CN104987526B - Composite foamed particle of polypropylene-based resin and preparation method and application - Google Patents

Composite foamed particle of polypropylene-based resin and preparation method and application Download PDF

Info

Publication number
CN104987526B
CN104987526B CN201510205097.4A CN201510205097A CN104987526B CN 104987526 B CN104987526 B CN 104987526B CN 201510205097 A CN201510205097 A CN 201510205097A CN 104987526 B CN104987526 B CN 104987526B
Authority
CN
China
Prior art keywords
polypropylene
particle
resin
based resin
composite foamed
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.)
Active
Application number
CN201510205097.4A
Other languages
Chinese (zh)
Other versions
CN104987526A (en
Inventor
唐涛
邢海平
邱健
姜治伟
谭海英
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Changchun Institute of Applied Chemistry of CAS
Original Assignee
Changchun Institute of Applied Chemistry of CAS
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Changchun Institute of Applied Chemistry of CAS filed Critical Changchun Institute of Applied Chemistry of CAS
Priority to CN201510205097.4A priority Critical patent/CN104987526B/en
Publication of CN104987526A publication Critical patent/CN104987526A/en
Application granted granted Critical
Publication of CN104987526B publication Critical patent/CN104987526B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

The invention discloses composite foamed particle of a kind of polypropylene-based resin and preparation method and application, belong to expanded material technical field.The technical problem that briquetting pressure is high, and preparation cost is high, molding cycle is grown is solved in the composite foamed granule die of polypropylene-based resin in the prior art.The expanded beads, medium method for releasing is dispersed through by blending resin particle and is prepared, the cell diameter of expanded beads increases successively from the inside to the outside, cortex mean cell diameter Rs and sandwich layer mean cell diameter R0Meet following relational expressions:1≤Rs/R0≤5;Wherein, blending resin particle contains matrix resin and inorganic interleaving agent, and the mass fraction of inorganic interleaving agent is 1 20%, and matrix resin is polypropylene-based resin, and inorganic interleaving agent is laminated inorganic matter.Steam consumption can be greatly reduced by preparing expanded moldings using the expanded beads of the present invention, shortened molding cycle, reduced the cost of preparation, and obtained expanded moldings surface is smooth, pliability is excellent.

