JP5463217B2 - Toner for electrophotography - Google Patents

Description

  The present invention relates to an electrophotographic toner, an aqueous dispersion of crystalline polyester used in the production of the toner, and a method for producing the same.

As one of the methods for producing an electrophotographic toner, an emulsion aggregation method has been proposed. This is because it has advantages such as enhancement of toner functions by structure control (core / shell) and improvement of image quality by control of toner surface shape.
For example, Patent Document 1 includes a core-shell structure electrostatic image developing toner having a shell on the surface of a core containing at least a resin and a colorant, and a resin-coated carrier, with heat storage stability and image fog as problems. A developer for developing an electrostatic image, wherein (1) the eight-point average film thickness of the electrostatic image developing toner shell is 100 to 300 nm, (2) the maximum film thickness of the shell is Hmax, and the minimum film When the thickness is Hmin, the ratio of both: Hmax / Hmin is 1.00 to 1.50, (3) When the glass transition temperature of the core is Tg1, and the glass transition temperature of the shell is Tg2, There is disclosed a developer for developing an electrostatic charge image, wherein 30 ° C. ≦ Tg1 ≦ 40 ° C., 45 ° C. ≦ Tg2 ≦ 55 ° C., and (4) the volume average particle diameter of the resin-coated carrier is 20 to 40 μm. .
In Patent Document 2, a resin resin fine particle dispersion containing at least one amorphous resin and a colorant are dispersed using a polyester resin that does not use a tin-based catalyst for the purpose of charging characteristics, color developability, and low-temperature fixing. A method for producing a toner for developing an electrostatic image, comprising mixing a colorant dispersion, aggregating the resin fine particles and the colorant to a toner particle diameter in an aqueous medium to form an aggregate, and heating and fusing the aggregate. It is disclosed.

JP 2009-288487 A JP 2007-004033 A

In the conventional emulsion aggregation method, an electrophotographic toner is obtained by preparing a resin dispersion and a colorant particle dispersion, mixing them, and aggregating particles in the mixed solution.
However, the resin was obtained by polycondensing an alcohol component containing an aliphatic diol having 2 to 12 carbon atoms and a carboxylic acid component containing 70 to 100 mol% of an aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms. When the crystalline polyester is used as a resin dispersion after production, the toner transferability and the pressure storage stability of the printed matter may be lowered.
An object of the present invention is to obtain an electrophotographic toner having high transfer efficiency and excellent pressurization storage stability of a printed matter, and to provide a method for producing an aqueous dispersion of crystalline polyester for the toner. is there.

The present invention relates to the following [1] to [4].
[1] One or more urea compounds selected from urea and alkylurea and / or one or more guanidine compounds selected from guanidine, alkylguanidine and acid addition salts thereof, and carbon in the presence of a neutralizing agent Crystalline polyester obtained by polycondensing an alcohol component containing an aliphatic diol having 2 to 12 carbon atoms and a carboxylic acid component containing 70 to 100 mol% of an aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms is an aqueous medium A method for producing an aqueous dispersion of crystalline polyester for toner, comprising a step of dispersing the toner in the toner.
[2] An aqueous dispersion of crystalline polyester for toner obtained by the production method according to [1].
[3] Manufacture of toner for electrophotography, comprising a step of subjecting the aqueous dispersion of crystalline polyester for toner according to [2] above to an aqueous dispersion of an amorphous resin to obtain aggregated particles. Method.
[4] An electrophotographic toner obtained by the production method according to [3].

  The aqueous dispersion of crystalline polyester for toner obtained by the production method of the present invention has a uniform dispersion diameter, and the electrophotographic toner obtained using the aqueous dispersion has excellent transfer efficiency and The obtained printed matter is excellent in pressure storage stability.

By using urea or guanidine during the production of the crystalline polyester dispersion, the inventors have improved the transfer efficiency of the toner obtained by agglomerating and coalescing the dispersion, and the pressure storage stability of the printed matter. It was found that (hereinafter, also simply referred to as storability) is improved.
The transfer efficiency of the toner increases because the presence of urea or guanidine at the time of dispersion of the crystalline polyester dissociates hydrogen bonds derived from the ester groups of the polyester and decreases the bonding force between the polyesters. It is presumed that the toner particles after the particle diameter was made uniform and the dispersed particles were aggregated and thermally fused were made more spherical.
In addition, the preservability of the printed matter is improved by the presence of urea or guanidine at the time of dispersion of the crystalline polyester, so that the hydrogen bond derived from the ester group of the crystalline polyester is broken and the crystalline polyester is recrystallized. It is presumed that it became easier to convert.
Each configuration will be described in detail below.

[Aqueous dispersion of crystalline polyester for toner and method for producing the same]
The aqueous dispersion of the crystalline polyester for toner of the present invention comprises one or more urea compounds selected from urea and alkyl urea and / or one or more guanidines selected from guanidine, alkyl guanidine and acid addition salts thereof. In the presence of a compound and a neutralizing agent, an alcohol component containing an aliphatic diol having 2 to 12 carbon atoms and a carboxylic acid component containing 70 to 100 mol% of an aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms are condensed. An aqueous dispersion produced by a method comprising a step of dispersing a crystalline polyester obtained by polymerization (hereinafter also simply referred to as “crystalline polyester”) in an aqueous medium.

(Crystalline polyester)
The crystalline polyester used in the present invention comprises at least an alcohol component containing an aliphatic diol having 2 to 12 carbon atoms and a carboxylic acid component containing 70 to 100 mol% of an aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms. Obtained by condensation polymerization.

Here, the crystallinity of a resin such as polyester is the crystallinity defined by the ratio between the softening point and the maximum endothermic peak temperature measured by a differential scanning calorimeter (DSC), that is, the “softening point / maximum endothermic peak temperature”. Expressed by an index. Generally, when the crystallinity index exceeds 1.4, the resin is amorphous, and when it is less than 0.6, the crystallinity is low and there are many amorphous portions. In the present invention, “crystalline polyester” refers to a polyester having a crystallinity index of 0.6 to 1.4, preferably 0.8 to 1.2, more preferably 0.9 to 1.1. “Amorphous resin” refers to a resin having a crystallinity index greater than 1.4 or less than 0.6.
The above “maximum endothermic peak temperature” refers to the temperature of the peak on the highest temperature side among the endothermic peaks observed under the measurement method conditions described in the examples. If the maximum peak temperature is within 20 ° C. from the softening point, the maximum peak temperature is the melting point of the crystalline resin (crystalline polyester), and the peak with the difference from the softening point exceeding 20 ° C. is glass of amorphous resin. The peak is attributed to the transition.
The crystallinity of the resin can be adjusted by the type and ratio of the raw material monomers, production conditions (for example, reaction temperature, reaction time, cooling rate) and the like.

<Alcohol component>
The alcohol component which is a raw material monomer of the crystalline polyester contains an aliphatic diol having 2 to 12 carbon atoms from the viewpoint of enhancing the crystallinity of the polyester.
Examples of the aliphatic diol having 2 to 12 carbon atoms include ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,7-heptanediol, 1,8-octanediol, 1,9-nonanediol, 1,10-decanediol, 1,11-undecanediol, 1,12-dodecanediol, neopentyl glycol and 1,4- Examples include butenediol. Among these, from the viewpoint of low-temperature fixability, pressure storage stability, and environmental stability of the toner, an aliphatic diol having 5 to 9 carbon atoms is preferable, and an aliphatic diol having 5 to 6 carbon atoms is more preferable. From the viewpoint of crystallinity, α, ω-linear alkanediol having 2 to 12 carbon atoms is preferable, α, ω-linear alkanediol having 5 to 9 carbon atoms is more preferable, and 1,6-hexanediol. Is more preferable.

  From the viewpoint of further improving the crystallinity of the crystalline polyester, the content of the aliphatic diol having 2 to 12 carbon atoms is preferably 70 mol% or more, more preferably 80 to 100 mol%, still more preferably in the alcohol component. 90 to 100 mol%. The content of one kind of α, ω-linear alkanediol having 2 to 12 carbon atoms in the alcohol component is preferably 70 mol% or more, more preferably 70 to 100 mol%, still more preferably 90 to 100 mol%. It is.

  Examples of the polyhydric alcohol component other than the aliphatic diol having 2 to 12 carbon atoms that can be used as the alcohol component include, for example, a polyoxypropylene adduct of 2,2-bis (4-hydroxyphenyl) propane, 2,2- Aromatic diols such as alkylene oxide adducts of bisphenol A represented by the following formula (I) including polyoxyethylene adducts of bis (4-hydroxyphenyl) propane; 3 such as glycerin, pentaerythritol, trimethylolpropane, etc. Alcohols having a value higher than that are listed.

（式中、Ｒは、炭素数２又は３のアルキレン基を示す。ｘ及びｙは、正の数を示し、ｘとｙの和は、１〜１６、好ましくは１．５〜５である。）

(In formula, R shows a C2-C3 alkylene group. X and y show a positive number, and the sum of x and y is 1-16, Preferably it is 1.5-5. )

<Carboxylic acid component>
As the carboxylic acid component which is a raw material monomer of the crystalline polyester, an aliphatic dicarboxylic acid compound having at least 8 to 12 carbon atoms is used from the viewpoint of low-temperature fixability of toner and storage stability of printed matter.
In the present invention, carboxylic acids, acid anhydrides thereof, derivatives thereof such as alkyl (carbon number 1 to 3) esters, and the like are collectively referred to as carboxylic acid compounds. The alkyl group of the alkyl ester is not included in the carbon number.
Examples of the aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms include suberic acid, azelaic acid, sebacic acid, 1,10-decanedicarboxylic acid and the like. Among these, an aliphatic dicarboxylic acid compound having 10 to 12 carbon atoms is preferable, and sebacic acid is more preferable from the viewpoint of low-temperature fixability, pressure storage stability, and environmental stability of the toner.
Content of a C8-C12 aliphatic dicarboxylic acid compound is 70-100 mol% in a carboxylic acid component, Preferably it is 80-100 mol%, More preferably, it is 90-100 mol%, More preferably, it is substantially 100 mol%. When the content is less than 70 mol% in the carboxylic acid component, the low-temperature fixability of the toner is lowered.

