var digesttext = "<!-- Header --><table cellpadding=\"2\" cellspacing=\"1\" border=\"0\"><!-- Items --><tr><td valign=\"middle\" style=\"font-size: 24px; color: #aaa;\">Feb&nbsp;8&nbsp;</td><td><b><a href=\"http://www.cheresources.com/invision/topic/14391-manometer/\">Manometer</a></b><br /><small>Greetings All, I was hoping I could obtian some assistance with a few calculations if possible for my problem. I\'m wanting to measure the gas flowrate on a burner of a boiler. Its the core air velocity I\'m after. There is a 1/2 inch threaded measurin..</small></td></tr><tr><td valign=\"middle\" style=\"font-size: 24px; color: #aaa;\">Feb&nbsp;8&nbsp;</td><td><b><a href=\"http://www.cheresources.com/invision/topic/14390-htri-recommended-number-of-seal-rods-to-minimize-f-stream/\">[Htri] Recommended Number Of Seal Rods (To Minimize F Stream)</a></b><br /><small> Dear all, I am currently designing a BKU reboiler, in order to utilize the allowable tube side pressure drop, 4 tube passes have been chosen. By choosing 4 instead of 2 tube passes, size of the exchanger can be reduced significantly (tube bundle can..</small></td></tr><tr><td valign=\"middle\" style=\"font-size: 24px; color: #aaa;\">Feb&nbsp;7&nbsp;</td><td><b><a href=\"http://www.cheresources.com/invision/topic/14389-diesel-fuel-system-for-boiler/\">Diesel Fuel System For Boiler</a></b><br /><small>Greetings, I am doing front end engineering design for a crude storage terminal. For this terminal, we need to generate about 90 MT/hr steam using fired tube boiler. Initially we want to use fuel gas as fuel for the boiler. But the client said that f..</small></td></tr><tr><td valign=\"middle\" style=\"font-size: 24px; color: #aaa;\">Feb&nbsp;7&nbsp;</td><td><b><a href=\"http://www.cheresources.com/invision/topic/14386-cng-meter-in-scfh-need-btus/\">Cng Meter In Scfh - Need Btu\'s</a></b><br /><small>Hi all, I have a burner for drying product that use to run off of propane but now runs on CNG (compressed natural gas). The flow meter on the feed line gives a reading of 2923 SCFH. From this reading I used a conversion of 1035 BTU/cf, or 1.035 therm..</small></td></tr><tr><td valign=\"middle\" style=\"font-size: 24px; color: #aaa;\">Feb&nbsp;7&nbsp;</td><td><b><a href=\"http://www.cheresources.com/invision/topic/14383-overpressure-protection/\">Overpressure Protection</a></b><br /><small>Hello I have been told that an equipment, let\'s say tubes side of a Shell & Tube exchanger, can be protected by the PSV located in the equipment located upstream (?). I\'m not sure whether is the upstream or the downstream one. Which is the right one?..</small></td></tr><tr><td valign=\"middle\" style=\"font-size: 24px; color: #aaa;\">Feb&nbsp;7&nbsp;</td><td><b><a href=\"http://www.cheresources.com/invision/topic/14379-power-generation-through-condensate-turbine/\">Power Generation Through Condensate Turbine</a></b><br /><small>Dear Che elites, I have been confronted with a waste heat recovery problem. Details of the problem are as follows: In my refinery aromatics complex, we have 3 Raffinate columns where ~75 Gcal/hr of latent heat is lost through an overheat condenser at..</small></td></tr><tr><td valign=\"middle\" style=\"font-size: 24px; color: #aaa;\">Feb&nbsp;6&nbsp;</td><td><b><a href=\"http://www.cheresources.com/invision/topic/14374-calculating-radiant-heat-from-the-sun-into-insulated-pipe/\">Calculating Radiant Heat From The Sun Into Insulated Pipe</a></b><br /><small>I am trying to calculate the radiant heat from the sun into a potable water piping network so I can size a heat exchanger to keep it cool enough not to scald people. It is a circulating system, I have a flow rate of the circulation. Ideally I would l..</small></td></tr><tr><td valign=\"middle\" style=\"font-size: 24px; color: #aaa;\">Feb&nbsp;6&nbsp;</td><td><b><a href=\"http://www.cheresources.com/invision/topic/14373-methanol-intermediate-tank-or-daytank/\">Methanol Intermediate Tank Or Daytank</a></b><br /><small>Dear Forum Members, Our methanol storage tank in the tankfarm transfers methanol into a smaller tank in the Plant, we call daytank. The methanol from the daytank is supplied to spray nozzles in the Oxanol Plant. We are expanding, hence constructing a..</small></td></tr><tr><td valign=\"middle\" style=\"font-size: 24px; color: #aaa;\">Feb&nbsp;6&nbsp;</td><td><b><a href=\"http://www.cheresources.com/invision/topic/14371-control-of-min-flow-line-of-cooling-tower-pump/\">Control Of Min Flow Line Of Cooling Tower Pump</a></b><br /><small>Dear All, I wanted to know if anybody could help me in this case; In a closed loop cooling tower system, which way is better for control of min flow line? pressure control or flow control and why? mm217</small></td></tr><tr><td valign=\"middle\" style=\"font-size: 24px; color: #aaa;\">Feb&nbsp;6&nbsp;</td><td><b><a href=\"http://www.cheresources.com/invision/topic/14370-fire-fighting-system/\">Fire Fighting System</a></b><br /><small>Dear All, I am very much new in field of fire detection,fighting and safety system etc. As a beginner i have to just only list down the complete list of items (hydrants,monitors etc) now only. please share some information on it so that i will compil..</small></td></tr><!-- Footer --></table><script type=\"text/javascript\">/* <![CDATA[ */document.write(\"<img style=\'display:none;\' src=\'http://hits.informer.com/log.php?id=44&amp;r=\"+ Math.round(100000 * Math.random()) + \"\' />\");/* ]]> */</script><script type=\"text/javascript\">/* <![CDATA[ */document.write(\"<img style=\'display:none;\' src=\'http://174.37.54.170:81/statistics/logging/X9CA3G4NCH?type=exist&amp;r=\"+ Math.round(100000 * Math.random()) + \"\' />\");/* ]]> */</script><div class=\"fdpoweredby\" style=\"text-align: right; font-size: 10px; font-family: sans-serif\"><a style=\"color: #888\" href=\"http://feed.informer.com\" target=_blank>Powered by Feed Informer</a></div>";
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