Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process
In this work, Heat transfer performance of shell and tube heat exchanger numerical investigated and validated experimentally in continuous polymer foaming process. The three-dimensional conjugate heat transfer method has been used for numerical investigation. Temperature distribution of the polymer...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Mughal, Waqas [verfasserIn] Xin, Chunling [verfasserIn] Zhang, Yun [verfasserIn] samo, Imran [verfasserIn] Abro, Masroor [verfasserIn] He, Yadong [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2019 |
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| Schlagwörter: |
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| Übergeordnetes Werk: |
Enthalten in: Chemical engineering research and design - Amsterdam : Elsevier, 1983, 151, Seite 231-241 |
|---|---|
| Übergeordnetes Werk: |
volume:151 ; pages:231-241 |
| DOI / URN: |
10.1016/j.cherd.2019.08.001 |
|---|
| Katalog-ID: |
ELV002994488 |
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| 245 | 1 | 0 | |a Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process |
| 264 | 1 | |c 2019 | |
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| 520 | |a In this work, Heat transfer performance of shell and tube heat exchanger numerical investigated and validated experimentally in continuous polymer foaming process. The three-dimensional conjugate heat transfer method has been used for numerical investigation. Temperature distribution of the polymer melt is quite essential for polymer processing. However, in this study mainly focused on temperature distribution, heat transfer rate, heat transfer coefficient and overall heat transfer coefficient was investigated. These parameters are numerically investigated on 10–50Kg.h−1 of mass flow rate, whereas inlet temperature of the melt was 200°C and oil temperature was 160, 170 and 180°C. The results validated experimentally on 1030 and 50Kg.h−1 of mass flow rate respectively. It has been investigated that, between 10–20Kg.h−1 of mass flow rate gives approximately homogeneous temperature distribution. However, the outer streams near the wall is temperature drop deteriorated as increasing mass flow rate. The heterogeneous temperature of the melt effected on heat transfer coefficient numerically investigated at outlet. The overall heat transfer coefficient increases as increasing mass flow rate, nonetheless, 170°C of oil temperature gives higher results than others. | ||
| 650 | 4 | |a Polymer melt | |
| 650 | 4 | |a Melt cooling | |
| 650 | 4 | |a Melt heat exchanger | |
| 650 | 4 | |a Shell and tube heat exchanger | |
| 650 | 4 | |a Melt heat transfer | |
| 700 | 1 | |a Xin, Chunling |e verfasserin |4 aut | |
| 700 | 1 | |a Zhang, Yun |e verfasserin |4 aut | |
| 700 | 1 | |a samo, Imran |e verfasserin |4 aut | |
| 700 | 1 | |a Abro, Masroor |e verfasserin |4 aut | |
| 700 | 1 | |a He, Yadong |e verfasserin |4 aut | |
| 773 | 0 | 8 | |i Enthalten in |t Chemical engineering research and design |d Amsterdam : Elsevier, 1983 |g 151, Seite 231-241 |h Online-Ressource |w (DE-627)312841965 |w (DE-600)2008006-2 |w (DE-576)090893190 |x 1744-3563 |7 nnns |
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10.1016/j.cherd.2019.08.001 doi (DE-627)ELV002994488 (ELSEVIER)S0263-8762(19)30379-X DE-627 ger DE-627 rda eng 540 660 DE-600 58.10 bkl Mughal, Waqas verfasserin aut Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier In this work, Heat transfer performance of shell and tube heat exchanger numerical investigated and validated experimentally in continuous polymer foaming process. The three-dimensional conjugate heat transfer method has been used for numerical investigation. Temperature distribution of the polymer melt is quite essential for polymer processing. However, in this study mainly focused on temperature distribution, heat transfer rate, heat transfer coefficient and overall heat transfer coefficient was investigated. These parameters are numerically investigated on 10–50Kg.h−1 of mass flow rate, whereas inlet temperature of the melt was 200°C and oil temperature was 160, 170 and 180°C. The results validated experimentally on 1030 and 50Kg.h−1 of mass flow rate respectively. It has been investigated that, between 10–20Kg.h−1 of mass flow rate gives approximately homogeneous temperature distribution. However, the outer streams near the wall is temperature drop deteriorated as increasing mass flow rate. The heterogeneous temperature of the melt effected on heat transfer coefficient numerically investigated at outlet. The overall heat transfer coefficient increases as increasing mass flow rate, nonetheless, 170°C of oil temperature gives higher results than others. Polymer melt Melt cooling Melt heat exchanger Shell and tube heat exchanger Melt heat transfer Xin, Chunling verfasserin aut Zhang, Yun verfasserin aut samo, Imran verfasserin aut Abro, Masroor verfasserin aut He, Yadong verfasserin aut Enthalten in Chemical engineering research and design Amsterdam : Elsevier, 1983 151, Seite 231-241 Online-Ressource (DE-627)312841965 (DE-600)2008006-2 (DE-576)090893190 1744-3563 nnns volume:151 pages:231-241 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_206 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 58.10 Verfahrenstechnik: Allgemeines AR 151 231-241 |
