DanWBR at 14:57, 8 January 2020

2020-01-08T14:57:34Z

DanWBR: Created page with " Introduction

Below is a table with all object property codes. Most of them are read-only. For example: with the Ma..."

2020-01-08T14:57:04Z

Created page with " Introduction </h2> Below is a table with all object property codes. Most of them are read-only. For example: with the Ma..."

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Introduction </h2>
Below is a table with all object property codes. Most of them are read-only. For example: with the Material Stream, you can write values only to properties from index 0 to 4, just like through the Property Grid in the Flowsheet GUI.

<h2>[<a href="/web/20161108225747/http://dwsim.inforside.com.br/wiki/index.php?title=Object_Property_Codes&action=edit&section=2" title="Edit section: Property Codes">edit</a>] Property Codes </h2>
<table>
<tr>
<td style="text-align: center; background:#f0f0f0;">DWSIM - Object Property Codes
</td>
<td style="text-align: center; background:#f0f0f0;">'
</td>
<td style="text-align: center; background:#f0f0f0;">'
</td>
<td style="text-align: center; background:#f0f0f0;">'
</td>
<td style="text-align: center; background:#f0f0f0;">'
</td></tr>
<tr>
<td>
</td></tr>
<tr>
<td> Object Type</td>
<td></td>
<td>Index</td>
<td>Property Code</td>
<td>Property Name (en-US)
</td></tr>
<tr>
<td> Material Stream</td>
<td>MS</td>
<td>0</td>
<td>PROP_MS_0</td>
<td>Temperature
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>1</td>
<td>PROP_MS_1</td>
<td>Pressure
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>2</td>
<td>PROP_MS_2</td>
<td>Mass Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>3</td>
<td>PROP_MS_3</td>
<td>Molar Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>4</td>
<td>PROP_MS_4</td>
<td>Volumetric Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>5</td>
<td>PROP_MS_5</td>
<td>Mixture Density
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>6</td>
<td>PROP_MS_6</td>
<td>Mixture Molar Weight
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>7</td>
<td>PROP_MS_7</td>
<td>Mixture Specific Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>8</td>
<td>PROP_MS_8</td>
<td>Mixture Specific Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>9</td>
<td>PROP_MS_9</td>
<td>Mixture Molar Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>10</td>
<td>PROP_MS_10</td>
<td>Mixture Molar Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>11</td>
<td>PROP_MS_11</td>
<td>Mixture Thermal Conductivity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>12</td>
<td>PROP_MS_12</td>
<td>Vapor Phase Density
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>13</td>
<td>PROP_MS_13</td>
<td>Vapor Phase Molar Weight
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>14</td>
<td>PROP_MS_14</td>
<td>Vapor Phase Specific Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>15</td>
<td>PROP_MS_15</td>
<td>Vapor Phase Specific Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>16</td>
<td>PROP_MS_16</td>
<td>Vapor Phase Molar Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>17</td>
<td>PROP_MS_17</td>
<td>Vapor Phase Molar Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>18</td>
<td>PROP_MS_18</td>
<td>Vapor Phase Thermal Conductivity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>19</td>
<td>PROP_MS_19</td>
<td>Vapor Phase Kinematic Viscosity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>20</td>
<td>PROP_MS_20</td>
<td>Vapor Phase Dynamic Viscosity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>21</td>
<td>PROP_MS_21</td>
<td>Vapor Phase Heat Capacity (Cp)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>22</td>
