CN1354201A - Preparation method of polyamide nano-composite-material - Google Patents
Preparation method of polyamide nano-composite-material Download PDFInfo
- Publication number
- CN1354201A CN1354201A CN01138007A CN01138007A CN1354201A CN 1354201 A CN1354201 A CN 1354201A CN 01138007 A CN01138007 A CN 01138007A CN 01138007 A CN01138007 A CN 01138007A CN 1354201 A CN1354201 A CN 1354201A
- Authority
- CN
- China
- Prior art keywords
- preparation
- composite
- polyamide
- nano
- screw extruder
- 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.)
- Granted
Links
Landscapes
- Polyamides (AREA)
Abstract
The present invention adopts one-step reaction extrusion technique to obtain polyamide nano composite material, and is characterized by that the montmorillonite treated by intercalation and caprolactam monomer and mixed, then reacted and extruded in double screw extruder so as to prepare high-performance nylon 6 and montmorillonite composite nano material. Said composite material possesses extensive application range.
Description
Technical field: the invention belongs to the polymer new material technology field, be specifically related to a kind of preparation method of polyamide nano-composite.
Background technology: traditional nylon 6 working methods are to be initiator with water, the hexanolactam ring-opening polymerization.The general tubular reactor (being the VK pipe) that adopts is finished the successive polymerization of so-called hydrolysis normal pressure, produces the nylon 6 slice with certain molecular weight and molecular weight distribution, and relative viscosity is 2.2～2.6, and the reaction times is 10～30hr, uses for general weaving.But some high-tenacity industry silk and engineering plastics require 2.8～3.5 with the relative viscosity of nylon 6, and general VK pipe normal pressure continuous polymerization is beyond one's reach, and must adopt more advanced polymerization technique and equipment.
The nylon nano matrix material be with Inorganic Fillers Filled in nylon 6, make that nylon dimensional stability height, rigidity improve, thermal characteristics improves, but impact property descends to some extent.The adding of nano material has two kinds of methods: with nanoparticle and polymer blending extrusion molding; Nanoparticle added in the polymer monomer carry out polymerization after fully disperseing, obtain nano composite material.
All the research that nylon 6 catalyzer are extruded in the narration reaction among U.S. Pat 5264541, US5290747, the US5298594, and many improvements have been done, relate generally to catalyzer such as isocyanates, carbonates, prepared nylon 6 relative viscosities are about 3.5.
Narrated the polymer composites that contains oxygen phenoxyl ether polyester polymers matrix among the CN1212716A, be suitable for the organic amine compound modified clay mineral as the organic inorganic materials of parent.
Narrated among the CN1138593A and a kind ofly produced nylon 6/ nano composite material with the intercalation polymeric method.It combines with polyamide substrate by the layered silicate Coulomb's force, and nanoparticle is dispersed in the polymeric amide with nanoscale, gets the high-performance nanometer composite polyamide-clay material.
" engineering plastics application " 1999.27 (12) .1-3 have reported preparation nylon 6/ Nano composite material of montmorillonite.It utilizes cation exchange reaction to embed the long-chain organic cation at the interlayer of polynite, and blend in twin screw extruder makes nano composite material with nylon and organic modification montmonrillonite.
Summary of the invention: the objective of the invention is to propose a kind of employing reaction extrusion molding make have higher draw tensile strength, flexural strength and modulus in flexure, especially its shock strength is apparently higher than the preparation method of the polyamide nano-composite of other material of the same type.
The present invention adopts the high performance nylon nano matrix material of reactive extrusion technology one step preparation.Reaction is extruded and is suitable for twin screw extruder as polymerization reactor, raw material mainly comprises monomer of polyamide, polynite, dispersion agent and anionic initiator, enter twin screw extruder after treatment, polymerization reaction time 1～20min, 200～300 ℃ of temperature of reaction, generally at reaction times 2～5min, 230～260 ℃ of temperature of reaction.Polymkeric substance is through pelletizing, cooling, the dry finished product nylon 6/nanometer advanced composite material that gets.This nano composite material must detect and the thermal property detection through mechanical property.
Reaction extrusion molding provided by the invention, be about to 100 parts of monomer of polyamide and dispersion agent 0.1-20 part, polynite 0.1-50 part and carry out pre-treatment, 100～180 ℃ of pressure range-0.1～1.0Mpa, temperature, jitter time is 0.5～3hr, then fully scattered mixture enters twin screw extruder, be metered into ionic initiator simultaneously, both proportionings are 0.01～2%.Monomer of polyamide generation ring-opening reaction, and carry out transfer reaction fast, form uniform dispersion system with polynite, thereby obtain the high performance nylon 6/nanometer advanced composite material of high-molecular weight.
The monomer of polyamide that the present invention is suitable for is hexanolactam, spicy inner formyl amine, laurolactam, diamine diacid salt.All available industrial-grade monomer is as raw material.
