Process for preparing hydrocyanic acid by catalytic dehydration of gaseous formamide—direct heating

Patent metadata

Field	Value
Publication number	US-9034293-B2
Application number	US-93584009-A
Country	US
Kind code	B2
Filing date	Mar 30, 2009
Priority date	Mar 31, 2008
Publication date	May 19, 2015
Grant date	May 19, 2015

Abstract

Process for preparing hydrocyanic acid by catalytic dehydration of gaseous formamide, wherein the dehydration of formamide is coupled with an exothermic reaction by the reactor used in the dehydration comprising two separate fluid paths which are separated by a common reactor wall, with one fluid path being provided for the dehydration of formamide and the second fluid path being provided for the exothermic reaction.

First claim

The invention claimed is:

1. A process for preparing hydrocyanic acid, comprising:
dehydrating gaseous formamide at temperatures of from 350 to 650° C. in the presence of a catalyst and 0.1 to 10 mol % oxygen in a reactor, and
coupling the dehydration of the gaseous formamide with an exothermic reaction in the reactor,
wherein the coupling of the dehydration and the exothermic reaction comprises two separate fluid paths separated by a common reactor wall in the reactor, with one fluid path being provided for the dehydration of formamide and the second fluid path being provided for the exothermic reaction and a specific thermal conductivity λ of the common reactor wall material is greater than 100 W/(mK),
wherein
the exothermic reaction is a catalytic combustion of combustible gases with introduction of oxygen, and
the reactor is a tube reactor or plate reactor comprising at least two parallel, superposed layers A and B, with the layer A having at least two parallel reaction channels in which the catalytic dehydration occurs and the layer B having at least two parallel channels in which the exothermic reaction occurs, and
the common reactor wall separating the fluid paths comprises a material selected from the group consisting of copper, silver, aluminum, magnesium and oxidation-resistant silicon-infiltrated silicon carbide.

2. The process according to claim 1 , wherein a side of the common reactor wall which is in contact with the combustible gas has a catalytically active coating.

3. The process according to claim 2 , wherein the catalytically active coating is selected from the group consisting of Pt, Pd, Ag, and Au, alloys comprising Pt, Pd, Ag, and Au, oxides selected from the group consisting of MgO, CoO, MoO 3 , NiO, ZnO, Cr 2 O 3 , WO 3 , SnO, CuO/Cu 2 O, MnO 2 and V 2 O 5 , mixed oxides selected from the group consisting of CuO—ZnO—Al 2 O 3 , CoO—MgO, CoO—La 2 O 3 , La 2 CuO 4 , Nd 2 CuO 4 , and Co—ZnONiO—MoO 3 , perovskites selected from the group consisting of LaMnO 3 , CoTiO 3 , LaTiO 3 and CoNiO 3 and spinels selected from the group consisting of CuAl 2 O 4 , MgAl 2 O 4 , (Cu, Zn)Al 2 O 4 , (Cu, Zn, Ba)Al 2 O 4 , (Cu, Zn, Mg)Al 2 O 2 , (Cu, Zn, Va) Al 2 O 4 and LaNiO 4 .

4. The process according to claim 1 , wherein the oxygen is introduced into the combustible gas or the combustible gas is introduced into the oxygen at a plurality of points along the fluid path for the exothermic reaction.

5. The process according to claim 1 , wherein the catalytic dehydration is carried out at a pressure of from 100 mbar to 4 bar.

6. The process according to claim 1 , wherein the catalytic dehydration is carried out at a length-specific space velocity of formamide of from 0.02 to 0.4 kg/(mh) in a region of laminar flow of the dehydration fluid path.

7. The process according to claim 1 , wherein the content of oxygen is from 0.5 to 3 mol %.

8. The process according to claim 1 , wherein
the catalytic dehydration is carried out in the presence of:
1) shaped bodies selected from the group consisting of highly sintered shaped bodies made up of aluminum oxide, highly sintered shaped bodies made up of aluminum oxide and silicon oxide and shaped chromium-nickel stainless steel bodies;
2) packings composed of steel or iron oxide on porous support materials or
3) a catalytically active coating on the side of the common reactor wall which is in contact with the formamide.

9. The process according to claim 1 , wherein the at least two parallel reaction channels of the layer A have an average hydraulic diameter of from 1 to 6 mm, and the at least two parallel channels of the layer B have an average hydraulic diameter of less than 4 mm.

10. The process according to claim 1 , wherein the fluid path for the dehydration of formamide and the fluid path for the exothermic reaction each have a length of from 2 to 100 cm.

Assignees

• Boehling Ralf
• Deckers Andreas
• Gritsch Achim
• Kotrel Stefan
• Basf Se

Inventors

• Boehling Ralf
• Deckers Andreas
• Gritsch Achim
• Kotrel Stefan

Classifications

• B01J2219/2474

  Mixing means, e.g. fins or baffles attached to the plates · CPC title

• C01C3/02

  Preparation, {separation or purification} of hydrogen cyanide {(C01C3/001 takes precedence)} · CPC title

• C01C3/0204 Primary

  from formamide or from ammonium formate · CPC title

• B01J2219/2481

  Catalysts in granular from between plates · CPC title

• B01J2219/2465

  Two reactions in indirect heat exchange with each other · CPC title