<td>PROP_MS_22</td>
<td>Vapor Phase Heat Capacity Ratio (Cp/Cv)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>23</td>
<td>PROP_MS_23</td>
<td>Vapor Phase Mass Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>24</td>
<td>PROP_MS_24</td>
<td>Vapor Phase Molar Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>25</td>
<td>PROP_MS_25</td>
<td>Vapor Phase Volumetric Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>26</td>
<td>PROP_MS_26</td>
<td>Vapor Phase Compressibility Factor
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>27</td>
<td>PROP_MS_27</td>
<td>Vapor Phase Molar Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>28</td>
<td>PROP_MS_28</td>
<td>Vapor Phase Mass Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>29</td>
<td>PROP_MS_29</td>
<td>Vapor Phase Volumetric Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>30</td>
<td>PROP_MS_30</td>
<td>Liquid Phase (Mixture) Density
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>31</td>
<td>PROP_MS_31</td>
<td>Liquid Phase (Mixture) Molar Weight
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>32</td>
<td>PROP_MS_32</td>
<td>Liquid Phase (Mixture) Specific Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>33</td>
<td>PROP_MS_33</td>
<td>Liquid Phase (Mixture) Specific Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>34</td>
<td>PROP_MS_34</td>
<td>Liquid Phase (Mixture) Molar Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>35</td>
<td>PROP_MS_35</td>
<td>Liquid Phase (Mixture) Molar Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>36</td>
<td>PROP_MS_36</td>
<td>Liquid Phase (Mixture) Thermal Conductivity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>37</td>
<td>PROP_MS_37</td>
<td>Liquid Phase (Mixture) Kinematic Viscosity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>38</td>
<td>PROP_MS_38</td>
<td>Liquid Phase (Mixture) Dynamic Viscosity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>39</td>
<td>PROP_MS_39</td>
<td>Liquid Phase (Mixture) Heat Capacity (Cp)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>40</td>
<td>PROP_MS_40</td>
<td>Liquid Phase (Mixture) Heat Capacity Ratio (Cp/Cv)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>41</td>
<td>PROP_MS_41</td>
<td>Liquid Phase (Mixture) Mass Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>42</td>
<td>PROP_MS_42</td>
<td>Liquid Phase (Mixture) Molar Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>43</td>
<td>PROP_MS_43</td>
<td>Liquid Phase (Mixture) Volumetric Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>44</td>
<td>PROP_MS_44</td>
<td>Liquid Phase (Mixture) Compressibility Factor
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>45</td>
<td>PROP_MS_45</td>
<td>Liquid Phase (Mixture) Molar Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>46</td>
<td>PROP_MS_46</td>
<td>Liquid Phase (Mixture) Mass Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>47</td>
<td>PROP_MS_47</td>
<td>Liquid Phase (Mixture) Volumetric Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>48</td>
<td>PROP_MS_48</td>
<td>Liquid Phase (1) Density
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>49</td>
<td>PROP_MS_49</td>
<td>Liquid Phase (1) Molar Weight
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>50</td>
<td>PROP_MS_50</td>
<td>Liquid Phase (1) Specific Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>51</td>
<td>PROP_MS_51</td>
<td>Liquid Phase (1) Specific Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>52</td>
<td>PROP_MS_52</td>
<td>Liquid Phase (1) Molar Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>53</td>
<td>PROP_MS_53</td>
<td>Liquid Phase (1) Molar Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>54</td>
