NO122874B - - Google Patents
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- NO122874B NO122874B NO170630A NO17063067A NO122874B NO 122874 B NO122874 B NO 122874B NO 170630 A NO170630 A NO 170630A NO 17063067 A NO17063067 A NO 17063067A NO 122874 B NO122874 B NO 122874B
- Authority
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- Prior art keywords
- mineral
- mixture
- emulsion
- solid particles
- addition
- Prior art date
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- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 25
- 239000011707 mineral Substances 0.000 claims description 25
- 238000000034 method Methods 0.000 claims description 20
- 239000000839 emulsion Substances 0.000 claims description 19
- 239000011230 binding agent Substances 0.000 claims description 17
- 239000000203 mixture Substances 0.000 claims description 17
- 239000004568 cement Substances 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 239000002245 particle Substances 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 8
- 150000001844 chromium Chemical class 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 7
- 239000010426 asphalt Substances 0.000 claims description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 4
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000004571 lime Substances 0.000 claims description 4
- 229910021538 borax Inorganic materials 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 239000004328 sodium tetraborate Substances 0.000 claims description 3
- 235000010339 sodium tetraborate Nutrition 0.000 claims description 3
- CJDPJFRMHVXWPT-UHFFFAOYSA-N barium sulfide Chemical compound [S-2].[Ba+2] CJDPJFRMHVXWPT-UHFFFAOYSA-N 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 150000002736 metal compounds Chemical class 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- MGJURKDLIJVDEO-UHFFFAOYSA-N formaldehyde;hydrate Chemical compound O.O=C MGJURKDLIJVDEO-UHFFFAOYSA-N 0.000 claims 1
- 102000004169 proteins and genes Human genes 0.000 claims 1
- 108090000623 proteins and genes Proteins 0.000 claims 1
- 235000010755 mineral Nutrition 0.000 description 23
- 239000000463 material Substances 0.000 description 14
- 239000000126 substance Substances 0.000 description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical class O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 9
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 6
- 239000000654 additive Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 238000000576 coating method Methods 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 239000010419 fine particle Substances 0.000 description 4
- 239000010453 quartz Substances 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000011339 hard pitch Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 239000005569 Iron sulphate Substances 0.000 description 2
- 238000001994 activation Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 2
- 239000002480 mineral oil Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000011295 pitch Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000005905 Hydrolysed protein Substances 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 241000785684 Sander lucioperca Species 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011696 chromium(III) sulphate Substances 0.000 description 1
- 235000015217 chromium(III) sulphate Nutrition 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000029142 excretion Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000009997 thermal pre-treatment Methods 0.000 description 1
- 230000009974 thixotropic effect Effects 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
- C02F1/681—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water by addition of solid materials for removing an oily layer on water
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B20/00—Use of materials as fillers for mortars, concrete or artificial stone according to more than one of groups C04B14/00 - C04B18/00 and characterised by shape or grain distribution; Treatment of materials according to more than one of the groups C04B14/00 - C04B18/00 specially adapted to enhance their filling properties in mortars, concrete or artificial stone; Expanding or defibrillating materials
- C04B20/10—Coating or impregnating
- C04B20/1018—Coating or impregnating with organic materials
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B20/00—Use of materials as fillers for mortars, concrete or artificial stone according to more than one of groups C04B14/00 - C04B18/00 and characterised by shape or grain distribution; Treatment of materials according to more than one of the groups C04B14/00 - C04B18/00 specially adapted to enhance their filling properties in mortars, concrete or artificial stone; Expanding or defibrillating materials
- C04B20/10—Coating or impregnating
- C04B20/1055—Coating or impregnating with inorganic materials
- C04B20/107—Acids or salts thereof
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B26/00—Compositions of mortars, concrete or artificial stone, containing only organic binders, e.g. polymer or resin concrete
- C04B26/02—Macromolecular compounds
- C04B26/26—Bituminous materials, e.g. tar, pitch
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/01—Use of inorganic substances as compounding ingredients characterized by their specific function
- C08K3/013—Fillers, pigments or reinforcing additives
-
- 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
- C08L95/005—Aqueous compositions, e.g. emulsions
-
- 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
- E01C19/05—Crushing, pulverising or disintegrating apparatus; Aggregate screening, cleaning, drying or heating apparatus; Dust-collecting arrangements specially adapted therefor
-
- 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
- E01C19/1013—Plant characterised by the mode of operation or the construction of the mixing apparatus; Mixing apparatus
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Structural Engineering (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Civil Engineering (AREA)
- Medicinal Chemistry (AREA)
- Architecture (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Polymers & Plastics (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Road Paving Structures (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
Fremgangsmåte for omhylling av pulverformige til kornformige partikler med bituminøse bindemidler. Process for encasing powdery to granular particles with bituminous binders.
