JP2008233297A - Method of manufacturing polyester resin for toner - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a manufacturing method for industrially and stably manufacturing a polyester resin superior in high temperature offset resistance in high productivity by having low temperature fixing. <P>SOLUTION: The method of manufacturing the polyester resin for toner directly supplies an organic peroxide diluted with a mold releasing agent into the polyester resin having molten unsaturated double bonds to perform cross-linking reaction. The melting point of the mold releasing agent diluting the organic peroxide is 120°C or lower in the method of manufacturing the polyester resin for the toner. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to a method for producing a polyester resin for toner.

  In the method of obtaining an image by the electrophotographic printing method and the electrostatic charge developing method, the electrostatic charge image formed on the photoreceptor is developed with toner charged in advance by friction and then fixed. As for the fixing method, there are a heat roller method in which a toner image obtained by development is fixed using a pressurized and heated roller, and a non-contact fixing method in which fixing is performed using an electric oven or flash beam light.

  In order to pass through these processes without any problem, the toner needs to maintain a stable charge amount first, and then needs to have good fixability to paper. In addition, since the apparatus includes a heating body in the fixing unit, the temperature rises in the apparatus, and thus the toner is required not to block in the apparatus.

  Recently, energy saving has been particularly demanded, and as a result, the temperature of the fixing unit has been lowered in the heat roller system. For this reason, the toner is strongly required to have a performance of fixing on paper at a lower temperature, that is, a low-temperature fixability. Moreover, in the heat roller system, since a so-called offset phenomenon occurs, it is assumed that offset resistance is required. Therefore, it is necessary to develop a low-temperature fixing property that exhibits fixing on paper even under a fixing temperature of 140 ° C. or lower, while maintaining offset resistance, and a wider working range, for example, a fixing temperature width of 50 ° C. or higher. There is a growing demand for toners to have.

  The binder resin for toner has a great influence on the toner characteristics as described above, and polystyrene resin, styrene-acrylic resin, polyester resin, epoxy resin, polyamide resin, etc. are known, but recently, transparent Polyester resin is especially attracting attention because it is easy to balance the fixing property and the fixing property.

  Conventionally, as a method for expanding the fixing temperature range of a polyester resin, a method using a non-linear polyester resin having a three-dimensional crosslinked structure using a tri- or higher functional monomer has been studied (for example, see Patent Document 1). However, although the non-linear polyester resin described in Patent Document 1 is excellent in high temperature offset resistance and can exhibit a high maximum fixing temperature, the level of low temperature fixing property is not yet sufficient.

  Then, using linear polyester resin which consists of a bivalent carboxylic acid compound and a bivalent alcohol compound as a means to improve low temperature fixability is examined (for example, refer patent document 2). However, a linear polyester resin having no three-dimensional structure is excellent in low-temperature fixability, but has a problem that a wide fixing temperature range cannot be obtained due to poor high-temperature offset resistance.

  Therefore, studies have been made to introduce an unsaturated group into a linear polyester resin and to react and crosslink with a polymerization initiator or the like (for example, see Patent Documents 3 to 6).

  In Patent Document 3, dicumyl peroxide is used as a polymerization initiator for an unsaturated polyester resin composed of a divalent carboxylic acid such as isophthalic acid and maleic anhydride and a divalent alcohol such as a bisphenol A propylene oxide adduct. A technique for crosslinking reaction is described. As the polymerization initiator, an organic peroxide that self-promotes and decomposes at high temperatures is used, but a method for stably supplying the organic peroxide is not described.

  In Patent Document 4, a polyester resin for toner including a crosslinked part and an uncrosslinked part can be obtained by crosslinking reaction of an unsaturated polyester resin composed of fumaric acid and a bisphenol A propylene oxide adduct. Are listed. As the polymerization initiator, an organic peroxide that self-promotes and decomposes at high temperatures is used, but a method for stably supplying the organic peroxide is not described.

