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Looking for usable FRI software

2009-06-09View Original

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Well, I downloaded that one from the forum, but it’s expired and won’t work at all. Could some expert please provide me with a working version?
Reply #22009-07-08
http://bbs.hcbbs.com/viewthread.php?tid=6699&highlight=FRI
Reply #32010-08-02
This post was last edited by wiseboy on 2010-8-2 12:02. China’s WTR must be very attractive. The intelligent features allow you to design professional-quality trays in a very short time. Many beginners with data knowledge may not be able to answer, but WTR will automatically add the default values for you. In extreme cases, you only need to enter 5 values: gas phase flow rate, gas phase density, liquid phase flow rate, liquid phase density, and liquid phase surface tension, and the calculation will be completed automatically! Report on Fluid Dynamics Calculations for Tray Towers ━━━━━━━━━━━━━ Process data: Gas phase density: 8.0369 kg/m3; Gas phase volumetric flow rate: 853.8770 m3/h; Gas phase mass flow rate: 6862.5072 kg/h; Foam density: 0.7000. Liquid phase density: 1515.4151 kg/m3; Liquid phase surface tension: 16.2996 Dyne/cm; Liquid phase volumetric flow rate: 9.4685 m3/h; Liquid phase mass flow rate: 14348.6842 kg/h. Tray structure data (1): Number of flow paths: 1; Tray spacing: 300.0000 mm; Stabilization zone: 70.0000 mm; Edge zone: 50.0000 mm; Wetting point percentage: 70.0493%; Wetting point gas velocity: 0.5832 m/s; Empty tower gas velocity: 0.4085 m/s; Flow factor: 0.1523; Downcomer pressure drop: 2.6392 mm; Height of clear liquid in downcomer: 140.9614 mm; Tower diameter: 950 mm; Downcomer residence time: 15 s; Specified tower diameter: 950 mm; Operating upper limit: 156%; Operating lower limit: 57%; Weir diameter ratio: 85.0000%; Weir height: 50.0000 mm; Weir tooth depth: 5.0000 mm; Gap between downcomer and tray: 25.0000 mm; Weir length: 807.5017 mm; Downcomer width: 224.7787 mm; Downcomer area: 18.0870%; Area of open section: 0.2969 m2; Liquid level above weir: 14.2203 mm; Height of clear liquid: 39.0828 mm; Lower limit of liquid phase flow rate: 1.0948 m3/h; Upper limit of liquid phase flow rate: 27.6921 m3/h. Tray structure data (2): Tray type: Tray; Pattern of holes: Equilateral triangular arrangement; Number of tray sections: 2; Hole diameter: 6.0000 mm; Hole spacing to diameter ratio: 3.0000; Tray thickness: 2.0000 mm; Hole spacing: 18.0000 mm; Number of holes: 1038.0000; Openness ratio: 9.8840%; Hole velocity: 8.0818 m/s; Pressure drop across dry tray: 35.0191 mm; Total pressure drop across tray: 74.1018 mm

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