DK172079B1 - Corrosion inhibitor systems and deicer compsns. - comprising sodium fluorophosphate and/or phosphonic acid deriv. salt - Google Patents

Corrosion inhibitor systems and deicer compsns. - comprising sodium fluorophosphate and/or phosphonic acid deriv. salt Download PDF

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DK172079B1
DK172079B1 DK106789A DK106789A DK172079B1 DK 172079 B1 DK172079 B1 DK 172079B1 DK 106789 A DK106789 A DK 106789A DK 106789 A DK106789 A DK 106789A DK 172079 B1 DK172079 B1 DK 172079B1
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process according
corrosion
sodium
concrete
sodium monofluorophosphate
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Allan Johnston
Dean A Mason
Darre F Lawless
Terence E Peel
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Domtar Inc
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Abstract

Corrosion inhibitor system compr1ses at least one of:-(A) Na fluorophosphate and (B) water-soluble salt of a phosphonic acid deriv. of formula:- RnR'N(CH2PO3H2)2-n where R and R' = alkyl, aminoalkyl or hydroxyalkyl; and n = 0 or 1. Deicer compsn. comprising the above corrosion inhibiting system is also claimed.

Description

DK 172079 B1DK 172079 B1

Den foreliggende opfindelse angår en fremgangsmåde til inhibering af korrosion af armeringsjern i jernbeton, især forårsaget af chloridioner og lignende, f.eks. korrosion forårsaget af korrosive afisningsmidler, syreregn og lig-5 nende. Opfindelsen angår også inhibering af en sådan korrosion, når der også anvendes et afisningsmiddel.The present invention relates to a method for inhibiting corrosion of reinforced iron in ferrous concrete, in particular caused by chloride ions and the like, e.g. corrosion caused by corrosive deicing agents, acid rain and the like. The invention also relates to the inhibition of such corrosion when a deicing agent is also used.

Udtrykket "korrosion forårsaget af chloridioner og lignende", der anvendes i beskrivelsen, betyder korrosion forårsaget af f.eks. NaCl, CaCl2, andre korrosive afisnings-10 midler eller vilkårlige andre produkter, der forårsager eller er tilbøjelige til at forårsage lignende korrosion.. Det betyder også, at systemer indeholdende natriumfluorphosphat ikke må anvendes til inhibering af stærkt sur korrosion, såsom batterikorrosion, da HF kan dannes og naturligvis er 15 korrosivt.The term "corrosion caused by chloride ions and the like" used in the specification means corrosion caused by e.g. NaCl, CaCl2, other corrosive de-icing agents, or any other products that cause or tend to cause similar corrosion. It also means that systems containing sodium fluorophosphate should not be used to inhibit highly acidic corrosion, such as battery corrosion, since HF can be formed and of course is corrosive.

Den foreliggende opfindelse vedrører også anvendelsen af et stort antal bærestoffer, såsom f.eks. gasformige, væskeformige og faste bærestoffer eller fortyndingsmidler, herunder f.eks., men ikke begrænset dertil, afisningsmidler, 20 sand, opløsningsmidler, fortyndingsmidler, overtræk, malinger, emulsioner, suspensioner, luftstråleanvendelser og lignende, til det korrosioninhiberende system.The present invention also relates to the use of a large number of carriers, such as e.g. gaseous, liquid and solid carriers or diluents, including, for example, but not limited to, deicing agents, sand, solvents, diluents, coatings, paints, emulsions, suspensions, air jet applications and the like, for the corrosion inhibiting system.

Det korrosioninhiberende system er et sådant, der indeholder i det mindste natriumfluorphosphat (Na2P03F, 25 der også er kendt under navnet natriummonofluorphosphat).The corrosion inhibiting system is one which contains at least sodium fluorophosphate (Na2 PO3F, also known by the name sodium monofluorophosphate).

Opfindelsen vedrører endvidere en fremgangsmåde til fremstilling af de korrosionsinhiberende systemer, fremgangsmåder til anvendelse heraf og de produkter, der hidrører derfra, og som i det mindste indeholder resterende mængder 30 af de korrosionsinhiberende systemer.The invention further relates to a process for the preparation of the corrosion inhibiting systems, methods of using them and the products derived therefrom, which contain at least the remaining amounts of 30 of the corrosion inhibiting systems.

Opfindelsen vedrører især korrosionsinhiberende systemer for armeret beton eller jernbeton.The invention relates in particular to corrosion inhibiting systems for reinforced concrete or iron concrete.

Natriumchlorid anvendes udbredt som et afisningsmiddel. Der er blevet foreslået mange måder til at overvinde 35 de korrosionsproblemer, der er forbundet med anvendelsen heraf. F.eks. er korrosionen af armeringsjern i beton blevet 2 DK 172079 B1 formindsket ved en forudgående overtrækning af armeringsjernet med epoxy før tilsætningen af beton, eller ved katodisk beskyttelse.Sodium chloride is widely used as a de-icing agent. Many ways have been proposed to overcome the corrosion problems associated with its use. Eg. For example, the corrosion of reinforcing iron in concrete has been reduced by a prior coating of the reinforcing iron with epoxy before the addition of concrete, or by cathodic protection.

De omgivelser, der normalt gives armeringsstål ved, 5 at det omgives af beton, er næsten ideelt egnede til forebyggelse af korrosion af stålet. Beton af høj kvalitet, der er anbragt korrekt, komprimeret og hærdet, tilvejebringer en meget alkalisk overtrækning af stålet med lav permeabilitet, hvilken overtrækning beskytter (passiverer) mod korrosion 10 og minimerer gennemtrængning af korrosions-inducerende faktorer, nemlig oxygen, vand og chlorid. Imidlertid kan ind-trægning af fugt, elektrolytter og oxygen ved diffusion eller gennem hårfine revner i betonen ødelægge det passive miljø og etablere galvaniske korrosionsceller og til sidst 15 ødelægge betonen på grund af de ekspansive kræfter, der tilvejebringes af det korroderende stål. Chloridsalte synes at være de kraftigst virkende ved tilvejebringelsen af denne type angreb. Betonstrukturer med lavere kvalitet beton eller med utilstrækkelig dækning af armeringsjernene og de, der 20 udsættes for hårde betingelser, såsom brodæk, der udsættes for afisningssalte, eller marine miljøer, er særligt modtagelige for hurtig forringelse. Størrelsen af dette problem og de økonomiske omkostninger ved reparation og genopbygning af landevejsstrukturer har ført til ekstensiv forskning i 25 løbet af de sidste 15 år med hensyn til elektrokemisk opførsel af stål i beton og mulige løsninger. Tidligere og nuværende forskningsbestræbelser har været fokuseret på vigtigheden af faktorer såsom tykkelsen af overdækningen, vand/-cement-forholdet, overtrukne armeringsjern, inhibitorblan-30 dinger til cement, beton med lav permeabilitet osv. i nykonstruktion, og overvågnings- og reparationsteknikker for eksisterende strukturer, f.eks. katodisk beskyttelse og membranbelægninger.The environment normally reinforced by reinforcing steel by being surrounded by concrete is almost ideally suited to preventing corrosion of the steel. High quality, properly applied, compacted and hardened concrete provides a very alkaline coating of the low permeability steel which protects (passivates) against corrosion 10 and minimizes penetration of corrosion-inducing factors, namely oxygen, water and chloride. However, ingress of moisture, electrolytes and oxygen by diffusion or through fine-grained cracks in the concrete can destroy the passive environment and establish galvanic corrosion cells and eventually destroy the concrete due to the expansive forces provided by the corrosive steel. Chloride salts appear to be the most powerful in providing this type of attack. Concrete structures with lower quality concrete or with insufficient coverage of the reinforcing bars and those exposed to harsh conditions, such as bridge decks exposed to deicing salts, or marine environments, are particularly susceptible to rapid deterioration. The magnitude of this problem and the economic cost of repairing and rebuilding road structures have led to extensive research over the past 15 years regarding the electrochemical behavior of steel in concrete and possible solutions. Past and current research efforts have focused on the importance of factors such as the thickness of the cover, water / cement ratio, coated reinforcement bars, cement inhibitor mixtures, low permeability concrete, etc. in new construction, and monitoring and repair techniques for existing structures. , for example. cathodic protection and membrane coatings.

