CN109228008A - A kind of emulsifier unit and its preparation process of highly resistance folding SBS composite material - Google Patents
A kind of emulsifier unit and its preparation process of highly resistance folding SBS composite material Download PDFInfo
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- CN109228008A CN109228008A CN201811028545.8A CN201811028545A CN109228008A CN 109228008 A CN109228008 A CN 109228008A CN 201811028545 A CN201811028545 A CN 201811028545A CN 109228008 A CN109228008 A CN 109228008A
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- emulsification
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- 239000002131 composite material Substances 0.000 title claims abstract description 34
- 238000002360 preparation method Methods 0.000 title claims abstract description 22
- 239000003995 emulsifying agent Substances 0.000 title claims abstract description 15
- 238000003756 stirring Methods 0.000 claims abstract description 58
- 238000004945 emulsification Methods 0.000 claims abstract description 43
- 239000000839 emulsion Substances 0.000 claims abstract description 20
- -1 flat holder Substances 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims description 63
- 238000002156 mixing Methods 0.000 claims description 51
- 238000011161 development Methods 0.000 claims description 48
- 239000000203 mixture Substances 0.000 claims description 41
- 230000008961 swelling Effects 0.000 claims description 39
- 239000004615 ingredient Substances 0.000 claims description 31
- 239000000084 colloidal system Substances 0.000 claims description 28
- 239000000344 soap Substances 0.000 claims description 22
- 230000000694 effects Effects 0.000 claims description 19
- 238000004321 preservation Methods 0.000 claims description 19
- 238000003860 storage Methods 0.000 claims description 19
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 18
- 238000007664 blowing Methods 0.000 claims description 17
- 239000011159 matrix material Substances 0.000 claims description 17
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 15
- 239000000835 fiber Substances 0.000 claims description 15
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 14
- 239000002994 raw material Substances 0.000 claims description 13
- 238000002347 injection Methods 0.000 claims description 12
- 239000007924 injection Substances 0.000 claims description 12
- 238000005496 tempering Methods 0.000 claims description 12
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 10
- 239000000654 additive Substances 0.000 claims description 10
- 230000000996 additive effect Effects 0.000 claims description 10
- 238000012216 screening Methods 0.000 claims description 10
- 238000010008 shearing Methods 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000001569 carbon dioxide Substances 0.000 claims description 9
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 9
- 238000000227 grinding Methods 0.000 claims description 9
- 238000003723 Smelting Methods 0.000 claims description 8
- 125000004122 cyclic group Chemical group 0.000 claims description 8
- 239000000758 substrate Substances 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000003963 antioxidant agent Substances 0.000 claims description 6
- 230000003078 antioxidant effect Effects 0.000 claims description 6
- 239000000314 lubricant Substances 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 6
- 244000043261 Hevea brasiliensis Species 0.000 claims description 5
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 5
- 239000004743 Polypropylene Substances 0.000 claims description 5
- 239000000919 ceramic Substances 0.000 claims description 5
- 239000006185 dispersion Substances 0.000 claims description 5
- 239000000395 magnesium oxide Substances 0.000 claims description 5
- 229920003052 natural elastomer Polymers 0.000 claims description 5
- 229920001194 natural rubber Polymers 0.000 claims description 5
- 229920001155 polypropylene Polymers 0.000 claims description 5
- 238000005485 electric heating Methods 0.000 claims description 4
- 229910017059 organic montmorillonite Inorganic materials 0.000 claims description 4
- 239000000498 cooling water Substances 0.000 claims description 3
- 238000007654 immersion Methods 0.000 claims description 3
- 230000002045 lasting effect Effects 0.000 claims description 3
- 239000000284 extract Substances 0.000 claims description 2
- 238000002955 isolation Methods 0.000 claims description 2
- 239000002826 coolant Substances 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 15
- 230000018109 developmental process Effects 0.000 description 40
- 238000000034 method Methods 0.000 description 30
- 230000008569 process Effects 0.000 description 20
- 239000000243 solution Substances 0.000 description 13
- 239000002904 solvent Substances 0.000 description 10
- 238000007792 addition Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
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- 230000033001 locomotion Effects 0.000 description 5
- 239000007921 spray Substances 0.000 description 5
- 230000004927 fusion Effects 0.000 description 4
- 229920002521 macromolecule Polymers 0.000 description 4
- 238000009792 diffusion process Methods 0.000 description 3
- 239000004816 latex Substances 0.000 description 3
- 229920000126 latex Polymers 0.000 description 3
- 238000012806 monitoring device Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000007600 charging Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000006071 cream Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000009775 high-speed stirring Methods 0.000 description 2
- 230000001965 increasing effect Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 238000004513 sizing Methods 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- SPSPIUSUWPLVKD-UHFFFAOYSA-N 2,3-dibutyl-6-methylphenol Chemical compound CCCCC1=CC=C(C)C(O)=C1CCCC SPSPIUSUWPLVKD-UHFFFAOYSA-N 0.000 description 1
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical group C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 description 1
- 244000198134 Agave sisalana Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- 241000282320 Panthera leo Species 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000003712 anti-aging effect Effects 0.000 description 1
- 230000000703 anti-shock Effects 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 235000010354 butylated hydroxytoluene Nutrition 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000002788 crimping Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
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- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 150000007974 melamines Chemical class 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 238000005502 peroxidation Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- ILRLTAZWFOQHRT-UHFFFAOYSA-N potassium;sulfuric acid Chemical compound [K].OS(O)(=O)=O ILRLTAZWFOQHRT-UHFFFAOYSA-N 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 description 1
Classifications
-
- 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
-
- 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
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L53/02—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes
-
- 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
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/20—Oxides; Hydroxides
- C08K3/22—Oxides; Hydroxides of metals
- C08K2003/2217—Oxides; Hydroxides of metals of magnesium
- C08K2003/222—Magnesia, i.e. magnesium oxide
-
- 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
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
- C08L2205/035—Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Accessories For Mixers (AREA)
Abstract
The invention discloses a kind of emulsifier units of highly resistance folding SBS composite material, including flat holder, emulsion chamber and banburying chamber are fixedly installed at the top of flat holder, the emulsion chamber includes the heat-flash device from top to bottom set gradually, mixed stirring device and Emulsification grinder, the heat-flash device and mixed stirring device are connected to the first direct current conduit and the second direct current conduit respectively, the heat-flash device, it is connected to by electromagnetism conducting tube between mixed stirring device and Emulsification grinder, and it is also connected to by air pump conveying device between heat-flash device and Emulsification grinder, it further include a kind of preparation process, based on the preparation process, the present invention is formed in the interior thereof netted or island structure, has stronger fracture resistance, realize the production of streamlined and staggered form, improve the efficiency of single unit system.
Description
Technical field
The present invention relates to technical field of composite preparation, specially a kind of emulsifier unit of highly resistance folding SBS composite material
And its preparation process.
Background technique
Polystyrene-polybutadiene-polystyrene block copolymer (SBS) is good, inexpensive with chemical stability and processes
Convenient advantage is one of general-purpose plastics important in current industrial application, but its impact strength is not high, easily-deformable, and
Also application and transport can be restrict due to its fracture resistance difference in practical applications, be based on drawbacks described above, seriously limit SBS
Extensive use.