  Patent Document 5 discloses a polyester resin for toner obtained by further curing an unsaturated polyester resin having an unsaturated double bond having a number average molecular weight of 1,000 to 4,000 in the presence of a heating or polymerization initiator. Is described. However, since the organic peroxide is added at a temperature much higher than the self-promoted decomposition temperature, there is a problem that it cannot be produced industrially.

  Patent Document 6 describes a toner comprising a saturated polyester resin having a melting start temperature of 50 ° C. or higher and lower than 100 ° C., and a crosslinked product of the unsaturated polyester resin. Since the organic peroxide is previously mixed with a super mixer, there is a problem that productivity is low.

If an organic peroxide can be supplied at a high temperature, it can be produced with high industrial productivity. However, a method for industrially supplying an organic peroxide that is unstable to heat is still disclosed. Absent.
JP-A-57-109825 JP-A-4-12367 Japanese Patent Laid-Open No. 3-135578 JP-A-5-249739 JP 59-49551 A JP-A-8-152743

  An object of the present invention is to provide a method for producing a polyester resin having low-temperature fixability and excellent high-temperature offset resistance in an industrially stable manner with high productivity.

  The gist of the present invention resides in a method for producing a polyester resin for a toner, in which an organic peroxide dispersed or dissolved in a release agent is supplied into a melted polyester resin having an unsaturated double bond to perform a crosslinking reaction.

  INDUSTRIAL APPLICABILITY According to the present invention, a polyester resin having low temperature fixability and excellent high temperature offset resistance can be produced industrially stably and with high productivity.

  In the present invention, it is necessary to supply an organic peroxide dispersed or dissolved in a release agent into a molten polyester resin having an unsaturated double bond to perform a crosslinking reaction.

  Since the organic peroxide, which is a crosslinking reaction initiator, is a self-promoting decomposable compound, if slight decomposition occurs in the initial stage, heat of decomposition is generated, and the decomposition is accelerated by the heat. That is, once decomposition starts, it has the property of reaching rapid decomposition in a short time.

  Therefore, when an organic peroxide is allowed to flow through a pipe in contact with the high temperature portion, the organic peroxide is heated in the pipe to cause a decomposition reaction, and it becomes difficult to stably supply the molten polyester resin.

  In the present invention, the organic peroxide is dispersed or dissolved in the release agent (the organic peroxide is diluted with the release agent). Since it becomes possible to supply stably into the polyester resin having a saturated double bond and the crosslinking reaction proceeds promptly after the supply, productivity can be increased.

  In addition, SADT (Self Accelerating Decomposition Temperature) is used as a standard of such a self-promoted decomposition temperature at which the organic peroxide is expected to be clearly decomposed. SADT is the lowest temperature that causes heat generation or decomposition of 6 ° C. or more within 7 days due to the relationship between heat of decomposition and heat dissipation when the product form of organic peroxide is about 50 liters.

  Further, as the release agent used for diluting the organic peroxide, it is preferable to use a release agent that does not inhibit the crosslinking reaction of unsaturated double bonds. For example, hydrocarbon release agents such as low molecular weight polyethylene and low molecular weight polypropylene. And aliphatic hydrocarbon waxes such as microcrystalline wax and paraffin wax, oxides of aliphatic hydrocarbon waxes such as oxidized polyethylene wax, and block compounds thereof.

  Among these, the melting point of the release agent is preferably 120 ° C. or less because mixing with the crosslinking reaction initiator is easy and the low-temperature fixability of the toner tends to be further improved. As the mold release agent having a melting point of 120 ° C. or less, paraffin wax is most preferable, and HNP series manufactured by Nippon Seiki Co., Ltd .: for example, HNP-3 (melting point 64 ° C.), HNP-5 (melting point 62 ° C.), HNP-9, 10 (Melting point 75 ° C.), HNP-11 (melting point 68 ° C.), HNP-12 (melting point 67 ° C.), HNP-51 (melting point 77 ° C.), SP series: SP-0165 (melting point 74 ° C.), SP-0160, for example (Melting point 71 ° C.), SP-0145 (melting point 62 ° C.), HNP-3 (melting point 64 ° C.), FT series: FT-0070 (melting point 72 ° C.), FT-0165 (melting point 73 ° C.) and the like.

