DK143449B - MODIFIED ASPHALTIC BITUMEN MASS - Google Patents
MODIFIED ASPHALTIC BITUMEN MASS Download PDFInfo
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- DK143449B DK143449B DK57068A DK57068A DK143449B DK 143449 B DK143449 B DK 143449B DK 57068 A DK57068 A DK 57068A DK 57068 A DK57068 A DK 57068A DK 143449 B DK143449 B DK 143449B
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- Prior art keywords
- bitumen
- sbr
- block copolymer
- viscosity
- block
- Prior art date
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- 239000010426 asphalt Substances 0.000 title description 72
- 229920001400 block copolymer Polymers 0.000 description 35
- 239000000203 mixture Substances 0.000 description 26
- 239000000463 material Substances 0.000 description 15
- 230000035515 penetration Effects 0.000 description 12
- 229920000642 polymer Polymers 0.000 description 9
- 239000003337 fertilizer Substances 0.000 description 7
- 239000004793 Polystyrene Substances 0.000 description 6
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 6
- 229920002223 polystyrene Polymers 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 229920001577 copolymer Polymers 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 238000005336 cracking Methods 0.000 description 3
- 150000001993 dienes Chemical class 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 229920001971 elastomer Polymers 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- 239000004416 thermosoftening plastic Substances 0.000 description 2
- YZCKVEUIGOORGS-NJFSPNSNSA-N Tritium Chemical compound [3H] YZCKVEUIGOORGS-NJFSPNSNSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 229940112822 chewing gum Drugs 0.000 description 1
- 235000015218 chewing gum Nutrition 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 238000007580 dry-mixing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 230000004720 fertilization Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 239000006187 pill Substances 0.000 description 1
- 229920001195 polyisoprene Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229920005604 random copolymer Polymers 0.000 description 1
- 239000000565 sealant Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052722 tritium Inorganic materials 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
- 239000004636 vulcanized rubber Substances 0.000 description 1
Classifications
-
- 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
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Civil Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Paints Or Removers (AREA)
Description
U3449U3449
Den foreliggende opfindelse angår en modificeret asphaltisk bitumenmasse, dvs. et materiale indeholdende asphaltisk bitumen, som er modificeret med bestemte blokcopolymere af styren og konjugerede diener.The present invention relates to a modified asphaltic bitumen mass, i.e. a material containing asphaltic bitumen modified with certain block copolymers of styrene and conjugated dienes.
5 Asphaltiske bitumener karakteriseres ved forskellige fysiske egenskaber og ved deres fremstillingsmåde. De ved direkte destillation fremstillede bitumener indeholder sædvanligvis de remanenser, som fås ved fraktioneret destillation af jordolier og jordoliefraktioner. Begarter fås often enten efter samme metode eller som præcipitat, når der udvindes ekstrakter 10 af visse oliefraktioner ved hjælp af et opløsningsmiddel. Krakkede bitumener fås som remanenser ved en krakningsbehandling, medens blæste bitumener er de produkter, som fås ved blæsning af ved direkte destillation fremstillede bitumener eller ved blæsning af et præcipitations-bitumen eller et krakningsbitumen.5 Asphaltic bitumen is characterized by different physical properties and their mode of manufacture. The bitumen produced by direct distillation usually contains the residuals obtained by fractional distillation of petroleum oils and petroleum fractions. Starter is often obtained either by the same method or as precipitate when extracting 10 of certain oil fractions by means of a solvent. Cracked bitumens are obtained as residuals by a cracking treatment, while blown bitumens are those obtained by blowing bitumen produced by direct distillation or by blowing a precipitation bitumen or cracking bitumen.
