CN101805523B - Superfine biological powder filling masterbatch and method for preparing same - Google Patents

Superfine biological powder filling masterbatch and method for preparing same Download PDF

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Publication number
CN101805523B
CN101805523B CN2010101448981A CN201010144898A CN101805523B CN 101805523 B CN101805523 B CN 101805523B CN 2010101448981 A CN2010101448981 A CN 2010101448981A CN 201010144898 A CN201010144898 A CN 201010144898A CN 101805523 B CN101805523 B CN 101805523B
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biological powder
superfine
superfine biological
powder
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CN101805523A (en
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王文广
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Henan Jiamusi new environmental protection material Co. Ltd.
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Abstract

The invention relates to superfine biological powder filling masterbatch and a method for preparing the same. The superfine biological powder filling masterbatch is characterized by facilitating the diffusion of the superfine biological powder in resin, improving the production environment in the workshop, reducing the product cost, improving the content of the biomass in the plastic product, emitting less carbon and being environmental friendly. The superfine biological powder filling masterbatch comprises one or more or the combination of at least three of the wax, the EVA, the PE, the PP, the PS, the PLA, the PHA, the PBS, the PBAT, the PPC and the PCL which are all carrier resin. The superfine biological powder refers to animal or plant power of over 300 meshes and other additives. The superfine biological powder filling masterbatch specifically comprises 20-70% of the carrier, ultra-fine powder 27-77% of superfine biological powder, 1-10% of compatible agent, 1-10% of dispersing agent, the 0.05-0.5% of surface treatment agent, of 0.5-2% of lubricant, 0-30% of filler, 0.2-2% of heat stabilizer, 0.1-0.5% of antioxidant and 0-2% of other additives. The superfine biological powder filling masterbatch is prepared by mixing, plastifying, extruding and granulating the components with the twin-screw extruder or the mixer or/and the single screw extruder.