The polynite that the present invention is suitable for be smectite content 83～99%, through amine salt and other tradable ion processing, interlamellar spacing is between 1nm～4nm, feed particles order number is at 200～600 orders.Polynite by being delaminated into the nano-grade thing, is dispersed in the polymkeric substance in polymerization process uniformly, thereby improves every performance of polymkeric substance greatly.
The twin screw extruder that the present invention is suitable for, its length-to-diameter ratio are 20-60, and cylindrical shell is a bimetallic material, leave a plurality of exhausts and processing mouth, the left-hand thread combination block is wherein arranged in the threaded block, and have high rotational speed, rotating speed is 50～600 rev/mins, and solid, liquid can add simultaneously.
The dispersion agent that the present invention is used mainly is water, alcohols, tensio-active agent, acids, bases, reaches energy uniform distribution in the polymkeric substance to promote polynite in monomer, and delaminates into nanometer particle.
Initiator of the present invention mainly is isocyanates, particularly HDI, TDI, MDI etc.Ester class such as diphenyl carbonate, dimethyl terephthalate (DMT) etc.Amides such as N-ethanoyl hexanolactam, amino hexanolactam.Polymerization reaction time is short, and polymericular weight is easy to control etc.
Nylon 6 nano-composite involved in the present invention be adopt the reaction extrusion molding to make to have higher draw tensile strength, flexural strength and modulus in flexure, especially its shock strength be apparently higher than other material of the same type.This material is widely used in fields such as electronics, machinery, food product pack, automobile, conveying belt.
Embodiment: the present invention is described in detail below in conjunction with embodiment.
Example 1
With caprolactam monomer 1000g, polynite 15g, dispersion agent 15g in reactor, vacuum condition is fully reaction dispersion down, the reaction jitter time is 2hr, the reaction dispersion temperature is 140 ℃, the material that will react scattered is squeezed into twin screw extruder with volume pump then, and initiator is squeezed in metering simultaneously, and both ratios were at 1000: 4, mixture reacts 3min, discharging in twin screw extruder.Through cool off, dry up, pelletizing, dry nylon 6/ nano composite material, material reaches nanoscale through X-ray diffraction, and homodisperse.Mechanical property result is as follows: tensile strength 86.3MPa, elongation at break 164.9%, flexural strength 145.7MPa, modulus in flexure 1650MPa, notched Izod impact strength 19.3KJ/m
2
Example 2
With caprolactam monomer 1000g, polynite 25g, dispersion agent 15g in reactor, vacuum condition is fully reaction dispersion down, the reaction jitter time is 2hr, the reaction dispersion temperature is 140 ℃, the material that will react scattered is squeezed into twin screw extruder with volume pump then, and initiator is squeezed in metering simultaneously, and both ratios were at 1000: 5, mixture reacts 4min, discharging in twin screw extruder.Through cool off, dry up, pelletizing, dry nylon 6/ nano composite material, material is to reach nanoscale through X-ray diffraction, and homodisperse.Mechanical property result is as follows: tensile strength 89.6MPa, elongation at break 142.5%, flexural strength 150.7MPa, modulus in flexure 1786MPa, notched Izod impact strength 16.6KJ/m
2
Claims (6)
1, a kind of preparation method of polyamide nano-composite; Adopt the high performance nylon nano matrix material of reactive extrusion technology one step preparation; It is characterized in that reacting extruding and be suitable for twin screw extruder as polymerization reactor, 100 parts of monomer of polyamide and dispersion agent 0.1-20 part, polynite 0.1-50 part are carried out pre-treatment, 100～180 ℃ of pressure-0.1～1.0Mpa, temperature, jitter time is 0.5～3hr, then fully scattered mixture enters twin screw extruder, be metered into ionic initiator simultaneously, both proportionings are 0.01～2%, polymerization reaction time 1～20min, 200～300 ℃ of temperature of reaction, polymkeric substance is through pelletizing, cooling, the dry finished product that gets.
2, a kind of preparation method of polyamide nano-composite as claimed in claim 1 is characterized in that the twin screw extruder that is suitable for, and its length-to-diameter ratio is 20-60, and rotating speed is 50～600 rev/mins, and solid, liquid can add simultaneously.
3, a kind of preparation method of polyamide nano-composite as claimed in claim 1 is characterized in that monomer of polyamide is hexanolactam, laurolactam, butyrolactam.
4, a kind of preparation method of polyamide nano-composite as claimed in claim 1, it is characterized in that smectite content is in 85～99% polynite, granular size is between 200～600 orders, and interlamellar spacing is between 1nm～4nm, and interlayer is through the polynite of cationic exchange.
5, a kind of preparation method of polyamide nano-composite as claimed in claim 1 is characterized in that dispersion agent is water, alcohols, tensio-active agent, acids, bases.
