CN111873427A - Preparation method of multi-component copolymerized nylon powder for selective laser sintering - Google Patents
Preparation method of multi-component copolymerized nylon powder for selective laser sintering Download PDFInfo
- Publication number
- CN111873427A CN111873427A CN202010695820.2A CN202010695820A CN111873427A CN 111873427 A CN111873427 A CN 111873427A CN 202010695820 A CN202010695820 A CN 202010695820A CN 111873427 A CN111873427 A CN 111873427A
- Authority
- CN
- China
- Prior art keywords
- powder
- copolymerized nylon
- grinding
- coarse material
- nylon powder
- 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
- 239000000843 powder Substances 0.000 title claims abstract description 122
- 239000004677 Nylon Substances 0.000 title claims abstract description 107
- 229920001778 nylon Polymers 0.000 title claims abstract description 107
- 238000000110 selective laser sintering Methods 0.000 title claims abstract description 42
- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- 239000000463 material Substances 0.000 claims abstract description 62
- 238000000227 grinding Methods 0.000 claims abstract description 60
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 44
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 23
- 239000012744 reinforcing agent Substances 0.000 claims abstract description 19
- 238000002156 mixing Methods 0.000 claims abstract description 17
- 102220043159 rs587780996 Human genes 0.000 claims abstract description 17
- 239000008187 granular material Substances 0.000 claims abstract description 15
- 238000000034 method Methods 0.000 claims abstract description 15
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 12
- 230000003078 antioxidant effect Effects 0.000 claims abstract description 12
- 239000000178 monomer Substances 0.000 claims description 21
- 239000012298 atmosphere Substances 0.000 claims description 18
- 239000002245 particle Substances 0.000 claims description 17
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 11
- 239000011324 bead Substances 0.000 claims description 11
- 229920001577 copolymer Polymers 0.000 claims description 11
- 229910021485 fumed silica Inorganic materials 0.000 claims description 11
- 239000011521 glass Substances 0.000 claims description 11
- 239000000654 additive Substances 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 8
- 230000000996 additive effect Effects 0.000 claims description 7
- 239000008188 pellet Substances 0.000 claims description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 6
- 239000004408 titanium dioxide Substances 0.000 claims description 6
- -1 PA10 Polymers 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 239000005543 nano-size silicon particle Substances 0.000 claims description 5
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 5
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 5
- 239000003365 glass fiber Substances 0.000 claims description 4
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 3
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 3
- 239000001110 calcium chloride Substances 0.000 claims description 3
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 3
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 3
- 239000000292 calcium oxide Substances 0.000 claims description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 3
- 239000004917 carbon fiber Substances 0.000 claims description 3
- FPAFDBFIGPHWGO-UHFFFAOYSA-N dioxosilane;oxomagnesium;hydrate Chemical compound O.[Mg]=O.[Mg]=O.[Mg]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O FPAFDBFIGPHWGO-UHFFFAOYSA-N 0.000 claims description 3
- 239000004575 stone Substances 0.000 claims description 3
- 238000005245 sintering Methods 0.000 abstract description 23
- 239000013058 crude material Substances 0.000 abstract description 4
- 241000761389 Copa Species 0.000 description 29
- 238000010298 pulverizing process Methods 0.000 description 26
- 238000004519 manufacturing process Methods 0.000 description 13
- 238000004364 calculation method Methods 0.000 description 7
- VSAWBBYYMBQKIK-UHFFFAOYSA-N 4-[[3,5-bis[(3,5-ditert-butyl-4-hydroxyphenyl)methyl]-2,4,6-trimethylphenyl]methyl]-2,6-ditert-butylphenol Chemical group CC1=C(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)C(C)=C(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)C(C)=C1CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 VSAWBBYYMBQKIK-UHFFFAOYSA-N 0.000 description 6
- 239000012043 crude product Substances 0.000 description 6
- 239000011164 primary particle Substances 0.000 description 5
- 238000009826 distribution Methods 0.000 description 4
- 239000002861 polymer material Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical compound CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 2
- 235000010354 butylated hydroxytoluene Nutrition 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- PADKXWJUAXDOGB-UHFFFAOYSA-N n-(3,5-ditert-butyl-4-hydroxyphenyl)propanamide Chemical compound CCC(=O)NC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 PADKXWJUAXDOGB-UHFFFAOYSA-N 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- SPIPLAVUQNWVMZ-UHFFFAOYSA-N (2,4-ditert-butylphenoxy)-fluorophosphinous acid Chemical compound CC(C)(C)C1=CC=C(OP(O)F)C(C(C)(C)C)=C1 SPIPLAVUQNWVMZ-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000011221 initial treatment Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- NFHFRUOZVGFOOS-UHFFFAOYSA-N palladium;triphenylphosphane Chemical compound [Pd].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 NFHFRUOZVGFOOS-UHFFFAOYSA-N 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
