Catalysts Containing Tungstate for the Synthesis of Alkylmercaptane and Method for The Production Thereof

Information

  • Patent Application
  • 20080033213
  • Publication Number
    20080033213
  • Date Filed
    July 05, 2005
    19 years ago
  • Date Published
    February 07, 2008
    16 years ago
Abstract
The invention relates to a catalyst containing alkali tungstate for the synthesis of alkylmercaptanes from alkanols and hydrogen sulphide, in addition to a method for the production of said catalyst, wherein the molar ratio of alkali to tungstan is<2:1.
Description
EXAMPLES
Example 1 (Comparative Example)

150 g of aluminium oxide I were impregnated with 21.0% by weight of caesium tungstate (Cs2.0WO4) with the aid of vacuum impregnation. To this end, the specific procedure was as follows:


To prepare the impregnation solution, 55.7 g of tungstic acid were suspended in 44.5 g of water and dissolved by adding 111.4 g of 25% ammonia solution and heating to 50° C. 74.6 g of Cs(OH).H2O were dissolved in 37.3 g of water and mixed with the first solution. The solution was subsequently stirred in a covered beaker for 48 hours. Thereafter, the solution was made up to a volume of 234 ml with 25 g of water.


The aluminium oxide was initially charged in a glass vessel which was evacuated to 150 mbar. By virtue of the opening of a tap, the impregnation solution was sucked into the evacuated glass vessel until the entire bed of shaped bodies was covered with the solution. After a wait time of 15 minutes and aeration of the glass vessel, the solution which had not been absorbed by the aluminium oxide ran back into the beaker. 79 ml of impregnation solution were absorbed by the aluminium oxide.


The granules were dried to remove the residual moisture at room temperature in an air current for the period of 1 hour and subsequently at 120° C. for 3 hours. Afterward, the granules were calcined at 455° C. for 3 hours.


Example 2 (Comparative Example)

Comparative Example 1 was repeated with 26.3% loading of the aluminium oxide with caesium tungstate (Cs2.0WO4).


Example 3 (Comparative Example)

Comparative Example 1 was repeated with 19.6% loading of the aluminium oxide with potassium tungstate (K2.0WO4) with use of KOH instead of Cs(OH).H2O.


Example 4

150 g of aluminium oxide (Spheralite 501A) was impregnated in a two-stage impregnation with a total of 26.7% by weight of promoter (K1.6WOy) with the aid of vacuum impregnation. The specific procedure was as follows:


64.5 g of tungstic acid were suspended in 50.7 g of water and dissolved by adding 126.9 g of 25% ammonia solution and heating to 50° C. 22.8 g of KOH were dissolved in 11.5 g of water and mixed with the first solution. The solution was subsequently stirred in a covered beaker for 48 hours. Thereafter, the solution was made up to a volume of 234 ml with 39 g of water. The aluminium oxide was initially charged in a glass vessel which was evacuated to 150 mbar. By virtue of the opening of a tap, the impregnation was sucked in until the entire bed of mouldings was covered with the solution. After a wait time of 15 minutes and aeration of the glass vessel, the solution which had not been absorbed by the aluminium oxide flowed back into the beaker. 76 ml of impregnation solution were absorbed by the aluminium oxide. Subsequently, the granules were dried at room temperature for 1 hour and at 120° C. for 3 hours, and calcined at 455° C. for 3 hours.


To carry out the second impregnation, an identical impregnation solution to that in the first step was prepared and applied in the same way by vacuum impregnation to the already laden catalyst from the first step. This was then followed again by drying at room temperature for 1 hour, followed by drying at 120° C. for 3 hours. Finally, the catalyst particles were calcined under air at 455° C. for 4 hours.


Example 5

150 g of aluminium oxide (Spheralite 501A) was impregnated in a two-stage impregnation with a total of 30.1% by weight of promoter (Rb0.9WOy) with the aid of vacuum impregnation. The specific procedure was as follows:


59.0 g of tungstic acid were suspended in 48.3 g of water and dissolved by adding 110.7 g of 25% ammonia solution and heating to 50° C. 41.5 g of RbOH were dissolved in 17.5 g of water and mixed with the first solution. The solution was subsequently stirred in a covered beaker for 48 hours. Thereafter, the solution was made up to a volume of 234 ml with 25 g of water. The aluminium oxide was initially charged in a glass vessel which was evacuated to 150 mbar. By virtue of the opening of a tap, the impregnation was sucked in until the entire bed of mouldings was covered with the solution. After a wait time of 15 minutes and aeration of the glass vessel, the solution which had not been absorbed by the aluminium oxide flowed back into the beaker. 75 ml of impregnation solution were absorbed by the aluminium oxide. Subsequently, the granules were dried at room temperature for 1 hour and at 120° C. for 3 hours, and calcined at 455° C. for 3 hours.


To carry out the second impregnation, an identical impregnation solution to that in the first step was prepared and applied in the same way by vacuum impregnation to the already laden catalyst from the first step. This was then followed again by drying at room temperature for 1 hour, followed by drying at 120° C. for 3 hours. Finally, the catalyst particles were calcined under air at 455° C. for 4 hours.