In order to expand the application field of SBS, toughening is generally carried out to SBS using inorganic rigid particle, improves the strong of material
Degree and toughness, but since the surface between inorganic rigid particle and SBS can differ larger, interfacial bonding is weak, makes phase between the two
Capacitive is poor, easily reunites, and affects dispersion of the inorganic rigid particle in SBS matrix, seriously limits modified effect.
In existing technical solution, a kind of ageing-resistant sisal fiber such as announced application No. is 201710551038.1 changes
Property SBS composite material, makes it have anti-aging and shock proof ability by multiple correlation material.But in summary technology
Scheme and reality there are the problem of, and combine the technical solution being widely used at present, there is also the main body of major defect
Present the following aspects:
(1) in existing formula, often lack the substance of facilitation, so that can not between SBS and other ingredients
Complete mutually fusion, therefore to reach design effect and just have to largely using expensive SBS, this is for SBS composite material
Extensive application for, higher cost；
(2) in existing technique, technical process control is complexity, needs to quantify the parameter of its production process then
It controls one by one, and the production process can't reach the performance required in design for SBS composite material；
(3) technique in the prior art and relevant preparation facilities are combined, one-stop flow line production technique is lacked, it is past
It is separated from each other, is then produced according to the process flow made, this will lead to following toward using between each process
The problem of two aspects: first, technique will be more complicated, need manually to carry out high-intensitive intervention, but also can not be timely
The addition of carry out ingredient and mixing；Secondly, can not achieve the intersection between technique for the cooperation processing between process
Cooperation needs other related equipment toward contact to cooperate and could complete relevant production process.
Summary of the invention
In order to overcome the shortcomings of that prior art, the present invention provide a kind of emulsifier unit of highly resistance folding SBS composite material
And its preparation process, it can effectively solve the problem of background technique proposes.
The technical solution adopted by the present invention to solve the technical problems is:
A kind of emulsifier unit of highly resistance folding SBS composite material, including substrate and be sequentially fixed on bottom susceptor on substrate,
H-type bracket and flat holder are fixedly installed with swelling room in the H-type cradle top, pass through material baffle below the swelling room
Development room is installed, and is equipped with electromagnetism conveying pipeline between swelling room and development room, the swelling room two sides pass through caching respectively
Pipe and the first direct current conduit be connected with constant temperature locker room and emulsion chamber, development room side by the second direct current conduit also with cream
Change room connection, and banburying chamber is installed also by material baffle in the bottom of emulsion chamber, the constant temperature locker room is fixedly mounted on bottom
On pedestal, and the emulsion chamber and banburying chamber are fixedly mounted on flat holder；
The emulsion chamber includes heat-flash device, mixed stirring device and the Emulsification grinder from top to bottom set gradually,
The heat-flash device and mixed stirring device are connected to the first direct current conduit and the second direct current conduit respectively, the heat-flash device,
It is connected to by electromagnetism conducting tube between mixed stirring device and Emulsification grinder, and in heat-flash device and Emulsification grinder
Between be also connected to by air pump conveying device；
Emulsification grinder includes colloid mill, and the inlet of the colloid mill is fixedly installed with two drainage tubes, and this two
Root drainage tube is connected separately with main drainage pump and mixed stirring device, and the main drainage pump is connected with soap lye room, the colloid mill
Outlet end multilevel screen is fixedly installed with by Y-shaped bracket, the equal and horizontal plane oblique of the multilevel screen, and in multistage
The bottom of every layer of sieve is fixedly installed with longitudinal vibration motor, and every layer of lower section of the multilevel screen is equipped with screening material pond, described
It is connect by secondary drainage tube with soap lye pond in screening material pond, and is fixedly installed with circulating pump in screening material pond, it is described
Circulating pump is connected to by diversion pipe with heat-flash device.
As a preferred technical solution of the present invention, the heat-flash device includes heat-flash hermetically sealed can, the heat-flash sealing
It is fixedly installed with the deflector arranged in the shape of a spiral inside tank, and is fixedly installed on the deflector for being located at top and heat-flash
The vertical chromatoplate in hermetically sealed can surface, the chromatoplate center is equipped with transporting corresponding with deflector hole, at the edge of chromatoplate
It is fixedly installed with the heat preservation baffler parallel with heat-flash hermetically sealed can surface, is equipped between the heat preservation baffler and heat-flash hermetically sealed can
Cyclic annular cyclic gap channel is directly connected in the bottom of heat preservation baffler with the deflector for being located at bottommost, the heat preservation barrier
It is fixedly installed on the inner wall of plate and deflector and forces hot plate.
Several auxiliary materials are equipped with as a preferred technical solution of the present invention, at the top of the mixed stirring device to enter
Pipe, and it is respectively equipped with blender and mixing drum at the mixed stirring device both ends and center, it is fixedly mounted on the blender
There are several pieces of stirring accessory lobes, the mixing drum is mounted on mixed stirring device by lateral shaft, vertical on the mixing drum
Several blocks of setback plates being parallel to each other are installed in mixing drum axial restraint, and solid by isolation flitch between adjacent wave folded plate
Dingan County is equipped with chain bucket.
As a preferred technical solution of the present invention, blowing is also fixedly installed on the inner wall of mixed stirring device both ends
Device, the blowing device include the blowing pump being located on the outside of mixed stirring device, and the blowing pump passes through injection tube and is located at
Several injection holes connection on mixed stirring device, the injection hole has several groups, and is located at mixed stirring device top
Pressure-control valve is equipped in the injection hole of portion and bottom.
As a preferred technical solution of the present invention, the constant temperature locker room includes tempering tower and terminal storage tank, institute
It states and is connected between tempering tower and terminal storage tank by drain pipe, the tempering tower is connected by extracting pump conveying device and development room
It is logical, several pieces of electric heating blocks are also uniformly installed, and pass through air pressure in terminal storage tank top on the terminal storage top tank structure
Pipe is connected with pulsometer.
In addition, including the following steps: the present invention also provides a kind of preparation process of highly resistance folding SBS composite material
Step 100, swelling add natural rubber, polypropylene, haloflex according to quality proportioning in pressure reaction still
Heat is until be in molten condition, and continue heat preservation and obtain matrix；
Step 200 mixes the matrix after swelling with SBS according to the proportion, and shearing grinding forms after mixture high-speed stirring again
It mixes, nano organic montmorillonite, toluene, methyl methacrylate is added according to the proportion and is developed for the first time, add after primary development
Matrix after entering swelling carries out secondary development；
Step 300, emulsion dispersion by the mixed material heating after development to 120~130 DEG C, and continue 1~2h of heat preservation, press
Lubricant and crosslinked at low temperature agent is added according to proportion, and the soap lye that emulsifier and high-temperature water are made into is added, by colloid mill by two
Person mixes overground emulsification；
Step 400, mixing, by the original after netted traction-resistant fibre, ceramic fibre, nano magnesia, antioxidant and emulsification
Material, which is placed in mixer, carries out internally mix, is granulated after circulating water through pelleter.
