From 7b6e723379e684ccd20e1ec2341786475480d635 Mon Sep 17 00:00:00 2001 From: Jolando Kisse Date: Tue, 3 Dec 2024 11:29:21 +0100 Subject: [PATCH 1/2] update density and viscosity properties for N2, O2, H2, CO2, CH4, Ethane to values at 1.01325 bar instead of 1 bar --- .../properties/carbondioxide/density.txt | 69 +++++++++-- .../properties/carbondioxide/viscosity.txt | 69 +++++++++-- src/pandapipes/properties/ethane/density.txt | 68 ++++++++-- .../properties/ethane/viscosity.txt | 68 ++++++++-- .../properties/hydrogen/density.txt | 116 ++++++++--------- .../properties/hydrogen/viscosity.txt | 114 ++++++++--------- src/pandapipes/properties/methane/density.txt | 70 +++++++++-- .../properties/methane/viscosity.txt | 70 +++++++++-- .../properties/nitrogen/density.txt | 117 +++++++++--------- .../properties/nitrogen/viscosity.txt | 116 ++++++++--------- src/pandapipes/properties/oxygen/density.txt | 115 ++++++++--------- .../properties/oxygen/viscosity.txt | 112 ++++++++--------- 12 files changed, 710 insertions(+), 394 deletions(-) diff --git a/src/pandapipes/properties/carbondioxide/density.txt b/src/pandapipes/properties/carbondioxide/density.txt index 89bb1c744..46d35ba4f 100644 --- a/src/pandapipes/properties/carbondioxide/density.txt +++ b/src/pandapipes/properties/carbondioxide/density.txt @@ -1,8 +1,61 @@ -263 2.027 -273 1.951 -283 1.88 -293 1.815 -303 1.754 -313 1.697 -323 1.644 -333 1.594 +# NIST Chemistry WebBook, SRD 69 +# https://webbook.nist.gov/cgi/fluid.cgi?P=1.01325&TLow=263.15&THigh=373.15&TInc=2&Applet=on&Digits=6&ID=C124389&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF +# Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) +# temperature in Kelvin, density in kg/m³ at 1.01325 bar +263.15 2.05376 +265.15 2.03788 +267.15 2.02226 +269.15 2.00687 +271.15 1.99173 +273.15 1.97681 +275.15 1.96213 +277.15 1.94766 +279.15 1.93341 +281.15 1.91938 +283.15 1.90555 +285.15 1.89192 +287.15 1.87849 +289.15 1.86526 +291.15 1.85221 +293.15 1.83934 +295.15 1.82666 +297.15 1.81416 +299.15 1.80183 +301.15 1.78966 +303.15 1.77767 +305.15 1.76583 +307.15 1.75416 +309.15 1.74264 +311.15 1.73127 +313.15 1.72005 +315.15 1.70898 +317.15 1.69806 +319.15 1.68727 +321.15 1.67662 +323.15 1.66611 +325.15 1.65573 +327.15 1.64548 +329.15 1.63536 +331.15 1.62536 +333.15 1.61549 +335.15 1.60574 +337.15 1.5961 +339.15 1.58658 +341.15 1.57718 +343.15 1.56789 +345.15 1.55871 +347.15 1.54963 +349.15 1.54066 +351.15 1.5318 +353.15 1.52304 +355.15 1.51438 +357.15 1.50582 +359.15 1.49735 +361.15 1.48898 +363.15 1.48071 +365.15 1.47253 +367.15 1.46444 +369.15 1.45643 +371.15 1.44852 +373.15 1.44069 + diff --git a/src/pandapipes/properties/carbondioxide/viscosity.txt b/src/pandapipes/properties/carbondioxide/viscosity.txt index 1bc429a2a..d6e9cf352 100644 --- a/src/pandapipes/properties/carbondioxide/viscosity.txt +++ b/src/pandapipes/properties/carbondioxide/viscosity.txt @@ -1,8 +1,61 @@ -263 13.22e-6 -273 13.71e-6 -283 14.2e-6 -293 14.69e-6 -303 15.17e-6 -313 15.65e-6 -323 16.13e-6 -333 16.61e-6 +# NIST Chemistry WebBook, SRD 69 +# https://webbook.nist.gov/cgi/fluid.cgi?P=1.01325&TLow=263.15&THigh=373.15&TInc=2&Digits=6&ID=C74840&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF +# Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) +# temperature in Kelvin, dynamic viscosity in kg/(m s) +263.15 1.32E-05 +265.15 1.33E-05 +267.15 1.34E-05 +269.15 1.35E-05 +271.15 1.36E-05 +273.15 1.37E-05 +275.15 1.38E-05 +277.15 1.39E-05 +279.15 1.40E-05 +281.15 1.41E-05 +283.15 1.42E-05 +285.15 1.43E-05 +287.15 1.44E-05 +289.15 1.45E-05 +291.15 