Polvamine-polyacryiate dispersant
The invention relates to a liquid dispersant based on polyamine-graft-polyacrylate blend, its preparation and its use in solvent borne systems.
Polyethyleneimine-polymethylmethacrylates are known from US6573313 describing the pre¬paration of a core shell latex obtained by an emulsion radical polymerization process which involves generating radicals on the nitrogen atoms of polyamine, which can then initiate the radical polymerization of acrylates. Products are supposed to be used as gene delivery carriers.
Grafted copolymers used as dispersants are e.g. polyamine-g-polyesters or polyamine-g-polyethers. The publications WOOO/024503, WO04/078333, WO99/049963, WO94/021368 refer to a series of PAl-based dispersants, of which the graft chain is end-cupped with one acid group, obtained from the condensation polymerization of hydroxycarboxylic acids, grafted onto PAl through both neutralization and amidification reactions between acid and amine groups. The graft chains are non-polar. Dispersants are mainly used in non-polar solvent-borne paint systems.
The publications WO01/080987, WO98/019784, US9599947, EP0208041 and WO99/055763, US6583213 claim a series of PAl-based dispersants, of which the graft chains are obtained from the ring-opening polymerization of lactones and/or their derivatives. The graft chain is polyester end-capped with one acid group, obtained by the carboxylic acid initiated ring-opening polymerization of lactones or alkyl substituted lactones, grafted onto PAl through both neutralization and amidification reactions between acid and amine groups; or the graft chain is polyester end-capped with one ethylenically unsaturated group, obtained by 2-hydroxy ethyl acrylate initiated ring-open polymerization of lactones, grafted onto PEI backbone via the Michael addition.
WO05/010109 claims a kind of PAl-based polyether liquid dispersant. The grafting chain is polyether end-capped with one acid group, which is obtained by the esterification of succinic anhydride and CH3-(EO)m-(PO)n-NH2. This polyether chain is grafted onto PAl via both neutralization and amidification reactions. The dispersants are applied in polar organic or water-borne paint systems.

Commonly, the graft chains of the claimed PAI-g-polyesters and PAI-g-polyethers possess high Tg and crystallizability, which confine their uses, e.g. low temperature applications are impossible, the storage stability is not good and so on. Besides that, these dispersants are all prepared by the "graft to" approach, i.e. synthesis the graft side chains first and then graft them onto the PAI backbones, thus at least two or multi-steps are needed for manufacturing.
US2002/143081 discloses amphiphilic nanoparticles comprising a core and a shell. The process for the manufacture of the particles involves graft polymerisation in an aqueous system of a vinylic monomer onto polyethyleneimine. The molecular weights of the graft copolymer and of the polymethylmethacrylate homopolymer range between 500 000 and 1000 000. The polydispersity Mw/Mn of the polymerized vinylic monomer ranges between 1.5 and 3.The core shell particles are used, for example, as drug carriers. It is only mentioned that the polymers find potential applications in leather finishing, paints paper and textile industrials. The use as dispersant is not specifically disclose.
One aspect of the invention is to provide a liquid dispersant having a good storage stability which can be used for low temperature applications and low viscosity applications in solvent based systems.
Thus, the invention relates to a liquid polyamine-g-polyacrylate grafted copolymer blend of the general formula 1 or a mixture of formula 1 and Y
T-(A1,A2)-Y 1
wherein
T is a polyamine or polyimine,
H I
A1 is a bridging bond which is selected from amide ( -^'^V^ ) or imide ( -^'^V^ ).
O 0
A2 is a -N-C- bridging bond,

Y is an acrylate residue of the general formula 2,

wherein,
Ri and R2 are, independently, hydrogen or Ci.2oalkyl, aryl, heteroaryl, substituted aryl,
n is a number of 1 - 1000, and
wherein the polyamine-g-polyacrylate grafted copolymer blend has an average molecular weight of 50 OOOg/mol to 150 000 g/mol and a polydispersity MJM^ greater than 3.
Definitions
The term "grafted copolymer" as used herein refers to a copolymer made by the so called "grafting from" process. Acrylate groups are attached as pendent groups along the polyamine backbone. The side chains are build up after being grafted to the polyamine backbone.
Liquid means no crystallization.
The term "polyamine-g-polyacrylate grafted copolymer blend" means that more than one copolymer is present obtainable by free-radical polymerization (A2 = NC), Michael addition (A2 = N-C) and transesterification (A1 = amide or imide).
The term "polyamine" means a compound comprising two or more primary or secondary amine groups per molecule. Polyamines are selected from poly(C2-6-alkyleneimine), poly-vinylamine, polyallylamine or poly(amide-amine) dendrimer, with a MW of 100 -100,000 g/mol, preferably 500-50,OOOg/mol.
Poly(C2-6-alkyleneimines) are e.g. polypropylene-imine or polyethylene imine, preferably polyethyleneimine.
n is preferably 5 to 100. The polyacrylate chain (n> 1) is obtainable from homo-polymerization of one kind of acrylate monomers, or from random copolymerization of two or more kinds of different acrylate monomers.
Ri is preferably hydrogen or methyl.