As a preferred technical solution of the present invention, in step 100, the specific steps heated in pressure reaction still
Are as follows:
Raw material are gradually added in pressure reaction still according to the proportion for step 101；
Step 102, the air being passed through into pressure reaction still in carbon dioxide or nitrogen pressure release reaction kettle, and continue
It is passed through carbon dioxide or nitrogen and increases pressure in pressure reaction still to 2~3MPa；
Step 103 is persistently heated to pressure reaction still, and control the pressure in pressure reaction still be maintained at 2~
Between 5MPa, until matrix is obtained in molten condition in pressure reaction still, it is lasting to keep the temperature.
As a preferred technical solution of the present invention, in step 200, the specific steps developed twice are as follows:
First development, sequentially adds ingredient, and continue high-speed stirred and mix them thoroughly, and the temperature improved in device is straight
It to 180~200 DEG C, persistently stirs at low speed, develops 3~4h；
Ingredient is successively added on the basis of primary development in secondary development according to the proportion, is acted on first by high-speed stirred
It mixes them thoroughly, further increases the temperature in device up to 200~210 DEG C, 4~5h is developed in consecutive low temperature stirring.
As a preferred technical solution of the present invention, in step 300, the specific steps of overground emulsification are as follows:
Raw material are added in mixture according to the proportion, and soap lye are added by step 301, are kept for 120~130 DEG C
Temperature impregnates 0.5-1h；
Step 302 soaks colloid mill by 80~100 DEG C of high temperature soap lyes, and continues to pour colloid with high temperature soap lye
Mill is preheated；
Mixture after immersion is sequentially imported and carries out grinding emulsification in colloid mill, and grinds emulsification number by step 303
Not less than 3 times.
As a preferred technical solution of the present invention, in step 400, the specific steps of mixing are carried out by mixer
Are as follows:
Step 401, the parameter for adjusting mixer, so that the smelting temperature of mixer is 250~280 DEG C, the revolving speed of screw rod
For 30~50r/min；
Additive is put into mixer by step 402 according to the proportion, first carries out the mixing of first time additive, and by mixing
Additive afterwards keeps original smelting temperature, is added in mixer mixes with the raw material after emulsification again, improve mixing again
Temperature improves the revolving speed of screw rod to 80~100r/min to 300~320 DEG C；
Step 403, during mixing, the temperature of control loop cooling water gradually reduces it by cooling according to gradient
Water temperature.
Compared with prior art, the beneficial effects of the present invention are:
The present invention can make full use of added SBS ingredient, be formed in the interior thereof netted or island by ingredient
Structure has stronger fracture resistance, in addition, cooperating relevant technique and device, can be realized one-stop streamlined production,
Realize that the operation of pipelining can also realize intersecting for different processes in the assembly line, in different processes or non-phase
Intervention and replenishment of ingredients can be directly carried out in adjacent process, realizes the production of staggered form, reduce ingredient maintenance, storage and addition etc.
Process and the device to match, improve the efficiency of single unit system.
Detailed description of the invention
Fig. 1 is flowage structure schematic diagram of the invention；
Fig. 2 is overall structure of the present invention；
Fig. 3 is present invention swelling cell structure schematic diagram；
Fig. 4 is present invention development cell structure schematic diagram；
Fig. 5 is heat-flash apparatus structure schematic diagram of the present invention；
Fig. 6 is mixed stirring device structural schematic diagram of the present invention；
Fig. 7 is Emulsification grinder structural schematic diagram of the present invention；
Figure label:
1- is swollen room；2- develops room；3- constant temperature locker room；The emulsion chamber 4-；5- banburying chamber；6- heat-flash device；7- mixing is stirred
Mix device；8- Emulsification grinder；9- the first air pump conveying device；10- substrate；11- bottom susceptor；12-H type bracket；13- is flat
Flat bracket；14- material baffle；15- electromagnetism conveying pipeline；16- caching pipe；17- the first direct current conduit；18- the second direct current conduit；
101- pressure reaction still；102- electric heating block；103- top cover；104- feed pipe；105- Pressure behaviour balanced valve；
106- broad-leaved blender；107- inflation air pump；
201- screw extruder；The first auxiliary material of 202- enters pipe；203- extracts pump conveying device；204- ladder platform；
205- high-speed stirred pond；206- agitating shaft；207- stirs accessory lobes；208- shearing is whetted a knife；209- develops pond；210- bubble spray head；
211- first forces hot plate；212- the second air pump conveying device；
301- tempering tower；302- terminal storage tank；303- pulsometer；
601- heat-flash hermetically sealed can；602- deflector；603- chromatoplate；604- keeps the temperature baffler；605- second forces hot plate；
The second auxiliary material of 701- enters pipe；702- blender；703- mixing drum；704- setback plate；705- chain bucket；706- spray
Blowing apparatus；707- blowing pump；708- injection tube；709- pressure-control valve；
801- colloid mill；802- drainage tube；The main drainage pump of 803-；804- soap lye room；805- multilevel screen；806- longitudinally shakes
Dynamic motor；807- screens material pond；808- grade drainage tube；809- circulating pump.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
The present invention provides the present invention provides the modified SBS composite-material formulas that a kind of highly resistance is rolled over, according to parts by weight
It is made of the following raw material:
SBS30-40 parts, 5-10 parts of natural rubber, 10-13 parts of polypropylene, 20-30 parts of haloflex, the organic illiteracy of nanometer
De- 10-20 parts of soil, traction-resistant fibre 6-8 parts netted, 6-8 parts of toluene, 10-20 parts of methyl methacrylate, 3-6 parts of ceramic fibre,
4-6 parts of nano magnesia, 1-3 parts of antioxidant, 2-4 parts of lubricant, 1-3 parts of crosslinked at low temperature agent.
Among the above, the netted traction-resistant fibre is specially mesh polypropylene-fibre, improved plant reticular fibre, asphalt mixtures modified by epoxy resin
Any one in rouge reticular fibre；The antioxidant is specially dibutyl hydroxy toluene, three filter melamines and styrene
Change phenol is (1~2) in mass ratio: (1~2): (0.5~1) mixing composition；The lubricant be zinc stearate, calcium stearate,
One of silicone master batch or paraffin or a variety of any combination；The crosslinked at low temperature agent is cumyl peroxide, tert-butyl
At least one of hydrogen peroxide, peroxidation sulfuric acid potassium.
In the present invention, the main function of the interaction of each ingredient in the present embodiment is as described below:
Well known to those skilled in the art, since the polarity of SBS is small, the intensity of adhesive property and bonding cannot
Enough meet demands, therefore just must first go through and to form matrix to change the polarity of SBS, so that SBS has certain bonding
Performance and adhesion strength.In the present invention, SBS is formed by latex by emulsification, then passes through additive and crosslinked at low temperature agent
The whip modified effect of equal materials, so that each component is swollen in the star-like reticular structure of SBS latex, thus the composite wood formed
The inierpeneirating network structure of material can effectively improve the flexibility and brittleness problems of existing SBS composite material, improve SBS composite wood
The fracture resistance of material.
In addition, netted traction-resistant fibre forms fine and close stacked structure during mixing, to be formed nondirectional
Netted or island structure improves the connection between component, it is formed integrated structure from mechanical angle, can be in machine
The fracture resistance of composite material after forming is improved on tool mechanics.
