Process for preparing a bituminous binder composition
View Patent ↗The present invention is directed to a process for preparing a polymer modified bituminous binder composition in the substantial absence of crosslinking agents by heating a bitumen component in a stirred tank to a temperature from 185° C. to 221° C.; adding a block copolymer composition to the bitumen component while the bitumen component is being stirred to form a homogeneous mixture of the bitumen component and the block copolymer composition; and continuing to stir the homogeneous mixture while maintaining the temperature from 185° C. to 221° C. for a period of time from 4 hours to 30 hours thereby forming a cured polymer modified bituminous binder composition. The block copolymer composition utilized in the process comprises a diblock copolymer comprising one block of a monovinylaromatic hydrocarbon and one block of a conjugated diene having a peak molecular weight from 30,000 to 78,000 and a vinyl content from 35 to 80 mol percent based on the number of repeat monomer units in the conjugated diene block, and optionally one or more block copolymers comprising at least two blocks of monovinylaromatic hydrocarbon and at least one block of conjugated diene, the block copolymer selected from linear triblock copolymers having a peak molecular weight that is 1.5 to 3.0 times the peak molecular weight of the diblock copolymer, multiarm coupled block copolymers having a peak molecular weight that is 1.5 to 9.0 times the peak molecular weight of the diblock copolymer, and mixtures thereof, wherein each block copolymer has a vinyl content from 35 to 80 mol percent based on the number of repeat monomer units in the conjugated diene block, wherein when both (i) and (ii) are present in the block copolymer composition, the ratio of (i) to (ii) is greater than 1:1. The present invention is further related to an alternative to this process, a specific class of bituminous binder compositions and concentrates and a specific class of block copolymer compositions.
1. A process for preparing a polymer modified bituminous binder composition in the substantial absence of crosslinking agents, said process comprising the steps of:
a. heating a bitumen component in a stirred tank to a temperature from 185° C. to 221° C.;
b. adding a block copolymer composition to the bitumen component while the bitumen component is being stirred to form a homogeneous mixture of the bitumen component and the block copolymer composition; and
c. continuing to stir the homogeneous mixture while maintaining the temperature from 185° C. to 221° C. for a period of time from 4 hours to 30 hours thereby forming a cured polymer modified bituminous binder composition;
wherein said block copolymer composition comprises
(i) a diblock copolymer comprising one block of a monovinylaromatic hydrocarbon and one block of a conjugated diene having a peak molecular weight from 30,000 to 78,000 and a vinyl content from 35 to 80 mol percent based on the number of repeat monomer units in the conjugated diene block, and
(ii) optionally one or more block copolymers comprising at least two blocks of monovinylaromatic hydrocarbon and at least one block of conjugated diene, the block copolymer selected from linear triblock copolymers having a peak molecular weight that is 1.5 to 3.0 times the peak molecular weight of the diblock copolymer, multiarm coupled block copolymers having a peak molecular weight that is 1.5 to 9.0 times the peak molecular weight of the diblock copolymer, and mixtures thereof, wherein each block copolymer has a vinyl content from 35 to 80 mol percent based on the number of repeat monomer units in the conjugated diene block,
wherein when both (i) and (ii) are present in the block copolymer composition, the ratio of (i) to (ii) is greater than 1:1, and wherein the melt index for the block copolymer composition is from about 20 g/10 min to about 35 g/10 min as determined by ASTM D 1238, condition G (200° C., 5 kg load).
2. The process of claim 1 wherein the ratio of (i) to (ii) in the block copolymer composition is greater than or equal to 3:2 and the amount of block copolymer composition added to the bitumen component is from 2 to 36 weight percent, based on the total weight of the polymer modified bituminous binder composition.
3. The process of claim 2 further comprising the addition of a block copolymer of the formula C-D-C or (C-D)nX during step (b), wherein C is styrene, D is butadiene, isoprene or mixtures thereof n is an integer from 2 to 6 and x is a coupling agent residue and the additional block copolymer is added in an amount up to 30% by weight, of the total amount of block copolymer added.
4. The process of claim 2 wherein the diblock copolymer (i) is of the formula A-B and the optional block copolymer (ii) is selected from block copolymers of the formula A-B-A and (A-B)nX wherein with regard to the formulas A is a block of monovinyl aromatic hydrocarbon, B is a block of conjugated diene, n is an integer from 2 to 6 and X is a coupling agent residue.