15 I reglen er bitumeners sprødhed og blødgøringspunkt ikke uafhængige af hinanden. Et bitumen med et højt blødgøringspunkt er sprødt ved lave temperaturer, medens et bitumen, som endnu er tilstrækkelig fleksibelt ved lav temperatur, har et lavt blødgøringspunkt. Det ville især 20 være ønskeligt at tilvejebringe et bitumenmateriale med lav sprødhed og højt blødgøringspunkt, når disse bitumener f.eks. skal anvendes til vejbelægningsformål eller ved tagbeklædning. Fra hollandsk patentansøgning nr. 6404385, svarende til belgisk patent nr. 646835, er det kendt, at der ved tilsætning af blokcopolymere med konfiguration A-B-A, hvor 25 hvert A, uafhængigt af det andet A, betegner en polystyrenblok med en molekylvægt på 2000 til 100.000, og B betegner en polymer blok af en konjugeret dien med en molekylvægt fra 5000 til 200.000, fås blandinger med forbedret viskositet ved forhøjet temperatur og forbedret strækbarhed og fleksibilitet ved lav temperatur. I disse blandinger er 30 blokcopolymerindholdet fra 0,01 til 75 vægtprocent. I USA patentskrift nr. 3.265.765 er det nævnt, at blokcopolymere af typæn A-B-A, hvor blokkene A er ikke-elastomere polymerblokke med molekylvægt 2000 - 100.000, og blok B er en elastomer polymerblok med molekylvægt mellem ca. 25.000 og 1.000.000, kan dispergeres i asphalt til 35 forbedring af viskositeten ved høj temperatur og til forbedring af strækkelighed og viskositet ved lav temperatur, men der gives ingen detaljerede oplysninger om mængden og om egenskaberne hos asphalten.15 As a rule, the brittleness and softening point of bitumen are not independent of each other. A bitumen with a high softening point is brittle at low temperatures, while a bitumen which is still sufficiently flexible at low temperature has a low softening point. In particular, it would be desirable to provide a low brittleness and high softening bitumen material when these bitumen e.g. must be used for road paving purposes or for roofing. From Dutch Patent Application No. 6404385, corresponding to Belgian Patent No. 646835, it is known that by the addition of block copolymers with configuration ABA, where each A, independently of the other A, denotes a polystyrene block having a molecular weight of 2000 to 100,000 and B represents a polymer block of a conjugated diene having a molecular weight of 5000 to 200,000, mixtures with improved viscosity at elevated temperature and improved extensibility and flexibility at low temperature are obtained. In these mixtures, the 30 block copolymer content is from 0.01 to 75% by weight. In United States Patent No. 3,265,765, it is mentioned that block copolymers of type A-B-A, where blocks A are non-elastomeric polymer blocks of molecular weight 2000 - 100,000, and block B is an elastomeric polymer block of molecular weight between approx. 25,000 and 1,000,000, can be dispersed in asphalt to improve high temperature viscosity and to improve extensibility and low temperature viscosity, but no detailed information on the amount and properties of the asphalt is provided.
U3449 2U3449 2
Det har nu vist sig, at ikke ethvert bitumen er blandbar med denne type blokcopolymer. Ifølge opfindelsen er det til opnåelse af en homogen blanding nødvendigt at anvende et bitumen, hvis blødgøringspunkt er højst 63°C. Endvidere har det vist sig, at bitlimenets blødgøringspunkt 5 er af essentiel betydning for egenskaberne hos bitumen/blokcopolymer-blandingen.It has now been found that not every bitumen is miscible with this type of block copolymer. According to the invention, to obtain a homogeneous mixture, it is necessary to use a bitumen whose softening point is at most 63 ° C. Furthermore, it has been found that the softening point 5 of the bitumen is essential for the properties of the bitumen / block copolymer mixture.
Opfindelsen angår derfor en modificeret asphaltisk bitumenmasse indeholdende en blokcopolymer med den almene formel A-B-A, hvor 10 hvert A, uafhængigt af det andet A, er en polystyrenblok med en molekylvægt på 2.000 - 100.000, og B betegner en polymerblok med en molekylvægt på 5.000 - 200.000 af en konjugeret dien, hvilken modificerede asphaltiske bitumenmasse er ejendommelig ved, at det asphaltiske bitumen har et blødgøringspunkt på højst 63°C og indeholder 15 0,1 - 24,9 vægtprocent, beregnet på massens vægt, af den blokcopolymere, at hver blok A har en gennemsnitlig molekylvægt mellem 10.000 og 30.000, og at blok B har en gennemsnitlig molekylvægt mellem 30.000 Og 125.000.The invention therefore relates to a modified asphaltic bitumen mass containing a block copolymer of the general formula ABA, wherein each 10 A, independently of the other A, is a polystyrene block having a molecular weight of 2,000 - 100,000 and B represents a polymer block having a molecular weight of 5,000 - 200,000 of a conjugated diene, the modified asphaltic bitumen mass being characterized in that the asphaltic bitumen has a softening point of not more than 63 ° C and contains 15 0.1 to 24.9% by weight of the mass copolymer of each block A has an average molecular weight between 10,000 and 30,000, and that block B has an average molecular weight between 30,000 and 125,000.
