CN103937150B - Flaxen fiber strengthens injection phenolic moulding plastics and preparation method thereof - Google Patents
Flaxen fiber strengthens injection phenolic moulding plastics and preparation method thereof Download PDFInfo
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- CN103937150B CN103937150B CN201410157469.6A CN201410157469A CN103937150B CN 103937150 B CN103937150 B CN 103937150B CN 201410157469 A CN201410157469 A CN 201410157469A CN 103937150 B CN103937150 B CN 103937150B
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/12—Making granules characterised by structure or composition
- B29B9/14—Making granules characterised by structure or composition fibre-reinforced
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- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
- B29B7/72—Measuring, controlling or regulating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/7461—Combinations of dissimilar mixers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
- B29B7/90—Fillers or reinforcements, e.g. fibres
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/12—Making granules characterised by structure or composition
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
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- B29B2009/125—Micropellets, microgranules, microparticles
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- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92514—Pressure
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
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- B29C2948/92561—Time, e.g. start, termination, duration or interruption
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
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- B29C2948/9259—Angular velocity
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92609—Dimensions
- B29C2948/92638—Length
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- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
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- B29C2948/00—Indexing scheme relating to extrusion moulding
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- B29C2948/92704—Temperature
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- B29C2948/00—Indexing scheme relating to extrusion moulding
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- B29C2948/00—Indexing scheme relating to extrusion moulding
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- B29C2948/92819—Location or phase of control
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- B29C2948/92895—Barrel or housing
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- B29C2948/00—Indexing scheme relating to extrusion moulding
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Abstract
The invention discloses a kind of flaxen fiber and strengthen injection phenolic moulding plastics and preparation method thereof.Preparing the main novolak resin of raw material of this phenolaldehyde moulding compound, hexamethylenetetramine, inorganic filler and flaxen fiber, the preparation method of this phenolaldehyde moulding compound comprises the following steps: 1) weigh each raw material, standby；2) taking inorganic filler and coupling agent, to be placed in ball mill or ball grinder ball milling uniform, the consumption of described coupling agent is 0.5～10wt% of inorganic filler consumption, and described inorganic filler is one or more the combination in aluminium hydroxide, silicon powder, calcite, Talcum, calcium carbonate, glass microballoon, Kaolin and potter's clay powder；3) take hexamethylenetetramine to pulverize, then mix homogeneously with surface treated inorganic filler and other raw material；4) material mixed is put into double screw extruder extrusion；5) pulverize after extruded stock cooling, to obtain final product.Phenolaldehyde moulding compound mechanical property obtained by this method is higher, water absorption is lower.
Description
Technical field
The present invention relates to phenolaldehyde moulding compound, be specifically related to a kind of flaxen fiber and strengthen injection phenolic moulding plastics and preparation method thereof.
Background technology
Phenolaldehyde moulding compound is with phenolic resin for base material, and be composite prepared by primary raw material in conjunction with other inserts, it have cheap, heat-resisting, product size is stable, electrical insulating property good, the combination property of the more high excellence of mechanical property, is widely used in electronics, electrical equipment, automobile and other industries [2].Along with economic development, the demand of high performance material improves constantly, and the performance requirement of phenolaldehyde moulding compound is also more and more higher, and the mechanical property of such material and thermostability etc. are all had higher requirement.
In prior art, mostly coordinate in formula and add reinforcing material to improve moulding compound thermostability or mechanical property so that it is can be more widely used in high-temperature field.If publication number is the patent of invention of CN1789327, disclose a kind of blend with tripolycyanamide-P-F copolymer resins or melamine formaldehyde resin/phenol-formaldehyde resin for matrix resin, to select inorfil and organic fiber be reinforcing agent, inorganic mineral is filler, adopts injection-type tripolycyanamide-P-F moulding compound that composite crosslinking curing system is prepared from.Though this material has higher heat distortion temperature (190 DEG C) and good insulating properties, but its mechanical property such as impact strength and bending strength are all poor, and wherein notch impact strength is only 2.0～2.2kJ/m2, bending strength is only between 70～80Mpa, it is difficult to adapt to some occasion that thermostability and mechanical property requirements is all higher.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of new injection molding flaxen fiber that passes through and strengthens injection phenolic moulding plastics and preparation method thereof, and phenolaldehyde moulding compound mechanical property obtained by this method is higher, water absorption is lower.
