CN110003637A - A kind of medical material and preparation method thereof - Google Patents

A kind of medical material and preparation method thereof Download PDF

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Publication number
CN110003637A
CN110003637A CN201910293812.2A CN201910293812A CN110003637A CN 110003637 A CN110003637 A CN 110003637A CN 201910293812 A CN201910293812 A CN 201910293812A CN 110003637 A CN110003637 A CN 110003637A
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particle
blending
medical material
tpe
preparation
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何光彬
李兆敏
秦明林
张百灵
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Maitong Medical Technology (jiaxing) Co Ltd
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Maitong Medical Technology (jiaxing) Co Ltd
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Priority to CN201910293812.2A priority Critical patent/CN110003637A/en
Publication of CN110003637A publication Critical patent/CN110003637A/en
Priority to PCT/CN2020/082925 priority patent/WO2020207320A1/en
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/22Compounding polymers with additives, e.g. colouring using masterbatch techniques
    • C08J3/226Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04Homopolymers or copolymers of ethene
    • C08J2323/08Copolymers of ethene
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2353/00Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2353/00Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
    • C08J2353/02Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers of vinyl aromatic monomers and conjugated dienes
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2371/00Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2375/00Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
    • C08J2375/04Polyurethanes
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2423/04Homopolymers or copolymers of ethene
    • C08J2423/08Copolymers of ethene
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2453/00Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2453/00Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
    • C08J2453/02Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers of vinyl aromatic monomers and conjugated dienes
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2471/00Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2475/00Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2491/00Characterised by the use of oils, fats or waxes; Derivatives thereof
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
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    • C08K3/02Elements
    • C08K3/08Metals
    • C08K2003/0887Tungsten
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    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
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    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/20Carboxylic acid amides

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
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  • Processes Of Treating Macromolecular Substances (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The invention discloses a kind of medical material and preparation method thereof, the preparation method includes the following steps: S1: thermoplastic elastomer (TPE) being passed through extrusion granulation, obtains thermoplastic elastomer (TPE) particle;S2: the thermoplastic elastomer (TPE) particle and filler blending extrusion that the step S1 is obtained obtain filler master batch;S3: the filler master batch and color masterbatch particle blending extrusion that the obtained thermoplastic elastomer (TPE) particle of the step S1 and the step S2 are obtained obtain medical material;S4: adding lubricant in the blending and modifying particle that the step S3 is obtained, and by blending extrusion, obtains the medical material that pellet melting index is 20-50g/min.Preparation method provided by the invention solves the thermoplastic elastic material of high-hard section ratio bad dispersibility, easily foaming and the problems such as poor fluidity in process.Prepared medical material may be used on the products such as electro physiology radio frequency ablation catheter and mapping catheter.

