AU607090B2

AU607090B2 – Organic sulfur-containing compounds as adjuvants for positive electrostatic liquid developers
– Google Patents

AU607090B2 – Organic sulfur-containing compounds as adjuvants for positive electrostatic liquid developers
– Google Patents
Organic sulfur-containing compounds as adjuvants for positive electrostatic liquid developers

Download PDF
Info

Publication number
AU607090B2

AU607090B2
AU47373/89A
AU4737389A
AU607090B2
AU 607090 B2
AU607090 B2
AU 607090B2
AU 47373/89 A
AU47373/89 A
AU 47373/89A
AU 4737389 A
AU4737389 A
AU 4737389A
AU 607090 B2
AU607090 B2
AU 607090B2
Authority
AU
Australia
Prior art keywords
liquid
carbon atoms
electrostatic
liquid developer
process according
Prior art date
1988-12-30
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)

Ceased

Application number
AU47373/89A
Other versions

AU4737389A
(en

Inventor
Lyla Mostafa El-Sayed
Torence John Trout
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

EIDP Inc

Original Assignee
EI Du Pont de Nemours and Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
1988-12-30
Filing date
1989-12-29
Publication date
1991-02-21

1989-12-29
Application filed by EI Du Pont de Nemours and Co
filed
Critical
EI Du Pont de Nemours and Co

1990-07-19
Publication of AU4737389A
publication
Critical
patent/AU4737389A/en

1991-02-21
Application granted
granted
Critical

1991-02-21
Publication of AU607090B2
publication
Critical
patent/AU607090B2/en

2009-12-29
Anticipated expiration
legal-status
Critical

Status
Ceased
legal-status
Critical
Current

Links

Espacenet

Global Dossier

Discuss

Classifications

G—PHYSICS

G03—PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY

G03G—ELECTROGRAPHY; ELECTROPHOTOGRAPHY; MAGNETOGRAPHY

G03G5/00—Recording members for original recording by exposure, e.g. to light, to heat, to electrons; Manufacture thereof; Selection of materials therefor

G03G5/02—Charge-receiving layers

G03G5/04—Photoconductive layers; Charge-generation layers or charge-transporting layers; Additives therefor; Binders therefor

G03G5/08—Photoconductive layers; Charge-generation layers or charge-transporting layers; Additives therefor; Binders therefor characterised by the photoconductive material being inorganic

G—PHYSICS

G03—PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY

G03G—ELECTROGRAPHY; ELECTROPHOTOGRAPHY; MAGNETOGRAPHY

G03G9/00—Developers

G03G9/08—Developers with toner particles

G03G9/12—Developers with toner particles in liquid developer mixtures

G03G9/135—Developers with toner particles in liquid developer mixtures characterised by stabiliser or charge-controlling agents

G03G9/1355—Ionic, organic compounds

G—PHYSICS

G03—PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY

G03G—ELECTROGRAPHY; ELECTROPHOTOGRAPHY; MAGNETOGRAPHY

G03G9/00—Developers

G03G9/08—Developers with toner particles

G03G9/12—Developers with toner particles in liquid developer mixtures

G03G9/135—Developers with toner particles in liquid developer mixtures characterised by stabiliser or charge-controlling agents