The preparation method that flaxen fiber of the present invention strengthens injection phenolic moulding plastics, wherein being used for preparing this flaxen fiber and strengthen the main novolak resin of raw material of injection phenolic moulding plastics, hexamethylenetetramine, inorganic filler and flaxen fiber, this flaxen fiber strengthens the preparation method of injection phenolic moulding plastics and specifically includes following steps:
1) each raw material is weighed, standby；
2) take inorganic filler coupling agent and carry out surface treatment, it is uniform that coupling agent and inorganic filler be specifically placed in ball mill or ball grinder ball milling, the consumption of described coupling agent is 0.5～10wt% of inorganic filler consumption, and described inorganic filler is one or more the combination in aluminium hydroxide, silicon powder, calcite, Talcum, calcium carbonate, glass microballoon, Kaolin and potter's clay powder；
3) take hexamethylenetetramine to pulverize, then mix homogeneously with surface treated inorganic filler and other raw material；
4) material mixed is put into double screw extruder extrusion；
5) pulverize after extruded stock cooling, to obtain final product.
The inorganic filler coupling agent of specific consumption is first carried out ball milling modification process by the method for the invention, it is effectively increased the interface compatibility between hydrophilic inorganic filler and oil loving phenolic resin as matrix resin, make inorganic filler when mixing with phenolic resin as matrix resin and other raw material, cohesive force between inorganic filler and matrix and other raw material is remarkably reinforced, so that plastics can injection molding while, mechanical property such as impact strength, the bending strength etc. that can also make plastics are increased dramatically, and water absorption is greatly reduced.
In above-mentioned preparation method, the raw material being used for preparing described flaxen fiber enhancing injection phenolic moulding plastics generally also includes accelerator and lubricant, may also include dyestuff further.Preparing the proportioning that described flaxen fiber strengthens between each raw material of injection phenolic moulding plastics as reinforcing material and can adopt the convenient source proportioning of injection molding phenolaldehyde moulding compound identical using flaxen fiber with existing, it is preferred that the weight proportion of each raw material is:
Linear phenol-aldehyde resin 100；
Hexamethylenetetramine 10～20；
Inorganic filler 20～90；
Length is the flaxen fiber 25～65 of 1～10mm；
Accelerator 0.5～8；
Lubricant 1～8；
Dyestuff 0～10.
The weight proportion of each raw material is more preferably:
Linear phenol-aldehyde resin 100；
Hexamethylenetetramine 13～18；
Inorganic filler 30～80；
Length is the flaxen fiber 35～55 of 1～10mm；
Accelerator 1～5；
Lubricant 2～5；
Dyestuff 0～6.
One or more the combination that accelerator in above-mentioned raw materials can be chosen from magnesium hydroxide, calcium hydroxide, magnesium oxide and calcium oxide.When being chosen as above two or two or more combinations of accelerator, the proportioning between them can be any proportioning.
Lubricant in above-mentioned raw materials can be chosen from one or more the combination in calcium stearate, zinc stearate, ethylene stearmide, stearic acid and tristerin.When being chosen as above two or two or more combinations of lubricant, the proportioning between them can be any proportioning.
One or more the combination that dyestuff in above-mentioned raw materials can be chosen from nigrosine, phthalocyanine blue, phthalocyanine green and iron oxide red.When being chosen as above two or two or more combinations of dyestuff, the proportioning between them can be any proportioning.