Description

A kind of medical material and preparation method thereof
Technical field
The present invention relates to a kind of bio-medical raw material and preparation method thereof more particularly to a kind of thermoplastic elastomer (TPE) are medical Material and preparation method thereof.
Background technique
It is that medicine covers painstaking effort to one of the significant contribution of human civilization at the end of the 20th century that Micro trauma, which intervenes medical technology, The science and technology such as pipe, the cerebrovascular, main artery, periphery, electro physiology.Micro-dimension medical tube is the key that Micro trauma interventional medical device Material, requirement of the Micro trauma interventional medical device to micro-dimension medical tube is very high, and technical difficulty is big, always by American-European institute, company Monopolization.In the past 20 years, the main difficult technical of China's Micro trauma interventional medical device micro-dimension medical tube industrialization includes medical Synthesis of polymer material, medical macromolecular materials modification, micro- extrusion, welding, grinding, braiding, spring, condensed state structure regulation etc. Key technology and key equipment.
There is good compatibility and heat fusing between the medical macromolecular materials of identical series different hardness, for minimally invasive When hurting interventional medical device, the different piece for selecting different materials to make conduit can according to need, to obtain hardness gradient Conduit.Because Micro trauma interventional medical device conduit and conveyer are usually all long, leading portion requires softness, to pass through people The curved blood vessel of body reaches lesion;And back segment requires have certain degree of hardness, just can guarantee there is foot during conduit enters human body Enough support forces.
Thermoplastic elastomer (TPE) is a kind of thermoplastic multi-block copolymer, due to its good biocompatibility, good Anticoagulant property and good toughness and elasticity, make it have a wide range of applications in field of biomedicine.Existing thermoplastic elastomehc Property body have the defects that in aspect of performance it is certain, such as high-hard section ratio thermoplastic elastomer (TPE) addition barium sulfate, waltherite, When tungsten powder etc. is as developer, but these fillers are in the thermoplastic elastomer (TPE) for being added to high-hard section ratio, processed The duration is short (< 1h) in journey, there are bad dispersibility, easily foams (bubble is more) and the problems such as poor fluidity, seriously affects The processing of later product.Therefore, it is necessary to the thermoplastic elastomer blending materials to existing high-hard section ratio to be modified.
Summary of the invention
The technical problem to be solved by the present invention is to thermoplastic elastomer (TPE)s when adding filler blending developing material, this is filled out It fills object and developing material bad dispersibility, easily foaming and poor fluidity in process is blended.
The present invention to solve above-mentioned technical problem and the technical solution adopted is that provide a kind of preparation method of medical material, Include the following steps: S1: by thermoplastic elastomer (TPE) by extrusion granulation, obtaining thermoplastic elastomer (TPE) particle;S2: by the step The thermoplastic elastomer (TPE) particle and filler blending extrusion that S1 is obtained, obtain filler master batch;S3: the step S1 is obtained The filler master batch and color masterbatch particle blending extrusion that thermoplastic elastomer (TPE) particle and the step S2 are obtained, obtain blending and modifying grain Son;S4: adding lubricant in the blending and modifying particle that the step S3 is obtained, and by blending extrusion, obtains pellet melting and refers to Number is the medical material of 20-50g/10min.
Preferably, the step S1 includes: by the thermoplastic elastomer (TPE) by twin-screw blending extrusion machine, and extrusion obtains Cylindrical thermoplastic elastomer (TPE) particle.
Preferably, in the step S1, the thermoplastic elastomer (TPE) is polyether block amide, thermoplastic polyurethane elastic At least one of body, styrene block copolymer, Styrene-Butadiene-Styrene Block Copolymer or octene copolymer.
Preferably, in the step S2, the filler is at least one of barium sulfate, waltherite or tungsten powder.
Preferably, in the step S2, the quality of the thermoplastic elastomer (TPE) particle is the filler master batch quality 40%~70%, the thermoplastic elastomer (TPE) particle and the filler squeeze out to obtain the filling through twin-screw blending extrusion machine Object master batch.
Preferably, in the step S3, the thermoplastic elastomer (TPE) mass particle is the blending and modifying mass particle 10%~40%, the filler master batch quality is the 20%-59% of the blending and modifying mass particle, the thermoplastic elastic Body particle, the filler master batch and the color masterbatch particle pass through after mixing evenly twin-screw blending extrusion machine squeeze out to obtain it is described Blending and modifying particle.
Preferably, the lubricant quality added in the step S4 is the 2%-10% of the blending and modifying mass particle.
Preferably, the twin-screw blending extrusion machine set temperature be 180-240 DEG C, screw speed be 400-1200 turn/ Minute.
Preferably, lubricant described in the step S4 is at least one of white oil, stearic amide or paraffin powder.
Another technical solution that the present invention uses to solve above-mentioned technical problem is to provide a kind of medical material, by above-mentioned Preparation method is produced.
The present invention compare the prior art have it is following the utility model has the advantages that medical material provided by the invention and preparation method thereof, Thermoplastic elastomer (TPE), using being blended after addition lubricant, effectively improves filler when adding filler blending developing material The blend uniformity and mobility of developing material is blended, it is easy to stick in process to solve filler blending developing material material The problems such as mould, agglomeration, bad dispersibility, easy foaming and poor fluidity, and this process implementing is simple, it is low in cost, it is easy to criticize Quantization production.Prepared medical material may be used on the products such as electro physiology radio frequency ablation catheter and mapping catheter.