Description

I-
AUSTRALIA
PATENTS ACT 1952 COMPLETE SPECIFICATION 807090 Form
(ORIGINAL)
FOR OFFICE USE Short Title: Int. Cl: Application Number: Lodged: Complete Specification-Lodged: Accepted: Lapsed: Published: Priority: Related Art: This document contains the amendments made under Section 49 and is correct for printing.
TO BE COMPLETED BY APPLICANT i si i
S.
S
S
S.
OS 55 0
S.
S
S..
S
S..
Name of Applicant: Address of Applicant: E. I. DU PONT AND COMPANY DE NEMOURS 1007 MARKET STREET
WILMINGTON
DELAWARE, 19898
U.S.A.
Actual Inventor: Address for Service: GRIFFITH HACK CO., 601 St. Kilda Road, Melbourne, Victoria 3004, Australia.
S* Se S C Sb
*S
S
*S
*5 0*
S.
Complete Specification for the invention entitled: ORGANIC SULFUR-CONTAINING COMPOUNDS AS ADJUVANTS FOR POSITIVE ELECTROSTATIC LIQUID DEVELOPERS.
The following statement is a full description of this invention S including the best method of performing it known to me:o
C
i il; lli-,~rcP; i -i I IM-0085
TITLE
ORGANIC SULFUR-CONTAINING COMPOUNDS AS ADJUVANTS FOR POSITIVE ELECTROSTATIC LIQUID DEVELOPERS
DESCRIPTION
TECHNICAL FIELD This invention relates to electrostatic liquid developers. More particularly this invention relates to a positive-working liquid electrostatic developer containing resin particles having dispersed therein certain organic sulfur-containing compounds.
BACKGROUND ART It is known that a latent electrostatic image can be developed with toner particles dispersed in an insulating nonpolar liquid. Such dispersed materials are known as liquid toners or liquid developers. A latent electrostatic image may be produced by providing a photoconductive layer with a uniform 20 electrostatic charge and subsequently discharging the •electrostatic charge by exposing it to a modulated I *beam of radiant energy. Other methods are known for forming latent electrostatic images. For example, one *method is providing a carrier with a dielectric I De 25 surface and transferring a preformed electrostatic charge to the surface. Useful liquid toners comprise a thermoplastic resin and dispersant nonpolar liquid.
Generally a suitable colorant is present such as a dye or pigment. The colored toner particles are dispersed 30 in the nonpolar liquid which generally has a highvolume resistivity in excess of 109 ohm centimeters, a :low dielectric constant below 3.0 and a high vapor e pressure. The toner particles are less than 10 lm average by area size as measured by a Horiba CAPA-500 o• 35 centrifugal automatic particle analyzer. After the ‘l i 2 latent electrostatic image has been formed, the image is developed by the colored toner particles dispersed in said dispersant nonpolar liquid and the image may subsequently be transferred to a carrier sheet.
Since the formation of proper images depends on the differences of the charge between the liquid developer and the latent electrostatic image to be developed, it has been found desirable to add a charge director compound and preferably adjuvants, e.g., polybutylene succinimide, an aromatic hydrocarbon, etc., to the liquid toner comprising the thermoplastic resin, dispersant nonpolar liquid, and preferably a colorant. Such liquid developers provide images of good resolution, but it has been found that charging and image quality are particularly pigment dependent.
Some formulations, suffer from poor image quality manifested by low resolution, poor solid area coverage (density), and/or image squash. In order to overcome such problems much research effort has been expended to develop new type charge directors and/or charging adjuvant for electrostatic liquid toners or developers.
It has been found that the above disadvantages can be overcome and improved positive electrostatic 25 liquid developers prepared containing a dispersant nonpolar liquid, ionic or zwitterionic charge director compound, a thermoplastic resin, and preferably a colorant and an adjuvant as described below. The improved electrostatic liquid developer when used to 30 develop an electrostatic image results in improved image quality, reduced squash, and improved solid area coverage independent of the pigment and charge director compound present.
0
S
S @o 2 3 i DISCLOSURE OF THE INVENTION In accordance with this invention there is provided a positive electrostatic liquid developer having improved charging and imaging characteristics consisting essentially of a nonpolar liquid having a Kauri-butanol value of less than 30, present in a major amount, thermoplastic resin particles having dispersed therein an adjuvant which is substantially insoluble in the nonpolar liquid at ambient temperatures and is an organic sulfur-containing compound selected from the group consisting of 0 0 i R-S=0 R O-S=0 RfS=0 OH- n=1-4 n OH n=1-6 OH n=1-2 and the salts of and 3, wherein R is alkyl of 1 to 30 carbon atoms, substituted alkyl of 1 to 30 carbon atoms, aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, the resin particles having an average by area 25 particle size of less than 10 pm, and a nonpolar liquid soluble ionic or zwitterionic charge director compound.
In accordance with an embodiment of this invention there is provided a process for preparing a positive electrostatic liquid developer for electrostatic imaging comprising i dispersing at an elevated temperature in a S*eI vessel a thermoplastic resin, an organic sulfurcontaining compound selected from the group consisting 35 of 3 _i I SIt R S=0 R -0-S=0 Rf S=o OH L n=1-4 OH n=l-6 H n=1-2 and the salts of and 3, wherein R is alkyl of 1 to 30 carbon atoms, substituted alkyl of 1 to 30 carbon atoms, aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, and a dispersant nonpolar liquid having a Kauri-butanol value of less than 30, while maintaining the temperature in the vessel at a temperature sufficient to plasticize and liquify the resin and below that at which the dispersant nonpolar liquid degrades and the resin decomposes, cooling the dispersion, either without stirring to form a gel or solid mass, followed by shredding the gel or solid mass and grinding by means of particulate media with or without the presence of additional liquid; with stirring to form a viscous I mixture and grinding by means of particular media with or without the presence of additional liquid; or 25 while grinding by means of particulate media to prevent the formation of a gel or solid mass with or without the presence of additional liquid; separating the dispersion of toner particles having an average by area particle size of less than 10 pmn from the particulate media, and adding to the dispersion during or subsequent to Step a nonpolar liquid soluble ionic or zwitterionic charge director compound.
Throughout the specification the below-listed 35 terms have the following meanings: *4 O4 I–t a In the claims appended hereto consisting essentially of means the composition of the electrostatic liquid developer does not exclude unspecified components which do not prevent the advantages of the developer from being realized. For example, in addition to the primary components, there can be present additional components, such as a colorant, fine particle size oxides, adjuvants, e.g., polybutylene succinimide, aromatic hydrocarbon, alkyl hydroxybenzylpolyamine, etc.
Q/m is the charge to mass ratio expressed as micro Coulombs/gram.
Conductivity is the conductivity of the developer measured in pmhos/cm at 5 hertz and 5 volts and can be referred to as BULK.
Grey Scale means a step wedge where the toned image density increased from Dmin to Dmax in constant increments.
The dispersant nonpolar liquids are, preferably, branched-chain aliphatic hydrocarbons and more particularly, Isopar®-G, Isopar®-H, Isopar®-K, Isopar®-L, and Isopar®-V. These hydrocarbon liquids are narrow cuts of isoparaffinic hydrocarbon fractions with extremely high levels of purity. For example, 0 25 the boiling range of Isopar®-G is between 1570C and 176 0 C, Isopar®-H between 176 0 C and 191°C, Isopar®-K between 1770 and 197°C, Isopar®-L between 188 0 C and 2060 and Isopar®-M between 2070C and 254 0 C and Isopar®-V between 254.4 0 C and 329.40C. Isopar®-L has a mid-boiling point of approximately 194 0 C. Isopar®- SM has a flash point of 800 and an auto-ignition temperature of 3380C. Stringent manufacturing specifications, such as sulphur, acids, carboxyl, and «chlorides are limited to a few parts per million.
35 They are substantially odorless, possessing only a e *0 very mild paraffinic odor. They have excellent odor stability and are all manufactured by the Exxon Corporation. High-purity normal paraffinic liquids, Norpar®12, Norpar®13 and Norpar@15, Exxon Corporation, may be used. These hydrocarbon liquids have the following flash points and auto-ignition temperatures: Auto-Ignition Liquid Flash Point Temp. (o°C Norpar®12 69 204 Norpar®13 93 210 118 210 All of the dispersant nonpolar liquids have an electrical volume resistivity in excess of 10 9 ohm centimeters and dielectric constant below 3.0. The vapor pressures at 25 0 C are less than 10 Torr.
Isopar®-G has a flash point, determined by the tag closed cup method, of 40 0 C, Isopar®-H has a flash point of 53 0 C determined by ASTM D 56. Isopar®-L and .d Isopar®-M have flash points of 61 0 C, and 80 0
C,
*respectively, determined by the same method. While e these are the preferred nonpolar liquids, the S* 25 essential characteristics of all suitable nonpolar liquids are the electrical volume resistivity and the C4, dielectric constant. In addition, a feature of the nonpolar liquids is a low Kauri-butanol value less than 30, preferably in the vicinity of 27 or 28, determined by ASTM D 1133. In the preparation of liquid developer the ratio of thermoplastic resin to nonpolar liquid is such that the combination of ingredients becomes fluid at the working temperature.
The nonpolar liquid is present in an amount of 85 to 99.9% by weight, preferably 97 to 99.5% by weight, based on the total weight of liquid developer. The ee** I n inl-i- ij i~l I total weight of solids in the liquid developer is 0.1 to 15%, preferably 0.5 to 3.0% by weight. The total weight of solids in the liquid developer is solely based on the ingredients described more fully below such as the resin, including components dispersed therein, pigment component, adjuvant, etc.
Useful thermoplastic resins or polymers include: ethylene vinyl acetate (EVA) copolymers (Elvax® resins, E. I. du Pont de Nemours and Company, Wilmington, DE), copolymers of ethylene and an a,Bethylenically unsaturated acid selected from the class consisting of acrylic acid and methacrylic acid, copolymers of ethylene (80 to 99.9%)/acrylic or methacrylic acid (20 to 0%)/alkyl (Ci to C 5 ester of methacrylic or acrylic acid (D to polyethylene, polystyrene, isotactic polypropylene (crystalline), ethylene ethyl acrylate series sold under the trademark Bakelite® DPD 6169, DPDA 6182 Natural and DTDA 9169 Natural by Union Carbide Corp., Stamford, CN; ethylene vinyl acetate resins, DQDA 6479 S Natural and DQDA 6832 Natural 7 also sold by Union Carbide Corp.; Surlyn® ionomer resin by E. I. du~Pont de-Nemours and Company, Wilmington, DE, etc., or blends thereof, polyesters, polyvinyl toluene, 25 polyamides, styrene/butadiene copolymers and epoxy resins. Terpene polymers such as described in Tsuneda U.S. Patent 4,259,428 cannot be used in this invention because of their relatively high solubility in the s ee nonpolar liquid. Preferred copolymers are the 30 copolymer of ethylene and an Ca,8-ethylenically unsaturated acid of either acrylic acid or methacrylic acid. The synthesis of copolymers of this type are described in Rees U.S. Patent 3,264,272, the ‘se disclosure of which is incorporated herein by 6 35 reference. For the purposes of preparing the 7 o eeCi preferred copolymers, the reaction of the acid containing copolymer- with the ionizable iTetal compound, as described in the Rees patent, is omitted.
The ethylene constituent is present in about 80 to 99.9t by weight of the copolymer and the acid comiponent in about 20 to 0.1% by weight of the copolymer. The acid number of the copolymers range from 1 to 120, preferably 54 to 90. Acid no. is milligrams potassium hydroxide required to neutralize 1 gram of polymer. The melt index (g/10 min) of 10 to 500 is determined by ASTM D 1238 Procedure A.
Particularly preferred copolymers of this type have an acid no. of 66 and 60 and a melt index of 100 and 500 determined at 190*C, respectively.
The thermoplastic res»ins described above optionally can have dispersed therein one organic sulfur containing compound of the following formulas: 0 0 tJ o 1)S S O 0 S 3 wherein R is alkyl of 1 to 30 carbon atoms, e.g., methyl, ethyl, propyl, butyl, pentyl, hexyl, decyl, dodecyl, hexadecyl, pentadecyl, etc.; substituted alkyl of 1 to 30 carbon atoms and substituted aryl of 6 to 30 carbon atoms, halogen, Br, Cl, F; hydroxy; alkoxy of 1 to 30 carbon atoms; aryloxy of 6 to 30 carbon atoms; aryl of 6 to 30 carbon atoms, benzene? naphthalene, anthracene, pentacene, pentathrene, etc.; and the salts of compounds (2) or, 0 and wherein the cation may be, for example, Na, 35 Ba, Ca, Mg, Mn, Al$ NH 3 etc. The sulfonic acid, organic sulfonates, organic sulfate, sulfinic acid, or i 9 1 their salts are substantially insoluble in the nonpolar liquid at ambient temperatures.
