point(pressure=0, temperature=0)) # 使用 defaultdict
LP_heater = {}
for i in range(qufu_1_turbine.HP+2, qufu_1_turbine.HP + 1+qufu_1_turbine.LP+1):
# 输入水侧进口参数
LP_water_inlet[i] = Point(
pressure=float(input(f"请输入{i}号低加水侧进口压力,单位MPa: ")),
temperature=float(input(f"请输入{i}号低加水侧进口温度,单位℃: "))
)
# 输入水侧出口参数
LP_water_outlet[i] = Point(
pressure=float(input(f"请输入{i}号低加水侧出口压力,单位MPa: ")),
temperature=float(input(f"请输入{i}号低加水侧出口温度,单位℃: "))
)
if i==qufu_1_turbine.HP+2:
LP_water_outlet[i] = Point(
pressure=float(input(f"请输入{i}号低加水侧出口压力,单位MPa: ")),
temperature=float(input(f"请输入{i}号低加水侧出口温度,单位℃: ")),
flow_rate=float(input(f"请输入{i}号低加水侧出口流量,单位t/h: "))
)
# 输入汽侧进口参数
LP_steam_inlet[i] = Point(
pressure=float(input(f"请输入{i}号低加汽侧进口压力,单位MPa: ")),
temperature=float(input(f"请输入{i}号低加汽侧进口温度,单位℃: "))
)
# 输入汽侧疏水参数
LP_steam_drain[i] = Point(
pressure=float(input(f"请输入{i}号低加汽侧疏水压力,单位MPa: ")),
temperature=float(input(f"请输入{i}号低加汽侧疏水温度,单位℃: "))
)
# 将数据存入字典
qufu_1_measurementpoint[f"{i}号低加水侧进口压力"] = LP_water_inlet[i].pressure
qufu_1_measurementpoint[f"{i}号低加水侧进口温度"] = LP_water_inlet[i].temperature
qufu_1_measurementpoint[f"{i}号低加水侧出口压力"] = LP_water_outlet[i].pressure
qufu_1_measurementpoint[f"{i}号低加水侧出口温度"] = LP_water_outlet[i].temperature
qufu_1_measurementpoint[f"{i}号低加汽侧进口压力"] = LP_steam_inlet[i].pressure
qufu_1_measurementpoint[f"{i}号低加汽侧进口温度"] = LP_steam_inlet[i].temperature
qufu_1_measurementpoint[f"{i}号低加汽侧疏水压力"] = LP_steam_drain[i].pressure
qufu_1_measurementpoint[f"{i}号低加汽侧疏水温度"] = LP_steam_drain[i].temperature
# 创建加热器实例
if i == qufu_1_turbine.HP+2:
# 首级加热器没有上一级疏水点
LP_heater[i] = Heater(
n=i,
water_inlet=LP_water_inlet[i],
water_outlet=LP_water_outlet[i],
steam_inlet=LP_steam_inlet[i],
steam_drain=LP_steam_drain[i],
n_minus_1_steam_drain=None, # 首级加热器没有上一级疏水点
N3=qufu_1_turbine.HP
)
elif i >= qufu_1_turbine.HP+3:
# 非首级加热器,使用上一级疏水点
LP_heater[i] = Heater(
n=i,
water_inlet=LP_water_inlet[i],
water_outlet=LP_water_outlet[i],
steam_inlet=LP_steam_inlet[i],
steam_drain=LP_steam_drain[i],
n_minus_1_steam_drain=LP_steam_drain[i - 1], # 使用上一级疏水点
N3=qufu_1_turbine.HP
)
# print(f"{i}号低加是否为首级加热器:", LP_heater[i].is_first_heater())
#
# print(f"{i}号低加上端差:", LP_heater[i].upper_difference(), "K")
# print(f"{i}号低加下端差:", LP_heater[i].lower_difference(), "K")
# print(f"{i}号低加温升:", LP_heater[i].temperature_rise(), "K")
Deae_water_outlet =Point(
pressure=float(input(f"除氧器出口压力,单位MPa: ")),
temperature=float(input(f"除氧器出口温度,单位℃: "))
)
Deae_steam_inlet = Point(
pressure=float(input(f"除氧器进汽压力,单位MPa: ")),
temperature=float(input(f"除氧器进汽温度,单位℃: "))
)
qufu_1_measurementpoint[f"除氧器出口压力"] = Deae_water_outlet.pressure
qufu_1_measurementpoint[f"除氧器出口温度"] = Deae_water_outlet.temperature
