JP2006119617A - Toner, method for manufacturing it, and image forming method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide toner superior in electrification performance and low-temperature fixability and capable of obtaining a high-quality image, a method for efficiently manufacturing the toner, an image forming method capable of improving the image quality employing the toner, and so forth. <P>SOLUTION: The toner includes a polyester resin which has a total organic carbon elution amount of ≤200 ppm/g (TOC amount) extracted from the toner after alkali-washing. The method for manufacturing the toner includes a toner granulation step for granulating the toner and a toner washing step for performing the alkali-washing until the total organic carbon elution amount (TOC amount) extracted from the toner after the alkali-washing amounts to ≤200 ppm/g. The image forming method or the like employs the toner. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a toner suitably used in an electrophotographic method, an electrostatic recording method, an electrostatic printing method, and the like, a manufacturing method thereof, a developer using the toner, a container containing a toner, a process cartridge, an image forming apparatus, and The present invention relates to an image forming method.

  Conventionally, in electrophotographic methods, electrostatic recording methods, electrostatic printing methods, etc., dry toners obtained by melt-kneading and pulverizing a toner binder such as a styrene resin, an acrylic resin, and a polyester resin, and a colorant are used. It is used.

  However, in recent years, there has been a strong demand for higher quality, higher image quality, lower temperature fixability, and the like, and conventional pulverized toners cannot meet these requirements. In other words, the pulverized and classified toner has a limit in the refinement of the toner and the yield of pulverization, and there is a problem that it is not possible to efficiently produce a toner having a small particle size, a sharp particle size distribution, and high image quality. there were.

  Therefore, in recent years, development of CP toner (CHEMICAL PREPARED TONER) has been actively performed. As the CP toner, for example, a polymerization toner produced by a suspension polymerization method, an emulsion polymerization aggregation method, a seed polymerization method, a dispersion polymerization method or the like using a vinyl monomer or the like, a polyester prepolymer, or the like is used. Extension toners produced by an extension reaction (see Patent Document 1) and the like have been proposed. Among these, extension toners are particularly excellent in that polyester resins that are advantageous for improving low-temperature fixability are used. .

  However, in the production process of the above-described extension toner, an oil phase obtained by dissolving or dispersing a toner material such as a polyester prepolymer, a release agent, and a colorant in an organic solvent is used together with a surfactant and resin fine particles. Therefore, the resin fine particles are present on the surface of the toner particles to be formed, and further, surfactants, ionic impurities, etc. adhere to the toner particles and the resin fine particles. Thus, when impurities adhere to the surface of toner particles or the like, there is a problem that the charging performance of the toner is lowered and the environmental resistance is greatly adversely affected. For this reason, it is indispensable to wash the toner particles and remove the deposits in order to suppress a decrease in the charging performance.

As a method for cleaning the toner particles, for example, a method has been proposed in which an emulsion aggregation toner is cleaned using an alkaline aqueous solution, an acid aqueous solution, and water in this order (see, for example, Patent Document 2).
However, even when this cleaning method is used for the extension toner, there is a problem that sufficient charging performance cannot be ensured by simply removing ionic impurities and surfactants.

  Therefore, a toner that has excellent charging performance, excellent environmental stability, excellent low-temperature fixability, high image quality, and a method for producing the same, and related technology using the toner have not yet been provided. Currently.

JP 2002-296839 A JP 2001-175028 A

  An object of the present invention is to solve various problems in the prior art and achieve the following objects. That is, the present invention provides a toner that has excellent charging performance, good environmental stability, excellent low-temperature fixability, high image quality, and an efficient manufacturing method thereof, and can improve image quality using the toner. An object is to provide a developer, a container containing toner, a process cartridge, an image forming apparatus, and an image forming method.

As a result of intensive studies, the present inventors have obtained the following knowledge. That is, the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner after the alkali cleaning of the toner containing the polyester resin is set to 200 ppm / g or less. The inventors have found that a toner having excellent charging performance, good environmental stability, excellent low-temperature fixability, and high image quality can be obtained.
Further, the inventors have found that the charging performance is particularly excellent by controlling the conditions such as pH, temperature, and time during the alkali cleaning, and have completed the present invention.

前記一般式（１）中、ｎ及びｍは、繰返単位数を表し、Ｌは１〜３の整数を表し、Ｒ^１及びＲ^２は、互いに同一であってもよいし、異なっていてもよく、水素原子又は炭化水素基を表す。
＜１３＞ 結晶性ポリエステル樹脂が、その赤外吸収スペクトルにおいて９６５±１０ｃｍ^−１及び９９０±１０ｃｍ^−１の少なくともいずれかにオレフィンのδＣＨ（面外変角振動）に基づく吸収を有する前記＜３＞から＜１２＞のいずれかに記載のトナーである。
＜１４＞ 結晶性ポリエステル樹脂が、炭素数２〜６のジオール化合物及びフマル酸化合物をモノマーユニットとして有する前記＜３＞から＜１３＞のいずれかに記載のトナーである。
＜１５＞ 炭素数２〜６のジオール化合物が、１，４−ブタンジオール、１，６−ヘキサンジオール及びこれらの誘導体から選択される前記＜１４＞に記載のトナーである。
＜１６＞ 樹脂微粒子の少なくとも１種のガラス転移温度が２０〜１００℃である前記＜４＞から＜１５＞のいずれかに記載のトナーである。
＜１７＞ 樹脂微粒子の重量平均分子量（Ｍｗ）が、８，０００〜２００，０００である前記＜４＞から＜１６＞のいずれかに記載のトナーである。
＜１８＞ 樹脂微粒子の体積平均粒径が、２０〜２００ｎｍである前記＜４＞から＜１７＞のいずれかに記載のトナーである。
＜１９＞ 樹脂微粒子のトナーに対する残存量が、熱分解クロマトグラフによる測定値で、０．５〜５．０質量％である前記＜４＞から＜１８＞のいずれかに記載のトナーである。 The present invention is based on the above findings of the present inventors, and means for solving the above problems are as follows. That is,
<1> A polyester resin is contained, and the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner after alkali washing is 200 ppm / g or less. Toner.
<2> In the above <1> obtained by reacting an active hydrogen group-containing compound and a polymer capable of reacting with the active hydrogen group-containing compound in an aqueous medium to produce particles containing at least an adhesive substrate The toner is described.
<3> The toner according to any one of <1> to <2>, including a crystalline polyester resin.
<4> The toner according to any one of <1> to <3>, including resin fine particles.
<5> The toner according to <4>, wherein the resin fine particles are at least one selected from a vinyl resin, a polyurethane resin, an epoxy resin, and a polyester resin.
<6> The toner according to any one of <1> to <5>, wherein the acid value of the polyester resin is 5 to 50 mgKOH / g.
<7> The toner according to any one of <1> to <6>, wherein the pH of the cleaning liquid after alkali cleaning is 6.0 to 11.0.
<8> The toner according to any one of <1> to <7>, wherein the conductivity of the cleaning liquid after solid-liquid separation and water cleaning is 0.5 to 60 μS / cm after alkali cleaning.
<9> The toner according to any one of <1> to <8>, wherein a hydrogen atom of a terminal carboxyl group in the polyester resin is substituted with a Na atom.
<10> The toner according to any one of <3> to <9>, wherein the crystalline polyester resin has a DSC endothermic peak temperature of 50 to 150 ° C.
<11> The molecular weight distribution by GPC of the ortho-dichlorobenzene soluble part of the crystalline polyester resin is 1,000 to 30,000 in terms of weight average molecular weight (Mw), and 500 to 6,000 in terms of number average molecular weight (Mn). The toner according to any one of <3> to <10>, wherein (Mw / Mn) is 2 to 8.
<12> The toner according to any one of <3> to <11>, wherein the crystalline polyester resin is represented by the following general formula (1).

In the general formula (1), n and m represent the number of repeating units, L represents an integer of 1 to 3, and R ¹ and R ² may be the same as or different from each other. Often represents a hydrogen atom or a hydrocarbon group.
<13> The crystalline polyester resin is, having an absorption based on the infrared absorption spectrum at 965 ± 10 cm ^-1 and 990 of at least olefin to any of ± 10cm ^-1 δCH (out-of-plane bending vibration) <3> To <12>.
<14> The toner according to any one of <3> to <13>, wherein the crystalline polyester resin has a diol compound having 2 to 6 carbon atoms and a fumaric acid compound as monomer units.
<15> The toner according to <14>, wherein the diol compound having 2 to 6 carbon atoms is selected from 1,4-butanediol, 1,6-hexanediol, and derivatives thereof.
<16> The toner according to any one of <4> to <15>, wherein the resin fine particles have a glass transition temperature of 20 to 100 ° C.
<17> The toner according to any one of <4> to <16>, wherein the resin fine particles have a weight average molecular weight (Mw) of 8,000 to 200,000.
<18> The toner according to any one of <4> to <17>, wherein the resin fine particles have a volume average particle diameter of 20 to 200 nm.
<19> The toner according to any one of <4> to <18>, wherein the residual amount of the resin fine particles with respect to the toner is 0.5 to 5.0% by mass as measured by pyrolysis chromatography.

<20> a toner granulating step for granulating a toner containing a polyester resin;
A toner cleaning step of at least alkali cleaning the granulated toner until the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner is 200 ppm / g or less. A method for producing a toner.
<21> The method for producing a toner according to <20>, wherein the pH of the cleaning liquid after alkali cleaning is 6.0 to 11.0.
<22> The method for producing a toner according to any one of <20> to <21>, wherein the conductivity of the cleaning liquid after solid-liquid separation and water cleaning is 0.5 to 60 μS / cm after alkali cleaning. is there.
<23> The method for producing a toner according to any one of <20> to <22>, wherein the alkali cleaning solution is a sodium hydroxide aqueous solution.
<24> The method for producing a toner according to any one of <20> to <23>, wherein the granulated toner is washed with an alkali, then with water, with an acid, and with water.
<25> The method for producing a toner according to any one of <20> to <23>, wherein the granulated toner is washed with water, washed with water, washed with acid, washed with water, washed with alkali, and washed with water. It is.
<26> The method for producing a toner according to <25>, wherein a hydrogen atom of a terminal carboxyl group in the polyester resin is substituted with a Na atom.
<27> The method for producing a toner according to any one of <20> to <26>, wherein the temperature during alkali cleaning is 10 to 70 ° C.
<28> Any of the above <20> to <27>, wherein the temperature T (° C.) during alkali cleaning is (Tg−10) ≦ T ≦ (Tg + 10), where Tg (° C.) is the glass transition temperature of the toner. A method for producing the toner according to claim 1.
<29> The method for producing a toner according to any one of <20> to <28>, wherein the alkali cleaning time is 1 to 72 hours.
<30> The method for producing a toner according to any one of <24> to <29>, wherein the cleaning solution for the acid cleaning is at least one of a hydrochloric acid aqueous solution and a nitric acid aqueous solution.
<31> The toner granulation step emulsifies or disperses an active hydrogen group-containing compound and a polymer capable of reacting with the active hydrogen group-containing compound in an aqueous medium, and reacts to produce an adhesive substrate. The method for producing a toner according to any one of <20> to <30>, wherein the toner is a step of obtaining particles containing at least the adhesive substrate.

<32> A developer comprising the toner according to any one of <1> to <19>.
<33> A toner-containing container filled with the toner according to any one of <1> to <19>.
<34> An electrostatic latent image carrier and an electrostatic latent image formed on the electrostatic latent image carrier are developed using the toner according to any one of <1> to <19> to be a visible image And a developing means for forming a process cartridge.
<35> an electrostatic latent image carrier, electrostatic latent image forming means for forming an electrostatic latent image on the electrostatic latent image carrier, and the electrostatic latent image of <1> to <19> Developing means for developing a visible image by developing using any of the toners, Transfer means for transferring the visible image to a recording medium, Fixing means for fixing the transferred image transferred to the recording medium, The image forming apparatus is characterized by having at least.
<36> An electrostatic latent image forming step of forming an electrostatic latent image on the electrostatic latent image carrier, and the electrostatic latent image using the toner according to any one of <1> to <19> An image comprising at least a developing step for developing to form a visible image, a transferring step for transferring the visible image to a recording medium, and a fixing step for fixing the transferred image transferred to the recording medium It is a forming method.

The toner of the present invention contains a polyester resin, and the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner after alkali washing is 200 ppm / g or less. In the toner, the alkali cleaning removes emulsifiers, dispersants, ionic impurities, and the like present on the surface of the toner particles. The total organic carbon elution amount extracted from the toner after the last alkali cleaning is controlled to a certain amount or less. In particular, when the polyester resin having a high acid value is used in order to improve pigment dispersibility, fixability, chargeability, etc., a relatively large amount of residual acid monomer remains, but the residual acid monomer can also be removed. For this reason, the toner has excellent charging performance, good environmental stability, excellent low-temperature fixability, and high image quality.
Further, when the toner contains resin fine particles, the resin fine particles contain a large amount of acidic groups and are present on the surface of the toner, which may cause charging inhibition or fixing inhibition under high humidity. Thus, the resin fine particles can be appropriately removed while securing the charging performance. Further, when the toner contains particles containing at least an adhesive substrate obtained by reacting the active hydrogen group-containing compound with a polymer capable of reacting, the aggregation resistance, charging property, fluidity, transferability, Excellent properties such as fixability. When image formation is performed using the toner, high image quality can be obtained under low-temperature fixing conditions.
In the toner of the present invention, the resin fine particles are at least one selected from vinyl resin, polyurethane resin, epoxy resin and polyester resin, and the acid value of the polyester resin is 5 to 50 mgKOH / g. Aspect, Aspect in which pH of cleaning liquid after alkali cleaning is 6.0 to 11.0, Aspect in which conductivity of cleaning liquid after solid-liquid separation and water cleaning after alkali cleaning is 0.5-60 μS / cm Are preferable.

The toner production method of the present invention includes a toner granulation step of granulating a toner containing a polyester resin,
A toner cleaning step of at least alkali cleaning the granulated toner until the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner is 200 ppm / g or less. In the toner production method of the present invention, the toner containing the polyester resin is granulated in the toner granulation step. In the toner washing step, the toner granulated in the toner granulation step until the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner becomes 200 ppm / g or less. , At least washed with alkali. The alkali cleaning removes emulsifiers, dispersants, ionic impurities, etc. present on the surface of the toner particles. Further, in order to improve pigment dispersibility, fixability, chargeability, etc., in the toner granulation step, when the polyester resin having a particularly high acid value is used, a relatively large amount of residual acid monomer remains. The residual acid monomer can also be removed. For this reason, the toner has excellent charging performance, good environmental stability, excellent low-temperature fixability, and high image quality.
Further, when the toner contains resin fine particles, the resin fine particles contain a large amount of acidic groups and are present on the surface of the toner, which may cause charging inhibition or fixing inhibition under high humidity. Thus, the resin fine particles can be appropriately removed while securing the charging performance. As a result, the toner of the present invention, which has excellent charging performance, excellent environmental stability, excellent low-temperature fixability, and high image quality, can be produced efficiently. Further, the toner granulation step emulsifies or disperses an active hydrogen group-containing compound and a polymer capable of reacting with the active hydrogen group-containing compound in an aqueous medium, and reacts to produce an adhesive substrate. However, in the step of obtaining particles containing at least the adhesive substrate, a toner having excellent properties such as aggregation resistance, chargeability, fluidity, transferability, and fixability can be efficiently produced.
In the toner production method of the present invention, the pH of the cleaning liquid after alkali cleaning is 6.0 to 11.0, the conductivity of the cleaning liquid after solid-liquid separation after water cleaning, and water cleaning. In which the temperature during alkali cleaning is 10 to 70 ° C. and the temperature T (° C.) during alkali cleaning is Tg (° C.). An embodiment in which (Tg-10) ≦ T ≦ (Tg + 10), an embodiment in which the alkali cleaning time is 1 to 72 hours, and the like are preferable.

  The developer of the present invention contains the toner of the present invention. For this reason, when an image is formed by electrophotography using the developer, a high-quality image with high image density and high sharpness is formed even under low-temperature fixing conditions.

  The toner container of the present invention is filled with the toner of the present invention. Therefore, when an image is formed by electrophotography using the toner of the present invention filled in the toner-containing container, a high-quality image with high image density and high sharpness is formed even under low-temperature fixing conditions.

  The process cartridge of the present invention comprises an electrostatic latent image carrier, and developing means for developing the electrostatic latent image formed on the electrostatic latent image carrier using the toner of the present invention to form a visible image. At least. The process cartridge can be attached to and detached from the image forming apparatus, is excellent in convenience, and uses the toner of the present invention, so that a high-quality image with high image density and high sharpness can be formed even under low-temperature fixing conditions.

  The image forming apparatus of the present invention includes an electrostatic latent image carrier, an electrostatic latent image forming unit that forms an electrostatic latent image on the electrostatic latent image carrier, and the electrostatic latent image of the present invention. The image forming apparatus includes at least a developing unit that forms a visible image by developing with toner, a transfer unit that transfers the visible image to a recording medium, and a fixing unit that fixes the transferred image transferred to the recording medium. In the image forming apparatus, the electrostatic latent image forming unit forms an electrostatic latent image on the electrostatic latent image carrier. The developing means develops the electrostatic latent image using the toner of the present invention to form a visible image. The transfer means transfers the visible image to a recording medium. The fixing unit fixes the transferred image transferred to the recording medium. As a result, a high-quality image with high image density and high sharpness is formed even under low-temperature fixing conditions.

  The image forming method of the present invention comprises an electrostatic latent image forming step of forming an electrostatic latent image on an electrostatic latent image carrier, and developing the electrostatic latent image with the toner of the present invention to make visible. It includes at least a developing step for forming an image, a transfer step for transferring the visible image to a recording medium, and a fixing step for fixing the transferred image transferred to the recording medium. In the image forming apparatus, an electrostatic latent image is formed on the electrostatic latent image carrier in the electrostatic latent image forming step. In the developing step, the electrostatic latent image is developed using the toner of the present invention to form a visible image. In the transfer step, the visible image is transferred to a recording medium. In the fixing step, the transferred image transferred to the recording medium is fixed. As a result, a high-quality image with high image density and high sharpness is formed even under low-temperature fixing conditions.

  According to the present invention, the conventional problems can be solved, the charging performance is excellent, the environmental stability is good, the low temperature fixability is excellent, the image quality is obtained, and the efficient manufacturing method thereof, and Further, it is possible to provide a developer, a container containing toner, a process cartridge, an image forming apparatus, and an image forming method capable of improving the image quality using the toner.

(toner)
The toner of the present invention contains a polyester resin, and the total organic carbon elution amount (TOC amount) extracted from the toner after alkali washing is 200 ppm / g or less, preferably resin fine particles, crystalline polyester It contains a resin and, if necessary, further contains other components such as a colorant, a release agent, and a charge control agent.
In addition, ppm / g means the amount of carbon in the organic component extracted from 1 g of dry toner.

  The toner of the present invention is not particularly limited and may be appropriately selected depending on the intended purpose. For example, the toner includes at least a binder resin, and is a known suspension polymerization method, emulsion polymerization method, or dissolution suspension method. In the aqueous medium, particles containing at least an adhesive substrate by reacting an active hydrogen group-containing compound and a polymer capable of reacting with the active hydrogen group-containing compound in an aqueous medium. The toner obtained by making it generate | occur | produced is mentioned suitably.

  In the toner of the present invention, it is preferable that the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner after alkali washing is smaller, for example, 200 ppm / g or less. It is necessary and is preferably 150 ppm / g or less, more preferably 100 ppm / g or less. When the TOC amount exceeds 200 ppm / g, the charging performance may be inferior, and the charging speed at the start-up and the charging performance under high temperature and high humidity may be deteriorated.