Suitable types of sulfur-containing compounds include: sulfonic acid (Structure 1 above) p-toluene sulfonic acid Ba salt of p-toluenesulfonic acid Na salt of 2-bromoethanesulfonic acid Na salt of 3-hydroxy-1-propanesulfonic acid benzenesulfonic acid 1-butanesulfonic acid Na salt of 1-butanesulfonic acid Na salt of 1-decanesulfonic acid Na salt of 1-dodecanesulfonic acid tetradecane sulfonic acid Na salt of tetradecane sulfonic acid Na salt of 4-bromo-l-butanesulfonic acid Na salt of 4-hydroxybutanesulfonic acid 1-pentanesulfonic acid 20 Na salt of 1-pentanesulfonic acid SO 00 Na salt of 1-hexanesulfonic acid *0 disodium salt of 1,4-butanedisulfonic acid :,oeMg salt of 1,4-butanedisulfonic acid Tetra Na salt of 1,3,6,8-pyrene tetrasulfonic acid *0 25 2-propanesulfonic acid sos. Na salt of propanesulfonic acid tri Na salt of naphthalene-1,3,6-trisulfonic acid tri Na salt of 8-hydroxy-1,3,6-pyrenetrisulfonic acid, ~and 30 tri Na salt of benzenetrisulfonic acid *.**dodecylbenzenesulfonate ethanesulfonate cyclohexylmethanesulfonate Soo* organic sulfates (structure 2 above) 35 decyl sodium sulfate a 0 r ,am~onium lauryl sulfate Li salt of dodecyl sulfate Na salt of 3-iodopropyl sulfate butyl sulfate Na salt of n-butyl sulfate pentyl sulfate n-undecyl sulfate tri Na salt of estriol trisulfate, hexa K salt of myo-inositol hexasulfate, and Na salt of dodecyl sulfate, sulfinic acid (structure 3 above) S. S S. 5 S S S
S
S
55
SSSS
S
SS*
*555 S S
S
*5
S
S.
S
S
5 55.555
S
p-toluenesulfinic acid benzenesulfinic acid Zn salt of benzenesulfinic acid, and Na salt of oxy-4,4-bis(benzene-sulfinic acid).
The sulfur-containing compounds are dispersed in the developer solids in an amount of 0.1 to 10 percent by weight, preferably 1 to 5 percent by weight, based on the total weight of the developer solids. A method 20 whereby the sulfur-containing compounds are dispersed in the thermoplastic resin is described below.
In addition, the resins have the following preferred characteristics: 1. Be able to disperse the adjuvant, colorant, 25 pigment, etc.
2. Be substantially insoluble in the dispersant liquid at temperatures below 40 0 C, so that the resin will not dissolve or solvate in storage, 3. Be able to solvate at temperatures above 30 50 0
C.
4. Be able to form particles between 0.1 pm and 5 pin, in diameter (preferred size), determined by Horiba CAPA-500 centrifugal particle analyzer; and between about 1 Jm and 15 pm, in diameter, e.g., 5 0O to LI.- -1 Ylr «~1~9 J C 11 determined by Malvern 3600E Particle Sizer as described below.
Be able to form a particle (average by area) of less than 10 1jm, determined by Horiba CAPA- 500 centrifugal automatic particle analyzer, manufactured by Horiba Instruments, Inc., Irvine, CA: solvent viscosity of 1.24 cps, solvent density of 0.76 g/cc, sample density of 1.32 using a centrifugal rotation of 1,000 rpm, a particle size range of 0.01 to less than 10 gm, and a particle size cut of 1.0 gm, and, about 30 pm average particle size, e.g., determined by Malvern 3600E Particle Sizer as described below, and 6. Be able to fuse at temperatures in excess of 70 0
C.
By solvation in 3. above, the resins forming the toner particles will become swollen, gelatinous or softened.
Suitable nonpolar liquid soluble ionic or zwitterionic charge director compounds which are 20 used in an amount of 0.1 to 10,000 mg/g, preferably 1 o 1,000 mg/g developer solids, include: positive charge directors, glyceride charge directors such as Emphos® D70-30C and Emphos® F27-85, two commercial products sold by Witco Chemical Corp., New York, New York; which are sodium salts of phosphated mono- and diglycerides with unsaturated and saturated acid substituents, respectively; lecithin, Basic Barium Petronate® Neutral Barium Petronate®, Basic Calcium Petronate®, Neutral Calcium Petronate®, oil- 30 soluble petroleum sulfonate manufactured by Sonneborn Division of Witco Chemical Corp., New York, NY, etc.
As indicated above, additional components that can be present in the electrostatic liquid developer are colorants, such as pigments or dyes and 35 combinations thereof, which are preferably present to 11 pL 12 render the latent iuage visible, though this need not be done in some’applications. The colorant, a pigment, may be present in the amount of up to about percent by weight based on the total weight of developer solids, preferably 0.01 to 30% by weight based on the total weight of developer solids. The amount of colorant may vary depending on the use of the developer. Examples of pigments are Monastral® Blue G Pigment Blue 15 C.I. No. 74160), Toluidine Red Y Pigment Red Quindo® Magenta (Pigment Red 122), Indo® Brilliant Scarlet (Pigment Red 123, C.I. No. 71145), Toluidine Red B (C.I.
Pigment Red®), Watchung® Red B Pigment Red 48), Permanent Rubine F6B13-1731 (Pigment Red 184), Hansa® Yellow (Pigment Yellow 98), Dalamar® Yellow (Pigment Yellow 74, C.I. No. 11741), Toluidine Yellow G (C.I.
Pigment Yellow Monastral® Blue B Pigment Blue 15), Monastral® Green B Pigment Green 7) Pigment Scarlet Pigment Red 60), Auric Brown Pigment Brown Monastral® Green G (Pigment Green Carbon Black, Sterling® NS N 774 (Pigment e: Black 7, C.I. No. 77266), etc.
Fine particle size oxides, silica, alumina, titania, etc.; preferably in the order of 0.5 pm or 25 less can be dispersed into the liquefied resin. These oxides can be used alone or in combination with the colorants. Metal particles can also be added.
Another additional component of the electrostatic liquid developer is an adjuvant selected from the 30 group consisting of polybutylene succinimide, aromatic hydrocarbon having a Kauri-butanol value of greater than 30, and alkylhydroxybenzylpolyamine. Other adjuvants may be used provided they do not affect the charge. The adjuvants are generally used in an amount 35 of 1 to 1000 mg/g, preferably 1 to 200 mg/g developer so*
IR
0* 13 solids. Examples of the above-described adjuvants include: polybutylene succinimide: OLOA®-1200 sold by Chevron Corp., analysis information appears in Kosel U.S. Patent 3,900,412, column 20, lines 5 to 13, the disclosure of which is incorporated herein by reference; Amoco 575 having a number average molecular weight of about 600 (vapor pressure osmometry) made by reacting maleic anhydride with polybutene to give an alkenylsuccinic anhydride which in turn is reacted with a polyamine. Amoco 575 is 40 to 45% surfactant, 36% aromatic hydrocarbon, and the remainder oil, etc.
aromatic hydrocarbon: benzene, toluene, naphthalene, substituted benzene and naphthalene compounds, trimethylbenzene, xylene, dimethylethylbenzene, ethylmethylbenzene, propylbenzene, Aromatic® 100 which is a mixture of C 9 and C 10 alkyl-substituted benzenes manufactured by Exxon Corp., etc.
alkvlhydroxvbenzvlpolvamine compounds of the S* formula:
*S
R
.OO wherein a is 2-8, b is 1-10, and Sand being soluble in nonpolar liquid.
30 The above benzyl amine groups are connected by methylene groups to form compounds such 13 i
!I
14 as H-PN-CH 2 -PN-H, H-PN-CH 2 -NP-H, H-PN-CH2-NP-CH 2
-PN-H,
and the like.
It is preferred that at least some of the R groups have 50 or more carbon atoms. The hydroxy or amine of the alkylhydroxybenzylpolyamine can be further modified. For example, boron halides such as boron trifluoride, boron triiodide and boron trichloride can form an interaction product with the phenolic hydroxy groups, hydroxy group substituents on a benzene ring. Boron oxide, boron oxide hydrate, boron trifluoride, boron triiodide, boron tribromide, boron trichloride, boric acid, boronic acids (such as alkyl-B-(OH)2 and aryl-B-
(OH)
2 tetraboric acid, metaboric acid and esters of boric acids can form interaction products with other polar groups such as primary and secondary amino (-NH 2 and -NH) groups as well as phenolic hydroxy groups.
Suitable such copolymers are commercially available compounds, copolymers sold by Amoco Petroleum Additives Co., Clayton, MO which may differ in molecular weight. Amoco 9250 which is said to have a g* number average molecular weight in the range of 1600 to 1800 (determined by osmometry) and is made by reacting a polybutene with a phenol to give an 25 alkylphenol which is reacted with a polyamine and an aldehyde. Amoco 595, and Amoco 9250 which are believed to be made by a process similar to the one used to make Amoco 9040, described above. Amoco 595 (sold as 45% surfactant, 30% aromatic hydrocarbon, and 30 oil) and Amoco 9250 (sold as 40-45% surfactant, 36% aromatic hydrocarbon, and oil) have number average molecular weights of about 1000 and 1600 to 1800, S» respectively. The number average molecular weights •can be determined by known osmometry techniques.
14 Th p The particles in the electrostatic liquid developer have an average by area particle size of less than 10 gm, preferably the average by area particle size is less than 5 pm. The resin particles of the developer may or may not be formed having a plurality of fibers integrally extending therefrom although the formation of fibers extending from the toner particles is preferred. The term «fibers» as used herein means pigmented toner particles formed with fibers, tendrils, tentacles, threadlets, fibrils, ligaments, hairs, bristles, or the like.
The positive electrostatic liquid developer can be prepared by a variety of processes. For example, into a-suitable mixing or blending vessel, e.g., attritor, heated ball mill, heated vibratory mill such as a Sweco Mill manufactured by Sweco Co., Los Angeles, CA, equipped with particulate media, for dispersing and grinding, Ross double planetary mixer manufactured by Charles Ross and Son, Hauppauge, NY, 20 etc., or a two-roll heated mill (no particulate media S6 Sa S.necessary) are placed at least one of thermoplastic *resin, organic sulfur-containing compound and dispersant polar liquid described above. Generally t, the resin, dispersant nonpolar liquid and optional S 25 colorant are placed in the vessel prior to starting too. the dispersing step. Optionally the colorant can be added after homogenizing the resin and the dispersant nonpolar liquid. Polar additive can also be present in the vessel, up to 100% based on the total weight of liquid including nonpolar liquid. The e dispersing step is generally accomplished at elevated temperature, the temperature or ingredients in «the vessel being sufficien: to plasticize and liquefy ,the resin but being below that at which the dispersant 35 nonpolar liquid or polar additive, if present,
S.
degrades and the resin and/or colorant decomposes. A preferred temperature range is 80 to 120 0 C. Other temperatures outside this range may be suitable, however, depending on the particular ingredients used.
The presence of the irregularly moving particulate media in the vessel is preferred to prepare the dispersion of toner particles. Other stirring means can be used as well, however, to prepare dispersed toner particles of proper size, configuration and morphology. Useful particulate media are particulate materials, spherical, cylindrical, etc., selected from the group consisting of stainless steel, carbon steel, alumina, ceramic, zirconium, silica, and sillimanite. Carbon steel particulate media is particularly useful when colorants other than black are used. A typical diameter range for the particulate media is in the range of 0.04 to 0.5 inch to approx. 13 mm).
After dispersing the ingredients in the vessel, with or without a polar additive present until the ee b desired dispersion is achieved, typically 2 hours with the mixture being fluids, the dispersion is cooled, I. in the range of 0 0 C to 65 0 C. Cooling may be accomplished, for e:cample, in the same vessel, such as S. 25 the attritor, while simultaneously grinding with particulate media to prevent the formation of a gel or solid mass; without stirring to form a gel or solid mass, followed by shredding the gel or solid mass and grinding, by means of particulate media; or with 30 stirring to form a viscous mixture and grinding by I* means of particulate media. Cooling can occur as described above with or without the presence of additional liquid. Additional liquid may be added at ot• any step during the preparation of the liquid 35 electrostatic developer to facilitate grinding or to a. a SO e6 e* 16
I
17 dilute the toner to the appropriate solids needed for toning. Additional liquid means dispersant nonpolar liquid, polar liquid or combinations thereof.
Cooling is accomplished by means known to those skilled in the art and is not limited to cooling by circulating cold water or a cooling material through an external cooling jacket adjacent the dispersing apparatus or permitting the dispersion to cool to ambient temperature. The resin precipitates out of the dispersant during the cooling. Toner particles of average particle size (by area) of less than 10 pm, as determined by a Horiba centrifugal particle analyzer described above, or other comparable apparatus, are formed by grinding for a relatively short period of time.
Another instrument for measuring average particle sizes is a Malvern 3600E Particle Sizer manufactured by Malvern, Southborough, MA which uses laser 😮 oo diffraction light scattering of stirred samples to determine average particle sizes. Since these instruments use different techniques to measure average particle size the readings differ. The following correlation of the average size of toner 0 particles in micrometers (pnm) for the two instruments is: 5 0 S0
S
o•
S
17 I» -me 18 Value Determined By Expected Range For Malvern 3600E Particle Sizer Horiba CAPA-500 9.9 3.4 6.4 1.9 4.6 1.3 10 2.8 0.8 1.0 3 0.2 0.6 This correlation is obtained by statistical analysis of average particle sizes for 67 liquid electrostatic developer samples (not of this invention) obtained on both instruments. The expected i 20 range of Horiba values was determined using a linear regression at a confidence level of 95%. In the claims appended to this specification, the particle size values are as measured using the Horiba •instrument.
After cooling and separating the dispersion of toner particles from the particulate media, if present, by means known to those skilled in the art, V it is possible to reduce the concentration of the toner particles in the dispersion, impart an 30 electrostatic charge of predetermined polarity to the S. toner particles, or a combination of these variations.
