JP4263667B2 - Measuring method of molecular weight distribution of toner - Google Patents

Description

  The present invention relates to a method for evaluating a toner for developing an electrostatic image.

  In electrophotographic devices and electrostatic recording devices, toner is attached to an electrostatic latent image formed on a photoreceptor, transferred to a transfer material, and then fixed to the transfer material by heat to form a toner image. is doing. Also, full-color image formation is generally performed by using four color toners of black, yellow, magenta, and cyan. Each toner is developed and each toner layer is superimposed on a transfer material. To obtain a full-color image.

  Here, controlling the molecular weight distribution of the toner is important in controlling the fixing property, image gloss, and the like. Conventionally, so-called GPC (gel permeation chromatography) is generally used as a means for measuring molecular weight distribution, and as its solvent, THF (tetrahydrofuran) at room temperature, thermal GPC with o-dichlorobenzene under heating, etc. It has been known. However, the solubility of the toner containing a crosslinking component in these solvents has been a problem. In the evaluation with THF, for example, attempts have been made to control the molecular weight distribution of the THF-soluble component or the ratio of the insoluble component (see, for example, Patent Documents 1 to 3). In some cases, the amount of soluble components in THF is as low as 50 wt%, and the upper and lower limits of fixing sufficient to control only the dissolved components (hot offset property, cold offset property, wrapping property, friction strength after fixing) In addition, it was not possible to satisfy the toner contamination on paper due to gloss, gloss offset, etc. Furthermore, it was not possible to obtain a developing system with less carrier contamination due to trace toner spent components, and toner with relatively high solubility. However, the inclusion of a resin-insoluble component means that when evaluating the exact molecular weight distribution, the distribution of all resins Was the problem would be no.

Japanese Patent No. 3413024 Japanese Patent No. 3397661 JP 2002-351143 A

  The object of the present invention is to solve the above-mentioned problems of the prior art, accurately evaluate the molecular weight distribution of the toner containing the crosslinking component, and to crosslink with sufficient solubility, sufficient detection sensitivity, and sufficient peak separation. It is to provide a molecular weight distribution measuring method by GPC method of component-containing toner.

As a result of intensive studies to achieve the above-mentioned problems, the present inventors have evaluated the dissolved component of HFIP (hexafluoroisopropanol), and the molecular weight distribution of a cross-linking component-containing toner (containing at least a colorant and a resin) It has been found that the molecular weight distribution of the crosslinking component-containing toner can be accurately evaluated by using the measurement method.
By using HFIP (hexafluoroisopropanol) that can be sufficiently dissolved up to highly crosslinked resin components, accurate molecular weight distribution evaluation to highly crosslinked components (high molecular weight components) that could not be sufficiently dissolved with conventional solvents such as THF (tetrahydrofuran) Made possible.
Further, by using a toner molecular weight distribution measuring method using a GPC method using an HFIP eluent in which 5 to 20 mM sodium trifluoroacetate is dissolved, the solubility of the toner and the separation property of the molecular weight distribution are used. Can be improved, which is more preferable.
The toner was dissolved in an HFIP solvent by sonication to a concentration of 0.5 to 5 mg / ml for 1 to 7 minutes, and the solution was filtered with a 0.25 to 0.65 μm filter. By using a toner molecular weight distribution measuring method characterized by analyzing the solution by GPC method, it is possible to improve the solubility of the toner, the separation of the molecular weight distribution, and the detection sensitivity, which is more preferable.
Further, it is more preferable in terms of the solubility of the toner to use a molecular weight distribution measuring method characterized in that the toner contains at least polyester.
Further, it is more preferable in terms of the solubility of the toner to use a molecular weight distribution measuring method characterized in that the toner contains at least a modified polyester.
In addition, it is more preferable in terms of the solubility of the toner to use a molecular weight distribution measuring method characterized in that the toner contains a modified polyester containing at least a nitrogen atom.

That is, the object is achieved according to the invention (1) "at least a colorant, a resin component of the polyester prepolymer with an amine and including a toner and a resin containing a modified polyester obtained by reacting the containing isocyanate groups a molecular weight distribution the toner of the measurement method of measuring, the measuring method, HFIP evaluates the dissolved components of (hexafluoroisopropanol), crosslinked form of the resin component having a molecular weight distribution Dressings containing measuring The HFIP is an eluent in which 5 to 20 mM sodium trifluoroacetate is dissolved, and the toner is sonicated so as to have a concentration of 0.5 to 5 mg / ml in the HFIP eluent. And the resulting solution is filtered through a 0.25 to 0.65 μm filter, and the resulting solution is analyzed by the GPC method. It is solved by measuring a toner ", which comprises the stages that.

  According to the present invention, the molecular weight distribution of a crosslinking component-containing toner can be accurately evaluated, the solubility of the crosslinking component-containing toner is sufficient, the detection sensitivity is sufficient, and the peak separation property is sufficient by the GPC method. A molecular weight distribution measurement method can be provided.

  Hereinafter, the present invention will be described in detail. Here, with respect to the toner, developer production method and material used in the present invention, the overall system relating to the electrophotographic process, the analytical measurement (evaluation) technique, and conditions, known ones can be used if the conditions are satisfied.

(Measurement conditions for HFIP dissolution GPC of toner)
In the present invention, the molecular weight distribution of the toner can be measured by GPC (gel permeation chromatography). GPC is a process in which a sample elutes in a gel column, and the elution time changes depending on the magnitude of the interaction with the gel. The larger the molecular weight, the smaller the interaction with the gel column and the faster the elution time (retention time). . Conversely, the smaller the molecular weight, the greater the interaction and the longer the elution time. By detecting the amount of the eluted component with an RI (photorefractometer) detector or the like, a chromatogram showing the relationship between the elution time and the eluted amount is obtained.
On the other hand, standard polystyrene and polymethylmethacrylate (PMMA) with molecular weight distribution defined by other analytical means are measured in the same way, the relationship between elution time and molecular weight is grasped, and the obtained calibration curve is used to determine the molecular weight distribution. The molecular weight distribution of the sample can be evaluated. HFIP (hexafluoroisopropanol) used as a solvent is the official name 1,1,1,3,3,3-hexafluoro-2-propanol (1,1,1,3,3,3-Hexafluoro-2-propanol). Are also described.

An example of GPC measurement conditions is shown below.
1) Equipment: HLC-8220GPC manufactured by TOSO
2) Solvent: HFIP + 10 mM sodium trifluoroacetate 3) Column; Shodex HFIP-LG + HFIP-806M × 2 bottles 4) Temperature: 40 ° C.
5) Flow rate: 0.8 ml / min
6) Sample: Measurement after filtration in a 0.45 μm filter after dissolution in a solvent. Concentration 2 mg / ml, injection volume 500 μl
7) Detector; RI detector (RI-8011)

The molecular weight distribution is calculated using the molecular weight calibration curve prepared with the monodisperse polymethylmethacrylate standard sample when the molecular weight of the sample is calculated under the above conditions.
The apparatus is preferably an apparatus resistant to HFIP solvent, and needs attention because it is easily deteriorated by an HFIP solvent such as a pump or a degasser. In addition, it is more preferable to use two or more columns previously substituted with HFIP in series in order to improve the separation of each molecular weight component.
In addition, it is more preferable that sodium trifluoroacetate is contained (dissolved) in the solvent in an amount of 5 to 20 mM, more preferably 8 to 15 mM, as a salt for improving the solubility and separation of each molecular weight component. If it is less than 5 mM, the effect is not exhibited, which is not preferable. Moreover, when it contains exceeding 20 mM, it is unpreferable at a column damage or a soluble point. It is also preferable to add another salt effect reagent instead of or in addition to sodium trifluoroacetate.

