Title of Invention	METHOD FOR THE APPLICATION OF ANTI-FOULING AGENTS
Abstract	The present invention relates to a method for applying an aqueous solution to the internal walls of a reactor for polymerizing vinyl chloride and/or vinyl acetate, which aqueous solution contains a salt of an anti-scaling agent which comprises a product of condensation of an aldehyde, a phenolic compound and an aromatic carboxylic acid hydroxylated at the aromatic nucleus, the method being characterized in that the pH- value of this aqueous solution is changed to a pH-value of less than 5.

Title of Invention

METHOD FOR THE APPLICATION OF ANTI-FOULING AGENTS

Abstract

The present invention relates to a method for applying an aqueous solution to the internal walls of a reactor for polymerizing vinyl chloride and/or vinyl acetate, which aqueous solution contains a salt of an anti-scaling agent which comprises a product of condensation of an aldehyde, a phenolic compound and an aromatic carboxylic acid hydroxylated at the aromatic nucleus, the method being characterized in that the pH- value of this aqueous solution is changed to a pH-value of less than 5.

Full Text	Method for the application of anti-fouling agent3 The present invention relates to a method for applying anti-scaiinc agents used in the polymerization cf vinyl chloride, vinyl acetate or mixtures thereof. Frier art The anti-scaling agents normally used in the polymerization cf vinyl chloride and/or vinyl acetate are products which can be obtained by condensation of formaldehyde and 1-naphthol, such as, for example, these described in European patent application Er-52412. European patent application EP-942 93 6, incorporated herein by reference, describes anti-scaling agents which comprise a product of condensation cf an aldehyde, a phenolic compound and an aromatic carboxylic acid hydrcxylated at the aromatic nucleus. Preferably the aldehyde is formaldehyde, the phenolic compound is 1-naphthol and the aromatic carboxylic acid hydroxylated at the aromatic nucleus is selected from salicylic acid, 4-hydroxybenzoic acid, a, P, or y-resorcylic acid, 2,3-dihydroxybenzoic acid, 2,5-dihydrcxybenzoic acid, 2-hydroxy-5-methoxybenzoic~ acid or 6-hydroxy-2-naphthoic acid; of these, the one greatly preferred is P-resorcylic acid (that is, 2,4-dihydroxybenzoic acid) , Statement of invention An anti-contaminating agent (or anti-scalirig agent) , in order to be effective and economically suitable for the production of PVC in suspension (PVC/S) , must satisfy the following conditions: • it must be stable, readily meterable and readily applicable with vapour under pressure (the polymerize* tion reactcr must in fact be kept closed in order to avoid very dangerous contaminations owing to the emission of gaseous vinyl chloride); • it must have an elevated capacity for coagulating rapidly upon variation in the pH-value at the moment when it comes into contact with the vapour (which is •normally at a pH-value of 9-10); • it must be able to form a coaaulum having a ce- latinous appearance and, if possible, be colourless (to avoid contaminating the finished product). The coagulum must preferably be of the "tacky gel" type in order to adhere to the internal walls of the reactors and to form a protective film (coating) owing to the action of the heat of the vapour. The gel deposited on the walls must further be able to penetrate uniformly into the micropores of the surface of the steel in order to prevent the formation of mi-croparticles of FVC which can give rise to the formation of the deposits. Furthermore, it must not be necessary to heat the internal walls of the reactor in order to promote the formation of the protective film; such an operation would in fact involve a delay in the production cycle; after the application, the protective film must be, among other things, strong enough to allow washing with water (pH-value 7) for the removal from the reactor of contaminating residues; the total application time must finally be as short as possible and require simple apparatuses which ensure * reliable and homogeneous application of the product. Results of this type are normally achieved by applying, with vapour under pressure, an aqueous solution containing 4-8% by weight anti-contaminating agent, at least 12-18% of which must remain on the internal walls of the reactor in the form of a protective film (such a method is described, for example, in "Fine Chemicals for PVC/S", Chapter 5, 1999, published by CIRS Spa, incorporated herein by reference); the method in question in fact allows extended and economical application cycles whereas mechanical or gas-operated spray apparatuses are not presently capable of achieving the above-mentioned objectives. The present inventicn relates to a novel method for the application of the anti-scaling agent known as EVERCLEAN® 104NS. The preparation of this anti- scaling agent, currently marketed by the owner 3V Sigma