Classifications
-
- 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
- B29C64/00—Additive manufacturing, i.e. manufacturing of three-dimensional [3D] objects by additive deposition, additive agglomeration or additive layering, e.g. by 3D printing, stereolithography or selective laser sintering
- B29C64/30—Auxiliary operations or equipment
- B29C64/307—Handling of material to be used in additive manufacturing
- B29C64/314—Preparation
-
- 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
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/10—Conditioning or physical treatment of the material to be shaped by grinding, e.g. by triturating; by sieving; by filtering
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B33—ADDITIVE MANUFACTURING TECHNOLOGY
- B33Y—ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3-D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3-D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- B33Y40/00—Auxiliary operations or equipment, e.g. for material handling
- B33Y40/10—Pre-treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B33—ADDITIVE MANUFACTURING TECHNOLOGY
- B33Y—ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3-D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3-D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- B33Y70/00—Materials specially adapted for additive manufacturing
- B33Y70/10—Composites of different types of material, e.g. mixtures of ceramics and polymers or mixtures of metals and biomaterials
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
- C08L77/02—Polyamides derived from omega-amino carboxylic acids or from lactams thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
- C08L77/06—Polyamides derived from polyamines and polycarboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/011—Nanostructured additives
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
- C08L2205/025—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Organic Chemistry (AREA)
- Polymers & Plastics (AREA)
- Mechanical Engineering (AREA)
- Medicinal Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Civil Engineering (AREA)
- Structural Engineering (AREA)
- Ceramic Engineering (AREA)
- Composite Materials (AREA)
- Physics & Mathematics (AREA)
- Optics & Photonics (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Polyamides (AREA)
Abstract
A preparation method of multi-component copolymerized nylon powder for selective laser sintering comprises the following steps: adding the multi-component copolymerized nylon granules into a cryogenic grinder, and carrying out primary grinding in liquid nitrogen at the temperature of-90 to-130 ℃ at the grinding rotor frequency of 15 to 30Hz to obtain multi-component copolymerized nylon powder coarse material with the D50 of 200 to 500 mu m; mixing the crude poly-copolymerized nylon powder with a grinding aid to obtain a mixed crude material, adding the mixed crude material into a cryogenic grinder, and carrying out secondary grinding in liquid nitrogen at the temperature of-100 to-160 ℃ at the grinding rotor frequency of 25 to 50Hz to obtain fine poly-copolymerized nylon powder with the D50=30 to 70 mu m; adding a flow assistant, an antioxidant and a reinforcing agent, and mixing at a low speed for 20-60 min to obtain the multi-component copolymerized nylon powder for selective laser sintering. According to the invention, the multielement copolymerized nylon granules are treated by a cryogenic grinding method to obtain powder coarse materials, and then the powder coarse materials are subjected to cryogenic grinding after the grinding aid is added, so that the multielement copolymerized nylon powder for selective laser sintering, which has low sintering temperature, high toughness and good surface quality, can be obtained.
Description
Technical Field
The invention belongs to the technical field of additive manufacturing, and particularly relates to a preparation method of multi-component copolymerized nylon powder for selective laser sintering.
Background
Additive manufacturing is a technology for manufacturing objects by using three-dimensional model data in a layer-by-layer stacking mode, and has the unique advantages of short production period in small batch, no redundant tailings in production, high production flexibility and the like, so the additive manufacturing has more and more attention in the manufacturing industry in recent years. The Selective Laser Sintering (SLS) technology has the unique advantages of simple manufacturing process, no need of a supporting structure, extremely high material utilization rate and the like, and becomes one of additive manufacturing technologies which are developed fastest and have industrial production capacity.
As is well known, there are three commonly used SLS sintered materials: high polymer powders, metal powders and ceramic powders. Wherein the high polymer material has lower melting point and higher viscosity, so that the forming is easier, and the high polymer material is widely applied to the industries of hand boards, spaceflight, medical treatment and the like. Among all high polymer materials, the nylon material has the highest absorption efficiency of laser, and nylon itself is used as one of five engineering plastics and has mature application in various industries. Therefore, among the polymer materials for SLS, nylon occupies 90% or more of the market.
