Chemistry of inorganic compounds – Oxygen or compound thereof – Metal containing
Reexamination Certificate
2000-02-29
2003-12-16
Silverman, Stanley S. (Department: 1754)
Chemistry of inorganic compounds
Oxygen or compound thereof
Metal containing
Reexamination Certificate
active
06663844
ABSTRACT:
SPECIFICATION
The present invention relates to shaped materials useful as catalyst for preparing cyclic lactams by reacting aminocarbonitriles with water, said shaped materials essentially comprising titanium dioxide.
DE-B 25 54 198 discloses shaped titanium dioxide articles obtained by shaping titanium dioxide and calcining the shaped articles at 300 to 800° C., the titanium dioxide being prepared by hydrolysis of a titanium salt and being treated, before or after said shaping, with from 0.01 to 50% by weight, based on titanium dioxide, of a mineral acid or of an organic acid.
However, such shaped articles have the disadvantage that titanium dioxide prepared by hydrolysis is insufficiently pure for catalytic purposes. This leads to losses in yield and selectivity in reactions where such shaped articles are used as catalyst.
DE-C 32 17 751 discloses moldings useful as catalyst which are up to 99% by weight pyrogenic titanium dioxide, have an SiO
2
content of from 0 to 1% by weight, accessible pore volume of 45-55% of the volume of the molding and a breaking strength of not less than 1.630 N. Such moldings have the disadvantage that their preparation requires the use of a molding aid, sieving of the mixture and conversion of the sieved mixture into a flowable powder in order that tablets may be produced with the aid of a tableting press. Pyrogenic titanium dixoide is produced by high temperature hydrolysis of a vaporizable titanium compound, normally titanium tetrachloride, in a detonating gas (mixture of hydrogen and oxygen gas) flame.
It is an object of the present invention to provide shaped materials comprising titanium dioxide as essential constituent which are useful as catalyst, which do not have the disadvantages mentioned and which can be produced in a technically simple and economical manner.
We have found that this object is achieved by shaped materials which are useful as catalyst and which have no soluble constituents under the reaction conditions, comprising pyrogenic titanium dioxide as essential constituent, said shaped materials being obtainable by shaping the pyrogenic titanium dioxide into shaped articles and, before or after said shaping, treating the pyrogenic titanium dioxide with from 0.1 to 30% by weight, based on the pyrogenic titanium dioxide, of an acid in which pyrogenic titanium dioxide is sparingly soluble.
The pyrogenic titanium dioxide can be present in various modifications such as amorphous, as anatase or as rutile or phase mixtures thereof.
The aforementioned titanium dioxide can be doped with, or comprise, compounds of main groups 1 to 7, especially 2, 3 or 4, of the periodic table, alumina, such as alpha- or gamma-alumina, or tin oxide, of transition groups 1 to 7 of the periodic table, of the elements of the iron group or of the lanthanides, preferably cerium oxide, or actinides and also mixtures thereof.
If desired, these catalysts may comprise up to 50% by weight in each case of copper, tin, zinc, manganese, iron, cobalt, nickel, ruthenium, palladium, platinum, silver or rhodium.
These catalytically active oxides are preparable in a conventional manner, for example by hydrolysis of the corresponding organics, alkoxides, salts with organic or inorganic acids and subsequent heating or calcining and also pyrogenically and are generally commercially available.
According to the invention, the oxides are treated with an acid before or after shaping. Suitable acids include organic acids such as oxalic acid, propionic acid, butyric acid, maleic acid or inorganic acids such as isopolyacids, heteropolyacids, sulfuric acid or hydrochloric acid. Particularly suitable catalysts are obtainable by treatment with acetic acid, formic acid, nitric acid, especially phosphoric acid.
It is also possible to use mixtures of acids.
The treatment can be carried out continuously or batchwise in one or more stages. The individual stages can be carried out with the same acid, different acids or identical or different mixtures of acids.
