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
  • C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
  • C21C5/56—Manufacture of steel by other methods
  • C21C5/562—Manufacture of steel by other methods starting from scrap
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P10/00—Technologies related to metal processing
  • Y02P10/20—Recycling

Definitions

• the superior technology of the important modern metal industry is the processing of large metals, which is growing in size.
• the main means of production of steel have become ⁇ their purpose is acid-based.
• experience in the process is processed up to 30% of the metal scrap.
• the means of production of the metal have ceased from the metal, which contains 100 small metals.
• ⁇ y ⁇ e ⁇ ssh ⁇ ua ⁇ atsii ⁇ nve ⁇ e ⁇ v is ⁇ lzuyuschi ⁇ ⁇ ve ⁇ duyu shi ⁇ u, l ⁇ azal, br ch ⁇ s ⁇ avnenyayu with ⁇ lassiches ⁇ im s ⁇ s ⁇ b ⁇ m ⁇ izv ⁇ ds ⁇ va s ⁇ ali znachi ⁇ eln ⁇ snyazilas ⁇ izv ⁇ dd ⁇ el- 20 n ⁇ s ⁇ ⁇ nve ⁇ e ⁇ a, umeny ⁇ ilas weight shi ⁇ y, zag ⁇ uzhaem ⁇ y in ⁇ nve ⁇ e ⁇ , ⁇ es ⁇ decreased ⁇ e ⁇ itsien ⁇ is ⁇ lz ⁇ vayaiya ⁇ ab ⁇ cheg ⁇ ⁇ bema ⁇ yave ⁇ e ⁇ v.
• the mass of hard disk loaded in the console decreased by 30-50%. This is due to the need to load a metal box, which has 25 more low bulk density (often at 1.0 t / m).
• the process has been known to have come from an acid supply from solid metal carriers (see the patent for 4198230, which is onwards since 21 October 2014).
• the solid energy source is loaded with a single appliance, then it is heated and melted in a non-oxidizing atmosphere.
• Downloading one-sided version with one unit, which has a low bulk supply, is used only by using the free mode of operation. This reduces the productivity of the converter by 30-50%. Otherwise, in connection with the download of the whole band, one - 2 - there is no reason for equal heating of it throughout the entire thickness.
• the basic task of the invention is to develop a method of working in an oxygen-inverted system.
• the left share of the busbar constitutes 30 to 35% of the mass of the consumer, which is required by the consumer, and that of 50 to 60 of the mass of the consumer, 5% of the consumer, ⁇ s- ⁇ avshi ⁇ sya e -n ⁇ si ⁇ eley and ⁇ e ⁇ ya ⁇ tsiya - ⁇ s ⁇ avsheesya ⁇ zhches ⁇ v ⁇ ⁇ e -n ⁇ si ⁇ eley and ⁇ ve ⁇ d ⁇ g ⁇ ene ⁇ g ⁇ n ⁇ si ⁇ eln, ⁇ i e ⁇ m nag ⁇ ev ⁇ e ⁇ v ⁇ y l ⁇ 'tion shi ⁇ y ⁇ susches ⁇ vlyayu ⁇ d ⁇ ⁇ las ⁇ ichn ⁇ g ⁇ s ⁇ s ⁇ yaniya
• a variant of the invention of the invention means that the years of service in the case of an inverted equipment are in the process of being loaded, which consumes 30%
• the bottom of the converter is equipped with iron oxides, converting to heating of the ⁇ -carriers, and also reduces the intense heating of the lower layers.
• the first portion of the sheet contains solid metallic materials in good condition with 50 to 60 masses that are required to be melted.
• the heat required reduces the coefficient of utilization of the heat of the energy and, consequently, the energy consumption Uvezhchesh ⁇ e mass ⁇ e, -n ⁇ si ⁇ ele ⁇ in le ⁇ v ⁇ y l ⁇ tsii shi ⁇ y b ⁇ lshe 60 ⁇ mass ⁇ ebuem ⁇ y on llav ⁇ u, ⁇ sl ⁇ zhnya- e ⁇ l ⁇ tsess yaag ⁇ eva, ⁇ s ⁇ l ⁇ u ⁇ ve ⁇ dye me ⁇ alliches ⁇ ie ⁇ e -n ⁇ si ⁇ ezh in chas ⁇ n ⁇ s ⁇ i me ⁇ all ⁇ m having neb ⁇ lshuyu nasy ⁇ nuyu ⁇ l ⁇ n ⁇ s ⁇ , zani
• the batch After downloading the converter, the batch begins to dispense in the converter, as a result of the mixture the mixture is discharged.
• the ejector I use a combined combination of blowing: top and bottom.
• the maximum productivity of the unit is achieved when the specific output of the oxidizer is lower and lower, equal to: ( ⁇ , 5-2.0). ⁇ ⁇ m case, eszh - 6 - the output of the oxidizer is more than two times higher than the discharge of the oxidizer from below, the efficiency of the converter is reduced, due to the increase of the amplification. 5 At the same time, there is a decrease in the stability of the event, in the upper part of the skin and the dusher. The percolation of the exhaust gas from the bottom is caused by an increase in the acidity of the carrier in the lower part of the burner due to the delay of the heating charge.
• Heating the cassettes makes it possible for the classy community of the ⁇ -carriers to be quick and easy to visualize at the beginning of the download in the crate. After being blown out, from 15 to 25 from the mass of the oxidizer required for melting it
• the yield is 48 to 52% of the total mass of the remaining carriers and 19.2 to 26% of the total mass required by the head of the public.
• the burner After downloading the second one, to reduce the loss of the burner, the burner will reduce the burner. - 7 - At the same time, the specific consumption of the oxidizer and the above are equal to I: (0, 9 * 1), Further reduction of the waste of the oxidizing agent is a result of a decrease in the consumption of waste. At the same time, the share of the busbar - the remaining good metal and solid energy - it is free to download and consume 15%
• the specific oxygen consumption of the light is 1.46 m / mia
• the specific acidity of the gas is 1, 54 m / min
• the specific gas rate of the bottom gas and the upper is 2 0.52 m / m.
• the first portion of the cake contains 502 kg of lota (5.5% of the mass) 21.0 kg of antifreeze (35% of the mass). Separate discharge of acid from the bottom - 1.00 m / min, above - 1.75 m (reduction of specific emissions of 1: 1.75). Specific
• the oxygen consumption for the combustion of natural gas is 45% of the mass more commercially available. 5 Approx. to the master of metal.
• the specific discharge of the waste is 10 ⁇ u - 1.46 m min, the load is 1.54 m / min (the specific discharge is 1: 0.95). m / min
• the potency of the melts was 40 minutes.
• the carbon content in the experience is 0.09%.
• the acid base in the store is 120m.
• the productivity of the condenser is 1220 kg / h. DIRECTIONS 4.
• the first one contains 456 kg of metal
• the first part of the mix contains 548 kg of solid metal (metal), which makes up 60% of the mass of the economy, and 19, 5% of the mass is 32%.
• the cleaned acid flow from the bottom is 1.75 m / min, and above - 1.0 m / min.
• the specific consumption of oxygen after loading the second curtain is 1.46 m / min, from the bottom - 1. 54 m / m.
• the melting pot lasted 41.6 minutes.
• the carbon content in the experience is 0.06.
• the best liquid experience is 820 kg.
• the productivity of the conveyor is 1200 kg / h. ⁇ . 6.
• the first share of the busbar contains 502 kg of foreign metals, which makes up 55% of the mass of 35 foreign carriers, and 19.5% of the body, excluding 32% of the body.
• the specific acid yield from below is 1, 2 m / m, ev Foodr ⁇ réelle - ⁇ , .8 m / min. ⁇ - - 12 - solution of specific acid consumption from below to above 1: 1.5.
• the specific output of fresh gas is above 0.69 m / min, from the bottom -0.375 m / min.
• a good discharge after loading the second door is 1.46 m / min, from the bottom - 1.54 m / min.
• the specific oxygen concentration after the load on the second side of the church is 1.46 m / mia, from the bottom - 5 m / glia.
• the first mixture contains 502 kg of solid metal and zinc carriers, which makes up 55% of the mass
• both 19.5 and ayatratsit which account for 32.5% of the total mass of the foreign energy carrier.
• the bottom discharge - 1.0 m / min, over-G, 75 m / min. 0- the ratio of specific oxygen consumption from below and above 1: 1.75.
• the specific output of the gas above is 0.69 m, from the bottom -0.375 m / s.
• the first version of the circuit board contains 502 kg of hard metal
• Example II Further, the lead is kept, as it is lysed in Example I.
• the durability of lavks is 40.5 minutes.
• the maintenance of the experience is 0.06.
• the acid flow to the melting site is 122 m.
• the productivity of the unit is 1209 kg / h.