  The organic peroxide is not particularly limited, and examples thereof include benzoyl peroxide, di-t-butyl peroxide, t-butyl cumyl peroxide, dicumyl peroxide, α, α-bis (t-butyl peroxide). Oxy) diisopropylbenzene, 2,5-dimethyl-2,5-bis (t-butylperoxy) hexane, di-t-hexyl peroxide, 2,5-dimethyl-2,5-di-t-butyl Peroxyhexine-3, acetyl peroxide, isobutyryl peroxide, octanonor peroxide, decanolyl peroxide, lauroyl peroxide, 3,3,5-trimethylhexanoyl peroxide, m-toluyl peroxide, t- Butyl peroxyisobutyrate, t-butyl peroxyneodecanoate, cumyl peroxyneodeca Ate, t-butyl peroxy 2-ethylhexanoate, t-butyl peroxy 3,5,5-trimethylhexanoate, t-butyl peroxylaurate, t-butyl peroxybenzoate, t-butyl Examples include peroxyisopropyl carbonate and t-butyl peroxyacetate.

  Moreover, in this invention, an unsaturated double bond is a carbon-carbon double bond, and has this in the principal chain and / or side chain of a polyester resin. In order to have an unsaturated double bond in the main chain and / or side chain of the polyester resin, a polycondensation reaction using a carboxylic acid compound having an unsaturated double bond and / or an alcohol compound having an unsaturated double bond These compounds may be incorporated as a constituent component of the polyester resin.

  Examples of the carboxylic acid compound having an unsaturated double bond include, but are not limited to, fumaric acid, maleic acid, maleic anhydride, citraconic acid, itaconic acid, tetrahydrophthalic acid and ester derivatives thereof, acrylic acid, Examples include crotonic acid, methacrylic acid, and ester derivatives thereof. The alcohol compound having an unsaturated double bond is not particularly limited, and examples thereof include 1,4-dihydroxy-2-butene.

  Among these, at least one selected from fumaric acid, maleic acid, and maleic anhydride is particularly preferable from the viewpoint of reactivity.

Furthermore, in the present invention, since the organic peroxide which is a crosslinking reaction initiator is supplied directly into the polyester resin having a molten unsaturated double bond,
Since the cross-linking reaction proceeds promptly after the supply, productivity can be improved. The melting apparatus is not particularly limited, but for example, a single screw extruder, a twin screw extruder, a continuous hermetic mixer, a gear extrusion, etc. Continuous melting apparatuses such as a machine, a disk extruder and a roll mill extruder, and a static mixer; batch hermetic melting apparatuses such as a Banbury mixer, a Brabender mixer, and a Haake mixer.

  Among these, the continuous melting apparatus is preferable because the organic peroxide can be dispersed in the polyester resin efficiently in a short time.

As the continuous melting apparatus, a known apparatus can be used, and examples thereof include the following.

(1) Sulzer mixer SMX type (SMX-15A: 6 elements, 12 elements) manufactured by Midori Machinery Co., Ltd. With piping 25A (inner diameter: 27.2 mm).

(2) NS mixer (WB-15A: 24 element) manufactured by Tokyo Nisshin Bellows Co., Ltd. Pipe 15A (inner diameter 16.1 mm).

Noritake Co., Ltd. static mixer (15A: 24 elements) with an inner diameter of 5 mm.

Ikegai twin screw extruder (PCM-29: L / D = 30)
Ikedai twin screw extruder (PCM-30: L / D = 40)
TOSHIBA MACHINE CO., LTD. Twin screw extruder (TEM-37-SS-16 / 7V: L / D = 64)
Nippon Steel Works' twin screw extruder (TEX30α-63BV-14V: L / D = 64)
Twin screw extruder manufactured by Plastic Engineering Laboratory Co., Ltd. (BTN-32: L / D = 64)
L represents the length of the extruder and D represents the diameter of the extruder.

  The method for preparing the organic peroxide dispersed or dissolved in the release agent is not particularly limited, but a method in which the organic peroxide is mixed with the release agent that has been heated and liquefied is preferable. Since the organic peroxide is dispersed or dissolved by the release agent, self-promoted decomposition can be suppressed even in such a heated state.

  The mass ratio of the organic peroxide to the release agent (dilution ratio X of the organic peroxide) is preferably 0.1 / 99.9 to 50/50. When the mass ratio of the organic peroxide to the release agent is 0.1 / 99.9 or more, the crosslinking reaction tends to be efficiently caused, and when the mass ratio is 50/50 or less, the self-promoted decomposition occurs. There is a tendency to be able to suppress.

  Further, when the dilution ratio of the organic peroxide diluted with the release agent is within the above range, the resin retention in the crosslinking reaction device is suppressed by the release action of the release agent in the crosslinking reaction device. Therefore, excessive progress of the crosslinking reaction of the unsaturated polyester resin is suppressed, and the material dispersibility of the toner tends to be better. The dilution ratio of the organic peroxide is more preferably 30/70 or less.

  Here, the crosslinking reaction of the unsaturated polyester resin is a reaction for forming a chemical bond between the molecules of the polyester resin.

  When an unsaturated polyester resin is subjected to a crosslinking reaction, a part thereof is changed to a crosslinking component having a high crosslinking density that is not soluble in THF (THF insoluble component), and a part thereof is a crosslinking component having a low crosslinking density that is dissolved in THF. And the rest remains unreacted. As a result, the resin obtained by the crosslinking reaction contains a THF-insoluble component (crosslinking component that does not dissolve in THF) and a THF soluble component (a crosslinking component that dissolves in THF and an unreacted polyester resin). Since the THF-insoluble matter is cross-linked at high density, it has an effect of imparting higher elasticity to the toner and tends to further improve the high-temperature offset resistance of the toner.

  However, since the THF-insoluble matter is cross-linked at a high density, it is difficult to disperse the toner material, and it is necessary to control the cross-linking reaction not to proceed excessively so that the material dispersibility is good.

  Although the Example of this invention is shown below, the embodiment of this invention is not limited to this. The evaluation methods for the resin and toner shown in this example are as follows.

Toner evaluation method (1) Fixing characteristics: high-temperature offset resistance Using an apparatus modified from the copier “PAGEPREST N4-612 II” (manufactured by Casio Denshi Kogyo Co., Ltd.), an unfixed image is produced and the fixing temperature region is tested. Went. The fixing roller used here is a fixing roller to which silicone oil is not applied, and has a nip width of 3 mm and a linear speed of 30 mm / min. Whether the solid image with a printing ratio of 1% printed on the top of A4 plain paper (manufactured by Daishowa Paper: BM64T) is attached to the roller by increasing the temperature setting by the heat roller by 5 ° C and smears the bottom margin of the paper. Was visually confirmed, and the highest setting temperature at which no contamination occurred was defined as the highest fixing temperature.

◎ + (very good): the maximum fixing temperature is 200 ° C. or higher ◎ (very good): the highest fixing temperature is 190 ° C. or higher and lower than 200 ° C. ○ + (good): the highest fixing temperature is 180 ° C. or higher and lower than 190 ° C. Possible): Maximum fixing temperature of 170 ° C. or more and less than 180 ° C. x (Inferior): Maximum fixing temperature of less than 170 ° C. (2) Fixing characteristics: Minimum fixing temperature The fixed image was repeatedly lowered to 100 ° C. while decreasing the set temperature by 5 ° C., and the fixed image was subjected to a rubbing test.