In the present invention, a carboxylic acid component other than the aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms can be used in combination. Examples include aromatic dicarboxylic acid compounds, aliphatic dicarboxylic acid compounds having 2 to 7 carbon atoms, and trivalent or higher aromatic polyvalent carboxylic acid compounds, but are not particularly limited thereto.
Specific examples of the aromatic dicarboxylic acid compound preferably include aromatic dicarboxylic acids such as phthalic acid, isophthalic acid and terephthalic acid, anhydrides of these acids, and alkyl (C1 to C3) esters thereof. Examples of the alkyl group in the alkyl ester include a methyl group, an ethyl group, a propyl group, and an isopropyl group. The content of the aromatic dicarboxylic acid compound is preferably 0 to 30 mol%, more preferably 0 to 20 mol%, still more preferably 0 to 10 mol% in the carboxylic acid component, from the viewpoint of the chargeability of the toner. .

Examples of the aliphatic dicarboxylic acid compound having 2 to 7 carbon atoms include oxalic acid, malonic acid, maleic acid, fumaric acid, citraconic acid, itaconic acid, glutaconic acid, succinic acid, adipic acid, etc .; dodecyl succinic acid, dodecenyl succinic acid, octenyl succinic acid Examples thereof include succinic acid derivatives such as acids; anhydrides of these acids and alkyl (C1 to C3) esters of those acids. The content of the aliphatic dicarboxylic acid compound having 2 to 7 carbon atoms is preferably 0 to 30 mol%, more preferably 0 to 20 mol%, still more preferably in the carboxylic acid component from the viewpoint of low-temperature fixability of the toner. 0 to 10 mol%.
Examples of the trivalent or higher polyvalent carboxylic acid compounds include 1,2,4-benzenetricarboxylic acid (trimellitic acid), 2,5,7-naphthalenetricarboxylic acid, and aromatic carboxylic acids such as pyromellitic acid, and these Derivatives such as acid anhydrides and alkyl (1 to 3 carbon atoms) esters may be mentioned. The content of the trivalent or higher polyvalent carboxylic acid compound is preferably 0 to 30 mol%, more preferably 0 to 20 mol%, still more preferably 0 to 10 in the carboxylic acid component from the viewpoint of the durability of the toner. Mol%.

<Molar ratio of alcohol component to carboxylic acid component>
The molar ratio of the alcohol component and the carboxylic acid component (carboxylic acid component / alcohol component), which is a raw material monomer for the condensation polymerization reaction, is preferably 1. in order to improve the low-temperature fixability, the pressure storage stability and the environmental stability. It is 03-1.20, More preferably, it is 1.03-1.15, More preferably, it is 1.04-1.12, More preferably, it is 1.05-1.10.

<Composite resin>
The crystalline polyester used in the present invention comprises polycondensation using (i) a raw material monomer of a styrene resin, and (ii) an amphoteric monomer capable of reacting with either the raw material monomer of the styrene resin and the alcohol component. Crystalline polyester can also be made into a composite resin by subjecting it to an addition polymerization reaction in addition to the reaction.
As a raw material monomer for the styrene-based resin component, styrene or styrene derivatives such as α-methylstyrene and vinyltoluene (hereinafter, styrene and styrene derivatives are collectively referred to as “styrene derivatives”) is used.

As the bi-reactive monomer capable of reacting with any of the styrene resin raw material monomer and the alcohol component, the molecule includes a hydroxyl group, a carboxyl group, an epoxy group, a primary amino group, and a secondary amino group. Examples thereof include compounds having at least one selected functional group. Among these, a compound having a hydroxyl group and / or a carboxyl group is preferable, and a compound having a carboxyl group and an ethylenically unsaturated bond is more preferable. By using such a bireactive monomer, the dispersibility of the resin that becomes the dispersed phase can be further improved.
As the both reactive monomers, at least one selected from the group consisting of acrylic acid, methacrylic acid, fumaric acid, maleic acid and maleic anhydride is preferable. From the viewpoint of the reactivity of condensation polymerization reaction and addition polymerization reaction, acrylic acid is preferable. More preferred is methacrylic acid or fumaric acid.

<Physical properties of crystalline polyester>
The physical properties of the crystalline polyester used in the present invention are as follows.
The softening point of the crystalline polyester is preferably 60 to 160 ° C., more preferably 60 to 120 ° C., still more preferably 65 to 100 ° C., and more preferably 65 to 90 ° C. from the viewpoint of toner transfer efficiency and print storage stability. Further preferred.
The melting point of the crystalline polyester is preferably 60 to 130 ° C., more preferably 65 to 110 ° C., and still more preferably 65 to 90 ° C. from the viewpoints of toner transfer efficiency and print storage stability.

The number average molecular weight of the crystalline polyester is usually preferably 1,000 or more, and more preferably 1,500 or more, from the viewpoint of toner transfer efficiency and print storage stability. However, considering the productivity of the crystalline polyester, the number average molecular weight is preferably 6,000 or less, more preferably 5,000 or less, and further preferably 4,500 or less. From the above viewpoint, the number average molecular weight of the crystalline polyester is preferably 1,000 to 6,000, more preferably 1,000 to 5,000, and still more preferably 1,500 to 4,500.
Further, the weight average molecular weight is preferably 3,000 or more, more preferably 5,000 or more, still more preferably 8,000 or more, preferably 100,000 or less, more preferably from the same viewpoint as the number average molecular weight. Is 50,000 or less, more preferably 30,000 or less, and still more preferably 20,000 or less. From the above viewpoint, the weight average molecular weight of the crystalline polyester is preferably 3,000 to 100,000, more preferably 5,000 to 50,000, still more preferably 5,000 to 30,000, and 8,000 to 20 1,000 is even more preferred.
In the present invention, the number average molecular weight and the weight average molecular weight of the crystalline polyester are both values obtained by measuring the chloroform-soluble content.
When crystalline polyester is used as the composite resin, the number average molecular weight of the styrene resin component in the crystalline polyester is 400 to 7,000 from the viewpoint of dispersibility in the crystalline resin that is the composite resin. Preferably, 1,000 to 4,000 is more preferable, and 1,500 to 3,000 is still more preferable. In the present invention, the number average molecular weight of the styrene resin refers to a value obtained by measuring a tetrahydrofuran (THF) soluble content.

The acid value of the crystalline polyester is preferably 10 to 40 mgKOH / g, more preferably 15 to 35 mgKOH / g, and still more preferably 20 to 30 mgKOH / g, from the viewpoints of toner transfer efficiency and print storage stability.
The hydroxyl value of the crystalline polyester is preferably 1 to 20 mgKOH / g, more preferably 5 to 15 mgKOH / g, and still more preferably 7 to 13 mgKOH / g, from the viewpoint of toner transfer efficiency and print storage stability.
The softening point, melting point, number average molecular weight, weight average molecular weight, acid value and hydroxyl value can be easily adjusted by adjusting the raw material monomer composition, polymerization initiator, molecular weight, catalyst amount, etc., or by selecting reaction conditions. .

(Method for producing crystalline polyester)
The crystalline polyester is obtained by a polycondensation reaction between an alcohol component and a carboxylic acid component, and the polycondensation reaction is preferably performed in the presence of an esterification catalyst. From the viewpoint of obtaining a polyester having high durability of the toner, More preferably, it is carried out in the presence of a cocatalyst and a pyrogallol compound. The same applies to the production of an amorphous resin described later.

<Esterification catalyst>
Examples of the esterification catalyst suitably used for the condensation polymerization include a titanium compound and a tin (II) compound having no Sn—C bond, and these may be used alone or in combination of two or more. it can.

As a titanium compound, the titanium compound which has a Ti-O bond is preferable, and the compound which has a C1-28 total carbon number alkoxy group, an alkenyloxy group, or an acyloxy group is more preferable.
Specific examples of titanium compounds include titanium diisopropylate bistriethanolamate [Ti (C ₆ H ₁₄ O ₃ N) ₂ (C ₃ H ₇ O) ₂ ], titanium diisopropylate bisdiethanolamate [Ti (C ₄ H ₁₀ O ₂ N) ₂ (C ₃ H ₇ O) ₂ ], titanium dipentylate bistriethanolamate [Ti (C ₆ H ₁₄ O ₃ N) ₂ (C ₅ H ₁₁ O) ₂ ], titanium diety rate bis triethanolaminate _{[Ti (C 6 H 14 O 3} N) 2 (C 2 H 5 O) 2 ], titanium dihydroxy octylate bis triethanolaminate _{[Ti (C 6 H 14 O 3} N) 2 (OHC 8 H ₁₆ O) ₂ ], titanium distearate bistriethanolamate [Ti (C ₆ H ₁₄ O ₃ N) ₂ (C ₁₈ H ₃₇ O) ₂ ], titanium triisopropylate triethanolamate [Ti (C _{6 H 14 O 3 N) 1 (} C 3 ₇ O) _3], and titanium monopropylate tris (triethanolaminate) _{[Ti (C 6 H 14 O 3} N) 3 (C 3 H 7 O) 1 ], and the like. Of these, titanium diisopropylate bistriethanolaminate, titanium diisopropylate bisdiethanolamate, and titanium dipentylate bistriethanolamate are preferred, and these are also available as commercial products of Matsumoto Trading Co., Ltd. It is.

