Abstract The synthesis of nitriles such as acrylonitrile by the ammoxidation of mixtures of an olefin such as propylene or isobutylene, ammonia and oxygen or air is operated out low molar feed ratios of ammonia: olefin in the range of 1.03 to 1.07:1 and high excess oxygen levels of 4 to 7 mol % in the reactor effluent gases without significant losses in nitrile yield or significantly increased levels of oxygenated by-products. Control under such conditions is effected by analyzing the reactor effluent gases, previously temperature-conditioned at 350° to 450° F and solids removed, by a mass spectrometer instrument operating in a closed gas sampling and conditioning circuit or loop outside the reactor, and adjucting the input feed gas mixture in response to said effluent gas analysis to maintain the prescribed low ammonia rate in the feed and the excess oxygen level in the effluent gases leaving the reactor. Material savings in ammonia are effected and also in the amount of sulfuric acid required to remove unreacted ammonia from the residual gases before release of same to the atmosphere.
In the synthesis of an unsaturated aliphatic nitrile selected from the class consisting of acrylonitrile and methacrylonitrile by the ammoxidation of a gaseous mixture of a 1-monoolefin selected from the class consists of propylene and isobutylene, ammonia and oxygen over a solid ammoxidation catalyst at a reaction temperature of from about 550° to about 1100° F., the improvement which comprises establishing the flow of a portion of the effluent gases leaving said catalyst through a gas sampling circuit, conditioning the said effluent gases flowing in said circuit by adjusting the temperature of said gases therein to a relatively constant temperature in the range of from about 350° to about 450° F. and removing solid particles therein larger than about 5 microns in diameter, periodically analyzing the resulting conditioned and low solids gases with a mass spectrometer to determine at least the concentration of unreacted ammonia and of unreacted oxygen therein, and where required in response to the resulting analysis, readjusting the composition of said gaseous mixture fed to said catalyst to insure in said gaseous mixture fed to the reactor an ammonia: monoolefin molar feed ratio between about 1.03:1 and about 1.07:1 and to insure in said effluent gases an unreacted oxygen content of from about 4 to about 7 mol percent.
Claim 2
Dependent Claim
212 words
In the synthesis of an unsaturated aliphatic nitrile selected from the class consisting of acrylonitrile and methacrylonitrile by the ammoxidation of a gaseous mixture of a 1-monoolefin selected from the class consists of propylene and isobutylene, ammonia and oxygen over a solid ammoxidation catalyst at a reaction temperature of from about 550° to about 1100° F., the improvement which comprises establishing the flow of a portion of the effluent gases leaving said catalyst through a gas sampling circuit, conditioning the said effluent gases flowing in said circuit by adjusting the temperature of said gases therein to a relatively constant temperature in the range of from about 350° to about 450° F. and removing solid particles therein larger than about 5 microns in diameter, periodically analyzing the resulting conditioned and low solids gases with a mass spectrometer to determine at least the concentration of unreacted ammonia and of unreacted oxygen therein, and where required in response to the resulting analysis, readjusting the composition of said gaseous mixture fed to said catalyst to insure in said gaseous mixture fed to the reactor an ammonia: monoolefin molar feed ratio between about 1.03:1 and about 1.07:1 and to insure in said effluent gases an unreacted oxygen content of from about 4 to about 7 mol percent.
Claim 3
Dependent Claim
26 words
The method as defined in claim 1 and further characterized by said reaction mixture consisting of propylene, ammonia and air and the nitrile produced is acrylonitrile.