Den lave korrosionshastighed for stål i ikke-kon-35 tamineret beton skyldes dannelsen i nærværelse af tilstrækkeligt oxygen af et stabilt, passivt lag af gamma-Fe203 på 3 DK 172079 B1 ståloverfladen i miljøet med høj pH-værdi (12-13) . Der er to almene mekanismer, ved hjælp af hvilke denne passiverende virkning kan ødelægges: (1) formindskelse af alkaliniteten ved udvaskning af basiske stoffer og/eller partiel reak-5 tion med C02, og (2) fysisk og elektrokemisk indvirkning, der involverer chlorid eller andre aggressive anioner. Når stålets passivitet først er ødelagt, forøges korrosionshastigheden drastisk med dannelsen af mikro- og makrokorrosionsceller. Oxidation af jern til ferroioner og dannelse af oxider 10 sker ved anoden (ligning 1) , medens reduktion af oxygen sker ved katoden (ligning 2).The low corrosion rate of steel in uncontaminated concrete is due to the formation in the presence of sufficient oxygen of a stable, passive layer of gamma-Fe2 O3 on the steel surface in the high pH environment (12-13). There are two general mechanisms by which this passivating effect can be destroyed: (1) decrease of alkalinity by leaching of basic substances and / or partial reaction with CO 2, and (2) physical and electrochemical action involving chloride. or other aggressive anions. Once the steel's passivity is destroyed, the rate of corrosion increases dramatically with the formation of micro and macro corrosion cells. Oxidation of iron to ferrous ions and formation of oxides 10 occurs at the anode (Equation 1), while reduction of oxygen occurs at the cathode (Equation 2).

(1) Fe -* Fe2+ + 2e + 02 -» Fe304 (2) 1/2 02 + H20 + 2e -* 20H"(1) Fe - * Fe2 + + 2nd + 02 - »Fe304 (2) 1/2 02 + H2O + 2nd - * 20H"

Det korroderende ståls anode- og katodeområder kan 15 være vidt adskilte. De afhænger af forskelle i chlorid eller anden anion og oxygenkoncentrationerne og påvirkes af pH-værdien nær stål/beton-grænsefladen.The anode and cathode regions of the corrosive steel can be widely spaced. They depend on differences in chloride or other anion and oxygen concentrations and are influenced by the pH near the steel / concrete interface.

I Chemical Abstracts, vol. 102, abstract nr. 189922r er det angivet, at der kan fremstilles et gipsmateriale, 20 der indeholder 0,1-5 vægt-% natriummonofluorphosphat og ikke koroderer metal. Gips indeholdende 0,1 vægt-% natrium-· monofluorphosphat bevirker således, at der opnås en stålkorrosionshastighed på 0,080 mm pr. år.In Chemical Abstracts, Vol. 102, Abstract No. 189922r, it is stated that a gypsum material 20 can be prepared containing 0.1-5% by weight of sodium monofluorophosphate and does not corrode metal. Gypsum containing 0.1% by weight of sodium monofluorophosphate causes a steel corrosion rate of 0.080 mm per year.

I EP-A-0 096 619 er der beskrevet beskyttelse af 25 metaloverflader i vandigt medium under anvendelse af generelt sparsomt vandopløselige ΐluorphosphater. En korrosionsinhi-berende virkning af natriumfluorphosphat på metaloverflader er beskrevet.EP-A-0 096 619 describes the protection of 25 metal surfaces in aqueous medium using generally sparingly water-soluble orluorophosphates. A corrosion inhibiting effect of sodium fluorophosphate on metal surfaces is described.

I EP-A-0 288 812 er der beskrevet erstatning af na-30 triumsulfat i detergenter med f luorphosphat er til eliminering eller formindskelse af den film, der dannes på glas med opvaskedetergenter,idet filmen betegnes som "korrosion".EP-A-0 288 812 discloses replacing sodium sulfate in fluorophosphate detergents for eliminating or reducing the film formed on glass with dishwashing detergents, the film being termed "corrosion".

I DE patentskrift nr. 1.771.508 beskrives en række phosphonsyrederivaters korrosionsinhiberende virkning på 35 metaloverflader.DE Patent No. 1,771,508 describes the corrosion inhibiting effect of a number of phosphonic acid derivatives on 35 metal surfaces.

Det har nu ifølge opfindelsen overraskende vist sig, 4 DK 172079 B1 at korrosion af armeringsjern i jernbeton kan inhiberes ved, at der på overfladen af jernbetonen anbringes et korrosions-inhiberende system, der indeholder i det mindste natrium-monofluorphosphat, og hvor dette stof i kontakt med vand 5 inhiberer korrosion af armeringsjernet; der er intet i den ovenfor omtalte, kendte teknik, der antyder, at der kan opnås en særdeles effektiv korrosionsbeskyttelse af armeringsjern i jernbeton ved simpel påføring af det nævnte system på jernbetonens overflade.It has now been found, according to the invention, surprisingly, that corrosion of reinforced iron in reinforced concrete can be inhibited by the application of a corrosion-inhibiting system containing at least sodium monofluorophosphate, and wherein this substance in contact with water 5 inhibits corrosion of the reinforcing iron; there is nothing in the prior art mentioned above that suggests that a highly effective corrosion protection of reinforced iron in iron concrete can be achieved by simply applying said system to the surface of the iron concrete.

10 Fremgangsmåden ifølge opfindelsen, der er af den i det foregående nævnte art, er således ejendommelighed, at der på overfladen af jernbetonen anbringes et korrosionsinhibitorsystem, som i det mindste indeholder natriummonofluorphosphat, og i hvilket natriummonofluorphosphatet i kontakt 15 med vand inhiberer korrosionen af armeringsjernene.The process according to the invention, which is of the aforementioned kind, is characterized in that a corrosion inhibitor system is provided which contains at least sodium monofluorophosphate and in which the sodium monofluorophosphate in contact with water inhibits the corrosion of the reinforcing iron.

Særligt hensigtsmæssige udførelsesformer for fremgangsmåden ifølge opfindelsen er angivet i krav 2-19.Particularly convenient embodiments of the method of the invention are set forth in claims 2-19.

I almindelighed er mindst ét afisningsmiddel også til stede i systemet. Sædvanligvis er der mindst 50 vægt-20 procent afisningsmiddel til stede, fortrinsvis mindst 70 vægtprocent, især mindst 85 vægtprocent og mest foretrukkent mindst 90% eller endog mindst 95 vægtprocent, især når afisningsmidlet er natriumchlorid.Generally, at least one deicing agent is also present in the system. Usually at least 50% by weight of deicing agent is present, preferably at least 70% by weight, especially at least 85% by weight and most preferably at least 90%, or even at least 95% by weight, especially when the deicing agent is sodium chloride.

Sædvanligvis vælges et afisningsmiddel eller afis-25 ningsmidler blandt natriumchlorid, calciumchlorid, magnesium-chlorid og kaliumchlorid, men det indeholder fortrinsvis natriumchlorid.Usually, a deicing agent or deicing agents are selected from sodium chloride, calcium chloride, magnesium chloride and potassium chloride, but it preferably contains sodium chloride.

I almindelighed anvendes der mindst 0,25 vægtprocent af det korrosionsinhiberende system. Mængden er naturligvis 30 i nogen udstrækning afhængig af mængden af afisningsmiddel (og vilkårlige andre materialer), der kan være til stede. Fortrinsvis er mængden mindre end 10% og især fra 2 til 5 vægtprocent.Generally, at least 0.25% by weight of the corrosion inhibiting system is used. The amount is, of course, to some extent dependent on the amount of deicing agent (and any other materials) that may be present. Preferably, the amount is less than 10% and especially from 2 to 5% by weight.

Som anført ovenfor indeholder det korrosionsinhiberen-35 de system natriumfluorphosphat. Et særligt anvendeligt afisningsmiddel er et, der som korrosionsinhiberende system 5 DK 172079 B1 indeholder 3 ± 0,5 vægtprocent af et natriumfluorphosphat-system.As noted above, the corrosion inhibiting system contains sodium fluorophosphate. A particularly useful de-icing agent is one which, as a corrosion inhibiting system, contains 3 ± 0.5% by weight of a sodium fluorophosphate system.