Description

Composite foamed particle of polypropylene-based resin and preparation method and application
Technical field
The invention belongs to expanded material technical field, and in particular to a kind of composite foamed particle of polypropylene-based resin and its system Preparation Method and application.
Background technology
The expanded bead molding that polypropylene-based resin is formed is due to good cushioning ability and heat resistance, in recent years Come, the application in automotive field, electronic product packaging field is more and more extensive.But the fusing point of polypropylene-based resin is higher, is In in-molded polypropylene resin foam particle, it is necessary at least 0.4Mpa water vapor pressure, 10-40kg vapor Amount.With environmental requirement more and more higher, the use of coal-burning boiler has become increasingly limited, and the consumption of vapor also results in The production cost more and more higher for the expanded bead molding that polypropylene-based resin is formed, in addition, in-molded polypropylene-based resin The molding cycle of expanded beads is longer.So need the PP composite material that a kind of in-molded time is short, briquetting pressure is small badly Expanded beads.
The content of the invention
Present invention aim to address the in-molded pressure height of PP composite material expanded beads in the prior art, prepare Cost is high, the technical problem of molding cycle length, there is provided a kind of composite foamed particle of polypropylene-based resin and preparation method thereof is with answering With.
It is as follows that the present invention solves the technical scheme that above-mentioned technical problem uses.
The composite foamed particle of polypropylene-based resin, medium method for releasing is dispersed through by blending resin particle and is prepared;
The cell diameter of the expanded beads increases successively from the inside to the outside, cortex mean cell diameter Rs and sandwich layer average bubble Bore dia R0Meet following relational expressions:1≤Rs/R0≤5;
The blending resin particle is cylindrical structural, a diameter of 0.5-2mm, highly 1-2 times for diameter, blending resin Containing matrix resin and inorganic interleaving agent in particle, matrix resin is polypropylene-based resin, and inorganic interleaving agent is laminated inorganic matter, The mass percent of inorganic interleaving agent is 1-20%.
Preferably, the polypropylene-based resin is ethylene-propylene random copolymer, the random copolymer of propene-1-butene -1, second One or more mixing in alkene-random copolymer of propene-1-butene -1.
Preferably, additive is also contained in the blending resin particle, the additive is toughener, antioxidant, anti-purple It is one or more in outside line agent, antistatic additive, fire retardant, matal deactivator, pigment, dyestuff, nucleator, bladder regulator The mass ratio of mixing, matrix resin and additive is 100:(0.1-30).
Preferably, the toughener is one or more mixing in PP-g-MA, POE-g-MA, PE-g-MA, described Bladder regulator is one or more mixing in Firebrake ZB, talcum powder, calcium carbonate, aluminium hydroxide.
Preferably, the inorganic interleaving agent is montmorillonite, mica, kaolin, graphene, one kind in lamellar graphite or more The mixing of kind.
Preferably, the cortex mean cell diameter Rs and sandwich layer mean cell diameter R0Meet following relational expressions:1.2≤ Rs/R0≤3。
The preparation method of the above-mentioned composite foamed particle of polypropylene-based resin, comprises the following steps:
Step 1: after matrix resin and inorganic interleaving agent are well mixed, add in extruder, co-extrusion is melted with wire Go out, cooling, pelletizing, obtain blending resin particle;
When also containing additive in blending resin particle, additive, matrix resin and inorganic interleaving agent are well mixed Afterwards, add in extruder, melted and be coextruded with wire, cooling, pelletizing, obtain blending resin particle;
Step 2: blending resin particle, foaming agent, surfactant, dispersant and decentralized medium are added into closed container In, temperature of low 5-10 DEG C than blowing temperature is heated under stirring, 10-60min is incubated, blowing temperature is warming up to, in constant temperature Continue to be incubated 15-60min under degree, open closed container, by blending resin particle, foaming agent, surfactant, dispersant and divide Dispersion media is discharged under the environment lower than the pressure in closed container, foaming, obtains the composite foamed particle of polypropylene-based resin;
