Process for producing polyketone

Information

  • Patent Application
  • 20080058493
  • Publication Number
    20080058493
  • Date Filed
    February 15, 2007
    17 years ago
  • Date Published
    March 06, 2008
    16 years ago
Abstract
The present invention relates to a process for preparing polyketone with improved catalytic activity and intrinsic viscosity, and specifically a process for preparing polyketone wherein an organometallic complex comprising acetate-palladium and 1,3-bis[bis(2-methoxy-5-methylphenyl)phosphino]propane is used as a catalyst component, and a mixed solvent of 70 to 90 vol % of acetic acid and 10 to 30 vol % of water is used as a liquid medium.
Description
EXAMPLES
Example 1

0.0129 g of palladium acetate, and 0.0366 g of 1,3-bis[bis(2-methoxy-5-methylphenyl)phosphino]propane (BIBMAPP) were dissolved in the mixture of 2249 ml of acetic acid and 417 ml of water. After removing the air from the solution under vacuum, the obtained solution was charged into a stainless-steel autoclave which had been purged with nitrogen. After sealing the autoclave, the contents were heated under stirring at a speed of 700 rpm. When the internal temperature reached 90° C., a mixed gas of carbon monoxide and ethylene (the molar ratio of 1:2) was added until the internal pressure of the autoclave became 65 bar. The contents were stirred for 1 hour while the internal temperature and the internal pressure were maintained at 90° C. and 65 bar, respectively. After cooling, the contents were taken out from the autoclave which had been degassed. The solution was filtered and then washed with methanol several times. The solution was dried under reduced pressure at room temperature to 80° C., to obtain 73 g of a polymer.


The results of 13C-NMR and IR confirmed that the polymer was polyketone which substantially consists of repeating units each derived from carbon monoxide and ethylene. The catalytic activity was equal to 11.8 kg/g-Pd·hr, and the intrinsic viscosity was 3.1 dl/g.


The results are summarized in Table 1.


Example 2

0.0129 g of palladium acetate, and 0.0366 g of 1,3-bis[bis(2-methoxy-5-methylphenyl)phosphino]propane (BIBMAPP) were dissolved in the mixture of 2249 ml of acetic acid and 417 ml of water. After removing the air from the solution under vacuum, the obtained solution was charged into a stainless-steel autoclave which had been purged with nitrogen. After sealing the autoclave, the contents were heated under stirring at a speed of 700 rpm. When the internal temperature reached 90° C., a mixed gas of carbon monoxide and ethylene (the molar ratio of 1:2) was added until the internal pressure of the autoclave became 70 bar. The contents were stirred for 15 hours while the internal temperature and the internal pressure were maintained at 90° C. and 70 bar, respectively. After cooling, the contents were taken out from the autoclave which had been degassed. The solution was filtered and then washed with methanol several times. The solution was dried under reduced pressure at room temperature to 80° C., to obtain 890.3 g of a polymer.


The results of 13C-NMR and IR confirmed that the polymer was polyketone which substantially consists of repeating units each derived from carbon monoxide and ethylene. The catalytic activity was equal to 9.5 kg/g-Pd·hr, and the intrinsic viscosity was 5.0 dl/g.


The results are summarized in Table 1.


Example 3

0.0236 g of palladium acetate, and 0.0674 g of 1,3-bis[bis(2-methoxy-5-methylphenyl)phosphino]propane (BIBMAPP) were dissolved in the mixture of 1350 ml of acetic acid and 250 ml of water. After removing the air from the solution under vacuum, the obtained solution was charged into a stainless-steel autoclave which had been purged with nitrogen. After sealing the autoclave, the contents were heated under stirring at a speed of 700 rpm. When the internal temperature reached 90° C., a mixed gas of carbon monoxide and ethylene (the molar ratio of 1:2) was added until the internal pressure of the autoclave became 45 bar. The contents were stirred for 1 hour while the internal temperature and the internal pressure were maintained at 90° C. and 45 bar, respectively. After cooling, the contents were taken out from the autoclave which had been degassed. The solution was filtered and then washed with methanol several times. The solution was dried under reduced pressure at room temperature to 80° C., to obtain 183.9 g of a polymer.


The results of 13C-NMR and IR confirmed that the polymer was polyketone which substantially consists of repeating units each derived from carbon monoxide and ethylene. The catalytic activity was equal to 16,24 kg/g-Pd·hr, and the intrinsic viscosity was 2.3 dl/g.


The results are summarized in Table 1.


