KR20040070157A - Material to improve quality of asphalt concrete, and the manufacturing method thereof - Google Patents
Material to improve quality of asphalt concrete, and the manufacturing method thereof Download PDFInfo
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- KR20040070157A KR20040070157A KR1020040056041A KR20040056041A KR20040070157A KR 20040070157 A KR20040070157 A KR 20040070157A KR 1020040056041 A KR1020040056041 A KR 1020040056041A KR 20040056041 A KR20040056041 A KR 20040056041A KR 20040070157 A KR20040070157 A KR 20040070157A
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- 239000011384 asphalt concrete Substances 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 239000000463 material Substances 0.000 title description 20
- 239000010426 asphalt Substances 0.000 claims abstract description 126
- 239000003607 modifier Substances 0.000 claims abstract description 79
- 238000000034 method Methods 0.000 claims abstract description 57
- 239000000203 mixture Substances 0.000 claims abstract description 33
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 229920001684 low density polyethylene Polymers 0.000 claims abstract description 14
- 239000004702 low-density polyethylene Substances 0.000 claims abstract description 14
- 238000005520 cutting process Methods 0.000 claims abstract description 7
- 238000001816 cooling Methods 0.000 claims abstract description 6
- 238000010298 pulverizing process Methods 0.000 claims abstract description 5
- 239000010920 waste tyre Substances 0.000 claims description 58
- 230000008569 process Effects 0.000 claims description 30
- 238000002156 mixing Methods 0.000 claims description 25
- 239000002245 particle Substances 0.000 claims description 20
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 15
- 239000000945 filler Substances 0.000 claims description 13
- 239000004568 cement Substances 0.000 claims description 10
- 239000006229 carbon black Substances 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 5
- 239000004576 sand Substances 0.000 claims description 5
- 239000000377 silicon dioxide Substances 0.000 claims description 5
- 239000004575 stone Substances 0.000 claims description 5
- 230000035515 penetration Effects 0.000 claims description 3
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 2
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 claims description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 2
- 239000003292 glue Substances 0.000 claims description 2
- 239000012188 paraffin wax Substances 0.000 claims description 2
- 229910052717 sulfur Inorganic materials 0.000 claims description 2
- 239000011593 sulfur Substances 0.000 claims description 2
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 claims description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims 1
- 239000002699 waste material Substances 0.000 claims 1
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 abstract description 23
- 238000005336 cracking Methods 0.000 abstract description 6
- 229920001577 copolymer Polymers 0.000 abstract description 4
- FACXGONDLDSNOE-UHFFFAOYSA-N buta-1,3-diene;styrene Chemical compound C=CC=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 FACXGONDLDSNOE-UHFFFAOYSA-N 0.000 abstract description 2
- 238000002360 preparation method Methods 0.000 abstract 1
- 238000005245 sintering Methods 0.000 abstract 1
- 238000000227 grinding Methods 0.000 description 19
- 238000004806 packaging method and process Methods 0.000 description 11
- 238000012856 packing Methods 0.000 description 9
- 229920000346 polystyrene-polyisoprene block-polystyrene Polymers 0.000 description 9
- 229920003023 plastic Polymers 0.000 description 8
- 239000004033 plastic Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 5
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 230000032683 aging Effects 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 238000002372 labelling Methods 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- VSKJLJHPAFKHBX-UHFFFAOYSA-N 2-methylbuta-1,3-diene;styrene Chemical compound CC(=C)C=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 VSKJLJHPAFKHBX-UHFFFAOYSA-N 0.000 description 1
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 229920000034 Plastomer Polymers 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000011246 composite particle Substances 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000013307 optical fiber Substances 0.000 description 1
- 229920005594 polymer fiber Polymers 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 239000012783 reinforcing fiber Substances 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L17/00—Compositions of reclaimed rubber
-
- 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
-
- E—FIXED CONSTRUCTIONS
- E01—CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
- E01C—CONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
- E01C19/00—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving
- E01C19/02—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving for preparing the materials
- E01C19/10—Apparatus or plants for premixing or precoating aggregate or fillers with non-hydraulic binders, e.g. with bitumen, with resins, i.e. producing mixtures or coating aggregates otherwise than by penetrating or surface dressing; Apparatus for premixing non-hydraulic mixtures prior to placing or for reconditioning salvaged non-hydraulic compositions
- E01C19/1059—Controlling the operations; Devices solely for supplying or proportioning the ingredients
- E01C19/1068—Supplying or proportioning the ingredients
-
- E—FIXED CONSTRUCTIONS
- E01—CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
- E01C—CONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
- E01C7/00—Coherent pavings made in situ
- E01C7/08—Coherent pavings made in situ made of road-metal and binders
- E01C7/18—Coherent pavings made in situ made of road-metal and binders of road-metal and bituminous binders
- E01C7/26—Coherent pavings made in situ made of road-metal and binders of road-metal and bituminous binders mixed with other materials, e.g. cement, rubber, leather, fibre
- E01C7/265—Coherent pavings made in situ made of road-metal and binders of road-metal and bituminous binders mixed with other materials, e.g. cement, rubber, leather, fibre with rubber or synthetic resin, e.g. with rubber aggregate, with synthetic resin binder
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2207/00—Properties characterising the ingredient of the composition
- C08L2207/20—Recycled plastic
- C08L2207/24—Recycled plastic recycling of old tyres and caoutchouc and addition of caoutchouc particles
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
- C08L2666/02—Organic macromolecular compounds, natural resins, waxes or and bituminous materials
- C08L2666/04—Macromolecular compounds according to groups C08L7/00 - C08L49/00, or C08L55/00 - C08L57/00; Derivatives thereof
- C08L2666/08—Homopolymers or copolymers according to C08L7/00 - C08L21/00; Derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
- C08L2666/02—Organic macromolecular compounds, natural resins, waxes or and bituminous materials
- C08L2666/24—Graft or block copolymers according to groups C08L51/00, C08L53/00 or C08L55/02; Derivatives thereof
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
- C08L2666/66—Substances characterised by their function in the composition
- C08L2666/72—Fillers; Inorganic pigments; Reinforcing additives
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Structural Engineering (AREA)
- Engineering & Computer Science (AREA)
- Civil Engineering (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Architecture (AREA)
- Materials Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Road Paving Structures (AREA)
Abstract
Description
본 발명은 아스팔트 콘크리트(이하 "아스콘"이라 한다) 품질을 개선시키기 위하여 사용되는 아스콘 개질재(改質材) 칩(Chip)에 관한 것으로, 보다 상세하게는 공중합체 폴리머인 스티렌 부타디엔 스티렌(Styrene Butadiene Styrene : 이하 "SBS"라 한다), 스티렌 이소프렌 스티렌(Styrene Isoprene Styrene : 이라 "SIS"라 한다), 저밀도 폴리에틸렌(Low Density Polyethylene : 이하 "LDPE"라 한다) 등 종래 사용되고 있는 아스콘 개질재를 아스콘 포장에 용이하게 적용시킬 수 있도록 개량한 아스콘 개질재 칩 및 그 제조방법에 관한 것이다.The present invention relates to an asphalt concrete modifier chip used to improve the quality of asphalt concrete (hereinafter referred to as "ascon"), and more specifically, a styrene butadiene styrene copolymer copolymer. Styrene: Ascon packaging is used for conventionally used ascon modifiers such as SBS, Styrene Isoprene Styrene, SIS, and Low Density Polyethylene (LDPE). The present invention relates to an improved ascon modifier chip and a method for manufacturing the same.