20 Det her omhandlede bitumen omfatter ved direkte destillation fremstillede, krakkede og blæste asphaltbitumener med den betingelse, at blødgørings-punktet ikke er højere end 63°C. Normalt ligger blødgøringspunkterne i området fra 21 til 63°C, fortrinsvis mellem 29 og 56°C. Fortrinsvis har det omhandlede bitumen en penetration, målt efter ASTM-metode 25 D5-61, mellem 150 - 300. Blødere bitumener beskrives sædvanligvis ved deres viskositet og er sådanne, som har en viskositet på 100 -1000 S SF (see. efter Saybolt-Furol) ved 99°C. Der kan anvendes blandinger af bitumener, f.eks. sådanne, som fås ved sammenblanding af en meget blød asphaltisk olie eller et blødt asphaltisk bitumen med et 30 bitumen, som har et forholdsvis højt blødgøringspunkt, til opnåelse af et produkt med et blødgøringspunkt, som er højst 63°C.The present bitumen comprises, by direct distillation, prepared, cracked and blown asphalt bitumen, provided that the softening point is not higher than 63 ° C. Usually, the softening points are in the range of 21 to 63 ° C, preferably between 29 and 56 ° C. Preferably, the bitumen in question has a penetration, measured by ASTM method 25 D5-61, between 150-300. Softer bitumens are usually described by their viscosity and are those having a viscosity of 100-1000 S SF (see Furol) at 99 ° C. Mixtures of bitumens, e.g. those obtained by admixing a very soft asphaltic oil or a soft asphaltic bitumen with a 30 bitumen having a relatively high softening point to obtain a product having a softening point not exceeding 63 ° C.
De blokcopolymere er i og for sig kendte, f.eks. fra hollandsk patentansøgning nr. 6404385 (belgisk patentskrift nr. 646835) og USA-patentskrift 35 nr. 3.265.765, En særlig hensigtsmæssig blokcopolymer har sammensætningen polys tyren-polyisopren - polys tyren.The block copolymers are known per se, e.g. from Dutch Patent Application No. 6404385 (Belgian Patent No. 646835) and U.S. Patent No. 353,665,765, A particularly suitable block copolymer has the composition polys tyrene-polyisoprene - polys tyrene.
143449 3143449 3
De blokcopolymere, som indeholder op til 50 vægtprocent af blokke A, beregnet på den copolymeres vægt, er de mest velegnede til forbedring af bitumenmassens bøjelighed.The block copolymers containing up to 50% by weight of blocks A, based on the weight of the copolymer, are most suitable for improving the flexibility of the bitumen mass.
5 De her angivne gennemsnitlige molekylvægte er de molekylvægte, som er beregnet på grundlag af i forvejen bestemte relationer mellem grænseviskositetstal (intrincis viscosity) og molekylvægt, hvilke relationer er konstateret ved, støttet af og suppleret ved tritium-tællemetoder. Disse metoder til molekylvægtbestemmelse har vist sig at stemme nøje overens.5 The average molecular weights given here are the molecular weights calculated on the basis of predetermined relations between intrinsic viscosity and molecular weight, which relationships are established by, supported by and supplemented by tritium counting methods. These molecular weight determination methods have been found to be closely matched.
1010
De omhandlede blokcopolymere har den specielle egenskab, at de opfører sig ligesom vulkaniserede kautsjukker, uden at de har været udsat for vulkanis eringsbehandling.The block copolymers in question have the special feature that they behave like vulcanized rubber jugs, without being subjected to vulcanization treatment.
15 Det har desuden vist sig, at det ved anvendelse af de omhandlede blok copolymere er unødvendigt at anvende apparater, som giver store forskydningskræfter, når de omhandlede materialer fremstilles ved sammenblanding af deres bestanddele. Det er endvidere unødvendigt at anvende de blokcopolymere i opløsning eller i form af emulsioner eller latexer, da ingen af 20 disse forholdsregler er nødvendige for opnåelse af en tilfredsstillende dispergering af de blokcopolymere i bitumenet med et blødgøringspunkt i det angivne område. Den omhandlede modificerede asphaltiske bitumen-masse fremstilles derfor mest hensigtsmæssigt ved, at dens bestanddele sammenblandes ved konventionel tør sammenblanding, dvs. uden anven-25 delse af opløsnings- eller emulgeringsmidler.Furthermore, it has been found that using copolymers of the present invention it is unnecessary to employ apparatus which give great shear forces when the materials in question are produced by mixing their constituents. Furthermore, it is unnecessary to use the block copolymers in solution or in the form of emulsions or latexes, since none of these precautions are necessary to obtain a satisfactory dispersion of the block copolymers in the bitumen with a softening point in the specified range. The modified asphaltic bitumen mass of the present invention is therefore most conveniently prepared by mixing its constituents by conventional dry mixing, i.e. without the use of solvents or emulsifiers.
