JPH0114922B2 - - Google Patents
Info
- Publication number
- JPH0114922B2 JPH0114922B2 JP15547481A JP15547481A JPH0114922B2 JP H0114922 B2 JPH0114922 B2 JP H0114922B2 JP 15547481 A JP15547481 A JP 15547481A JP 15547481 A JP15547481 A JP 15547481A JP H0114922 B2 JPH0114922 B2 JP H0114922B2
- Authority
- JP
- Japan
- Prior art keywords
- polyvinyl butyral
- temperature
- manufacturing
- weight
- acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 229920002037 poly(vinyl butyral) polymer Polymers 0.000 claims description 76
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 24
- 238000006243 chemical reaction Methods 0.000 claims description 19
- 150000003839 salts Chemical class 0.000 claims description 15
- 239000006185 dispersion Substances 0.000 claims description 14
- 239000008346 aqueous phase Substances 0.000 claims description 13
- 238000004519 manufacturing process Methods 0.000 claims description 13
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 11
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 11
- 230000002378 acidificating effect Effects 0.000 claims description 10
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 7
- 229910017604 nitric acid Inorganic materials 0.000 claims description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- BMYNFMYTOJXKLE-UHFFFAOYSA-N 3-azaniumyl-2-hydroxypropanoate Chemical compound NCC(O)C(O)=O BMYNFMYTOJXKLE-UHFFFAOYSA-N 0.000 claims description 5
- 238000006359 acetalization reaction Methods 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 2
- 229910052791 calcium Inorganic materials 0.000 claims description 2
- 239000011575 calcium Substances 0.000 claims description 2
- 229910052749 magnesium Inorganic materials 0.000 claims description 2
- 239000011777 magnesium Substances 0.000 claims description 2
- 239000010936 titanium Substances 0.000 claims description 2
- 229910052719 titanium Inorganic materials 0.000 claims description 2
- 229910052725 zinc Inorganic materials 0.000 claims description 2
- 239000011701 zinc Substances 0.000 claims description 2
- 239000011229 interlayer Substances 0.000 description 23
- 239000005340 laminated glass Substances 0.000 description 18
- 239000004014 plasticizer Substances 0.000 description 18
- 238000000034 method Methods 0.000 description 16
- ZTQSAGDEMFDKMZ-UHFFFAOYSA-N Butyraldehyde Chemical compound CCCC=O ZTQSAGDEMFDKMZ-UHFFFAOYSA-N 0.000 description 14
- 239000000843 powder Substances 0.000 description 10
- 230000000704 physical effect Effects 0.000 description 9
- 238000001556 precipitation Methods 0.000 description 8
- 239000011521 glass Substances 0.000 description 7
- HGBOYTHUEUWSSQ-UHFFFAOYSA-N valeric aldehyde Natural products CCCCC=O HGBOYTHUEUWSSQ-UHFFFAOYSA-N 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 229910001622 calcium bromide Inorganic materials 0.000 description 6
- WGEFECGEFUFIQW-UHFFFAOYSA-L calcium dibromide Chemical compound [Ca+2].[Br-].[Br-] WGEFECGEFUFIQW-UHFFFAOYSA-L 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 239000003377 acid catalyst Substances 0.000 description 5
- 239000010419 fine particle Substances 0.000 description 5
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- VNDYJBBGRKZCSX-UHFFFAOYSA-L zinc bromide Chemical compound Br[Zn]Br VNDYJBBGRKZCSX-UHFFFAOYSA-L 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 3
- 230000000181 anti-adherent effect Effects 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000011978 dissolution method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- OTCKOJUMXQWKQG-UHFFFAOYSA-L magnesium bromide Chemical compound [Mg+2].[Br-].[Br-] OTCKOJUMXQWKQG-UHFFFAOYSA-L 0.000 description 2
- 229910001623 magnesium bromide Inorganic materials 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000005070 ripening Effects 0.000 description 2
- 239000000344 soap Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- 229940102001 zinc bromide Drugs 0.000 description 2
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical compound [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 description 2
- JEYLQCXBYFQJRO-UHFFFAOYSA-N 2-[2-[2-(2-ethylbutanoyloxy)ethoxy]ethoxy]ethyl 2-ethylbutanoate Chemical compound CCC(CC)C(=O)OCCOCCOCCOC(=O)C(CC)CC JEYLQCXBYFQJRO-UHFFFAOYSA-N 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- WNLRTRBMVRJNCN-UHFFFAOYSA-L adipate(2-) Chemical compound [O-]C(=O)CCCCC([O-])=O WNLRTRBMVRJNCN-UHFFFAOYSA-L 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000006482 condensation reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000035936 sexual power Effects 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