Spa, is described in detail in Example 25 of already-mentioned European patent application EP-942936; it refers to a basic aqueous solution having a brown colour and a pH-value of between 11 and 12.4 (normally 11.54) which, as is known in the art, is applied to the internal walls of the reactors for polymerizing vinyl chloride and/or vinyl acetate by spraying in a vapour stream using an apparatus which is similar to that illustrated in Figure 1. However, this application method allows the desired anti-scaling effect to be achieved only in part. In fact, when operating in such conditions, a coagulum which adheres sufficiently to the internal walls of the reactors, thereby .forming the necessary protective film, is not obtained; on the contrary, the great majority of the anti-scaling agent applied in this manner (approximately 99%) is'collected unchanged at the bottom of the reactor before the start of the polymerization reaction, thus necessitating further applications. It has now been surprisingly found that, by acidifying before application the solution of EVERCLEAN® 104NS to a pH-value" of less than 5 and, preferably, in the range between 2.5 and 4.5, there is obtained coagulation of the anti- scaling agent which can therefore be applied with greater effectiveness to the walls of the reactor. The problem addressed by the present invention is therefore to provide a method for applying an aquecus solution containing an alkali metal and/or alkaline •earth metal salt, preferably a sodium salt, of an anti-scaling agent comprising a product of condensation of an aldehyde, a phenolic compound and an aromatic car-boxylic acid hydroxy1ated at the aromatic nucleus, characterized in that the pH-value of this aqueous solution is changed to a pH-value of less than 5 and, preferably, in the range between 2.5 and 4.5. Preferably the aldehyde is formaldehyde, the phenolic compound is 1-naphthol and the aromatic carboxylic acid hydroxylated at the aromatic nucleus is 2,4-dihydroxybenzoic acid; the aqueous solution usually contains 4-8% by weight of the alkali metal and/or alkaline earth metal salt of this anti-scaling agent and has a pH-value in the range between 11 and 12.4. The method according to the present invention provides for contact on the wall (that is, on the internal walls of the polymerization reactor) , or in the mixer, between the solution of the anti-scaling agent and a solution of an organic and/or inorganic acid, for example, citric, oxalic, tartaric, hydrochloric, nitric and/or sulphuric acid, which in the presence of vapour ensure a sufficient reduction in the pH-value to allow the coagulation and the formation of the protective film. This aqueous solution preferably contains from 1 to 10% by weight citric acid, preferably 5%. According to the greatly preferred embodiment of the present invention, the salt of the anti-scaling agent and the aqueous solution of the organic and/or inorganic acid are mixed with each other before being ap- plied to the internal walls of the polymerization"reactor; the mixture of gel and condensate obtained in this manner is applied to the internal wails of the polymerization reactor in a stream of vapour. A suitable apparatus for the application according to the present •invention is, for example, illustrated in Figure 2 (wherein the valves are designated using the letter V). The pressure of the vapour is not binding for the purposes of the present: invention and can vary according to the type of installation; the pressures normally used are, however, in the range between approximately 2 and 2 0 .bar; the application time is normally in the range between 15 and 45 seconds. As will be appreciated from the Examples reproduced below, which must not be taken to limit the present invention, the method claimed here has the advantage of providing the anti-scaling agent corresponding to European patent application EP-942936 in the form of a coagulate product. This product can therefore be readily applied to the internal walls of a reactor for polymerizing vinyl chloride and/or vinyl acetate, thereby forming a protective film which adheres to the walls at a rate greater than 12% by weight relative to the quantity loaded. In this manner, it is thus possible adequately to protect the reactor by eliminating almost completely the formation of deposits even after long periods of activity, thereby minimizing the necessity of interrupting the production cycle to allow the in-. stallation to be cleaned; the large quantity of anti-scaling agent which remains attached to the wall further allows a reduction in the quantity of anti-scaling agent to be used, with obvious economic advantages. Examples Example 1 There was loaded into a reactor, measuring 10 m3 with walls of stainless steel, provided with an application apparatus of "he type schematically depicted in Figure 1, 1 kg of an aqueous solution containing 6% by weight sodium salt of the anti-scaling