Donetsk National Technical Univercity - Rutkovskaya Nadezhda: Abstract of master's work

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Rutkovskaya Nadezhda Leonidovna

Theme:

 

Analysis of resource saving and improvements of technology of utilization of secondary resources of oxygen-converter manufacture of steel at the metallurgical enterprises of Ukraine 

Advisor:

  Candidate of technical science of sub-faculty OTP Peristyi M.M.


Abstract of master's work


INTRODUCTION

Topicality of theme

Last years in connection with education and accumulation of a significant amount of a waste and necessity of the decision of environmental problems value of their utilization is increase. Prevailing in steel-smelting manufacture oxygen-converter process develops in a direction material and energy economy.

In the waste of converter manufacture except metals among nonmetallic resources: secondary fire-resistant materials, slags, sludges and a dust. Special attention it is necessary to give sludges converter manufacture, which are investigated less other secondary resources. Besides sludges converter manufactures are most hard utilization. Difficulties in utilization of these sludges arise because of the raised maintenance in them of nonferrous metals, especially zinc and the lead, which maintenance frequently exceeds in scarce zinc and lead ores, which in Ukraine practically are not present.

  The purposes

  • to develop actions for decrease in negative influence of a waste of converter manufacture on environment;

  • to develop resource economy technology for converter repartition;

  • to improve available schemes of preparation of secondary material resources of converter manufacture to utilization, having provided with that fuller utilization of the given waste;

  • to prove economic efficiency from introduction resource economy technologies and use of essentially new schemes of preparation of a waste to utilization.

    Tasks

  • to consider sources and metallurgical value of a secondary material waste of converter manufacture;

  • to consider process of formation of production wastes;

  • to reveal dependence of quantity of a formed waste on a kind of used treatment facilities and applied technology of melt converter steel;

  • to formulate the basic directions of increase of ecological safety of converter manufacture;

  • to estimate economic benefit at transition converter manufactures on more perfect technology production of  steel and utilization of  wastes;

  • to state a complex estimation of the developed technology production to converter steel and utilization of production wastes.

Scientific novelty of work consists that earlier examined the questions, concerning utilization of a waste of steel-smelting manufacture as a whole. The given work considers resource economy technologies and ways of utilization of a waste of converter manufacture.

Practical value of work consists that the considered technological actions ecologically and economically expediently to introduce at the metallurgical enterprises of Ukraine thereby raising ecological safety of converter manufacture.

ANALYSIS OF RESOURCE SAVING AND IMPROVEMENT OF TECHNOLOGY OF UTILIZATION OF SECONDARY RESOURCES OF OXYGEN-CONVERTER MANUFACTURE OF STEEL AT THE METALLURGICAL ENTERPRISES OF UKRAINE

 One of decrease ways of material capacity production and economy of a source of raw materials is increase of level of use of production wastes which are inevitably formed both in sphere of production of goods, and in consumption sphere. The factory floor experience shows, that use of a waste converter manufacture is technically realizable and economic.

Despite spent job level of use of secondary material resources still is insufficiently high for the various reasons, but first of all in the absence of objects of the corresponding preparation, not enough the developed technologies, absence of the systematized literature and first of all help character.

Now the basic method of use sludge gas purifications of converters is their additive to agglomeration mix.

For utilization on agglomeration factory converter sludge must be preliminary dehydrated. Now the most rational scheme of dehydration is the scheme providing a condensation sludge of a pulp in radial thickeners, filtering on vacuum-filters and drying in siccative drums. At presence at the enterprise in enough of a dry waste (lime, agglomerate elimination etc.) it is possible to replace drying with mixing sludges with this waste.

The cheme of utilization sludges of converter manufaction

 

Sometimes converter sludge on agglomeration factory it is used without mechanical and thermal dehydration, it is direct in the form of a dense pulp after a condensation (300—700 g/l) in radial thickeners or in hydrocyclones and radial thickeners. Sludge in the sprayed kind moves in a mixing drum of agglomeration factory. Advantage of such way — low capital expenses and working costs. A necessary condition of successful operation of schemes is the reliable automatic dosage of sludge in a mixing drum depending on humidity mix and density condensed sludge.

