CN108929538A - A kind of nylon composite and preparation method thereof - Google Patents

A kind of nylon composite and preparation method thereof Download PDF

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Publication number
CN108929538A
CN108929538A CN201710380891.1A CN201710380891A CN108929538A CN 108929538 A CN108929538 A CN 108929538A CN 201710380891 A CN201710380891 A CN 201710380891A CN 108929538 A CN108929538 A CN 108929538A
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molecular weight
nylon
nylon composite
parts
temperature
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杨桂生
吴安琪
范继贤
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Hefei Genius New Materials Co Ltd
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Hefei Genius New Materials Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L77/00Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
    • C08L77/02Polyamides derived from omega-amino carboxylic acids or from lactams thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/02Making granules by dividing preformed material
    • B29B9/06Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/011Nanostructured additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/014Additives containing two or more different additives of the same subgroup in C08K
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2207/00Properties characterising the ingredient of the composition
    • C08L2207/06Properties of polyethylene
    • C08L2207/062HDPE

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The present invention provides a kind of nylon composite and preparation method thereof, is related to technical field of polymer materials.Nylon composite of the present invention is prepared from the following raw materials:Nylon 6, nylon66 fiber, Research of Grafting Malaic Anhydride Onto Polyethylene, modified with ultrahigh molecular weight polyethylene glass fibre, odor adsorption master batch, silicon carbide, lubricant, antioxidant.Nylon composite of the present invention has significant raising in terms of wear-resisting property, and has excellent mechanical property, and odor adsorption master batch is added in raw material and cooperates high density polyethylene (HDPE) matrix, ensure that the low odor profiles of nylon composite.

Description

A kind of nylon composite and preparation method thereof
Technical field
The present invention relates to technical field of polymer materials, and in particular to a kind of nylon composite and preparation method thereof.
Background technique
Nylon is a computer MSR Information system development under the outstanding scientist's Tomas Carothers (Carothers) in the U.S. and its leader It out, is the first synthetic fibers occurred in the world.Nylon is a kind of saying of Fypro (polyamide fibre), is generally divided into Nylon 6, nylon66 fiber.6 appearance of nylon is milky to faint yellow, has toughness, shock resistance, there is higher mechanical strength and heat-resisting Property, shock strength is preferable, and fusing point is higher, and moulding processability is good, and water imbibition is big, saturated water absorption 11% or so, it is meltable in In sulfated phenolic or formic acid, brittle temperature is the degree of minus 20 degrees -30.
Although nylon has many excellent performances, in the more demanding field of some pairs of smells, wear-resisting properties, nylon Application will receive very big limitation.Therefore it needs to further decrease its smell, coefficient of friction and wear rate, is answered to expand it Use field.
Summary of the invention
In view of the shortcomings of the prior art, the present invention provides a kind of nylon composite and preparation method thereof, solves the prior art Middle nylon smell is big, the technical issues of wearing no resistance.
In order to achieve the above object, technical solution of the present invention is achieved by the following technical programs:
A kind of nylon composite, the nylon composite are made of raw material from the following weight:54-90 parts of nylon 6,1-5 Part nylon66 fiber, 1-5 parts of Research of Grafting Malaic Anhydride Onto Polyethylene, 5-45 parts of modified with ultrahigh molecular weight polyethylene glass fibres, 1-5 parts of smells Adsorb master batch, 0.1-0.5 parts of silicon carbide, 0.2-1 parts of lubricants, 0.1-1 parts of antioxidant.
Preferably, 6 melting means of nylon is 5-8g/10min, and the nylon66 fiber melting means is 8-10g/10min.
Preferably, the odor adsorption master batch is by high density polyethylene (HDPE), hydrophobicity diatomite, hydrophobic active charcoal, needle-shaped Zeolite molecular sieve, zinc ricinate, nano silica, calcium stearate, melamine are uniformly mixed, then in double screw extruder Middle extruding pelletization forms.