  The toner is dissolved in an HFIP solvent by sonication to a concentration of 0.5 to 5 mg / ml, more preferably 1 to 3 mg / ml, and preferably 1 to 7 minutes, more preferably 3 to 7 minutes. More preferably, the solution is filtered through a filter of 0.25 to 0.65 μm, more preferably 0.35 to 0.55 μm, and then the solution is analyzed by the GPC method. Here, a concentration of less than 0.5 mg / ml is not preferable in terms of detection sensitivity. Moreover, when it exceeds 5 mg / ml, it is unpreferable at the point of solubility and peak separability. Further, if the ultrasonic time is less than 1 minute, the solubility is not sufficient, and if it exceeds 7 minutes, re-aggregation of components such as pigments occurs, which is not preferable in terms of solubility. On the other hand, when the filter diameter is less than 0.25, the pigment component in the toner is clogged and the filterability is impaired, which is not preferable. On the other hand, when the average particle diameter exceeds 0.65 μm, pigment aggregates or the like enter the column as they are, which is not preferable in terms of column damage and separability.

(Modified polyester resin)
In the present invention, the following modified polyester resins can be used as the polyester resin that can be used in the toner. For example, a polyester prepolymer (A) having an isocyanate group can be used. The polyester prepolymer (A) having an isocyanate group is a polycondensate of a polyol (1) and a polycarboxylic acid (2), and a polyester having an active hydrogen group further reacted with a polyisocyanate (3), etc. Is mentioned. Examples of the active hydrogen group possessed by the polyester include hydroxyl groups (alcoholic hydroxyl groups and phenolic hydroxyl groups), amino groups, carboxyl groups, mercapto groups, and the like. Among these, alcoholic hydroxyl groups are preferred.

Examples of the polyol (1) include a diol (1-1) and a tri- or higher valent polyol (1-2). (1-1) alone or (1-1) and a small amount of (1-2) Mixtures are preferred.
Diol (1-1) includes alkylene glycol (ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,4-butanediol, 1,6-hexanediol, etc.); alkylene ether glycol (diethylene glycol) , Triethylene glycol, dipropylene glycol, polyethylene glycol, polypropylene glycol, polytetramethylene ether glycol, etc.); alicyclic diols (1,4-cyclohexanedimethanol, hydrogenated bisphenol A, etc.); bisphenols (bisphenol A, bisphenol) F, bisphenol S, etc.); alkylene oxide (ethylene oxide, propylene oxide, butylene oxide, etc.) adduct of the above alicyclic diol; Alkylene oxide phenol compound (ethylene oxide, propylene oxide, butylene oxide, etc.), etc. adducts. Among them, preferred are alkylene glycols having 2 to 12 carbon atoms and alkylene oxide adducts of bisphenols, and particularly preferred are alkylene oxide adducts of bisphenols and alkylene glycols having 2 to 12 carbon atoms. It is a combined use.
The trihydric or higher polyol (1-2) includes 3 to 8 or higher polyhydric aliphatic alcohols (glycerin, trimethylolethane, trimethylolpropane, pentaerythritol, sorbitol, etc.); trihydric or higher phenols (Trisphenol PA, phenol novolak, cresol novolak, etc.); and alkylene oxide adducts of the above trivalent or higher polyphenols.

Examples of the polycarboxylic acid (2) include dicarboxylic acid (2-1) and trivalent or higher polycarboxylic acid (2-2). (2-1) alone and (2-1) with a small amount of ( The mixture of 2-2) is preferable.
Dicarboxylic acid (2-1) includes alkylene dicarboxylic acid (succinic acid, adipic acid, sebacic acid, etc.); alkenylene dicarboxylic acid (maleic acid, fumaric acid, etc.); aromatic dicarboxylic acid (phthalic acid, isophthalic acid, terephthalic acid) And naphthalenedicarboxylic acid). Of these, preferred are alkenylene dicarboxylic acids having 4 to 20 carbon atoms and aromatic dicarboxylic acids having 8 to 20 carbon atoms. Examples of the trivalent or higher polycarboxylic acid (2-2) include aromatic polycarboxylic acids having 9 to 20 carbon atoms (trimellitic acid, pyromellitic acid, and the like). In addition, as polycarboxylic acid (2), you may make it react with polyol (1) using the acid anhydride or lower alkyl ester (methyl ester, ethyl ester, isopropyl ester, etc.) of the above-mentioned thing.

  The ratio of the polyol (1) to the polycarboxylic acid (2) is usually 2/1 to 1/1, preferably 1. as the equivalent ratio [OH] / [COOH] of the hydroxyl group [OH] and the carboxyl group [COOH]. 5/1 to 1/1, more preferably 1.3 / 1 to 1.02 / 1.

  Examples of the polyisocyanate (3) include aliphatic polyisocyanates (tetramethylene diisocyanate, hexamethylene diisocyanate, 2,6-diisocyanatomethylcaproate, etc.); alicyclic polyisocyanates (isophorone diisocyanate, cyclohexylmethane diisocyanate, etc.); aromatic Diisocyanates (tolylene diisocyanate, diphenylmethane diisocyanate, etc.); araliphatic diisocyanates (α, α, α ′, α′-tetramethylxylylene diisocyanate, etc.); isocyanurates; polyisocyanates such as phenol derivatives, oximes, caprolactams, etc. And a combination of two or more of these.

  The ratio of the polyisocyanate (3) is usually 5/1 to 1/1, preferably 4 /, as an equivalent ratio [NCO] / [OH] of the isocyanate group [NCO] and the hydroxyl group [OH] of the polyester having a hydroxyl group. 1 to 1.2 / 1, more preferably 2.5 / 1 to 1.5 / 1. When [NCO] / [OH] exceeds 5, low-temperature fixability deteriorates. If the molar ratio of [NCO] is less than 1, the urea content in the modified polyester will be low, and the hot offset resistance will deteriorate. The content of the polyisocyanate (3) component in the prepolymer (A) having an isocyanate group at the terminal is usually 0.5 to 40% by weight, preferably 1 to 30% by weight, more preferably 2 to 20% by weight. It is. If it is less than 0.5% by weight, the hot offset resistance deteriorates, and it is disadvantageous in terms of both heat-resistant storage stability and low-temperature fixability. On the other hand, if it exceeds 40% by weight, the low-temperature fixability deteriorates.

  The number of isocyanate groups contained per molecule in the prepolymer (A) having an isocyanate group is usually 1 or more, preferably 1.5 to 3 on average, more preferably 1.8 to 2.5 on average. It is. If it is less than 1 per molecule, the molecular weight of the modified polyester after crosslinking and / or elongation becomes low, and the hot offset resistance deteriorates.