The concentration of the toner particles in the dispersion is reduced by the addition of additional dispersant nonpolar liquid as described previously 35 above. The dilution is normally conducted to reduce 18 I 1 19 the concentration of toner particles to between 0.1 to percent by weight, preferably 0.3 to 3.0, and more preferably 0.5 to 2 weight percent with respect to the dispersant nonpolar liquid. One or more ionic or zwitterionic charge director compounds of the type set out above, can be added to impart a positive charge. The addition may occur at any time during the process; preferably at the end of the process, after the particulate media, if used, are removed and the concentration of toner particles is accomplished.
If a diluting dispersant nonpolar liquid is also added, the charge director compound can be added prior to, concurrently with, or subsequent thereto. It is believed that upon addition of the charge director compound some leaching of the organic sulfurcontaining compound into the dispersant nonpolar liquid occurs. If an adjuvant compound of a type described above, polybutylene succinimide, a* aromatic hydrocarbon, alkylhydroxylbenzylpolyamine, 20 etc., has not been previously added in the preparation **o of the developer, it can be added prior to or subsequent to the developer being charged. Preferably the adjuvant compound is added after the dispersing step.
Two other process embodiments for preparing the electrostatic liquid developer include: dispersing a thermoplastic resin, optionally a colorant, and/or one of the organic sulfur-containing compounds of this invention in the absence of a dispersant nonpolar liquid having a Kauri-butanol value of less than 30 to form a solid mass.
shredding the solid mass, grinding the shredded solid mass by means 35 of particulate media in the presence of a liquid taken i l II1111″: «11 II I l 1 from the group consisting of a polar liquid having a Kauri-butanol value of at least 30, a nonpolar liquid having a Kauri-butanol value of less than 30, and combinations thereof, separating the dispersion of toner particles having an average by area particle size of less than 10 pm from the particulate media, and adding additional nonpolar liquid, polar liquid or combinations thereof to reduce the concentration of toner particles to between 0.1 to 15.0 percent by weight with respect to the liquid; and adding to the dispersion a nonpolar soluble ionic or zwitterionic charge director compound; and dispersing a thermoplastic resin, optionally a colorant, and/or one of the organic sulfur-containing compounds of this invention in the absence of a dispersant nonpolar liquid having a Kauri-butanol value of less than 30 to form a solid mass, 20 shredding the solid mass, redispersing the shredded solid mass at an I, elevated temperature in a vessel in the presence of a dispersant nonpolar liquid having a Kauri-butanol value of less than 30, optionally a colorant, while maintaining the temperature in the vessel at a temperature sufficient to plasticize and liquify the resin and below that at which the dispersant nonpolar liquid degrades and the resin and/or colorant decomposes, cooling the dispersion, either without stirring to form a gel or solid mass, followed by shredding the gel or solid mass and grinding by means of particulate media with or without the presence of additional liquid; 21 with stirring to form a viscous mixture and grinding by means of particulate media with or without the presence of additional liquid; or while grinding by means of particulate media to prevent the formation of a gel or solid mass with or without the presence of additional liquid; separating the dispersion of toner particles having an average by area particle size of less than 10 Jm from the particulate media, and adding additional nonpolar liquid, polar liquid or combinations thereof to reduce the concentration of toner particles to between 0.1 to 15.0 percent by weight with respect to the liquid; and adding to the dispersion a nonpolar soluble ionic or zwitterionic charge director compound.
A preferred mode of the invention is described in Example 1.
INDUSTRIAL APPLICABILITY 20 The positive liquid electrostatic developers of ee this invention demonstrate improved image quality, resolution, solid area coverage (density), and toning of fine details, evenness of toning, and reduced squash independent of charge director or pigment present. The particles are exclusively charged positive. The developers of the invention are useful in copying, making office copies of black and i white as well as various colors; highlight color copying or color proofing, a reproduction of an image using the standard colors yellow, cyan, magenta together with black as desired. In copying and proofing the toner particles are applied to a latent electrostatic image and can be transferred, if desired. Other uses envisioned for the positive 35 liquid electrostatic developers include: digital 22 color proofing, lithographic printing plates and resists.
EXAMELES
The following controls and examples wherein the parts and percentages are by weight illustrate but do not limit the invention. In the examples the melt indices are determined by ASTM D 1238, Procedure A; the average particle sizes by areas were determined by 1C a Malvern 3600 Particle Size Analyzer, or the Horiba CAPA 500 centrifugal automatic particle analyzer, as indicated; and weight average molecular weights are determined by gel permeation chromatography (GPC).
Image quality of the toners of the invention was determined on a modified Savin 870 copier unless specifically noted. This device consists of a Savin 870 copier with the modifications described below.
Mechanical modifications include addition of a pretransfer corona and removing the anodized layer 20 from the surface of the reverse roll while decreasing o the diameter of the roll spacers to maintain the same gap between the roll and photoconductor.
Electrical modifications to the copier include: disconnecting the image density feedback loop from the development electrode and connecting the electrode to a Keithly high voltage supply (Model 247), Keithley, Cleveland, OH, connecting a Keithly high voltage supply (Model 247) to the modified reverse roll, and disconnecting the transfer corona and connecting same to a Trek (Model 610) high voltage supply, Trek, Medina, NY..
i i Irrrr~ 0
S
S.
S
S
*5
S
S..
0*OS
OS
0 S S 5 S. S
S
055e
SS
OS 0 55 6 S S
SS
The modified Savin 870 was then used to evaluate both positive and negative toners depending on the voltages and biases used. To evaluate positive toners the copier was run in a positive mode: reversed image target was used with negative transfer corona voltages and positive development bias. The reversed image target consists of white characters and lines, etc. on a black background.
The principal of operation is described below.
The photoconductor is charged positive (near 1000V) by means of the charging corona. The copy is imaged onto the photoconductor inducing the latter to discharge to lower voltages (in order of increasing discharge-black areas and white areas). When adjacent to the toner electrode the photoconductor has fields at its surface such that positive toner particles will deposit at the white imaged areas, and negative toner particles, if present, will deposit at the black imaged areas. If necessary, toner background is removed by the biased 20 reverse roll. The toner is then transferred to paper by the transfer corona (the transfer force due to the negative charge sprayed on the back of the paper).
The toner is then thermally fused. Actual voltages and biases used can be found in the examples. lp/mm means line pairs/mm.
Table 1 below contains developer formulation and performance information. Measurement results of the charge to mass ratio in micro Coulombs/gram for each developer is given. The developer Q/m ratios 30 were measured with the following procedure: a light aluminum pan was weighed, placed on the spacers of the cell, and developer was then placed in the cell (filling the volume between the cell base and pan bottom (thickness 0.060 inch (1.52 mm). A 180 pf 35 capacitor is charged to 1000V, placed across the cell 23 1.
24 and a Keithley 616 Electrometer, Keithley, Cleveland, Oh was placed in series with the cell. The developer is deposited for 4 seconds. The total charge flow through the cell was measured on the electrometer which was proportional to the charge of the deposited developer. The pan with the deposited developer was removed from the cell, dried on a hot plate for about 20-30 minutes at 130 0 C, and the change in weight was recorded using a Mettler balance (AE100), Mettler, Hightstown, Ny, accurate to 0.1 mg. Q/m is then calculated by the following formula: Q/m AQ/Am.
This process is repeated using a voltage of -1000 V to deposit particles of the developer with the opposite polarity. Q/m values are given with the sign of the developer particles. The ratio is the ratio of the weights of the deposited positive developer particles to the negative particles.
Table 2 below shows the solubility in nonpolar liquid and the effect achieved by various organic 20 sulfur-containing compounds.
CONTROL 1 The following ingredients were placed in a Union Process IS Attritor, Union Process Company, Akron, Ohio: 1 S* 0 *S S
S
S.
S.
S..
Ingredienta Amount (a) *00* S S 5* 0 S0 0 S5
S
SeeS 5* SO S Copolymer of ethylene (89%) and methacrylic acid melt 30 index at 190 0 C is 100, acid no.
is 66 Heucophthal Blue G XBT-583D, Heubach, Inc., Newark, NJ Isopar®-L, nonpolar liquid having a Kauri-butanol value of 27, Exxon Corporation 200.00 50.00 1000.00 The ingredients were heated to 100 0 C +/-10 0 C and milled at a rotor speed of 230 rpm with 0.01875 inch (4.76 mm) diameter stainless steel balls for two hours. The attritor was cooled to ambient temperature while milling was continued and 700 grams of Isopar®- L (Exxon) were added. Milling was continued and the average particle size was monitored. Particle size measured with the Malvern 3600 Particle Size Analyzer was 6.3 pim. This corresponded to a 16 hour cold grind. The particulate media were removed and the toner was diluted to 2% solids with additional Isopar®-L and charged with 40 mg Basic Barium Petronate® (BBP)/g of toner solids resulting in conductivity of 25 pmhos/cm. Image quality was determined using a modified Savin 870 copier set up to evaluate positive toners. The copier was run with a i reversed image target and the following biases: development housing bias was +600V and transfer corona i was -6 kV. The image quality was very poor with 20 almost no discernable image. Image showed areas of i reversed image indicating that the toner was negatively charged and there was not enough image to measure resolution. Q/m measurement also showed toner was negatively charged with Q/m -92 and the ratio of the deposited positive particle weights/deposited negative particle weights Results are shown in Table 1 below.
CONTROL 2 The procedure of Control 1 was repeated with the i. following exceptions: no pigment was used. The toner O was cold ground for a 6 hours with final Malvern 3600 Particle Size Analyzer average particle size of im. The toner was diluted to 2% solids with *i 35 additional Isopar®-L and charged with 40 mg Basic 26 Barium Petronate®/g of toner solids resulting in conductivity of 29 pmhos/cm. Image quality was determined using a modified Savin 870 copier set up to evaluate negative toners. The copier was run with a standard image target and the following biases: development housing bias was +500V and transfer corona was +6 kV. Image quality showed a fair image and the toner was negatively charged. Q/m measurement also showed toner was negatively charged with Q/m -159 and the ratio of the deposited positive particle weight/deposited negative particle weights 0 Results are shown in Table 1 below.
CONTROL 3 In a Union Process 01 Attritor, Union Process Company, Akron, Ohio, were placed the following ingredients: Inaredients Amount (a) Terpolymer of methyl acrylate 35.00 (67.3%)/methacrylic acid ethyl hexyl acrylate (29.6%) weight average molecular weight of 172,000, acid no. is 13 Columbia Red Med, RD 2392 f’e’ Paul Uhlich Co., Hastings-On-Hudson, NY Isopar®-L, as described in Control 1 200.0 to The ingredients were heated to 90 0 C to 110 0 C and milled 0.1875 inch (4.76 mm) diameter stainless steel balls for 2 hours. The attritor was cooled to ambient temperature while milling was continued. Milling was 6 continued for 24.5 hours and the average particle size was 1.0 irm as measured on the Horiba CAPA-500 centrifugal automatic particle analyzer. The 26 L ~i~L~ 27 particulate media were removed and the dispersion of toner particles was then diluted to 2% solids with additional Isopar®-L and charged with 266 mg Emphos®D70-30C(EP)/g of toner solids) resulting in conductivity of 17 pmhos/cm. Images were made by means of a photoconducting film, such as are described in Mattor U.S.Patent 3,314,788 and Paulin et al. U.S. Patent 4,248,952, the disclosures of which are incorporated herein by reference, and which has a base support, 0.007 inch (0.18 mm) polyethylene terephthalate, bearing two layers, the outer layer being an organic photoconductive layer, and the inner layer next to the support being an electrically conductive layer such as aluminum, a portion of outer layer being removed along at least one edge thereof to define a strip of the conductive layer and on the exposed strip a conductive paint such as carbon black was placed so as to permit the conductive layer to be *G grounded. The photoconducting film used was passed 20 over a -1000V scorotron at 0. inch/second (1.27 cm/second), discharged selecti* -ly using a cathode ray tube, and toned with the developer using a developerfilled gap between a -350 V development electrode and the charged film. The images were fused in an oven at 115 0 F (46 0 C) for 1 minute, and cooled to room temperature. Using the imaging method described in this control, reverse or negative images were obtained. Results are shown in Table 1 below.
