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<p class=MsoNormal><font size=2 color=navy face=Arial><span style='font-size:
10.0pt;font-family:Arial;color:navy'>I am looking for information (articles,
research papers, case studies) on the effect of the location of the pump
relative to a plate and frame heat exchanger in a closed piping system. Some
of the issues are (1) the vertical height of the piping system (1000’ to
2000’), how high can you go, (2) pumping thru HX, (3) pumping away from
HX, (4) pump and HX located at bottom of system, (5) pump and HX at top of
system, and (6) pump start up. What are the issues when the HX is
replaced with other equipment such as chillers and boilers?</span></font></p>
<p class=MsoNormal><font size=2 color=navy face=Arial><span style='font-size:
10.0pt;font-family:Arial;color:navy'> </span></font></p>
<p class=MsoNormal><font size=2 color=navy face=Arial><span style='font-size:
10.0pt;font-family:Arial;color:navy'>Varkie Thomas</span></font></p>
<p class=MsoNormal><font size=2 color=navy face=Arial><span style='font-size:
10.0pt;font-family:Arial;color:navy'>Skidmore, Owings & Merrill</span></font></p>
<p class=MsoNormal><font size=2 color=navy face=Arial><span style='font-size:
10.0pt;font-family:Arial;color:navy'>312-360-4467</span></font></p>
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12.0pt'> </span></font></p>
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