For returning of sludge of gas purifications in the converter it is necessary its preliminary fragmentation. There are also methods of fragmentation, developed specially for converter sludges.

The fragmentation of sludge for converter manufacture it is applied in the following scheme. Gas purification sewage converter shops arrives in a trap where the largest particles are besieged. Having poured traps gets through the mixing chamber to a radial thickener. In the mixing chamber limy milk also moves. Plums of a radial thickener goes on a reuse to gas purification system, and condensed sludge - on a funnel feeding drum-type vacuum-filter. 28–32 % dehydrated to humidity sludge from the vacuum-filter and the large fraction caught in a trap, the tape conveyor move in a feeder of the rotating tubular furnace where are carried out drying of sludge, it balling and roasting of pellets at temperature 1150˚С. The pellets are cooled in cooling drum and are loaded into the railway car.

The prospective volume of use of sludge of converter gas purifications is utilized as the additive to agglomeration mix. For returning the sludge in converter manufacture it is necessary to develop, leaning against foreign experience, the effective scheme of preparation sludges, which would allow to receive a conditioned material in a kind of pellets or briquettes. Such scheme would allow to remove a problem of without zinc-plating of converter sludges for which till now there is no cheap technology of removal of zinc.

In another way utilizations ferriferous dusts and sludges of converter manufacture their inclusion in charge makeup is by manufacture of cement and other building materials, and also of some paints, for example, ochre and dyes.

Pulp and dehydrated sludge can use only on agglomeration factory (or factories on manufacture of pellets) as only in mix these manufactures it is possible to submit the humidified materials. In particular, the pulp can be submitted to mixing drums of these manufactures. Thus, as the requirement for moisture on agglomeration factory can exceed quantity of moisture arriving with a pulp, sometimes it is necessary even to add moisture in the amalgamator. However because of increase in expenses of a pas transportation is expedient for using this method only at a close arrangement in territory of the enterprise steel-smelting and agglomeration shops.

One of perspective methods of preparation of sludges to utilization is drying of the sprayed pulp in a stream (preferably) heated gases. At method test good results, however a method yet have been received has not found introduction in manufacture. This method is expedient for combining with giving received at its use dense (pastelike) sludges in mixers (drums-pelletizers) of agglomeration factory: sludge with moisture load 40 – 50 % (on weight) are sprayed by evolvent atomizers that provides uniform humidifying of mix. Last way is attractive the simplicity, however there are the difficulties connected with a dosage of sludges. For the purpose of increase of reliability of the specified way careful study of a method of a dosage and processing of assemblages of the dosing device are made.

Recently in connection with an intensification oxygen-converter process carrying out from the unit with gases of large fractions of a dust departing from it has amplified. Therefore it is necessary to spend classification of sewage before their receipt on the basic constructions. Radial sediment bowls are most widely applied to dehydration of converter sludges, for example, by diameter 30 m, which at specific load 2 m3 / (m2·h) allow to receive the clarified water with the residual maintenance of a suspension which are not exceeding 200 mg/l.

The preparation of converter sludges to utilization in agglomeration mix is expedient for making together with a waste containing iron. In a case when at the metallurgical enterprise are available martin and converter manufacture, it is the most expedient to make their joint preparation sludges to utilization.

The converter slagsб from which even metal is rather full taken, contain a number of valuable elements. They are rather rational for using in metallurgy, for example in agglomeration and blast-furnace productions and foundry manufacture, as a gumboil instead of limestone.

Now in our country and abroad converter slags process mainly in a firm status. Them split up, subject to rough selection of metal, sometimes again split up and separate. Way of processing widely tested and introduced in manufacture converter in a liquid status is not present till now some slags. Only at separate factories test semiindustrial or industrial granulation installations.

Depending on time of stay in bowls (from the moment of filling to canting) and volume their slag can arrive for processing in liquid or in a firm status. It is shown, what even later 2 h after filling to 80 % a liquid melt in a bowl remains in a liquid status.