CONTROL 4 2 The toner was prepared as described in Example 2 except for the following changes: 200 grams of Isopar®-L and 88 grams of Isopar®-H, and 0.9 gram of 1-hexadecanesulfonic acid (HDSA) was added in place of 35 2-bromoethanesulfonic acid, sodium salt. Milling was 27 1 28 continued for 27 hours and the average particle size of 1.30 m was measured on the Horiba CAPA-500 centrifugal automatic particle analyzer. The particulate media were removed and the dispersion of toner particles was then diluted to 2% solids with Isopar®-L and charged with 40 mg Basic Barium Petronate®/g of toner solids to obtain a conductivity of 19 pmhos/cm. Image quality was determined using a modified Savin 870 copier set up to evaluate positive toners. The copier was run with a reversed image target and the following biases: development housing bias was +600V and transfer corona was -6 kV. Image quality was poor and image indicated that the toner was negatively charged. Image demonstrated 4 Ip/mm resolution of unfilled lines and poor density. Q/m measurement also showed that the toner was negatively charged with Q/m -66 and the ratio of the deposited positive particle weights/deposited negative particle weights 0. Results are shown in Table 1 below. An 20 equivalent weight amount of 1-hexadecanesulfonic acid (0.04% by weight based on the amount used in the 2% solids toner) is substantially soluble in Isopar®-L, demonstrating that a salt soluble in the nonpolar liquid does not enhance positive charging. Results 25 are shown in Table 2 below.
CONTROL The procedure of Control 1 was repeated with the following exceptions: 0.80 gram of p-toluenesulfonic 30 acid, Fisher Scientific, Pittsburgh, PA (pTSA), was added to the toner carrier liquid after dilution and no charge director was added resulting in conductivity of 0 pmho/cm. Image quality was determined using a modified Savin 870 copier set up to evaluate positive o: 35 toners. The copier was run with a reversed image .28 S se 28 ~i -nj- r I target and the following biases: development housing bias was +600V and transfer corona was -6 kV. Image quality was poor with faint washed-out reversed image indicating that the toner was weakly positive or bipolar. Image demonstrated 10 Ip/mm resolution but features were not filled in and density was very low.
Q/m measurement showed toner was bipolar with Q/m -4 and the ratio of the deposited positive particle weights/deposited negative particle weights 0.09.
Results are shown in Table 1 below.
CONTROL 6 The procedure of Control 1 was repeated with the following exceptions: 0.80 gram of p-toluene-sulfonic acid, Aldrich Chemical Co. (pTSA) was added to the tonf carrier liquid after dilution and charging with mg Basic Barium Petronate®/g of toner solids resulting in conductivity of 26 pmhos/cm. Image quality was determined using a modified Savin 870 20 copier set up to evaluate positive toners. The copier was run with a reversed image target and the following biases: development housing bias was +600V and transfer corona was -6 kV. Image quality was fair with reversed image indicating that the toner was 25 negatively charged. The reversed image was blotchy with 10 Ip/mm resolution of unfilled lines and fair density. Q/m measurement also showed toner was negatively charged with Q/m -104 and the ratio of the deposited positive particle weights/deposited s.
30 negative particle weights 0. Results are shown in Table 1 below.
The procedure of Control 1 was repeated with the 35 following exceptions: 51.28 grams of Heucophthal Blue e 00 0 00 i v I ,1
I
G XBT-583D were used instead of 50.00. In addition 5.13 grams of p-toluenesulfonic acid, Fisher Scientific, Pittsburgh, PA (pTSA) was added at the beginning. The toner was cold ground for 17 hours with final Malvern 3600 Particle Size Analyzer average particle size of 4.0 lm. The toner was diluted to 2% solids with additional Isopar®-L and charged with mg Basic Barium Petronate®/g of toner solids resulting in conductivity of 9 pmhos/cm. Image quality was determined using a modified Savin 870 copier set up to evaluate positive toners. The copier was run with a reversed image target and the following biases: development housing bias was +700V and transfer corona was -6 kV. Image quality was very good and image indicated that the toner was positively charged. Image demonstrated 7 Ip/mm resolution and good density. Q/m measurement also showed toner was positively charged with Q/m +109 and the deposited negative particle weight was 0. An equivalent amount 20 of p-toluenesulfonic acid by weight based on the amount used in 2% solids toner) was substantially insoluble in Isopar®-L. Results are shown in Table 1 below.
25 EXAMPLE 2 The following ingredients were placed in a Union Process 01 Attritor, Union Process Company, Akron, Ohio:
S
S
*D S
S
S.
S..
S
S..
e
S
55 5 0 00 31 Inredients Amount (g) Copolymer of ethylene 35.00 and methacrylic acid melt index at 190 0 C is 100, acid no.
is 66 Isopar®-L as described in Control 1 125.0 Heucophthal Blue G XBT-583D, 8.97 Heubach, Inc., Newark, NJ 2-Bromoethanesulfonic acid, Na salt 0.90 (Br ESA), Aldrich Chemical Co.
The ingredients were heated to 90 0 C to 110 0 C and milled at a rotor speed of 230 rpm with 0.1875 inch (4.76 mm) diameter stainless steel balls for 2 hours.
The attritor was cooled to ambient temperature while milling was continued and then 88 grams of Isopar®-H (Exxon Corp.) was added. Milling was continued for 24.5 hours and the average Malvern 3600 Particle Size Analyzer particle size was 8.2 pm. The particulate media were removed and the dispersion of toner 0 S 25 particles was then diluted to 2% solids with sea additional Isopar®-L and charged with 40 mg Basic Barium Petronate®/g of toner solids resulting in conductivity of 17 pmhos/cm. Image quality was 0i» determined using a modified Savin 870 copier set up to evaluate positive toners. The copier was run with a reversed image target and the following biases: development housing bias was +600V and transfer corona was -6 kV. Image quality was very good and image indicated that the toner was positively charged.
Image demonstrated 10 Ip/mm resolution and good density. Q/m measurement also showed toner was positively charged with Q/m +66 and the deposited negative particle weight was 0. An equivalent amount of 2-bromoethanesulfonic acid (0.04% by weight based *31 31 32 on the amount used in 2% solids toner) was substantially insoluble in Isopar®-L. Results are found in Table 1 below.
EXAMPLE 3 The procedure of Example 2 was repeated with the following changes: the Na salt of 3-hydroxy-lpropanesulfonic acid, Aldrich Chemical Co. (HOPSA) was used in place of the Na salt of 2-bromoethanesulfonic acid. The toner was cold ground for 23.5 hours with final average Malvern particle size of 7.0 pm. The toner was diluted to 2% solids with additional Isopar®-L and charged with 40 mg Basic Barium Petronate®/g of toner solids resulting in conductivity of 16 pmhos/cm. Image quality was determined using a modified Savin 870 copier set up to evaluate positive toners. The copier was run with a reversed image target and the following biases: development housing bias was +600V and transfer corona 20 was -6kV. Image quality was very good and image indicated that the toner was positively charged.
Image demonstrated 10 Ip/mm resolution and good density. Q/m measurement also showed toner was positively charged with Q/m +132 and the deposited 25 negative particle weight was 0. An equivalent amount of Na salt of 3-hydroxy-l-propanesulfonic acid (0.04% by weight based on the amount used in 2% solids toner) was substantially insoluble in Isopar®-L. Results are shown in Table 1 below.
EXAMPLE 4 The procedure of Example 1 was repeated with the following exceptions: the Barium salt of p- Toluenesulfonic acid, Aldrich Chemical Co. (BapTSA) 35 was used in place of the p-toluenesulfonic acid. The 33 toner was cold ground for 17 hours with final average particle size of 3.6 pun. The toner was diluted to 2% solids with additional Isopar®-L and charged with mg Basic Barium Petronate®/g of toner solids resulting in conductivity of 14 pmhos/cm. Image quality was determined using a modified Savin 870 copier set up to evaluate positive toners. The copier was run with a reversed image target and the following biases: development housing bias was +600V and transfer corona was -6 kV. Image quality was very good and image indicated that the toner was positively charged. Image demonstrated 10 Ip/mm resolution and good density. Q/m measurement also showed toner was positively charged with Q/m +309 and the ratio of the deposited positive particle weights/deposited negative particle weights =12.5. An equivalent amount of the Ba salt of p-toluenesulfonic acid (0.04% by weight based on the amount used in 2% solids toner) was substantially insoluble in Isopar®-L. Results V 20 are shown in Table 1 below.
too .o EXAMPLE *The toner was prepared as described in Example 2 to* with the following exceptions: 200 grams of 0090 25 Isopar®-L were used instead of 125 grams of Isopar®-L and 88 grams of Isopar®-H, and 0.9 gram of benzenesulfonic acid, Aldrich Chemical Co. (BzSA) was added in place of 2-bromoethanesulfonic acid, sodium salt. The ingredients were heated to 90° to 110 0 C and 30 milled for 3 hours. The attritor was cooled to an O ambient temperature while milling was continued.
Milling was continued for 27 hours and the average particle size of 1.59 pm was measured on the Horiba CAPA-500 centrifugal automatic particle analyzer. The 35 particulate media were removed and the dispersion of 33
I
L-
i i i-~ toner particles was then diluted to 2% solids with additional Isopar®-L and charged with 40 mg Bas Barium Petronate®/g of toner solids to obtain a conductivity of 6 pmhos/cm. Image quality was determined using a modified Savin 870 copier set up to evaluate positive toners. The copier was run with a reversed image target and the following biases: development housing bias was +600V and transfer corona was -6 kV. Image quality was very good and the image indicated that the toner was positively charged. Q/m measurement also showed toner was positively charged with Q/m +51 and the deposited negative particle weight was 0. An equivalent amount of benzenesulfonic acid (0.04% by weight based on the amount in 2% solids toner) was substantially insoluble in Isopar®-L.
Results are shown in Table 1 below.
EXAMPLE 6 The procedure of Example 2 was repeated with the 20 following exceptions: 40 grams of resin were used instead of 35 grams, 0.82 g of paratoluenesulfonic acid was used instead of 2-bromoethanesulfonic acid, sodium salt and no pigment was added. In the cold milling step, 125 grams of additional Isopar®-L were added instead of 88 grams. The toner was cold ground for 23 hours with final average particle size of 11.0 pn. The toner was diluted to 2% solids with additional Isopar®-L and charged with 40 mg Basic Barium Petronate®/g of toner solids resulting in 30 conductivity of 250 pmhos/cm. Inmage quality was determined using a modified Savin 870 copier set up to evaluate positive toners. The copier was run with a reversed image target and the following biases: development housing bias was +500V and transfer corona 35 was -6 kV. Image quality was very good with reverse
S
S*
i *000 000;:
O
0 S O
OS
0 image indicating that the toner was positively charged. The image demonstrated toning of fine lines and good density. Lp/mm could not be determined due to the lack of pigment in the image. Q/m measurement also showed toner was positively charged with Q/m =+573 and the deposited negative particle weight was 0. An equivalent amount of paratoluenesulfonic acid (0.04% by weight based on the amount used in 2% solids toner) was substantially insoluble in Isopar®-L.
Results are shown in Table 1 below.
EXAMPLE 7 Toner was prepared as described in Control 3 except that 0.7 gram of p-toluenesulfonic acid (pTSA) was added during the hot step. Milling was continued for 22 hours and the average particle size was 1.4 pm as measured on the Horiba CAPA-500 centrifugal automatic particle analyzer. The dispersion was diluted, charged and evaluated. Evaluations were carried out as described in Control 3. Images showed good resolution, and grey scale. Results are shown in Table 1 below.
EXAMPLE 8 25 The procedure of example 2 was repeated with the following changes: sodium n-butyl sulphate, Lancaster Synthesis (NanBS) was used in place of the 2bromoethanesulfonic acid. The toner was cold ground for 19 hours with final average Malvern 3600 Particle Size Analyzer particle size of 7.6 gm. The toner was diluted to 2% solids with additional Isopar®-L and charged with 40 mg Basic Barium Petronate®/g of toner Ssolids resulting in conductivity of 10 pmhos/cm.
Image quality was determined using a modified Savin 35 870 copier set up to evaluate positive toners. The 2 ft I 36 copier was run with a reversed image target and the following biazes: development housing bias was +1000V and transfer corona was -9kV. Image quali.ty was good and image indicated that the toner was positively charged. Image demonstrated 8.5 lp/rnm resolution and good density. Q/m +30.1 and t,-he ratio of the deposited positive particle weights/deposited negative particle weights 140. Results are found in Table 1 below.
.0Tal1
BULK
(nmhr-nh/r’mT Fly AMT P Trq~k 1 (7 (mn S. Sb S
S
OS
6 55* S. go S S a
‘S
I
S..
0 El 055 0565 S Sa 00 S SO
S
*5 55 0 06 S SO
S
*6.5
SO
5* 6 65 d
SO
0* Cl C2 C3 C4 20 C6 El E2 E3 E4 25 ES E6 E7 E8 30 1 2 3
H-DSA
pTSA 1 pTSAI pTSA B rESA
HOPSA
BapTSA BzSA pTSA pTSA NanBS added Cy is RD is RD 3 Cy (20) Cy (20) Cy (20) Cy (20) Cy (20) CY (20) Cy (20) Cy (20) RD (1 6) Cy (20) after di cyan red EP (266) BBP (4 0) BBP (4 0) BBP (4 0) BBP (4 0) BBP (4 0) BBP (4 0) BBP (4 0) BBP (4 0) EP (266) BBP (4 0) Cy(20) 2 BBP(40) BBP (4 0) 25 29 17 19 0 26 9 17 16 14 6 250 20 10 92 159 2.63 66 4 -104 109 66 132 309 51 573 +1500 lution 37 Table 2 Solubility in nonpolar Sulfur-Containing Compound Liquid Effect p-toluenesulfonic Acid I p-toluenesulfonic Acid, Ba Salt I Hydroxypropanesulfonic Acid, Na Salt I Bromoethanesulfonic Acid, Na Salt I Benzenesulfonic Acid I Hexadecanesulfonic Acid S Sodium n-butylsulphate I 00 37