As an analysis method of the total organic carbon elution amount (total organic carbon (TOC) amount), for example, a total organic carbon meter (“TOC-5000A”; manufactured by Shimadzu Corporation) is used, and the toner after alkali cleaning is used. It can be measured by determining the amount of carbon extracted from, specifically, it can be measured by the following method. That is,
First, (1) when the sample to be measured is a wet cake or a dispersion, the solid content (% by mass) of the sample is measured. When the sample is a solid toner, the solid content is 100% by mass. (2) 7.5 g of the sample (wet cake, dispersion liquid, toner, etc.) is precisely weighed in a 140 ml bottle (this is S1), and (3) 47 KOHaq (aqueous solution) having a pH of 9 is added to (2). (4) Apply ultrasonic waves at 30 ° C. or lower for 30 minutes, (5) centrifuge approximately 1.5 ml in a microtube, and (6) obtained in (5) above. The supernatant in the obtained separated product is filtered using a 0.2 μ micro filter, ultrafine particles are removed and returned to the micro tube. (7) After the filter is washed with tap water and pure water, (5) The precipitate in the separated product obtained in (1) is filtered through a 1 μm filter, and (8) 2 drops of HCl (35% by mass) aq is added to the filtrate obtained in (7), so that the pH becomes 3 or less. (9) The solution obtained in (8) above is Weigh (referred to as T1), (10) Add pure water to the solution obtained in (8) above, dilute to 6.0 mg, and weigh precisely (referred to as T2) (10) The obtained treatment liquid is burned at a high temperature, carbon in an organic substance contained in the treatment liquid is generated as carbon dioxide gas, and the carbon dioxide gas is analyzed with infrared rays to measure the TOC amount. (This is referred to as a TOC measurement value) (11) The TOC amount can be calculated based on the following mathematical formula.
<Formula>
TOC (ppm / g) = TOC measurement value × (S1 + S2) / {S1 × (solid content (mass%) / 100)} × T2 / T1

  As pH of the washing | cleaning liquid after alkali washing, it is preferable that it is 6.0-11.0, for example, and 8.0-10.0 are more preferable. If the pH is less than 6.0, it may not be possible to improve the charging performance and ensure the environmental stability by alkali washing, and if it exceeds 11.0, hydrolysis reaction of the polyester resin may occur. Therefore, it is not preferable.

The conductivity of the cleaning liquid after solid-liquid separation and water cleaning after alkali cleaning is preferably 0.5 to 60 μS / cm, and more preferably 5.0 to 20 μS / cm, for example. If the conductivity is less than 0.5 μS / cm or exceeds 60 μS / cm, the charging performance may not be improved.
In order to set the conductivity of the cleaning liquid within the numerical range, it is important to remove anionic impurities present on the surfaces of the toner and the resin fine particles. In order to prevent this, it is preferable to perform water washing after the alkali washing.

  In the toner of the present invention, it is preferable that a hydrogen atom of a terminal carboxyl group in the polyester resin is substituted with a Na atom. When the alkali cleaning is performed, the hydrogen atom of the terminal carboxyl group in the polyester resin is replaced with Na atom to become (—COONa), and a toner having excellent charging performance and good charge rising can be obtained.

  The alkali cleaning method is not particularly limited as long as it can remove an emulsifier, a dispersant, an ionic impurity, etc. present on the surface of the toner or the resin fine particles. For example, a method of washing with an aqueous solution of an alkali metal salt or the like can be used. Various conditions such as temperature and time during alkali cleaning will be described in the toner production method of the present invention described later.

-Polyester resin-
There is no restriction | limiting in particular as an acid value of the said polyester resin, Although it can select suitably according to the objective, For example, 5-50 mgKOH / g is preferable and 20-30 mgKOH / g is more preferable. It is preferable to use a polyester resin having a relatively high acid value from the viewpoint of improving pigment dispersibility, fixability, chargeability and the like. The polyester resin having a high acid value generates a large amount of residual acid monomer on the surface of the toner particles, but can be removed by the alkali washing.

-Resin fine particles-
The resin fine particles are used for the purpose of controlling the shape (circularity, particle size distribution, etc.) of the toner.
Since the resin fine particles contain a large amount of acidic groups, if they are present on the surface of the toner particles, they may cause charging inhibition or fixing inhibition under high humidity. Can be removed.

There is no restriction | limiting in particular as glass transition temperature (Tg) of the said resin fine particle, Although it can select suitably according to the objective, At least 1 sort (s) of glass transition temperature (Tg) of the said resin fine particle is 20-20, for example. It is preferably 100 ° C. When the glass transition temperature (Tg) is less than 20 ° C, the heat-resistant storage stability may be deteriorated, and when it exceeds 100 ° C, the low-temperature fixability may be deteriorated.
The glass transition temperature (Tg) can be measured by the following method using, for example, a TG-DSC system TAS-100 (manufactured by Rigaku Corporation). First, about 10 mg of toner is put in an aluminum sample container, and the sample container is placed on a holder unit and set in an electric furnace. After heating from room temperature to 120 ° C. at a heating rate of 10 ° C./min, the sample is allowed to stand at 120 ° C. for 10 minutes, and the sample is cooled to room temperature and left for 10 minutes. Thereafter, the DSC curve is measured with a differential scanning calorimeter (DSC) after heating to 120 ° C. under a nitrogen atmosphere at a heating rate of 10 ° C./min. From the obtained DSC curve, using the analysis system in the TG-DSC system TAS-100 system, the glass transition temperature (Tg) is calculated from the contact point between the tangent line of the endothermic curve near the glass transition temperature (TG) and the baseline. can do.

The weight average molecular weight (Mw) of the fine resin particles is preferably 8,000 to 200,000, preferably 10,000 to 100,000 in terms of molecular weight distribution by GPC (gel permeation chromatography) soluble in tetrahydrofuran (THF). Is more preferable. When the weight average molecular weight (Mw) is less than 8,000, the heat resistant storage stability may be deteriorated, and when it exceeds 200,000, the low temperature fixability may be deteriorated.
The measurement of the molecular weight distribution by the gel permeation chromatography (GPC) can be performed, for example, as follows.
That is, first, the column is stabilized in a 40 ° C. heat chamber. At this temperature, tetrahydrofuran (THF) as a column solvent is allowed to flow at a flow rate of 1 ml per minute, and 50 to 200 μl of a tetrahydrofuran sample solution of a resin whose sample concentration is adjusted to 0.05 to 0.6 mass% is injected and measured. In measuring the molecular weight of the sample, the molecular weight distribution of the sample is calculated from the relationship between the logarithmic value of the calibration curve created by several monodisperse polystyrene standard samples and the count number. Examples of standard polystyrene samples for preparing the calibration curve include Pressure Chemical Co. Or Toyo Soda Kogyo Co., Ltd. having a molecular weight of ^{6 × 10 2, 2.1 × 10} 2, 4 × 10 2, 1.75 × 10 4, 1.1 × 10 5, 3.9 × 10 5, 8.6 It is preferable to use those of × 10 ⁵ , 2 × 10 ⁶ , and 4.48 × 10 ⁶ and use at least about 10 standard polystyrene samples. As the detector, an RI (refractive index) detector can be used.

  The content (residual amount) of the resin fine particles in the toner is not particularly limited and may be appropriately selected depending on the intended purpose. For example, 0.5 to 5.0% by mass is preferable, and 1.0 -3.0 mass% is more preferable. When the content is less than 0.5% by mass, the storage stability of the toner deteriorates, and blocking may be observed during storage or use. When the content exceeds 5.0% by mass, Resin fine particles inhibit the seepage of wax, and sufficient releasability cannot be obtained, and offset may occur.

  The content (residual amount) of the resin fine particles in the toner can be measured by various methods. Substances or functional groups derived only from the resin fine particles can be measured using, for example, a pyrolysis gas chromatograph mass spectrometer. It is possible to calculate from the peak area. There is no restriction | limiting in particular as said detector, Although it can select suitably according to the objective, A mass spectrometer is suitable.

The resin fine particle is not particularly limited as long as it is a resin that can form an aqueous dispersion in an aqueous medium, and can be appropriately selected from known resins according to the purpose, and may be a thermoplastic resin. It may be a thermosetting resin, for example, vinyl resin, polyurethane resin, epoxy resin, polyester resin, polyamide resin, polyimide resin, silicon resin, phenol resin, melamine resin, urea resin, aniline resin, ionomer resin, polycarbonate resin. , Etc.
These may be used individually by 1 type and may use 2 or more types together. Among these, it is preferably formed of at least one selected from a vinyl resin, a polyurethane resin, an epoxy resin, and a polyester resin in that an aqueous dispersion of fine spherical resin particles can be easily obtained. Particularly preferred are those containing an acidic group such as a sulfonic acid group.
The vinyl resin is a polymer obtained by homopolymerizing or copolymerizing a vinyl monomer. For example, a styrene- (meth) acrylic acid ester resin, a styrene-butadiene copolymer, a (meth) acrylic acid-acrylic acid ester polymer. Styrene-acrylonitrile copolymer, styrene-maleic anhydride copolymer, styrene- (meth) acrylic acid copolymer, and the like.
Moreover, as the resin fine particles, a copolymer comprising a monomer having at least two unsaturated groups can be used.
The monomer having at least two unsaturated groups is not particularly limited and may be appropriately selected depending on the intended purpose. For example, a sodium salt of ethylene oxide methacrylate adduct sulfate (“Eleminol RS-30”). "; Manufactured by Sanyo Chemical Industries Ltd.), divinylbenzene, 1,6-hexanediol acrylate and the like.

  The resin fine particles can be obtained by polymerization according to a known method appropriately selected according to the purpose, but is preferably obtained as an aqueous dispersion of the resin fine particles. The method for preparing the aqueous dispersion of the resin fine particles is, for example, (1) In the case of the vinyl resin, a vinyl monomer is used as a starting material and is selected from suspension polymerization, emulsion polymerization, seed polymerization, and dispersion polymerization. (2) In the case of polyaddition or condensation resin such as polyester resin, polyurethane resin, epoxy resin, etc., a precursor (monomer, oligomer). Etc.) or a solvent solution thereof is dispersed in an aqueous medium in the presence of an appropriate dispersant, and then heated or added with a curing agent to cure to produce an aqueous dispersion of resin fine particles (3) ) In the case of polyaddition or condensation resin such as polyester resin, polyurethane resin, epoxy resin, etc., it may be a precursor (monomer, oligomer, etc.) or a solvent solution thereof (liquid). (4) Preliminary polymerization reaction (addition polymerization, ring-opening polymerization, polyaddition, addition) After the resin prepared by any polymerization reaction mode such as condensation and condensation polymerization is pulverized using a mechanical pulverizer or jet type pulverizer and then classified to obtain resin fine particles , A method of dispersing in water in the presence of an appropriate dispersant, (5) prepared in advance by a polymerization reaction (any polymerization reaction mode such as addition polymerization, ring-opening polymerization, polyaddition, addition condensation, condensation polymerization, etc.) (6) A polymerization reaction (addition polymerization) in advance, in which resin fine particles are obtained by spraying a resin solution in which the resin is dissolved in a solvent to obtain resin fine particles and then dispersing the resin fine particles in water in the presence of an appropriate dispersant. , Ring-opening polymerization, polyaddition, addition condensation The resin fine particles can be obtained by adding a poor solvent to a resin solution prepared by dissolving a resin prepared in a solvent by a polymerization reaction method such as condensation polymerization or by cooling a resin solution previously dissolved in a solvent by heating. And then removing the solvent to obtain resin particles, and then dispersing the resin particles in water in the presence of a suitable dispersant. (7) Polymerization reaction (addition polymerization, ring-opening polymerization, heavy polymerization) in advance (Any polymerization reaction mode such as addition, addition condensation, and condensation polymerization may be used.) A resin solution prepared by dissolving a resin prepared in a solvent in a solvent is dispersed in an aqueous medium, and then heated or heated. (8) A resin prepared in advance by a polymerization reaction (which may be any polymerization reaction mode such as addition polymerization, ring-opening polymerization, polyaddition, addition condensation or condensation polymerization) is used as a solvent. In the dissolved resin solution A method of dissolving a suitable emulsifier and then adding water to carry out phase inversion emulsification is preferable.

-Crystalline polyester resin-
The crystalline polyester resin has crystallinity and exhibits a heat-melting characteristic that causes a sudden viscosity drop near the fixing start temperature. In other words, the heat resistant storage stability is good due to crystallinity until just before the melting start temperature, and at the melting start temperature, fixing occurs with a sharp drop in viscosity (sharp melt property). A compatible toner can be produced. In addition, the mold release width (the difference between the low temperature fixing lower limit temperature and the hot offset occurrence temperature) is also excellent.

  The crystalline polyester resin is not particularly limited and may be appropriately selected depending on the intended purpose. Examples thereof include diol compounds having 2 to 6 carbon atoms as alcohol components, particularly 1,4-butanediol, 1, Using 6-hexanediol and those derivatives containing 80 mol% or more, preferably 85 to 100 mol%, and at least maleic acid, fumaric acid, succinic acid, and derivatives thereof as acidic components A crystalline polyester resin represented by the following general formula (1) is preferably exemplified.

前記一般式（１）中、ｎ及びｍは、繰返単位数を表し、Ｌは１〜３の整数を表し、Ｒ^１及びＲ^２は、互いに同一であってもよいし、異なっていてもよく、水素原子又は炭化水素基を表す。

In the general formula (1), n and m represent the number of repeating units, L represents an integer of 1 to 3, and R ¹ and R ² may be the same as or different from each other. Often represents a hydrogen atom or a hydrocarbon group.

In order to control the crystallinity and softening point of the crystalline polyester resin, when the crystalline polyester is synthesized, a trihydric or higher polyhydric alcohol such as glycerin is used as the alcohol component, trimellitic anhydride is used as the acid component, etc. Non-linear polyesters obtained by condensation polymerization by adding a trivalent or higher polyvalent carboxylic acid may be used. The molecular structure of the crystalline polyester can be confirmed by solid NMR.
The weight average molecular weight (Mw) of the crystalline polyester resin is preferably 1,000 to 30,000, more preferably 1,000 to 6,500 in terms of molecular weight distribution by GPC of the soluble portion of orthodichlorobenzene. When the weight average molecular weight (Mw) is less than 1,000, the heat resistant storage stability may be deteriorated, and when it exceeds 30,000, the low temperature fixability may be deteriorated.
The number average molecular weight (Mn) of the crystalline polyester resin is preferably 500 to 6,000, more preferably 500 to 2,000 in terms of molecular weight distribution by GPC of the soluble part of orthodichlorobenzene. Moreover, as (Mw / Mn), 2-8 are preferable and 2-5 are more preferable.
In the molecular weight distribution by GPC, the peak position of the molecular weight distribution diagram in which the horizontal axis represents log (M) and the vertical axis represents mass% is in the range of 3.5 to 4.0, and the peak half-value width is 1 .5 or less is preferable.

The melting temperature and F1 _{/ 2} temperature of the crystalline polyester resin are preferably low as long as the heat resistant storage stability is not deteriorated. For example, the DSC endothermic peak temperature is preferably 50 to 150 ° C. When the melting temperature and the F _1/2 temperature are less than 50 ° C., the heat-resistant storage stability is deteriorated, and blocking tends to occur at the temperature inside the developing device. Therefore, the low temperature fixability may be deteriorated.

The molecular structure of the crystalline polyester resin can be confirmed, for example, by X-ray diffraction, GC / MS, LC / MS, IR measurement in addition to NMR measurement using a solution or solid. In terms of ease, IR measurement is preferred.
The crystalline polyester resin preferably has an absorption based on at least the olefin to any of the infrared absorption spectrum at 965 ± 10 cm ^-1 and 990 ± 10cm ^-1 δCH (out-of-plane bending vibration). When absorption based on δCH of the olefin is present at the position, the low-temperature fixability is improved.

The acid value of the crystalline polyester is preferably 8 mgKOH / g or more and more preferably 20 mgKOH / g or more in order to achieve low-temperature fixability from the viewpoint of the affinity between paper and resin. On the other hand, in order to improve hot offset property, 45 mgKOH / g or less is preferable.
The hydroxyl value of the crystalline polyester resin is preferably from 0 to 50 mgKOH / g, more preferably from 5 to 50 mgKOH / g, from the viewpoint of improving low-temperature fixability and charging characteristics.

-Adhesive substrate-
The adhesive substrate exhibits adhesiveness to a recording medium such as paper, and is formed by reacting the active hydrogen group-containing compound and a polymer capable of reacting with the active hydrogen group-containing compound in the aqueous medium. It may contain at least a polymer and may further contain a binder resin appropriately selected from known binder resins.

There is no restriction | limiting in particular as a weight average molecular weight of the said adhesive base material, Although it can select suitably according to the objective, For example, 1,000 or more are preferable and 2,000-10,000,000 are more preferable. 3,000 to 1,000,000 are particularly preferred.
When the weight average molecular weight is less than 1,000, the hot offset resistance may be deteriorated.

There is no restriction | limiting in particular as glass transition temperature (Tg) of the said adhesive base material, Although it can select suitably according to the objective, For example, 30-70 degreeC is preferable and 40-65 degreeC is more preferable. In the toner of the present invention, since a polyester resin subjected to a crosslinking reaction and an extension reaction coexists, the toner exhibits good storage stability even when the glass transition temperature is lower than that of a conventional polyester toner.
When the glass transition temperature (Tg) is less than 30 ° C., the heat-resistant storage stability of the toner may deteriorate, and when it exceeds 70 ° C., the low-temperature fixability may not be sufficient.

The storage elastic modulus of the adhesive substrate is not particularly limited and may be appropriately selected depending on the intended purpose. For example, the temperature (TG ′) at which the measurement frequency is 20 Hz is 10,000 dyne / cm ² , Usually, it is 100 ° C. or higher, and preferably 110 to 200 ° C. When the (TG ′) is less than 100 ° C., the hot offset resistance may be deteriorated.
The viscosity of the adhesive substrate is not particularly limited and may be appropriately selected depending on the intended purpose. For example, the temperature (Tη) at which a measurement frequency of 20 Hz is 1,000 poise is usually 180 ° C. or lower. Yes, 90-160 degreeC is preferable. When the (Tη) exceeds 180 ° C., the low-temperature fixability may be deteriorated.
Therefore, from the viewpoint of achieving both hot offset resistance and low-temperature fixability, the (TG ′) is preferably higher than the (Tη). That is, the difference (TG′−Tη) between (TG ′) and (Tη) is preferably 0 ° C. or higher, more preferably 10 ° C. or higher, and further preferably 20 ° C. or higher. The larger the difference, the better.
Further, from the viewpoint of achieving both low-temperature fixability and heat-resistant storage stability, the (TG′−Tη) is preferably 0 to 100 ° C., more preferably 10 to 90 ° C., and still more preferably 20 to 80 ° C.

Specific examples of the adhesive substrate are not particularly limited and may be appropriately selected depending on the intended purpose. Particularly preferred are polyester resins.
There is no restriction | limiting in particular as said polyester-type resin, Although it can select suitably according to the objective, For example, a urea modified polyester-type resin etc. are mentioned especially suitably.
The urea-modified polyester-based resin includes an amine (B) as the active hydrogen group-containing compound and an isocyanate group-containing polyester prepolymer (A) as a polymer that can react with the active hydrogen group-containing compound. It is obtained by reacting in a medium.
The urea-modified polyester resin may contain a urethane bond in addition to the urea bond. In this case, the molar ratio of the urea bond to the urethane bond (urea bond / urethane bond) is particularly limited. However, 100/0 to 10/90 is preferable, 80/20 to 20/80 is more preferable, and 60/40 to 30/70 is particularly preferable.
When the urea bond is less than 10, the hot offset resistance may be deteriorated.

