CN116813891B - Fatty acid modified polyester, preparation method and offset printing compound - Google Patents

Fatty acid modified polyester, preparation method and offset printing compound Download PDF

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CN116813891B
CN116813891B CN202310924006.7A CN202310924006A CN116813891B CN 116813891 B CN116813891 B CN 116813891B CN 202310924006 A CN202310924006 A CN 202310924006A CN 116813891 B CN116813891 B CN 116813891B
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acid
percent
fatty acid
stirring
modified polyester
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CN116813891A (en
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郑学飞
成宇聪
黄志彬
林剑雄
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Huizhou Huahong New Material Co ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/16Dicarboxylic acids and dihydroxy compounds
    • C08G63/20Polyesters having been prepared in the presence of compounds having one reactive group or more than two reactive groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • C08G63/82Preparation processes characterised by the catalyst used
    • C08G63/85Germanium, tin, lead, arsenic, antimony, bismuth, titanium, zirconium, hafnium, vanadium, niobium, tantalum, or compounds thereof
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D11/00Inks
    • C09D11/02Printing inks
    • C09D11/10Printing inks based on artificial resins
    • C09D11/101Inks specially adapted for printing processes involving curing by wave energy or particle radiation, e.g. with UV-curing following the printing

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Polyesters Or Polycarbonates (AREA)

Abstract

The embodiment of the invention discloses fatty acid modified polyester, a preparation method and an offset printing compound, which comprise the following components in parts by mass: 17.1 to 19.8 percent of basf Sovermol750 polyol, 17.4 to 20.3 percent of trimethylolpropane, 2.6 to 3.1 percent of pentaerythritol, 15.6 to 18.1 percent of hydrogenated bisphenol A, 2 to 10 percent of monobasic fatty acid, 8.8 to 24.6 percent of p-methylbenzoic acid, 15.1 to 17.5 percent of isophthalic acid, 7.5 to 8.7 percent of terephthalic acid, 1.9 to 2.2 percent of dimer fatty acid, 0.35 to 0.41 percent of pyromellitic anhydride and 0.62 to 0.72 percent of trimellitic anhydride. 0.1 to 0.3 percent of antioxidant and 0.03 to 0.1 percent of catalyst. The invention introduces Bayer Sovermol750 polyol and trimethylolpropane into the formula for use, and improves the polymerization degree of the resin by reducing the content of monobasic fatty acid and using high-functional anhydride, thereby realizing the unification of high color concentration and high wear resistance, and the synthesized polyester resin has high color concentration, good wear resistance and high photocuring speed.

