High temperature resistance polyester resin used for powder coating of low TGIC consumption and preparation method thereof
Technical field
The invention belongs to polymeric material field, relate to a kind of high temperature resistance polyester resin, particularly a kind of high temperature resistance polyester resin used for powder coating of low TGIC consumption.
Background technology
Powder coating has solvent-free, pollution-free, recyclable, environmental protection, the saving energy and resource, reduces labor intensity and film physical strength high; thus be rapidly developed, be widely used in household electrical appliances, car paint, aluminum alloy doors and windows and metal and nonmetallic external decoration coating protection.
TGIC curing powder coating is one of maximum powder coating of existing market occupation rate, and wherein TGIC heat resistant powder coating, and being heat resistant type vibrin, to add TGIC be solidifying agent.Wherein heat resistant type vibrin is the critical material in powder coating.The performance of heat resistant type vibrin directly determines that the performance of powder coating and TGIC are the usage quantity of solidifying agent.Because TGIC is poisonous, therefore need to reduce its consumption as far as possible.
Summary of the invention
The present invention, in order to solve the problem, provides a kind of high temperature resistance polyester resin, reaches the object adopting the solidifying agent TGIC of low consumption to obtain the powder coating of resisting high-temperature yellowing equally.
For achieving the above object, the present invention is by the following technical solutions:
The invention provides a kind of high temperature resistance polyester resin used for powder coating of low TGIC consumption, comprise the raw material of following parts by weight:
Further, described high temperature resistance polyester resin comprises the raw material of following parts by weight:
Further, described high temperature resistance polyester resin comprises the raw material of following parts by weight:
Further, described high temperature resistance polyester resin comprises the raw material of following parts by weight:
Further, described high temperature resistance polyester resin also comprises oxidation inhibitor, and described oxidation inhibitor is polynary hindered phenol type antioxidant 1098 and phosphite ester kind antioxidant 890 compound use.
Further, polynary hindered phenol type antioxidant 1098 is 1: 100-250 with the mass ratio of terephthalic acid, and phosphite ester kind antioxidant 890 is 1: 100-150 with the mass ratio of terephthalic acid.
As one embodiment of the present invention, polynary hindered phenol type antioxidant 1098 is 1:1 with the mass ratio of phosphite ester kind antioxidant 890.
The present invention also provides a kind of preparation method of above-mentioned high temperature resistance polyester resin, comprises the following steps:
Synthesis reactor temperature is risen to 90-100 DEG C, add neopentyl glycol, TriMethylolPropane(TMP), terephthalic acid, hexanodioic acid, m-phthalic acid, Mono-n-butyltin, heat up 248-250 DEG C of maintenance under the protection of reaction nitrogen, until the acid number of thing is 5-10mgKOH/g, be cooled to 210-220 DEG C, drop into end-capping reagent m-phthalic acid or (with) hexanodioic acid, be warming up to 242-245 DEG C of maintenance, until reactant acid number is 46-49mgKOH/g, carry out vacuum operating, until reactant acid number is 28-32mgKOH/g, be cooled to 205-210 DEG C, drop into curing catalyst quaternary ammonium salt and antioxidant, maintain and get final product discharging in 15-30 minute.
Compared with prior art, the technical program has the following advantages:
High temperature resistance polyester resin of the present invention by using TriMethylolPropane(TMP), and controls its usage quantity, makes vibrin have high molecular weight and high reticulated structure; By controlling acid-alcohol ratio, control the acid value scope of finished product between 28-32, thus when making vibrin and solidifying agent curing cross-linked, reduce TGIC consumption.In prior art, the part by weight of TGIC and vibrin is 7:93, and uses high temperature resistance polyester resin of the present invention, and the part by weight of TGIC and vibrin is 6/94, even lower.Simultaneously obtained vibrin resisting high-temperature yellowing.
Further, by adjusting the rational proportion of each raw material further, the high temperature resistance polyester resin surface obtained is smooth, and aberration is only 0.52 (270*1h).