The blowing temperature is the blowing temperature of matrix resin in blending resin particle;
The blending resin particle, surfactant, the weight part ratio of dispersant and decentralized medium are 100:(0.0001- 0.5):(0.1-15):(100-500);
The pressure of foaming agent is 0.6-6MPa in the closed container.
Preferably, the foaming agent is propane, butane, hexane, heptane, cyclobutane, hexamethylene, chlorofluoromethane, fluoroform Alkane, 1,2- Difluoroethanes, HFA 134a, monochloro methane, chloroethanes, dichloromethane, nitrogen, oxygen, air, carbon dioxide In one or more mixing.
The application of the above-mentioned composite foamed particle of polypropylene-based resin, it is that the composite foamed particle of polypropylene-based resin is placed in mould It is in-molded in tool, obtain expanded moldings, the in-molded pressure with the expanded beads mould of corresponding matrix resin The pressure of shaping is identical, and the in-molded vapor dosage water in-molded less than the expanded beads of corresponding matrix resin steams Gas dosage, in-molded cycle are shorter than the expanded beads in-molded cycle of corresponding matrix resin.
Preferably, the in-molded pressure of the composite foamed particle of the polypropylene-based resin is 0.28-0.46MPa (G), The in-molded cycle is 100-140s, and the consumption of in-molded vapor is 20-35kg/kg.
Compared with prior art, the beneficial effects of the invention are as follows:
1st, the composite foamed particle of polypropylene-based resin of the invention, is by containing polypropylene-based resin and inorganic interleaving agent Blending resin particle, foam and form in the presence of foaming agent, because the presence of inorganic interleaving agent have impact on the infiltration of foaming agent Property, cause foaming agent radial distribution in blending resin particle to be present, i.e. foaming agent is higher than in blending resin particle surface concentration Blending resin granular center, by controlling foaming condition to control the time of penetration of blending resin particle and foaming agent, it can obtain Blending resin particle with the distribution of density of foaming agent gradient, then by discharging foaming agent and blending resin particle to normal pressure Under, so as to obtain the expanded beads of the present invention, there is excellent amalgamation between expanded beads of the invention;
2nd, the preparation method of the composite foamed particle of polypropylene-based resin of the invention is simple, easily operation;
3rd, the composite foamed particle of polypropylene-based resin of the invention, general forming machine can be used to be molded, in-molded When, because the cell diameter of expanded beads outer layer is big, cell wall is thin, reduces the steam of expanded beads bonding needs, shaping week Phase shortens, so polypropylene resin foam formed body, which is made, by the expanded beads can greatly reduce steam consumption, steam Consumption is 20-35kg/kg, shortening molding cycle, molding cycle 100-140s, reduces the cost of preparation, obtained foaming Formed body surface is smooth, pliability is excellent, is suitable for various packaging materials, padded coaming etc..
Brief description of the drawings
Fig. 1 is the electron scanning micrograph of the blending resin particle section of the embodiment of the present invention 1.
Embodiment
In order to further appreciate that the present invention, the preferred embodiments of the invention are retouched with reference to embodiment State, but it is to be understood that these descriptions are simply for further explanation the features and advantages of the present invention rather than to patent of the present invention It is required that limitation.
The composite foamed particle of polypropylene-based resin, medium method for releasing is dispersed through by blending resin particle and is prepared, this is multiple The cell diameter for closing expanded beads increases successively from the inside to the outside, cortex mean cell diameter Rs and sandwich layer mean cell diameter R0It is full Foot states relational expression:1≤Rs/R0≤ 5, as 1≤Rs/R0<When 1.2, because expanded beads cortex cell diameter and sandwich layer abscess are straight Connect that difference is smaller, it is not fairly obvious to shorten molding cycle and reduce the effect of steam consumption, when 3<Rs/R0When≤5, skin foaming Particle cortex cell diameter is excessive, and cell wall is excessively thin, and easily being collapsed during vapor hot briquetting causes expanded moldings Dimensional discrepancy is excessive, and it is advantageous to 1.2≤Rs/R0≤ 3, by industrial general