Foreliggende oppfinnelse angår en fremgangsmåte for omhylling av pulverformige til kornformige, fuktige, ikke opphetede faste partikler med bituminose bindemidler under anvendelse av metallforbindelser* The present invention relates to a method for coating powdery to granular, moist, unheated solid particles with bituminous binders using metal compounds*
Oppfinnelsen tilsikter forst og fremst å anvise en fremgangsmåte hvor man ved fremstillingen av bituminost blandegods, faeks. for veibygging, unngår den ellers vanlige stovutvik-ling, d.v.s. en bortgang av meget fine partikler under The invention is primarily intended to provide a method in which, in the production of bituminous mixed materials, e.g. for road construction, avoids the otherwise usual road development, i.e. a passing of very fine particles below
torkeprosessen. the drying process.
Ved kjente fremgangsmåter for fremstilling av bituminost blandegods, f.eks» for veibygging, sorteres fortrinnsvis det til et lite restvanninnhold av ca. 0, 5% torkede og for det meste opp til 160-200°C opphetede mineral, tilfores over en vekt til en blander og omhylles her med bituminost bindemiddel. En forutsetning for omhyllingen er, som omtalt, en termisk forbehandling av mineralet, ved hvilken forbehandling det skjer en utskilling av finpartiklene som medtas av torkegasstrommen. For å befri avgasstromraen fra dens stovinnhold og for igjen å kunne tilfore dette stov til blandegodset, i hvilket det utover en viktig funksjon, likesom for å forhindre utillatelig hoy stovemisjon, In known methods for producing bituminous mixed material, e.g. for road construction, it is preferably sorted to a low residual water content of approx. 0.5% dried and mostly up to 160-200°C heated mineral is fed over a weight into a mixer and coated here with bituminous binder. A prerequisite for the coating is, as discussed, a thermal pre-treatment of the mineral, during which pre-treatment a separation of the fine particles carried in by the drying gas flow takes place. In order to free the exhaust gas space from its dust content and to be able to add this dust to the mixture, in which it has an important function, as well as to prevent unacceptably high dust emissions,
kreves der ofte kompliserte tekniske hjelpemidler, slik som sykloner, våtvaskere, filter etc. i et sådant omfang at en okonomisk behandling av et sådant blandegods, spesielt i boligområder, industrielle tettbebyggelser, naturvern-områder etc, for hvilke er foreskrevet opprettholdelse av bestemte tillatte emisjonsverdier, ikke lenger er mulig* Ifolge oppfinnelsen unngår man under omhyllingen av partik-lene utskillelse av finpartikler, d.v.s. dannelse av stciv, ved at mineralske faste partikler, som i sin mineralstruktur inneholder vann og/eller på sin overflate fuktighet, forst i kald tilstand blandes med et flytende bituminost bindemiddel, fortrinnsvis under tilsetning av basiske kromsalter som vedheftningsforbedrer, og at i tilslutning dertil det oppnådde blandegods. i en torkeanordning, fortrinnsvis en tørketrommel, underkastes en varmebehandling ved en temperatur av over 80°C, fortrinnsvis 140°C. often complicated technical aids are required, such as cyclones, wet scrubbers, filters etc. to such an extent that an economical treatment of such mixed goods, especially in residential areas, industrial agglomerations, nature conservation areas etc., for which the maintenance of certain permitted emission values is prescribed , is no longer possible* According to the invention, during the encapsulation of the particles, excretion of fine particles is avoided, i.e. formation of stciv, in that mineral solid particles, which in their mineral structure contain water and/or moisture on their surface, are first mixed in a cold state with a liquid bituminous binder, preferably with the addition of basic chromium salts that improve adhesion, and that in addition to that the obtained mixed goods. in a drying device, preferably a dryer, is subjected to a heat treatment at a temperature of over 80°C, preferably 140°C.
