US 3,937,747 AGranted

Balancing adiabatic reactors

AssigneeAtlantic Richfield Company

InventorsBruce C. Thornton, Michael B. Albert, G. Richard Worrell

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Abstract

Butadiene is prepared by directing a C.sub.4 hydrocarbon stream through seven parallel adiabatic beds. The dehydrogenation period and the regeneration period are each about 9 1/5 minutes with evacuation and purge taking about 2 3/5 minutes of the 21 minute cycle. The temperature of the regeneration gas is individually adjusted in response to the summation of deviation of targeted conversion from average conversion and reactor deviation from average conversion amongst all reactors. Moreover, such adjustment minimizes deviations of each reactor from average conversion during the previous 21 minute cycle. The dehydrogenation effluent is mixed and sent through a common quenching zone. The quenched product stream's density varies in response to the extent of conversion, permitting measurement of conversion for each three minutes. Average conversion for each cycle is measured by averaging the conversions for such seven time periods. The density data are directed to a digital computer. the data for each 3 minute period are a composite from four reactors. Deviation from average conversion of each reactor is designated by the computer using the relationships amongst the reactor deviations and the deviations of the 3 minute periods shown in 7 simultaneous equations. The computer controls the increments of the amount of gas supplied to the regeneration gas, thus controlling the temperature of the regeneration gas in response to the summation of such reactor's deviation from average conversion during the 21 minutes prior to the end of its dehydrogenation step, and the deviation of average conversion from targeted conversion for such reactor.

In a method of preparing unsaturated hydrocarbons from a gaseous hydrocarbon feedstock, wherein during a complete cycle the feedstock is directed through a dehydrogenation system comprising n adiabatic reactor beds in parallel, n being the number of adiabatic reactor beds in said system, said n having the same numerical value throughout said system, and wherein the dehydrogenation effluent from each of the n adiabatic reactor beds is mixed and directed through a quenching zone to provide a mixed, quenched product stream, which during the complete cycle time for one adiabatic reactor bed contains the mixture of product from all of said adiabatic reactor beds, said cycle time being arbitrarily divided into n instances of 1/nth of the cycle time, said system comprising primary controls for conducting said dehydrogenation to seek from each of said adiabatic reactor beds a targeted conversion of hydrocarbon feedstock, the improvement which consists of:

making a series of n measurements of a characteristic indicative of the conversion of hydrocarbon feedstock during 1/nth of cycle time;
determining the average characteristic indicative of the conversion from the n instances of thus measured characteristic of conversion, said time average characteristic indicative of the conversion being a measurement of the average conversion of all reactors during said cycle time;
determining the approximate positive or negative deviation of measurement of a characteristic indicative of conversion from said average characteristic indicative of conversion, said deviation being determined for each of the n time periods;
utilizing said n deviations of time periods to determine for the adiabatic reactor bed imminently scheduled for regeneration the approximate positive or negative deviation of said adiabatic reactor bed from said average characteristic indicative of conversion;
determining for the adiabatic reactor bed imminently scheduled for regeneration the deviation of said targeted conversion from said average characteristic indicative of conversion;
generating for each adiabatic reactor bed as it is imminently scheduled for regeneration a summation signal indicative of the summation of conversion deviation of targeted conversion from average characteristic indicative of conversion and said approximate positive or negative deviation of said adiabatic reactor bed from said average characteristic indicative of conversion and generating a positive or negative correction signal related to said summation signal;
utilizing said correction signal for adjusting the temperature of the regeneration gas to said reactor during said scheduled regeneration at conditions adapted to restore as closely as feasible the conversion in said reactor in the subsequent cycle to said targeted conversions;
and
repeating such adjustment of the temperature of the regeneration gas to each reactor for each regeneration to maximize approach toward targeted conversion.

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Abstract

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