Summary of the invention
In order to solve above-mentioned technical problem existing in prior art, the object of the present invention is to provide a kind of automatic foot-mat modified PVC PP Pipe Compound.
In order to solve the problems of the technologies described above, realize foregoing invention object, present invention employs following technical scheme:
A kind of automatic foot-mat modified PVC PP Pipe Compound, it is characterized in that containing in massfraction: polyvinyl chloride resin: 100 parts, DOTP:8 ~ 10 part, DOP:28 ~ 32 part, isobornyl methacrylate: 25 ~ 30 parts, the calcium carbonate of surface modification: 20 ~ 25 parts, polyoxypropylene diamine (D-400): 2.5 ~ 3.0 parts, antioxidant 1024:0.25 ~ 0.30 part, polyethylene wax: 0.8 ~ 1.0 part, hard barium: 1.8 ~ 2.0 parts, calcium zinc stabilizer: 3.5 ~ 5.0 parts.
Wherein, described automatic foot-mat modified PVC PP Pipe Compound is made up of the component of following massfraction meter: polyvinyl chloride resin: 100 parts, DOTP:8 ~ 10 part, DOP:28 ~ 32 part, isobornyl methacrylate: 25 ~ 30 parts, the calcium carbonate of surface modification: 20-25 part, polyoxypropylene diamine (D-400): 2.5-3.0 part, polyethylene wax: 0.8-1.0 part, hard barium: 1.8-2.0 part, calcium zinc stabilizer: 3.5 ~ 5.0 parts.
Wherein, described surface modification calcium carbonate add rigidity and the dimensional stability that effectively can improve polyvinyl chloride resin.The diameter of the calcium carbonate of surface modification is 1-100 μm in the present invention, is preferably 5 ~ 20 μm.
Wherein, described surface modification refers to the process through following steps:
1) prepare the methylcarbonate of described calcium carbonate quality 200% to 250%, be uniformly mixed 20 ~ 30 minutes after adding filler, obtain premixed slurries;
2) be that the surface-modifying agent of described calcium carbonate quality 8 ~ 10% joins in described premixed slurries by quality, be uniformly mixed 20 ~ 30 minutes, and grind;
3) slurry after grinding is filtered, and carry out vacuum-drying in 120 ~ 150 DEG C, the calcium carbonate of described surface modification can be obtained.
Wherein, described surface-modifying agent is the compound with following formula:
In described formula, A is octyl phenol and the reacted residue of isocyanate groups; R is ditane-4,4, the part in-vulcabond except isocyanate groups; Wherein, m and n is integer, and 5≤m≤10,3≤n≤5.
Wherein, described compound can by ditane-4,4, the polyether glycol of-vulcabond and different polymerization degree first reacts by a certain percentage and forms the urethane that molecular chain two ends are isocyanate groups in toluene, acetone and other organic solvent, add octyl phenol again carry out end-blocking preparation to it and obtain, in reaction process, for increasing speed of response, catalyzer conventional in the urethane such as stannous octoate, dibutyl tin laurate building-up process can be used.The polymerization degree that can control polyether glycol used, to control the m value in general formula (I), controls the n value in general formula (I) by the mol ratio controlled between polyether glycol and vulcabond.
Wherein, described polyvinyl chloride resin is S-1000, S-1300 or the mixture of the two; If be the mixture of S-1000, S-1300, wherein the mass ratio of S-1000 and S-1300 is 2:8 ~ 8:2.
Wherein, described calcium zinc stabilizer is mediated by the Trimethyllaurylammonium bromide of the calcium stearate of the molecular sieve ZSM-5 of 8 ~ 12 mass parts, 12 ~ 15 mass parts, the zinc stearate of 10 ~ 12 mass parts, oxidation inhibitor 1024 and 10 ~ 12 mass parts of 2.0 ~ 2.5 mass parts and is formed at 90 ~ 100 DEG C.
A second aspect of the present invention, also relate to the preparation method of above-mentioned automatic foot-mat modified PVC PP Pipe Compound, it comprises the following steps:
(1) stir in the calcium carbonate of polyvinyl chloride resin, DOTP, DOP, isobornyl methacrylate, surface modification, polyoxypropylene diamine (D-400), antioxidant 1024, polyethylene wax, hard barium and calcium zinc stabilizer input high speed agitator according to proportioning raw materials, stirring velocity is 1000 ~ 1200 revs/min, whipping temp is 80 ~ 100 DEG C, churning time is 8 ~ 10 minutes, obtains compound;
(2) compound is carried out extruding pelletization in screw extrusion press, the temperature of each section of screw extrusion press is respectively: the temperature of the first section is 130 ~ 135 DEG C, the temperature of the second section is 145 ~ 150 DEG C, the temperature of the 3rd section is 160 ~ 165 DEG C, the temperature of the 4th section is 165 ~ 170 DEG C, the temperature of the 5th section is 160 ~ 165 DEG C, and the temperature of the 6th section is 135 ~ 140 DEG C, can obtain described automatic foot-mat modified PVC PP Pipe Compound after discharging.