(Crosslinking agent and extender)
In the present invention, amines can be used as a crosslinking agent and / or an extender. As amines (B), diamine (B1), triamine or higher polyamine (B2), amino alcohol (B3), amino mercaptan (B4), amino acid (B5), and amino groups of (B1) to (B5) (B6) etc. that are blocked. Examples of the diamine (B1) include aromatic diamines (phenylenediamine, diethyltoluenediamine, 4,4′diaminodiphenylmethane, etc.); alicyclic diamines (4,4′-diamino-3,3′dimethyldicyclohexylmethane, diaminecyclohexane, Isophorone diamine etc.); and aliphatic diamines (ethylene diamine, tetramethylene diamine, hexamethylene diamine etc.) and the like. Examples of the trivalent or higher polyamine (B2) include diethylenetriamine and triethylenetetramine. Examples of amino alcohol (B3) include ethanolamine and hydroxyethylaniline. Examples of amino mercaptan (B4) include aminoethyl mercaptan and aminopropyl mercaptan. Examples of the amino acid (B5) include aminopropionic acid and aminocaproic acid. As (B6) which blocked the amino group of (B1) to (B5), ketimine compounds obtained from the amines and ketones (acetone, methyl ethyl ketone, methyl isobutyl ketone, etc.) of (B1) to (B5), Examples include oxazoline compounds. Among these amines (B), preferred are (B1) and a mixture of (B1) and a small amount of B2.

  Furthermore, if necessary, the molecular weight of the modified polyester after completion of the reaction can be adjusted by using a terminator for crosslinking and / or elongation. Examples of the terminator include monoamines (diethylamine, dibutylamine, butylamine, laurylamine, etc.), and those blocked (ketimine compounds).

  The ratio of amines (B) is the equivalent ratio [NCO] / [NHx] of isocyanate groups [NCO] in the prepolymer (A) having isocyanate groups and amino groups [NHx] in amines (B). The ratio is usually 1/2 to 2/1, preferably 1.5 / 1 to 1 / 1.5, more preferably 1.2 / 1 to 1 / 1.2. When [NCO] / [NHx] is greater than 2 or less than 1/2, the molecular weight of the urea-modified polyester (i) becomes low and the hot offset resistance deteriorates.

(Unmodified polyester)
In the present invention, it is important not only to use the modified polyester (A) alone, but also to contain the unmodified polyester (C) as a toner binder component together with the (A). By using (C) in combination, low-temperature fixability and glossiness when used in a full-color device are improved. Examples of (C) include polycondensates of polyol (1) and polycarboxylic acid (2) similar to the polyester component of (A), and preferred polyols, polycarboxylic acids, ratios thereof and the like ( Same as A). (C) is not limited to unmodified polyester, but may be modified with a chemical bond other than a urea bond, and may be modified with, for example, a urethane bond. It is preferable that (A) and (C) are at least partially compatible in terms of low-temperature fixability and hot offset resistance. Accordingly, the polyester component (A) and (C) preferably have similar compositions. When (A) is contained, the weight ratio of (A) to (C) is usually 5/95 to 75/25, preferably 10/90 to 25/75, more preferably 12/88 to 25/75, Particularly preferred is 12/88 to 22/78. If the weight ratio of (A) is less than 5%, the hot offset resistance deteriorates, and it is disadvantageous in terms of both heat-resistant storage stability and low-temperature fixability.

  The peak molecular weight of (C) is usually 1000-30000, preferably 1500-10000, more preferably 2000-8000. If it is less than 1000, heat-resistant storage stability will deteriorate, and if it exceeds 30000, low-temperature fixability will deteriorate. The hydroxyl value of (C) is preferably 5 or more, more preferably 10 to 120, and particularly preferably 20 to 80. If it is less than 5, it is disadvantageous in terms of both heat-resistant storage stability and low-temperature fixability. The acid value of (C) is usually from 0.5 to 40, preferably from 5 to 35. By having an acid value, it tends to be negatively charged. Further, those having an acid value and a hydroxyl value exceeding these ranges are easily affected by the environment under high temperature and high humidity and low temperature and low humidity, and are liable to cause image deterioration.

In the present invention, the glass transition point (Tg) of the toner is usually 40 to 70 ° C., preferably 45 to 55 ° C. If it is less than 40 ° C., the heat-resistant storage stability of the toner deteriorates, and if it exceeds 70 ° C., the low-temperature fixability becomes insufficient. Due to the coexistence of the crosslinked and / or elongated polyester resin, the toner for developing an electrostatic charge image of the present invention exhibits good storage stability even when the glass transition point is low, as compared with known polyester-based toners. As the storage elastic modulus of the toner, the temperature (TG ′) at which the measurement frequency is 20 Hz is 10000 dyne / cm ² is usually 100 ° C. or higher, preferably 110 to 200 ° C. If it is less than 100 ° C., the resistance to hot offset deteriorates. As the viscosity of the toner, the temperature (Tη) at 1000 poise at a measurement frequency of 20 Hz is usually 180 ° C. or less, preferably 90 to 160 ° C. If it exceeds 180 ° C., the low-temperature fixability deteriorates. That is, from the viewpoint of achieving both low temperature fixability and hot offset resistance, TG ′ is preferably higher than Tη. In other words, the difference between TG ′ and Tη (TG′−Tη) is preferably 0 ° C. or higher. More preferably, it is 10 degreeC or more, Most preferably, it is 20 degreeC or more. The upper limit of the difference is not particularly limited. Further, from the viewpoint of achieving both heat-resistant storage stability and low-temperature fixability, the difference between Tη and Tg is preferably 0 to 100 ° C. More preferably, it is 10-90 degreeC, Most preferably, it is 20-80 degreeC.

(Coloring agent)
As the colorant of the present invention, known dyes and pigments can be used, such as carbon black, nigrosine dye, iron black, naphthol yellow S, Hansa yellow (10G, 5G, G), cadmium yellow, yellow iron oxide, Ocher, yellow lead, titanium yellow, polyazo yellow, oil yellow, Hansa yellow (GR, A, RN, R), pigment yellow L, benzidine yellow (G, GR), permanent yellow (NCG), Vulcan fast yellow (5G) , R), Tartrazine Lake, Quinoline Yellow Lake, Anthrazan Yellow BGL, Isoindolinone Yellow, Bengala, Red Dan, Lead Zhu, Cadmium Red, Cadmium Mercury Red, Antimon Zhu, Permanent Red 4R, Para Red, Fayce Red, Parachlor Ortoni Roaniline Red, Resol Fast Scarlet G, Brilliant Fast Scarlet, Brilliant Carmine B, Permanent Red (F2R, F4R, FRL, FRLL, F4RH), Fast Scarlet VD, Belkan Fast Rubin B, Brilliant Scarlet G, Resol Rubin GX, Permanent Red F5R, Brilliant Carmine 6B, Pigment Scarlet 3B, Bordeaux 5B, Toulouse Maroon, Permanent Bordeaux F2K, Helio Bordeaux BL, Bordeaux 10B, Bon Maroon Light, Bon Maroon Medium, Eosin Lake, Rhodamine Lake B, Rhodamine Lake Y, Alizarin Lake, Thioindigo red B, thioindigo maroon, oil red, quinacridone red, pyrazolone , Polyazo Red, Chrome Vermillion, Benzidine Orange, Perinone Orange, Oil Orange, Cobalt Blue, Cerulean Blue, Alkaline Blue Lake, Peacock Blue Lake, Victoria Blue Lake, Metal Free Phthalocyanine Blue, Phthalocyanine Blue, Fast Sky Blue, Indanthrene Blue (RS, BC), Indigo, Ultramarine Blue, Bitumen, Anthraquinone Blue, Fast Violet B, Methyl Violet Lake, Cobalt Purple, Manganese Purple, Dioxane Violet, Anthraquinone Violet, Chrome Green, Zinc Green, Chrome Oxide, Pyridian, Emerald Green, Pigment Green B, Naphthol Green B, Green Gold, Acid Green Lake, Malachite Green Lake, Fu Talocyanine green, anthraquinone green, titanium oxide, zinc white, litbon and mixtures thereof can be used. The content of the colorant is usually 1 to 15% by weight, preferably 3 to 10% by weight, based on the toner.

