CN105017486A - Special macromolecular wax-containing resin for high definition digital developing agent and preparation method thereof - Google Patents
Special macromolecular wax-containing resin for high definition digital developing agent and preparation method thereof Download PDFInfo
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- CN105017486A CN105017486A CN201410178938.2A CN201410178938A CN105017486A CN 105017486 A CN105017486 A CN 105017486A CN 201410178938 A CN201410178938 A CN 201410178938A CN 105017486 A CN105017486 A CN 105017486A
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Abstract
The invention discloses special macromolecular wax-containing resin for a high definition digital developing agent and a preparation method thereof. The special macromolecular wax-containing resin is prepared from 70-85 parts of styrene, 17-23 parts of butyl acrylate, 3-5 parts of methyl methacrylate, 3-5 parts of isooctyl ester, 2-4 parts of di-tert-butyl peroxide, 2-4 parts of divinyl benzene, 0.1-0.3 part of tert-dodecylmercaptan and 3-8 parts of PP-wax through the steps of mixing, dropwise adding reaction, smashing and sieving. High-speed digital copier carbon powder produced through the resin has wide molecular weight distribution, can meet the deviation resistance requirements, have excellent fusion performance under low temperature fixation, avoid roll sticking and the generation of waste powder, and not only can improve the transfer rate of a high-speed digital copier and reduce use cost, but also avoid pollution to the environment.
Description
Technical field
The present invention relates to technical field of polymer materials, particularly relate to a kind of making high-speed digital duplicator carbon dust main raw material---high-definition digital photographic developer special polymer content of wax resin and preparation method thereof.
Background technology
High-definition digital photographic developer special polymer content of wax resin is the main raw material producing high-speed digital used in copy machines carbon dust.At present, the resin that on market, high-speed digital duplicator carbon dust uses adopts the vinylbenzene, Butyl acrylate and the dibutyl maleinate resin that suspend and make, and molecular weight distribution is little, and melting index is high, and high temperature not easily dissolves.The high-speed digital duplicator carbon dust made with this resin, in use easy roll banding and fixing difference, can produce a large amount of useless powder, and transferring rate is lower, use cost is high, not only taste weight, and pollutes the environment.
Summary of the invention
The object of the invention is to overcome existing defect, a kind of high-definition digital photographic developer special polymer content of wax resin is provided, with the high-speed digital duplicator carbon dust of this production of resins, there is comparatively wide molecular weight distribution, adding polymer content can meet anti-offset resistance, excellent melting behaviour is had under low-temperature fixing, not roll banding, fixing good, useless powder can not be produced, not only can improve the transferring rate of high-speed digital duplicator carbon dust, reduce use cost, not only tasteless, also can not to environment.
Another object of the present invention is to provide the preparation method of a kind of high-definition digital photographic developer special polymer content of wax resin.
Above-mentioned purpose of the present invention is realized by following technical solution:
The invention provides a kind of high-definition digital photographic developer special polymer content of wax resin, the weight part of its constitutive material is:
Present invention also offers the preparation method of a kind of high-definition digital photographic developer special polymer content of wax resin, comprise the following steps:
(1) vinylbenzene of 70-85 part, the Butyl acrylate of 17-23 part, 3-5 part methymethacrylate and 3-5 part isooctyl is taken, pumping into header tank stirs after 15-20 minute, add the ditertiary butyl peroxide of 2-4 part, the tert-dodecyl mercaptan of 0.1-0.3 part and the Vinylstyrene of 2-4 part again, continue uniform stirring, make compound for subsequent use;
(2) add the solvent xylene of 70-85 part and the PP wax of 3-8 part in a kettle., spacer carries out electrically heated simultaneously, continues uniform stirring, is warmed up to 135-140 DEG C;
(3) start to drip with the compound made in step (1), control 4 hours and drip off, then be incubated 4 hours, insulation terminates normal pressure 2 hours again;
(4) normal pressure terminates, and starts to vacuumize, de-dimethylbenzene, time 3 hours, and during de-dimethylbenzene, bottom valve must be heated in heating jacket preheating;
(5) the material pressurized air in reactor is released;
(6) with pulverizer, the work in-process crossed through cooling process are pulverized;
(7) with 120 eye mesh screens, the work in-process through pulverizing being sieved, making its particle diameter be 0.15-0.3 μm, high-definition digital photographic developer special polymer content of wax resin can be obtained.