Flaxen fiber described in above-mentioned raw materials can be sisal fiber, flax fiber or ramee, or arbitrarily two or more and combination with arbitrary proportion in them.Preferably selecting length is the flaxen fiber of 2～6mm.
The step 2 of above-mentioned preparation method) in, it will be preferred that controlling the rotating speed 10～60rpm of ball mill or ball grinder, Ball-milling Time is 10～120min, so that the product of final molding is obtained in that better mechanical property and water absorption.
The step 2 of above-mentioned preparation method) in, described coupling agent can be silane coupler, titanate coupling agent or aluminate coupling agent, and the consumption of described coupling agent is preferably 3～8wt% of inorganic amount of filler, more preferably 4～6wt% of inorganic filler consumption.
The step 2 of above-mentioned preparation method) in, one or more the combination that described inorganic filler is preferably selected from silicon powder, calcite, Talcum, calcium carbonate and glass microballoon, more preferably one or more the combination in calcite, calcium carbonate and glass microballoon.When being chosen as above two or two or more combinations of inorganic filler, the proportioning between them can be any proportioning.
In the step 3) of above-mentioned preparation method, generally hexamethylenetetramine is crushed to and is not less than 80 orders.
In the step 4) of above-mentioned preparation method, when extruding with double screw extruder, the barrel temperature generally arranging double screw extruder is 75～100 DEG C, and screw rod revolution is 70～90rpm.
The step 5 of above-mentioned preparation method) in, being crushed to diameter after extruded stock cooling is the regular of 1～6mm or irregular granular.
Present invention additionally comprises the flaxen fiber prepared by said method and strengthen injection phenolic moulding plastics, the simply supported beam unnotched impact strength of this moulding compound is at 10.0kJ/m2Above, simply supported beam notch impact strength is at 2.9kJ/m2Above, bending strength is at more than 105Mpa.
Technique during the moulding compound thermoset injection machine injection moulding that said method prepares is as follows: mold temperature is 150～190 DEG C, and barrel temperature is 80～100 DEG C, and injection pressure is 60～100MPa, and hardening time is 10～20s/mm.
Compared with prior art, the method of the invention is by carrying out ball-milling treatment with the coupling agent of specific consumption to inorganic filler, on the one hand, coupling agent molecule is made uniformly to be wrapped in inorganic filler surface, reduce the probability occurring to reunite between filler, improve the dispersibility of filler, make inorganic filler when mixing with phenolic resin as matrix resin and other raw material, cohesive force between inorganic filler and matrix and other raw material is remarkably reinforced, so that plastics can injection molding while, the mechanical property such as impact strength of plastics can also be made, bending strengths etc. are increased dramatically；On the other hand, the hydroxyl of the hydrophilic group of coupling agent and filling surface interacts and forms hydrogen bond, reduces the content of filling surface hydroxyl, thus the probability that when constraining curing molding, hydroxyl interacts with moisture in air；Additionally, through the filler of coupling agent surface treatment in postorder blend step, being effectively increased the interface compatibility between filler and resin, filler and resin are closely linked, and reduce the surface area of filler, enable the free hydroxyl group with aqueous phase mutual effect to reduce, furthermore, coupling agent itself also forms hydrophobic coat at filling surface, can effectively slow down the rate of water absorption of plastics, therefore, the water absorption of gained plastics is greatly reduced.
Detailed description of the invention
With embodiment, the present invention is further described below, but the invention is not limited in these embodiments.
Double screw extruder used in following embodiment is thermosetting parallel dual-screw extruding machine.
Number described in following embodiment is weight portion.