아스콘은 아스팔트와 굵은 골재, 잔골재 및 포장용 채움재 (석회석분, 시멘트 등)를 가열혼합 또는 상온에서 혼합한 것으로 도로포장이나 주차장 등에 널리 사용되고 있다. 그러나, 아스콘에 포함된 아스팔트는 그 물성이 기온의 변화에 민감한 것이어서, 아스콘 포장은 하절기 소성변형으로 포장체에 심한 굴곡이 생겨 자동차의 통행에 지장을 초래하기도 하고, 한편으로 동절기 기온이 급강하는 경우에는 포장체에 균열이 생겨 포장체의 수명을 크게 단축시키기도 한다.Ascon is a mixture of asphalt and coarse aggregates, fine aggregates, and pavement fillers (limestone powder, cement, etc.) at room temperature or at room temperature. However, the asphalt contained in ascon is sensitive to changes in temperature, and ascon pavement is a plastic deformation in summer, which causes severe bends in the pavement, which hinders the traffic of cars. In some cases, cracks in the package may greatly shorten the life of the package.
아스콘 개질재는 이러한 아스콘의 문제점을 개선하기 위하여 사용되는 것으로, 아스팔트와 결합하여 아스팔트의 물성을 변화시킴으로써, 하절기 소성변형을 방지하고, 동절기 균열 형성을 방지하고, 또한 포장체의 미끄럼 저항성을 증대시키는 기능을 한다.Ascon modifier is used to improve the problem of ascon, and combines with asphalt to change the physical properties of asphalt, to prevent plastic deformation in summer, to prevent the formation of winter cracking, and to increase the slip resistance of the package. Do it.
종래 널리 사용되고 있는 아스콘 개질재로는 SBS, SIS 또는 LDPE 등이 있으며, 이들 개질재가 아스팔트에 작용하여 아스팔트의 물성을 변화시키는 개념은 도 1에 도시된 바와 같다. 즉, SBS, SIS 또는 LDPE 등의 개질재는 일반적으로 아스콘에 사용되는 아스팔트 양의 약 2-10%를 투입하여 사용되는 것인데, 이들 개질재 입자가 아스팔트 입자와 결합되면, 이들 개질재의 성질에 의하여 하절기 아스팔트의 소성변형이 방지되고, 동절기 균열형성이 방지되며, 또한 포장체의 미끄럼 저항성이 증대되는 것이다.Ascon modifiers widely used in the prior art include SBS, SIS or LDPE, the concept that these modifiers act on the asphalt to change the physical properties of the asphalt is as shown in FIG. In other words, modifiers such as SBS, SIS, or LDPE are generally used by adding about 2-10% of the amount of asphalt used in ascon. When these modifier particles are combined with the asphalt particles, Plastic deformation of the asphalt is prevented, winter crack formation is prevented, and the slip resistance of the package is increased.
이들 개질재들에 대하여 살펴보면 아래와 같다.These modifiers are as follows.
SBS는 탄력성이 좋은 부타디엔과 딱딱한 성질의 스티렌이 임의적으로 반응하여 공중합체된 폴리머로서, 이를 고온으로 용해하여 아스팔트에 투입하면, 높은 공용온도에서도 단단한 아스콘 혼합물이 되며, 중간 공용온도에서도 피로균열에 저항 할 수 있는 탄성이 있는 혼합물이 되고, 낮은 공용온도에서도 온도균열에 저항할 수 있는 변하지 않는 강성을 갖는 혼합물이 된다.SBS is a polymer copolymerized by random reaction of high elastic butadiene and hardened styrene. When it is dissolved at high temperature and put into asphalt, it is a hard ascon mixture at high common temperature and resistant to fatigue cracking at medium common temperature. It is an elastic mixture that can be used, and a mixture having an unchanging stiffness that can resist temperature cracking even at a low common temperature.
그러나 SBS는 물성이 고온에서 용융되는 것이어서 아스팔트에 투입되어 아스팔트와 충분히 혼합시키기 위해서는 150℃이상의 고온을 낼 수 있는 가열장치와 특수 혼합장치인 고전단(high shear) 혼합장치가 반드시 필요한데, 이러한 장치는 가격이 고가일 뿐만 아니라 부피가 커서 각 아스콘 생산공장으로 이동하는 것이 용이하지 않다. 따라서, SBS를 아스콘 개질재로 사용하기 위해서는 아스팔트 제조공장에 가열장치 및 고전단 혼합장치를 설치하여 아스팔트에 미리 SBS를 투입하여 아스팔트와 충분히 혼합한 후, 그 개질재가 포함된 아스팔트를 공사 현장으로 운반하여 사용할 수밖에 없으며, 그렇게 하기 위해서는 아스콘 제조공장에 별도의 아스팔트 탱크를 설치하여야 한다.However, SBS is required to be heated at a high temperature of 150 ° C and a high shear mixing device, which is a special mixing device, in order for the physical property to be melted at a high temperature and mixed with the asphalt to be sufficiently mixed with the asphalt. Not only is it expensive, but also bulky, making it difficult to move to each asphalt plant. Therefore, in order to use SBS as an asphalt modifier, a heating device and a high shear mixing device are installed in an asphalt manufacturing plant, and SBS is pre-injected into the asphalt, mixed with asphalt sufficiently, and the asphalt containing the modifier is transported to the construction site. In order to do so, a separate asphalt tank should be installed at the asphalt concrete plant.
이와 같이, SBS를 개질재로 사용하는 종래의 방법은 고가의 장비가 마련하여야 하고, 또한 공정이 복잡하여 상당히 많은 시간이 요구된다. 더구나, 개질재를 아스팔트와 혼합된 상태로 오래 보존하면 아스팔트와 개질재의 분리현상이 발생하여 개질재 투여의 효과가 없게 되므로, 사전에 미리 준비해 둘 수 없다는 문제점이 있다. 이러한 문제점들로 인하여, SBS의 개질재로서의 우수성에도 불구하고, 아직까지 널리 사용되지 못하고 있는 실정이다.As such, the conventional method of using SBS as a modifier requires expensive equipment and requires a considerable time due to the complicated process. In addition, when the modifier is stored in a mixed state with the asphalt for a long time, separation of the asphalt and the modifier occurs and the effect of the modifier is not effective. Therefore, there is a problem in that it cannot be prepared in advance. Due to these problems, despite the excellence as a modifier of SBS, it is not yet widely used.
SBS와 동종의 공중합체 폴리머로서 아스콘의 개질재로 사용되는 것에는 엘라스토머(Elastomer)인 SIS와, 플라스토머(plastomer)로서 널리 사용되는 아스팔트용폴리머로는 LDPE 등이 있는데, 이들 개질재를 사용하기 위해서는 SBS와 마찬가지로 고온가열장치 및 고전단 혼합장치가 필요하며, 또한 개질재를 아스팔트와 혼합된 상태로 오래 보존하면 아스팔트와 개질재의 분리현상이 발생하므로 사전에 미리 준비하여 보관할 수 없다는 문제점이 있어, 이들 개질재 역시 아직 널리 사용되지 못하고 있는 실정이다.As the copolymer polymer of the same type as SBS, as the modifier of ascone, SIS, which is an elastomer, and asphalt polymer, which are widely used as a plastomer, include LDPE. To do this, high temperature heating device and high shear mixing device are required like SBS. Also, if the modifier is kept in the mixed state with asphalt for a long time, the separation phenomenon of the asphalt and the modifier may occur, so it may not be prepared and stored in advance. However, these modifiers are not widely used yet.