Specific examples of other preferable titanium compounds include tetra-n-butyl titanate [Ti (C ₄ H ₉ O) ₄ ], tetrapropyl titanate [Ti (C ₃ H ₇ O) ₄ ], tetrastearyl titanate [Ti ( C ₁₈ H ₃₇ O) ₄ ], tetramyristyl titanate [Ti (C ₁₄ H ₂₉ O) ₄ ], tetraoctyl titanate [Ti (C ₈ H ₁₇ O) ₄ ], dioctyl dihydroxyoctyl titanate [Ti (C ₈ H ₁₇ O) ₂ (OHC ₈ H ₁₆ O) ₂ ], dimyristyl dioctyl titanate [Ti (C ₁₄ H ₂₉ O) ₂ (C ₈ H ₁₇ O) ₂ ] and the like. Among these, tetrastearyl titanate, tetramyristyl titanate, tetraoctyl titanate, and dioctyl dihydroxy octyl titanate are preferable. These can be obtained by reacting, for example, titanium halide with a corresponding alcohol. It is also available as a commercial product such as

Examples of the tin (II) compound having no Sn—C bond include a tin (II) compound having a Sn—O bond, a tin (II) compound having a Sn—X (X represents a halogen atom) bond, and the like. Preferred examples include tin (II) compounds having a Sn-O bond.
Examples of tin (II) compounds having a Sn-O bond include tin (II) oxalate, tin (II) diacetate, tin (II) dioctanoate, tin (II) dilaurate, tin (II) distearate, and Tin (II) carboxylate having a carboxylic acid group having 2 to 28 carbon atoms such as tin (II) dioleate; dioctyloxytin (II), dilauroxytin (II), distearoxytin (II), and dioleoxytin (II) Dialkoxytin (II) having an alkoxy group having 2 to 28 carbon atoms, such as tin oxide (II) and tin sulfate (II).
Examples of the compound having a Sn-X (X represents a halogen atom) bond include tin (II) halides such as tin (II) chloride and tin (II) bromide. Among these, fatty acid tin (II) represented by (R ¹ COO) ₂ Sn (wherein R ¹ represents an alkyl group or alkenyl group having 5 to 19 carbon atoms) from the viewpoint of the charge rising effect and catalytic ability. ), (R ² O) ₂ Sn (wherein R ² represents an alkyl group or alkenyl group having 6 to 20 carbon atoms), and tin oxide (II) represented by SnO Fatty acid tin (II) and tin (II) oxide represented by (R ¹ COO) ₂ Sn are more preferred, tin (II) dioctanoate, tin (II) distearate, and tin (II) oxide Is more preferably used.

  The amount of the esterification catalyst present is preferably 0.01 to 1 part by weight, more preferably 0.1 to 0.6 part by weight, based on 100 parts by weight of the total amount of the alcohol component and the carboxylic acid component.

<Pyrogallol compound>
A pyrogallol compound has a benzene ring in which three hydrogen atoms adjacent to each other are substituted with a hydroxyl group, and pyrogallol, gallic acid, gallic acid ester, 2,3,4-trihydroxybenzophenone, 2,2 ′, Examples include benzophenone derivatives such as 3,4-tetrahydroxybenzophenone, and catechin derivatives such as epigallocatechin and epigallocatechin gallate.
The abundance of the pyrogallol compound in the condensation polymerization reaction is preferably 0.001 to 1 part by weight, and preferably 0.005 to 0.005 parts per 100 parts by weight of the total amount of the alcohol component and carboxylic acid component subjected to the condensation polymerization reaction. 4 parts by weight is more preferable, and 0.01 to 0.2 parts by weight is still more preferable. Here, the abundance of the pyrogallol compound means the total amount of the pyrogallol compound subjected to the condensation polymerization reaction.
The weight ratio of the pyrogallol compound to the esterification catalyst (pyrogallol compound / esterification catalyst) is preferably 0.01 to 0.5, more preferably 0.03 to 0.3, from the viewpoint of toner durability. 0.05 to 0.2 is more preferable.

The polycondensation of the alcohol component and the carboxylic acid component can be performed, for example, at a temperature of 120 to 250 ° C. in an inert gas atmosphere in the presence of the esterification catalyst.
In addition, for example, all monomers are charged together to increase the strength of the resin, or divalent monomers are first reacted to reduce low molecular weight components, and then trivalent or higher monomers are added and reacted. A method may be used. Further, the reaction may be accelerated by reducing the pressure of the reaction system in the latter half of the polymerization.

(Method for producing aqueous dispersion of crystalline polyester for toner)
The method of the present invention comprises one or more urea compounds selected from urea and alkyl urea and / or one or more guanidine compounds selected from guanidine, alkyl guanidine and acid addition salts thereof, and the presence of a neutralizing agent. A crystalline polyester obtained by polycondensing an alcohol component containing an aliphatic diol having 2 to 12 carbon atoms and a carboxylic acid component containing 70 to 100 mol% of an aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms. In a water-based medium.
The crystalline polyester used in the above step is preferably one that has been stored for a certain period after production by a condensation polymerization reaction in order to exhibit the effects of the present invention. The storage period is preferably 2 weeks or more, more preferably 1 month or more, and although there is no particular deadline, for example, about 3 years can be mentioned. The temperature during storage is preferably 0 to 40 ° C, more preferably 5 to 35 ° C. Since a structure involving hydrogen bonds is gradually formed during storage, when toner is manufactured using the crystalline polyester after storage as a resin dispersion, the transferability of the toner and the storage stability of the printed matter are significantly reduced. It is considered to be.

  Here, the aqueous medium is a medium containing water, and may contain a solvent such as an organic solvent. In the medium, water is preferably 70% by weight or more, preferably 80% by weight or more, and more preferably. Contains 90% by weight or more, more preferably 99% by weight or more. In addition, when using a solvent, the solubility of resin is considered and the organic solvent which melt | dissolves in the water mentioned later is preferable. The “aqueous dispersion of crystalline polyester” refers to a liquid in which crystalline polyester is dispersed in an aqueous medium. The same applies to an aqueous dispersion of an amorphous resin described later.

Examples of the neutralizing agent include alkali metal hydroxides such as lithium hydroxide, sodium hydroxide, and potassium hydroxide; organic bases such as ammonia, trimethylamine, ethylamine, diethylamine, triethylamine, triethanolamine, and tributylamine. .
The degree of neutralization of the crystalline polyester is preferably 40 to 120 mol%, and preferably 40 to 100 mol% from the viewpoint of making the dispersed particle size uniform and small, and improving the transfer efficiency of the toner and the storage stability of the printed matter. Is preferable, and 50-80 mol% is still more preferable.

  As the urea compound used in the present invention, one or more urea compounds selected from the group consisting of urea and alkyl urea are used. Urea is preferable from the viewpoint of making the dispersed particle size uniform and improving the transfer efficiency of the toner and the storage stability of the printed matter. Specific examples of the alkyl urea include N-alkyl substituted ureas such as methyl urea, dimethyl urea, trimethyl urea, tetramethyl urea, ethyl urea, diethyl urea and the like. As an alkyl group, C1-C6 is preferable, C1-C3 is more preferable, and the alkyl group which has a hydroxyl group may be sufficient. The number of substituents of the alkyl group in the urea compound is preferably 1 or 2.

As the guanidine compound used in the present invention, one or more guanidine compounds selected from the group consisting of guanidine, alkylguanidine and acid addition salts thereof are used, and acid addition salts are preferable. In addition, guanidine is preferable from the viewpoints of uniforming the dispersed particle diameter and improving the transfer efficiency of the toner and the storage stability of the printed matter.
Specific examples of the alkylguanidine include N such as methylguanidine, ethylguanidine, n-propylguanidine, isopropylguanidine, n-butylguanidine, 2-methylpropylguanidine, t-butylguanidine, n-pentylguanidine, n-hexylguanidine and the like. -Alkyl substituted guanidines. As an alkyl group, C1-C6 is preferable, C1-C3 is more preferable, and the alkyl group which has a hydroxyl group may be sufficient. The number of substituents of the alkyl group in the guanidine compound is preferably 1 or 2. Examples of the acid addition salt include inorganic acid salts such as hydrochloride, nitrate, and carbonate, and organic acid salts such as succinate, acetate, glutamate, lactate, citrate, and oxalate.

The amount of the urea compound used in the method of the present invention is such that the dispersed particle size is made uniform and small, and from the viewpoint of improving the transfer efficiency of the toner and the storage stability of the printed matter, Preferably 0.3 to 15 parts by weight, preferably 0.5 to 15 parts by weight, more preferably 0.5 to 10 parts by weight, still more preferably 1 to 8 parts by weight, still more preferably 2 to 8 parts by weight. is there.
The total amount of the guanidine compound used in the method of the present invention is based on 100 parts by weight of the crystalline polyester from the viewpoint of making the dispersed particle size uniform and small, and improving the transfer efficiency of the toner and the storage stability of the printed matter. And preferably 0.3 to 15 parts by weight, preferably 0.5 to 15 parts by weight, more preferably 0.5 to 10 parts by weight, still more preferably 1 to 8 parts by weight, still more preferably 2 to 8 parts by weight. Part.
The total use amount of the urea compound and the guanidine compound in the method of the present invention is such that the dispersed polyester particle diameter is made uniform and small, and from the viewpoint of improving the toner transfer efficiency and the storability of the printed matter, the crystalline polyester 100 Preferably 0.3 to 15 parts by weight, preferably 0.5 to 15 parts by weight, more preferably 0.5 to 10 parts by weight, still more preferably 1 to 8 parts by weight, and still more preferably, relative to parts by weight. 2 to 8 parts by weight.

In the method of the present invention, the molar ratio between the total number of moles of the urea compound and the guanidine compound and the total number of unneutralized carboxy groups and hydroxyl groups of the crystalline polyester (the total mole of the urea compound and the guanidine compound) The number / the total number of moles of unneutralized carboxy groups and hydroxyl groups of the crystalline polyester) is preferably from the viewpoint of making the dispersed particle diameter uniform and small, and improving the transfer efficiency of the toner and the storage stability of the printed matter. It is 0.1-10, More preferably, it is 0.3-5, More preferably, it is 0.5-3.
The total number of moles of unneutralized carboxy groups and hydroxyl groups of the crystalline polyester can be determined from the following formula.
Total number of moles of unneutralized carboxy group and hydroxyl group of crystalline polyester = [acid value of crystalline polyester (KOHmg / g) × [(100−neutralization degree) / 100] + hydroxyl value of crystalline polyester (KOHmg / g)] / 56000 × [weight of resin (g)]
(However, when the degree of neutralization exceeds 100, the number of moles of unneutralized carboxy groups in the polyester is 0. The degree of neutralization can be determined by the calculation formula described below.)

As the method of the present invention, the following methods (A) and (B) are preferably used.
<Method (A)>
Method (A) is a method for producing an aqueous dispersion of crystalline polyester for toner, comprising the following steps A1 and A2.
Step A1: Crystallinity obtained by polycondensing an alcohol component containing an aliphatic diol having 2 to 12 carbon atoms and a carboxylic acid component containing 70 to 100 mol% of an aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms A step of mixing a polyester, a urea compound and / or a guanidine compound, a neutralizing agent, an organic solvent and water, and further, if necessary, a surfactant to obtain a dispersion of crystalline polyester.
Step A2: A step of obtaining an aqueous dispersion of the crystalline polyester by removing the organic solvent from the dispersion obtained in Step A1.

