Vinyl functional interpenetrating network polymers produced by physically mixing vinyl functional resins with thermoplastic resin compositions, methods of use and methods of preparation
The present disclosure pertains to methods and/or systems for making a SIPN and/or an IPN by physically mixing at least one vinyl functional thermoset with at least one thermoplastic resin. For example, a method of producing a resin composition comprising: mixing at least one vinyl functional thermoset resin with at least one thermoplastic resin wherein: the two resins are sufficiently miscible at a mixing viscosity of at least at least 5,000 cPs measured at the temperature of mixing and the mixing results in sufficient laminar flow such that a substantial portion of the resin mixture forms an IPN and/or a SIPN. The IPNs and/or SPINs formed have one or more superior properties over mixtures of the same resins.
1. A method of producing a pseudo interpenetrating network (SIPN) composition or an interpenetrating polymer network (IPN) composition, comprising:
physical alloy mixing of at least one vinyl functional thermoset resin with at least one thermoplastic resin;
wherein the two resins are miscible when the mixture has a viscosity during mixing of at least 10,000 cPs measured at the temperature of mixing, and wherein the mixture has a Reynolds number during mixing that is below 2100.
2. The method of claim 1 , wherein the two resins are sufficiently miscible when the mixture has a viscosity during mixing of at least 5000 cPs at the temperature of mixing and the two resins are capable of forming a SIPN or an IPN while still in the liquid state.
3. The method of claim 1 , wherein the two resins are sufficiently miscible at a mixing viscosity of at least 5,000 cPs measured at the temperature of mixing and the mixing results in sufficient laminar flow such that a substantial portion of the resin mixture forms an IPN or a SIPN while still in the liquid state.
4. The method of claim 1 , wherein the two resins are sufficiently miscible at a mixing viscosity of at least 5,000 cPs measured at the temperature of mixing and upon sufficient laminar flow mixing the two resins form an IPN or a SIPN resin composition while still in the liquid state that is substantially free of thermoplastic micelles.
5. The method of claim 4 , wherein the SIPN composition or IPN composition is cured, and upon curing comprises one or more of:
i) a flexural yield stress greater than 45 MPa;
ii) an elongation in the range of between 6.5% to 35%;
iii) a HDT in the range of between 65 and 125° C.;
iv) an unnotched Izod strength of greater than 3 Joules/cm;
v) a modulus in the range of between 1.5 GPa and 3.8 GPa;
vi) a linear shrinkage less than 2%; or
vii) a volume shrinkage of less than 6%.
6. The method of claim 4 , wherein the SIPN composition or IPN composition is cured, and upon curing comprises:
i) a flexural yield stress greater than 45 MPa;
ii) an elongation in the range of between 6.5% to 35%;
iii) a HDT in the range of between 65 and 125° C.;
iv) an unnotched Izod strength of greater than 3 Joules/cm;
v) a modulus in the range of between 1.5 GPa and 3.8 GPa;
vi) a linear shrinkage less than 2%; and
vii) a volume shrinkage of less than 6%.
7. The method of claim 1 , wherein the mixture has a viscosity that produces a substantial portion of laminar flow during the mixing.
8. The method of claim 1 , wherein the Reynolds number in the mixer during mixing of the resin composition is below 2000.
9. A method of producing a moulded product comprising:
a) selecting at least one liquid IPN or SIPN resin composition produced according to the method of claim 1 ;
b) catalyzing the IPN or SIPN with at least one catalyzing agent; and
c) pouring or pumping the resin composition into a mould and allowing it to cure.
10. A continuous liquid interpenetrating polymer network (IPN) production process, comprising:
pumping a resin mixture through a heat exchanger/chiller plant and static mixer configuration of sufficient length to produce laminar flow for the creation of a liquid IPN at a predetermined exit temperature of about 14° C. for thermoset/polycaprolactone IPNs of about 4° C. for VINNAPAS 8588/thermoset liquid IPNs, and exit temperatures lower than 4° C. for some higher molecular weight polystyrene and acrylic thermoplastic thermoset IPNs.
11. The method of claim 1 , wherein the method further comprises dissolving the at least one thermoplastic resin is dissolved in a chlorinated solvent selected from one or more of the following: trichloroethane, dichloroethane, and carbon tetrachloride, and then mixing the solution with the at least one vinyl functional thermoset resin.
12. The method of claim 11 , wherein the at least one vinyl functional thermoset resin is a liquid vinyl functional thermoset.
13. The method of claim 12 , wherein the at least one thermoplastic resin is 10% to 30% PMMA, relative to the total weight of polymers in the SIPN composition or IPN composition.
14. The method of claim 12 , wherein the at least one thermoplastic resin is 10% to 30% polystyrene, relative to the total weight of polymers in the SIPN composition or IPN composition.
15. The method of claim 14 , wherein the temperature is held at between 18° C. to 22° C. when mixing the solution with the at least one liquid vinyl functional thermoset resin.
16. The method of claim 12 , wherein the at least one thermoplastic resin is 10% to 30% of at least one soluble thermoplastic, relative to the total weight of polymers in the SIPN composition or IPN composition.
17. The method of claim 16 , wherein the temperature is held at between 18° C. to 22° C. when mixing the solution with the at least one liquid vinyl functional thermoset resin.
18. The method of claim 12 , wherein the at least one thermoplastic resin is 10% to 30% ABS, relative to the total weight of polymers in the SIPN composition or IPN composition.
19. The method of claim 18 , wherein the temperature is held at between 18° C. to 22° C. when mixing the solution with the at least one liquid vinyl functional thermoset resin.