/*
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Text[...]=[Range,The desired temperature drop of the fluid measured as the difference between incoming and outgoing fluid temperatures.]

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Text[0]=["Me Email","Click here to send me an email "]
Text[1]=["Home Page","Click here to go to my Web site."]
Text[2]=["Range","The desired temperature drop of the fluid measured as the difference between incoming and outgoing fluid temperatures."]
Text[3]=["Approach","The desired temperature difference between outgoing fluid and the refrigerant"]
Text[4]=["Pressure Drop","Acceptable level of fluid system pressure drop through the chiller barrel at computed gallons per minute (gpm) flow rate."]
Text[5]=["Capacity","Necessary heat removal (tonnage) at maximum operating load.<br>After determining fluid temperature drop (Range), find the capacity table identified for the particular range. (If no table exists for that specific point, use the next lowest temperature range for which a table exists.) At the top of the table, various approach temperatures are given.  Find the approach desired and read down the tons column until you reach a capacity adequate to do the job.  The water pressure drop (psi) is listed next to the capacity figure.  To determine gpm, multiply tons by the gpm factor, whic is noted below each range chart.<br><br>Chiller barrels may be sized by other methods as well.  Where the desired temperature range is known (difference between incoming and outgoing fluid), determine the Btu/hr capacity needed by multiplying the temperature range by gpm flow and convert to pounds of water per hour using the multiplier 500.<br>Range x gpm x 500 = Btu/hr"]
Text[6]=["Conformance","Nominal Tonnage Rating Basis<br><br>Nominal ratings are based on ARI standard 480, specific conditions being:<br> 1 ton=12,000Btu/hr&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;100&deg;F.liquid entering TXV<br> 54&deg;F.inlet water&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;7&deg; superheat<br> 44&deg;F.outlet water&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;35&deg;F R22 Saturated Suction<br>0.0001ft&#178;hr&deg;F/Btu additive fouling factor <br><br>All models are designed and constructed to meet ASME Boiler and Pressure Vessel Code Section VIII, Division 1. ASME code for the shell side is available upon request.<br><br>Tube Side: 300 PSE at 200&deg; F<br>Shell Side: 200 PSI at 200&deg; F (non-code)<br><br>ER evoparotr shells are constructed with ASME grade carbon steel. Enhanced copper tubing is mechanically expanded for a superior seal into machined carbon steel tubesheets. Tubing wall thickness is 0.018 inches. Removable endplates, refrigerant and water connections are constructed from carbon steel. All baffles are made from corrosion resistant materials."]
Text[7]=["Construction","ER evaporator shells are constructed with ASME grade carbon steel. Enhanced copper tubing is mechanically expanded for a superior seal into machined carbon steel tubesheets. Tubing wall thickness is 0.018 inches. Removable endplates, refrigerant and water connections are constructed from carbon steel. All baffles are made from corrosion resistant materials. <br><br>Tube Side: 300 PSE at 200&deg; F<br>Shell Side: 200 PSI at 200&deg; F (non-code)"]
Text[8]=["Water Flow Rate","There is one baffle configuration per ER model. As a result, the water flow rate at the job site will need to be adjusted to obtain the design water flow rate. At a range of 10&deg;F, the water flow rate should be 2.4 gpm/ton."]
Text[9]=["Refrigerant Connections","The refrigerant side configuration for the ER evaporators is 3-Pass with nozzles at opposite ends. As a result, the refrigerant nozzles are on teh same ends, but may not be in the same locations as the other OEM Single Pass evaporators."]
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Text[13]=["different style","Wow this is a new style and position! "]
Text[14]=["This is The title","this is the text"]
Text[15]=["","This is only text"]
Text[16]=["","Some Lists <li>list one</li> <li>list two</li> <li>list three</li> <li>list four</li>"]


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