  For the fixing rate, use the printing paper used for the above fixing temperature range evaluation, fold the printed portion and apply a load of 5 kg / cm 2, and then apply cellophane tape (Nitto Denko Packaging System, product number: N.29). The amount of light in the printed part before and after this operation was measured with a Macbeth light meter, and the fixing rate was calculated from the measured value.

Fixing rate (%) = (light quantity after cellophane tape peeling test) / (light quantity before test) × 100 (%)
◎ + (very good): minimum fixing temperature is 120 ° C. or less ◎ (very good): minimum fixing temperature is over 120 ° C. and 130 ° C. or less ○ + (good): minimum fixing temperature is over 130 ° C. to 140 ° C. Below (can be used): Minimum fixing temperature exceeds 140 ° C. and 150 ° C. or less × (Inferior): Minimum fixing temperature exceeds 150 ° C. (3) Fixing characteristics: fixing temperature range Difference between maximum fixing temperature and minimum fixing temperature Was determined based on the following criteria.

◎ (very good): fixing temperature range of 70 ° C. or higher ○ + (good): fixing temperature range of 60 ° C. or higher and lower than 70 ° C. (available): fixing temperature range of 50 ° C. or higher and lower than 60 ° C. x (inferior) : Fixing temperature width is less than 50 ° C. Synthesis Example 1
95 mol parts of terephthalic acid and 5 mol parts of fumaric acid as acid components, 65 mol parts of ethylene glycol and 40 mol parts of neopentyl glycol as alcohol components, and 1000 ppm of tributyltin oxide based on the total acid components The container was charged. Next, the temperature is raised and heated so that the temperature in the reaction system becomes 260 ° C., this temperature is maintained, and the esterification reaction is carried out until no water is distilled from the reaction system. Thus, a polyester resin (a) was obtained. The charge composition of the polyester resin (a) is shown in Table 1.

Synthesis example 2
80 mol parts of terephthalic acid and 20 mol parts of fumaric acid as the acid component, 80 mol parts of ethylene glycol and 40 mol parts of 1,4-cyclohexanedimethanol as the alcohol component, and 1500 ppm of antimony trioxide with respect to the total acid component Then, 2000 ppm of a hindered phenol compound (AO-60 manufactured by Asahi Denka Kogyo Co., Ltd.) with respect to all acid components was charged into the same reaction vessel as in Synthesis Example 1.

  Next, the temperature was raised and heated so that the temperature in the reaction system became 260 ° C., and this temperature was maintained, and the esterification reaction was continued until no water was distilled from the reaction system. Subsequently, the temperature in the reaction system was set to 225 ° C., the pressure in the reaction vessel was reduced, and a condensation reaction was performed while distilling the diol component from the reaction system. The reaction was continued until the viscosity of the reaction system increased with the reaction and the torque of the stirring blade reached a value indicating the desired softening temperature. And when the predetermined torque was shown, the reaction material was taken out and cooled, and polyester resin (b) was obtained. Table 1 shows the charged composition of the polyester resin (b).

Example 1
90 parts by mass of a mold release agent (SP-0160 manufactured by Nippon Seiki Co., Ltd.) is heated to 80 ° C. and melted, and 10 parts by mass of 2,5-dimethyl-2,5-bis (t-butylperoxy) hexane. An organic peroxide (I-1) diluted with a release agent was obtained.

  The organic peroxide (I-1) diluted with a release agent was charged into a microfeeder manufactured by Furu Science Co., Ltd. The temperature of the syringe part of the micro feeder can be controlled by a jacket, and the temperature was kept at 80 ° C.

  Up to the position of L / D = 20 of a twin screw extruder (Ikegai PCM-30: L / D = 40) is a set temperature of 150 ° C. and a residence time of about 2 minutes, and the polyester resin (a) is 85 mass. And 15 parts by mass of polyester resin (b) were supplied and melted. From the center, 1 part by mass of organic peroxide (I-1) diluted with a release agent by a microfeeder was added. Organic peroxide diluted with polyester resin (a), polyester resin (b), and release agent (I-1) from the position of L / D = 21 at an external temperature setting of 180 ° C. and a residence time of about 2 minutes ) Were mixed to obtain a polyester resin (C-1).