Description

Fatty acid modified polyester, preparation method and offset printing compound
Technical Field
The invention belongs to the technical field of high polymer material modification, and particularly relates to fatty acid modified polyester, a preparation method and an offset printing compound.
Background
Offset printing is one of the most widely used printing modes in the printing field. The UV (ultraviolet light curing) offset printing binders (resins) have a high pigment content and polyester resins or alkyd resins having a good pigment dispersion are generally selected as the main resin component for better color dispersion.
The color density refers to the density of color, also called saturation of color, and is a parameter indicating the selective absorption capacity of color light, that is, the reflected color density value measured under the complementary color filter. The higher the color density, the stronger the absorption capacity for the color light, that is, the higher the saturation of the color. Generally, higher color density can improve the color rendition and quality of the printed matter, and can also improve the printing efficiency and production benefit.
Wear resistance refers to resistance to mechanical friction, wear. The wear resistance is good, the quality of printed matters can be guaranteed, and the wear and damage are reduced, so that the service life of the product is prolonged. In addition, the printing ink can be applied to special printing fields, such as printing of materials such as metal cans and glass. These materials have smooth surfaces, low friction coefficients, and high hardness, which makes printing very difficult. But the wear resistance is good, the surface properties of the materials can be well adapted, high-speed and accurate printing is realized, and the quality of printed matters is ensured. Besides being applied to the printing of common products such as packaging boxes, cartons and the like, the printing ink can also be applied to special fields such as textile industry, plastic industry and the like. These industries need to perform high-speed production, and at the same time, also need to protect the surface of the product from damage, improve the wear resistance and service life of the product, and ensure the production efficiency and the product quality.
It is well known in the art of alkyd or polyester resin synthesis that the wetting characteristics and color concentration of the final product can be improved by increasing the content of monobasic fatty acids in the formulation, or by increasing the content of polyol soft segments (e.g., ethylene glycol or polyethylene glycol); however, too much incorporation of the monohydric fatty acid or the polyol soft segment may result in deterioration of the abrasion resistance of the final product.
Disclosure of Invention
The embodiment of the invention provides fatty acid modified polyester, which comprises the following components in parts by mass:
17.1 to 19.8 percent of Basoff Sovermol750 polyol,
17.4 To 20.3 percent of trimethylolpropane,
Pentaerythritol 2.6-3.1%,
15.6 To 18.1 percent of hydrogenated bisphenol A,
2-10% Of monobasic fatty acid,
8.8 To 24.6 percent of p-methylbenzoic acid,
15.1 To 17.5 percent of isophthalic acid,
7.5 To 8.7 percent of terephthalic acid,
1.9 To 2.2 percent of dimer fatty acid,
0.35 To 0.41 percent of pyromellitic anhydride,
0.62 To 0.72 percent of trimellitic anhydride.
Specifically, the basf Sovermol750 polyol has better fluidity, pentaerythritol can improve the body bone, and hydrogenated bisphenol A can keep the balance of wettability and solidification speed. Trimethylolpropane is a commonly used triol that forms the basic backbone. Isophthalic acid and terephthalic acid are commonly used dibasic acids that form the backbone of the molecule, and dimerized fatty acids can improve the flexibility of the formulation. In polyester formulations, monoacids are generally used in order to control the molecular weight and to adjust the hydroxyl number.
Preferably, the monobasic fatty acid is stearic acid, the mass fraction is 3-7%, and the mass fraction of p-methylbenzoic acid is 15-25%.
0.1 To 0.3 percent of antioxidant,
0.03 To 0.1 percent of catalyst. Specifically, the antioxidant is bht.
Specifically, the catalyst is stannous octoate.
Specifically, the monobasic fatty acid is any one of stearic acid, palmitic acid, oleic acid, coconut oleic acid, dodecanol stearic acid or lauric acid.
A method for preparing a fatty acid modified polyester comprising:
Adding 17.1-19.8% of Basoff Sovermol750 polyhydric alcohol, 17.4-20.3% of trimethylolpropane, 15.6-18.1% of hydrogenated bisphenol, 0.1-0.3% of antioxidant and 0.1% of catalyst into a reaction kettle according to the mass fraction ratio, heating at 98-105 ℃, and stirring until the components are uniformly dispersed;
Stirring 0.35-0.41% of pyromellitic anhydride and 0.62-0.72% of trimellitic anhydride for 1h at the temperature of 100-103 ℃ to carry out anhydration reaction;
Heating to 180 ℃, stopping stirring, sequentially adding 2.6-3.1% of pentaerythritol, 4.2-29.6% of monobasic fatty acid, 15.1-17.5% of isophthalic acid, 7.5-8.7% of terephthalic acid and 1.9-2.2% of dimer fatty acid, stirring, introducing nitrogen, heating to 200 ℃, preserving heat for at least 1h, heating to 210 ℃, preserving heat for at least 1h, heating to 230 ℃, preserving heat for at least 5h, sampling and measuring an acid value, introducing cold oil into a reaction kettle, cooling to below 170 ℃ and discharging after the acid value is less than 30.
Specifically, the antioxidant is bht.
Specifically, the catalyst is stannous octoate.
Specifically, the monobasic fatty acid is any one of stearic acid, palmitic acid, oleic acid, coconut oleic acid, dodecanol stearic acid or lauric acid.
A method of making a UV offset composite comprising:
Crushing the fatty acid modified polyester solid, adding trimethylolpropane triacrylate and para-hydroxyanisole, and stirring at 90-103 ℃ until the solid is completely dissolved;
adding photoinitiator, stirring to dissolve completely, adding toner, stirring for dispersing, blending into paste, and grinding with a three-roller inking machine.