From steel-smelting slags for use as a turnaround product in metallurgical repartition the greatest interest represents slag of converter manufacture. Converter slag incorporates such components valuable to metallurgical repartition as CaO, MgO, MnO, CaF2, Al2O3, FeO. Besides, in converter slag of current manufacture contains from 3 to 9 % of iron in a kind of «prill».

Basicity of final converter slag is at level 2,8 – 3,5, and maintenance СаО and in converter slag is in limestone approximately at one level (46 – 52 %). It allows using converter slag instead of limestone in furnaces and cupola-furnaces foundry shops.

As show thermodynamic calculations, heat expenses on dissociation limestone and reception of slag liquid melt approximately in 1,5 - 1,7 times more than at application of converter slag.

If to consider also that limestone the natural material, which stocks, finally, are limited, and converter slag is a manufacture withdrawal, advantage of its use in metallurgical repartition instead of limestone undoubtedly.

Processing converter slag of current manufacture is made on a stationary site of conversion slag with use of a way of thermocrushing. Separate processing of liquid slag and ladle leavings is provided. Technology of primary processing converter slags on a stationary site concerns:

- slag transportation on a site;

- slag plums in holes-trenches;

- movement slag carriage in section for knockout ladle leavings and knockout of the last;

- thermocrushing and cooling of slag by water;

- working out of the cooled down slag by a dredge;

- extraction of the  large-sized scrap metal;

- transportation of the cooled down slag by motor transport on a crushing-and-sorting site.

On a stationary site of conversion liquid slag only from converters goes. Plums of slag from converters it is made in the pure, prepared bowls without fight of a brick, industrial dust, scrap metal and other waste. The bowls filled with slag in as much as possible short terms (that the quantity of liquid slag in a bowl by the moment of canting was not less than 50 %) arrive on a stationary site.

The technology of thermocrushing switches on leyel-by-leyel pouring of liquid slag to depth of a layer of slag 1,5 – 2 m in special sections, an irrigation water with the expense 0,1 – 0,15 m3/th on 1m2 the areas after canting of every portion slag. In holes-sections the thermocrushed slag is developed by a dredge and shipped or is direct in auto dump-body trucks or is formed in a temporary stack. The fractional structure the thermocrushed slag supposes direct loading of slag in blast furnaces without additional crushing.

The thermocrushed converter slag can be used in mix blast furnaces and cupola furnace; the crushed ladle leavings can be used in mix blast furnaces, and also after crushing on the crushing-and-sorting plant -200 – in agglomeration  mix (fraction <10 mm).

It is shipped to consumers thermocrushed slag, on a chemical compound should have СаО not less than 45 %, SiO2 no more than 20 %, Fecom not less than 10 %, humidity no more than 7 %. The maintenance of extraneous impurity should not exceed 5 %.

The operational experience of Enakievsky metallurgical plant shows that in agglomeration mix it is possible to use converter slag of fraction of 0-10 mm with the expense of agglomerate of 30-50 kg/t without deterioration of technical and economic indicators of work agglomeration factory. To blast furnaces and cupola furnaces of foundry shops goes converter slag of fraction of 10-40 mm. At use converter slag in martin furnaces instead of limestone at the expense of earlier formation slag fuller removal of phosphorus in slag is observed.

SUMMARY

Thus, from the economic and ecological points of view the use highly effective gas-purifying systems with the organization full and complex utilization of waste will allow to increase technical and economic indicators of manufacture of steel and considerably to lower environmental contamination level. Use of converter slag instead of limestone in metallurgical repartition very favorably as will allow to lower the expense natural mix materials and coke and also to reduce emissions of carbonic gas and a dust. The organization of the processes supervising movement of zinc in metallurgical processes, will allow to lower essentially negative influence of zinc on technology of domain manufacture at utilization dust, which to fly out at the steel-smelting units, and also it is rational to solve a question of reception of additional quantity of scarce zinc from a ferrous metallurgy waste. The complex approach to the decision of environmental problems converter manufactures will allow improving essentially ecological conditions at metallurgical combines of the country.

LITERATURE

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