From: Steven Baltakatei Sandoval <baltakatei@gmail.com>
Date: Thu, 20 Apr 2023 07:20:12 +0000 (+0000)
Subject: feat(unitproc/python/):Add EVA-2020-02-2 humidity conversions
X-Git-Tag: 0.8.2^2~15
X-Git-Url: https://zdv2.bktei.com/gitweb/BK-2020-03.git/commitdiff_plain/b9f7f61801c58ec9d948a4ddf442b54d96790bf8?ds=inline

feat(unitproc/python/):Add EVA-2020-02-2 humidity conversions

- Note: See:
  - https://zdv2.bktei.com/gitweb/EVA-2020-02.git
  - https://zdv2.bktei.com/gitweb/EVA-2020-02-2.git
  - https://gitlab.com/baltakatei/ninfacyzga-01
---

diff --git a/unitproc/python/bkt-humidity b/unitproc/python/bkt-humidity
new file mode 100644
index 0000000..437adc7
--- /dev/null
+++ b/unitproc/python/bkt-humidity
@@ -0,0 +1,185 @@
+#!/usr/bin/env python3
+# Desc: Humidity conversion functions from EVA-2020-02-2
+# Ref/Attrib: https://gitlab.com/baltakatei/ninfacyzga-01
+
+def rel_to_abs(T,P,RH):
+    """Returns absolute humidity given relative humidity.
+
+    Inputs:
+    --------
+    T : float
+        Absolute temperature in units Kelvin (K).
+    P : float
+        Total pressure in units Pascals (Pa).
+    RH : float
+        Relative humidity in units percent (%).
+
+    Output:
+    --------
+    absolute_humidity : float
+        Absolute humidity in units [kg water vapor / kg dry air].
+
+    References:
+    --------
+    1. Sonntag, D. "Advancements in the field of hygrometry". 1994. https://doi.org/10.1127/metz/3/1994/51
+    2. Green, D. "Perry's Chemical Engineers' Handbook" (8th Edition). Page "12-4". McGraw-Hill Professional Publishing. 2007.
+
+    Version: 0.0.1
+    Author: Steven Baltakatei Sandoval
+    License: GPLv3+
+    """
+
+    import math;
+
+    # Check input types
+    T = float(T);
+    P = float(P);
+    RH = float(RH);
+
+    #debug
+    # print('DEBUG:Input Temperature   (K)  :' + str(T));
+    # print('DEBUG:Input Pressure      (Pa) :' + str(P));
+    # print('DEBUG:Input Rel. Humidity (%)  :' + str(RH));
+
+    # Set constants and initial conversions
+    epsilon = 0.62198 # (molar mass of water vapor) / (molar mass of dry air)
+    t = T - 273.15; # Celsius from Kelvin
+    P_hpa = P / 100; # hectoPascals (hPa) from Pascals (Pa)
+
+    # Calculate e_w(T), saturation vapor pressure of water in a pure phase, in Pascals
+    ln_e_w = -6096*T**-1 + 21.2409642 - 2.711193*10**-2*T + 1.673952*10**-5*T**2 + 2.433502*math.log(T); # Sonntag-1994 eq 7; e_w in Pascals
+    e_w = math.exp(ln_e_w);
+    e_w_hpa = e_w / 100; # also save e_w in hectoPascals (hPa)
+    # print('DEBUG:ln_e_w:' + str(ln_e_w)); # debug
+    # print('DEBUG:e_w:' + str(e_w)); # debug
+
+    # Calculate f_w(P,T), enhancement factor for water
+    f_w = 1 + (10**-4*e_w_hpa)/(273 + t)*(((38 + 173*math.exp(-t/43))*(1 - (e_w_hpa / P_hpa))) + ((6.39 + 4.28*math.exp(-t / 107))*((P_hpa / e_w_hpa) - 1))); # Sonntag-1994 eq 22.
+    # print('DEBUG:f_w:' + str(f_w)); # debug
+
+    # Calculate e_prime_w(P,T), saturation vapor pressure of water in air-water mixture, in Pascals
+    e_prime_w = f_w * e_w; # Sonntag-1994 eq 18
+    # print('DEBUG:e_prime_w:' + str(e_prime_w)); # debug
+
+    # Calculate e_prime, vapor pressure of water in air, in Pascals
+    e_prime = (RH / 100) * e_prime_w;
+    # print('DEBUG:e_prime:' + str(e_prime)); # debug
+
+    # Calculate r, the absolute humidity, in [kg water vapor / kg dry air]
+    r = (epsilon * e_prime) / (P - e_prime);
+    # print('DEBUG:r:' + str(r)); # debug
+
+    return float(r);
+
+def rel_to_dpt(T,P,RH):
+    """Returns dew point temperature given relative humidity.
+
+    Inputs:
+    --------
+    T : float
+        Absolute temperature in units Kelvin (K).
+    P : float
+        Total pressure in units Pascals (Pa).
+    RH : float
+        Relative humidity in units percent (%).
+
+    Output:
+    --------
+    T_d : float
+        Dew point temperature in units Kelvin (K).
+
+    References:
+    --------
