Manufacturing method and device for aromatic vinyl compound-vinyl cyanide compound polymer
A technology of aromatic vinyl and vinyl cyanide, applied in chemical instruments and methods, separation methods, vacuum distillation, etc., can solve the problems of high cost, environmental pollution of volatile components, etc., reduce wastewater treatment costs and improve condensation Efficiency, the effect of the amount of reduction
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
preparation example Construction
[0026] According to the preparation method of the aromatic vinyl compound-vinyl cyanide compound polymer of the present invention, comprising: using a volatilization tank to obtain the aromatic vinyl compound-vinyl cyanide compound polymer, residual aromatic vinyl A step of separating volatile components from the polymerization product of cyanide monomer and organic solvent; and a step of condensing the separated volatile components using a condenser or two or more condensers connected in series, wherein the The preparation method includes the step of spraying an organic solvent onto the separated volatile components being transported from the vaporizer to the condenser; or, when using two or more condensers connected in series A step of spraying an organic solvent or an aromatic vinyl monomer onto the volatile components that have not been condensed in the first condenser and are being transported to the second condenser. According to the preparation method of the present inv...
Embodiment 1
[0083] The volatile components were separated according to separation condition A. The separated volatile components are then condensed in a first condenser according to condensation condition A, and the uncondensed volatile components are then transferred to a second condenser and condensed there. At this point, toluene is sprayed at a flow rate of 45 kg / hr onto the volatile components that are being transported to the first condenser after separation in the volatilizer, not to the uncondensed in the first condenser and being transported to the second condenser The volatile components are sprayed.
Embodiment 2
[0085] The volatile components were separated according to separation condition A. The separated volatile components are then condensed in a first condenser according to condensation condition A, and the uncondensed volatile components are then transferred to a second condenser and condensed there. At this time, the volatile components that are being transported to the first condenser after being separated in the volatilizer are not injected, and styrene is injected at a flow rate of 30 kg / hr into the first condenser that is not condensed and is being forwarded to the second condenser. On the volatile components transmitted by the condenser.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