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• Engineering & Computer Science (AREA)
• Chemical & Material Sciences (AREA)
• Manufacturing & Machinery (AREA)
• Materials Engineering (AREA)
• Metallurgy (AREA)
• Organic Chemistry (AREA)
• Carbon Steel Or Casting Steel Manufacturing (AREA)
• Treatment Of Steel In Its Molten State (AREA)
• Manufacture And Refinement Of Metals (AREA)

Priority Applications (8)

Applications Claiming Priority (1)

Publications (1)

Family

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Family Applications (1)

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Cited By (1)

Citations (3)

• 1985
  • 1985-12-19 DD DD85284777A patent/DD253645A5/de not_active IP Right Cessation
  • 1985-12-23 WO PCT/SU1985/000104 patent/WO1987003914A1/ru active Application Filing
  • 1985-12-23 GB GB8717488A patent/GB2191786B/en not_active Expired - Lifetime
  • 1985-12-23 AT AT0909385A patent/AT393693B/de not_active IP Right Cessation
  • 1985-12-23 BR BR8507321A patent/BR8507321A/pt unknown
  • 1985-12-23 DE DE19853590891 patent/DE3590891T1/de not_active Withdrawn
  • 1985-12-23 HU HU852766D patent/HU198968B/hu not_active IP Right Cessation
  • 1985-12-23 JP JP86501531A patent/JPS63501879A/ja active Pending

Patent Citations (3)

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