The ceramic fibre and nano magnesia being disposed therein, enhance the hardness of SBS composite material, and this it is inorganic at
Divide and be filled in reticular structure, the connection between each structure can be enhanced, improve the heat resistance, intensity and anti-impact of composite material
Hit performance.A certain proportion of antioxidant is added, the chain reaction of free radical can be blocked, preferable protection can be played and made
With.
In the present invention, as shown in Figure 1, additionally providing a kind of preparation process of highly resistance folding SBS composite material, including it is as follows
Step:
Step 100, swelling add natural rubber, polypropylene, haloflex according to quality proportioning in pressure reaction still
Heat is until be in molten condition, and continue heat preservation and obtain matrix.
Swelling is high molecular polymer the phenomenon that volume expands in a solvent, due to high molecular relative molecular mass
Greatly and there is polydispersity, molecular shape has the different type of linear, branching and crosslinking, and aggregated structure has crystalline state and non-knot
The types such as crystalline substance, therefore, high molecular dissolution phenomena are more much more complex than small molecule compound.
The phenomenon that swelling refers to that solvent molecule diffuses into inside macromolecule, makes its volume expansion.Swelling is macromolecule material
Expect that peculiar phenomenon, reason are that solvent molecule differs greatly with coil dimension, molecular motion velocities differ greatly, solvent
Molecular diffusion rates are very fast, and diffusion of the macromolecule into solvent is slow.It therefore, is that solvent molecule seeps first when macromolecule dissolution
It penetrates into inside high molecular material, increases its volume, that is, be swollen.This stone lion weaving in, polypropylene with solvent molecule not
It is disconnected to penetrate into natural rubber and haloflex, while the small molecule material in high molecular material can also interpenetrate, from
And a complicated process for interpenetrating and tangling is formed, it is convenient for forming netted or island structure first by swelling process
Basic structure.And with the continuous infiltration of solvent molecule, the high molecular material volume of swelling constantly increases, macromolecular chain segment fortune
Enhancing is moved, then reaches the movement of entire macromolecular chain by the coordinated movement of various economic factors of segment, macromolecular progresses into solution, is formed
Thermodynamically stable homogeneous system, i.e. dissolution phase.Molten condition is formed after dissolution, on the one hand temperature with higher, just
In the mutual fusion of other ingredients；Another aspect in the state of high temperature keep can make scattered molecule it
Between continue relative motion, form more stable reticular structure.
In step 100, the specific steps heated in pressure reaction still are as follows:
Raw material are gradually added in pressure reaction still according to the proportion for step 101；
Step 102, the air being passed through into pressure reaction still in carbon dioxide or nitrogen pressure release reaction kettle, and continue
It is passed through carbon dioxide or nitrogen and increases pressure in pressure reaction still to 2~3MPa；
Step 103 is persistently heated to pressure reaction still, and control the pressure in pressure reaction still be maintained at 2~
Between 5MPa, until matrix is obtained in molten condition in pressure reaction still, it is lasting to keep the temperature.
In the present embodiment, it is the pressure improved in device by being passed through nitrogen or carbon dioxide one side, promotes
Dissolution and mixing, still further aspect be then so that carbon dioxide or it is nitrogen gas dissolved change the polarity of solvent in a solvent, promote
Ingredient therein mutually merges.Specifically when selecting carbon dioxide as the pressure medium chemically reacted, low with viscosity,
Diffusion coefficient is big, nontoxic, non-ignitable, chemically inert advantage, can not only avoid that initiator is added in above-mentioned reaction, subtract
The introducing of impurity is lacked, has also had many advantages, such as that the reaction time is short.
Step 200 mixes the matrix after swelling with SBS according to the proportion, and shearing grinding forms after mixture high-speed stirring again
It mixes, nano organic montmorillonite, toluene, methyl methacrylate is added according to the proportion and is developed for the first time, add after primary development
Matrix after entering swelling carries out secondary development.
In this step, first by proportion addition auxiliary material, then each component is enabled to be sufficiently mixed by high-speed stirred,
And due to being high molecular material, mixed viscosity is stronger, and the simple mixing that is stirred can not reach accordingly
Mixed effect, therefore in order to reach optimal mixed effect, the effect of shearing grinding is reached by the shearing force that high-speed stirred is formed
Fruit, to promote optimal mixing, so that being mutually sufficiently mixed between each component.
In step 200, the specific steps developed twice are as follows:
First development, sequentially adds ingredient, and continue high-speed stirred and mix them thoroughly, and the temperature improved in device is straight
It to 180~200 DEG C, persistently stirs at low speed, develops 3~4h；
Ingredient is successively added on the basis of primary development in secondary development according to the proportion, is acted on first by high-speed stirred
It mixes them thoroughly, further increases the temperature in device up to 200~210 DEG C, 4~5h is developed in consecutive low temperature stirring.
In the present invention, it is acted on by development twice, swelling can be successively added into development room or by pre- place
The raw material of reason, it can raw material can be more fully mixed therein, it can be in the case where application less material
Reach estimated mixed effect.In the present embodiment, the materials such as the SBS being swollen can be enabled adequately to enter molecule
Between form reticular structure, the secondary host material that is gradually added can make it reach full growth, achieve the purpose that improve using material,
To reduce the application of expensive material.
In addition, the relationship between also needing to consider in the present invention to be swollen and is compatible, however due to having examined in the foregoing
Consider compatible situation, be formulated by improving, changes the relationship between polarity, it is therefore, anti-by improving on the basis of above-mentioned
The temperature answered promotes swelling, especially after increasing auxiliary material, since the state of auxiliary material does not reach the locating shape of swelling
State, swelling efficiency can greatly be improved by improving temperature.
Further, in order to improve the efficiency of swelling and development, be added auxiliary material or ingredient such as nano organic montmorillonite,
Before toluene, methyl methacrylate, it is necessary to pre-process to these ingredients or auxiliary material, and the normal method handled is then
It is pulverization process to be carried out to inorganic constituents, and organic principle is then carried out also to heat while pulverization process, then divides
It is not added.
Step 300, emulsion dispersion by the mixed material heating after development to 120~130 DEG C, and continue 1~2h of heat preservation, press
Lubricant and crosslinked at low temperature agent is added according to proportion, and the soap lye that emulsifier and high-temperature water are made into is added, by colloid mill by two
Person mixes overground emulsification.
In this step, the effect that crosslinked at low temperature agent is added is so that each component swells in the star-like netted of SBS latex
In structure, thus the inierpeneirating network structure of the composite material formed, and the effect of lubricant is to promote the phase between each ingredient
Mutually fusion；And the addition emulsifier and soap lye of selectivity can then help mixture quickly to be emulsified.
In step 300, the specific steps of overground emulsification are as follows:
Raw material are added in mixture according to the proportion, and soap lye are added by step 301, are kept for 120~130 DEG C
Temperature impregnates 0.5-1h；
Step 302 soaks colloid mill by 80~100 DEG C of high temperature soap lyes, and continues to pour colloid with high temperature soap lye
Mill is preheated；
Mixture after immersion is sequentially imported and carries out grinding emulsification in colloid mill, and grinds emulsification number by step 303
Not less than 3 times.
