Polydienes and diene copolymers having organophosphine functionality
A copolymer and organophosphine technology, which is applied in the field of polydiene and diene copolymers with organophosphine functions, can solve the problems of unpredictable composition selection and polymerization system poisoning
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
preparation example Construction
[0079] The reactive polymer can be prepared by allowing a conjugated diene monomer, optionally with a monomer copolymerizable with the conjugated diene monomer, in the presence of an effective amount of an initiator (i.e., an amount of a phosphorus-containing organolithium compound). Aggregate together to achieve. The introduction of the initiator, conjugated diene monomer, optionally comonomer, and any solvent (if employed) forms the polymerization mixture in which the reactive polymer is formed. The amount of initiator to be employed may depend on factors such as the type of initiator used, purity of ingredients, polymerization temperature, desired rate and conversion of polymerization, desired molecular weight, and the interplay of many other factors.
[0080] In one or more embodiments, the amount of initiator used (i.e., the amount of phosphorus-containing organolithium compound) can be from about 0.05 to about 100 mmol per 100 grams of monomer, in other embodiments from ...
example
[0168] Sample 1: Non-functional polymer for control
[0169] Into a 7.57 L stainless steel reactor equipped with turbine stirrer blades were charged 1.55 kg hexane, 0.39 kg 35.0 wt% styrene / hexane and 2.50 kg 21.8 wt% 1,3-butadiene / hexane. The reactor was charged with 3.44 mL of 1.65M n-butyllithium / hexane, 2.06 mL of 1.60M 2,2-ditetrahydrofurylpropane (DTHFP) / hexane and the batch was heated to 87° C. heat temperature. After approximately 30 minutes of exotherm, drain a portion of the contents into isopropanol with antioxidant (BHT). The polymer was drum dried to yield a polymer with the properties listed in Table 1.
[0170] Sample 2: Synthesis of SBR Initiated by Butyllithium-Vinyldiphenylphosphine Adduct
[0171] Into a 7.57 L stainless steel reactor equipped with turbine stirrer blades were charged 1.55 kg hexane, 0.39 kg 35.0 wt% styrene / hexane and 2.50 kg 21.8 wt% 1,3-butadiene / hexane. The reactor was charged with 3.44 mL of 1.65M n-butyllithium / hexane, 4.36 mL of 1....
PUM
| Property | Measurement | Unit |
|---|---|---|
| glass transition temperature | aaaaa | aaaaa |
| dispersity | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 