agent which is obtained • as described in .Example 25 of European patent application EP-942935. The product was sprayed for 30 seconds on the inside of the reactor with vapour at a pressure - of 5 atmospheres. After the application, the condensate was collected at the bottom of the reactor. The condensate was analyzed in order to determine the pH-value and the possible presence of coagulate. The pH-value was 10 and the condensate contained no precipitate gel . The condensate was further treated once more with hydrochloric acid until a pK-value of 3.8 was reached and there was finally observed a coagulate of dark brown/black appearance which was found to correspond to more than 99% by weight of the anti-scaling agent initially loaded. Example 2 The procedure described in Example 1 was repeated and the apparatus schematically depicted in Figure 2 was used (wherein 1 litre citric acid at a concentration of 5% by weight was loaded into tank B) - After spraying in the reactor, the condensate was collected and it was observed that the condensate had a pH-value of 3.2 and 'contained 85% coagulated anti-scaling product (while the remaining 15% was left deposited on the internal walls of the reactor as a protective film). Examples 3-4 The procedure of Examples 1 and 2 was repeat ad with similar results when operating v/ith vapour at a pressure of IS atmospheres. Examples 5-3 The procedure of Examples 1-4 was repeated with similar • results using EVERCLEAN'3 104NS, which is commercially-available, in place of the product obtained according to Example 25 of European patent application EP-942936. Claims 1. A method for■applying an aqueous solution to che internal walls of a reactor for polymerizing vinyl chloride and/cr vinyl acetate, which aqueous solution- contains a salt of an anti-scaling agent which ccrr.- ■ prises a product of condensation of an aldehyde, a phenolic compound and an aromatic carboxylic acid hydroxy-lated at the aromatic nucleus, the method being characterized in that the pH-value of this aqueous solution is changed to a-pH-vaiue of less than 5. 2. A method according to claim 1, characterized in that the pH-value of the aqueous solution is changed ;c a pH-value in the range between 2.5 and 4.5. 3. A method according to claim 1, characterized in that the salt of the anti-scaling agent is an alkali metal and/or alkaline earth metal salt, preferably sodium. 4. A method according to claims 1 to 3, characterized in that the pH-value is changed to those values by means of acidification with an aqueous solution of an organic and/or inorganic acid. 5. A method according to claim 4, characterized in that the acid is selected from citric, oxalic, tartaric, hydrochloric, nitric and/or sulphuric acid, preferably citric acid. 6. A method according to claims 4 and .5, characterized in that the aqueous solution contains from 1 to 10% by weight citric acid, preferably 5%. 7. A method according to claims 1 to 6, characterized in that the aqueous solution which contains the salt of the anti-scaling agent and the aqueous solution of the organic and/or inorganic acid are mixed with each other before the polymerization reaction. 8. A method according to claim 7, characterized in that the aqueous solution which contains the salt of the anti-scaling agent and the aqueous solution of the organic and/or inorganic acid are mixed with each other before being applied to the internal walls of the po lymerization reaccer. 9. A method according to claim 8, characterized in that the mixture thereby obtained is applied to the internal walls of the polymerization reactor in a stream of vapour. 10. A method according to claim 9, characterized in that the aqueous solution thereby obtained is applied to the internal walls of the polymerization reactor at a pressure in the range between 2 and 20 bar. 11. A method according to claim 10, characterized in that the aqueous solution thereby obtained is applied to the internal walls of the polymerization reactor for a period of time of from 15 to 45 seconds. 12. A method according to claim 7, characterized in that the aqueous solution which contains the salt of the anti-scaling agent and the aqueous solution of the organic and/or inorganic acid are mixed with each other on the wall. 13. A method according to claim 1, characterized in that the aldehyde is formaldehyde/ the phenolic compound is 1-naphthol and the aromatic carboxylic acid hydroxylated at the aromatic nucleus is 2,4-dihydroxybenzoic acid. ' 14. A method according to claim 1, characterized in that the ar.ti-scaling agent is EVERCLEAN® 104NS. 15. A method according to claim 1, characterized in that the aqaeous solution contains 4-8% by weight of the alkali metal and/or alkaline earth metal salt of the anti-scaling agent. I6. A method according to claim 1, characterized method for applying an aqueous solution substantially as here in described with reference to he accompanying drawings.