The colorant used in the present invention can also be used as a master batch combined with a resin.
As the binder resin to be kneaded together with the production of the master batch or the master batch, in addition to the modified and unmodified polyester resins mentioned above, styrene such as polystyrene, poly p-chlorostyrene, and polyvinyl toluene, and polymers of substituted products thereof; Styrene-p-chlorostyrene copolymer, styrene-propylene copolymer, styrene-vinyltoluene copolymer, styrene-vinylnaphthalene copolymer, styrene-methyl acrylate copolymer, styrene-ethyl acrylate copolymer Styrene-butyl acrylate copolymer, styrene-octyl acrylate copolymer, styrene-methyl methacrylate copolymer, styrene-ethyl methacrylate copolymer, styrene-butyl methacrylate copolymer, styrene-α- Chloromethyl methacrylate copolymer, Tylene-acrylonitrile copolymer, styrene-vinyl methyl ketone copolymer, styrene-butadiene copolymer, styrene-isoprene copolymer, styrene-acrylonitrile-indene copolymer, styrene-maleic acid copolymer, styrene-malein Styrene copolymers such as acid ester copolymers; polymethyl methacrylate, polybutyl methacrylate, polyvinyl chloride, polyvinyl acetate, polyethylene, polypropylene, polyester, epoxy resin, epoxy polyol resin, polyurethane, polyamide, polyvinyl butyral, poly Acrylic resin, rosin, modified rosin, terpene resin, aliphatic or alicyclic hydrocarbon resin, aromatic petroleum resin, chlorinated paraffin, paraffin wax, etc. The

  The master batch can be obtained by mixing and kneading a resin for a master batch and a colorant under a high shear force to obtain a master batch. In this case, an organic solvent can be used in order to enhance the interaction between the colorant and the resin. In addition, a so-called flushing method called watering paste containing water of colorant is mixed and kneaded with resin and organic solvent, and the colorant is transferred to the resin side to remove moisture and organic solvent components. Since it can be used as it is, it does not need to be dried and is preferably used. For mixing and kneading, a high shear dispersion device such as a three-roll mill is preferably used.

(Release agent)
Further, a wax can be contained together with the toner binder and the colorant. Known waxes can be used as the wax of the present invention, such as polyolefin wax (polyethylene wax, polypropylene wax, etc.); long chain hydrocarbon (paraffin wax, sasol wax, etc.); carbonyl group-containing wax, etc. It is done. Of these, carbonyl group-containing waxes are preferred. Carbonyl group-containing waxes include polyalkanoic acid esters (carnauba wax, montan wax, trimethylolpropane tribehenate, pentaerythritol tetrabehenate, pentaerythritol diacetate dibehenate, glycerin tribehenate, 1,18 -Octadecanediol distearate, etc.); polyalkanol esters (trimellitic acid tristearyl, distearyl maleate, etc.); polyalkanoic acid amides (ethylenediamine dibehenyl amide, etc.); polyalkylamides (trimellitic acid tristearyl amide, etc.) And dialkyl ketones (such as distearyl ketone). Among these carbonyl group-containing waxes, polyalkanoic acid esters are preferred. The melting point of the wax of the present invention is usually 40 to 160 ° C, preferably 50 to 120 ° C, more preferably 60 to 90 ° C. A wax having a melting point of less than 40 ° C. has an adverse effect on heat resistant storage stability, and a wax having a melting point of more than 160 ° C. tends to cause a cold offset when fixing at a low temperature. Further, the melt viscosity of the wax is preferably 5 to 1000 cps, more preferably 10 to 100 cps as a measured value at a temperature 20 ° C. higher than the melting point. Waxes exceeding 1000 cps have poor effects for improving hot offset resistance and low-temperature fixability. The content of the wax in the toner is usually 0 to 40% by weight, preferably 3 to 30% by weight.

(Charge control agent)
The toner of the present invention may contain a charge control agent as necessary. Known charge control agents can be used, such as nigrosine dyes, triphenylmethane dyes, chromium-containing metal complex dyes, molybdate chelate pigments, rhodamine dyes, alkoxy amines, quaternary ammonium salts (fluorine-modified 4 Secondary ammonium salts or compounds, tungsten simple substances or compounds, fluorine activators, salicylic acid metal salts, and metal salts of salicylic acid derivatives. Specifically, Nitronine-based dye Bontron 03, quaternary ammonium salt Bontron P-51, metal-containing azo dye Bontron S-34, oxynaphthoic acid metal complex E-82, salicylic acid metal complex E- 84, E-89 of a phenol-based condensate (manufactured by Orient Chemical Industry Co., Ltd.), TP-302 of a quaternary ammonium salt molybdenum complex, TP-415 (manufactured by Hodogaya Chemical Industry Co., Ltd.), quaternary ammonium Copy charge PSY VP2038 of salt, copy blue PR of triphenylmethane derivative, copy charge of quaternary ammonium salt NEG VP2036, copy charge NX VP434 (manufactured by Hoechst), LRA-901, LR-147 which is a boron complex (Nippon Carlit), copper phthalocyanine, perylene, quinacridone Azo pigments, sulfonate group, carboxyl group, and polymer compounds having a functional group such as a quaternary ammonium salt.

  In the present invention, the amount of charge control agent used is determined by the toner production method including the type of binder resin, the presence or absence of additives used as necessary, and the dispersion method, and is uniquely limited. However, it is preferably used in the range of 0.1 to 10 parts by weight with respect to 100 parts by weight of the binder resin. The range of 0.2 to 5 parts by weight is preferable. When the amount exceeds 10 parts by weight, the chargeability of the toner is too high, the effect of the main charge control agent is reduced, the electrostatic attractive force with the developing roller is increased, the flowability of the developer is reduced, and the image density is reduced. Incurs a decline. These charge control agents can be dissolved and dispersed after being melt-kneaded with a masterbatch and resin, and of course, they can be added directly when dissolved and dispersed in an organic solvent. May be.

(External additive)
As an external additive for assisting fluidity, developability and chargeability of the colored particles obtained in the present invention, in addition to oxide fine particles, inorganic fine particles and hydrophobized inorganic fine particles are used in combination as external additives. It is more desirable that the primary particles subjected to the hydrophobization treatment contain at least one kind of inorganic fine particles having an average particle diameter of 1 to 100 nm, more preferably 5 nm to 70 nm. Further, it is more preferable that the hydrophobized primary particles contain at least one kind of inorganic fine particles having an average particle diameter of 20 nm or less and at least one kind of inorganic fine particles of 30 nm or more. Moreover, it is preferable that the specific surface area by BET method is 20-500 m < ² > / g.

