NO147218B - PROCEDURE FOR THE PREPARATION OF ROAD CONSTRUCTION OF CONCRETE BRONZE - Google Patents

PROCEDURE FOR THE PREPARATION OF ROAD CONSTRUCTION OF CONCRETE BRONZE Download PDF

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Publication number
NO147218B
NO147218B NO811715A NO811715A NO147218B NO 147218 B NO147218 B NO 147218B NO 811715 A NO811715 A NO 811715A NO 811715 A NO811715 A NO 811715A NO 147218 B NO147218 B NO 147218B
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Prior art keywords
fibers
acrylonitrile
acid
filaments
percent
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NO811715A
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Norwegian (no)
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NO147218C (en
NO811715L (en
Inventor
Ola Oeystein Thorsnes
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Selvaagebygg As
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Priority claimed from NO802490A external-priority patent/NO802490L/en
Priority to NO811715A priority Critical patent/NO147218C/en
Application filed by Selvaagebygg As filed Critical Selvaagebygg As
Priority to PCT/NO1981/000034 priority patent/WO1982000678A1/en
Priority to AU75303/81A priority patent/AU7530381A/en
Priority to IL63606A priority patent/IL63606A0/en
Priority to ES505356A priority patent/ES505356A0/en
Priority to GR65844A priority patent/GR75739B/el
Priority to IT8115196U priority patent/IT8115196V0/en
Priority to PT73552A priority patent/PT73552B/en
Priority to IT12610/81A priority patent/IT1145928B/en
Publication of NO811715L publication Critical patent/NO811715L/en
Publication of NO147218B publication Critical patent/NO147218B/en
Publication of NO147218C publication Critical patent/NO147218C/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28BSHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28B19/00Machines or methods for applying the material to surfaces to form a permanent layer thereon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28BSHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28B7/00Moulds; Cores; Mandrels
    • B28B7/34Moulds, cores, or mandrels of special material, e.g. destructible materials
    • B28B7/342Moulds, cores, or mandrels of special material, e.g. destructible materials which are at least partially destroyed, e.g. broken, molten, before demoulding; Moulding surfaces or spaces shaped by, or in, the ground, or sand or soil, whether bound or not; Cores consisting at least mainly of sand or soil, whether bound or not
    • EFIXED CONSTRUCTIONS
    • E01CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01CCONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C19/00Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving
    • E01C19/02Machines, 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
    • E01C19/025Machines, 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 for preparing hydraulic-cement-bound mixtures of which at least one ingredient has previously been deposited on the surface, e.g. in situ mixing of concrete
    • EFIXED CONSTRUCTIONS
    • E01CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01CCONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C19/00Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving
    • E01C19/50Removable forms or shutterings for road-building purposes; Devices or arrangements for forming individual paving elements, e.g. kerbs, in situ
    • E01C19/508Devices or arrangements for forming individual paving elements in situ, e.g. by sectioning a freshly-laid slab
    • EFIXED CONSTRUCTIONS
    • E01CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01CCONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C9/00Special pavings; Pavings for special parts of roads or airfields
    • E01C9/001Paving elements formed in situ; Permanent shutterings therefor ; Inlays or reinforcements which divide the cast material in a great number of individual units
    • EFIXED CONSTRUCTIONS
    • E02HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
    • E02DFOUNDATIONS; EXCAVATIONS; EMBANKMENTS; UNDERGROUND OR UNDERWATER STRUCTURES
    • E02D29/00Independent underground or underwater structures; Retaining walls
    • E02D29/02Retaining or protecting walls
    • E02D29/0258Retaining or protecting walls characterised by constructional features
    • E02D29/0266Retaining or protecting walls characterised by constructional features made up of preformed elements
    • EFIXED CONSTRUCTIONS
    • E04BUILDING
    • E04CSTRUCTURAL ELEMENTS; BUILDING MATERIALS
    • E04C1/00Building elements of block or other shape for the construction of parts of buildings
    • E04C1/40Building elements of block or other shape for the construction of parts of buildings built-up from parts of different materials, e.g. composed of layers of different materials or stones with filling material or with insulating inserts

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  • Engineering & Computer Science (AREA)
  • Architecture (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Ceramic Engineering (AREA)
  • Environmental & Geological Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Mining & Mineral Resources (AREA)
  • Paleontology (AREA)
  • General Engineering & Computer Science (AREA)
  • Road Paving Structures (AREA)
  • Revetment (AREA)

Description

Fremgangsmåte til å forbedre hvitheten og mottageligheten for basiske farvestoffer av termoplastiske fibre. Process for improving the whiteness and receptivity to basic dyes of thermoplastic fibers.

