Process for manufacturing a carbon catalyst

Details Process for manufacturing a carbon catalyst Process for manufacturing a carbon catalyst

1989-10-24

1991-11-12

Konopka, Paul E.

Catalyst, solid sorbent, or support therefor: product or process

Catalyst or precursor therefor

Inorganic carbon containing

264 295, 423239, 502430, 502432, 502434, B01J 2118, B01J 2020, C01B 3110, B01D 5336

Patent

active

050648012

DESCRIPTION:

BRIEF SUMMARY
The invention relates to a process for the manufacturing a carbon catalyst for use in the NO.sub.x reduction with ammonia, wherein ground and oxidized hard coal mixed with binders is molded, carbonized at temperatures between 700.degree. and 900.degree. C. and subsequently activated with steam.
It is known from the German open application124 33 076 that activated carbons act as catalysts in the reduction of-nitrogen oxide with the use of ammonia.
In the German open application 35 12 168 it is disclosed that activated cokes, which have not been subjected to steam activation, have a better catalytic action in the reduction of nitrogen oxides with ammonia. But even with the use of activated coke, the NO-conversion is still comparatively low.
It is the object of the invention to produce a carbon catalyst which has an improved catalytic activity, and thus a higher degree of NO-conversion.
This object is attained by subjecting activated cokes to an activation treatment with steam at temperatures between 800.degree. and 850.degree. C. and a dwelling time of 45 to 100 minutes, until an activation degree of 5 to 15% is reached. The activation degree is defined as the rate of the carbon weight loss percentage to the weight of the initial material. This because in tests it has been surprisingly established that such carbon catalysts have a higher NO.sub.x -conversion, than non-activated active cokes and than activated carbons with an activation degree of over 15%.
The carbon catalysts produced this way have -a mean random reflectance R.sub.r between 4.5 and 5.5%. The determination of the mean random reflectance (mean random reflectance) R.sub.r (%) of coal and carbon catalysts is performed with a "T.A.S." of the Firm Leitz in agreement with DIN 22 020 (T.A.S.=Texture Analysis System). Thereby, it is a matter of the arithmetic mean of the mean random reflectance of the randomly cut mirror-finished catalysts particles which are bound in a synthetic resin.
Considered in this determination were 250 image areas, each having 512 times 512 image points. This results in a total of over 65 Million individual values determining the reflectance distribution. From there, the arithmetic mean of the mean random reflectance R.sub.r (%) is calculated. This method is normally used in coal petrography. The process wherein the originally sedimentated vegetable matter is transformed via peat coal into brown coal and hard coal is called carbonization. The carbonization degree is not a directly measurable value. Therefore, a certain physical or chemical property has to be measured which during the carbonization process changes constantly, e.g. the reflectance degree of the vitrain.
Surprisingly, it has been proven that also the pregraphitic crystal structure of the carbon catalysts can be closer characterized due to this method. It has been found that carbon catalysts with a mean random reflectance of 4.5 to 5.5% have a particularly strong catalytic activity so that particularly favorable NO.sub.x -conversions can be achieved therewith and which are superior to the conversions obtained with non-activated active coke or activated carbon.


EXAMPLE

An activated coke is produced in the known manner, molding ground and oxidized hard coal mixed with binders, and carbonizing them at temperatures between 700.degree. and 900.degree. C. This activated coke is subsequently activated in a fluidized bed with steam at temperatures between 800.degree. and 900.degree. C. The dwelling times and the temperatures depending on the activation degree are indicated in the following Table 1.


TABLE 1 ______________________________________ dwelling time temperature activation degree (min) (.degree.C.) (%) ______________________________________ 45 800 5.0 80 800 9.0 80 850 12.0 100 850 15.0 30 900 19.0 70 900 50.0 90 900 65.0 ______________________________________
The carbon catalysts produced according to the example are tested as to their catalytic activity in the reduction of NO.sub.x with ammonia in a reactor with a diameter of

REFERENCES:
patent: 3623999 (1971-11-01), Jungten et al.
patent: 4124529 (1978-11-01), Jungten et al.
A Dictionary of Mining, Mineral and Related Terms, Paul W. Thrush, U.S. Department of the Interior, p. 526 (1968).
Ullmanns Encyclopedia of Technical Chemistry, vol. 14, pp. 126-129, 296-297, 620-623 (1977).

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