한편으로, 분쇄폐타이어도 그 물성이 공중합체 폴리머와 유사한 점이 있기 때문에 개질재로 사용될 수 있다. 특히 분쇄폐타이어를 도로 포장재의 일부로 사용하는 경우에는, 자원재활용의 측면에서 유용성이 크다는 점뿐만 아니라, 분쇄폐타이어의 탄성에 의하여 도로에 탄력이 생기고 이로 인하여 도로 주행시 승차감이 좋게 되는 장점들이 있다. 그러나, 분쇄폐타이어를 아스팔트 골재 등과 혼합하여 포장을 하는 경우에, 분쇄폐타이어가 아스팔트와 일체화되지 않고 단순히 섞여있는 상태에서는 분쇄폐타이어가 일종의 이물질로 작용하게 되고 따라서 오히려 포장체의 내구성을 저하시키는 결과를 초래하게 된다.On the other hand, the ground waste tire can also be used as a modifier because its physical properties are similar to the copolymer polymer. Particularly, in the case of using the crushed waste tire as part of the road pavement, not only is it useful in terms of resource recycling, but also the elasticity of the crushed waste tire causes elasticity on the road, and thus there is an advantage in that the riding comfort is good when driving on the road. However, in the case of packaging by mixing the crushed waste tire with asphalt aggregate, etc., in the state where the crushed waste tire is not integrated with the asphalt but simply mixed, the crushed waste tire acts as a kind of foreign matter, and thus, deteriorates the durability of the package. Will result.
분쇄폐타이어 사용에 있어 위와 같은 문제점을 해소하기 위한 것으로, 습식 방법인 맥도날드 방식이 있다. 맥도날드 방식은 아스팔트에 분쇄폐타이어 10-25%를 첨가하여 190-220℃로 30분-1시간이상 고온, 고속 혼합하여 분쇄폐타이어와 아스팔트를 일체화시켜 사용하는 기술이다. 즉, 맥도날드 방식에 의하면, 아스팔트와 분쇄폐타이어가 고온에서 고속으로 혼합됨으로서 아스팔트가 분쇄폐타이어 입자 표면에 공고히 결합되어 일체화를 이루게 된다.In order to solve the above problems in the use of grinding waste tires, there is a McDonald's method of the wet method. McDonald's method is a technology that uses 10-25% of crushed waste tires in asphalt and mixes the crushed waste tires and asphalt at high temperature and high speed at 190-220 ° C. for 30 minutes to 1 hour. That is, according to the McDonald's method, the asphalt and the crushed waste tires are mixed at a high speed at a high speed, so that the asphalt is firmly bonded to the crushed waste tire particles surface to form an integration.
그러나 이 맥도날드 방식에서는 분쇄폐타이어와 아스팔트가 고온에서 계속적으로 12시간이상 접촉되게 되면, 이로 인하여 분쇄폐타이어가 아스팔트에 완전 용해되어질 가능성이 있으며, 그렇게 되면 분쇄폐타이어를 투입하는 효과가 떨어지게 되고, 결과적으로 아스콘의 전체 품질이 저하되는 문제가 발생될 수 있다. 뿐만 아니라, 맥도날드 방식을 적용하기 위해서는 고가의 숙성장비가 필요하고, 또한 이동식 대형 아스팔트 탱크, 숙성장비, 분쇄폐타이어 트럭, 아스팔트 트럭, 숙성인원 등이 준비되어야 하므로 경제적 부담이 크고, 생산 공정이 번거롭다는 단점이 있다.However, in this McDonald's method, when the crushed waste tire and asphalt are continuously contacted at a high temperature for more than 12 hours, there is a possibility that the crushed waste tire is completely dissolved in the asphalt, thereby reducing the effect of injecting the crushed waste tire, As a result, a problem may occur in which the overall quality of the asphalt concrete is degraded. In addition, in order to apply the McDonald's method, expensive aging equipment is required, and a mobile large asphalt tank, aging equipment, crushed waste tire truck, asphalt truck, aging personnel, etc. must be prepared. The disadvantage is that it is beneficial.
분쇄폐타이어와 아스팔트를 일체화시키는 다른 방법으로 본 발명의 발명자에 의하여 제시된 특허 제394092호의 방법이 있는데, 이 방법은 먼저 분쇄폐타이어를 간접 가열하여 분쇄폐타이어의 표면을 겔화시키고, 이에 150-300℃로 가열된 아스팔트를 혼합하여 (표면이 겔화된) 분쇄폐타이어 입자와 아스팔트를 일체화시킨 칩을 제조하여 사용하는 것이다. 이 방법은 간단한 공정으로 분쇄폐타이어와 아스팔트를 일체화를 이룰 수 있기 때문에 전술한 맥도날드 방식에 비하여 매우 경제적이다.Another method of integrating the grinding waste tire and asphalt is the method of Patent No. 394092 proposed by the inventor of the present invention, which first indirectly heats the grinding waste tire to gel the surface of the grinding waste tire, and thus 150-300 By mixing the asphalt heated to ℃ to produce a chip in which the ground (gelled) crushed waste tire particles and asphalt integrated. This method is very economical compared to the above-described McDonald's method because it can integrate the grinding waste tire and asphalt in a simple process.
특허 제394092호의 방법에 의하여 제조된 칩의 개념은 도 2a 및 도 2b에 도시된 바와 같다. 즉, 도 2a에서 보듯이, 일차로 분쇄폐타이어의 표면이 겔화되고 그 겔화된 표면에 아스팔트가 결착되어 전체로서 일체화되며, 또한 도 2b에서 보듯이, 분쇄폐타이어와 일체화된 아스팔트가 추후 추가적으로 투입되는 아스팔트 입자들과 자연스럽게 결착 혼합되어 지는 것이다. 따라서, 특허 제394092호의 방법에 의하면, 분쇄폐타이어가 아스팔트와 (단순히 섞여 있는 상태가 아니라) 보다 공고히 결합된다.The concept of a chip manufactured by the method of patent 394092 is as shown in Figs. 2A and 2B. That is, as shown in Fig. 2a, the surface of the pulverized waste tire is first gelled and asphalt is bound to the gelled surface to be integrated as a whole, and as shown in Fig. 2b, the asphalt integrated with the crushed waste tire is additionally added later. It naturally binds and mixes with the asphalt particles. Therefore, according to the method of patent 394092, the crushed waste tire is more firmly bonded with asphalt (not simply mixed).
그러나 분쇄폐타이어를 사용하는 주된 목적은 자원 재활용을 통한 환경 보호와 포장체에 탄력을 부여하여 차량 주행 시 승차감을 좋게 한다는 것이므로, 분쇄폐타이어를 사용한다고 하여 포장체의 내구성이 향상되는 것은 아니다. 따라서 분쇄폐타이어를 사용하는 경우에는 포장체의 내구성을 향상시키는 방안이 별도로 강구될 필요성이 있는데, 특허 제394092호에서는 그러한 내구성 향상을 위한 방안이 제시되지 못하였다.However, the main purpose of using the crushed waste tires is to improve the riding comfort when driving the vehicle by providing environmental protection and resilience to the package through the recycling of resources, the use of crushed waste tires does not improve the durability of the package. Therefore, in the case of using the crushed waste tires, there is a need to separately devise a method for improving the durability of the package, and Patent No. 394092 does not provide a method for improving such durability.