In step A1, the order of addition of the urea compound and / or the guanidine compound is not limited, and after mixing the crystalline polyester, the urea compound and / or the guanidine compound and the organic solvent, water, a neutralizing agent, and further necessary If necessary, a surfactant may be mixed to obtain a dispersion of crystalline polyester. Crystalline polyester, neutralizing agent, organic solvent, water, and if necessary, a surfactant may be mixed to obtain a crystalline polyester. After obtaining the dispersion liquid, a urea compound and / or a guanidine compound may be added to the dispersion liquid.
More preferably, from the viewpoint of toner transfer efficiency and print storage stability, after dissolving the crystalline polyester in an organic solvent, a urea compound and / or a guanidine compound is added to the resulting solution to further neutralize it. It is preferable to add an agent and water to obtain a dispersion.
It is considered that the mobility of the crystalline polyester is increased by the organic solvent, and the effect of the urea compound and / or the guanidine compound can be enhanced.
In the step A1, it is preferable to obtain a dispersion at 30 to 90 ° C., more preferably 40 to 80 ° C. from the viewpoint of dispersibility of the crystalline polyester.
In step A2, a method of obtaining an aqueous dispersion of crystalline polyester by removing the organic solvent from the dispersion by distillation or the like is more preferable.

As an organic solvent, from the viewpoint of improving the dispersibility of the crystalline polyester, the transfer efficiency of the toner with the urea-based and guanidine-based compounds, and the storage stability of the printed material, the solubility parameter (SP value: POLYMER HANDBOOK THIRD EDITION 1989 by John Wiley & Sons). , when expressed in Inc), preferably it has a 15.0～26.0MPa ^1/2, more preferably those which are 16.0~24.0MPa ^1/2, 17.0~22.0MPa ^{1 /} More preferred is ² .
Specific examples include alcohol solvents such as ethanol (26.0), isopropanol (23.5), and isobutanol (21.5); acetone (20.3), methyl ethyl ketone (19.0), methyl isobutyl ketone. Ketone solvents such as (17.2) and diethyl ketone (18.0); ether solvents such as dibutyl ether, tetrahydrofuran (18.6), and dioxane (20.5); ethyl acetate (18.6) Is mentioned. The value in parentheses indicates the SP value. Among these, methyl ethyl ketone and ethyl acetate are preferable from the viewpoint of dispersibility of the crystalline polyester.
Examples of the surfactant include anionic surfactants such as sulfate ester, sulfonate, phosphate ester, and soap (such as alkyl ether carboxylate); amine salt type, quaternary ammonium salt Examples include cationic surfactants such as molds; nonionic surfactants described later.
In mixing, it is preferable to stir with a commonly used mixing stirrer such as an anchor blade. Moreover, the method of removing the organic solvent in the step A2 is not limited to distillation, and can be performed by any method.

In the said method (A), the total usage-amount and mole number of a urea type compound and a guanidine type compound are as above-mentioned.
In the method (A), the neutralizing agent and the degree of neutralization are as described above.
The amount of the organic solvent used is preferably from 100 to 1,000, based on 100 parts by weight of the crystalline polyester, from the viewpoint of enhancing the dispersibility of the crystalline polyester, the transfer efficiency of the toner with the urea-based and guanidine-based compounds, and the storage stability of the printed matter. Parts by weight, more preferably 150 to 600 parts by weight, still more preferably 200 to 400 parts by weight.
The amount of water used when mixing with the crystalline polyester is preferably 100 to 1000 parts by weight, more preferably 120 to 500 parts by weight, with respect to 100 parts by weight of the organic solvent, from the viewpoint of dispersibility of the crystalline polyester. More preferably, it is 130 to 300 parts by weight.
When using a surfactant, the amount used is preferably 0.1 to 20 parts by weight, more preferably 0.5 to 100 parts by weight with respect to 100 parts by weight of the crystalline polyester, from the viewpoint of dispersibility of the crystalline polyester. 10 parts by weight.

<Method (B)>
Method (B) is a method for producing an aqueous dispersion of crystalline polyester for toner, comprising the following steps B1 and B2.
Step B1: Crystallinity obtained by polycondensing an alcohol component containing an aliphatic diol having 2 to 12 carbon atoms and a carboxylic acid component containing 70 to 100 mol% of an aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms A step of mixing with a polyester, a urea compound and / or a guanidine compound, a nonionic surfactant, a neutralizing agent, and, if necessary, a surfactant.
Step B2: A step of obtaining an aqueous dispersion of the crystalline polyester by adding water to the mixed solution obtained in Step B1.

In step B1, the order of addition of the urea compound and / or guanidine compound is not limited, and the crystalline polyester, urea compound and / or guanidine compound, nonionic surfactant and neutralizing agent, and further if necessary It may be mixed with other surfactants and stirred, crystalline polyester, nonionic surfactants and neutralizers, and further mixed with other surfactants if necessary, urea compounds and It may be mixed with a guanidine compound and / or stirred.
More preferably, after mixing a crystalline polyester, a urea compound and / or a guanidine compound and a nonionic surfactant, a neutralizing agent and, if necessary, another surfactant are mixed. .
It is considered that the mobility of the crystalline polyester is increased by the nonionic surfactant, and the effect of the urea compound and / or the guanidine compound can be enhanced.
The neutralizing agent and the degree of neutralization are as described above. The temperature of step B1 is preferably 30 to 200 ° C, more preferably 40 to 150 ° C, from the viewpoint of mixing the crystalline polyester with the nonionic surfactant.
In Steps B1 and B2, substantially no organic solvent is used.

When the polyester is mixed with the nonionic surfactant, the nonionic surfactant is compatible with the polyester, the viscosity of the resulting mixture is lowered, and the softening point of the polyester is apparently lowered. In the method (B), using this phenomenon, the apparent softening point of the polyester compatible with the nonionic surfactant can be lowered below the boiling point of water. Even with a polyester having a softening point, a dispersion in which the polyester is dispersed in water can be obtained by adding water in step B2.
In addition, since the method (B) only needs to have at least water and a nonionic surfactant, it can be applied to a resin insoluble in an organic solvent, and there is no need for an equipment burden for recovering the organic solvent and maintaining the working environment. In addition, since a special device required when using mechanical means is unnecessary, there is an advantage that the resin particle dispersion can be produced economically.

  Examples of the nonionic surfactant include polyoxyethylene alkylaryl ethers such as polyoxyethylene nonylphenyl ether; polyoxyethylene alkyl ethers such as polyoxyethylene oleyl ether and polyoxyethylene lauryl ether; polyoxy Polyoxyethylene sorbitan esters such as ethylene sorbitan monolaurate and polyoxyethylene sorbitan monostearate; polyoxyethylene fatty acids such as polyethylene glycol monolaurate, polyethylene glycol monostearate, and polyethylene glycol monooleate Examples of esters include oxyethylene / oxypropylene block copolymers. In addition, an anionic surfactant or a cationic surfactant may be used in combination with the nonionic surfactant.

As the nonionic surfactant, it is preferable to select a nonionic surfactant having good compatibility with the crystalline polyester. In order to obtain a stable polyester dispersion, the HLB of the nonionic surfactant is preferably 12-18 (Davies method). Depending on the type of crystalline polyester, two or more different HLB nonions It is more preferable to use a functional surfactant. For example, in the case of a highly hydrophilic resin, at least one nonionic surfactant having an HLB of 12 to 18 may be used. In the case of a highly hydrophobic resin, a low HLB, for example, 7 to 10 is used. It is preferable to adjust the weighted average of both HLBs to 12 to 18 by using those having the same level and those having a high HLB, for example, 14 to 20 in combination. In this case, it is presumed that those having an HLB of about 7 to 10 can compatibilize the crystalline polyester, and those having a high HLB can stabilize the dispersion of the resin in water.
The clouding point of the nonionic surfactant is preferably 70 to 105 ° C, more preferably 80 to 105 ° C when the polyester is atomized under normal pressure and water.

In the method (B), the total amount used and the number of moles used of the urea compound and the guanidine compound are as described above.
The amount of the nonionic surfactant used is from the viewpoint of lowering the melting point of the crystalline polyester with respect to 100 parts by weight of the crystalline polyester, and from the viewpoint of increasing the transfer efficiency of the toner by the urea-based and guanidine-based compounds and the storage stability of the printed matter. Is preferably 5 parts by weight or more, and preferably 80 parts by weight or less from the viewpoint of controlling the nonionic surfactant remaining in the toner. Therefore, from the viewpoint of making these compatible, the amount of the nonionic surfactant used is preferably 5 to 80 parts by weight, more preferably 10 to 70 parts by weight, more preferably 20 to 60 parts by weight based on 100 parts by weight of the crystalline polyester. Part by weight is more preferred. In addition, in process B1, unless the present invention is impaired, a part of water may be contained. The mixed solution obtained in step B1 is preferably a solution or a dispersion.
In step B2, an aqueous dispersion is obtained by adding water to the mixed solution obtained in step 1.
The amount of water added is preferably 100 to 5000 parts by weight, more preferably 200 to 3000 parts by weight, and still more preferably 300 to 2000 parts by weight with respect to 100 parts by weight of the crystalline polyester.

(Aqueous dispersion of crystalline polyester for toner)
The solid content concentration of the aqueous dispersion of crystalline polyester is preferably adjusted to 3 to 50% by weight, more preferably 5 to 30% by weight, and still more preferably 7 to 15% by weight by adding water as appropriate.
From the viewpoint of improving the transfer efficiency of the toner and the storage stability of the printed matter, the average particle size of the obtained dispersed particles of the crystalline polyester is preferably 0.05 to 0.8 μm in terms of volume median particle size, and preferably 0.05 to 0. 0.5 μm is more preferable, and 0.05 to 0.25 μm is still more preferable.
The CV value (%) of the dispersed particles of the crystalline polyester is preferably 30 or less, more preferably 25 or less, and from the viewpoint of production efficiency, from the viewpoint of improving the transfer efficiency of the toner due to the uniformity of the particles and the storage stability of the printed matter. 5 or more are preferable, 15 or more are more preferable, and from these viewpoints, 5 to 30 are preferable, 15 to 30 are more preferable, and 15 to 25 are even more preferable.
The crystalline polyester particles dispersed in the aqueous dispersion obtained by the production method of the present invention are characterized by a small volume median particle size and a small variation coefficient (CV value) of particle size distribution. Therefore, the electrophotographic toner of the present invention obtained using the aqueous dispersion of the crystalline polyester is excellent in toner transfer efficiency and printed matter storability.