At present, the commercially successful nylon materials in the market mainly comprise high-temperature materials with better mechanical properties such as PA11 and PA12, and PA6 with extremely high modulus, and composites thereof. The multi-component copolymerized nylon (COPA) with many advantages such as low sintering main temperature, low crystallinity and good toughness is rarely reported. The fundamental reason is that the COPA material is prepared by polycondensation of monomers such as PA6, P66, PA12 and PA610, and the complexity of the self-repeating monomers determines that the preparation route is complex and the requirements on equipment and process are precise when the COPA adopts a solvent method commonly used by other SLS nylon materials, such as CN201811252408 and CN 201910865021. Obviously, the preparation of the COPA by using a solvent method not only significantly increases the manufacturing cost, but also more importantly, the monomer of the COPA has greater risks of unstable structural damage such as fracture, grafting and recombination in a solvent synthesis route, and finally, the materials of different batches have obvious performance fluctuation. Therefore, the most popular method for processing COPA powder in the conventional field is cryogenic pulverization. In recent years, there are numerous documents and patents that optimize cryogenic grinding schemes, such as CN106111289A, CN 210617323U. However, the above schemes mainly develop optimization around low production efficiency and production cost, but inherent defects of the copious cooling pulverized COPA powder, such as wide particle size distribution, low apparent density, irregular powder particle shape and the like, cannot be remarkably improved under the condition of not changing a hardware structure, so that the powder has relatively poor flowability, the mechanical property of a finished workpiece is insufficient, and the use of the COPA powder in the SLS technical field is greatly limited.
Disclosure of Invention
Aiming at the technical problems in the prior art, the invention provides a preparation method of a multi-component copolymerized nylon powder for selective laser sintering, which aims to solve the technical problems of wide particle size distribution, low apparent density, irregular powder particle shape and the like of the multi-component copolymerized nylon powder prepared by the prior art.
In order to solve the technical problems, the invention provides a preparation method of a multi-component copolymerized nylon powder for selective laser sintering, which comprises the following steps:
step one, adding the multi-component copolymerized nylon granules into a cryogenic grinder, and carrying out primary grinding at a grinding rotor frequency of 15-30 Hz in a liquid nitrogen environment atmosphere at the temperature of-90 to-130 ℃ to obtain multi-component copolymerized nylon powder coarse material with D50 of 200-500 mu m;
step two, mixing the multicomponent copolymer nylon powder coarse material and a grinding aid to obtain a mixed coarse material, adding the mixed coarse material into a cryogenic grinder, and carrying out secondary grinding in a liquid nitrogen environment atmosphere at-100 to-160 ℃ at a grinding rotor frequency of 25 to 50Hz to obtain the multicomponent copolymer nylon fine powder with D50=30 to 70 mu m;
adding a flow assistant, an antioxidant and a reinforcing agent into the multi-component copolymerized nylon fine powder, and mixing at a low speed of 100-300 r/min for 20-60 min to obtain multi-component copolymerized nylon powder for selective laser sintering; wherein,
the weight ratio of the multielement copolymerized nylon fine powder to the flow additive to the antioxidant to the reinforcing agent is as follows: 100: 0.2-3: 0.1-2: 0-50.
As a further preferable embodiment of the present invention, the mixing of the multicomponent copolymerized nylon powder coarse material and the grinding aid to obtain a mixed coarse material specifically includes:
and stirring the multi-component copolymerized nylon powder coarse material and the grinding aid in a high-speed stirrer at a rotating speed of 600-1500 r/min for 2-10 min to prepare a mixed coarse material.
As a further preferable scheme of the invention, the calculation formula of the grinding aid in the weight percentage M of the mixed coarse material is as follows:
wherein D is the average particle size of the grinding aid, D is D50 of the multi-component copolymerized nylon powder coarse material, ρ D is the density of the grinding aid, ρ D is the density of the multi-component copolymerized nylon powder coarse material, K is the coverage coefficient, and K is 20-200%.
As a further preferred embodiment of the present invention, K = 100%.
In a further preferred embodiment of the present invention, the multicomponent copolymerized nylon pellet has a repeating monomer structure composed of three or more nylon monomers.
In a further preferred embodiment of the present invention, the poly-copolymerized nylon pellets have a repeating monomer structure consisting of monomers PA6 and PA66, and any one of monomers PA46, PA610, PA10, PA12 and PA 1212.
In a further preferred embodiment of the present invention, the temperature of the liquid nitrogen environment in the second step is 10 to 30 ℃ below the embrittlement point of the multicomponent copolymerized nylon pellet.
In a further preferred embodiment of the present invention, the grinding aid is one or a mixture of two or more of a flow aid, an antioxidant and a reinforcing agent, and the grinding aid has an average particle diameter of 0.01 to 10 μm.
As a further preferable scheme of the present invention, the flow assistant is one or more of fumed silica, nano silicon carbide, nano calcium oxide, nano alumina, titanium dioxide and calcium carbonate.
As a further preferable scheme of the invention, the reinforcing agent is one or more of glass beads, glass fibers, carbon fibers, micaceous stone, calcium chloride, titanium dioxide and talcum powder.