1.46E-05 +293.15 1.47E-05 +295.15 1.48E-05 +297.15 1.49E-05 +299.15 1.50E-05 +301.15 1.51E-05 +303.15 1.52E-05 +305.15 1.52E-05 +307.15 1.53E-05 +309.15 1.54E-05 +311.15 1.55E-05 +313.15 1.56E-05 +315.15 1.57E-05 +317.15 1.58E-05 +319.15 1.59E-05 +321.15 1.60E-05 +323.15 1.61E-05 +325.15 1.62E-05 +327.15 1.63E-05 +329.15 1.64E-05 +331.15 1.65E-05 +333.15 1.66E-05 +335.15 1.67E-05 +337.15 1.68E-05 +339.15 1.69E-05 +341.15 1.69E-05 +343.15 1.70E-05 +345.15 1.71E-05 +347.15 1.72E-05 +349.15 1.73E-05 +351.15 1.74E-05 +353.15 1.75E-05 +355.15 1.76E-05 +357.15 1.77E-05 +359.15 1.78E-05 +361.15 1.79E-05 +363.15 1.80E-05 +365.15 1.81E-05 +367.15 1.81E-05 +369.15 1.82E-05 +371.15 1.83E-05 +373.15 1.84E-05 + diff --git a/src/pandapipes/properties/ethane/density.txt b/src/pandapipes/properties/ethane/density.txt index 2a2e3f738..e5685ab63 100644 --- a/src/pandapipes/properties/ethane/density.txt +++ b/src/pandapipes/properties/ethane/density.txt @@ -1,8 +1,60 @@ -263 1.390053 -273 1.3375445 -283 1.288947 -293 1.2437865 -303 1.202 -313 1.162619 -323 1.1259435 -333 1.0915365 +# NIST Chemistry WebBook, SRD 69 +# https://webbook.nist.gov/cgi/fluid.cgi?P=1.01325&TLow=263.15&THigh=373.15&TInc=2&Digits=6&ID=C74840&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF +# Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) +# temperature in Kelvin, density in kg/m³ at 1.01325 bar +263.15 1.40821 +265.15 1.39722 +267.15 1.38642 +269.15 1.37578 +271.15 1.36532 +273.15 1.35501 +275.15 1.34486 +277.15 1.33487 +279.15 1.32503 +281.15 1.31534 +283.15 1.30579 +285.15 1.29638 +287.15 1.28711 +289.15 1.27797 +291.15 1.26897 +293.15 1.2601 +295.15 1.25135 +297.15 1.24272 +299.15 1.23422 +301.15 1.22583 +303.15 1.21756 +305.15 1.2094 +307.15 1.20136 +309.15 1.19342 +311.15 1.18558 +313.15 1.17786 +315.15 1.17023 +317.15 1.1627 +319.15 1.15527 +321.15 1.14794 +323.15 1.1407 +325.15 1.13355 +327.15 1.1265 +329.15 1.11953 +331.15 1.11265 +333.15 1.10586 +335.15 1.09914 +337.15 1.09252 +339.15 1.08597 +341.15 1.0795 +343.15 1.07311 +345.15 1.06679 +347.15 1.06055 +349.15 1.05438 +351.15 1.04829 +353.15 1.04227 +355.15 1.03631 +357.15 1.03043 +359.15 1.02461 +361.15 1.01886 +363.15 1.01317 +365.15 1.00755 +367.15 1.00199 +369.15 0.996487 +371.15 0.99105 +373.15 0.985671 diff --git a/src/pandapipes/properties/ethane/viscosity.txt b/src/pandapipes/properties/ethane/viscosity.txt index 3ebb22176..dd3b48a12 100644 --- a/src/pandapipes/properties/ethane/viscosity.txt +++ b/src/pandapipes/properties/ethane/viscosity.txt @@ -1,8 +1,60 @@ -263 8.37765e-6 -273 8.6845e-6 -283 8.9845e-6 -293 9.28135e-6 -303 9.500e-6 -313 9.88765e-6 -323 10.1945e-6 -333 10.4945e-6 +# NIST Chemistry WebBook, SRD 69 +# https://webbook.nist.gov/cgi/fluid.cgi?P=1.01325&TLow=263.15&THigh=373.15&TInc=2&Digits=6&ID=C74840&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF +# Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) +# temperature in Kelvin, dynamic viscosity in kg/(m s) +263.15 8.19E-06 +265.15 8.25E-06 +267.15 8.31E-06 +269.15 8.37E-06 +271.15 8.43E-06 +273.15 8.49E-06 +275.15 8.55E-06 +277.15 8.61E-06 +279.15 8.67E-06 +281.15 8.73E-06 +283.15 8.79E-06 +285.15 8.85E-06 +287.15 8.91E-06 +289.15 8.97E-06 +291.15 9.03E-06 +293.15 9.09E-06 +295.15 9.15E-06 +297.15 9.20E-06 +299.15 9.26E-06 +301.15 9.32E-06 +303.15 9.38E-06 +305.15 9.44E-06 +307.15 9.50E-06 +309.15 9.56E-06 +311.15 9.62E-06 +313.15 9.68E-06 +315.15 9.73E-06 +317.15 9.79E-06 +319.15 9.85E-06 +321.15 9.91E-06 +323.15 9.97E-06 +325.15 1.00E-05 +327.15 1.01E-05 +329.15 1.01E-05 +331.15 1.02E-05 +333.15 1.03E-05 +335.15 1.03E-05 +337.15 1.04E-05 +339.15 1.04E-05 +341.15 1.05E-05 +343.15 1.05E-05 +345.15 1.06E-05 +347.15 1.07E-05 +349.15 1.07E-05 +351.15 1.08E-05 +353.15 1.08E-05 +355.15 1.09E-05 +357.15 1.09E-05 +359.15 1.10E-05 +361.15 1.11E-05 +363.15 1.11E-05 +365.15 1.12E-05 +367.15 1.12E-05 +369.15 1.13E-05 +371.15 1.13E-05 +373.15 1.14E-05 diff --git a/src/pandapipes/properties/hydrogen/density.txt b/src/pandapipes/properties/hydrogen/density.txt index 9e7b631c3..d77e7ba10 100644 --- a/src/pandapipes/properties/hydrogen/density.txt +++ b/src/pandapipes/properties/hydrogen/density.txt @@ -1,60 +1,60 @@ # NIST Chemistry WebBook, SRD 69 -# https://webbook.nist.gov/cgi/fluid.cgi?Action=Load&ID=C1333740&Type=IsoBar&Digits=5&P=1&THigh=373.15&TLow=263.15&TInc=2&RefState=DEF&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fmol&WUnit=m%2Fs&VisUnit=uPa*s&STUnit=N%2Fm +# https://webbook.nist.gov/cgi/fluid.cgi?Action=Load&ID=C1333740&Type=IsoBar&Digits=6&P=1.01325&THigh=373.15&TLow=263.15&TInc=2&RefState=DEF&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fmol&WUnit=m%2Fs&VisUnit=uPa*s&STUnit=N%2Fm # Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) -# temperature in Kelvin, nominal density in kg/Nm^3 at 1 bar -263.15 0.092080 -265.15 0.091386 -267.15 0.090702 -269.15 0.090028 -271.15 0.089364 -273.15 0.088710 -275.15 0.088066 -277.15 0.087430 -279.15 0.086804 -281.15 0.086187 -283.15 0.085578 -285.15 0.084978 -287.15 0.084387 -289.15 0.083803 -291.15 0.083228 -293.15 0.082660 -295.15 0.082100 -297.15 0.081548 -299.15 0.081003 -301.15 0.080465 -303.15 0.079934 -305.15 0.079411 -307.15 0.078894 -309.15 0.078383 -311.15 0.077880 -313.15 0.077383 -315.15 0.076892 -317.15 0.076407 -319.15 0.075928 -321.15 0.075456 -323.15 0.074989 -325.15 0.074528 -327.15 0.074072 -329.15 0.073622 -331.15 0.073178 -333.15 0.072739 -335.15 0.072305 -337.15 0.071876 -339.15 0.071452 -341.15 0.071034 -343.15 0.070620 -345.15 0.070211 -347.15 0.069806 -349.15 0.069407 -351.15 0.069012 -353.15 0.068621 -355.15 0.068235 -357.15 0.067853 -359.15 0.067475 -361.15 0.067101 -363.15 0.066732 -365.15 0.066367 -367.15 0.066005 -369.15 0.065648 -371.15 0.065294 -373.15 0.064944 +# temperature in Kelvin, nominal density in kg/Nm^3 at 1.01325 bar +263.15 0.0932971 +265.15 0.0925936 +267.15 0.0919006 +269.15 0.0912179 +271.15 0.0905453 +273.15 0.0898825 +275.15 0.0892294 +277.15 0.0885857 +279.15 0.0879512 +281.15 0.0873258 +283.15 0.0867091 +285.15 0.0861012 +287.15 0.0855017 +289.15 0.0849105 +291.15 0.0843274 +293.15 0.0837523 +295.15 0.083185 +297.15 0.0826253 +299.15 0.0820731 +301.15 0.0815282 +303.15 0.0809905 +305.15 0.0804599 +307.15 0.0799362 +309.15 0.0794192 +311.15 0.0789089 +313.15 0.0784051 +315.15 0.0779077 +317.15 0.0774166 +319.15 0.0769316 +321.15 0.0764527 +323.15 0.0759797 +325.15 0.0755125 +327.15 0.0750511 +329.15 0.0745952 +331.15 0.0741449 +333.15 0.0736999 +335.15 0.0732603 +337.15 0.0728259 +339.15 0.0723966 +341.15 0.0719723 +343.15 0.071553 +345.15 0.0711385 +347.15 0.0707288 +349.15 0.0703238 +351.15 0.0699235 +353.15 0.0695276 +355.15 0.0691362 +357.15 0.0687492 +359.15 0.0683665 +361.15 0.0679881 +363.15 0.0676138 +365.15 0.0672436 +367.15 0.0668774 +369.15 0.0665152 +371.15 0.0661569 +373.15 0.0658025 diff --git a/src/pandapipes/properties/hydrogen/viscosity.txt b/src/pandapipes/properties/hydrogen/viscosity.txt index d19ba3246..42230d6d9 100644 --- a/src/pandapipes/properties/hydrogen/viscosity.txt +++ b/src/pandapipes/properties/hydrogen/viscosity.txt @@ -1,60 +1,60 @@ # NIST Chemistry WebBook, SRD 69 -# https://webbook.nist.gov/cgi/fluid.cgi?P=1&TLow=263.15&THigh=373.15&TInc=2&Applet=on&Digits=5&ID=C1333740&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fmol&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF +# https://webbook.nist.gov/cgi/fluid.cgi?P=1.01325&TLow=263.15&THigh=373.15&TInc=2&Digits=6&ID=C1333740&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=uPa*s&STUnit=N%2Fm&RefState=DEF # Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) # temperature in Kelvin, dynamic viscosity in kg/(m s) -263.15 8.18510E-06 -265.15 8.22770E-06 -267.15 8.27010E-06 -269.15 8.31250E-06 -271.15 8.35470E-06 -273.15 8.39690E-06 -275.15 8.43890E-06 -277.15 8.48090E-06 -279.15 8.52270E-06 -281.15 8.56450E-06 -283.15 8.60610E-06 -285.15 8.64760E-06 -287.15 8.68910E-06 -289.15 8.73040E-06 -291.15 8.77170E-06 -293.15 8.81280E-06 -295.15 8.85390E-06 -297.15 8.89490E-06 -299.15 8.93570E-06 -301.15 8.97650E-06 -303.15 9.01720E-06 -305.15 9.05780E-06 -307.15 9.09830E-06 -309.15 9.13880E-06 -311.15 9.17910E-06 -313.15 9.21940E-06 -315.15 9.25950E-06 -317.15 9.29960E-06 -319.15 9.33960E-06 -321.15 9.37950E-06 -323.15 9.41930E-06 -325.15 9.45900E-06 -327.15 9.49870E-06 -329.15 9.53830E-06 -331.15 9.57780E-06 -333.15 9.61720E-06 -335.15 9.65650E-06 -337.15 9.69580E-06 -339.15 9.73490E-06 -341.15 9.77400E-06 -343.15 9.81300E-06 -345.15 9.85200E-06 -347.15 9.89080E-06 -349.15 9.92960E-06 -351.15 9.96830E-06 -353.15 1.00070E-05 -355.15 1.00460E-05 -357.15 1.00840E-05 -359.15 1.01220E-05 -361.15 1.01610E-05 -363.15 1.01990E-05 -365.15 1.02370E-05 -367.15 1.02750E-05 -369.15 1.03130E-05 -371.15 1.03510E-05 -373.15 1.03890E-05 +263.15 8.16352E-06 +265.15 8.20642E-06 +267.15 8.24922E-06 +269.15 8.29192E-06 +271.15 8.33451E-06 +273.15 8.37701E-06 +275.15 8.41941E-06 +277.15 8.46171E-06 +279.15 8.50392E-06 +281.15 8.54603E-06 +283.15 8.58805E-06 +285.15 8.62997E-06 +287.15 8.67181E-06 +289.15 8.71355E-06 +291.15 8.75520E-06 +293.15 8.79677E-06 +295.15 8.83825E-06 +297.15 8.87964E-06 +299.15 8.92094E-06 +301.15 8.96216E-06 +303.15 9.00329E-06 +305.15 9.04434E-06 +307.15 9.08531E-06 +309.15 9.12620E-06 +311.15 9.16701E-06 +313.15 9.20773E-06 +315.15 9.24838E-06 +317.15 9.28895E-06 +319.15 9.32944E-06 +321.15 9.36985E-06 +323.15 9.41019E-06 +325.15 9.45045E-06 +327.15 9.49063E-06 +329.15 9.53074E-06 +331.15 9.57078E-06 +333.15 9.61075E-06 +335.15 9.65064E-06 +337.15 9.69046E-06 +339.15 9.73021E-06 +341.15 9.76989E-06 +343.15 9.80950E-06 +345.15 9.84904E-06 +347.15 9.88851E-06 +349.15 9.92792E-06 +351.15 9.96725E-06 +353.15 1.00065E-05 +355.15 1.00457E-05 +357.15 1.00849E-05 +359.15 1.01239E-05 +361.15 1.01629E-05 +363.15 1.02019E-05 +365.15 1.02408E-05 +367.15 1.02796E-05 +369.15 1.03183E-05 +371.15 1.03570E-05 +373.15 1.03957E-05 diff --git a/src/pandapipes/properties/methane/density.txt b/src/pandapipes/properties/methane/density.txt index 47b40753a..59c8d984c 100644 --- a/src/pandapipes/properties/methane/density.txt +++ b/src/pandapipes/properties/methane/density.txt @@ -1,9 +1,61 @@ -# temperature in Kelvin, nominal density in kg/Nm^3 at 1 bar -263 0.735423 -273 0.7082593 -283 0.6830463 -293 0.65957345 -303 0.6376665 -313 0.6171823 -323 0.59797715 -333 0.57993365 +# NIST Chemistry WebBook, SRD 69 +# https://webbook.nist.gov/cgi/fluid.cgi?P=1.01325&TLow=263.15&THigh=373.15&TInc=2&Digits=6&ID=C74828&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF +# Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) +# temperature in Kelvin, density in kg/m³ at 1.01325 bar +263.15 0.744962 +265.15 0.739293 +267.15 0.73371 +269.15 0.728211 +271.15 0.722795 +273.15 