Ved anvendelse av hoye temperaturer og/eller anvendelse av på passende måte avstemte bindemidler kan man i enkelt tilfelle avstå fra tilsetning av vedheftningsforbedrende til-set ningsmidler og allikevel oppnå omhyllinger som oppfyller det tilsiktede formål» When using high temperatures and/or using suitably coordinated binders, it is possible in some cases to refrain from adding adhesion-improving additives and still achieve coatings that fulfill the intended purpose."
Ved gjennomføring av denne fremgangsmåte, f.eks. for veibygging, ér det hensiktsmessig i praksis til de ennå ikke torkede mineralstoffer, som normalt har et fuktighetsinnhold av 3-5JC H •WO, i en blander, fortrinnsvis over finfordelings-organer, samtidig å tilfore bindemidlet og de nevnte tilsetninger, slik at det oppnås en tilstrekkelig statisk for-deling av disse stoffer på overflaten av mineralstoffene. Etter skjedd tilsetning og oppnåelse av den onskede bland-ingstilstand tilfores blandegodset - ved diskontinuerlig drift - over en utjevningsbeholder og en uttagningsanord- -ning kontinuerlig til en torke, fortrinnsvis en torketrommel, og oppvarmes i denne til en temperatur av over 80°C, fortrinnsvis 140°C. Allerede ved overskridelse av 80°C-terskelen inntrer aktiveringsprosessen, d.v.s. kromsaltopplosningen fortrenger det ved overflaten av mineralstoffene vedheftende og i porene innleirede vann og gjor de enkelte mineral-partikler varig vannavstotende. 1 motsetning til mange kjente vedheftningsmiddeltilsetninger blir virkningen av kromsaltene ikke nedsatt av de hoye temperaturer. When carrying out this procedure, e.g. for road construction, it is practical in practice to add the not yet dried mineral substances, which normally have a moisture content of 3-5JC H•WO, in a mixer, preferably over fine distribution devices, at the same time as the binder and the aforementioned additives, so that the a sufficient static distribution of these substances on the surface of the mineral substances is achieved. After the addition has taken place and the desired mixing state has been achieved, the mixture is fed - in discontinuous operation - via a leveling container and a removal device continuously to a drier, preferably a drier, and is heated in this to a temperature of over 80°C, preferably 140°C. Already when the 80°C threshold is exceeded, the activation process begins, i.e. the chromium salt solution displaces the water adhering to the surface of the mineral substances and embedded in the pores and makes the individual mineral particles permanently water-repellent. In contrast to many known adhesive additives, the effect of the chromium salts is not reduced by the high temperatures.
De på denne måte forbehandlede flater binder gjennom aktiv-ering av adhesjonskreftene bindemidlet og avstedkommer samtidig med den i trommelen foregående ekstra omrulling av godset en fullstendig omhylling av de enkelte mineralpartik-ler. The surfaces pre-treated in this way bind the binder through the activation of the adhesion forces and, at the same time as the previous extra rolling of the goods in the drum, result in a complete envelopment of the individual mineral particles.
Hvis blandingen etter avslutningen av varmetilforselen avkjoles til 60°C eller under denne temperatur, får man en lagringsbar og strobar, men ved utetemperatur ned fra 10°C fortettbar blanding. If, after the end of the heat supply, the mixture is cooled to 60°C or below this temperature, a storable and strobeable mixture is obtained, but at outside temperatures below 10°C it can be densified.
Det ifolge den beskrevne fremgangsmåte aktiverte materiale tillater overraskende nok en ekstra losning av interessante problemer, av hvilke det i denne sammenheng skal omtales spesielt ett. Det dreier seg om sammenforingen av disse aktiverte mineraler, fortrinnsvis sandarter med mineral-oljer, andre oljer eller oljeholdige stoffer, hvorved det oppstår en varig binding mellom mineralstoffene og oljene. The material activated according to the described method surprisingly allows an additional solution of interesting problems, of which one in particular will be mentioned in this context. It concerns the bringing together of these activated minerals, preferably pike perch, with mineral oils, other oils or oily substances, whereby a permanent bond is created between the mineral substances and the oils.
Ved bestroing med aktivert sand resp. påsproytning av aktivert sand kan eksempelvis på vann flytende mineralolje varig bringes til å synke (tankbåtulykker), slik som praktiske forsok har vist. When lining with activated sand or spraying activated sand can, for example, cause liquid mineral oil on water to sink permanently (tanker accidents), as practical trials have shown.
