Summary of the invention
The present invention is just in order to overcome above-mentioned deficiency, a kind of water-washing resistant moisture-permeable water-proof polyurethane resin is provided, fabric is after the several times washing, still possess good moisture-permeability waterproof heat-insulating property, the water-wash resistance of fabric, high water pressure resistance, surperficial scratch resistance and pleasant softness etc. all are improved.Specifically, water-washing resistant moisture-permeable water-proof polyurethane resin is characterized in that hydrophilic parts and lipophilicity partly coexist, molecular-weight average is 10000-200000g/mol, resin viscosity is 20000-100000cps/25 ℃, and the solid content of resin is 20-60%, and its structural formula is:
In the formula, R is the part except that the NCO base in the diisocyanate compound, R
1Be the part except the OH base in the polyalcohols compound, R
2Be the part except the OH base in the glycols chainextender, R
3Be that the part except the OH base in the compound of OH base is arranged on one side, m and k are the integers more than 1.
The manufacture method of this water-washing resistant moisture-permeable water-proof polyurethane resin is, polyalcohols compound, glycols chainextender joined in the reactor drop into diisocyanate compound whole or over half after fully stirring, react 1-3 hour (reference reaction formula 1) down in 70-90 ℃, the total OH and the NCO equivalence ratio of diisocyanates are 1: 1 in polyalcohols compound, the glycols chainextender, and the OH base equivalence ratio of polyalcohols compound and glycols chainextender is 1: 1-10; Keep 70-90 ℃, diisocyanate compound (reference reaction formula 2) the adjusting resin viscosity that drops into organic solvent, remainder in batches reaches 40000-700000cps, when solid content is 25-65%, drops into terminator (reference reaction formula 3); Drop into organic solvent and regulate resin viscosity to 20000-100000cps/25 ℃, solid content is 20-60%.
In this manufacture method, diisocyanate compound is a 2,4 toluene diisocyanate, 2, the 6-tolylene diisocyanate, isophorone diisocyanate, hydrogenation hexichol (base) methane cyanate, hexamethylene diisocyanate, dimethyl alkane 4, a kind of or combination of 4 '-vulcabond.
The polyalcohols compound can be that molecular weight is 400 ~ 6,000 polyoxyethylene glycol, polyether glycol, polytetramethylene glycol, polyester polybinary alcohol, with polyoxyethylene glycol or and the multipolymer of polypropylene glycol, a kind of or combination of polycarbonate diol.
The glycols chainextender is an ethylene glycol, glycol ether, propylene glycol, 1,4-butyleneglycol, 3-methyl isophthalic acid, 5-pentanediol, neopentyl glycol, 1,6-hexylene glycol, isophorone diamine, a kind of or combination of TriMethylolPropane(TMP).
There is the compound of OH base can be as one side of terminator at methyl alcohol, butanols, isopropylcarbinol, 2-Ethylhexyl Alcohol, butyl glycol ether, butyl carbitol, propylene glycol monomethyl ether is selected between the propylene-glycol ethyl ether to use.
The organic solvent that uses during resin is synthetic is generally to be butanone, dimethyl formamide, toluene, vinyl acetic monomer, acetone, Virahol.
Reaction formula 1:
(in the formula, R is the part except the NCO base in the diisocyanate compound, R
1Part in the polyalcohols compound except the OH base, R
2Part in the glycols chainextender except the OH base, m and k are the integers more than 1)
Reaction formula 2:
(in the formula, R is the part except the NCO base in the diisocyanate compound, R
1Be the part except the OH base in the polyalcohols compound, R
2Be the part except the OH base in the glycols chainextender, m and k are the integers more than 1).
Reaction formula 3:
(in the formula, R is the part except the NCO base in the diisocyanate compound, R
1Be the part except the OH base in the polyalcohols compound, R
2Be glycol part except the OH base in chainextender, R
3Be that the part except the OH base in the compound of OH base is arranged on one side, m and k are the integers more than 1).
In order to shorten the reaction times, also can add the organic silver catalyzer in of the present invention, under the situation that does not influence reaction, the catalyzer usage quantity is few more good more, if input amount is many, untapped catalyzer can reduce its hydrolytic resistance in the reaction in resin, so the add-on of catalyzer is no more than 0.1% of polyalcohols compound weight.Because the diisocyanate compound kind is more, participate in the speed faster or slower of reaction, selective reaction faster in manufacture method, when promptly regulating resin viscosity, the reaction back segment adds catalyzer, otherwise, if during the slower diisocyanate compound of selective reaction, drop into catalyzer in the reaction leading portion.
In the end also can add auxiliary agent (as add tranquilizer, silicone oil, matting agent, acidifying prevents agent, modification agent etc.) in the manufacture method of the present invention and obtain finished product.
The molecular-weight average of urethane (PU) resin that obtains by this manufacture method is 10000-200000g/mol, and resin viscosity is 20000-100000cps/25 ℃, and the solid content of resin is 20-60%, its water-wash resistance is strong, high water pressure resistance, and feel is soft, the surface scratch resistance, reference table one.