Any known one can be used as long as the conditions are satisfied. For example, silica fine particles, hydrophobic silica, fatty acid metal salts (such as zinc stearate and aluminum stearate), metal oxides (such as titania, alumina, tin oxide, and antimony oxide), fluoropolymers, and the like may be contained.
Particularly suitable additives include hydrophobized silica, titania, titanium oxide, and alumina fine particles. Examples of the silica fine particles include HDK H 2000, HDK H 2000/4, HDK H 2050EP, HVK21, HDK H 1303 (above Hoechst), and R972, R974, RX200, RY200, R202, R805, and R812 (above Nippon Aerosil). Further, as titania fine particles, P-25 (Nippon Aerosil), STT-30, STT-65C-S (above Titanium Industry), TAF-140 (Fuji Titanium Industry), MT-150W, MT-500B, MT-600B MT-150A (taker above). In particular, as hydrophobized titanium oxide fine particles, T-805 (Nippon Aerosil), STT-30A, STT-65S-S (above Titanium Industry), TAF-500T, TAF-1500T (above Fuji Titanium Industry), MT -100S, MT-100T (above Taka), IT-S (Ishihara Sangyo), etc.

  In order to obtain hydrophobized oxide fine particles, silica fine particles, titania fine particles, and alumina fine particles, hydrophilic fine particles are treated with a silane coupling agent such as methyltrimethoxysilane, methyltriethoxysilane, or octyltrimethoxysilane. Can be obtained. In addition, silicone oil-treated oxide fine particles and inorganic fine particles obtained by treating silicone oil with heat if necessary to treat it with inorganic fine particles are also suitable.

  Examples of the silicone oil include dimethyl silicone oil, methylphenyl silicone oil, chlorophenyl silicone oil, methyl hydrogen silicone oil, alkyl modified silicone oil, fluorine modified silicone oil, polyether modified silicone oil, alcohol modified silicone oil, amino modified silicone. Oil, epoxy-modified silicone oil, epoxy-polyether-modified silicone oil, phenol-modified silicone oil, carboxyl-modified silicone oil, mercapto-modified silicone oil, acrylic, methacryl-modified silicone oil, α-methylstyrene-modified silicone oil, and the like can be used. Examples of the inorganic fine particles include silica, alumina, titanium oxide, barium titanate, magnesium titanate, calcium titanate, strontium titanate, iron oxide, copper oxide, zinc oxide, tin oxide, quartz sand, clay, mica, and silica ash. Examples thereof include stone, diatomaceous earth, chromium oxide, cerium oxide, bengara, antimony trioxide, magnesium oxide, zirconium oxide, parium sulfate, barium carbonate, calcium carbonate, silicon carbide, and silicon nitride. Of these, silica and titanium dioxide are particularly preferred. The amount added may be 0.1 to 5% by weight, preferably 0.3 to 3% by weight, based on the toner. The average particle size of the primary particles of the inorganic fine particles is 100 nm or less, preferably 3 nm or more and 70 nm or less. If it is smaller than this range, the inorganic fine particles are buried in the toner, and the function is hardly exhibited effectively. On the other hand, if it is larger than this range, the surface of the photoreceptor is undesirably damaged.

In addition, polymer fine particles such as polystyrene obtained by soap-free emulsion polymerization, suspension polymerization and dispersion polymerization, methacrylic acid ester and acrylic acid ester copolymer, polycondensation system such as silicone, benzoguanamine and nylon, thermosetting resin And polymer particles.
Such a fluidizing agent can be surface-treated to increase hydrophobicity and prevent deterioration of flow characteristics and charging characteristics even under high humidity. For example, silane coupling agents, silylating agents, silane coupling agents having an alkyl fluoride group, organic titanate coupling agents, aluminum coupling agents, silicone oils, modified silicone oils and the like are preferable surface treatment agents. .

  Examples of the cleaning property improver for removing the developer after transfer remaining on the photoreceptor or the primary transfer medium include, for example, zinc stearate, calcium stearate, fatty acid metal salts such as stearic acid, such as polymethyl methacrylate fine particles, polystyrene fine particles, etc. And polymer fine particles produced by soap-free emulsion polymerization. The polymer fine particles preferably have a relatively narrow particle size distribution and a volume average particle size of 0.01 to 1 μm.

(Resin fine particles)
In the present invention, resin fine particles can be contained as required. The resin fine particles used have a glass transition point (Tg) of 40 to 100 ° C., a weight average molecular weight of 9000 to 200,000 is more preferable, and as described above, the glass transition point (Tg) is less than 40 ° C., and When the weight average molecular weight is less than 9,000, the storage stability of the toner is deteriorated, and blocking occurs during storage and in the developing machine. When the glass transition point (Tg) exceeds 100 ° C. and / or the weight average molecular weight exceeds 200,000, the resin fine particles inhibit the adhesiveness to the fixing paper, and the minimum fixing temperature increases.

  More preferably, the residual ratio with respect to the toner particles is 0.5 to 5.0 wt%. When the residual ratio is less than 0.5 wt%, the storability of the toner deteriorates, blocking occurs during storage and in the developing machine, and when the residual amount exceeds 5.0 wt%, the resin The fine particles inhibit the exudation of the wax, and the effect of releasing the wax cannot be obtained, and the occurrence of offset is observed.

The residual ratio of the resin fine particles can be measured by analyzing a substance caused by the resin fine particles, not by the toner particles, using a pyrolysis gas chromatograph mass spectrometer, and calculating from the peak area.
The detector is preferably a mass spectrometer, but is not particularly limited.

  The resin fine particles may be known resins as long as they can form an aqueous dispersion, and may be thermoplastic resins or thermosetting resins. For example, vinyl resins, polyurethane resins, epoxy resins, polyester resins, polyamide resins, Examples include polyimide resins, silicon resins, phenol resins, melamine resins, urea resins, aniline resins, ionomer resins, and polycarbonate resins. As the resin fine particles, two or more of the above resins may be used in combination. Of these, vinyl resins, polyurethane resins, epoxy resins, polyester resins, and combinations thereof are preferred because an aqueous dispersion of fine spherical resin particles is easily obtained.

  The vinyl resin is a polymer obtained by homopolymerization or copolymerization of a vinyl monomer, such as a styrene- (meth) acrylate resin, a styrene-butadiene copolymer, a (meth) acrylic acid-acrylate polymer, Examples include styrene-acrylonitrile copolymers, styrene-maleic anhydride copolymers, styrene- (meth) acrylic acid copolymers, and the like.

(Production method)
The toner binder can be produced by the following method. The polyol (1) and the polycarboxylic acid (2) are heated to 150 to 280 ° C. in the presence of a known esterification catalyst such as tetrabutoxytitanate or dibutyltin oxide, and the generated water is distilled off as necessary. Thus, a polyester having a hydroxyl group is obtained. Next, this is reacted with polyisocyanate (3) at 40 to 140 ° C. to obtain a prepolymer (A) having an isocyanate group.

The dry toner of the present invention can be produced by the following method, but is not limited thereto.
(Toner production method in aqueous medium)
The aqueous phase used in the present invention is used by adding resin fine particles in advance. The water used for the aqueous phase may be water alone, or a solvent miscible with water may be used in combination. Examples of the miscible solvent include alcohol (methanol, isopropanol, ethylene glycol, etc.), dimethylformamide, tetrahydrofuran, cellosolves (methyl cellosolve, etc.), lower ketones (acetone, methyl ethyl ketone, etc.), and the like.