qufu_1_measurementpoint[f"除氧器进汽压力"] = Deae_steam_inlet.pressure
qufu_1_measurementpoint[f"除氧器进汽温度"] = Deae_steam_inlet.temperature
#5除氧器
Deae = Heater(
n=qufu_1_turbine.HP+1,
water_inlet=LP_heater[qufu_1_turbine.HP+2].water_outlet,
water_outlet=Deae_water_outlet,
steam_inlet=Deae_steam_inlet,
steam_drain=Deae_water_outlet,
n_minus_1_steam_drain=HP_heater[qufu_1_turbine.HP].steam_drain, # 首级加热器没有上一级疏水点
N3=qufu_1_turbine.HP+2
)
#6凝汽器
Cond_water_inlet = Point(
pressure=float(input(f"凝汽器水侧循环水进口压力,单位MPa: ")),
temperature=float(input(f"凝汽器水侧循环水进口温度,单位℃: "))
)
Cond_water_outlet = Point(
pressure=float(input(f"凝汽器热井出口压力,单位MPa: ")),
temperature=float(input(f"凝汽器热井出口温度,单位℃: "))
)
qufu_1_measurementpoint[f"凝汽器水侧循环水进口压力"] = Cond_water_inlet.pressure
qufu_1_measurementpoint[f"凝汽器水侧循环水进口温度"] = Cond_water_inlet.temperature
qufu_1_measurementpoint[f"凝汽器热井出口压力"] = Cond_water_outlet.pressure
qufu_1_measurementpoint[f"凝汽器热井出口温度"] = Cond_water_outlet.temperature
Cond = Heater(
n=qufu_1_turbine.HP + qufu_1_turbine.LP+2,
water_inlet=Cond_water_inlet,
water_outlet=Cond_water_outlet,
steam_inlet=qufu_case[qufu_1_turbine.CN].outlet,
steam_drain=Cond_water_outlet,
n_minus_1_steam_drain=None, # 首级加热器没有上一级疏水点
N3=qufu_1_turbine.HP + qufu_1_turbine.LP+4
)
#7轴封漏汽
HP_back_gland=Point(
pressure=float(input(f"高压缸后轴封漏汽压力,单位MPa: ")),
temperature=float(input(f"高压缸后轴封漏汽温度,单位℃: ")),
flow_rate=float(input(f"高压缸后轴封漏汽流量,单位t/h: "))
)
qufu_1_measurementpoint[f"高压缸后轴封漏汽压力"] = HP_back_gland.pressure
qufu_1_measurementpoint[f"高压缸后轴封漏汽温度"] = HP_back_gland.temperature
qufu_1_measurementpoint[f"高压缸后轴封漏汽流量"] = HP_back_gland.flow_rate
if qufu_1_turbine.is_combined is False:
HP_front_gland = Point(
pressure=float(input(f"高压缸前轴封漏汽压力,单位MPa: ")),
temperature=float(input(f"高压缸前轴封漏汽温度,单位℃: ")),
flow_rate=float(input(f"高压缸前轴封漏汽流量,单位t/h: "))
)
IP_front_gland = Point(
pressure=float(input(f"中压缸前轴封漏汽压力,单位MPa: ")),
temperature=float(input(f"中压缸前轴封漏汽温度,单位℃: ")),
flow_rate=float(input(f"中压缸前轴封漏汽流量,单位t/h: "))
)
qufu_1_measurementpoint[f"高压缸前轴封漏汽压力"] = HP_front_gland.pressure
qufu_1_measurementpoint[f"高压缸前轴封漏汽温度"] = HP_front_gland.temperature
qufu_1_measurementpoint[f"高压缸前轴封漏汽流量"] = HP_front_gland.flow_rate
qufu_1_measurementpoint[f"中压缸前轴封漏汽压力"] = IP_front_gland.pressure
qufu_1_measurementpoint[f"中压缸前轴封漏汽温度"] = IP_front_gland.temperature
qufu_1_measurementpoint[f"中压缸前轴封漏汽流量"] = IP_front_gland.flow_rate
IP_back_gland=Point(
pressure=float(input(f"中压缸后轴封漏汽压力,单位MPa: ")),
temperature=float(input(f"中压缸后轴封漏汽温度,单位℃: ")),
flow_rate=float(input(f"中压缸后轴封漏汽流量,单位t/h: "))
)
qufu_1_measurementpoint[f"中压缸后轴封漏汽压力"] = IP_back_gland.pressure
qufu_1_measurementpoint[f"中压缸后轴封漏汽温度"] = IP_back_gland.temperature
