Method and apparatus for controlling FCC effluent with near-infrared spectroscopy
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example 1
[0040]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 Feed withwith Onlywith OnlyNormalMultivariableRateROTOperationOptimizationVariedVariedFeed PropertiesAPI24.621.821.821.8UOP K11.6911.7711.7711.77Concarbon (%)0.150.590.590.59Nitrogen (ppm)1150162162162Sulfur (%)0.340.550.550.551-ring Aromatics35292929(%)2-ring Aromatics34262626(%)3-ring Aromatics17252525(%)4-ring14202020Aromatics+(%)ProcessConditionsFeed Rate10095.383...
example 2
[0042]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.
[0043]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
The Effect or Riser Temperature
[0044]One of the most common types of process variable studies completed via the use of reaction effluent testing is the impact of riser outlet temperature on FCC reactor yields. This is one of the most fundamental sets of data required to optimize the performance of the FCC unit. Table 1 contains results from a riser temperature test runs series. For this study, reactor effluent samples were collected at three different riser outlet temperatures, with the maximum riser temperature constrained by the ability to handle gas volumes in the FCC gas plant.
TABLE 1Effect of Riser Outlet Temperature on FCC Product YieldsRiser Outlet Temperature: F.+15° F.Base−18° F.Unit Conversion: Volume % FF+1.4Base−3.2Gasoline Yield: Volume %−0.3Base+0.2Total C3 plus C4 Yield: Volume % FF+1.3Base−3.8Ethane and Lighter Yield: Weight % FF+0.51Base−0.63Coke Yield: Weight % FF+0.17Base−0.18
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