requirement, the particle diameter of composite foamed particle is generally 2- 5mm.Wherein, blending resin particle is cylindrical structural, a diameter of 0.5-2mm, highly 1-2 times for diameter, blending resin Grain mainly contains matrix resin and inorganic interleaving agent, it is also possible to which, containing additive, the quality of inorganic interleaving agent accounts for blending resin The 1-20%, preferably 2-5% of grain gross mass.The composite foamed particle can be in the foaming of the matrix resin in blending resin particle Carried out under the in-molded pressure of particle in-molded, it is not necessary to improve pressure, shorten molding cycle, reduce steam consumption, one As in-molded pressure be 0.28-0.46MPa (G), steam consumption 20-35kg/kg, molding cycle 100-140s.
In above-mentioned matrix resin, polypropylene-based resin is those skilled in the art's common used material, ethylene-propylene random copolymerization Thing, the random copolymer of propene-1-butene -1, the random copolymer of ene-propylene-butene -1 etc., it can also be more that can use one kind The mixing of kind in any proportion.Additive can be toughener, antioxidant, ultraviolet screener, antistatic additive, fire retardant, metal Passivator, pigment, dyestuff, nucleator, bladder regulator etc..Wherein, toughener can be PP-g-MA, POE-g-MA, PE-g- MA etc.;Bladder regulator can be the inorganic powders such as Firebrake ZB, talcum powder, calcium carbonate, aluminium hydroxide.Specific additive and its use Measure and be modified typical additives and dosage for polypropylene-based resin, the mass ratio of general matrix resin and additive is 100: (0.1-30)。
Above-mentioned inorganic interleaving agent, it is laminated inorganic matter, it can also be a variety of mixing in any proportion that can use a kind of, Such as montmorillonite, mica, kaolin, graphene, lamellar graphite.
The preparation method of the above-mentioned composite foamed particle of polypropylene-based resin comprises the following steps:
Step 1: after matrix resin and inorganic interleaving agent are well mixed, add in extruder, co-extrusion is melted with wire Go out, cool down, pelletizing, obtain blending resin particle;
Wherein, the hybrid mode of matrix resin and inorganic interleaving agent does not limit, as long as well mixed, can such as adopt With solution mixing or mixing in situ;When also containing additive in blending resin particle, by additive, matrix resin and inorganic Interleaving agent mixes in the lump, or by matrix resin replace with it is additive agent modified after matrix resin, other operations are constant;
Extruder can be double screw extruder or single screw extrusion machine, and extrusion temperature is more than matrix resin fusing point Can;
Step 2: blending resin particle, foaming agent, surfactant, dispersant and decentralized medium are added in autoclave, The temperature of low 5-10 DEG C of the blowing temperature than the matrix resin in blending resin particle is heated under stirring, is incubated 10-60min, Soaking time is less than 10min, and foaming agent infiltration is poor, it is difficult to powerful expanded beads are obtained, soaking time is more than 60min, Foaming agent obtains osmotic equilibrium in resin particle, and expanded beads sandwich layer is identical with cortex cell diameter, cannot be of the invention Effect, is warming up to blowing temperature, continues at a constant temperature after being incubated 15-60min, foaming agent infiltration blending resin particle, beats Autoclave is driven, while more than vapour pressure of the pressure in autoclave in foaming agent is kept, by blending resin particle, foaming Agent, surfactant, dispersant and decentralized medium are discharged under the environment lower than the pressure in autoclave, are generally released to air In pressure ring border, foaming, the composite foamed particle of polypropylene-based resin is obtained.Wherein, decentralized medium is water or alcohols, from operation angle Degree consideration, preferably water.Surfactant is neopelex.Dispersant is kaolin, talcum powder, calcium carbonate, phosphoric acid Calcium, alkali calcium phosphate etc..Foaming agent can be organic system physical blowing agent, such as propane, butane, hexane, heptane aliphatic alkane Class, chlorofluoromethane, fluoroform, 1,2- Difluoroethanes, HFA 134a, monochloro methane, chloroethanes, dichloromethane etc. The annular aliphatic alkanes such as halo alkanes, cyclobutane, hexamethylene;Can also be inorganic system's physical blowing agent, as nitrogen, oxygen, air, Carbon dioxide etc.;Organic system physical blowing agent and inorganic