Embodiment 1
1) following component is weighed standby: linear phenol-aldehyde resin (i.e. thermoplastic phenolic resin, lower same) 100 parts, the silicon powder 80 parts of hexamethylenetetramine 10 parts, 400～600 orders, length are the sisal fiber 25 parts of 2～5mm, 3 parts of magnesium hydroxide, calcium stearate 1 part；
2) taking silicon powder and be equivalent to the titanate coupling agent of its consumption 0.5% and be placed in ball grinder to carry out ball milling, control the rotating speed 10rpm of ball grinder, Ball-milling Time is 10min；
3) take hexamethylenetetramine and be crushed to 80 orders, then mix homogeneously with surface treated silicon powder and other component；
4) material mixed being put into double screw extruder extrusion, the barrel temperature of described double screw extruder is 75～90 DEG C, and screw rod revolution is 80rpm；
5) extruded stock is crushed to the irregular granular that diameter is 1～6mm after being cooled to room temperature, obtains flaxen fiber of the present invention and strengthens injection phenolic moulding plastics.
Comparative example 1-1
1) with the step 1 of embodiment 1)；
2) take the sisal fiber titanate coupling agent being equivalent to its consumption 0.5% and carry out conventional surface process；
3) take hexamethylenetetramine and be crushed to 80 orders, then mix homogeneously with surface treated sisal fiber and other component；
4) with the step 4 of embodiment 1)；
5) extruded stock is crushed to the irregular granular that diameter is 1～6mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Comparative example 1-2
1) with the step 1 of embodiment 1)；
2) take hexamethylenetetramine and be crushed to 80 orders, then mix homogeneously with other component；
3) with the step 4 of embodiment 1)；
4) extruded stock is crushed to the irregular granular that diameter is 1～6mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Embodiment 2
1) following component is weighed standby: linear phenol-aldehyde resin 100 parts, hexamethylenetetramine 15 parts, 50 parts of the calcite of 600～800 orders, length are the sisal fiber 45 parts of 1～10mm, 5 parts of magnesium hydroxide, zinc stearate 2 parts, iron oxide red 5 parts；
2) taking calcite and be equivalent to the aluminate coupling agent of its consumption 3% and be placed in ball grinder to carry out ball milling, control the rotating speed 50rpm of ball grinder, Ball-milling Time is 80min；
3) take hexamethylenetetramine and be crushed to 100 orders, then mix homogeneously with surface treated calcite and other component；
4) material mixed being put into double screw extruder extrusion, the barrel temperature of described double screw extruder is 90～100 DEG C, and screw rod revolution is 90rpm；
5) extruded stock is crushed to the irregular granular that diameter is 2～5mm after being cooled to room temperature, obtains flaxen fiber of the present invention and strengthens injection phenolic moulding plastics.
Comparative example 2-1
1) with the step 1 of embodiment 2)；
2) take the sisal fiber aluminate coupling agent being equivalent to its consumption 3% and carry out conventional surface process；
3) take hexamethylenetetramine and be crushed to 100 orders, then mix homogeneously with surface treated sisal fiber and other component；
4) with the step 4 of embodiment 2)；
5) extruded stock is crushed to the irregular granular that diameter is 2～5mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Comparative example 2-2
1) with the step 1 of embodiment 2)；
2) take hexamethylenetetramine and be crushed to 100 orders, then mix homogeneously with other component；
3) with the step 4 of embodiment 2)；
4) extruded stock is crushed to the irregular granular that diameter is 2～5mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Embodiment 3
1) following component is weighed by weight percentage standby: linear phenol-aldehyde resin 100 parts, hexamethylenetetramine 20 parts, the calcium carbonate 30 parts of 100～300 orders, length are the flax fiber 55 parts of 5～10mm, calcium oxide 1 part, zinc stearate 5 parts；
2) taking calcium carbonate and be equivalent to the silane coupler of its consumption 5% and be placed in ball grinder to carry out ball milling, control the rotating speed 30rpm of ball grinder, Ball-milling Time is 60min；
3) take hexamethylenetetramine and be crushed to 80 orders, then mix homogeneously with surface treated calcium carbonate and other component；
4) material mixed being put into double screw extruder extrusion, the barrel temperature of described double screw extruder is 75～85 DEG C, and screw rod revolution is 90rpm；
5) extruded stock is crushed to the irregular granular that diameter is 4～6mm after being cooled to room temperature, obtains flaxen fiber of the present invention and strengthens injection phenolic moulding plastics.
