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Recovery fraction

Light Ends Recovery, Fractionation, and Conversion Propylenes and butylenes may be recovered for feed to a polymerization plant for production of high octane... [Pg.220]

C46 General Oxidation (including Disinfection) --Other R13 Solvents/Organics Recovery - Fractionation... [Pg.48]

BOTTOM PRCOUCt CF L15.8.7H MCLES) liquid top PRCOUCT OF tlS.8,7H MOLESl VAPOR TCP PRODUCT OF E15.8.7H MOLESl component AMCUMS/I5L20.8) I COMPONENT recovery FRACTIONS/(5E20.B11... [Pg.332]

TOTAL PRODUCT MASS BALANCES ANO RECOVERY FRACTIONS... [Pg.350]

TOTAL PRODUCT NASS BALANCES AND RECOVERY FRACTIONS RECOVERY FRACTION SUMMATIONS FOR EACH COMPONENT... [Pg.355]

Step 4b. For leaching a vegetation ash sample, strong mineral acids such as HN03 can be used. Note A leach recovery fraction must be determined that applies specifically to the matrix, radioanalyte, leaching solution, and leaching program (temperature, relative volumes, time) under consideration. [Pg.102]

Effective escape depth d vs. angle of ejected electrons 9 for the case of 99% recovery and 90%> recovery (( = fraction recovered)... [Pg.227]

Separations with High Recovery Fractions Should Be Done Last. This heuristic follows 5 and is justified by the same arguments. [Pg.209]

A distillation column with a partial reboiler and a total condenser is being used to separate a mixture of benzene, toluene, and 1,2,3-trimethylbenzene. The feed, 40 mol% benzene, 30 mol% toluene, and 30 mol% 1,2,3-trimethylbenzene, enters the column as a saturated vapor. We desire 95% recovery of the toluene in the distillate and 95% of the 1,2,3-trimethylbenzene in the bottoms. The reflux is returned as a saturated liquid, and constant molar overflow can be assumed. The column operates at a pressure of 1 atm. Find the number of equilibrium stages required at total reflux, and the recovery fraction of benzene in the distillate. Solutions of benzene, toluene, and 1,2,3-trimethylbenzene are ideal. [Pg.371]

Application of (12-104) requires iterative calculation procedures to establish values of necessary absorption factors, stripping factors, and recovery fractions. [Pg.255]

Reciprocating plate contactor, 516-522 Recovery fraction, 461 Rectift ing section, 293 Redlich-Kwong equation, 148, 599 Reflux, 12 drum, 514 total, 323, 435 Refluxed stripper, 9, 13 Reflux ratio cost, 451 external, 310 internal, 310 minimum, 323, 443... [Pg.383]

See other pages where Recovery fraction is mentioned: [Pg.30]    [Pg.4]    [Pg.6]    [Pg.10]    [Pg.261]    [Pg.17]    [Pg.315]    [Pg.350]    [Pg.350]    [Pg.350]    [Pg.352]    [Pg.352]    [Pg.352]    [Pg.355]    [Pg.330]    [Pg.331]    [Pg.384]    [Pg.68]    [Pg.60]    [Pg.77]    [Pg.579]    [Pg.584]    [Pg.30]    [Pg.621]    [Pg.621]    [Pg.185]    [Pg.264]    [Pg.264]    [Pg.265]    [Pg.266]    [Pg.137]    [Pg.94]   
See also in sourсe #XX -- [ Pg.77 ]



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