SE423534B - MASS ON BASIS OF BREND, CORNED DOLOMIT AND WITH ORGANIC AND INORGANIC ADDITIVES FOR INFO LINING OF CONTAINERS FOR MOLD STEEL OR IRON - Google Patents
MASS ON BASIS OF BREND, CORNED DOLOMIT AND WITH ORGANIC AND INORGANIC ADDITIVES FOR INFO LINING OF CONTAINERS FOR MOLD STEEL OR IRONInfo
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- SE423534B SE423534B SE7713575A SE7713575A SE423534B SE 423534 B SE423534 B SE 423534B SE 7713575 A SE7713575 A SE 7713575A SE 7713575 A SE7713575 A SE 7713575A SE 423534 B SE423534 B SE 423534B
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
- C04B35/6303—Inorganic additives
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- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D41/00—Casting melt-holding vessels, e.g. ladles, tundishes, cups or the like
- B22D41/02—Linings
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
- C04B35/03—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on magnesium oxide, calcium oxide or oxide mixtures derived from dolomite
- C04B35/06—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on magnesium oxide, calcium oxide or oxide mixtures derived from dolomite based on oxide mixtures derived from dolomite
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- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
- C04B35/6303—Inorganic additives
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
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- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
- C04B35/632—Organic additives
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/66—Monolithic refractories or refractory mortars, including those whether or not containing clay
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D1/00—Casings; Linings; Walls; Roofs
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- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
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- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
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- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
- C04B2235/32—Metal oxides, mixed metal oxides, or oxide-forming salts thereof, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
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- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
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- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
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Description
15 20 25 30 35 40 77i1zs7s-4. t' 2 effektivt förhindra-en'hvdratisering, dvs undantaget av fuktighet ur luften. Sådana massor på basis av bränd dolomit, vilka innehål- ler de vanliga, kända, organiska tillsatserna, är därför inte lag- ringsbara en längre tid. I Bortsett från den möjliga förlängningen av lagringsbarheten _genom mineralolja och fettsyror innehåller de basiska massorna på basis av dolomit, såsom magnesia, i samtliga här nämnda patentskrif- *ter tillsatser av tjära eller beck, som vid tillsats till dessa massor betyder en avsevärd olägenhet i form av rök eller lukt. Till- satser av oorganiska bindemedel är inte nämnda. g Ändamålet med uppfinningen är att åstadkomma massor på basis av bränd dolomít, som är lagringsbara under en längre tid, exempel- vis tre månader eller längre, utan väsentlig hydratisering, dvs massornas egenskaper försämras inte genom upptagning av fuktighet från luften. ' Det har nu befunnits, att sådana massor kan framställas på basis av bränd dolomit med den för användningsändamålet anpassade kornuppbyggnaden och organiska och oorganiska tillsatser, om man som organisk tillsats använder en naturlig triglyceridolja eller en blandning av sådana triglyceridoljor och ett torrt, oorganiskt, malt bindemedel. . 15 20 25 30 35 40 77i1zs7s-4. t '2 effectively prevent hydration, ie the exclusion of moisture from the air. Such pulps based on burnt dolomite, which contain the usual, known, organic additives, are therefore not storable for a long time. Apart from the possible prolongation of the shelf life through mineral oil and fatty acids, the basic masses based on dolomite, such as magnesia, contain in all the patents mentioned here * additives of tar or pitch, which when added to these masses means a considerable inconvenience in form. of smoke or odor. Additives of inorganic binders are not mentioned. The object of the invention is to provide pulps based on burnt dolomite, which can be stored for a longer period, for example three months or longer, without significant hydration, ie the properties of the pulps are not impaired by absorbing moisture from the air. It has now been found that such pulps can be prepared on the basis of burnt dolomite with the grain structure adapted for the purpose of use and organic and inorganic additives, if a natural triglyceride oil or a mixture of such triglyceride oils and a dry, inorganic, malt is used as the organic additive. binder. .
Massan enligt uppfinningen kännetecknas av en halt av 1-6 viktprocent av en naturlig triglyceridolja eller av en blandning gav triglyceridoljor och en halt av 2-6 viktprocent av torrt, oorga- niskt, malt bindemedel och eventuellt av en tillsats av pappersmjöl 'och/eller kolhaltiga ämnen.The pulp according to the invention is characterized by a content of 1-6% by weight of a natural triglyceride oil or by a mixture yielding triglyceride oils and a content of 2-6% by weight of dry, inorganic, ground binder and optionally by an addition of paper flour and / or carbonaceous substances.
