SE451949B - PROCEDURE FOR THE PREPARATION OF CURRENTS - Google Patents

PROCEDURE FOR THE PREPARATION OF CURRENTS

Info

Publication number
SE451949B
SE451949B SE8106735A SE8106735A SE451949B SE 451949 B SE451949 B SE 451949B SE 8106735 A SE8106735 A SE 8106735A SE 8106735 A SE8106735 A SE 8106735A SE 451949 B SE451949 B SE 451949B
Authority
SE
Sweden
Prior art keywords
powder
ferro
mixed
dry
weight
Prior art date
Application number
SE8106735A
Other languages
Swedish (sv)
Other versions
SE8106735L (en
Inventor
P Courvoisier
D Stadie
M Morgenstern
Original Assignee
Vft Verkaufsges Teer
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Vft Verkaufsges Teer filed Critical Vft Verkaufsges Teer
Publication of SE8106735L publication Critical patent/SE8106735L/en
Publication of SE451949B publication Critical patent/SE451949B/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/0025Adding carbon material
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/06Methods of shaping, e.g. pelletizing or briquetting
    • C10L5/10Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Geology (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Metallurgy (AREA)
  • Treatment Of Steel In Its Molten State (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Glanulating (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Ceramic Products (AREA)
  • Processing Of Solid Wastes (AREA)
  • Powder Metallurgy (AREA)

Description

451 949 2 Problemet enligt uppfinningen är att utveckla ett för- farande för framställning av uppkolningsmedel med hög skrym- täthet, vilka jämfört med jämförbara uppkolningsmedel uppvi- sar en förhöjd upplösningshastighet i stål- och järnsmältor. 451 949 2 The problem according to the invention is to develop a process for the production of high-bulk carburizing agents density, which compared to comparable carburizing agents increased dissolution rate in steel and iron melts.

Problemet löses enligt uppfinningen genom ett framställ- ningsförfarande för uppkolningsmedel genom kompaktering av kolpulver med bindemedel därigenom, att för ökning av form- kropparnas täthet blandningen försätts med en komponent med hög täthet med en korndiameter mindre än 2 mm.The problem is solved according to the invention by a preparation carbonation process by compacting carbon powder with binder in that, in order to increase the body density the mixture is added with a component with high density with a grain diameter less than 2 mm.

Som komponent med hög täthet kan användas metallpulver av legeringskomponenterna i det stål som skall framställas i varje särskilt fail såsom t.ex. Fe, cr, Ni, w, co, Mo, Mn, V eller Cu enskilt eller som blandning. Likaså är det möj- ligt att använda metallspån såsom t.ex. grågjutspân eller icke slaggbildande tillsatser såsom t.ex. ferromangan och ferrokisel.Metal powder can be used as a component with high density of the alloying components of the steel to be produced in each particular fail such as e.g. Fe, cr, Ni, w, co, Mo, Mn, V or Cu alone or as a mixture. It is also possible it is possible to use metal chips such as e.g. gray cast iron or non-slag-forming additives such as e.g. ferromanganese and ferrous silicon.

Som kolpulver kan användas pulvren av alla vanliga upp- kolningsmedel, vilka förutom en hög kolhalt endast innehål- ler små mängder skadliga beledsagande ämnen såsom svavel, väte, kväve och aska. Synnerligen fördelaktiga är emeller- tid pulver av kolmaterial med utpräglad grafitartad struktur såsom premiumkoks eller elektrografit.As carbon powder, the powders of all common carbonators, which, in addition to a high carbon content, contain only small amounts of harmful excipients such as sulfur, hydrogen, nitrogen and ash. Particularly advantageous, however, are time powder of carbon material with a pronounced graphite-like structure such as premium coke or electrographite.

Kompakteringen kan äga rum genom extrudering, brikette- ring eller pelletisering, till vilken i beroende av binde- medelsslaget en torkning eller kalcinering av formkropparna måste ansluta sig, för att halten flyktiga beståndsdelar eller väte skall minskas. Bindemedlet får icke öka andelen skadliga beledsagande element i uppkolningsmedlet.Compaction can take place by extrusion, briquetting pelletization, to which, depending on the binding means a drying or calcination of the shaped bodies must adhere, in order to the content of volatile constituents or hydrogen should be reduced. The binder must not increase the proportion harmful accompanying elements in the carburizing agent.