| spelling |
10.1016/j.cherd.2019.08.001 doi (DE-627)ELV002994488 (ELSEVIER)S0263-8762(19)30379-X DE-627 ger DE-627 rda eng 540 660 DE-600 58.10 bkl Mughal, Waqas verfasserin aut Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier In this work, Heat transfer performance of shell and tube heat exchanger numerical investigated and validated experimentally in continuous polymer foaming process. The three-dimensional conjugate heat transfer method has been used for numerical investigation. Temperature distribution of the polymer melt is quite essential for polymer processing. However, in this study mainly focused on temperature distribution, heat transfer rate, heat transfer coefficient and overall heat transfer coefficient was investigated. These parameters are numerically investigated on 10–50Kg.h−1 of mass flow rate, whereas inlet temperature of the melt was 200°C and oil temperature was 160, 170 and 180°C. The results validated experimentally on 1030 and 50Kg.h−1 of mass flow rate respectively. It has been investigated that, between 10–20Kg.h−1 of mass flow rate gives approximately homogeneous temperature distribution. However, the outer streams near the wall is temperature drop deteriorated as increasing mass flow rate. The heterogeneous temperature of the melt effected on heat transfer coefficient numerically investigated at outlet. The overall heat transfer coefficient increases as increasing mass flow rate, nonetheless, 170°C of oil temperature gives higher results than others. Polymer melt Melt cooling Melt heat exchanger Shell and tube heat exchanger Melt heat transfer Xin, Chunling verfasserin aut Zhang, Yun verfasserin aut samo, Imran verfasserin aut Abro, Masroor verfasserin aut He, Yadong verfasserin aut Enthalten in Chemical engineering research and design Amsterdam : Elsevier, 1983 151, Seite 231-241 Online-Ressource (DE-627)312841965 (DE-600)2008006-2 (DE-576)090893190 1744-3563 nnns volume:151 pages:231-241 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_206 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 58.10 Verfahrenstechnik: Allgemeines AR 151 231-241 |
| allfields_unstemmed |
10.1016/j.cherd.2019.08.001 doi (DE-627)ELV002994488 (ELSEVIER)S0263-8762(19)30379-X DE-627 ger DE-627 rda eng 540 660 DE-600 58.10 bkl Mughal, Waqas verfasserin aut Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier In this work, Heat transfer performance of shell and tube heat exchanger numerical investigated and validated experimentally in continuous polymer foaming process. The three-dimensional conjugate heat transfer method has been used for numerical investigation. Temperature distribution of the polymer melt is quite essential for polymer processing. However, in this study mainly focused on temperature distribution, heat transfer rate, heat transfer coefficient and overall heat transfer coefficient was investigated. These parameters are numerically investigated on 10–50Kg.h−1 of mass flow rate, whereas inlet temperature of the melt was 200°C and oil temperature was 160, 170 and 180°C. The results validated experimentally on 1030 and 50Kg.h−1 of mass flow rate respectively. It has been investigated that, between 10–20Kg.h−1 of mass flow rate gives approximately homogeneous temperature distribution. However, the outer streams near the wall is temperature drop deteriorated as increasing mass flow rate. The heterogeneous temperature of the melt effected on heat transfer coefficient numerically investigated at outlet. The overall heat transfer coefficient increases as increasing mass flow rate, nonetheless, 170°C of oil temperature gives higher results than others. Polymer melt Melt cooling Melt heat exchanger Shell and tube heat exchanger Melt heat transfer Xin, Chunling verfasserin aut Zhang, Yun verfasserin aut samo, Imran verfasserin aut Abro, Masroor verfasserin aut He, Yadong verfasserin aut Enthalten in Chemical engineering research and design Amsterdam : Elsevier, 1983 151, Seite 231-241 Online-Ressource (DE-627)312841965 (DE-600)2008006-2 (DE-576)090893190 1744-3563 nnns volume:151 pages:231-241 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_206 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 58.10 Verfahrenstechnik: Allgemeines AR 151 231-241 |
