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gulleyassociates.comgulleyassociates.com/publishedart/ShellPressureDrop.pdf · calculation that can be improved is for the shell side of shell- and-tube heat exchangers. This revised

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Page 1: gulleyassociates.comgulleyassociates.com/publishedart/ShellPressureDrop.pdf · calculation that can be improved is for the shell side of shell- and-tube heat exchangers. This revised
Page 2: gulleyassociates.comgulleyassociates.com/publishedart/ShellPressureDrop.pdf · calculation that can be improved is for the shell side of shell- and-tube heat exchangers. This revised
Page 3: gulleyassociates.comgulleyassociates.com/publishedart/ShellPressureDrop.pdf · calculation that can be improved is for the shell side of shell- and-tube heat exchangers. This revised
Page 4: gulleyassociates.comgulleyassociates.com/publishedart/ShellPressureDrop.pdf · calculation that can be improved is for the shell side of shell- and-tube heat exchangers. This revised
Page 5: gulleyassociates.comgulleyassociates.com/publishedart/ShellPressureDrop.pdf · calculation that can be improved is for the shell side of shell- and-tube heat exchangers. This revised