Skal bindingen av mineralstoffene skje gjennom en emulsjon, Should the binding of the mineral substances take place through an emulsion,
er det hensiktsmessig å foreta omhyllingen av de faste stoffer ved hjelp av en på basis av hydrolyserte proteinforbindelser overstabilisert, alkalisk bitumenemulsjon, is it appropriate to encase the solids using an alkaline bitumen emulsion overstabilised on the basis of hydrolysed protein compounds,
som er aktivert ved metallsalter, fortrinnsvis kromsalter, which is activated by metal salts, preferably chromium salts,
og til hvilken settes boraks og en vannopplosning av formaldehyd. and to which is added borax and a water solution of formaldehyde.
Ved anvendelse av en sådan emulsjon elimineres praktisk When using such an emulsion is practically eliminated
talt de ved temperaturer over 25°C, spesielt over 40°C opptredende vanskeligheter, uten at mengden av aktiveringsmiddel behover dkes. Tilsetningen av boraks til den basiske kromsaltopplosning gjor emulsjonen ufolsom overfor temperatur- -er innenfor det praktiske arbeidsområde. Likeså er den gunstige innflytelse av tilsetningen av en vannopplosning av formaldehyd fastslått ved praktiske forsSk. mentioned the difficulties occurring at temperatures above 25°C, especially above 40°C, without the amount of activator needing to be covered. The addition of borax to the basic chromium salt solution makes the emulsion insensitive to temperatures within the practical working range. Likewise, the beneficial influence of the addition of a water solution of formaldehyde has been established by practical research.
Det har enn videre vist seg at det ved fremstilling av Furthermore, it has been shown that in the production of
slike blandinger, eksempelvis også ved fremstilling av oppslemminger, er hensiktsmessig til emulsjonen i overens-stemmelse med plastisiteten hos bindemidlet å sette sement i en til den onskede stivhet hos blandingen nodvendig mengde. such mixtures, for example also when producing slurries, it is appropriate to add cement to the emulsion in accordance with the plasticity of the binder in an amount necessary for the desired stiffness of the mixture.
Med en sådan emulsjon er det f«eks. mulig å fremstille With such an emulsion, it is e.g. possible to produce
en i kald tilstand innbyggbar stopeasfalt, som oppviser hittil ikke kjente egenskaper, så som f.eks. overordentlig rask binding t.o.m. ved stor innbyggingstykkelse og en i praksis uvesentlig krymping ved torkings- resp. herdings-prosessen. a stopeasphalt that can be installed in a cold state, which exhibits hitherto unknown properties, such as e.g. extremely fast binding up to in the case of a large build-in thickness and a practically insignificant shrinkage during drying or the curing process.
Det er særlig hensiktsmessig at det til emulsjonen settes It is particularly appropriate that it is added to the emulsion
en blanding av hurtig-bindende sement og kalk i et forhold av hundre vektdeler hurtig-bindende sement til tretti til hundre deler kalk. Ved denne tilsetning kan veibeleggene belastes etter kort tid» Inntrengningsdybden står derved i et direkte forhold til mengden av biturnen i emulsjonen og til mengden av kalk-sementblanding» a mixture of quick-setting cement and lime in a ratio of one hundred parts by weight of quick-setting cement to thirty to one hundred parts of lime. With this addition, the road surfaces can be loaded after a short time" The depth of penetration is thus directly related to the amount of biturne in the emulsion and to the amount of lime-cement mixture"
En ytterligere positiv påvirkning av bindingstiden ved anvendelse av vanlig sement istedenfor hurtigbindende sement kan oppnås ved at det. til sementen settes jernsulfat (FeSO^7 HO) i et sådant forhold at jernsulfåtets aciditet lett overstiger alkaliteten hos sementen. A further positive influence on the setting time when using regular cement instead of quick-setting cement can be achieved by iron sulphate (FeSO^7 HO) is added to the cement in such a ratio that the acidity of the iron sulphate easily exceeds the alkalinity of the cement.
Dessuten kan bariumsulfid anvendes istedenfor kromsalt som aktiveringsmiddel og istedenfor sement som hydraulisk bindemiddel. I dette tilfelle skjer reaksjonen ifolge formelen BaS + 9 HjO ■ Ba(OH)27 H20 + H2S. Også dette er særlig fordelaktig ved fremstilling av oppslemninger og kaldt innbyggbar stopeasfalt. In addition, barium sulphide can be used instead of chromium salt as an activating agent and instead of cement as a hydraulic binder. In this case, the reaction takes place according to the formula BaS + 9 HjO ■ Ba(OH)27 H20 + H2S. This is also particularly advantageous in the production of slurries and cold-build asphalt.