R2 is preferably hydrogen or an alkyl chain having 1-20 carbon atoms including linear or branched chains. Examples are methyl, ethyl, propyl, isopropyl, n-butyl, sec. butyl, tert. butyl, n-hexyl, 2-hydroxy ethyl, 2-methoxy ethyl, 2-ethoxy ethyl, bornyl, isobornyl, isodecyl, lauryl, myristyl, stearyl, cyclohexyl.
Aryl is preferably phenyl, naphthyl.
Substituted aryl is preferably substituted phenyl and substituted naphthyl with the substituent of methyl, ethyl, propyl, isopropyl, n-butyl, sec. butyl, tert. butyl, n-hexyl, chloro.
Heteroaryl is preferably bornyl, isobornyl, furfuryl.
Preferred is a liquid polyamine-g-polyacrylate grafted copolymer blend according to claim 1, wherein T is polyethyleneimine, Ri is hydrogen or methyl and Rj is Ci.2oalkyl and n is 5 to 100.
Process
The inventive polyamine-g-polyacrylate grafted copolymer blend is prepared by copolymerizing in an organic solvent a polyamine and an acrylate monomer in the presence of a free radical initiator wherein
1. the weight ratio of polyamine to the acrylate monomer ranges from 1 ;5 to 1:100;
2. the weight ratio of free radical initiator to acrylate monomer ranges from 1:5 to 1:100;
3. the process being carried out in one pot at a temperature of from 10 °C to 200 °C under an inert gas atmosphere,
4. the process comprising at least a transesterification reaction of the acrylate with the polyamine to obtain a polyamine amide or a polyamine imide, a Michael addition reaction of a polyamine with an acrylate monomer to obtain a polyamine acrylate and a grafting polymerisation of a polyamine and acrylate monomers to obtain polyamine-g-polyacrylate.
The invention further relates to a liquid polyamine-g-polyacrylate grafted copolymer blend obtainable by a process according to the above process.

Acrylate monomers can be represented as CH2=CRiCOOR2 where Ri and R2 are, independently, hydrogen or alkyl, aryl, heteroaryl, substituted aryl, such as n-butyl acrylate, methyl acrylate, methyl methacrylate, iso-butyl methacrylate, tert-butyl acrylate, n-butyl methacrylate, 2-hydroxyl ethyl acrylate, 2-hydroxyl ethyl methacrylate, isobornyl acrylate, isobornyl methacrylate, glycidyl methacrylate, glycidyl acrylate, cyclohexyl acrylate, cyclohexyl methacrylate, etc.
Free radical initiators can be selected from 2,2'-azo-bis(isobutyronitrile) (AIBN), potassium persulfate, 2,2'-azobis(2-amidinopropane) dihydrochloride, and alkyl hydro¬peroxides, such as benzoyl peroxide, di-tert-butyl peroxide, t-butyl hydroperoxide, cumene hydroperoxide, p-isopropyl cumene hydroperoxide, p-menthane hydroperoxide, or pinane hydroperoxide, etc.
Preferred is 2,2'-azo-bis(isobutyronitrile).
The weight ratio of polyamine to the acrylate monomer is preferably 1:5 to 1:50. The weight ratio of free radical initiator to acrylate monomer is preferably 1: 5 to 1.50. This weight ratio determines the molecular weight of the polyacrylate moiety.
The reaction temperature is preferably 20°C to 120 °C
Inert gas is preferably nitrogen.
The scheme below is a representative reaction scheme for the preparation of the polyamine-g-polyacrylate grafted copolymer blend.

