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US4797342A Expired / Lapsed US ⏱️ 0.0 years remaining

Processes for the preparation of liquid developers with low vapor pressure components

Assignee: Xerox Corp
•
Filing: 1987-11-23
•
Granted: 1989-01-10
•
Expires: 2007-11-23
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Abstract

Abstract A process for the preparation of liquid developer compositions which comprises mixing a resin with a low vapor pressure oil at elevated temperatures permitting the resin to melt and enabling the formation of a resin oil mixture; thereafter adding to the oil resin mixture at elevated temperatures pigment particles, and stirring until the pigment has become dispersed in the resin; followed by attriting the mixture while cooling, for example, to ambient temperatures; thereafter filtering the aforementioned mixture, and dispersing the product in a low viscosity oil; and subsequently adding to the formed mixture a charge control additive.

Inventors

  • 👤 Melvin D. Croucher
  • 👤 Raymond W. Wong
  • 👤 Stephan Drappel

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 07:20
CPC Classifications
G; G03; G03G; G03G9/00; G03G9/08; G03G9/12; G03G9/135; G03G9/1355

Claims Analysis

Total Claims: 21
Claim 1
Independent Claim 79 words
A process for the preparation of liquid developer compositions which comprises admixing molten resin components in a vehicle component possessing a vapor pressure of from about 0.01 to about 0.1 millimeter of mercury; thereafter adding thereto pigment particles; subsequently cooling and attriting the aforementioned resulting mixture thereby enabling entrapment of the vehicle in the developer composition; thereafter filtering and dispersing the resulting particles in a low viscosity oil; and adding to the formed composition a charge control director component.
Claim 2
Dependent Claim 79 words
A process for the preparation of liquid developer compositions which comprises admixing molten resin components in a vehicle component possessing a vapor pressure of from about 0.01 to about 0.1 millimeter of mercury; thereafter adding thereto pigment particles; subsequently cooling and attriting the aforementioned resulting mixture thereby enabling entrapment of the vehicle in the developer composition; thereafter filtering and dispersing the resulting particles in a low viscosity oil; and adding to the formed composition a charge control director component.
Claim 3
Dependent Claim 100 words
A process for the preparation of liquid developer compositions which comprises mixing a resin with a low vapor pressure oil at elevated temperatures permitting the resin to melt and enabling the formation of a resin oil mixture; thereafter adding to the oil resin mixture at elevated temperatures pigment particles, and stirring until the pigment has become dispersed in the resin; cooling the mixture with attrition, thereby enabling entrapment of said oil in the developer composition; thereafter filtering the aforementioned mixture, and dispersing the product in a low viscosity oil; and subsequently adding to the formed mixture a charge control additive.
Claim 4
Dependent Claim 100 words
A process for the preparation of liquid developer compositions which comprises mixing a resin with a low vapor pressure oil at elevated temperatures permitting the resin to melt and enabling the formation of a resin oil mixture; thereafter adding to the oil resin mixture at elevated temperatures pigment particles, and stirring until the pigment has become dispersed in the resin; cooling the mixture with attrition, thereby enabling entrapment of said oil in the developer composition; thereafter filtering the aforementioned mixture, and dispersing the product in a low viscosity oil; and subsequently adding to the formed mixture a charge control additive.
Claim 5
Dependent Claim 23 words
A process in accordance with claim 2 wherein the mixing is accomplished at a temperature of from about 90° to about 110° C.
Claim 6
Dependent Claim 34 words
A process in accordance with claim 2 wherein the low vapor pressure oil is present in the mixture in an amount of from about 80 percent by weight to about 90 percent by weight.
Claim 7
Dependent Claim 25 words
A process in accordance with claim 2 wherein the vapor pressure of the oil selected is from about 0.01 to about 0.1 millimeter of mercury.
Claim 8
Dependent Claim 25 words
A process in accordace with claim 2 wherein the low vapor pressure oil is selected from the group consisting of Isopar V and Magiesol 60.
Claim 9
Dependent Claim 26 words
A process in accordance with claim 2 wherein the pigment particles are selected from the group consisting of carbon black, cyan, magenta, yellow, or mixtures thereof.
Claim 10
Dependent Claim 28 words
A process in accordance with claim 7 wherein the pigment is present in an amount of from about 3 percent by weight to about 25 percent by weight.
Claim 11
Dependent Claim 52 words
A process in accordance with claim 2 wherein subsequent to dispersion of the pigment in the resin particles the mixture is allowed to cool to room temperature over a period of from about 3 to about 5 hours enabling particles with an average diameter of from about 2 to about 3 microns.
Claim 12
Dependent Claim 26 words
A process in accordance with claim 2 wherein the charge director is present in an amount of from about 0.01 to about 2 percent by weight.
Claim 13
Dependent Claim 22 words
A process in accordance with claim 2 wherein the charge director is selected from the group consisting of polyisobutylene succinimide and lecithin.
Claim 14
Dependent Claim 24 words
A process in accordance with claim 2 wherein the developers possess an image transfer efficiency of from about 80 percent to about 99.8 percent.
Claim 15
Dependent Claim 30 words
A process in accordance with claim 2 wherein the charge control additive is present in an amount of from about 0.02 percent by weight to about 0.05 percent by weight.
Claim 16
Dependent Claim 30 words
A process in accordance with claim 2 wherein the charge director is selected from a group consisting of salts of cadmium, calcium, manganese, magnesium, and zinc salts of heptanoic acid.
Claim 17
Dependent Claim 27 words
A process in accordance with claim 2 wherein the charge director is selected from barium, aluminum, cobalt, manganese, zinc, cerium and zirconium salts of 2-ethyl hexanoic acid.
Claim 18
Dependent Claim 30 words
A process in accordance with claim 1 wherein the charge director is selected from the group consisting of the barium, aluminum, zinc, copper, lead and iron salts of stearic acid.
Claim 19
Dependent Claim 22 words
A process in accordance with claim 1 wherein the charge director is selected from the group consisting of polyisobutylene succinimide and lecithin.
Claim 20
Dependent Claim 18 words
A process in accordace with claim 1 wherein the low viscosity oil is Isopar G or Isopar L.
Claim 21
Dependent Claim 18 words
A process in accordance with claim 2 wherein the low viscosity oil is Isopar G or Isopar L.

References Cited (Backward Citations)

US3954640A Cited
US4024292A Cited
US4268597A Cited
US4454215A Cited
JPS57201243A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-01-10 1992-07-11 1993-01-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-01-10 1996-07-11 1997-01-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-01-10 2000-07-11 2001-01-10 $7700.00 Window Closed / Lapsed

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