Process for the manufacture of catalytic elements and catalytic elements so produced

• US 4,895,821 A
• Filed: 08/12/1988
• Issued: 01/23/1990
• Est. Priority Date: 08/14/1987
• Status: Expired due to Fees

• Current Assignee: Didier Engineering GmbH Federal Republic of Germany, Didier-Werke AG Federal Republic of Germany
• Original Assignee: Didier Engineering GmbH, Didier-Werke AG (RHI Magnesita NV)
• Inventors: Merkel, Klaus, Buhler, Eugen, Flockenhaus, Claus, Kainer, Hartmut, Schenelle, Wilfried, Laue, Karl-Heinrich, Grimm, Daniel
• Primary Examiner(s): SHINE, WILLIAM
• Application Number:
  US07/231,716
• Time in Patent Office: 529 Days
• Field of Search: 502/210, 502/213, 502/217, 502/221, 502/222, 502/204, 502/207
• US Class Current: 502/204
• CPC Class Codes: B01D 53/8628 Processes characterised by a specific catalyst
• CPC Class Codes: B01J 23/74 Iron group metals
• CPC Class Codes: B01J 23/862 Iron and chromium
• CPC Class Codes: B01J 27/053 Sulfates

Abstract

This invention relates to a process for the manufacture of catalysts for the reduction of nitrogen oxides in exhaust gases or for chemical air cleaning processes, in which catalyst moldings are produced from iron oxide or mixtures of iron oxide and chromium oxide and/or manganese oxide, which are reduced to grain sizes less than 2 mm, with the use of inorganic binders and sulfuric acid, and with the possible addition of activating additives.

In accordance with the invention:

(a) either the mixture of the solid primary material is reacted with sulfuric acid, a mixture of sulfuric acid and phosphoric acid or a sulfuric acid or mixture of sulfuric acid and phosphoric acid containing sulfate, hydrogen sulfate, phosphate or hydrogen phosphate of ammonium, aluminum, iron, vanadium, manganese, molybdenum, chromium, copper and/or cobalt, and moldings are formed from this mixture, or the mixture of the solid primary material is formed into moldings after the addition of fluid and/or phosphoric acid and/or phosphates, and these moldings are treated with sulfuric acid or a sulfuric acid containing sulfate or hydrogen sulfate of ammonium, aluminum, iron, vanadium, manganese, molybdenum, chromium, copper, and

(b) then, on the moldings obtained in Step (a), a drying treatment is performed at 110° C. to 250° C., followed by a tempering treatment at 250° C. to 600° C.

The catalysts manufactured using the process described by the invention have a low sensitivity to moisture and good activity.

Claims

1. A process for the manufacture of catalytic elements, said process comprising the steps of:

(a) providing a primary catalytic material, said primary catalytic material being a member selected from the group consisting essentially of iron oxide, a mixture of iron oxide and chromium oxide, a mixture of iron oxide and manganese oxide, and a mixture of iron oxide, chromium oxide and manganese oxide and combinations of members of the group;

(b) mixing a binder means with said primary catalytic material for binding said primary catalytic material;

(c) molding said mixed primary catalytic material and binder means produced in said step (b) to produce green catalytic elements;

(d) subjecting said green catalytic elements to a first temperature treatment of 100°

C. to 250°

C. to set said binder means;

(e) treating said catalytic elements obtained from said step (d) with a mixture of sulfuric acid and phosphoric acid; and

(f) subjecting said catalytic elements obtained from said step (e) to a second temperature treatment in the range between about 100°

C. and about 600°

C. to temper said catalytic elements.

2. A process for the manufacture of catalytic elements according to claim 1, wherein at least a portion of said sulfuric acid is replaced by a member selected from the group consisting essentially of a water soluble sulfate, an acid soluble sulfate, ammonium hydrogen sulfate, iron hydrogen sulfate, vanadium hydrogen sulfate, nickel hydrogen sulfate, molybdenum hydrogen sulfate, aluminum hydrogen sulfate, manganese hydrogen sulfate, copper hydrogen sulfate, cobalt hydrogen sulfate, chromium hydrogen sulfate and combinations of members of the group.

3. A process for the manufacture of catalytic elements according to claim 1, wherein at least a portion of said phosphoric acid is replaced by a member selected from the group consisting essentially of a water soluble phosphate, an acid soluble phosphate, ammonium hydrogen phosphate, iron hydrogen phosphate, vanadium hydrogen phosphate, nickel hydrogen phosphate, molybdenum hydrogen phosphate, aluminum hydrogen phosphate, manganese hydrogen phosphate, copper hydrogen phosphate, cobalt hydrogen phosphate, chromium hydrogen phosphate and combinations of members of the group.

4. A process for the manufacture of catalytic elements according to claim 2, wherein at least a portion of said phosphoric acid is replaced by a member selected from the group consisting essentially of a water soluble phosphate, an acid soluble phosphate, ammonium hydrogen phosphate, iron hydrogen phosphate, vanadium hydrogen phosphate, nickel hydrogen phosphate, molybdenum hydrogen phosphate, aluminum hydrogen phosphate, manganese hydrogen phosphate, copper hydrogen phosphate, cobalt hydrogen phosphate, chromium hydrogen phosphate and combinations of members of the group.

5. A process for the manufacture of catalytic elements according to claim 1, wherein said mixture comprising sulfuric acid and phosphoric acid with which said catalytic elements are treated in said step (e) has at least one ratio of:

SO₄^-2 to PO₄^-3 ;

HSO₄^- to HPO₄^-2 ; and

HSO₄^- to H₂ PO₄^- ;

which lies within the range of from 100;

1 to 1;

100.