The transesterification reaction can be described as follows:
, ?' ^ — R2-OH ^- -^ "^1

Polyamine )— NH, + .;:;;:=*\^0, »- Q Polyamine V-N
' ' n R2 '"^^—: -^ H
O O

A polyamine amide is obtained by the above shown transesterification process. In the presence of the free radical initiator the polyamine amide is further reacted to polyamine amid-polyacrylate copolymer of the formula A, wherein Ri and R2 are as defined above.




polyamine V-NHj +
Os
R,

O

~R,

The Michael addition can be described as follows:



Polyamine)—NHj "^

0.
R.

O

^R,

The nucleophilic addition of the polyamine to the unsaturated bond of the acrylate leads to a polyamine acrylate of the formula B, wherein Ri and R2 are as defined above.
The grafting copolymerization can be described as follows


Polyamine ">—NH

initiator

In a grafting from process the polyamine is used as macroinitiator to initiate the free radical polymerization. The acrylate chain is built up to obtain a polyamine-g-polyacrylate of the formula C, wherein Ri and R2 are as defined above.
The radical polymerisation leads to polyacrylates Y.



O.
R.

O

~R.

initiator

The invention further relates to a liquid polyamine-g-polyacrylate grafted copolymer blend comprising a blend of


and
and

and
wherein Ri, and R2 and n is as defined above and wherein the polyamine-g-polyacrylate grafted copolymer blend has an average molecular weight of 50 OOOg/mol to 150 000 g/mol and a polydispersity MJM^ greater than 3.
The blend comprising (A + B + C + Y) is a transparent amber liquids with low Tg and no crystallization. The blend is used as dispersant for all low temperature applications. The dispersants are soluble in various organic solvents in a wide range of non-polar to polar. In applications, the dispersants surprisingly show excellent pigment dispersion effect, especially for TPA paints due to good compatibility of the dispersants with TPAs. As a consequence, the pigment concentrates show low viscosity, which means high pigment loading and therefore high productivity can be achieved. The dispersants show less flocculation, less seeding, high gloss, better chromatic properties, lower viscosity of pigment concentrates, lower temperature storage stability etc. The coatings show high gloss and good chromatic properties, an obvious superior performance to the prior arts are achieved in alkyd, CAB and TPA paint systems.

Dispersant solutions keep stable at lower temperatures (50% solutions, stable at < -15°C for at least 2 weeks), which means the invention product is easy in use, and can be applied in the low temperature applications.
In addition, the glass transition temperature, crystallizability, and polarity of the dispersants can be easily adjusted by adjusting the type of acrylate monomer, the ratio of acrylate monomer to polyamine, the ratio of free radical initiator to acrylate monomer, and reaction conditions.
Accessibility of the starting materials
Polyethyleneimine with different molecular weight are commercial products from Nippon
Shukubai.
Polyvinylamine with the MW 10,000 are commercially available from Mitsubishi Kasei.
Polyallylamine with MW of 10,000 are commercially available from Nitto Boseki.
Polypropyleneimine dendrimer are commercially available from DSM Fine Chemicals, and
poly(amide-amine) dendrimer are commercially available from Aldrich Chemical Company.
Acrylate monomers, 2,2'-azo-bis(isobutyronitrile) and t-butyl hydroperoxide are normal
commercial products.
Use
The polyamine-g-polyacrylate grafted copolymer blend can be used as dispersant in a broad application fields, such as coatings, inks, electronic materials, especially in low temperature and low viscosity applications.
The inventive polyamine-graft-polyacrylates are used in solvent based systems such as in solvent based organic and inorganic pigments dispersion e.g. in alkyd, CAB (cellulose acetate butyrate), UV (Ultraviolet) and TPA (thermoplastic acrylate) paint systems, in general industrial coatings especially in automotive coatings, as well as in printing inks and graphic arts.

EXAMPLES Example 1
The mixture of PEI SP-200 (MW 10,000) 5.0 g, BA 50.0 g, AIBN 6.3 g, and toluene 85 mL were stirred under nitrogen at 35 °C for 24 h, and then 60 °C for 70 h. Then, toluene was removed under vacuum system. The product was obtained as a yellow liquid.