(Amorphous resin)
The amorphous resin used in the electrophotographic toner of the present invention is preferably a condensation polymerization resin obtained by condensation polymerization of an alcohol component and a carboxylic acid component. In the present invention, the amorphous resin includes an alcohol component containing 70 mol% or more of an alkylene oxide adduct of bisphenol A represented by the above formula (I) and / or an aliphatic diol having 2 to 12 carbon atoms and a carboxyl group. A polyester resin obtained by polycondensation with an acid component is preferred.

<Alcohol component>
The alkylene oxide adduct of bisphenol A or an aliphatic diol having 2 to 12 carbon atoms can be used. Examples of the aliphatic diol having 2 to 12 carbon atoms include those described in the above-mentioned crystalline polyester, an aliphatic diol having 2 to 5 carbon atoms is preferable, and 1,2-propanediol is more preferable.
Among these, an alkylene oxide adduct of bisphenol A is preferable because the storability of the printed matter is improved.
The total content of the alkylene oxide adduct of bisphenol A is preferably 70 mol% or more, more preferably 80 to 100 mol%, still more preferably 90 to 100 mol% in the alcohol component.
Examples of the alcohol other than the alkylene oxide adduct of bisphenol A or the aliphatic diol having 2 to 12 carbon atoms that can be contained in the alcohol component include trivalent or higher alcohols similar to those used for the crystalline polyester. it can.

<Carboxylic acid component>
The carboxylic acid component of the amorphous resin preferably contains an aromatic dicarboxylic acid compound, more preferably a terephthalic acid compound, from the viewpoint of enhancing the storage stability of the printed material. Note that an amorphous resin obtained using a terephthalic acid compound as a carboxylic acid component and an amorphous resin obtained without using a terephthalic acid compound may be prepared and used in combination. In addition, as an aromatic dicarboxylic acid compound, what was described in the above-mentioned crystalline polyester is mentioned.
When the aromatic dicarboxylic acid compound is contained, the content thereof is preferably 30 to 95 mol%, more preferably 40 to 90 mol%, still more preferably 50 in the carboxylic acid component, from the viewpoint of enhancing the storage stability of the printed matter. -85 mol%.

Examples of the divalent carboxylic acid that can be used other than the aromatic dicarboxylic acid compound include oxalic acid, malonic acid, maleic acid, fumaric acid, citraconic acid, itaconic acid, glutaconic acid, succinic acid, adipic acid, etc. An aliphatic dicarboxylic acid having 10 (preferably 4 to 10 carbon atoms, more preferably 4 to 8 carbon atoms); an alkyl group having 8 to 20 carbon atoms such as dodecyl succinic acid, dodecenyl succinic acid, octenyl succinic acid, or 8 to 20 carbon atoms And succinic acid substituted with an alkenyl group of the above; anhydrides of these acids and alkyl (carbon number 1 to 3) esters of these acids.
When the aliphatic dicarboxylic acid having 2 to 10 carbon atoms is contained, the content thereof is preferably 5 to 60 mol%, more preferably 5 to 40 mol%, still more preferably 5 to 30 mol in the carboxylic acid component. %. When the succinic acid substituted with the alkyl group having 8 to 20 carbon atoms or the alkenyl group having 8 to 20 carbon atoms is contained, the content thereof is preferably 3 to 30 mol%, more preferably in the carboxylic acid component. It is 5-20 mol%, More preferably, it is 5-15 mol%.
Examples of trivalent or higher polyvalent carboxylic acid compounds other than aromatic dicarboxylic acid compounds that can be used include the same compounds as those used for the crystalline polyester.
When the trivalent or higher polyvalent carboxylic acid compound is contained, the content thereof is preferably 3 to 40 mol%, more preferably 5 to 35 mol%, still more preferably 5 to 30 mol% in the carboxylic acid component. is there.

<Physical properties of amorphous resin>
The softening point of the amorphous resin is preferably 70 to 180 ° C., more preferably 90 to 150 ° C., from the viewpoint of low-temperature fixability of the toner and storage stability of the printed matter. The amorphous resin used in the present invention is a combination of a resin having a high softening point (hereinafter referred to as a high softening point resin) and a resin having a low softening point (hereinafter referred to as a low softening point resin). In addition, the toner is more excellent in terms of low-temperature fixability, pressure storage stability, and environmental stability. When the high softening point resin and the low softening point resin are used in combination, one or both of them may be used.
Specifically, the softening point of the high softening point resin is preferably 110 to 150 ° C, and the softening point of the low softening point resin is preferably 90 ° C or higher and lower than 110 ° C. The softening point of the high softening point resin used in combination and the softening point of the low softening point resin are preferably different by 10 ° C. or more, more preferably 15 to 40 ° C.
When the high softening point resin and the low softening point resin are used in combination, the weight ratio of the high softening point resin to the low softening point resin (high softening point resin / low softening point resin) is preferably 1/3 to 3/1. / 3 to 2/1 is more preferable, and 1/2 to 1/1 is still more preferable.

The acid value of the amorphous resin is preferably 1 to 40 mgKOH / g, more preferably 2 to 35 mgKOH / g, and more preferably 3 to 30 mgKOH / g from the viewpoint of improving the dispersion of the amorphous resin in the aqueous dispersion. g is more preferable.
The glass transition temperature (Tg) of the amorphous resin is preferably 45 to 80 ° C., more preferably 55 to 75 ° C., from the viewpoints of low-temperature fixability of the toner and storage stability of the printed matter.
The number average molecular weight of the amorphous resin is preferably 1,000 to 6,000, and more preferably 2,000 to 5,000. The weight average molecular weight is preferably 10,000 or more, more preferably 30,000 or more, and preferably 1,000,000 or less. The number average molecular weight and the weight average molecular weight of the amorphous resin are both values obtained by measuring the tetrahydrofuran soluble content.
The softening point, acid value, Tg, number average molecular weight and weight average molecular weight can be adjusted by adjusting the raw material monomer composition, polymerization initiator, molecular weight, catalyst amount, etc., or by selecting reaction conditions.

<Modified amorphous resin>
The amorphous resin used in the present invention includes a modified amorphous resin.
Examples of the modified amorphous resin include a urethane-modified polyester in which the resin is modified with a urethane bond, an epoxy-modified polyester in which the polyester is modified with an epoxy bond, and a hybrid resin having two or more resins including a polyester component. Can be mentioned.
As the amorphous resin, either one of the polyester resin and the modified amorphous resin may be used in combination. Specifically, the polyester and / or a hybrid having a polyester and a styrene resin may be used. Resin may be used.
The aqueous dispersion of the amorphous resin is preferably produced by the method for producing an aqueous dispersion of the crystalline polyester, except that the crystalline polyester is replaced with an amorphous resin, from the viewpoint of toner transfer efficiency.
The volume median particle size of the aqueous dispersion of the amorphous resin is preferably 0.05 to 0.8 μm, more preferably 0.05 to 0.5 μm, from the viewpoint of finely dispersing the crystalline polyester in the toner particles. 0.05 to 0.25 μm is more preferable.

[Method for producing toner for electrophotography]
The toner production method of the present invention comprises an aqueous dispersion of crystalline polyester obtained by the above method and an aqueous dispersion of amorphous resin (preferably an aqueous dispersion of crystalline polyester, an aqueous dispersion of amorphous resin, and And a step of obtaining agglomerated particles by subjecting the dispersion of the colorant to an aggregating step, and a step of obtaining the agglomerated particles by further subjecting the obtained agglomerated particles to a coalesced step.
The toner of the present invention is preferably obtained by a production method including the following step 1 and step 2.
Step 1: Crystallinity obtained by polycondensing an alcohol component containing an aliphatic diol having 2 to 12 carbon atoms and a carboxylic acid component containing 70 to 100 mol% of an aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms A step of subjecting an aqueous dispersion of polyester and an aqueous dispersion of an amorphous resin to an aggregation step to obtain an aqueous dispersion of aggregated particles.
Step 2: A step of subjecting the aggregated particles obtained in Step 1 to a coalescing step to obtain coalesced particles.
Hereinafter, step 1 and step 2 will be described in order.

<Step 1>
Step 1 is a step of obtaining an aqueous dispersion of aggregated particles by subjecting an aqueous dispersion of crystalline polyester and an aqueous dispersion of amorphous resin to an aggregation step.
The weight ratio [crystalline polyester / amorphous resin] of the crystalline polyester and the amorphous resin is preferably 5/95 to 40/60, preferably 6/94 to 60/60 from the viewpoint of toner transfer efficiency and print storage stability. 30/70 is more preferable, and 7/93 to 25/75 is still more preferable.
In the agglomeration process, additives such as colorants, charge control agents, release agents, conductivity modifiers, extender pigments, reinforcing fillers such as fibrous substances, antioxidants, and anti-aging agents are added before agglomeration. You may let them. The additive can also be used as an aqueous dispersion.

  There is no restriction | limiting in particular as a coloring agent, A well-known coloring agent is mentioned, According to the objective, it can select suitably. Specifically, carbon black, inorganic composite oxide, chrome yellow, hansa yellow, benzidine yellow, selenium yellow, quinoline yellow, permanent orange GTR, pyrazolone orange, vulcan orange, watch young red, permanent red, brilliantamine 3B, Brilliantamine 6B, Dupont Oil Red, Pyrazolone Red, Resol Red, Rhodamine B Lake, Lake Red C, Bengal, Aniline Blue, Ultramarine Blue, Calco Oil Blue, Methylene Blue Chloride, Phthalocyanine Blue, Phthalocyanine Green, Malachite Green Oxalate, etc. Various pigments: acridine, xanthene, azo, benzoquinone, azine, anthraquinone, indico, Indigo dyes, phthalocyanine, aniline black, polymethine, triphenylmethane dyes, diphenylmethane dyes, thiazine, and include various dyes of thiazole, and the like. These can be used alone or in combination of two or more. The addition amount of the colorant is preferably 0.1 to 20 parts by weight, and more preferably 1 to 10 parts by weight with respect to 100 parts by weight of the total amount of the crystalline polyester and the amorphous resin.

  Examples of charge control agents include chromium azo dyes, iron azo dyes, aluminum azo dyes, and salicylic acid metal complexes. Various charge control agents may be used alone or in combination of two or more. When the charge control agent is added, the addition amount is preferably 0.1 to 8 parts by weight, more preferably 0.3 to 7 parts by weight with respect to 100 parts by weight of the total amount of the crystalline polyester and the amorphous resin. .