Foreliggende oppfinnelse angår en The present invention relates to a

fremgangsmåte til å forbedre (hvitheten av termoplastiske fibre og på samme tid øke sådanne fibres mottagelighet for basiske farvestoffer. Særlig angår oppfinnelsen en method for improving the whiteness of thermoplastic fibers and at the same time increasing the receptivity of such fibers to basic dyes. In particular, the invention relates to a

■fremgangsmåte til å forbedre hvitheten av acrylpolymerisatfibre under spinning og . ■method of improving the whiteness of acrylic polymer fibers during spinning and .

tørring av sådanne fibre .med samtidig for-bedring av mottageligheten for basiske farvestoffer av formede gjenstander som består av acrylnitril-polymerisater, sampolymerisater- terpolymerisater og .høyere interpolymerisater av acrylnitril og -blandinger av sådanne polymerisater. drying of such fibers with the simultaneous improvement of the receptivity to basic dyes of shaped articles consisting of acrylonitrile polymers, copolymers terpolymers and higher interpolymers of acrylonitrile and mixtures of such polymers.

Fibre som består av acrylnitrilpolymerisater og -interpolymerisater 'har mange meget gode egenskaper som gjør dem særlig fordelaktig i tekstilindustrien. Således har slike syntetiske fibre en meget god motstandsdyktighet mot -vaskning, slitasje og dannelse av uønskede folder, sammen med bløthet, et behagelig «grep» og en meget fordelaktig evne til å bibeholde sin form. Imidlertid har sådanne fibre en meget uønsket egenskap, nemlig at de ikke har den hvithetsgrad som er ønskelig ved deres anvendelse i tekstilindustrien. De fleste syntetiske acrylfibre får ved frem-stillingen av samme en svak gulaktig far-vetone eller farve som er meget uheldig. Der er foreslått tallrike metoder som tar sikte på å fjerne-denne misfarvning. ©et er således anvendt konvensjonelle tølekemidler for tekstilmaterialer, men anvendelsen av sådanne har vært helt mislykket idet sådanne konvensjonelle .blekemidler visstnok fjerner den opprinnelige 'inisfarvning av fibrene, imen oiten at disse .er stabile over-for ultrafiolette stråler i slik grad at ;de i alminnelighet tblir misfarvet i løpet av ca. 2 timers innvirkning av .sådanne stråler. Dessuten .virker temperaturer på ca. 150° C eller høyere i retning av å øke denne misfarvning .av fibrene. Fibers consisting of acrylonitrile polymers and interpolymers have many very good properties which make them particularly advantageous in the textile industry. Thus, such synthetic fibers have a very good resistance to -washing, wear and tear and the formation of unwanted folds, together with softness, a comfortable "grip" and a very advantageous ability to retain their shape. However, such fibers have a very undesirable property, namely that they do not have the degree of whiteness that is desirable for their use in the textile industry. Most synthetic acrylic fibers get a faint yellowish color tone or color when they are produced, which is very unfortunate. Numerous methods have been proposed which aim to remove this discolouration. Thus, conventional bleaching agents have been used for textile materials, but the use of such has been completely unsuccessful, as such conventional bleaching agents supposedly remove the original initial coloring of the fibers, while these are stable against ultraviolet rays to such an extent that they generally becomes discolored within approx. 2 hours of exposure to such rays. In addition, temperatures of approx. 150° C or higher in the direction of increasing this discoloration of the fibers.

Ved hjelp av foreliggende oppfinnelse skaffes der en fremgangsmåte til fremstilling av acrylfibre med godtagbar hvithet og som bibeholder denne forbedréde hvithet når de utsettes for innvirkning av ultrafiolette stråler og .av varme..Samtidig har, som foran nevnt, fibre som er behand-let i overensstemmelse .med.oppfinnelsen,\en forbedret mottagelighet for basiske farvestoffer. With the help of the present invention, a method is obtained for the production of acrylic fibers with acceptable whiteness and which maintains this improved whiteness when they are exposed to the influence of ultraviolet rays and heat. At the same time, as mentioned above, fibers which have been treated in accordance .with.the.invention,\an improved receptivity to basic dyes.

Det karakteristiske hovedtrekk ved oppfinnelsen er at man behandler termoplastiske fibre med en vandig oppløsning av •underfosforsyrling eller en blanding & v denne syre og vannoppløselige metallsalter av samme, i en /konsentrasjon på 0,01 til 1,0 pst. The characteristic main feature of the invention is that thermoplastic fibers are treated with an aqueous solution of hypophosphoric acid or a mixture of this acid and water-soluble metal salts thereof, in a concentration of 0.01 to 1.0 percent.