Claims (7)

1. A positive electrostatic liquid developer having improved charging and imaging characteristics consisting essentially of a nonpolar liquid having a Kauri- butanol value of less than 30, present in a major amount, thermoplastic resin particles having dispersed therein an adjuvant which is substantially insoluble in the nonpolar liquid at ambient temperatures and is an organic sulfur-containing compound selected from the group consisting of R-S=0 R-O-S=0 R S=0 {OH n=l-4 {OH n=1-6 (3 H n=1-2 and the salts of and 3, wherein R is alkyl of 1 to 30 carbon atoms, substituted alkyl of 1 to 30 carbon atoms, aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, the resin particles having an average by area 25 particle size of less than 10 pm, and a nonpolar liquid soluble ionic or zwitterionic charge director compound.

2. An electrostatic liquid developer according to claim 1 wherein the sulfur-containing compound is 30 of the formula: I R-= SOH n 38 l I E C~ wherein R is alkyl of 1 to 30 carbon atoms, substituted alkyl of 1 to 30 carbon atoms, aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, and n is 1 to 4, and their salts.

3. An electrostatic liquid developer according to claim 2 wherein the sulfur-containing compound is p-toluenesulfonic acid.

4. An electrostatic liquid developer according to claim 2 wherein the sulfur-containing compound is p-toluenesulfonic acid, barium salt. An electrostatic liquid developer according to claim 1 wherein the sulfur-containing compound is of the formula: o-0-S=o OH n wherein R is alkyl of 1 to 30 carbon atoms, substituted alkyl of 1 to 30 carbon atoms, aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, and n is 1 to 6, and their salts.

6. An electrostatic liquid developer according 25 to claim 5 wherein the sulfur-containing compound is n-butylsulfate, sodium salt.

7. An electrostatic liquid developer according to claim 5 wherein the sulfur-containing compound is decylsulfate, sodium salt. 30 8. An electrostatic liquid developer according to claim 1 wherein component is present in 85 to