Example 4

0.0129 g of palladium acetate, and 0.0366 g of 1,3-bis[bis(2-methoxy-5-methylphenyl)phosphino]propane (BIBMAPP) were dissolved in the mixture of 2249 ml of acetic acid and 417 ml of water. After removing the air from the solution under vacuum, the obtained solution was charged into a stainless-steel autoclave which had been purged with nitrogen. After sealing the autoclave, the contents were heated under stirring at a speed of 700 rpm. When the internal temperature reached 90° C., a mixed gas of carbon monoxide and ethylene (the molar ratio of 1:2) was added until the internal pressure of the autoclave became 70 bar. The contents were stirred for 1 hour while the internal temperature and the internal pressure were maintained at 90° C. and 70 bar, respectively. After cooling, the contents were taken out from the autoclave which had been degassed. The solution was filtered and then washed with methanol several times. The solution was dried under reduced pressure at room temperature to 80° C., to obtain 72.5 g of a polymer.


The results of 13C-NMR and IR confirmed that the polymer was polyketone which substantially consists of repeating units each derived from carbon monoxide and ethylene. The catalytic activity was equal to 11.6 kg/g-Pd·hr, and the intrinsic viscosity was 4.2 dl/g.


The results are summarized in Table 1.



















TABLE 1

















Partial





Catalyst system
Solvent
Input



pressure



Catalytic
Amount
[Amount of
(ml)
ratio
Rx
Rx
Polymerization
of



















I.V.
Activity
produced
catalyst input(g)]
Acetic

Ligand/
Temp
Pressure
Time
gas




















(dl/g)
(Kg/gPd · hr)
(g)
Pd
Ligand
acid
water
Pd
(° C.)
(bar)
(hr)
(CO:Et)























Ex. 1
3.1
11.8
73
Pd(OAc)2
BIBMAPP
2249
417
1.2
90
65
1
1:2






0.0129
0.0366


Ex. 2
5.0
9.5
890.3
Pd(OAc)2
BIBMAPP
2249
417
1.2
90
70
15
1:2






0.0129
0.0366


Ex. 3
2.3
16.24
183.9
Pd(OAc)2
BIBMAPP
1350
250
1.2
90
45
1
1:2






0.0236
0.0674


Ex. 4
4.2
11.6
72.5
Pd(OAc)2
BIBMAPP
2249
417
1.2
90
70
1
1:2






0.0129
0.0366





Pd(OAc)2: Palladium acetate


BIBMAPP: 1,3-Bis[bis(2-methoxy-5-methylphenyl)phosphino]propane






Comparative Example 1

0.0129 g of palladium acetate, and 0.0307 g of 1,3-bis[di(2-methoxyphenyl)phosphino]propane were dissolved in the mixture of 2249 ml of acetic acid and 417 ml of water. After removing the air from the solution under vacuum, the obtained solution was charged into a stainless-steel autoclave which had been purged with nitrogen. After sealing the autoclave, the contents were heated under stirring at a speed of 700 rpm. When the internal temperature reached 90° C., a mixed gas of carbon monoxide and ethylene (the molar ratio of 1:2) was added until the internal pressure of the autoclave became 65 bar. The contents were stirred for 1 hour while the internal temperature and the internal pressure were maintained at 90° C. and 65 bar, respectively. After cooling, the contents were taken out from the autoclave which had been degassed. The solution was filtered and then washed with methanol several times. The solution was dried under reduced pressure at room temperature to 80° C., to obtain 58.4 g of a polymer.


The results of 13C-NMR and IR confirmed that the polymer was polyketone which substantially consists of repeating units each derived from carbon monoxide and ethylene. The catalytic activity was equal to 9.4 kg/g-Pd·hr, and the intrinsic viscosity was 3.1 dl/g.


The results are summarized in Table 2.


Comparative Example 2

0.0129 g of palladium acetate, and 0.0307 g of 1,3-bis[di(2-methoxyphenyl)phosphino]propane were dissolved in the mixture of 2249 ml of acetic acid and 417 ml of water. After removing the air from the solution under vacuum, the obtained solution was charged into a stainless-steel autoclave which had been purged with nitrogen. After sealing the autoclave, the contents were heated under stirring at a speed of 700 rpm. When the internal temperature reached 90° C., a mixed gas of carbon monoxide and ethylene (the molar ratio of 1:2) was added until the internal pressure of the autoclave became 70 bar. The contents were stirred for 15 hours while the internal temperature and the internal pressure were maintained at 90° C. and 70 bar, respectively. After cooling, the contents were taken out from the autoclave which had been degassed. The solution was filtered and then washed with methanol several times. The solution was dried under reduced pressure at room temperature to 80° C., to obtain 690.2 g of a polymer.


The results of 13C-NMR and IR confirmed that the polymer was polyketone which substantially consists of repeating units each derived from carbon monoxide and ethylene. The catalytic activity was equal to 7.4 kg/g-Pd·hr, and the intrinsic viscosity was 4.9 dl/g.


The results are summarized in Table 2.