In the examples of the present invention basf Sovermol 750 is a branched polyol with an average functionality of 3. According to the invention, by replacing part of trimethylolpropane with the Sovermol 750, the mechanical hardness of the resin film is improved, and the excellent performance is maintained.
The formula of the invention has low content of monobasic fatty acid, which is less than 10 percent (weight percent); the conventional monobasic fatty acid modified polyesters have relatively high monobasic fatty acid content, typically up to 15 to 30 weight percent. The lower content of monobasic fatty acid brings better film forming performance.
The hydrogenated bisphenol A is adopted to replace common micromolecular dihydric alcohol such as 1, 4-butanediol, neopentyl glycol and 1, 6-hexanediol, and the hydrogenated bisphenol A is matched with polybasic acid anhydrides such as trimellitic anhydride, pyromellitic anhydride and the like to be used, so that better balance of body bone and wettability is maintained.
The invention has the beneficial effects that: the invention introduces the formula of the basf Sovermol 750 polyol and the trimethylolpropane to use, and improves the polymerization degree of the resin by reducing the content of monobasic fatty acid and using high-functional anhydride, thereby realizing the unification of high color concentration and high wear resistance, and the offset printing compound prepared by the synthetic polyester resin has high color concentration, good wear resistance, high photo-curing speed and good wettability, and meets the requirements of high-grade UV curing offset printing resin. In addition, the production process is simpler, the time consumption is short, the energy is saved, no organic solvent is added in the reaction process, raw materials are easy to obtain, no waste gas is generated, and the method is environment-friendly and has good economic performance.
Detailed Description
In order to enable those skilled in the art to better understand the present invention, the following description will make clear and complete descriptions of the technical solutions according to the embodiments of the present invention with reference to the accompanying drawings. The examples of the present invention provide the following modified formulations of fatty acid modified polyesters, table 1 is a parameter of molecular weight and functionality of each component.
TABLE 1 component parameters
Molecular weight Functionality of
Basoff Sovermol750 polyol 525 3
tmp 134.2 3
Pentaerythritol 136.2 4
Hydrogenated bisphenol a 240.38 2
Para-methylbenzoic acid 136.15 1
Stearic acid 284.5 1
Isophthalic acid 166.1 2
Terephthalic acid 166.1 2
Dimerized fatty acids 146.21 2
Pyromellitic anhydride 218.12 4
Trimellitic anhydride 192.1 3
Palmitic acid 256.4 1
Oleic acid 282.46 1
Coconut oleic acid 343.38 1
Dodecahydroxy stearic acid 300.48 1
Tables 2 to 9 show the formulations of examples 1 to 8, wherein the amount of the additive was measured in kg.
TABLE 2 example 1
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 136.15 1 1
Stearic acid 455.2 1.6 1.6
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
The method for modifying polyester with fatty acid provided in example 1 is as follows:
1. Putting the Pasteur Sovermol750 polyol, the trimethylolpropane, the hydrogenated bisphenol, 0.1% of antioxidant bht and 0.1% of catalyst stannous octoate into a reaction kettle according to the mass shown in Table 2, heating at 98 ℃, and stirring until the materials are uniformly dispersed;
2. stirring pyromellitic anhydride and trimellitic anhydride for 1h at the temperature of 100 ℃ to carry out an anhydration reaction;
3. Heating to 180 ℃, stopping stirring, sequentially adding pentaerythritol, monobasic fatty acid stearic acid, isophthalic acid, terephthalic acid and dimerized fatty acid, stirring, introducing nitrogen, heating to 200 ℃, preserving heat for 1h, heating to 210 ℃, preserving heat for 1h, heating to 230 ℃, preserving heat for 5h, sampling to measure the acid value, introducing cold oil into a reaction kettle, cooling to 170 ℃ and discharging after the acid value is less than 30.
TABLE 3 example 2
The method for modifying polyesters with fatty acids provided in example 2 is as follows:
1. Putting the Pasteur Sovermol750 polyol, the trimethylolpropane, the hydrogenated bisphenol, the antioxidant bht with the mass fraction of 0.3% and the stannous octoate with the mass fraction of 0.3% into a reaction kettle according to the mass shown in the table 3, heating at 105 ℃, and stirring until the materials are uniformly dispersed;
2. Stirring pyromellitic anhydride and trimellitic anhydride for 1h at the temperature of 103 ℃ to carry out an anhydration reaction;
3. Heating to 180 ℃, stopping stirring, sequentially adding pentaerythritol, monobasic fatty acid stearic acid, isophthalic acid, terephthalic acid and dimerized fatty acid, stirring, introducing nitrogen, heating to 200 ℃, preserving heat for 1h, heating to 210 ℃, preserving heat for 1h, heating to 230 ℃, preserving heat for 5h, sampling to measure the acid value, introducing cold oil into a reaction kettle, cooling to 170 ℃ and discharging after the acid value is less than 30.
TABLE 4 example 3
The method for modifying polyester with fatty acid provided in example 3 is as follows:
1. Putting the Pasteur Sovermol750 polyol, the trimethylolpropane, the hydrogenated bisphenol, the antioxidant bht with the mass fraction of 0.2% and the stannous octoate with the mass fraction of 0.2% into a reaction kettle according to the mass shown in the table 4, heating at 100 ℃, and stirring until the materials are uniformly dispersed;
2. stirring pyromellitic anhydride and trimellitic anhydride for 1h at the temperature of 100 ℃ to carry out an anhydration reaction;
3. Heating to 180 ℃, stopping stirring, sequentially adding pentaerythritol, monobasic fatty acid stearic acid, isophthalic acid, terephthalic acid and dimerized fatty acid, stirring, introducing nitrogen, heating to 200 ℃, preserving heat for 1h, heating to 210 ℃, preserving heat for 1h, heating to 230 ℃, preserving heat for 5h, sampling to measure the acid value, introducing cold oil into a reaction kettle, cooling to 170 ℃ and discharging after the acid value is less than 30.