The preparation method of the multicomponent copolymerized nylon powder for selective laser sintering comprises the steps of carrying out primary treatment on multicomponent copolymerized nylon granules by a cryogenic grinding method to obtain powder coarse materials, then adding a grinding aid and carrying out secondary cryogenic grinding, thus obtaining the multicomponent copolymerized nylon powder for selective laser sintering with low sintering temperature, high toughness and good surface quality. And the grinding aid is quantitatively added into the copolymerized nylon coarse powder, so that the covering degree of the aid on the surface of the copolymerized nylon powder reaches an ideal range, and the aid can generate a uniform collision effect on the copolymerized nylon powder in the cryogenic grinding process. The efficiency of cryogenic processing is improved, and meanwhile, the toughness of the material is not reduced. The multi-component copolymerized nylon finished powder has the advantages of optimal particle size distribution, apparent density and more regular powder particle shape, and the comprehensive performance of the material is improved; the phenomena of cracking, powder throwing, dust raising and the like of the powder in the selective laser sintering process are avoided, the mechanical performance and the sintering stability of the selective laser sintering workpiece are improved finally, and the application field of selective laser sintering is widened.
Detailed Description
In order to solve the technical problems in the prior art, the invention provides a multi-component copolymerized nylon powder for selective laser sintering, which comprises the following steps:
step one, adding the multicomponent copolymer nylon granules into a cryogenic grinder, and carrying out primary grinding at a grinding rotor frequency of 15-30 Hz in a liquid nitrogen environment atmosphere at the temperature of-90 to-130 ℃ to obtain crude multicomponent copolymer nylon powder with D50 of 200-500 mu m;
and step two, mixing the multicomponent copolymer nylon powder coarse material with a grinding aid to obtain a mixed coarse material, adding the mixed coarse material into a cryogenic grinder, and carrying out secondary grinding at a grinding rotor frequency of 25-50 Hz in a liquid nitrogen environment atmosphere with the temperature of-100 to-160 ℃ (preferably 10-30 ℃ below the embrittlement point of the multicomponent copolymer nylon granules) to obtain the multicomponent copolymer nylon fine powder with the D50= 30-70 mu m.
Adding a flow assistant, an antioxidant and a reinforcing agent into the multi-component copolymerized nylon fine powder, and mixing at a low speed of 100-300 r/min for 20-60 min to obtain multi-component copolymerized nylon powder for selective laser sintering; wherein,
the weight ratio of the multielement copolymerized nylon fine powder to the flow additive to the antioxidant to the reinforcing agent is as follows: 100: 0.2-3: 0.1-2: 0-50. In the third step, it should be noted that, in the fine powder of the multicomponent copolymerized nylon, the reinforcing agent may be added or not added, that is, the content of the reinforcing agent is 0. Preferably, the content of the reinforcing agent is 10-30, so that the size stability and the mechanical property of the multi-component copolymerized nylon material workpiece can be ensured, and the toughness of the multi-component copolymerized nylon material workpiece can also be ensured, namely the performance of the multi-component copolymerized nylon material workpiece is better ensured.
In order to further improve the particle size distribution and the flowability of the powder, preferably, the mixing of the multipolymer nylon powder coarse material and the grinding aid to obtain the mixed coarse material specifically comprises:
and stirring the multi-component copolymerized nylon powder coarse material and the grinding aid in a high-speed stirrer at a rotating speed of 600-1500 r/min for 2-10 min to prepare a mixed coarse material.
In order to achieve the best grinding effect of the grinding aid on the semi-finished powder without reducing the toughness of the material, it is further preferable that the calculation formula of the grinding aid in the weight percentage M of the mixed coarse material is as follows:
wherein D is the average particle size of the grinding aid, D is D50 of the multi-component copolymerized nylon powder coarse material, ρ D is the density of the grinding aid, ρ D is the density of the multi-component copolymerized nylon powder coarse material, K is the coverage coefficient, and K is 20-200%. Further preferably, K = 100%.
Specifically, the multi-component copolymerized nylon granules are of a repeating monomer structure consisting of three or more nylon monomers, wherein the nylon monomers are PA6, PA66, PA610, PA10, PA12 and the like, and preferably, the multi-component copolymerized nylon granules are of a repeating monomer structure consisting of monomer PA6, PA66 and any one of monomer PA46, PA610, PA10, PA12 and PA1212, so that the multi-component copolymerized nylon powder sintered by selective laser has the beneficial effects of low melting point and higher toughness.
Specifically, the grinding aid is one or a mixture of more than two of a flow aid, an antioxidant and a reinforcing agent, and the average particle size of the grinding aid is 0.01-10 μm. A single agent is preferred as a grinding aid (e.g., only a flow aid, only an antioxidant, or only a reinforcing agent) to provide better dispersion of the grinding aid on the surface of the nylon powder.