Specific embodiment
The present invention will be further described with reference to the examples below.
Embodiment 1
Firstly, the thermoplastic elastomer (TPE) of predetermined amount is passed through twin-screw blending extrusion machine, its internal crafters is removed, is squeezed It is granulated out, obtains cylindrical thermoplastic elastomer (TPE) particle.The twin-screw blending extrusion machine may include multistage temperature, and each section Temperature range can be same or different.In the present embodiment, each section of temperature range is different, but each section of temperature range It is set in 180-240 DEG C of section.The screw speed of the twin-screw blending extrusion machine is set as 500 revs/min.Specifically Ground, the thermoplastic elastomer (TPE) can be the thermoplastic elastomer (TPE) of high-hard section ratio, such as can be polyether block amide (PEBA), thermoplastic polyurethane elastomer (TPU), styrene block copolymer (SBC), s-B-S block The materials such as copolymer (SBS) or octene copolymer (POE).In the present invention, thermoplastic elastomer (TPE) can be by soft segment and hard section structure At definition of the hard section ratio greater than or equal to 90% is the thermoplastic elastomer (TPE) of high-hard section ratio.
Then, obtained thermoplastic elastomer (TPE) particle is blended according to a certain percentage with filler, is blended and squeezes through twin-screw Machine squeezes out the filler master batch being blended out.In the present embodiment, the filler can be developing material, such as can be At least one of barium sulfate, waltherite or tungsten powder etc..The quality of the thermoplastic elastomer (TPE) particle is the filler master batch The 40%~70% of quality.In 180-240 DEG C of section, screw rod turns the set temperature of each section of the twin-screw blending extrusion machine Speed is 400-1200 revs/min.
Then, thermoplastic elastomer (TPE) particle, filler master batch and color masterbatch particle are stirred evenly according to predetermined ratio, is passed through Twin-screw blending extrusion machine squeezes out, and obtains the blending and modifying particle of corresponding color.The thermoplastic elastomer (TPE) mass particle can be with It is the 10%~40% of the blending and modifying mass particle, the filler master batch quality can be the blending and modifying particle matter The 20%-59% of amount.
Finally, adding lubricant in obtained blending and modifying particle, the lubricant quality of addition is blending and modifying particle The 2% of quality, lubricant can be at least one of white oil, stearic amide, paraffin powder etc., and twin-screw blending extrusion machine is set Fixed temperature is 180~220 DEG C, and 400~1200 revs/min of screw speed, the pellet melting index being blended is 20-50g/ min.Addition lubricant effect be reduce material between and material and process equipment surface frictional force, to reduce melt Flow resistance reduces melt viscosity, improves the mobility of melt, avoid the adherency of melt and equipment, improve the light of product surface Slippery.A kind of numerical value of mobility when melt index is expression plastic material processing.Its test method is first plastic pellet to be allowed to exist In certain time (10 minutes), under certain temperature and pressure, it is melted into plastic liquid, is then 2.095mm circle by a diameter Gram (g) number that pipe is flowed out.Its value is bigger, indicates that the processing fluidity of the plastic material is better, on the contrary then poorer.Melt index The viscosity flow characteristic of thermoplastic in the molten state can be characterized, to the quality for guaranteeing thermoplastic and its product, to adjustment Production technology has important directive significance.
Embodiment 2
The present embodiment is identical as the product structure of embodiment 1 and production technology, and difference is the ratio of the lubricant added Example is different, and the lubricant quality of addition is the 5% of blending and modifying mass particle, and the pellet melting index being blended is 22g/ 10min~29g/10min.
Embodiment 3
The present embodiment is identical as the product structure of embodiment 1 and production technology, and difference is the ratio of the lubricant added Example is different, and the lubricant quality of addition is the 8% of blending and modifying mass particle, and the pellet melting index being blended is 35g/ 10min~39g/10min.
Embodiment 4
The present embodiment is identical as the product structure of embodiment 1 and production technology, and difference is the ratio of the lubricant added Example is different, and the lubricant quality of addition is the 10% of blending and modifying mass particle, and the pellet melting index for being blended out is 43g/ 10min~48g/10min.
To sum up, the preparation method of medical material provided by the invention has the advantage that
A) thermoplastic elastomer (TPE) of high-hard section ratio is solved by way of blending in addition barium sulfate, waltherite, tungsten When developing material is blended in the fillers such as powder, bad dispersibility in process, the problem of easily foaming.
B) using being blended after adding a kind of lubricant, the blending for effectively improving the thermoplastic elastomer (TPE) of high-hard section ratio is equal Even property and mobility solve the material the process poor fluidity the problems such as.
C) method preparation process provided by the invention is simple, can carry out successional large-scale production.By to double spiral shells The regulation of bar blending extrusion machine temperature, screw speed and lubricant ratio can reach molten to material particles after blending and modifying Melt the control of index.
Although the present invention is disclosed as above with preferred embodiment, however, it is not to limit the invention, any this field skill Art personnel, without departing from the spirit and scope of the present invention, when can make a little modification and perfect therefore of the invention protection model It encloses to work as and subject to the definition of the claims.

