METHOD FOR CATALYTIC GENERATION OF FORMIC ACID AT AN OXYGEN PARTIAL PRESSURE BELOW 1 BAR AND REGENERATION OF THE CATALYST USED THEREFOR

Abstract

The invention relates to a method for the catalytic generation of formic acid at an oxygen partial pressure below 1 bar and regeneration of the catalyst used therefor.

Claims

1. A method for catalytic generation of formic acid at an oxygen partial pressure of less than 1 bar and regeneration of the catalyst used in this process, wherein a polyoxometallate ion of the general formula [PMo.sub.xV.sub.yO.sub.40].sup.n, which serves as the catalyst, is brought in contact with an alpha-hydroxyaldehyde, an alpha-hydroxycarboxylic acid, a carbohydrate, a glycoside or a polymer containing a carbon chain with at least one OH group bound repeatedly as a substituent to the carbon chain and/or an O, N or S atom occurring repeatedly in the carbon chain in a liquid solution (12) in a vessel (10), at a temperature above 70 C. and below 120 C., wherein 6x11 and 1y6 and 3<n<10 and x+y=12, wherein n, x and y each denote an integer, wherein the catalyst thereby reduced is returned to its starting state by oxidation, wherein the contacting takes place in the vessel (10) at an oxygen partial pressure of less than 1 bar, wherein a portion of the liquid solution (12) is discharged from the vessel (10) for oxidation of the catalyst, then is exposed to oxygen or a gas mixture containing oxygen at an oxygen partial pressure of 1 to 500 bar and next is fed back to the remainder of the liquid solution (12), wherein the oxygen partial pressure in the vessel is always kept below 1 bar, wherein the oxygen partial pressure acting on that portion of the liquid solution (12) is lowered from 1 to 500 bar to less than 5 bar before that portion of the liquid solution (12) is fed back to the remainder of the liquid solution (12).

2. The method according to claim 1, wherein the alpha-hydroxyaldehyde, the alpha-hydroxycarboxylic acid, the carbohydrate, the glycoside or the polymer is present in the liquid solution (12) in the form of solids distributed therein.

3. The method according to claim 1, wherein the polymer is a polyester, a polyamine or a polyamide, in particular polyhexamethylene adipamide.

4. The method according to claim 1, wherein the contacting takes place at atmospheric pressure in the vessel (10), wherein the gas pressure in the vessel is always kept at atmospheric pressure.

5. The method according to claim 1, wherein that portion of the liquid solution (12) is discharged continuously from the vessel (10), oxidized at an oxygen partial pressure of 1 to 500 bar and then fed continuously back to the remainder of the liquid solution (12).

6. The method according to claim 4, wherein the oxidation is carried out continuously.

7. The method according to claim 1, wherein that portion of the liquid solution (12) is cooled before being exposed to the oxygen or the gas mixture and then is exposed to the oxygen partial pressure of 1 to 500 bar at a temperature at most 95 C., at most 85 C., at most 75 C., at most 65 C., at most 55 C., at most 45 C., at most 35 C. or at most 25 C.

8. The method according to claim 1, wherein that portion of the liquid solution (12) is conveyed by means of at least one pump or a high-density solids pump.

9. The method according to claim 1, wherein that portion of the liquid solution (12) is exposed to the oxygen partial pressure of 1 to 500 bar in an additional vessel.

10. The method according to claim 9, wherein the oxygen or the gas mixture is fed to that portion of the liquid solution (12), the additional vessel is a housing (18) of a screw compactor, and the oxygen partial pressure is built up by the fact that that portion of the liquid solution (12) is compressed together with the oxygen or the gas mixture by means of the screw compactor.

11. The method according to claim 9, wherein the additional vessel is a housing of (18) a static mixer, wherein the oxygen or the gas mixture is fed to that portion of the liquid solution (12), wherein that portion of the liquid solution (12) is passed together with the oxygen or the gas mixture under the oxygen partial pressure of 1 to 500 bar through the static mixer or at least through a portion of the static mixer.

12. The method according to claim 1, wherein the oxygen partial pressure acting upon that portion of the liquid solution (12) is reduced from 1 to 500 bar to less than 1 bar or to the oxygen partial pressure prevailing at atmospheric pressure before that portion of the liquid solution (12) is fed back to the remainder of the liquid solution (12).

13. The method according to claim 1, wherein during or after the reduction in the oxygen partial pressure acting upon that portion of the liquid solution (12) or after that portion of the liquid solution (12) has been fed back to the remainder of the liquid solution (12), gas (29) which has outgassed from that portion of the liquid solution (12) or the liquid solution (12), is allowed to escape or is removed from an apparatus suitable for carrying out the method.