  The toner particles are obtained by forming a dispersion composed of a polyester prepolymer (A) having an isocyanate group dissolved or dispersed in an organic solvent in an aqueous phase and reacting with amines (B). As a method for stably forming droplets of an organic solvent containing a dispersion composed of a polyester prepolymer (A) in an aqueous phase, the polyester prepolymer (A) dissolved or dispersed in an organic solvent in an aqueous phase may be used. And a method of adding a toner raw material composition to be dispersed by a shearing force. Polyester prepolymer (A) dissolved or dispersed in an organic solvent and other toner composition (hereinafter referred to as toner raw material), colorant masterbatch, release agent, charge control agent, unmodified The polyester resin or the like may be mixed when forming the dispersion in the aqueous phase, but after the toner raw material is mixed in advance and dissolved or dispersed in an organic solvent, the mixture is added to the aqueous phase and dispersed. Is more preferable. In the present invention, other toner raw materials such as a colorant, a release agent, and a charge control agent do not necessarily have to be mixed when forming particles in the aqueous phase. It may be added. For example, after forming particles containing no colorant, the colorant can be added by a known dyeing method.

  The dispersion method is not particularly limited, and known equipment such as a low-speed shear method, a high-speed shear method, a friction method, a high-pressure jet method, and an ultrasonic wave can be applied. In order to make the particle size of the dispersion 2 to 20 μm, a high-speed shearing type is preferable. When a high-speed shearing disperser is used, the rotational speed is not particularly limited, but is usually 1000 to 30000 rpm, preferably 5000 to 20000 rpm. The dispersion time is not particularly limited, but in the case of a batch method, it is usually 0.1 to 5 minutes. The temperature during dispersion is usually 0 to 150 ° C. (under pressure), preferably 40 to 98 ° C. Higher temperatures are preferred in that the dispersion of the polyester prepolymer (A) has a low viscosity and is easy to disperse.

  The amount of the aqueous phase used is usually 50 to 2000 parts by weight, preferably 100 to 1000 parts by weight, based on 100 parts of the toner composition containing the polyester prepolymer (A). If the amount is less than 50 parts by weight, the dispersion state of the toner composition is poor, and toner particles having a predetermined particle diameter cannot be obtained. If it exceeds 20000 parts by weight, it is not economical. Moreover, a dispersing agent can also be used as needed. It is preferable to use a dispersant because the particle size distribution becomes sharp and the dispersion is stable.

  Anionic surfactants such as alkylbenzene sulfonates, α-olefin sulfonates, phosphate esters, alkylamine salts, amino acids as dispersants for emulsifying and dispersing the oily phase in which the toner composition is dispersed in the aqueous phase Alcohol fatty acid derivatives, polyamine fatty acid derivatives, amine salt types such as imidazoline, quaternary ammonium such as alkyltrimethylammonium salt, dialkyldimethylammonium salt, alkyldimethylbenzylammonium salt, pyridinium salt, alkylisoquinolinium salt, benzethonium chloride Nonionic surfactants such as salt-type cationic surfactants, fatty acid amide derivatives, polyhydric alcohol derivatives, such as alanine, dodecyldi (aminoethyl) glycine, di (octylaminoethyl) glycine and N-alkyl-N, N − Amphoteric surfactants such as ammonium betaine.

Further, by using a surfactant having a fluoroalkyl group, the effect can be obtained in a very small amount. Preferred anionic surfactants having a fluoroalkyl group include fluoroalkyl carboxylic acids having 2 to 10 carbon atoms and metal salts thereof, disodium perfluorooctanesulfonyl glutamate, 3- [omega-fluoroalkyl (C6-C11 ) Oxy] -1-alkyl (C3-C4) sodium sulfonate, 3- [omega-fluoroalkanoyl (C6-C8) -N-ethylamino] -1-propanesulfonic acid sodium, fluoroalkyl (C11-C20) carvone Acids and metal salts, perfluoroalkylcarboxylic acids (C7 to C13) and metal salts thereof, perfluoroalkyl (C4 to C12) sulfonic acids and metal salts thereof, perfluorooctanesulfonic acid diethanolamide, N-propyl-N- ( 2-hydroxyethyl) -Fluorooctanesulfonamide, perfluoroalkyl (C6-C10) sulfonamidopropyltrimethylammonium salt, perfluoroalkyl (C6-C10) -N-ethylsulfonylglycine salt, monoperfluoroalkyl (C6-C16) ethyl phosphate, etc. Is mentioned.
Product names include Surflon S-111, S-112, S-113 (Asahi Glass Co., Ltd.), Florard FC-93, FC-95, FC-98, FC-129 (Sumitomo 3M Co., Ltd.), Unidyne DS-101. DS-102 (Daikin Kogyo Co., Ltd.), Mega-Fac F-l0, F-l20, F-113, F-191, F-812, F-833 (Dainippon Ink Co., Ltd.), Xtop EF-102 , 103, 104, 105, 112, 123A, 123B, 306A, 501, 201, 204 (manufactured by Tochem Products), and Fagento F-100, F150 (manufactured by Neos).

  In addition, as the cationic surfactant, aliphatic quaternary ammonium salts such as aliphatic primary, secondary or secondary amic acid, perfluoroalkyl (C 6 -C 10) sulfonamidopropyltrimethylammonium salt which right the fluoroalkyl group, Benzalkonium salt, benzethonium chloride, pyridinium salt, imidazolinium salt, trade names include Surflon S-121 (Asahi Glass), Florard FC-135 (Sumitomo 3M), Unidyne DS-202 (Daikin Industries) ), Megafuck F-150, F-824 (Dainippon Ink Co., Ltd.), Xtop EF-132 (Tochem Products Co., Ltd.), Footgent F-300 (Neos Co., Ltd.) and the like.

  Further, tricalcium phosphate, calcium carbonate, titanium oxide, colloidal silica, hydroxyapatite and the like can be used as an inorganic compound dispersant that is hardly soluble in water.

  Further, the dispersed droplets may be stabilized by a polymer protective colloid. For example, acrylic acid, methacrylic acid, α-cyanoacrylic acid, α-cyanomethacrylic acid, itaconic acid, crotonic acid, fumaric acid, maleic acid or maleic anhydride and other (meth) acrylic monomers containing hydroxyl groups Bodies such as β-hydroxyethyl acrylate, β-hydroxyethyl methacrylate, β-hydroxypropyl acrylate, β-hydroxypropyl methacrylate, γ-hydroxypropyl acrylate, γ-hydroxypropyl methacrylate, 3-acrylate Chloro-2-hydroxypropyl, 3-chloro-2-hydroxypropyl methacrylate, diethylene glycol monoacrylate, diethylene glycol monomethacrylate, glycerol monoacrylate, glycerol monomethacrylate, N -Methylol acrylamide, N-methylol methacrylamide, etc., vinyl alcohol or ethers with vinyl alcohol, such as vinyl methyl ether, vinyl ethyl ether, vinyl propyl ether, etc., or esters of compounds containing vinyl alcohol and carboxyl groups, such as Pinyl acetate, pinyl propionate, vinyl butyrate, etc., acrylamide, methacrylamide, diacetone acrylamide or their methylol compounds, acid chlorides such as acrylic acid chloride, methacrylic acid chloride, pinyl pyridine, vinyl pyrrolidone, vinyl imidazole, ethylene imine, etc. Homopolymers or copolymers such as those having nitrogen atoms or heterocyclic rings thereof, polyoxyethylene, polyoxypropylene, polymers Oxyethylene alkylamine, polyoxypropylene alkylamine, polyoxyethylene alkylamide, polyoxypropylene alkylamide, polyoxyethylene nonyl phenyl ether, polyoxyethylene lauryl phenyl ether, polyoxyethylene stearyl phenyl ester, polyoxyethylene nonylphenyl Polyoxyethylenes such as esters, celluloses such as methyl cellulose, hydroxyethyl cellulose, and hydroxypropyl cellulose can be used.