Fremgangsmåten kan også anvendes for omhylling av andre stoffer enn mineralske, f.eks. knust hardbek av alle slags, hardbekgranulat, oppblåste polystyrener eller andre plaster, sagespon og liknende. Slike blandinger egner seg utmerket for anvendelse som isoleringsmateriale og tillater også fremstilling av formstykker, f.eks. sylindre eller halv-sylindre for rbrisolasjoner. The method can also be used for enveloping substances other than mineral, e.g. crushed hard pitch of all kinds, hard pitch granules, inflated polystyrene or other plastics, sawdust and the like. Such mixtures are excellently suited for use as insulating material and also allow the production of shaped pieces, e.g. cylinders or half-cylinders for insulations.
I denne sammenheng skal eksempelvis også omtales de med de knuste omhyllede hardbeker forbundne muligheter. In this context, for example, the possibilities associated with the crushed sheathed hard beaker should also be mentioned.
Omhyller man hardbek, dannes en strbbar, under trykk og/eller forhoyet temperatur aggiomerbar blanding, som,lagt om-kring hete rorflater, oppviser interessante virkninger, nemlig smeltning av massen nærmest inntil den hete kontakt-flate og sammensintring av en del av de lenger borte fra den hete flate liggende omhyllede bekkorn under opprettholdelse av en viss poreandel, hvorved det oppstår en utmerket isoleringsvirkning. Et liknende resultat oppnås også uten temperaturforhoyelse ved utovelse av trykk, f.eks. hvis man innleirer i grofter i marken for nedlegging bestemte ror i omhyllede bekmasser og i tilslutning dertil belaster med gjenfyllingsmaterialet. If hard pitch is encased, a hardenable, agglomerable mixture is formed under pressure and/or elevated temperature, which, placed around hot pipe surfaces, exhibits interesting effects, namely melting of the mass closest to the hot contact surface and sintering of part of the longer ones away from the hot flat lying enveloped pitch grains while maintaining a certain pore proportion, whereby an excellent insulating effect occurs. A similar result is also achieved without increasing the temperature by applying pressure, e.g. if one embeds in roughs in the ground for laying down certain rudders in shrouded pitch masses and in addition loads with the backfilling material.
Disse spesialemulsjoner tillater omhylling av alle pulverformige til kornformige materialer gjennom sine sterkt tixotrope egenskaper, som opptrer ved surgjoring av emul-sjonene. These special emulsions allow the coating of all powdery to granular materials through their strongly thixotropic properties, which occur when the emulsions are acidified.
Derved kan f.eks. mineralblandinger også uten sand og fyll-materiale omhylles, uten at det t.o.m. ved store emulsjons-doseringer behover fryktes en bortflyting av emulsjonen. Om-vendt omhylles til kornform overforte mineralfunn fra den minste til den groveste kornform inklusive pulver, så som jernoksyd, kalkstein eller kvarts, individuelt og fullstendig, uten at emulsjonen under denne omhyllingsprosess oppdeles i sine bestanddeler og uten at en utspeding av emulsjonen med vann er nodvendig. Det samme gjelder også selvsagt for organiske stoffer, eksempelvis for omhylling av trepulver. Det er videre fastslått at man kan blande alle klassiske asfaltblandinger kaldt istedenfor varmt ved samme mineral-og bindemiddelmengder gjennom anvendelse av de beskrevne Thereby, e.g. mineral mixtures also without sand and filler material are encased, without even if large emulsion dosages are needed, there is a fear that the emulsion will float away. On the other hand, mineral finds from the smallest to the coarsest grain form, including powder, such as iron oxide, limestone or quartz, are individually and completely enveloped in grain form, without the emulsion being divided into its components during this encasing process and without diluting the emulsion with water. necessary. The same of course also applies to organic substances, for example for encasing wood powder. It has also been established that all classic asphalt mixes can be mixed cold instead of hot with the same mineral and binder quantities through the use of the described
det^ed it^ed
emulsjoner, hvorved/den ettertorkxng, som kan skje bare ved solbestråling eller ved temperaturer opp til omtrent 160°C, dannes et bituminost blandegods, som med hensyn til sitt ytre ikke atskiller seg fra klassisk, varmblandet blandegods, men som oppviser hittil ikke kjente egenskaper; ved-hef tningsevnen, særskilt på sure steinarter, så som kvarts-eller kiselstein, forbedres så betraktelig at materialet utgjor et kaldt lagringsbart og osbart men også ved temperaturer fra 10 til 30°C innbyggbart blandegods. Dermed emulsions, whereby/the post-drying, which can only take place by sunlight or at temperatures up to approximately 160°C, a bituminous mixed material is formed, which in terms of its appearance does not differ from classical, hot-mixed mixed material, but which exhibits hitherto unknown properties ; the adhesion, especially on acidic rock types, such as quartz or silica, is improved so considerably that the material forms a cold storable and non-dissolving mixable material that can also be incorporated at temperatures from 10 to 30°C. Thus