Preferably, the modified with ultrahigh molecular weight polyethylene glass fibre is to impregnate through ultra-high molecular weight polyethylene dispersion liquid Treated modified with ultrahigh molecular weight polyethylene glass fibre, and the molecular weight of ultra-high molecular weight polyethylene is 4,800,000, fracture is stretched Long rate is 3%-10%.
Preferably, the high density polyethylene (HDPE) crystallinity 80%, molecular weight are 300,000.
Preferably, the ultra-high molecular weight polyethylene dispersion liquid is that the super high molecular weight that average grain diameter is 0.1-0.2 μm is poly- Vinyl is suspended in the colloidal solution formed in liquid water, and the viscosity of colloidal solution is 0.05Pas, concentration is 60wt%.
Preferably, the lubricant is at least one of silicone powder, white oil, silicone oil, paraffin, stearic acid, zinc stearate.
Preferably, the antioxidant is four [β-(3,5- di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol esters and Asia Tricresyl phosphate (2,4- di-tert-butyl-phenyl) ester mixes, and the weight part ratio of the two is 2:3-1:1.
A kind of preparation method of nylon composite, includes the following steps:
S1, will be immersed in ultra-high molecular weight polyethylene dispersion liquid after glass fibre cleaning, drying, take out drying and 190-210 DEG C is baked and banked up with earth, is sintered, and modified with ultrahigh molecular weight polyethylene glass fibre is made;
S2, each raw material for weighing parts by weight, nylon 6, nylon66 fiber, Research of Grafting Malaic Anhydride Onto Polyethylene, odor adsorption is female Grain, silicon carbide, lubricant and antioxidant pour into blender, stir evenly and are placed in double screw extruder, by supra polymer Weight polyethylene modified glass fibre is added from the glass fiber opening of double screw extruder, is granulated after melting extrusion.
Preferably, area's temperature of double screw extruder described in step S2 is 180-190 DEG C, two area's temperature are 180-190 DEG C, three area's temperature be 190-200 DEG C, four area's temperature are 210-220 DEG C, five area's temperature are 230-250 DEG C, six area's temperature are 245- 250℃;Twin-screw engine speed is 500rpm.
The present invention provides a kind of nylon composite and preparation method thereof, and advantage is compared with prior art:
1. in the raw material of nylon composite of the present invention, 6 melting means of nylon is 5-8g/10min, nylon66 fiber melting means is 8-10g/ 10min can adjust the mobility of 6 melt of nylon after being added, guarantee that in process, nylon 6 is plasticized uniformly, melting is mixed Close smooth, raw material modified with ultrahigh molecular weight polyethylene glass fibre is using extraordinary ultra-high molecular weight polyethylene dispersion liquid to glass fibers Dimension progress impregnation avoids glass fiber impregnated dipping in the process not exclusively, and the situation of disconnected fibre occurs in fiber, great to improve Dispersibility of the glass in nylon matrix, and nylon composite obtained is made to have significant raising in terms of wear-resisting property, and Maintain excellent mechanical property;
2. ultra-high molecular weight polyethylene molecular weight is 4,800,000 in the present invention, elongation at break 3%-10%, use is this Powder particle avoids the fiber impregnation inefficient occurred during fiber impregnation, and not exclusively, the skills such as disconnected fibre occurs to dipping in fiber The appearance of art problem;
3. the dosage of raw material silicon carbide of the present invention is down to 0.1-0.5 parts, the silicon carbide of low dosage had both avoided a large amount of uses Caused by nylon combination physical performance decline, in turn ensure the synergistic effect that silicon carbide plays nylon composite wear-resisting property, mention The high wear-resisting property of nylon composite;
4. odor adsorption master batch of the present invention uses crystallinity 80%, the high density polyethylene (HDPE) that molecular weight is 300,000 is as base Body improves the compatibility of itself and fiber, nylon when as gas absorption master batch, ensure that master batch in composition system Dispersibility ensure that the low odor profiles of nylon composite;
5. odor adsorption master batch reduces the small molecule content in composition, significantly reduce total volatile organism TVOC, And while guaranteeing composition low odor characteristics, every physical and mechanical property, material moulding processability not by shadow It rings;
6. using area's temperature of double screw extruder for 180-190 DEG C, two in nylon composite preparation method of the present invention Area's temperature is 180-190 DEG C, three area's temperature are 190-200 DEG C, four area's temperature are 210-220 DEG C, five area's temperature are 230-250 DEG C, six area's temperature be 245-250 DEG C;Twin-screw engine speed is 500rpm, and such processing temperature, engine speed make nylon group It closes object to block at the charging that process is not in, and with the advantages of feeding saturation, plasticizing is uniform, not overflow.