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The present invention relates to a method for producing polyvinyl butyral, and more specifically, when an interlayer film for laminated glass is produced by adding a plasticizer, the adhesion of the interlayer films to each other at room temperature (hereinafter referred to as self-adhesion of the interlayer film) is greatly improved. The present invention relates to a method for producing polyvinyl butyral that yields a polyvinyl butyral interlayer film for laminated glass. The methods for producing polyvinyl butyral that are widely used industrially today are broadly divided into precipitation methods and dissolution methods. In this internal precipitation method, for example, butyraldehyde is added to an aqueous solution of polyvinyl alcohol in the presence of an acid catalyst, a butyralization reaction is carried out at a relatively low temperature of 20°C or less to produce fine precipitates of polyvinyl butyral, and then the precipitation is further continued. This method involves stirring and heating for a period of time. The dissolution method is, for example, a method in which polyvinyl alcohol is dispersed in an organic solvent such as isopropyl alcohol, and butyraldehyde is added in the presence of an acid catalyst, and the mixture is heated and reacted for a long time. However, interlayer films for laminated glass obtained by adding plasticizers to polyvinyl butyral produced by these conventional methods have strong adhesion on the film surface, so the films tend to stick to each other during winding after film formation. In order to prevent such adhesion, methods include spraying an anti-adhesive agent such as sodium bicarbonate on the surface of the film or cooling the interlayer film to a temperature of 20° C. or lower. However, the method of spraying an anti-adhesive agent has the disadvantage that it requires a washing process and a drying process to remove the anti-adhesive agent before bonding the polyvinyl butyral film and glass. The problem is that a refrigeration device is required for the production, packaging, transportation, storage, and use of the interlayer film, which is expensive, and the emergence of an interlayer film that is substantially free of self-adhesion at room temperature has been awaited. In view of the above-mentioned current state of the method for producing polyvinyl butyral, the present invention provides an interlayer film for laminated glass with greatly improved self-adhesion by adding a plasticizer to the obtained polyvinyl butyral to produce an interlayer film for laminated glass. The purpose is to provide a method for producing polyvinyl butyral obtained by acetalizing polyvinyl alcohol, and the gist thereof is to disperse hydrochloric acid, hydrobromic acid, 30 in the strongly acidic region in the presence of at least one respective water-soluble salt of nitric acid and nitric acid.
The present invention provides a method for producing polyvinyl butyral with improved self-adhesiveness, characterized by maintaining the temperature at a temperature of 0.degree. C. or higher. The polyvinyl butyral used in the present invention may be polyvinyl acetate as a starting material as long as it is obtained by acetalizing polyvinyl alcohol. Widely used. However, since it is dispersed in the aqueous phase, it is preferred to use polyvinyl butyral which is also produced in the aqueous phase.
In this case, it is particularly preferred industrially to react polyvinyl alcohol and butyraldehyde in the presence of an acid catalyst to precipitate polyvinyl butyral in the aqueous phase, without separating the resin from the reaction system. This means post-treatment in the same aqueous phase. However, it is of course possible to use dried polyvinyl butyral powder obtained by conventionally known methods such as the above-mentioned precipitation method or dissolution method. As for the polyvinyl butyral used in the present invention, when polyvinyl butyral obtained by keeping the temperature at 30°C or higher is used as an interlayer film for laminated glass, it is desirable that the degree of butyralization is 60 to 75 mol%. The degree of oxidation is 95 mol% or more, and
It is preferable that the resin be made from polyvinyl alcohol containing 98 mol% or more, since a resin with good transparency can be obtained in the end. In addition, if the average degree of polymerization of polyvinyl alcohol at this time is too low, the effect of improving self-adhesion when forming an interlayer film by adding a plasticizer is poor, and if it is too high, the viscosity is high, which is inconvenient for industrial acetalization. Therefore, it is usually 800~
3000 are used. Preferred examples of water-soluble salts of hydrochloric acid, hydrobromic acid and nitric acid in the present invention include magnesium, calcium, zinc,
Examples include those having a valence of two or more, such as aluminum, iron, and titanium. These salts may be used alone or in appropriate combinations, and the amount used is usually 2 to 100 parts by weight, preferably 5 to 30 parts by weight, per 100 parts by weight of the dispersed polyvinyl butyral. The concentration of the polyvinyl butyral dispersion in the present invention is not particularly limited as long as the resin is dispersed in the aqueous phase, but it is usually 3 to 15% by weight.