Comparative example 3-1
1) with the step 1 of embodiment 3)；
2) take the flax fiber silane coupler being equivalent to its consumption 5% and carry out conventional surface process；
3) take hexamethylenetetramine and be crushed to 80 orders, then mix homogeneously with surface treated flax fiber and other component；
4) with the step 4 of embodiment 3)；
5) extruded stock is crushed to the irregular granular that diameter is 4～6mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Comparative example 3-2
1) with the step 1 of embodiment 3)；
2) take hexamethylenetetramine and be crushed to 80 orders, then mix homogeneously with its component；
3) with the step 4 of embodiment 3)；
4) extruded stock is crushed to the irregular granular that diameter is 4～6mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Embodiment 4
1) following component is weighed by weight percentage standby: linear phenol-aldehyde resin 100 parts, hexamethylenetetramine 18 parts, the glass microballoon 20 parts of 600～800 orders, length are the flax fiber 35 parts of 1～6mm, magnesium oxide 8 parts, stearic acid 0.5 part；
2) taking glass microballoon and be equivalent to the aluminate coupling agent of its consumption 6% and be placed in ball grinder to carry out ball milling, control the rotating speed 60rpm of ball grinder, Ball-milling Time is 100min；
3) take hexamethylenetetramine and be crushed to 120 orders, then mix homogeneously with surface treated glass microballoon and other component；
4) material mixed being put into double screw extruder extrusion, the barrel temperature of described double screw extruder is 75～80 DEG C, and screw rod revolution is 85rpm；
5) extruded stock is crushed to the irregular granular that diameter is 6mm after being cooled to room temperature, obtains flaxen fiber of the present invention and strengthens injection phenolic moulding plastics.
Comparative example 4-1
1) with the step 1 of embodiment 4)；
2) take the flax fiber aluminate coupling agent being equivalent to its consumption 6% and carry out conventional surface process；
3) take hexamethylenetetramine and be crushed to 120 orders, then mix homogeneously with surface treated flax fiber and other component；
4) with the step 4 of embodiment 4)；
5) extruded stock is crushed to the irregular granular that diameter is 6mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Comparative example 4-2
1) with the step 1 of embodiment 4)；
2) take hexamethylenetetramine and be crushed to 120 orders, then mix homogeneously with other component；
3) with the step 4 of embodiment 4)；
4) extruded stock is crushed to the irregular granular that diameter is 6mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Embodiment 5
1) following component is weighed by weight percentage standby: linear phenol-aldehyde resin 100 parts, hexamethylenetetramine 16 parts, 90 parts of the potter's clay powder of 200～400 orders, length are the ramee 65 parts of 5～8mm, calcium hydroxide 0.5 part, ethylene stearmide 8 parts, nigrosine 8 parts；
2) taking potter's clay powder and be equivalent to the silane coupler of its consumption 8% and be placed in ball grinder to carry out ball milling, control the rotating speed 20rpm of ball grinder, Ball-milling Time is 120min；
3) take hexamethylenetetramine and be crushed to 160 orders, then mix homogeneously with surface treated potter's clay powder and other component；
4) material mixed being put into double screw extruder extrusion, the barrel temperature of described double screw extruder is 80～95 DEG C, and screw rod revolution is 75rpm；
5) extruded stock is crushed to the irregular granular that diameter is 2mm after being cooled to room temperature, obtains flaxen fiber of the present invention and strengthens injection phenolic moulding plastics.