<td>PROP_MS_54</td>
<td>Liquid Phase (1) Thermal Conductivity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>55</td>
<td>PROP_MS_55</td>
<td>Liquid Phase (1) Kinematic Viscosity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>56</td>
<td>PROP_MS_56</td>
<td>Liquid Phase (1) Dynamic Viscosity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>57</td>
<td>PROP_MS_57</td>
<td>Liquid Phase (1) Heat Capacity (Cp)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>58</td>
<td>PROP_MS_58</td>
<td>Liquid Phase (1) Heat Capacity Ratio (Cp/Cv)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>59</td>
<td>PROP_MS_59</td>
<td>Liquid Phase (1) Mass Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>60</td>
<td>PROP_MS_60</td>
<td>Liquid Phase (1) Molar Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>61</td>
<td>PROP_MS_61</td>
<td>Liquid Phase (1) Volumetric Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>62</td>
<td>PROP_MS_62</td>
<td>Liquid Phase (1) Compressibility Factor
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>63</td>
<td>PROP_MS_63</td>
<td>Liquid Phase (1) Molar Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>64</td>
<td>PROP_MS_64</td>
<td>Liquid Phase (1) Mass Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>65</td>
<td>PROP_MS_65</td>
<td>Liquid Phase (1) Volumetric Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>66</td>
<td>PROP_MS_66</td>
<td>Liquid Phase (2) Density
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>67</td>
<td>PROP_MS_67</td>
<td>Liquid Phase (2) Molar Weight
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>68</td>
<td>PROP_MS_68</td>
<td>Liquid Phase (2) Specific Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>69</td>
<td>PROP_MS_69</td>
<td>Liquid Phase (2) Specific Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>70</td>
<td>PROP_MS_70</td>
<td>Liquid Phase (2) Molar Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>71</td>
<td>PROP_MS_71</td>
<td>Liquid Phase (2) Molar Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>72</td>
<td>PROP_MS_72</td>
<td>Liquid Phase (2) Thermal Conductivity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>73</td>
<td>PROP_MS_73</td>
<td>Liquid Phase (2) Kinematic Viscosity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>74</td>
<td>PROP_MS_74</td>
<td>Liquid Phase (2) Dynamic Viscosity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>75</td>
<td>PROP_MS_75</td>
<td>Liquid Phase (2) Heat Capacity (Cp)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>76</td>
<td>PROP_MS_76</td>
<td>Liquid Phase (2) Heat Capacity Ratio (Cp/Cv)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>77</td>
<td>PROP_MS_77</td>
<td>Liquid Phase (2) Mass Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>78</td>
<td>PROP_MS_78</td>
<td>Liquid Phase (2) Molar Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>79</td>
<td>PROP_MS_79</td>
<td>Liquid Phase (2) Volumetric Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>80</td>
<td>PROP_MS_80</td>
<td>Liquid Phase (2) Compressibility Factor
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>81</td>
<td>PROP_MS_81</td>
<td>Liquid Phase (2) Molar Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>82</td>
<td>PROP_MS_82</td>
<td>Liquid Phase (2) Mass Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>83</td>
<td>PROP_MS_83</td>
<td>Liquid Phase (2) Volumetric Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>84</td>
<td>PROP_MS_84</td>
<td>Aqueous Phase Density
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>85</td>
<td>PROP_MS_85</td>
<td>Aqueous Phase Molar Weight
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>86</td>