Description

A kind of superfine biological powder filling masterbatch and preparation method thereof
Technical field:
The present invention relates to a kind of superfine biological powder filling masterbatch and preparation method thereof.Masterbatch of the present invention is mainly used in the filling-modified of various types of resins, is beneficial to the abundant dispersion of superfine biological powder in resin, can directly mix the post-treatment moulding with various types of resins.The effect of this invention masterbatch is: reduce product cost, improve production environment, reduce petroleum base resin consumption, improve biomass content in the product, reduce emission amount of carbon dioxide, increase the environmental protection composition.After resin is filled masterbatch of the present invention, when content less to the resin influence when following 30%.
Technical background:
Resource and environmental problem are two challenges greatly that human social development faces, and also are the two big bottlenecks that plastics industry realizes Sustainable development.Prior resin mostly is that raw material is synthetic with the oil, consumes a large amount of petroleum resources.And oil is Nonrenewable resources, always has one day that exhausts.The spending rate that how to reduce oil is the main purpose of patent of the present invention.Superfine biological powder content in goods can reach about 27%~77% among the present invention; Can save 27%~77% petroleum base resin; And superfine biological powder is the recyclable regenerative resource; Inexhaustible, and emission amount of carbon dioxide is merely about 20% of petroleum base resin when burning.
The patent that relates to ultra-fine plant powder masterbatch in the market is for blank; The patent approaching with it all is inorganics filled masterbatch, do not have biological material, secondly is that to adopt petroleum base synthetic resins fully be main raw material to vector resin; Do not have environmental-protecting performance, specifically be listed below:
1,02131310.5 1 kinds of polyolefin packing materials and working method thereof
2,86107768 polyolefin modified filler masterbatch and method of manufacture thereof
3,88101604 is the novel filling master batch of properties-correcting agent with the Al-system coupling agent
4,87107742.6 parent material for filling of high-pressure polyethylene
5,88106061.5 parent material for miniature glass pearls plastics and complete processing thereof
6,89105786.2 1 kinds of filling-modified masterbatch of polyolefine and working method thereof
7,98120630.1 polyolefin packing materials and production technique thereof
8,01107047.1 polyolefin packing material and preparation method thereof
9,200510025550.X filling parent material of calcium carbonate and production technique thereof
10,200510010542.8 profax resin dedicated filling mother stocks
11,200610119119.6 mother filler of black plastic and preparation method thereof
12,200810141355.7 transparent enhanced filling mastre batch
Technology contents:
Problem of environmental pollution and at the scattering problem of resin when the objective of the invention is to solve superfine biological powder and directly being used for producing.
The present invention also aims to reduce product cost, improved the biomass content of plastics, and give its low-carbon environment-friendly performance.
Another object of the present invention is to disclose above-mentioned superfine biological powder filling masterbatch and preparation method thereof.
Filling master batch of the present invention mainly is made up of following different materials: vector resin, superfine biological powder, compatilizer, dispersion agent, surface treatment agent, lubricant, mineral filler, thermo-stabilizer, oxidation inhibitor and other auxiliary agent.
Carrier comprised one or more compsn such as each base polymer such as wax class, EVA, PE (comprising VLDPE, ULDPE), PP, PVC, PS, ABS, PET, TPU, PMMA, SBS, PLA, PHA, PBS, PBAT, PPC, PCL during material according to the invention constituted; Preferred base polymer PLA, PHA, PBS, PBAT, PPC, PCL one or both and the two or more mixture wherein of degrading fully, vector contg is generally 20%~70%.
Superfine biological powder during material according to the invention constitutes is that bar, leaf, fruit and the shell of natural phant is like straw powder, powdered rice hulls, wood powder and bamboo powder etc.; The shell of animal, hoof, bone, angle, hair are like feather meal, bone meal, oyster shell whiting etc.; Granularity reaches more than 300 orders, and superfine biological powder content is generally 27%~77%.
Compatilizer during material according to the invention constitutes is meant functional group's graft product of polymkeric substance; Concrete like maleic anhydride grafted polyethylene, maleic anhydride inoculated polypropylene, maleic anhydride graft PHA, maleic anhydride graft PBS etc., the content of compatilizer is generally 1%~10%.
Dispersion agent during material according to the invention constitutes is meant polyethylene wax, Poly Propylene Wax, OPE, EVA wax etc., and purpose is to improve the dispersing uniformity of ultra-fine plant powder in resin, and the content of dispersion agent is generally 1%~10%.
Surface treatment agent during material according to the invention constitutes is meant coupling agent, and coupling agent comprises titanate coupling agent, aluminate coupling agent, aluminium titanium composite coupler, silane coupling agent.Mainly be in order to improve the interface binding power between ultra-fine plant powder and the vector resin, the content of surface treatment agent is generally 0.05%~0.5%.
Lubricant during material according to the invention constitutes is meant one or more the compsn in white oil, paraffin, Triple Pressed Stearic Acid, stearylamide, amine hydroxybenzene, the erucicamide, and the content of lubricant is generally 0.5%~2%.
Weighting agent during material according to the invention constitutes is meant one or more of mineral fillers such as lime carbonate, talcum powder, permanent white
Compsn.Selected powder fineness should be greater than 325 orders, preferred 1250 purpose powders.The content of mineral filler is generally 0%~30%
Thermo-stabilizer during material according to the invention constitutes is meant organic tin, metallic soap class compound such as calcium/zinc etc., and preferred compound is a thermo-stabilizer of the present invention, and content is generally about 0.2%~2%.
Oxidation inhibitor during material according to the invention constitutes is meant primary antioxidant and the composite use of auxiliary antioxidant, and like antioxidant 1010/168, content is 0.1%~0.5%.
Other auxiliary agent during material according to the invention constitutes is meant nucleator, chainextender, brightening agent, whitening agent, softening agent, deodovization agent, release agent one or both and two or more compsns wherein.Content is generally 0%~2%.
To the filling master batch demands of different, the basic proportioning of various components that in system of the present invention, constitutes filling master batch is: carrier 20%~70%, superfine biological powder 27%~77% according to goods; Compatilizer 1%~10%, dispersion agent 1%~10%, surface treatment agent 0.05%~0.5%; Lubricant 0.5%~2%, weighting agent 0%~30%, thermo-stabilizer 0.2%~2%; Oxidation inhibitor 0.1%~0.5%, other auxiliary agent 0%~2%.
Filler parent granule of the present invention prepares through following method:
1. the weighting agent that adds for needs need carry out pre-treatment; Treatment process is to put in the mixed at high speed by the accurate weighing weighting agent of prescription; Do not handling in the oven dry of mixed at high speed under 60 ℃ of situation; Change low speed over to and add corresponding surface treatment agent after drying is good, about 40~50 ℃, carry out mixed at high speed down again and handled 3~15 minutes, it is for use to put into low mixed machine cooling mixing after handling well.
2. put into the high-speed mixer high speed by other components in the prescription weighing prescription and mix, temperature is controlled at 50~60 ℃, and the mixed at high speed time is approximately 5~20 minutes, and superfine biological powder is scatter fully.
3. mixing plasticizing granulation mode of the present invention has two kinds:
A kind of is that each component mixes in high-speed mixer will be filled a prescription; Mixing temperature is not higher than 60 ℃; Mixing time is about 2~8 minutes; Then the material that mixes is put into mixing plasticizing granulation under 70~150 ℃ of temperature in the twin screw extruder, the rotating speed of twin screw is controlled at PM 80~500 to be changeed.
Another kind is together to put into a component in the prescription in Banbury mixer/single screw extrusion machine; Under 70~150 ℃, plastify with mixer mixing; Mixing time was at 5~20 minutes; Adopt single screw extrusion machine at 60~130 ℃ of following extruding pelletizations then, promptly obtain Wholly-degradable primary color master batch of the present invention.
Granulation mode of the present invention can be water-cooled stretching and granulation, water ring granulation, granulation underwater or the fervent granulation of flour milling.Should carry out drying for the particle that needs water-cooled, drying temperature is 60~70 ℃, and be lower than 0.5% with moisture content time of drying is standard.
Twin screw extruder according to the invention adopts cord wood cocurrent and parallel twin screw, and the twin screw length-to-diameter ratio should not surpass 48: 1 and be advisable with greater than 28: 1, preferably selects 40: 1. in case material in screw rod, be heated for a long time and cause decomposition.
Banbury mixer/single screw extrusion machine according to the invention; Wherein Banbury mixer adopts the adding pressure type Banbury mixer, and the single screw extrusion machine length-to-diameter ratio should not be not more than 20: 1, selects get final product in 8: 1 or 10: 1; Screw rod should be adopted gradual change shape screw rod for well, shears the possibility of degrading to reduce because of material is forced.
Application example is following:
Instance one:
Prescription: (unit is kg)
Figure GSB00000790785400031
The preparation method adopts the twin-screw mixer extruding pelletization, and method is following:
The high-speed mixer temperature is elevated to 110 ℃, then load weighted lime carbonate is dropped into the high-speed mixer high speed and mix, by the friction between lime carbonate and the high-speed mixer inwall;, the temperature of lime carbonate is reached more than 100 ℃, drop into the phthalate ester coupling agent that measures behind about 2~3min; Carry out high-speed stirring and mix, 110 ℃ of mixing temperatures, the treatment time is 5 minutes; And then changing the low speed cooling mixing over to, the material of handling well is emitted for use.
And then drop into the P34HB, calcium/zinc stabilizer, 1010,168, maleic anhydride graft PHA and the paraffin that have measured successively and under at a high speed, mixed one to three minute, change the low speed cooling and stirring then over to and mix, emit the good material of compounding.The material that is mixed is joined in the hopper of twin screw the mixing plasticizing extruding pelletization then through twin screw.The twin screw extruder screw slenderness ratio of selecting for use is 36: 1; Screw diameter is φ 75; The twin screw processing temperature is followed successively by 80 ℃-100 ℃-110 ℃-120 ℃-125 ℃-130 ℃-130 ℃-135 ℃-130 ℃ from feeding section to the head setting; Wherein two districts, back are head temperature, and the front is a body temperature for six sections.Screw speed is 120 rev/mins.Water ring granulation mode is adopted in granulation, carries out the drying cooling then and gets final product.
Instance two:
Above material adopts Banbury mixer/single screw extrusion machine to prepare, and concrete grammar is following:
Above material put into after good in the Banbury mixer not being higher than 150 by the prescription weighing in the lump spend under the temperature conditionss and carry out mixing plasticizing, mixing time is as the criterion with material plasticizing fully, wants to carry out more than three times exhaust during this period at least and material is overturn.Evenly also plasticizing is complete to make various material thorough mixing. and put into then and carry out granulation in the single screw extrusion machine; The single screw extrusion machine temperature is controlled at 70~130 degree and gets final product, and the particle of making is sieved just obtain superfine biological powder filling masterbatch of the present invention then.This masterbatch by a certain percentage be filled moulding (as: PHA, PBS, PLA etc.) and simply mix after, can directly be used to produce various products.