본 발명은 종래 개질재들의 문제점들을 해소하기 위하여 안출된 것으로, 본 발명의 목적은 고가의 장치나 복잡한 과정을 거치지 않고도 용이하게 사용할 수 있는 개질재 칩을 제공하는 것이다. 즉, 본 발명은 종래 개질재들에 아스팔트를 일체화가 되게 혼합하여 칩으로 제조한 후 아스콘에 투입 사용으로써, 개질재의 아스콘 투입에 별도 고가의 장비나 복잡한 공정이 필요하지 않도록 하는 것을 목적으로 한다.The present invention has been made to solve the problems of the conventional modifiers, the object of the present invention is to provide a modifier chip that can be easily used without going through expensive devices or complicated processes. That is, the present invention aims to avoid the need for a separate expensive equipment or complicated process for adding the asphalt concrete to the asphalt concrete after mixing the asphalt to be integrated with the conventional modifiers to be integrated into the asphalt after the production of chips.
본 발명의 다른 목적은 분쇄폐타이어 사용에 따른 장점을 최대한 살리면서 동시에 포장체의 내구성을 향상시킬 수 있도록 하는 것이다. 즉, 본 발명은 분쇄폐타이어와 개질재를 함께 혼합한 칩을 제조하여 사용함으로써, 분쇄폐타이어 사용에 따른 장점을 살리면서 동시에 분쇄폐타이어 사용으로 인하여 초래될 수 있는 내구성 저하의 문제점을 방지할 수 있도록 하는 것을 목적으로 한다.Another object of the present invention to improve the durability of the package while at the same time take full advantage of the use of grinding waste tires. In other words, the present invention by manufacturing and using a chip mixed with a grinding waste tire and a modifier material, while utilizing the advantages of using the grinding waste tire at the same time to prevent the problem of durability degradation that may be caused by using the grinding waste tire. The purpose is to make it possible.
도 1은 아스팔트 콘크리트에서 개질재의 작용을 도시한 개념도,1 is a conceptual diagram showing the action of the modifier in asphalt concrete,
도 2a는 분쇄폐타이어 입자와 아스팔트의 결합을 도시한 개념도,Figure 2a is a conceptual diagram showing the combination of the grinding waste tire particles and asphalt,
도 2b는 도 2a의 결합이 아스팔트 전체에 확산된 것을 도시한 개념도,FIG. 2B is a conceptual diagram illustrating that the bond of FIG. 2A is spread over the asphalt; FIG.
도 3a는 아스팔트와 개질재의 결합을 도시한 개념도,3a is a conceptual diagram showing the combination of asphalt and modifiers,
도 3b는 도 3a의 결합에서 아스팔트가 활성화된 상태를 도시한 개념도이다.3B is a conceptual diagram illustrating a state in which asphalt is activated in the combination of FIG. 3A.
본 발명의 개질재 칩은 종래 개질제인 SBS, SIS, LDPE 등을 별도의 가열장치나 고전단 설비 없이도, 추후 아스팔트 및 골재 등과 용이하게 혼합될 수 있도록 하는 것이다. 보다 구체적으로는, 본 발명의 방법은 SBS, SIS, LDPE 등의 개질재를 아스팔트와 함께 가열하여 용융 혼합 후, 이를 압축기 등을 이용하여 적당한 크기로 배출하면서 공랭식 또는 수랭식으로 냉각시키고, 그 후 분쇄기 또는 절단기로 분쇄 또는 절단하여 소정 크기의 칩으로 제조하는 것이다.The reformer chip of the present invention is to be easily mixed with conventional asphalt, aggregate and SBS, SIS, LDPE, etc., without a separate heating device or high shear equipment. More specifically, the method of the present invention is melted by mixing the modified materials such as SBS, SIS, LDPE with asphalt, and then cooled by air-cooled or water-cooled while discharging them to a suitable size using a compressor or the like, and then grinder Or by grinding or cutting with a cutter to produce a chip of a predetermined size.
이하 본 발명에 대하여 상세히 설명한다.Hereinafter, the present invention will be described in detail.
본 발명의 개질재 칩 제조방법은 SBS, SIS 또는 LDPE 등의 개질재의 하나 또는 둘 이상 혼합한 것 1 중량부에 대하여 아스팔트를 0.2-3 중량부 준비하는 공정, 전기 공정에서 준비된 아스팔트를 150-250℃로 가열하여 용융 상태로 만드는 공정, 전기 공정의 용융된 아스팔트에 개질재를 서서히 투입하면서 가열 혼합하는 공정, 전기 공정의 혼합물을 압출기 등을 이용하여 소정의 크기로 배출하면서 공냉 또는 수냉의 방식으로 식히는 공정, 및 전기 공정의 냉각된 혼합물을 적당한 크기로 분쇄 또는 절단하여 칩을 제조하는 공정으로 이루어 진 것이다.The method of manufacturing a modifier chip of the present invention is a step of preparing 0.2-3 parts by weight of asphalt based on 1 part by weight of one or more of a modifier such as SBS, SIS, or LDPE, and 150-250 asphalt prepared in an electrical process. Heating process to make it into molten state, heating and mixing the modified materials into molten asphalt of electric process, and discharging the mixture of electric process to a predetermined size using extruder or the like by air or water cooling method. The cooling process, and the process of preparing a chip by grinding or cutting the cooled mixture of the electrical process to a suitable size.
이와 같이 하여 제조된 본 발명의 개질재 칩은 적당한 용기에 넣어 보관하였다가 아스콘 포장 현장에서 아스콘의 타 재료들과 함께 아스콘 믹서에 투입하여 사용하면 된다.The reformer chip of the present invention prepared as described above may be stored in an appropriate container, and then used in an ascon mixer together with other materials of ascon at the ascon packaging site.
아스팔트는 약 60℃에서 연화되는데 반하여 아스팔트와 골재 채움재 등이 혼합된 아스콘은 약 150℃이상에서 연화된다. 본 발명은 이러한 현상을 활용한 것으로, 본 발명의 개질재 칩이 아스콘 믹서에 투입되면, (타 아스콘 재료들이 연화되기 전인) 60℃ 근방에서 본 발명의 개질재 칩에 함유된 아스팔트가 미리 연화 (활성화)되어 개질재와 분리되기 때문에, 개질재 입자들이 (추후 150℃ 근방에서 연화되는) 아스콘 전반에 용이하게 분산되어지는 것이다.Asphalt softens at about 60 ℃, while asphalt mixed with asphalt and aggregate fillers softens at about 150 ℃ or higher. The present invention utilizes such a phenomenon, and when the modifier chip of the present invention is put into an ascon mixer, the asphalt contained in the modifier chip of the present invention is softened in advance around 60 ° C (before other ascon materials are softened). Activator), which separates it from the modifier, so that the modifier particles are easily dispersed throughout the ascon (which subsequently softens around 150 ° C).