5. The process of claim 4 wherein the temperature is from 196° C. to 218° C.
6. The process of claim 4 wherein the block copolymer composition comprises A-B and A-B-A wherein each A is styrene and each B is butadiene, the ratio of (i) to (ii) in the block copolymer composition is from 3:2 to 10:1 the peak molecular weight of A-B is from 48,000 to 78,000 and the vinyl content is from 46 to 70 mol percent based on the number of repeat monomer units in the conjugated diene block of A-B, and the peak molecular weight of A-B-A is 1.8 to 2.5 times the peak molecular weight of A-B and the vinyl content is from 46 to 70 mol percent based on the number of repeat monomer units in the conjugated diene block of A-B-A and the polystyrene content of A-B is from 25 to 35% and the polystyrene content of A-B-A is from 25 to 35%.
7. The process of claim 4 wherein the block copolymer composition comprises A-B and (A-B)nX wherein each A is styrene, each B is butadiene, and n is 2 to 4, the ratio of (i) to (ii) in the block copolymer composition is from 3:2 to 10:1 the peak molecular weight of A-B is from 48,000 to 78,000 and the vinyl content from 46 to 70 mol percent based on the number of repeat monomer units in the conjugated diene block of A-B, and the peak molecular weight of (A-B)nX is 1.8 to 5.0 times the peak molecular weight of A-B and the vinyl content is from 46 to 70 mol percent based on the number of repeat monomer units in the conjugated diene block of (A-B)nX, and A-B has a polystyrene content from 25 to 35% and (A-B)nX has a polystyrene content from 25 to 35%.
8. The process of claim 4 wherein the polymer modified bituminous binder composition produced is in the form of a concentrate having from 6 to 30 weight percent block copolymer composition, based on the total weight of the concentrate.
9. The process of claim 8 which further comprises the step of diluting the homogeneous mixture either during or after the curing of the polymer of the polymer modified binder composition.
10. The process of claim 4 wherein the block copolymer composition is a diblock copolymer composition of the formula A-B wherein A is styrene and B is butadiene, the polystyrene content is from 25% to 35%.
11. The process of claim 4 wherein the amount of block copolymer composition added to the bitumen component is from 2 to 10 weight percent, based on the total final weight of the polymer modified bituminous binder composition to be used.
12. The process of claim 2 wherein the temperature is from 198° C. to 216° C.; the block copolymer composition comprises (i) the diblock copolymer of the formula A-B wherein A is styrene and B is butadiene, the peak molecular weight is from 48,000 to 78,000, the vinyl content is from 50 to 65 mol percent based on the number of repeat monomer units in the conjugated diene block, and the diblock copolymer has a polystyrene content from 22 to 37% and (ii) the multiarm coupled block copolymer of the formula (A-B)2X wherein each A is styrene and each B is butadiene, the peak molecular weight is from 1.8 to 5.0 times the peak molecular weight of the diblock copolymer, X is the residue of a coupling agent, the vinyl content is from 50 to 65 mol percent based on the number of repeat monomer units in the conjugated diene block, and the multiarm block copolymer has a polystyrene content from 22% to 37%.
13. A bituminous binder composition substantially free of cross-linking agents, said bituminous binder composition comprising:
a. 64 to 98% by weight of a bitumen component; and
b. 2 to 36% by weight of a block copolymer composition comprising
(i) a diblock copolymer comprising one block of a monovinylaromatic hydrocarbon and one block of a conjugated diene having a peak molecular weight from 30,000 to 78,000 and a vinyl content from 35 to 80 mol percent based on the number of repeat monomer units in the conjugated diene block, and
(ii) a block copolymer comprising at least two blocks of monovinylaromatic hydrocarbon and at least one block of conjugated diene, the block copolymer selected from linear triblock copolymers having a peak molecular weight that is 1.5 to 3.0 times the peak molecular weight of the diblock copolymer, multiarm coupled block copolymers having a peak molecular weight that is 1.5 to 9.0 times the peak molecular weight of the diblock copolymer, and mixtures thereof, wherein each block copolymer has a vinyl content from 35 to 80 mol percent based on the number of repeat monomer units in the conjugated diene block,
wherein the melt index for the block copolymer composition is from about 20 g/10 min to about 35 g/10 min as determined by ASTM D 1238, condition G (200° C., 5 kg load) and wherein the ratio of (i) to (ii) in the block copolymer composition is greater than 1:1.