Abbreviations of chemicals and their suppliers
ABBREVIATION CHEMICAL NAME SUPPLIER
PEI Polyethyleneimine Nippon Shukubai
PVA Polyvinylamine Mitsubishi Kasei
PAA Polyallylamine Nitto Boseki
DPPI Dendritic polypropyleneimine DSM Fine Chemicals
DPAMAM Dendritic poiy(amide-amine) Aldrich Chemical Company
TEPA Tetraethylene pentamine

BA n-Butyl acrylate

MA Methyl acrylate

MMA Methyl methacrylate

i-BMA Iso-butyl methacrylate

t-BA Tert-butyl acrylate

BMA n-Butyl methacrylate

AIBN 2,2'-Azo-bis(isobutyronitrile)

TBHP t-Butyl hydroperoxide

d-TBP Di-tert-butyl peroxide

BPO Benzoyl peroxide

Example 2-64
Example 2-64 were all prepared in a similar manner as Example 1 except that the type and amounts of polyamine, acrylate monomer, free radical initiator, and the reaction condition were varied as detailed in Table 1 below.
Table 1.

Example Raw materials Reaction condition Appearance

Polyamine Acrylate monomer Free radical initiator

2 PEl, SP-200 5.0 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60 "C for 70 h yellow liquid
3 PEl, SP-200 5.0 g BA 150 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h viscous yellow liquid
4 PEl SP-018 (MW 1,800) 5.0 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h yellow liquid
5 PEl SP-006 (MW 600) 5,0 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h yellow liquid
6 TEPA 3.0 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h yellow liquid
7 PVA200 (MW 10,000) 3.3 g BA 100 g AIBN 6.3 g 35 X for 24 h 60 °C for 70 h viscous yellow liquid
8 PAA150 (MW 10,000) 4.4 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h viscous yellow liquid
9 DPPI CU-D32 (MW 3,500) 8.5 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h yellow liquid
10 DPPI CU-D64 (MW 7,100) BA 100 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h yellow liquid

8.5 g
11 DPAMAM(G3) (MW 6,900) 16.7 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h yellow liquid
12 DPAMAM(G4) (MW 14,200) 17.1 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h yellow liquid
13 PEI, SP-200 5.0 g BA 100 g AIBN 5.0 g 35 °C for 24 h 60 °C for 70 h yellow liquid
14 PEI, SP-200 5.0 g BA 100 g AIBN 3.8 g 35 °C for 24 h 60 "C for 70 h viscous yellow liquid
15 PEI, SP-200 5.0 g BA 100 g AIBN 2.5 g 35 °C for 24 h 60 "C for 70 h viscous yellow liquid
16 PEI, SP-200 5.0 g BA 100 g AIBN 1.7g 35 °C for 24 h 60 °C for 70 h viscous yellow liquid
17 PEI, SP-200 5.0 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60 °C for 30 h yellow liquid
18 PEI, SP-200 5.0 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60°Cfor lOOh yellow liquid
19 PEI, SP-200 5.0 g BA 100 g AIBN 6.3 g 35 °C for 24 h 60°Cfor120h yellow liquid
20 PEI, SP-200 5.0 g BA 100 g AIBN 6.3 g 35 °C for 24 h 90 °C for 20 h yellow liquid
21 PEI, SP-200 5.0 g BA 100 g AIBN 6.3 g 35 °C for 24 h 90 °C for 50 h yellow liquid
22 PEI, SP-200 5.0 g BA 100 g AIBN 6.3 g 35 °C for 24 h 90 °C for 80 h yellow liquid
23 PEI, SP-200 5.0 g BMA 111 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h viscous yellow liquid
24 PEI, SP-200 5.0 g MA 67 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h viscous yellow liquid