  Preferable specific examples of the urea-modified polyester resin include the following (1) to (10), that is, (1) a polyester pre-reacted polycondensate of bisphenol A ethylene oxide 2 mol adduct and isophthalic acid with isophorone diisocyanate. A mixture of a polymer urealated with isophorone diamine and a polycondensate of bisphenol A ethylene oxide 2 mol adduct and isophthalic acid, and (2) a polycondensate of bisphenol A ethylene oxide 2 mol adduct and isophthalic acid A mixture of a polyester prepolymer reacted with diisocyanate and uread with isophoronediamine, a bicondensate of bisphenol A ethylene oxide 2 mol adduct and terephthalic acid, (3) bisphenol A ethylene oxide 2 mol A polyester prepolymer obtained by reacting an adduct / bisphenol A propylene oxide 2 mol adduct and a polycondensate of terephthalic acid with isophorone diisocyanate, and urethanized with isophorone diamine, and bisphenol A ethylene oxide 2 mol adduct / bisphenol A propylene. Mixture of oxide 2 mol adduct and polycondensate of terephthalic acid, (4) Bisphenol A ethylene oxide 2 mol adduct / bisphenol A propylene oxide 2 mol adduct and terephthalic acid polycondensate were reacted with isophorone diisocyanate. A mixture of a polyester prepolymer uread with isophoronediamine, a bisphenol A propylene oxide 2-mole adduct and a polycondensate of terephthalic acid, (5) bisphenol A A polyester prepolymer obtained by reacting a polycondensate of tylene oxide 2 mol adduct and terephthalic acid with isophorone diisocyanate and uread with hexamethylenediamine, and a polycondensate of bisphenol A ethylene oxide 2 mol adduct and terephthalic acid (6) Polyester prepolymer obtained by reacting a polycondensate of bisphenol A ethylene oxide with 2 mol of bisphenol A and isophorone diisocyanate with urea and hexamethylenediamine and 2 mol of bisphenol A ethylene oxide. Product / bisphenol A propylene oxide 2 mol adduct and terephthalic acid polycondensate, (7) bisphenol A ethylene oxide 2 mol adduct and terephthalic acid polycondensate A mixture of a polyester prepolymer reacted with socyanate with urethanized with ethylenediamine and a polycondensate of bisphenol A ethylene oxide 2 mol adduct and terephthalic acid, (8) bisphenol A ethylene oxide 2 mol adduct and isophthalic acid (9) Bisphenol A ethylene, a mixture of a polyester prepolymer obtained by reacting a polycondensate of bisphenol with diphenylmethane diisocyanate and uread with hexamethylene diamine, a bicondensate of bisphenol A ethylene oxide and a polycondensate of isophthalic acid, Polyester prepolymer obtained by reacting polycondensate of oxide 2 mol adduct / bisphenol A propylene oxide 2 mol adduct and terephthalic acid / dodecenyl succinic anhydride with diphenylmethane diisocyanate Mixture of uremer with hexamethylenediamine and bisphenol A ethylene oxide 2-mole adduct / bisphenol A propylene oxide 2-mole adduct and terephthalic acid polycondensate, (10) bisphenol A ethylene oxide 2-mole addition And a mixture of a polyester prepolymer obtained by reacting a polycondensate of isophthalic acid and toluene diisocyanate with urea diisocyanate with hexamethylenediamine, a bicondensate of bisphenol A ethylene oxide and a polycondensate of isophthalic acid, etc. Preferably mentioned.

-Active hydrogen group-containing compound-
The active hydrogen group-containing compound acts as an elongation agent, a crosslinking agent, or the like when a polymer capable of reacting with the active hydrogen group-containing compound undergoes an elongation reaction, a crosslinking reaction, or the like in the aqueous medium.
The active hydrogen group-containing compound is not particularly limited as long as it has an active hydrogen group, and can be appropriately selected depending on the purpose. For example, the polymer capable of reacting with the active hydrogen group-containing compound is In the case of the isocyanate group-containing polyester prepolymer (A), the amines (B) can be increased in molecular weight by a reaction such as an elongation reaction or a crosslinking reaction with the isocyanate group-containing polyester prepolymer (A). Is preferred.
There is no restriction | limiting in particular as said active hydrogen group, According to the objective, it can select suitably, For example, a hydroxyl group (alcoholic hydroxyl group or phenolic hydroxyl group), an amino group, a carboxyl group, a mercapto group etc. are mentioned. These may be used individually by 1 type and may use 2 or more types together. Among these, an alcoholic hydroxyl group is particularly preferable.

The amines (B) are not particularly limited and may be appropriately selected depending on the intended purpose. Examples thereof include diamine (B1), trivalent or higher polyamine (B2), amino alcohol (B3), and amino mercaptan. (B4), amino acid (B5), and those obtained by blocking the amino groups of B1 to B5 (B6).
These may be used individually by 1 type and may use 2 or more types together. Among these, diamine (B1), a mixture of diamine (B1) and a small amount of a trivalent or higher polyamine (B2) are particularly preferable.

Examples of the diamine (B1) include aromatic diamines, alicyclic diamines, aliphatic diamines, and the like. Examples of the aromatic diamine include phenylenediamine, diethyltoluenediamine, 4,4′diaminodiphenylmethane, and the like. Examples of the alicyclic diamine include 4,4′-diamino-3,3′dimethyldicyclohexylmethane, diaminecyclohexane, and isophoronediamine. Examples of the aliphatic diamine include ethylene diamine, tetramethylene diamine, and hexamethylene diamine.
Examples of the trivalent or higher polyamine (B2) include diethylenetriamine and triethylenetetramine.
Examples of the amino alcohol (B3) include ethanolamine and hydroxyethylaniline.
Examples of the amino mercaptan (B4) include aminoethyl mercaptan and aminopropyl mercaptan.
Examples of the amino acid (B5) include aminopropionic acid and aminocaproic acid.
Examples of the block (B6) in which the amino group of B1 to B5 is blocked include, for example, a ketimine obtained from any of the amines (B1) to (B5) and ketones (acetone, methyl ethyl ketone, methyl isobutyl ketone, etc.) Compounds, oxazolyzone compounds, and the like.

  In addition, a reaction terminator can be used to stop the elongation reaction, the crosslinking reaction, etc. between the active hydrogen group-containing compound and the polymer capable of reacting with the active hydrogen group-containing compound. Use of the reaction terminator is preferable in that the molecular weight and the like of the adhesive substrate can be controlled within a desired range. Examples of the reaction terminator include monoamines (diethylamine, dibutylamine, butylamine, laurylamine, etc.) or those blocked (ketimine compounds).

As a mixing ratio of the amines (B) and the isocyanate group-containing polyester prepolymer (A), the isocyanate group [NCO] in the isocyanate group-containing prepolymer (A) and the amines (B) The mixing equivalent ratio ([NCO] / [NHx]) of the amino group [NHx] is preferably 1/3 to 3/1, more preferably 1/2 to 2/1, It is particularly preferably 1.5 to 1.5 / 1.
When the mixing equivalent ratio ([NCO] / [NHx]) is less than 1/3, the low-temperature fixability may be lowered. When the mixing equivalent ratio exceeds 3/1, the molecular weight of the urea-modified polyester resin becomes low. The hot offset resistance may be deteriorated.

--Polymer capable of reacting with active hydrogen group-containing compound--
The polymer capable of reacting with the active hydrogen group-containing compound (hereinafter sometimes referred to as “prepolymer”) is not particularly limited as long as it has at least a site capable of reacting with the active hydrogen group-containing compound. However, it can be appropriately selected from known resins, and examples thereof include polyol resins, polyacrylic resins, polyester resins, epoxy resins, and derivative resins thereof.
These may be used individually by 1 type and may use 2 or more types together. Among these, a polyester resin is particularly preferable in terms of high fluidity and transparency during melting.

The site capable of reacting with the active hydrogen group-containing compound in the prepolymer is not particularly limited and may be appropriately selected from known substituents. For example, an isocyanate group, an epoxy group, a carboxylic acid, An acid chloride group, and the like.
These may be contained singly or in combination of two or more. Among these, an isocyanate group is particularly preferable.

Among the prepolymers, it is easy to adjust the molecular weight of the polymer component, and oil-less low-temperature fixing characteristics in dry toners, in particular, good releasability and fixability even in the absence of a release oil application mechanism to a fixing heating medium. It is particularly preferable that it is a urea bond-forming group-containing polyester resin (RMPE) in that it can be secured.
As said urea bond production | generation group, an isocyanate group etc. are mentioned, for example. When the urea bond generating group in the urea bond generating group-containing polyester resin (RMPE) is the isocyanate group, the isocyanate group-containing polyester prepolymer (A) and the like are particularly preferable as the polyester resin (RMPE). It is done.

  The isocyanate group-containing polyester prepolymer (A) is not particularly limited and may be appropriately selected depending on the intended purpose. For example, it is a polycondensate of a polyol (PO) and a polycarboxylic acid (PC), And what made the said active hydrogen group containing polyester resin react with polyisocyanate (PIC), etc. are mentioned.

  There is no restriction | limiting in particular as said polyol (PO), According to the objective, it can select suitably, For example, diol (DIO), trihydric or more polyol (TO), diol (DIO), and trihydric or more polyol A mixture with (TO), etc. are mentioned. These may be used individually by 1 type and may use 2 or more types together. Among these, the diol (DIO) alone or a mixture of the diol (DIO) and a small amount of the trivalent or higher polyol (TO) is preferable.

Examples of the diol (DIO) include alkylene glycols, alkylene ether glycols, alicyclic diols, alkylene oxide adducts of alicyclic diols, bisphenols, alkylene oxide adducts of bisphenols, and the like.
The alkylene glycol is preferably one having 2 to 12 carbon atoms, such as ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,4-butanediol, 1,6-hexanediol, and the like. Can be mentioned. Examples of the alkylene ether glycol include diethylene glycol, triethylene glycol, dipropylene glycol, polyethylene glycol, polypropylene glycol, polytetramethylene ether glycol, and the like. Examples of the alicyclic diol include 1,4-cyclohexanedimethanol and hydrogenated bisphenol A. Examples of the alkylene oxide adduct of the alicyclic diol include those obtained by adding an alkylene oxide such as ethylene oxide, propylene oxide, butylene oxide to the alicyclic diol. Examples of the bisphenols include bisphenol A, bisphenol F, and bisphenol S. Examples of the alkylene oxide adduct of the bisphenol include those obtained by adding an alkylene oxide such as ethylene oxide, propylene oxide, butylene oxide to the bisphenol.
Among these, alkylene glycols having 2 to 12 carbon atoms, alkylene oxide adducts of bisphenols and the like are preferable, and alkylene oxide adducts of bisphenols, alkylene oxide adducts of bisphenols and alkylene glycols having 2 to 12 carbon atoms. Mixtures are particularly preferred.

The trivalent or higher polyol (TO) is preferably 3 to 8 or higher, for example, a trivalent or higher polyhydric aliphatic alcohol, a trivalent or higher polyphenol, a trivalent or higher polyphenol. And alkylene oxide adducts.
Examples of the trihydric or higher polyhydric aliphatic alcohol include glycerin, trimethylolethane, trimethylolpropane, pentaerythritol, sorbitol and the like. Examples of the trihydric or higher polyphenols include trisphenol PA, phenol novolak, cresol novolak, and the like. Examples of the alkylene oxide adduct of the trihydric or higher polyphenol include those obtained by adding an alkylene oxide such as ethylene oxide, propylene oxide, butylene oxide to the trihydric or higher polyphenol.

  The mixture mass ratio (DIO: TO) of the diol (DIO) and the trivalent or higher polyol (TO) in the mixture of the diol (DIO) and the trivalent or higher polyol (TO) is 100: 0.01-10 are preferable and 100: 0.01-1 are more preferable.

There is no restriction | limiting in particular as said polycarboxylic acid (PC), Although it can select suitably according to the objective, For example, dicarboxylic acid (DIC), trivalent or more polycarboxylic acid (TC), dicarboxylic acid (DIC) ) And a tri- or higher valent polycarboxylic acid.
These may be used individually by 1 type and may use 2 or more types together. Among these, dicarboxylic acid (DIC) alone or a mixture of DIC and a small amount of trivalent or higher polycarboxylic acid (TC) is preferable.
Examples of the dicarboxylic acid include alkylene dicarboxylic acid, alkenylene dicarboxylic acid, aromatic dicarboxylic acid, and the like.
Examples of the alkylene dicarboxylic acid include succinic acid, adipic acid, and sebacic acid. As said alkenylene dicarboxylic acid, a C4-C20 thing is preferable, For example, a maleic acid, a fumaric acid, etc. are mentioned. As said aromatic dicarboxylic acid, a C8-C20 thing is preferable, For example, a phthalic acid, an isophthalic acid, a terephthalic acid, naphthalene dicarboxylic acid etc. are mentioned.
Among these, alkenylene dicarboxylic acid having 4 to 20 carbon atoms and aromatic dicarboxylic acid having 8 to 20 carbon atoms are preferable.

The trivalent or higher polycarboxylic acid (TO) is preferably a trivalent to octavalent or higher one, and examples thereof include aromatic polycarboxylic acids.
The aromatic polycarboxylic acid preferably has 9 to 20 carbon atoms, and examples thereof include trimellitic acid and pyromellitic acid.

  As the polycarboxylic acid (PC), the dicarboxylic acid (DIC), the trivalent or higher polycarboxylic acid (TC), and a mixture of the dicarboxylic acid (DIC) and the trivalent or higher polycarboxylic acid, Any acid anhydride or lower alkyl ester selected from can also be used. Examples of the lower alkyl ester include methyl ester, ethyl ester, isopropyl ester and the like.

  Mixing mass ratio (DIC: TC) of the dicarboxylic acid (DIC) and the trivalent or higher polycarboxylic acid (TC) in the mixture of the dicarboxylic acid (DIC) and the trivalent or higher polycarboxylic acid (TC) There is no restriction | limiting in particular, According to the objective, it can select suitably, For example, 100: 0.01-10 are preferable and 100: 0.01-1 are more preferable.

  The mixing ratio for the polycondensation reaction between the polyol (PO) and the polycarboxylic acid (PC) is not particularly limited and may be appropriately selected depending on the intended purpose. For example, in the polyol (PO) The equivalent ratio ([OH] / [COOH]) of the hydroxyl group [OH] to the carboxyl group [COOH] in the polycarboxylic acid (PC) is usually preferably 2/1 to 1/1. More preferably, it is 0.5 / 1 to 1/1, and particularly preferably 1.3 / 1 to 1.02 / 1.

There is no restriction | limiting in particular as content in the said isocyanate group containing polyester prepolymer (A) of the said polyol (PO), Although it can select suitably according to the objective, For example, 0.5-40 mass% is preferable. 1-30 mass% is more preferable, and 2-20 mass% is especially preferable.
When the content is less than 0.5% by mass, the hot offset resistance deteriorates, and it may be difficult to achieve both the heat-resistant storage stability and the low-temperature fixability of the toner, and exceeds 40% by mass. In some cases, the low-temperature fixability may deteriorate.

The polyisocyanate (PIC) is not particularly limited and may be appropriately selected depending on the intended purpose. Examples thereof include aliphatic polyisocyanates, alicyclic polyisocyanates, aromatic diisocyanates, araliphatic diisocyanates, and isocyanurates. And those blocked with phenol derivatives, oximes, caprolactams, and the like.
Examples of the aliphatic polyisocyanate include tetramethylene diisocyanate, hexamethylene diisocyanate, 2,6-diisocyanatomethylcaproate, octamethylene diisocyanate, decamethylene diisocyanate, dodecamethylene diisocyanate, tetradecamethylene diisocyanate, trimethylhexane diisocyanate, Examples include tetramethylhexane diisocyanate. Examples of the alicyclic polyisocyanate include isophorone diisocyanate and cyclohexylmethane diisocyanate. Examples of the aromatic diisocyanate include tolylene diisocyanate, diphenylmethane diisocyanate, 1,5-naphthylene diisocyanate, diphenylene-4,4′-diisocyanate, 4,4′-diisocyanato-3,3′-dimethyldiphenyl, 3- Examples thereof include methyldiphenylmethane-4,4′-diisocyanate and diphenyl ether-4,4′-diisocyanate. Examples of the araliphatic diisocyanate include α, α, α ′, α′-tetramethylxylylene diisocyanate. Examples of the isocyanurates include tris-isocyanatoalkyl-isocyanurate, triisocyanatocycloalkyl-isocyanurate, and the like.
These can be used alone or in combination of two or more.

As a mixing ratio when the polyisocyanate (PIC) and the active hydrogen group-containing polyester resin (for example, a hydroxyl group-containing polyester resin) are reacted, the isocyanate group [NCO] in the polyisocyanate (PIC) and the hydroxyl group-containing component are used. The mixing equivalent ratio ([NCO] / [OH]) with the hydroxyl group [OH] in the polyester resin is usually preferably 5/1 to 1/1, and preferably 4/1 to 1.2 / 1. More preferred is 3/1 to 1.5 / 1.
When the isocyanate group [NCO] exceeds 5, low-temperature fixability may be deteriorated, and when it is less than 1, offset resistance may be deteriorated.

There is no restriction | limiting in particular as content in the said isocyanate group containing polyester prepolymer (A) of the said polyisocyanate (PIC), Although it can select suitably according to the objective, For example, 0.5-40 mass% is Preferably, 1-30 mass% is more preferable, and 2-20 mass% is still more preferable.
When the content is less than 0.5% by mass, the hot offset resistance is deteriorated, and it may be difficult to achieve both heat-resistant storage stability and low-temperature fixability. When the content exceeds 40% by mass, Low temperature fixability may deteriorate.

As an average number of the isocyanate groups contained per molecule of the isocyanate group-containing polyester prepolymer (A), 1 or more is preferable, 1.2 to 5 is more preferable, and 1.5 to 4 is more preferable.
When the average number of the isocyanate groups is less than 1, the molecular weight of the polyester resin (RMPE) modified with the urea bond-forming group is lowered, and the hot offset resistance may be deteriorated.

  The weight average molecular weight (Mw) of the polymer capable of reacting with the active hydrogen group-containing compound is 1,000 to 30,000 in terms of molecular weight distribution by GPC (gel permeation chromatography) soluble in tetrahydrofuran (THF). Preferably, 1,500-15,000 are more preferable. When the weight average molecular weight (Mw) is less than 1,000, the heat resistant storage stability may be deteriorated, and when it exceeds 30,000, the low temperature fixability may be deteriorated.

--Binder resin--
There is no restriction | limiting in particular as said binder resin, According to the objective, it can select suitably, For example, although a polyester resin etc. are mentioned, Undenatured polyester resin (unmodified polyester resin) is especially preferable.
When the unmodified polyester resin is contained in the toner, low-temperature fixability and glossiness can be improved.
Examples of the unmodified polyester resin include those similar to the urea bond-forming group-containing polyester resin, that is, a polycondensate of a polyol (PO) and a polycarboxylic acid (PC). The unmodified polyester resin is partially compatible with the urea bond-forming group-containing polyester resin (RMPE), that is, has a similar structure that is compatible with each other. It is preferable in terms of resistance to hot offset.

The weight average molecular weight (Mw) of the unmodified polyester resin is preferably 1,000 to 30,000, preferably 1,500 to 15, in terms of molecular weight distribution by GPC (gel permeation chromatography) soluble in tetrahydrofuran (THF). 1,000 is more preferable, 1,500 to 10,000 is still more preferable, and 2,000 to 8,000 is particularly preferable. When the weight average molecular weight (Mw) is less than 1,000, the heat resistant storage stability may be deteriorated. Therefore, the content of the component having the weight average molecular weight (Mw) of less than 1,000 as described above. Needs to be 8 to 28% by mass. On the other hand, when the weight average molecular weight (Mw) exceeds 30,000, the low-temperature fixability may be deteriorated.
The glass transition temperature of the unmodified polyester resin is usually 30 to 70 ° C, more preferably 35 to 70 ° C, still more preferably 35 to 50 ° C, and particularly preferably 35 to 45 ° C. When the glass transition temperature is less than 30 ° C., the heat-resistant storage stability of the toner may deteriorate, and when it exceeds 70 ° C., the low-temperature fixability may be insufficient.
The hydroxyl value of the unmodified polyester resin is preferably 5 mgKOH / g, more preferably 10 to 120 mgKOH / g, and still more preferably 20 to 80 mgKOH / g. If the hydroxyl value is less than 5, it may be difficult to achieve both heat-resistant storage stability and low-temperature fixability.
The acid value of the unmodified polyester resin is usually 1.0 to 50.0 mg KOH / g, and preferably 3.0 to 25.0. Generally, it becomes easy to be negatively charged by giving an acid value to the toner.
If the hydroxyl value and the acid value are out of the numerical ranges, respectively, they are easily affected by the environment in a high-temperature, high-humidity and low-temperature, low-humidity environment, and image degradation is likely to occur.
When the unmodified polyester resin is contained in the toner, the mixing mass ratio (RMPE / PE) of the urea bond-forming group-containing polyester resin (RMPE) and the unmodified polyester resin (PE) is 5/95. -25/75 is preferable, and 10 / 90-25 / 75 is more preferable.
When the mixing mass ratio of the unmodified polyester resin (PE) exceeds 95, the hot offset resistance is deteriorated, and it may be difficult to achieve both heat-resistant storage stability and low-temperature fixability. Glossiness may deteriorate.
As content of the said non-modified polyester resin in the said binder resin, 50-100 mass% is preferable, for example, 60-95 mass% is more preferable, 70-90 mass% is still more preferable. If the content is less than 50% by mass, the amount of the modified polyester resin becomes excessive, the low-temperature fixability is inferior, and the chargeability may be affected.