14. The bituminous binder composition of claim 13 wherein the diblock copolymer (i) is of the formula A-B and the block copolymer (ii) is selected from block copolymers of the formula A-B-A and (A-B)nX wherein with regard to the formulas A is a block of monovinyl aromatic hydrocarbon, B is a block of conjugated diene, n is an integer from 2 to 6 and X is a coupling agent residue.
15. The bituminous binder composition of claim 14 wherein the block copolymer composition comprises A-B and A-B-A wherein each A is styrene and each B is butadiene, the peak molecular weight of A-B is from 48,000 to 78,000 and the vinyl content is from 46 to 70 mol percent based on the number of repeat monomer units in the conjugated diene block of A-B, and the peak molecular weight of A-B-A is 1.8 to 2.5 times the peak molecular weight of A-B and the vinyl content is from 46 to 70 mol percent based on the number of repeat monomer units in the conjugated diene block of A-B-A, and the polystyrene content of A-B is from 25 to 35% and the polystyrene content of A-B-A is from 25 to 35%.
16. The bituminous binder composition of claim 14 wherein the block copolymer composition comprises A-B and (A-B)nX wherein each A is styrene, each B is butadiene, and n is 2 to 4, the peak molecular weight of A-B is from 48,000 to 78,000 and the vinyl content from 46 to 70 mol percent based on the number of repeat monomer units in the conjugated diene block of A-B, and the peak molecular weight of (A-B)nX is 1.8 to 5.0 times the peak molecular weight of A-B and the vinyl content is from 46 to 70 mol percent based on the number of repeat monomer units in the conjugated diene block of (A-B)nX, and A-B has a polystyrene content from 25 to 35% and (A-B)nX has a polystyrene content from 25 to 35%.
17. The bituminous binder composition of claim 14 further comprising the addition of a block copolymer of the formula C-D-C or (C-D)nX during step (b), wherein C is styrene, D is butadiene, isoprene or mixtures thereof, n is an integer from 2 to 6 and X is a coupling agent residue, and the additional block copolymer is added in an amount up to 30% by weight, of the total amount of block copolymer added.
18. A process for preparing a polymer modified bituminous binder composition in the substantial absence of crosslinking agents, said process comprising the steps of:
a. heating a bitumen component in a stirred tank until it reaches a molten state;
b. adding a block copolymer composition to the bitumen component;
c. raising the temperature of the bitumen component and block copolymer composition to from about 185° C. to about 221° C. while stirring the bitumen component and block copolymer composition in order to form a homogeneous mixture of the bitumen component and the block copolymer composition; and
d. continuing to stir the homogeneous mixture while maintaining the temperature for a total period of time from about 4 hours to about 30 hours until a cured polymer modified bituminous binder composition is obtained;
wherein said block copolymer composition comprises
(i) a diblock copolymer comprising one block of a monovinylaromatic hydrocarbon and one block of a conjugated diene having a peak molecular weight from 30,000 to 78,000 and a vinyl content from 35 to 80 mol percent based on the number of repeat monomer units in the conjugated diene block of the diblock copolymer, and
(ii) optionally a block copolymer comprising at least two blocks of monovinylaromatic hydrocarbon and at least one block of conjugated diene, the block copolymer selected from linear triblock copolymers having a peak molecular weight that is 1.5 to 3.0 times the peak molecular weight of the diblock copolymer and multiarm coupled block copolymers having a peak molecular weight that is 1.5 to 9.0 times the peak molecular weight of the diblock copolymer wherein each optional block copolymer has a vinyl content from 35 to 80 mol percent based on the number of repeat monomer units in the conjugated diene block of the optional block copolymer,
wherein the melt index for the block copolymer composition is from about 20 g/10 min to about 35 g/10 min as determined by ASTM D 1238, condition G (200° C., 5 kg load) and wherein when both (i) and (ii) are present, the ratio of (i) to (ii) is greater than 1:1.
19. The process of claim 18 wherein the stirring in step (b) is at high shear and the stirring in step (c) is at low shear and the process optionally comprises the further step of diluting the homogeneous mixture either during or after the curing of the polymer modified bituminous binder composition.