<td>PROP_MS_86</td>
<td>Aqueous Phase Specific Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>87</td>
<td>PROP_MS_87</td>
<td>Aqueous Phase Specific Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>88</td>
<td>PROP_MS_88</td>
<td>Aqueous Phase Molar Enthalpy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>89</td>
<td>PROP_MS_89</td>
<td>Aqueous Phase Molar Entropy
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>90</td>
<td>PROP_MS_90</td>
<td>Aqueous Phase Thermal Conductivity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>91</td>
<td>PROP_MS_91</td>
<td>Aqueous Phase Kinematic Viscosity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>92</td>
<td>PROP_MS_92</td>
<td>Aqueous Phase Dynamic Viscosity
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>93</td>
<td>PROP_MS_93</td>
<td>Aqueous Phase Heat Capacity (Cp)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>94</td>
<td>PROP_MS_94</td>
<td>Aqueous Phase Heat Capacity Ratio (Cp/Cv)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>95</td>
<td>PROP_MS_95</td>
<td>Aqueous Phase Mass Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>96</td>
<td>PROP_MS_96</td>
<td>Aqueous Phase Molar Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>97</td>
<td>PROP_MS_97</td>
<td>Aqueous Phase Volumetric Flow
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>98</td>
<td>PROP_MS_98</td>
<td>Aqueous Phase Compressibility Factor
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>99</td>
<td>PROP_MS_99</td>
<td>Aqueous Phase Molar Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>100</td>
<td>PROP_MS_100</td>
<td>Aqueous Phase Mass Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>101</td>
<td>PROP_MS_101</td>
<td>Aqueous Phase Volumetric Fraction
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>102</td>
<td>PROP_MS_102</td>
<td>Molar Fraction (Mixture)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>103</td>
<td>PROP_MS_103</td>
<td>Mass Fraction (Mixture)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>104</td>
<td>PROP_MS_104</td>
<td>Molar Flow (Mixture)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>105</td>
<td>PROP_MS_105</td>
<td>Mass Flow (Mixture)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>106</td>
<td>PROP_MS_106</td>
<td>Molar Fraction (Vapor Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>107</td>
<td>PROP_MS_107</td>
<td>Molar Fraction (Overall Liquid Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>108</td>
<td>PROP_MS_108</td>
<td>Molar Fraction (Liquid Phase 1)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>109</td>
<td>PROP_MS_109</td>
<td>Molar Fraction (Liquid Phase 2)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>110</td>
<td>PROP_MS_110</td>
<td>Molar Fraction (Aqueous Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>111</td>
<td>PROP_MS_111</td>
<td>Mass Fraction (Vapor Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>112</td>
<td>PROP_MS_112</td>
<td>Mass Fraction (Overall Liquid Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>113</td>
<td>PROP_MS_113</td>
<td>Mass Fraction (Liquid Phase 1)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>114</td>
<td>PROP_MS_114</td>
<td>Mass Fraction (Liquid Phase 2)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>115</td>
<td>PROP_MS_115</td>
<td>Mass Fraction (Aqueous Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>116</td>
<td>PROP_MS_116</td>
<td>Molar Flow (Vapor Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>117</td>
<td>PROP_MS_117</td>
<td>Molar Flow (Overall Liquid Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>118</td>
<td>PROP_MS_118</td>