qufu_1_measurementpoint[f"中压缸后轴封漏汽流量"] = IP_back_gland.flow_rate
LP_front_gland=Point(
pressure=float(input(f"低压缸前轴封漏汽压力,单位MPa: ")),
temperature=float(input(f"低压缸前轴封漏汽温度,单位℃: ")),
flow_rate=float(input(f"低压缸前轴封漏汽流量,单位t/h: "))
)
qufu_1_measurementpoint[f"低压缸前轴封漏汽压力"] = LP_front_gland.pressure
qufu_1_measurementpoint[f"低压缸前轴封漏汽温度"] = LP_front_gland.temperature
qufu_1_measurementpoint[f"低压缸前轴封漏汽流量"] = LP_front_gland.flow_rate
LP_back_gland=Point(
pressure=float(input(f"低压缸后轴封漏汽压力,单位MPa: ")),
temperature=float(input(f"低压缸后轴封漏汽温度,单位℃: ")),
flow_rate=float(input(f"低压缸后轴封漏汽流量,单位t/h: "))
)
qufu_1_measurementpoint[f"低压缸后轴封漏汽压力"] = LP_back_gland.pressure
qufu_1_measurementpoint[f"低压缸后轴封漏汽温度"] = LP_back_gland.temperature
qufu_1_measurementpoint[f"低压缸后轴封漏汽流量"] = LP_back_gland.flow_rate
#8其他必须的常规参数
reheat_spray_water=Point(
pressure=float(input(f"再热器减温水压力,单位MPa: ")),
temperature=float(input(f"再热器减温水温度,单位℃: ")),
flow_rate=float(input(f"再热器减温水流量,单位t/h: "))
)
qufu_1_measurementpoint[f"再热器减温水压力"] = reheat_spray_water.pressure
qufu_1_measurementpoint[f"再热器减温水温度"] = reheat_spray_water.temperature
qufu_1_measurementpoint[f"再热器减温水流量"] = reheat_spray_water.flow_rate
superheat_spray_water=Point(
pressure=float(input(f"过热器减温水压力,单位MPa: ")),
temperature=float(input(f"过热器减温水温度,单位℃: ")),
flow_rate=float(input(f"过热器减温水流量,单位t/h: "))
)
qufu_1_measurementpoint[f"过热器减温水压力"] = superheat_spray_water.pressure
qufu_1_measurementpoint[f"过热器减温水温度"] = superheat_spray_water.temperature
qufu_1_measurementpoint[f"过热器减温水流量"] = superheat_spray_water.flow_rate
generator_power=float(input(f"发电机功率,单位kW: "))
generator_xiaolv=float(input(f"发电机效率,单位/ "))
mechanical_loss=float(input(f"机械损失,单位kW: "))
DL_deae_flow=float(input(f"除氧器当量流量,单位t/h: "))
mf_inlet_flow=float(input(f"给水泵密封水进水流量,单位t/h: "))
mf_outlet_flow=float(input(f"给水泵密封水回水流量,单位t/h: "))
cond_water_flow=float(input(f"主凝结水流量,单位t/h: "))
qufu_1_measurementpoint[f"发电机功率"] = generator_power
qufu_1_measurementpoint[f"发电机效率"] = generator_xiaolv
qufu_1_measurementpoint[f"机械损失"] = mechanical_loss
qufu_1_measurementpoint[f"除氧器当量流量"] = DL_deae_flow
qufu_1_measurementpoint[f"给水泵密封水进水流量"] = mf_inlet_flow
qufu_1_measurementpoint[f"给水泵密封水回水流量"] = mf_outlet_flow
qufu_1_measurementpoint[f"主凝结水流量"] = cond_water_flow
current_time = datetime.now().strftime("%Y%m%d_%H%M%S")
filename = f'qufu_1_measurementpoint_{current_time}.csv'
# 将字典转换为DataFrame并保存为CSV文件
df = pd.DataFrame(list(qufu_1_measurementpoint.items()), columns=['参数', '值'])
df.to_csv(filename, index=False, encoding='utf-8-sig')
print(f"数据已成功保存到 {filename} 文件中。")
利用8个参数定义一个汽轮机,然后根据这8个参数生成汽轮机性能试验时的测点清单-pycharm-源代码(适用所有类型汽轮机)
CODE-boy12025-03-13 8:40
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