Further, use polynary hindered phenol type antioxidant 1098 with phosphite ester kind antioxidant 890 compound as oxidation inhibitor, aberration is less than 1 (300*1h), and under preferable case, polynary hindered phenol type antioxidant 1098 is 1:1 with the mass ratio of phosphite ester kind antioxidant 890, and aberration is only 0.54 (300*1h).
Embodiment
Below in conjunction with specific embodiment, the present invention will be further described.
Embodiment 1:
Take raw material by following mass fraction, prepare high temperature resistance polyester resin
Neopentyl glycol 20 parts, TriMethylolPropane(TMP) 6 parts, terephthalic acid 30 parts, m-phthalic acid 30 parts, hexanodioic acid 4.5 parts.
Synthesis reactor temperature is risen to 90-100 DEG C, add neopentyl glycol, TriMethylolPropane(TMP), terephthalic acid, hexanodioic acid, m-phthalic acid, Mono-n-butyltin, heat up 248-250 DEG C of maintenance under the protection of reaction nitrogen, until the acid number of thing is 5-10mgKOH/g, be cooled to 210-220 DEG C, drop into end-capping reagent m-phthalic acid or (with) hexanodioic acid, be warming up to 242-245 DEG C of maintenance, until reactant acid number is 46-49mgKOH/g, carry out vacuum operating, until reactant acid number is 28-32mgKOH/g, be cooled to 205-210 DEG C, drop into curing catalyst quaternary ammonium salt and antioxidant, maintain and get final product discharging in 15-30 minute.
Embodiment 2:
Take raw material by following mass fraction, prepare high temperature resistance polyester resin
Neopentyl glycol 25 parts, TriMethylolPropane(TMP) 6 parts, terephthalic acid 40 parts, m-phthalic acid 30 parts, hexanodioic acid 4 parts.
Synthesis reactor temperature is risen to 90-100 DEG C, add neopentyl glycol, TriMethylolPropane(TMP), terephthalic acid, hexanodioic acid, m-phthalic acid, Mono-n-butyltin, heat up 248-250 DEG C of maintenance under the protection of reaction nitrogen, until the acid number of thing is 5-10mgKOH/g, be cooled to 210-220 DEG C, drop into end-capping reagent m-phthalic acid or (with) hexanodioic acid, be warming up to 242-245 DEG C of maintenance, until reactant acid number is 46-49mgKOH/g, carry out vacuum operating, until reactant acid number is 28-32mgKOH/g, be cooled to 205-210 DEG C, drop into curing catalyst quaternary ammonium salt and antioxidant, maintain and get final product discharging in 15-30 minute.
Embodiment 3:
Take raw material by following mass fraction, prepare high temperature resistance polyester resin
Neopentyl glycol 30 parts, TriMethylolPropane(TMP) 6 parts, terephthalic acid 60 parts, m-phthalic acid 10 parts, hexanodioic acid 6 parts.
Synthesis reactor temperature is risen to 90-100 DEG C, add neopentyl glycol, TriMethylolPropane(TMP), terephthalic acid, hexanodioic acid, m-phthalic acid, Mono-n-butyltin, heat up 248-250 DEG C of maintenance under the protection of reaction nitrogen, until the acid number of thing is 5-10mgKOH/g, be cooled to 210-220 DEG C, drop into end-capping reagent m-phthalic acid or (with) hexanodioic acid, be warming up to 242-245 DEG C of maintenance, until reactant acid number is 46-49mgKOH/g, carry out vacuum operating, until reactant acid number is 28-32mgKOH/g, be cooled to 205-210 DEG C, drop into curing catalyst quaternary ammonium salt and antioxidant, maintain and get final product discharging in 15-30 minute.
Embodiment 4:
Take raw material by following mass fraction, prepare high temperature resistance polyester resin
Neopentyl glycol 35 parts, TriMethylolPropane(TMP) 6 parts, terephthalic acid 50 parts, m-phthalic acid 20 parts, hexanodioic acid 5 parts.