  When the non-modified polyester resin (b) and the crystalline polyester resin (c) are contained in the toner, the urea bond-forming group-containing polyester resin (a), the unmodified polyester resin (b), and the crystalline The mixing mass ratio with the polyester resin (c) is usually (a) / (b) + (c) of 5/95 to 25/75, preferably 10/90 to 25/75, and 12/88 to 25/75 is more preferable, 12/88 to 22/78 is still more preferable, and the mass ratio of (b) to (c) is 99/1 to 50/50, and 95/5 to 60/40. Is preferable, and 90/10 to 65/35 is more preferable. When the mass ratio is out of the numerical range, the hot offset resistance is deteriorated, and it may be difficult to achieve both heat resistant storage stability and low temperature fixability.

--- Aqueous medium--
There is no restriction | limiting in particular as said aqueous medium, It can select suitably from well-known things, For example, water, a solvent miscible with this water, a mixture thereof, etc. are mentioned.
The solvent miscible with water is not particularly limited as long as it is miscible with water, and examples thereof include alcohol, dimethylformamide, tetrahydrofuran, cellosolves, and lower ketones.
Examples of the alcohol include methanol, isopropanol, ethylene glycol and the like. Examples of the cell solves include methyl cell solve. Examples of the lower ketones include acetone and methyl ethyl ketone.
These may be used individually by 1 type and may use 2 or more types together. Among these, methanol is preferable.

-Other ingredients-
The other components are not particularly limited and may be appropriately selected depending on the purpose. For example, colorants, mold release agents, charge control agents, inorganic fine particles, fluidity improvers, cleaning improvers, magnetic properties, and the like. Examples include materials, metal soaps, and the like.

The colorant is not particularly limited and may be appropriately selected from known dyes and pigments according to the purpose. For example, 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, Lead Red, Lead Red, Cadmium Red, Cad Muum Mercury Red, Antimon Zhu, Permanent Red 4R, PA Red, Faise Red, Parachlor Ortho Nitroaniline Red, Resol Fast Scarlet G, Brilliant Fast Scarlet, Brilliant Carmine BS, Permanent Red (F2R, F4R, FRL, FRLL, F4RH), Fast Scarlet VD, Belkan Fast Rubin B, Brilliant Scarlet G, Risor Rubin GX, Permanent Red F5R, Brilliant Carmine 6B, Pigment Scarlet 3B, Bordeaux 5B, Toluidine 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, Oh Lured, Quinacridone Red, Pyrazolone Red, Polyazo Red, Chrome Vermilion, 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, Oxidation Chrome, Pyridian, Emerald Green, Pigment Green B, Naphthol Green B, Green Gold, Ash Examples include green lake, malachite green lake, phthalocyanine green, anthraquinone green, titanium oxide, zinc white, and lithobon.
These may be used individually by 1 type and may use 2 or more types together.

The content of the colorant in the toner is not particularly limited and may be appropriately selected depending on the intended purpose, but is preferably 1 to 15% by mass, and more preferably 3 to 10% by mass.
When the content is less than 1% by mass, a reduction in the coloring power of the toner is observed, and when the content exceeds 15% by mass, a poor dispersion of the pigment in the toner occurs. The characteristics may be degraded.

  The colorant may be used as a master batch combined with a resin. The resin is not particularly limited and may be appropriately selected from known ones according to the purpose. For example, styrene or a substituted polymer thereof, a styrene copolymer, polymethyl methacrylate, polybutyl methacrylate , Polyvinyl chloride, polyvinyl acetate, polyethylene, polypropylene, polyester, epoxy resin, epoxy polyol resin, polyurethane, polyamide, polyvinyl butyral, polyacrylic acid resin, rosin, modified rosin, terpene resin, aliphatic hydrocarbon resin, alicyclic ring Aromatic hydrocarbon resin, aromatic petroleum resin, chlorinated paraffin, paraffin, and the like. These may be used individually by 1 type and may use 2 or more types together.

  Examples of the polymer of styrene or a substituted product thereof include polyester resin, polystyrene, poly p-chlorostyrene, polyvinyl toluene, and the like. Examples of the styrene copolymer include a styrene-p-chlorostyrene copolymer, a styrene-propylene copolymer, a styrene-vinyltoluene copolymer, a styrene-vinylnaphthalene copolymer, and a styrene-methyl acrylate copolymer. Polymer, 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, styrene-acrylonitrile copolymer, styrene-vinyl methyl ketone copolymer, styrene-butadiene copolymer, styrene-isoprene copolymer, styrene An acrylonitrile-indene copolymer, Styrene - maleic acid copolymer, styrene - maleic acid ester copolymer, and the like.

  The masterbatch can be produced by mixing or kneading the masterbatch resin and the colorant under high shear. At this time, it is preferable to add an organic solvent in order to enhance the interaction between the colorant and the resin. Also, the so-called flushing method is preferable in that the wet cake of the colorant can be used as it is, and there is no need to dry it. This flushing method is a method in which an aqueous paste containing water of a colorant is mixed or kneaded together with a resin and an organic solvent, and the colorant is transferred to the resin side to remove moisture and organic solvent components. For the mixing or kneading, for example, a high shear dispersion device such as a three-roll mill is preferably used.

There is no restriction | limiting in particular as said mold release agent, According to the objective, it can select suitably from well-known things, For example, waxes etc. are mentioned suitably.
Examples of the waxes include carbonyl group-containing waxes, polyolefin waxes, and long-chain hydrocarbons. These may be used individually by 1 type and may use 2 or more types together. Among these, a carbonyl group-containing wax is preferable.
Examples of the carbonyl group-containing wax include polyalkanoic acid esters, polyalkanol esters, polyalkanoic acid amides, polyalkylamides, dialkyl ketones, and the like. Examples of the polyalkanoic acid ester include carnauba wax, montan wax, trimethylolpropane tribehenate, pentaerythritol tetrabehenate, pentaerythritol diacetate dibehenate, glycerin tribehenate, and 1,18-octadecane. Examples thereof include diol distearate. Examples of the polyalkanol ester include tristearyl trimellitic acid and distearyl maleate. Examples of the polyalkanoic acid amide include dibehenyl amide. Examples of the polyalkylamide include trimellitic acid tristearylamide. Examples of the dialkyl ketone include distearyl ketone. Of these carbonyl group-containing waxes, polyalkanoic acid esters are particularly preferred.
Examples of the polyolefin wax include polyethylene wax and polypropylene wax.
Examples of the long chain hydrocarbon include paraffin wax and sazol wax.

There is no restriction | limiting in particular as melting | fusing point of the said mold release agent, Although it can select suitably according to the objective, 40-160 degreeC is preferable, 50-120 degreeC is more preferable, 60-90 degreeC is especially preferable.
When the melting point is less than 40 ° C., the wax may adversely affect the heat-resistant storage stability, and when it exceeds 160 ° C., cold offset may easily occur during fixing at a low temperature.
The melt viscosity of the release agent 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 of the wax.
If the melt viscosity is less than 5 cps, the releasability may be lowered, and if it exceeds 1,000 cps, the effect of improving hot offset resistance and low-temperature fixability may not be obtained.

There is no restriction | limiting in particular as content in the said toner of the said mold release agent, Although it can select suitably according to the objective, 0-40 mass% is preferable and 3-30 mass% is more preferable.
When the content exceeds 40% by mass, the fluidity of the toner may be deteriorated.

The charge control agent is not particularly limited and may be appropriately selected from known materials according to the purpose. However, since a color tone may change when a colored material is used, a material that is colorless to nearly white is used. Preferably, for example, triphenylmethane dyes, molybdate chelate pigments, rhodamine dyes, alkoxyamines, quaternary ammonium salts (including fluorine-modified quaternary ammonium salts), alkylamides, phosphorus alone or compounds thereof, tungsten Examples thereof include a single substance or a compound thereof, a fluorine-based activator, a metal salt of salicylic acid, and a metal salt of a salicylic acid derivative. These may be used individually by 1 type and may use 2 or more types together.
Commercially available products may be used as the charge control agent. Examples of the commercially available products include quaternary ammonium salt Bontron P-51, oxynaphthoic acid metal complex E-82, and salicylic acid metal complex. E-84, phenolic condensate E-89 (above, manufactured by Orient Chemical Co., Ltd.), quaternary ammonium salt molybdenum complex TP-302, TP-415 (above, manufactured by Hodogaya Chemical Co., Ltd.), fourth Copy charge PSY VP2038 of quaternary ammonium 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 which is a boron complex -147 (manufactured by Nippon Carlit), quinacridone, azo pigments, other sulfonic acid groups, carbo Sill group, polymer compounds having a functional group such as quaternary ammonium salts, and the like.
The charge control agent may be melted and kneaded with the master batch and then dissolved or dispersed, or may be added together with each component of the toner when directly dissolving or dispersing in the organic solvent, or It may be fixed on the toner surface after the toner particles are manufactured and after alkali cleaning described later.

  The content of the charge control agent in the toner varies depending on the type of the binder resin, the presence / absence of an additive, a dispersion method, and the like, and cannot be generally specified. On the other hand, 0.1-10 mass parts is preferable, and 0.2-5 mass parts is more preferable. When the content is less than 0.1 parts by mass, the charge controllability may not be obtained. When the content exceeds 10 parts by mass, the chargeability of the toner becomes too large, and the effect of the main charge control agent is reduced. As a result, the electrostatic attractive force with the developing roller increases, which may lead to a decrease in developer fluidity and a decrease in image density.

The inorganic fine particles are not particularly limited and may be appropriately selected from known ones according to the purpose. For example, silica, alumina, titanium oxide, barium titanate, magnesium titanate, calcium titanate, titanate Strontium, zinc oxide, tin oxide, silica sand, clay, mica, wollastonite, diatomaceous earth, chromium oxide, cerium oxide, pengala, antimony trioxide, magnesium oxide, zirconium oxide, barium sulfate, barium carbonate, calcium carbonate, carbonized Examples include silicon and silicon nitride. These may be used individually by 1 type and may use 2 or more types together.
The primary particle diameter of the inorganic fine particles is preferably 5 nm to 2 μm, and more preferably 5 nm to 500 nm. The specific surface area of the inorganic fine particles by BET method is preferably 20 to 500 m ² / g.
The content of the inorganic fine particles in the toner is preferably 0.01 to 5.0% by mass, and more preferably 0.01 to 2.0% by mass.

The fluidity improver means a material that can be surface treated to increase hydrophobicity and prevent deterioration of flow characteristics and charging characteristics even under high humidity. For example, a silane coupling agent, a silylating agent, Examples thereof include a silane coupling agent having an alkyl fluoride group, an organic titanate coupling agent, an aluminum coupling agent, silicone oil, and modified silicone oil.
The cleaning improver is added to the toner in order to remove the developer after transfer remaining on the photoreceptor or the primary transfer medium. For example, a fatty acid metal salt such as zinc stearate, calcium stearate, stearic acid, Examples thereof include polymer fine particles produced by soap-free emulsion polymerization such as methyl methacrylate fine particles and polystyrene fine particles. The polymer fine particles preferably have a relatively narrow particle size distribution, and those having a volume average particle size of 0.01 to 1 μm are suitable.
There is no restriction | limiting in particular as said magnetic material, According to the objective, it can select suitably from well-known things, For example, iron powder, a magnetite, a ferrite, etc. are mentioned. Among these, white is preferable in terms of color tone.

  The toner of the present invention has the following volume average particle diameter (Dv), volume average particle diameter (Dv) / number average particle diameter (Dn), average circularity, penetration, low temperature fixability, offset generation temperature. It preferably has heat characteristics, image density, BET specific surface area, and the like.

The volume average particle diameter (Dv) of the toner is preferably 3 to 8 μm.
When the volume average particle size is less than 3 μm, in the two-component developer, the toner may be fused to the surface of the carrier during a long period of stirring in the developing device, and the charging ability of the carrier may be reduced. In the developer, toner filming on the developing roller and toner fusion to a member such as a blade are likely to occur because the toner is thinned, and if it exceeds 8 μm, the resolution is high and the resolution is high. It becomes difficult to obtain an image having an image quality, and when the balance of the toner in the developer is performed, the variation in the particle diameter of the toner may increase.

The ratio (Dv / Dn) of the volume average particle diameter (Dv) to the number average particle diameter (Dn) in the toner is, for example, preferably 1.00 to 1.25, more preferably 1.10 to 1.25. preferable.
When the ratio of the volume average particle diameter to the number average particle diameter (Dv / Dn) is less than 1.00, with the two-component developer, the toner is fused to the surface of the carrier during long-term stirring in the developing device, The chargeability of the carrier may be reduced, and the cleaning property may be deteriorated. In the case of a one-component developer, the filming of the toner on the developing roller and the thinning of the toner are performed. Toner fusion may easily occur, and if it exceeds 1.25, it becomes difficult to obtain a high-resolution and high-quality image, and toner particles in the case where the balance of the toner in the developer is performed Variation in diameter may be large.

  The volume average particle diameter and the ratio (Dv / Dn) between the volume average particle diameter and the number average particle diameter are measured using, for example, a particle size measuring device “Multisizer II” manufactured by Beckman Coulter, Inc. Can do.

The average circularity is a value obtained by dividing the perimeter of an equivalent circle having the same projected shape as the toner shape by the perimeter of the actual particles, and is preferably 0.900 to 0.980, for example, 0.950 to 0 .975 is more preferred. The particles having an average circularity of less than 0.940 are preferably 15% or less.
If the average circularity is less than 0.900, satisfactory transferability and a high-quality image free from dust may not be obtained. If the average circularity exceeds 0.980, image formation employing blade cleaning or the like is employed. In the system, defective cleaning occurs on the photoconductor and transfer belt, and in the case of image formation with a high image area ratio such as photographic images, an untransferred image is formed due to poor paper feed, etc. As a result, the accumulated toner may become a transfer residual toner on the photoconductor, which may cause background smearing of the image, or may contaminate the charging roller for charging the photoconductor in contact with the original charging ability. It may become impossible to demonstrate.
The average circularity is measured, for example, by an optical detection band method in which a suspension containing toner is passed through an imaging unit detection band on a flat plate, and a particle image is optically detected and analyzed by a CCD camera. For example, it can be measured using a flow type particle image analyzer FPIA-2100 (manufactured by Sysmex Corporation).

As said penetration, for example, the penetration measured by a penetration test (JIS K2235-1991) needs to be 15 mm or more, and 20-30 mm is more preferable.
When the penetration is less than 15 mm, the heat resistant storage stability may be deteriorated.
The penetration can be measured according to JIS K2235-1991. Specifically, a 50 ml glass container is filled with toner and left in a thermostatic bath at 50 ° C. for 20 hours. The penetration can be measured by cooling the toner to room temperature and performing a penetration test. In addition, it has shown that the said heat-resistant preservation | save property is excellent, so that the said penetration value is large.

As the low temperature fixability, from the viewpoint of achieving both a reduction in fixing temperature and no occurrence of offset, a lower fixing lower temperature is preferable, and a higher offset generation temperature is preferable, and both a reduction in fixing temperature and no occurrence of offset are compatible. As a temperature range that can be set, the lower limit fixing temperature is less than 150 ° C., and the offset generation temperature is 200 ° C. or more.
The fixing minimum temperature is, for example, an image forming apparatus, a transfer sheet is set, a copy test is performed, and the obtained fixed image is rubbed with a pad. The fixing roll temperature is the lower limit fixing temperature.
For example, the offset generation temperature may be set by using an image forming apparatus to set a transfer sheet, and develop a single color of yellow, magenta, cyan, and black, and a solid image of red, blue, and green as intermediate colors in each single color. The temperature of the fixing belt can be adjusted to be variable, and the temperature at which no offset occurs can be determined.

The thermal characteristics are also called flow tester characteristics, and are evaluated as, for example, a softening temperature (Ts), an outflow start temperature (Tfb), a 1/2 method softening point (T1 / 2), and the like.
These thermal characteristics can be measured by an appropriately selected method. For example, the thermal characteristics can be obtained from a flow curve measured using an elevated flow tester CFT500 type (manufactured by Shimadzu Corporation).
There is no restriction | limiting in particular as said softening temperature (Ts), According to the objective, it can select suitably, For example, 30 degreeC or more is preferable and 50-120 degreeC is more preferable. When the softening temperature (Ts) is less than 30 ° C., at least one of heat resistant storage stability and low temperature storage stability may deteriorate.
There is no restriction | limiting in particular as said outflow start temperature (Tfb), According to the objective, it can select suitably, For example, 50 degreeC or more is preferable and 60-150 degreeC is more preferable. When the outflow start temperature (Tfb) is less than 50 ° C., at least one of heat resistant storage stability and low temperature storage stability may deteriorate.
The 1/2 method softening point (T1 / 2) is not particularly limited and may be appropriately selected depending on the intended purpose. For example, 60 ° C. or higher is preferable, and 80 to 170 ° C. is more preferable. If the 1/2 method softening point (T1 / 2) is less than 60 ° C., at least one of heat resistant storage stability and low temperature storage stability may be deteriorated.

The image density is, for example, preferably 1.40 or more, more preferably 1.45 or more, and 1.50 or more, as measured by a spectrometer (X-Light, 938 Spectrodensitometer). Is particularly preferred.
If the image density is less than 1.40, the image density may be low and high image quality may not be obtained.
The image density is, for example, an image of 1.00 ± 0.05 mg / cm on the copy paper (TYPE 6000 <70W>; manufactured by Ricoh Co., Ltd.) using imagio Neo 450 (manufactured by Ricoh Co., Ltd.). surface temperature of the fixing roller ² of the solid image was formed at 160 ± 2 ° C., the image density of any six in the obtained solid image, the spectrometer (X- Rite, 938 spectrometer densitometer) a It can measure by using and measuring and calculating the average value.

The BET specific surface area in the toner, for example, preferably ^{0.5~8.0m 2 / g, 0.5~7.5m 2 /} g is more preferable.
When the BET specific surface area is less than 0.5 m ² / g, the organic fine particles remaining on the toner surface become a film or cover the entire toner surface, and the resin fine particles are fixed to the binder resin component inside the toner. While the adhesion to paper may be inhibited and the minimum fixing temperature may be increased, if it exceeds 8.0 m ² / g, the resin fine particles inhibit the exudation of the wax, and the wax releasability effect is exerted. In some cases, offset is not obtained.
The specific surface area of the toner can be measured according to the BET method. For example, the specific surface area measuring device Tristar 3000 (manufactured by Shimadzu Corporation) is used to adsorb nitrogen gas on the sample surface and the BET multipoint method is used. can do.

  The coloration of the toner of the present invention is not particularly limited and can be appropriately selected according to the purpose, and can be at least one selected from black toner, cyan toner, magenta toner and yellow toner. This toner can be obtained by appropriately selecting the type of the colorant.

  Since the toner of the present invention has a small amount of emulsifier, dispersant, ionic impurities, etc. present on the surface, it has excellent charging performance, good environmental stability, excellent low-temperature fixability, and forms a high-quality image. can do. The toner of the present invention includes the adhesive base obtained by reacting the active hydrogen group-containing compound and a polymer capable of reacting with the active hydrogen group-containing compound in an aqueous medium to form particles. And excellent properties such as agglomeration resistance, chargeability, fluidity, transferability, and fixability. Therefore, the toner of the present invention can be suitably used in various fields, and can be more suitably used for image formation by electrophotography. The following toner-containing container, developer, and process of the present invention are described below. It can be particularly suitably used for a cartridge, an image forming apparatus and an image forming method.

(Toner production method)
The toner production method of the present invention includes at least a toner granulation step and a toner washing step, and further includes other steps appropriately selected as necessary.

<Toner granulation process>
The toner granulating step is a step of granulating the toner containing the polyester resin. The toner obtained in the toner granulation step and before drying may be hereinafter referred to as “wet cake” or “filter cake”.
The toner granulation step is not particularly limited as long as it is a step of granulating toner, and is appropriately selected from among steps of granulating toner by a known suspension polymerization method, emulsion polymerization method, dissolution suspension method, and the like. The active hydrogen group-containing compound and the polymer capable of reacting with the active hydrogen group-containing compound are emulsified or dispersed in an aqueous medium and reacted to produce an adhesive substrate. A step of obtaining particles containing at least the adhesive substrate is preferable.

  In the toner granulation step, for example, preparation of an aqueous medium phase, preparation of an organic solvent phase, preparation of an emulsification or dispersion, and others (synthesis of a polymer (prepolymer) capable of reacting with the active hydrogen group-containing compound, Synthesis of the active hydrogen group-containing compound).