Example 6

150 g of aluminium oxide (Spheralite 501A) was impregnated in a two-stage impregnation with a total of 29.4% by weight of promoter (K0.7CS0.7WOy) with the aid of vacuum impregnation. The specific procedure was as follows:


61.3 g of tungstic acid were suspended in 49.1 g of water and dissolved by adding 122.7 g of 25% ammonia solution and heating to 50° C. 9.8 g of KOH and 29.0 g of Cs(OH).H2O were dissolved in 14.5 g of water and mixed with the first solution. The solution was subsequently stirred in a covered beaker for 48 hours. Thereafter, the solution was made up to a volume of 234 ml with 47 g of water. The aluminium oxide was initially charged in a glass vessel which was evacuated to 150 mbar. By virtue of the opening of a tap, the impregnation was sucked in until the entire bed of mouldings was covered with the solution. After a wait time of 15 minutes and aeration of the glass vessel, the solution which had not been absorbed by the aluminium oxide flowed back into the beaker. 75 ml of impregnation solution were absorbed by the aluminium oxide. Subsequently, the granules were dried at room temperature for 1 hour and at 120° C. for 3 hours, and calcined at 455° C. for 3 hours.


To carry out the second impregnation, an identical impregnation solution to that in the first step was prepared and applied in the same way by vacuum impregnation to the already laden catalyst from the first step. This was then followed again by drying at room temperature for 1 hour, followed by drying at 120° C. for 3 hours. Finally, the catalyst particles were calcined under air at 455° C. for 4 hours.


Example 7

150 g of aluminium oxide (Spheralite 501A) was impregnated in a two-stage impregnation with a total of 31.0% by weight of promoter (Na0.3Cs1.1WOy) with the aid of vacuum impregnation. The specific procedure was as follows:


61.1 g of tungstic acid were suspended in 48.9 g of water and dissolved by adding 122.1 g of 25% ammonia solution and heating to 50° C. 3.2 g of NaOH and 44.6 g of Cs(OH).H2O were dissolved in 22.3 g of water and mixed with the first solution. The solution was subsequently stirred in a covered beaker for 48 hours. Thereafter, the solution was made up to a volume of 234 ml with 40 g of water. The aluminium oxide was initially charged in a glass vessel which was evacuated to 150 mbar. By virtue of the opening of a tap, the impregnation was sucked in until the entire bed of mouldings was covered with the solution. After a wait time of 15 minutes and aeration of the glass vessel, the solution which had not been absorbed by the aluminium oxide flowed back into the beaker. 74 ml of impregnation solution were absorbed by the aluminium oxide. Subsequently, the granules were dried at room temperature for 1 hour and at 120° C. for 3 hours, and calcined at 455° C. for 3 hours.


To carry out the second impregnation, an identical impregnation solution to that in the first step was prepared and applied in the same way by vacuum impregnation to the already laden catalyst from the first step. This was then followed again by drying at room temperature for 1 hour, followed by drying at 120° C. for 3 hours. Finally, the catalyst particles were calcined under air at 455° C. for 4 hours.


Example 8 (Use Example)

The catalysts were tested with regard to their performance data in the synthesis of methyl mercaptan from hydrogen sulphide and methanol.


The synthesis was carried out in a stainless steel tube of internal diameter 18 mm and a length of 500 mm. The catalyst bed of in each case 76 ml was secured in the reaction tube on both sides by inert beds of glass spheres. The reaction tube was heated to the reaction temperature of about 320° C. using a jacket comprising a thermal oil.


The experimental conditions can be taken from the following list:


















GHSV:
1300 h−1 (based on standard conditions)



LHSV:
0.84 h−1 (based on liquid MeOH)



Reaction temperature:
320° C.



Mass ratio
1.9



H2S/MeOH:



Pressure:
9 bar










The reaction mixture comprising the products methyl mercaptan, dimethyl sulphide and dimethyl ether, and comprising the unconverted starting materials methanol and hydrogen sulphide is analyzed by online gas chromatography.


When the tungsten fraction in relation to the alkali metal fraction in the catalyst is increased, a distinct increase in activity can be seen with simultaneously improved selectivity. In comparison to the prior art, this leads to a yield increase of up to 10%. The selectivity can be increased to up to ˜96.5% by adjusting the alkali metal-tungstate ratio, and the methanol conversion rises. In the industrial scale synthesis of methyl mercaptan, this also leads to considerable cost savings in the removal of the reaction products from unconverted methanol and by-products.


In addition, the results of Examples 4 to 7 show that at least a portion of the alkali metals can be exchange for one another in order to selectively adjust the activity and selectivity of the catalyst or in order to save raw material costs in the catalyst synthesis.