Specific embodiment
In order to make the object, technical scheme and advantages of the embodiment of the invention clearer, below with reference to the embodiment of the present invention pair Technical solution in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is a part of the invention Embodiment, instead of all the embodiments.Based on the embodiments of the present invention, those of ordinary skill in the art are not making wound Every other embodiment obtained under the premise of the property made labour, shall fall within the protection scope of the present invention.
Modified with ultrahigh molecular weight polyethylene glass fibre and odor adsorption master batch are prepared by following method in embodiment It forms:
The impregnation of modified with ultrahigh molecular weight polyethylene glass fibre:Superelevation will be immersed in after glass fibre cleaning, drying In molecular weight polyethylene dispersion liquid, then takes out and dry and baked and banked up with earth at 200 DEG C, be sintered to obtain modified with ultrahigh molecular weight polyethylene glass Fiber;Ultra-high molecular weight polyethylene dispersion liquid is that the polyvinyl resin with super-high molecular weight that average grain diameter is 0.1-0.2 μm is suspended in The colloidal solution formed in liquid water, the viscosity of the colloidal solution is 0.05Pas, concentration 60wt%.
The preparation of odor adsorption master batch:100 parts of high density polyethylene (HDPE), 5 parts of hydrophobicity diatomite, hydrophobic active charcoal 10 Part, 5 parts of needle-shaped zeolite molecular sieve, 10 parts of zinc ricinate, 5 parts of nano silica, 1 part of calcium stearate, 5 parts of melamine, Row is uniformly mixed, and then extruding pelletization obtains odor adsorption master batch in double screw extruder.
Ultra-high molecular weight polyethylene number molecular weight is 4,800,000, elongation at break 3%-10%.
High density polyethylene (HDPE) crystallinity 80%, molecular weight are 300,000.
Lubricant is at least one of silicone powder, white oil, silicone oil, paraffin, stearic acid, zinc stearate.
6 melting means of nylon is 5-8g/10min.
Nylon66 fiber melting means is 8-10g/10min.
Embodiment 1:
The present embodiment nylon composite is made of raw material from the following weight:70 parts of nylon, 6,1 parts of nylon66 fibers, 1 part of poly- second Alkene grafted maleic anhydride, 25 parts of modified with ultrahigh molecular weight polyethylene glass fibres, 3 parts of odor adsorption master batches, 0.5 part of silicon carbide, 1 Part silicone powder, 0.5 part of antioxidant, 1098,0.5 parts of irgasfos 168s;
The preparation method of the present embodiment nylon composite, includes the following steps:
S1, it will be immersed in ultra-high molecular weight polyethylene dispersion liquid after glass fibre cleaning, drying, take out drying and 190 It DEG C bakes and banks up with earth, be sintered, modified with ultrahigh molecular weight polyethylene glass fibre is made;
S2, each raw material for weighing parts by weight, nylon 6, nylon66 fiber, Research of Grafting Malaic Anhydride Onto Polyethylene, odor adsorption is female Grain, silicon carbide, lubricant and antioxidant pour into blender, stir evenly and are placed in double screw extruder, by supra polymer Weight polyethylene modified glass fibre is added from the glass fiber opening of double screw extruder, is granulated after melting extrusion.
Wherein, area's temperature of double screw extruder is 180 DEG C, two area's temperature are 180 DEG C, three area's temperature are 190 DEG C, four Area's temperature is 210 DEG C, five area's temperature are 230 DEG C, six area's temperature are 245 DEG C;Twin-screw engine speed is 500rpm.
