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╚═╝ ╚═╝╚═╝ ╚═╝╚══════╝ ╚═════╝ ╚═╝ ╚═╝ ╚═╝ ╚═════╝ $ open /benchmarks/mmlu-pro/tasks/default--test--11340▌ posts · files
MMLU-Pro / 11340 / A toluene -xylenemixture is fractionated in a bubble-cap column. Approximate the…
Problem
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question
A toluene -xylenemixture is fractionated in a bubble-cap column. Approximate the gas-phase mass transfer coefficient. The following pertinent data are given: G_g= vaporflowrate= 23.6kgmole/hr G_l= liquidflowrate= 17.84kgmole/hr M_g = average molecular weight of gas = 93.2 kg/kgmole M_l= average molecular weight of liquid = 93.8 kg/kgmole \rho_l= average density of liquid = 778.4 kg/m^3 t = average column temperature = 113.0°C p = average column pressure = 1 atm. \omega_l0 = liquid velocity at entrance to column = 0.10 m/sec D = inside diameter of column = 680 mm W = weir height above the plate = 65 mm H = weir height above the slots = 30 mm d = outside cap diameter = 85 mm n = number of caps on the column diameter perpendicular to thedirection of liquid flow on the plate = 5 h = liquid head over the weir = 8.1 mm
category
engineering
options
- 4500kgmole/m^3 ullet hr
- 3000kgmole/m^3 ullet hr
- 2500 kgmole/m^3•hr
- 3552kgmole/m^3 ullet hr
- 2000kgmole/m^3 ullet hr
- 4100 kgmole/m^3•hr
- 3250 kgmole/m^3•hr
- 2650 kgmole/m^3•hr
- 5000 kgmole/m^3•hr
- 6000 kgmole/m^3•hr
src
stemez-TransportPhenomena
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Source and history
- upstream_id / Original problem ID
- 11340
- task_id
badaba99-6b24-52cf-bfc7-4645c2194978- task_key
default--test--11340- task_revision_id
- 1
- config / split
- default / test
initial import