Comparative example 5-1
1) with the step 1 of embodiment 5)；
2) take the ramee silane coupler being equivalent to its consumption 8% and carry out conventional surface process；
3) take hexamethylenetetramine and be crushed to 160 orders, then mix homogeneously with surface treated ramee and other component；
4) with the step 4 of embodiment 5)；
5) extruded stock is crushed to the irregular granular that diameter is 2mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Comparative example 5-2
1) with the step 1 of embodiment 5)；
2) take hexamethylenetetramine and be crushed to 160 orders, then mix homogeneously with other component；
3) with the step 4 of embodiment 5)；
4) extruded stock is crushed to the irregular granular that diameter is 2mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Embodiment 6
1) following component is weighed by weight percentage standby: linear phenol-aldehyde resin 100 parts, hexamethylenetetramine 13 parts, the kaolin powder 80 parts of 200～300 orders, length are the ramee 50 parts of 5～8mm, calcium oxide 3 parts, glyceryl stearate 5 parts；
2) taking kaolin powder and be equivalent to the silane coupler of its consumption 10% and be placed in ball grinder to carry out ball milling, control the rotating speed 20rpm of ball grinder, Ball-milling Time is 120min；
3) take hexamethylenetetramine and be crushed to 160 orders, then mix homogeneously with surface treated kaolin powder and other component；
4) material mixed being put into double screw extruder extrusion, the barrel temperature of described double screw extruder is 80～100 DEG C, and screw rod revolution is 80rpm；
5) extruded stock is crushed to the irregular granular that diameter is 2～5mm after being cooled to room temperature, obtains flaxen fiber of the present invention and strengthens injection phenolic moulding plastics.
Comparative example 6-1
1) with the step 1 of embodiment 5)；
2) take the ramee silane coupler being equivalent to its consumption 10% and carry out conventional surface process；
3) take hexamethylenetetramine and be crushed to 160 orders, then mix homogeneously with surface treated ramee and other component；
4) with the step 4 of embodiment 5)；
5) extruded stock is crushed to the irregular granular that diameter is 2～5mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Comparative example 6-2
1) with the step 1 of embodiment 5)；
2) take hexamethylenetetramine and be crushed to 160 orders, then mix homogeneously with other component；
3) with the step 4 of embodiment 5)；
4) extruded stock is crushed to the irregular granular that diameter is 2～5mm after being cooled to room temperature, and the flaxen fiber obtaining contrast strengthens injection phenolic moulding plastics.
Respectively by the phenolaldehyde moulding compound obtained by above-described embodiment 1～6, comparative example 1-1～comparative example 6-1 and comparative example 1-2～contrast row 6-2 respectively with thermoset injection machine by following technique injection moulding: mold temperature is 170 DEG C, barrel temperature is 90 DEG C, injection pressure is 60MPa, and hardening time is 20s/mm.The moulding compound of gained carries out mechanical electric performance comparison with German PF51 phenolaldehyde moulding compound, shown in result such as table 1 below, table 2 and table 3:
Table 1:
Table 2:
Table 3:
Above impact strength records according to GB/T1043；
Bending strength records according to GB/T9341；
Load deformation temperature is more according to GB/T1634, and pressure is record under 8.00MPa.
From above-mentioned table 1, table 2 and table 3, the phenolaldehyde moulding compound prepared by technique of the present invention has the mechanical electric performance close with external advanced same type of material, and impact strength therein, electrical strength and load deformation temperature are substantially better than Germany's PF51 material especially；In addition, the phenolaldehyde moulding compound that technique of the present invention prepares is that in three kinds of techniques (technique of the present invention, to flaxen fiber process of surface treatment, any raw material is not carried out the technique that surface treatment directly mixes), impact strength, bending strength and water absorption performance are best；The phenolaldehyde moulding compound prepared by technique of the present invention is compared with the moulding compound that flaxen fiber process of surface treatment is prepared, when basic other performance of maintenance is constant, (unnotched impact strength at least improves 18.2% to have higher unnotched impact strength and bending strength, bending strength at least improves 26.3%), and water absorption lower (water absorption at least reduces 18.5%).