Fortrinnsvis anvendes .underfosforsyr-lingen eller blandingen av denne med nevnte metallsalter i enkonsentrasjon fra 0,1 .pst. til 0,5 pst. Preferably, the underphosphoric acid or its mixture with said metal salts is used in a concentration of 0.1%. to 0.5 percent

Som vannoppløselige salter av underfosforsyrling kan anvendes alkalimetallsal-,ter eller jordalkalimetallsalter. Behandlingsmidlet pH-verdi bør holdes på 7 eller lavere, fortrinnsvis under 4. Alkali metal salts or alkaline earth metal salts can be used as water-soluble salts of hypophosphoric acid. The pH value of the treatment agent should be kept at 7 or lower, preferably below 4.

Oppløsningen av behandlingsmidlet kan tilføres fibrene ved påsprøytning, i sluttbehandlingsbadet ved anvendelse av veker, ved anvendelse av valser eller på annen passende måte. The solution of the treatment agent can be supplied to the fibers by spraying, in the final treatment bath using wicks, using rollers or in another suitable way.

De polymere materialer som fremgangsmåten ifølge oppfinnelsen kan anvendes på, er materialer bestående av polyacrylnitril, sampolymerisater, deriblant bi-nære eller ternære polymerisater som inneholder minst 80 vektpst. acrylnitril i poly-merisatmolekylet, eller blandinger som inneholder polyacrylnitril eller sampolymerisater omfattende acrylnitril med fra 2 til 50 pst. andre polymere materialer, slik at blandingene har et innhold av polymeri-sert acrylnitril på minst 80 vektpst. De overtrukne polymerisater som anvendes ved fremgangsmåten ifølge oppfinnelsen er alt-så dem som inneholder minst 80 pst. acrylnitril og som i alminnelighet er anerkjent som fiberdannende acrylnitril-polymerisater, men fremgangsmåten ifølge oppfinnelsen kan også anvendes på polymerisater som inneholder mindre enn 80 pst. acrylnitril. Acrylnitrilpolymerisater som inneholder mindre enn 80 pst. acrylnitril er for-delaktige til fremstilling av film, over-trekksmidler, materialer for støpning og lakker. The polymeric materials to which the method according to the invention can be applied are materials consisting of polyacrylonitrile, copolymers, including binary or ternary polymers containing at least 80 wt. acrylonitrile in the polymer molecule, or mixtures containing polyacrylonitrile or copolymers comprising acrylonitrile with from 2 to 50% other polymeric materials, so that the mixtures have a polymerized acrylonitrile content of at least 80% by weight. The coated polymers used in the method according to the invention are those which contain at least 80% acrylonitrile and which are generally recognized as fiber-forming acrylonitrile polymers, but the method according to the invention can also be used on polymers which contain less than 80% acrylonitrile . Acrylonitrile polymers containing less than 80 percent acrylonitrile are advantageous for the production of film, coating agents, materials for casting and varnishes.

De polymere materialer kan f. eks. være et sampolymerisat av 80 til 98 pst. acrvlnitril oe fra 2 til 20 r>st. av en annen The polymeric materials can e.g. be a copolymer of 80 to 98 percent acrylonitrile and from 2 to 20 percent. by another

monomer som inneholder gruppen monomer containing the group

og som er sampolymeriserbar med acrylnitril. Blandt egnede monoolefinmonomere, er acrylsyre, a-kloracrylsyre og methacryl-syre, acrylater, som methylmethacrylat, ethylmethacrylat, butylmethacrylat, meth-oxymethyl-methacrylat, (3-klorethylmeth-acrylat og de tilsvarende estere av acrylsyre og a-kloracrylsyre, vinylklorid, vinylfluorid, vinylbromid, vinylidenklorid, 1-klor-l-brom-ethylen, methacrylnitril, acrylamid og methacrylamid, a-kloracrylsyreamid eller monoalkylsubstituerte derivater av disse, methylvinylketon, vinylcarboxylater, som vinylacetat, vinylkloracetat, vinylpro-pionat og vinylstearat, N-vinylimider, som N-vinylfthalsyreimid og N-vinylsuccinimid, methylenmalonsyreestere, itaconsyre og itaconsyreestere, N-vinylcarbazol, vinylfu-ran, alkylvinylestere, vinylsulfonsyre, ethy-len-a,p-dicarboxylsyrer eller anhydrider og andre derivater av disse, som diethylcitra-conat, diethylmesaconat, styren, vinylnaf-thalen, vinyl-substituerte tertiære hetero-cycliske aminer, som vinylpyridiner og alkyl-substituerte vinylpyridiner, f. eks. 2-vinylpyridin, 4-vinylpyridin, 2-methyl-5-vinylpyridin, 1-vinylimidazol og alkyl-substituerte 1-vinylimidazoler, som 2-, 4- eller 5-methyl-l-vinylimidazol, samt andre polymeriserbare materialer som inneholder gruppen and which is copolymerizable with acrylonitrile. Among suitable monoolefin monomers are acrylic acid, α-chloroacrylic acid and methacrylic acid, acrylates, such as methyl methacrylate, ethyl methacrylate, butyl methacrylate, methoxymethyl methacrylate, (3-chloroethyl methacrylate and the corresponding esters of acrylic acid and α-chloroacrylic acid, vinyl chloride, vinyl fluoride . N-vinylphthalic acid imide and N-vinylsuccinimide, methylenemalonic acid esters, itaconic acid and itaconic acid esters, N-vinylcarbazole, vinylfuran, alkyl vinylesters, vinylsulfonic acid, ethylene-α,β-dicarboxylic acids or anhydrides and other derivatives thereof, such as diethylcitraconate, diethylmesaconate, styrene, vinylnaphthalene, vinyl-substituted tertiary heterocyclic amines, such as vinylpyridines and alkyl-substituted vinylpyridines, e.g. ks. 2-vinylpyridine, 4-vinylpyridine, 2-methyl-5-vinylpyridine, 1-vinylimidazole and alkyl-substituted 1-vinylimidazoles, such as 2-, 4- or 5-methyl-1-vinylimidazole, as well as other polymerizable materials containing the group

