{"kind":"task","effective_mode":"full","benchmark":{"kind":"benchmark","effective_mode":"full","slug":"mmlu-pro","formal_name":"MMLU-Pro","introduction":"MMLU-Pro rebuilds MMLU with ten answer options instead of four and removes items that no longer separate models. Questions span fourteen academic and professional subjects.","introduction_ja":"","introduction_en":"","category":"Category not supplied","task_count":null,"acquisition_status":"Acquisition status not supplied","official_url":"https://huggingface.co/datasets/TIGER-Lab/MMLU-Pro","indexing_mode":"index","profile":{"resources":[],"task_format":"","scoring":"","metric":"","size":"","answer_access":"","license":"","citation":"","maintainer":"","released":"","why_hard":"","related":[],"history":"","construction":"","limitations":"","saturation":"","scores":[]}},"task_id":"badaba99-6b24-52cf-bfc7-4645c2194978","task_key":"default--test--11340","task_revision_id":"1","upstream_id":"11340","short_description":"A toluene -xylenemixture is fractionated in a bubble-cap column. Approximate the…","config":"default","split":"test","body":"{\"category\":\"engineering\",\"options\":\"['4500kgmole/m^3 \\\\x08ullet hr', '3000kgmole/m^3 \\\\x08ullet hr', '2500 kgmole/m^3•hr', '3552kgmole/m^3 \\\\x08ullet hr', '2000kgmole/m^3 \\\\x08ullet 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']\",\"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\",\"src\":\"stemez-TransportPhenomena\"}","display_format":"text","language":"","answer_status":"published","assets":[],"source_url":"https://huggingface.co/datasets/TIGER-Lab/MMLU-Pro","history":"initial import","indexing_mode":"index","subproblems":[],"grids":[]}