Release agents include fatty acid amides such as oleic acid amide, erucic acid amide, ricinoleic acid amide, and stearic acid amide; plant waxes such as carnauba wax, rice wax, candelilla wax, wood wax, and jojoba oil; Animal waxes such as beeswax; waxes such as mineral and petroleum waxes such as montan wax, ozokerite, ceresin, microcrystalline wax, and Fischer-Tropsch wax; polyolefin waxes, paraffin waxes and silicones. You may use a mold release agent individually by 1 type or in combination of 2 or more types. The melting point of the release agent is preferably 60 to 140 ° C., more preferably 60 to 100 ° C., from the viewpoints of low-temperature fixability, carrier contamination resistance and charge rate.
When adding a mold release agent, the addition amount is 0.5 to 10 weight with respect to 100 weight part of total amounts of crystalline polyester and an amorphous resin from a viewpoint of the dispersibility in a resin particle (A). Part is preferred, 1 to 8 parts by weight is more preferred, and 1 to 7 parts by weight is still more preferred.
In the aggregation process, the solid content concentration in the system is preferably 5 to 50% by weight, more preferably 5 to 30% by weight, and still more preferably 5 to 20% by weight in order to cause uniform aggregation.

The pH in the system in the aggregation step is preferably 2 to 10, more preferably 2 to 9, and still more preferably 3 to 8, from the viewpoint of achieving both the dispersion stability of the mixed solution and the aggregation property of the resin particles.
From the same point of view, the temperature in the system in the aggregation process is equal to or higher than the “softening point of the mixed resin−60 ° C.” (meaning a temperature lower by 60 ° C. than the softening point of the mixed resin, the same shall apply hereinafter). The following is preferable. When using a master batch, the weighted average temperature including the resin used in the master batch is taken as the softening point of the mixed resin. In this specification, the “softening point of the mixed resin” refers to a temperature obtained by weighted averaging of the softening point of the crystalline polyester and the softening point of the amorphous resin.

In addition, additives such as a colorant and a charge control agent may be mixed in advance with crystalline polyester or amorphous resin when preparing resin particles, and each additive is separately dispersed in a dispersion medium such as water. A dispersion liquid prepared may be prepared and mixed with an aqueous dispersion liquid of crystalline polyester and an aqueous dispersion liquid of amorphous resin, and may be subjected to an aggregation step.
When the additive is preliminarily mixed with the crystalline polyester or amorphous resin when preparing the resin particles, it is preferable to melt-knead the crystalline polyester and the additive in advance.
For melt kneading, it is preferable to use an open roll type biaxial kneader. An open roll type biaxial kneader is a kneader in which two rolls are arranged close to each other in parallel, and a heating function or a cooling function can be imparted by passing a heat medium through each roll. Therefore, the open-roll type twin-screw kneader is an open-type part to be melt-kneaded, and is provided with a heating roll and a cooling roll, so that it occurs during melt-kneading unlike a normal twin-screw extruder. The kneading heat can be easily dissipated.
In the case of preparing a dispersion in which each additive is separately dispersed in a dispersion medium such as water, Step 1 includes an aqueous dispersion of crystalline polyester, an aqueous dispersion of an amorphous resin, and a dispersion of a colorant. It is preferable that it is a process which attaches | subjects to an aggregation process and obtains the aqueous dispersion of a resin particle (A).

In the aggregation process, an aggregating agent can be added in order to effectively perform aggregation. As the flocculant, a quaternary salt cationic surfactant, polyethyleneimine, and the like are used in the organic system, and an inorganic metal salt, an inorganic ammonium salt, a divalent or higher metal complex, and the like are used in the inorganic system.
Examples of the inorganic metal salt include metal salts such as sodium sulfate, sodium chloride, calcium chloride, calcium nitrate, barium chloride, magnesium chloride, zinc chloride, aluminum chloride, and aluminum sulfate; polyaluminum chloride, polyaluminum hydroxide, and Examples thereof include inorganic metal salt polymers such as calcium polysulfide. Examples of the inorganic ammonium salt include ammonium sulfate, ammonium chloride, and ammonium nitrate.
When the flocculant is added, the addition amount is preferably 60 parts by weight or less, and 55 parts by weight or less with respect to 100 parts by weight of the total amount of the crystalline polyester and the amorphous resin, from the viewpoint of environmental resistance characteristics of the toner. More preferred is 50 parts by weight or less.
The flocculant is preferably added after being dissolved in an aqueous medium, and it is preferable that the flocculant is sufficiently stirred at the time of addition of the flocculant and after completion of the addition.

From the viewpoint of uniformly dispersing a mixture of an aqueous dispersion containing crystalline polyester, an aqueous dispersion of an amorphous resin, and various additives used as necessary, the temperature is preferably less than the softening point of the mixed resin. More preferably, the dispersion treatment is performed at a temperature of “the softening point −30 ° C.” or lower. Specifically, the temperature is preferably 65 ° C. or less, more preferably 55 ° C. or less, and the dispersion treatment should be performed at a temperature higher than 0 ° C. from the viewpoint of fluidity of the medium and production energy of the aqueous dispersion of the resin. It is more preferable to carry out at 10 ° C. or higher.
From these viewpoints, a uniform resin dispersion can be prepared by a usual method such as stirring at a temperature of preferably about 0 to 65 ° C., more preferably about 10 to 55 ° C. for dispersion treatment.

As a method of dispersion treatment, high-speed stirring such as Ultra Disper (trade name, manufactured by Asada Tekko Co., Ltd.), Ebara Milder (trade name, manufactured by Ebara Manufacturing Co., Ltd.), and TK Homomixer (trade name, manufactured by Primix Co., Ltd.) High pressure homogenizer (trade name, manufactured by Izumi Food Machinery Co., Ltd.), homovalve type high pressure homogenizer represented by Minilab 8.3H type (trade name, manufactured by Rannie); Microfluidizer (trade name, manufactured by Microfluidics) ) And Nanomizer (trade name, manufactured by Nanomizer Co., Ltd.).
The amount of the aqueous medium used is preferably 100 to 3000 parts by weight, preferably 400 to 3000 parts by weight with respect to 100 parts by weight of the total amount of the crystalline polyester and the amorphous resin, from the viewpoint of obtaining aggregated particles having a uniform particle size. More preferred is 800 to 3000 parts by weight.

  The volume-median particle size of the aggregated particles obtained in Step 1 is preferably 1 to 10 μm, more preferably 2 to 8 μm, and more preferably 3 to 7 μm from the viewpoint of uniformly coalescing in the subsequent Step 2 to produce the coalesced particles. Is more preferable.

<Process 2>
Step 2 is a step in which the aggregated particles obtained in Step 1 are subjected to a coalescing step to obtain coalesced particles.
In step 2, after adding a coagulation terminator to the aqueous dispersion of aggregated particles obtained in step 1 as necessary, coalescence particles can be obtained by heating as necessary.
The temperature in the system in Step 2 is not less than “softening point of mixed resin−30 ° C.” or more, “the softening point + 10 ° C.” from the viewpoints of target particle size, particle size distribution, shape control and particle fusing property. Or less, more preferably “the softening point−25 ° C.” or more and “the softening point + 10 ° C.” or less, more preferably “the softening point−20 ° C.” or more and “the softening point + 10 ° C.” or less. Specifically, it is preferably maintained at 40 to 90 ° C, more preferably 50 to 80 ° C. The stirring speed is preferably a speed at which the aggregated particles do not settle.
In addition, when using an aggregation terminator, it is preferable to use a surfactant as the aggregation terminator, and it is more preferable to use an anionic surfactant. Of the anionic surfactants, it is more preferable to use at least one selected from the group consisting of alkyl ether sulfates, alkyl sulfates, and linear alkylbenzene sulfonates.

[Electrophotographic toner]
The resin particles obtained in the aggregation step and / or the coalescence step are appropriately subjected to a solid-liquid separation step such as filtration, a washing step, and a drying step, whereby the toner for electrophotography of the present invention (simply referred to as toner). There is).
In the washing step, it is preferable to use an acid in order to remove metal ions on the surface of the toner in order to ensure sufficient charging characteristics and reliability as the toner. Further, it is preferable to completely remove the added nonionic surfactant by washing, and washing with an aqueous solution below the cloud point of the nonionic surfactant is preferred. The washing is preferably performed a plurality of times.
In the drying step, any method such as a vibration type fluidized drying method, a spray drying method, a freeze drying method, a flash jet method, or the like can be employed. The water content after drying of the toner is preferably adjusted to 1.5% by weight or less, more preferably 1.0% by weight or less, from the viewpoint of chargeability.

The electrophotographic toner of the present invention is a polycondensation of an alcohol component containing an aliphatic diol having 2 to 12 carbon atoms and a carboxylic acid component containing 70 to 100 mol% of an aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms. The crystalline polyester and amorphous resin obtained by making it contain, and the said urea type compound and / or the said guanidine type compound are contained.
In the toner, the total content of the urea compound and the guanidine compound is preferably 1 to 1000 ppm from the viewpoint of uniformizing the dispersed particle size and reducing the particle size, and improving the transfer efficiency of the toner and the storage stability of the printed matter. More preferably, it is 10-500 ppm, and still more preferably 20-100 ppm.

(External additive)
Since the toner obtained as described above has low fusing property at the time of external addition treatment, an auxiliary agent such as a fluidizing agent can be easily added to the toner particle surface as an external additive. Examples of external additives include silica fine particles whose surfaces are hydrophobized, titanium oxide fine particles, alumina fine particles, cerium oxide fine particles, and inorganic fine particles such as carbon black; polymer fine particles such as polycarbonate, polymethyl methacrylate, and silicone resin. Fine particles can be used.
The number average particle diameter of the external additive is preferably 4 to 200 nm, more preferably 8 to 30 nm. The number average particle diameter of the external additive is determined using a scanning electron microscope or a transmission electron microscope.

  When the external additive is added, the addition amount is 0.8 to 5 parts by weight with respect to 100 parts by weight of the toner before the processing with the external additive, from the viewpoint of environmental stability of charge degree and weighted storage stability. 1 to 5 parts by weight is more preferable, and 1.5 to 3.5 parts by weight is still more preferable. However, when hydrophobic silica is used as the external additive, 0.8 to 3.5 parts by weight, preferably 1 to 3 parts by weight of hydrophobic silica is used with respect to 100 parts by weight of the toner before processing with the external additive. By using this, the desired effect can be obtained.

