Abstract A process for producing 2,6-dichlorobenzonitrile by ammoxidation comprising contacting a starting gas consisting of 2,6-dichlorotoluene, air and ammonia, which comprises carrying out this reaction under the following conditions: (a) the concentration of 2,6-dichlorotoluene in the starting gas is 2.6 mole % or more. (b) the reactor effluent gas is contacting with water to cool to a temperature in the range of 50° to 90° C., whereby 2,6-dichlorobenzonitrile in the reactor effluent gas is collected as a slurry in which solidified 2,6-dichlorobenzonitrile is dispersed in water, and 2,6-dichlorobenzonitrile is obtained from the slurry, and (c) the cooled reactor effluent gas from which 2,6-dichlorobenzonitrile has been removed is contacted with water again to cool to a temperature in the range of 0° to 40° C., whereby unreacted 2,6-dichlorotoluene in the gas is collected as a dispersion in which it is dispersed in water and 2,6-dichlorotoluene is recovered from the dispersion. Also, there is disclosed a process for purifying 2,6-dichlorobenzonitrile obtained by subjecting 2,6-dichlorotoluene to ammoxidation, which comprises subjecting the 2,6-dichlorobenzonitrile to solid-liquid separation procedure in a molten state.
Inventors
👤 Yutaka Kiyomiya
👤 Yasumasa Yamaguchi
👤 Masahiro Ushigome
👤 Hiroshi Murata
Bibliographic Details
Application Number—
JurisdictionUS
Data Sourcegoogle_patents
Last Synchronized2026-11-07 04:03
CPC Classifications
C; C07; C07C; C07C255/00
Claims Analysis
Total Claims: 3
Claim 1
Independent Claim
154 words
A process for producing 2,6-dichlorobenzonitrile comprises contacting a starting gas consisting of 2,6-dichlorotoluene, air and ammonia with a fluidized bed a metallic oxide ammoxidation catalyst is carried on a carrier under the following conditions: (a) the concentration of 2,6-dichlorotoluene in the starting gas is 2.6 mole % or more, (b) the reactor effluent gas is contacted with water to cool to a temperature in the range of 50° to 90° C., whereby 2,6-dichlorobenzonitrile in the reaction product gas is collected as a slurry in which solidified 2,6-dichlorobenzonitrile is dispersed in water, and 2,6-dichlorobenzonitrile is obtained from the slurry, and (c) the cooled reactor effluent gas from which 2,6-dichlorobenzonitrile has been removed is contacted with water again to cool to a temperature in the range of 0° to 40° C., whereby unreacted 2,6-dichlorotoluene in the gas is collected as a dispersion in which it is dispersed in water and 2,6-dichlorotoluene is recovered from the dispersion.
Claim 2
Dependent Claim
154 words
A process for producing 2,6-dichlorobenzonitrile comprises contacting a starting gas consisting of 2,6-dichlorotoluene, air and ammonia with a fluidized bed a metallic oxide ammoxidation catalyst is carried on a carrier under the following conditions: (a) the concentration of 2,6-dichlorotoluene in the starting gas is 2.6 mole % or more, (b) the reactor effluent gas is contacted with water to cool to a temperature in the range of 50° to 90° C., whereby 2,6-dichlorobenzonitrile in the reaction product gas is collected as a slurry in which solidified 2,6-dichlorobenzonitrile is dispersed in water, and 2,6-dichlorobenzonitrile is obtained from the slurry, and (c) the cooled reactor effluent gas from which 2,6-dichlorobenzonitrile has been removed is contacted with water again to cool to a temperature in the range of 0° to 40° C., whereby unreacted 2,6-dichlorotoluene in the gas is collected as a dispersion in which it is dispersed in water and 2,6-dichlorotoluene is recovered from the dispersion.
Claim 3
Dependent Claim
59 words
A process for producing 2,6-dichlorobenzonitrile according to claim 1, wherein the process is carried out under the condition capable of meeting further at least one selected from the following ones: (a') the concentration of 2,6-dichlorotoluene in the starting gas is 3 mole % or more, and (d) the conversion of 2,6-dichlorotoluene in the ammoxidation ranges from 80 to 97%.