25 PEI, SP-200 5.0 g MMA 78 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h solid
26 PEI, SP-200 5.0 g t-BA 100g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h viscous yellow liquid
27 PEI, SP-200 5.0 g i-BMA 111 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h viscous yellow liquid
28 PEI, SP-200 5.0 g BA 100 g TBHP 6.9 g 35 "C for 24 h 90 "C for 70 h yellow liquid
29 PEI, SP-200 5.0 g BA 100 g TBHP 5.5 g 35 °C for 24 h 90 °C for 70 h yellow liquid
30 PEI, SP-200 5.0 g BA lOOg TBHP 4.1 g 35 °C for 24 h 90 °C for 70 h yellow liquid
31 PEI, SP-200 5.0 g BA lOOg TBHP 2.8 g 35 °C for 24 h 90 °C for 70 h viscous yellow liquid
32 PEI, SP-200 5.0 g BA 100 g TBHP 1.4 g 35 °C for 24 h 90 °C for 70 h viscous yellow liquid
33 PEI, SP-200 5.0 g BA 100 g TBHP 6.9 g 35 °C for 24 h 120 X for 20 h yellow liquid
34 PEI, SP-200 5.0 g BA lOOg TBHP 6.9 g 35 °C for 24 h 120°Cfor40h yellow liquid
35 PEI, SP-200 5.0 g BA 100 g TBHP 6.9 g 35 °C for 24 h 120°Cfor80h yellow liquid
36 PEI, SP-200 5.0 g BA 100 g d-TBP 5.6 g 35 °C for 24 h 90 °C for 70 h yellow liquid
37 PEI, SP-200 5.0 g BA 100 g d-TBP 3.4 g 35 °C for 24 h 90 °C for 70 h yellow liquid
38 PEI, SP-200 5.0 g BA lOOg BPO 10.6 g 35 °C for 24 h 90 °C for 70 h yellow liquid
39 PEI, SP-200 5.0 g BA 100 g BPO 6.4 g 35 °C for 24 h 90 °C for 70 h yellow liquid
40 PEI, SP-200 BA80g AIBN 35 °C for 24 h yellow liquid

5.0 g MMA16g 6.3 g 60 X for 70 h
41 PEI, SP-200 5.0 g BA60g MMA 31 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
42 PEI, SP-200 5.0 g BA60g MA27g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
43 PEI, SP-200 5.0 g BABOg t-BA 40 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h yellow liquid
44 PEI, SP-200 5.0 g BA60g BMA 44 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
45 PEI, SP-200 5.0 g BA40g MMA 47 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
46 PEI, SP-200 5.0 g BA20g MMA 62 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h solid
47 PEI, SP-200 5.0 g MA54g i-BMA 22 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
48 PEI, SP-200 5.0 g MA40g i-BMA 44 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
49 PEI, SP-200 5.0 g MA40g MMA 31 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h solid
50 PEI, SP-200 5.0 g MA40g t-BA 40 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
51 PEI, SP-200 5.0 g MA27g i-BMA 67 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
52 PEI, SP-200 5.0 g MA13g i-BMA 89 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
53 PEI, SP-200 5.0 g MMA 31 g t-BA 60 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid

54 PEI, SP-200 5.0 g i-BA 40 g t-BA 60 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h yellow liquid
55 PEI, SP-200 5.0 g i-BA 60 g t-BA 40 g AIBN 6.3 g 35 °C for 24 h 60 X for 70 h yellow liquid
56 PEI, SP-200 5.0 g BMA 66 g t-BA 40 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h yellow liquid
57 PEI, SP-200 5.0 g BMA 44 g t-BA 60 g AIBN 6.3 g 35 °C for 24 h 60 °C for 70 h yellow liquid
58 PEI, SP-200 5.0 g BMA 66 g i-BA 40 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
59 PEI, SP-200 5.0 g BMA 44 g i-BA 60 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h yellow liquid
60 PEI, SP-200 5.0 g BA40g MMA 23 g i-BA 30 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
61 PEI, SP-200 5.0 g BA60g MMA 16 g i-BA 20 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid
62 PEI, SP-200
5.0 g MA13g BMA 67 g t-BA 20 g AIBN
6.3 g 35 X for 24 h
60 X for 70 h yellow liquid
63 PEI, SP-200 5.0 g MA20g BMA 44 g t-BA 30 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h yellow liquid
64 PEI, SP-200 5.0 g MMA 23 g BMA 44 g t-BA 30 g AIBN 6.3 g 35 X for 24 h 60 X for 70 h viscous yellow liquid

The molecular weight of the examples was listed in Table 2 below. Table 2.

Example Mn Mw Mw/Mn
2 8,650 42,400 4.9
12 21,600 83,000 3.8
22 18,400 81,200 4.4
26 10,060 52,300 5.2
27 9,320 45,700 4.9
43 13,300 42,100 3.2
54 14,040 63,200 4.5
62 10,050 55,300 5.5
Mw : weight average molecular weight Mn: number average molecular weight
Performance Screening
In order to test the dispersion effect of the obtained samples. Resin Free Pigment Concentrates were prepared according to the Formulation 1. The mill base was dispersed in Scandex Shaker for 1.5 h with the help of glass beads. Afterwards the mill base was filtered and stored at room temperature overnight. Let-downs (Formulation 2) for testing were based on a stoving enamel, a CAB base coat and a TPA base coat. Formulation 3 shows the paint formulations for the stoving enamel, CAB paints and TPA paints. The paint preparation was mixed under high speed stirring for 5 minutes at 2000 rpm, and applied on polyester film with a 35 - 75 [^m film thickness. After preparing draw-downs, the rest of paints were diluted 1:1 with butyl acetate for a pour-out test.
First, the competitive grades were synthesized according to patents, e.g. WO 9421368, USP 6583213, and USP 6599947 and so on. The performance of these grades was tested according to Formulations 1, 2, and 3. Results showed competitive product A performs better than the others, which was then taken as a representative dispersant in the text.