At this time, a trace amount of aldehyde may be present in the dispersion, and the amount thereof is usually 1% by weight or less of the dispersion. In order to prevent the polyvinyl butyral particles from becoming coarse, it is preferable to add the water-soluble salt to the polyvinyl butyral dispersion before a too long period of time has elapsed at a high temperature after polyvinyl alcohol is acetalized. In the present invention, in order to obtain a polyvinyl butyral dispersion in a strongly acidic region, conventionally known hydrochloric acid, sulfuric acid,
Dry polyvinyl butyral may be added to a strongly acidic aqueous phase obtained using an inorganic acid such as nitric acid or an organic acid such as para-toluenesulfonic acid, and after dispersing the polyvinyl butyral in the aqueous phase, An acid may be added or the polyvinyl butyral may be precipitated in a strongly acidic aqueous phase. The strongly acidic region in the present invention is usually PH2 or less, preferably PH1 or less, although it depends on the temperature of the polyvinyl butyral dispersion. Furthermore, when it is necessary to increase the degree of butyralization of polyvinyl butyral, the degree of butyralization can be increased by making a predetermined amount of butyraldehyde exist in the dispersion. In addition, the upper limit of the temperature for ripening polyvinyl butyral is not particularly set, but it is generally set at 90°C or lower, and 30°C or lower.
The time for maintaining the temperature at or above .degree. C. is usually 1 to 20 hours, including the time for raising and lowering the temperature of the dispersion. To produce polyvinyl butyral by the method of the present invention, usually an acid catalyst is added to an aqueous polyvinyl alcohol solution at a temperature exceeding 20°C, the reaction system is then cooled, and butyraldehyde is added to cause a condensation reaction to precipitate polyvinyl butyral. Polyvinyl butyral is prepared by precipitating it at a low temperature such as 20°C or lower and dispersing it in an aqueous phase. In this way, the temperature of the reaction system is kept low during precipitation in order to obtain the precipitate in the form of fine particles or powder, and the lower limit of the temperature should be a temperature that does not freeze the reaction system, and there are no particular restrictions. Although it is not something that will be done,
Usually a temperature of -6°C or higher is employed. Next, while the pH of the reaction system is 2 or less, at least one of the above salts is added and the reaction system is heated and kept at a temperature of 30°C or higher to further advance the reaction, and then the catalyst is neutralized with a base. Then, the reaction product is taken out and washed and purified using conventional methods. In this way, polyvinyl butyral obtained by acetalization of polyvinyl alcohol is dispersed in an aqueous phase, and then a strong acid is added to the polyvinyl butyral in the presence of at least one water-soluble salt of hydrochloric acid, hydrobromic acid, and nitric acid. If an interlayer film for laminated glass is manufactured by adding a plasticizer by maintaining the temperature of the dispersion liquid at 30°C or higher in the temperature range, an interlayer film that has virtually no self-adhesion at room temperature can be obtained. The reason why polyvinyl butyral with improved self-adhesiveness is produced is not yet fully clear, but it is speculated as follows. Since the butyralization reaction is an equilibrium reaction, the degree of butyralization becomes approximately constant in an equilibrium state where the reaction has progressed to a certain extent. In conventional production methods, the reaction was generally stopped before the degree of butyralization reached a certain level, and the remaining hydroxyl groups in the polyvinyl butyral at this time are thought to be randomly arranged. However, when this polyvinyl butyral is dispersed in an aqueous phase and the temperature of the dispersion is maintained at 30°C or higher in a strongly acidic region in the presence of the above salt, hydroxyl groups are generated by the reverse butyralization reaction that occurs in a strongly acidic region. tends to exhibit association by hydrogen bonding, while the butyralization reaction is more likely to occur selectively with hydroxyl groups that do not have a strong tendency to associate than with hydroxyl groups that have a strong tendency to associate. Therefore, as the final equilibrium