system's physical blowing agent can also be used in combination;From being readily obtained low table From the point of view of the expanded beads for seeing density, the inorganic system preferably more than one or both of nitrogen, oxygen, air, carbon dioxide Physical blowing agent.Generally, the mass ratio of blending resin particle, surfactant, dispersant and decentralized medium is 100: (0.0001-0.5):(0.1-15):(100-500), the loading of the foaming agent in autoclave used in the species of foaming agent, The apparent density of blowing temperature and target expanded beads suitably selects, and typically under blowing temperature, ensures foaming agent in autoclave Pressure be 0.6-6MPa.It should be noted that usually require that the apparent density of expanded beads is smaller, the pressure in above-mentioned autoclave Power is higher, it is desirable to which the apparent density of target expanded beads is bigger, and the pressure in above-mentioned autoclave is lower.
The application of the above-mentioned composite foamed particle of polypropylene-based resin, it is that the composite foamed particle of polypropylene-based resin is placed in mould It is in-molded in tool, water cooling, until the face pressure of the formed body in mould reaches 0.030-0.039MPa (G), it is removed from the molds Formed body, 8-24h is maintained at 50-80 DEG C, is cooled to room temperature, obtains expanded moldings, wherein, in-molded pressure is together The pressure that the expanded beads of matrix resin in mixed resin particle are in-molded is identical, generally 0.28-0.46MPa (G), in mould The vapor dosage that the expanded beads of the more corresponding matrix resin of vapor dosage of shaping are in-molded reduces 5%-30%, disappears Consumption is typically only 20-35kg/kg, the in-molded cycle time of expanded beads of in-molded cycle more corresponding matrix resin 5%-30%, in-molded cycle are generally 100-140s, define the expanded beads of matrix resin by matrix resin body (poly- third Alkene system resin body) be dispersed through medium release foaming be prepared, compared with the present invention, that is, be added without inorganic interleaving agent, its His condition is all identical.
The composite foamed particle cortex mean cell diameter Rs of polypropylene-based resin of the present invention and sandwich layer mean cell diameter R0 Assay method it is as follows:An expanded beads are first bisected into two parts, amplifying its section under the microscope afterwards makes section complete Into shooting its section, as shown in Figure 1.According to its photo, straight line is drawn on photo makes section substantially be bisected into two parts, with straight The length of line does great circle as diameter, and the quantity divided by great circle circumference income value for all abscesses that great circle circumference passes through are as one The cortex mean cell diameter of individual expanded beads.Using the center of circle of great circle as the center of circle, make by diameter of a quarter of axis of great circle Roundlet, the quantity divided by roundlet circumference income value of all abscesses that roundlet circumference passes through are put down as the sandwich layer of an expanded beads Equal cell diameters.Identical operation is carried out to 20 expanded beads, average value of doing sums respectively is as cortex mean cell diameter Rs and sandwich layer mean cell diameter R0
With reference to embodiments and comparative example further illustrates the present invention.
Embodiment 1-15
The preparation of the composite foamed particle of polypropylene-based resin:
Step 1: by the composition and proportioning of Tables 1 and 2, the matrix resin of 100 parts by weight and inorganic is added into extruder Interleaving agent, melting extrusion, cooling, pelletizing obtain a diameter of 1mm, length 1.8mm, and average weight is 1.8mg blending resin Particle;
Step 2: the above-mentioned blending resin particle of 100 parts by weight (1000g), 300 parts by weight are added into 5L autoclave (carbon dioxide being filled with ensures hair for water, 0.05 parts by weight neopelex, 0.3 parts by weight kaolin clay and carbon dioxide Pressure at a temperature of bubble in autoclave is 6MPa), warming while stirring is to 5 DEG C lower than the blowing temperature of corresponding Tables 1 and 2 Temperature, 15min is incubated, blowing temperature and foamed time in Tables 1 and 2 is then respectively adopted, make foaming agent infiltration blending tree Fat particle, open autoclave, supply carbon dioxide into autoclave, keep pressure in autoclave foaming agent vapour pressure with While upper, under release blending resin particle, water, neopelex, kaolin and carbon dioxide to atmospheric pressure environment, Foaming, obtains composite foamed particle.
