Processes for preparing crosslinked resins and toner compositions therefrom
AssigneeXerox Corporation
InventorsRobert D. Bayley, Carol A. Fox, Thomas R. Hoffend
Life of this patent
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Abstract
A reactive melt mixing process for preparing toner resin, comprising: melting a reactive base resin, thereby forming a polymer melt; adding to said polymer melt a free radical initiator compound and optionally a vinyl monomer compound to form a second melt; and heating and mixing under high shear said second melt with optional addition of a vinyl monomer compound to form a partially crosslinked and partially gelled toner resin.
Claims35
A reactive melt mixing process for preparing toner resin, comprising:
- (a) melting a reactive base resin, thereby forming a first polymer melt;
- (b) adding to said polymer melt a free radical initiator compound to form a second melt;
- and
- (c) heating and mixing under high shear said second melt to form a third melt containing a partially crosslinked and partially gelled toner resin and wherein a free radical reactive vinyl monomer compound is added to either (b) or (c) as a crosslinking component.
A reactive melt mixing process for preparing a low fix temperature toner resin, comprising:
- preblending a reactive base resin, a high temperature half life free radical initiator compound and optionally an unreactive resin or wax as a free radical initiator diluent;
- feeding the mixture to an extruder;
- heating the mixture at a temperature of from about 70.degree. C. to about 120.degree. C. to melt the base resin and to further disperse the free radical initiator therein but without significant free radical initiator degradation or;
- simultaneously adding to the melt mixture a vinyl monomer for forming crosslinked segments comprised of said vinyl monomers between adjacent reactive resin molecules;
- heating to a higher temperature of from about 130.degree. C. to about 200.degree. C. to cause free radical initiator degradation;
- retaining the polymer melt in the extruder for a sufficient residence time of from about 10 seconds to about 10 minutes to complete the crosslinking;
- providing sufficiently high shear during the vinyl monomer interchain crosslinking reaction thereby keeping the gel particles formed during crosslinking small in size and well distributed in the polymer melt;
- optionally devolatilizing the melt to remove any effluent volatiles;
- and pumping the crosslinked resin melt through a die to a pelletizer.
Dependencies are inferred from the claim text.