Comparative Example 3

0.0236 g of palladium acetate, and 0.0559 g of 1,3-bis[di(2-methoxyphenyl)phosphino]propane were dissolved in the mixture of 1350 ml of acetic acid and 250 ml of water. After removing the air from the solution under vacuum, the obtained solution was charged into a stainless-steel autoclave which had been purged with nitrogen. After sealing the autoclave, the contents were heated under stirring at a speed of 700 rpm. When the internal temperature reached 90° C., a mixed gas of carbon monoxide and ethylene (the molar ratio of 1:2) was added until the internal pressure of the autoclave became 45 bar. The contents were stirred for 1 hour while the internal temperature and the internal pressure were maintained at 90° C. and 45 bar, respectively. After cooling, the contents were taken out from the autoclave which had been degassed. The solution was filtered and then washed with methanol several times. The solution was dried under reduced pressure at room temperature to 80° C., to obtain 164.2 g of a polymer.


The results of 13C-NMR and IR confirmed that the polymer was polyketone which substantially consists of repeating units each derived from carbon monoxide and ethylene. The catalytic activity was equal to 14.5 kg/g-Pd·hr, and the intrinsic viscosity was 2.1 dl/g.


The results are summarized in Table 2.


Comparative Example 4

0.0129 g of palladium acetate, and 0.0307 g of 1,3-bis[di(2-methoxyphenyl)phosphino]propane were dissolved in the mixture of 2249 ml of acetic acid and 417 ml of water. After removing the air from the solution under vacuum, the obtained solution was charged into a stainless-steel autoclave which had been purged with nitrogen. After sealing the autoclave, the contents were heated under stirring at a speed of 700 rpm. When the internal temperature reached 90° C., a mixed gas of carbon monoxide and ethylene (the molar ratio of 1:2) was added until the internal pressure of the autoclave became 70 bar. The contents were stirred for 1 hour while the internal temperature and the internal pressure were maintained at 90° C. and 70 bar, respectively. After cooling, the contents were taken out from the autoclave which had been degassed. The solution was filtered and then washed with methanol several times. The solution was dried under reduced pressure at room temperature to 80° C., to obtain 57.3 g of a polymer.


The results of 13C-NMR and IR confirmed that the polymer was polyketone which substantially consists of repeating units each derived from carbon monoxide and ethylene. The catalytic activity was equal to 9.2 kg/g-Pd·hr, and the intrinsic viscosity was 4.1 dl/g.


The results are summarized in Table 2.



















TABLE 2

















Partial





Catalyst system
Solvent
Input



pressure



Catalytic
Amount
[Amount of
(ml)
ratio
Rx
Rx
Polymerization
of



















I.V.
Activity
produced
catalyst input(g)]
Acetic

Ligand/
Temp
Pressure
Time
gas




















(dl/g)
(Kg/gPd · hr)
(g)
Pd
Ligand
acid
water
Pd
(° C.)
(bar)
(hr)
(CO:Et)























Ex. 1
3.1
9.4
58.4
Pd(OAc)2
BDOMPP
2249
417
1.2
90
65
1
1.2






0.0129
0.0307


Ex. 2
4.9
7.4
690.2
Pd(OAc)2
BDOMPP
2249
417
1.2
90
70
15
1.2






0.0129
0.0307


Ex. 3
2.1
14.5
164.2
Pd(OAc)2
BDOMPP
1350
250
1.2
90
45
1
1.2






0.0236
0.0559


Ex. 4
4.1
9.2
57.3
Pd(OAc)2
BDOMPP
2249
417
1.2
90
70
1
1.2






0.0129
0.0307





Pd(OAc)2: Palladium acetate


BDOMPP: 1,3-Bis[di(methoxyphenyl)phosphino]propane






EFFECTS OF THE INVENTION

According to the present invention, a process for prep According to the present invention, by using 1,3-bis[bis(2-methoxy-5-methylphenyl)phosphino]propane as the ligand of the catalyst component, a mixed solvent of 70 to 90 vol % of acetic acid and 10 to 30 vol % of water as a liquid medium, and palladium acetate as a transition metal complex, a process for preparing polyketone with the improved catalytic activity and the improved activity even with a shorter reaction time, is provided.

Claims
  • 1. A process for preparing polyketone, comprising copolymerization of carbon monoxide and an ethylenically unsaturated compound in a liquid medium in the presence of a catalyst, wherein the catalyst is an organometallic complex comprising (a) a Group 9, Group 10 or Group 11 transition metal complex, and (b) a ligand containing a Group 15 element, andthe (b) component is 1,3-bis[bis(2-methoxy-5-methylphenyl)phosphino]propane.
  • 2. The process for preparing polyketone according to claim 1, wherein the liquid medium is a mixed solvent of 70 to 90 vol % of acetic acid and 10 to 30 vol % of water.
  • 3. The process for preparing polyketone according to claim 1, wherein the (a) component is palladium acetate.
  • 4. The process for preparing polyketone according to claim 1, wherein the molar ratio of the (a) component: the (b) component of the catalyst is 1:1.2.
Priority Claims (1)
Number Date Country Kind
10-2006-0083274 Aug 2006 KR national