14. The method according to claim 1, wherein the polymer is a polymer without a plasticizer.

15. The method according to claim 1, wherein n=3+y.

Description

[0033] The present invention will now be explained in greater detail on the basis of an exemplary embodiment.

[0034] FIG. 1 shows a schematic diagram of an apparatus suitable for carrying out the process and

[0035] FIG. 2 shows a schematic diagram of an alternative apparatus suitable for carrying out the process.

[0036] FIG. 1 shows a vessel 10 with a liquid solution 12 contained therein. The liquid solution 12 contains the catalyst and an alpha-hydroxyaldehyde, an alpha-hydroxycarboxylic acid, a carbohydrate, a glycoside or a polymer having a carbon chain with at least one OH group bound repeatedly to the carbon chain as a substituent and/or with an O, N or S atom occurring repeatedly in the carbon chain. The liquid solution is regulated at a temperature above 70 C. and below 120 C. An outlet line 16 with a filter 14 connected in front of it for removing a portion of the liquid solution 12 is provided on the vessel 10. A portion of the liquid solution goes through the outlet line 16 into the housing 18 of the screw compactor, where the screw compactor 20 driven by the drive 22 by means of the driveshaft 23 compresses that portion of the liquid solution 12 introduced into the housing 18 of the screw compactor with the air 25 introduced into it through the air inlet connection 24. That portion of the liquid solution 12 is pressed against the perforated mask 26. In doing so, an oxygen partial pressure of definitely more than 1 bar is built up in the screw compactor. The pressure depends on the resistance with which the perforated mask 26 opposes that portion of the liquid solution 12 and on the design of the screw compactor, in particular the pitch of the compressor screw 20 and the rotational speed at which the compressor screw 20 is rotated by the drive 22. Downstream from the perforated mask 26, that portion of the liquid solution 12 collects at a reduced oxygen partial pressure, wherein outgassing gas 29 can escape through the vent connection 28. That portion of the liquid solution 12 then passes through the inlet line 30 back to the remainder of the liquid solution 12 in the vessel 10. To do so, that portion of the liquid solution 12 can be conveyed through the inlet 30 by means of a pump (not shown here).

[0037] FIG. 2 shows a vessel 10 with liquid solution 12 contained therein. The liquid solution 12 contains the catalyst and an alpha-hydroxyaldehyde, an alpha-hydroxycarboxylic acid, a carbohydrate, a glycoside or a polymer containing a carbon chain having at least one OH group bound repeatedly as a substituent to the carbon chain and/or having an O, N or S atom occurring repeatedly in the carbon chain. The liquid solution is regulated at a temperature above 70 C. and below 120 C. An outlet line 16 with a filter 14 connected upstream for removing a portion of the liquid solution 12 is provided on the vessel 10. That portion of the liquid solution 12 enters the pump 31 through the outlet line 16 and goes from there through the connecting line 32 at an elevated pressure into the static mixer 34. Air 25 is introduced at an oxygen partial pressure of 1 to 500 bar into the static mixer through air inlet connection 24 in the housing 33 of the static mixer 34 and becomes mixed there with that portion of the liquid solution flowing in through the static mixer 34. An oxygen partial pressure of 1 to 500 bar is maintained in the static mixer 34 by means of the pump 31. That portion of the liquid solution 12 is pressed against the perforated mask 26. The oxygen partial pressure in the static mixer 34 depends on the pressure and the resistance built up by the pump 31 and on the resistance with which the perforated mask 26 opposes that part of the liquid solution 12. Behind the perforated mask 26, that portion of the liquid solution 12 collects at a reduced oxygen partial pressure, wherein outgassing gas 29 can escape through the vent connection 28. That portion of the liquid solution 12 then passes through the inlet line 30 back to the remainder of the liquid solution 12 in the vessel 10. To do so, that portion of the liquid solution can be conveyed through the inlet line 30 by means of a pump (not shown here).

LIST OF REFERENCE NUMERALS

[0038] 10 vessel

[0039] 12 liquid solution

[0040] 14 filter

[0041] 16 outlet line

[0042] 18 housing of a screw compactor

[0043] 20 compressor screw

[0044] 22 drive

[0045] 23 driveshaft

[0046] 24 air inlet connection

[0047] 25 air

[0048] 26 perforated mask

[0049] 28 degassing connection

[0050] 29 gas

[0051] 30 inlet line

[0052] 31 pump

[0053] 32 connecting line

[0054] 33 housing of a static mixer

[0055] 34 static mixer