Det er også muligt at anvende et vandopløseligt salt af et phosphonsyrederivat, især valgt blandt et salt af 5 triethylentetraminhexakismethylenphosphonsyre og ethylhexyl-iminobis-methylenphosphonsyre, i det korrosionsinhiberende system.It is also possible to use a water-soluble salt of a phosphonic acid derivative, especially selected from a salt of triethylenetetramine hexakismethylene phosphonic acid and ethylhexyl-iminobis-methylene phosphonic acid, in the corrosion inhibiting system.

Det korrosionsinhiberende materiale kan også indeholde mindst ét amid af en fedtsyre, især kokosamid. Et særligt 10 anvendeligt korrosionsinhiberende materiale er et, der indeholder natriumfluorphosphat, kokosamid og et phosphcjnsyrede-rivat.The corrosion inhibiting material may also contain at least one amide of a fatty acid, especially cocosamide. A particularly useful corrosion inhibiting material is one which contains sodium fluorophosphate, cocosamide and a phosphonic acid derivative.

Det korrosionsinhiberende materiale kan også indeholde natriumsilicat, sædvanligvis i et vægtforhold mellem natrium-15 monofluorphosphat og natriumsilicat på 1-10:1-2,5, fortrinsvis omkring 1:1.The corrosion inhibiting material may also contain sodium silicate, usually in a weight ratio of sodium monofluorophosphate to sodium silicate of 1-10: 1-2.5, preferably about 1: 1.

Afisningsmidlet opløses sædvanligvis i et egnet opløsningsmiddel, ofte i et vandigt medium og især således, at der dannes en i det væsentlige mættet opløsning.The de-icing agent is usually dissolved in a suitable solvent, often in an aqueous medium, and especially so as to form a substantially saturated solution.

2 0 Der kan også være mindst ét j ordkonditioneringsmiddel til stede i afisningsmidlet.There may also be at least one soil conditioner present in the deicing agent.

Ved hjælp af fremgangsmåden! ifølge den foreliggende opfindelse kan man afise en udendørs overflade, idet der over overfladen anbringes et afisningsmiddel, som anvendes 25 ifølge den foreliggende opfindelse. Fortrinsvis blandes j afisningsmidlet med det korrosionsinhiberende system og anbringes over betonoverfladen, hvor sammenblandingen og belægningen udføres på i det væsentlige samme tidspunkt.Using the procedure! According to the present invention, an outdoor surface can be de-iced by placing a de-icing agent used over the surface of the present invention. Preferably, the de-icing agent is mixed with the corrosion inhibiting system and applied over the concrete surface where the mixing and coating is carried out at substantially the same time.

Det korrosionsinhiberende system kan øve indflydelse på 30 afisningsmidlet, før det lægges over betonoverfladen. Afisningsmidlet eller det korrosionsinhiberende system kan anbringes som en vandig opløsning i koncentratform.The corrosion inhibiting system can exert influence on the de-icing agent before it is applied over the concrete surface. The deicing agent or the corrosion inhibiting system can be applied as an aqueous solution in concentrate form.

Især foretrukne afisningsmidler er (a) et, der indeholder mindst 85 vægtprocent afisningsmiddel og mindst 35 0,25 vægtprocent af et korrosionsinhiberende materiale, der indeholder natriumfluorphosphat; (b) et, der indeholder 6 DK 172079 B1 natriumfluorphosphat og natriumsilicat i et vægtforhold på i det væsentlige 1:1; og (c) et, i hvilket afisningsmidlet er et korrosivt afisningsmiddel med mindst 95 vægtprocent natriumchlorid.Particularly preferred deicing agents are (a) one containing at least 85% by weight of deicing agent and at least 35% by weight of a corrosion inhibiting material containing sodium fluorophosphate; (b) one containing sodium fluorophosphate and sodium silicate in a weight ratio of substantially 1: 1; and (c) one in which the deicing agent is a corrosive deicing agent having at least 95% by weight of sodium chloride.

5 Ved hjælp af den foreliggende opfindelse kan der tilvejebringes der armeret beton, der indeholder armeringsjern, hvor betonen mindst indeholder resterende mængder af det omhandlede afisningsmiddel.By means of the present invention, reinforced concrete may be provided containing reinforcing iron, the concrete containing at least residual amounts of the de-icing agent.

Særligt foretrukne afisningsmidler er: 10 (a) et, i hvilket det korrosionsinhiberende system er natriummonofluorphosphat; (b) et, der indeholder mindst 70 vægtprocent af afisningsmidlet og mindst 0,25 vægtprocent af et korrosionsinhiberende system indeholdende natriumfluorphosphat; 15 (c) et, i hvilket det korrosionsinhiberende materiale indeholder natriumfluorphosphat og natriumsilicat; (d) et, der indeholder af natriumf luorphosphat og natriumchlorid; og (e) et, i hvilket det korrosionsinhiberende materiale 20 også omfatter et vandopløseligt salt af mindst ét phosphon- syrederivat som defineret ovenfor.Particularly preferred deicing agents are: (a) one in which the corrosion inhibiting system is sodium monofluorophosphate; (b) one containing at least 70% by weight of the deicing agent and at least 0.25% by weight of a corrosion inhibiting system containing sodium fluorophosphate; (C) one in which the corrosion inhibiting material contains sodium fluorophosphate and sodium silicate; (d) one containing sodium phosphorus phosphate and sodium chloride; and (e) one in which the corrosion inhibiting material 20 also comprises a water-soluble salt of at least one phosphonic acid derivative as defined above.

Ved hjælp af den foreliggende opfindelse kan der tilvejebringes der en udendørs overflade, der indeholder i det mindste resterende mængder af et afisningsmiddel af den 25 omhandlede art.By means of the present invention, an outdoor surface may be provided which contains at least residual amounts of a de-icing agent of the kind in question.

Ifølge opfindelsen kan der anvendes et korrosionsinhiberende system, der består af mindst ét stof, der er valgt blandt (a) natriumfluorphosphat, 30 (b) et vandopløseligt salt af mindst ét phosphon- syrederivat med den almene formelAccording to the invention, a corrosion inhibiting system consisting of at least one substance selected from (a) sodium fluorophosphate may be used, (b) a water-soluble salt of at least one phosphonic acid derivative of the general formula

Rn R' N (CH2 P03 H2) 2-n i hvilken R og R' uafhængigt af hinanden er valgt blandt alkyl, aminoalkyl og hydroxyalkyl, og n betyder 0 eller 1.R n R 'N (CH 2 PO 3 H2) 2-n in which R and R' are independently selected from alkyl, aminoalkyl and hydroxyalkyl, and n means 0 or 1.

35 Systemet forekommer fortrinsvis i et egnet bærestof. Det kan være opløst i et vandigt medium, fortrinsvis ved en 7 DK 172079 B1 koncentration, der i det væsentlige er tæt på en mættet opløsning.Preferably, the system is present in a suitable carrier. It may be dissolved in an aqueous medium, preferably at a concentration which is substantially close to a saturated solution.

Det korrosionsinhiberende system kan f.eks. være på en form, der er valgt blandt (1) overtræk og malinger, især 5 maling, og (2) emulsioner og suspensioner. Bærestoffet kan være ikke-vandigt. Det kan endog være sand.The corrosion inhibiting system can e.g. be in a form selected from (1) coatings and paints, especially 5 paints, and (2) emulsions and suspensions. The carrier may be non-aqueous. It may even be true.

Det korrosionsinhiberende system kan f.eks. anvendes på en udendørs overflade.The corrosion inhibiting system can e.g. applied to an outdoor surface.