elimineres to i praksis stadig oftere tilbakevendende mangler, nemlig for det forste den dårlige vedheftnings-evnen hos bindemidlet på forskjellige mineraler, spesielt kvartsholdige mineraler, og for det andre ubrukbarheten av varmt blandet men for innbyggingen avkjolt bituminost blandegods* Blandegodset ifolge den ovenfor beskrevne fremgangsmåte forblir, som nevnt, i form av frie korn men i en fortettingsbar tilstand. in practice, two increasingly frequent shortcomings are eliminated, namely, firstly, the poor adhesion of the binder to various minerals, especially quartz-containing minerals, and secondly, the unusability of hot-mixed but cooled-down bituminous mixture* The mixture according to the above-described method remains , as mentioned, in the form of free grains but in a densifiable state.
Det har videre vist seg at det med disse emulsjoner kaldt fremstilte blandegods ved åpen eller lukket byggemåte med eller uten tilsetning av sement, kalk eller slike fyllstoffer, torket i luften eller gjennom direkte eller indirekte opphetning, for så vidt gjennomløper en kritisk tilstand som mineralstof fene etter fordampning av 80-90JÉ It has also been shown that cold mixed materials produced with these emulsions by open or closed construction with or without the addition of cement, lime or such fillers, dried in the air or through direct or indirect heating, to the extent that they pass through a critical condition such as mineral substances after evaporation of 80-90JÉ
av vannet ved bevegelse progressivt avhylles. Denne fore-teelse forsvinner raskt igjen med stigende temperatur og fremskridende torkningsgrad ved samtidig ytterligere bevegelse av blandegodset. En torking med eller uten opphetning av et på basis av denne emulsjon fremstilt bituminost blandegods uten bevegelse av materialet tillater likeledes en fullstendig omhylling av de faste stoffer, så snart over 90% av vannet er fordampet, uten at det finner sted en gjennomloping av den nevnte kritiske avhyllingsfase. of the water when moving is progressively shed. This phenomenon quickly disappears again with rising temperature and advancing degree of drying by simultaneous further movement of the mixing material. A drying with or without heating of a bituminous mixture produced on the basis of this emulsion without movement of the material also allows a complete envelopment of the solids, as soon as more than 90% of the water has evaporated, without the aforementioned critical unwrapping phase.
Som allerede tidligere nevnt betyr fremgangsmåten ifolge oppfinnelsen praktisk talt en omveltning av den klassiske varmblandingsprosess, ved hvilken det i tørketrommelen torkede og opphetede mineral blandes i en blander med det bituminbse bindemiddel. Tvertom blandes ved den foreliggende fremgangsmåte i blånderen det fuktige mineral sammen med bindemidlet og de nevnte tilsetninger og gjennomløper forst i tilslutning hertil tørketrommelen. Da herved også de mineralet vedheftende resp. tilsatte fine partikler allerede er kommet i beroring med bindemidlet, medrives de ikke lenger i tørketrommelen av varmgasstrommen og bort-føres, slik at de hittil uunngåelige, kostbare avstovnings-anlegg blir overflodige. Dette betyr at allerede eksister-ende blandeanlegg som arbeider etter varmblandingsmetoden uten kostbare ombyggingsarbeider kan omstilles til fremgangsmåten ifolge oppfinnelsen. Det har vist seg fordelaktig derved ved anvendelse av ro tas jonst rommel torker å utstyre trommelen med slepekjeder, som for det forste befordrer mineralets bevegelse og for det andre beskytter trommelen fra forurensninger. As already mentioned earlier, the method according to the invention practically means an upheaval of the classic hot mixing process, whereby the mineral dried and heated in the dryer is mixed in a mixer with the bituminous binder. On the contrary, in the present method, the moist mineral is mixed in the mixer together with the binder and the aforementioned additives and first passes through the dryer in connection with this. Then herewith also the mineral adhering resp. added fine particles have already come into contact with the binder, they are no longer entrained in the dryer by the hot gas drum and carried away, so that the hitherto unavoidable, expensive dedusting facilities become redundant. This means that already existing mixing plants that work according to the hot mixing method can be converted to the method according to the invention without expensive rebuilding work. It has therefore proved advantageous when using ro tas jonst rommel dryers to equip the drum with drag chains, which firstly promote the movement of the mineral and secondly protect the drum from contamination.