state approaches, the tendency for hydroxyl groups to remain in a chain within the molecule increases, which increases the rigidity of the resulting polyvinyl butyral, which leads to self-adhesion when used as an interlayer film. It is thought that this contributes to the reduction, or improvement, of sexual performance. The present inventors have found that by keeping a dispersion of polyvinyl butyral in a strongly acidic region at a relatively high temperature for a long period of time, and adding a plasticizer to the polyvinyl butyral, even in the absence of the above salt, an interlayer film with improved self-adhesion was obtained. However, when the above-mentioned salt is used in the present invention, the above-mentioned temperature and time conditions are significantly relaxed, which is advantageous in the process. In addition, for example, after fine particles of polyvinyl butyral are precipitated by a precipitation method, if they are kept at high temperature for a long time in the absence of the above salt, coarsening due to agglomeration of the precipitated particles is likely to occur, and some of the coarse particles are The acid catalyst and the base used to neutralize it tended to remain, reducing transparency and thermal stability; however, the above-mentioned salt has the effect of preventing fine particles from becoming coarse, and thus improving transparency. There is almost no reduction in thermal stability. As the plasticizer used for the polyvinyl butyral obtained by the method of the present invention, any of those conventionally used as a plasticizer for polyvinyl butyral can be used, such as triethylene glycol di2-ethyl butyrate, triethylene glycol Examples include general-purpose plasticizers such as di-2-ethylhexoate. Furthermore, dibutoxydiethylene glycol adipate and the like are preferably used. The amount of plasticizer added is preferably 30 to 60 parts by weight per 100 parts by weight of polyvinyl butyral. If the plasticizer content is less than 30 parts by weight, the penetration resistance will decrease when used as an interlayer film for laminated glass, and if the plasticizer content exceeds 60 parts by weight, a so-called bleed phenomenon will occur in which the plasticizer seeps onto the film surface, resulting in poor performance of laminated glass. This is because it has an adverse effect on transparency and adhesion when used as an interlayer film. The method of the present invention is configured as described above, and according to the present invention, when an interlayer film for laminated glass is manufactured by adding a plasticizer, an interlayer film for laminated glass with significantly improved self-adhesion at room temperature can be obtained. The resulting polyvinyl butyral can be obtained under industrially advantageous temperature and time conditions compared to the case where none of the water-soluble salts of hydrochloric acid, hydrobromic acid and nitric acid are used. Furthermore, when fine polyvinyl butyral particles are used in the present invention, it is possible to obtain polyvinyl butyral with good transparency and thermal stability in which almost no coarse particles remain. Examples of the present invention are shown below. % simply means weight %. In addition, each physical property value in Examples was based on the following measuring method. 1 Transparency A sample obtained by sandwiching polyvinyl butyral between two glass plates was placed in a heated oven to melt the polyvinyl butyral, and then allowed to cool at room temperature. The obtained sample was observed under white light, and those without bluishness, turbidity, etc. were evaluated as good. 2. Thermal stability A test tube containing polyvinyl butyral was immersed in a heated oil bath, and the thermal stability was determined to be good if the polyvinyl butyral did not change color even after a predetermined period of time at 120°C. Generally, when neutralization or water washing is incomplete, catalysts such as hydrochloric acid remain in polyvinyl butyral.
When this test is performed, polyvinyl butyral is colored yellow. 3 Self-adhesiveness Add 42 parts by weight of the specified plasticizer to 100 parts by weight of polyvinyl butyral, mix for 15 minutes using a Laikai machine, and knead for 3 minutes at 120°C using a roll.
A uniform film with a smooth surface and a thickness of 0.76 mm was prepared by pressing at 150° C. and 40 kg/cm 2 for 3 minutes.
Cut this film into a rectangular shape of 3cm x 10cm, stack the two pieces together and apply a load of 6kg.