Ved denne udførelsesform foretrækkes det til tider, 10 at mindst én bestanddel indeholder natriumfluorphosphat sammen med natriumsilicat. I en sådan blanding er vægtforholdet mellem natriumfluorphosphat og natriumsilicat fortrinsvis 1-10 : 1-2,5, især i det væsentlige 1:1,In this embodiment, it is sometimes preferred that at least one component contains sodium fluorophosphate together with sodium silicate. In such a mixture, the weight ratio of sodium fluorophosphate to sodium silicate is preferably 1-10: 1-2.5, especially substantially 1: 1,

Den udendørs overflade kan f.eks. sprayes eller males 15 med det korrosionsinhiberende system.The outdoor surface can e.g. is sprayed or painted with the corrosion inhibiting system.

Vandet tillader fortrængning af det korrosionsinhiberende system, såsom natriumfluorphosphat, på jernarmeringer-ne.The water allows displacement of the corrosion inhibiting system, such as sodium fluorophosphate, on the iron reinforcements.

Afisningsmidler er kendte. Ved afisningsmidler menes 20 i almindelighed et hvilket som helst produkt, der er i stand til at sænke vands frysepunkt, og som har de andre nødvendige karakteristika, der er nødvendige for ikke at forårsage skadelige væsentlige virkninger på omgivelserne eller dets tiltænkte anvendelse. F.eks. må det ikke være fedtet, hvis 25 det skal anvendes til veje. Dette omfatter glycoler, (f.eks. ethylenglycoler) , calci'ummagnesiumacetat, methanol, cal-ciumchlorid, magnesiumchlorid, urinstof, natriumformiat og i almindelighed andre afisningsmidler, der i almindelighed er tilgængelige. Det omfatter også korrosive afisningsmidler, 30 og korrosionsinhibitorerne anvendt ifølge den foreliggende opfindelse er af særlig fordel sammen med sådanne korrosive afisningsmidler.Deicing agents are known. By de-icing means, in general, is meant any product capable of lowering the freezing point of water and having the other necessary characteristics necessary not to cause detrimental significant effects on the environment or its intended use. Eg. it must not be greasy if it is to be used for roads. This includes glycols, (e.g., ethylene glycols), calcium magnesium acetate, methanol, calcium chloride, magnesium chloride, urea, sodium formate, and generally other deicing agents generally available. It also comprises corrosive de-icing agents, and the corrosion inhibitors used in the present invention are of particular advantage with such corrosive de-icing agents.

Opfindelsen vedrører også et korrosionsinhiberende system i et stort antal egnede bærestoffer. Som eksempler 35 kan bærestoffet være en egnet gasart, væske eller en fast fase. Det omfatter f.eks., men ikke begrænset hertil, afis- 8 DK 172079 B1 ningsmidler, malinger, overtræk, fortyndingsmidler, emulsioner, suspensioner, opløsningsmidler og luftstrålepåførs-ler.The invention also relates to a corrosion inhibiting system in a large number of suitable carriers. As Examples 35, the carrier may be a suitable gas, liquid or solid phase. It includes, for example, but not limited to, deicing agents, paints, coatings, diluents, emulsions, suspensions, solvents and air jet applications.

Nogle foretrukne udførelsesformer omfatter vandige 5 opløsninger af natriumfluorphosphat, især natriumflourphos-phat og natriumsilicat, ganske særlig foretrukket opløsninger, der faktisk er mættede, dvs. så tæt på mættethed som muligt, for så at blive fortyndet ved anvendelsen. Andre foretrukne udførelsesformer omfatter overtræk og malinger, 10 der indeholder natriumfluorphosphat.Some preferred embodiments include aqueous solutions of sodium fluorophosphate, especially sodium fluorophosphate and sodium silicate, particularly preferred solutions that are actually saturated, i.e. as close to saturation as possible, and then diluted with application. Other preferred embodiments include coatings and paints containing sodium fluorophosphate.

De udendørs overflader kan tør- eller vådsprayes, overtrækkes, males eller dyppes i en beholder indeholdende det korrosive inhiberende system.The outdoor surfaces can be dry or wet sprayed, coated, painted or dipped in a container containing the corrosive inhibitory system.

Ved korrosive afisningsmidler forstås i modsætning 15 til afisningsmidler et afisningsmiddel, der kan forårsage korrosion og som indeholder salte, såsom natriumchlorid, calciumchlorid, magnesiumchlorid, kaliumchlorid, natriumfor-miat og andre korrosive afisningsmidler og andre produkter, der har ioner, der virker som chloridionerne.By contrast, in the case of deicing agents, corrosive deicing agents are defined as deicing agents which can cause corrosion and which contain salts such as sodium chloride, calcium chloride, magnesium chloride, potassium chloride, sodium formate and other corrosive deicing agents and other products having ions acting as the chloride ions.

20 Ved et korrosionsinhiberende system indeholdende fluorphosphat eller alternativt et system indeholdende fluor-phosphat menes fluorphosphat alene og i kombination med andre komponenter, såsom natriumsilicat med eller uden andre tilsætningsstoffer som ønsket, f .eks. jordkonditioneringsmid-25 ler, såsom CaS04, urinstof, andet mineralholdigt materiale, nitrogensubstanser og lignende, i mængder, der ikke i det væsentlige påvirker afisningsmidlets afisningskarakteristika som beskrevet nedenfor.By a corrosion inhibiting system containing fluorophosphate or alternatively a system containing fluorophosphate is meant fluorophosphate alone and in combination with other components such as sodium silicate with or without other additives as desired, e.g. soil conditioners, such as CaSO4, urea, other mineral-containing material, nitrogenous substances and the like, in amounts that do not substantially affect the de-icing characteristics of the de-icing agent as described below.

Opfindelsen omhandler også produkter indeholdende i 30 det mindste resterende mængder af de korrosionsinhiberende systemer, hvilket vil sige enten i form af de korrosionsinhiberende systemer eller som en resterende mængde hidrørende fra virkningen af de korrosionsinhiberende systemer på produkterne eller på en komponent af produkterne, eller fra 35 ældning, vask, regn osv. Disse produkter har i almindelighed udendørs overflader, der er udsat for luft, chloridioner 9 DK 172079 B1 og lignende.The invention also relates to products containing at least the remaining amounts of the corrosion inhibiting systems, that is, either in the form of the corrosion inhibiting systems or as a residual amount arising from the effect of the corrosion inhibiting systems on the products or on a component of the products, or from the products. aging, washing, rain, etc. These products generally have outdoor surfaces exposed to air, chloride ions 9 DK 172079 B1 and the like.

Der er fortrinsvis her tale om afisningsmidler med formindskede korrosionskarakteristika, hvilke består af almindeligt salt (NaCl) med mindst 0,25% og fortrinsvis 2 5 til 5 vægtprocent af et system indeholdende natriumfluor-phosphat, med eller uden natriumsilicat. Vægtforholdet mellem natriumfluorphosphat og natriumsilicat kan f.eks. være 1-10:1-2,5 men er fortrinsvis ca. 1:1. Disse afisningsmidler foretrækkes især, da det gængse salts afisningsegenskab i 10 det væsentlige opretholdes, medens deres korrosive karakteristika inhiberes, især med hensyn til armeringsjernet, når de anvendes i forbindelse med armeret beton eller jernbeton.Preferably, these are de-icing agents with diminished corrosion characteristics which consist of common salt (NaCl) of at least 0.25% and preferably 2.5 to 5% by weight of a system containing sodium fluorophosphate, with or without sodium silicate. The weight ratio of sodium fluorophosphate to sodium silicate can be, e.g. be 1-10: 1-2.5, but is preferably approx. 1: 1. These deicing agents are particularly preferred since the deicing properties of the common salt are substantially maintained while their corrosive characteristics are inhibited, especially with respect to the reinforcing iron when used in connection with reinforced concrete or iron concrete.