The aqueous medium phase can be prepared, for example, by dispersing the resin fine particles in the aqueous medium. There is no restriction | limiting in particular as the addition amount in this aqueous medium of this resin fine particle, According to the objective, it can select suitably, For example, 0.5-10 mass% is preferable.
The organic solvent phase is prepared in the organic solvent by the active hydrogen group-containing compound, the polymer capable of reacting with the active hydrogen group-containing compound, the crystalline polyester resin, the colorant, the release agent, It can be performed by dissolving or dispersing a toner material such as a charge control agent and the unmodified polyester resin.
In the toner material, components other than the polymer (prepolymer) capable of reacting with the active hydrogen group-containing compound are added when the resin fine particles are dispersed in the aqueous medium in the aqueous medium phase preparation. It may be added and mixed in the aqueous medium, or when the toner solution is added to the aqueous medium phase, it may be added to the aqueous medium phase together with the toner solution.

The organic solvent is not particularly limited as long as it is a solvent that can dissolve or disperse the toner raw material, and can be appropriately selected according to the purpose, and has a boiling point of less than 150 ° C. in terms of ease of removal. For example, toluene, xylene, benzene, carbon tetrachloride, methylene chloride, 1,2-dichloroethane, 1,1,2-trichloroethane, trichloroethylene, chloroform, monochlorobenzene, dichloroethylidene, methyl acetate, ethyl acetate, Examples thereof include methyl ethyl ketone and methyl isobutyl ketone. Among these, ethyl acetate, toluene, xylene, benzene, methylene chloride, 1,2-dichloroethane, chloroform, carbon tetrachloride and the like are particularly preferable. These may be used individually by 1 type and may use 2 or more types together.
There is no restriction | limiting in particular as the usage-amount of the said organic solvent, According to the objective, it can select suitably, For example, 40-300 mass parts is preferable with respect to 100 mass parts of said toner raw materials, and 60-140 mass parts is. More preferably, 80-120 mass parts is still more preferable.

The emulsification or dispersion can be prepared by emulsifying or dispersing the previously prepared organic solvent phase in the previously prepared aqueous medium phase. When the active hydrogen group-containing compound and the polymer capable of reacting with the active hydrogen group-containing compound are subjected to an elongation reaction or a crosslinking reaction during the emulsification or dispersion, the adhesive base material is generated.
The adhesive substrate (for example, the urea-modified polyester resin) includes, for example, (1) a polymer that can react with the active hydrogen group-containing compound (for example, the isocyanate group-containing polyester prepolymer (A)). The organic solvent phase is emulsified or dispersed in the aqueous medium phase together with the active hydrogen group-containing compound (for example, the amines (B)) to form a dispersion, and both are extended in the aqueous medium phase. Or (2) the organic solvent phase is emulsified or dispersed in the aqueous medium to which the active hydrogen group-containing compound has been added in advance to form a dispersion, and the aqueous medium It may be generated by extending or cross-linking both in the phase, or (3) after the organic solvent phase is added and mixed in the aqueous medium, the active hydrogen group The organic compound is added to form a dispersion, it may be generated by extension reaction to crosslinking reaction from particle interfaces in the aqueous medium phase. In the case of (3), a modified polyester resin is preferentially produced on the surface of the toner to be produced, and a concentration gradient can be provided in the toner particles.

  The reaction conditions for producing the adhesive base material by the emulsification or dispersion are not particularly limited, depending on the combination of the polymer capable of reacting with the active hydrogen group-containing compound and the active hydrogen group-containing compound. The reaction time is preferably 10 minutes to 40 hours, more preferably 2 hours to 24 hours, and the reaction temperature is preferably 0 to 150 ° C, more preferably 40 to 98 ° C.

  In the aqueous medium phase, as a method for stably forming the dispersion containing a polymer capable of reacting with the active hydrogen group-containing compound (for example, the isocyanate group-containing polyester prepolymer (A)), for example, In an aqueous medium phase, a polymer capable of reacting with the active hydrogen group-containing compound (for example, the isocyanate group-containing polyester prepolymer (A)), the colorant, the release agent, the charge control agent, the unmodified Examples thereof include a method in which the toner material such as polyester resin is added and dispersed by a shearing force.

The dispersion is not particularly limited as a method thereof, and can be appropriately selected using a known disperser. Examples of the disperser include a low-speed shear disperser, a high-speed shear disperser, and a friction type. Examples thereof include a disperser, a high-pressure jet disperser, and an ultrasonic disperser. Among these, a high-speed shearing disperser is preferable in that the particle size of the dispersion can be controlled to 2 to 20 μm.
When the high-speed shearing disperser is used, conditions such as the rotation speed, dispersion time, and dispersion temperature are not particularly limited and can be appropriately selected according to the purpose. For example, the rotation speed is 1 3,000 to 30,000 rpm is preferable, 5,000 to 20,000 rpm is more preferable, and the dispersion time is preferably 0.1 to 5 minutes in the case of a batch system, and the dispersion temperature is under pressure. 0-150 degreeC is preferable and 40-98 degreeC is more preferable. The dispersion temperature is generally easier when the temperature is higher.

In the emulsification or dispersion, the amount of the aqueous medium used is preferably 50 to 2,000 parts by mass, more preferably 100 to 1,000 parts by mass with respect to 100 parts by mass of the toner raw material.
When the amount used is less than 50 parts by mass, the toner is not well dispersed, and toner particles having a predetermined particle size may not be obtained. When the amount exceeds 2,000 parts by mass, the production cost increases. Sometimes.

In the emulsification or dispersion, if necessary, it is preferable to use a dispersant from the viewpoint of sharpening the particle size distribution and performing stable dispersion.
There is no restriction | limiting in particular as said dispersing agent, According to the objective, it can select suitably, For example, surfactant, a poorly water-soluble inorganic compound dispersing agent, a polymeric protective colloid, etc. are mentioned. These may be used individually by 1 type and may use 2 or more types together. Among these, surfactants are preferable.

Examples of the surfactant include an anionic surfactant, a cationic surfactant, a nonionic surfactant, and an amphoteric surfactant.
Examples of the anionic surfactant include alkylbenzene sulfonates, α-olefin sulfonates, phosphate esters and the like, and those having a fluoroalkyl group are preferable. Examples of the anionic surfactant having a fluoroalkyl group include a fluoroalkylcarboxylic acid having 2 to 10 carbon atoms or a metal salt thereof, disodium perfluorooctanesulfonylglutamate, 3- [omega-fluoroalkyl (6 carbon atoms). -11) Oxy] -1-alkyl (carbon number 3-4) sodium sulfonate, 3- [omega-fluoroalkanoyl (carbon number 6-8) -N-ethylamino] -1-propanesulfonic acid sodium, fluoroalkyl (Carbon number 11-20) carboxylic acid or its metal salt, perfluoroalkyl carboxylic acid (carbon number 7-13) or its metal salt, perfluoroalkyl (carbon number 4-12) sulfonic acid or its metal salt, perfluoro Octanesulfonic acid diethanolamide, N-propyl-N- (2-hydroxy Ethyl) perfluorooctanesulfonamide, perfluoroalkyl (carbon number 6-10) sulfonamidopropyltrimethylammonium salt, perfluoroalkyl (carbon number 6-10) -N-ethylsulfonylglycine salt, monoperfluoroalkyl (carbon number) 6-16) Ethyl phosphate and the like. Examples of commercially available surfactants having a fluoroalkyl group include Surflon S-111, S-112, S-113 (Asahi Glass Co., Ltd.); Fluorard FC-93, FC-95, FC-98, FC- 129 (manufactured by Sumitomo 3M); Unidyne DS-101, DS-102 (manufactured by Daikin Industries); Megafac F-110, F-120, F-113, F-191, F-812, F-833 (large) Nihon Ink Co., Ltd.); Xtop EF-102, 103, 104, 105, 112, 123A, 123B, 306A, 501, 201, 204 (manufactured by Tochem Products Co.); Footent F-100, F150 (Neos) Manufactured) and the like.

  Examples of the cationic surfactant include amine salt type surfactants and quaternary ammonium salt type cationic surfactants. Examples of the amine salt type surfactant include alkylamine salts, aminoalcohol fatty acid derivatives, polyamine fatty acid derivatives, imidazolines, and the like. Examples of the quaternary ammonium salt type cationic surfactant include alkyltrimethylammonium salt, dialkyldimethylammonium salt, alkyldimethylbenzylammonium salt, pyridinium salt, alkylisoquinolinium salt, benzethonium chloride and the like. . Among the cationic surfactants, aliphatic quaternary ammonium such as aliphatic primary, secondary or tertiary amine acids having a fluoroalkyl group, perfluoroalkyl (6 to 10 carbon atoms) sulfonamidopropyltrimethylammonium salt, etc. Salts, benzalkonium salts, benzethonium chloride, pyridinium salts, imidazolinium salts, and the like. Commercially available products of the cationic surfactant include, for example, Surflon S-121 (manufactured by Asahi Glass Co., Ltd.); Florard FC-135 (manufactured by Sumitomo 3M); F-824 (manufactured by Dainippon Ink Co., Ltd.); Xtop EF-132 (manufactured by Tochem Products); Footgent F-300 (manufactured by Neos).

Examples of the nonionic surfactant include fatty acid amide derivatives and polyhydric alcohol derivatives.
Examples of the amphoteric surfactant include alanine, dodecyldi (aminoethyl) glycine, di (octylaminoethyl) glycine, N-alkyl-N, N-dimethylammonium betaine, and the like.

Examples of the poorly water-soluble inorganic compound dispersant include tricalcium phosphate, calcium carbonate, titanium oxide, colloidal silica, and hydroxyapatite.
Examples of the polymeric protective colloid include acids, (meth) acrylic monomers containing hydroxyl groups, vinyl alcohol or ethers of vinyl alcohol, esters of vinyl alcohol and compounds containing carboxyl groups, amides Examples thereof include homopolymers or copolymers such as compounds or their methylol compounds, chlorides, those having a nitrogen atom or a heterocyclic ring thereof, polyoxyethylenes, and celluloses.
Examples of the acids include acrylic acid, methacrylic acid, α-cyanoacrylic acid, α-cyanomethacrylic acid, itaconic acid, crotonic acid, fumaric acid, maleic acid, maleic anhydride, and the like. Examples of the (meth) acrylic monomer containing a hydroxyl group include β-hydroxyethyl acrylate, β-hydroxyethyl methacrylate, β-hydroxypropyl acrylate, β-hydroxypropyl methacrylate, and γ-acrylate. -Hydroxypropyl, γ-hydroxypropyl methacrylate, 3-chloro-2-hydroxypropyl acrylate, 3-chloro-2-hydroxypropyl methacrylate, diethylene glycol monoacrylate, diethylene glycol monomethacrylate, glycerol monoacrylate Glycerin monomethacrylic acid ester, N-methylol acrylamide, N-methylol methacrylamide and the like. Examples of the vinyl alcohol or ethers with vinyl alcohol include vinyl methyl ether, vinyl ethyl ether, vinyl propyl ether, and the like. Examples of the esters of vinyl alcohol and a compound containing a carboxyl group include vinyl acetate, vinyl propionate, and vinyl butyrate. Examples of the amide compound or these methylol compounds include acrylamide, methacrylamide, diacetone acrylamide acid, or these methylol compounds. Examples of the chlorides include acrylic acid chloride and methacrylic acid chloride. Examples of the homopolymer or copolymer such as those having a nitrogen atom or a heterocyclic ring thereof include vinyl pyridine, vinyl pyrrolidone, vinyl imidazole, and ethylene imine. Examples of the polyoxyethylene are polyoxyethylene, polyoxypropylene, polyoxyethylene alkylamine, polyoxypropylene alkylamine, polyoxyethylene alkylamide, polyoxypropylene alkylamide, polyoxyethylene nonylphenyl ether, polyoxyethylene Examples thereof include oxyethylene lauryl phenyl ether, polyoxyethylene stearyl phenyl ester, and polyoxyethylene nonyl phenyl ester. Examples of the celluloses include methyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, and the like.

In the preparation of the emulsification or dispersion, a dispersion stabilizer can be used as necessary.
Examples of the dispersion stabilizer include acids that are soluble in acids and alkalis such as calcium phosphate.
When the dispersion stabilizer is used, the calcium phosphate salt can be removed from the fine particles by a method of dissolving the calcium phosphate salt with an acid such as hydrochloric acid and then washing with water or a method of decomposing with an enzyme.

  In the preparation of the emulsification or dispersion, a catalyst for the extension reaction or the crosslinking reaction can be used. Examples of the catalyst include dibutyltin laurate and dioctyltin laurate.

The organic solvent is removed from the obtained dispersion (emulsified slurry). The organic solvent is removed by (1) a method in which the whole reaction system is gradually heated to completely evaporate and remove the organic solvent in the droplets, and (2) the emulsion dispersion is sprayed into a dry atmosphere. And a method of completely removing the water-insoluble organic solvent in the droplets to form toner fine particles and evaporating and removing the aqueous dispersant together.
The dry atmosphere in which the emulsified dispersion is sprayed is not particularly limited and may be appropriately selected depending on the intended purpose.For example, a gas obtained by heating air, nitrogen, carbon dioxide gas, combustion gas, etc., in particular, is used. Among the solvents, various air streams heated to a temperature equal to or higher than the boiling point of the solvent having the highest boiling point can be used. Moreover, you may form a dry atmosphere by a short time process using a spray dryer, a belt dryer, a rotary kiln, etc.
When the organic solvent is removed, toner particles are formed.

  Through the above steps, the toner containing the polyester resin is granulated.

<Toner cleaning process>
In the toner cleaning step, the toner granulated in the toner granulation step is extracted until the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner is 200 ppm / g or less. This is a step of at least alkali cleaning. By this toner cleaning step, the emulsifier, dispersant, ionic impurities, etc. present on the surface of the toner or the resin fine particles can be removed, and the charging performance can be improved.
The toner obtained by the toner washing step and before the external additive treatment may be hereinafter referred to as “toner base particles”.
In addition, ppm / g means the amount of carbon in the organic component extracted from 1 g of dry toner. In the case where the alkali cleaning is performed a plurality of times, the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner after at least the final alkali cleaning is 200 ppm / g or less. is necessary.

  In the toner cleaning step, it is preferable that the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner after alkali cleaning is smaller, for example, at least until it becomes 200 ppm / g or less. The alkali cleaning is necessary, and is preferably 150 ppm / g or less, and more preferably 100 ppm / g or less. When the TOC amount exceeds 200 ppm / g, the charging performance may be inferior, and in particular, the rising charging speed and the charging performance under high temperature and high humidity may be deteriorated.

As an analysis method of the total organic carbon elution amount (total organic carbon (TOC) amount), for example, a total organic carbon meter (“TOC-5000A”; manufactured by Shimadzu Corporation) is used, and the toner after alkali cleaning is used. It can be measured by determining the amount of carbon extracted from, specifically, it can be measured by the following method. That is,
First, (1) when the sample to be measured is a wet cake or a dispersion, the solid content (% by mass) of the sample is measured. When the sample is a solid toner, the solid content is 100% by mass. (2) 7.5 g of the sample (wet cake, dispersion liquid, toner, etc.) is precisely weighed in a 140 ml bottle (this is S1), and (3) 47 KOHaq (aqueous solution) having a pH of 9 is added to (2). (4) Apply ultrasonic waves at 30 ° C. or lower for 30 minutes, (5) centrifuge approximately 1.5 ml in a microtube, and (6) obtained in (5) above. The supernatant in the obtained separated product is filtered using a 0.2 μ micro filter, ultrafine particles are removed and returned to the micro tube. (7) After the filter is washed with tap water and pure water, (5) The precipitate in the separated product obtained in (1) is filtered through a 1 μm filter, and (8) 2 drops of HCl (35% by mass) aq is added to the filtrate obtained in (7), so that the pH becomes 3 or less. (9) The solution obtained in (8) above is Weigh (referred to as T1), (10) Add pure water to the solution obtained in (8) above, dilute to 6.0 mg, and weigh precisely (referred to as T2) (10) The obtained treatment liquid is burned at a high temperature, carbon in an organic substance contained in the treatment liquid is generated as carbon dioxide gas, and the carbon dioxide gas is analyzed with infrared rays to measure the TOC amount. (This is referred to as a TOC measurement value) (11) The TOC amount can be calculated based on the following mathematical formula.
<Formula>
TOC (ppm / g) = TOC measurement value × (S1 + S2) / {S1 × (solid content (mass%) / 100)} × T2 / T1

The toner cleaning method is not particularly limited as long as at least alkali cleaning is performed, and can be appropriately selected according to the purpose. For example, after alkali cleaning, water cleaning, acid cleaning, water cleaning, A method of washing with water, washing with acid, washing with water and washing with alkali after alkali washing is preferable.
By performing the alkali cleaning, it is possible to remove emulsifiers, dispersants, ionic impurities, and the like present on the toner particle surfaces.
In particular, in the toner, the particles containing at least the adhesive substrate are used as a dispersion (emulsification) stabilizer in order to sharpen the particle size distribution. However, if the resin particles are excessively present on the toner surface. In addition to hindering the fixing property, the charging property may be adversely affected. In this respect, since the resin fine particles contain an acidic component, they can be easily removed by swelling or dissolving by alkali washing. Moreover, although the said amines are used for the production | generation of the said adhesive base material, unreacted amines form an association with the acidic group (carboxyl group) in the said polyester resin, and elongation reaction after emulsification is carried out. In addition to the smooth progress, the acidity of the polyester resin may be lowered, and the chargeability may be impaired or the adhesion to paper may be reduced. In this regard, when the alkali cleaning is performed, the hydrogen atom of the terminal carboxyl group in the polyester resin is replaced with Na atom, and then the acid cleaning is performed to restore the terminal carboxyl group in the polyester resin, and the extension reaction. Can proceed again.

-Alkaline cleaning-
In the alkali cleaning, the pH of the cleaning liquid after alkali cleaning is preferably 6.0 to 11.0, and more preferably 8.0 to 10.0, for example. If the pH is less than 6.0, it may not be possible to improve the charging performance and ensure the environmental stability by alkali washing, and if it exceeds 11.0, hydrolysis reaction of the polyester resin may occur. Therefore, it is not preferable.

  The temperature T (° C.) during the alkali cleaning is not particularly limited as long as the toner does not melt or coalesce, and can be appropriately selected according to the purpose, but is generally about 10 to 70 ° C. For example, 15 to 60 ° C. is preferable, and when the glass transition temperature of the toner is Tg (° C.), (Tg−10) ≦ T ≦ (Tg + 10) is more preferable. When the temperature at the time of washing is near the glass transition temperature Tg, the charging performance of the toner is further improved. This is because, since the polymer chain is moving at a temperature near the glass transition temperature Tg, impurities incorporated in the matrix or in the vicinity of the toner surface are easily washed, and carboxylic acid groups that contribute to charging, etc. It is conceivable that the polar group is easily exposed on the surface.

The alkali washing time is not particularly limited as long as the hydrolysis reaction of the polyester resin does not occur, and can be appropriately selected depending on the purpose. In terms of improving work efficiency, for example, 1 to 72 hours are preferable, and 1 to 30 hours are more preferable.
The number of times of alkali washing is not particularly limited and may be appropriately selected according to the purpose. However, it is preferable to carry out the washing several times from the viewpoint of obtaining a toner excellent in charging property and fixing property.

  In the alkali cleaning, it is preferable that the hydrogen atom of the terminal carboxyl group in the polyester resin in the toner after the alkali cleaning is substituted with Na atom. When the alkali cleaning is performed, the hydrogen atom of the terminal carboxyl group in the polyester resin is replaced with Na atom to become (-COONa), and thus a toner having excellent charging performance and good rise resistance can be obtained.

  The alkali cleaning solution is not particularly limited as long as it is an alkaline aqueous solution, and can be appropriately selected from known compounds, such as alkali metal salts such as sodium hydroxide and potassium hydroxide, ammonia and the like. An aqueous solution may be mentioned. These may be used individually by 1 type and may use 2 or more types together. Among these, a sodium hydroxide aqueous solution is preferable.

The cleaning liquid after the alkali cleaning is preferably subjected to solid-liquid separation. When the alkali cleaning is performed, impurities (such as resin fine particles to be described later) come off as solid particles from the toner surface. At this time, if the cleaning liquid is filtered while containing the impurities, the impurities are also collected together with the toner and coexist in the toner.
The solid-liquid separation method is not particularly limited and may be appropriately selected depending on the intended purpose. For example, a decanter (precipitation separation device) can be preferably used.

-Washing-
The water cleaning is preferably performed after the alkali cleaning or the acid cleaning. If the acid cleaning is performed without performing the water cleaning after the alkali cleaning, the anionic impurities are reattached before being completely cleaned, the cleaning becomes insufficient, and charging performance is improved and environmental stability is ensured. I can not plan.
As the cleaning liquid for the water cleaning, for example, ion exchange water is preferable.