Formulations 1. Preparation of Pigment Concentrates

Ingredients/Pigment Concentrate No. 1 2 3
1) Dispersant (100% solid) 5.35 5.40 3.62
2) 1-methoxy-2-propyl acetate (MPA) 19.65 26.60 31.38
3) Pigment White 21 75.00
4) Pigment Black 7 (Special Black 100) 18.00
5) Pigment Blue 15:2 15.00
6) 3.0 mm glass beads 100.0 100.0 100.0
Total (g) 200.0 150.0 150.0
Formulations 2. Let-down systems

a) Stoving Enamel Vialkyd AC 451 68.4
Maprenal MF 650 31.4
Ciba®EFKA®3030 0.2
Total 100
b) CAB base coat CAB 531-1 11.2
Butyl acetate 51.9
Uracron CR 226 XB 32.1
Uramex MF 821 4.8
Total Paraloid B66 100.0 40
c) TPA base coat

Xylene 8.0
Toluene 38
MPA 13.5
Ciba®EFKA®3030 0.5
Total 100.0
Vialkyd AC 451. alkyd resin, UCB Maprenal MF 650: melamine resin, Degussa

Ciba®EFKA®3030 is a modified polysiloxane solution slip and levelling agent
CAB-531 cellulose acetate butyrate material commercially available from Eastman Chemical
Uracron CR 226 XB: DSM Coating Resins Uracron CR, OH acrylic
Uramex MF 821: DSM Coating Resins Uramex (amino)
Paraloid 866 thermoplastic acrylate, Rohm Haas
Formulation 3. CAB and stoving enamel paints
Code 1 2 3
Let-down (formulation 2a or 2b) 9.0 7.5 7.0
PC white (No. 2 in Formulation 1) - 2.0 3.0
PC color (No. 4 - 6 in Formulation 1) 1.0 0.5
Total/g PO.O |l0.0 |l0.0
The performance of examples 1 - 64 in Table 1 were tested according to Formulations 1, 2 and 3. It was observed that the pigment concentrates flow well and their viscosities were comparable or lower than the competitive product A. The rheological behavior of the pigment concentrates was measured with a Thermo-Haake RheoStress 600 equipment under the CR mode. The initial viscosities (r|o) and dynamic viscosities (nO of the pigment concentrations are listed in Table 3. According to the viscosity curves, the Pigment White concentrate (PW 21) is a Newtonian flow, while the Pigment Black concentrate (Special Black-100) is a pseudoplastic flow. The Pigment Blue concentrate (PB 15:2) is plastic flows with thixotropic properties, but could easily flow under a low shear stress (T, in Table 3).
Table 3. Rheological data of Pigment Concentrates
\ I Special Black I
PW21 PB15:2
100
Example ,
Ho Ht Ho Ht T/Pa Ht
mPas mPas mPas mPas (Yield point) mPas
Competitive
1000 360 >1000 300 50 150
product A
2 480 210 620 160 30 90
12 450 200 600 155 30 85
22 700 330 380 80 25 75

26 520 220 330 70 20 70
27 750 300 400 80 25 75
43 560 250 370 80 35 90
54 450 210 350 65 18 60
62 340 180 520 150 25 65
Competitive product A is prepared according to USP6583213, Ex. 9. (2-Hydroxyethylacrylate- epsilon-caprolactone-, .delta.-valerolactone (1:8:8) PEl (13:1)
Tested in stove enamel paint, CAB paint and especially in TPA paint, the performance of the dispersants was generally very good with satisfactory results, e.g. high gloss (on average, above 80 at 60°), no seeding, no rub-out, good color strength, etc (Table 4).
Table 4. The dispersion effect in TPA paint system