It was left for 48 hours in a desiccator kept at a temperature of 20°C. One end of the sample obtained in this way was peeled off from each other, and the peeled film was bent in a direction of 90°C to form a T-shape, and then both ends of the peeled film were held in a tensile tester and heated to 20°C. The T-peel strength was measured at a tensile speed of 500 mm/min. 4 Impact resistance 100 parts by weight of polyvinyl butyral and 42 parts by weight of plasticizer
Add and knead parts by weight, and use an extruder to measure the thickness.
0.76 mm of plasticized polyvinyl butyral was obtained.
This film was sandwiched between two glass plates of 3.0 mm thickness and 30 cm x 30 cm, and heated and pressed under conventionally known conditions to obtain a laminated glass. After storing this laminated glass at the specified temperature for more than 8 hours, the outer frame
Placed horizontally on a square iron frame with a size of 31cm x 31cm, an inner frame of 26cm x 26cm, and a height of 20cm, weighing 2.268Kg (5 pounds).
A steel ball was dropped from a specified height onto the center of the laminated glass. The height at which 50% of the steel balls penetrate the laminated glass is defined as the penetration resistance. The laminated glass sample used was one in which the Bummel value, which will be described later, was set to 6, which is within the range normally used as a product, by using a plasticizer mixed with an appropriate amount of metal soap. 5. Adhesion to glass The laminated glass was adjusted by leaving it at a temperature of -18°C ± 0.6°C for 16 hours, and was crushed by hitting it with a hammer with a head weighing 0.45 kg until the particle size of the glass became 6 mm or less. After the glass has peeled off, the degree of exposure of the film is determined using pre-graded limit samples.
The results were expressed as Bummel values according to Table 1.
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ãã§ãã€ãã[Table] Example 1 Concentrated hydrochloric acid (concentration 35
%) was added thereto, and 6.7 kg of butyraldehyde was added dropwise over 30 minutes while stirring at 13°C, resulting in the precipitation of white fine particles of polyvinyl butyral. Furthermore, 7 kg of 35% concentrated hydrochloric acid was added and stirred to bring the pH of the reaction system below 0.5, and 15.3 kg of a 16% aqueous solution of calcium bromide was added (the amount of calcium bromide was determined based on 100 parts by weight of the final polyvinyl butyral). (20 parts by weight) at a heating rate of 20°C/hour.
The temperature was raised to 40°C and the temperature was maintained for an additional 6 hours for ripening, and then sodium hydroxide was added to neutralize the reaction system and the pH was adjusted to 9.6. The time that the temperature was maintained at 30°C or higher was 6.8 hours. The obtained resin was washed with water and dried according to a conventional method to obtain a white fine powder. The degree of butyralization of this polyvinyl butyral was 66.4%. Polyvinyl butyral obtained in this way,
Triethylene glycol = di-2-ethyl butyrate 4.2 as a plasticizer to 10 kg of the polyvinyl butyral.
The physical properties of the interlayer film obtained by adding Kg and the laminated glass obtained from the interlayer film were as shown in Table 2. Example 2 Polyvinyl butyral powder was obtained in the same manner as in Example 1 except that ferric chloride was used instead of calcium bromide. Its physical properties were as shown in Table 2. Example 3 In the same manner as in Example 1, fine white particles of polyvinyl butyral were precipitated in the reaction system.
Further, polyvinyl butyral powder was obtained in the same manner as in Example 1, except that magnesium bromide was added instead of calcium bromide, the temperature was raised to 60°C, and the temperature was maintained for 3 hours. Its physical properties were as shown in Table 2. Example 4 Polyvinyl butyral powder was obtained in the same manner as in Example 1 except that zinc nitrate was used instead of calcium bromide. Its physical properties were as shown in Table 2. Example 5 Concentrated hydrochloric acid (concentration 35
%) and 6.7 kg of butyraldehyde was added over a period of 30 minutes while stirring at 13°C, resulting in the precipitation of white fine particles of polyvinyl butyral.
Add 7 kg of concentrated hydrochloric acid and stir the reaction system for 20 minutes.
