Importance of accounting for the piping system and boundary conditions in determining the maximum surge pressure following heat-exchanger tube-rupture

Author:

Botros Kamal K.

Publisher

Elsevier BV

Subject

Industrial and Manufacturing Engineering,Management Science and Operations Research,Energy Engineering and Power Technology,Safety, Risk, Reliability and Quality,General Chemical Engineering,Food Science,Control and Systems Engineering

Reference20 articles.

1. Boiler and Pressure Vessel Code, Section VIII, Division 1: Rules for Construction of Pressure Vessels;American Society of Mechanical Engineers,2014

2. Sizing, Selection, and Installation of Pressure-relieving Devices, Part I, Sizing and Selection, Appendix C, Sizing for Two-phase Liquid/vapor Relief;American Petroleum Institute, API 520,2014

3. Pressure-relieving and Depressuring Systems;American Petroleum Institute. API 521,2014

4. Aspen Technology (2014), Inc. Aspen Plus (Version 8.6) [Computer software].

5. Generalized contraction coefficient of an orifice for subsonic and supercritical flows”, ASME;Benedict;J. Basic Eng.,1971

Cited by 2 articles. 订阅此论文施引文献 订阅此论文施引文献,注册后可以免费订阅5篇论文的施引文献,订阅后可以查看论文全部施引文献

1. Shock Wave Evaluation in Shell and Tube Heat Exchanger Tube Rupture Scenario;Journal of Thermal Science and Engineering Applications;2024-02-19

2. Dynamic modeling of heat exchanger tube rupture;BMC Chemical Engineering;2020-03-04

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