Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of water-based co-polypropylene yogurt liquid, uses the present invention to prepare Pressuresensitive Tape and has that rate of drying is fast, resistance to low temperature good, the characteristics of difficult drop-off.
For solving the problems of the technologies described above, a kind of water-based co-polypropylene of the present invention yogurt liquid, by butyl acrylate, emulsifying agent, defoamer, wetting agent, tertbutyl peroxide, rongalite, mercaptan, ammonium persulphate, bicarbonate of ammonia, Hydroxyethyl acrylate, vinylformic acid, ammoniacal liquor and deionized water form, each ingredients weight parts is respectively: butyl acrylate: 525 parts, emulsifying agent: 3.8 parts, defoamer: 0.3-0.4 part, wetting agent: 1.0-1.2 part, tertbutyl peroxide: 0.9 part, rongalite: 0.9 part, mercaptan: 0.15 part, ammonium persulphate: 2.5 parts, bicarbonate of ammonia: 0.7 part, Hydroxyethyl acrylate: 11.1 parts, vinylformic acid: 5.5 parts, ammoniacal liquor: 6 parts and deionized water: 448 parts.
Described emulsifying agent is emulsifying agent A-501 and Emulsifier O C-46, and weight part is respectively 0.3 part and 3.5 parts.
The weight part of described wetting agent is that 1.0 parts, the weight part of defoamer are 0.3 part.
The weight part of described wetting agent is that 1.2 parts, the weight part of defoamer are 0.4 part.
A kind of method for preparing the described water-based co-polypropylene of claim 1 yogurt liquid comprises the following steps:
(1), to the deionized water that adds 200 weight parts in reactor, start to stir, heat temperature raising, mixing speed is 40-50rpm, is warming up to the bicarbonate of ammonia that adds 0.7 weight part after 60 ℃ and the emulsifying agent of 0.3 weight part;
(2), to the deionized water that adds 198 weight parts in the monomer tank, start to stir, add successively the emulsifying agent of 3.5 weight parts, the Hydroxyethyl acrylate of 11.1 weight parts, the vinylformic acid of 5.5 weight parts, the butyl acrylate of 525 weight parts, the mercaptan of 0.15 weight part, be stirred to after above-mentioned mixing liquid viscosity is greater than 200cp and stop stirring, get above-mentioned mixed solution 30 weight parts standby, again to the ammonium persulphate that adds 0.7 weight part in the monomer tank, obtain monomer mixed solution afterwards;
(3), the reactor in step (1) is warming up to 70 ℃ of left and right, the 30 weight part mixed solutions that take out in step (2) are joined in reactor, temperature rises to the ammonium persulphate that 82 ℃ of left and right add 1.8 weight parts after stable;
(4), after being continued to be warming up to 85 ℃, the reactor in step (3) starts to drip prepared monomer mixed solution in step (2), in controlling 1 hour, temperature of reaction kettle is down to 83 ± 1 ℃ by 85 ℃, continue to drip prepared monomer mixed solution in step (2), 3.5 be added dropwise to complete in hour, dropping temperature is controlled at 83 ± 1 ℃, drip and finish rear insulation 1 hour, 83 ± 1 ℃ of holding temperatures;
(5), in step (4), the reactor insulation is cooled to 65 ℃ after finishing, add the deionized water of 10 weight parts and the tertbutyl peroxide of 0.9 weight part, add the deionized water of 10 weight parts and the rongalite of 0.9 weight part after static 10 minutes, continue cooling after static 30 minutes;
(6), the reactor in step (5) adds the wetting agent of 1.0-1.2 weight part while being cooled to 50 ℃, add the chlorine water of 6 weight parts and the defoamer of 0.3-0.4 weight part after being cooled to below 45 ℃, be cooled to below 38 ℃ after 100 order net filtrations packings.
After testing, technical indicator is as follows for water-based co-polypropylene yogurt liquid of the present invention:
Color: milky white liquid
PH value: 7-9
Solid content (%): 55 ± 1%
Viscosity: 60-200cp
180 degree peeling forces (N): >=6.0
Initial bonding strength 13# ball (cm) :≤5.0
0 degree is held viscous force (h/25mmKg) >=24
The present invention has following performance: odorless, nontoxic, high solid fast containing, rate of drying, have and good just glue, peel off and hold viscous force.
Embodiment
Below in conjunction with embodiment, the present invention is described in further detail.
Embodiment:
At first to the deionized water that adds 200 weight parts in reactor, start to stir, heat temperature raising, mixing speed is 40-50rpm, is warming up to the bicarbonate of ammonia that adds 0.7 weight part after 60 ℃ and the emulsifying agent of 0.3 weight part; Then to the deionized water that adds 198 weight parts in the monomer tank, start to stir, add successively the emulsifying agent of 3.5 weight parts, the Hydroxyethyl acrylate of 11.1 weight parts, the vinylformic acid of 5.5 weight parts, the butyl acrylate of 525 weight parts, the mercaptan of 0.15 weight part, be stirred to after above-mentioned mixing liquid viscosity is greater than 200cp and stop stirring, get above-mentioned mixed solution 30 weight parts standby, again to the ammonium persulphate that adds 0.7 weight part in the monomer tank, obtain monomer mixed solution afterwards; Reactor is warming up to 70 ℃ of left and right, the 30 weight part mixed solutions that take out are joined in reactor, temperature rises to after stablize 82 ℃ of left and right the ammonium persulphate that adds 1.8 weight parts; Start to drip monomer mixed solution after again reactor being continued to be warming up to 85 ℃, in controlling 1 hour, temperature of reaction kettle is down to 83 ± 1 ℃ by 85 ℃, continue to drip monomer mixed solution, 3.5 be added dropwise to complete in hour, dropping temperature is controlled at 83 ± 1 ℃, drip and finish rear insulation 1 hour, 83 ± 1 ℃ of holding temperatures; Be cooled to 65 ℃ after question response still insulation afterwards finishes, add the deionized water of 10 weight parts and the tertbutyl peroxide of 0.9 weight part, add the deionized water of 10 weight parts and the rongalite of 0.9 weight part after static 10 minutes, continue cooling after static 30 minutes; Last question response still adds the wetting agent of 1.0-1.2 weight part while being cooled to 50 ℃, add the chlorine water of 6 weight parts and the defoamer of 0.3-0.4 weight part after being cooled to below 45 ℃, be cooled to below 38 ℃ after 100 order net filtrations packings.