The composite foamed particle that embodiment 1-15 is obtained is washed respectively, centrifugation, is placed 24h under atmospheric pressure and is maintained Afterwards, the apparent density of expanded beads is determined, as a result as shown in Table 1 and Table 2.
The application of above-mentioned composite foamed particle:
Forming machine is using the small-scale forming machine for the saturated vapour pressure for being resistant to 0.48MPa (G), and mould is using tool There is the metal pattern of 100mm × 100mm × 50mm molding spaces.In the state of metal pattern leaves gap (about 5mm), by compound hair Particles filled into metal pattern, matched moulds is steeped, after discharging the air in metal pattern, embodiment 1-15 composite foamed particle is distinguished Apply the steam pressure of Tables 1 and 2, after in-molded, water cooling, until the face pressure of the formed body in metal pattern reaches 0.039MPa (G) formed body, is taken out from metal pattern, 24h is maintained at 80 DEG C, is cooled to room temperature, obtain expanded moldings.
Embodiment 1-15 molding cycles and vapor amounts specified and Tables 1 and 2, the hair obtained respectively to embodiment 1-15 Compressive strength, the outward appearance of bubble formed body are measured, as a result as shown in Table 1 and Table 2.
Comparative example 1-3
The preparation of the expanded beads of matrix resin:
Step 1: by the composition of table 2, matrix resin is added into extruder, melting extrusion, cooling, pelletizing, obtains diameter For 1mm, length 1.8mm, average weight is 1.8mg matrix resin particles;
Step 2: it is identical with the step of embodiment 1-15 two, obtain the expanded beads of matrix resin.
The expanded beads of the obtained matrix resins of comparative example 1-3 are washed respectively, centrifuged, 24h is placed under atmospheric pressure and enters After row maintenance, the apparent density of expanded beads is determined, as a result as shown in table 2.
The application of above-mentioned composite foamed particle:It is identical with embodiment 1-15.
Comparative example 1-3 molding cycles and vapor amounts specified and table 2, the foaming obtained respectively to comparative example 1-3 Compressive strength, the outward appearance of body are measured, as a result as shown in table 2.
Table 1 is embodiment 1-9 proportioning, condition of molding and testing result
Table 2 is embodiment 10-15 and comparative example 1-3 proportioning, condition of molding and testing result
In Tables 1 and 2, A represents ethylene-propylene random copolymer (140 DEG C of fusing point), and B represents propene-1-butene -1 randomly altogether Polymers (135 DEG C of fusing point), C represent the random copolymer of ene-propylene-butene -1 (146 DEG C).Molding cycle represents that shaping is produced per mould Time required for product, steam consumption represent the steam by weight required for every kilogram of expanded beads, expanded bead molding Outward appearance is characterized by the hollow number between the expanded beads in 100 expanded beads areas.Hollow between expanded beads at 50 with On be denoted as X, less than 50 at be denoted as O.
As can be seen from Table 1 and Table 2, embodiment 1-15 polypropylene-based resin composite foamed particle consumption water vapour amount with Corresponding comparative example 1-3 compares, and reduces 5%-30%, and molding cycle shortens 5%-30%.The water particularly consumed in embodiment 8 Vapor volume reduces 37% compared with comparative example 1.The steam vapour amount that embodiment 15 consumes reduces 20% compared with comparative example 3. Illustrate the expanded beads of the present invention, forming process reclaimed water steam consumption can be greatly reduced, shorten molding cycle.Wherein, it is real The expanded beads of example 9 are applied because expanded beads cortex cell diameter is excessive, cause end article degraded appearance, so the present invention is excellent Select 1.2≤Rs/R0≤3。
Obviously, the explanation of above example is only intended to help the method and its core concept for understanding the present invention.It should refer to Go out, under the premise without departing from the principles of the invention, can also be to this hair for the those of ordinary skill of the technical field Bright to carry out some improvement and modification, these are improved and modification is also fallen into the protection domain of the claims in the present invention.