Enligt en speciell utföringsform av förfarandet blandas grafitpulver med en korndiameter 5 2 mm meä k0mP0flenten med hög täthet i förhållandet 1 : 10 till 10 : 1 under tillsats av!1 % hydroxietylcellulosa i torrt tillstånd och blandas med 10-25 % vatten i beroende av finheten hos komponenterna av fast material och mindre än 1 % av en bas av en alkali- eller jordalkalimetall eller ammoniakvatten, räknat på den torra blandningen. Denna nassa kompakteras därpå på i och för sig känt sätt till 3 till 15 mm stora presskroppar, som därpå torkas 5 till 20 tim vid 80 till 180°C. ä. .S7 s 451 949 I följande exempel skall uppfinningen förklaras närmare utan att den därigenom inskränks.According to a special embodiment of the process is mixed graphite powder with a grain diameter 5 2 mm with k0mP0 fl either with high density in the ratio 1:10 to 10: 1 during addition of 1% hydroxyethylcellulose in the dry state and mix with 10-25% water depending on the fineness of the components of solid material and less than 1% of a base of an alkali metal or alkaline earth metal or ammonia water, based on it dry the mixture. This nassa is then compacted on i and known method for 3 to 15 mm large compacts, which then dried for 5 to 20 hours at 80 to 180 ° C. ä. .S7 s 451 949 In the following examples, the invention will be explained in more detail without thereby being restricted.

Exempel 1 129 viktdelar grägjutspån med kornstorlekar under 2 mm blandas torrt med 69 viktdelar grafitpulver med kornstorlekar mellan 0 och 2 mm (analys i tabell 1) och 2 viktdelar hydroxi- etylcellulosa i 5 min. Efter tillsättning av 40 viktdelar vatten homogeniseras massan ytterligare 5 min. Därefter till- sätts 0,06 vikt-% 10%-ig natronlut. Efter ytterligare 2 min blandningstid bearbetas den färdiga massan i en strängpress med en 35 mm kraftig matris, som uppvisar cylindriska borr- ningar med 5 mm diameter, till presskroppar, som därpå torkas till en restfuktighet av mindre än 0,5 %. De torra presskrop- parna har en skrymtäthet av 1600 kg/m” och en kolhalt av 37 vikt-%.Example 1 129 parts by weight of turf shavings with grain sizes below 2 mm mix dry with 69 parts by weight of graphite powder with grain sizes between 0 and 2 mm (analysis in Table 1) and 2 parts by weight of hydroxy ethylcellulose for 5 min. After adding 40 parts by weight water, the mass is homogenized for another 5 minutes. Then add 0.06% by weight of 10% strength sodium hydroxide solution is added. After another 2 min mixing time, the finished mass is processed in an extruder with a 35 mm strong die, which has cylindrical bores 5 mm diameter, into compacts, which are then dried to a residual humidity of less than 0.5%. The dry compact the pairs have a bulk density of 1600 kg / m ”and a carbon content of 37 weight-%.

Exempel 2 Enligt exempel 1 framställs presskroppar ur_69 viktdelar grågjutspån och 129 viktdelar grafitpulver. De torkade press- kropparna har en skrymtäthet av 1100 kg/ma och en kolhalt av 70 vikt-%.Example 2 According to Example 1, compacts are prepared from 69 parts by weight gray castings and 129 parts by weight of graphite powder. The dried presses the bodies have a bulk density of 1100 kg / ma and a carbon content of 70% by weight.

Av de i tabell II angivna uppkolningsmedlen bestämdes under jämförbara betingelser den av stålsmältan upptagna kol- mängden som mått på upplösningshastigheten. Försöken genom- fördes i en 5 ton-induktionsugn. Man tillsatte i varje sär- skilt fall samma kolmängd av 30 kg. Provtagningen ägde rum varje gång efter 5, 10 och 15 min. Den till totalmängden hän- förda av smältan upptagna kolmängden (kolutbytet) visas i diagram.Of the carburizing agents listed in Table II were determined under comparable conditions, the carbon absorbed by the steel melt the amount as a measure of the dissolution rate. The experiments were carried out was placed in a 5 ton induction furnace. In each case, separate case the same amount of coal of 30 kg. The sampling took place each time after 5, 10 and 15 min. The total quantity carried the amount of carbon absorbed by the melt (carbon yield) is shown in diagrams.