Claims (10)
1. the preparation method that flaxen fiber strengthens injection phenolic moulding plastics, it is characterized in that: prepare this flaxen fiber and strengthen the main novolak resin of raw material of injection phenolic moulding plastics, hexamethylenetetramine, inorganic filler and flaxen fiber, described flaxen fiber strengthens the preparation method of injection phenolic moulding plastics and comprises the following steps:
1) each raw material is weighed, standby；
2) taking inorganic filler coupling agent and carry out surface treatment, it is uniform that coupling agent and inorganic filler be specifically placed in ball mill or ball grinder ball milling, and the consumption of described coupling agent is 0.5～10wt% of inorganic filler consumption, and described inorganic filler is calcium carbonate；
3) take hexamethylenetetramine to pulverize, then mix homogeneously with surface treated inorganic filler and other raw material；
4) material mixed is put into double screw extruder extrusion；
5) pulverize after extruded stock cooling, to obtain final product.
2. preparation method according to claim 1, it is characterised in that: step 2) in, the rotating speed 10～60rpm of described ball mill or ball grinder, Ball-milling Time is 10～120min.
3. preparation method according to claim 1, it is characterised in that: step 2) in, the consumption of described coupling agent is 4～6wt% of inorganic filler consumption.
4. preparation method according to claim 1, it is characterised in that: the barrel temperature of described double screw extruder is 75～100 DEG C, and screw rod revolution is 70～90rpm.
5. the preparation method according to any one of Claims 1 to 4, it is characterised in that: the raw material of the flaxen fiber enhancing injection phenolic moulding plastics that preparation is described also includes accelerator, lubricant and dyestuff.
6. preparation method according to claim 5, it is characterised in that: the weight proportion of the raw material of the flaxen fiber enhancing injection phenolic moulding plastics that preparation is described is:
Linear phenol-aldehyde resin 100；
Hexamethylenetetramine 10～20；
Inorganic filler 20～90；
Length is the flaxen fiber 25～65 of 1～10mm；
Accelerator 0.5～8；
Lubricant 1～8；
Dyestuff 0～10.
7. preparation method according to claim 6, it is characterised in that: the weight proportion of each raw material of the flaxen fiber enhancing injection phenolic moulding plastics that preparation is described is:
Linear phenol-aldehyde resin 100；
Hexamethylenetetramine 13～18；
Inorganic filler 30～80；
Length is the flaxen fiber 35～55 of 1～10mm；
Accelerator 1～5；
Lubricant 2～5；
Dyestuff 0～6.
8. preparation method according to claim 6, it is characterised in that: described accelerator is one or more the combination in magnesium hydroxide, calcium hydroxide, magnesium oxide and calcium oxide.
9. preparation method according to claim 6, it is characterised in that: described lubricant is one or more the combination in calcium stearate, zinc stearate, ethylene stearmide, stearic acid and tristerin.
10. the flaxen fiber that method according to any one of claim 1～9 prepares strengthens injection phenolic moulding plastics.
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| CN105924892A (en) * | 2016-06-30 | 2016-09-07 | 禹州市远大塑料电器有限责任公司 | Reinforced phenolic aldehyde molding compound without glass fibers |
| CN107556698B (en) * | 2017-10-12 | 2019-08-09 | 溧阳市乔森塑料有限公司 | A kind of high temperature resistant urea moulding material and preparation method thereof |
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| CN102417692A (en) * | 2011-11-08 | 2012-04-18 | 桂林电器科学研究院 | Cotton fiber reinforced injection type phenolic molding compound and preparation method thereof |
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Effective date of registration: 20190926 Address after: 541004 Dongcheng Road, Guilin, the Guangxi Zhuang Autonomous Region, No. 8 Patentee after: Guilin Jinge Electrotechnical Electronic Material Science & Technology Co., Ltd. Address before: 541004 No. 8 Dongcheng Road, Qixing District, Guilin, the Guangxi Zhuang Autonomous Region Patentee before: Guilin Electrical Equipment Scientific Research Institute Co., Ltd. |