De;r er mange forskellige måder, der kan anvendes til påføring af afisningsmidler. F.eks. kan afisningsmidler 15 anvendes med sand. Afisningsmidlet med formindskede korrosionskarakteristika kan tørblandes eller vådblandes, hvad enten det blandes på fast form eller blandes in situ på de steder, hvor der er behov for det. F.eks. kan det fremstilles ved tørblanding af natriumchlorid med det system, der in-20 deholder fluorphosphat. Systemet indeholdende fluorphosphat kan også til specifikke slutanvendelser opløses, suspenderes eller emulgeres i et egnet opløsningsmiddel eller fortyndingsmiddel, f.eks. vand, glycoler, sand, fortrinsvis med den mindst mulige fortynding med tilstrækkeligt vand til at 25 opnå en viskositet, hvorved systemet indeholdende natrium-fluorphosphat vil være let at spraye over natriumchloridet eller spraye mod natriumchloridet, hvad enten det er på et anlæg eller i et salt- og/eller sanddispergerende bærestof, f.eks. således, at systemet øver indflydelse på natrium-30 chloridet og/eller sandet, før det lægges over en overflade, såsom f.eks. en betonoverflade. Systemet kan også sprayes på sammen med natriumchloridet, eller systemet kan fordeles i natriumchloridet ved hjælp af vilkårlige andre metoder. Natriumchloridet kan f.eks. tilføres ved hjælp af endeløse 35 transportbånd, såsom bæltetransportbånd, eller ved andre metoder. Spraying af systemet udføres således, at der opnås 10 DK 172079 B1 de ønskede niveauer, f.eks. 0,25 til 10 vægtprocent, eller om ønsket højere, og fortrinsvis 2 til 5 vægtprocent af systemet indeholdende natriumfluorphosphat i det hidtil ukendte afisningsmiddel med reducerede korrosionskarakteristika.There are many different ways that can be used to apply deicing agents. Eg. For example, deicing agents 15 can be used with sand. The de-icing agent with diminished corrosion characteristics can be dry-blended or wet-blended, whether solid-blended or in-situ blended where needed. Eg. it can be prepared by dry blending sodium chloride with the fluorophosphate-containing system. The fluorophosphate-containing system may also be dissolved, suspended or emulsified in a suitable solvent or diluent for specific end uses, e.g. water, glycols, sand, preferably with the least possible dilution with sufficient water to achieve a viscosity, whereby the system containing sodium fluorophosphate will be easy to spray over the sodium chloride or spray against the sodium chloride, whether on a plant or in a plant. salt and / or sand dispersing carrier, e.g. so that the system exerts influence on the sodium chloride and / or sand before it is applied over a surface such as e.g. a concrete surface. The system can also be sprayed on together with the sodium chloride or the system can be distributed into the sodium chloride by any other method. The sodium chloride may e.g. is supplied by endless conveyor belts such as belt conveyor belts or by other methods. Spraying of the system is carried out so as to achieve the desired levels, e.g. 0.25 to 10% by weight, or if desired higher, and preferably 2 to 5% by weight of the sodium fluorophosphate-containing system in the novel de-icing agent with reduced corrosion characteristics.

5 Dette afisningsmateriale, såsom salt, og det korro- sionsinhiberende system, der har reducerede korrosionskarakteristika, har ikke desto mindre de karakteristika, der er nødvendige for et godt afisningsmiddel, der i det væsentlige er uændrede, såsom f.eks. friktion, frysepunkt, hastigheden, 10 hvormed is gennemtrænges, og ismeltningshastigheden.This de-icing material, such as salt, and the corrosion inhibiting system having reduced corrosion characteristics nevertheless have the characteristics necessary for a good de-icing agent which is substantially unchanged, such as e.g. friction, freezing point, speed, ice penetration, and ice melting rate.

Afisningsmaterialet med korrosionskarakteris_tika kan i stedet for natriumchlorid indeholde andre afisningsmidler som ovenfor anført, og hvad der er nævnt om natriumchlorid, kan i almindelighed også siges om disse andre korrosive afis-15 ningsmidler.The de-icing material with corrosion characteristics may contain, instead of sodium chloride, other de-icing agents as stated above, and what has been mentioned about sodium chloride can generally also be said of these other corrosive de-icing agents.

De korrosive afisningsmidler behøver ikke kun at indeholde fluorphosphat med eller uden natriumsilicat, skønt de korrosive afisningsmidler mindre foretrukket kan anvendes med eller uden amider af en fedtsyre, f.eks. såsom de, der 20 har 8 til 24 C-atomer (f.eks. kokosamid i et niveau med en acceptabel toksicitet). Skønt mindre foretrukne kan der også anvendes salte af derivater af phosphonsyre som beskrevet ovenover. Typiske eksempler på disse derivater af phosphonsyre omfatter natriumsalt eller andre forenelige 25 opløselige salte af triethylentetraminhexakis-(methylen-phosphonsyre) og natriumsalt af ethylhexyliminobis-(methylen-phosphonsyre) eller en kombination deraf.The corrosive de-icing agents need not only contain fluorophosphate with or without sodium silicate, although the corrosive de-icing agents may be less preferably used with or without amides of a fatty acid, e.g. such as those having 20 to 24 C atoms (e.g., cocosamide at an acceptable toxicity level). Although less preferred, salts of phosphonic acid derivatives can also be used as described above. Typical examples of these phosphonic acid derivatives include sodium salt or other compatible soluble salts of triethylenetetramine hexakis (methylene phosphonic acid) and sodium salt of ethylhexyliminobis (methylene phosphonic acid) or a combination thereof.

En metode til at fremstille disse derivater af phosphonsyre på består i at omsætte en amin med formaldehyd og 30 phosphonsyre. Afisningsmidlet kan bringes på pelletform om ønsket.One method of preparing these phosphonic acid derivatives is to react an amine with formaldehyde and phosphonic acid. The deicing agent can be brought in pellet form if desired.

De korrosionsinhiberende systemer, der er beskrevet ovenfor, kan anvendes med eller uden afisningsmidler til inhibering af korrosion. De korrosionsinhiberende systemer 35 kan også være til stede i et egnet bærestof, enten en gas, væske eller på fast form, såsom et vandigt eller et andet 11 DK 172079 B1 medium, der danner en opløsning med eller uden afisningsmidler, f.eks. vandige mættede opløsninger, eller som et overtræk, en emulsion, suspension eller en maling til nogle anvendelser. Malingen, erfiulsionen, suspensionen eller over-5 trækket kan om ønsket anvendes til overtrækning af metaller, såsom armeringsjern, bilstrukturer, brostrukturer, sanitetsledninger, kulverter eller andre udendørs overflader af metal. Luft kan også anvendes til at dispergere det korros ions inhiberende system samt andre egnede gasser.The corrosion inhibiting systems described above can be used with or without deicing agents to inhibit corrosion. The corrosion inhibiting systems 35 may also be present in a suitable carrier, either a gas, liquid or solid, such as an aqueous or other medium which forms a solution with or without deicing agents, e.g. aqueous saturated solutions, or as a coating, an emulsion, suspension or a paint for some applications. The paint, inheritance, suspension or coating may, if desired, be used for coating metals, such as reinforcing bars, car structures, bridge structures, sanitary pipes, culverts or other outdoor metal surfaces. Air can also be used to disperse the corrosion inhibiting system as well as other suitable gases.

10 De følgende eksempler tjener til illustration af bestemte udførelsesformer for opfindelsen.The following examples serve to illustrate particular embodiments of the invention.

Eksempel 1-4.Examples 1-4.

Den anvendte analyse er ASTM-G-31-72 som vedtaget 15 igen i 1985 for korrosive afisningsmidler og med de systemer, der er beskrevet i tabel I. Korrosionshastigheden, der resulterer i vægttab, udtrykkes som mm pr. år. Som det let kan ses, har systemer indeholdende fluorphosphat og silicat en signifikant positiv virkning med hensyn til at reducere 20 korrosionen, således som det fremgår af eksemplerne.The analysis used is ASTM-G-31-72 as adopted 15 again in 1985 for corrosive deicing agents and with the systems described in Table I. The corrosion rate resulting in weight loss is expressed as mm per mm. year. As can be readily seen, systems containing fluorophosphate and silicate have a significant positive effect in reducing corrosion, as shown in the Examples.

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Eksempel 5Example 5

Det følgende illustrerer pH's virkning på korrosionshastigheden med natriumchlorid alene eller med følgende: A: der er Na2P03F, og 5 B: der er Na2PC>3F :Na2SiC>3 :Na 1 ignosulfonat: 1:1:1 under anvendelse af den metode, der er beskrevet i eksemplerne 1 til 4.The following illustrates the effect of pH on the corrosion rate with sodium chloride alone or with the following: A: there is Na2 PO3F, and 5 B: there is Na2PC> 3F: Na2SiC> 3: Na1 ignosulfonate: 1: 1: 1 using the method used. are described in Examples 1 to 4.