Såsom framgår av diagrammet är upplösningshastigheten för de enligt uppfinningen framställda uppkol ingsmedlen liksom även deras kolutbyte efter 15 min högre ä vid det bästa kända uppkolningsmedlet grafit. 451 9119 4 Tabell I Analys av den finkorniga grafiten Kolhalt 99,2 % vattenhalt 0,013 % kvävehalt 0,05 % svavelhalt 0,02 % flyktigt 0,57 % aska - 0,15 % fuktighet 0,2 % Procenttalen avser vikt-%.As can be seen from the diagram, the dissolution rate is for the carburizing agents prepared according to the invention as well even their carbon yield after 15 min higher ä at best known carburizing agent graphite. 451 9119 4 Table I Analysis of the fine-grained graphite Carbon content 99.2% water content 0.013% nitrogen content 0.05% sulfur content 0.02% volatile 0.57% ash - 0.15% humidity 0.2% The percentages refer to% by weight.

Tabell II Uppkolningsmedel Kornstorlek [mm] A1 (enligt exempel 1) A2 (enligt exempel 2) grafit petroleumkoks beckkoks U1U1U1 Skrymtäthet [kg/m”] 1600 1100 800 soo 450 Kolhalt [vikt-%] 37 70 99 97 98 100' 90- 80- 70- 60~ 50- A0' 30- 20- 10' 451 949 Diagram Kolupptagning av olika uppkolningsmedel w / .,., / // ä* - / / b. / 3 / m 9-1 E. å + A1 X A2 O Gra_fit .I Ü Petroleumkoks _ A Beckkoks -------c- Reaktions tid [min] I 10 15Table II Carburizing agent Grain size [mm] A1 (according to Example 1) A2 (according to Example 2) graphite petroleum coke beckkoks U1U1U1 Bulk density [kg / m ”] 1600 1100 800 soo 450 Coal content [weight-%] 37 70 99 97 98 100 ' 90- 80- 70- 60 ~ 50- A0 ' 30- 20- 10 ' 451 949 Chart Carbon uptake of various carburizing agents w / .,., / // ä * - / / b. / 3 / m 9-1 E. å + A1 X A2 O Gra_fit .IN Ü Petroleum coke _ A Beckkoks ------- c- Reaction time [min] IN 10 15

Claims (1)

än "A xD 4> vb CP Patentkrav Förfarande för framställning av uppkolningsmedel med förhöjd upplösningshastighet genom kompaktering av kolpulver med ett bindemedel) k ä n n e t e c k n a t av att grafitpul- ver med en maximal korndiameter av 2 mm blandas torrt med rena metallpulver av legeringskomponenterna i stål, finför-' delade metallspån såsom t.ex. grågöt och/eller pulver av legeringar av de vid järn- och stålframställning brukliga tunga tillsatsämnena såsom t.ex. ferromangan och ferrokisel i förhållandet 1:10 till 10:1 under tillsats av 1% hydroxi- etylcellulosa, blandas med 10-25% vatten och mindre än 1% av en bas av en alkali- eller jordalkalimetall eller ammo- niakvatten, räknat på den torra blandningen, och därpå kom- pakteras på i och för sig känt sätt till 3 till 15 mm stora: formkroppar, som därpå torkas vid 80 till 180°C 5 till 20 timmar. .elProcess for the production of carburizing agents with increased dissolution rate by compacting carbon powder with a binder) characterized in that graphite powder having a maximum grain diameter of 2 mm is dry-mixed with pure metal powders of the steel alloy components, finely divided metal chips such as, for example, gray ingot and / or powder of alloys of the heavy additives customary in iron and steel production, such as ferro-manganese and ferro-silicon in the ratio 1:10 to 10: 1 with the addition of 1% hydroxy ethylcellulose, mixed with 10-25% water and less than 1% of a base of an alkali or alkaline earth metal or ammonia water, based on the dry mixture, and then compacted in a manner known per se to 3 to 15 mm large: shaped bodies, which are then dried at 80 to 180 ° C for 5 to 20 hours
SE8106735A 1981-01-16 1981-11-12 PROCEDURE FOR THE PREPARATION OF CURRENTS SE451949B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE3101168A DE3101168C2 (en) 1981-01-16 1981-01-16 "Process for the production of carburizing agents with increased dissolution rate"