(Physical properties of electrophotographic toner)
The volume median particle size of the electrophotographic toner of the present invention is preferably from 1 to 10 μm, more preferably from 2 to 8 μm, and even more preferably from 3 to 7 μm, from the viewpoints of high image quality and productivity of the toner.
In the toner of the present invention, the weight ratio of the crystalline polyester and the amorphous resin [crystalline polyester / amorphous resin] is 5/95 to 40/60 from the viewpoint of toner transfer efficiency and print storage stability. Preferably, 6 / 94-30 / 70 is more preferable, and 7 / 93-25 / 75 is still more preferable.
The acid value of the binder resin used for the toner is preferably 1 to 40 mgKOH / g, more preferably 2 to 35 mgKOH / g, and more preferably 3 to 30 mgKOH / g from the viewpoints of toner chargeability, transfer efficiency, and print storage stability. Is more preferable.
The softening point of the binder resin used for the toner is preferably 80 to 160 ° C., more preferably 80 to 150 ° C., and further preferably 90 to 140 ° C. from the viewpoints of low-temperature fixability of the toner, transfer efficiency, and print storage stability. preferable. Moreover, 45-80 degreeC is preferable and 50-70 degreeC is more preferable from the same viewpoint as the glass transition temperature of the binder resin.

The electrophotographic toner of the present invention is a known toner binder resin different from the binder resin, for example, a styrene resin such as polyester or styrene-acrylic resin, or an epoxy resin, as long as the effects of the present invention are not impaired. Further, it may contain a resin such as polycarbonate or polyurethane.
In the electrophotographic toner of the present invention, the content of the binder resin for toner of the present invention is preferably 50% by weight or more, more preferably 70% by weight or more, and more preferably 80% by weight or more in the total binder resin. 90% by weight or more is still more preferable, and it is still more preferable that it is substantially 100% by weight.
The electrophotographic toner of the present invention can be used as a one-component developer or a two-component developer mixed with a carrier.

Hereinafter, “%” and “parts” are “% by weight” and “parts by weight” unless otherwise specified.
[Measurement of resin properties]
Measurement of resin physical properties such as crystalline polyester and amorphous resin obtained in Examples and Comparative Examples, volume median particle size (D ₅₀ ) of each particle, and calculation of CV value were performed as follows.

<Softening point of resin>
Using a flow tester (manufactured by Shimadzu Corporation, trade name: “CFT-500D”), a 1 g sample was heated at a heating rate of 6 ° C./min, and a load of 1.96 MPa was applied by a plunger. The nozzle was extruded from a nozzle having a length of 1 mm and a length of 1 mm. The amount of plunger drop of the flow tester was plotted against the temperature, and the temperature at which half of the sample flowed out was taken as the softening point.

<Maximum peak temperature and melting point of endothermic resin>
Using a differential scanning calorimeter (DSC; manufactured by TA Instruments Japan Co., Ltd., trade name: “Q-100”), it was cooled from room temperature (20 ° C.) to 0 ° C. at a cooling rate of 10 ° C./min. The sample was allowed to stand for 1 minute, and then measured while the temperature was raised to 180 ° C. at a temperature raising rate of 10 ° C./min. Of the observed endothermic peaks, the peak temperature at the highest temperature is the maximum endothermic peak temperature (the maximum peak temperature of the 1st RUN endotherm), and if the maximum peak temperature is within 20 ° C of the softening point, the crystal The melting point of the crystalline polyester.

<Number average molecular weight and weight average molecular weight of crystalline polyester>
By the following method, the molecular weight distribution was measured by gel permeation chromatography (GPC) method, and the number average molecular weight M _n and the weight average molecular weight M _w of the resin were determined.
(1) Preparation of sample solution The resin was dissolved in chloroform so that the concentration was 0.5 g / 100 mL. Subsequently, this solution was filtered using a fluororesin filter having a pore size of 2 μm (manufactured by Sumitomo Electric Industries, Ltd., trade name: FP-200) to remove insoluble components to obtain a sample solution.
(2) Molecular weight measurement Using the following apparatus, chloroform was flowed as an eluent at a flow rate of 1 ml per minute, and the column was stabilized in a constant temperature bath at 40 ° C. Measurement was performed by injecting 100 μl of the sample solution. The molecular weight of the sample was calculated based on a calibration curve prepared in advance. The calibration curve at this time includes several types of monodisperse polystyrene (monodisperse polystyrene manufactured by Tosoh Corporation; 2.63 × 10 ³ , 2.06 × 10 ⁴ , 1.02 × 10 ⁵ , GL Sciences Inc.) Monodispersed polystyrenes made from 2.10 × 10 ³ , 7.00 × 10 ³ , 5.04 × 10 ⁴ (number average molecular weight)) were used as standard samples.
Measuring device: CO-8010 (trade name, manufactured by Tosoh Corporation)
Analytical column: GMH _XL + G3000H _XL (both trade names, manufactured by Tosoh Corporation)

<Resin acid value, hydroxyl value>
The acid value of the resin was measured based on the method of JIS K 0070. However, only the measurement solvent was changed from the mixed solvent of ethanol and ether specified in JIS K 0070 to a mixed solvent of acetone and toluene (acetone: toluene = 1: 1 (volume ratio)).
Moreover, the hydroxyl value of resin was measured on condition of the following based on JISK1557.
Sample amount: 2g
Acetylating reagent: 10 mL of a mixed solution of 65 mL of acetic anhydride and 935 mL of pyridine
Catalyst: None Reaction temperature: 99 ° C
Reaction time: 2 hours Solvent: Mixed solvent of acetone and toluene (acetone: toluene = 1: 1 (volume ratio))
Titration solution: 0.5 mol / L KOH ethanol solution

<Degree of neutralization of resin>
The degree of neutralization (mol%) when the resin is anionic was determined by the following formula.
Degree of neutralization = {[weight of neutralizer (g) / equivalent of neutralizer] / [[acid value of resin (KOH mg / g) × resin weight (g)] / (56 × 1000)]} × 100

<Volume Median Particle Size (D ₅₀ ) and CV Value of Resin Particles, Colorant Fine Particles, Release Agent Fine Particles, and Charge Control Agent Fine Particles>
Using a laser diffraction particle size analyzer (Horiba, Ltd., trade name: “LA-920”), distilled water is added to the measurement cell, and the volume-median particle size is adjusted so that the absorbance is in the proper range. (D ₅₀ ) was measured.
The CV value was calculated according to the following formula. A lower CV value of the resin particles in the aqueous dispersion indicates that the particle diameters are uniform.
CV value (%) = (standard deviation of particle size distribution / volume median particle size (D ₅₀ )) × 100

<Glass transition temperature of amorphous resin>
Using a differential scanning calorimeter (DSC; manufactured by TA Instruments Japan, trade name: “Q-100”), 0.01 to 0.02 g of a sample was weighed into an aluminum pan, and 200 ° C. The sample was cooled to 0 ° C at a rate of temperature decrease of 10 ° C / min from that temperature, and the sample was heated at a rate of temperature increase of 10 ° C / min. The temperature at the intersection with the tangent indicating the maximum slope from the portion to the peak apex was defined as the glass transition temperature.

Production Examples 1-3
(Production of crystalline polyesters A to C)
The monomer of the condensation polymerization resin component in the blending amount shown in Table 1 is put into a 10 L four-necked flask equipped with a nitrogen introduction tube, a dehydration tube, a stirrer and a thermocouple, and heated to 140 ° C. for 6 hours. Then, the reaction was carried out while raising the temperature to 200 ° C. at 10 ° C./hour. After reacting at 200 ° C. to a reaction rate of 80%, 20 g of tin 2-ethylhexanoate was added, and further reacted at 200 ° C. for 2 hours. Furthermore, reaction was performed at 8 kPa for 2 hours to obtain crystalline polyesters A to C. Here, the reaction rate is a value converted with 100% as the completion of the theoretical reaction water discharge calculated from the carboxy group and hydroxyl group of the alcohol component and carboxylic acid component.

Examples 1-7 and Comparative Examples 1-4
(Preparation of aqueous dispersion of crystalline polyester)
600 g of methyl ethyl ketone was put into a 5 L container equipped with a stirrer, reflux condenser, dropping funnel, thermometer and nitrogen introduction tube, and the crystalline polyester produced in Production Examples 1 to 3 (room temperature (20 ° C.) stored for 1 month) Product) 200 g of each was added at 70 ° C. to dissolve the crystalline polyester. Furthermore, urea 50% aqueous solution, guanidine hydrochloride 50% aqueous solution or phenylurea 50% aqueous solution in the amount shown in Table 2 was added and stirred at 60 ° C. for 5 minutes. A 5% aqueous solution of potassium hydroxide was added to the resulting solution to neutralize it to a degree of neutralization of 80 mol%, followed by the addition of 2500 g of ion-exchanged water, followed by reduced pressure at a stirring rate of 250 r / min. Then, methyl ethyl ketone was distilled off at 70 ° C. to 30 ppm or less. The solid content concentration of the aqueous dispersion of the crystalline polyester was measured, and ion-exchanged water was added so that the solid content concentration was 10% by weight to obtain a crystalline polyester dispersion.

As is apparent from Table 2, the aqueous dispersions of Comparative Examples 1 to 4 in which urea or guanidine was not added when the crystalline polyester was dispersed in the aqueous medium had a high CV value of 78 to 90% and a particle size. And the volume-median particle size was as large as 480 to 540 nm.
In contrast, the aqueous dispersions of Examples 1 to 7 to which urea or guanidine was added when the crystalline polyester was dispersed in the aqueous medium had a CV value in the range of 17 to 37% and a volume-median particle size. Was in the range of 160-330 nm.
From this, it can be seen that the aqueous dispersions of Examples 1 to 7 have a uniform and small particle size compared to the aqueous dispersions of Comparative Examples 1 to 4.

Production Examples 4 and 5
(Production of amorphous resins AA and AB)
Raw materials other than trimellitic anhydride shown in Table 3, and 40 g of tin octylate and 2 g of gallic acid monohydrate were placed in a 10 L four-necked flask equipped with a nitrogen introduction tube, a dehydration tube, a stirrer and a thermocouple. The mixture was allowed to react at 230 ° C. for 8 hours, and then reacted at 8.3 kPa for 1 hour. Further, trimellitic anhydride was added at 210 ° C. and reacted until reaching the softening point shown in Table 3 to produce amorphous resins AA and AB.