Adopt such scheme, have the following advantages:
Owing to containing PP wax in a kind of high-definition digital photographic developer of the present invention special polymer content of wax resin, can meet anti-offset resistance, low-temperature fixing anti-caking effect, add Vinylstyrene as linking agent simultaneously, improve resin polymer ratio, there is excellent melt performance in low-temperature fixing, good dispersity, image stabilization is beautiful, the manuscript printed not fugitive color.Useless powder would not be produced with in the high-speed digital duplicator carbon dust high-definition digital photographic developer special polymer content of wax resin use procedure of this production of resins.Therefore with the high-speed digital duplicator carbon dust resin of production of resins of the present invention, not only transferring rate is high, use cost is low, not only tasteless, also can avoid environmental pollution.
Because resin of the present invention adopts solvent method to produce, wherein separant is solvent xylene, the resin content of wax that reflects can be made even, and separant solvent xylene can recycle, and the high-speed digital duplicator carbon dust standby by this resin-made is not only evenly mixing, without white tiles, compatible good, carried charge is even, and it is beautiful to have printing manuscript lovely luster, good resolution, level advantages of higher.
Embodiment
Below the preferred embodiments of the present invention are described, should be appreciated that preferred embodiment described herein is only for instruction and explanation of the present invention, is not intended to limit the present invention.
Embodiment 1:
(1) vinylbenzene of 70 parts, the Butyl acrylate of 23 parts, 3 parts of methymethacrylates and 3 parts of isooctyls are taken, pump into after header tank stirs 15 minutes, add the ditertiary butyl peroxide of 2 parts, the tert-dodecyl mercaptan of 0.1 part and the Vinylstyrene of 2 parts again, continue uniform stirring, make compound for subsequent use;
(2) the PP wax of the dimethylbenzene of 70 parts and 3 parts is pumped into reactor
Heat (a) open condenser cooling water;
B () drives electrically heated switch;
C () opens after pumping into header tank, stir and prepare to drip, pressure falls branch's lower boiling dimethylbenzene (before 138 DEG C);
(3) heat to 138 DEG C and start to drip the compound made in step (1), control, at 4 hours, in dropping process, to want average rate to drip, as a part of lower boiling dimethylbenzene will be pressed when finding that temperature reduces, keep reaction normal;
(4) drip end, stir and still will open and can not stop, be incubated 4 hours, temperature controls at 138 DEG C, regulate electrically heated switch, if temperature rises fast, close 1 group or 2 groups of heating collars, open reactor vacuum valve, reclaim jar valve, dimethylbenzene sucks withdrawing can automatically;
(5) insulation terminates to start normal pressure 2 hours, should establish electrically heated 1 group or 2 groups newly, rise to 150 DEG C in normal pressure process;
(6) normal pressure terminates, and starts to vacuumize, de-dimethylbenzene, time 3 hours, and during de-dimethylbenzene, bottom valve must be heated in heating jacket preheating;
(7), during discharging, air compressor air binder is opened
To have an optimistic view of a () opens vacuum main valve after, the situation that under visor, material rises, if it is fast to rise, open point;
B () etc. open sufficient liquid-ring vacuum pump after (11KW), material sinking, drives secondary Roots vaccum pump (3KW) again during stirring;
C secondarys such as () is normal after, then drive third stage Roots vaccum pump (4KW);
D () is finally waited until and is extracted into glass visor without can discharging after melted paraxylene;
(8) material is placed in go-cart pallet cools;
Within (9) second days, by after first for lumpy material in pallet coarse reduction, then carry out fine powder and be broken to present resin particle diameter;
(10) with 120 eye mesh screens, the work in-process through pulverizing being sieved, making its particle diameter be 0.15 μm, high-definition digital photographic developer special polymer content of wax resin can be obtained.
Embodiment 2:
(1) vinylbenzene of 75 parts, the Butyl acrylate of 20 parts, 4 parts of methymethacrylates and 4 parts of isooctyls are taken, pump into after header tank stirs 15 minutes, add the ditertiary butyl peroxide of 3 parts, the tert-dodecyl mercaptan of 0.2 part and the Vinylstyrene of 3 parts again, continue uniform stirring, make compound for subsequent use;
(2) the PP wax of the dimethylbenzene of 80 parts and 5 parts is pumped into reactor
Heat (a) open condenser cooling water;
B () drives electrically heated switch;
C () opens after pumping into header tank, stir and prepare to drip, pressure falls branch's lower boiling dimethylbenzene (before 140 DEG C);
(3) heat to 140 DEG C and start to drip the compound made in step (1), control, at 4 hours, in dropping process, to want average rate to drip, as a part of lower boiling dimethylbenzene will be pressed when finding that temperature reduces, keep reaction normal;
(4) drip end, stir and still will open and can not stop, be incubated 4 hours, temperature controls at 140 DEG C, regulate electrically heated switch, if temperature rises fast, close 1 group or 2 groups of heating collars, open reactor vacuum valve, reclaim jar valve, dimethylbenzene sucks withdrawing can automatically;
(5) insulation terminates to start normal pressure 2 hours, should establish electrically heated 1 group or 2 groups newly, rise to 155 DEG C in normal pressure process;
(6) normal pressure terminates, and starts to vacuumize, de-dimethylbenzene, time 3 hours, and during de-dimethylbenzene, bottom valve must be heated in heating jacket preheating;
(7), during discharging, air compressor air binder is opened
To have an optimistic view of a () opens vacuum main valve after, the situation that under visor, material rises, if it is fast to rise, open point;
B () etc. open sufficient liquid-ring vacuum pump after (11KW), material sinking, drives secondary Roots vaccum pump (3KW) again during stirring;
C secondarys such as () is normal after, then drive third stage Roots vaccum pump (4KW);
D () is finally waited until and is extracted into glass visor without can discharging after melted paraxylene;
(8) material is placed in go-cart pallet cools;
Within (9) second days, by after first for lumpy material in pallet coarse reduction, then carry out fine powder and be broken to present resin particle diameter;
(10) with 120 eye mesh screens, the work in-process through pulverizing being sieved, making its particle diameter be 0.23 μm, high-definition digital photographic developer special polymer content of wax resin can be obtained.
Embodiment 3:
(1) vinylbenzene of 85 parts, the Butyl acrylate of 17 parts, 5 parts of methymethacrylates and 5 parts of isooctyls are taken, pump into after header tank stirs 15 minutes, add the ditertiary butyl peroxide of 4 parts, the tert-dodecyl mercaptan of 0.3 part and the Vinylstyrene of 4 parts again, continue uniform stirring, make compound for subsequent use;
(2) the PP wax of the dimethylbenzene of 85 parts and 8 parts is pumped into reactor
Heat (a) open condenser cooling water;
B () drives electrically heated switch;
C () opens after pumping into header tank, stir and prepare to drip, pressure falls branch's lower boiling dimethylbenzene (before 139 DEG C);
(3) heat to 139 DEG C and start to drip the compound made in step (1), control, at 4 hours, in dropping process, to want average rate to drip, as a part of lower boiling dimethylbenzene will be pressed when finding that temperature reduces, keep reaction normal;
(4) drip end, stir and still will open and can not stop, be incubated 4 hours, temperature controls at 139 DEG C, regulate electrically heated switch, if temperature rises fast, close 1 group or 2 groups of heating collars, open reactor vacuum valve, reclaim jar valve, dimethylbenzene sucks withdrawing can automatically;
(5) insulation terminates to start normal pressure 2 hours, should establish electrically heated 1 group or 2 groups newly, rise to 160 DEG C in normal pressure process;
(6) normal pressure terminates, and starts to vacuumize, de-dimethylbenzene, time 3 hours, and during de-dimethylbenzene, bottom valve must be heated in heating jacket preheating;
(7), during discharging, air compressor air binder is opened
To have an optimistic view of a () opens vacuum main valve after, the situation that under visor, material rises, if it is fast to rise, open point;
B () etc. open sufficient liquid-ring vacuum pump after (11KW), material sinking, drives secondary Roots vaccum pump (3KW) again during stirring;
C secondarys such as () is normal after, then drive third stage Roots vaccum pump (4KW);
D () is finally waited until and is extracted into glass visor without can discharging after melted paraxylene;
(8) material is placed in go-cart pallet cools;
Within (9) second days, by after first for lumpy material in pallet coarse reduction, then carry out fine powder and be broken to present resin particle diameter;
(10) with 120 eye mesh screens, the work in-process through pulverizing being sieved, making its particle diameter be 0.3 μm, high-definition digital photographic developer special polymer content of wax resin can be obtained.
Finally, it should be noted that above what enumerate is only 3 kinds of specific embodiments of the present invention.Obviously, the present invention is not limited to above embodiment, can also have a lot of distortion.All distortion that those of ordinary skill in the art can directly derive or associate from content disclosed by the invention, all should think protection scope of the present invention.
Containing PP wax in a kind of high-definition digital photographic developer of the present invention special polymer content of wax resin, can meet anti-offset resistance, low-temperature fixing anti-caking effect, add Vinylstyrene as linking agent simultaneously, improve resin polymer ratio, there is excellent melt performance in low-temperature fixing, good dispersity, image stabilization is beautiful, the manuscript printed not fugitive color.Useless powder would not be produced with in the high-speed digital duplicator carbon dust high-definition digital photographic developer special polymer content of wax resin use procedure of this production of resins.Therefore with the high-speed digital duplicator carbon dust resin of production of resins of the present invention, not only transferring rate is high, use cost is low, not only tasteless, also can avoid environmental pollution.Because resin of the present invention adopts solvent method to produce, wherein separant is solvent xylene, the resin content of wax that reflects can be made even, and separant solvent xylene can recycle, and the high-speed digital duplicator carbon dust standby by this resin-made is not only evenly mixing, without white tiles, compatible good, carried charge is even, and it is beautiful to have printing manuscript lovely luster, good resolution, level advantages of higher.
Claims (2)
1. a high-definition digital photographic developer special polymer content of wax resin, is characterized in that the weight part of its constitutive material is:
2. the preparation method of a kind of high-definition digital photographic developer according to claim 1 special polymer content of wax resin, is characterized in that comprising the following steps:
(1) vinylbenzene of 70-85 part, the Butyl acrylate of 17-23 part, 3-5 part methymethacrylate and 3-5 part isooctyl is taken, pumping into header tank stirs after 15-20 minute, add the ditertiary butyl peroxide of 2-4 part, the tert-dodecyl mercaptan of 0.1-0.3 part and the Vinylstyrene of 2-4 part again, continue uniform stirring, make compound for subsequent use;
(2) add the solvent xylene of 70-85 part and the PP wax of 3-8 part in a kettle., spacer carries out electrically heated simultaneously, continues uniform stirring, is warmed up to 135-140 DEG C;
(3) start to drip with the compound made in step (1), control 4 hours and drip off, then be incubated 4 hours, insulation terminates normal pressure 2 hours again;
(4) normal pressure terminates, and starts to vacuumize, de-dimethylbenzene, time 3 hours, and during de-dimethylbenzene, bottom valve must be heated in heating jacket preheating;
(5) the material pressurized air in reactor is released;
(6) with pulverizer, the work in-process crossed through cooling process are pulverized;
(7) with 120 eye mesh screens, the work in-process through pulverizing being sieved, making its particle diameter be 0.15-0.3 μm, high-definition digital photographic developer special polymer content of wax resin can be obtained.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201410178938.2A CN105017486A (en) | 2014-04-29 | 2014-04-29 | Special macromolecular wax-containing resin for high definition digital developing agent and preparation method thereof |
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| CN201410178938.2A CN105017486A (en) | 2014-04-29 | 2014-04-29 | Special macromolecular wax-containing resin for high definition digital developing agent and preparation method thereof |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108563103A (en) * | 2018-04-28 | 2018-09-21 | 无锡佳腾磁性粉有限公司 | High-definition digital copper gold dry type bi-component ink powder and preparation method thereof |
| CN108594608A (en) * | 2018-04-28 | 2018-09-28 | 无锡佳腾磁性粉有限公司 | Green laser printer dry type ink powder and preparation method thereof |
| CN108646528A (en) * | 2018-04-28 | 2018-10-12 | 无锡佳腾磁性粉有限公司 | Bronze red Ultraluminescence anti-fake printer dry type ink powder and preparation method thereof |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1138168A (en) * | 1995-05-31 | 1996-12-18 | 佳能株式会社 | Toner for developing electrostatic images, and process for producing the same |
| US20050004261A1 (en) * | 2003-04-07 | 2005-01-06 | Seiko Epson Corporation | Aqueous ink composition and method of manufacturing the same |
| CN1944485A (en) * | 2006-09-19 | 2007-04-11 | 张家港市威迪森油墨有限公司 | Blend polymerizing preparing method for copolymer resin |
| CN101206419A (en) * | 2007-12-20 | 2008-06-25 | 周学良 | Polymer resin for colorful laser printer carbon powder and method of producing the same |
| CN102321311A (en) * | 2011-06-14 | 2012-01-18 | 湖北远东卓越科技有限公司 | Method for preparing special low-temperature resin for digital copier carbon powder |
| CN102854763A (en) * | 2011-06-28 | 2013-01-02 | 柯尼卡美能达商用科技株式会社 | Toner for electrostatic latent image development |
-
2014
- 2014-04-29 CN CN201410178938.2A patent/CN105017486A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1138168A (en) * | 1995-05-31 | 1996-12-18 | 佳能株式会社 | Toner for developing electrostatic images, and process for producing the same |
| US20050004261A1 (en) * | 2003-04-07 | 2005-01-06 | Seiko Epson Corporation | Aqueous ink composition and method of manufacturing the same |
| CN1944485A (en) * | 2006-09-19 | 2007-04-11 | 张家港市威迪森油墨有限公司 | Blend polymerizing preparing method for copolymer resin |
| CN101206419A (en) * | 2007-12-20 | 2008-06-25 | 周学良 | Polymer resin for colorful laser printer carbon powder and method of producing the same |
| CN102321311A (en) * | 2011-06-14 | 2012-01-18 | 湖北远东卓越科技有限公司 | Method for preparing special low-temperature resin for digital copier carbon powder |
| CN102854763A (en) * | 2011-06-28 | 2013-01-02 | 柯尼卡美能达商用科技株式会社 | Toner for electrostatic latent image development |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108563103A (en) * | 2018-04-28 | 2018-09-21 | 无锡佳腾磁性粉有限公司 | High-definition digital copper gold dry type bi-component ink powder and preparation method thereof |
| CN108594608A (en) * | 2018-04-28 | 2018-09-28 | 无锡佳腾磁性粉有限公司 | Green laser printer dry type ink powder and preparation method thereof |
| CN108646528A (en) * | 2018-04-28 | 2018-10-12 | 无锡佳腾磁性粉有限公司 | Bronze red Ultraluminescence anti-fake printer dry type ink powder and preparation method thereof |
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Application publication date: 20151104 |