Claims (10)

1. a kind of preparation method of medical material, which comprises the steps of:
S1: thermoplastic elastomer (TPE) is passed through into extrusion granulation, obtains thermoplastic elastomer (TPE) particle;
S2: the thermoplastic elastomer (TPE) particle and filler blending extrusion that the step S1 is obtained obtain filler master batch;
S3: the filler master batch and Masterbatch that the obtained thermoplastic elastomer (TPE) particle of the step S1 and the step S2 are obtained Sub- blending extrusion obtains blending and modifying particle;
S4: adding lubricant in the blending and modifying particle that the step S3 is obtained, and by blending extrusion, obtains pellet melting and refers to Number is the medical material of 20-50g/10min.
2. the preparation method of medical material as described in claim 1, which is characterized in that the step S1 includes: by the heat Thermoplastic elastic passes through twin-screw blending extrusion machine, and extrusion obtains cylindrical thermoplastic elastomer (TPE) particle.
3. the preparation method of medical material as described in claim 1, which is characterized in that the thermoplastic elastomer (TPE) is that polyethers is embedding Section amide, thermoplastic polyurethane elastomer, styrene block copolymer, Styrene-Butadiene-Styrene Block Copolymer or pungent At least one of alkene copolymer.
4. the preparation method of medical material as described in claim 1, which is characterized in that in the step S2, the filler For at least one of barium sulfate, waltherite or tungsten powder.
5. the preparation method of medical material as described in claim 1, which is characterized in that in the step S2, the thermoplasticity The quality of elastomer particle is the 40%~70% of the filler master batch quality, and the thermoplastic elastomer (TPE) particle is filled out with described Object is filled to squeeze out to obtain the filler master batch by twin-screw blending extrusion machine.
6. the preparation method of medical material as described in claim 1, which is characterized in that in the step S3, the thermoplasticity Elastomer particle quality is the 10%~40% of the blending and modifying mass particle, and the filler master batch quality is the blending The 20%-59% of modified particle quality, the thermoplastic elastomer (TPE) particle, the filler master batch and the color masterbatch particle stir It squeezes out to obtain the blending and modifying particle by twin-screw blending extrusion machine after uniformly.
7. the preparation method of medical material as described in claim 1, which is characterized in that the lubricant added in the step S4 Quality is the 2%-10% of the blending and modifying mass particle.
8. the preparation method of the medical material as described in claim 2,5 or 6, which is characterized in that the twin-screw blending extrusion Machine set temperature is 180-240 DEG C, and screw speed is 400-1200 revs/min.
9. the preparation method of medical material as described in claim 1, which is characterized in that lubricant described in the step S4 is At least one of white oil, stearic amide or paraffin powder.
10. a kind of medical material, which is characterized in that the medical material is by the described in any item preparation methods of claim 1-9 It produces.
CN201910293812.2A 2019-04-12 2019-04-12 A kind of medical material and preparation method thereof Pending CN110003637A (en)

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CN111040429A (en) * 2019-12-30 2020-04-21 脉通医疗科技(嘉兴)有限公司 Medical tube and preparation method thereof
WO2020207320A1 (en) * 2019-04-12 2020-10-15 脉通医疗科技(嘉兴)有限公司 Medical material and preparation method thereof
CN111939328A (en) * 2020-08-18 2020-11-17 西安乐析医疗科技有限公司 Novel peritoneal dialysis tube and manufacturing method thereof
CN113861379A (en) * 2020-06-30 2021-12-31 三元科技(深圳)有限公司 Manufacturing method of TPU (thermoplastic polyurethane) medical cable and medical cable

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CN104861303A (en) * 2015-06-12 2015-08-26 福路明精密管材(北京)有限公司 Medical polypropylene composite material and preparation method thereof
CN105727375A (en) * 2016-02-02 2016-07-06 乐普(北京)医疗器械股份有限公司 Nylon blend and preparation method and application thereof
CN108276638A (en) * 2017-12-29 2018-07-13 深圳职业技术学院 A kind of tubing and preparation method thereof with X-ray developing function

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* Cited by examiner, † Cited by third party
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WO2020207320A1 (en) * 2019-04-12 2020-10-15 脉通医疗科技(嘉兴)有限公司 Medical material and preparation method thereof
CN111040429A (en) * 2019-12-30 2020-04-21 脉通医疗科技(嘉兴)有限公司 Medical tube and preparation method thereof
CN111040429B (en) * 2019-12-30 2021-12-24 脉通医疗科技(嘉兴)有限公司 Medical tube and preparation method thereof
CN113861379A (en) * 2020-06-30 2021-12-31 三元科技(深圳)有限公司 Manufacturing method of TPU (thermoplastic polyurethane) medical cable and medical cable
CN111939328A (en) * 2020-08-18 2020-11-17 西安乐析医疗科技有限公司 Novel peritoneal dialysis tube and manufacturing method thereof

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Application publication date: 20190712