Synthesis reactor temperature is risen to 90-100 DEG C, add neopentyl glycol, TriMethylolPropane(TMP), terephthalic acid, hexanodioic acid, m-phthalic acid, Mono-n-butyltin, heat up 248-250 DEG C of maintenance under the protection of reaction nitrogen, until the acid number of thing is 5-10mgKOH/g, be cooled to 210-220 DEG C, drop into end-capping reagent m-phthalic acid or (with) hexanodioic acid, be warming up to 242-245 DEG C of maintenance, until reactant acid number is 46-49mgKOH/g, carry out vacuum operating, until reactant acid number is 28-32mgKOH/g, be cooled to 205-210 DEG C, drop into curing catalyst quaternary ammonium salt and antioxidant, maintain and get final product discharging in 15-30 minute.
Embodiment 5:
Take raw material by following mass fraction, prepare high temperature resistance polyester resin
Neopentyl glycol 40 parts, TriMethylolPropane(TMP) 6 parts, terephthalic acid 60 parts, m-phthalic acid 10 parts, hexanodioic acid 6 parts.
Synthesis reactor temperature is risen to 90-100 DEG C, add neopentyl glycol, TriMethylolPropane(TMP), terephthalic acid, hexanodioic acid, m-phthalic acid, Mono-n-butyltin, heat up 248-250 DEG C of maintenance under the protection of reaction nitrogen, until the acid number of thing is 5-10mgKOH/g, be cooled to 210-220 DEG C, drop into end-capping reagent m-phthalic acid or (with) hexanodioic acid, be warming up to 242-245 DEG C of maintenance, until reactant acid number is 46-49mgKOH/g, carry out vacuum operating, until reactant acid number is 28-32mgKOH/g, be cooled to 205-210 DEG C, drop into curing catalyst quaternary ammonium salt and antioxidant, maintain and get final product discharging in 15-30 minute.
Embodiment 6-9 is as shown in the table:
The proportioning table of table 1 embodiment 6-9
Sample number into spectrum |
Neopentyl glycol |
TriMethylolPropane(TMP) |
Terephthalic acid |
M-phthalic acid |
Hexanodioic acid |
6 |
40 |
2 |
55 |
10 |
5 |
7 |
35 |
4 |
55 |
10 |
5 |
8 |
30 |
6 |
55 |
10 |
5 |
9 |
25 |
8 |
55 |
10 |
5 |
Vibrin its significant parameter obtained by upper table 1 is specific as follows:
The parameter of the vibrin that table 2 embodiment 6-9 obtains
As above shown in table 2, the vibrin that embodiment 8 is obtained, meets smooth surface, and acid value and viscosity and shock resistance requirement, aberration is minimum simultaneously, is preferred embodiment.
Below based on the proportioning of embodiment 8, add antioxidant.Antioxidant selects polynary hindered phenol type antioxidant and phosphite ester kind antioxidant to share, and wherein polynary hindered phenol type antioxidant selects 1010,1076,1098; Phosphite ester kind antioxidant selects 890,168.
In following table, the amount of antioxidant is the ratio of two kinds of antioxidants.
The different ratios of the different antioxidant of table 3 is with the use of the impact on obtained vibrin aberration
As can be seen from upper table 3, select polynary hindered phenol type antioxidant to select 1098 to select 890 to share with phosphite ester kind antioxidant, and when the mass ratio of 1098:890 is 1:1, aberration is minimum.
Although the present invention with preferred embodiment openly as above; but it is not for limiting the present invention; any those skilled in the art without departing from the spirit and scope of the present invention; the Method and Technology content of above-mentioned announcement can be utilized to make possible variation and amendment to technical solution of the present invention; therefore; every content not departing from technical solution of the present invention; the any simple modification done above embodiment according to technical spirit of the present invention, equivalent variations and modification, all belong to the protection domain of technical solution of the present invention.