Aspen simulation of pulverized coal gasification
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Block: DECOMP Model: RYIELD * WARNING: THE SPECIFIED YIELDS HAVE BEEN NORMALIZED BY A FACTOR OF (0.99575) TO ENSURE AN OVERALL MATERIAL BALANCE. INFORMATION ELEMENT NO. 2 IN THE ULTANAL ATTRIBUTES IS SET TO ZERO; THIS VALUE IS MISSING IN THE COMP-ATTR FORM AS WELL AS IN THE INLET STREAM. INFORMATION ELEMENT NO. 3 IN THE ULTANAL ATTRIBUTES IS ALSO SET TO ZERO; ITS VALUE IS MISSING IN THE COMP-ATTR FORM AND IN THE INLET STREAM. INFORMATION ELEMENT NO. 4 IN THE ULTANAL ATTRIBUTES IS SET TO ZERO; AGAIN, THIS VALUE IS MISSING IN THE COMP-ATTR FORM AND IN THE INLET STREAM. INFORMATION ELEMENT NO. 5 IN THE ULTANAL ATTRIBUTES IS SET TO ZERO; ITS VALUE IS ALSO MISSING IN THE COMP-ATTR FORM AND IN THE INLET STREAM. INFORMATION ELEMENT NO. 6 IN THE ULTANAL ATTRIBUTES IS SET TO ZERO; THE VALUE IS MISSING IN THE COMP-ATTR FORM AND IN THE INLET STREAM. INFORMATION ELEMENT NO. 7 IN THE ULTANAL ATTRIBUTES IS SET TO ZERO; ITS VALUE IS MISSING IN THE COMP-ATTR FORM AND IN THE INLET STREAM. * WARNING: IN THE SUBS-ATTR SENTENCE, (9) VALUES WERE ENTERED WHILE (10) VALUES WERE EXPECTED. * WARNING: IN THE SAME SUBS-ATTR SENTENCE, (4) VALUES WERE ENTERED WHEN (10) VALUES WERE REQUIRED. Why are the values for 2.3.4.5.6 all equal to 0? What have I done wrong?
Also, when using Aspen for simulation, if the actual operating data of the reaction apparatus are available, it is possible to derive the reaction kinetic equations. How is this done?
You must have forgotten to enter the elemental analysis data for the feed stream. If I’m not mistaken, you want to use a RYIELD reactor to process unconventional feed streams of coal; in that case, you should enter the elemental analysis data of the coal in the Comp-Attr field of the coal stream. If you do not enter anything, ASPEN will automatically set it to the default value of 0.
Did you get it wrong? ASPEN allows you to input reaction kinetics data to simulate reactions, but it cannot derive kinetic equations from actual operational data.
But someone said that if he’s given the actual operational data, he can deduce the actual reaction process, right? ? ? ?
Could an expert explain the process of a simulated vaporization furnace? Or how about giving an example? Thank you