Compared with prior art, PVC PP Pipe Compound of the present invention has following beneficial effect:
Automatic foot-mat modified PVC PP Pipe Compound of the present invention not only has preferably elasticity, and sound-absorbing, vibration damping and abrasion resistance properties are good, long service life.
Embodiment
Below in conjunction with specific embodiments the raw material of automatic foot-mat modified PVC PP Pipe Compound of the present invention, preparation technology and performance etc. are described in detail.
Embodiment 1
Use calcium carbonate superfine powder in the present embodiment, the average out to of described calcium carbonate 5 μm.The calcium carbonate of described surface modification prepares by the following method: first, prepares the methylcarbonate of described calcium carbonate quality 200%, is uniformly mixed 20 minutes, obtains premixed slurries after adding filler; Then, be that the surface-modifying agent of described calcium carbonate quality 10% joins in described premixed slurries by quality, be uniformly mixed 30 minutes, and grind; Finally, the slurry after grinding is filtered, and carries out vacuum-drying in 120 DEG C, the calcium carbonate of described surface modification can be obtained.Described surface-modifying agent is the compound with following formula:
In formula, A is octyl phenol and the reacted residue of isocyanate groups; R is ditane-4,4, the part in-vulcabond except isocyanate groups; M is 6, and n is 3.Described compound can by ditane-4,4, the polyether glycol of-vulcabond and different polymerization degree first reacts by a certain percentage and forms the urethane that molecular chain two ends are isocyanate groups in toluene, acetone and other organic solvent, add octyl phenol again carry out end-blocking preparation to it and obtain, in reaction process, for increasing speed of response, catalyzer conventional in the urethane such as stannous octoate, dibutyl tin laurate building-up process can be used.The polymerization degree that can control polyether glycol used, to control the m value in general formula (I), controls the n value in general formula (I) by the mol ratio controlled between polyether glycol and vulcabond.
Comparative example 1
Calcium carbonate superfine powder is used, the average out to of described calcium carbonate 5 μm in this comparative example.Described calcium carbonate utilizes dimethyl silicone oil to carry out surface treatment, and the mass ratio of described dimethyl silicone oil and calcium carbonate is 1:10.
Embodiment 2
The formula of the automatic foot-mat modified PVC PP Pipe Compound described in the present embodiment is as follows: the polyvinyl chloride resin of 100 mass parts, the DOTP of 8 mass parts, the DOP of 32 mass parts, the isobornyl methacrylate of 28 mass parts, the surface modified calcium carbonate (surface modified calcium carbonate that embodiment 1 method obtains) of 25 mass parts, the polyoxypropylene diamine D-400 of 3.0 mass parts, the antioxidant 1024 of 0.30 mass parts, the polyethylene wax of 0.8 mass parts, the hard barium of 2.0 mass parts, and part calcium zinc stabilizer CZ-1 of 4.0 quality.Preparation technology is as follows: (1) stirs in the calcium carbonate of polyvinyl chloride resin, DOTP, DOP, isobornyl methacrylate, surface modification, polyoxypropylene diamine D-400, antioxidant 1024, polyethylene wax, hard barium and calcium zinc stabilizer input high speed agitator according to proportioning raw materials, stirring velocity is 1200 revs/min, whipping temp is 90 DEG C, churning time is 8 minutes, obtains compound; (2) compound is carried out extruding pelletization in screw extrusion press, the temperature of each section of screw extrusion press is respectively: the temperature of the first section is 130 ~ 135 DEG C, the temperature of the second section is 145 ~ 150 DEG C, the temperature of the 3rd section is 160 ~ 165 DEG C, the temperature of the 4th section is 165 ~ 170 DEG C, the temperature of the 5th section is 160 ~ 165 DEG C, the temperature of the 6th section is 135 ~ 140 DEG C, by cyclopneumatic separator feeding after extruding pelletization, utilize bolting then to pack, described modified PVC PP Pipe Compound can be obtained.