0.717459 +275.15 0.712202 +277.15 0.707022 +279.15 0.701917 +281.15 0.696886 +283.15 0.691927 +285.15 0.687038 +287.15 0.682219 +289.15 0.677467 +291.15 0.672781 +293.15 0.66816 +295.15 0.663602 +297.15 0.659107 +299.15 0.654672 +301.15 0.650297 +303.15 0.64598 +305.15 0.641721 +307.15 0.637517 +309.15 0.633369 +311.15 0.629274 +313.15 0.625233 +315.15 0.621243 +317.15 0.617304 +319.15 0.613415 +321.15 0.609575 +323.15 0.605783 +325.15 0.602038 +327.15 0.598339 +329.15 0.594685 +331.15 0.591076 +333.15 0.587511 +335.15 0.583989 +337.15 0.580509 +339.15 0.57707 +341.15 0.573672 +343.15 0.570314 +345.15 0.566995 +347.15 0.563715 +349.15 0.560472 +351.15 0.557267 +353.15 0.554099 +355.15 0.550966 +357.15 0.547869 +359.15 0.544806 +361.15 0.541778 +363.15 0.538783 +365.15 0.535821 +367.15 0.532892 +369.15 0.529994 +371.15 0.527129 +373.15 0.524294 + diff --git a/src/pandapipes/properties/methane/viscosity.txt b/src/pandapipes/properties/methane/viscosity.txt index 09082cb80..a0401baac 100644 --- a/src/pandapipes/properties/methane/viscosity.txt +++ b/src/pandapipes/properties/methane/viscosity.txt @@ -1,9 +1,61 @@ -# temperature in Kelvin, dynamic viscosity in kg/(m s) -263 10.0397e-6 -273 10.3945e-6 -283 10.6945e-6 -293 10.9945e-6 -303 11.326e-6 -313 11.6945e-6 -323 11.9945e-6 -333 12.2945e-6 +# NIST Chemistry WebBook, SRD 69 +# https://webbook.nist.gov/cgi/fluid.cgi?P=1.01325&TLow=263.15&THigh=373.15&TInc=2&Digits=6&ID=C74828&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF +# Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) +# temperature in Kelvin, dynamic viscosity in Pa*s (or kg/(m s)) at 1.01325 bar +263.15 9.92E-06 +265.15 9.99E-06 +267.15 1.01E-05 +269.15 1.01E-05 +271.15 1.02E-05 +273.15 1.03E-05 +275.15 1.03E-05 +277.15 1.04E-05 +279.15 1.05E-05 +281.15 1.05E-05 +283.15 1.06E-05 +285.15 1.07E-05 +287.15 1.07E-05 +289.15 1.08E-05 +291.15 1.08E-05 +293.15 1.09E-05 +295.15 1.10E-05 +297.15 1.10E-05 +299.15 1.11E-05 +301.15 1.12E-05 +303.15 1.12E-05 +305.15 1.13E-05 +307.15 1.14E-05 +309.15 1.14E-05 +311.15 1.15E-05 +313.15 1.16E-05 +315.15 1.16E-05 +317.15 1.17E-05 +319.15 1.17E-05 +321.15 1.18E-05 +323.15 1.19E-05 +325.15 1.19E-05 +327.15 1.20E-05 +329.15 1.21E-05 +331.15 1.21E-05 +333.15 1.22E-05 +335.15 1.22E-05 +337.15 1.23E-05 +339.15 1.24E-05 +341.15 1.24E-05 +343.15 1.25E-05 +345.15 1.26E-05 +347.15 1.26E-05 +349.15 1.27E-05 +351.15 1.27E-05 +353.15 1.28E-05 +355.15 1.29E-05 +357.15 1.29E-05 +359.15 1.30E-05 +361.15 1.30E-05 +363.15 1.31E-05 +365.15 1.32E-05 +367.15 1.32E-05 +369.15 1.33E-05 +371.15 1.33E-05 +373.15 1.34E-05 + diff --git a/src/pandapipes/properties/nitrogen/density.txt b/src/pandapipes/properties/nitrogen/density.txt index 8e62c1ff4..820af74c1 100644 --- a/src/pandapipes/properties/nitrogen/density.txt +++ b/src/pandapipes/properties/nitrogen/density.txt @@ -1,60 +1,61 @@ # NIST Chemistry WebBook, SRD 69 -# https://webbook.nist.gov/cgi/fluid.cgi?P=1&TLow=263.15&THigh=373.15&TInc=2&Applet=on&Digits=5&ID=C7727379&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF +# https://webbook.nist.gov/cgi/fluid.cgi?P=1.01325&TLow=263.15&THigh=373.15&TInc=2&Applet=on&Digits=6&ID=C7727379&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF # Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) -# temperature in Kelvin, density in kg/m³ at 1 bar -263.15 1.28110 -265.15 1.27140 -267.15 1.26180 -269.15 1.25240 -271.15 1.24320 -273.15 1.23400 -275.15 1.22500 -277.15 1.21620 -279.15 1.20740 -281.15 1.19880 -283.15 1.19030 -285.15 1.18190 -287.15 1.17370 -289.15 1.16550 -291.15 1.15750 -293.15 1.14960 -295.15 1.14180 -297.15 1.13410 -299.15 1.12650 -301.15 1.11900 -303.15 1.11160 -305.15 1.10430 -307.15 1.09710 -309.15 1.09000 -311.15 1.08290 -313.15 1.07600 -315.15 1.06920 -317.15 1.06240 -319.15 1.05570 -321.15 1.04910 -323.15 1.04260 -325.15 1.03620 -327.15 1.02990 -329.15 1.02360 -331.15 1.01740 -333.15 1.01130 -335.15 1.00520 -337.15 0.99927 -339.15 0.99336 -341.15 0.98753 -343.15 0.98177 -345.15 0.97607 -347.15 0.97044 -349.15 0.96487 -351.15 0.95936 -353.15 0.95392 -355.15 0.94854 -357.15 0.94323 -359.15 0.93797 -361.15 0.93276 -363.15 0.92762 -365.15 0.92253 -367.15 0.91750 -369.15 0.91252 -371.15 0.90760 -373.15 0.90273 +# temperature in Kelvin, density in kg/m³ at 1.01325 bar +263.15 1.29807 +265.15 1.28825 +267.15 1.27857 +269.15 1.26903 +271.15 1.25964 +273.15 1.25039 +275.15 1.24127 +277.15 1.23228 +279.15 1.22342 +281.15 1.21469 +283.15 1.20609 +285.15 1.1976 +287.15 1.18924 +289.15 1.18099 +291.15 1.17285 +293.15 1.16483 +295.15 1.15692 +297.15 1.14911 +299.15 1.14141 +301.15 1.13381 +303.15 1.12631 +305.15 1.11891 +307.15 1.11161 +309.15 1.1044 +311.15 1.09728 +313.15 1.09026 +315.15 1.08333 +317.15 1.07648 +319.15 1.06972 +321.15 1.06305 +323.15 1.05645 +325.15 1.04994 +327.15 1.04351 +329.15 1.03716 +331.15 1.03088 +333.15 1.02468 +335.15 1.01856 +337.15 1.01251 +339.15 1.00652 +341.15 1.00061 +343.15 0.994773 +345.15 0.988999 +347.15 0.983293 +349.15 0.977651 +351.15 0.972075 +353.15 0.966562 +355.15 0.961111 +357.15 0.955721 +359.15 0.950392 +361.15 0.945121 +363.15 0.939909 +365.15 0.934755 +367.15 0.929656 +369.15 0.924613 +371.15 0.919625 +373.15 0.91469 + diff --git a/src/pandapipes/properties/nitrogen/viscosity.txt b/src/pandapipes/properties/nitrogen/viscosity.txt index f31feeebe..bde9dac2c 100644 --- a/src/pandapipes/properties/nitrogen/viscosity.txt +++ b/src/pandapipes/properties/nitrogen/viscosity.txt @@ -1,60 +1,60 @@ # NIST Chemistry WebBook, SRD 69 -# https://webbook.nist.gov/cgi/fluid.cgi?P=1&TLow=263.15&THigh=373.15&TInc=2&Applet=on&Digits=5&ID=C7727379&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF +# https://webbook.nist.gov/cgi/fluid.cgi?P=1.01325&TLow=263.15&THigh=373.15&TInc=2&Applet=on&Digits=6&ID=C7727379&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF # Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) -# temperature in Kelvin, dynamic viscosity in Pa*s (or kg/(m s)) at 1 bar -263.15 16.154E-6 -265.15 16.251E-6 -267.15 16.348E-6 -269.15 16.445E-6 -271.15 16.541E-6 -273.15 16.637E-6 -275.15 16.732E-6 -277.15 16.828E-6 -279.15 16.923E-6 -281.15 17.017E-6 -283.15 17.112E-6 -285.15 17.206E-6 -287.15 17.300E-6 -289.15 17.394E-6 -291.15 17.487E-6 -293.15 17.580E-6 -295.15 17.673E-6 -297.15 17.766E-6 -299.15 17.858E-6 -301.15 17.950E-6 -303.15 18.042E-6 -305.15 18.133E-6 -307.15 18.225E-6 -309.15 18.316E-6 -311.15 18.407E-6 -313.15 18.497E-6 -315.15 18.588E-6 -317.15 18.678E-6 -319.15 18.767E-6 -321.15 18.857E-6 -323.15 18.946E-6 -325.15 19.036E-6 -327.15 19.124E-6 -329.15 19.213E-6 -331.15 19.302E-6 -333.15 19.390E-6 -335.15 19.478E-6 -337.15 19.565E-6 -339.15 19.653E-6 -341.15 19.740E-6 -343.15 19.827E-6 -345.15 19.914E-6 -347.15 20.001E-6 -349.15 20.087E-6 -351.15 20.174E-6 -353.15 20.260E-6 -355.15 20.345E-6 -357.15 20.431E-6 -359.15 20.516E-6 -361.15 20.601E-6 -363.15 20.686E-6 -365.15 20.771E-6 -367.15 20.856E-6 -369.15 20.940E-6 -371.15 21.024E-6 -373.15 21.108E-6 +# temperature in Kelvin, dynamic viscosity in Pa*s (or kg/(m s)) at 1.01325 bar +263.15 1.61E-05 +265.15 1.62E-05 +267.15 1.63E-05 +269.15 1.64E-05 +271.15 1.65E-05 +273.15 1.66E-05 +275.15 1.67E-05 +277.15 1.68E-05 +279.15 1.69E-05 +281.15 1.70E-05 +283.15 1.71E-05 +285.15 1.72E-05 +287.15 1.73E-05 +289.15 1.74E-05 +291.15 1.75E-05 +293.15 1.76E-05 +295.15 1.77E-05 +297.15 1.78E-05 +299.15 1.79E-05 +301.15 1.79E-05 +303.15 1.80E-05 +305.15 1.81E-05 +307.15 1.82E-05 +309.15 1.83E-05 +311.15 1.84E-05 +313.15 1.85E-05 +315.15 1.86E-05 +317.15 1.87E-05 +319.15 1.88E-05 +321.15 1.89E-05 +323.15 1.89E-05 +325.15 1.90E-05 +327.15 1.91E-05 +329.15 1.92E-05 +331.15 1.93E-05 +333.15 1.94E-05 +335.15 1.95E-05 +337.15 1.96E-05 +339.15 1.96E-05 +341.15 1.97E-05 +343.15 1.98E-05 +345.15 1.99E-05 +347.15 2.00E-05 +349.15 2.01E-05 +351.15 2.02E-05 +353.15 2.03E-05 +355.15 2.03E-05 +357.15 2.04E-05 +359.15 2.05E-05 +361.15 2.06E-05 +363.15 2.07E-05 +365.15 2.08E-05 +367.15 2.08E-05 +369.15 2.09E-05 +371.15 2.10E-05 +373.15 2.11E-05 diff --git a/src/pandapipes/properties/oxygen/density.txt b/src/pandapipes/properties/oxygen/density.txt index 99b8f946e..69501d479 100644 --- a/src/pandapipes/properties/oxygen/density.txt +++ b/src/pandapipes/properties/oxygen/density.txt @@ -1,60 +1,61 @@ # NIST Chemistry WebBook, SRD 69 # https://webbook.nist.gov/cgi/fluid.cgi?P=1&TLow=263.15&THigh=373.15&TInc=2&Applet=on&Digits=5&ID=C7782447&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF' # Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) -# temperature in Kelvin, density in kg/m³ at 1 bar -263.1500 1.4642 -265.1500 1.4531 -267.1500 1.4421 -269.1500 1.4314 -271.1500 1.4208 -273.1500 1.4103 -275.1500 1.4000 -277.1500 1.3899 -279.1500 1.3799 -281.1500 1.3700 -283.1500 1.3603 -285.1500 1.3508 -287.1500 1.3413 -289.1500 1.3320 -291.1500 1.3228 -293.1500 1.3138 -295.1500 1.3048 -297.1500 1.2960 -299.1500 1.2873 -301.1500 1.2788 -303.1500 1.2703 -305.1500 1.2619 -307.1500 1.2537 -309.1500 1.2456 -311.1500 1.2375 -313.1500 1.2296 -315.1500 1.2218 -317.1500 1.2141 -319.1500 1.2064 -321.1500 1.1989 -323.1500 1.1915 -325.1500 1.1841 -327.1500 1.1769 -329.1500 1.1697 -331.1500 1.1626 -333.1500 1.1556 -335.1500 1.1487 -337.1500 1.1419 -339.1500 1.1351 -341.1500 1.1285 -343.1500 1.1219 -345.1500 1.1153 -347.1500 1.1089 -349.1500 1.1025 -351.1500 1.0963 -353.1500 1.0900 -355.1500 1.0839 -357.1500 1.0778 -359.1500 1.0718 -361.1500 1.0658 -363.1500 1.0600 -365.1500 1.0541 -367.1500 1.0484 -369.1500 1.0427 -371.1500 1.0371 -373.1500 1.0315 +# temperature in Kelvin, density in kg/m³ at 1.01325 bar +263.15 1.48358 +265.15 1.47234 +267.15 1.46127 +269.15 1.45036 +271.15 1.43962 +273.15 1.42903 +275.15 1.4186 +277.15 1.40832 +279.15 1.3982 +281.15 1.38821 +283.15 1.37837 +285.15 1.36866 +287.15 1.3591 +289.15 1.34966 +291.15 1.34036 +293.15 1.33118 +295.15 1.32213 +297.15 1.31321 +299.15 1.3044 +301.15 1.29571 +303.15 1.28713 +305.15 1.27867 +307.15 1.27032 +309.15 1.26208 +311.15 1.25394 +313.15 1.24591 +315.15 1.23798 +317.15 1.23015 +319.15 1.22242 +321.15 1.21479 +323.15 1.20725 +325.15 1.19981 +327.15 1.19246 +329.15 1.18519 +331.15 1.17802 +333.15 1.17093 +335.15 1.16393 +337.15 1.15701 +339.15 1.15017 +341.15 1.14341 +343.15 1.13673 +345.15 1.13013 +347.15 1.12361 +349.15 1.11716 +351.15 1.11078 +353.15 1.10448 +355.15 1.09825 +357.15 1.09209 +359.15 1.08599 +361.15 1.07997 +363.15 1.07401 +365.15 1.06812 +367.15 1.06229 +369.15 1.05652 +371.15 1.05082 +373.15 1.04518 + diff --git a/src/pandapipes/properties/oxygen/viscosity.txt b/src/pandapipes/properties/oxygen/viscosity.txt index f550f45e1..f94d3a156 100644 --- a/src/pandapipes/properties/oxygen/viscosity.txt +++ b/src/pandapipes/properties/oxygen/viscosity.txt @@ -2,59 +2,59 @@ # https://webbook.nist.gov/cgi/fluid.cgi?P=1&TLow=263.15&THigh=373.15&TInc=2&Applet=on&Digits=5&ID=C7782447&Action=Load&Type=IsoBar&TUnit=K&PUnit=bar&DUnit=kg%2Fm3&HUnit=kJ%2Fkg&WUnit=m%2Fs&VisUnit=Pa*s&STUnit=N%2Fm&RefState=DEF' # Eric W. Lemmon, Mark O. McLinden and Daniel G. Friend, "Thermophysical Properties of Fluid Systems" in NIST Chemistry WebBook, NIST Standard Reference Database Number 69, Eds. P.J. Linstrom and W.G. Mallard, National Institute of Standards and Technology, Gaithersburg MD, 20899, https://doi.org/10.18434/T4D303, (retrieved June 10, 2020) # temperature in Kelvin, dynamic viscosity in Pa*s (or kg/(m s)) at 1 bar -263.15 18.480E-6 -265.15 18.596E-6 -267.15 18.711E-6 -269.15 18.826E-6 -271.15 18.941E-6 -273.15 19.055E-6 -275.15 19.169E-6 -277.15 19.283E-6 -279.15 19.396E-6 -281.15 19.509E-6 -283.15 19.622E-6 -285.15 19.735E-6 -287.15 19.847E-6 -289.15 19.959E-6 -291.15 20.071E-6 -293.15 20.182E-6 -295.15 20.293E-6 -297.15 20.404E-6 -299.15 20.514E-6 -301.15 20.624E-6 -303.15 20.734E-6 -305.15 20.844E-6 -307.15 20.953E-6 -309.15 21.062E-6 -311.15 21.171E-6 -313.15 21.279E-6 -315.15 21.388E-6 -317.15 21.496E-6 -319.15 21.603E-6 -321.15 21.711E-6 -323.15 21.818E-6 -325.15 21.925E-6 -327.15 22.031E-6 -329.15 22.138E-6 -331.15 22.244E-6 -333.15 22.350E-6 -335.15 22.455E-6 -337.15 22.561E-6 -339.15 22.666E-6 -341.15 22.770E-6 -343.15 22.875E-6 -345.15 22.979E-6 -347.15 23.083E-6 -349.15 23.187E-6 -351.15 23.291E-6 -353.15 23.394E-6 -355.15 23.497E-6 -357.15 23.600E-6 -359.15 23.703E-6 -361.15 23.805E-6 -363.15 23.907E-6 -365.15 24.009E-6 -367.15 24.111E-6 -369.15 24.212E-6 -371.15 24.314E-6 -373.15 24.415E-6 +263.15 1.85666E-05 +265.15 1.86826E-05 +267.15 1.87983E-05 +269.15 1.89136E-05 +271.15 1.90286E-05 +273.15 1.91433E-05 +275.15 1.92577E-05 +277.15 1.93717E-05 +279.15 1.94854E-05 +281.15 1.95988E-05 +283.15 1.97119E-05 +285.15 1.98247E-05 +287.15 1.99371E-05 +289.15 2.00493E-05 +291.15 2.01611E-05 +293.15 2.02727E-05 +295.15 2.03839E-05 +297.15 2.04948E-05 +299.15 2.06055E-05 +301.15 2.07158E-05 +303.15 2.08259E-05 +305.15 2.09356E-05 +307.15 2.10451E-05 +309.15 2.11543E-05 +311.15 2.12632E-05 +313.15 2.13718E-05 +315.15 2.14801E-05 +317.15 2.15882E-05 +319.15 2.16960E-05 +321.15 2.18035E-05 +323.15 2.19107E-05 +325.15 2.20176E-05 +327.15 2.21243E-05 +329.15 2.22307E-05 +331.15 2.23368E-05 +333.15 2.24427E-05 +335.15 2.25483E-05 +337.15 2.26537E-05 +339.15 2.27588E-05 +341.15 2.28636E-05 +343.15 2.29682E-05 +345.15 2.30725E-05 +347.15 2.31765E-05 +349.15 2.32803E-05 +351.15 2.33839E-05 +353.15 2.34872E-05 +355.15 2.35903E-05 +357.15 2.36931E-05 +359.15 2.37956E-05 +361.15 2.38980E-05 +363.15 2.40001E-05 +365.15 2.41019E-05 +367.15 2.42035E-05 +369.15 2.43049E-05 +371.15 2.44060E-05 +373.15 2.45069E-05 From 9e500350ce5ad652b858e5c1d8a0c26e951edc4a Mon Sep 17 00:00:00 2001 From: Jolando Kisse Date: Tue, 3 Dec 2024 11:36:34 +0100 Subject: [PATCH 2/2] update CHANGELOG.rst --- CHANGELOG.rst | 6 ++++-- 1 file changed, 4 insertions(+), 2 deletions(-) diff --git a/CHANGELOG.rst b/CHANGELOG.rst index 49fc6afcc..98c0e82dc 100644 --- a/CHANGELOG.rst +++ b/CHANGELOG.rst @@ -1,6 +1,10 @@ Change Log ============= +[upcoming release] - 202x-xx-xx +------------------------------- +- [FIXED] density and viscosity properties for gases are now taken at 1.01325 bar instead of 1 bar + [0.11.0] - 2024-11-07 ------------------------------- - [ADDED] heat_consumer plotting @@ -28,8 +32,6 @@ Change Log - [FIXED] alpha also applied to mdot - [REMOVED] support for Python 3.8 due to EOL - - [0.10.0] - 2024-04-09 -------------------------------