


{"id":217940,"date":"2022-07-07T06:18:01","date_gmt":"2022-07-07T06:18:01","guid":{"rendered":"\/forum\/forums\/topic\/liquid-rgp-file-in-fluent\/"},"modified":"2022-07-07T06:18:01","modified_gmt":"2022-07-07T06:18:01","slug":"liquid-rgp-file-in-fluent","status":"closed","type":"topic","link":"https:\/\/innovationspace.ansys.com\/forum\/forums\/topic\/liquid-rgp-file-in-fluent\/","title":{"rendered":"Liquid RGP file in FLUENT"},"content":{"rendered":"<p class=\"0\"><span lang=\"EN-US\">Hi<\/span><!--[endif]--><\/p>\n<p class=\"0\">&nbsp;<\/p>\n<p class=\"0\"><span lang=\"EN-US\">I am currently using FLUENT to analyze simple flow for various temperatures and pressure conditions.<\/span><\/p>\n<p class=\"0\"><span lang=\"EN-US\">The fluid flowing inside the tube is aviation fuel that does not exist in the NIST database and is calculated at various temperatures and pressures, so the required physical properties were entered through the RGP file. (The temperature and pressure ranges are set to include liquid, gas, and supercritical conditions)<\/span><!--[endif]--><\/p>\n<p class=\"0\"><span lang=\"EN-US\">The RGP file was made by referring to the format 12.7.1 Organization of an .rgp File in ANSYS CFX-Solver Modeling Guide (2021R2) and the Sample .rgp File in 12.7.1.2 and the required physical properties such as enthalpy, sound speed, and more, were calculated using fitting formulas from various sources.<\/span><!--[endif]--><\/p>\n<p class=\"0\"><span lang=\"EN-US\">When calculated using this, the physical properties of the gaseous state were calculated as values of the gaseous state, but in the liquid state, they were calculated as values between the values of the saturated liquid and the saturated gas at that pressure.<\/span><!--[endif]--><\/p>\n<p class=\"0\"><span lang=\"EN-US\">In order to observe the results of using other substances, the genRGP.py file was executed through CMD to generate the RGP file of water and to analyze it at the temperature and pressure of the liquid state. (The accuracy is set to 1e-3, the temperature and pressure ranges are set to include liquid, gas, and supercritical conditions) <\/span><span lang=\"EN-US\">In this case, it was calculated as the properties for the liquid state I set.<\/span><!--[endif]--><\/p>\n<p class=\"0\"><span lang=\"EN-US\">As such, I would like to know whether the original liquid state is not recognized well when the user creates the RGP file through manuals such as ANSYS CFX-Solver Modeling Guide.<\/span><!--[endif]--><\/p>\n<p class=\"0\"><span lang=\"EN-US\">And if someone knew how to solve these problems, I would appreciate it if you could let me know.<\/span><\/p>\n<p class=\"0\">&nbsp;<\/p>\n<p class=\"0\"><span lang=\"EN-US\">Thanks<\/span><\/p>\n<div id=\"hwpEditorBoardContent\" class=\"hwp_editor_board_content\" data-hjsonver=\"1.0\" data-jsonlen=\"10335\"><!--[data-hwpjson]{\n\"documentPr\": {\n\"di\": \"\",\n\"dp\": {\n\"dn\": \"test.hwp\",\n\"ta\": 1,\n\"d1\": 5,\n\"d2\": 1,\n\"dv\": 0,\n\"dr\": 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{\n\"np\": \"01D891C89A00CCA000000004\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA000000004\": {\n\"np\": \"01D891C89A00CCA000000005\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"I am currently using FLUENT to analyze simple flow for various temperatures and pressure conditions.\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA000000005\": {\n\"np\": \"01D891C89A00CCA000000006\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"The fluid flowing inside the tube is aviation fuel that does not exist in the NIST database and is interpreted at various temperatures and pressures, so the required physical properties were entered through the RGP file. (The temperature and pressure ranges are set to include liquid, gas, and supercritical conditions)\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA000000006\": {\n\"np\": \"01D891C89A00CCA000000007\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA000000007\": {\n\"np\": \"01D891C89A00CCA000000008\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"The RGP file was prepared by referring to the format 12.7.1 Organization of an .rgp File in ANSYS CFX-Solver Modeling Guide (2021R2) and the Sample .rgp File in 12.7.1.2 and the required physical properties such as enthalpy, sound speed, and more, were calculated using fitting formulas from various sources.\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA000000008\": {\n\"np\": \"01D891C89A00CCA000000009\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA000000009\": {\n\"np\": \"01D891C89A00CCA00000000A\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"When calculated using this, the physical properties of the gaseous state were calculated as values of the gaseous state, but in the liquid state, they were calculated as values between the values of the saturated liquid and the saturated gas at that pressure.\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA00000000A\": {\n\"np\": \"01D891C89A00CCA00000000B\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA00000000B\": {\n\"np\": \"01D891C89A00CCA00000000C\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"In order to observe the results of using other substances, the genRGP.py file was executed through CMD to generate the RGP file of water and to analyze it at the temperature and pressure of the liquid state. (The accuracy is set to 1e-3, the temperature and pressure ranges are set to include liquid, gas, and supercritical conditions)\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA00000000C\": {\n\"np\": \"01D891C89A00CCA00000000D\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"In this case, it was calculated as the properties for the liquid state I set.\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA00000000D\": {\n\"np\": \"01D891C89A00CCA00000000E\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA00000000E\": {\n\"np\": \"01D891C89A00CCA00000000F\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"As such, I would like to know whether the original liquid state is not recognized well when the user creates the RGP file through manuals such as ANSYS CFX-Solver Modeling Guide.\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA00000000F\": {\n\"np\": \"01D891C89A00CCA000000010\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"\"\n}\n]\n}\n]\n},\n\"01D891C89A00CCA000000010\": {\n\"np\": \"\",\n\"id\": -2147483648,\n\"pp\": \"01D891C89A00CCA000000015\",\n\"si\": \"01D891C89A00CCA000000016\",\n\"bf\": 0,\n\"ru\": [\n{\n\"cp\": \"01D891C89A00CCA000000013\",\n\"ch\": [\n{\n\"t\": \"And if someone knew how to solve these problems, I would appreciate it if you could let me know.\"\n}\n]\n}\n]\n}\n},\n\"sl\": { },\n\"cs\": {\n\"01D891C89A00CCA000000000\": {\n\"cc\": 2,\n\"ci\": 1936024420,\n\"td\": 0,\n\"tv\": 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}\n}--><\/div>\n","protected":false},"template":"","class_list":["post-217940","topic","type-topic","status-closed","hentry","topic-tag-ansys-fluent","topic-tag-rgp"],"aioseo_notices":[],"acf":[],"custom_fields":[{"0":{"_bbp_subscription":["240305","22555"],"_bbp_author_ip":["23.218.93.111"]," _bbp_last_reply_id":["0"]," _bbp_likes_count":["0"],"_btv_view_count":["1284"],"_bbp_topic_status":["unanswered"],"_bbp_status":["publish"],"_bbp_topic_id":["217940"],"_bbp_forum_id":["27792"],"_bbp_engagement":["22555","240305"],"_bbp_voice_count":["2"],"_bbp_reply_count":["3"],"_bbp_last_reply_id":["218382"],"_bbp_last_active_id":["218382"],"_bbp_last_active_time":["2022-07-14 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