Inhiberende pH 6 pH 8 pH 10 pH 12 10 system % 264 t. 693 t.Inhibitory pH 6 pH 8 pH 10 pH 12 10 System% 264 t 693 t.

mm/år mm/år mm/år mm/år mm/år (mpy) (mpy) (mpy) (mpy) (mpy) 15 0 0,0498 0,0389 0,0523 (2,36) (1,96) (1,84) (1,53) (2,06) 6% A 0,0124 0,0244 0,0320 ( - ) (0,53) (0,49) (0,96) (1,26) 20 4% A 0,0198 0,0310 0,0287 (1,51) (0,41) (0,78) (1,22) (1,13) 2% A 0,0226 0,0325 0,0264 25 (1,95) (0,68) (0,89) (1,28) (1,04) 6% B 0,0127 0,0086 0,0259 ( - ) (0,49) (0,50) (0,34) (1,02) 30 4% B 0,0132 0,0135 0,0302 (0,68) (0,34) (0,52) (0,53) (1,19) 2% B 0,0226 0,0208 0,0246 (1,49) (1,14) (0,89) (0,82) (0,97) 35mm / year mm / year mm / year mm / year mm / year (mpy) (mpy) (mpy) (mpy) (mpy) 15 0 0.0498 0.0389 0.0523 (2.36) (1.96 ) (1.84) (1.53) (2.06) 6% A 0.0124 0.0244 0.0320 (-) (0.53) (0.49) (0.96) (1.26) ) 20 4% A 0.0198 0.0310 0.0287 (1.51) (0.41) (0.78) (1.22) (1.13) 2% A 0.0226 0.0325 0, 0264 25 (1.95) (0.68) (0.89) (1.28) (1.04) 6% B 0.0127 0.0086 0.0259 (-) (0.49) (0, 50) (0.34) (1.02) 4% B 0.0132 0.0135 0.0302 (0.68) (0.34) (0.52) (0.53) (1.19) 2% B 0.0226 0.0208 0.0246 (1.49) (1.14) (0.89) (0.82) (0.97) 35

Eksempel 6-7Examples 6-7

Det følgende påviser de formindskede korrosionskarakteristika for et system indeholdende natriumchlorid under 40 anvendelse af den følgende fremgangsmåde:The following demonstrates the diminished corrosion characteristics of a system containing sodium chloride using the following procedure:

Armeringsjern/betonprøver fremstilles ud fra 5,08 cm (¾11) armeringsjernstokke, og beton med en blandingssammensætning på 1:1:5 (Portlandcement:vand:sand). Natriumchlorid sættes til blandingsvandet til dannelse af et chloridniveau 45 i betonen på 11,87 kg/m3 Cl-. Betondækket er 5 mm, og det udsatte armerings jernområde er 14 cm3. Korrosionshastigheder- 14 DK 172079 B1 ne måles under anvendelse af vekselstrømsimpedans-målingsmetoden; ved sekvensvise vekselstrømsimpedansmålinger overføres en sinusbølge med fikseret amplitude, sædvanligvis af størrelsesordenen 10 mV, til det indstøbte stål med aftagende 5 frekvenser, og både faseskift og modulus for impedans af stålet måles som en funktion af frekvensen. Dette er beskrevet af F. Manfeld i "Recording an Analysis of AC Impedance Data for Corrosion Studies - I", Corrosion - Nace, bind 36, nr. 5, s. 301-307, maj 1981 og bind 38, nr. 11, side 570-580, 10 november 1982, og K. Hladky, L. Callow, J. Dawson, "Corrosion Rates from Impedance Measurements: An Introduction", Br.Reinforcement iron / concrete samples are prepared from 5.08 cm (¾11) reinforcing bars, and concrete with a mixture composition of 1: 1: 5 (Portland cement: water: sand). Sodium chloride is added to the mixing water to form a chloride level 45 in the concrete of 11.87 kg / m 3 Cl-. The concrete deck is 5 mm and the exposed reinforced iron area is 14 cm3. The corrosion rates are measured using the AC impedance measurement method; for sequential alternating current impedance measurements, a fixed-amplitude sine wave, usually of the order of 10 mV, is transmitted to the embedded steel of decreasing 5 frequencies, and both phase shifts and modulus of impedance of the steel are measured as a function of frequency. This is described by F. Manfeld in "Recording an Analysis of AC Impedance Data for Corrosion Studies - I", Corrosion - Nace, Vol. 36, No. 5, pp. 301-307, May 1981, and Vol. 38, No. 11, pages 570-580, November 10, 1982, and K. Hladky, L. Callow, J. Dawson, "Corrosion Rates from Impedance Measurements: An Introduction", Br.

Corro J., bind 15, nr. l, s. 20-25, 1980.Corro J., Volume 15, No. 1, pp. 20-25, 1980.

Tabel IITable II

15 3 % 1 s saltopløsning3% 1 s brine

Eksempel Antal dage, nr. hvori mate- % af komponenter rialet udsæt- Korrosions- 20 i afisningsmid- tes for på- hastighed let virkning mm/år 6 98 NaCl 85 0,0155Example Number of days, no. In which the material% of the component is exposed to corrosion 20 in de-icing medium for speed light effect mm / year 6 98 NaCl 85 0.0155

25 2 Na2P03F2 Na2 PO3F

7 98 NaCl 75 0,0414 2 phosphonsyrede- rivat som i ek-30 sempel 47 98 NaCl 75 0.0414 2 phosphonic acid derivative as in Example 4

Prøve B 100 NaCl , 85 0,0605Sample B 100 NaCl, 85 0.0605

Eksempel 8-19 35 I de følgende eksempler følges korrosionsstrømmen i en MACROCELL-korrosionsanalyse under anvendelse af armerede jernplader som følger:Examples 8-19 35 In the following examples, the corrosion current is followed in a MACROCELL corrosion analysis using reinforced iron sheets as follows:

To måtter af armeringsjern anbringes i beton under anvendelse af luftiblandet beton af gennemsnitlig kvalitet.Two reinforcing iron mats are placed in concrete using average quality air-mixed concrete.

40 Forskellige niveauer natriumchlorid sammenblandes i adskillige af topmåttelagene for at accelerere korrosionen og simulere det miljø, der er til stede i gamle brodæk. En dæmning anbringes på toppen af hver plade, og 6%'s opløsnin 15 DK 172079 B1 ger af afisningsmiddelprodukt opdæmmes med en dybde på 1,69 cm. Opløsningerne efterfyldes hver anden uge.40 Different levels of sodium chloride are blended into several of the top gauge layers to accelerate corrosion and simulate the environment present in old bridge decks. An embankment is placed on top of each plate and the 6% solution of de-icing agent product is dammed to a depth of 1.69 cm. The solutions are replenished every two weeks.

Armeringsjernenes top- og bundsæt forbindes elektrisk og momentan tænd og sluk i serier med en 1,0 Ohm-modstand 5 installeres mellem de to måtter.The top and bottom sets of the reinforcing bars are connected electrically and instantaneously on and off in series with a 1.0 Ohm resistor 5 installed between the two mats.

Den korrosionsstrøm, der flyder mellem top- og bundmåtterne, måles som spændingsfaldet over modstanden, når knappen er tilsluttet (normal stilling). Den drivende kraft (potentialeforskel) mellem top- og bundmåtter måles som 10 "instant-off "-spænding mellem de to måtter (knappen er momentant slået fra,· spændingsmålingen foretages inden for 2 sekunder). Korrosionspotentialer for topmåtterne måles mod mættede kalomelelektroder med knappen i normal "tænd"-stilling.The corrosion current flowing between the top and bottom mats is measured as the voltage drop across the resistor when the button is connected (normal position). The driving force (potential difference) between the top and bottom mats is measured as 10 "instant off" voltage between the two mats (the button is momentarily switched off, · the voltage measurement is made within 2 seconds). Corrosion potentials for the top mats are measured against saturated calomel electrodes with the button in normal "on" position.