Med hensyn til fremgangsmåtens okonomi, f.eks. ved stdvfri fremstilling av varmasfalt er å bemerke at det t.o.m. ved krav om stdrst mulig vedheftningsevne bare er nodvendig med en liten mengde tilsetninger. Således er f.eks. for et kvarts-holdig materiale 125 g basisk kromsulfat med kornstdrrelse fra 0 til 12 mm, opplost i 375 cm^ vann, tilstrekkelig pr. tonn blandegods. Denne tilsetning er tilstrekkelig for å oppnå en absolutt vannufolsomhet for blandegodset. With regard to the economy of the method, e.g. in the case of stdv-free production of hot asphalt, it is worth noting that even if the highest possible adhesion is required, only a small amount of additives is necessary. Thus, e.g. for a quartz-containing material 125 g of basic chromium sulphate with grain size from 0 to 12 mm, dissolved in 375 cm^ of water, sufficient per tons of mixed goods. This addition is sufficient to achieve absolute water tolerance for the mixed material.
Claims (4)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8758A FR1516830A (en) | 1966-12-02 | 1966-12-02 | Coating products and processes using plastic and hydraulic binders |
FR8884A FR92194E (en) | 1966-12-02 | 1967-05-02 | Coating products and processes using plastic and hydraulic binders |
Publications (1)
Publication Number | Publication Date |
---|---|
NO122874B true NO122874B (en) | 1971-08-23 |
Family
ID=26235467
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO170630A NO122874B (en) | 1966-12-02 | 1967-11-22 |
Country Status (12)
Country | Link |
---|---|
AT (1) | AT291843B (en) |
BE (1) | BE707335A (en) |
CH (1) | CH511053A (en) |
DE (1) | DE1594815C3 (en) |
DK (1) | DK141821B (en) |
FI (1) | FI52749C (en) |
FR (2) | FR1516830A (en) |
GB (1) | GB1209449A (en) |
NL (1) | NL6716147A (en) |
NO (1) | NO122874B (en) |
SE (1) | SE343314B (en) |
YU (1) | YU32283B (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1803113A1 (en) * | 1968-10-15 | 1971-01-21 | Wibau Gmbh | Process for the production of bituminous hot mix for building purposes |
FR2094932A5 (en) * | 1971-02-24 | 1972-02-04 | Muntzer Emile | |
FR2369331A1 (en) * | 1976-10-29 | 1978-05-26 | Muntzer Emile | Modified bitumen emulsions - treated with redox reagent, acid and demulsifier |
DE2963801D1 (en) * | 1978-04-08 | 1982-11-11 | Rheinische Kalksteinwerke | A filler suitable for use in road-surfacing bituminous compositions |
DE2840884C3 (en) * | 1978-09-20 | 1981-05-14 | Wibau Industrie und Verwaltung GmbH, 6466 Gründau | Process for the low-dust drying of bituminous mixes |
DE2848145C2 (en) * | 1978-11-07 | 1981-01-22 | Munderich, Paul, 6466 Gruendau | Process for processing bituminous mix in road construction or the like. and device for carrying out the method |
DE2903235C2 (en) * | 1979-01-29 | 1981-03-12 | Carl-Hermann 3220 Alfeld Heise | Device for processing bituminous mix |
DE2914286C2 (en) * | 1979-04-09 | 1982-03-25 | Wibau Industrie und Verwaltung GmbH, 6466 Gründau | Process for the preparation of bituminous mix in a drum mixer fired in cocurrent with a suction system connected in the end area of the drum mixer |
DE3010918C2 (en) * | 1980-03-21 | 1983-03-10 | Sallmann, Hans Christian | Rotary drum, especially for processing bituminous mixes |