6. A process for the manufacture of catalytic elements according to claim 5, wherein said at least one ratio is within the range of from 10:

1 to 1;

10.

7. A process for the manufacture of catalytic elements according to claim 4, wherein said mixture comprising sulfuric acid and phosphoric acid with which said catalytic elements are treated in said step (e) has at least one ratio of:

SO₄^-2 to PO₄^-3 ;

HSO₄^- to HPO₄^-2 ; and

HSO₄^- to H₂ PO₄^- ;

which lies within the range of from 100;

1 to 1;

100.

8. A process for the manufacture of catalytic elements according to claim 7, wherein said at least one ratio is within the range of from 10:

1 to 1;

10.

9. A process for the manufacture of catalytic elements according to claim 1, wherein said first temperature treatment in said step (d) is carried out in a first temperature range of from about 100°

C. to about 250°

C., and wherein said second temperature treatment of said step (f) is carried out in a second temperature range of from about 250°

C. to about 600°

C.

10. A process for the manufacture of catalytic elements according to claim 9, wherein said second temperature treatment is carried out so as to have a maximum temperature of between about 350°

C. and about 450°

C.

11. A process for the manufacture of catalytic elements according to claim 10, wherein, during said second temperature treatment, the temperature to which said catalytic elements are subjected is elevated at a rate of between about 5°

C./h and about 200°

C./h.

12. A process for the manufacture of catalytic elements according to claim 1, wherein said binder means comprises an inorganic binder, said inorganic binder being a member selected from the group consisting essentially of alumina, kaolin, an aluminaceous compound, a magnesium compound, a calcium compound, a cement, particulate SiO₂ and combinations of members of the group.

13. A process for the manufacture of catalytic elements according to claim 12, additionally comprising the further step of adding to said primary catalytic material an additive to increase the binding effect of said binder means, said additive being a member selected from the group consisting essentially of olivine, talcum, particulate SiO₂, magnesium hydroxide, aluminum hydroxide, iron hydroxide, calcium hydroxide, magnesium carbonate, aluminum carbonate, iron carbonate, calcium carbonate, magnesium hydrogen carbonate, aluminum hydrogen carbonate, iron hydrogen carbonate, calcium hydrogen carbonate and combinations of members of the group.

14. A process for the manufacture of catalytic elements according to claim 1, wherein said iron oxide, chromium oxide and manganese oxide have grain sizes smaller than about 0.2 mm and further comprising the step of mixing an activating additive with at least one of said primary catalytic material provided in said step (a) and said mixture of said primary catalytic material and said binder means produced in said step (b), said activating additive being a member selected from the group consisting essentially of an element, an oxide and a salt, said element being a member selected from the group consisting essentially of vanadium, copper, cobalt, uranium, tungsten, nickel, molybdenum, manganese, tin, zinc, beryllium, boron, yttrium, niobium, antimony, zirconium, bismuth, silver and rare earth elements, said oxide being an oxide of a member selected from the group consisting essentially of vanadium, copper, cobalt, uranium, tungsten, nickel, molybdenum, manganese, tin, zinc, beryllium, boron, yttrium, niobium, antimony, zirconium, bismuth, silver and rare earth elements, and said salt being a salt of a member selected from the group consisting essentially of vanadium, copper, cobalt, uranium, tungsten, nickel, molybdenum, manganese, tin, zinc, beryllium, boron, yttrium, niobium, antimony, zirconium, bismuth, silver and rare earth elements.

15. A process for the manufacture of catalytic elements according to claim 14, wherein said iron oxide, chromium oxide and manganese oxide have grain sizes smaller than about 0.09 mm.

16. A process for the manufacture of catalytic elements according to claim 1, further comprising the step of following said first temperature treatment and prior to said second temperature treatment, soaking said catalytic elements with a solution comprising aluminum hydroxide chloride.

17. A process for the manufacture of catalytic elements according to claim 1, wherein said second temperature treatment of said step (f) to temper said catalytic elements is conducted in a reduced O₂ content atmosphere of about 0.05 to about 10 vol.-% O₂.

18. A process for the manufacture of catalytic elements according to claim 17, wherein said reduced O₂ -content atmosphere is of about 2 to about 4 vol.-% O₂.

19. A process for the manufacture of catalytic elements according to claim 1, wherein said binder means of said step (b) is a member selected from the group consisting essentially of organic binders, inorganic binders and combinations of members of the group.

20. A process for the manufacture of catalytic elements according to claim 19, wherein said organic binders comprise a member selected from the group consisting essentially of powder resins, furan resins, modified furfuryl alcohol resins, phenol formaldehyde resins and combinations of members of the group.

21. A process for the manufacture of catalytic elements according to claim 1, wherein said treatment of said catalytic elements with sulfuric acid and phosphoric acid of said step (e) comprises a simultaneous treatment of said catalytic elements with a mixture of said sulfuric acid and said phosphoric acid.

22. A process for the manufacture of catalytic elements according to claim 1, wherein said treatment of said catalytic elements with said sulfuric acid and said phosphoric acid of said step (e) comprises an initial treatment of said catalytic elements with said sulfuric acid followed by a subsequent treatment with said phosphoric acid.

23. A process for the manufacture of catalytic elements according to claim 1, wherein said treatment of said catalytic elements with said sulfuric acid and said phosphoric acid of said step (e) comprises an initial treatment of said catalytic elements with said phosphoric acid followed by a subsequent treatment with said sulfuric acid.

24. A catalyst for the reduction of nitrogen oxides manufactured according to the process of claim 1.