15 I tabel III [Cl-] betyder kg chlorid pr. m3, hvor samme portion anvendes i eksemplerne 8, 12 og 16 som med prøven W osv.In Table III [Cl-], kg of chloride per m3, where the same portion is used in Examples 8, 12 and 16 as with the sample W, etc.

Analyse 20 En analyse af korrosionsprodukter på armeringsjern fra prøve C og eksempel 8 er foretaget.Analysis 20 An analysis of corrosion products on reinforcing iron from Sample C and Example 8 was made.

Korrosionsproduktlaget for prøve C er hovedsageligt sammensat af jernoxider/hydroxider med små mængder natrium og chlor (fra opløsningen) og silicium (siliciumdioxid fra 25 aggregatblandingen) til stede. Betonsiden af grænsefladen viser, at calcium er til sted både som oxider/hydroxider og carbonater.The corrosion product layer for Sample C is composed mainly of iron oxides / hydroxides with small amounts of sodium and chlorine (from the solution) and silicon (silica from the aggregate mixture) present. The concrete side of the interface shows that calcium is present both as oxides / hydroxides and carbonates.

Korrosionsproduktlaget fra eksempel 8 er mere komplekst. Laget er ganske tykt og har et højere calciumindhold 30 end de ikke-inhiberede overflader. Calcium er til stede som calciumoxid/hydroxid og ingen antydning af tilstedeværende carbonattyper. Der er også tegn på tilstedeværelse af væsentlige mængder chrom, nitrogen og aluminium i filmen.The corrosion product layer of Example 8 is more complex. The layer is quite thick and has a higher calcium content 30 than the non-inhibited surfaces. Calcium is present as calcium oxide / hydroxide and no indication of the carbonate types present. There is also evidence of the presence of significant amounts of chromium, nitrogen and aluminum in the film.

Der blev også påvist spor af phosphor.Traces of phosphorus were also detected.

3 5 Som en foreløbig forklaring synes det, at inhibitorens virkning kan være en ændring af det lokale miljø på grund 16 DK 172079 B1 af en reaktion eller forebyggelse af en reaktion med beton-bestanddelene. Hovedforskellen mellem det inhiberede (eksempel 8) og det ikke-inhiberede (prøve C) er mængden og naturen af det calcium, der er til stede i korros ionsprodukt f ilmene.As a preliminary explanation, it seems that the effect of the inhibitor may be a change in the local environment due to a reaction or prevention of a reaction with the concrete components. The main difference between the inhibited (Example 8) and the uninhibited (Sample C) is the amount and nature of the calcium present in the corrosion product films.

5 Mætning med CO2 af betonlaget sammen med tilstedeværelse af chlorider af et vigtigt forstadium for korrosion af stålarme-ringen. Man fandt, at den her omhandlede inhibitor påvirker denne mætningsreaktion med C02 og således mekanismen for korrosionsinhiberende mængder til ændring af det lokale 10 miljø tilladende opretholdelse af en stabil passiv film i stedet for inkorporering af inhibitorforbindelsen i filmen til dannelse af et mere beskyttende lag på overfladen.5 Saturation with CO2 of the concrete layer together with the presence of chlorides, an important precursor for corrosion of the steel reinforcement. It was found that the present inhibitor affects this saturation reaction with CO 2 and thus the mechanism of corrosion inhibiting amounts to alter the local environment permitting the maintenance of a stable passive film instead of incorporating the inhibitor compound into the film to form a more protective layer on the surface. .

DK 172079 B1 17 0)DK 172079 B1 17 0)

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Eksempel 2QExample 2Q

Det følgende vil tjene til illustration af de formindskede korrosionskarakteristika for en 4%' s afisningsmiddelopløsning. Den procentvise inhibering beregnes som pro-5 centvis reduktion af korrosionshastigheden i forhold til korrosionhastigheden for den samme afisningsmiddelopløsning uden Na2P03F-systemet.The following will serve to illustrate the diminished corrosion characteristics of a 4% deicing agent solution. The percent inhibition is calculated as a percentage reduction of the corrosion rate relative to the corrosion rate of the same deicing agent solution without the Na2 PO3F system.

Gennemsnitlig 10 Afisnings- % Na2P03F korrosions- % Inhibe- middel system hastighed mm/år ring 100 CaCl2 0 0,0699 15 94 CaCl2 6 Na2P03F 0,0307 56 94 CaCl2 6* 0,0302 56,7 100 MgCl2 0 0,0594 20 94 MgCl2 6 Na2P03F 0,0343 42,3 94 MgCl2 6* 0,0351 41 25 Eksempel 21Average 10 De-icing% Na2PO3F Corrosion% Inhibitor System Speed mm / year ring 100 CaCl2 0 0.0699 15 94 CaCl2 6 Na2PO3F 0.0307 56 94 CaCl2 6 * 0.0302 56.7 100 MgCl2 0 0.0594 20 94 MgCl2 6 Na2 PO3F 0.0343 42.3 94 MgCl2 6 * 0.0351 41 Example 21

Det følgende eksempel tjener til illustration af virkningen af koncentrationen af Na2P03F-systemet med tiden under anvendelse af en 4%'s natriumchloridafisningsopløsning som følger: 30The following example serves to illustrate the effect of the concentration of the Na2 PO3F system over time using a 4% sodium chloride deicing solution as follows:

Afisnings- % Na2P03F Korrosionshastighed middel system 264 t 639 t mm/år mm/år 35--—--— 100 NaCl 0,0599 0,0498 96 NaCl 4 Na2P03F 0,0384 0,0104 98 NaCl 2 Na2P03F 0,0495 0,0173 96 NaCl 4* 0,0173 0,0086 40 98 NaCl 2* 0,0290 0,0378 *Na2P03F + Na2Si03 + natriumlignosulfonat i et vægtforhold på 1:1:1.Defrost% Na2 PO3F Corrosion Rate Mean System 264 t 639 t mm / year mm / year 35 - - - 100 NaCl 0.0599 0.0498 96 NaCl 4 Na2 PO3F 0.0384 0.0104 98 NaCl 2 Na2 PO3F 0.0495 0 , 0173 96 NaCl 4 * 0.0173 0.0086 40 98 NaCl 2 * 0.0290 0.0378 * Na2 PO3F + Na2 SiO3 + sodium lignosulfonate in a weight ratio of 1: 1: 1.

19 DK 172079 B119 DK 172079 B1

Eksempel 22Example 22

Det følgende eksempel tjener til illustration af de formindskede korrosionskarakteristika for det foretrukne afisningsmiddel på forskellige metaller.The following example serves to illustrate the diminished corrosion characteristics of the preferred deicing agent on various metals.

55

NaCl-afis- Korrosionshastighed ningsmid- Na2PC>3F- Blødt Galvanise- del system stål ret stål Aluminium % % mm/år mm/år mm/år 10 ------——- 100 0,0599 0,0665 0,0180 97,6 0,8 ligno- sulfonat 0,0193 0,0490 0,0051 15NaCl Newspaper- Corrosion Rate- Na2PC> 3F- Soft Galvanized Part Steel Steel Steel Aluminum%% mm / year mm / year mm / year 10 --------- 100 0.0599 0.0665 0, 0180 97.6 0.8 lignosulfonate 0.0193 0.0490 0.0051 15

0,8 Na2Si03 0,8 Na2P03F0.8 Na2 SiO3 0.8 Na2 PO3F

20 99% 1% lignosul- 0,0472 0,0429 0,0168 fonat 99% 1% Na2Si03 0,0277 0,0884 0,0246 25 99% 1% Na2P03F 0,0572 0,0307 0,005199% 1% lignosul 0.0472 0.0429 0.0168 phonate 99% 1% Na2 SiO3 0.0277 0.0884 0.0246 99% 1% Na2 PO3F 0.0572 0.0307 0.0051

Eksempel 23-24Examples 23-24

Det følgende eksempel tjener til at illustrere, at de formindskede korrosionskarakteristika for afisningsmid-30 ler med Na2P03F og Na2Si03 og/eller lignosulfonat skyldes Na2P03F alene eller med Na2SiC>3 og ikke lignosulfonatet.The following example serves to illustrate that the diminished corrosion characteristics of de-icing agents with Na2 PO3F and Na2SiO3 and / or lignosulfonate are due to Na2PO3F alone or with Na2SiC> 3 and not the lignosulfonate.