Full Text

Method for the application of anti-fouling agent3 The present invention relates to a method for applying anti-scaiinc agents used in the polymerization cf vinyl chloride, vinyl acetate or mixtures thereof. Frier art
The anti-scaling agents normally used in the polymerization cf vinyl chloride and/or vinyl acetate are products which can be obtained by condensation of formaldehyde and 1-naphthol, such as, for example, these described in European patent application Er-52412. European patent application EP-942 93 6, incorporated herein by reference, describes anti-scaling agents which comprise a product of
condensation cf an aldehyde, a phenolic compound and an aromatic carboxylic acid hydrcxylated at the aromatic nucleus. Preferably the aldehyde is formaldehyde, the phenolic compound is 1-naphthol and the aromatic carboxylic acid hydroxylated at the aromatic nucleus is
selected from salicylic acid, 4-hydroxybenzoic acid, a,
P, or y-resorcylic acid, 2,3-dihydroxybenzoic acid, 2,5-dihydrcxybenzoic acid, 2-hydroxy-5-methoxybenzoic~ acid or 6-hydroxy-2-naphthoic acid; of these, the one greatly preferred is P-resorcylic acid (that is, 2,4-dihydroxybenzoic acid) , Statement of invention
An anti-contaminating agent (or anti-scalirig agent) , in order to be effective and economically suitable for the production of PVC in suspension (PVC/S) , must satisfy the following conditions:
• it must be stable, readily meterable and readily applicable with vapour under pressure (the polymerize* tion reactcr must in fact be kept closed in order to

avoid very dangerous contaminations owing to the emission of gaseous vinyl chloride);
• it must have an elevated capacity for coagulating
rapidly upon variation in the pH-value at the moment
when it comes into contact with the vapour (which is
•normally at a pH-value of 9-10);
• it must be able to form a coaaulum having a ce-
latinous appearance and, if possible, be colourless (to
avoid contaminating the finished product).
The coagulum must preferably be of the "tacky gel" type in order to adhere to the internal walls of the reactors and to form a protective film (coating) owing to the action of the heat of the vapour.
The gel deposited on the walls must further be able to penetrate uniformly into the micropores of the surface of the steel in order to prevent the formation of mi-croparticles of FVC which can give rise to the formation of the deposits.
Furthermore, it must not be necessary to heat the internal walls of the reactor in order to promote the formation of the protective film; such an operation would in fact involve a delay in the production cycle; after the application, the protective film must be, among other things, strong enough to allow washing with water (pH-value 7) for the removal from the reactor of contaminating residues; the total application time must finally be as short as possible and require simple apparatuses which ensure * reliable and homogeneous application of the product.
Results of this type are normally achieved by applying, with vapour under pressure, an aqueous solution containing 4-8% by weight anti-contaminating agent, at least 12-18% of which must remain on the internal walls of the reactor in the form of a protective film (such a

method is described, for example, in "Fine Chemicals for PVC/S", Chapter 5, 1999, published by CIRS Spa, incorporated herein by reference); the method in question in fact allows extended and economical application cycles whereas mechanical or gas-operated spray apparatuses are not presently capable of achieving the above-mentioned objectives.
The present inventicn relates to a novel method for the application of the anti-scaling agent known as EVERCLEAN® 104NS. The preparation of this anti- scaling agent, currently marketed by the owner 3V Sigma Spa, is described in detail in Example 25 of already-mentioned European patent application EP-942936; it refers to a basic aqueous solution having a brown colour and a pH-value of between 11 and 12.4 (normally 11.54) which, as is known in the art, is applied to the internal walls of the reactors for polymerizing vinyl chloride and/or vinyl acetate by spraying in a vapour stream using an apparatus which is similar to that illustrated in Figure 1.
However, this application method allows the desired anti-scaling effect to be achieved only in part. In fact, when operating in such conditions, a coagulum which adheres sufficiently to the internal walls of the reactors, thereby .forming the necessary protective film, is not obtained; on the contrary, the great majority of the anti-scaling agent applied in this manner (approximately 99%) is'collected unchanged at the bottom of the reactor before the start of the polymerization reaction, thus necessitating further applications. It has now been surprisingly found that, by acidifying before application the solution of EVERCLEAN® 104NS to a pH-value" of less than 5 and, preferably, in the range between 2.5 and 4.5, there is obtained coagulation of