Ved tilstedeværelsen af de mindre mængder af blokcopolymere i bitumen-materialeme, fortrinsvis fra 0,2 til 10 vægtprocent, bliver de fysiske egenskaber til deres tilsigtede anvendelser, f.eks. i vejbelægninger og 30 ved beklædning af tage, forbedret. Således skal der f.eks. ved forbedringen i egenskaberne ved forholdsvis høje temperaturer forebygges opbuling og spordannelse i asphaltvejbelægning ved varme sommertemperaturer. Forbedringerne i egenskaber ved kolde betingelser medfører, at revnedannelse på grund af sprødhed formindskes kraftigt. Ved tilsætning 35 af de blokcopolymere til bituminøse tagbeklædningsmaterialer forbedres deres fysiske egenskaber med hensyn til trækstyrke og bøjelighed, og de får mindre tilbøjelighed til at "falde sammen". De gode fysiske egenskaber hos de på denne måde fremstillede materialer muliggør deres an- 4 143449 ven delse som specialiserede produkter, f.eks. tagbeklædning, vejbelægninger, boreslam på bitumenbasis, fuge tætningsmidler samt til andre anvendelsesformål. Materialerne kan modificeres ved hjælp af fyldmaterialer. Materialernes modul forøges væsentligt ved tilstedeværelse af termoplas-5 tiske stoffer, som er forenelige med systemet. Tilstedeværelsen af polystyren forbedrer også de resulterende materialers bearbejdelighed.In the presence of the smaller amounts of block copolymers in the bitumen materials, preferably from 0.2 to 10% by weight, the physical properties of their intended applications, e.g. in pavements and 30 in roofing, improved. Thus, e.g. By the improvement in the properties of relatively high temperatures, bulging and spore formation in asphalt pavement are prevented at hot summer temperatures. The improvements in cold-weather properties result in a sharp reduction in cracking due to brittleness. By adding 35 of the block copolymers to bituminous roofing materials, their physical properties with respect to tensile strength and flexibility are improved and they are less likely to "collapse". The good physical properties of the materials prepared in this way enable their use as specialized products, e.g. roofing, paving, bitumen-based drilling mud, joint sealants and other applications. The materials can be modified using filler materials. The modulus of the materials is greatly increased by the presence of thermoplastic substances which are compatible with the system. The presence of polystyrene also improves the workability of the resulting materials.
Et særligt interessant anvendelsesområde for de omhandlede materialer er til fremstilling af gødningskugler eller -piller med langsom frigørelse 10 af gødningen. Der tænkes her på sådanne kugler eller piller, hvor gødningsmidlet blandes med de omhandlede materialer i en sådan mængde, at gødningen bindes i egnede forme og størrelser til gødskning. Tilstedeværelsen af den blokcopolymere sammen med det asphaltiske bitumen medfører ikke blot en forøgelse af styrken af bitumenet, men bevirker 15 også en elastomer påvirkning derved, at den forebygger, at pillerne eller kuglerne går i stykker på grund af skarpe temperatur- og størrelsesændringer, som kan forekomme under skiftende fryse- og tøbetingelser.A particularly interesting area of application for the materials in question is for the production of fertilizers or slow release fertilizers 10 of the fertilizer. Here, such bullets or pills are envisaged where the fertilizer is mixed with the materials concerned in such an amount that the fertilizer is bound in suitable molds and sizes for fertilization. The presence of the block copolymer together with the asphaltic bitumen not only increases the strength of the bitumen, but also causes an elastomeric action by preventing the pellets or bullets from breaking due to sharp temperature and size changes that can occur. occur under changing freezing and molding conditions.
20 De omhandlede pellets kan være overtrukket med en overfladefilm af materialet, som ikke indeholder gødningsmidlet, således at de let kan håndteres, uden at gødningsmidlet er udsat for atmosfæren, før det er anbragt i jorden.The pellets in question may be coated with a surface film of the material which does not contain the fertilizer so that they can be easily handled without the fertilizer being exposed to the atmosphere before being placed in the soil.
25 En anden anvendelse er pelletisering af lavtkoncentrerede mineraimalme.Another use is the pelletization of low-concentration mineral mines.
De her omhandlede materialer opfylder ikke blot den funktion, at de binder de pulveriserede malme til en hvilken som helst ønsket pellet-størrelse, men de kan også samtidig virke som reduktionsmidler og som brændstoffer ved rensningsprocessen.These materials not only fulfill the function of binding the powdered ores to any desired pellet size, but they can also simultaneously act as reducing agents and as fuels in the purification process.
3030
Eksempel 1.Example 1.
