High throughput process for reactive extrusion of epoxy resin

a technology of reactive extrusion and high throughput, which is applied in the direction of plastic/resin/waxes insulators, organic insulators, electrical appliances, etc., can solve the problems of inefficient throughput, high cost of process, and high cost of operation, and achieve the effect of promoting reaction

Inactive Publication Date: 2005-02-24
VALSPAR SOURCING INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Unfortunately, however, these processes are expensive.
They also unfortunately require the use of large amounts of solvent that poses manufacturing and potential environmental concerns.
Unfortunately, however, the methods disclosed in these patents have been found to yield inefficient throughput and, hence, are expensive to operate.

Method used

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  • High throughput process for reactive extrusion of epoxy resin
  • High throughput process for reactive extrusion of epoxy resin
  • High throughput process for reactive extrusion of epoxy resin

Examples

Experimental program
Comparison scheme
Effect test

example 1

A BisTPH catalyzed advanced epoxy resin was processed at a throughput rate of 11.8 kg per hour. The charge to the extruder was as follows:

Catalyzed EPON 828:7.7 kg per hourBPA:4.1 kg per hour

The barrel temperature profile was controlled to keep the melt temperature at 240° C., and the screw speed (250 RPM) maintained to maximize both throughput and residence time. The die head temperature was 180° C., with a single port opening. For this Example the total amount of catalyst equaled 0.1 wt. % based on the total weight of reactants. The extrudate was collected, air cooled, and crushed for analysis. The extrudate yielded in range (0.038-0.041) epoxy values (i.e., epoxy value=equivalents of oxirane per 100 grams of resin).

example 2

A BisTPH catalyzed advanced epoxy resin was processed at a maximum optimized throughput rate of 18.1 kg per hour. The charge to the extruder was as follows:

Catalyzed EPON 828:11.8 kg per hourBPA: 6.3 kg per hour

The barrel temperature profile was controlled to keep the melt temperature at 260° C., and the screw speed (325 RPM) maintained to maximize both throughput and residence time. The die head temperature was 180° C., with a single port opening. For this Example the total amount of catalyst equaled 0.1 wt. % based on the total weight of reactants. The extrudate was collected, air cooled, and crushed for analysis. The extrudate yielded in range (0.038-0.041) epoxy values.

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Abstract

The present invention provides low cost resins (e.g., advanced epoxy resins), processes for making these resins, and coatings made with theses resins. Specifically, the present invention provides high throughput extrusion processing of advanced epoxy resins using an appropriate amount of an iminium salt catalyst. Preferred iminium salt catalysts are stable at room temperature in the reaction mixture (thereby enabling the pre-mixing of ingredients and the stable storage of the pre-mixed ingredients) and yet are highly efficient at the processing temperatures described herein. An example of one such advance epoxy resin is the reaction product of diglycidyl ether of bisphenol A with bisphenol A in the presence of an iminium salt catalyst. Preferred processes are performed using no solvent or only negligible amounts of solvent. One preferred extrusion process utilizes an intermeshing co-rotating twin-screw extruder, however, other types of extruders may alternatively be employed.

Description

FIELD The present invention relates to the high throughput extrusion processing of advanced epoxy resins and coating compositions containing same. BACKGROUND Packaging coatings (e.g., for the interior of beverage cans and the like) previously have been formulated from advanced epoxy resins. For such purposes, it is desirable for the coating composition to have both good dry adhesion and wet adhesion properties. Traditionally, batch processes have been used for the preparation of advanced epoxy resins. Unfortunately, however, these processes are expensive. They also unfortunately require the use of large amounts of solvent that poses manufacturing and potential environmental concerns. Attempts have been made previously to process advanced epoxy resins using extruders. U.S. Pat. Nos. 4,612,156 and 5,310,854 describe two such attempts. Unfortunately, however, the methods disclosed in these patents have been found to yield inefficient throughput and, hence, are expensive to operate....

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B29C48/405C08G59/68C08L63/00
CPCB29C47/0004B29C47/0021C08G59/688B29C47/662B29C47/40B29C48/022B29C48/08B29C48/682B29C48/405
Inventor BOCHAN, ALANMALLEN, THOMAS R.LUCARELLI, MIKE A.
Owner VALSPAR SOURCING INC
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