De polymere materialer kan videre væ-re ternære eller høyere interpolymerisater, f. eks. produkter erholdt ved interpolyme-risering av acrylnitril og to eller flere andre monomere av de ovenfor nevnte. De ternære polymerisater kan fortrinnsvis være polymerisater av acrylnitril, methacryloni-tril og 2-vinylpyridin. Andre foretrukne ternære polymerisater inneholder 80 til 98 pst. acrylnitril, fra 1 fra 10 pst. av et vinylpyridin eller et 1-vinylimidazol og fra 1 til 18 pst. av et annet stoff som methacrylnitril eller vinylklorid. The polymeric materials can further be ternary or higher interpolymers, e.g. products obtained by interpolymerization of acrylonitrile and two or more other monomers of those mentioned above. The ternary polymers can preferably be polymers of acrylonitrile, methacrylonitrile and 2-vinylpyridine. Other preferred ternary polymers contain 80 to 98 percent of acrylonitrile, from 1 to 10 percent of a vinylpyridine or a 1-vinylimidazole and from 1 to 18 percent of another substance such as methacrylonitrile or vinyl chloride.

De polymere materialer kan også være blandinger av (1) et polyacrylnitril eller et binært interpolymerisat fra 80 til 99 pst. acrylnitril og fra 1 til 20 pst. av minst ett annet stoff som inneholder gruppen The polymeric materials can also be mixtures of (1) a polyacrylonitrile or a binary interpolymer from 80 to 99 percent acrylonitrile and from 1 to 20 percent of at least one other substance containing the group

med (2) fra 2 til 50 vektpst. av en blanding av et sampolymerisat av fra 10 til 70 pst. acrylnitril og fra 30 til 90 pst. av minst én annen polymeriserbar monomer som inneholder grupper with (2) from 2 to 50 wt. of a mixture of a copolymer of from 10 to 70 percent acrylonitrile and from 30 to 90 percent of at least one other polymerizable monomer containing groups

Når det polymere materiale er en blanding, er det fortrinnsvis en blanding av et sampolymerisat av 90 til 98 pst. acrylnitril og fra 2 til 10 pst. av en annen mono-ole-finmonomer, som vinylacetat, med en til-strekkelig mengde av et sampolymerisat av fra 10 til 70 pst. acrylnitril og fra 30 til 90 pst. av et vinyl-substituert tertiært heterocyklisk amin, som vinylpyridin eller 1-vinylimidazol, således at man får et farvbart materiale med et totalinnhold av vinyl-substituert tertiært heterocyklisk amin på fra 2 til 10 pst. beregnet på blandingens vekt. When the polymeric material is a blend, it is preferably a blend of a copolymer of 90 to 98 percent acrylonitrile and from 2 to 10 percent of another mono-olefin monomer, such as vinyl acetate, with a sufficient amount of a copolymer of from 10 to 70 percent acrylonitrile and from 30 to 90 percent of a vinyl-substituted tertiary heterocyclic amine, such as vinylpyridine or 1-vinylimidazole, so that a dyeable material is obtained with a total content of vinyl-substituted tertiary heterocyclic amine of from 2 to 10 percent calculated on the weight of the mixture.

I det følgende beskrives som eksempler noen utførelsesformer for oppfinnelsen. I disse er mengdeforhold angitt i vektpst. når ikke annet er nevnt. In the following, some embodiments of the invention are described as examples. In these, quantity ratios are stated in weight units. when not otherwise mentioned.

Eksempel 1. Example 1.

En spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat og et konvensjonelt oppløsningsmiddel ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. De erholdte filamenter ble strukket, vasket (med «20 wash roll wraps») og derpå ført gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad til hvilket der var tilsatt 40 ml 50 pst.'s underfosforsyrling. Fibrene ble derpå tørket og deres farve og hvithet bestemt. De viste 2,2 ren-hetsenheter og 85,1 lyshetsenheter («brigthness units») målt ved refleks i et General Electric Spektrofotometer. Fra disse verdier for renhet og lyshet ble hvitheten beregnet til 89,8. A spinning solution containing 93% acrylonitrile and 7% vinyl acetate and a conventional solvent was extruded into filaments in a conventional coagulation bath consisting of water and solvent. The filaments obtained were stretched, washed (with "20 wash roll wraps") and then passed through 2000 ml of a conventional finishing bath to which was added 40 ml of 50 per cent hypophosphoric acid. The fibers were then dried and their color and whiteness determined. They showed 2.2 purity units and 85.1 brightness units ("brightness units") measured by reflection in a General Electric Spectrophotometer. From these values for purity and lightness, the whiteness was calculated to be 89.8.

Eksempel 2. Example 2.

En spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. De erholdte filamenter ble strukket, vasket (med «8 vash roll wraps») og derpå ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad til hvilket der var tilsatt 40 ml 50 pst.'s underfosforsyrling. Fibrene ble derpå tørket. Ved bestemmelser som angitt i eksempel 1 ble deres renhet funnet å være 2,5, lyshet 84,7 og hvithet 87,5. A spinning solution containing 93% acrylonitrile and 7% vinyl acetate was extruded into filaments in a conventional coagulation bath consisting of water and solvent. The filaments obtained were stretched, washed (with "8 wash roll wraps") and then passed through 2000 ml of a conventional finishing bath to which was added 40 ml of 50% hypophosphoric acid. The fibers were then dried. As determined in Example 1, their purity was found to be 2.5, brightness 84.7 and whiteness 87.5.

Eksempel 3. Example 3.

En spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. Fibrene ble derpå strukket, vasket (med «20 vash roll wraps») og ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad som ikke inneholdt tilsetningsmidler ifølge oppfinnelsen. Fibrene ble derpå tørket. Ved bestemmelser som angitt i eksempel 1, ble deres renhet funnet å være 5.8, lyshet 81,6, hvorav lysheten ble beregnet til 45. A spinning solution containing 93% acrylonitrile and 7% vinyl acetate was extruded into filaments in a conventional coagulation bath consisting of water and solvent. The fibers were then stretched, washed (with "20 wash roll wraps") and passed through 2000 ml of a conventional finishing bath which did not contain additives according to the invention. The fibers were then dried. By determinations as indicated in Example 1, their purity was found to be 5.8, brightness 81.6, of which the brightness was calculated to be 45.

Eksempel 4. Example 4.

Man gikk frem nøyaktig som angitt i eksempel 3, med unntagelse av at der ble anvendt normal vaskning («6 vash roll wraps»). Ved bestemmelser som angitt i eksempel 1 ble fibrenes renhet funnet å være 5,5, lysheten 81,7, hvorav hvitheten ble beregnet til 47,5. The procedure was exactly as indicated in example 3, with the exception that normal washing was used ("6 wash roll wraps"). By determinations as indicated in example 1, the purity of the fibers was found to be 5.5, the lightness 81.7, of which the whiteness was calculated to be 47.5.

Eksempel 5. Example 5.

En spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad som besto av vann og opp-løsningsmiddel. De erholdte filamenter ble strukket, vasket (med «20 wash roll wraps») og ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad som var tilsatt 8 ml 50 pst.'s underfosforsyrling. Fibrene ble derpå tørket. Ved bestemmelse som angitt i eksempel 1, ble deres renhet funnet å være 3.2, deres lyshet 85,2 og hvithet 82,9. A spinning solution containing 93% acrylonitrile and 7% vinyl acetate was extruded into filaments in a conventional coagulation bath consisting of water and solvent. The filaments obtained were stretched, washed (with "20 wash roll wraps") and passed through 2000 ml of a conventional finishing bath to which was added 8 ml of 50% hypophosphoric acid. The fibers were then dried. By determination as indicated in Example 1, their purity was found to be 3.2, their brightness 85.2 and whiteness 82.9.

Eksempel 6. Example 6.

En spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. De erholdte filamenter ble strukket, vasket (med «6 wash roll wraps») og ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad som var tilsatt 8 ml 50 pst.'s underfosforsyrling. Fibrene ble derpå tørket. Ved bestemmelser som angitt i eksempel 1, ble fibrenes renhet funnet å være 3,2, deres lyshet 84,7 og hvithet 82,6. A spinning solution containing 93% acrylonitrile and 7% vinyl acetate was extruded into filaments in a conventional coagulation bath consisting of water and solvent. The filaments obtained were stretched, washed (with "6 wash roll wraps") and passed through 2000 ml of a conventional finishing bath to which was added 8 ml of 50% hypophosphoric acid. The fibers were then dried. By determinations as indicated in Example 1, the purity of the fibers was found to be 3.2, their brightness 84.7 and their whiteness 82.6.