Det bitumen, som anvendes til de i det følgende beskrevne sammeniignings-35 forsøg, har følgende egenskaber: Penetration: 85 dmm ved 25°C, ring- og kugle-blødgøringspunkt: 47,5°C. Den ved forsøgene anvendte blokcopolymere (som i tabellerne betegnes "SIS") har den almene sammensætning polysty-ren-polyisopren-polystyren, idet blokmolekylvægtene er 10.000 - 75.000 - 143449 5 10.000. Til sammenligning fremstilles der tilsvarende baln dinger, i hvilke der anvendes den samme asphalt, men i hvilke der i stedet for den blok-copolymere anvendes en typisk tilfældig copolymerkautsjuk, kendt under betegnelsen "SBR", som er en copolymer med tilfældig fordeling af styren 5 og butadien. Det anvendte materiale er en typisk SBR med et styrenind- hold på 23,5% og en Mooney-viskositet, ML-4, på 52.The bitumen used for the comparative experiments described below has the following properties: Penetration: 85 dmm at 25 ° C, annular and ball softening point: 47.5 ° C. The block copolymers used in the experiments (referred to in the tables as "SIS") have the general composition of polystyrene-polyisoprene-polystyrene, with the block molecular weights being 10,000 - 75,000 - 143449. For comparison, similar coatings are prepared in which the same asphalt is used, but in which the typical copolymer rubber known as "SBR", which is a random copolymer of styrene, is used instead of the block copolymer. and butadiene. The material used is a typical SBR with a styrene content of 23.5% and a Mooney viscosity, ML-4, of 52.
Viskositeten af bitumenet uden tilblanding og af blandingerne med de to typer elastomere konstateres med et microviskosimeter med glidende plade. 10 I tabel I er angivet de opnåede resultater.The viscosity of the bitumen without admixture and of the mixtures with the two types of elastomers is ascertained by a sliding plate microviscosimeter. Table I shows the results obtained.
Tabel ITable I
Blokcopolymer/bitumen-blandinger: viskositets-temperatur- data, målt med et microviskosimeter med glidende plade.Block copolymer / bitumen mixtures: viscosity-temperature data, measured with a sliding plate microviscosimeter.
15 -15 -
Forholdet Polymer Viskositet, poise ved 0,1 See. 1Polymer Viscosity Ratio, Poise at 0.1 See. 1
mellem polymer og bitumen 20°C 30 C 45°C 60°Cbetween polymer and bitumen 20 ° C 30 C 45 ° C 60 ° C
20 η I c T~ 1:500 Bitumen kontrol 0,54x10 0,62x10 0,72x10 0,84x10 SIS 0,52 0,63 0,81 1,09 SBR 0,49 0,62 0,58 0,73 1:200 Bitumen kontrol 0,54xl07 0,62x10® 0,72x10® 0,87xl01 SIS 0,56 0,79 0,9 1,42 25 SBR 0,36 0,66 0,54 0,63 1:100 Bitumen kontrol 0,54xl07 0,62x10® 0,62x10® 0,87xl01 SIS 1,00 0,85 0,95 2,4 SBR 0,3 0,77 0,67 0,77 1:20 Bitumen kontrol 0,54xl07 0,62x10® 0,72x10® 0,85xl01 SIS 2,7 3,7 3,8 9,1 30 SBR 0,19 0,80 0,95 0,82 1:10 Bitumen kontrol 0,54xl07 0,62x10® 0,72x10® 0,87xl01 SIS 4,6 6,7 14,7 25 SBR 0,49 2,0 3,0 4,1 3520 η I c T ~ 1: 500 Bitumen control 0.54x10 0.62x10 0.72x10 0.84x10 SIS 0.52 0.63 0.81 1.09 SBR 0.49 0.62 0.58 0.73 1 : 200 Bitumen control 0.54x107 0.62x10® 0.72x10® 0.87xl01 SIS 0.56 0.79 0.9 1.42 25 SBR 0.36 0.66 0.54 0.63 1: 100 Bitumen control 0.54x107 0.62x10® 0.62x10® 0.87xl01 SIS 1.00 0.85 0.95 2.4 SBR 0.3 0.77 0.67 0.77 1:20 Bitumen Control 0.54x107 0, 62x10® 0.72x10® 0.85xl01 SIS 2.7 3.7 3.8 9.1 SBR 0.19 0.80 0.95 0.82 1:10 Bitumen Control 0.54x107 0.62x10® 0, 72x10® 0.87xl01 SIS 4.6 6.7 14.7 25 SBR 0.49 2.0 3.0 4.1 35
De relative ændringer i blandingernes viskositet varierer ikke meget -3 med forskydningshastigheden i det afprøvede område (4 x 10 og x 10 * reciprokke sekunder). Viskositeteme i tabel I bestemmes ved 6 143449 en konstant forskydningshastighed på 1 x 10_1 reciprokke sekunder.The relative changes in the viscosity of the mixtures do not vary much -3 with the shear rate in the area tested (4 x 10 and x 10 4 reciprocal seconds). The viscosities of Table I are determined at 6 143449 a constant shear rate of 1 x 10 10 reciprocal seconds.