도 3a는 본 발명의 개질재 칩의 개념을 도시한 것이고, 도 3b는 본 발명의 개질재 칩의 아스팔트가 연화되어 활성화되는 개념을 도시한 것이다. 즉, 도 3a에 도시되어 있듯이, 본 발명의 개질재 칩이 아스팔트와 결착되어 있다가, 아스콘 믹서에서 연화되면 도 3b에 도시되어 있듯이 아스팔트가 활성화되어 개질재 입자와 분리되므로, 그 분리된 개질재 입자들이 자유로이 아스콘 전반에 분산되어 진다.FIG. 3A illustrates the concept of the reformer chip of the present invention, and FIG. 3B illustrates the concept in which the asphalt of the reformer chip of the present invention is softened and activated. That is, as shown in Fig. 3a, when the modifier chip of the present invention is bound with asphalt, and softened in an asphalt concrete mixer, the asphalt is activated and separated from the modifier particles as shown in Fig. 3b. The particles are freely dispersed throughout the asphalt.
본 발명에서 주재료로 아스팔트를 사용하는 것은 아스팔트가 열에 잘 녹고 아스팔트 콘크리트의 주재료인 아스팔트와 같은 재질로서 분산이 쉽고, 빠르게 이루어질 수 있기 때문이다. 본 발명에서 사용되는 아스팔트로는, 도로포장용 아스팔트, 컷트백 아스팔트, 브라운 아스팔트, 천연 아스팔트, 타르 등 어느 것이나 사용할 수 있으나, 아스팔트의 감온성 효과를 증대시킬 수 있기 위해서는 브라운 아스팔트 또는 천연 아스팔트, 침입도 40 이하의 저 침입도의 아스팔트를 사용하는 것이 바람직하다.The use of asphalt as the main material in the present invention is because the asphalt melts well in heat and is easily dispersed in a material such as asphalt, which is the main material of asphalt concrete, and can be made quickly. As the asphalt used in the present invention, any one of road paving asphalt, cutback asphalt, brown asphalt, natural asphalt, tar and the like can be used. It is preferable to use the asphalt of the following low penetration.
본 발명의 개질재 칩 제조에 있어서 아스팔트를 개질재 1 중량부에 대하여 0.2-3 중량부로 사용하는 것이 바람직하다. 아스팔트를 개질재 1 중량부에 대하여 3 중량부 이상 사용하면, 최종 제품인 개질재 칩의 부피가 너무 커져 운반이나 사용에 불편이 많고, 한편으로 아스팔트를 0.2 중량부 이하로 사용하면 아스팔트와 개질재가 충분히 혼합되지 못하고 개질재 입자끼리 뭉쳐 있을 가능성이 높다. 그렇게 되면 개질재 칩이 아스콘 믹서에서 연화되어 분산될 때 분산력이 떨어져 전체 아스팔트와의 혼합이 충분히 되지 못하는 문제점이 발생할 수 있다.In manufacturing the modifier chip of the present invention, it is preferable to use asphalt at 0.2-3 parts by weight with respect to 1 part by weight of the modifier. If asphalt is used in an amount of 3 parts by weight or more based on 1 part by weight of the modifier, the volume of the modifier chip, which is the final product, is too large to be inconvenient to transport or use. On the other hand, when asphalt is used in an amount of 0.2 parts by weight or less, the asphalt and the modifier are sufficiently There is a high possibility that the particles of the modifier may not be mixed and aggregated together. In this case, when the modifier chip is softened and dispersed in the asphalt concrete, the dispersion force may be insufficient, and thus, the mixing chip may not be sufficiently mixed with the entire asphalt.
용융된 아스팔트에 개질재를 투입 혼합함에 있어서는 온도가 150-250℃로 유지되도록 계속 가열하는 것이 필요하다. 이때 미세 채움재를 투입 혼합할 수 있으나, 미세 채움재는 개질재와 아스팔트가 충분히 혼합된 후에 투입하는 것이 바람직하다. 미세 채움재로는 카본블랙, 석분, 규사분, 시멘트 등이 있는데, 이들 미세 채움재를 추가 혼합하면 아스콘의 강도 및 내구성을 향상시키는 효과가 있다.In the mixing and mixing of the modifier to the molten asphalt, it is necessary to continue heating to maintain the temperature at 150-250 ° C. At this time, the fine filler may be added and mixed, but the fine filler is preferably added after the reforming material and the asphalt are sufficiently mixed. Examples of the fine filler include carbon black, stone powder, silica sand, and cement, and further mixing these fine fillers has the effect of improving the strength and durability of the asphalt concrete.
가열 혼합된 혼합물을 냉각 후 분쇄 또는 절단하여 칩을 제조함에 있어서, 분쇄 또는 절단되는 개체의 크기는 되도록 5㎜ 이하로 작게 하는 것이 좋으며, 바람직하게는 3㎜ 이하로 하는 것이 좋다. 본 발명의 개질재 칩의 크기를 되도록 작게 하는 이유는 아스콘 믹서에서 연화되는데 소요되는 시간을 줄이기 위함이다.In the manufacture of the chip by cooling or pulverizing or cutting the mixed mixture, the size of the object to be crushed or cut is preferably as small as 5 mm or less, preferably 3 mm or less. The reason for reducing the size of the modifier chip of the present invention is to reduce the time it takes to soften in the asphalt concrete mixer.
한편, 본 발명의 개질재 칩은 분쇄폐타이어를 혼합하여 제조할 수도 있다. 본 발명의 개질재 칩에 분쇄폐타이어를 혼합하게 되면, 분쇄폐타이어 사용의 장점인 자원재활용 및 도로 포장체에 탄성 부여 등의 효과를 누릴 수 있음과 동시에, 개질재 사용의 장점인 아스콘의 하절기 소성변형 방지, 동절기 균열형성 방지, 내구성 강화 등의 효과를 누릴 수 있다.On the other hand, the modifier chip of the present invention may be prepared by mixing the grinding waste tires. When the crushed waste tire is mixed with the modified chip of the present invention, it is possible to enjoy the effects of recycling the resources and elasticity of the road pavement, which are advantages of using the crushed waste tire, and at the same time, the summer season of ascon which is an advantage of using the modified material. It can enjoy the effects of plastic deformation prevention, winter crack formation prevention and durability enhancement.
본 발명에 있어서 분쇄폐타이어를 혼합하여 개질재 칩을 제조하는 방법은 분쇄폐타이어와 유재 아스팔트 등이 일체화되도록 혼합한 후에, (앞서 설명한) 개질재와 아스팔트의 혼합물을 추가 혼합하여, (유재 아스팔트와 일체화된) 분쇄폐타이어와 결착시켜 칩으로 제조하는 것이다.In the present invention, a method of manufacturing a modified chip by mixing the crushed waste tires is mixed so that the crushed waste tires and oil asphalt, etc. are integrated, and then further mixed with the mixture of the modified material and asphalt (described above), It is made into a chip by binding with the crushed waste tire (integrated with).