The conductivity of the cleaning liquid after the alkali cleaning, solid-liquid separation, and water cleaning is preferably, for example, 0.5 to 60 μS / cm, and more preferably 2 to 20 μS / cm. If the conductivity is less than 0.5 μS / cm or exceeds 60 μS / cm, the charging performance may not be improved.
In order to set the conductivity of the cleaning liquid within the numerical range, it is important to remove anionic impurities present on the surfaces of the toner and the resin fine particles. In order to prevent this, it is preferable to perform water washing after the alkali washing.

-Acid cleaning-
In the acid cleaning, the pH of the cleaning liquid (slurry during acid cleaning) at the time of acid cleaning is preferably 1 to 5, for example, and more preferably 1 to 4.
From the viewpoint of improving charging performance and ensuring environmental stability, the conductivity of the cleaning liquid after the acid cleaning is important as in the alkali cleaning. That is, the conductivity of the cleaning liquid after the acid cleaning is preferably 60 μS / cm or less, for example. If the conductivity exceeds 60 μS / cm, the charging performance may not be improved.
In order to set the conductivity of the cleaning liquid within the numerical range, it is important to remove the cationic impurities. In order to prevent this, it is preferable to perform water washing after the acid washing.
The temperature and time for acid cleaning are the same as in the alkali cleaning.

In the acid cleaning, it is preferable that the terminal carboxyl group in the polyester resin in the toner after the acid cleaning is not substituted (is —COOH). When the terminal carboxyl group is not substituted, that is, (—COOH), the polarity of the polyester resin is increased, so that the affinity for paper is increased and the minimum fixing temperature can be lowered. At the same time, the charging polarity of the toner can be increased to negative charging.
The acid cleaning solution is not particularly limited as long as it is an acidic aqueous solution, and can be appropriately selected from known compounds. Examples thereof include aqueous solutions of hydrochloric acid, acetic acid, phosphoric acid, nitric acid, and the like. These may be used individually by 1 type and may use 2 or more types together. Among these, hydrochloric acid and nitric acid are preferable.

  Through the above steps, until the toner granulated in the toner granulation step has a total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner of 200 ppm / g or less, At least washed with alkali.

<Other processes>
The washed toner particles can be dried or the like, and then classified or the like as desired. The classification can be performed, for example, by removing the fine particle portion by a cyclone, decanter, centrifugation, or the like in the liquid, and the classification operation may be performed after obtaining the powder after drying. It is preferable to carry out in a liquid. At that time, the obtained unnecessary fine particles and coarse particles can be returned to the kneading step and used for the formation of particles. The fine particles or the coarse particles may be in a wet state.

The toner particles thus obtained are mixed with particles of the colorant, release agent, charge control agent, etc. (external additive treatment), and a mechanical impact force is applied to the toner particles. It is possible to prevent the particles such as the release agent from detaching from the surface.
Hereinafter, the toner after the external additive treatment may be simply referred to as “toner”.
As the method for applying the mechanical impact force, for example, a method in which an impact force is applied to the mixture by blades rotating at a high speed, a mixture is introduced into a high-speed air stream and accelerated to appropriately collide particles or composite particles. The method of making it collide with a board, etc. are mentioned. As an apparatus used for this method, for example, an ong mill (manufactured by Hosokawa Micron), an I-type mill (manufactured by Nippon Pneumatic Co., Ltd.) to reduce the pulverization air pressure, a hybridization system (Nara Machinery Co., Ltd.) Product), kryptron system (manufactured by Kawasaki Heavy Industries, Ltd.), automatic mortar, and the like.

  Through the above steps, the toner washed in the toner washing step is dried and classified to produce a toner.

  According to the toner manufacturing method of the present invention, the toner granulated in the toner granulation step has a total organic carbon elution amount (TOC amount) extracted from the toner in the toner washing step of 200 ppm / g. Since it is washed with alkali until the following, the emulsifier, dispersant, ionic impurities, etc. present on the surface of the toner or resin fine particles are removed, the charging performance is excellent, the environmental stability is good, and the low temperature fixability It is possible to efficiently produce a toner that is excellent in quality and can provide high image quality.

(Developer)
The developer of the present invention contains at least the toner of the present invention and other components appropriately selected such as the carrier. The developer may be a one-component developer or a two-component developer. However, when it is used for a high-speed printer or the like corresponding to the recent improvement in information processing speed, the life is improved. In view of the above, the two-component developer is preferable.
In the case of the one-component developer using the toner of the present invention, even if the balance of the toner is performed, there is little fluctuation in the particle diameter of the toner, and the filming of the toner on the developing roller or the toner is made thin. Therefore, toner is not fused to a member such as a blade, and good and stable developability and images can be obtained even when the developing device is used (stirred) for a long time. Further, in the case of the two-component developer using the toner of the present invention, even if the balance of the toner over a long period of time is performed, the fluctuation of the toner particle diameter in the developer is small, and even in the long-term stirring in the developing device, Good and stable developability can be obtained.

  There is no restriction | limiting in particular as said carrier, Although it can select suitably according to the objective, What has a core material and the resin layer which coat | covers this core material is preferable.

  There is no restriction | limiting in particular as a material of the said core material, It can select suitably from well-known things, For example, 50-90 emu / g manganese-strontium (Mn-Sr) type material, manganese-magnesium (Mn-) Mg) -based materials and the like are preferable, and high magnetization materials such as iron powder (100 emu / g or more) and magnetite (75 to 120 emu / g) are preferable in terms of securing image density. In addition, a weakly magnetized material such as a copper-zinc (Cu—Zn) -based (30 to 80 emu / g) is advantageous in that it can weaken the contact with the photoconductor in which the toner is in a spiked state and is advantageous in improving the image quality. Is preferred. These may be used alone or in combination of two or more.

The core material has a volume average particle size of preferably 10 to 150 μm, and more preferably 40 to 100 μm.
When the average particle size (volume average particle size (D ₅₀ )) is less than 10 μm, in the distribution of carrier particles, the number of fine powder systems increases, and the magnetization per particle may be lowered to cause carrier scattering. If the thickness exceeds 150 μm, the specific surface area may decrease and toner scattering may occur. In the case of a full color with many solid portions, reproduction of the solid portions may be particularly poor.

  The material of the resin layer is not particularly limited and can be appropriately selected from known resins according to the purpose. For example, amino resins, polyvinyl resins, polystyrene resins, halogenated olefin resins, Polyester resin, polycarbonate resin, polyethylene resin, polyvinyl fluoride resin, polyvinylidene fluoride resin, polytrifluoroethylene resin, polyhexafluoropropylene resin, copolymer of vinylidene fluoride and acrylic monomer, vinylidene fluoride And a copolymer of vinyl fluoride, a fluoroterpolymer such as a terpolymer of tetrafluoroethylene, vinylidene fluoride, and a non-fluorinated monomer, and a silicone resin. These may be used individually by 1 type and may use 2 or more types together.

  Examples of the amino resin include urea-formaldehyde resin, melamine resin, benzoguanamine resin, urea resin, polyamide resin, and epoxy resin. Examples of the polyvinyl resin include acrylic resin, polymethyl methacrylate resin, poly Examples include acrylonitrile resin, polyvinyl acetate resin, polyvinyl alcohol resin, and polyvinyl butyral resin. Examples of the polystyrene resin include polystyrene resin and styrene acrylic copolymer resin. Examples of the halogenated olefin resin include polyvinyl chloride. Examples of the polyester resin include polyethylene terephthalate resin and polybutylene terephthalate resin.

  The resin layer may contain conductive powder or the like, if necessary. Examples of the conductive powder include metal powder, carbon black, titanium oxide, tin oxide, and zinc oxide. The average particle diameter of these conductive powders is preferably 1 μm or less. When the average particle diameter exceeds 1 μm, it may be difficult to control electric resistance.

For example, the resin layer is prepared by dissolving the silicone resin or the like in a solvent to prepare a coating solution, and then uniformly coating the coating solution on the surface of the core material by a known coating method, drying, and baking. It can be formed by doing. Examples of the coating method include a dipping method, a spray method, and a brush coating method.
There is no restriction | limiting in particular as said solvent, Although it can select suitably according to the objective, For example, toluene, xylene, methyl ethyl ketone, methyl isobutyl ketone, cersol butyl acetate, etc. are mentioned.
The baking is not particularly limited, and may be an external heating method or an internal heating method. For example, a stationary electric furnace, a fluid electric furnace, a rotary electric furnace, a burner furnace, etc. The method of using, the method of using a microwave, etc. are mentioned.

The amount of the resin layer in the carrier is preferably 0.01 to 5.0% by mass.
When the amount is less than 0.01% by mass, the uniform resin layer may not be formed on the surface of the core material. When the amount exceeds 5.0% by mass, the resin layer becomes thick. In some cases, granulation of carriers occurs, and uniform carrier particles may not be obtained.

  When the developer is the two-component developer, the content of the carrier in the two-component developer is not particularly limited and may be appropriately selected depending on the intended purpose. For example, 90 to 98% by mass Is preferable, and 93-97 mass% is more preferable.

Since the developer of the present invention contains the toner, it is excellent in charging performance, low-temperature fixability, etc., and can stably form a high-quality image.
The developer of the present invention can be suitably used for image formation by various known electrophotographic methods such as a magnetic one-component development method, a non-magnetic one-component development method, and a two-component development method. It can be particularly suitably used for containers, process cartridges, image forming apparatuses and image forming methods.

(Toner container)
The toner-containing container of the present invention is formed by filling the container of the toner of the present invention or the developer.
There is no restriction | limiting in particular as said container, It can select suitably from well-known things, For example, what has a container main body and a cap containing a toner etc. are mentioned suitably.
The size, shape, structure, material, etc. of the container body containing toner is not particularly limited and can be appropriately selected according to the purpose. For example, the shape is preferably cylindrical. The spiral surface irregularities are formed on the peripheral surface, and the toner as the contents can be transferred to the discharge port side by rotating, and part or all of the spiral part has a bellows function, etc. Is particularly preferred.
The material of the toner-containing container body is not particularly limited, and those having good dimensional accuracy are preferable. For example, a resin is preferably used. Among them, for example, polyester resin, polyethylene resin, polypropylene resin, polystyrene resin, Preferable examples include vinyl chloride resin, polyacrylic acid, polycarbonate resin, ABS resin, polyacetal resin, and the like.
The toner-containing container of the present invention is easy to store and transport, has excellent handleability, and is preferably used for replenishing toner by being detachably attached to the process cartridge and image forming apparatus of the present invention described later. Can do.

(Process cartridge)
The process cartridge of the present invention develops an electrostatic latent image carrier carrying an electrostatic latent image and the electrostatic latent image carried on the electrostatic latent image carrier using a developer to form a visible image. At least a developing means for forming the film, and other means appropriately selected as necessary.
The developing means includes a developer container that contains the toner or developer of the present invention, and a developer carrier that carries and transports the toner or developer contained in the developer container. And a layer thickness regulating member for regulating the thickness of the toner layer to be carried.
The process cartridge of the present invention can be detachably provided in various electrophotographic apparatuses, and is preferably detachably provided in the electrophotographic apparatus of the present invention described later.

(Image forming method and image forming apparatus)
The image forming method of the present invention includes at least an electrostatic latent image forming step, a developing step, a transfer step, and a fixing step, and further other steps appropriately selected as necessary, for example, a static elimination step, a cleaning step, Includes recycling and control processes.
The image forming apparatus of the present invention includes at least an electrostatic latent image carrier, an electrostatic latent image forming unit, a developing unit, a transfer unit, and a fixing unit, and further appropriately selected as necessary. It has other means, for example, static elimination means, cleaning means, recycling means, control means and the like.

-Electrostatic latent image forming step and electrostatic latent image forming means-
The electrostatic latent image forming step is a step of forming an electrostatic latent image on the electrostatic latent image carrier.
There are no particular restrictions on the material, shape, structure, size, etc. of the electrostatic latent image bearing member (sometimes referred to as “photoconductive insulator” or “photosensitive member”), and among the known ones The shape is preferably a drum shape, and examples of the material include inorganic photoconductors such as amorphous silicon and selenium, and organic photoconductors such as polysilane and phthalopolymethine. It is done. Among these, amorphous silicon or the like is preferable in terms of long life.

The formation of the electrostatic latent image can be performed, for example, by uniformly charging the surface of the electrostatic latent image carrier and then performing imagewise exposure, and is performed by the electrostatic latent image forming unit. be able to.
The electrostatic latent image forming means includes, for example, at least a charger that uniformly charges the surface of the electrostatic latent image carrier and an exposure device that exposes the surface of the electrostatic latent image carrier imagewise. Prepare.

The charging can be performed, for example, by applying a voltage to the surface of the electrostatic latent image carrier using the charger.
The charger is not particularly limited and may be appropriately selected depending on the purpose. And a non-contact charger using corona discharge such as a corotron and a scorotron.

The exposure can be performed, for example, by exposing the surface of the latent electrostatic image bearing member imagewise using the exposure device.
The exposure device is not particularly limited as long as it can expose the surface of the electrostatic latent image carrier charged by the charger so as to form an image to be formed, and is appropriately selected according to the purpose. For example, various exposure devices such as a copying optical system, a rod lens array system, a laser optical system, and a liquid crystal shutter optical system can be used.
In the present invention, a back light system in which imagewise exposure is performed from the back surface side of the electrostatic latent image carrier may be adopted.

-Development process and development means-
The developing step is a step of developing the electrostatic latent image using the toner or the developer of the present invention to form a visible image.
The visible image can be formed, for example, by developing the electrostatic latent image using the toner or the developer of the present invention, and can be performed by the developing unit.
The developing unit is not particularly limited as long as it can be developed using, for example, the toner or the developer of the present invention, and can be appropriately selected from known ones. For example, the toner of the present invention Preferred examples include a developer containing at least a developer, and at least a developing device capable of contacting or non-contacting the toner or the developer with the electrostatic latent image. More preferred is a developing device.

  The developing unit may be a dry developing type, a wet developing type, a single color developing unit, or a multi-color developing unit. For example, a toner having a stirrer for charging the toner or the developer by frictional stirring and a rotatable magnet roller is preferable.

  In the developing device, for example, the toner and the carrier are mixed and agitated, and the toner is charged by friction at that time, and held on the surface of the rotating magnet roller in a raised state to form a magnetic brush. . Since the magnet roller is disposed in the vicinity of the electrostatic latent image carrier (photoconductor), a part of the toner constituting the magnetic brush formed on the surface of the magnet roller is electrically attracted. It moves to the surface of the electrostatic latent image carrier (photoconductor) by force. As a result, the electrostatic latent image is developed with the toner, and a visible image is formed with the toner on the surface of the electrostatic latent image carrier (photoconductor).

  The developer accommodated in the developing device is a developer containing the toner of the present invention, but the developer may be a one-component developer or a two-component developer. The toner contained in the developer is the toner of the present invention.

-Transfer process and transfer means-
The transfer step is a step of transferring the visible image onto a recording medium. After the primary transfer of the visible image onto the intermediate transfer member using an intermediate transfer member, the visible image is transferred onto the recording medium. A primary transfer step of forming a composite transfer image by transferring a visible image onto an intermediate transfer body using two or more colors, preferably full color toner as the toner, and a composite transfer image; A mode including a secondary transfer step of transferring the transfer image onto the recording medium is more preferable.
The transfer can be performed, for example, by charging the latent electrostatic image bearing member (photoconductor) of the visible image using a transfer charger, and can be performed by the transfer unit. The transfer means includes a primary transfer means for transferring a visible image onto an intermediate transfer member to form a composite transfer image, and a secondary transfer means for transferring the composite transfer image onto a recording medium. Embodiments are preferred.
The intermediate transfer member is not particularly limited and may be appropriately selected from known transfer members according to the purpose. For example, a transfer belt and the like are preferable.

The transfer means (the primary transfer means, the secondary transfer means) is a transfer for peeling and charging the visible image formed on the electrostatic latent image carrier (photoconductor) to the recording medium side. It is preferable to have at least a vessel. There may be one transfer means or two or more transfer means.
Examples of the transfer device include a corona transfer device using corona discharge, a transfer belt, a transfer roller, a pressure transfer roller, and an adhesive transfer device.
The recording medium is not particularly limited and can be appropriately selected from known recording media (recording paper).

-Fixing process and fixing means-
The fixing step is a step of fixing the visible image transferred to the recording medium using a fixing unit, and may be performed each time the toner of each color is transferred to the recording medium, or for the toner of each color. You may perform this simultaneously in the state which laminated | stacked this.
The fixing unit is not particularly limited and may be appropriately selected depending on the intended purpose, but a known heating and pressing unit is preferable. Examples of the heating and pressing means include a combination of a heating roller and a pressure roller, a combination of a heating roller, a pressure roller, and an endless belt.
The heating in the heating and pressurizing means is usually preferably 80 ° C to 200 ° C.
In the present invention, for example, a known optical fixing device may be used together with or in place of the fixing step and the fixing unit depending on the purpose.

The neutralization step is a step of performing neutralization by applying a neutralization bias to the electrostatic latent image carrier, and can be suitably performed by a neutralization unit.
The neutralizing means is not particularly limited and may be appropriately selected from known neutralizers as long as it can apply a neutralizing bias to the latent electrostatic image bearing member. Preferably mentioned.

The cleaning step is a step of removing the electrophotographic toner remaining on the electrostatic latent image carrier, and can be suitably performed by a cleaning unit.
The cleaning means is not particularly limited as long as it can remove the electrophotographic toner remaining on the electrostatic latent image carrier, and can be appropriately selected from known cleaners. Suitable examples include brush cleaners, electrostatic brush cleaners, magnetic roller cleaners, blade cleaners, brush cleaners, web cleaners, and the like.

The recycling step is a step of recycling the electrophotographic color toner removed in the cleaning step to the developing unit, and can be suitably performed by the recycling unit.
There is no restriction | limiting in particular as said recycling means, A well-known conveyance means etc. are mentioned.

The control means is a process for controlling the respective steps, and can be suitably performed by the control means.
The control means is not particularly limited as long as the movement of each means can be controlled, and can be appropriately selected according to the purpose. Examples thereof include devices such as a sequencer and a computer.

  One mode for carrying out the image forming method of the present invention by the image forming apparatus of the present invention will be described with reference to FIG. An image forming apparatus 100 shown in FIG. 1 includes a photosensitive drum 10 (hereinafter referred to as “photosensitive member 10”) as the electrostatic latent image carrier, a charging roller 20 as the charging unit, and exposure as the exposure unit. The apparatus 30 includes a developing device 40 as the developing means, an intermediate transfer member 50, a cleaning device 60 as the cleaning means having a cleaning blade, and a static elimination lamp 70 as the static elimination means.

  The intermediate transfer member 50 is an endless belt, and is designed to be movable in the direction of an arrow by three rollers 51 that are arranged inside and stretched. Part of the three rollers 51 also functions as a transfer bias roller that can apply a predetermined transfer bias (primary transfer bias) to the intermediate transfer member 50. The intermediate transfer body 50 is provided with a cleaning device 90 having a cleaning blade in the vicinity thereof, and for transferring (secondary transfer) a developed image (toner image) to a transfer sheet 95 as a final transfer material. A transfer roller 80 serving as a transfer unit to which a transfer bias can be applied is disposed to face the transfer roller 80. Around the intermediate transfer member 50, a corona charger 58 for applying a charge to the toner image on the intermediate transfer member 50 is formed between the photosensitive member 10 and the intermediate transfer member 50 in the rotation direction of the intermediate transfer member 50. It is arranged between the contact portion and the contact portion between the intermediate transfer member 50 and the transfer paper 95.

  The developing device 40 includes a developing belt 41 as the developer carrying member, and a black developing unit 45K, a yellow developing unit 45Y, a magenta developing unit 45M, and a cyan developing unit 45C provided around the developing belt 41. . The black developing unit 45K includes a developer accommodating portion 42K, a developer supplying roller 43K, and a developing roller 44K. The yellow developing unit 45Y includes a developer accommodating portion 42Y, a developer supplying roller 43Y, and a developing roller 44Y. The magenta developing unit 45M includes a developer accommodating portion 42M, a developer supplying roller 43M, and a developing roller 44M, and the cyan developing unit 45C includes a developer accommodating portion 42C and a developer supplying roller 43C. And a developing roller 44C. The developing belt 41 is an endless belt, is rotatably stretched around a plurality of belt rollers, and a part thereof is in contact with the photoconductor 10.