Det fremgår af tabel I, at så lidt som 0,2 vægtprocent af den blokco-polymere i betydelig grad forøger bitumenets viskositet ved 20°C. Den relative virkning på viskositeten stiger stadig, når man går fra 20°C 5 til 60°C og fra en kautsjukkoncentration på 0,2 vægtprocent til det maksimale, som er afprøvet i denne serie, nemlig 10 vægtprocent. På grund af de omhandlede blokcopolymeres termoplastiske karakter er blandingernes fluiditet over 100°C tilstrækkelig ved bearbejdningstempera-tureme. Det fremgår klart, at den blokcopolymere ved en given kon-10 centration er betydelig bedre end en typisk SBR-kautsjuk til modificering af asphalts viskositet. Der kræves således ca. 5 vægtprocent uvulkaniseret SBR, før viskositeten påvirkes i kendelig grad.It is clear from Table I that as little as 0.2% by weight of the block copolymer significantly increases the viscosity of the bitumen at 20 ° C. The relative effect on viscosity still increases when going from 20 ° C 5 to 60 ° C and from a chewing gum concentration of 0.2% by weight to the maximum tested in this series, namely 10% by weight. Due to the thermoplastic nature of the block copolymers in question, the fluidity of the blends above 100 ° C is sufficient at the processing temperatures. It is clear that at a given concentration, the block copolymer is significantly better than a typical SBR rubber for modifying asphalt viscosity. Thus, approx. 5% by weight of unvulcanized SBR before viscosity is significantly affected.
Der foretages målinger af den dynamiske stivhed (dvs. det dynamiske 15 forskydningsmodul) i et microelastometer ved 0, 15 og 30°C. Resultaterne ved frekvenser på 10 og 40 cycler pr. sekund er vist i tabel II for blandinger indeholdende 1 vægtprocent af den blokcopolymere.Measurements of the dynamic stiffness (ie the dynamic shear modulus) are made in a microelastometer at 0, 15 and 30 ° C. The results at frequencies of 10 and 40 cycles per per second is shown in Table II for mixtures containing 1% by weight of the block copolymer.
Tabel IITable II
2020
Blandinger af blokcopolymer og bitumen i forholdet 1:100: Data for dynamisk stivhed-temperatur, målt på microelastometer.1: 100 block copolymer and bitumen mixtures: Dynamic stiffness temperature data, measured on microelastometer.
22
Dynamisk stivhed (dyn/cm )Dynamic stiffness (dyn / cm)
Temperatur Polymer 10 cycler/sek. 40 cycler/sek.Temperature Polymer 10 cycles / sec. 40 cycles / sec.
25 ___ 0°C Bitumen kontrol 1,50 x 1010 1,75 x 1010 SIS 0,24 0,32 SBR 0,20 0,23 15°C Bitumen kontrol 0,85 x 10^ 1,50 x 108 30 SBR 1,08 1,90 30°C Bitumen kontrol 0,23 x 108 0,92 x 108 SIS 0,81 1,90 SBR 0,48 1,6025 ___ 0 ° C Bitumen control 1.50 x 1010 1.75 x 1010 SIS 0.24 0.32 SBR 0.20 0.23 15 ° C Bitumen control 0.85 x 10 ^ 1.50 x 108 30 SBR 1 , 08 1.90 30 ° C Bitumen control 0.23 x 108 0.92 x 108 SIS 0.81 1.90 SBR 0.48 1.60
Den relative forøgelse af bitumens dynamiske stivhed, som fremkaldes af SBR i blandingen indeholdende 1% SBR, er tydeligt større end viskositeten i samme blanding.The relative increase of the bitumen dynamic stiffness induced by the SBR in the mixture containing 1% SBR is clearly greater than the viscosity of the same mixture.
35 7 U3U935 7 U3U9
Tabel III viser blødgøringspunkter bestemt ved ASTM-prøvemetode 36-26 samt penetrationer ved 25°C (ASTM-prøvemetode D5-61). Det vil ses, at den blokcopolymere i de fleste af de afprøvede produkter formindsker bitumenets penetration, medens det normale SBR faktisk fremkalder en 5 forøgelse af penetrationen.Table III shows softening points determined by ASTM test method 36-26 and penetrations at 25 ° C (ASTM test method D5-61). It will be seen that in most of the tested products, the block copolymer decreases the bitumen penetration, while the normal SBR actually induces an increase in penetration.
Tabel IIITable III
Blokcopolymer/bitumen-blandinger, blødgøringspunkt og penetrationsdata.Block copolymer / bitumen blends, softening point and penetration data.
