Modelling and Simulation of Twin-Bed Pressure Swing Adsorption Plants

PDF Publication Title:

Modelling and Simulation of Twin-Bed Pressure Swing Adsorption Plants ( modelling-and-simulation-twin-bed-pressure-swing-adsorption- )

Previous Page View | Next Page View | Return to Search List

Text from PDF Page: 058

4 Experimental program 45 Fig. 4.5-3. The measured air demand is scattered around the Monte Carlo-simulated mean value – especially in the case of the 100 ppm data set, the experimentally found value is far from the peak of the normal distribution function. However, the deliberated data point cannot be considered as incorrect, but only as less likely to be measured. Tab. 4.5-3 Results of the reproducibility test Productivity [m3n/h N2 / m3 CMS] 1 2 58.17 3 4 58.16 5 6 58.15 7 8 58.16 9 10 58.16 𝐗̅ 𝛔 0.007 𝛔𝐗̅ Air demand [m3n/h air / m3n/h N2] Explicit method Implicit method GMB OMB 4.93 4.94 4.93 4.94 4.94 4.94 4.94 4.97 4.94 4.97 0.014 0.022 Relative error δexp [%] 0.20 0.20 0.00 0.61 0.61 58.16 4.95 4.97 0.40 58.15 4.96 4.98 0.40 58.17 4.96 4.97 0.20 58.16 4.97 4.99 0.40 58.17 4.93 4.92 0.20 58.16 4.95 4.96 0.01 % 0.29 % 0.45 % Fig. 4.5-3 Normal distribution of the air demand at different product purity levels The distribution of the relative error δsim is presented in Fig. 4.5-4. The relative error δsim of the air demand is determined in every Monte Carlo run from the difference between Eq. 4.4-5 and 4.4-6. δsim surpasses δexp with a corresponding probability at every deliberated product purity level. This finding confirms that determination and comparison of differently calculated air demand values provide a very sensitive method to prove; and thus, to accept or to discard experimental high-purity data.

PDF Image | Modelling and Simulation of Twin-Bed Pressure Swing Adsorption Plants

PDF Search Title:

Modelling and Simulation of Twin-Bed Pressure Swing Adsorption Plants

Original File Name Searched:

dissertation_marcinek.pdf

DIY PDF Search: Google It | Yahoo | Bing

CO2 Organic Rankine Cycle Experimenter Platform The supercritical CO2 phase change system is both a heat pump and organic rankine cycle which can be used for those purposes and as a supercritical extractor for advanced subcritical and supercritical extraction technology. Uses include producing nanoparticles, precious metal CO2 extraction, lithium battery recycling, and other applications... More Info

Heat Pumps CO2 ORC Heat Pump System Platform More Info

CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com (Standard Web Page)