본 발명의 분쇄폐타이어를 혼합하여 개질재 칩을 제조하는 공정은, 5㎜ 이하 크기로 분쇄된 분쇄폐타이어를 100-150℃가 되도록 간접 가열하여 입자의 표면을 겔화시키는 공정, 전기 공정의 표면이 겔화된 분쇄폐타이어 1 중량부에 유재아스팔트, 도로용 아스팔트, 브라운 아스팔트, 천연아스팔트, 컷트백 아스팔트 중의 하나를 0.05-0.5 중량부를 혼합시키는 공정, 전기 공정의 혼합물에 카본블랙, 석분, 규사분, 시멘트 등의 미세 채움재를 0.02-0.3 중량부 추가 혼합하는 공정, 전기 공정의 혼합물에 SBS, SIS 또는 LDEP 등의 개질재와 아스팔트의 혼합물을 추가하여 150-250℃로 가열 혼합하는 공정, 전기 공정의 혼합물을 압출기 등을 이용하여 소정의 크기로 배출하면서 공랭 또는 수랭의 방식으로 식히는 공정, 및 전기 공정의 냉각된 혼합물을 적당한 크기로 분쇄 또는 절단하여 칩을 제조하는 공정으로 이루어 진 것이다.The process of mixing the pulverized waste tire of the present invention to produce a modifier chip includes a step of indirectly heating the pulverized waste tire crushed to a size of 5 mm or less to 100-150 ° C. to gel the surface of the particles, and the surface of the electric process. A process of mixing 0.05-0.5 parts by weight of one of the materials asphalt, road asphalt, brown asphalt, natural asphalt and cutback asphalt to 1 part by weight of this gelled crushed waste tire; Adding 0.02-0.3 parts by weight of fine fillers such as cement and cement, adding a mixture of asphalt and a modified material such as SBS, SIS or LDEP to the mixture of the electrical process and heating and mixing at 150-250 ° C., the electrical process To cool the mixture in an air-cooled or water-cooled manner while discharging the mixture to a predetermined size using an extruder or the like, and pulverizing the cooled mixture of the electric process to an appropriate size. Or it is made of a process of manufacturing the chip by cutting.
위 공정에서 분쇄폐타이어를 100-150℃로 가열하는 것은 분쇄폐타이어의 표면을 겔화시키되 분쇄폐타이어 입자들이 과대 팽창되는 것을 방지하기 위함이다. 온도를 100℃ 이하로 가열하면 분쇄폐타이어 표면의 겔화가 어렵고, 150℃ 이상으로 가열하면 분쇄폐타이어 입자들이 과대 팽창될 우려가 있다.In the above process, the grinding waste tire is heated to 100-150 ° C. in order to gel the surface of the grinding waste tire, but to prevent the particles from being excessively expanded. When the temperature is heated to 100 ° C. or less, gelation of the surface of the crushed waste tire is difficult, and when heated to 150 ° C. or more, the crushed waste tire particles may be over-expanded.
위 공정들 중 분쇄폐타이어와 아스팔트를 일체화시킴에 있어서, 분쇄폐타이어 1 중량부에 대하여 아스팔트의 사용량을 0.05-0.5 중량부로 한 것은 0.05 중량부 이하의 경우 분쇄폐타이어 코팅량이 부족하게 되어 분쇄폐타이어와 아스팔트의 일체화(숙성)가 제대로 이루어지지 못할 염려가 있고, 0.5 중량부 이상의 경우에는 아스팔트가 과량으로 되어 사용되어 최종 제품인 개질재 칩의 부피가 너무 크게 되어 사용에 불편함을 초래할 수 있기 때문이다.In integrating the crushed waste tire and asphalt in the above processes, the amount of asphalt used is 0.05-0.5 parts by weight based on 1 part by weight of the crushed waste tires, the amount of coating of the crushed waste tires is insufficient in the case of 0.05 parts by weight or less There is a concern that tires and asphalt may not be properly integrated (maturation), and in case of 0.5 parts by weight or more, asphalt is used in excess, and the volume of the modifier chip, the final product, is too large, which may cause inconvenience. to be.
위 공정에 있어서, 분쇄폐타이어와 아스팔트의 혼합물에 카본블랙, 석분 규사분, 시멘트 등의 미세 채움재를 추가 혼합하는 이유는 분쇄폐타이어가 150℃의 고열에서 팽창되면서 분쇄폐타이어의 입자끼리 붙음을 방지하기 위함이다. 이들 미세 채움재를 0.02 중량부 이하로 사용하면 분쇄폐타이어 입자끼리의 부착을 충분히 방지할 수 없고, 또한 0.3 중량부 이상 사용은 불필요한 중량만 높이게 되므로, 이들 미세 채움재의 사용은 0.02-0.3 중량부로 한정하는 것이 바람직하다.In the above process, the reason for further mixing the fine fillers such as carbon black, stone silica sand powder, cement, etc. in the mixture of the grinding waste tire and asphalt is because the grinding waste tire is expanded at a high temperature of 150 ℃ to adhere the particles of the grinding waste tire. This is to prevent. If these fine fillers are used in an amount of 0.02 parts by weight or less, the adhesion of the crushed waste tire particles cannot be prevented sufficiently, and the use of these fine fillers is limited to 0.02-0.3 parts by weight since use of 0.3 parts by weight or more increases only unnecessary weight. It is desirable to.
위 공정에 있어서, SBS, SIS, LDPE 등의 개질재와 아스팔트 혼합물을 추가하여 150-250℃로 가열 혼합하는 것은, 분쇄폐타이어 사용으로 인하여 초래될 수 있는 포장체 내구성 저하를 방지하고 나아가 포장체의 하절기 소성변형방지, 동절기 균열방지의 효과를 얻기 위함이다. 용융된 아스팔트와 개질재를 투입 혼합함에 있어서는 온도가 150-250℃로 유지되도록 계속 가열하는 것이 필요하다.In the above process, adding and mixing the asphalt mixture with the modified materials such as SBS, SIS, LDPE and heated to 150-250 ℃, to prevent the degradation of the package body durability that can be caused by the use of grinding waste tires and further This is to obtain the effect of preventing plastic deformation in summer and preventing cracking in winter. In dosing and mixing molten asphalt and modifiers, it is necessary to continue heating to maintain the temperature at 150-250 ° C.
이때 개질재와 아스팔트 혼합물의 사용량은 포장되는 아스콘 전체에 사용되는 아스팔트 양을 감안하여 정한다. 즉, 투입되는 SBS, SIS 또는 LDPE 등 개질재의 총량이 아스콘 전체 아스팔트 사용량에 대하여 2-10%가 적정량임을 감안하여 정하여야 한다. 따라서 본 발명의 개질재 칩에 있어서 그에 함유된 SBS, SIS 또는 LDPE 등의 비율이 높은 경우에는 본 발명의 개질재 칩 투입량을 적게 하여야 할 것이고, 반대로 이들 개질재의 함유 비율이 적은 경우에는 본 발명의 개질재 칩 투입량을 많이 하여야 할 것이다.At this time, the amount of the modifier and the asphalt mixture is determined in consideration of the amount of asphalt used for the entire asphalt asphalt. That is, the total amount of modifiers such as SBS, SIS or LDPE to be injected should be determined in consideration of 2-10% of the total amount of asphalt used as asphalt. Therefore, when the ratio of SBS, SIS, or LDPE contained in the modifier chip of the present invention is high, the input amount of the modifier chip of the present invention should be reduced, and conversely, when the content of these modifiers is small, You will have to do a lot of modifier chip input.
본 발명의 개질재 칩 제조방법에 있어서, 필요에 따라 황, 파라핀, 아교, 송진 등을 혼합할 수도 있다. 물론, 필요에 따라 광섬유, 셀룰로오스 섬유, 폴리머 섬유 등의 보강섬유를 첨가할 수도 있다. 본 발명에 이러한 재료들을 혼합하여 사용하면, 아스콘의 품질을 극대화시킬 수 있다.In the modifier chip manufacturing method of the present invention, sulfur, paraffin, glue, rosin, etc. may be mixed as necessary. Of course, if necessary, reinforcing fibers such as optical fibers, cellulose fibers, and polymer fibers may be added. By using such materials in the present invention, it is possible to maximize the quality of ascon.