Enligt en föredragen utföringsform uppgår halten av triglyce- ridolja till 2-4 viktprocent. Det anses fördelaktigt att använda en vegetabilisk triglycerídolja, särskilt sojaolja.According to a preferred embodiment, the content of triglyceride oil amounts to 2-4% by weight. It is considered advantageous to use a vegetable triglyceride oil, especially soybean oil.
Vidare har det befunnits att en tillsats av 0,5-3 víktprocent av torkat pappersmjöl ytterligare förbättrar bearbetbarheten hos massan enligt uppfinningen i slungmaskinen, enär en snabb torkning Det är fördelaktigt att låta :ni- Ytterligare till- efter införandet blir möjlig. satsen av pappersmjöl uppgå till 1-2 viktprocent. satser av kolhaltigt material i form av sot, grafit, mald koks är möjliga. Ovannämnda uppgifter angående viktprocent är räknade på torr totalmassa.Furthermore, it has been found that an addition of 0.5-3% by weight of dried paper flour further improves the processability of the pulp according to the invention in the slung machine, since a rapid drying It is advantageous to allow: ni- Further addition after the introduction becomes possible. the batch of paper flour amounts to 1-2% by weight. batches of carbonaceous material in the form of soot, graphite, ground coke are possible. The above information regarding weight percentage is calculated on dry total mass.
Användningen av massan enligt uppfinningen sker på känt sätt, ekempelvis slungas den färdiga massan för färdigställning av skän- ken för flytande stål eller järn genom slunghuvudet hos slungmaski- 10 15 20 25 35 40 7713575-4 3 “__ _” s ,l_fl.._.“. nen med stor hastighet uppifrån in i det fria rummet mellan skänk- väggen och den införda schablonen.The pulp according to the invention is used in a known manner, for example the finished pulp for throwing the ladle for liquid steel or iron is thrown through the sling head of the slunging machine 3 15 __ _ ”s, l_ fl .. _. “. at high speed from the top into the free space between the sideboard wall and the inserted stencil.
Efter färdigställníngen avlägsnas schablonen. Massan äger en så stor inre sammanhållningskraft, att den bibehåller sin form och har en så hög råhållfasthet att den tål även transport för vidare- behandling, exempelvis vägen fram till skänkbrännaren,utan skador.After completion, the stencil is removed. The pulp has such a large internal cohesive force that it retains its shape and has such a high raw strength that it can also withstand transport for further processing, for example the road to the ladle burner, without damage.
Mätvärdet med den för ändamålet vanliga intrycksdjupmätanordningen enligt Fischer ligger över 90. Den iordningställda skänken uppvär- mes sedan och sintras genom den första ifyllda flytande stål- eller järnsmältan.The measured value with the standard impression depth measuring device according to Fischer is above 90. The prepared ladle is then heated and sintered through the first filled liquid steel or iron melt.
Den enligt uppfinningen använda massan utvinnes ur bränd dolo- mit ur varje naturligt förekommande dolomit genom konventionell bränning och anslutande krossníng och/eller malning och eventuellt avsiktníng av kornfraktíoner och hopklippning av kornfraktioner.The pulp used according to the invention is recovered from burnt dolomite from any naturally occurring dolomite by conventional firing and subsequent crushing and / or grinding and, if necessary, grinding of grain fractions and cutting of grain fractions.
Med begreppet dolomit förstår man icke blott en substans med den kemiska sammansättningen CaC03°MgC05, utan även material i vilka den mängdmässiga andelen av CaC03 och MgCO3 är underkastad större svängningar, vidare material, i vilka en del av magnesium i dolomi- ten är ersatt med järn eller mangan. Sålunda är exempelvis dolomit med 54,5 % CaC03 och 42,8 % MgCO5 och dolomit med 3,9 % CaC03 och 89,22 MgC03 kända som naturliga mineral.By the term dolomite is meant not only a substance with the chemical composition CaCO 3 ° MgCO 5, but also materials in which the quantitative proportion of CaCO 3 and MgCO 3 is subject to larger fluctuations, further materials in which a part of magnesium in the dolomite is replaced by iron or manganese. Thus, for example, dolomite with 54.5% CaCO 3 and 42.8% MgCO 5 and dolomite with 3.9% CaCO 3 and 89.22 MgCO 3 are known as natural minerals.
Kornuppbyggnaden hos den brända dolomiten som användes enligt uppfinningen för framställning av massan bör vara så att 55 % har en korñstorlek under 0,09 mm, dvs har konsistensen av mjöl,och res- ten 65 % en normal kornuppbyggnad av 0,09-4 mm eller upp till 6 mm.The grain structure of the fired dolomite used according to the invention for the production of the pulp should be such that 55% has a grain size below 0.09 mm, ie has the consistency of flour, and the remaining 65% has a normal grain structure of 0.09-4 mm or up to 6 mm.
