IP Library Granted Patent US 9,181,178
Granted Patent B2
US 9,181,178 · App. 14/381,047 · Granted Nov 10, 2015

Method for producing acrylonitrile

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 9,181,178
App. No.
14/381,047
Granted
Nov 10, 2015
Kind
B2
Abstract

The invention relates to a method for producing acrylonitrile which includes a vapor phase catalytic ammoxidation process of performing vapor phase catalytic ammoxidation by bringing a source gas containing propylene, molecular oxygen, and ammonia into contact with a fluidized bed catalyst to obtain acrylonitrile. The method is characterized in that the fluidized bed catalyst is a catalyst containing iron, antimony, and tellurium, and the vapor phase catalytic ammoxidation process is performed while maintaining an adsorbed amount of ammonia per specific surface area (m 2 /g) of the fluidized bed catalyst in the range of 0.01 to 0.22 μmol/m 2 . According to the method for producing acrylonitrile of the invention, it is possible to stably maintain a high acrylonitrile yield over a long period of time.

Claims (6)

1. A method for producing acrylonitrile, the method comprising a vapor phase catalytic ammoxidation process of performing vapor phase catalytic ammoxidation by bringing a source gas containing propylene, molecular oxygen, and ammonia into contact with a fluidized bed catalyst to obtain acrylonitrile,

wherein the fluidized bed catalyst is a catalyst containing iron, antimony, and tellurium, and

the vapor phase catalytic ammoxidation process is performed while maintaining an adsorbed amount of ammonia per specific surface area (m 2 /g) of the fluidized bed catalyst in the range of 0.01 to 0.22 μmol/m 2 .

2. The method for producing acrylonitrile according to claim 1 , wherein the fluidized bed catalyst is represented by the following Formula (1);

Fe 10 Sb a A b Te c D d E e O x .(SiO 2 ) y   (1)

(in Formula (1), Fe, Sb, Te, O, and SiO 2 represent iron, antimony, tellurium, oxygen, and silica, respectively, A represents at least one kind of element selected from the group consisting of vanadium, molybdenum, and tungsten, D represents at least one kind of element selected from the group consisting of magnesium, calcium, strontium, barium, titanium, zirconium, niobium, chromium, manganese, cobalt, nickel, copper, silver, zinc, boron, aluminum, gallium, indium, thallium, germanium, tin, lead, phosphorus, arsenic, and bismuth, E represents at least one kind of element selected from the group consisting of lithium, sodium, potassium, rubidium, and cesium, and a, b, c, d, e, x, and y represent an atomic ratio and a is 3 to 100, b is 0.1 to 5, c is 0.1 to 10, d is 0 to 50, e is 0 to 5, y is 10 to 200, and x is a number of oxygen atom required to satisfy a valence of each of the components except silica; However, b, d, and e represent a sum of an atomic ratio of each element in a case in which A, D, and E contain two or more kinds of elements).

Assignments (2)
CHANGE OF NAME Recorded Sep 5, 2017
From: MITSUBISHI RAYON CO., LTD.
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 043750/0834 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 26, 2014
From: WATANABE, HIROKAZU; YANAGITA, MOTOO; KARASUDA, TAKASHI; NISHIDA, KAZUFUMI; MIYAKI, KENICHI
To: MITSUBISHI RAYON CO., LTD.
Reel/Frame 033610/0796 →