Embodiment 2:
The present embodiment nylon composite is made of raw material from the following weight:54 parts of nylon, 6,2 parts of nylon66 fibers, 2 parts of poly- second Alkene grafted maleic anhydride, 30 parts of modified with ultrahigh molecular weight polyethylene glass fibres, 1 part of odor adsorption master batch, 0.2 part of silicon carbide, 0.2 part of silicone powder, 0.1 part of antioxidant, 1098,0.1 parts of irgasfos 168s;
The preparation method of the present embodiment nylon composite, includes the following steps:
S1, it will be immersed in ultra-high molecular weight polyethylene dispersion liquid after glass fibre cleaning, drying, take out drying and 210 It DEG C bakes and banks up with earth, be sintered, modified with ultrahigh molecular weight polyethylene glass fibre is made;
S2, each raw material for weighing parts by weight, nylon 6, nylon66 fiber, Research of Grafting Malaic Anhydride Onto Polyethylene, odor adsorption is female Grain, silicon carbide, lubricant and antioxidant pour into blender, stir evenly and are placed in double screw extruder, by supra polymer Weight polyethylene modified glass fibre is added from the glass fiber opening of double screw extruder, is granulated after melting extrusion.
Wherein, area's temperature of double screw extruder is 190 DEG C, two area's temperature are 190 DEG C, three area's temperature are 200 DEG C, four Area's temperature is 220 DEG C, five area's temperature are 250 DEG C, six area's temperature are 250 DEG C;Twin-screw engine speed is 500rpm.
Embodiment 3:
The present embodiment nylon composite is made of raw material from the following weight:90 parts of nylon, 6,5 parts of nylon66 fibers, 5 parts of poly- second Alkene grafted maleic anhydride, 20 parts of modified with ultrahigh molecular weight polyethylene glass fibres, 5 parts of odor adsorption master batches, 0.1 part of silicon carbide, 0.5 part of silicone powder, 0.2 part of antioxidant, 1098,0.3 parts of irgasfos 168s;
The preparation method of the present embodiment nylon composite, includes the following steps:
S1, it will be immersed in ultra-high molecular weight polyethylene dispersion liquid after glass fibre cleaning, drying, take out drying and 200 It DEG C bakes and banks up with earth, be sintered, modified with ultrahigh molecular weight polyethylene glass fibre is made;
S2, each raw material for weighing parts by weight, nylon 6, nylon66 fiber, Research of Grafting Malaic Anhydride Onto Polyethylene, odor adsorption is female Grain, silicon carbide, lubricant and antioxidant pour into blender, stir evenly and are placed in double screw extruder, by supra polymer Weight polyethylene modified glass fibre is added from the glass fiber opening of double screw extruder, is granulated after melting extrusion.
Wherein, area's temperature of double screw extruder is 180 DEG C, two area's temperature are 180 DEG C, three area's temperature are 190 DEG C, four Area's temperature is 210 DEG C, five area's temperature are 230 DEG C, six area's temperature are 245 DEG C;Twin-screw engine speed is 500rpm.
Embodiment 4:
The present embodiment nylon composite is made of raw material from the following weight:60 parts of nylon, 6,2 parts of nylon66 fibers, 2 parts of poly- second Alkene grafted maleic anhydride, 5 parts of modified with ultrahigh molecular weight polyethylene glass fibres, 1 part of odor adsorption master batch, 0.3 part of silicon carbide, 0.3 part of lubricant, 0.3 part of antioxidant;
The preparation method of the present embodiment nylon composite, includes the following steps:
S1, it will be immersed in ultra-high molecular weight polyethylene dispersion liquid after glass fibre cleaning, drying, take out drying and 200 It DEG C bakes and banks up with earth, be sintered, modified with ultrahigh molecular weight polyethylene glass fibre is made;
S2, each raw material for weighing parts by weight, nylon 6, nylon66 fiber, Research of Grafting Malaic Anhydride Onto Polyethylene, odor adsorption is female Grain, silicon carbide, lubricant and antioxidant pour into blender, stir evenly and are placed in double screw extruder, by supra polymer Weight polyethylene modified glass fibre is added from the glass fiber opening of double screw extruder, is granulated after melting extrusion.