Naturligtvis kan det övre gränsvärdet hos kornstorleken ligga vid 2 eller 3 mm. Det är fördelaktigt att andelen av kqrnfraktionen under 0,09 mm är upp till 50 %.Of course, the upper limit of the grain size can be 2 or 3 mm. It is advantageous that the proportion of the grain fraction below 0.09 mm is up to 50%.
Det vid massorna enligt uppfinningen använda bindemedlet kan vara exempelvis torrt, malt natrium- eller kaliumsílikat, natrium- Det är fördelaktigt Binde- eller kaliumetafosfat eller en blandning därav. att bindemedlet tillsättes i en mängd av 2-6 viktprocent. medlet är företrädesvis en oorganisk, vattenlöslig substans. ställningen av massan enligt uppfinningen kan ske på vilket som helst känt arbetssätt för blandning av de torra beståndsdelarna, Fram- exempelvis kan först den brända dolomiten och det torra, malda bindemedlet blandas med varandra och sedan införes motsvarande mängd av den naturliga triglyceridoljan. Man kan emellertid göra så, att först blandas den brända dolomiten med triglyccridoljan, och sedan blandas denna blandning med det torra, malda bindemedlet, för att 10 ß pm pß ' 30 35 Ä0 o skänkoljor nämnas: f7713575-4 4 , triglyceridoljan företrädesvis skall avsättas på de brända dolomit- kornen, för att minska hydratiseringsbenägenheten hos den brända dolomiten. V 7 Det föredrages emellertid att tillsätta triglyceridoljan och blanda in denna före en eventuell triglyceridoljan inte skall absorberas i det högporösa pappersmjölet.The binder used in the compositions according to the invention may be, for example, dry, ground sodium or potassium silicate, sodium binder or potassium metaphosphate or a mixture thereof. that the binder is added in an amount of 2-6% by weight. the agent is preferably an inorganic, water-soluble substance. the positioning of the pulp according to the invention can take place in any known method of mixing the dry constituents. For example, first the burnt dolomite and the dry, ground binder can be mixed with each other and then the corresponding amount of the natural triglyceride oil is introduced. However, it is possible to first mix the burnt dolomite with the triglyceride oil, and then mix this mixture with the dry, ground binder, so that 10 β μm pß '30 o pouring oils are mentioned: f7713575-4 4, the triglyceride oil should preferably be deposited on the fired dolomite grains, to reduce the tendency to hydrate the burned dolomite. However, it is preferred to add the triglyceride oil and mix it in before any triglyceride oil is to be absorbed into the highly porous paper flour.
Det är fördelaktigt att tillsatsen av triglyceridoljan utföres tillsats av pappersmjöl, för att så, att triglyceridoljan, eventuellt efter värmning upp till en tem- peratur av 60°C för att minska viskositeten, sprutas med ett mun- -stycke på den i en blandare rörliga massan av fasta beståndsdelar, esä att man uppnår en så likformig fördelning som möjligt och man undviker en onödigt lång blandningstid.It is advantageous that the addition of the triglyceride oil is carried out with the addition of paper flour, so that the triglyceride oil, possibly after heating up to a temperature of 60 ° C to reduce the viscosity, is sprayed with a nozzle onto it in a mixer movable the mass of solid constituents, so as to achieve as uniform a distribution as possible and to avoid an unnecessarily long mixing time.
Vid pappersmjölet, vilket eventuellt tillsättes enligt uppfin- ningen, är det fråga om ett sönderdelat papper, som är sönderdelat till en maximal fiberlängd av 1-3 mm oçh torkat.In the case of the paper flour, which may be added according to the invention, it is a matter of a shredded paper, which is shredded to a maximum fiber length of 1-3 mm and dried.
Det har visat sig, att genom tillsatsen av pappersmjöl till massan enligt uppfinningen har tiden för upphettningen efter på- förandet av massan, exempelvis medelst en slungmaskín, minskats.It has been found that by adding paper flour to the pulp according to the invention, the time for heating after the pulp has been applied, for example by means of a sling machine, has been reduced.
Tillsatsen av sot, grafít eller mald koks åstadkommer ett gynn- sammare förhållande av massan gentemot kemiskt angrepp av smältan.The addition of soot, graphite or ground coke creates a more favorable ratio of the pulp to chemical attack by the melt.