Eksempel 7. Example 7.

En spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad. De erholdte filamenter ble strukket, vasket (med «20 wash roll wraps») og derpå ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad til hvilket der var tilsatt 40 ml 50 pst.'s underfosforsyrling. Fibrene ble derpå tørket. Ved bestemmelser som angitt i eksempel 1 ble deres renhet funnet å være 1,9, deres lyshet 84,1 og hvithet 90,6. A spinning solution containing 93% acrylonitrile and 7% vinyl acetate was extruded into filaments in a conventional coagulation bath. The filaments obtained were stretched, washed (with "20 wash roll wraps") and then passed through 2000 ml of a conventional finishing bath to which was added 40 ml of 50% hypophosphoric acid. The fibers were then dried. As determined in Example 1, their purity was found to be 1.9, their brightness 84.1 and their whiteness 90.6.

Eksempel 8. Example 8.

En;„ spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. De erholdte filamenter ble strukket, vasket (med «6 wash roll wraps») og derpå ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad som var tilsatt 40 ml 50 pst.'s underfosforsyrling samt 4 gram natriumhypofosfit. Fibrene ble derpå tørket. Ved bestemmelse som angitt i eksempel 1 ble deres renhet funnet å være 2.3, deres lyshet 86,0 og hvithet 89,8. A spinning solution containing 93% acrylonitrile and 7% vinyl acetate was extruded into filaments in a conventional coagulation bath consisting of water and solvent. The obtained filaments were stretched, washed (with "6 wash roll wraps") and then passed through 2000 ml of a conventional finishing bath to which was added 40 ml of 50% hypophosphoric acid and 4 grams of sodium hypophosphite. The fibers were then dried. By determination as indicated in Example 1, their purity was found to be 2.3, their brightness 86.0 and whiteness 89.8.

Eksempel 9. Example 9.

En spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. De erholdte filamenter ble strukket, vasket (med «20 wash roll wraps») A spinning solution containing 93% acrylonitrile and 7% vinyl acetate was extruded into filaments in a conventional coagulation bath consisting of water and solvent. The obtained filaments were stretched, washed (with "20 wash roll wraps")

og derpå ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad til hvilket der var tilsatt 8 ml 50 pst.'s underfosforsyrling samt 20 gram natriumhypofosfit. Fibrene ble derpå tørket. Ved bestemmelser som angitt i eksempel 1 ble deres renhet funnet å være 3,9, deres lyshet 85,3 og hvithet 77,0. and then passed through 2000 ml of a conventional final treatment bath to which 8 ml of 50% hypophosphoric acid and 20 grams of sodium hypophosphite had been added. The fibers were then dried. As determined in Example 1, their purity was found to be 3.9, their brightness 85.3 and their whiteness 77.0.

Eksempel 10. Example 10.

En spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. De erholdte filamenter ble strukket, vasket (med «6 wash roll wraps») A spinning solution containing 93% acrylonitrile and 7% vinyl acetate was extruded into filaments in a conventional coagulation bath consisting of water and solvent. The obtained filaments were stretched, washed (with "6 wash roll wraps")

og derpå ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad som var tilsatt 8 ml 50 pst.'s underfosforsyrling samt. 20 gram natriumhypofosfit. Ved bestem-, meiser som angitt i eksempel 1 ble filamen-tenes renhet funnet å være 3,9, deres lys-i het 85,5 og deres hvithet 76,5. j Eksempel 11. and then led through 2000 ml of a conventional final treatment bath to which 8 ml of 50 per cent hypophosphoric acid had been added as well as. 20 grams of sodium hypophosphite. By determination as indicated in Example 1, the purity of the filaments was found to be 3.9, their brightness 85.5 and their whiteness 76.5. j Example 11.

En spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. Fibrene ble derpå strukket, vasket (med «20 wash roll wraps») og der- A spinning solution containing 93% acrylonitrile and 7% vinyl acetate was extruded into filaments in a conventional coagulation bath consisting of water and solvent. The fibers were then stretched, washed (with "20 wash roll wraps") and then

på ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad som var tilsatt 8 on led through 2000 ml of a conventional finishing bath which had been added 8

ml 50 pst.'s underfosforsyrling samt 4 gram natriumhypofosfit. Fibrene ble derpå tør-ket. Ved bestemmelser som angitt i eksem- ml of 50% hypophosphorous acid and 4 grams of sodium hypophosphite. The fibers were then dried. In the case of provisions as stated in exem-

pel 1 ble deres renhet funnet å være 3,5, deres lyshet 85,6 og deres hvithet 80,5. pel 1 their purity was found to be 3.5, their brightness 85.6 and their whiteness 80.5.

