Method for rejuvenating a bitumen containing composition
A method for rejuvenating a bitumen containing compositions includes adding to the bitumen containing compositions a distillation residue of cashew nut shell liquid (CNSL). The distillation residue may be obtained by distillation of cashew nut shell liquid up to a temperature of between 250 and 350° C. The bitumen containing composition may be selected from: bitumen, asphalt, roof covering, insulating material, shore covering material, and anti-drum plates.
1. A method for rejuvenating a bitumen containing compositions, said method comprising adding to the bitumen containing compositions a distillation residue of cashew nut shell liquid (CNSL), said distillation residue being obtained by distillation of cashew nut shell liquid up to a temperature of between 250 and 350° C.
2. The method according to claim 1 , wherein the distillation residue has a viscosity which is comprised between 1,000 and 30,000 mPa·s − .
3. The method according to claim 1 , wherein the distillation residue has an average saturation factor of 1 to 5.
4. The method according to claim 1 , wherein the bitumen containing composition is selected from the group consisting of bitumen, asphalt, roof covering, insulating material, shore covering material, and anti-drum plates.
5. The method according to claim 1 , wherein the bitumen containing compositions is in addition made up with one of more of the following substances selected from the group consisting of resin, vegetable resin, oil, vegetable oil, paraffins, polymers and synthetic waxes.
6. A bitumen containing composition which has been rejuvenated by application of a method according to claim 1 .
7. The bitumen containing composition according to claim 6 , wherein the rejuvenated bitumen containing compositions is selected from the group consisting of asphalt, insulating material, roofing material, shore covering material and anti-drum plates.
8. The method according to claim 1 , wherein the distillation residue has a viscosity which is comprised between 1,000 and 10,000 mPa·s −1 .
9. The method according to claim 1 , wherein the distillation residue has a viscosity which is comprised between 1,000 and 2,500 mPa·s −1 .
10. The method according to claim 1 , wherein the distillation residue has a viscosity which is substantially 1,500 mPa·s −1 .
11. The method according to claim 1 , wherein the distillation residue has an average saturation factor of 1.2 to 1.3.
12. The method according to claim 5 , wherein the polymers are selected from the group consisting of EVA, SBS, APP, PE and metallocenes.