  In addition, when an acid such as calcium phosphate salt or an alkali-soluble one is used as the dispersion stabilizer, the calcium phosphate salt is removed from the fine particles by a method such as washing with water after dissolving the calcium phosphate salt with an acid such as hydrochloric acid. To do. It can also be removed by operations such as enzymatic degradation.

When a dispersant is used, the dispersant may remain on the surface of the toner particles, but it is preferable from the charged surface of the toner that the dispersant is washed and removed after the elongation and / or crosslinking reaction.
The elongation and / or cross-linking reaction time is selected depending on the reactivity of the isocyanate group structure of the prepolymer (A) and the amines (B), but is usually 10 minutes to 40 hours, preferably 2 to 24 hours. is there. The reaction temperature is generally 0 to 150 ° C, preferably 40 to 98 ° C. Moreover, a well-known catalyst can be used as needed. Specific examples include dibutyltin laurate and dioctyltin laurate.

  In order to remove the organic solvent from the obtained emulsified dispersion, a method in which the temperature of the entire system is gradually raised to completely evaporate and remove the organic solvent in the droplets can be employed. Alternatively, the emulsified dispersion can be sprayed into a dry atmosphere to completely remove the water-insoluble organic solvent in the droplets to form toner fine particles, and the aqueous dispersant can be removed by evaporation together. . As a dry atmosphere in which the emulsified dispersion is sprayed, a gas obtained by heating air, nitrogen, carbon dioxide gas, combustion gas, or the like, in particular, various air currents heated to a temperature equal to or higher than the boiling point of the highest boiling solvent used is generally used. Sufficient quality can be obtained by short-time treatment such as spray dryer, belt dryer, rotary kiln.

Further, as a method of removing the organic solvent, air can be blown away by a rotary evaporator or the like.
Thereafter, rough separation is performed by centrifugation, the emulsified dispersion is washed in a washing tank, and the drying process is repeated in a hot air dryer, and the solvent is removed and dried to obtain a toner base.
Thereafter, a ripening step is further performed, so that the hollow state inside the toner can be controlled, which is more preferable. It is preferably 30 to 55 ° C. (more preferably 40 to 50 ° C.), and more preferably aging for 5 to 36 hours (more preferably 10 to 24 hours).

When the particle size distribution at the time of emulsification dispersion is wide and washing and drying processes are performed while maintaining the particle size distribution, the particle size distribution can be adjusted by classification into a desired particle size distribution.
In the classification operation, the fine particle portion can be removed in the liquid by a cyclone, a decanter, centrifugation, or the like. Of course, the classification operation may be performed after obtaining the powder after drying, but it is preferably performed in a liquid from the viewpoint of efficiency. The unnecessary fine particles or coarse particles obtained can be returned to the kneading step and used for the formation of particles. At that time, fine particles or coarse particles may be wet.
The dispersant used is preferably removed from the obtained dispersion as much as possible, but it is preferable to carry out it simultaneously with the classification operation described above.
Mixing or giving mechanical impact force to the powder mixture after drying with different types of particles such as fine particles of release agent, charge control fine particles, fluidizing agent fine particles, and colorant fine particles By immobilizing and fusing on the surface, it is possible to prevent the dissociation of foreign particles from the surface of the resulting composite particle.
Specific means include a method of applying an impact force to the mixture by blades rotating at high speed, a method of injecting and accelerating the mixture in a high-speed air stream, and causing particles or composite particles to collide with an appropriate collision plate, etc. is there. As equipment, Ong mill (manufactured by Hosokawa Micron Co., Ltd.), I-type mill (manufactured by Nippon Pneumatic Co., Ltd.) has been modified to reduce the pulverization air pressure, hybridization system (manufactured by Nara Machinery Co., Ltd.), kryptron Examples include a system (manufactured by Kawasaki Heavy Industries, Ltd.) and an automatic mortar.
Finally, an external additive such as inorganic fine particles and a toner are mixed with a Henschel mixer or the like, and coarse particles are removed with an ultrasonic sieve or the like to obtain a final toner.

EXAMPLES Hereinafter, although an Example demonstrates this invention further, this invention is not limited to this.
In addition, "part" in an Example shows a weight part.

Example 1
(Manufacture of toner)
・ Synthetic production example 1 of organic fine particle emulsion
In a reaction vessel equipped with a stirrer and a thermometer, water 683 parts, sodium salt of ethylene oxide methacrylate adduct sulfate (Eleminol RS-30, manufactured by Sanyo Chemical Industries), 166 parts of methacrylic acid, butyl acrylate 110 And 1 part of ammonium persulfate were added and stirred at 3800 rpm for 30 minutes to obtain a white emulsion. The system was heated to raise the system temperature to 75 ° C. and reacted for 4 hours. Further, 30 parts of a 1% ammonium persulfate aqueous solution was added, and the mixture was aged at 75 ° C. for 6 hours, and an aqueous dispersion of vinyl resin (methacrylic acid-butyl acrylate-methacrylic acid ethylene oxide adduct sulfate sodium salt copolymer). [Fine particle dispersion 1] was obtained. The volume average particle diameter of [fine particle dispersion 1] measured by LA-920 was 110 nm. A portion of [Fine Particle Dispersion 1] was dried to isolate the resin component. The Tg of the resin was 58 ° C., and the weight average molecular weight was 130,000.

・ Aqueous phase adjustment production example 2
990 parts of water, 83 parts of [fine particle dispersion 1], 37 parts of a 48.3% aqueous solution of dodecyl diphenyl ether disulfonate (Eleminol MON-7: manufactured by Sanyo Chemical Industries) and 90 parts of ethyl acetate are mixed and stirred. A milky white liquid was obtained. This is designated as [Aqueous Phase 1].

・ Synthetic production example 3 of low molecular weight polyester
In a reaction vessel equipped with a condenser, a stirrer and a nitrogen inlet tube, 229 parts of bisphenol A ethylene oxide 2-mole adduct, 529 parts of bisphenol A propylene oxide 3-mole adduct, 208 parts terephthalic acid, 46 parts adipic acid and dibutyl Add 2 parts of tin oxide, react at 230 ° C. for 11 hours at normal pressure, and further react for 5 hours under reduced pressure of 10-15 mmHg, then add 44 parts of trimellitic anhydride into the reaction vessel, and at 180 ° C. at normal pressure. By reacting for 4 hours, [low molecular weight polyester 1] was obtained. [Low molecular polyester 1] had a number average molecular weight of 7,800, a weight average molecular weight of 16,500, a Tg of 46 ° C., and an acid value of 25.