Claims (8)

1. the composite foamed particle of polypropylene-based resin, it is characterised in that medium method for releasing is dispersed through by blending resin particle and prepared Form;
The cell diameter of the expanded beads increases successively from the inside to the outside, and cortex mean cell diameter Rs and sandwich layer Average Cell are straight Footpath R0Meet following relational expressions:1≤Rs/R0≤5;
The blending resin particle is cylindrical structural, a diameter of 0.5-2mm, highly 1-2 times for diameter, blending resin particle In contain matrix resin and inorganic interleaving agent, matrix resin is polypropylene-based resin, and inorganic interleaving agent is laminated inorganic matter, inorganic The mass percent of interleaving agent is 1-20%;
The inorganic interleaving agent is one or more mixing in montmorillonite, mica, kaolin, graphene, lamellar graphite.
2. the composite foamed particle of polypropylene-based resin according to claim 1, it is characterised in that the polypropylene-based resin For one in ethylene-propylene random copolymer, the random copolymer of propene-1-butene -1, the random copolymer of ene-propylene-butene -1 Kind or a variety of mixing.
3. the composite foamed particle of polypropylene-based resin according to claim 1, it is characterised in that the blending resin particle In also contain additive, the additive is toughener, antioxidant, ultraviolet screener, antistatic additive, fire retardant, metal passivation The mass ratio of one or more mixing in agent, pigment, dyestuff, nucleator, bladder regulator, matrix resin and additive is 100:(0.1-30)。
4. the composite foamed particle of polypropylene-based resin according to claim 3, it is characterised in that the toughener is PP- One or more mixing in g-MA, POE-g-MA, PE-g-MA, the bladder regulator are Firebrake ZB, talcum powder, carbonic acid One or more mixing in calcium, aluminium hydroxide.
5. the composite foamed particle of polypropylene-based resin according to claim 1, it is characterised in that the cortex Average Cell Diameter Rs and sandwich layer mean cell diameter R0Meet following relational expressions:1.2≤Rs/R0≤3。
6. the preparation method of the composite foamed particle of polypropylene-based resin described in claim 1-5 any one, it is characterised in that Comprise the following steps:
Step 1: after matrix resin and inorganic interleaving agent are well mixed, add in extruder, melted and be coextruded with wire, it is cold But, pelletizing, blending resin particle is obtained;
When also containing additive in blending resin particle, after additive, matrix resin and inorganic interleaving agent are well mixed, add Enter in extruder, melted and be coextruded with wire, cooling, pelletizing, obtain blending resin particle;
Step 2: blending resin particle, foaming agent, surfactant, dispersant and decentralized medium are added in closed container, stir Mix down and be heated to temperature of low 5-10 DEG C than blowing temperature, be incubated 10-60min, be warming up to blowing temperature, at a constant temperature after Continue insurance warm 15-60min, closed container is opened, by blending resin particle, foaming agent, surfactant, dispersant and decentralized medium It is discharged under the environment lower than the pressure in closed container, foams, obtain the composite foamed particle of polypropylene-based resin;
The blowing temperature is the blowing temperature of matrix resin in blending resin particle;
The blending resin particle, surfactant, the weight part ratio of dispersant and decentralized medium are 100:(0.0001-0.5): (0.1-15):(100-500);
The pressure of foaming agent is 0.6-6MPa in the closed container.
7. the preparation method of the composite foamed particle of polypropylene-based resin according to claim 6, it is characterised in that the hair Infusion be propane, butane, hexane, heptane, cyclobutane, hexamethylene, chlorofluoromethane, fluoroform, 1,2- Difluoroethanes, 1,1,1, One or more mixing in 2- HFC-134as, monochloro methane, chloroethanes, dichloromethane, nitrogen, oxygen, air, carbon dioxide.
8. the application of the composite foamed particle of polypropylene-based resin described in claim 1-5 any one, it is by polypropylene-based tree The composite foamed particle of fat is placed in mould, in-molded, obtains expanded moldings, it is characterised in that the in-molded pressure Power is identical with the pressure that the expanded beads of corresponding matrix resin are in-molded, and in-molded vapor dosage is less than corresponding The in-molded vapor dosage of the expanded beads of matrix resin, the in-molded cycle be shorter than corresponding to matrix resin foaming The grain in-molded cycle;
The in-molded pressure of the composite foamed particle of polypropylene-based resin is 0.28-0.46MPa (G), in-molded Cycle is 100-140s, and the consumption of in-molded vapor is 20-35kg/kg.
CN201510205097.4A 2015-04-27 2015-04-27 Composite foamed particle of polypropylene-based resin and preparation method and application Active CN104987526B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510205097.4A CN104987526B (en) 2015-04-27 2015-04-27 Composite foamed particle of polypropylene-based resin and preparation method and application