The preparation methods used in examples 4-14 below refer to the methods shown in examples 1-3, and are not described in detail herein.
TABLE 5 example 4
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 217.84 1.6 1.6
Stearic acid 284.5 1 1
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
TABLE 6 example 5
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 245.07 1.8 1.8
Stearic acid 227.6 0.8 0.8
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
TABLE 7 example 6
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 272.3 2 2
Stearic acid 170.7 0.6 0.6
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
TABLE 8 example 7
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 299.53 2.2 2.2
Stearic acid 113.8 0.4 0.4
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
TABLE 9 example 8
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 326.76 2.4 2.4
Stearic acid 56.9 0.2 0.2
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
TABLE 10 example 9
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 340.375 2.5 2.5
Stearic acid 28.45 0.1 0.1
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
TABLE 11 example 10
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 353.99 2.6 2.6
Stearic acid 0 0 0
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
TABLE 12 example 11
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 136.15 2.4 2.4
Palmitic acid 256.4 0.2 0.2
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
TABLE 13 example 12
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 326.76 2.4 2.4
Oleic acid 56.492 0.2 0.2
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
TABLE 14 example 13
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 326.76 2.4 2.4
Coconut oleic acid 68.676 0.2 0.2
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
TABLE 15 example 14
Feeding amount Molar mass Functional group
Basoff Sovermol750 polyol 262.5 0.5 1.5
tmp 268.4 2 6
Pentaerythritol 40.86 0.3 1.2
Hydrogenated bisphenol a 240.38 1 2
Para-methylbenzoic acid 326.76 2.4 2.4
Dodecahydroxy stearic acid 60.096 0.2 0.2
Isophthalic acid 232.54 1.4 2.8
Terephthalic acid 116.27 0.7 1.4
Dimerized fatty acids 29.242 0.2 0.4
Pyromellitic anhydride 5.453 0.025 0.1
Trimellitic anhydride 9.605 0.05 0.15
According to the invention, after the fatty acid modified polyester solid prepared in examples 1-14 is crushed, the crushed solid is put into a 200 g open iron tank, and then trimethylolpropane triacrylate and para-hydroxyanisole are added, the temperature is controlled at 90-103 ℃, and the stirring and dispersing machine is controlled to stir at a low speed of 300r/min until the solid is completely dissolved. Adding a photoinitiator 907, a photoinitiator pbz, controlling the temperature to be 90-103 ℃, and controlling the speed of a stirring and dispersing machine 300r/min to stir at a low speed until the materials are completely dissolved. The stirring speed is controlled, the toner is slowly added, the lower speed is started, the toner is stirred and dispersed at a high speed, the toner is blended into paste, and the paste is rolled and ground to the qualified fineness by a three-roller inking machine, and then the following test is carried out.
The testing method comprises the following steps:
1. color density
The fatty acid modified polyesters prepared in the above examples 1 to 14 were prepared into UV offset printing compositions according to the above preparation methods, printed on the surface of the same medium, and after the sample was printed with a color development instrument by visual method, the sample to be tested was compared with a colorimetric card.
2. Abrasion resistance
Referring to GB/T23989-2009, the color of the silver paperboard is uniformly developed by a color development instrument, after the silver paperboard is fully cured by a UV light curing machine, a sample plate is repeatedly rubbed by a cloth load of 500 g which is dipped with 95% ethanol until the ground color is exposed.
3. Curing speed
The color of the silver paperboard is uniformly developed by a color development instrument, the light curing is carried out at the speed of 20m/min, the ultraviolet light intensity is 80 mJ/square centimeter, and the finger drying method is used for determining whether the silver paperboard is completely cured.
Test results:
The color density, abrasion resistance and curing speed obtained by the formulations of examples 1 to 14 were examined in the above-described manner, and as apparent from examples 11, 12 and 14, the color density was deteriorated when stearic acid was replaced with equimolar palmitic acid, oleic acid and dodecahydroxystearic acid in the formulations of the above examples of the present invention. From example 13, it was found that when stearic acid was replaced with equimolar coconut oleic acid, the color density was not changed, the abrasion resistance was deteriorated, and the curing speed was lowered, so that stearic acid was the most preferable. Among them, examples 7 and 8 exhibited better color density and abrasion resistance, and the photo-curing speed was faster. As is clear from examples 9 and 10, the color density becomes worse as the stearic acid content is reduced, so that the test effect is best when 3 to 7% by mass of the monobasic fatty acid stearic acid is used, and 15 to 25% by mass of p-methylbenzoic acid is used.
TABLE 16 test results
It is apparent that the above examples are given by way of illustration only and are not limiting of the embodiments. Other variations or modifications of the above teachings will be apparent to those of ordinary skill in the art. It is not necessary here nor is it exhaustive of all embodiments. While still being apparent from variations or modifications that may be made by those skilled in the art are within the scope of the invention.
The foregoing is only a partial embodiment of the present invention, and it should be noted that it will be apparent to those skilled in the art that modifications and adaptations can be made without departing from the principles of the present invention, and such modifications and adaptations are intended to be comprehended within the scope of the present invention.