99.9% by weight, based on the total weight of liquid developer, the total weight of developer solids is 0.1 to 15.0% by weight, and component is present in an amount of 0.1 to 10,000 mg/g developer solids. I I 9. An electrostatic liquid developer according to claim 8 wherein the sulfur-containing compound is present in 0.1 to 10% by weight based on the total weight of the developer solids. 10. An electrostatic liquid developer according to claim 1 containing up to about 60% by weight of a colorant based on the total weight of developer solids. 11. An electrostatic liquid developer according to claim 10 wherein the colorant is a pigment. 12. An electrostatic liquid developer according to claim 10 wherein the colorant is a dye. 13. An electrostatic liquid developer according to claim 1 wherein a fine particle size oxide is present. 14. An electrostatic liquid developer according to claim 1 wherein an additional compound is present which is an adjuvant selected from the group consisting of polybutylene succinimide, aromatic S* 20 hydrocarbon and alkylhydroxybenzylpolyamine. 15. An electrostatic liquid developer according to claim 10 wherein an additional compound is present which is an adjuvant selected from the group consisting of polybutylene succinimide, aromatic 25 hydrocarbon and alkylhydroxybenzylpolyamine. 16. An electrostatic liquid developer according to claim 14 wherein a polybutylene succinimide adjuvant compound is present. S» 17. An electrostatic liquid developer according 30 to claim 14 wherein an aromatic hydrocarbon adjuvant compound is present. 18. An electrostatic liquid developer according to claim 1 wherein the thermoplastic resin is a copolymer of ethylene and an a,B-ethylenically L 1.4 ii 41 unsaturated acid selected from the group consisting of acrylic acid and methacrylic acid. 19. An electrostatic liquid developer according to claim 1 wherein the thermoplastic resin is polystyrene. An electrostatic liquid developer according to claim 1 wherein the thermoplastic resin is a copolymer of ethylene (80 to 99.9%)/acrylic or methacrylic acid (20 to 0%)/alkyl ester of acrylic or methacrylic acid wherein alkyl is 1 to 5 carbon atoms (0 to 21. An electrostatic liquid developer according to claim 10 wherein the thermoplastic resin is a copolymer of ethylene (80 to 99.9%)/acrylic or methacrylic acid (20 to 0%)/alkyl ester of acrylic or methacrylic acid wherein alkyl is 1 to 5 carbon atoms (0 to 22. An electrostatic liquid developer according to claim 20 wherein the thermoplastic resin is a o. 20 copolymer of ethylene (89%)/methacrylic acid (13%/ ohaving a melt index at 190 0 C of 100. 23. An electrostatic liquid developer according to claim 1 wherein the particles have an Avrage by o* area particle size of less than 5 iem. 24. An electrostatic liquid developer according to claim 1 wherein component is an oil-soluble petroleum sulfonate. 25. An electrostatic liquid developer according to claim 1 wherein component is ,ithin. 26. A process for preparing ap itive electrostatic liquid developer for electrostatic imaging comprising dispersing at an elevated temperature in a vessel a thermoplastic resin, sulfur-containing z 0 substituted alkyl of to 30 carbon atoms, aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, and a dispersant nonpolar liquid having a Kauri-butanol value of less than 30, while maintaining compound of the formula the vessel eted from the groupre sufficient to plasticize and liquify the resin and below that at which the dispersant nonpolar liquid considegrades and the resin decomposes, (oo-S=0 s= OH 1 n=l-4 I OH n=l-6 IOH Jn=l-2 and the salts of and either wherein R is alkyl of 1 to 30 carbon atoms, ubstituted alky* of to 30 carbon atoms,form aryl of 6 to 30 carbos, followed by shrtituteddi aryl of 6 to 30 carbon atoms, and a grinding by mespersant nonpolarticulate media with Kauri-btutanol valupresence of addiless than 30, while maintaining the temperature in the vessel at a tform a viscousture sufficient to plasticize by means of particulate media below that aor without which the dispersant nonpolar liquid; or while grinding by means of particulate media to prevent the formation of a gel or liquid; or 20 cool separating the dispersion of toner i| without stirring to form a gel or partsolid mass, followed by shredding the gel or soidze of malss and grinding by means of particulate media with S,or without presence of additional liquid; 25 with stirring to form a viscous mixture and grinding by means of particulate media with or without the presence of additional liquid; or while grinding by means of I particulate media to prevent the formation of a gel or 30 solid mass with or without the presence of additional liquid; or separating the dispersion of toner ‘particles having an average by area particle size of less than 10 CAm from the particulate media, and o• r 43 43 adding to the dispersion during or subsequent to Step A a nonpolar liquid soluble ionic or zwitterionic charge director compound. 27. A process according to claim 26 wherein the sulfur-containing compound is of the formula 0 P-S=0 I OH n wherein R is alkyl of 1 to 30 carbon atoms, substituted alkyl of 1 to 30 carbon atoms, aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, and n is 1 to 4, and their salt. 28. A process according to claim 27 wherein the sulfur-containing compound is p-toluenesulfonic acid. 29. A process according to claim 27 wherein the sulfur-containing compound is p-toluenesulfonic acid, S barium salt. A process according to claim 26 wherein the .sulfur-containing compound is the sulfur-containing S* compound is of the formula S* I OH n wherein R is alkyl of 1 to 30 carbon atoms, substituted alkyl of 1 to 30 carbon atoms, aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, and n is 1 to 6, and their salts. S* 35 31. A process according to claim 30 wherein the sulfur-containing compound is n-butylsulfate, sodium salt. a 00 43 44 32. A process according to claim 30 wherein the sulfur-containing compound is decylsulfate, sodium salt. 33. A process according to claim 26 wherein there is present in the vessel up to 100% by weight of a polar additive having a Kauri-butanol value of at least 30, the percentage based on the total weight of the liquid. 34. A process according to claim 26 wherein the particulate media are selected from the group consisting of stainless steel, carbon steel, ceramic, alumina, zirconium, silica and sillimanite. A process according to claim 26 wherein the thermoplastic resin is a copolymer of ethylene and an a,8-ethylenically unsaturated acid selected from the group consisting of acrylic acid and methacrylic acid. 36. A process according to claim 26 wherein the thermoplastic resin is a copolymer of ethylene (80 to 99.9%)/acrylic or methacrylic acid (20 to 0%)/alkyl 20 ester of acrylic or methacrylic acid wherein alkyl is 1 to 5 carbon atoms (0 to 37. A process according to claim 36 wherein the thermoplastic resin is a copolymer of ethylene (89%) methacrylic acid having a melt index at 190 0 C of 25 100. 38. A process according to claim 26 wherein at least one colorant is present in dispersing step and the temperature is maintained in the vessel at a temperature sufficient to plasticize and liquify the 30 resin and below that at which the dispersant nonpolar liquid degrades and the resin and colorant decomposes. e 39. A process according to claim 26 wherein the charge director compound is an oil-soluble petroleum sulfonate. *4 44 I A process according to claim 26 wherein the charge director is lecithin. 41. A process according to claim 26 wherein the additional dispersant nonpolar liquid polar liquid or combinations thereof is present to reduce the concentration of toner particles to between 0.1 to percent by weight with respect to the liquid. 42. A process according to claim 41 wherein the concentration of toner particles is reduced by additional dispersant nonpolar liquid. 43. A process according to claim 26 wherein cooling the dispersion is accomplished while grinding by means of particulate media to prevent the formation of a gel or solid mass with or without the presence of additional liquid. 44. A process according to claim 26 wherein cooling the dispersion is accomplished without stirring to form a gel or solid mass, followed by shredding the gel or solid mass and grinding by means 20 of particulate media with or without the presence of **additional liquid. 0 45. A process according to claim 26 wherein cooling the dispersion is accomplished with stirring to form a viscous mixture and grinding by means of particulate media with or without the presence of additional liquid. 46. A process according to claim 26 wherein an adjuvant compound selected from the group consisting of polybutylene succinimide, aromatic hydrocarbon, and alkylhydroxybenzylpolyamine is added to the liquid ueveloper. 47. A process according to claim 38 wherein an adjuvant compound selected from the group consisting of polybutylene succinimide and an aromatic *0 *0 xr* I I 46 hydrocarbon, and alkylhydroxybenzylpolyamine is added to the liquid developer. 48. A process for preparing electrostatic liquid developer comprising dispersing an organic sulfur- containing compound of the formula selected from the group consisting of r° 0 R-S=O R-0-S=0 (3) ,OH n=l-4 OH n=l-6 -H n=l-2 and the salts of and wherein R is alkyl of 1 to 30 carbon atoms, substituted alkyl of 1 to 30 carbon atoms, aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, in a thermoplastic resin in the absence of a dispersant nonpolar liquid having a Kauri-butanol value of less than 30 to form a solid mass. shredding the solid mass, grinding the shredded solid mass by S 25 means of particulate media in the presence of a liquid selected from the group consisting of a polar liquid having a Kauri-butanol value of at least 30, a nonpolar liquid having a Kauri-butanol value of less 3 than 30, and combinations thereof. S 30 separating the dispersion of toner S particles having an average by area particle size of A a less than 10 m from the particulate media, and adding additional nonpolar liquid, polar liquid or combinations thereof to reduce the *0 35 concentration of toner particles to between 0.1 to 15.0 percent by weight with respect to the liquid; and I* SI 47 adding to the dispersion a liquid soluble ionic or zwitterionic charge director compound. 49. A process for preparing electrostatic liquid developer comprising dispersing an organic sulfur- containing compound of the formula selected from the group consisting of 0 0 R-S=0 R-0-S=0 S= OH J n=1-4 OH j n=1-6 OH n=l-2 and the salts of and wherein R is alkyl of 1 to 30 carbon atoms, substituted alkyl of 1 to 30 carbon atoms, aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, substituted aryl of 6 to 30 carbon atoms, in a thermoplastic resin in the absence of a dispersant nonpolar liquid having a Kauri-butanol value of less 0 than 30 to form a solid mass. shredding the solid mass, 25 redispersing the shredded solid mass •j at an elevated temperature in a vessel in the presence of a dispersant nonpolar liquid having a Kauri-butanol value of less than 30, while maintaining the temperature in the vessel at a temperature sufficient 30 to plasticize and liquify the resin and below that at which the dispersant nonpolar liquid degrades and the resin decomposes, S. cooling the dispersion, either without stirring to form a gel or 35 solid mass, followed by shredding the gel or solid I 48 mass and grinding by means of particulate media with or without the presence of additional liquid; with stirring to form a viscous mixture and grinding by means of particulate media with or without the presence of additional liquid; or while grinding by means of particulate media to prevent the formation of a gel or solid mass with or without the presence of additional liquid; separating the dispersion of toner particles having an average by area particle size of less than 10 pim from the particulate media, and adding additional nonpolar liquid, polar liquid or combinations thereof to reduce the concentration of toner particles to between 0.1 to 15.0 percent by weight with respect to the liquid; and adding to the dispersion a liquid soluble ionic or zwitterionic charge director compound. 20 50. A process according to claim 49 wherein at least one colorant is present in redispersing step S. and the temperature is maintained in the vessel at a temperature sufficient to plasticize and liquify the resin and below that at which the dispersant nonpolar liquid degrades and the resin and colorant decomposes. DATED THIS 29TH DAY OF DECEMBER 1989 e E. I. DU PONT DE NEMOURS AND COMPANY By its Patent Attorneys: GRIFFITH HACK CO. Fellows Institute of Patent Attorneys of Australia 48

AU47373/89A
1988-12-30
1989-12-29
Organic sulfur-containing compounds as adjuvants for positive electrostatic liquid developers

Ceased

AU607090B2
(en)

Applications Claiming Priority (2)

Application Number
Priority Date
Filing Date
Title

US292291

1988-12-30

US07/292,291

US4917985A
(en)

1988-12-30
1988-12-30
Organic sulfur-containing compounds as adjuvants for positive electrostatic liquid developers

Publications (2)

Publication Number
Publication Date

AU4737389A

AU4737389A
(en)

1990-07-19

AU607090B2
true

AU607090B2
(en)

1991-02-21

Family
ID=23124041
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

AU47373/89A
Ceased

AU607090B2
(en)

1988-12-30
1989-12-29
Organic sulfur-containing compounds as adjuvants for positive electrostatic liquid developers