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10.1016/j.cherd.2019.08.001 doi (DE-627)ELV002994488 (ELSEVIER)S0263-8762(19)30379-X DE-627 ger DE-627 rda eng 540 660 DE-600 58.10 bkl Mughal, Waqas verfasserin aut Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier In this work, Heat transfer performance of shell and tube heat exchanger numerical investigated and validated experimentally in continuous polymer foaming process. The three-dimensional conjugate heat transfer method has been used for numerical investigation. Temperature distribution of the polymer melt is quite essential for polymer processing. However, in this study mainly focused on temperature distribution, heat transfer rate, heat transfer coefficient and overall heat transfer coefficient was investigated. These parameters are numerically investigated on 10–50Kg.h−1 of mass flow rate, whereas inlet temperature of the melt was 200°C and oil temperature was 160, 170 and 180°C. The results validated experimentally on 1030 and 50Kg.h−1 of mass flow rate respectively. It has been investigated that, between 10–20Kg.h−1 of mass flow rate gives approximately homogeneous temperature distribution. However, the outer streams near the wall is temperature drop deteriorated as increasing mass flow rate. The heterogeneous temperature of the melt effected on heat transfer coefficient numerically investigated at outlet. The overall heat transfer coefficient increases as increasing mass flow rate, nonetheless, 170°C of oil temperature gives higher results than others. Polymer melt Melt cooling Melt heat exchanger Shell and tube heat exchanger Melt heat transfer Xin, Chunling verfasserin aut Zhang, Yun verfasserin aut samo, Imran verfasserin aut Abro, Masroor verfasserin aut He, Yadong verfasserin aut Enthalten in Chemical engineering research and design Amsterdam : Elsevier, 1983 151, Seite 231-241 Online-Ressource (DE-627)312841965 (DE-600)2008006-2 (DE-576)090893190 1744-3563 nnns volume:151 pages:231-241 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_206 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 58.10 Verfahrenstechnik: Allgemeines AR 151 231-241 |
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10.1016/j.cherd.2019.08.001 doi (DE-627)ELV002994488 (ELSEVIER)S0263-8762(19)30379-X DE-627 ger DE-627 rda eng 540 660 DE-600 58.10 bkl Mughal, Waqas verfasserin aut Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier In this work, Heat transfer performance of shell and tube heat exchanger numerical investigated and validated experimentally in continuous polymer foaming process. The three-dimensional conjugate heat transfer method has been used for numerical investigation. Temperature distribution of the polymer melt is quite essential for polymer processing. However, in this study mainly focused on temperature distribution, heat transfer rate, heat transfer coefficient and overall heat transfer coefficient was investigated. These parameters are numerically investigated on 10–50Kg.h−1 of mass flow rate, whereas inlet temperature of the melt was 200°C and oil temperature was 160, 170 and 180°C. The results validated experimentally on 1030 and 50Kg.h−1 of mass flow rate respectively. It has been investigated that, between 10–20Kg.h−1 of mass flow rate gives approximately homogeneous temperature distribution. However, the outer streams near the wall is temperature drop deteriorated as increasing mass flow rate. The heterogeneous temperature of the melt effected on heat transfer coefficient numerically investigated at outlet. The overall heat transfer coefficient increases as increasing mass flow rate, nonetheless, 170°C of oil temperature gives higher results than others. Polymer melt Melt cooling Melt heat exchanger Shell and tube heat exchanger Melt heat transfer Xin, Chunling verfasserin aut Zhang, Yun verfasserin aut samo, Imran verfasserin aut Abro, Masroor verfasserin aut He, Yadong verfasserin aut Enthalten in Chemical engineering research and design Amsterdam : Elsevier, 1983 151, Seite 231-241 Online-Ressource (DE-627)312841965 (DE-600)2008006-2 (DE-576)090893190 1744-3563 nnns volume:151 pages:231-241 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_206 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 58.10 Verfahrenstechnik: Allgemeines AR 151 231-241 |
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Mughal, Waqas @@aut@@ Xin, Chunling @@aut@@ Zhang, Yun @@aut@@ samo, Imran @@aut@@ Abro, Masroor @@aut@@ He, Yadong @@aut@@ |
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Mughal, Waqas |
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Mughal, Waqas ddc 540 bkl 58.10 misc Polymer melt misc Melt cooling misc Melt heat exchanger misc Shell and tube heat exchanger misc Melt heat transfer Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process |
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540 660 DE-600 58.10 bkl Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process Polymer melt Melt cooling Melt heat exchanger Shell and tube heat exchanger Melt heat transfer |
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ddc 540 bkl 58.10 misc Polymer melt misc Melt cooling misc Melt heat exchanger misc Shell and tube heat exchanger misc Melt heat transfer |
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ddc 540 bkl 58.10 misc Polymer melt misc Melt cooling misc Melt heat exchanger misc Shell and tube heat exchanger misc Melt heat transfer |
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ddc 540 bkl 58.10 misc Polymer melt misc Melt cooling misc Melt heat exchanger misc Shell and tube heat exchanger misc Melt heat transfer |
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Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process |
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Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process |
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Mughal, Waqas Xin, Chunling Zhang, Yun samo, Imran Abro, Masroor He, Yadong |
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10.1016/j.cherd.2019.08.001 |
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numerical investigation of polymer melt heat transfer using shell and tube heat exchanger in continuous polymer foaming process |
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Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process |
| abstract |
In this work, Heat transfer performance of shell and tube heat exchanger numerical investigated and validated experimentally in continuous polymer foaming process. The three-dimensional conjugate heat transfer method has been used for numerical investigation. Temperature distribution of the polymer melt is quite essential for polymer processing. However, in this study mainly focused on temperature distribution, heat transfer rate, heat transfer coefficient and overall heat transfer coefficient was investigated. These parameters are numerically investigated on 10–50Kg.h−1 of mass flow rate, whereas inlet temperature of the melt was 200°C and oil temperature was 160, 170 and 180°C. The results validated experimentally on 1030 and 50Kg.h−1 of mass flow rate respectively. It has been investigated that, between 10–20Kg.h−1 of mass flow rate gives approximately homogeneous temperature distribution. However, the outer streams near the wall is temperature drop deteriorated as increasing mass flow rate. The heterogeneous temperature of the melt effected on heat transfer coefficient numerically investigated at outlet. The overall heat transfer coefficient increases as increasing mass flow rate, nonetheless, 170°C of oil temperature gives higher results than others. |
| abstractGer |
In this work, Heat transfer performance of shell and tube heat exchanger numerical investigated and validated experimentally in continuous polymer foaming process. The three-dimensional conjugate heat transfer method has been used for numerical investigation. Temperature distribution of the polymer melt is quite essential for polymer processing. However, in this study mainly focused on temperature distribution, heat transfer rate, heat transfer coefficient and overall heat transfer coefficient was investigated. These parameters are numerically investigated on 10–50Kg.h−1 of mass flow rate, whereas inlet temperature of the melt was 200°C and oil temperature was 160, 170 and 180°C. The results validated experimentally on 1030 and 50Kg.h−1 of mass flow rate respectively. It has been investigated that, between 10–20Kg.h−1 of mass flow rate gives approximately homogeneous temperature distribution. However, the outer streams near the wall is temperature drop deteriorated as increasing mass flow rate. The heterogeneous temperature of the melt effected on heat transfer coefficient numerically investigated at outlet. The overall heat transfer coefficient increases as increasing mass flow rate, nonetheless, 170°C of oil temperature gives higher results than others. |
| abstract_unstemmed |
In this work, Heat transfer performance of shell and tube heat exchanger numerical investigated and validated experimentally in continuous polymer foaming process. The three-dimensional conjugate heat transfer method has been used for numerical investigation. Temperature distribution of the polymer melt is quite essential for polymer processing. However, in this study mainly focused on temperature distribution, heat transfer rate, heat transfer coefficient and overall heat transfer coefficient was investigated. These parameters are numerically investigated on 10–50Kg.h−1 of mass flow rate, whereas inlet temperature of the melt was 200°C and oil temperature was 160, 170 and 180°C. The results validated experimentally on 1030 and 50Kg.h−1 of mass flow rate respectively. It has been investigated that, between 10–20Kg.h−1 of mass flow rate gives approximately homogeneous temperature distribution. However, the outer streams near the wall is temperature drop deteriorated as increasing mass flow rate. The heterogeneous temperature of the melt effected on heat transfer coefficient numerically investigated at outlet. The overall heat transfer coefficient increases as increasing mass flow rate, nonetheless, 170°C of oil temperature gives higher results than others. |
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Numerical investigation of polymer melt heat transfer using Shell and tube heat exchanger in continuous polymer foaming process |
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