+    1. Sonntag, D. "Advancements in the field of hygrometry". 1994. https://doi.org/10.1127/metz/3/1994/51
+    2. Green, D. "Perry's Chemical Engineers' Handbook" (8th Edition). Page "12-4". McGraw-Hill Professional Publishing. 2007.
+
+    Version: 0.0.1
+    Author: Steven Baltakatei Sandoval
+    License: GPLv3+
+    """
+
+    import math;
+
+    # Check input types
+    T = float(T);
+    P = float(P);
+    RH = float(RH);
+
+    #debug
+    # print('DEBUG:Input Temperature   (K)  :' + str(T));
+    # print('DEBUG:Input Pressure      (Pa) :' + str(P));
+    # print('DEBUG:Input Rel. Humidity (%)  :' + str(RH));
+
+    # Set constants and initial conversions
+    epsilon = 0.62198 # (molar mass of water vapor) / (molar mass of dry air)
+    t = T - 273.15; # Celsius from Kelvin
+    P_hpa = P / 100; # hectoPascals (hPa) from Pascals (Pa)
+
+    # Calculate e_w(T), saturation vapor pressure of water in a pure phase, in Pascals
+    ln_e_w = -6096*T**-1 + 21.2409642 - 2.711193*10**-2*T + 1.673952*10**-5*T**2 + 2.433502*math.log(T); # Sonntag-1994 eq 7; e_w in Pascals
+    e_w = math.exp(ln_e_w);
+    e_w_hpa = e_w / 100; # also save e_w in hectoPascals (hPa)
+    # print('DEBUG:ln_e_w:' + str(ln_e_w)); # debug
+    # print('DEBUG:e_w:' + str(e_w)); # debug
+
+    # Calculate f_w(P,T), enhancement factor for water
+    f_w = 1 + (10**-4*e_w_hpa)/(273 + t)*(((38 + 173*math.exp(-t/43))*(1 - (e_w_hpa / P_hpa))) + ((6.39 + 4.28*math.exp(-t / 107))*((P_hpa / e_w_hpa) - 1))); # Sonntag-1994 eq 22.
+    # print('DEBUG:f_w:' + str(f_w)); # debug
+
+    # Calculate e_prime_w(P,T), saturation vapor pressure of water in air-water mixture, in Pascals
+    e_prime_w = f_w * e_w; # Sonntag-1994 eq 18
+    # print('DEBUG:e_prime_w:' + str(e_prime_w)); # debug
+
+    # Calculate e_prime, vapor pressure of water in air, in Pascals
+    e_prime = (RH / 100) * e_prime_w;
+    # print('DEBUG:e_prime:' + str(e_prime)); # debug
+
+    n = 0; repeat_flag = True;
+    while repeat_flag == True:
+        # print('DEBUG:n:' + str(n)); # debug
+
+        # Calculate f_w_td, the enhancement factor for water at dew point temperature.
+        if n == 0:
+            f = 1.0016 + 3.15*10**-6*P_hpa - (0.074 / P_hpa); # Sonntag-1994 eq 24
+            f_w_td = f; # initial approximation
+        elif n > 0:
+            t_d_prev = float(t_d); # save previous t_d value for later comparison
+            f_w_td = 1 + (10**-4*e_w_hpa)/(273 + t_d)*(((38 + 173*math.exp(-t_d/43))*(1 - (e_w_hpa / P_hpa))) + ((6.39 + 4.28*math.exp(-t_d / 107))*((P_hpa / e_w_hpa) - 1))); # Sonntag-1994 eq 22.
+        # print('DEBUG:f_w_td:' + str(f_w_td)); # debug
+
+        # Calculate e, the vapor pressure of water in the pure phase, in Pascals
+        e = (e_prime / f_w_td); # Sonntag-1994 eq 9 and 20
+        # print('DEBUG:e:' + str(e)); # debug
+
+        # Calculate y, an intermediate dew point calculation variable
+        y = math.log(e / 611.213);
+        # print('DEBUG:y:' + str(y)); # debug
+
+        # Calculate t_d, the dew point temperature in degrees Celsius
+        t_d = 13.715*y + 8.4262*10**-1*y**2 + 1.9048*10**-2*y**3 + 7.8158*10**-3*y**4;# Sonntag-1994 eq 10
+        # print('DEBUG:t_d:' + str(t_d)); # debug
+
+        if n == 0:
+            # First run
+            repeat_flag = True;
+        else:
+            # Test t_d accuracy
+            t_d_diff = math.fabs(t_d - t_d_prev);
+            # print('DEBUG:t_d     :' + str(t_d)); # debug
+            # print('DEBUG:t_d_prev:' + str(t_d_prev)); # debug
+            # print('DEBUG:t_d_diff:' + str(t_d_diff)); # debug
+            if t_d_diff < 0.01:
+                repeat_flag = False;
+            else:
+                repeat_flag = True;
+
+        # Calculate T_d, the dew point temperature in Kelvin
+        T_d = 273.15 + t_d;
+        # print('DEBUG:T_d:' + str(T_d)); # debug
+
+        if n > 100:
+            return T_d; # good enough
+
+        # update loop counter
+        n += 1;
+    return T_d;