SE451949B - PROCEDURE FOR THE PREPARATION OF CURRENTS - Google Patents
PROCEDURE FOR THE PREPARATION OF CURRENTSInfo
- 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
Links
- 238000000034 method Methods 0.000 title claims description 6
- 238000002360 preparation method Methods 0.000 title description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 20
- 238000005255 carburizing Methods 0.000 claims description 9
- 239000003795 chemical substances by application Substances 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 5
- 238000004090 dissolution Methods 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 229920000663 Hydroxyethyl cellulose Polymers 0.000 claims description 3
- 239000004354 Hydroxyethyl cellulose Substances 0.000 claims description 3
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 3
- 239000011230 binding agent Substances 0.000 claims description 3
- 229940071826 hydroxyethyl cellulose Drugs 0.000 claims description 3
- 235000019447 hydroxyethyl cellulose Nutrition 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 2
- 229910000616 Ferromanganese Inorganic materials 0.000 claims description 2
- 239000000654 additive Substances 0.000 claims description 2
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 2
- 239000002585 base Substances 0.000 claims description 2
- DALUDRGQOYMVLD-UHFFFAOYSA-N iron manganese Chemical compound [Mn].[Fe] DALUDRGQOYMVLD-UHFFFAOYSA-N 0.000 claims description 2
- 229910000851 Alloy steel Inorganic materials 0.000 claims 1
- 229910000519 Ferrosilicon Inorganic materials 0.000 claims 1
- 239000003513 alkali Substances 0.000 claims 1
- 229910045601 alloy Inorganic materials 0.000 claims 1
- 239000000956 alloy Substances 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000002956 ash Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000002006 petroleum coke Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 229910001060 Gray iron Inorganic materials 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 241001229135 Nassa Species 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 239000000546 pharmaceutical excipient Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000000161 steel melt Substances 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/0025—Adding carbon material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS 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
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
- C10L5/10—Methods 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)
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)
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 |
-
1981
- 1981-01-16 DE DE3101168A patent/DE3101168C2/en not_active Expired
- 1981-11-12 SE SE8106735A patent/SE451949B/en not_active IP Right Cessation
- 1981-11-18 NL NL8105217A patent/NL8105217A/en not_active Application Discontinuation
- 1981-11-23 GB GB8135181A patent/GB2091233B/en not_active Expired
- 1981-12-03 BE BE0/206734A patent/BE891344A/en not_active IP Right Cessation
- 1981-12-14 FR FR8123312A patent/FR2498202A1/en active Granted
- 1981-12-15 IT IT49915/81A patent/IT1172155B/en active
-
1982
- 1982-01-13 JP JP57002919A patent/JPS57140635A/en active Granted
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 |
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