US20010018400A1

US20010018400A1 - Completely metallic oxidation catalyst

Info

Publication number: US20010018400A1
Application number: US09/230,466
Authority: US
Inventors: Wilfried Herda; Ulrich Heubner; Jurgen Koppe; Hartmus Lausch
Original assignee: Wilfred Herda
Current assignee: WILFRED HERDA
Priority date: 1996-07-26
Filing date: 1997-07-23
Publication date: 2001-08-30
Anticipated expiration: 2017-07-23
Also published as: CA2262883A1; CN1103247C; US6274532B1; JP2000515805A; EP0914207A1; WO1998004347A1; AU4115697A; CN1226190A; EP0914207B1; DE19630250C1; DE59703442D1; AU720058B2; KR20000029572A; AU1741699A; ATE200744T1

Abstract

A completely metallic catalyst for the oxidation of mixtures in the gaseous phase which contain carbon monoxide, hydrocarbons and/or soot, has a surface doped with a metallic element and is subjected to a second thermal treatment in an oxygen-containing atmosphere.

Description

The invention relates to a completely-metallic catalyst for the oxidation of mixtures containing carbon monoxide and/or hydrocarbons and/or soot in the gaseous phase, as defined in the preamble to claim 1.

DE 44 16 469 C1 discloses a completely-metallic oxidation catalyst that contains nickel, manganese, chromium and iron and is used in the total oxidation of hydrocarbons into carbon dioxide and water. This catalyst is produced from an alloy, which contains (in mass percent) 10 to 50% nickel, up to 50% copper, up to 10% manganese, 10 to 30% chromium and up to 50% iron, through thermal treatment in an oxygen-containing atmosphere for a period of 0.25 to 10 hours at temperatures of 400 to 1000° C. A reduction with a hydrocarbon-containing mixture can follow this oxidizing thermal treatment.

A disadvantage of this and other known oxidation catalysts is that they do not oxidize the organic components in gas flows below 400° C., and soot particles in particular are not oxidized in the temperature range below 500° C.

Thus, in the presence of soot particles, the danger exists that the catalyst surface will be covered by soot particles at relatively-low working temperatures below 500° C. such that they no longer have a catalytic effect. This is inevitably the case when an exhaust-gas catalyst is not used in the optimum working and temperature range, for example during the startup phase of motor-vehicle diesel catalysts. For these and numerous other applications, it is preferable for the catalyst to already have a catalytic effect in the relatively “cold” phase, i.e., at temperatures of up to 300° C.

It is the object of the invention to provide an effective catalyst for the total oxidation of gas mixtures containing hydrocarbons and/or soot, the catalyst being simple to produce and easy to dispose of, already having a catalytic effect in a low temperature range, being regenerable with little effort, and simultaneously possessing a high thermal conductivity.

This object is accomplished by the features in the characterizing portion of claim 1.

Advantageous embodiments of the invention are characterized in the dependent claims.

The catalyst can be used in wire or chip form, or any other form having a sufficiently-large specific surface.

The catalyst of the invention makes use of a layer that adheres well and has a high degree of catalytic effectiveness, and has a high catalytic activity and a high thermal conductivity.

In the catalysts of the invention, a possible drop in the catalytic activity—possibly following a mechanical, chemical or physical-chemical cleaning of the surface—can be eliminated through a repeated thermal treatment followed by another treatment with an aqueous solution containing oxidizable, organic substances, e.g. sugar, starch, latex, polyacrylate and/or polyvinyl alcohol, and another modification with at least one of the following elements: boron, aluminum, indium, germanium, tin, lead, scandium, yttrium, lanthanum, titanium, zirconium, vanadium, niobium, chromium, molybdenum, tungsten, manganese, technetium, rhenium, iron, cobalt, nickel, copper, cerium, praseodymium and neodymium in the above-described manner.

The consumed, and no longer regenerable, catalyst is melted and processed again into the catalyst of the invention.

The invention is explained by the following examples (all values in mass percent).

EXAMPLES

Respectively 2.0 g catalyst in wire form having a diameter of 0.25 mm were placed in a tubular reactor. The experiments were performed at different temperatures and with a pressure of 1 bar under the following loads: 10 Nl/h air with 5,000 ppm of one of the following hydrocarbons.