<td>Molar Flow (Liquid Phase 1)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>119</td>
<td>PROP_MS_119</td>
<td>Molar Flow (Liquid Phase 2)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>120</td>
<td>PROP_MS_120</td>
<td>Molar Flow (Aqueous Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>121</td>
<td>PROP_MS_121</td>
<td>Mass Flow (Vapor Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>122</td>
<td>PROP_MS_122</td>
<td>Mass Flow (Overall Liquid Phase)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>123</td>
<td>PROP_MS_123</td>
<td>Mass Flow (Liquid Phase 1)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>124</td>
<td>PROP_MS_124</td>
<td>Mass Flow (Liquid Phase 2)
</td></tr>
<tr>
<td> </td>
<td>MS</td>
<td>125</td>
<td>PROP_MS_125</td>
<td>Mass Flow (Aqueous Phase)
</td></tr>
<tr>
<td> Energy Stream</td>
<td>ES</td>
<td>0</td>
<td>PROP_ES_0</td>
<td>Power
</td></tr>
<tr>
<td> Valve</td>
<td>VA</td>
<td>0</td>
<td>PROP_VA_0</td>
<td>Calculation Mode
</td></tr>
<tr>
<td> </td>
<td>VA</td>
<td>1</td>
<td>PROP_VA_1</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> </td>
<td>VA</td>
<td>2</td>
<td>PROP_VA_2</td>
<td>Outlet Pressure
</td></tr>
<tr>
<td> </td>
<td>VA</td>
<td>3</td>
<td>PROP_VA_3</td>
<td>Temperature Drop
</td></tr>
<tr>
<td> Pipe Segment</td>
<td>PS</td>
<td>0</td>
<td>PROP_PS_0</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> </td>
<td>PS</td>
<td>1</td>
<td>PROP_PS_1</td>
<td>Temperature Drop
</td></tr>
<tr>
<td> </td>
<td>PS</td>
<td>2</td>
<td>PROP_PS_2</td>
<td>Heat Exchanged
</td></tr>
<tr>
<td> Pump</td>
<td>PU</td>
<td>0</td>
<td>PROP_PU_0</td>
<td>Pressure Increase (Head)
</td></tr>
<tr>
<td> </td>
<td>PU</td>
<td>1</td>
<td>PROP_PU_1</td>
<td>Efficiency
</td></tr>
<tr>
<td> </td>
<td>PU</td>
<td>2</td>
<td>PROP_PU_2</td>
<td>Delta-T
</td></tr>
<tr>
<td> </td>
<td>PU</td>
<td>3</td>
<td>PROP_PU_3</td>
<td>Power Required
</td></tr>
<tr>
<td> Tank</td>
<td>TK</td>
<td>0</td>
<td>PROP_TK_0</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> Separator Vessel</td>
<td>SV</td>
<td>0</td>
<td>PROP_SV_0</td>
<td>Separation Temperature
</td></tr>
<tr>
<td> </td>
<td>SV</td>
<td>1</td>
<td>PROP_SV_1</td>
<td>Separation Pressure
</td></tr>
<tr>
<td> Compressor</td>
<td>CO</td>
<td>0</td>
<td>PROP_CO_0</td>
<td>Pressure Increase (Head)
</td></tr>
<tr>
<td> </td>
<td>CO</td>
<td>1</td>
<td>PROP_CO_1</td>
<td>Efficiency
</td></tr>
<tr>
<td> </td>
<td>CO</td>
<td>2</td>
<td>PROP_CO_2</td>
<td>Delta-T
</td></tr>
<tr>
<td> </td>
<td>CO</td>
<td>3</td>
<td>PROP_CO_3</td>
<td>Power Required
</td></tr>
<tr>
<td> Expander (Turbine)</td>
<td>TU</td>
<td>0</td>
<td>PROP_TU_0</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> </td>
<td>TU</td>
<td>1</td>
<td>PROP_TU_1</td>
<td>Efficiency
</td></tr>
<tr>
<td> </td>
<td>TU</td>
<td>2</td>
<td>PROP_TU_2</td>
<td>Delta-T
</td></tr>
<tr>
<td> </td>
<td>TU</td>
<td>3</td>
<td>PROP_TU_3</td>
<td>Power Generated
</td></tr>
<tr>
<td> Heater</td>
<td>HT</td>
<td>0</td>
<td>PROP_HT_0</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> </td>
<td>HT</td>
<td>1</td>
<td>PROP_HT_1</td>
<td>Efficiency
</td></tr>
<tr>
<td> </td>
<td>HT</td>
<td>2</td>
<td>PROP_HT_2</td>
<td>Outlet Temperature
</td></tr>
<tr>
<td> </td>
<td>HT</td>
<td>3</td>
<td>PROP_HT_3</td>
<td>Heat Added
</td></tr>
<tr>
<td> </td>
<td>HT</td>
<td>4</td>
<td>PROP_HT_4</td>
<td>Delta-T
</td></tr>
<tr>
<td> Cooler</td>
<td>CL</td>
<td>0</td>
<td>PROP_CL_0</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> </td>
<td>CL</td>
<td>1</td>
<td>PROP_CL_1</td>
<td>Efficiency
</td></tr>
<tr>
<td> </td>
<td>CL</td>
<td>2</td>
<td>PROP_CL_2</td>
<td>Outlet Temperature
</td></tr>
<tr>
<td> </td>
<td>CL</td>