  The supply pressure of the organic peroxide (I) diluted with the mold release agent in the microfeeder was 0.2 MPa and was stable. The SADT of 2,5-dimethyl-2,5-bis (t-butylperoxy) hexane is 80 ° C. Table 2 shows polyester resin (a), polyester resin (b), organic peroxide, blending amount of diluent, organic peroxide SADT, organic peroxide dilution rate X, organic peroxide supply temperature, etc. Shown in

  94 parts by mass of a polyester resin (C-1), 3 parts by mass of a quinacridone pigment (E02 manufactured by Clariant), 2 parts by mass of carnauba wax, and 1 part by mass of a negatively chargeable charge control agent LR-147 (manufactured by Nippon Carlit) Mix, melt knead using a twin-screw extruder at an external temperature setting of 160 ° C. and a residence time of 1 minute, coarsely pulverize, finely pulverize with a jet mill pulverizer, and fine powder with an average particle size of 5 μm with a classifier Obtained.

  To the fine powder thus obtained, silica (R-972, manufactured by Nippon Aerosil Co., Ltd.) was added so as to be 0.2 parts by mass, and mixed and adhered with a Henschel mixer to obtain toner 1. This toner was mounted on a non-magnetic one-component dry copying machine and its performance was evaluated. Table 3 shows the evaluation results of the toner.

Example 2
75 parts by mass of a mold release agent (SP-0160 manufactured by Nippon Seiki Co., Ltd.) was heated to 80 ° C. and melted to obtain 25 masses of 2,5-dimethyl-2,5-bis (t-butylperoxy) hexane. Part was added to obtain organic peroxide (I-2) diluted with a mold release agent, and 0.4 parts by mass of organic peroxide (I-2) diluted with a mold release agent using a microfeeder. A polyester resin (C-2) was obtained in the same manner as in Example 1 except that it was added.

  The supply pressure of the organic peroxide (I-2) diluted with the mold release agent in the microfeeder was 0.2 MPa and was stable.

  Further, Toner 2 was obtained in the same manner as in Example 1 except that polyester resin (C-2) was used. Table 3 shows the evaluation results of the toner.

Example 3
95 parts by weight of mold release agent (SP-0160 manufactured by Nippon Seiki Co., Ltd.) was heated to 80 ° C. and melted, and 5 parts by mass of t-butylperoxy 2-ethylhexanoate was added. A diluted organic peroxide (I-3) was obtained, and the same as in Example 1 except that 2 parts by mass of the organic peroxide (I-3) diluted with a release agent was added by a microfeeder. A polyester resin (C-3) was obtained by the method.

  The supply pressure of the organic peroxide (I-3) diluted with the mold release agent in the microfeeder was 0.2 MPa and was stable.

  A toner 3 was obtained in the same manner as in Example 1 except that the polyester resin (C-3) was used. Table 3 shows the evaluation results of the toner.

Comparative Example 1
The same procedure as in Example 1 was conducted except that t-butylperoxy 2-ethylhexanoate was charged into a microfeeder and 0.1 parts by mass of t-butylperoxy-2-ethylhexanoate was added by the microfeeder. It was.

After a while from the start of production, t-butylperoxy 2-ethylhexanoate is self-promoted and decomposed in the microfeeder, and since the supply pressure has increased, it is difficult to continue the production and the production is stopped, so a polyester resin is obtained. I couldn't.

Claims (3)

  A method for producing a polyester resin for a toner, in which an organic peroxide dispersed or dissolved in a release agent is supplied into a melted polyester resin having an unsaturated double bond to perform a crosslinking reaction.   The method for producing a polyester resin for a toner according to claim 1, wherein the release agent has a melting point of 120 ° C. or less.   The method for producing a polyester resin for toner according to claim 1 or 2, wherein the mass ratio of the organic peroxide to the release agent is 0.1 / 99.9 to 50/50.