After increasing the temperature to 40â at a heating rate of â/1 hour and keeping it at that temperature for 3 hours, it was neutralized and washed with water using a conventional method to obtain a butyralization degree of 65.8 mol% and an average particle size of 175ÎŒ.
dry polyvinyl butyral was obtained. 6 kg of 35% hydrochloric acid was added to 8.4 kg of a 12% aqueous solution of zinc bromide to disperse 10 kg of the above dry polyvinyl butyral (PH of the dispersion was 0.5 or less), and the dispersion was heated at 48°C for 5 hours. After the mixture was maintained, sodium hydroxide was added to neutralize it to a pH of 8.6, and the same procedure as in Example 1 was carried out to obtain polyvinyl butyral powder.
Its physical properties were as shown in Table 2. Comparative Example 1 Polyvinyl butyral powder was obtained in the same manner as in Example 1 except that calcium bromide was not added. Its physical properties were as shown in Table 2. Comparative Example 2 Polyvinyl butyral powder was obtained in the same manner as in Example 3 except that magnesium bromide was not added. Its physical properties were as shown in Table 2. Comparative Example 3 A polyvinyl butyral powder in the latter stage was obtained in the same manner as in Example 5 except that zinc bromide was not used. Its physical properties were as shown in the second display.
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[Table] * Glass containing metallic soap in the interlayer film and having a pummel value of 6 was used as a sample.
Claims (1)
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é èšèŒã®è£œé æ¹æ³ã ïŒ æ°Žæº¶æ§å¡©ã®éœæ§æåããã°ãã·ãŠã ãã«ã«ã·
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ã第ïŒé ã第ïŒé äœããïŒé ã«èšèŒã®è£œé æ¹æ³ã ïŒ åŒ·é žæ§é åã®PHãïŒä»¥äžã§ãã第ïŒé ã第ïŒ
é äœããïŒé ã«èšèŒã®è£œé æ¹æ³ã ïŒ ã¢ã»ã¿ãŒã«åã«ããåŸãããããªããã«ãã
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補é æ¹æ³ã[Scope of Claims] 1. Polyvinyl butyral obtained by acetalization of polyvinyl alcohol is dispersed in an aqueous phase in the presence of at least one water-soluble salt of hydrochloric acid, hydrobromic acid, and nitric acid. A method for producing polyvinyl butyral with improved self-adhesion, which comprises maintaining the polyvinyl butyral at a temperature of 30°C or higher in a strongly acidic region. 2 The first type in which the amount of water-soluble salt is 2 parts by weight or more based on 100 parts by weight of polyvinyl butyral in the dispersion.
Manufacturing method described in section. 3. The manufacturing method according to item 1 or 2, wherein the positive component of the water-soluble salt is at least one of magnesium, calcium, zinc, aluminum, iron, and titanium. 4. The manufacturing method according to any one of Items 1 to 3, wherein the time for maintaining the temperature at 35°C or higher is 1 to 20 hours. 5 Items 1 to 4 where the pH in the strongly acidic region is 2 or more
1. The manufacturing method according to any one of the above. 6. The manufacturing method according to any one of Items 1 to 5, wherein the polyvinyl butyral obtained by acetalization is aged in the same aqueous phase without being separated from the reaction system.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15547481A JPS5857406A (en) | 1981-09-29 | 1981-09-29 | Production of polyvinyl butyral having improved autohesion |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15547481A JPS5857406A (en) | 1981-09-29 | 1981-09-29 | Production of polyvinyl butyral having improved autohesion |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5857406A JPS5857406A (en) | 1983-04-05 |
JPH0114922B2 true JPH0114922B2 (en) | 1989-03-15 |
Family
ID=15606834
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15547481A Granted JPS5857406A (en) | 1981-09-29 | 1981-09-29 | Production of polyvinyl butyral having improved autohesion |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5857406A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6483024A (en) * | 1987-09-25 | 1989-03-28 | Kyukyu Yakuhin Kogyo Kk | Cataplasm for cold |
CN100575368C (en) * | 2004-08-04 | 2009-12-30 | 积氎ååŠå·¥äžæ ªåŒäŒç€Ÿ | The manufacture method of the manufacture method of polyvinyl acetal resin, polyvinyl butyral resin and esterified polyvinyl alcohol resin |
-
1981
- 1981-09-29 JP JP15547481A patent/JPS5857406A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5857406A (en) | 1983-04-05 |
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