Production Examples 6-9
(Preparation of aqueous dispersion of amorphous resin 1)
In a 5 L container equipped with a stirrer, reflux condenser, dropping funnel, thermometer and nitrogen introduction tube, 600 g of methyl ethyl ketone and “Kao Akypo RLM-100” as an anionic surfactant (trade name, manufactured by Kao Corporation) , Component: polyoxyethylene lauryl ether acetic acid) 2 g was added, and amorphous resin AA or AB 100 g was added at 50 ° C. to dissolve the amorphous resin.
5% aqueous potassium hydroxide solution was added to the resulting solution to neutralize it to a degree of neutralization of 80 mol%, and then 2000 g of ion exchanged water was added, followed by a stirring speed of 250 r / min. Under reduced pressure, methyl ethyl ketone was distilled off at a temperature of 50 ° C. or lower to 30 ppm or lower. The solid content concentration of the aqueous dispersion of the amorphous resin was measured, and ion-exchanged water was added so that the solid content concentration was 10% by weight to obtain an aqueous dispersion (AA1, AB1) of the amorphous resin. .

(Preparation of aqueous dispersion of amorphous resin 2)
Aqueous dispersions AA2 and AB2 of amorphous resin were obtained in the same manner as in Example 3, except that the crystalline polyester A of Example 3 was replaced with the amorphous resins AA and AB of Production Examples 4 and 5.

Production Example 10
(Preparation of colorant dispersion)
50 g of copper phthalocyanine (manufactured by Dainichi Seika Kogyo Co., Ltd., model number: ECB-301), 5 g of nonionic surfactant (manufactured by Kao Corporation, trade name: “Emulgen (registered trademark) 150”) and 200 g of ion-exchanged water Were mixed, copper phthalocyanine was dissolved, and dispersed for 10 minutes using a homogenizer to obtain a colorant dispersion containing colorant fine particles. The volume median particle size (D ₅₀ ) of the colorant fine particles was 120 nm.

Production Example 11
(Preparation of release agent dispersion)
Paraffin wax (Nippon Seiwa Co., Ltd., trade name: “HNP9”, melting point: 85 ° C.) 50 g, cationic surfactant (manufactured by Kao Corporation, trade name: “Sanisol (registered trademark) B50”) 5 g Then, 200 g of ion-exchanged water was heated to 95 ° C., and the paraffin wax was dispersed using a homogenizer, followed by dispersion treatment using a pressure discharge type homogenizer to obtain a release agent dispersion containing release agent fine particles. . The volume median particle size (D ₅₀ ) of the release agent fine particles was 550 nm.

Production Example 12
(Preparation of charge control agent dispersion)
50 g of a charge control agent (Orient Chemical Industries, trade name: “Bontron E-84”), 5 g of a nonionic surfactant (trade name: “Emulgen (registered trademark) 150”, manufactured by Kao Corporation), and 200 g of ion-exchanged water was mixed, and glass beads were used and dispersed for 10 minutes using a sand grinder to obtain a charge control agent dispersion liquid containing charge control agent fine particles. The volume median particle size (D ₅₀ ) of the charge control agent fine particles was 500 nm.

Examples 8-15, Comparative Examples 5-8
(Method for producing electrophotographic toner)
The dispersion of the amorphous resin and the aqueous dispersion of the crystalline polyester were mixed so that the solid content weight ratio of the amorphous resin AA, the amorphous resin AB, and the crystalline polyester was the ratio shown in Table 5. 300 g of resin dispersion, 8 g of colorant dispersion, 6 g of release agent dispersion, 2 g of charge control agent dispersion, and 52 g of deionized water were placed in a 2 L container.
Next, 146 g of a 6.2 wt% aqueous ammonium sulfate solution was added dropwise at room temperature with stirring at 100 r / min with a chi-type stirrer over 30 minutes. Then, it heated up, stirring, when it became 50 degreeC, it fixed to 50 degreeC and hold | maintained for 3 hours. After forming aggregated particles by this, a dilute solution obtained by diluting 4.2 g of a polyoxyethylene dodecyl ether sodium sulfate aqueous solution (solid content 28 wt%) with 37 g of deionized water was added as an aggregation terminator.
Subsequently, the temperature was raised to 80 ° C. at 0.16 ° C./min, and after maintaining at 80 ° C. for 1 hour from the time when the temperature reached 80 ° C., the heating was terminated. As a result, coalesced particles were formed, and then gradually cooled to room temperature, and toner particles were obtained through a suction filtration process, a washing process, and a drying process.
Further, 2.0 parts by weight of hydrophobic silica “NAX-50” (trade name, manufactured by Nippon Aerosil Co., Ltd., number average particle diameter 40 nm), 1.5 parts by weight of hydrophobic silica with respect to 100 parts by weight of toner particles. Silica “R972” (trade name, manufactured by Nippon Aerosil Co., Ltd., number average particle size 16 nm) was stirred into a 10 L Henschel mixer (manufactured by Mitsui Mining Co., Ltd.) in the ST (upper blade) -A0 (lower blade) type. A blade was attached, and stirring was performed at 3000 rpm for 2 minutes to perform an external addition process to obtain a toner.

[Evaluation]
<Toner transfer efficiency (transfer residue)>
A toner was mounted on a color printer “MICROLINE 5400” (trade name, manufactured by Oki Data Co., Ltd.), and a solid image was printed. At this time, the toner amount of the solid image on the photoconductor is adjusted to 0.40 to 0.50 mg / cm ² , the machine is stopped during the printing of the solid image, and the mending is performed on the photoconductor after passing through the transfer portion. A tape was affixed, the toner that was not transferred and remained on the photoconductor was transferred to a mending tape, and the mending tape was peeled off from the photoconductor. The hue difference between the peeled and unused mending tape was measured with a color difference meter “X-Rite” (trade name, manufactured by X-Rite), and the transfer efficiency was evaluated based on the color difference density ΔE. . If ΔE is less than 5.0, the transfer efficiency is good. The results are shown in Table 5.

<Pressurized storage stability of printed matter>
The following tests were carried out using toner from the third day, the first month, and the third month (storage conditions: 25 ° C., 50% RH) after toner production.
A toner was mounted on a copying machine “AR-505” (trade name, manufactured by Sharp Corporation), and an image was printed without fixing (printing area: 2 cm × 12 cm, adhesion amount: 0.5 mg / cm ² ). The fixing machine of the copying machine was fixed offline at 140 ° C. and 20 mm / sec for 100 sheets. Note that “CopyBond SF-70NA” (trade name, manufactured by Sharp Corporation, 75 g / m ² ) was used as the fixing paper.
The fixed images were overlaid, and a 2 kg weight was placed on the images, and left in an environment of 50 ° C. and 50% relative humidity for 12 hours, and the storage stability was evaluated based on the following criteria. The fusing property was evaluated every 4 hours.
5: None of the printed matter obtained using the toner on the third day, the first month, and the third month after the toner production was fused even if it was left for 12 hours after printing.
4: The printed matter obtained using the toner on the third day and the first month after the production of the toner did not fuse even when left for 12 hours after the printing, but the printed matter obtained using the toner in the third month after the production of the toner Then, it was fused for the first time after leaving for 12 hours after printing.
3: The printed matter obtained using the toner on the third day after the production of the toner did not fuse even after being left for 12 hours after the printing, but the printed matter obtained using the toner in the first month after the production of the toner was used after the printing. It was fused for the first time by leaving it alone.
2: The printed matter obtained using the toner on the third day after the production of the toner did not fuse even if it was left for 12 hours after the printing, but the printed matter obtained using the toner in the first month after the production of the toner 8 It was fused for the first time by leaving it alone.
1: The printed matter obtained using the toner on the third day after the production of the toner did not fuse even after being left for 12 hours after the printing, but the printed matter obtained using the toner in the first month after the production of the toner 4 Fused over time.

  As is apparent from Table 5, the toners of Comparative Examples 5 to 8 have a high color difference density ΔE, and prints obtained using the toner after storage at room temperature are inferior in storage stability, whereas Examples 8 to 15 It can be seen that this toner has higher transfer efficiency than the toner of the comparative example and is excellent in the preservation of printed matter.

  The aqueous dispersion of crystalline polyester for toner obtained by the present invention has a small dispersed particle size and is uniform. The toner obtained by using this aqueous dispersion has characteristics such as high transfer efficiency and excellent pressurization storage stability of printed matter. Therefore, the toner used in electrophotography, electrostatic recording method, electrostatic printing method, etc. It can be suitably used as a photographic toner.

Claims (7)

  In the presence of one or more urea compounds selected from urea and alkyl urea and / or one or more guanidine compounds selected from guanidine, alkyl guanidine and acid addition salts thereof, and a neutralizing agent, Disperse in an aqueous medium a crystalline polyester obtained by polycondensation of an alcohol component containing 12 aliphatic diols and a carboxylic acid component containing 70 to 100 mol% of an aliphatic dicarboxylic acid compound having 8 to 12 carbon atoms A method for producing an aqueous dispersion of crystalline polyester for toner, comprising the step of: The method for producing an aqueous dispersion of crystalline polyester for toner according to claim 1, comprising the following steps A1 and A2.
Step A1: A step of mixing the crystalline polyester, the urea compound and / or guanidine compound, an organic solvent, a neutralizing agent and water to obtain a dispersion of crystalline polyester.
Step A2: A step of obtaining an aqueous dispersion of crystalline polyester by removing the organic solvent from the dispersion obtained in Step A1.   3. The crystalline polyester for toner according to claim 1, wherein a total use amount of the urea compound and the guanidine compound is 0.3 to 15 parts by weight with respect to 100 parts by weight of the crystalline polyester. A method for producing an aqueous dispersion.   An aqueous dispersion of crystalline polyester for toner obtained by the production method according to claim 1.   A method for producing an electrophotographic toner, comprising a step of subjecting the aqueous dispersion of crystalline polyester for toner according to claim 4 to an aqueous dispersion of an amorphous resin to obtain an aggregated particle.   The method for producing an electrophotographic toner according to claim 5, further comprising a step of subjecting the obtained aggregated particles to a coalescing step to obtain coalesced particles.   An electrophotographic toner obtained by the production method according to claim 5.