A kind of preparation method of polyurethane stock solution for automobile steering wheel
Technical field
The present invention relates to the synthetic field of chemical industry, be specifically related to polyurethane stock solution, refer to especially new polyurethane material of a kind of polyurethane stock solution for automobile steering wheel and preparation method thereof.
Background technology
Along with the development of automobile industry, automobile has entered the ordinary people family.The city resident can drive to go to work, travel or finish some public affair at present.The officer who drives holds bearing circle, can be to the place that you think.According to incompletely statistics, have the driver of car to drive at least two hours average every day, hand will contact bearing circle two hours.Driving if hold a strong bearing circle of comfortableness, is a kind of enjoyment.The comfortableness of bearing circle thoughts also is a standard of automobile class simultaneously.Comfortableness when bearing circle is held in raising so people also try every possible means, thus various types of vehicle steering comes out with sheath.Fabric protecting casing of steering wheel, leather sheath, synthetic leather sheath that various materials are arranged in the market.The sheath higher gears of leather wherein.The sheath of synthetic leather is owing to airtight, so that the comfortableness of sheath is relatively poor.So the steering wheel protector for car of the synthetic leather that the exploitation comfortableness is strong becomes the very interested problem of urethane resin production.
In fact since the sixties in last century, the flexible PU foam sheath has been housed all on nearly all vehicle steering.But this sheath is general flexible PU foam, and is airtight and have a high resilience, namely constantly gives pressure of hand, so hand is felt very ill.Occur a kind of slow rebound polyurethane stoste on the markets in 2008, be applied on the steering wheel protector for car, the quality of steering wheel protector for car is obviously improved.But we find that this sheath has the surface of polarity, very easily adsorb dust and be difficult to clean.When every day hand all contact sheath, have sweat stain on the sheath, more breed bacteria.Have automatic cleaning action the slow rebound polyurethane stoste that can be used for steering wheel protector for car have no report.
Summary of the invention
The objective of the invention is the shortcoming and defect that exists in order to overcome prior art, and provide have germicidal action, the preparation method of a kind of polyurethane stock solution for automobile steering wheel of the self-cleaning function such as decomposing protein.
For achieving the above object, technical scheme of the present invention is to comprise following operation:
(1) silicon oil modified polyester polyol preparation:
Butyleneglycol 100 parts, hydroxy silicon oil is added in the reactor, behind the 75-85 ℃ of vacuum hydro-extraction 2-2.5h, the adipic acid that adds 50 parts, be warming up to 150-180 ℃, temperature remains unchanged, water constantly is excluded from reactive system, until after not having water to get rid of from system, the temperature of reactive system continues to raise, temperature rises to 230-250 ℃, insulation 1-2h, whole operating under the protective atmosphere carried out, and carries out vacuum pumping, keeps vacuumizing state and getting its sample and analyze, determine hydroxyl value and acid number, if the acid number of sample does not reach 0.3-0.5mgKOH/g, hydroxyl value does not reach 60-70 mgKOH/g, continues to vacuumize, until hydroxyl value and acid number reach above-mentioned requirements, temperature in the kettle remains on 220~230 ℃ during vacuumizing;
(2) preparation of polyurethane stock solution for automobile steering wheel:
Put A material and B material by following set of dispense, the acquisition polyurethane stock solution for automobile steering wheel, in mass fraction:
The A material:
Silicon oil modified polyester polyol 30-60
Slow resilience polyethers 20-30
Suds-stabilizing agent 0.4-1.5
Amino catalyzer 2.0-4.5
Tin-based catalyst 0.5-1.2
Nano TiO 2 4-8
Water 0.5-2.5
The B material:
Liquefied mdi 70-80
PAPI 30-40。
Further arrange is that the control condition that described step (1) vacuumizes is carried out vacuum pumping for opening vacuum pump with the condition of 0.02MPa 1h, 0.04MPa 1.5h, 0.06MPa 1.5h, 0.08 MPa 1.5h, 0.099 Mpa 4h successively.
Further arranging is that described protective atmosphere is nitrogen atmosphere.
Advantage of the present invention is
(a
)The present invention improves a kind of hydroxyl silicon oil modified polyester polyol
Hydroxyl silicon oil modified polyester polyol provided by the invention is a kind ofly by chemical reaction method siloxane bond to be added in the molecule of polyester polyol, makes polyester polyol have certain hydrophobicity.When using this polyester polyol to be prepared into the soft bubble plastics of polyurethane slow rebound, the polarity of flexible PU foam is less, does not touch with one's hand, and feel is smooth.
(b) the present invention is by chemical additive process, with nano-TiO
2Add in the flexible PU foam.
Nano-TiO
2Be a kind of inorganic oxide, can strengthen the mechanical property of polyurethane material, simultaneously nano-TiO
2Has germicidal action.The what is more important nano-TiO
2A kind of optical catalysts, under the irradiation of UV-light, can decomposing protein etc. biomass, so can automatically remove microorganism on the polyurethane foam.
(c) the invention provides the preparation method that a kind of preparation steering wheel protector for car is used polyurethane stock solution.
Below in conjunction with embodiment the present invention is done further introduction.
Embodiment
Below by embodiment the present invention is carried out concrete description; only be used for the present invention is further specified; can not be interpreted as the restriction to protection domain of the present invention, the technician in this field can make some nonessential improvement and adjustment to the present invention according to the content of foregoing invention.