Similarly, the oxides can be treated with an acid in the form mentioned before and after shaping.
Preferably, the oxides are treated with an acid before shaping.
The amount of acid used according to the invention is from 0.1 to 30%, preferably from 0.1 to 10%, especially from 0.1 to 5%, by weight, reckoned as pure acid, based on pyrogenic titanium dioxide. The acid can be mixed with a liquid diluent, such as water.
The catalysts can be prepared from the oxides without additives. It is similarly possible to add additives such as binders, for example titanium dioxide sols, salts of the oxides used, soluble titanium salt compounds, hydrolyzable titanium compounds such as titanium alkoxides or aluminum salts, such as pore-formers, for example methylcellulose, carbon fibers, fibers of organic polymers, melamine, starch powder, preferably before shaping.
The shaped articles can be present in various forms, for example as ball, tablet, cylinder, hollow cylinder, pellet, granule or strand. Such shaped articles are preparable in a conventional manner using appropriate shaping machines such as tableting machines, extruders, rotary granulators, pelletizers or combinations thereof.
The shaped material, if desired after an acid treatment, is advantageously dried, especially at from 20 to 120° C., preferably in an inert gas atmosphere or in the air, and then calcined, especially at from 400-750° C., preferably in an inert gas atmosphere or in the air.
The shaped materials can advantageously be used as catalyst for preparing cyclic lactams by reacting aminocarbonitriles with water in the liquid phase in a fixed bed reactor.
To this end, the heterogeneous catalysts can be arranged in a fixed bed. The reaction can take place in a conventional manner, for example in a downflow or preferably upflow mode, especially continuously, by bringing the reaction mixture into contact with the catalyst bed.
The starting materials used in the process of the present invention are aminocarbonitriles, preferably those of the general formula I
where n and m are each 0, 1, 2, 3, 4, 5, 6, 7, 8 or 9 and n+m totals at least 3, preferably at least 4.
R
1
and R
2
can in principle be substituents of any type. It is merely necessary to ensure that the desired cyclization reaction is not affected by the substituents. Preferably, R
1
and R
2
are independently C
1
-C
6
-alkyl or C
5
-C
7
-cycloalkyl or C
6
-C
12
-aryl.
Particularly preferred starting compounds are aminocarbonitriles of the general formula
H
2
N—(CH
2
)
m
—C≡N
where m is 3, 4, 5 or 6, especially 5. When m=5, the starting compound is 6-aminocapronitrile.
In the process of the present invention, the above-described aminocarbonitriles can be reacted with water in the liquid phase using heterogeneous catalysts to form cyclic lactams. Use of aminocarbonitriles of the formula I results in the corresponding cyclic lactams of the formula II
where n, m, R
1
and R
2
are each as defined above. Particularly preferred lactams are those where n is 0 and m is 4, 5 or 6, especially 5 (caprolactam being obtained in the latter case).
The reaction can be carried out in the liquid phase at generally from 140 to 320° C., preferably at from 160 to 280° C.; the pressure is generally within the range from 1 to 250 bar, preferably from 5 to 150 bar, it being necessary to ensure that the reaction mixture is predominantly liquid under the conditions employed. The residence times are generally within the range from 1 to 120, preferably from 1 to 90, and especially from 1 to 60, min. In some cases, residence times of from 1 to 10 min have proven to be completely adequate.
The amount of water used per mole of aminocarbonitrile is generally at least 0.01 mol, preferably within the range from 0.1 to 20 mol, especially within the range from 1 to 5 mol.
The aminocarbonitrile can be advantageously used in the form of a from 1 to 50% strength by weight, especially from 5 to 50% strength by weight, particularly preferably from 5 to 30% strength by weight, solution in water (in which case the solvent is also reactant) or in
Flick Klemens
Fuchs Eberhard
BASF - Aktiengesellschaft
Johnson Edward M.
Keil & Weinkauf
Silverman Stanley S.
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