1010
Forholdet Polymer Blødgøringspunkt, Penetration, mellem °C mm polymer og bitumen 1:500 Bitumen kontrol 48 72 15 SIS 48 66 SBR 48,5 72 1:200 Bitumen kontrol 48 72 SIS 48,5 68 1:100 Bitumen kontrol 48 72 20 SIS 50 67 SBR 50 79 1:20 Bitumen kontrol 48 72 SIS - 67 SBR 57 96 1:10 Bitumen kontrol 48 72 25 SIS 71 67 SBR 67 84 30 Eksempel 2.Ratio Polymer Softening Point, Penetration, between ° C mm Polymer and Bitumen 1: 500 Bitumen Control 48 72 15 SIS 48 66 SBR 48.5 72 1: 200 Bitumen Control 48 72 SIS 48.5 68 1: 100 Bitumen Control 48 72 20 SIS 50 67 SBR 50 79 1:20 Bitumen control 48 72 SIS - 67 SBR 57 96 1:10 Bitumen control 48 72 25 SIS 71 67 SBR 67 84 30 Example 2.
Blokcopolymeren, som anvendes i dette eksempel, har den almindelige struktur polystyren-polybutadien-polystyren, og molekylvægtene i blokkene er 14.000 - 65.000 - 14.000. Denne blokcopolymere blandes 35 med asphaltiske bitumener med forskellige blødgøringspunkter, hen holdsvis 39, 65 og 86°C (ring- og kuglemetoden). I hver blanding er mængden af blokcopolymeren 10 vægtprocent. I nedenstående tabel 1A3Å49 8 er penetrationen (25°C, dmm), blødgøringspunktet (°C) og Fraass-brud-punkt (°C) anført for disse bitumener og for blandingerne af bitumen-blokcopolymere.The block copolymer used in this example has the general structure of polystyrene-polybutadiene-polystyrene, and the molecular weights of the blocks are 14,000 - 65,000 - 14,000. This block copolymer is mixed with asphaltic bitumens with different softening points, respectively 39, 65 and 86 ° C (ring and ball method). In each mixture, the amount of the block copolymer is 10% by weight. Table 1A3Å49 8 below shows the penetration (25 ° C, dmm), the softening point (° C) and the Fraass break point (° C) for these bitumens and for the mixtures of bitumen block copolymers.
5 Tabel5 Table
Bitumen eller blanding Penetration Blødgøringspunkt Fraass-brud-. deraf dmm °C punkt, °CBitumen or Mixture Penetration Softening Point Fraass fracture. hence dmm ° C point, ° C
10 1) bitumen 180/200 190 39 - 24 2) do + blokcopolymer 73 110 25 3) bitumen 20/30 22 65 -8 4) do + blokcopolymer 18 105 + 1 15 5) bitumen R 85/25 22 86 - 14 6) do + blokcopolymer 22 123 kan ikke bestemmes10 1) bitumen 180/200 190 39 - 24 2) do + block copolymer 73 110 25 3) bitumen 20/30 22 65 -8 4) do + block copolymer 18 105 + 1 15 5) bitumen R 85/25 22 86 - 14 6) do + block copolymer 22 123 cannot be determined
Af indholdet i tabellen fremgår det, at der med bitumen 180/200 fås 20 en blanding med meget mindre penetration og et blødgøringspunkt, som er 71°C højere end for selve bitumenet, hvorimod Fraass-brudpunktet endog er faldet en smule. Med bitumen 20/30 er faldet i penetrationen relativt lille, og stigningen i blødgøringspunktet for blandingen er kun 45°C; brudpunktet er steget til +1°C. Med bitumen R 85/25 fås en 25 blanding med uændret penetration, og stigningen i blødgøringspunktet er kun 37°C. Bestemmelsen af Fraass-brudpunkt er ikke mulig (jfr. nedenfor).From the contents of the table it appears that with bitumen 180/200, 20 is obtained a mixture with much less penetration and a softening point which is 71 ° C higher than for the bitumen itself, whereas the Fraass breaking point has even slightly decreased. With bitumen 20/30, the decrease in penetration is relatively small and the increase in the softening point of the mixture is only 45 ° C; the breaking point has risen to + 1 ° C. With bitumen R 85/25, a mixture with unchanged penetration is obtained and the increase in the softening point is only 37 ° C. Determination of Fraass break point is not possible (see below).