  In the image forming apparatus 100 shown in FIG. 1, for example, the charging roller 20 charges the photosensitive drum 10 uniformly. The exposure device 30 performs imagewise exposure on the photosensitive drum 10 to form an electrostatic latent image. The electrostatic latent image formed on the photosensitive drum 10 is developed by supplying toner from the developing device 40 to form a visible image (toner image). The visible image (toner image) is transferred (primary transfer) onto the intermediate transfer member 50 by the voltage applied from the roller 51, and further transferred (secondary transfer) onto the transfer paper 95. As a result, a transfer image is formed on the transfer paper 95. The residual toner on the photoconductor 10 is removed by the cleaning device 60, and the charge on the photoconductor 10 is temporarily removed by the charge eliminating lamp 70.

  Another mode for carrying out the image forming method of the present invention by the image forming apparatus of the present invention will be described with reference to FIG. The image forming apparatus 100 shown in FIG. 2 does not include the developing belt 41 in the image forming apparatus 100 shown in FIG. 1, and a black developing unit 45K, a yellow developing unit 45Y, a magenta developing unit 45M, and Except for the fact that the cyan developing unit 45C is disposed directly opposite, it has the same configuration as the image forming apparatus 100 shown in FIG. In FIG. 2, the same components as those in FIG. 1 are denoted by the same reference numerals.

Another mode for carrying out the image forming method of the present invention by the image forming apparatus of the present invention will be described with reference to FIG. An image forming apparatus 100 shown in FIG. 3 is a tandem color image forming apparatus. The tandem image forming apparatus 100 includes a copying apparatus main body 150, a paper feed table 200, a scanner 300, and an automatic document feeder (ADF) 400.
The copying apparatus main body 150 is provided with an endless belt-like intermediate transfer member 50 at the center. The intermediate transfer member 50 is stretched around the support rollers 14, 15, and 16 and can be rotated clockwise in FIG. 3. An intermediate transfer body cleaning device 17 for removing residual toner on the intermediate transfer body 50 is disposed in the vicinity of the support roller 15. The intermediate transfer body 50 stretched by the support roller 14 and the support roller 15 is a tandem type in which four image forming means 18 of yellow, cyan, magenta, and black are arranged in parallel and facing each other along the conveyance direction. A developing device 120 is disposed. An exposure device 21 is disposed in the vicinity of the tandem developing device 120. A secondary transfer device 22 is disposed on the side of the intermediate transfer member 50 opposite to the side on which the tandem developing device 120 is disposed. In the secondary transfer device 22, a secondary transfer belt 24, which is an endless belt, is stretched around a pair of rollers 23, and the transfer paper conveyed on the secondary transfer belt 24 and the intermediate transfer body 50 are in contact with each other. Is possible. A fixing device 25 is disposed in the vicinity of the secondary transfer device 22. The fixing device 25 includes a fixing belt 26 that is an endless belt, and a pressure roller 27 that is pressed against the fixing belt 26.
In the tandem image forming apparatus 100, a sheet reversing device 28 for reversing the transfer paper for image formation on both sides of the transfer paper is disposed in the vicinity of the secondary transfer device 22 and the fixing device 25. Yes.

  Next, formation of a full-color image (color copy) using the tandem developing device 120 will be described. That is, first, a document is set on the document table 130 of the automatic document feeder (ADF) 400, or the automatic document feeder 400 is opened and the document is set on the contact glass 32 of the scanner 300. 400 is closed.

  When a start switch (not shown) is pressed, when the document is set on the automatic document feeder 400, the document is transported and moved onto the contact glass 32, and then the document is set on the contact glass 32. Immediately after that, the scanner 300 is driven, and the first traveling body 33 and the second traveling body 34 travel. At this time, light from the light source is irradiated by the first traveling body 33 and reflected light from the document surface is reflected by the mirror in the second traveling body 34 and is received by the reading sensor 36 through the imaging lens 35 to be color. An original (color image) is read and used as black, yellow, magenta, and cyan image information.

  Each image information of black, yellow, magenta and cyan is stored in each image forming means 18 (black image forming means, yellow image forming means, magenta image forming means and cyan image forming means in the tandem developing device 120. ) And black, yellow, magenta and cyan toner images are formed in the respective image forming means. That is, each image forming means 18 (black image forming means, yellow image forming means, magenta image forming means, and cyan image forming means) in the tandem developing device 120 is photosensitive as shown in FIG. On the basis of the body 10 (the black photoreceptor 10K, the yellow photoreceptor 10Y, the magenta photoreceptor 10M, and the cyan photoreceptor 10C), the charger 60 that uniformly charges the photoreceptor, and each color image information. The photosensitive member is exposed to each color image corresponding image (L in FIG. 4), and an electrostatic latent image corresponding to each color image is formed on the photosensitive member. A developing device 61 that develops using color toner (black toner, yellow toner, magenta toner, and cyan toner) to form a toner image of each color toner, and the toner image is transferred to the intermediate transfer member 5. The image forming apparatus includes a transfer charger 62 for transferring the image on the surface, a photoconductor cleaning device 63, and a static eliminator 64, and each monochrome image (black image, yellow image, magenta image) based on image information of each color. And cyan images) can be formed. The black image, the yellow image, the magenta image, and the cyan image formed in this way are formed on the black photoconductor 10K on the intermediate transfer member 50 that is rotationally moved by the support rollers 14, 15, and 16, respectively. The black image, the yellow image formed on the yellow photoconductor 10Y, the magenta image formed on the magenta photoconductor 10M, and the cyan image formed on the cyan photoconductor 10C are sequentially transferred (primary transfer). Is done. Then, the black image, the yellow image, the magenta image, and the cyan image are superimposed on the intermediate transfer member 50 to form a composite color image (color transfer image).

On the other hand, in the paper feed table 200, one of the paper feed rollers 142 is selectively rotated to feed out a sheet (recording paper) from one of the paper feed cassettes 144 provided in multiple stages in the paper bank 143. Each sheet is separated and sent to the paper feed path 146, transported by the transport roller 147, guided to the paper feed path 148 in the copying machine main body 150, and abutted against the registration roller 49 and stopped. Alternatively, the sheet feed roller 142 is rotated to feed out sheets (recording paper) on the manual feed tray 54, separated one by one by the separation roller 52, put into the manual feed path 53, and abutted against the registration roller 49 and stopped. . The registration roller 49 is generally used while being grounded, but may be used in a state where a bias is applied to remove paper dust from the sheet.
Then, the registration roller 49 is rotated in synchronization with the synthesized color image (color transfer image) synthesized on the intermediate transfer member 50, and a sheet (recording paper) is interposed between the intermediate transfer member 50 and the secondary transfer device 22. The secondary color transfer device 22 transfers the composite color image (color transfer image) onto the sheet (recording paper), thereby transferring the color image onto the sheet (recording paper). Is formed. The residual toner on the intermediate transfer member 50 after image transfer is cleaned by the intermediate transfer member cleaning device 17.

  The sheet (recording paper) on which the color image has been transferred is conveyed by the secondary transfer device 22 and sent to the fixing device 25, where the combined color image (color) is generated by heat and pressure. (Transfer image) is fixed on the sheet (recording paper). Thereafter, the sheet (recording paper) is switched by the switching claw 55 and discharged by the discharge roller 56 and stacked on the paper discharge tray 57, or switched by the switching claw 55 and reversed by the sheet reversing device 28 and transferred again. After being guided to the position and recording an image on the back surface, the image is discharged by the discharge roller 56 and stacked on the discharge tray 57.

  In the image forming apparatus and the image forming method of the present invention, since the toner of the present invention having excellent charging performance, good environmental stability, and excellent low-temperature fixability is used, high image quality can be obtained efficiently.

  Examples of the present invention will be described below, but the present invention is not limited to the following examples.

(Synthesis Example 1)
-Synthesis of crystalline polyester resin (1)-
In a 5-liter four-necked flask equipped with a nitrogen inlet tube, dehydration tube, stirrer and thermocouple, 2,070 g of 1,4-butanediol, 2,535 g of fumaric acid, 291 g of trimellitic anhydride, and hydroquinone 4 Then, the mixture was reacted at 160 ° C. for 5 hours, heated to 200 ° C. for 1 hour, and further reacted at 8.3 kPa for 1 hour to synthesize a crystalline polyester resin (1).
The obtained crystalline polyester resin (1) has a melting temperature (Tm) of 128 ° C., a DSC endothermic peak temperature of 130 ° C., and the molecular weight distribution by GPC of the soluble part of orthodichlorobenzene is 900 in terms of number average molecular weight (Mn). The weight average molecular weight (Mw) was 3,500, and the Mw / Mn was 3.89. Further, in the infrared absorption spectrum was measured for absorption based on δCH olefin (out-of-plane deformation vibration), it was 970 cm ^-1. Table 1 shows the characteristics of the crystalline polyester resin (1).

(Synthesis Examples 2 to 6)
-Synthesis of crystalline polyester resins (2) to (6)-
In Synthesis Example 1, the crystalline polyester resins (2) to (6) of Synthesis Examples 2 to 6 were synthesized in the same manner as Synthesis Example 1 except that the amount of the acid component used was changed as shown in Table 1. did. Table 1 shows the characteristics of the obtained crystalline polyester resin.

(Preparation Example 1)
-Preparation of crystalline polyester resin dispersion (1)-
100 g of the crystalline polyester resin (4) synthesized in Synthesis Example 4 and 400 g of ethyl acetate were taken in a metal 2 L container, heated and dissolved at 79 ° C., and then cooled in an ice-water bath. To this, 500 ml of glass beads (3 mmφ) was added and pulverized for 10 hours with a batch type sand mill (made by Campehapio Co., Ltd.). A crystalline polyester resin dispersion (1) having a concentration of 50% by mass was obtained.

(Preparation Examples 2 to 6)
-Preparation of crystalline polyester resin dispersions (2) to (6)-
Crystalline polyester resin dispersions (2) to (6) of Preparation Examples 2 to 6 were prepared in the same manner as Preparation Example 1 except that the dispersion conditions were changed as shown in Table 2 in Preparation Example 1.

Example 1
<Toner granulation process>
Toner was produced while producing an adhesive substrate as follows.

-Preparation of organic solvent phase-
--- Synthesis of unmodified polyester (low molecular weight polyester)-
In a reaction vessel equipped with a cooling tube, a stirrer and a nitrogen introduction tube, 220 parts by mass of bisphenol A ethylene oxide 2 mol adduct, 529 parts by mass of bisphenol A propion oxide 3 mol adduct, 208 parts by mass of terephthalic acid, 46 masses of adipic acid And 2 parts by mass of dibutyltin oxide were added and reacted at 230 ° C. for 8 hours under normal pressure. Next, after reacting the reaction solution under a reduced pressure of 10 to 15 mmHg for 5 hours, 44 parts by weight of trimellitic anhydride was added to the reaction vessel, and the reaction was performed at 180 ° C. for 2 hours under normal pressure. A modified polyester was synthesized.
The obtained unmodified polyester had a number average molecular weight (Mn) of 2,500, a weight average molecular weight (Mw) of 6,700, a glass transition temperature (Tg) of 43 ° C., and an acid value of 25.

-Preparation of master batch (MB)-
540 parts by mass of carbon black (“Printtex35”; manufactured by Dexa Corporation, DBP oil absorption = 42 ml / 100 mg, pH = 9.5) as a colorant, polyester resin (“RS801”; manufactured by Sanyo Chemical Industries, acid value = 10, 1200 parts by mass of weight average molecular weight (Mw) = 20,000, glass transition temperature (Tg) = 64 ° C.) and 1200 parts by mass of water were mixed with a Henschel mixer (manufactured by Mitsui Mining Co., Ltd.). The mixture was kneaded at 150 ° C. for 30 minutes with two rolls, rolled and cooled, and pulverized to a size of 1 mm in diameter using a pulverizer (manufactured by Hosokawa Micron Corporation) to prepare a master batch.

In a reaction vessel in which a stir bar and a thermometer were set, 378 parts by mass of the unmodified polyester, 92 parts by mass of carnauba wax, 22 parts by mass of CCA (“salicylic acid metal complex E-84”; manufactured by Orient Chemical Industries), and ethyl acetate 947 parts by mass were charged, and the temperature was raised to 80 ° C. with stirring, maintained at 80 ° C. for 5 hours, and then cooled to 30 ° C. over 1 hour. Next, 500 parts by mass of the master batch and 500 parts by mass of ethyl acetate were charged into a reaction vessel and mixed for 1 hour to obtain a raw material solution.
1324 parts by mass of the obtained raw material solution was transferred to a reaction vessel, and using a bead mill (“Ultra Visco Mill”; manufactured by Imex Co., Ltd.), the liquid feeding speed was 1 kg / hr, the disk peripheral speed was 6 m / sec, and 0.5 mm zirconia. The carbon black and carnauba wax were dispersed in 3 passes under the condition of 80% by volume of beads. Next, 1042.3 parts by mass of a 65% by mass ethyl acetate solution of the unmodified polyester was added to the wax dispersion. The organic solvent phase (1) was prepared by passing through a bead mill under the same conditions as described above for dispersion.
The solid content concentration (130 ° C., 30 minutes) of the obtained organic solvent phase was 50% by mass.

-Preparation of oil phase mixture-
--Synthesis of prepolymer--
In a reaction vessel equipped with a cooling tube, a stirrer and a nitrogen introduction tube, 682 parts by mass of bisphenol A ethylene oxide 2 mol adduct, 81 parts by mass of bisphenol A propylene oxide 2 mol adduct, 283 parts by mass of terephthalic acid, trimellitic anhydride 22 parts by mass of acid and 2 parts by mass of dibutyltin oxide were charged and reacted at 230 ° C. for 8 hours under normal pressure. Subsequently, it was made to react under reduced pressure of 10-15mHg for 5 hours, and the intermediate polyester was synthesize | combined.
The resulting intermediate polyester has a number average molecular weight (Mn) of 2,100, a weight average molecular weight (Mw) of 9,500, a glass transition temperature (Tg) of 55 ° C., an acid value of 0.5, and a hydroxyl value of 51.
Next, 410 parts by mass of the intermediate polyester, 89 parts by mass of isophorone diisocyanate, and 500 parts by mass of ethyl acetate are charged in a reaction vessel equipped with a cooling pipe, a stirrer, and a nitrogen introduction pipe, and reacted at 100 ° C. for 5 hours. Thus, a prepolymer (polymer capable of reacting with the active hydrogen group-containing compound) was synthesized.
The free isocyanate content of the obtained prepolymer was 1.53% by mass.

--Synthesis of ketimine (the active hydrogen group-containing compound)-
In a reaction vessel equipped with a stir bar and a thermometer, 170 parts by mass of isophoronediamine and 75 parts by mass of methyl ethyl ketone were charged and reacted at 50 ° C. for 5 hours to synthesize a ketimine compound (the active hydrogen group-containing compound).
The amine value of the obtained ketimine compound (the active hydrogen machine-containing compound) was 418.

  Into a reaction vessel, 664 parts by mass of the organic solvent phase, 109.4 parts by mass of the prepolymer, and 4.6 parts by mass of the ketimine compound are charged, and TK type homomixer (manufactured by Tokushu Kika) is used. The oil phase mixture was obtained by mixing at 000 rpm for 1 minute.

-Preparation of aqueous medium phase-
--Preparation of fine particle dispersion-
In a reaction vessel in which a stir bar and a thermometer were set, 683 parts of water, 11 parts by weight of sodium salt of ethylene oxide methacrylate adduct sulfate ("Eleminol RS-30"; manufactured by Sanyo Chemical Industries), 83 parts by weight of styrene, 83 parts by weight of methacrylic acid, 110 parts by weight of butyl acrylate, and 1 part by weight of ammonium persulfate were charged and stirred at 400 rpm for 15 minutes to obtain a white emulsion. The emulsion was heated to raise the system temperature to 75 ° C. and reacted for 5 hours. Next, 30 parts by mass of a 1% by mass ammonium persulfate aqueous solution was added, and the mixture was aged at 75 ° C. for 5 hours, and then vinyl resin particles (copolymer of sodium salt of styrene-methacrylic acid-butyl acrylate-methacrylic acid ethylene oxide adduct sulfate). An aqueous dispersion of polymer) (fine particle dispersion) was prepared.
The volume average particle size of the fine particles contained in the obtained fine particle dispersion was measured using a particle size distribution measuring device (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. there were. Further, a part of the fine particle dispersion (1) was dried to isolate the resin component, and the glass transition temperature (Tg) of the resin component was measured to be 59 ° C. and the weight average molecular weight (Mw) was measured. As a result, it was 150,000.

  990 parts by weight of water, 83 parts by weight of the fine particle dispersion, 37 parts by weight of a 48.5% by weight aqueous solution of sodium dodecyl diphenyl ether disulfonate (“Eleminol MON-7”; manufactured by Sanyo Chemical Industries), and 90 parts by weight of ethyl acetate, Mixing and stirring were performed to obtain a milky white liquid (aqueous medium phase).

-Emulsification / Dispersion-
In the reaction vessel, 809 parts by mass of the oil phase mixture and 1200 parts by mass of the aqueous medium were added, and the mixture was mixed with the TK homomixer at a rotation speed of 13,000 rpm for 20 minutes to prepare an emulsified slurry.
Next, the emulsified slurry was charged into a reaction vessel equipped with a stirrer and a thermometer, and after desolvation at 30 ° C. for 8 hours, aging was performed at 40 ° C. for 4 hours to obtain a dispersion slurry (1). It was.
The obtained dispersion slurry (1) had a volume average particle diameter of 5.00 μm and a number average particle diameter of 4.50 μm as measured by Multisizer II (manufactured by Beckman Coulter, Inc.).

<Toner cleaning process>
After 100 parts by mass of the dispersed slurry was filtered under reduced pressure, 300 parts by mass of ion-exchanged water was added to the filter cake, and mixed with a TK homomixer (at 12,000 rpm for 10 minutes) to prepare a slurry. Here, the glass transition temperature (Tg) of the toner was 43 ° C.

-Alkali cleaning (1)-
While stirring the resulting slurry, a 10% by mass aqueous sodium hydroxide solution was added so that the pH would be 10.5, and after alkali washing at a liquid temperature of 25 ° C. for 2 hours, Solid-liquid separation was performed using a decanter (precipitation separator), and filtration under reduced pressure was further performed to obtain a filter cake.
Here, based on the following method, the total organic carbon elution amount (the TOC amount) extracted from the filter cake after the alkali washing was measured using a total organic carbon meter (“TOC-5000A”; manufactured by Shimadzu Corporation). Measured.

The obtained filter cake was dried and the solid content was measured. Next, 7.5 g of the filter cake is precisely weighed into a 140 ml bottle (S1), 47.5 g of pH 9 KOHaq (aqueous solution) is added (S2), ultrasonic waves are applied at 30 ° C. or lower for 30 minutes, and the microtube is used. About 1.5 ml was centrifuged. The supernatant in the obtained separated product is filtered using a 0.2 μ micro filter, after removing ultrafine particles, returned to the micro tube, the filter is washed with tap water and pure water, and the precipitate in the separated product is collected. Was filtered through a 1 μm filter, and 2 drops of HCl (35% by mass) aq were added to the obtained filtrate to confirm that the pH was 3 or less. The obtained solution was precisely weighed (T1), pure water was further added, diluted to 6.0 mg, and precisely weighed (T2). The obtained treatment liquid is burned at 680 ° C., carbon in an organic substance contained in the treatment liquid is generated as carbon dioxide gas, the carbon dioxide gas is analyzed with infrared rays, and the alkali-washed filter cake is used. The total organic carbon elution amount (total organic carbon (TOC) amount) to be extracted was measured (TOC measurement value), and the TOC amount per 1 g (dry product) of toner was calculated based on the following mathematical formula.
<Formula>
TOC (ppm / g) = TOC measurement value × (S1 + S2) / {S1 × (solid content (mass%) / 100)} × T2 / T1
As a result, the TOC amount was 180 ppm / g. The results are shown in Table 6.

-Washing (1)-
An operation of adding 300 parts by mass of ion-exchanged water to the filter cake obtained by the alkali washing, mixing with a TK homomixer (rotating at 12,000 rpm for 10 minutes) and then filtering is performed on the filtrate after washing with water. This was repeated until the conductivity reached 20 μS / cm to obtain a filter cake.