DE3789379D1 (en) * | 1986-12-15 | 1994-04-21 | Emile Muntzer | Process for the preparation of a bituminous, ready-to-use cold mix based on a bitumen emulsion and a mixture of minerals. |
FR2608185B1 (en) * | 1986-12-15 | 1989-06-16 | Muntzer Emile | METHODS AND DEVICES FOR COLD BITUMINOUS COATINGS BY INTEGRATING A BITUMEN EMULSION FACTORY INTO THE CIRCUITS OF A COATING STATION |
FR2612214B2 (en) * | 1986-12-15 | 1990-02-23 | Muntzer Emile | PROCESSES FOR THE MANUFACTURE OF CATIONIC, STABLE AND ACTIVATED BITUMINOUS EMULSIONS IN ALKALINE MEDIA |
FR2729407A1 (en) * | 1994-12-29 | 1996-07-19 | Dubrac Freres | Method of production of asphalt and bituminous mastics |
FR2728804B1 (en) * | 1995-01-03 | 1997-03-21 | Muntzer Emile Jacques | PROCESS FOR THE PREPARATION OF AN EMULSION, RESULTING EMULSIONS AND COATINGS WITH THE EMULSIONS OBTAINED |
AU4490596A (en) * | 1995-01-03 | 1996-07-31 | Emile Jacques Muntzer | Method for coating carriers, emulsion used therein, resulting coated materials, and devices for producing and laying coated materials |
FR2742174B3 (en) * | 1995-12-12 | 1997-10-10 | Elf Aquitaine | PROCESS FOR THE PREPARATION OF BITUMINOUS COATINGS CONTAINING WASTE OF PLASTIC MATERIALS AND HAVING IMPROVED CHARACTERISTICS |
US20030044522A1 (en) * | 2001-05-08 | 2003-03-06 | Yukio Isozaki | Process and apparatus for producing mixture for asphalt pavement and method for paving roads by use thereof |
DE102005004906B4 (en) * | 2005-02-02 | 2008-03-27 | Carsten Hänel-Labryga | Mastic asphalt and process for its production |
CN112877031B (en) * | 2021-01-25 | 2023-09-01 | 义乌壹统胶科技有限公司 | Preparation process of internal sinking flip type plate powdery adhesive |
-
1966
- 1966-12-02 FR FR8758A patent/FR1516830A/en not_active Expired
-
1967
- 1967-05-02 FR FR8884A patent/FR92194E/en not_active Expired
- 1967-10-21 DE DE1594815A patent/DE1594815C3/en not_active Expired
- 1967-10-27 AT AT09743/67A patent/AT291843B/en not_active IP Right Cessation
- 1967-11-22 NO NO170630A patent/NO122874B/no unknown
- 1967-11-23 DK DK585967AA patent/DK141821B/en unknown
- 1967-11-27 SE SE16212/67A patent/SE343314B/en unknown
- 1967-11-28 NL NL6716147A patent/NL6716147A/xx unknown
- 1967-11-29 FI FI673203A patent/FI52749C/en active
- 1967-11-30 BE BE707335D patent/BE707335A/xx unknown
- 1967-11-30 GB GB54576/67A patent/GB1209449A/en not_active Expired
- 1967-11-30 CH CH1685867A patent/CH511053A/en not_active IP Right Cessation
- 1967-12-02 YU YU2363/67A patent/YU32283B/en unknown
Also Published As
Publication number | Publication date |
---|---|
FR92194E (en) | 1968-10-04 |
SE343314B (en) | 1972-03-06 |
DE1594815A1 (en) | 1970-08-20 |
YU236367A (en) | 1974-02-28 |
FR1516830A (en) | 1968-02-05 |
DK141821C (en) | 1980-11-24 |
DE1594815B2 (en) | 1973-05-17 |
DK141821B (en) | 1980-06-23 |
YU32283B (en) | 1974-08-31 |
FI52749B (en) | 1977-08-01 |
DE1594815C3 (en) | 1973-12-06 |
BE707335A (en) | 1968-04-01 |
NL6716147A (en) | 1968-06-04 |
CH511053A (en) | 1971-08-15 |
GB1209449A (en) | 1970-10-21 |
AT291843B (en) | 1971-06-15 |
FI52749C (en) | 1977-11-10 |
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