TABLE 1







Experimental results















mol.








alkali
Loading
Methanol


Catalyst
Alkali
metal:W
[% by
conversion
Selectivity
Yield


Example
metal
ratio
wt.]
[%]
[%]
[%]
















CE1
Cs
  2:1
21.0
82.4
93.3
76.9


CE2
Cs
  2:1
26.3
79.5
94.7
75.2


CE3
K
  2:1
19.6
76.0
95.2
72.4


E4*)
K
1.6:1
26.7
85.6
95.1
81.4


E5*)
Rb
0.9:1
30.1
73.2
96.6
70.7


E6*)
K, Cs
1.4:1
29.4
88.5
95.4
84.4


E7*)
Na, Cs
1.4:1
31.0
88.4
95.8
84.7





CE1: Catalyst according to Comparative Example 1


*)multistage impregnation





Claims
  • 1. Catalyst comprising a catalytically active tungstate which contains at least one chemically bound alkali metal and tungsten with a molar ratio of alkali metal to tungsten of<2:1, cesium occurring only in combination with another alkali element.
  • 2. Catalytically active tungstate according to claim 1 which contains at least two alkali metals and tungsten in a molar ratio of the sum of the alkali metals to tungsten of<2:1.
  • 3. Catalyst according to claim 1, consisting of a coated catalyst in which a support core is coated with the catalytically active tungstate of with a support material impregnated with this tungstate.
  • 4. Catalyst according to claim 1, in which the support material impregnated with the catalytically active tungstate has been processed to give an unsupported catalyst.
  • 5. Catalyst according to claim 1, in which the surface of a support body is impregnated with a catalytically active oxidic composition composed of alkali metals and tungsten with a molar ratio of alkali metal(s) to tungsten of<2:1.
  • 6. Catalyst according to claim 1, characterized in that the molar ratio of alkali metal(s) to tungsten in the tungstate is<2:1 to 0.9:1.
  • 7. Catalyst according to claim 6, characterized in that the ratio ranges from 1.9:1 to 1:1.
  • 8. Catalyst according to claim 1, characterized in that the oxidic composition corresponds to the general formula AxWOy in which
  • 9. Catalyst according to claim 1, characterized in that it comprises the tungstate in an amount of 8 to 45% by weight, preferably 20 to 36% by weight.
  • 10. Catalyst according to claim 1, characterized in that the support body or the support material consists of an oxidic inorganic compound.
  • 11. Catalyst according to claim 10, characterized in that the support body or the support material consists of aluminium oxide (Al203).
  • 12. Catalyst according to claim 10, characterized in that the support material has a specific surface area of 180 to 400 m2/g (BET) and a total pore volume of 0.3 to 1.2 ml/g.
  • 13. Catalyst according to claim 1, characterized in that the alkali metal is potassium.
  • 14. Catalyst according to claim 1, characterized in that the alkali metal is rubidium.
  • 15. Catalyst according to claim 2, characterized in that the alkali metals are potassium and cesium.
  • 16. Catalyst according to claim 2, characterized in that the alkali metals are sodium and cesium.
  • 17. Catalyst according to claim 2, characterized in that the alkali metals are rubidium and cesium.
  • 18. Catalyst according to claim 2, characterized in that the alkali metals are sodium and potassium.
  • 19. Catalyst according to claim 2, characterized in that the alkali metals are rubidium and potassium.
  • 20. Process for preparing a catalyst comprising alkali metal tungstate, in which the following process steps are carried out: a) impregnation of the support body or of the support material with an aqueous solution which comprises soluble alkali metal and tungsten compounds in the desired molar alkali metal/W ratio,b) predrying of the resulting impregnated shaped body or of the finely divided support material (catalyst precursor) at room temperature,c) optional drying at 100 to 200° C. to remove the residual moisture,d) subsequent calcining at temperatures of 300 to 600° C. for the period of 2 to 10 hours ande) obtaining the supported catalyst or the impregnated finely divided support material with a content of 8 to 45% by weight, preferably 15 to 36% by weight, of a promoter of the general composition AxWOy in which A, x and y are each as defined above, and subsequentlyf) the finely divided impregnated support material is suspended with addition of known assistants and applied to an inert support core or extruded and compressed.
  • 21. Process according to claim 20, characterized in that steps a to c and optionally d are repeated at least once.
  • 22. Process according to claim 20, characterized in that, in the case of repeated impregnation, the impregnation solution used first comprises one to two thirds of the intended total amount of alkali metals and tungsten.
  • 23. Process according to claim 20, characterized in that the support bodies or the support material are sprayed repeatedly with the impregnation solution and portions of the residual moisture are removed at a temperature up to 120° C. between these treatment steps, before moving on to treatment step b).
  • 24. Process according to claim 20, characterized in that the catalyst is heat-treated after the application of the impregnated support material to the core after the extrusion or compression.
  • 25. Process for preparing alkyl mercaptans by reacting alkanols and hydrogen sulphide in the presence of the catalyst according to claim 1.
  • 26. Process according to claim 25 for preparing methyl mercaptan by reacting methyl alcohol and hydrogen sulphide.
Priority Claims (1)
Number Date Country Kind
10 2004 037 739.1 Aug 2004 DE national
PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/EP05/07211 7/5/2005 WO 00 12/6/2006