Wherein, area's temperature of double screw extruder is 180 DEG C, two area's temperature are 180 DEG C, three area's temperature are 190 DEG C, four Area's temperature is 210 DEG C, five area's temperature are 230 DEG C, six area's temperature are 245 DEG C;Twin-screw engine speed is 500rpm.
Wherein, 6 melting means of nylon is 5g/10min, and the nylon66 fiber melting means is 8g/10min;Ultra-high molecular weight polyethylene changes Property glass fibre be modified with ultrahigh molecular weight polyethylene glass fibre after ultra-high molecular weight polyethylene dispersion liquid impregnation, And the average grain diameter of polyvinyl resin with super-high molecular weight is 0.1 μm, and the molecular weight of ultra-high molecular weight polyethylene is 4,800,000, is broken Splitting elongation is 3%;Lubricant is silicone powder, white oil, silicone oil, paraffin mix;Antioxidant is four [β-(3,5- bis- tertiary fourths Base -4- hydroxy phenyl) propionic acid] pentaerythritol ester and phosphorous acid three (2,4- di-tert-butyl-phenyl) ester mix, and the two Weight part ratio is 2:3.
Embodiment 5:
The present embodiment nylon composite is made of raw material from the following weight:70 parts of nylon, 6,4 parts of nylon66 fibers, 3 parts of poly- second Alkene grafted maleic anhydride, 45 parts of modified with ultrahigh molecular weight polyethylene glass fibres, 5 parts of odor adsorption master batches, 0.4 part of silicon carbide, 1 Part lubricant, 1 part of antioxidant;
The preparation method of the present embodiment nylon composite, includes the following steps:
S1, it will be immersed in ultra-high molecular weight polyethylene dispersion liquid after glass fibre cleaning, drying, take out drying and 200 It DEG C bakes and banks up with earth, be sintered, modified with ultrahigh molecular weight polyethylene glass fibre is made;
S2, each raw material for weighing parts by weight, nylon 6, nylon66 fiber, Research of Grafting Malaic Anhydride Onto Polyethylene, odor adsorption is female Grain, silicon carbide, lubricant and antioxidant pour into blender, stir evenly and are placed in double screw extruder, by supra polymer Weight polyethylene modified glass fibre is added from the glass fiber opening of double screw extruder, is granulated after melting extrusion.
Wherein, area's temperature of double screw extruder is 180 DEG C, two area's temperature are 180 DEG C, three area's temperature are 190 DEG C, four Area's temperature is 210 DEG C, five area's temperature are 230 DEG C, six area's temperature are 245 DEG C;Twin-screw engine speed is 500rpm.
Wherein, 6 melting means of nylon is 8g/10min, and the nylon66 fiber melting means is 10g/10min;Ultra-high molecular weight polyethylene changes Property glass fibre be modified with ultrahigh molecular weight polyethylene glass fibre after ultra-high molecular weight polyethylene dispersion liquid impregnation, And the average grain diameter of polyvinyl resin with super-high molecular weight is 0.2 μm, and the molecular weight of ultra-high molecular weight polyethylene is 4,800,000, is broken Splitting elongation is 10%;Lubricant is silicone powder, paraffin, stearic acid, zinc stearate mix;Antioxidant is four [β-(3,5- Di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester and phosphorous acid three (2,4- di-tert-butyl-phenyl) ester mix, and The weight part ratio of the two is 1:1.
Comparative example:
Common activated carbon of sorbent, the poly- molybdenum disulfide of common anti-wear agent, by 70 parts of Buddhist nuns are added in this comparative example raw material Dragon 6,3 parts, 5 parts molybdenum disulfide of active carbon, 1 part of silicone powder, 0.5 part of antioxidant, 1098,0.5 parts of irgasfos 168s pour into high-speed stirring It mixes in machine, high-speed stirred, mixes to adding twin-screw extrude after uniformly, 25 parts of glass fibre is added from glass fiber opening, warp It is granulated after melting extrusion.