			Conv.
			to CO₂
		T	and H₂O
Hydrocarbon	Catalyst	[° C.]	[%]

Example 1:	An alloy comprising 56.6% Fe, 16.5%	350	100
n-hexane	Cr, 24.2% Mn, 1.0% Mo, 0.8% Cu,
	0.40% N, remainder Ni, Ti, Nb, Al,
	C, P, was annealed for 1 hr at 875°
	C. with air. After cooling, the
	alloy was placed in 10 ml of an
	aqueous solution containing 1.5%
	polyvinyl alcohol, 50 g/l Cu²⁺ ions
	and 10 mg/l Mn²⁺ ions for 15 min.,
	removed and annealed again for 1 hr
	at 450° C. in air.
Example 2:	An alloy comprising 71.8% Mn,	350	100
benzene	17.55% Cu, 10.4% Ni, 0.1% Fe, 0.04%
	Si, 0.009% S and 0.017% C was
	annealed for 1.5 hrs at 650° C. in
	an air-containing environment.
	After cooling, the alloy was placed
	in an aqueous solution containing
	2% starch and 200 g/l Cu²⁺ ions for
	15 min., removed and annealed again
	for 1 hr at 500° C. in air.
Example 3:	An alloy comprising 71.8% Mn,	300	92
n-hexane	17.55% Cu, 10.4% Ni, 0.1% Fe, 0.04%
	Si, 0.009% S and 0.017% C was
	annealed for 1.5 hrs at 650° C. in
	an air-containing environment.
	After cooling, the alloy was placed
	in an aqueous solution containing 2
	g/l Cu²⁺ ions for 10 min., then in
	a 2% polyvinyl-alcohol solution,
	removed and annealed again for 1 hr
	at 500° C. in air.
Example 4:	An alloy comprising 53.72% Fe,	350	100
toluene	24.2% Cr, 17.7% Ni, 6.14% Mn, 4.34%
	Mo, 0.53% Cu, 0.17% Nb, 0.12% Al,
	0.46% N, 0.004% S, 0.012% C and
	0.017% P was annealed for 2 hrs at
	900° C. with air. After cooling,
	the alloy was placed in 10 ml of an
	aqueous solution containing 1%
	polyvinyl alcohol, 100 g/l Fe³⁺
	ions, 100 g/l Cu²⁺ ions and 2 g/l
	Mo⁶⁺ ions for 10 min., removed and
	annealed again for 1 hr at 700° C.
	in air.
Example 5:	An alloy comprising 50.85% Co,	325	100
n-hexane	19.95% Cr, 14.8% W, 2.28% Fe, 1.53%
	Mn, 0.096% C, 0.004% S and 0.006% p
	was annealed for 0.45 hr at 1000° C.
	with air. After cooling, the alloy
	was placed in 10 ml of a 5% aqueous
	crystallized-sugar solution for 3
	min., then placed in a solution
	containing 150 g/l Cu²⁺ ions, 5 g/l
	W⁶⁺ ions and 25 g/l Co²⁺ ions,
	removed and annealed again for 1 hr
	at 725° C. in air.
Example 6:	An alloy comprising 68.01% Cu,	385	94
n-hexane	30.6% Ni, 0.70% Fe, 0.67% Mn,
	0.008% C, 0.010% Zn, 0.004% S and
	0.002% P was annealed for 1.2 hrs
	at 875° C. with air. After cooling,
	the alloy was placed in 10 ml of an
	aqueous solution containing 5%
	crystallized sugar, 0.5% polyvinyl
	and 20 g/l Cu²⁺ ions for 2 minutes,
	removed and annealed again for 1 hr
	at 725° C. in air.
Example 7:	An alloy comprising 37.3% Ni,	315	96
n-hexane	35.73% Fe, 19.45% Cr, 3.2% Cu,
	2.33% Mo, 1.51% Mn, 0.2% Nb,
	0.26% Si, 0.015% P, 0.006% C and
	0.003% S was annealed for 2 hrs at
	910° C. with air. After cooling, the
	alloy was placed in a 1% aqueous
	polyvinyl-alcohol solution for 2.5
	min., then placed in a solution
	containing 150 gIl Cu²⁺ ions,
	removed and annealed again for 1 hr
	at 880° C. in air.
Example 8:	An alloy comprising 61.05% Ni,	375	85
n-hexane	22.5% Cr, 15.3% Mo, 0.68% Fe, 0.26%
	Al, 0.14% Mn, 0.03% Co, 0.006% C,
	0.004% P and 0.002% S was annealed
	for 1 hr at 880° C. with air. After
	cooling, the alloy was placed in a
	solution containing 1.3% polyvinyl
	alcohol, 100 g/l Cu²⁺ ions and 5
	g/l V⁴⁺ ions for 4 min., removed
	and annealed again for 1 hr at 450°
	C. in air.
Example 9:	An alloy comprising 45.64% Fe,	370	80
n-hexane	24.7% Ni, 20.9% Cr, 6.43% Mo, 0.90%
	Cu, 0.89% Mn, 0.192% N, 0.017% P,
	0.006% C and 0.003% S was annealed
	for 0.5 hr at 1010° C. with air.
	After cooling, the alloy was placed
	in an aqueous solution containing
	1.5% starch and 0.2% polyvinyl
	alcohol for 3 min., then in a
	solution containing 10 g/l Cu²⁺
	ions, 1 g/l W⁶⁺ ions, 1 g/l Al ions
	and 1 g/l Mn²⁺ ions, removed and
	annealed again for 1.5 hrs at 460°
	C. in air.
Example 10:	An alloy comprising 32.08% Fe,	385	95
n-hexane	31.3% Ni, 26.85% Cr, 1.54% Mn,
	1.34% Cu, 0.202% N, 0.015% P, 0.01%
	C and 0.003% S was annealed for 2
	hrs at 825° C. with air. After
	cooling, the alloy was placed in 10
	ml of a solution containing 1.5%
	polyvinyl alcohol, 60 g/l Cu²⁺ ions
	and 10 g/l Ni²⁺ ions for 2 min.,
	removed and annealed again for 0.5
	hr in air.