Embodiment 1
At 0.5m
3Reactor in add the butyleneglycol of 50kg, 10kg hydroxy silicon oil, sealed reactor.Add thermal material to 80 ℃, begin to vacuumize to system, vacuum tightness 0.01MPa stops behind the 2h vacuumizing.Open reactor, add the 300kg adipic acid.Pass into nitrogen protection to reactor, and heat up, temperature rises to 110 ℃ has the water of a little to get rid of reactor, and temperature continues to rise, until 150 ℃, temperature remains unchanged, until the water of reactive system is got rid of fully.Temperature continues to heat up, and keeps temperature of reaction under 220 ℃, and 4h is carried out in reaction, and the acid number of assaying reaction sample is when acid number reaches 20 mgKOH/g.Beginning progressively vacuumizes, 0.02MPa 1h, 0.04MPa 1.5h, 0.06MPa 1.5h, 0.08 MPa 1.5h, then begin pumping high vacuum (0.099 Mpa, 4h), get its sample and analyze, determine hydroxyl value and acid number, if the hydroxyl value of sample and acid number do not reach requirement, continue to vacuumize, until hydroxyl value and acid number reach requirement (acid number 0.3-0.5mgKOH/g, hydroxyl value reaches 60-70 mgKOH/g).Temperature in the kettle remains on 230 ℃ during this period.Can not stop vacuum pump during sampling analysis during noting vacuumizing, change to prevent product quality.Reach the hydroxyl value and acid number of needs until sample after, discharging namely obtains silicon oil modified polyester polyol.
Get the silicon oil modified polyester polyol 30kg of above-mentioned preparation, slow resilience polyethers 20kg, suds-stabilizing agent 0.4 kg, amino catalyzer 2.0 kg, tin-based catalyst 0.5 kg, nano-TiO
24 kg, water 0.5 kg form the A material; Liquefied mdi 70kg, PAPI 30kg form the B material.
MDI of the present invention is diphenylmethanediisocyanate, and PAPI is polymethylene multi-phenenyl isocyanate, by those skilled in the art are known.
Embodiment 2
At 0.5m
3Reactor in add the butyleneglycol of 50kg, 10kg hydroxy silicon oil, sealed reactor.Add thermal material to 100 ℃, begin to vacuumize to system, vacuum tightness 0.01MPa stops behind the 2h vacuumizing.Open reactor, add the 300kg adipic acid.Pass into nitrogen protection to reactor, and heat up, temperature rises to 110 ℃ has the water of a little to get rid of reactor, and temperature continues to rise, until 160 ℃, temperature remains unchanged, until the water of reactive system is got rid of fully.Temperature continues to heat up, and keeps temperature of reaction under 230 ℃, and 4h is carried out in reaction, and the acid number of assaying reaction sample is when acid number reaches 30 mgKOH/g.Beginning progressively vacuumizes, 0.02MPa 1h, 0.04MPa 1.5h, 0.06MPa 1.5h, 0.08 MPa 1.5h, then begin pumping high vacuum (0.099 Mpa, 4h), get its sample and analyze, determine hydroxyl value and acid number, if the hydroxyl value of sample and acid number do not reach requirement, continue to vacuumize, until hydroxyl value and acid number reach requirement (acid number 0.3-0.5mgKOH/g, hydroxyl value reaches 60-70 mgKOH/g).Temperature in the kettle remains on 220~230 ℃ during this period.Can not stop vacuum pump during sampling analysis during noting vacuumizing, change to prevent product quality.Reach the hydroxyl value and acid number of needs until sample after, discharging namely obtains silicon oil modified polyester polyol.
Embodiment 3
At 0.5m
3Reactor in add the butyleneglycol of 50kg, 10kg hydroxy silicon oil, sealed reactor.Add thermal material to 90 ℃, begin to vacuumize to system, vacuum tightness 0.01MPa stops behind the 2h vacuumizing.Open reactor, add the 300kg adipic acid.Pass into nitrogen protection to reactor, and heat up, temperature rises to 110 ℃ has the water of a little to get rid of reactor, and temperature continues to rise, until 155 ℃, temperature remains unchanged, until the water of reactive system is got rid of fully.Temperature continues to heat up, and keeps temperature of reaction under 225 ℃, and 4h is carried out in reaction, and the acid number of assaying reaction sample is when acid number reaches 25 mgKOH/g.Beginning progressively vacuumizes, 0.02MPa 1h, 0.04MPa 1.5h, 0.06MPa 1.5h, 0.08 MPa 1.5h, then begin pumping high vacuum (0.099 Mpa, 4h), get its sample and analyze, determine hydroxyl value and acid number, if the hydroxyl value of sample and acid number do not reach requirement, continue to vacuumize, until hydroxyl value and acid number reach requirement (acid number 0.3-0.5mgKOH/g, hydroxyl value reaches 60-70 mgKOH/g).Temperature in the kettle remains on 230 ℃ during this period.Can not stop vacuum pump during sampling analysis during noting vacuumizing, change to prevent product quality.Reach the hydroxyl value and acid number of needs until sample after, discharging namely obtains silicon oil modified polyester polyol.
With polyurethane stock solution for automobile steering wheel of the present invention for the manufacture of automobile steering wheel cover, first the component weighing in each component in the A material and the B material is dropped into batch mixing reactor separately, start stirring, after two batching kettles stir 0.5h respectively, A material and B material are heated to respectively 45 ℃, A is expected, the B material is poured into rapidly in the mould that has been heated to required temperature, build and cover tightly mould lid, cross 10~15min, open mould lid, take out sample, put into temperature and be 65 ℃ baking oven, go out about 5 minutes, cooling off its density of mensuration of carrying out density in about 5 minutes is 35kg/m
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