이하, 실시예에 의거 본 발명을 설명한다.EMBODIMENT OF THE INVENTION Hereinafter, this invention is demonstrated based on an Example.
(실시예)(Example)
300m 구간을 정하여 차량 통행을 위한 아스콘 도로포장을 함에 있어서, 그 중 100m는 일반 아스콘으로 포장하고(이하 "포장A"라 한다), 100m는 본 발명의 (분쇄폐타이어가 혼합되지 아니한) 개질재 칩을 첨가한 아스콘 포장(이하 "포장B"라 한다)을 하기로 하고, 나머지 100m는 본 발명의 분쇄폐타이어가 혼합된 개질재 칩을 첨가한 아스콘 포장(이하 "포장C"라 한다)을 하기로 하였다.In the case of paving asphalt road for vehicle traffic by setting the 300m section, 100m of which is packed with general asphalt (hereinafter referred to as "packing A"), 100m is the modifier of the present invention (without crushed tire) Ascon packaging containing chips (hereinafter referred to as "packing B") will be described, and the remaining 100m is used ascon packaging (hereinafter referred to as "packing C") containing modified chip mixed with the crushed waste tire of the present invention. It was decided as follows.
본 실시예에서 포장B에 사용된 개질재는, 천연아스팔트인 길소나이트(Gilsonite) 90㎏, 카본블랙 10㎏를 200℃로 가열하여 완전히 용융시키고, 이에 SBS 60㎏를 서서히 투입하면서 교반기로 교반하여 완전하게 혼합시키고, 이 혼합물을 폭 30㎝ 두께 0.5㎝로 수조에 투입하여 냉각시킨 다음 즉시 꺼내서 고무분쇄기로 5㎜의 크기로 분쇄하여 제조한 것이다. 이 개질재 칩은 사전에 제조하여 3㎏ 씩 계량하여 PP 비닐 포장에 보관해 둔 것이다.In the present embodiment, the modifier used in the packaging B is completely heated by heating 90 kg of natural asphalt Gilsonite and 10 kg of carbon black to 200 ° C., and completely stirring SBS 60 kg while stirring with a stirrer. The mixture was mixed to make a mixture, and the mixture was poured into a water tank with a thickness of 30 cm and 0.5 cm, cooled, and immediately taken out and ground to a size of 5 mm with a rubber grinder. The modifier chips were manufactured in advance and weighed in 3 kg and stored in PP plastic packaging.
본 실시예에서 포장C에 사용된 개질재는, 열 매체가 설치된 이중 벽의 1차 믹서에서 0.6㎜ 이하로 분쇄된 분쇄폐타이어 100㎏을 50℃로 가열하고, 이에 브라운아스팔트를 15㎏을 투입하여 혼합하여 5분경과 후 5㎏의 시멘트를 투입하여 분쇄폐타이어의 입자를 이완시키면서 140℃로 가열 혼합하고, 이 혼합물에 150-250℃로가열된 혼합된 SBS 30㎏과 브라운 아스팔트 30㎏을 투입하여 혼합하고, 이 혼합물을 압출기 호퍼에 투입, 압출하여 지름 10㎜로 빼내어 수조에서 냉각 시킨 후 3㎜로 분쇄 하였다. 이 개질재 칩 역시 사전에 제조하여 3㎏ 씩 계량하여 PP 비닐 포장에 보관해 둔 것이다.In the present embodiment, the modifier used in the packaging C was heated 100 kg of the crushed waste tires pulverized to 0.6 mm or less in a double-wall primary mixer equipped with a heat medium at 50 ° C., and 15 kg of brown asphalt was added thereto. After 5 minutes of mixing, 5 kg of cement was added and the mixture was heated and mixed at 140 ° C. while releasing the particles of the crushed waste tires, and 30 kg of mixed SBS and 30 kg of brown asphalt heated to 150-250 ° C. were added to the mixture. After mixing, the mixture was introduced into an extruder hopper, extruded, and pulled out to a diameter of 10 mm, cooled in a water bath, and then ground to 3 mm. The modifier chip was also manufactured in advance and weighed 3 kg and stored in a PP plastic package.
포장A는 개질재를 사용하지 아니한 일반적인 아스콘 포장이다. 그리고, 포장B와 포장C는 개질재를 사용하였다는 점만이 포장A와 다를 뿐, 사용된 자재들은 일반 아스콘 포장의 자재와 거의 동일하였다. 본 실시예에서는 기존의 시멘트 콘크리트 포장체 상부에 포장A, 포장B 및 포장C를 오버레이(overlay)식으로 포장하였으며, 포장A, 포장B 및 포장C에 사용된 자재 및 사용비율은 표2와 같다.Package A is a typical ascon package without modifiers. In addition, the packaging B and the packaging C differed from the packaging A only in that the modified materials were used, and the materials used were almost the same as those of the general asphalt concrete package. In this embodiment, pavement A, pavement B, and pavement pavement were packaged on the top of the existing cement concrete pavement, and the materials used and ratios used in pavement A, pavement B, and pavement are shown in Table 2. .
(표 2)Table 2
본 실시예에 사용된 골재의 입도와 합성 입도분포 (갭입도 기준 : Filler로서 CaCo33% 포함)는 표3과 같다.The particle size and synthetic particle size distribution of the aggregate used in this example (gap particle size criteria: CaCo 3 as filler 3%) are shown in Table 3.
(표 3)Table 3
본 실시예에서 상기의 재료들을 155-163℃로 가열 혼합한 후 덤프트럭으로 현장으로 운반하여 포설하였다. 포장B의 개질재는 현장에서 아스콘 믹서에 투입, 혼합시켜 바로 사용하였다. 현장 포설에 있어서는 통상의 방법에 따라 휘니샤로 포설한 다음 마카담, 탠덤로라와 타이어 로라로 다짐하였다. 다만, 포장C의 경우는 타이어 로라를 사용하지 않았다. 타이어 로라를 사용하면 분쇄폐타이어가 타이어 로라에 붙을 우려가 있기 때문에, 분쇄폐타이어를 사용한 아스콘 배합에서는 일반적으로 타이어 로라를 사용하지 않는다.In this embodiment, the above materials were heated and mixed at 155-163 ° C. and transported to a site by a dump truck. The modifier of package B was put in an ascon mixer on site and mixed and used immediately. In the field installation, it was installed in Hunisha according to the usual method, and then pledged to Macadam, Tandem Laura, and Tire Laura. In the case of Package C, however, tire rollers were not used. Since the use of tire rollers may cause the crushed waste tires to stick to the tire rollers, the tire rollers are generally not used in the ascon formulation using the crushed waste tires.
본 실시예에서 포장된 포장A, 포장B 및 포장C에 대하여 동적 안정도, 회복탄성계수 및 마모량을 시험하였는바, 그 결과는 표4와 같다.In this example, the package stability A, package B and package C was tested for dynamic stability, recovery modulus and the amount of wear, the results are shown in Table 4.