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510205097.4A CN104987526B (en) 2015-04-27 2015-04-27 Composite foamed particle of polypropylene-based resin and preparation method and application

Publications (2)

Publication Number Publication Date
CN104987526A CN104987526A (en) 2015-10-21
CN104987526B true CN104987526B (en) 2017-11-17

Family

ID=54299435

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510205097.4A Active CN104987526B (en) 2015-04-27 2015-04-27 Composite foamed particle of polypropylene-based resin and preparation method and application

Country Status (1)

Country Link
CN (1) CN104987526B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107353489B (en) * 2017-08-22 2019-09-13 中国科学院长春应用化学研究所 A kind of polyolefine resin sparkling material and preparation method thereof
CN107383636B (en) * 2017-08-22 2021-03-19 中国科学院长春应用化学研究所 Low-thermal-conductivity-coefficient foamed particles and preparation method thereof
CN107353427B (en) * 2017-08-22 2020-05-19 中国科学院长春应用化学研究所 Easily-filled resin foaming particles and preparation method thereof
CN109577017A (en) * 2017-09-28 2019-04-05 上海译科实业有限公司 A kind of foaming agent and preparation method thereof for synthetic leather
CN107880386A (en) * 2017-11-14 2018-04-06 东莞市鑫益电子科技有限公司 A kind of preparation method of nanometer particle-modified polypropylene material
CN109080060B (en) * 2018-07-25 2021-06-11 南通德亿新材料有限公司 Seamless forming process for thermoplastic elastomer foaming beads
CN112011127A (en) * 2020-09-10 2020-12-01 无锡会通轻质材料股份有限公司 Polypropylene expanded beads with different cell sizes and selectively distributed cells and preparation method thereof
CN112608555B (en) * 2020-12-14 2022-05-10 金发科技股份有限公司 Foaming agent master batch and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1647903A (en) * 2004-01-13 2005-08-03 株式会社Jsp Thermoplastic resin pellet, process for preparing thermoplastic resin pellets and expanded thermoplastic resin bead
CN101896543A (en) * 2007-12-11 2010-11-24 Kaneka株式会社 Process for producing expanded polyolefin resin bead and expanded polyolefin resin bead
CN103249537A (en) * 2010-12-15 2013-08-14 株式会社Jsp Process for producing molded body of expanded polyolefin resin particles, and molded body of expanded polyolefin resin particles

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8063177B2 (en) * 2007-10-11 2011-11-22 Kaneka Corporation Pre-expanded polypropylene resin particle, and method for production thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1647903A (en) * 2004-01-13 2005-08-03 株式会社Jsp Thermoplastic resin pellet, process for preparing thermoplastic resin pellets and expanded thermoplastic resin bead
CN101896543A (en) * 2007-12-11 2010-11-24 Kaneka株式会社 Process for producing expanded polyolefin resin bead and expanded polyolefin resin bead
CN103249537A (en) * 2010-12-15 2013-08-14 株式会社Jsp Process for producing molded body of expanded polyolefin resin particles, and molded body of expanded polyolefin resin particles

Also Published As

Publication number Publication date
CN104987526A (en) 2015-10-21

Similar Documents

Publication Publication Date Title
CN104987526B (en) Composite foamed particle of polypropylene-based resin and preparation method and application
CN104974370B (en) A kind of preparation method of thermoplastic polyurethane bead and the bead moulding process
TWI444417B (en) Polypropylene resin foamed beads and molded articles
US10221292B2 (en) Polypropylene resin foamed particles, in-mold foam molded body of polypropylene resin, and method for manufacturing same
CN112512771A (en) Biodegradable and industrially compostable injection molded microcellular flexible foam and method for producing the same
CN101962455B (en) Injection microcellular foamed wood-plastic composite material and preparation method thereof
CN103012832B (en) Preparation method of foamed polypropylene
CN103642200A (en) Foaming thermoplastic polyurethane bead and preparation method thereof
CN104877162B (en) The composite foamed particle of in-situ micro-fibril polypropylene-based resin and its application
CN101318383A (en) Manufacturing method of light wood-plastic composite panel
CN107835832A (en) Propylene resin expanded particle and expanded particle formed body
KR20060065717A (en) Method of manufacturing thermoplastic resin foam particle
CN104861195B (en) Fiber/polypropylene system resin compounded expanded beads and its application
CN105504330B (en) A kind of preparation method of expanded particle and its expanded particle being prepared and application
CN109501107A (en) A kind of low-density, polymer foams of high foamability and preparation method thereof
CN106674583A (en) Foamed polypropylene bead and preparation method thereof
CN107057303A (en) A kind of blending and modifying aromatic polyester microcellular foam material and preparation method thereof
CN109721851B (en) Light high-strength polypropylene foam material and preparation method and application thereof
CN107501595A (en) A kind of method of non-melt state expanded polypropylene plastics
MX2007012266A (en) Method for producing polystyrene foam particles with a high density.
CN104704033B (en) Foaming polystyrene series resin particle and its manufacture method, pre-expanded particles and expanded moldings
CN104513430B (en) A kind of rattan imitating PP foam material and preparation method thereof
WO2016098698A1 (en) Polypropylene resin foamed particles
CN113512228A (en) General polyester high-power expanded bead and preparation method thereof
JPS6377947A (en) Production of expanded particle of styrene-acrylonitrile-butadiene copolymer

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant