发布时间:2024-05-27 17:49:26 - 更新时间:2024年06月29日 15:22
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This specification covers the design, construction, inspection and testing of cylindrical shell and plain tube heat exchangers for application
Gaskets for shell and tube heat exchangers
本文件规定了典型管壳式热交换器式的能效测试与评价方法、能效指标。 本文件适用于液-液相变工况和弓形折流板光管管束管壳热交换器,适用的测试介质: a)壳测介质为THERMINOL 55导热油(热流体); b)管侧介质为水(冷流体
Energy Efficiency Evaluation of Typical Shell-and-Tube Heat Exchangers
This International Standard specifies requirements and gives recommendations for the mechanical design,material selection,fabrication,inspection
Petroleum, petrochemical and natural gas industries - Shell-and-tube heat exchangers (ISO 16812:2007); English version EN ISO 16812:2007
GB/T 29463的本部分规定了缠绕式垫片的结构型式与尺寸。本部分适用于设计压力为0.25 MPa~6.4 MPa、工作温度-70℃~450℃的管壳式热交换器用缠绕式垫片。本部分仅适用于凹凸密封面
Gaskets used in tube-shell heat exchangers.Part 2:Spiral wound gasket
GB/T27698 的本部分規定了管亮式熟交換器用換熱管液一液元相雙‵汽一液有相夔冷凝‵流劫沸騰蒸发有相变和池沸腾蒸发有相变测试工况的传热和流体阻力性能测试方法。 本部分适用的测试流体为单组分或只作单组分考虑的液-液、汽-液”本部分只考虑换热管材料的导热热阻,未考虑换热管内外侧污垢热阻
Test method for the performance of heat exchangers and heat exchange element.Part 5:Heat transfer tube for tubular heat exchangers
GB/T 29463的本部分规定了管壳式热交换器用金属包垫片的结构型式与尺寸。 本部分适用于设计压力为0.25MPa~6.4MPa、设计温度为-20℃~450℃的管壳式热交换器用金属包垫片
Gaskets used in tube-shell heat exchangers.Part 1:Metallic jacketed gaskets
GB/T 29463的本部分规定了非金属软垫片的结构型式与尺寸。本部分适用于设计压力为0.25 MPa~4.0 MPa,设计温度为-20℃~350℃的管壳式热交换器用非金属软垫片
Gaskets used in tube-shell heat exchangers.Part 3:Nonmetallic gaskets
GB/T 28713的本部分规定了管壳式热交换器用波节管的基本参数及技术要求。本部分适用于管壳式热交换器用波节管,其公称压力不大于4.0 MPa,工作温度高于-20°C、低于450°C,工作介质适用于碳素钢及不锈钢的场合
Enhanced heat transfer elements used in tube-shell heat exchangers.Part 3:Wavy tubes
GB/T 28713的本部分规定了管壳式热交换器用螺纹管的基本参数及技术要求。本部分适用于管外总热阻(包括介质膜热阻和污垢热阻)为控制热阻的传热场合。本部分不适用于管外固体粉尘含量较高或易于结焦的场合
Enhanced heat transfer elements used in tube-shell heat exchangers.Part 1:Threaded tubes
Petroleum, petrochemical and natural gas industries - Shell-and-tube heat exchangers (ISO 16812:2019) (Endorsed by Asociación Española de Normalización in April of 2019.)
GB/T27698本部分规定了管壳式热交换器液-液相变、汽-液冷凝有相变、汽-液蒸发有相变测试工况的传热和流体阻力性能测试方法。 本部分适用的测试流体为液体-液体、蒸汽-液体。 本部分只考虑传热管材料的导热热阻,未考虑传热管内外侧污垢热阻
Test method for the performance of heat exchangers and heat exchange element.Part 2:Tubular heat exchanger
ESDU 87019 draws on the available data in the literature to predict the critical velocity through the bundle for the onset of fluidelastic instability
Flow induced vibration in tube bundles with particular reference to shell and tube heat exchangers.