(표 4)Table 4
표4에서 보듯이, 포장B 및 포장C의 경우 소형변형의 기준인 동적 안정도가 개질재를 사용하지 않은 포장A에 비하여 급격히 향상되었고, 저온균열의 기준인 저온에서 회복탄성계수가 개질재를 사용하지 않은 포장A에 비하여 1/3 수준으로 안정되었으며, 라벨링 시험에 의한 마모량 역시 개질재를 사용하지 않은 포장A에 비하여 약 1/4에 해당할 정도로 개선되었음을 알 수 있었다.As shown in Table 4, for package B and package C, the dynamic stability, which is the criterion for small deformation, was dramatically improved compared to package A without modifier, and the modulus of recovery elasticity at low temperature, which is the criterion for low temperature cracking, was used. It was found to be stabilized at 1/3 level compared to the unpacked package A, and the amount of wear by the labeling test was also improved to about 1/4 compared to the package A without the modifier.
본 발명은 공중합체 폴리머인 SBS, SIS 또는 LDPE 등 종래 사용되고 있는 아스콘 개질재를 아스콘 포장에 용이하게 적용시킬 수 있도록 개량한 아스콘 개질재 및 그 제조방법에 관한 것으로, 본 발명의 아스콘 개질재는 그 사용이 용이 간편할 뿐만 아니라, 하절기 소성변형방지, 동절기 균열형성방지 및 미끄럼 저항의 향상 등 아스콘 품질을 충분히 개선시킬 수 있는 매우 유용한 것이다.The present invention relates to an improved ascon modifier and a method for producing the same, which can be easily applied to an ascon package, which is a conventionally used ascon modifier such as SBS, SIS, or LDPE, which is a copolymer polymer, and the ascon modifier of the present invention is used for the same. In addition to the ease of use, it is very useful to sufficiently improve ascon quality such as preventing plastic deformation in summer, preventing crack formation in winter and improving sliding resistance.
Claims (11)
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| KR10-2004-0056041A KR100492459B1 (en) | 2004-07-19 | 2004-07-19 | Material to improve quality of asphalt concrete, and the manufacturing method thereof |
| PCT/KR2005/002330 WO2006009386A1 (en) | 2004-07-19 | 2005-07-19 | Material in the shape of chip to improve quaility of asphalt concrete, and the manufacturing method thereof |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| KR100616800B1 (en) * | 2005-01-13 | 2006-08-29 | 주식회사 유닉스라바 | Manufacturing method of drainable packaging binder |
| CN1295280C (en) * | 2004-08-13 | 2007-01-17 | 中国石化镇海炼油化工股份有限公司 | Polymer modified asphalt special for formula one autodrome and its production method |
| KR100674127B1 (en) * | 2005-03-09 | 2007-01-24 | 황익현 | Modified chips of asphalt concrete and methods of manufacturing the same |
| CN101691733B (en) * | 2009-08-27 | 2011-07-20 | 东盟营造工程有限公司 | Mixing and stirring method and device in construction of SBS modified stone mastic asphalt |
| KR101242750B1 (en) * | 2012-09-19 | 2013-03-11 | 강원대학교산학협력단 | Manufacturing method of solid asphalt and manufacturing method of asphalt concrete using the same |
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| KR100669079B1 (en) | 2005-12-28 | 2007-01-16 | 한국건설기술연구원 | Asphalt modifier and its manufacturing method and method of manufacturing asphalt concrete produced using asphalt modifier |
| KR100990663B1 (en) * | 2008-05-14 | 2010-10-29 | 김준혁 | Asphalt color pavement composition with enhanced permeability, heat shielding function and anti-slip function, colored pattern permeable pavement using the same and construction method |
| KR101106763B1 (en) | 2009-02-23 | 2012-01-18 | 황익현 | Composition of asphalt concrete that can be constructed at medium temperature and its manufacturing method |
| KR100993100B1 (en) * | 2009-07-03 | 2010-11-08 | 황익현 | Method for road pavement of polymer cement concrete by compacting thereof and polymer cement concrete used in the method |
| KR101676936B1 (en) * | 2010-03-08 | 2016-11-16 | 체이스 코오포레이션 | Polymer modified binder and plant mix modifier for asphalt and process of making |
| KR101453127B1 (en) * | 2010-09-27 | 2014-10-27 | 주식회사 엘지화학 | Modified asphalt composition and method for preparing modified asphalt |
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| CN102505601B (en) * | 2011-11-21 | 2014-06-11 | 重庆大学 | Fast repairing method for asphalt concrete pavement |
| KR101359688B1 (en) * | 2012-03-30 | 2014-02-10 | (주)신행건설 | A support for height adjustment a manhole-box and construction method using it |
| KR101845316B1 (en) | 2017-06-28 | 2018-05-18 | 주식회사 오에이티엠엔씨 | High softening point reformed asphalt composition and waterproofing coating using the same |
| CN111138794B (en) * | 2020-01-09 | 2022-11-15 | 国路高科(北京)工程技术研究院有限公司 | SBS (styrene butadiene styrene) modifier adopting granulation-free dry method, preparation method and application thereof |
| KR102438827B1 (en) | 2021-02-22 | 2022-08-31 | 황익현 | Apparatus and method for asphalt chip manufacturing, asphalt chip and asphalt mix using therefore |
| CN115725028A (en) * | 2021-08-26 | 2023-03-03 | 中国石油天然气股份有限公司 | Melting graft modified SBS particles and its preparation method and application |
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| JPS6112752A (en) * | 1984-06-27 | 1986-01-21 | Nisshin Kogyo Kk | Self-hardening rubber asphalt waterproofing material containing tire crushed rubber |
| US5710196A (en) * | 1996-08-27 | 1998-01-20 | General Electric Company | Asphalt compositions containing acrylonitrile-butadiene-styrene copolymer |
| KR100317436B1 (en) * | 1999-08-02 | 2001-12-22 | 박승범 | A Manufacturing Methods of High Function Recycled Asphalt Concrete Mixtures using Crumb Rubber and Polymer Modifier for Pavement |
| KR100394092B1 (en) * | 2000-07-22 | 2003-08-09 | 한국기술산업 주식회사 | A paving method for porous and noiseless pavement using grinded waste tires |
| JP2002082615A (en) * | 2000-09-06 | 2002-03-22 | Masanori Yanagisawa | Label form |
-
2004
- 2004-07-19 KR KR10-2004-0056041A patent/KR100492459B1/en not_active Expired - Lifetime
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1295280C (en) * | 2004-08-13 | 2007-01-17 | 中国石化镇海炼油化工股份有限公司 | Polymer modified asphalt special for formula one autodrome and its production method |
| KR100616800B1 (en) * | 2005-01-13 | 2006-08-29 | 주식회사 유닉스라바 | Manufacturing method of drainable packaging binder |
| KR100674127B1 (en) * | 2005-03-09 | 2007-01-24 | 황익현 | Modified chips of asphalt concrete and methods of manufacturing the same |
| CN101691733B (en) * | 2009-08-27 | 2011-07-20 | 东盟营造工程有限公司 | Mixing and stirring method and device in construction of SBS modified stone mastic asphalt |
| KR101242750B1 (en) * | 2012-09-19 | 2013-03-11 | 강원대학교산학협력단 | Manufacturing method of solid asphalt and manufacturing method of asphalt concrete using the same |
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| Publication number | Publication date |
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| WO2006009386A1 (en) | 2006-01-26 |
| KR100492459B1 (en) | 2005-06-02 |
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