<td>3</td>
<td>PROP_CL_3</td>
<td>Heat Removed
</td></tr>
<tr>
<td> </td>
<td>CL</td>
<td>4</td>
<td>PROP_CL_4</td>
<td>Delta-T
</td></tr>
<tr>
<td> Recycle</td>
<td>RY</td>
<td>0</td>
<td>PROP_RY_0</td>
<td>Maximum Iterations
</td></tr>
<tr>
<td> </td>
<td>RY</td>
<td>1</td>
<td>PROP_RY_1</td>
<td>Mass Flow Tolerance
</td></tr>
<tr>
<td> </td>
<td>RY</td>
<td>2</td>
<td>PROP_RY_2</td>
<td>Temperature Tolerance
</td></tr>
<tr>
<td> </td>
<td>RY</td>
<td>3</td>
<td>PROP_RY_3</td>
<td>Pressure Tolerance
</td></tr>
<tr>
<td> </td>
<td>RY</td>
<td>4</td>
<td>PROP_RY_4</td>
<td>Mass Flow Error
</td></tr>
<tr>
<td> </td>
<td>RY</td>
<td>5</td>
<td>PROP_RY_5</td>
<td>Temperature Error
</td></tr>
<tr>
<td> </td>
<td>RY</td>
<td>6</td>
<td>PROP_RY_6</td>
<td>Pressure Error
</td></tr>
<tr>
<td> Energy Recycle</td>
<td>ER</td>
<td>0</td>
<td>PROP_ER_0</td>
<td>Maximum Iterations
</td></tr>
<tr>
<td> </td>
<td>ER</td>
<td>1</td>
<td>PROP_ER_1</td>
<td>Power Tolerance
</td></tr>
<tr>
<td> </td>
<td>ER</td>
<td>2</td>
<td>PROP_ER_2</td>
<td>Power Error
</td></tr>
<tr>
<td> Conversion Reactor</td>
<td>CR</td>
<td>0</td>
<td>PROP_CR_0</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> Equilibrium Reactor</td>
<td>EQ</td>
<td>0</td>
<td>PROP_EQ_0</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> Gibbs Reactor</td>
<td>GR</td>
<td>0</td>
<td>PROP_GR_0</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> CSTR</td>
<td>CS</td>
<td>0</td>
<td>PROP_CS_0</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> PFR</td>
<td>PR</td>
<td>0</td>
<td>PROP_PR_0</td>
<td>Pressure Drop
</td></tr>
<tr>
<td> Heat Exchanger</td>
<td>HX</td>
<td>0</td>
<td>PROP_HX_0</td>
<td>Global Heat Transfer Coefficient (U)
</td></tr>
<tr>
<td> </td>
<td>HX</td>
<td>1</td>
<td>PROP_HX_1</td>
<td>Heat Exchange Area (A)
</td></tr>
<tr>
<td> </td>
<td>HX</td>
<td>2</td>
<td>PROP_HX_2</td>
<td>Heat Load
</td></tr>
<tr>
<td> Shortcut Column</td>
<td>SC</td>
<td>0</td>
<td>PROP_SC_0</td>
<td>Reflux Ratio
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>1</td>
<td>PROP_SC_1</td>
<td>Heavy Key Molar Fraction
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>2</td>
<td>PROP_SC_2</td>
<td>Light Key Molar Fraction
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>3</td>
<td>PROP_SC_3</td>
<td>Condenser Pressure
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>4</td>
<td>PROP_SC_4</td>
<td>Reboiler Pressure
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>5</td>
<td>PROP_SC_5</td>
<td>Minimun Reflux Ratio
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>6</td>
<td>PROP_SC_6</td>
<td>Minimum Stages
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>7</td>
<td>PROP_SC_7</td>
<td>Optimal Feed Stage
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>8</td>
<td>PROP_SC_8</td>
<td>Stripping Liquid Molar Flow
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>9</td>
<td>PROP_SC_9</td>
<td>Rectify Liquid Molar Flow
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>10</td>
<td>PROP_SC_10</td>
<td>Stripping Vapor Molar Flow
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>11</td>
<td>PROP_SC_11</td>
<td>Rectify Vapor Molar Flow
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>12</td>
<td>PROP_SC_12</td>
<td>Condenser Duty
</td></tr>
<tr>
<td> </td>
<td>SC</td>
<td>13</td>
<td>PROP_SC_13</td>
<td>Reboiler Duty
</td></tr>
<tr>
<td> Distillation Column</td>
<td>DC</td>
<td>0</td>
<td>PROP_DC_0</td>
<td>Condenser Pressure
</td></tr>
<tr>
<td> </td>
<td>DC</td>
<td>1</td>
<td>PROP_DC_1</td>
<td>Reboiler Pressure
</td></tr>
<tr>
<td> </td>
<td>DC</td>
<td>2</td>
<td>PROP_DC_2</td>
<td>Condenser Pressure Drop
</td></tr>
<tr>