the anti- scaling agent which can therefore be applied with greater effectiveness to the walls of the reactor. The problem addressed by the present invention is therefore to provide a method for applying an aquecus solution containing an alkali metal and/or alkaline •earth metal salt, preferably a sodium salt, of an anti-scaling agent comprising a product of condensation of an aldehyde, a phenolic compound and an aromatic car-boxylic acid hydroxy1ated at the aromatic nucleus, characterized in that the pH-value of this aqueous solution is changed to a pH-value of less than 5 and, preferably, in the range between 2.5 and 4.5. Preferably the aldehyde is formaldehyde, the phenolic compound is 1-naphthol and the aromatic carboxylic acid hydroxylated at the aromatic nucleus is 2,4-dihydroxybenzoic acid; the aqueous solution usually contains 4-8% by weight of the alkali metal and/or alkaline earth metal salt of this anti-scaling agent and has a pH-value in the range between 11 and 12.4. The method according to the present invention provides for contact on the wall (that is, on the internal walls of the polymerization reactor) , or in the mixer, between the solution of the anti-scaling agent and a solution of an organic and/or inorganic acid, for example, citric, oxalic, tartaric, hydrochloric, nitric and/or sulphuric acid, which in the presence of vapour ensure a sufficient reduction in the pH-value to allow the coagulation and the formation of the protective film. This aqueous solution preferably contains from 1 to 10% by weight citric acid, preferably 5%. According to the greatly preferred embodiment of the present invention, the salt of the anti-scaling agent and the aqueous solution of the organic and/or inorganic acid are mixed with each other before being ap-

plied to the internal walls of the polymerization"reactor; the mixture of gel and condensate obtained in this manner is applied to the internal wails of the polymerization reactor in a stream of vapour. A suitable apparatus for the application according to the present •invention is, for example, illustrated in Figure 2 (wherein the valves are designated using the letter V). The pressure of the vapour is not binding for the purposes of the present: invention and can vary according to the type of installation; the pressures normally used are, however, in the range between approximately 2 and 2 0 .bar; the application time is normally in the range between 15 and 45 seconds.
As will be appreciated from the Examples reproduced below, which must not be taken to limit the present invention, the method claimed here has the advantage of providing the anti-scaling agent corresponding to European patent application EP-942936 in the form of a coagulate product. This product can therefore be readily applied to the internal walls of a reactor for polymerizing vinyl chloride and/or vinyl acetate, thereby forming a protective film which adheres to the walls at a rate greater than 12% by weight relative to the quantity loaded. In this manner, it is thus possible adequately to protect the reactor by eliminating almost completely the formation of deposits even after long periods of activity, thereby minimizing the necessity of interrupting the production cycle to allow the in-. stallation to be cleaned; the large quantity of anti-scaling agent which remains attached to the wall further allows a reduction in the quantity of anti-scaling agent to be used, with obvious economic advantages. Examples Example 1

There was loaded into a reactor, measuring 10 m3 with walls of stainless steel, provided with an application apparatus of "he type schematically depicted in Figure 1, 1 kg of an aqueous solution containing 6% by weight sodium salt of the anti-scaling agent which is obtained • as described in .Example 25 of European patent application EP-942935. The product was sprayed for 30 seconds on the inside of the reactor with vapour at a pressure - of 5 atmospheres. After the application, the condensate was collected at the bottom of the reactor. The condensate was analyzed in order to determine the pH-value and the possible presence of coagulate. The pH-value was 10 and the condensate contained no precipitate gel .
The condensate was further treated once more with hydrochloric acid until a pK-value of 3.8 was reached and there was finally observed a coagulate of dark brown/black appearance which was found to correspond to more than 99% by weight of the anti-scaling agent initially loaded. Example 2
The procedure described in Example 1 was repeated and the apparatus schematically depicted in Figure 2 was used (wherein 1 litre citric acid at a concentration of 5% by weight was loaded into tank B) -
After spraying in the reactor, the condensate was collected and it was observed that the condensate had a pH-value of 3.2 and 'contained 85% coagulated anti-scaling product (while the remaining 15% was left deposited on the internal walls of the reactor as a protective film). Examples 3-4

The procedure of Examples 1 and 2 was repeat ad with similar results when operating v/ith vapour at a pressure of IS atmospheres. Examples 5-3
The procedure of Examples 1-4 was repeated with similar • results using EVERCLEAN'3 104NS, which is commercially-available, in place of the product obtained according to Example 25 of European patent application EP-942936.