Claims

1. A completely-metallic catalyst for the oxidization of mixtures containing carbon monoxide and/or hydrocarbons and/or soot in the gaseous phase, the catalyst being obtainable through an oxidizing thermal treatment of an alloy that may contain manganese, nickel, copper, chromium and iron in an oxygen-containing atmosphere at a temperature of 250 to 1250° C. for 0.05 to 5 hours, and a subsequent treatment with an oxidizable, organic substance, characterized in that an alloy containing at least three of the following elements: manganese, nickel, copper, cobalt, chromium, molybdenum, tungsten, titanium, zirconium, vanadium, niobium, aluminum and iron with a total content of at least 95 mass percent, and up to 5 mass percent of P, N, Si and S and other typical contaminations, the alloy being subjected to an oxidizing thermal treatment in an oxygen-containing atmosphere; after cooling, the alloy is treated with an aqueous solution or emulsion containing an oxidizable, organic substance, with the surface and/or regions near the surface of the alloy being doped with one of the following elements: boron, aluminum, indium, germanium, tin, lead, scandium, yttrium, lanthanum, titanium, zirconium, vanadium, niobium, chromium, molybdenum, tungsten, manganese, technetium, rhenium, iron, cobalt, nickel, copper, cerium, praseodymium or neodymium; and the alloy is subsequently subjected to a second thermal treatment in an oxygen-containing atmosphere over a period of 5 min. to 3 hrs at a temperature of 250 to 1250° C.

2. The completely-metallic catalyst according to

claim 1

, characterized in that the elements of the aqueous solution or emulsion used to dope the surface and/or the regions near the surface of the alloy are added in a concentration that corresponds at the maximum to the saturation concentration of the metallic compound.

3. The completely-metallic catalyst according to

claim 1

, characterized in that the elements used to dope the surface and/or the regions near the surface of the alloy are applied prior to the treatment with the aqueous solution or emulsion, or after the treatment with the aqueous solution or emulsion, in an intermediate thermal treatment in a temperature range of 30 to 1250° C.