Eksempel 12. Example 12.

En spinneoppløsning inneholdende 93 pst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. De erholdte filamenter ble strukket, vasket (med «6 wash roll wraps») A spinning solution containing 93% acrylonitrile and 7% vinyl acetate was extruded into filaments in a conventional coagulation bath consisting of water and solvent. The obtained filaments were stretched, washed (with "6 wash roll wraps")

og derpå ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad som var tilsatt 8 ml 50 pst.'s underfosforsyrling samt 4 gram natriumhypofosfit. Filamentene ble derpå tørket. Ved bestemmelser som angitt i eksempel 1 ble deres renhet funnet å være 3,9, deres lyshet 36,0 og deres hvithet 76,8. and then passed through 2000 ml of a conventional finishing bath to which 8 ml of 50% hypophosphoric acid and 4 grams of sodium hypophosphite had been added. The filaments were then dried. As determined in Example 1, their purity was found to be 3.9, their lightness 36.0 and their whiteness 76.8.

Eksempel 13. Example 13.

En spinneoppløsning inneholdende 93 ost. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i 'et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. De erholdte filamenter ble strukket, vasket (med «20 wash roll wraps») A spinning solution containing 93 cheese. acrylonitrile and 7% vinyl acetate were extruded into filaments in a conventional coagulation bath consisting of water and solvent. The obtained filaments were stretched, washed (with "20 wash roll wraps")

og derpå ledet gjennom 2000 ml av et kon-vensionelt sluttbehandlingsbad som ikke inneholdt tilsetningsmidler ifølge oppfinnelsen. De erholdte filamenter ble tørket og farvet med «Sevron Blue 2G, C. I. Basic Blue 22» på konvensjonell måte. Der ble herved tilsatt en kjent mengde f arvestoff til farveoppløsningen og den mengde farvestoff som var tilbake efter farvningen, and then passed through 2000 ml of a conventional finishing bath which did not contain additives according to the invention. The obtained filaments were dried and dyed with "Sevron Blue 2G, C.I. Basic Blue 22" in a conventional manner. A known amount of dye was added to the dye solution and the amount of dye that remained after dyeing,

ble bestemt. Det ble funnet at opptagelsen av det basiske farvestoff var 3,7 pst. was determined. It was found that the uptake of the basic dye was 3.7 per cent.

Eksempel 14. Example 14.

En spinneoppløsning inneholdende 93 Dst. acrylnitril og 7 pst. vinylacetat ble eks-trudert til filamenter i et konvensjonelt koaguleringsbad bestående av vann og opp-løsningsmiddel. De erholdte filamenter ble strukket, vasket (med «20 wash roll wraps») A spinning solution containing 93 Dst. acrylonitrile and 7% vinyl acetate were extruded into filaments in a conventional coagulation bath consisting of water and solvent. The obtained filaments were stretched, washed (with "20 wash roll wraps")

og derpå ledet gjennom 2000 ml av et konvensjonelt sluttbehandlingsbad som var til-latt 4 ml 50 pst.'s underfosforsyrling og 20 gram natriumhypofosfit. Filamentene ble derpå tørket og farvet med «Sevron Blue 2G. C. I. Basic Blue 22». Ved bestemmelse nå samme måte som i eksempel 13 ble det funnet at opptagelsen av dette basiske farvestoff var 6,0 pst. and then passed through 2000 ml of a conventional finishing bath which was allowed 4 ml of 50% hypophosphoric acid and 20 grams of sodium hypophosphite. The filaments were then dried and stained with "Sevron Blue 2G. C. I. Basic Blue 22". When determined in the same way as in example 13, it was found that the uptake of this basic dye was 6.0 percent.

Det er således med tilsetningsmidlene ifølge oppfinnelsen ikke bare mulig å oppnå hvitere fibre og filamenter enn hva der tid-ligere var mulig, men dessuten oppnåes der en nesten 100 pst.'s økning i opptagelsen av basiske farvestoffer. Fibrene får også på annen måte en forbedret farvbarhet, idet den forbedrede hvithet også gir bedre farve ved påfølgende farvning av fibrene. Thus, with the additives according to the invention, it is not only possible to obtain whiter fibers and filaments than was previously possible, but also an almost 100 percent increase in the absorption of basic dyes is achieved. The fibers also get an improved dyeability in another way, as the improved whiteness also gives better color when the fibers are subsequently dyed.