När massan enligt uppfinningen föreligger i bearbetningsbar form kan den smulas och slungas medelst en slungmaskin. _ De enligt uppfinningen använda naturliga triglyceridoljorna består av de så kallade feta oljorna, dvs flytande fetter, som vä- sentligen består av blandade glycerinestrar av högre fettsyror med jämnt antal kolatomer, och de så kallade torkande oljorna, dvs fly- tande fetter med en förhållandevis hög andel av flerfaldigt omättade fettsyror. - Som exempel för sådana naturliga triglyceridoljor kan följande Sojaolja, blåst sojaolja, linolja, majsgroddolja, vallmoolja, rovolja, saflorolja, olivolja, bomullsfröolja, jordnöts- olja, träolja osv. Exempel på animaliska triglyceridoljor är de olika fiskoljorna, exempelvis síllolja, leverolja (torsk), sardin- olja, valolja och valravsolja§ Eventuellt kan dessa naturliga tri- glyceridoljor underkastas en förbehandling, exempelvis en blåsning, såsom vid blåst sojaolja. Eventuellt kan även en konventionell för- behandling av triglyceridoljan genomföras, exempelvis en behandling med blekjord eller ett luktborttagande medel.When the pulp according to the invention is in processable form, it can be crumbled and thrown by means of a sling machine. The natural triglyceride oils used according to the invention consist of the so-called fatty oils, i.e. liquid fats, which essentially consist of mixed glycerin esters of higher fatty acids with an even number of carbon atoms, and the so-called drying oils, i.e. liquid fats with a relatively high proportion of polyunsaturated fatty acids. As examples of such natural triglyceride oils, the following Soybean oil, blown soybean oil, linseed oil, corn germ oil, poppy oil, beet oil, safflower oil, olive oil, cottonseed oil, peanut oil, wood oil, etc. Examples of animal triglyceride oils are the various fish oils, for example herring oil, liver oil (cod), sardine oil, whale oil and horseradish oil§ These natural triglyceride oils may be subjected to a pre-treatment, for example a blowing, such as with blown soybean oil. Optionally, a conventional pretreatment of the triglyceride oil can also be carried out, for example a treatment with bleaching earth or an deodorant.
Av de ovan uppräknade exemplen räknas linolja, sojaolja och saflorolja till de torkandc oljorna. 7713575-4 5 Det har visat sig särskilt fördelaktigt vid massorna enligt uppfinningen att använda sojaolja och särskilt avsyrad och blekt sojaolja, som vid sin användning är miljövänlig beträffande rök- och luktutvecklíng. Sojaoljan har en flytpunkt av minus 10-16OC (enligt Ubbelohde-metoden) och en flampunkt av 28Z°C (DIN 7732, s 1).Of the examples listed above, linseed oil, soybean oil and safflower oil are among the drying oils. It has proved particularly advantageous in the pulps according to the invention to use soybean oil and in particular deacidified and bleached soybean oil, which in its use is environmentally friendly with regard to the development of smoke and odor. The soybean oil has a pour point of minus 10-16OC (according to the Ubbelohde method) and a flash point of 28Z ° C (DIN 7732, p. 1).
Naturligtvis kan i stället för en enda triglyceridolja även en blandning av sådana triglyceridoljor användas. Triglyceridoljor- na skall vara flytande vid en temperatur av 10°C.Of course, instead of a single triglyceride oil, a mixture of such triglyceride oils can also be used. The triglyceride oils must be liquid at a temperature of 10 ° C.
Uppfinningen skall nedan förklaras med hjälp av följande exem- pel: Exempel 1. 1000 kg av en blandning av bränd dolomit med en korn- storlek av 35 viktprocent mindre än 0,09 mm och 65 viktprocent mel- lan 0,09 och 3 mm införes i en till 180°C upphettad blandare. Där- efter påsprutades medelst ett munstycke 4 viktprocent, räknat pà_ färdig massa (vattenfri), av en i handeln vanligen förekommande soja- olja. Efter påsprutningen och inblandníngen av sojaoljan erhölls en massa med smulig konsistens. Till denna massa sattes som oorganiskt bindemedel 2,0 viktprocent finmalt natriumfosfat och 0,5 víktprocent finmalt natriumsilikat (kornstorlek mindre än 0,09 mm) och blandning- en fortsattes under ytterligare 4 minuter. Blandningstidens längd uppgick till 12 minuter. Denna massa infördes genom slungning på innerväggen av en råstâlsskänk som slitfoder. Blandningen kan även ske vid rumstemperatur i en kall blandare.The invention will be explained below by means of the following examples: Example 1. 1000 kg of a mixture of fired dolomite with a grain size of 35% by weight less than 0.09 mm and 65% by weight between 0.09 and 3 mm are introduced in a mixer heated to 180 ° C. Then, by means of a nozzle, 4% by weight, calculated on the finished pulp (anhydrous), was sprayed on a soybean oil commonly used in the trade. After the spraying and mixing of the soybean oil, a mass with a crumbly consistency was obtained. To this mass were added as inorganic binder 2.0% by weight of finely ground sodium phosphate and 0.5% by weight of finely ground sodium silicate (grain size less than 0.09 mm) and mixing was continued for a further 4 minutes. The length of the mixing time was 12 minutes. This mass was introduced by throwing on the inner wall of a crude steel ladle as wear lining. The mixing can also take place at room temperature in a cold mixer.