Claims (1)

1. superfine biological powder filling masterbatch, it is characterized in that: its composition is made up of vector resin, superfine biological powder, compatilizer, dispersion agent, surface treatment agent, lubricant, mineral filler, thermo-stabilizer, oxidation inhibitor and other auxiliary agent; Concrete proportioning is a vector resin 20%~70%, superfine biological powder 27%~77%, compatilizer 1%~10%; Dispersion agent 1%~10%, surface treatment agent 0.05%~0.5%, lubricant 0.5%~2%; Mineral filler 0%~30%, thermo-stabilizer 0.2%~2%, oxidation inhibitor 0.1%~0.5%; Other auxiliary agent 0%~2%, wherein:
(1) said vector resin is specially polymer-wax class, EVA, VLDPE, ULDPE, LDPE, LLDPE, PP, PVC, PS, ABS, PET, TPU, PMMA, SBS, PLA, PHA, PBS, PBAT, PPC, PCL one or both and above compsn;
(2) said superfine biological powder is specially two types of plant and animals, and the plant class is specially straw powder, powdered rice hulls, wood powder and bamboo powder, and the animal class is specially feather meal, bone meal and oyster shell whiting, reaches more than 300 orders with dodging quick-fried method processing back granularity;
(3) said compatilizer is specially functional group's graft product of polymkeric substance, is specially maleic anhydride grafted polyethylene, maleic anhydride inoculated polypropylene, maleic anhydride graft PHA, maleic anhydride graft PBS.
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