Math Problem Solver

Total fluid entering kg/h 61333

DRY GAS KG/HR , MW 60700 17.52

STEAM KG/HR 633

DRY GAS

MW %MOL

AIR 28.966

O2 32

N2 28.016 1.07

WATER VAPOR 18.016

CO 28.01

CO2 44.01 0.14

H2S 34.076

H2 2.016

METHANE 16.042 93.04

ETHYLENE 28.052

ETHANE 30.068 3.66

PROPYLENE 42.078

PROPANE 44.094 1.2

I-BUTANE 58.12 0.22

N-BUTANE 58.12 0.29

I-PENTANE 72.146 0.1

N-PENTANE 72.146 0.09

HEXANES 86.172 0.13

HEPTANES 100.198 0.06

100

AVG.MOL WT. 17.52 SO I PROVIDE FREASH ALL DATA NOW TABLE IS FOR DRY GAS BUT STREAM IN SOME % PRESENT THAT NOT COVER IN TABLE SO WE HAVE TO ADD STREAM AS WATER VAPOR SO FIND MOL % IS OUR GOAL FOR THAT I HAVE IN MIND PALN IS FROM MOLE % WE CAN FIND KG/HR QUNTITY FROM THAT VAPOUR - STREAM FIND VALUE , THAT VALUE IS WATER MOL% CONVERT IS THAT CORRECT WAY , PLEASE CHECK AND DO ALSO YOUR OWN METHOD IF IT BEATER BUT GIVEN:

Steam = 633 kg/h IN THIS POINT FOR STREAM OTHER VALUE GIVEN STREAM AND VAPOUR BOTH DIFFERENT ,NOTING ASSUMED ALL VALVUE GIVEN USE THAT NO ASSUMED