Claims (8)

1. The fatty acid modified polyester is characterized by comprising the following components in parts by mass:
17.1 to 19.8 percent of Basoff Sovermol 750 polyol,
17.4 To 20.3 percent of trimethylolpropane,
Pentaerythritol 2.6-3.1%,
15.6 To 18.1 percent of hydrogenated bisphenol A,
2-10% Of monobasic fatty acid,
8.8 To 24.6 percent of p-methylbenzoic acid,
15.1 To 17.5 percent of isophthalic acid,
7.5 To 8.7 percent of terephthalic acid,
1.9 To 2.2 percent of dimer fatty acid,
0.35 To 0.41 percent of pyromellitic anhydride,
0.62 To 0.72 percent of trimellitic anhydride,
0.1 To 0.3 percent of antioxidant,
0.03-0.1% Of catalyst;
the monobasic fatty acid is any one of stearic acid, oleic acid or coconut oleic acid.
2. The fatty acid modified polyester of claim 1, wherein the antioxidant is bht.
3. The fatty acid modified polyester of claim 1, wherein the catalyst is stannous octoate.
4. The fatty acid modified polyester according to claim 1, wherein the monobasic fatty acid is stearic acid, the mass fraction is 3 to 7%, and the mass fraction of p-methylbenzoic acid is 15 to 24.6%.
5. A method for preparing a fatty acid-modified polyester, comprising:
Adding 17.1-19.8% of Basoff Sovermol 750 polyhydric alcohol, 17.4-20.3% of trimethylolpropane, 15.6-18.1% of hydrogenated bisphenol A,0.1-0.3% of antioxidant and 0.1% of catalyst into a reaction kettle according to the mass fraction ratio, heating at 98-105 ℃, and stirring until the components are uniformly dispersed;
Stirring 0.35-0.41% of pyromellitic anhydride and 0.62-0.72% of trimellitic anhydride at 100-103 ℃ for 1h;
Heating to 180 ℃, stopping stirring, sequentially adding 2.6-3.1% of pentaerythritol, 2-10% of monobasic fatty acid, 15.1-17.5% of isophthalic acid, 7.5-8.7% of terephthalic acid and 1.9-2.2% of dimer fatty acid, stirring, introducing nitrogen, heating to 200 ℃, preserving heat for at least 1h, heating to 210 ℃, preserving heat for at least 1h, heating to 230 ℃, preserving heat for at least 5h, sampling to measure acid value, introducing cold oil into a reaction kettle to cool until the acid value is less than 30, and discharging until the temperature is below 170 ℃;
Wherein the monobasic fatty acid is any one of stearic acid, oleic acid or coconut oleic acid.
6. The method of claim 5, wherein the antioxidant is bht.
7. The method according to claim 5, wherein the catalyst is stannous octoate.
8. A method of preparing a UV offset composite comprising:
Crushing the fatty acid modified polyester solid according to any one of claims 1 to 4, adding trimethylolpropane triacrylate and para-hydroxyanisole, and stirring at 90-103 ℃ until completely dissolved;
adding photoinitiator, stirring to dissolve completely, adding toner, stirring for dispersing, blending into paste, and grinding with a three-roller inking machine.
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