Method and apparatus for controlling catalytic cracking by near-infrared spectroscopy
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example 1
[0043]Different feedstocks will result in different yields from the FCC process. If the unit is operating against a constraint, the process will need to adjust to avoid exceeding an equipment limitation. Typical process variables include feed rate, reactor temperature, feed preheat and pressure. The process response from each of the variables is non-linear. The optimum set of conditions to maximize profitability to unit constraints will typically vary depending upon the feed quality. The following is an example of different operating conditions required to maximize profitability for a change in feed:
New FeedNew FeedNew FeedNormalwith Multi-with Onlywith OnlyOper-variableRateROTationOptimizationVariedVariedFeed PropertiesAPI24.621.821.821.8UOP K11.6911.7711.7711.77Concarbon (%)0.150.590.590.59Nitrogen (ppm)1150162162162Sulfur (%)0.340.550.550.551-ring Aromatics (%)352929292-ring Aromatics (%)342626263-ring Aromatics (%)172525254-ring Aromatics+ (%)14202020Process ConditionsFeed Rate ...
example 2
[0045]FIG. 2 is a Table which shows samples, including hydrotreater chargers and products and FCC feeds used to control weight percents of each hydrocarbon class.
[0046]Two hundred fifty samples, including hydrotreater charges and products and FCC feeds were used to create a PLS model for predicting weight percents of each hydrocarbon class. The samples were analyzed using the online NIR. Wavelengths were chosen for each group and a summary appears in FIG. 2.
example 3
[0047]FIGS. 3 and 4 illustrate typical NIR absorption spectra of FCC feed samples and the resulting 2nd derivative spectra.
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