Publications (2)

Publication Number Publication Date
SE8106735L SE8106735L (en) 1982-07-17
SE451949B true SE451949B (en) 1987-11-09

Family

ID=6122709

Family Applications (1)

Application Number Title Priority Date Filing Date
SE8106735A SE451949B (en) 1981-01-16 1981-11-12 PROCEDURE FOR THE PREPARATION OF CURRENTS

Country Status (8)

Country Link
JP (1) JPS57140635A (en)
BE (1) BE891344A (en)
DE (1) DE3101168C2 (en)
FR (1) FR2498202A1 (en)
GB (1) GB2091233B (en)
IT (1) IT1172155B (en)
NL (1) NL8105217A (en)
SE (1) SE451949B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6089510A (en) * 1983-10-19 1985-05-20 Mihato Kogyosho:Kk Recarburizer for iron and steel
JPS60169512A (en) * 1984-02-13 1985-09-03 Nippon Kokan Kk <Nkk> Carburizer for metallurgy
FI126583B (en) * 2014-03-31 2017-02-28 Outotec Finland Oy Process and carrier for transporting reducing agent such as coke into a metallurgical furnace and production process for the carrier
JP6622755B2 (en) * 2017-06-09 2019-12-18 株式会社サンアール Carburizing agent for steel making and steel making method

Also Published As

Publication number Publication date
BE891344A (en) 1982-03-31
SE8106735L (en) 1982-07-17
JPS57140635A (en) 1982-08-31
JPH0245685B2 (en) 1990-10-11
FR2498202B3 (en) 1984-09-07
GB2091233B (en) 1984-12-19
IT8149915A0 (en) 1981-12-15
DE3101168C2 (en) 1984-07-26
NL8105217A (en) 1982-08-16
DE3101168A1 (en) 1982-08-05
FR2498202A1 (en) 1982-07-23
GB2091233A (en) 1982-07-28
IT1172155B (en) 1987-06-18

Similar Documents

Publication Publication Date Title
JPH0210201B2 (en)
KR102493172B1 (en) Cast iron inoculants and methods of producing cast iron inoculants
JPH0432122B2 (en)
US4123257A (en) Method of treating a plating sludge
US4504441A (en) Method of preventing segregation of metal powders
CA1204596A (en) Refining agent of molten metal and methods for producing the same
SE451949B (en) PROCEDURE FOR THE PREPARATION OF CURRENTS
JP2002501440A (en) Prealloyed copper-containing powder and its use in the production of diamond tools
ES366038A1 (en) Alloy, atomized and homogeneous dust, based on iron, of low carbon content, used primarily for the manufacture of sintered, temperable, high strength steels. (Machine-translation by Google Translate, not legally binding)
JP6993646B2 (en) Inoculant for cast iron
US4286987A (en) Composition for iron powder compact infiltrant
CA3134580C (en) Mixed powder for powder metallurgy
DE3015079A1 (en) METHOD FOR DESULFURING MELTED STEEL OR MELTED IRON
RU2121510C1 (en) Method of modifying cast irons and steels
US4348230A (en) Briquettes of silicon and ferrosilicon dust
PL183768B1 (en) Desulphurising calcium carbide mixture
SU398670A1 (en) 1 P&#39;G &#39;&#34;&#39; METAL-CERAMIC HARD ALLOY ^^ * ^ = &#39;
JPS55145149A (en) Sintered iron alloy having both strength and toughness
AT166213B (en) Additive for the introduction of alloying elements into molten iron or steel
US4035183A (en) Method for making aluminum-containing ferroalloy
JPH0269353A (en) Carbon material for sliding current collection
SU1747503A1 (en) Charge for melting low-phosphorus manganese slag
CA1153157A (en) Briquettes of silicon and ferrosilicon dust
CN116622936A (en) Ferromanganese composite additive and preparation method thereof
JP2005068483A (en) Production method for sintered compact of mn-based high-damping alloy

Legal Events

Date Code Title Description
NAL Patent in force

Ref document number: 8106735-7

Format of ref document f/p: F

NUG Patent has lapsed

Ref document number: 8106735-7

Format of ref document f/p: F