Country Status (10)

Country
Link

US
(1)

US4917985A
(en)

EP
(1)

EP0376303A3
(en)

JP
(1)

JPH02228675A
(en)

KR
(1)

KR900010479A
(en)

CN
(1)

CN1044349A
(en)

AU
(1)

AU607090B2
(en)

CA
(1)

CA2006217A1
(en)

DK
(1)

DK674089A
(en)

FI
(1)

FI896346A0
(en)

NO
(1)

NO895335L
(en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US5035972A
(en)

*

1989-10-31
1991-07-30
E. I. Du Pont De Nemours And Company
AB diblock copolymers as charge directors for negative electrostatic liquid developer

US5130221A
(en)

*

1990-03-07
1992-07-14
Dximaging
Salts of acid-containing ab diblock copolymers as charge directors for positive-working electrostatic liquid developers

EP0456177A1
(en)

*

1990-05-11
1991-11-13
Dximaging
Hydrocarbon soluble sulfonic or sulfamic acids as charge adjuvants for positive electrostatic liquid developers

US5066821A
(en)

*

1990-05-11
1991-11-19
Dximaging
Process for preparing positive electrostatic liquid developers with acidified charge directors

US5525448A
(en)

*

1994-03-31
1996-06-11
Xerox Corporation
Liquid developer compositions with quaternized polyamines

US7144671B2
(en)

*

2003-09-30
2006-12-05
Samsung Electronics Company
Adjuvants for negatively charged toners

US7070900B2
(en)

*

2003-09-30
2006-07-04
Samsung Electronics Company
Adjuvants for positively charged toners

US8252854B2
(en)

*

2007-07-03
2012-08-28
Hewlett-Packard Development Company, L.P.
Sulfonated or phosphonated latex polymers for ink-jet printing

Citations (3)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

AU2587888A
(en)

*

1987-11-25
1989-05-25

E.I. Du Pont De Nemours And Company

Glycerides as charge directors for liquid electrostatic developers

AU588155B2
(en)

*

1987-08-03
1989-09-07

E.I. Du Pont De Nemours And Company

Liquid electrostatic developers containing modified resin particles

AU599506B2
(en)

*

1987-08-10
1990-07-19

E.I. Du Pont De Nemours And Company

Stabilizers for electrostatic liquid developers

Family Cites Families (18)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US3681243A
(en)

*

1968-05-30
1972-08-01
Ricoh Kk
Liquid developer for electrophotography containing stain texture preventing agent

GB1448350A
(en)

*

1973-06-14
1976-09-02
Canon Kk
Liquid developer for electrostatic latent image

JPS5624943B2
(en)

*

1973-12-28
1981-06-09

GB1571787A
(en)

*

1975-09-16
1980-07-16
Agfa Gevaert
Electrophoretic developer

US4259428A
(en)

*

1978-03-16
1981-03-31
Canon Kabushiki Kaisha
Liquid developer for electrostatic latent image

US4425418A
(en)

*

1981-05-19
1984-01-10
Konishiroku Photo Industry Co., Ltd.
Liquid developers for electrophotography and developing method using the same

US4879197A
(en)

*

1985-04-12
1989-11-07
Mitsubishi Paper Mills, Ltd.
Method of developing electronic photograph with liquid developer and cleaning excess thereof

US4760009A
(en)

*

1985-12-04
1988-07-26
E. I. Du Pont De Nemours And Company
Process for preparation of liquid toner for electrostatic imaging

US4734352A
(en)

*

1986-04-22
1988-03-29
E. I. Du Pont De Nemours And Company
Polyhydroxy charging adjuvants for liquid electrostatic developers

US4702985A
(en)

*

1986-04-28
1987-10-27
E. I. Du Pont De Nemours And Company
Aminoalcohols as adjuvant for liquid electrostatic developers

US4702984A
(en)

*

1986-04-30
1987-10-27
E. I. Dupont De Nemours And Company
Polybutylene succinimide as adjuvant for electrostatic liquid developer

US4707429A
(en)

*

1986-04-30
1987-11-17
E. I. Du Pont De Nemours And Company
Metallic soap as adjuvant for electrostatic liquid developer

US4681831A
(en)

*

1986-06-30
1987-07-21
E. I. Du Pont De Nemours And Company
Chargeable resins for liquid electrostatic developers comprising partial ester of 3-hydroxypropanesulfonic acid

US4780389A
(en)

*

1987-02-13
1988-10-25
E. I. Du Pont De Nemours And Company
Inorganic metal salt as adjuvant for negative liquid electrostatic developers

US4758494A
(en)

*

1987-02-13
1988-07-19
E. I. Du Pont De Nemours And Company
Inorganic metal salt as adjuvant for negative liquid electrostatic developers

US4772528A
(en)

*

1987-05-06
1988-09-20
E. I. Du Pont De Nemours And Company
Liquid electrostatic developers composed of blended resins

US4783388A
(en)

*

1987-06-17
1988-11-08
E. I. Du Pont De Nemours And Company
Quaternaryammonium hydroxide as adjuvant for liquid electrostatic developers

US4820605A
(en)

*

1987-11-25
1989-04-11
E. I. Du Pont De Nemours And Company
Modified liquid electrostatic developer having improved image scratch resistance

1988

1988-12-30
US
US07/292,291
patent/US4917985A/en
not_active
Expired – Fee Related

1989

1989-12-20
CA
CA002006217A
patent/CA2006217A1/en
not_active
Abandoned

1989-12-28
EP
EP19890124071
patent/EP0376303A3/en
not_active
Withdrawn

1989-12-28
JP
JP1338849A
patent/JPH02228675A/en
active
Pending

1989-12-29
FI
FI896346A
patent/FI896346A0/en
not_active
Application Discontinuation

1989-12-29
DK
DK674089A
patent/DK674089A/en
not_active
Application Discontinuation

1989-12-29
KR
KR1019890020635A
patent/KR900010479A/en
not_active
Application Discontinuation

1989-12-29
NO
NO89895335A
patent/NO895335L/en
unknown

1989-12-29
AU
AU47373/89A
patent/AU607090B2/en
not_active
Ceased

1989-12-30
CN
CN89109856A
patent/CN1044349A/en
active
Pending

Patent Citations (3)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

AU588155B2
(en)

*

1987-08-03
1989-09-07
E.I. Du Pont De Nemours And Company
Liquid electrostatic developers containing modified resin particles

AU599506B2
(en)

*

1987-08-10
1990-07-19
E.I. Du Pont De Nemours And Company
Stabilizers for electrostatic liquid developers

AU2587888A
(en)

*

1987-11-25
1989-05-25
E.I. Du Pont De Nemours And Company
Glycerides as charge directors for liquid electrostatic developers

Also Published As

Publication number
Publication date

DK674089A
(en)

1990-07-01

US4917985A
(en)

1990-04-17

DK674089D0
(en)

1989-12-29

AU4737389A
(en)

1990-07-19

NO895335L
(en)

1990-07-02

NO895335D0
(en)

1989-12-29

CA2006217A1
(en)

1990-06-30

EP0376303A3
(en)

1990-11-28

KR900010479A
(en)

1990-07-07

CN1044349A
(en)

1990-08-01

JPH02228675A
(en)

1990-09-11

FI896346A0
(en)

1989-12-29

EP0376303A2
(en)

1990-07-04

Similar Documents

Publication
Publication Date
Title

US5034299A
(en)

1991-07-23

Mineral acids as charge adjuvants for positive liquid electrostatic developers

US4702985A
(en)

1987-10-27

Aminoalcohols as adjuvant for liquid electrostatic developers

US5066821A
(en)

1991-11-19

Process for preparing positive electrostatic liquid developers with acidified charge directors

US5028508A
(en)

1991-07-02

Metal salts of beta-diketones as charging adjuvants for electrostatic liquid developers

US4886726A
(en)

1989-12-12

Glycerides as charge directors for liquid electrostatic developers

US4758494A
(en)

1988-07-19

Inorganic metal salt as adjuvant for negative liquid electrostatic developers

US5106717A
(en)

1992-04-21

Ab diblock copolymers as toner particle dispersants for electrostatic liquid developers

US5009980A
(en)

1991-04-23

Aromatic nitrogen-containing compounds as adjuvants for electrostatic liquid developers

US4957844A
(en)

1990-09-18

Liquid electrostatic developer containing multiblock polymers

AU607090B2
(en)

1991-02-21

Organic sulfur-containing compounds as adjuvants for positive electrostatic liquid developers

US5866292A
(en)

1999-02-02

Liquid developer compositions with copolymers

US4663264A
(en)

1987-05-05

Liquid electrostatic developers containing aromatic hydrocarbons

US4780389A
(en)

1988-10-25

Inorganic metal salt as adjuvant for negative liquid electrostatic developers

US4794066A
(en)

1988-12-27

Process for preparation of liquid electrostatic developer

US4971883A
(en)

1990-11-20

Metal alkoxide modified resins for negative-working electrostatic liquid developers

AU610032B2
(en)

1991-05-09

Bipolar liquid electrostatic developer

AU600617B2
(en)

1990-08-16

Monofunctional amines as adjuvant for liquid electrostatic developers

US5244766A
(en)

1993-09-14

Halogenated resins for liquid developers

US4917986A
(en)

1990-04-17

Phosphorous-containing compounds as adjuvant for positive electrostatic liquid developers

US5002848A
(en)

1991-03-26

Substituted carboxylic acids as adjuvants for positive electrostatic liquid developers

US4937158A
(en)

1990-06-26

Nickel (II) salts as charging adjuvants for electrostatic liquid developers

US5077171A
(en)

1991-12-31

Carbohydrate products of photosynthesis as charging adjuvant for positive liquid electrostatic developers

US4950576A
(en)

1990-08-21

Chromium, molybdenum and tungsten compounds as charging adjuvants for electrostatic liquid developers

CA2042097A1
(en)

1991-11-12

Hydrocarbon soluble sulfonic or sulfamic acids as charge adjuvants for positive electrostatic liquid developers

AU605439B2
(en)

1991-01-10

The use of high percent solids for improved liquid toner preparation

Download PDF in English