Claims (6)

1. Fremgangsmåte til å forbedre hvitheten av termoplastiske fibre, særlig acrylfibre. og på samme tid øke fibrenes mottagelighet for basiske farvestoffer, karakterisert ved at man behandler fibrene med underfosforsyrling eller blandinger av underfosforsyrling med vannoppløselige metallsalter av denne syre, i konsentrasjo-ner fra 0,01 pst. til 1 pst.1. Process for improving the whiteness of thermoplastic fibers, especially acrylic fibers. and at the same time increase the receptivity of the fibers to basic dyes, characterized by treating the fibers with hypophosphoric acid or mixtures of hypophosphoric acid with water-soluble metal salts of this acid, in concentrations from 0.01 percent to 1 percent. 2. Anvendelse av fremgangsmåte ifølge påstand 1 på fibre som inneholder minst 80 pst. acrylnitril og opp til 20 pst. av en annen monoolefinmonomer som er sampolymeriserbar med acrylnitril.2. Application of the method according to claim 1 on fibers containing at least 80% of acrylonitrile and up to 20% of another monoolefin monomer which is copolymerizable with acrylonitrile. 3. Anvendelse som angitt i påstand 2, karakterisert ved at fibrene består av 93 pst. acrylnitril og 7 pst. vinylacetat.3. Use as stated in claim 2, characterized in that the fibers consist of 93% acrylonitrile and 7% vinyl acetate. 4. Anvendelse som angitt i påstand 3, karakterisert ved at behandlings-oppløsningens pH-verdi er under 7.4. Use as stated in claim 3, characterized in that the treatment solution's pH value is below 7. 5. Anvendelse som angitt i påstand 4, karakterisert ved at behandlings midlet er en blanding av underfosforsyrling og kalium- eller natriumhypofosfit.5. Application as stated in claim 4, characterized by that treatment the agent is a mixture of hypophosphoric acid and potassium or sodium hypophosphite. 6. Anvendelse som angitt i påstand 4, karakterisert ved at behandlingsmidlet er en blanding av underfosforsyrling og kalsiumhypofosfit.6. Use as stated in claim 4, characterized in that the treatment agent is a mixture of hypophosphorous acid and calcium hypophosphite.
NO811715A 1980-08-21 1981-05-20 PROCEDURE FOR THE PREPARATION OF ROAD CONSTRUCTION OF CONCRETE BRONZE NO147218C (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
NO811715A NO147218C (en) 1980-08-21 1981-05-20 PROCEDURE FOR THE PREPARATION OF ROAD CONSTRUCTION OF CONCRETE BRONZE
PCT/NO1981/000034 WO1982000678A1 (en) 1980-08-21 1981-08-17 A method for making a construction from stones of concrete
AU75303/81A AU7530381A (en) 1980-08-21 1981-08-17 A method for making a construction from stones or concrete
IL63606A IL63606A0 (en) 1980-08-21 1981-08-19 Method for erecting a building construction from concrete blocks
ES505356A ES505356A0 (en) 1980-08-21 1981-08-20 METHOD FOR THE CONSTRUCTION OF A CONSTRUCTION FROM CONCRETE STONES
GR65844A GR75739B (en) 1980-08-21 1981-08-21
IT12610/81A IT1145928B (en) 1980-08-21 1981-08-21 METHOD FOR THE CONSTRUCTION OF BUILDINGS FORMING BLOCKS OR CONCRETE STONES
IT8115196U IT8115196V0 (en) 1980-08-21 1981-08-21 METHOD FOR THE CONSTRUCTION OF BUILDINGS FORMING BLOCKS OR CONCRETE STONES
PT73552A PT73552B (en) 1980-08-21 1981-08-21 A method for making a construction from stones of concrete

Applications Claiming Priority (2)

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NO802490A NO802490L (en) 1980-08-21 1980-08-21 PROCEDURE FOR THE PREPARATION OF SURFACE TIRE (SURFACE TIRE)
NO811715A NO147218C (en) 1980-08-21 1981-05-20 PROCEDURE FOR THE PREPARATION OF ROAD CONSTRUCTION OF CONCRETE BRONZE

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NO147218B true NO147218B (en) 1982-11-15
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ES (1) ES505356A0 (en)
GR (1) GR75739B (en)
IL (1) IL63606A0 (en)
IT (2) IT8115196V0 (en)
NO (1) NO147218C (en)
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US1777926A (en) * 1929-01-29 1930-10-07 Sackoncrete Company Masonry construction
US2095989A (en) * 1934-03-09 1937-10-19 William W Lillard Building unit
US3922832A (en) * 1967-09-18 1975-12-02 Edward T Dicker Construction method of assembling bagged, settable modules
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IL63606A0 (en) 1981-11-30
WO1982000678A1 (en) 1982-03-04
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PT73552A (en) 1981-09-01
NO147218C (en) 1983-02-23
NO811715L (en) 1982-02-22
PT73552B (en) 1983-09-27
AU7530381A (en) 1982-03-17
ES8304249A1 (en) 1982-06-16
IT8115196V0 (en) 1981-08-21
IT8112610A0 (en) 1981-08-21
GR75739B (en) 1984-08-02
ES505356A0 (en) 1982-06-16

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