In above-mentioned steps, before formally entering overground emulsification, colloid mill is soaked by soap lye first, is soaked
Effect be two aspect: first, pre-wetting colloid mill can prevent the biggish mixture of viscosity to be bonded in colloid mill
On, but also can prevent colloid mill itself from absorbing water so that mixture is dehydrated；Second, colloid mill is preheated by soap lye,
So that colloid mill is in environment identical with mixture before life's work, avoid due to environment difference mixture being gone out
Existing crimping or other improper situations.
Step 400, mixing, by the original after netted traction-resistant fibre, ceramic fibre, nano magnesia, antioxidant and emulsification
Material, which is placed in mixer, carries out internally mix, is granulated after circulating water through pelleter.
Mixer is mainly by being equipped with a pair of of specific shape and the opposite rotor turned round, in the close of adjustable temperature and pressure
The machinery plasticated and be kneaded to polymer material to intermittence under closed state, in mixer, material is sheared everywhere
With the effect of friction, the temperature of the materials inside made is steeply risen, and viscosity reduces, and is increased the wettability on each component surface, is made
It can be come into full contact between each component.Material is crushed in the gap of mixer inner wall by the shearing of strength, therefore, at this
It is best able to be adequately compressed mixing in step, and reticular structure is also more capable of forming by extraneous ingredient, in this step
Various other auxiliary materials are added convenient for forming island structure.After adding ingredient, the fin on closed-smelting machine rotor enables material edge
The axial movement of rotor is played the role of being stirred, and ingredient is enable to be uniformly mixed in sizing material, shears and breaks repeatedly when ingredient
Broken, mixture is iteratively produced deformation and restores deformation, and being stirred continuously for rotor nog makes ingredient be uniformly dispersed in sizing material, and
Reach certain dispersion degree.
In step 400, the specific steps of mixing are carried out by mixer are as follows:
Step 401, the parameter for adjusting mixer, so that the smelting temperature of mixer is 250~280 DEG C, the revolving speed of screw rod
For 30~50r/min；
Additive is put into mixer by step 402 according to the proportion, first carries out the mixing of first time additive, and by mixing
Additive afterwards keeps original smelting temperature, is added in mixer mixes with the raw material after emulsification again, improve mixing again
Temperature improves the revolving speed of screw rod to 80~100r/min to 300~320 DEG C；
Step 403, during mixing, the temperature of control loop cooling water gradually reduces it by cooling according to gradient
Water temperature.
Each component is carrying out mixing after mixing in mixer, so that sufficiently fusion mixes between each component, so that
Each component in composite material compositions can be combined with each other, to increase the intensity and impact property of SBS composite material.
In above-mentioned steps, by multiple mixing, ingredient can be added in mixture in progressive form, thus just
In the reticular structure for forming more phases time, and under the mixing of mixer, the reticular structure of more phases time can intersect, thus
The secondary island structure for intersecting, being stacked of more phases is formed, the stability of structure can be better than reticular structure, can be more into one
The fracture resistance of the raising composite material of step.
Based on above-mentioned preparation process, the present invention also provides corresponding preparation facilities, as shown in Figures 2 to 7, in the present invention
The preparation facilities of offer can be realized the operation of pipelining, it can completely realize that the SBS is multiple on same production line
The production of condensation material, and the advantage is that and can not only realize that the operation of pipelining can also be realized not in the assembly line
With intersecting for process, it can directly carry out intervening in different processes or non-adjacent process and replenishment of ingredients, realization are handed over
The production of V shape, the device for reducing the processes such as ingredient maintenance, storage and addition and matching, improves the efficiency of single unit system.
Based on above-mentioned, which includes substrate 10 and is sequentially fixed on bottom susceptor 11 on substrate 10, H-type bracket
12 and flat holder 13, substrate 10 be the basis of whole device, and set gradually the bottom susceptor 11 in face on it, H-type bracket
12 and flat holder 13 form load position by high and low, the other preparation facilities of placement can be facilitated, and can make by high and low
Material may rely on air pressure or gravity substantially during transportation, reduce the number and range of artificial direct intervention.
It is fixedly installed with swelling room 1 at the top of H-type bracket 12, is swollen below room 1 and development room is equipped with by material baffle 14
2, and electromagnetism conveying pipeline 15 is equipped between swelling room 1 and development room 2, swelling 1 two sides of room pass through caching pipe 16 and first respectively
Direct current conduit 17 is connected with constant temperature locker room 3 and emulsion chamber 4, development room 2 side by the second direct current conduit 18 also with cream
Change room 4 to connect, and banburying chamber 5, the fixed peace in the constant temperature locker room 3 are installed also by material baffle 14 in the bottom of emulsion chamber 4
In bottom susceptor 11, and the emulsion chamber 4 and banburying chamber 5 are fixedly mounted on flat holder 13.
Among the above, swelling room 1 carries out swelling operation, and development room 2 carries out multiple development operation, and is swollen 1 He of room
It develops and is connected between room 2 by electromagnetism conveying pipeline 15, it can be in order to execute the material transferring after corresponding operating, due in this reality
It applies in mode, the matrix after needing to be used for multiple times swelling, therefore, after the swelling of interim or short-term storage is played by constant temperature locker room 3
Matrix effect, corresponding emulsion chamber 4 execute corresponding emulsification procedure, and banburying chamber 5 executes mixing operation, passes through the phase of multiple devices
Mutually cooperation is to realize preparation process.
As the preferred of present embodiment, being swollen room 1 includes the pressure reaction still 101 for being fixedly mounted on center, pressure
By several equally distributed top covers 103 for pulling out button and being equipped with semi-ellipsoid shape above reaction kettle 101, in pressure reaction still 101
It is connected between top cover 103 by air-tightness rubber washer, complementing each other to form between pressure reaction still 101 and top cover 103
Closed environment is fixedly installed with several equally distributed electricity on 101 inner wall of pressure reaction still and adds to realize that high pressure is swollen
Heat block 102 is fixedly installed with several mutually independent feed pipes 104, the feed pipe 104 being independently arranged on the top cover 103
It can disaggregatedly feed, and be unlikely in feeding stage confusion reigned, and more independent chargings as desired
Multiple groups charging while progress may be implemented in pipe 104, avoids missing corresponding feed time during operation, and pushing up
The center of lid 103 is fixedly installed with Pressure behaviour balanced valve 105, which is used for the control of pressure, in reality
In the production on border, by setting corresponding threshold value, when up to or over the threshold value, Pressure behaviour balanced valve 105 will be opened
It is dynamic, corresponding pressure is discharged, to guarantee that the pressure in pressure reaction still 101 is constant, is passed through below Pressure behaviour balanced valve 105
Outstanding staking is fixedly installed with broad-leaved blender 106, and broad-leaved blender 106 provides slow stirring condition, promotes swelling, airtight
Inflation air pump 107 is equipped with by gas-guide tube on property rubber washer.
Developing room 2 includes the screw extruder 201 being connected to electromagnetism conveying pipeline 15, and in the screw extruder 201
Arrival end is equipped with several first auxiliary materials and enters pipe 202, one of them first auxiliary material enters pipe 202 by extracting pump conveying device
203 are connected to constant temperature locker room 3.
In present embodiment, increase screw extruder 201 in development room 2, effect is then to carry out according to demand
Preparatory extruding makes it is possible, firstly, to just carry out extrusion process to the ingredient being not handled by when material does not enter development room 2
Its state that can be squeezed in advance in a mixing is convenient for subsequent development, improves production efficiency；Secondly as needing again
Secondary addition ingredient, and the viscosity of former mixture is larger, ingredient is directly added into mixture, mixed effect is general, and works as
When mixed effect is poor, it is impossible to enough conditions for meeting development, in the present invention, also needed after mixture is added in ingredient into
Therefore row shear agitation, can be realized above-mentioned so that developmental condition can be preferably in by screw extruder 201
Multiple functions, and for screw extruder 201, above-mentioned work can be completed in a step, same what is improved efficiency
When, the use of other corollary equipments can also be reduced.
It is fixedly installed with ladder platform 204 in 12 two sides of H-type bracket for being equipped with development room 2, two ladders are flat
It is respectively equipped with development monitoring device on platform 204 and carries position and discharge monitoring device load position.As preferred embodiment, in the present invention
In, development is that certain time is relatively long, and the step that condition is more harsh, it is therefore desirable to according to the precision of preparation and specific
Production technology corresponding parameter is monitored, and monitor corresponding parameter and then need to be arranged corresponding monitoring device, due to
In the present invention, it is arranged using the mode of high infraversion malposition, for the ease of actual production requirement, in H-type bracket
Corresponding load position is set on 12, is convenient for monitoring.
The outlet end of screw extruder 201 is fixedly installed with high-speed stirred pond 205, squeezes by screw extruder 201 mixed
Mixture after conjunction is directly entered high-speed stirred pond 205, and is fixedly installed with agitating shaft at the center in high-speed stirred pond 205
206, interlaced stirring accessory lobes 207 are fixedly installed on agitating shaft 206, are realized by high-speed stirred effect final mixed
It closes, and considers the viscosity of mixture, in the present embodiment, the rate of stirring is 3000~4500r/min, is only led to
Common mechanical stirring is crossed, can't more fully be mixed, it is therefore, secondary in stirring according to the defect that existing machinery stirs
It is fixedly installed with shearing sharpening 208 on leaf 207, the segmentation of mixture is realized by the shear action of shearing sharpening 208, in height
Development pond 209 is equipped with below fast stirring pool 205, the mixture after the operation such as high-speed stirred, shearing is reaching developmental condition
When will be directly entered development pond 209 and carry out multiple development, development 209 bottom of pond is uniformly equipped with several bubble spray heads
210, bubble spray head 210 will will do it disturbance during development, reinforce the effect finally developed, and in development pond 209
It is fixedly installed in bottom and side wall and forces hot plate 211 in the first of rectangular-ambulatory-plane, for reinforcing heat, met in development room 2
Temperature requirements, development 209 bottom of pond are fixedly installed with the second air pump conveying device 212 being connected to screw extruder 201.
The constant temperature locker room 3 includes tempering tower 301 and terminal storage tank 302, wherein tempering tower 301 faces as one
When the structure that stores, will be useless directly having used and have already passed through the mixture of swelling and temporarily store, in tempering tower 301
In be able to maintain identical pressure and temperature in original swelling room 1 so that mixture keeps original state, terminal storage tank
302 storage organizations short-term as one store the secondary mixture not used temporarily so as to subsequent production relaying
It is continuous to use, it is connected between tempering tower 301 and terminal storage tank 302 by drain pipe.Tempering tower 301 is by extracting pump conveying dress
It sets 203 and enters pipe 202 with one of them first auxiliary material on extruser 201 and be connected to, on 302 inner wall of terminal storage tank also
It is even that several pieces of electric heating blocks 102 are installed, and pulsometer 303 is connected with by pneumatic tube at the top of terminal storage tank 302, it is above-mentioned
Supporting structure is in order to enable terminal storage tank 302 is able to maintain environment identical with swelling room 1.
Emulsion chamber 4 includes heat-flash device 6, mixed stirring device 7 and the Emulsification grinder 8 from top to bottom set gradually,
Heat-flash device 6 and mixed stirring device 7 are connected to the first direct current conduit 17 and the second direct current conduit 18 respectively, and heat-flash device 6 mixes
It closes and is connected to by electromagnetism conducting tube 15 between agitating device 7 and Emulsification grinder 8, and in heat-flash device 6 and emulsification grinding
It is also connected to by the first air pump conveying device 9 between device 8.
In the present invention, heat-flash device 6 is to provide heat-flash effect, and can pass through heating power during continuous heating
It learns principle and carries out convection current, during being in circulating-heating always, so that mixture is available uniform strong in whole device
Heating.
Due to needing that different ingredients is added in different steps, stirring and mixing are always through entire work
In sequence, and in the end of process, mixture will be more sticky, and conventional stirring can not reach corresponding mixed
It closes, and shear-mixed in the foregoing is also difficult to reach large range of mixing, therefore, the mixed stirring device 7 in the present invention
It will be stirred using the principle of " waterwheel ", and stirring cooperated to be mixed, and also cooperation blowing during mixing
System reduces its viscosity, promotes flowing and mixing.
Wherein, Emulsification grinder 8 is core apparatus therein, it will is thoroughly mixed to mixture, so as to most
Meet to enter eventually and carry out mixing and molding in mixer, therefore, which will directly affect the quality of final SBS composite material.
Preferably, heat-flash device 6 includes heat-flash hermetically sealed can 601, is fixedly installed with helically inside heat-flash hermetically sealed can 601
The deflector 602 of shape arrangement, and be fixedly installed on the deflector 602 for being located at top and hang down with 601 surface of heat-flash hermetically sealed can
Straight chromatoplate 603,603 center of chromatoplate are equipped with transporting corresponding with deflector 602 hole, fix at the edge of chromatoplate 603
The heat preservation baffler 604 parallel with 601 surface of heat-flash hermetically sealed can, the heat preservation baffler 604 and heat-flash hermetically sealed can 601 are installed
Between be equipped with cyclic annular cyclic gap channel, directly connect in bottom and the deflector 602 positioned at bottommost of heat preservation baffler 604
It connects, is fixedly installed with second on the inner wall of the heat preservation baffler 604 and deflector 602 and forces hot plate 605.
In heat-flash device 6, second, which forces hot plate 605, heats mixture, and after heated, viscosity will drop
It is low, but also will can be floated upwards due to density, being disposed therein spiral helicine deflector 602 will be provided to floating
Dynamic channel, and the heat preservation baffler 604 being set side by side with heat-flash hermetically sealed can 601 forms cyclic annular cyclic gap channel, thus structure
At an inner cycle channel thermodynamically, reach hydronic purpose.
It is equipped with several second auxiliary materials at the top of mixed stirring device 7 and enters pipe 701, and at 7 liang of the mixed stirring device
End and center are respectively equipped with blender 702 and mixing drum 703, and several pieces of stirring accessory lobes are fixedly installed on blender 702, stir
Cylinder 703 is mounted on mixed stirring device 7 by lateral shaft, is equipped on mixing drum 703 perpendicular to mixing drum axial restraint
Several blocks of setback plates 704 being parallel to each other, and chain bucket is fixedly installed with by the way that flitch is isolated between adjacent wave folded plate 704
705。
Among the above, constantly sticky mixture is carried by chain bucket 705, to realize in wider range
Flowing, when entirety due to constantly actively carry and realize flowing when, the blender 702 at 7 both ends of mixed stirring device is set
Normal mixing can be realized.