Ved blanding af det asphaltiske bitumen og blokcopolymeren, som ud-30 føres ved forhøjet temperatur, iagttages følgende: blanding (2) er en homogen og lavviskos væske efter 3 timers omrøring ved 160°C. Blanding (4) er efter 3 timers omrøring ved 180°C homogen, men blandingen har høj viskositet, og omrøringen er vanskelig. Blanding (6) er ikke homogen selv efter 6 timers blanding ved 200°C; blandingen er meget 35 stiv efter afkøling og meget inhomogen, og blokcopolymeren danner en så grov dispersion i det asphaltiske bitumen, at en pålidelig Fraass-bestemmelse ikke kan udføres.When mixing the asphaltic bitumen and the block copolymer carried out at elevated temperature, observe the following: mixture (2) is a homogeneous and low viscous liquid after stirring at 160 ° C for 3 hours. Mixture (4) is homogeneous at 180 ° C after 3 hours of stirring, but the mixture has high viscosity and stirring is difficult. Mixture (6) is not homogeneous even after 6 hours of mixing at 200 ° C; the mixture is very stiff after cooling and very inhomogeneous, and the block copolymer forms such a coarse dispersion in the asphaltic bitumen that a reliable Fraass determination cannot be performed.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US61618867A | 1967-02-15 | 1967-02-15 | |
| US61618867 | 1967-02-15 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| DK143449B true DK143449B (en) | 1981-08-24 |
| DK143449C DK143449C (en) | 1982-02-15 |
Family
ID=24468387
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DK57068A DK143449C (en) | 1967-02-15 | 1968-02-13 | MODIFIED ASPHALTIC BITUMEN MASS |
Country Status (9)
| Country | Link |
|---|---|
| AT (1) | AT277042B (en) |
| BE (1) | BE710702A (en) |
| CH (1) | CH511267A (en) |
| DE (1) | DE1720169C3 (en) |
| DK (1) | DK143449C (en) |
| FR (1) | FR1557193A (en) |
| GB (1) | GB1177725A (en) |
| NL (1) | NL140888B (en) |
| SE (1) | SE357374B (en) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3363912A (en) * | 1965-05-07 | 1968-01-16 | John W. Holloway | Seal gasket |
| CH527247A (en) * | 1968-09-03 | 1972-08-31 | Shell Int Research | Bituminous mass |
| FR2367102A1 (en) * | 1976-10-08 | 1978-05-05 | Elf Union | COMPOSITIONS OF BITUMES CONTAINING POLYMERS |
| FR2376188A1 (en) * | 1976-12-28 | 1978-07-28 | Elf Union | PROCESS FOR PREPARING COMPOSITIONS OF POLYMERIC BITUMES |
| US4394482A (en) | 1980-07-14 | 1983-07-19 | Owens-Corning Fiberglas Corporation | Modified asphalt composition |
| FR2580658B1 (en) * | 1985-04-22 | 1987-06-05 | Beugnet Sa | COATING COMPOSITION BASED ON BITUMEN AND RECOVERY RUBBER POWDER |
| US5324758A (en) * | 1988-08-11 | 1994-06-28 | Sohwa Shell Sekiyu Kabushiki Kaisha | Vibration damping material of asphalt cement |
| JP2607383B2 (en) * | 1988-08-11 | 1997-05-07 | 昭和シェル石油株式会社 | Asphalt vibration damping material |
| WO1994009072A1 (en) * | 1992-10-22 | 1994-04-28 | Shell Internationale Research Maatschappij B.V. | Bituminous binder composition |
| EP2220167A1 (en) * | 2007-12-12 | 2010-08-25 | Taieb Marzouki | Method for transporting straight run bitumen, and bitumen mixture |
| FR2965270B1 (en) | 2010-09-24 | 2014-11-07 | Eiffage Travaux Publics | BITUMEN AND RUBBER BINDER FOR PAVEMENT COATING OR THE LIKE, PROCESS FOR PRODUCING THE SAME AND USES THEREOF |
-
1968
- 1968-02-13 DE DE19681720169 patent/DE1720169C3/en not_active Expired
- 1968-02-13 GB GB690668A patent/GB1177725A/en not_active Expired
- 1968-02-13 BE BE710702D patent/BE710702A/xx not_active IP Right Cessation
- 1968-02-13 NL NL6801997A patent/NL140888B/en not_active IP Right Cessation
- 1968-02-13 CH CH209168A patent/CH511267A/en not_active IP Right Cessation
- 1968-02-13 FR FR1557193D patent/FR1557193A/fr not_active Expired
- 1968-02-13 DK DK57068A patent/DK143449C/en not_active IP Right Cessation
- 1968-02-13 SE SE184068A patent/SE357374B/xx unknown
- 1968-02-13 AT AT136468A patent/AT277042B/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| DE1720169C3 (en) | 1974-07-11 |
| DE1720169A1 (en) | 1969-10-02 |
| SE357374B (en) | 1973-06-25 |
| AT277042B (en) | 1969-12-10 |
| NL140888B (en) | 1974-01-15 |
| NL6801997A (en) | 1968-08-16 |
| CH511267A (en) | 1971-08-15 |
| FR1557193A (en) | 1969-02-14 |
| GB1177725A (en) | 1970-01-14 |
| BE710702A (en) | 1968-08-13 |
| DK143449C (en) | 1982-02-15 |
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