IP Library Granted Patent US 7,109,382
Granted Patent B2
US 7,109,382 · App. 10/312,520 · Granted Sep 19, 2006

Method for the production of formaldehyde

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 7,109,382
App. No.
10/312,520
Granted
Sep 19, 2006
Kind
B2
Abstract

A method for formaldehyde production through catalytic oxidation of methanol, comprising the steps of feeding to a first oxidation catalytic bed ( 2 ) a gas flow comprising methanol and oxygen at a predetermined crossing linear flow rate, obtaining at the outlet of said first catalytic bed ( 2 ) a flow of gaseous reaction products comprising unreacted methanol, and feeding the flow of gaseous products to a second oxidation catalytic bed ( 6 ) is distinguished by the fact that the flow of gaseous reaction products comprising unreacted methanol is fed to the second catalytic bed ( 6 ) with a crossing linear flow rate substantially equal to said predetermined first catalytic bed ( 2 ) feeding flow rate.

Claims (6)

1. A method for the production of formaldehyde through catalytic oxidation of methanol, comprising the steps of:

feeding to a first oxidation catalytic bed a gas flow comprising methanol and oxygen at a predetermined crossing linear flow velocity, obtaining at the outlet of said first catalytic bed a flow of gaseous reaction products comprising unreacted methanol; and

feeding said flow of gaseous products to a second oxidation catalytic bed;

wherein said flow of gaseous reaction products comprising unreacted methanol is fed to said second catalytic bed with a crossing linear flow velocity substantially equal to said predetermined first catalytic bed feeding flow velocity.

2. The method according to claim 1 , wherein said gaseous reaction products fed to said second catalytic bed have a temperature that is controlled in a temperature range comprised between 200 and 300 C.

3. The method according to claim 2 , wherein said temperature range is comprised between 210 and 260 C.

Assignments (2)
MERGER Recorded Dec 4, 2014
From: AMMONIA CASALE SA; UREA CASALE SA; METHANOL CASALE SA; CASALE CHEMICALS SA
To: CASALE SA
Reel/Frame 034533/0456 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 4, 2003
From: SIOLI, GIANCARLO
To: CASALE CHEMICALS S.A.
Reel/Frame 013850/0213 →