Wherein area's temperature of double screw extruder is 180 DEG C, two area's temperature are 180 DEG C, three area's temperature are 190 DEG C, four Area's temperature is 210 DEG C, five area's temperature are 230 DEG C, six area's temperature are 245 DEG C;Twin-screw engine speed is 500rpm.
To nylon composite prepared by above-described embodiment 1-3 and comparative example 1, detect respectively its mechanical property, oder levels, TVOC and wear-resisting property.Wherein mechanical property is detected using ASTM standard, and oder levels, TVOC are carried out using GMW standard Detection, wear-resisting property are measured according to standard GB/T 5478-2008, and physical data see the table below 1.
The different properties of sample test results of table 1
As can be seen from Table 1, addition odor adsorption master batch can be obviously improved the smell and emission characteristics of material, make Low smell, high abrasion-resistance nylon composition TVOC are lower than 50ugC/g.In addition, the abrasion index of products of the present invention is extremely low, it is in Excellent wear-resisting property is revealed.The glass fibre of institute's impregnation of the present invention significantly improves glass in the dispersion of nylon matrix Property, make low smell, it is low distribute, high abrasion-resistance nylon composition have anti-wear agent additive amount it is few, wear-resisting protrusion, mechanical property significantly changes Kind advantage.
In conclusion 6 melting means of nylon is 5-8g/10min in the raw material of nylon composite of the present invention, nylon66 fiber melting means is 8-10g/10min can adjust the mobility of 6 melt of nylon after being added, guarantee that nylon 6 is plasticized uniformly in process, Melting mixing is smooth, and raw material modified with ultrahigh molecular weight polyethylene glass fibre is using extraordinary ultra-high molecular weight polyethylene dispersion liquid pair Glass fibre progress impregnation avoids glass fiber impregnated dipping in the process not exclusively, and the situation of disconnected fibre occurs in fiber, greatly Improve glass in the dispersibility of nylon matrix, and have nylon composite obtained in terms of wear-resisting property and significantly mention Height, and maintain excellent mechanical property;
Ultra-high molecular weight polyethylene molecular weight is 4,800,000, elongation at break 3%-10% in the present invention, using this powder Last particle avoids the fiber impregnation inefficient occurred during fiber impregnation, and not exclusively, the technologies such as disconnected fibre occurs to dipping in fiber The appearance of problem;
The dosage of raw material silicon carbide of the present invention is down to 0.1-0.5 parts, and the silicon carbide of low dosage had both avoided a large amount of uses and made At nylon combination physical performance decline, in turn ensure the synergistic effect that silicon carbide plays nylon composite wear-resisting property, improve The wear-resisting property of nylon composite;
Odor adsorption master batch of the present invention uses crystallinity 80%, the high density polyethylene (HDPE) that molecular weight is 300,000 as matrix, When as gas absorption master batch, the compatibility of itself and fiber, nylon is improved, ensure that dispersion of the master batch in composition system Property, into ensure that the low odor profiles of nylon composite;Odor adsorption master batch reduces the small molecule content in composition, makes always to volatilize Property organic matter TVOC significantly reduce, and while guaranteeing composition low odor characteristics, every physical and mechanical property, material Moulding processability it is unaffected;
Use area's temperature of double screw extruder for 180-190 DEG C, 2nd area in nylon composite preparation method of the present invention Temperature is 180-190 DEG C, three area's temperature are 190-200 DEG C, four area's temperature are 210-220 DEG C, five area's temperature are 230-250 DEG C, Six area's temperature are 245-250 DEG C;Twin-screw engine speed is 500rpm, and such processing temperature, engine speed make nylon combination The advantages of object blocks at the charging that process is not in, and has feeding saturation, and plasticizing is uniform, not overflow.