In specific implementation, the flow assistant is one or more of fumed silica, nano silicon carbide, nano calcium oxide, nano aluminum oxide, titanium dioxide and calcium carbonate; the reinforcing agent is one or more of glass beads, glass fibers, carbon fibers, mica stones, calcium chloride, titanium dioxide and talcum powder; the antioxidant is 1,3, 5-trimethyl-2, 4, 6-tris (3, 5-di-tert-butyl-4-hydroxybenzyl) benzene, 2, 6-di-tert-butyl-4-methyl-phenol; n, N ' -di (3, 5-di-tert-butyl-4-hydroxyphenyl propionamide), 2,2' -ethylene bis ((4, 6-di-tert-butylphenyl) fluorophosphite, and tetrakis ((2, 4-di-tert-butylphenyl) -4,4' -biphenylbisphosphite, or a mixture of two or more thereof.
The invention also provides the multielement copolymerized nylon powder for selective laser sintering, which is prepared by the preparation method of the multielement copolymerized nylon powder for selective laser sintering in any embodiment.
In order to make the technical solutions of the present invention better understood and realized by those skilled in the art, the technical solutions of the present invention are described in detail below by way of examples.
Comparative example 1
COPA pellets consisting of PA6, PA66 and PA10 were charged into a cryogenic pulverizer and pulverized at a pulverizing rotor frequency of 50Hz in a liquid nitrogen atmosphere at-160 ℃ to obtain a COPA fine powder of D50=50 μm. Adding 0.5 part of fumed silica, 0.8 part of 1,3, 5-trimethyl-2, 4, 6-tri (3, 5-di-tert-butyl-4-hydroxybenzyl) benzene and 30 parts of glass beads with the average particle size of 10 mu m into the COPA fine powder, and mixing at a low speed of 200r/min for 30min to obtain the multi-component copolymerized nylon powder for selective laser sintering. And sintering the powder in an SLS device at a sintering main temperature of 112 ℃ to obtain a finished workpiece.
Example 1
The COPA granules consisting of PA6, PA66 and PA10 are added into a cryogenic pulverizer, primary pulverization is carried out in a liquid nitrogen environment atmosphere at-100 ℃ at a pulverization rotor frequency of 20Hz to obtain a crude poly-copolymerized nylon powder material with D50=400 μm, 30 parts of glass beads with the average particle size of 10 μm are added into 100 parts of the crude poly-copolymerized nylon powder material, the mixture is stirred in a high-speed stirrer at a rotating speed of 800r/min for 8min, the mixed crude material is added into the cryogenic pulverizer again, secondary pulverization is carried out in a liquid nitrogen environment atmosphere at-140 ℃ at a pulverization rotor frequency of 45Hz to obtain the COPA fine powder with D50=50 μm. Adding 0.5 part of fumed silica and 0.8 part of 1,3, 5-trimethyl-2, 4, 6-tri (3, 5-di-tert-butyl-4-hydroxybenzyl) benzene into the COPA fine powder, and mixing at a low speed of 200r/min for 30min to obtain the multi-copolymerized nylon powder for selective laser sintering. And sintering the powder in an SLS device at the sintering main temperature of 113 ℃ to obtain a finished workpiece.
Example 2
Adding COPA granules consisting of PA6, PA66 and PA10 into a cryogenic pulverizer, performing primary pulverization in a liquid nitrogen environment atmosphere at-100 ℃ at a pulverizing rotor frequency of 20Hz to obtain a nylon powder coarse material with D50=400 μm, adding 14.7 parts of glass beads with an average primary particle size of 10 μm into 100 parts of the nylon powder coarse material according to the formula calculation amount, stirring in a high-speed stirrer at a rotating speed of 800r/min for 8min, adding the mixed coarse material into the cryogenic pulverizer again, and performing secondary pulverization in a liquid nitrogen environment atmosphere at-140 ℃ at a pulverizing rotor frequency of 45Hz to obtain COPA fine powder with D50=50 μm. 0.5 part of fumed silica, 0.8 part of 1,3, 5-trimethyl-2, 4, 6-tris (3, 5-di-tert-butyl-4-hydroxybenzyl) benzene and 35.3 parts of glass beads with the average particle size of 10 mu m are added into the COPA fine powder and mixed at a low speed of 200r/min for 30min to obtain the multi-component copolymerized nylon powder for selective laser sintering. And sintering the powder in an SLS device at a sintering main temperature of 114 ℃ to obtain a finished workpiece.