Embodiment 3
The formula of the automatic foot-mat modified PVC PP Pipe Compound described in the present embodiment is as follows: the polyvinyl chloride resin of 100 mass parts, the DOTP of 10 mass parts, the DOP of 28 mass parts, the isobornyl methacrylate of 30 mass parts, the surface modified calcium carbonate (surface modified calcium carbonate that embodiment 1 method obtains) of 25 mass parts, the polyoxypropylene diamine D-400 of 2.5 mass parts, the antioxidant 1024 of 0.30 mass parts, the polyethylene wax of 1.0 mass parts, the hard barium of 1.8 mass parts, and part calcium zinc stabilizer CZ-1 of 4.0 quality.Preparation technology is as follows: (1) stirs in the calcium carbonate of polyvinyl chloride resin, DOTP, DOP, isobornyl methacrylate, surface modification, polyoxypropylene diamine D-400, antioxidant 1024, polyethylene wax, hard barium and calcium zinc stabilizer input high speed agitator according to proportioning raw materials, stirring velocity is 1200 revs/min, whipping temp is 90 DEG C, churning time is 8 minutes, obtains compound; (2) compound is carried out extruding pelletization in screw extrusion press, the temperature of each section of screw extrusion press is respectively: the temperature of the first section is 130 ~ 135 DEG C, the temperature of the second section is 145 ~ 150 DEG C, the temperature of the 3rd section is 160 ~ 165 DEG C, the temperature of the 4th section is 165 ~ 170 DEG C, the temperature of the 5th section is 160 ~ 165 DEG C, the temperature of the 6th section is 135 ~ 140 DEG C, by cyclopneumatic separator feeding after extruding pelletization, utilize bolting then to pack, described modified PVC PP Pipe Compound can be obtained.
Embodiment 4
Compared with embodiment 2, the calcium zinc stabilizer that the present embodiment adopts is mediated by the Trimethyllaurylammonium bromide of the calcium stearate of the molecular sieve ZSM-5 of 10 mass parts, 15 mass parts, the zinc stearate of 10 mass parts, oxidation inhibitor 1024 and 12 mass parts of 2.0 mass parts and is formed at 100 DEG C.
Embodiment 5
Compared with embodiment 3, the calcium zinc stabilizer that the present embodiment adopts is mediated by the Trimethyllaurylammonium bromide of the calcium stearate of the molecular sieve ZSM-5 of 12 mass parts, 12 mass parts, the zinc stearate of 12 mass parts, oxidation inhibitor 1024 and 12 mass parts of 2.5 mass parts and is formed at 100 DEG C.
Comparative example 2
The formula of the automatic foot-mat modified PVC PP Pipe Compound described in this comparative example is as follows: the polyvinyl chloride resin of 100 mass parts, the DOTP of 8 mass parts, the DOP of 32 mass parts, the isobornyl methacrylate of 28 mass parts, the surface modified calcium carbonate (surface modified calcium carbonate that comparative example 1 obtains) of 25 mass parts, the polyoxypropylene diamine D-400 of 3.0 mass parts, the antioxidant 1024 of 0.30 mass parts, the polyethylene wax of 0.8 mass parts, the hard barium of 2.0 mass parts, and part calcium zinc stabilizer CZ-1 of 4.0 quality.Preparation technology is as follows: (1) stirs in the calcium carbonate of polyvinyl chloride resin, DOTP, DOP, isobornyl methacrylate, surface modification, polyoxypropylene diamine D-400, antioxidant 1024, polyethylene wax, hard barium and calcium zinc stabilizer input high speed agitator according to proportioning raw materials, stirring velocity is 1200 revs/min, whipping temp is 90 DEG C, churning time is 8 minutes, obtains compound; (2) compound is carried out extruding pelletization in screw extrusion press, the temperature of each section of screw extrusion press is respectively: the temperature of the first section is 130 ~ 135 DEG C, the temperature of the second section is 145 ~ 150 DEG C, the temperature of the 3rd section is 160 ~ 165 DEG C, the temperature of the 4th section is 165 ~ 170 DEG C, the temperature of the 5th section is 160 ~ 165 DEG C, the temperature of the 6th section is 135 ~ 140 DEG C, by cyclopneumatic separator feeding after extruding pelletization, utilize bolting then to pack, described modified PVC PP Pipe Compound can be obtained.
Comparative example 3
The formula of the automatic foot-mat modified PVC PP Pipe Compound described in this comparative example is as follows: the polyvinyl chloride resin of 100 mass parts, the DOTP of 10 mass parts, the DOP of 28 mass parts, the isobornyl methacrylate of 30 mass parts, the surface modified calcium carbonate (surface modified calcium carbonate that comparative example 1 obtains) of 25 mass parts, the polyoxypropylene diamine D-400 of 2.5 mass parts, the antioxidant 1024 of 0.30 mass parts, the polyethylene wax of 1.0 mass parts, the hard barium of 1.8 mass parts, and part calcium zinc stabilizer CZ-1 of 4.0 quality.Preparation technology is as follows: (1) stirs in the calcium carbonate of polyvinyl chloride resin, DOTP, DOP, isobornyl methacrylate, surface modification, polyoxypropylene diamine D-400, antioxidant 1024, polyethylene wax, hard barium and calcium zinc stabilizer input high speed agitator according to proportioning raw materials, stirring velocity is 1200 revs/min, whipping temp is 90 DEG C, churning time is 8 minutes, obtains compound; (2) compound is carried out extruding pelletization in screw extrusion press, the temperature of each section of screw extrusion press is respectively: the temperature of the first section is 130 ~ 135 DEG C, the temperature of the second section is 145 ~ 150 DEG C, the temperature of the 3rd section is 160 ~ 165 DEG C, the temperature of the 4th section is 165 ~ 170 DEG C, the temperature of the 5th section is 160 ~ 165 DEG C, the temperature of the 6th section is 135 ~ 140 DEG C, by cyclopneumatic separator feeding after extruding pelletization, utilize bolting then to pack, described modified PVC PP Pipe Compound can be obtained.