-Acid cleaning-
To the filter cake obtained by the water washing (1), 300 parts by mass of ion-exchanged water was added and mixed with a TK homomixer (rotation speed: 12,000 rpm for 10 minutes) to prepare a slurry. A 10% by mass aqueous hydrochloric acid solution was added to the slurry so that the pH was 3.0, and after acid washing at a liquid temperature of 25 ° C. for 30 minutes, filtration was performed to obtain a filter cake.

-Water washing (2)-
The operation of adding 300 parts by mass of ion-exchanged water to the filter cake obtained by the acid washing, mixing with a TK homomixer (rotating at 12,000 rpm for 10 minutes) and then filtering is performed on the filtrate after washing with water. The process was repeated until the conductivity reached 10 μS / cm to obtain a filter cake.

-Alkali cleaning (2)-
To the filter cake obtained by the water washing (2), 300 parts by mass of ion-exchanged water was added and mixed with a TK homomixer (rotation speed: 12,000 rpm for 10 minutes) to prepare a slurry. A 10% by mass aqueous sodium hydroxide solution was added to the slurry so that the pH was 7.0, and after alkaline washing at a liquid temperature of 25 ° C. for 2 hours, the resulting washing liquid was decanted (precipitation separator). Was separated into solid and liquid and further filtered under reduced pressure to obtain a filter cake.
The obtained filter cake was dried and the solid content was measured. Subsequently, the amount of TOC per 1 g of toner (dried product) was calculated in the same manner as in the alkali cleaning (1). As a result, the TOC amount was 90 ppm / g. The results are shown in Table 6.

-Water washing (3)-
The operation of adding 300 parts by mass of ion-exchanged water to the filter cake obtained by the alkali washing (2), mixing with a TK homomixer (rotating at 12,000 rpm for 10 minutes) and then filtering is performed after washing with water. This was repeated until the filtrate had a conductivity of 17 μS / cm to obtain a final filter cake.

-Dry-
The obtained final filter cake was dried with a circulating dryer at 40 ° C. for 48 hours and sieved with a mesh of 75 μm to obtain toner base particles of Example 1.

-External additive treatment-
Henschel mixer (manufactured by Mitsui Mining Co., Ltd.) was added 0.7 parts by weight of hydrophobic silica as an external additive and 0.3 parts by weight of hydrophobized titanium oxide with respect to 100 parts by weight of the obtained toner base particles of Example 1. The toner of Example 1 was manufactured by mixing using the toner.

(Examples 2 to 7)
In Example 1, toner base particles of Examples 2 to 7 were produced in the same manner as in Example 1 except that the toner cleaning conditions were changed to the cleaning conditions shown in Table 1, respectively. In Examples 3 to 4 and Examples 6 to 7, after alkali washing, water washing, acid washing, water washing, and alkali washing were performed only once.
The obtained filter cake was dried and the solid content was measured. Subsequently, the amount of TOC per 1 g (dry product) of toner was calculated in the same manner as in the alkali cleaning (1) in Example 1. The results are shown in Table 6.
The obtained toner base particles of Examples 2 to 7 were each subjected to external additive treatment in the same manner as in Example 1 to produce toners of Examples 2 to 7.

(Example 8)
<Toner granulation process>
In the preparation of the oil phase mixture in Example 1, an oil phase mixture was prepared in the same manner as in Example 1, except that 200 parts by mass of the crystalline polyester resin dispersion (1) obtained in Preparation Example 1 was added. And a dispersion slurry (2) was obtained using the oil phase mixture.

<Toner cleaning process>
With respect to the obtained dispersion slurry (2), toner base particles of Example 8 were produced in the same manner as in Example 1 except that the cleaning conditions of the toner were changed to the cleaning conditions shown in Table 5.
In the same manner as in Example 1, the amount of TOC per 1 g (dry product) of toner after alkali washing was measured. The results are shown in Table 6.

-External additive treatment-
About the obtained toner base particles of Example 8, an external additive was added in the same manner as in Example 1 to produce the toner of Example 8.

(Examples 9 to 13)
<Toner granulation process>
In the preparation of the oil phase mixed phase in Example 1, the same as Example 1 except that 200 parts by mass of the crystalline polyester resin dispersions (2) to (6) obtained in Preparation Examples 2 to 6 were added. An oil phase mixture was prepared, and dispersion slurries (3) to (7) were obtained using the oil phase mixture. Table 4 shows the relationship between the crystalline polyester resin dispersion and the dispersion slurry in the oil phase mixture.

<Toner cleaning process>
In Example 1, toner base particles of Examples 9 to 13 were produced in the same manner as in Example 1 except that the toner cleaning conditions were changed to the cleaning conditions shown in Table 5.
In the same manner as in Example 1, the amount of TOC per 1 g (dry product) of toner after alkali washing was measured. The results are shown in Table 6.

-External additive treatment-
External toners were added to the obtained toner base particles of Examples 9 to 13 in the same manner as in Example 1 to prepare toners of Examples 9 to 13, respectively.

(Example 14)
In the preparation of the aqueous medium phase in Example 1, the dispersion slurry was prepared in the same manner as in Example 1 except that the fine particle dispersion was replaced with the fine particle dispersion prepared by the following method. The toner washing step was performed according to the conditions to produce toner base particles, and an external additive treatment was further carried out to produce a toner.

-Preparation of fine particle dispersion-
In a reaction vessel in which a stir bar and a thermometer are set, 683 parts of water, 11 parts by weight of sodium salt of ethylene oxide methacrylate adduct sulfate ("Eleminol RS-30"; manufactured by Sanyo Chemical Industries), 80 parts by weight of styrene, 83 parts by weight of methacrylic acid, 110 parts by weight of butyl acrylate, 12 parts by weight of butyl thioglycolate, and 1 part by weight of ammonium persulfate were charged and stirred at 400 rpm for 15 minutes to obtain a white emulsion. The emulsion was heated to raise the system temperature to 75 ° C. and reacted for 5 hours. Next, 30 parts by mass of a 1% by mass ammonium persulfate aqueous solution was added, and the mixture was aged at 75 ° C. for 5 hours, and then vinyl resin particles (copolymer of sodium salt of styrene-methacrylic acid-butyl acrylate-methacrylic acid ethylene oxide adduct sulfate). An aqueous dispersion of polymer) (fine particle dispersion) was prepared.
The volume average particle diameter of the fine particles contained in the obtained fine particle dispersion was measured using a particle size distribution measuring apparatus (“LA-920”; manufactured by Horiba, Ltd.) using a laser light scattering method. there were. In addition, a part of the fine particle dispersion (2) was dried to isolate the resin, and the glass transition temperature (Tg) of the resin was measured to find that it was 42 ° C. and the weight average molecular weight (Mw) was measured. As a result, it was 30,000.

(Example 15)
In Example 3, a toner was manufactured in the same manner as in Example 3 except that the cleaning conditions in the toner cleaning step were reinforced with alkali cleaning conditions as shown in Table 5. In the same manner as in Example 1, the amount of TOC per 1 g (dry product) of toner after alkali washing was measured. The results are shown in Table 6.

(Comparative Example 1)
In Example 3, the cleaning conditions in the toner cleaning step were changed as shown in Table 5, and after alkaline cleaning, water cleaning was not performed, and then acid cleaning was performed, the same as in Example 3 Thus, a toner was produced. In the same manner as in Example 1, the amount of TOC per 1 g (dry product) of toner after alkali washing was measured. The results are shown in Table 6.

(Comparative Example 2)
In Example 3, a toner was manufactured in the same manner as in Example 3 except that the cleaning condition in the toner cleaning step was weakened as shown in Table 5 under the alkaline cleaning condition. In the same manner as in Example 1, the amount of TOC per 1 g (dry product) of toner after alkali washing was measured. The results are shown in Table 6.

(Comparative Example 3)
In Example 3, the toner was manufactured in the same manner as in Example 3 except that the cleaning conditions in the toner cleaning step were changed as shown in Table 5 and no alkali cleaning was performed. In the same manner as in Example 1, the amount of TOC per 1 g (dry product) of toner after alkali washing was measured. The results are shown in Table 6.

  Next, a conventional method is performed from 5% by mass of each of the toners of Examples 1 to 15 and Comparative Examples 1 to 3 that have been treated with external additives and 95% by mass of a copper-zinc ferrite carrier having an average particle diameter of 40 μm coated with a silicone resin. Thus, developers of Examples 1 to 15 and Comparative Examples 1 to 3 were produced.

  Using the obtained toners and developers, (a) toner particle size (b) charge amount, and (c) fixability (offset generation temperature and fixing lower limit temperature) were evaluated as follows. The results are shown in Table 7.

(A) Toner Particle Size Toner particle size is determined by measuring the volume average particle size (Dv) and number average particle size (Dn) of the toner using a particle size measuring device (“Multisizer II”; manufactured by Beckman Coulter, Inc.). Measurement was performed at a diameter of 100 μm. From these results, the particle size distribution (volume average particle size (Dv) / number average particle size (Dn)) was calculated.

(B) Charge amount 7 parts by mass of the toners obtained in Examples 1 to 15 and Comparative Examples 1 to 3 were weighed against 100 parts by mass of a copper-zinc ferrite carrier having an average particle diameter of 40 μm coated with a silicone resin, In a humidity (HH) environment (temperature of 30 ° C., humidity of 90%) and in an intermediate temperature / humidity (NN) environment (temperature of 25 ° C., humidity of 50%), it is allowed to stand for 24 hours, and then charged into a metal cylinder that can be sealed. After rotating and stirring at a speed of 280 rpm for 1 minute, blowing was performed to measure the charge amount.

(C) Fixability (offset generation temperature and fixing lower limit temperature)
Using tandem color electrophotographic apparatus (image Neo 450, manufactured by Ricoh Co., Ltd.), using plain paper (TYPE 6200, manufactured by Ricoh Co., Ltd.) and cardboard transfer paper (copy printing paper <135>, manufactured by NBS Ricoh Co., Ltd.) The fixability (offset generation temperature and fixing lower limit temperature) was evaluated. The tandem color electrophotographic apparatus can continuously print A4 size paper every 45 minutes.

<Offset generation temperature>
Image formation is performed using the tandem-type color electrophotographic apparatus on each of the plain paper with a single color of yellow, magenta, cyan, and black, and a solid image of red, blue, and green as each intermediate color. 0.0 ± 0.1 mg / cm ² of toner was adjusted to be developed. The obtained image was fixed by changing the temperature of the fixing belt (heating roller), and the fixing temperature at which an offset occurred (offset generation temperature) was measured.

<Fixing temperature limit>
For the image, the tandem color electrophotographic apparatus was used to set the cardboard and perform a copy test. The fixing roll temperature at which the residual ratio of the image density after rubbing the obtained fixed image with a pad was 70% or more was determined as the minimum fixing temperature.

  From the results in Table 7, the following is clear. That is, in Examples 1 to 15, a toner having excellent charging performance, in particular, having excellent charging performance and good environmental stability even when stored for a long time under high temperature and high humidity. The toner was also found to be excellent in hot offset resistance and low-temperature fixability. In Example 15, since the alkali cleaning conditions were strengthened, it was found that the alkali became excessive, eroded the polyester resin, and the particle size distribution of the toner was destroyed.

  Furthermore, the total organic carbon elution amount per 1 g (dry product) of the toner obtained by Examples 1 to 15 and Comparative Examples 1 to 3 and subjected to the alkali washing of the dried and external additive-treated toner, The relationship with the charge rising property was evaluated based on the following method. The results are shown in Table 8 and FIG.

<Total organic carbon elution amount (total organic carbon (TOC) amount)>
The amount of TOC was measured using a total organic carbon meter (“TOC-5000A”; manufactured by Shimadzu Corporation). First, 7.5 g of each toner after alkali washing was precisely weighed into a 140 ml bottle (S1), 47.5 g of pH 9 KOHaq (aqueous solution) was added (S2), and ultrasonic waves were applied at 30 ° C. or lower for 30 minutes. About 1.5 ml was centrifuged in a microtube. The supernatant in the obtained separated product is filtered using a 0.2 μ micro filter, after removing ultrafine particles, returned to the micro tube, the filter is washed with tap water and pure water, and the precipitate in the separated product is collected. Was filtered through a 1 μm filter, and 2 drops of HCl (35% by mass) aq were added to the obtained filtrate to confirm that the pH was 3 or less. The obtained solution was precisely weighed (T1), pure water was further added, diluted to 6.0 mg, and precisely weighed (T2). The obtained treatment liquid is burned at 680 ° C., carbon in the organic substance contained in the treatment liquid is generated as carbon dioxide gas, the carbon dioxide gas is analyzed with infrared rays, and extracted from the toner after the alkali cleaning. The total organic carbon elution amount (total organic carbon (TOC) amount) was measured (TOC measurement value), and the TOC amount per 1 g (dry product) of the toner was calculated based on the following mathematical formula. The solid content of the toner is 100% by mass.
<Formula>
TOC (ppm / g) = TOC measurement value × (S1 + S2) / {S1 × (solid content (mass%) / 100)} × T2 / T1

<Charge rise characteristics>
7 parts by mass of the toners obtained in Examples 1 to 15 and Comparative Examples 1 to 3 are weighed against 100 parts by mass of a copper-zinc ferrite carrier having an average particle diameter of 40 μm coated with a silicone resin, and charged into a metal cylinder that can be sealed. The mixture was rotated and stirred at a speed of 280 rpm for 15 seconds, and then blown to measure the charge amount. In addition, it means that the larger the negative charge amount, the better the charge rising property, and the negative charge amount is preferably larger than −20 μC / g. In this case, the toner replenished by the image forming apparatus is quickly charged and a good image can be obtained.

  From Table 8 and FIG. 5, the TOC amount and the charge rising property are closely related. In Examples 1 to 15, since the TOC amount is low even in the toner after drying and external additive treatment, It was found that it had excellent standing characteristics. On the other hand, it was found that the toners of Comparative Examples 1 to 3 had a high TOC amount and were inferior in charge rising property.

  The toner of the present invention has excellent charging performance, good environmental stability, and excellent low-temperature fixability. For this reason, it is suitably used for high-quality image formation. The developer, toner-containing container, process cartridge, image forming apparatus and image forming method of the present invention using the toner of the present invention are suitably used for high-quality image formation.

FIG. 1 is a schematic explanatory view showing an example in which the image forming method of the present invention is carried out by the image forming apparatus of the present invention. FIG. 2 is a schematic explanatory view showing another example in which the image forming method of the present invention is carried out by the image forming apparatus of the present invention. FIG. 3 is a schematic explanatory view showing an example in which the image forming method of the present invention is implemented by the image forming apparatus (tandem color image forming apparatus) of the present invention. 4 is a partially enlarged schematic explanatory diagram of the image forming apparatus shown in FIG. FIG. 5 is a graph showing an example of the relationship between the TOC amount extracted from the toner after the alkali cleaning and the charge amount of the toner.

Explanation of symbols

10 Photoconductor (Photoconductor drum)
10K black photoconductor 10Y yellow photoconductor 10M magenta photoconductor 10C cyan photoconductor 14 support roller 15 support roller 16 support roller 17 intermediate transfer cleaning device 18 image forming means 20 charging roller 21 exposure device 22 secondary transfer device 23 Roller 24 Secondary transfer belt 25 Fixing device 26 Fixing belt 27 Pressure roller 28 Sheet reversing device 30 Exposure device 32 Contact glass 33 First traveling member 34 Second traveling member 35 Imaging lens 36 Reading sensor 40 Developing device 41 Developing belt 42K Developer container 42Y Developer container 42M Developer container 42C Developer container 43K Developer supply roller 43Y Developer supply roller 43M Developer supply roller 43C Developer supply roller 44K Developer roller 44Y Developer roller 44M Developer Roller 44C Developing roller 45K Black developing unit 45Y Yellow developing unit 45M Magenta developing unit 45C Cyan developing unit 49 Registration roller 50 Intermediate transfer member 51 Roller 52 Separating roller 53 Manual feed path 54 Manual feed tray 55 Switching claw 56 Discharge roller 57 discharge tray 58 corona charger 60 cleaning device 61 developing device 62 transfer charger 63 photoconductor cleaning device 64 static eliminator 70 static elimination lamp 80 transfer roller 90 cleaning device 95 transfer paper 100 image forming device 110 belt type fixing device 120 tandem development Machine 130 document table 142 paper feed roller 143 paper bank 144 paper feed cassette 145 separation roller 146 paper feed path 147 transport roller 148 paper feed path 150 copier main body 200 paper feed table 300 CANA 400 Automatic Document Feeder (ADF)

Claims (25)

  A toner comprising a polyester resin, wherein the total organic carbon elution amount (total organic carbon (TOC) amount) extracted from the toner after alkali cleaning is 200 ppm / g or less.   The toner according to claim 1, which is obtained by reacting an active hydrogen group-containing compound and a polymer capable of reacting with the active hydrogen group-containing compound in an aqueous medium to produce particles containing at least an adhesive substrate.   The toner according to claim 1, comprising a crystalline polyester resin.   The toner according to claim 1, comprising resin fine particles.   The toner according to claim 4, wherein the resin fine particles are at least one selected from a vinyl resin, a polyurethane resin, an epoxy resin, and a polyester resin.   The toner according to claim 1, wherein the acid value of the polyester resin is 5 to 50 mg KOH / g.   The toner according to claim 1, wherein the pH of the cleaning liquid after alkali cleaning is 6.0 to 11.0.   The toner according to claim 1, wherein the conductivity of the cleaning liquid after solid-liquid separation after water washing and water washing is 0.5 to 60 μS / cm.   The toner according to any one of claims 3 to 8, wherein the crystalline polyester resin has a DSC endothermic peak temperature of 50 to 150 ° C.   The molecular weight distribution by GPC of the ortho-dichlorobenzene soluble part of the crystalline polyester resin is 1,000 to 30,000 in terms of weight average molecular weight (Mw), and 500 to 6,000 in terms of number average molecular weight (Mn). The toner according to claim 3, wherein (Mw / Mn) is 2 to 8. The toner according to claim 3, wherein the crystalline polyester resin is represented by the following general formula (1).

In the general formula (1), n and m represent the number of repeating units, L represents an integer of 1 to 3, and R ¹ and R ² may be the same as or different from each other. Often represents a hydrogen atom or a hydrocarbon group. Any crystalline polyester resin is from claim 3 having an absorption based on at least one the olefin δCH its infrared absorption spectrum in 965 ± 10 cm ^-1 and 990 ± 10 cm ^-1 (out-of-plane deformation vibration) 11 Toner according to. A toner granulating step for granulating a toner containing a polyester resin;
And a toner cleaning step of at least alkali cleaning the granulated toner until the total organic carbon elution amount (TOC amount) extracted from the toner is 200 ppm / g or less. Method.   The method for producing a toner according to claim 13, wherein the pH of the cleaning liquid after the alkali cleaning is 6.0 to 11.0.   The method for producing a toner according to claim 13, wherein the conductivity of the cleaning liquid after solid-liquid separation after water washing and water washing is 0.5 to 60 μS / cm.   The method for producing a toner according to claim 13, wherein the alkali cleaning solution is an aqueous sodium hydroxide solution.   The toner production method according to claim 13, wherein the granulated toner is washed with water, washed with acid, washed with acid, and washed with water.   The toner production method according to claim 13, wherein the granulated toner is washed with water, washed with water, washed with acid, washed with water, washed with alkali, and washed with water.   The method for producing a toner according to any one of claims 13 to 18, wherein the temperature during alkali cleaning is 10 to 70 ° C.   20. The temperature T (° C.) at the time of alkali cleaning is (Tg−10) ≦ T ≦ (Tg + 10), where Tg (° C.) is the glass transition temperature of the toner. Production method.   21. The method for producing a toner according to claim 13, wherein the alkali cleaning time is 1 to 72 hours.   In the toner granulation step, an active hydrogen group-containing compound and a polymer capable of reacting with the active hydrogen group-containing compound are emulsified or dispersed in an aqueous medium and reacted to produce an adhesive substrate. The method for producing a toner according to any one of claims 13 to 21, which is a step of obtaining particles containing at least an adhesive substrate.   A developer comprising the toner according to claim 1.   A toner-containing container filled with the toner according to claim 1. An electrostatic latent image forming step for forming an electrostatic latent image on the electrostatic latent image carrier, and developing the electrostatic latent image with the toner according to any one of claims 1 to 12 to form a visible image An image forming method comprising: a developing step for forming the image; a transfer step for transferring the visible image to a recording medium; and a fixing step for fixing the transferred image transferred to the recording medium.

Images