Example 3
Adding COPA granules consisting of PA6, PA66 and PA10 into a cryogenic pulverizer, performing primary pulverization in a liquid nitrogen environment atmosphere at-100 ℃ at a pulverizing rotor frequency of 20Hz to obtain a crude multi-component copolymerized nylon powder material with D50=400 μm, adding 14.7 parts of glass beads with an average primary particle size of 10 μm into 100 parts of the crude multi-component copolymerized nylon powder material according to the formula calculation amount, stirring in a high-speed stirrer at a rotating speed of 800r/min for 8min, putting the mixed crude material into the cryogenic pulverizer again, and performing secondary pulverization in a liquid nitrogen environment atmosphere at-140 ℃ at a pulverizing rotor frequency of 45Hz to obtain a COPA fine powder with D50=50 μm. Adding 0.5 part of fumed silica, 0.8 part of 1,3, 5-trimethyl-2, 4, 6-tri (3, 5-di-tert-butyl-4-hydroxybenzyl) benzene and 15.3 parts of glass beads with the average particle size of 10 mu m into the COPA fine powder, and mixing at a low speed of 200r/min for 30min to obtain the multi-component copolymerized nylon powder for selective laser sintering. And sintering the powder in an SLS device at a sintering main temperature of 112 ℃ to obtain a finished workpiece.
Example 4
Adding COPA granules consisting of PA6, PA66 and PA12 into a cryogenic pulverizer, performing primary pulverization in a liquid nitrogen environment atmosphere at-110 ℃ at a pulverization rotor frequency of 15Hz to obtain a multi-component copolymerized nylon powder coarse material with D50=400 μm, adding 0.10 part of fumed silica with 70nm average primary particle size into 100 parts of the multi-component copolymerized nylon powder coarse material according to a formula calculation amount, stirring for 6min in a high-speed stirrer at a rotating speed of 1000r/min, adding the mixed coarse material into the cryogenic pulverizer again, and performing secondary pulverization in a liquid nitrogen environment atmosphere at-150 ℃ at a pulverization rotor frequency of 43Hz to obtain COPA fine powder with D50=45 μm. Adding 0.4 part of fumed silica, 0.3 part of 1,3, 5-trimethyl-2, 4, 6-tris (3, 5-di-tert-butyl-4-hydroxybenzyl) benzene and 10 parts of glass beads into the COPA fine powder, and mixing at a low speed of 300r/min for 40min to obtain the multi-component copolymerized nylon powder for selective laser sintering. And sintering the powder in an SLS device at a sintering main temperature of 122 ℃ to obtain a finished workpiece.
Example 5
Adding COPA granules consisting of PA6, PA66 and PA12 into a cryogenic pulverizer, performing primary pulverization in a liquid nitrogen environment atmosphere at-120 ℃ at a pulverization rotor frequency of 25Hz to obtain a crude product of multi-component copolymerized nylon powder with D50=400 μm, adding 0.16 part of fumed silica with 100nm average primary particle size into 100 parts of the crude product of multi-component copolymerized nylon powder according to a formula calculation amount, stirring for 6min in a high-speed stirrer at a rotating speed of 1000r/min, adding the mixed crude product into the cryogenic pulverizer again, and performing secondary pulverization in a liquid nitrogen environment atmosphere at-160 ℃ at a pulverization rotor frequency of 40Hz to obtain a COPA fine powder with D50=46 μm. Adding 0.34 part of fumed silica, 0.2 part of 2, 6-di-tert-butyl-4-methyl-phenol and 20 parts of glass beads into the COPA fine powder, and mixing at a low speed of 200r/min for 45min to obtain the multi-component copolymerized nylon powder for selective laser sintering. And sintering the powder in an SLS device at a sintering main temperature of 112 ℃ to obtain a finished workpiece.
Example 6
Adding COPA granules consisting of PA6, PA66 and PA1212 into a cryogenic pulverizer, performing primary pulverization in a liquid nitrogen environment atmosphere at-120 ℃ at a pulverizing rotor frequency of 30Hz to obtain a crude product of the multi-component copolymerized nylon powder with D50=450 μm, adding 0.05 part of nano silicon carbide with an average primary particle size of 40nm to 100 parts of the crude product of the multi-component copolymerized nylon powder according to a formula calculation amount, stirring in a high-speed stirrer at a rotating speed of 1000r/min for 6min, adding the mixed crude product into the cryogenic pulverizer again, and performing secondary pulverization in a liquid nitrogen environment atmosphere at-150 ℃ at a pulverizing rotor frequency of 43Hz to obtain a fine COPA powder with D50=55 μm. Adding 0.95 part of nano silicon carbide, 0.8 part of N, N' -bis (3, 5-di-tert-butyl-4-hydroxyphenyl propionamide) and 20 parts of glass fiber into the COPA fine powder, and mixing at a low speed of 250r/min for 45min to obtain the multi-component copolymerized nylon powder for selective laser sintering. And sintering the powder in an SLS device at a sintering main temperature of 126 ℃ to obtain a finished workpiece.
TABLE 1 data of various performance tests on sintered workpiece of multicomponent copolymerized nylon powder for selective laser sintering
As can be seen from table 1, by comparing examples 1 and 2 with comparative example 1, the flowability of the final powder can be improved by adding a proper amount of grinding aid to the primarily pulverized polynary copolymerized nylon powder as the grinding aid, so that the powder has better powder spreading surface and sintering bath at the selective laser sintering stage, the sintering of the final powder is more compact, and the mechanical properties of the workpiece are improved.
On the other hand, as is clear from comparison between example 1 and example 2, the sintering temperatures are almost the same because the mass ratios of the raw material components are the same. However, in the example 1, a high content of grinding aid is added in the primary cryogenic cooling process, the excessive grinding aid not only completely covers the nylon powder, but also early collides with the grinding aid to agglomerate, and although the finally sintered workpiece also plays a role in enhancing, the agglomerated reinforcing agent is equivalent to an insufficient point in the workpiece, so that the elongation at break is remarkably reduced.
Comparing example 2 and example 3, the content of the reinforcing agent in the preferred range not only can perform a reinforcing function to the material, but also the toughness of the material is not poor.
From examples 3 and 4, it can be seen that the multicomponent copolymerized nylon powder having good fluidity and excellent mechanical properties can be obtained by quantitatively adding various single additives as a grinding aid.
As can be seen from examples 2, 3, 4, 5 and 6, the method is generally applicable to multi-copolymerized nylon with different repeating monomers, the sintering temperature of the materials with different repeating monomers is maintained at a low temperature level, and the obtained finished powder has good powder flowability, sintering stability and mechanical properties.
The above-mentioned embodiments only express various embodiments of the present invention, and the description thereof is more specific and detailed, but not meant to limit the scope of the invention. It will be apparent to those skilled in the art that various changes and modifications can be made without departing from the spirit and scope of the invention, and the scope of the invention is to be determined by the appended claims.
Claims (10)
1. A preparation method of multi-component copolymerized nylon powder for selective laser sintering is characterized by comprising the following steps:
step one, adding the multicomponent copolymer nylon granules into a cryogenic grinder, and carrying out primary grinding at a grinding rotor frequency of 15-30 Hz in a liquid nitrogen environment atmosphere at the temperature of-90 to-130 ℃ to obtain crude multicomponent copolymer nylon powder with D50 of 200-500 mu m;
step two, mixing the multicomponent copolymer nylon powder coarse material and a grinding aid to obtain a mixed coarse material, adding the mixed coarse material into a cryogenic grinder, and carrying out secondary grinding at a grinding rotor frequency of 25-50 Hz in a liquid nitrogen environment atmosphere at-100 to-160 ℃ to obtain the multicomponent copolymer nylon fine powder with D50= 30-70 mu m;
adding a flow assistant, an antioxidant and a reinforcing agent into the multi-component copolymerized nylon fine powder, and mixing at a low speed of 100-300 r/min for 20-60 min to obtain multi-component copolymerized nylon powder for selective laser sintering; wherein,
the weight ratio of the multielement copolymerized nylon fine powder to the flow additive to the antioxidant to the reinforcing agent is as follows: 100: 0.2-3: 0.1-2: 0-50.
2. The method of claim 1, wherein mixing the multicomponent copolymerized nylon powder coarse material with a grinding aid to obtain a mixed coarse material specifically comprises:
and stirring the multi-component copolymerized nylon powder coarse material and the grinding aid in a high-speed stirrer at a rotating speed of 600-1500 r/min for 2-10 min to prepare a mixed coarse material.
3. The preparation method according to claim 2, wherein the formula for calculating the weight percentage M of the grinding aid to the mixed coarse material is as follows:
wherein D is the average particle size of the grinding aid, D is D50 of the multi-component copolymerized nylon powder coarse material, ρ D is the density of the grinding aid, ρ D is the density of the multi-component copolymerized nylon powder coarse material, K is the coverage coefficient, and K is 20-200%.
4. The method of claim 3, wherein K = 100%.
5. The method of claim 1, wherein the multipolymer nylon pellets have a repeating monomer structure consisting of three or more nylon monomers.
6. The method of claim 5, wherein the poly-copolymerized nylon pellets have a repeating monomer structure consisting of the monomers PA6 and PA66, and any one of the monomers PA46, PA610, PA10, PA12 and PA 1212.
7. The preparation method according to claim 1, wherein the liquid nitrogen environment temperature in the second step is 10-30 ℃ below the brittle point of the multicomponent copolymerized nylon pellets.
8. The method according to any one of claims 1 to 7, wherein the grinding aid is one or a mixture of two or more of a flow aid, an antioxidant and a reinforcing agent, and the grinding aid has an average particle diameter of 0.01 to 10 μm.
9. The preparation method according to claim 8, wherein the flow assistant is one or more of fumed silica, nano silicon carbide, nano calcium oxide, nano alumina, titanium dioxide and calcium carbonate.