Comparative example 4
The formula of the automatic foot-mat modified PVC PP Pipe Compound described in this comparative example is as follows: the polyvinyl chloride resin of 100 mass parts, the DOTP of 8 mass parts, the DOP of 32 mass parts, the isobornyl methacrylate of 28 mass parts, the surface modified calcium carbonate (surface modified calcium carbonate that embodiment 1 method obtains) of 25 mass parts, the polyethylene wax of antioxidant 1024,0.8 mass parts of 0.30 mass parts, the hard barium of 2.0 mass parts, and part calcium zinc stabilizer CZ-1 of 4.0 quality.Preparation technology is as follows: (1) stirs in the calcium carbonate of polyvinyl chloride resin, DOTP, DOP, isobornyl methacrylate, surface modification, antioxidant 1024, polyethylene wax, hard barium and calcium zinc stabilizer input high speed agitator according to proportioning raw materials, stirring velocity is 1200 revs/min, whipping temp is 90 DEG C, churning time is 8 minutes, obtains compound; (2) compound is carried out extruding pelletization in screw extrusion press, the temperature of each section of screw extrusion press is respectively: the temperature of the first section is 130 ~ 135 DEG C, the temperature of the second section is 145 ~ 150 DEG C, the temperature of the 3rd section is 160 ~ 165 DEG C, the temperature of the 4th section is 165 ~ 170 DEG C, the temperature of the 5th section is 160 ~ 165 DEG C, the temperature of the 6th section is 135 ~ 140 DEG C, by cyclopneumatic separator feeding after extruding pelletization, utilize bolting then to pack, described modified PVC PP Pipe Compound can be obtained.
Comparative example 5
The formula of the automatic foot-mat modified PVC PP Pipe Compound described in this comparative example is as follows: the polyvinyl chloride resin of 100 mass parts, the DOTP of 8 mass parts, the DOP of 32 mass parts, the surface modified calcium carbonate (surface modified calcium carbonate that embodiment 1 method obtains) of 25 mass parts, the polyoxypropylene diamine D-400 of 3.0 mass parts, the polyethylene wax of antioxidant 1024,0.8 mass parts of 0.30 mass parts, the hard barium of 2.0 mass parts, and part calcium zinc stabilizer CZ-1 of 4.0 quality.Preparation technology is as follows: (1) stirs in the calcium carbonate of polyvinyl chloride resin, DOTP, DOP, isobornyl methacrylate, surface modification, polyoxypropylene diamine D-400, antioxidant 1024, polyethylene wax, hard barium and calcium zinc stabilizer input high speed agitator according to proportioning raw materials, stirring velocity is 1200 revs/min, whipping temp is 90 DEG C, churning time is 8 minutes, obtains compound; (2) compound is carried out extruding pelletization in screw extrusion press, the temperature of each section of screw extrusion press is respectively: the temperature of the first section is 130 ~ 135 DEG C, the temperature of the second section is 145 ~ 150 DEG C, the temperature of the 3rd section is 160 ~ 165 DEG C, the temperature of the 4th section is 165 ~ 170 DEG C, the temperature of the 5th section is 160 ~ 165 DEG C, the temperature of the 6th section is 135 ~ 140 DEG C, by cyclopneumatic separator feeding after extruding pelletization, utilize bolting then to pack, described modified PVC PP Pipe Compound can be obtained.
The modified PVC PP Pipe Compound utilizing embodiment 2 ~ 5 and comparative example 2 ~ 5 to obtain prepares automatic foot-mat.The testing method utilizing GB/T1040-1992, GB2411-1980 to specify carries out performance test, and test result is as shown in table 1.
Table 1
Wherein, described agingly refer in air oven aging, temperature is 100 DEG C, and the time is 200 hours.
The foregoing is only specific embodiment of the present invention; can not be interpreted as limiting scope of the present invention with this, the equivalent distortion made in all scopes claimed at claims of the present invention and the embodiment of change are all in the present invention's scope required for protection.