It should be noted that the above embodiments are merely illustrative of the technical solutions of the present invention, rather than its limitations;Although ginseng According to previous embodiment, invention is explained in detail, those skilled in the art should understand that:It still can be with It modifies the technical solutions described in the foregoing embodiments or equivalent replacement of some of the technical features;And These are modified or replaceed, the spirit and model of technical solution of various embodiments of the present invention that it does not separate the essence of the corresponding technical solution It encloses.

Claims (10)

1. a kind of nylon composite, which is characterized in that the nylon composite is made of raw material from the following weight:54-90 parts Nylon 6,1-5 part nylon66 fiber, 1-5 parts of Research of Grafting Malaic Anhydride Onto Polyethylene, 5-45 parts of modified with ultrahigh molecular weight polyethylene glass fibres, 1-5 parts of odor adsorption master batches, 0.1-0.5 parts of silicon carbide, 0.2-1 parts of lubricants, 0.1-1 parts of antioxidant.
2. nylon composite according to claim 1, it is characterised in that:6 melting means of nylon is 5-8 g/10min, institute Stating nylon66 fiber melting means is 8-10 g/10min.
3. nylon composite according to claim 1, it is characterised in that:The odor adsorption master batch is by high-density polyethylene Alkene, hydrophobicity diatomite, hydrophobic active charcoal, needle-shaped zeolite molecular sieve, zinc ricinate, nano silica, calcium stearate, Melamine is uniformly mixed, then extruding pelletization forms in double screw extruder.
4. nylon composite according to claim 1, it is characterised in that:The modified with ultrahigh molecular weight polyethylene glass fibers Dimension is the modified with ultrahigh molecular weight polyethylene glass fibre after ultra-high molecular weight polyethylene dispersion liquid impregnation, and superelevation is divided The molecular weight of sub- weight northylen is 4,800,000, elongation at break 3%-10%.
5. nylon composite according to claim 1, it is characterised in that:The high density polyethylene (HDPE) crystallinity 80%, molecule Amount is 300,000.
6. nylon composite according to claim 4, it is characterised in that:The ultra-high molecular weight polyethylene dispersion liquid is flat The polyvinyl resin with super-high molecular weight that equal partial size is 0.1-0.2 μm is suspended in the colloidal solution formed in liquid water, and colloid is molten The viscosity of liquid is 0.05Pas, concentration 60wt%.
7. nylon composite according to claim 1, it is characterised in that:The lubricant be silicone powder, white oil, silicone oil, At least one of paraffin, stearic acid, zinc stearate.
8. nylon composite according to claim 1, it is characterised in that:The antioxidant is four [β-(3,5- bis- tertiary fourths Base -4- hydroxy phenyl)Propionic acid] pentaerythritol ester and phosphorous acid three (2,4- di-tert-butyl-phenyl) ester mix, and the two Weight part ratio is 2:3-1:1.
9. a kind of preparation method of the nylon composite as described in any in claim 1-8, which is characterized in that including following step Suddenly:
S1, it will be immersed in ultra-high molecular weight polyethylene dispersion liquid after glass fibre cleaning, drying, take out drying and in 190-210 It DEG C bakes and banks up with earth, be sintered, modified with ultrahigh molecular weight polyethylene glass fibre is made;
S2, each raw material for weighing parts by weight, by nylon 6, nylon66 fiber, Research of Grafting Malaic Anhydride Onto Polyethylene, odor adsorption master batch, carbon SiClx, lubricant and antioxidant pour into blender, stir evenly and are placed in double screw extruder, by superhigh molecular weight polyethylene Alkene modified glass-fiber is added from the glass fiber opening of double screw extruder, is granulated after melting extrusion.
10. preparation method according to claim 9, it is characterised in that:One area's temperature of double screw extruder described in step S2 Degree is 180-190 DEG C, two area's temperature are 180-190 DEG C, three area's temperature are 190-200 DEG C, four area's temperature are 210-220 DEG C, five Area's temperature is 230-250 DEG C, six area's temperature are 245-250 DEG C;Twin-screw engine speed is 500rpm.
CN201710380891.1A 2017-05-25 2017-05-25 A kind of nylon composite and preparation method thereof Withdrawn CN108929538A (en)

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Application publication date: 20181204