<td> </td>
<td>DC</td>
<td>3</td>
<td>PROP_DC_3</td>
<td>Reflux Ratio
</td></tr>
<tr>
<td> </td>
<td>DC</td>
<td>4</td>
<td>PROP_DC_4</td>
<td>Distillate Molar Flow
</td></tr>
<tr>
<td> </td>
<td>DC</td>
<td>5</td>
<td>PROP_DC_5</td>
<td>Condenser Duty
</td></tr>
<tr>
<td> </td>
<td>DC</td>
<td>6</td>
<td>PROP_DC_6</td>
<td>Reboiler Duty
</td></tr>
<tr>
<td> </td>
<td>DC</td>
<td>7</td>
<td>PROP_DC_7</td>
<td>Number of Stages
</td></tr>
<tr>
<td> Absorption Column</td>
<td>AC</td>
<td>0</td>
<td>PROP_AC_0</td>
<td>Top Stage Pressure
</td></tr>
<tr>
<td> </td>
<td>AC</td>
<td>1</td>
<td>PROP_AC_1</td>
<td>Bottom Stage Pressure
</td></tr>
<tr>
<td> </td>
<td>AC</td>
<td>2</td>
<td>PROP_AC_2</td>
<td>Number of Stages
</td></tr>
<tr>
<td> Reboiled Absorber</td>
<td>RA</td>
<td>0</td>
<td>PROP_RA_0</td>
<td>Top Stage Pressure
</td></tr>
<tr>
<td> </td>
<td>RA</td>
<td>1</td>
<td>PROP_RA_1</td>
<td>Reboiler Pressure
</td></tr>
<tr>
<td> </td>
<td>RA</td>
<td>2</td>
<td>PROP_RA_2</td>
<td>Boil-Up Ratio
</td></tr>
<tr>
<td> </td>
<td>RA</td>
<td>3</td>
<td>PROP_RA_3</td>
<td>Reboiler Duty
</td></tr>
<tr>
<td> </td>
<td>RA</td>
<td>4</td>
<td>PROP_RA_4</td>
<td>Number of Stages
</td></tr>
<tr>
<td> Refluxed Absorber</td>
<td>RF</td>
<td>0</td>
<td>PROP_RF_0</td>
<td>Condenser Pressure
</td></tr>
<tr>
<td> </td>
<td>RF</td>
<td>1</td>
<td>PROP_RF_1</td>
<td>Bottom Stage Pressure
</td></tr>
<tr>
<td> </td>
<td>RF</td>
<td>2</td>
<td>PROP_RF_2</td>
<td>Condenser Pressure Drop
</td></tr>
<tr>
<td> </td>
<td>RF</td>
<td>3</td>
<td>PROP_RF_3</td>
<td>Reflux Ratio
</td></tr>
<tr>
<td> </td>
<td>RF</td>
<td>4</td>
<td>PROP_RF_4</td>
<td>Distillate Molar Flow
</td></tr>
<tr>
<td> </td>
<td>RF</td>
<td>5</td>
<td>PROP_RF_5</td>
<td>Condenser Duty
</td></tr>
<tr>
<td> </td>
<td>RF</td>
<td>6</td>
<td>PROP_RF_6</td>
<td>Number of Stages
</td></tr>
<tr>
<td> Orifice Plate</td>
<td>OP</td>
<td>0</td>
<td>PROP_OP_0</td>
<td>Pressure Tappings
</td></tr>
<tr>
<td> </td>
<td>OP</td>
<td>1</td>
<td>PROP_OP_1</td>
<td>Orifice Diameter
</td></tr>
<tr>
<td> </td>
<td>OP</td>
<td>2</td>
<td>PROP_OP_2</td>
<td>Beta (d/D)
</td></tr>
<tr>
<td> </td>
<td>OP</td>
<td>3</td>
<td>PROP_OP_3</td>
<td>Correction Factor
</td></tr>
<tr>
<td> </td>
<td>OP</td>
<td>4</td>
<td>PROP_OP_4</td>
<td>Overall Pressure Drop
</td></tr>
<tr>
<td> </td>
<td>OP</td>
<td>5</td>
<td>PROP_OP_5</td>
<td>Orifice Pressure Drop
</td></tr>
<tr>
<td> </td>
<td>OP</td>
<td>6</td>
<td>PROP_OP_6</td>
<td>Delta T
</td></tr>
<tr>
<td>
</td></tr></table>

@@ Line 1: / Line 1: @@
-<span class="mw-headline" id="Introduction"> Introduction </span></h2>
+== Introduction ==
 <p>Below is a table with all object property codes. Most of them are read-only. For example: with the Material Stream, you can write values only to properties from index 0 to 4, just like through the Property Grid in the Flowsheet GUI.
 </p>

@@ Line 2: / Line 2: @@
 <p>Below is a table with all object property codes. Most of them are read-only. For example: with the Material Stream, you can write values only to properties from index 0 to 4, just like through the Property Grid in the Flowsheet GUI.
 </p>
-<h2><span class="editsection">[<a href="/web/20161108225747/http://dwsim.inforside.com.br/wiki/index.php?title=Object_Property_Codes&amp;action=edit&amp;section=2" title="Edit section: Property Codes">edit</a>]</span> <span class="mw-headline" id="Property_Codes"> Property Codes </span></h2>
+<h2><span class="mw-headline" id="Property_Codes"> Property Codes </span></h2>
 <table>
 <tr>

Object Property Codes - Revision history

DanWBR at 14:58, 8 January 2020

DanWBR at 14:57, 8 January 2020

DanWBR: Created page with " Introduction