10. The preparation method according to claim 9, wherein the reinforcing agent is one or more of glass beads, glass fibers, carbon fibers, micaceous stone, calcium chloride, titanium dioxide and talcum powder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010695820.2A CN111873427B (en) | 2020-07-20 | 2020-07-20 | Preparation method of multi-component copolymerized nylon powder for selective laser sintering |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010695820.2A CN111873427B (en) | 2020-07-20 | 2020-07-20 | Preparation method of multi-component copolymerized nylon powder for selective laser sintering |
Publications (2)
Publication Number | Publication Date |
---|---|
CN111873427A true CN111873427A (en) | 2020-11-03 |
CN111873427B CN111873427B (en) | 2022-08-16 |
Family
ID=73154747
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010695820.2A Active CN111873427B (en) | 2020-07-20 | 2020-07-20 | Preparation method of multi-component copolymerized nylon powder for selective laser sintering |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111873427B (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106111295A (en) * | 2016-06-21 | 2016-11-16 | 江苏密友粉体新装备制造有限公司 | A kind of deep cooling crush superfines preparation method |
CN106380610A (en) * | 2016-09-23 | 2017-02-08 | 江西师范大学 | Method for preparing polyether sulfone powder consumable item for 3D printing of laser sintering and molding |
-
2020
- 2020-07-20 CN CN202010695820.2A patent/CN111873427B/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106111295A (en) * | 2016-06-21 | 2016-11-16 | 江苏密友粉体新装备制造有限公司 | A kind of deep cooling crush superfines preparation method |
CN106380610A (en) * | 2016-09-23 | 2017-02-08 | 江西师范大学 | Method for preparing polyether sulfone powder consumable item for 3D printing of laser sintering and molding |
Also Published As
Publication number | Publication date |
---|---|
CN111873427B (en) | 2022-08-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2857154C (en) | Agglomerated boron nitride particles, composition containing said particles, and three-dimensional integrated circuit having layer comprising said composition | |
JP2016135729A (en) | Boron nitride aggregated particle, and method for producing the same, composition containing the same, and molding containing the same | |
JP2015006980A (en) | Boron nitride aggregated particle, aggregated bn particle-containing resin composition, and heat-radiation sheet | |
CN109749442B (en) | Polyimide powder material for selective laser sintering and preparation method and application thereof | |
JP2017036415A (en) | Heat release resin sheet and device containing heat release resin sheet | |
CN111362698A (en) | Novel isotropic nuclear-grade graphite material and preparation method thereof | |
CN109534828A (en) | A kind of prilling process of silicon carbide composite ceramic materials | |
CN111873427B (en) | Preparation method of multi-component copolymerized nylon powder for selective laser sintering | |
CN115198168B (en) | FeCrAl alloy powder and preparation method thereof | |
CN112812497A (en) | Wear-resistant PEEK composite material | |
CN114350234A (en) | High-toughness bending-resistant powder coating and preparation method thereof | |
WO2003040060A1 (en) | Boron carbide based sintered compact and method for preparation thereof | |
CN111423723A (en) | Reinforced polyphenylene sulfide composition for 5G and preparation method thereof | |
CN113667130A (en) | Thermoplastic polyamide elastomer powder for selective laser sintering and preparation method thereof | |
CN111690861B (en) | Contains TiO2Cermet cutter material and preparation method thereof | |
CN107963632B (en) | Porous silicon dioxide modified material and preparation method thereof | |
CN114477837B (en) | Water reducing agent and preparation method thereof | |
CN112126220A (en) | Reinforced wear-resistant PA/UHMWPE alloy material and preparation method thereof | |
CN114853488B (en) | Silicon carbide-based furnace eye repairing material and production process thereof | |
CN111363351A (en) | Polyamide 66 composition and preparation method thereof | |
CN104878235A (en) | Metal-binding silicon carbide ceramic and preparation method thereof | |
CN114892038B (en) | High sphericity Cr-base alloy-TiB with excellent fluidity 2 Micro-nano powder and preparation method thereof | |
CN1234645C (en) | Ceramic sliding bearing and producing method thereof | |
CN113121210A (en) | Nano-grade alumina ceramic powder, composite ceramic material and preparation method thereof | |
CN105274417B (en) | A method of preparing Nd-Fe-B magnet steel using neodymium-iron-boron air stream millby tailing |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
CB02 | Change of applicant information |
Address after: No. 181, Linyu Road, national high tech Industrial Development Zone, Changsha City, Hunan Province, 410205 Applicant after: Hunan Huashu High Tech Co.,Ltd. Address before: No. 181, Linyu Road, national high tech Industrial Development Zone, Changsha City, Hunan Province, 410205 Applicant before: HUNAN FARSOON HIGH-TECH Co.,Ltd. |
|
CB02 | Change of applicant information | ||
GR01 | Patent grant | ||
GR01 | Patent grant |