Inhibitorblandingen af Na2P03F og Na2SiC>3 undersøges for dets virkning på en prøve af blødt stål i en saltvandsopløsning (korrosionen af et armerings jern i en lille arme-35 ringsjern-betonprøve (eksempel 23)).The inhibitor mixture of Na2 PO3F and Na2SiC> 3 is examined for its effect on a sample of soft steel in a saline solution (the corrosion of a reinforcing iron in a small reinforcing iron concrete sample (Example 23)).

23 - Betonprøver23 - Concrete samples

Armeringsjern/betonprøver fremstilles som i eksemplerne 6 og 7 ud fra 1,27 cm (M") armeringsstokke og beton med 40 en sammensætning på 1:1:5 (Portlandcement:vand:sand). Betondækket er 5 mm og det udsatte armeringsjernområde er ca. 35 cm2. Prøverne udsættes for 3%'s NaCl + inhibitor-opløsninger (i den anførte koncentration) i det anførte antal dage, hvor- 20 DK 172079 B1 efter der analyseres (korrosionshastighed) under anvendelse af vekselstrømsimpedansteknikken.Reinforcement iron / concrete samples are prepared as in Examples 6 and 7 from 1.27 cm (M ") reinforcing sticks and concrete having a composition of 1: 1: 5 (Portland cement: water: sand). The concrete deck is 5 mm and the exposed reinforcing iron area is The samples are exposed to 3% NaCl + inhibitor solutions (at the indicated concentration) for the indicated number of days, after which the analyte (corrosion rate) is analyzed using the AC impedance technique.

21 DK 172079 B1 d •ro21 DK 172079 B1 d • ro

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Claims (19)

1. Fremgangsmåde til inhibering af korrosion af armeringsjern i jernbeton, kendetegnet ved, at der på overfladen af jernbetonen anbringes et korrosionsinhibi- 5 torsystem, som i det mindste indeholder natriummonofluor-phosphat, og i hvilket natriummonofluorphosphatet i kontakt med vand inhiberer korrosionen af armeringsjernene.A method of inhibiting corrosion of reinforcing iron in ferrous concrete, characterized in that a corrosion inhibitor system is provided which contains at least sodium monofluorophosphate at least on the surface of the iron concrete, in which the sodium monofluorophosphate in contact with water inhibits the corrosion of the reinforcement. 2. Fremgangsmåde ifølge krav 1, kendetegnet ved, at systemet er natriummonofluorphosphat.Process according to claim 1, characterized in that the system is sodium monofluorophosphate. 3. Fremgangsmåde ifølge krav 1 eller 2, kende tegnet ved, at systemet er opløst i et vandigt medium.Process according to claim 1 or 2, characterized in that the system is dissolved in an aqueous medium. 4. Fremgangsmåde ifølge krav l, kendetegnet ved, at systemet indeholder natriummonofluorphosphat og natriumsilicat.Process according to claim 1, characterized in that the system contains sodium monofluorophosphate and sodium silicate. 5. Fremgangsmåde ifølge krav 4, kendeteg net ved, at systemet indeholder natriummonofluorphosphat og natriumsilicat i et vægtforhold på 1-10:1-2,5.Process according to claim 4, characterized in that the system contains sodium monofluorophosphate and sodium silicate in a weight ratio of 1-10: 1-2.5. 6. Fremgangsmåde ifølge krav 5, kendeteg net ved, at systemet indeholder natriummonofluorphosphat 20 og natriumsilicat i et vægtforhold på ca. 1:1.Process according to claim 5, characterized in that the system contains sodium monofluorophosphate 20 and sodium silicate in a weight ratio of approx. 1: 1. 7. Fremgangsmåde ifølge krav 1, kendeteg net ved, at systemet er natriummonofluorphosphat, kokos-amid og et vandopløseligt salt af mindst ét phosphonsyre-derivat med den almene formel RnRlN^CH2P03H2^2-n, hvor R ogProcess according to claim 1, characterized in that the system is sodium monofluorophosphate, coconut amide and a water-soluble salt of at least one phosphonic acid derivative of the general formula RnR1N ^ CH2 PO3H2 ^ 2-n, wherein R and 25 R1 hver for sig er valgt blandt alkyl, aminoalkyl og hydroxy-alkyl, og n er 0 eller 1.R 1 is independently selected from alkyl, aminoalkyl and hydroxyalkyl, and n is 0 or 1. 8. Fremgangsmåde ifølge krav 1, kendeteg net ved, at systemet er opløst i et egnet bærestof.Process according to claim 1, characterized in that the system is dissolved in a suitable carrier. 9. Fremgangsmåde ifølge krav 1, kendete g- 30 net ved, at systemet indeholder et ikke-vandigt bærestof.9. A process according to claim 1, characterized in that the system contains a non-aqueous carrier. 10. Fremgangsmåde ifølge krav 1, kendetegnet ved, at systemet indeholder sand.Method according to claim 1, characterized in that the system contains sand. 11. Fremgangsmåde ifølge et hvilket som helst af kravene 1-10, kendetegnet ved, at overfladen er 35 en udendørs overflade af jernbeton.Method according to any one of claims 1-10, characterized in that the surface is an outdoor surface of iron concrete. 12. Fremgangsmåde ifølge krav 11, kendete g- DK 172079 B1 net ved, at overfladen er en jernbetonoverflade af en bro.12. A method according to claim 11, characterized in that the surface is a reinforced concrete surface of a bridge. 13. Fremgangsmåde ifølge et hvilket som helst af kravene 1-12, kendetegnet ved, at overfladen sprayes med systemet.Method according to any one of claims 1-12, characterized in that the surface is sprayed with the system. 14. Fremgangsmåde ifølge et hvilket som helst af ' kravene 1-13, kendetegnet ved, at systemet også indeholder et afisningsmiddel.Process according to any one of claims 1-13, characterized in that the system also contains a de-icing agent. 15. Fremgangsmåde ifølge krav 14, kendetegnet ved, at afisningsmidlet er et korrosivt afisningsmid- 10 del, der indeholder mindst ét af stofferne natriumchlorid, calciumchlorid, magnesiumchlorid og kaliumchlorid.Process according to claim 14, characterized in that the de-icing agent is a corrosive de-icing agent containing at least one of the substances sodium chloride, calcium chloride, magnesium chloride and potassium chloride. 16. Fremgangsmåde ifølge krav 14 eller 15, kendetegnet ved, at det korrosive afisningsmiddel er natriumchlorid.Process according to claim 14 or 15, characterized in that the corrosive de-icing agent is sodium chloride. 17. Fremgangsmåde ifølge et hvilket som helst af kravene 14-16, kendetegnet ved, at det korrosive afisningsmiddel blandes med natriummonofluorphosphatet og anbringes over betonoverfladen, idet sammenblandingen og anbringelsen udføres på i det væsentlige samme tidspunkt.Process according to any of claims 14-16, characterized in that the corrosive de-icing agent is mixed with the sodium monofluorophosphate and applied over the concrete surface, the mixing and application being carried out at substantially the same time. 18. Fremgangsmåde ifølge et hvilket som helst af kravene 14-16, kendetegnet ved, at natriummono-fluorphosphatet blandes med det korrosive afisningsmiddel, inden det anbringes over betonoverfladen.Process according to any one of claims 14-16, characterized in that the sodium monofluorophosphate is mixed with the corrosive de-icing agent before it is applied over the concrete surface. 19. Fremgangsmåde ifølge et hvilket som helst af 25 kravene 14-17, kendetegnet ved, at systemet anbringes som en vandig opløsning på koncentratform.Process according to any one of claims 14-17, characterized in that the system is applied as an aqueous solution in concentrate form.
DK106789A 1989-03-06 1989-03-06 Corrosion inhibitor systems and deicer compsns. - comprising sodium fluorophosphate and/or phosphonic acid deriv. salt DK172079B1 (en)

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