Synthetic production example 4 of intermediate polyester
In a reaction vessel equipped with a cooling pipe, a stirrer and a nitrogen introduction pipe, 682 parts of bisphenol A ethylene oxide 2-mole adduct, 81 parts of bisphenol A propylene oxide 2-mole adduct, 283 parts of terephthalic acid, trimellitic anhydride 22 And 2 parts of dibutyltin oxide were added, reacted at 230 ° C. for 8 hours at normal pressure, and further reacted for 5 hours at a reduced pressure of 10 to 15 mmHg to obtain [Intermediate Polyester 1]. [Intermediate Polyester 1] had a number average molecular weight of 3200, a weight average molecular weight of 10300, Tg of 54 ° C., an acid value of 0.5, and a hydroxyl value of 52.
Next, 410 parts of [Intermediate polyester 1], 89 parts of isophorone diisocyanate, and 500 parts of ethyl acetate are placed in a reaction vessel equipped with a cooling pipe, a stirrer and a nitrogen introduction pipe, and reacted at 100 ° C. for 5 hours. Polymer 1] was obtained. [Prepolymer 1] had a free isocyanate weight% of 1.53%.

・ Synthetic production example 5 of ketimine
In a reaction vessel equipped with a stir bar and a thermometer, 170 parts of isophoronediamine and 75 parts of methyl ethyl ketone were charged and reacted at 50 ° C. for 4 hours and half to obtain [ketimine compound 1]. The amine value of [ketimine compound 1] was 417.

・ Synthetic production example 6 of master batch (MB)
Add 1200 parts of water, 540 parts of carbon black (Printex35, manufactured by Dexa) [DBP oil absorption = 42 ml / 100 mg, pH = 9.5], 1200 parts of polyester resin, and mix with a Henschel mixer (made by Mitsui Mining Co., Ltd.). Was kneaded for 1 hour at 110 ° C. using two rolls, rolled and cooled, and pulverized with a pulverizer to obtain [Masterbatch 1].

・ Production Example 7 of Oil Phase Production
In a container equipped with a stir bar and a thermometer, 378 parts of [Low molecular weight polyester 1], 110 parts of Carnauba WAX, and 947 parts of ethyl acetate were charged, heated to 80 ° C. with stirring, and kept at 80 ° C. for 5 hours. It was cooled to 30 ° C at 1 hour. Next, 500 parts of [Masterbatch 1] and 500 parts of ethyl acetate were placed in a container and mixed for 1 hour to obtain [Raw material solution 1].
[Raw material solution 1] 1324 parts are transferred to a container, and using a bead mill (Ultra Visco Mill, manufactured by Imex Co., Ltd.), a liquid feeding speed of 1 kg / hr, a disk peripheral speed of 6 m / sec, and 0.5 mm zirconia beads are 80 vol% Carbon black and WAX were dispersed under conditions of filling and 3 passes. Next, 1324 parts of a 65% ethyl acetate solution of [low molecular weight polyester 1] was added, and the bead mill under the above conditions was passed twice to obtain [Pigment / WAX Dispersion 1]. The solid content concentration of [Pigment / WAX Dispersion 1] (130 ° C., 30 minutes) was 50%.

・ Emulsification⇒ Solvent removal production example 8
[Pigment / WAX Dispersion 1] 749 parts, [Prepolymer 1] 115 parts, [Ketimine Compound 1] 2.9 parts in a container and TK homomixer (manufactured by Tokushu Kika) at 5,000 rpm for 2 minutes After mixing, 1200 parts of [Aqueous phase 1] was added to the container, and mixed with a TK homomixer at 13,000 rpm for 25 minutes to obtain [Emulsion slurry 1].
[Emulsion slurry 1] was put into a container equipped with a stirrer and a thermometer, and after removing the solvent at 30 ° C. for 8 hours, aging was carried out at 40 ° C. for 24 hours to obtain [Dispersion slurry 1].

・ Washing⇒Drying production example 9
[Dispersion Slurry 1] After filtering 100 parts under reduced pressure,
(1): 100 parts of ion-exchanged water was added to the filter cake, mixed with a TK homomixer (rotation speed: 12,000 rpm for 10 minutes), and then filtered.
(2): 100 parts of a 10% aqueous sodium hydroxide solution was added to the filter cake of (1), mixed with a TK homomixer (30 minutes at 12,000 rpm), and then filtered under reduced pressure.
(3): 100 parts of 10% hydrochloric acid was added to the filter cake of (2), mixed with a TK homomixer (rotation speed: 12,000 rpm for 10 minutes), and then filtered.
(4): Add 300 parts of ion-exchanged water to the filter cake of (3), mix with a TK homomixer (10 minutes at 12,000 rpm) and then filter twice to obtain [Filter cake 1]. It was.
[Filter cake 1] was dried at 45 ° C. for 48 hours in a circulating dryer. Thereafter, sieved with a mesh of 75 μm, [Toner Base Particle 1] was obtained.
Thereafter, 100 parts of [toner base particle 1] and 1 part of hydrophobized silica were mixed with a Henschel mixer to obtain a toner.
The obtained toner was measured under the measurement conditions shown in Table 1, and the obtained evaluation results are also shown in Table 1.

Comparative Examples 1-8
In Example 1, evaluation was performed in the same manner as in Example 1 except that measurement conditions were measured under the conditions shown in Table 1. The evaluation results obtained are also shown in Table 1.

Comparative Example 9
Measurement and evaluation were performed in the same manner except that the solvent used in Example 1 was changed to THF (tetrahydrofuran). In the case of THF, since the salt effect cannot be expected, sodium trifluoroacetate was not contained in the solvent. The evaluation results obtained are shown in Table 1.

Comparative Example 10
Measurement and evaluation were conducted in the same manner except that the solvent used in Example 1 was changed to o-dichlorobenzene. In the case of o-dichlorobenzene, since a salt effect cannot be expected, sodium trifluoroacetate was not contained in the solvent. The evaluation results obtained are shown in Table 1.

(Evaluation item)
1) Soluble toner is dissolved in excess of each eluent with ultrasonic waves for 5 minutes. When the solubility is 0 or more and less than 50 wt% x, when 50 wt% or more and less than 80 wt%, Δ, when 80 wt% or more and less than 100 wt% ○.
2) Peak separability Using the PMMA standard polymers having molecular weights of 34500 and 15100, the separability of peaks of each molecular weight was evaluated. Each peak can be separated sufficiently and left symmetrical and good without tailing the peak end ◎, but the left and right symmetry is slightly worse, but each peak can be separated sufficiently and the peak end tailed A good sample was marked with ◯, a sample with insufficient separation of each peak was marked with Δ, and a sample with no peak separation was marked with ×.
3) Detection sensitivity The S / N (signal-to-noise ratio) of the GPC chromatogram was 500 or more, and the detection sensitivity was sufficient.

Claims (1)

And at least a colorant, a toner measuring method for measuring the molecular weight distribution of the resin component of the polyester prepolymer with an amine resin and a in including toners containing modified polyester obtained by reacting the containing isocyanate groups the measuring method is to evaluate the dissolved components of HFIP (hexafluoroisopropanol), a Dressings containing measuring the molecular weight distribution of the resin component of the crosslinked form, the HFIP is trifluoroacetic acid in 5~20mM An eluent in which sodium is dissolved, and the toner is dissolved in the HFIP eluent by sonication to a concentration of 0.5 to 5 mg / ml for 1 to 7 minutes. Toner characterized by including each step of filtering through a 0.65 μm filter and analyzing the resulting solution by GPC method Measurement method.