GB/T 28713的本部分规定了管壳式热交换器用奥氏体不锈钢波纹管的基本参数及技术要求、本部分适用于公称压力不大于4.0 MPa,工作温度高于-20 ℃、低于450℃,工作介质应适合奥氏体不锈钢的场合
Enhanced heat transfer elements used in tube-shell heat exchangers.Part 2:Stainless steel corrugated tubes
This International Standard specifies requirements and gives recommendations for the mechanical design, material selection, fabrication, inspection
Petroleum and natural gas industries - Shell-and-tube heat exchangers
This specification covers the design, construction, inspection and testing of cylindrical shell and plain tube heat exchangers for application
Gaskets for shell and tube heat exchangers
本文件规定了典型管壳式热交换器式的能效测试与评价方法、能效指标。 本文件适用于液-液相变工况和弓形折流板光管管束管壳热交换器,适用的测试介质: a)壳测介质为THERMINOL 55导热油(热流体); b)管侧介质为水(冷流体
Energy Efficiency Evaluation of Typical Shell-and-Tube Heat Exchangers
This International Standard specifies requirements and gives recommendations for the mechanical design,material selection,fabrication,inspection
Petroleum, petrochemical and natural gas industries - Shell-and-tube heat exchangers (ISO 16812:2007); English version EN ISO 16812:2007
GB/T 29463的本部分规定了缠绕式垫片的结构型式与尺寸。本部分适用于设计压力为0.25 MPa~6.4 MPa、工作温度-70℃~450℃的管壳式热交换器用缠绕式垫片。本部分仅适用于凹凸密封面
Gaskets used in tube-shell heat exchangers.Part 2:Spiral wound gasket
GB/T27698 的本部分規定了管亮式熟交換器用換熱管液一液元相雙‵汽一液有相夔冷凝‵流劫沸騰蒸发有相变和池沸腾蒸发有相变测试工况的传热和流体阻力性能测试方法。 本部分适用的测试流体为单组分或只作单组分考虑的液-液、汽-液”本部分只考虑换热管材料的导热热阻,未考虑换热管内外侧污垢热阻
Test method for the performance of heat exchangers and heat exchange element.Part 5:Heat transfer tube for tubular heat exchangers
GB/T 29463的本部分规定了管壳式热交换器用金属包垫片的结构型式与尺寸。 本部分适用于设计压力为0.25MPa~6.4MPa、设计温度为-20℃~450℃的管壳式热交换器用金属包垫片
Gaskets used in tube-shell heat exchangers.Part 1:Metallic jacketed gaskets
GB/T 29463的本部分规定了非金属软垫片的结构型式与尺寸。本部分适用于设计压力为0.25 MPa~4.0 MPa,设计温度为-20℃~350℃的管壳式热交换器用非金属软垫片
Gaskets used in tube-shell heat exchangers.Part 3:Nonmetallic gaskets
GB/T 28713的本部分规定了管壳式热交换器用波节管的基本参数及技术要求。本部分适用于管壳式热交换器用波节管,其公称压力不大于4.0 MPa,工作温度高于-20°C、低于450°C,工作介质适用于碳素钢及不锈钢的场合
Enhanced heat transfer elements used in tube-shell heat exchangers.Part 3:Wavy tubes
GB/T 28713的本部分规定了管壳式热交换器用螺纹管的基本参数及技术要求。本部分适用于管外总热阻(包括介质膜热阻和污垢热阻)为控制热阻的传热场合。本部分不适用于管外固体粉尘含量较高或易于结焦的场合
Enhanced heat transfer elements used in tube-shell heat exchangers.Part 1:Threaded tubes
Petroleum, petrochemical and natural gas industries - Shell-and-tube heat exchangers (ISO 16812:2019) (Endorsed by Asociación Española de Normalización in April of 2019.)
GB/T27698本部分规定了管壳式热交换器液-液相变、汽-液冷凝有相变、汽-液蒸发有相变测试工况的传热和流体阻力性能测试方法。 本部分适用的测试流体为液体-液体、蒸汽-液体。 本部分只考虑传热管材料的导热热阻,未考虑传热管内外侧污垢热阻
Test method for the performance of heat exchangers and heat exchange element.Part 2:Tubular heat exchanger
ESDU 87019 draws on the available data in the literature to predict the critical velocity through the bundle for the onset of fluidelastic instability
Flow induced vibration in tube bundles with particular reference to shell and tube heat exchangers.
GB/T 28713的本部分规定了管壳式热交换器用奥氏体不锈钢波纹管的基本参数及技术要求、本部分适用于公称压力不大于4.0 MPa,工作温度高于-20 ℃、低于450℃,工作介质应适合奥氏体不锈钢的场合
Enhanced heat transfer elements used in tube-shell heat exchangers.Part 2:Stainless steel corrugated tubes
This International Standard specifies requirements and gives recommendations for the mechanical design, material selection, fabrication, inspection
Petroleum and natural gas industries - Shell-and-tube heat exchangers