En andra del utav denna massa lagrades tre månader i ett väl tillslutet rum. Efter denna lagríngstid visade det sig att den lag- rade massan var lika bearbetbar som färskt framställd massa.A second part of this mass was stored for three months in a tightly closed room. After this storage time, it turned out that the stored pulp was as processable as freshly produced pulp.
Exempel 2. Arbetssättet enligt exempel 1 upprepades med det undan- taget, att i stället för den normala sojaoljan användes en blekt och avsyrad sojaolja.Example 2. The procedure of Example 1 was repeated with the exception that instead of the normal soybean oil a bleached and deacidified soybean oil was used.
Claims (8)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB5168376A GB1540306A (en) | 1976-12-10 | 1976-12-10 | Lining materials |
Publications (2)
Publication Number | Publication Date |
---|---|
SE7713575L SE7713575L (en) | 1978-06-11 |
SE423534B true SE423534B (en) | 1982-05-10 |
Family
ID=10460991
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE7713575A SE423534B (en) | 1976-12-10 | 1977-11-30 | MASS ON BASIS OF BREND, CORNED DOLOMIT AND WITH ORGANIC AND INORGANIC ADDITIVES FOR INFO LINING OF CONTAINERS FOR MOLD STEEL OR IRON |
Country Status (7)
Country | Link |
---|---|
AT (1) | AT368115B (en) |
BE (1) | BE861684A (en) |
DE (1) | DE2747636C2 (en) |
FR (1) | FR2373495A1 (en) |
GB (1) | GB1540306A (en) |
IT (1) | IT1090708B (en) |
SE (1) | SE423534B (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3119548C1 (en) * | 1981-05-16 | 1982-12-09 | Chamotte- u. Tonwerk Kurt Hagenburger, 6719 Hettenleidelheim | Wear layer of a metallurgical vessel lined with permanent lining with a layer not sintered towards the permanent lining |
GB8705736D0 (en) * | 1987-03-11 | 1987-04-15 | Jet Refractories Ltd | Refractory composition |
DE3842691A1 (en) * | 1988-12-19 | 1990-06-21 | Didier Werke Ag | Refractory mortars or refractory kits and their use |
CN113484217B (en) * | 2021-07-06 | 2024-06-18 | 西南石油大学 | Simulation experiment method for white cloud petrochemical removal process |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1257051B (en) * | 1964-09-23 | 1967-12-21 | Harbison Walker Refractories | Refractory pulp mixture |
CA949986A (en) * | 1970-06-10 | 1974-06-25 | George H. Williams | Refractories with a non-aqueous bond |
-
1976
- 1976-12-10 GB GB5168376A patent/GB1540306A/en not_active Expired
-
1977
- 1977-10-24 DE DE2747636A patent/DE2747636C2/en not_active Expired
- 1977-11-04 AT AT788077A patent/AT368115B/en not_active IP Right Cessation
- 1977-11-29 IT IT5199277A patent/IT1090708B/en active
- 1977-11-30 SE SE7713575A patent/SE423534B/en not_active IP Right Cessation
- 1977-12-09 BE BE183314A patent/BE861684A/en not_active IP Right Cessation
- 1977-12-09 FR FR7737269A patent/FR2373495A1/en active Granted
Also Published As
Publication number | Publication date |
---|---|
ATA788077A (en) | 1982-01-15 |
BE861684A (en) | 1978-03-31 |
AT368115B (en) | 1982-09-10 |
GB1540306A (en) | 1979-02-07 |
DE2747636C2 (en) | 1986-01-30 |
FR2373495A1 (en) | 1978-07-07 |
FR2373495B1 (en) | 1985-03-01 |
DE2747636A1 (en) | 1978-06-15 |
SE7713575L (en) | 1978-06-11 |
IT1090708B (en) | 1985-06-26 |
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