Table one
*Annotate:
Water Vapour Permeability survey method: ASTM E96; 2000 (73.4 (23 ℃ of) ﹠amp of Procedure BW-Inverted Water Method at; 50 ± 2%RH.
Water pressure resistance survey method: AATCC 127-2003;-Hydrostatic Head; Rate of increase of water pressure; 60cm/min, temp of distilled water; 20 degree C).
Washing condition: AATCC 135-2004; Test No. (1) IIIB; Machine wash at 105 degree F with 4Ibloading, normal cycle, line dry).
Embodiment
Embodiment 1, by weight:
Drop into 75 parts of polyester polybinary alcohol (molecular-weight average 4000) in the reactor, 125 parts of polyoxyethylene glycol (molecular-weight average 2450), 50 parts of polytetramethylene glycol (molecular-weight average 2000), 4.9 part neopentyl glycol, stir thorough mixing, drop into 12.4 parts of tolylene diisocyanates again, reactor temperature maintains between 70-90 ℃ and reflected 1-3 hour; Keep temperature of reaction, drop into 104.58 parts of toluene in batches, 146.4 part dimethyl formamide, 17.8 part dimethyl alkane 4,4 '-vulcabond reaches 40000-70000cps to the viscosity of resin, solid content reaches after 45% the benchmark, add 0.8 part of terminator methyl alcohol, 97.63 parts of dimethyl formamides, termination reaction.
* it is as shown in the table that it makes prescription;
Material name |
Input amount |
(molecular-weight average: 4000) (molecular-weight average: 2450) (molecular-weight average: 2000) neopentyl glycol tolylene diisocyanate dimethyl alkane 4,4 '-vulcabond dimethyl formamide methylbenzene methanol for polytetramethylene glycol for polyoxyethylene glycol for polyester polybinary alcohol |
75.00 125.00 50.00 4.90 12.40 17.80 244.03 104.58 0.80 |
Add up to |
634.51 |
Embodiment 2,
Drop into 50 parts of polyester polybinary alcohol (molecular-weight average: 4000) in the reactor, 125 parts of polyoxyethylene glycol (molecular-weight average: 4000), 75 parts of polytetramethylene glycol (molecular-weight average: 2000), 4.9 part neopentyl glycol, fully mix the back and drop into 14.3 parts of isophorone diisocyanates, reactor temperature maintains 70-90 ℃, reacts 1-3 hour; Keep temperature of reaction, drop into 69.2 parts of toluene in batches, 42.3 part dimethyl formamide, 16.0 part dimethyl alkane 4,4 '-vulcabond stirs, and is 40000-70000cps to the viscosity of resin, and solid content reaches 65%, add 0.3 part of terminator 2-Ethylhexyl Alcohol, 42.3 parts of dimethyl formamide termination reactions.
* it is as shown in the table that it makes prescription;
Material name |
Input amount |
(molecular-weight average: 4000) (molecular-weight average: 4000) (molecular-weight average: 2000) neopentyl glycol isophorone diisocyanate dimethyl alkane 4,4 '-vulcabond dimethyl formamide toluene 2-Ethylhexyl Alcohol for polytetramethylene glycol for polyoxyethylene glycol for polyester polybinary alcohol |
50.00 125.00 75.00 4.90 14.30 16.0 84.60 69.2 0.3 |
Add up to |
439.3 |
Embodiment 3,
Drop into 20 parts of polyester polybinary alcohol (molecular-weight average: 4000) in the reactor, 60 parts of polyoxyethylene glycol (molecular-weight average: 4000), 20 parts of polytetramethylene glycol (molecular-weight average: 2000), 8.4 parts of neopentyl glycol, 11.7 part throwing ethylene glycol heats up, and fully mixes.Drop into 75 parts of dimethyl alkane 4 again, temperature maintains 70-90 ℃ of reaction 1-3 hour in the 4 '-vulcabond, reactor; Keep temperature of reaction, add 0.05 part of organic silver catalyzer, drop into 58.5 parts of toluene in batches, 182.25 parts of dimethyl formamides, 176.4 part butanone, to resin viscosity is 40000-70000cps, and solid content reaches 25%, adds 0.3 part of terminator propylene-glycol ethyl ether, 58.5 part toluene, 182.25 part dimethyl formamide, 15.7 parts of auxiliary agents, termination reaction.
* it is as shown in the table that it makes prescription;
Material name |
Input amount |
Polyester polybinary alcohol (molecular weight: 4000) polyoxyethylene glycol (molecular weight: 4000) polytetramethylene glycol (molecular weight: 2000) neopentyl glycol ethylene glycol dimethyl alkane 4,4 '-vulcabond dimethyl formamide toluene butanone auxiliary agent organic silver catalyzer propylene-glycol ethyl ether |
20.00 60.00 20.00 8.40 11.70 75.0 364.50 117.60 176.40 15.70 0.05 0.30 |
Add up to |
846.6 |