Blowing device 706 is also fixedly installed on 7 both ends inner wall of mixed stirring device, the blowing device 706 includes
It is located at the blowing pump 707 in 7 outside of mixed stirring device, the blowing pump 707 passes through injection tube 708 and is located at mixed stirring device
Several injection holes connection on 7, the injection hole has several groups, and is located at the spray at the top and bottom of mixed stirring device
Pressure-control valve 709 is equipped in aperture blowing.
The polarity feature of 706 binder matrix of blowing device injects significant component of gas thereto and promotes its reduction
Viscosity improves mobility, and this process is different in different level in mixed stirring device 7, and different layers may be implemented
Otherness flowing on face, further increases its mobility.
Emulsification grinder 8 includes colloid mill 801, and the inlet of the colloid mill 801 is fixedly installed with two drainage tubes
802, and two drainage tubes 802 are connected separately with main drainage pump 803 and mixed stirring device 7, main drainage pump 803 is connected with soap
Liquid chamber 804, is soaked in advance and is preheated, and the outlet end of colloid mill 801 is fixedly installed with multilevel screen by Y-shaped bracket
805, the equal and horizontal plane oblique of multilevel screen 805, and longitudinal vibration electricity is fixedly installed with every layer of multilevel screen 805 of bottom
Machine 806, for multiple emulsification cannot will be carried out according to different ranks by the structure that multilevel screen 805 screens, until
It can satisfy corresponding emulsification demand position, and the every layer of lower section of multilevel screen 806 is equipped with screening material pond 807, the screening material
It is connect by secondary drainage tube 808 with soap lye pond 804 in pond 807, and is fixedly installed with circulating pump in screening material pond 807
809, the circulating pump 809 is connected to by diversion pipe with heat-flash device 6, and for having already passed through the mixed of the screening of multilevel screen 806
Material is closed, if since technologic demand is also required to carry out duplicate emulsification again, until reaching technologic emulsification demand.
It is obvious to a person skilled in the art that invention is not limited to the details of the above exemplary embodiments, Er Qie
In the case where without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter
From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the present invention is by appended power
Benefit requires rather than above description limits, it is intended that all by what is fallen within the meaning and scope of the equivalent elements of the claims
Variation is included within the present invention.Any reference signs in the claims should not be construed as limiting the involved claims.
Claims (10)
1. a kind of emulsifier unit of highly resistance folding SBS composite material, including substrate (10) and sequentially it is fixed on substrate (10)
Bottom susceptor (11), H-type bracket (12) and flat holder (13) are fixedly installed with swelling room at the top of the H-type bracket (12)
(1), development room (2) is installed by material baffle (14) below the swelling room (1), and swelling room (1) and develop room (2) it
Between be equipped with electromagnetism conveying pipeline (15), swelling room (1) two sides pass through respectively caching pipe (16) and the first direct current conduit (17) company
Be connected to constant temperature locker room (3) and emulsion chamber (4), development room (2) side by the second direct current conduit (18) also with emulsion chamber
(4) it connects, and is equipped with banburying chamber (5) in the bottom of emulsion chamber (4) also by material baffle (14), the constant temperature locker room (3)
It is fixedly mounted on bottom susceptor (11), and the emulsion chamber (4) and banburying chamber (5) are fixedly mounted on flat holder (13),
It is characterized by:
The emulsion chamber (4) includes the heat-flash device (6) from top to bottom set gradually, mixed stirring device (7) and emulsification grinding
Device (8), the heat-flash device (6) and mixed stirring device (7) respectively with the first direct current conduit (17) and the second direct current conduit
(18) it is connected to, passes through electromagnetism conducting tube between the heat-flash device (6), mixed stirring device (7) and Emulsification grinder (8)
(15) it is connected to, and is also connected to by the first air pump conveying device (9) between heat-flash device (6) and Emulsification grinder (8)；
Emulsification grinder (8) includes colloid mill (801), and the inlet of the colloid mill (801) is fixedly installed with two drainages
It manages (802), and two drainage tubes (802) are connected separately with main drainage pump (803) and mixed stirring device (7), the master draws
Stream pump (803) is connected with soap lye room (804), and the outlet end of the colloid mill (801) is fixedly installed with multistage by Y-shaped bracket
Sieve (805), the equal and horizontal plane oblique of the multilevel screen (805), and in the fixed peace in every layer of multilevel screen (805) of bottom
Equipped with longitudinal vibration motor (806), every layer of lower section of the multilevel screen (806) is equipped with screening material pond (807), the screening material
It is connect by secondary drainage tube (808) with soap lye pond (804) in pond (807), and is fixedly mounted in screening material pond (807)
Have circulating pump (809), the circulating pump (809) is connected to by diversion pipe with heat-flash device (6).
2. a kind of emulsifier unit of highly resistance folding SBS composite material according to claim 1, it is characterised in that: the heat-flash
Device (6) includes heat-flash hermetically sealed can (601), and leading of arranging in the shape of a spiral is fixedly installed with inside the heat-flash hermetically sealed can (601)
Flowing plate (602), and be located at top deflector (602) on be fixedly installed with it is vertical with heat-flash hermetically sealed can (601) surface
Chromatoplate (603), chromatoplate (603) center is equipped with transporting corresponding with deflector (602) hole, in chromatoplate (603)
Edge is fixedly installed with the heat preservation baffler (604) parallel with heat-flash hermetically sealed can (601) surface, the heat preservation baffler (604)
Cyclic annular cyclic gap channel is equipped between heat-flash hermetically sealed can (601), in the bottom of heat preservation baffler (604) and positioned at bottommost
Deflector (602) be directly connected to, be fixedly installed with the on the inner wall of heat preservation baffler (604) and deflector (602)
Two force hot plate (605).
3. a kind of emulsifier unit of highly resistance folding SBS composite material according to claim 1, it is characterised in that: the mixing
It is equipped with several second auxiliary materials at the top of agitating device (7) to enter pipe (701), and at the mixed stirring device (7) both ends in
The heart is respectively equipped with blender (702) and mixing drum (703), and several pieces of stirring accessory lobes are fixedly installed on the blender (702),
The mixing drum (703) is mounted on mixed stirring device (7) by lateral shaft, perpendicular to stirring on the mixing drum (703)
It mixes an axial restraint and several blocks of setback plates (704) being parallel to each other is installed, and pass through isolation between adjacent wave folded plate (704)
Flitch is fixedly installed with chain bucket (705).
4. a kind of emulsifier unit of highly resistance folding SBS composite material according to claim 3, it is characterised in that: stirred in mixing
It mixes and is also fixedly installed with blowing device (706) on the inner wall of device (7) both ends, the blowing device (706) includes being located at mixing to stir
The blowing pump (707) on the outside of device (7) is mixed, the blowing pump (707) is by injection tube (708) and is located at mixed stirring device
(7) several injection holes connection on, the injection hole has several groups, and is located at the top and bottom of mixed stirring device
Pressure-control valve (709) are equipped in injection hole.
