Process for the purification of waste from acrylonitrile production
AssigneesErdolchemie GmbH, Bayer Aktiengesellschaft
InventorsArnold Hausweiler, Adolf Mayer, Feliks Bitners
Life of this patent
Estimating the term…
Loading patent…
AssigneesErdolchemie GmbH, Bayer Aktiengesellschaft
InventorsArnold Hausweiler, Adolf Mayer, Feliks Bitners
Estimating the term…
Waste water resulting from the production of acrylonitrile by gas phase oxidation of propylene and ammonia with oxygen as washing water in the recovery section is purified by treating the waste water with 0.4 to 1 ton of steam per ton of waste water in a detoxification column attached to or following the separation column (for the separation of acetonitrile and acrylonitrile from the waste water in the acrylonitrile process) at a temperature from 100.degree. to 125.degree. C, at a pressure of 0 to 2 (gauge) atmospheres; separating the non-volatile resinous organic compounds from the thus treated waste water in an evaporator and using the vapors from the top of said evaporator to heat the said separation column and detoxification column; and optionally adding an organic amine to said distillation column or to said evaporator.
Process for the purification of waste water from a process for preparing acrylonitrile by the gas phase oxidation of propylene and ammonia with oxygen in admisture with solid catalyst wherein water is used for the separation of acrylonitrile from the reaction mixture, said waste water being substantially free of acrylonitrile, acetonitrile and hydrogen cyanide and containing volatile and toxic and high-boiling and resinous organic compounds, which comprises:
Process for the purifiction of waste water which contains volatile and toxic and high-boiling and resinous organic compounds from a production plant for acrylonitrile by gas-phase oxidation of propylene and ammonia with oxygen in the presence of a solid catalyst, wherein the waste water, in order to remove and destroy the toxic compounds, is treated in a detoxification column having from 7 to 20 distribution baffles which is attached to the lower end of a column for the separation of acetonitrile from the waste water at a temperature of from 100.degree. to 125.degree. C and a pressure of from 0 to 2 atm. gauge with from 0.4 to 1.0 t steam per t of waste water flowing to the detoxification column, and, further, wherein the sump effluent of the detoxification column is passed into an evaporation vessel and substantially evaporated, the vapors are used for heating the detoxification column and the column for separating acetonitrile from the wash water and are discharged into a flowing water system and wherein the resulting aqueous solution in the evaporation vessel is drawn off together with from 1 to 60 wieght percent of high-boiling and resinous organic compounds.
Dependencies are inferred from the claim text.