Claims
1. A method for■applying an aqueous solution to che
internal walls of a reactor for polymerizing vinyl
chloride and/cr vinyl acetate, which aqueous solution-
contains a salt of an anti-scaling agent which ccrr.-
■ prises a product of condensation of an aldehyde, a phenolic compound and an aromatic carboxylic acid hydroxy-lated at the aromatic nucleus, the method being characterized in that the pH-value of this aqueous solution is changed to a-pH-vaiue of less than 5.
2. A method according to claim 1, characterized in that the pH-value of the aqueous solution is changed ;c a pH-value in the range between 2.5 and 4.5.
3. A method according to claim 1, characterized in that the salt of the anti-scaling agent is an alkali metal and/or alkaline earth metal salt, preferably sodium.
4. A method according to claims 1 to 3, characterized in that the pH-value is changed to those values by means of acidification with an aqueous solution of an organic and/or inorganic acid.
5. A method according to claim 4, characterized in that the acid is selected from citric, oxalic, tartaric, hydrochloric, nitric and/or sulphuric acid, preferably citric acid.
6. A method according to claims 4 and .5, characterized in that the aqueous solution contains from 1 to 10% by weight citric acid, preferably 5%.
7. A method according to claims 1 to 6, characterized in that the aqueous solution which contains the salt of the anti-scaling agent and the aqueous solution of the organic and/or inorganic acid are mixed with each other before the polymerization reaction.

8. A method according to claim 7, characterized in
that the aqueous solution which contains the salt of
the anti-scaling agent and the aqueous solution of the
organic and/or inorganic acid are mixed with each other
before being applied to the internal walls of the po
lymerization reaccer.
9. A method according to claim 8, characterized in that the mixture thereby obtained is applied to the internal walls of the polymerization reactor in a stream of vapour.
10. A method according to claim 9, characterized in that the aqueous solution thereby obtained is applied to the internal walls of the polymerization reactor at a pressure in the range between 2 and 20 bar.
11. A method according to claim 10, characterized in that the aqueous solution thereby obtained is applied to the internal walls of the polymerization reactor for a period of time of from 15 to 45 seconds.
12. A method according to claim 7, characterized in that the aqueous solution which contains the salt of the anti-scaling agent and the aqueous solution of the organic and/or inorganic acid are mixed with each other on the wall.
13. A method according to claim 1, characterized in that the aldehyde is formaldehyde/ the phenolic compound is 1-naphthol and the aromatic carboxylic acid hydroxylated at the aromatic nucleus is 2,4-dihydroxybenzoic acid. '
14. A method according to claim 1, characterized in that the ar.ti-scaling agent is EVERCLEAN® 104NS.
15. A method according to claim 1, characterized in that the aqaeous solution contains 4-8% by weight of the alkali metal and/or alkaline earth metal salt of the anti-scaling agent.

I6. A method according to claim 1, characterized
method for applying an aqueous solution substantially as here in described with reference to
he accompanying drawings.

Documents:

2244-chenp-2004 abstract granted.pdf

2244-chenp-2004 claims granted.pdf

2244-chenp-2004 description (complete) granted.pdf

2244-chenp-2004 drawings granted.pdf

2244-chenp-2004-claims.pdf

2244-chenp-2004-correspondnece-others.pdf

2244-chenp-2004-correspondnece-po.pdf

2244-chenp-2004-description(complete).pdf

2244-chenp-2004-drawings.pdf

2244-chenp-2004-form 1.pdf

2244-chenp-2004-form 3.pdf

2244-chenp-2004-form 5.pdf

2244-chenp-2004-form18.pdf

2244-chenp-2004-pct.pdf

« Previous Patent

Next Patent »

Patent Number

225541

Indian Patent Application Number

2244/CHENP/2004

PG Journal Number

52/2008

Publication Date

26-Dec-2008

Grant Date

19-Nov-2008

Date of Filing

06-Oct-2004

Name of Patentee

AKZO NOBEL N.V

Applicant Address

VELPERWEG 76, NL-6824 BM ARNHEM,

Inventors:

#	Inventor's Name	Inventor's Address
1	CARLIN FRANCESCO	CORTE ARCO VALARESCO 3, I-35100 PADOVA ,

PCT International Classification Number

C08F2/00

PCT International Application Number

PCT/IT02/00230

PCT International Filing date

2002-04-11

PCT Conventions:

#	PCT Application Number	Date of Convention	Priority Country
1			NA