5. a kind of emulsifier unit of highly resistance folding SBS composite material according to claim 1, it is characterised in that: the constant temperature
Locker room (3) includes tempering tower (301) and terminal storage tank (302), the tempering tower (301) and terminal storage tank (302) it
Between by drain pipe connect, the tempering tower (301) by extract pump conveying device (203) with develop room (2) be connected to, the end
Several pieces of electric heating blocks (102) are also uniformly installed, and logical at the top of terminal storage tank (302) on storage tank (302) inner wall of end
It crosses pneumatic tube and is connected with pulsometer (303).
6. a kind of preparation process of highly resistance folding SBS composite material, which comprises the steps of:
Step 100, swelling heat natural rubber, polypropylene, haloflex directly according to quality proportioning in pressure reaction still
Extremely it is in molten condition, and continues heat preservation and obtain matrix；
Step 200 mixes the matrix after swelling with SBS according to the proportion, and shearing grinding forms after mixture high-speed stirred again, presses
Nano organic montmorillonite, toluene, methyl methacrylate is added according to proportion to be developed for the first time, swelling is added after primary development
Matrix afterwards carries out secondary development；
Step 300, emulsion dispersion by the mixed material heating after development to 120~130 DEG C, and continue 1~2h of heat preservation, according to matching
Than lubricant and crosslinked at low temperature agent is added, and the soap lye that emulsifier and high-temperature water are made into is added, is mixed the two by colloid mill
Close overground emulsification；
Step 400, mixing, by the raw material after netted traction-resistant fibre, ceramic fibre, nano magnesia, antioxidant and emulsification
It is placed in mixer and carries out internally mix, be granulated after circulating water through pelleter.
7. a kind of preparation process of highly resistance folding SBS composite material according to claim 6, which is characterized in that in step 100
In, the specific steps that are heated in pressure reaction still are as follows:
Raw material are gradually added in pressure reaction still according to the proportion for step 101；
Step 102, the air being passed through into pressure reaction still in carbon dioxide or nitrogen pressure release reaction kettle, and be continually fed into
Carbon dioxide or nitrogen increase the pressure in pressure reaction still to 2~3MPa；
Step 103 is persistently heated to pressure reaction still, and controls the pressure in pressure reaction still and be maintained at 2~5MPa
Between, until matrix is obtained in molten condition in pressure reaction still, it is lasting to keep the temperature.
8. a kind of preparation process of highly resistance folding SBS composite material according to claim 6, which is characterized in that in step 200
In, the specific steps developed twice are as follows:
First development, sequentially adds ingredient, and continue high-speed stirred and mix them thoroughly, improve the temperature in device until
It 180~200 DEG C, persistently stirs at low speed, develops 3~4h；
Ingredient is successively added on the basis of primary development in secondary development according to the proportion, makes it by high-speed stirred effect first
It is sufficiently mixed, further increases the temperature in device up to 200~210 DEG C, 4~5h is developed in consecutive low temperature stirring.
9. a kind of preparation process of highly resistance folding SBS composite material according to claim 6, which is characterized in that in step 300
In, the specific steps of overground emulsification are as follows:
Raw material are added in mixture according to the proportion, and soap lye are added by step 301, keep 120~130 DEG C of temperature
Impregnate 0.5-1h；
Step 302 soaks colloid mills by 80~100 DEG C of high temperature soap lyes, and continue to pour with high temperature soap lye colloid mill into
Row preheating；
Mixture after immersion is sequentially imported and carries out grinding emulsification in colloid mill by step 303, and it is not low to grind emulsification number
In 3 times.
10. a kind of preparation process of highly resistance folding SBS composite material according to claim 6, which is characterized in that in step
In 400, the specific steps of mixing are carried out by mixer are as follows:
Step 401, the parameter for adjusting mixer, so that the smelting temperature of mixer is 250~280 DEG C, the revolving speed of screw rod is 30
~50r/min；
Additive is put into mixer by step 402 according to the proportion, first carries out the mixing of first time additive, and will be after mixing
Additive keeps original smelting temperature, is added in mixer mixes with the raw material after emulsification again, improve smelting temperature again
To 300~320 DEG C, the revolving speed of screw rod is improved to 80~100r/min；
Step 403, during mixing, the temperature of control loop cooling water gradually reduces it by coolant water temperature according to gradient.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811028545.8A CN109228008B (en) | 2018-09-03 | 2018-09-03 | Emulsification device of high-fracture-resistance SBS composite material and preparation process thereof |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811028545.8A CN109228008B (en) | 2018-09-03 | 2018-09-03 | Emulsification device of high-fracture-resistance SBS composite material and preparation process thereof |
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| CN109228008A true CN109228008A (en) | 2019-01-18 |
| CN109228008B CN109228008B (en) | 2020-11-17 |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0716442A (en) * | 1993-06-30 | 1995-01-20 | Matsue Stainless Kosakusho:Kk | Method and device for dissolving high polymer material |
| CN205073951U (en) * | 2015-10-21 | 2016-03-09 | 山东凯文科技职业学院 | A equipment for production of emulsification modified asphalt |
| CN205099614U (en) * | 2015-09-29 | 2016-03-23 | 山东省建设建工（集团）有限责任公司 | Emulsification modified asphalt production facility |
| CN106221253A (en) * | 2016-08-29 | 2016-12-14 | 四川知行路桥集团有限公司 | A kind of production technology of waste and old rubber modified asphalt regeneration |
| CN107325305A (en) * | 2017-08-10 | 2017-11-07 | 青岛科技大学 | A kind of filler slurry atomization drying consecutive production equipment |
-
2018
- 2018-09-03 CN CN201811028545.8A patent/CN109228008B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0716442A (en) * | 1993-06-30 | 1995-01-20 | Matsue Stainless Kosakusho:Kk | Method and device for dissolving high polymer material |
| CN205099614U (en) * | 2015-09-29 | 2016-03-23 | 山东省建设建工（集团）有限责任公司 | Emulsification modified asphalt production facility |
| CN205073951U (en) * | 2015-10-21 | 2016-03-09 | 山东凯文科技职业学院 | A equipment for production of emulsification modified asphalt |
| CN106221253A (en) * | 2016-08-29 | 2016-12-14 | 四川知行路桥集团有限公司 | A kind of production technology of waste and old rubber modified asphalt regeneration |
| CN107325305A (en) * | 2017-08-10 | 2017-11-07 | 青岛科技大学 | A kind of filler slurry atomization drying consecutive production equipment |
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|---|---|
| CN109228008B (en) | 2020-11-17 |
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Effective date of registration: 20231226 Address after: 061000 Dongguang Economic Development Zone Packaging and Machinery Equipment Manufacturing Park B, Dongguang County, Cangzhou City, Hebei Province Patentee after: Cangzhou Liankong New Material Co.,Ltd. Address before: No. 8, Group 6, Zone 2, Nanxinlizhuang Village, Xiongzhou Town, Xiong County, Baoding City, Hebei Province, 071800 Patentee before: Zhang Wenlong |
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