Example Gloss of
20760°
white drawdow black m blue Seedin white g
black blue Gloss c 20°/60° white )f pour 0 black Jt blue
Competitive product A 51/76 46/76 60/80 5 3 4 63/83 62/81 42/77
2 72/82 75/83 78/85 1 1 1 70/81 74/83 54/82
9 70/81 76/84 75/83 2 1 1 69/80 75/84 52/80
12 71/82 72/83 79/87 2 2 1 70/82 72/82 58/85
19 69/80 74/82 75/81 2 1 2 67/79 71/80 51/79
22 74/83 74/84 76/83 1 1 2 71/82 73/82 52/80
26 71/80 74/82 77/84 2 1 1 69/80 73/83 52/81
27 73/82 74/84 77/86 1 1 1 71/82 72/82 55/83
40 70/81 68/79 76/83 2 2 2 67/78 70/80 50/79
42 71/83 74/80 77/85 1 2 1 69/80 72/80 53/83
43 70/81 76/84 75/82 2 1 2 70/80 75/84 52/80

59 71/81 73/82 76/84 1 2 2 69/79 71/82 53/81
64 73/83 73/82 79/86 1 1 1 71/81 72/81 55/83
Explanation results: s = seeding; 1 = no seeding, and 5 = a lot of seeding
In the solubility test, samples were dissolved in various solvents first with a concentration of 50% (w/w), and then kept for one month at 25°C and -15°C, respectively. Obviously, the dispersants of this invention have improved solubility compared to that of competitive products (Table 5). It indicates that the invention samples have less crystallizability, and their compatibility in various solvent systems is better than that of the competitive product A.
Table 5. Solubility of samples in various solvent (50%, w/w)

Explanation results: +: solubility is good, and the solution is clear;
+ -: solubility is medium and partially crystallized; -: solubility is poor and totally crystallized.

Example MPA n-butyl acetate 2-Butanone Xylene

25°C -15°C 25°C -15°C 25°C -15°C 25°C -15X
Product A + - - + - - + + - + + -
2 + + + + + + + +
12 + + + + + + + +
26 + + + + + + + +
27 + + + + + + + +
40 + + + + + + + +
43 + + + + + + + +
54 + + + + + + + +
62 + + + + + + + +

Claims:
1. A liquid polyamine-g-polyacrylate grafted copolymer blend of the general formula 1 or a
mixture of formula 1 and Y

wherein
T is a polyamine or polyimine,

wherein,
Ri and Ra are, independently, hydrogen or Ci.2oa!kyl, aryl, heteroaryl, substituted aryl.
n is a number of 1 - 1000,
wherein the polyamine-g-polyacrylate grafted copolymer blend has an average molecular weight of 50 OOOg/mol to 150 000 g/mol and a polydispersity Mw/Mp greater than 3.
2. A polyamine-g-polyacrylate grafted copolymer blend according to claim 1, wherein T is polyethyleneimine, Ri is hydrogen or methyl and R2 is Ci.2oalkyl and n is 5 to 100.
3. A process for the preparation of a polyamine-g-polyacrylate grafted copolymer blend as defined in claim 1, by copolymerizing in an organic solvent a polyamine and an acrylate monomer in the presence of a free radical initiator wherein

1. the weight ratio of polyamine to the acrylate monomer ranges from 1:5 to 1:100;
2. the weight ratio of free radical initiator to acrylate monomer ranges from 1:5 to 1:100;

3. the process being carried out in one pot at a temperature of from 10 °C to 200 °C
under an inert gas atmosphere,
4. the process comprising at least a transesterification reaction of the acrylate with the
polyamine to obtain a polyamine amide or a poiyamine imide, a Michael addition
reaction of a polyamine with an acrylate monomer to obtain a polyamine acrylate and
a grafting polymerisation of a polyamine and acrylate monomers to obtain polyamine-
g-polyacrylate.
4. A liquid polyamine-g-polyacrylate grafted copolymer blend obtainable by a process
according to claim 3.
5. A liquid polyamine-g-polyacrylate grafted copolymer blend comprising a blend of

wherein Ri and R2 and n is as defined in claim 1 or 2 and wherein the polyamine-g-polyacrylate grafted copolymer blend has an average molecular weight of 50 OOOg/mol to 150 000 g/mol and a polydispersity MJM^ greater than 3.
6. Use of a polyamine-g-polyacrylate grafted copolymer blend according to claim 1, as
dispersant.