6, a kind of preparation method of polyamide nano-composite as claimed in claim 1 is characterized in that initiator is isocyanates, ester class, acyl caprolactam.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011380071A CN1155661C (en) | 2001-12-20 | 2001-12-20 | Preparation method of polyamide nano-composite-material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011380071A CN1155661C (en) | 2001-12-20 | 2001-12-20 | Preparation method of polyamide nano-composite-material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1354201A true CN1354201A (en) | 2002-06-19 |
| CN1155661C CN1155661C (en) | 2004-06-30 |
Family
ID=4674302
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB011380071A Expired - Fee Related CN1155661C (en) | 2001-12-20 | 2001-12-20 | Preparation method of polyamide nano-composite-material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1155661C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100386384C (en) * | 2003-09-03 | 2008-05-07 | 中国科学院长春应用化学研究所 | Detaching type polymer/montmorillonite composite material and preparing method thereof |
| CN100439082C (en) * | 2003-12-26 | 2008-12-03 | 南化集团研究院 | Method for preparing glass fiber reinforced nylon 6 material |
| CN101016411B (en) * | 2006-08-21 | 2010-05-12 | 中国神马集团有限责任公司 | On-line modified producing method for engineering plastics |
| CN101544758B (en) * | 2009-05-04 | 2011-05-11 | 肖金亭 | Microwave radiation polymerization method for polyamide |
| CN101564874B (en) * | 2009-05-27 | 2012-07-04 | 靳柱山 | Method for preparing nanometer heat-insulation composite material |
| WO2019127417A1 (en) * | 2017-12-27 | 2019-07-04 | 上海锦湖日丽塑料有限公司 | High-strength and easy-to-electroplate polyamide composite material and preparation method therefor |
-
2001
- 2001-12-20 CN CNB011380071A patent/CN1155661C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100386384C (en) * | 2003-09-03 | 2008-05-07 | 中国科学院长春应用化学研究所 | Detaching type polymer/montmorillonite composite material and preparing method thereof |
| CN100439082C (en) * | 2003-12-26 | 2008-12-03 | 南化集团研究院 | Method for preparing glass fiber reinforced nylon 6 material |
| CN101016411B (en) * | 2006-08-21 | 2010-05-12 | 中国神马集团有限责任公司 | On-line modified producing method for engineering plastics |
| CN101544758B (en) * | 2009-05-04 | 2011-05-11 | 肖金亭 | Microwave radiation polymerization method for polyamide |
| CN101564874B (en) * | 2009-05-27 | 2012-07-04 | 靳柱山 | Method for preparing nanometer heat-insulation composite material |
| WO2019127417A1 (en) * | 2017-12-27 | 2019-07-04 | 上海锦湖日丽塑料有限公司 | High-strength and easy-to-electroplate polyamide composite material and preparation method therefor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1155661C (en) | 2004-06-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR100689210B1 (en) | High-viscous moulding materials with nano-scale fillers | |
| CN101074316A (en) | Production of super-toughened fire-retardant composite modified nylon mother material | |
| CN1081207C (en) | Nanometer composite polyamide-clay material and its preparation | |
| CN1155661C (en) | Preparation method of polyamide nano-composite-material | |
| CN103937232A (en) | Method for preparing montmorillonite nylon 6 composite material | |
| CN101735448A (en) | Method for preparing polyamide-6 nano composite material | |
| CN106751783A (en) | High visocity nylon 6 composite prepared by a kind of melting extrusion chain extending reaction and preparation method thereof | |
| CN1263802C (en) | Polyester/lamellar silicate nano composite material and preparation method thereof | |
| CN1215741A (en) | Potassium titanate crystal whisker reinforced polyimide composite material | |
| CN108976782B (en) | Hyperbranched epoxy resin modified nylon composite material and preparation method thereof | |
| CN1436205A (en) | Method for producing nanoreinforced thermoplastic polymers | |
| US11440231B2 (en) | Process for the preparation of a reinforced polyamide by extrusion | |
| CN1546552A (en) | Semi-continuous preparation method of poly p-phenylene terephthalamide resin | |
| CN1359979A (en) | Process for preparing nylon 6/montmorillonite composite | |
| CN112745667B (en) | Composite reinforced nylon material and preparation method thereof | |
| CN1169861C (en) | Semi-continuous direct polycondensation preparation of p-aramid pulp | |
| CN1422898A (en) | Degradable polymer/natural mineal filler composite material and preparation method thereof | |
| CN101402751B (en) | Resin composite material and method of producing the same | |
| CN1384130A (en) | Prepn process of nano composite polymer/laminated silicate material | |
| CN102675639B (en) | Polyetherimide product and method for preparing same | |
| CN114031939A (en) | Nylon/titanic acid nanosheet composite material and preparation method thereof | |
| KR100522137B1 (en) | A method for preparing polymer / clay nanocomposites by using reactive extrusion | |
| CN1284827C (en) | Master batch of polyamide/rectorite nano composite materials and method for preparing same | |
| CN113004686A (en) | Nylon biomass composite material and preparation method thereof | |
| CN1127534C (en) | Polyamide/silicate nanometer composite material and its preparation method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |