CN1004707B - Coal-oxygen composite blowing process for oxygen converter - Google Patents
Coal-oxygen composite blowing process for oxygen converter Download PDFInfo
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- CN1004707B CN1004707B CN87100551.4A CN87100551A CN1004707B CN 1004707 B CN1004707 B CN 1004707B CN 87100551 A CN87100551 A CN 87100551A CN 1004707 B CN1004707 B CN 1004707B
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- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 88
- 239000001301 oxygen Substances 0.000 title claims abstract description 88
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 77
- 238000000034 method Methods 0.000 title claims abstract description 33
- 238000007664 blowing Methods 0.000 title claims abstract description 32
- 239000002131 composite material Substances 0.000 title claims abstract description 11
- 239000003245 coal Substances 0.000 claims abstract description 67
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 49
- 239000010959 steel Substances 0.000 claims abstract description 49
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 19
- 239000007921 spray Substances 0.000 claims abstract description 15
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 14
- 238000003723 Smelting Methods 0.000 claims abstract description 13
- 238000005516 engineering process Methods 0.000 claims description 31
- 239000002817 coal dust Substances 0.000 claims description 30
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 21
- 239000000843 powder Substances 0.000 claims description 19
- 238000002347 injection Methods 0.000 claims description 16
- 239000007924 injection Substances 0.000 claims description 16
- 229940098458 powder spray Drugs 0.000 claims description 12
- 239000007789 gas Substances 0.000 claims description 11
- 229910052757 nitrogen Inorganic materials 0.000 claims description 11
- 238000009628 steelmaking Methods 0.000 claims description 7
- OLBVUFHMDRJKTK-UHFFFAOYSA-N [N].[O] Chemical compound [N].[O] OLBVUFHMDRJKTK-UHFFFAOYSA-N 0.000 claims description 6
- 238000002485 combustion reaction Methods 0.000 claims description 6
- 238000005507 spraying Methods 0.000 claims description 6
- 239000012159 carrier gas Substances 0.000 claims description 4
- 229910052698 phosphorus Inorganic materials 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims 2
- 239000002893 slag Substances 0.000 abstract description 29
- 230000000694 effects Effects 0.000 abstract description 6
- 238000011084 recovery Methods 0.000 abstract description 4
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 abstract description 3
- 238000006477 desulfuration reaction Methods 0.000 abstract description 3
- 229910052748 manganese Inorganic materials 0.000 abstract description 3
- 239000011572 manganese Substances 0.000 abstract description 3
- 230000001105 regulatory effect Effects 0.000 abstract description 3
- 238000003756 stirring Methods 0.000 abstract description 3
- 230000023556 desulfurization Effects 0.000 abstract description 2
- 238000005261 decarburization Methods 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 16
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 10
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 9
- 239000005864 Sulphur Substances 0.000 description 9
- 241000209094 Oryza Species 0.000 description 8
- 235000007164 Oryza sativa Nutrition 0.000 description 8
- 229910052742 iron Inorganic materials 0.000 description 8
- 235000009566 rice Nutrition 0.000 description 8
- 208000034953 Twin anemia-polycythemia sequence Diseases 0.000 description 6
- 238000005192 partition Methods 0.000 description 6
- 238000002844 melting Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 235000009508 confectionery Nutrition 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000003345 natural gas Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 241001062472 Stokellia anisodon Species 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000010079 rubber tapping Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005262 decarbonization Methods 0.000 description 2
- 238000010410 dusting Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 206010011416 Croup infectious Diseases 0.000 description 1
- 241000721047 Danaus plexippus Species 0.000 description 1
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 1
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- 241001417490 Sillaginidae Species 0.000 description 1
- 230000003044 adaptive effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 238000005502 peroxidation Methods 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 230000005514 two-phase flow Effects 0.000 description 1
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Abstract
The invention relates to a composite converting process of bottom blowing coal oxygen for an oxygen top-blown converter. The whole smelting process is regulated and controlled by a top-blown oxygen lance: the bottom coal-oxygen spray gun can spray coal oxygen from beginning to end without influencing top blowing operation so as to achieve the effects of heat compensation and molten pool stirring. The invention can effectively improve the heat supply in the furnace and increase the scrap steel ratio in the furnace charge. Meanwhile, even under the condition of low carbon content in the molten pool, the high decarburization speed can be maintained, the oxidizability of the slag is reduced, and the over oxidation phenomenon of the molten pool is eliminated. The invention can also improve the desulfurization capability of the slag and improve the recovery rate of manganese.
Description
The invention belongs to converter steelmaking process.Be applicable to that mainly top-blown oxygen converter carries out thermal compensation, improve the ability that cold conditions raw material (steel scrap, the pig iron, sponge iron etc.) are accepted in converter.
Common converter steelmaking is the physical chemistry heat that relies on furnace charge itself, improves bath temperature, and the heat of heat fused steel scrap is provided.Therefore, the add-on of steel scrap is subjected to the strictness restriction of the physical chemistry heat of molten iron own, and scrap ratio fluctuates 5～25%.This is that converter process is compared with open-hearth process, a main drawback.In recent years, in order to save blast-furnace coke and other reason, downward trend all appearred in the silicone content of hot metal in steelmaking both at home and abroad, had reduced the chemical heat of molten iron.After adopting existing top-bottom blowing technology, the oxidational losses of iron reduces, the also corresponding ability that reduces the converter scrap melting.In order to remedy this problem, the various countries metallargist has proposed various process programs, improves the thermo-efficiency of converter.At present, round the employing of converter coal powder injection technology, many new process for smelting steel have appearred in succession.Its purpose all is in order to improve the converter adding amount of scrap steel, to strengthen the adaptive faculty of converter to furnace charge.
The external converter compensated technology of having succeeded in developing or having researched and developed can be divided into top-blown method and subaeration two big classes.
Subaeration is representative (" SteelmaKing Proceedings ", 1982, Vol65,287～295) with the KMS method of West Germany Clockner-CRA technology development co..This technology is transformed into the bottom blowing coaloust-oxygen gun to the BOTTOM OXYGEN rifle of bottom-blown converter.Spray gun adopts three layers of sleeve structure; The pipe core coal injection, middle circumferential weld winding-up oxygen, outer circumferential weld leads to heat-eliminating medium.Smelt mid-term, bottom blowing coal oxygen provides heat to the molten bath, melting waste steel.Smelting initial stage and later stage, coal dust switches to lime powder, normally smelts.For improving thermo-efficiency, the oxygen rifle is installed at the bottom-blown converter top, the burning furnace gas.Still adopt subaeration oxygen rifle resist technology, with Sweet natural gas or methane gas protection furnace bottom coaloust-oxygen gun.Be solution dephosphorization in early stage, and form slag as early as possible, improve molten bath thermo-efficiency, adopt end spray lime powder technology.One kilogram of coal dust of this technology is fusible approximately 6 kilograms of steel scraps.
The KMS method is the thermal compensation Technology that is applicable to bottom-blown converter.It has kept the metallurgical characteristics of bottom-blown converter, does not resemble top-blown method, a large amount of foamy slags is arranged in the stove in the smelting process, thereby thermo-efficiency is lower.There is following shortcoming in this technology: be the cooling coal oxygen injection lance, steel per ton need consume Sweet natural gas 2.7 mark rice
3Or oily 3～5 kilograms; The partition ratio of smelting sulphur between slag steel in latter stage only is 8～12.
Top-blown method is representative with the TAPS method (" iron と steel " 1986, No 15,71～84) of Japan and the ALCI method (" Steelmaking Proeedings " 1985, Vol68,129～136) of Luxembourg.This technology is feature with the top blast coal dust, and converter Coal powder spray technology is combined with secondary burning technology, improves the top blown converter scrap ratio.The TAPS method was carried out 15 tons of converter experiments.Adopt TAPS oxygen rifle,, for powder speed coal dust is sprayed into bath short time with higher smelting in try one's best mid-term.For improving the recovery rate of coal dust, need to adopt " blowing firmly " technology, reduce the rifle position, coal dust is sprayed into molten steel.One kilogram of coal dust of every winding-up can add 4 kilograms of steel scraps.The ALCI method was carried out experiment on 250 tons of LBE combined blown converters of monarch Tianjin factory.This technology is basic identical with the TAPS method, one kilogram of fusible 4～6 kilograms of steel scrap of coal dust.
TAPS and ALCI method are applicable to the thermal compensation technology that top-blown method is smelted, and its main drawback is: adopt top Coal powder spray technology, interrupted smelting process, the amount of dusting and the time of dusting are restricted, and thermo-efficiency is low; Adopt " blowing firmly " technology Coal powder spray, make CO in the furnace gas
2Content reduces, and has disturbed the normal running of top rifle; After can't solving a large amount of adding steel scraps, it is low to smelt the initial stage bath temperature, forms caused excessive slag of low temperature foamy slag and splash problem in the stove; Desulfuration efficiency is low, and the partition ratio of sulphur only is 4～6 between the slag steel.
West Germany Krupp institute has proposed another kind of processing method-COIN method.This technology sprays into coal dust and oxygen by the bottom, molten bath, and directly adopts coal dust protection jet pipe.But call oneself according to the said firm, can not carry out refining simultaneously with this working method.
The object of the present invention is to provide a kind of thermo-efficiency height, scrap ratio (or other cold burden ratio) height, cost is low, can improve the quality of products, and obtains the top blown oxygen converter thermal compensation process for making technology of good metallurgical effect.
Solution of the present invention is as follows:
On the furnace bottom of top blown oxygen converter, one or many (it is big or small and different to look stove) coal oxygen injection lances are installed.Both carry out top blowing oxygen, carried out the composite blow technology of bottom blowing coal oxygen again.Rely on top rifle operation that smelting process is regulated and controlled on the one hand, try hard to keep top blowing oxygen converter slag fast, the advantage that thermo-efficiency is high; Bring into play bottom blowing coal oxygen recovery rate of iron height on the other hand, the molten bath is stirred strong, and heat supplied is big, and the characteristics stably that blow are so that obtain best metallurgical effect.Simultaneously, directly adopt coal dust to make refrigerant protection bottom spray gun, replace the Sweet natural gas or the solar oil of common usefulness, reduce cost.
In the whole process of coal oxygen top-bottom blowing, rely on the adjusting of top blow oxygen lance rifle position and oxygen flow, the control smelting process.From start to finish from bottom coal injection and part of oxygen, give full play to the characteristics of high-level efficiency heat supply simultaneously.Injecting coal quantity can be regulated, and does not disturb the operation of top blow oxygen lance.
In order to improve the heating benefit of coal, top blow oxygen lance adopts multihole lance (comprising the double flow duct spray gun), to strengthen the secondary combustion of furnace gas.
The present invention adopts little coal oxygen than (ratio that is pulverized coal flow and oxygen flow is less) when the blowing beginning, provides heat to the molten bath, accelerates the molten bath and heats up, so can avoid adding the molten bath cooling for a long time of steel scrap amount too much, overflow slag and splash phenomenon occur.
Blowing mid-term, strong in order to prevent the stirring of bottom blowing coal oxygen, slag easily returns dried trend, and the top rifle adopts the soft blow operation of " high rifle position, big oxygen pressure, dispersion oxygen supply ".In time adjust the rifle position and strengthen emulsification and the oxygenizement of top oxygen jet, guarantee certain FeO content in the slag, promote the dissolving of lime slag.
Smelt latter stage, continue to molten bath injection coal oxygen, the metallurgical effect that obtains mainly shows: (1) molten bath in latter stage still keeps higher decarbonization rate, but FeO is low in the slag, prevents the molten bath peroxidation.Facts have proved that during the smelting low carbon steel, FeO is all identical with subaeration with oxygen content in steel in the slag.(2) sweetening power of raising slag, the partition ratio of sulphur reaches 10～20 between the slag steel, is higher than the end-blown converter steel-making method of end spray lime powder.(3) also beneficial to dephosphorization.Blow latter stage, suitably improve BOTTOM OXYGEN and press, control coal oxygen ratio is less than 1.0.
Solution of the present invention can further describe with following accompanying drawing.
Accompanying drawing 1 is a process flow sheet of the present invention.
Accompanying drawing 2 is the influence of fixed carbon content to the melting waste steel ability.
Accompanying drawing 3 is the pulverized coal flow of single coaloust-oxygen gun and the relation between oxygen supply intensity;
Accompanying drawing 4 is the influence of bottom blowing coal oxygen comparison furnace gas combustion case;
Accompanying drawing 5 is a nitrogen in steel content and the relation of BOTTOM OXYGEN nitrogen ratio;
Accompanying drawing 6 is the relation of critical velocity curve and powder to air ratio;
Accompanying drawing 7 is the variation of Coal powder spray processing parameter at the bottom of six tons of converters.
In the accompanying drawing 1,1 is hopper, and 2 is vibratory screening apparatus, the 3rd, and storage powder jar, the 4th, powder spraying pot, 5 are the bottom blowing coaloust-oxygen gun, the 6th, top blow oxygen lance, the 7th, the nitrogen Controlling System, 8 are converter, 9 is discharge gate, the 10th, power transportation pipe, the 11st, BOTTOM OXYGEN feed channel.
Before smelting beginning, by nitrogen Controlling System 7 to powder spraying pot 4 pressurisings.The discharge gate 9 of opening powder spraying pot after the pressurising is by defeated pulverized coal channel 10 and furnace bottom oxygen coal 5 molten bath coal injection in converter 8.Open oxygen valve simultaneously, by coaloust-oxygen gun to the molten bath oxygen supply.
Coaloust-oxygen gun is a double-layer sleeve structure: interior pipe delivering oxygen; Outside circumferential weld pulverized coal conveying.Coal dust is protected the furnace bottom oxygen-blowing gun as heat-eliminating medium.
Dust stable after, add a small amount of slag charge from fire door to converter 8 earlier, add steel scrap thereafter.If the scrap ratio height, add-on can add greatly in two batches.Follow hot metal charging.Behind the hot metal charging, shake positive body of heater, the blowing of decline top rifle.Open and to control top gun gun bit when blowing well, changed first slag rapidly.Improve BOTTOM OXYGEN simultaneously and press, guarantee to spray into the abundant burning of coal dust.Open and blew the back 3～5 minutes, enter carbon period, the C-O reaction is violent.Should in time improve top blast rifle position, avoid or alleviate the mid-term slag returning dried.At this moment, bottom blowing coal oxygen ratio is controlled at about 1.0.Blowing after 10～12 minutes, tends to be steady in the molten bath.The top rifle that should in time descend improves the molten bath decarbonization rate.The carbon flame is received stove (carbon of falling the stove fluctuates 0.03～0.10%) of fire back, tapping.
Thermo-efficiency height of the present invention, according to practice result, 1 kilogram of fusible 7～9 kilograms of steel scrap of coal dust of jetting.As shown in Figure 2.Ordinate is the ability (1 kilogram of steel scrap/kilogram coal) of one kilogram of coal dust melting waste steel among the figure; Abscissa is a fixed carbon content in the coal dust.By also finding out among the figure, coal dust fixed carbon content has a significant impact coal powder injection thermo-efficiency.This technology to the requirement of coal dust is: fixed carbon is greater than 70%, and sulphur content is less than 0.5%, and moisture content is 0.5～1.5% hard coal coal dust.The granularity requirements of coal dust is less than 100 orders.Also can replace coal dust with coke powder.
The pulverized coal flow Gs(kilogram of bottom winding-up/minute) should be according to selected coal, secondary combustion intensity and desired increase steel scrap amount W are calculated as follows:
Gs=W/6.5(1+2B) (%C) the t(kilogram/minute)
B is the post-combustion rate of furnace gas in the formula; T is duration of blast (branch), (%C) is fixed carbon content in the coal, and W compares the steel scrap amount that increases of requiring during with Coal powder spray not.
P
CoAnd P
Co2Be respectively CO and CO in the furnace gas
2Dividing potential drop.
The pulverized coal flow of single coaloust-oxygen gun winding-up and the ability of oxygen supply intensity and melting waste steel, as shown in Figure 3.Ordinate is a single spray gun oxygen supply intensity (mark rice among the figure
3/ minute); Abscissa is single rifle Coal powder spray flow (kilogram/minute).Oxygen supply pressure in bottom is 6～12 kilograms per centimeter
2, oxygen supply intensity is 0.6～1.5 mark rice
3/ ton divides, and end oxygen-supplying amount accounts for 15～30% of top oxygen-supplying amount.
Accompanying drawing 4 is the influence of bottom blowing coal oxygen comparison furnace gas combustion case.Ordinate is P among the figure
Co2/ P
Co+ P
Co2; Abscissa is that coal oxygen is than (weight ratio).Drawn by this figure, end coal powder injection oxygen weight ratio should be controlled in 0.4～1.2 scope, can improve the thermo-efficiency of coal powder injection.
Accompanying drawing 7 has provided the changing conditions of Coal powder spray processing parameter at the bottom of six tons of converters.Ordinate is each process operation parameter (as cylinder pressure, powder dropping amount, a throughput ratio etc.) among the figure, and abscissa is the time.Adopting above-mentioned powder injection process, is stable to the molten bath pulverized coal conveying.
Adopt injection coal composite blow technology for oxygen of the present invention, obtained the excellent metallurgical effect, mainly be:
(1) improves the stirring condition of smelting the molten bath in latter stage, reduced the oxidisability of slag.In the low-carbon (LC) district, iron oxide content and oxygen content in steel and subaeration are suitable in the slag;
(2) partition ratio of manganese reduces between the slag steel, has improved the rate of recovery of manganese; Simultaneously, improved the sweetening power of slag, the partition ratio of sulphur is up to 10～20 between the slag steel.
(3) control BOTTOM OXYGEN nitrogen volume flow ratio is greater than certain numerical value, and as greater than 5.0, then the nitrogen in steel amount can be controlled in the following level of 60PPm.
(4) thermo-efficiency height.One kilogram of fusible 7～9 kilograms of steel scrap of coal dust.Scrap ratio can reach 40～50%, to technological operation with all there is not too big influence tap to tap time.
The present invention compares with bottom blowing coal spraying process-KMS method, or compares with the TAPS method with top blast coal spraying process-PLCI, all has following advantage:
(1) directly adopt coal dust to make heat-eliminating medium protection bottom blowing coaloust-oxygen gun, the ton steel is saved Sweet natural gas 2.7 mark rice
3Or oily 3～5 kilograms.
(2) metallurgical effect is good, and slag desulfurization capacity is strong, and the partition ratio of sulphur reaches 10～20 between the slag steel.
(3) thermo-efficiency height, 7～9 kilograms of one kilogram of fusible steel scraps of coal dust.
(4) Coal powder spray and molten bath refining are carried out simultaneously, and coal powder injection time and injecting coal quantity are unrestricted, can adopt high scrap ratio operation, and need not prolong tap to tap time.
Embodiment one
At the furnace bottom of six tons of top-blown oxygen converters a spray oxygen spray gun is installed, spray gun is made heat-eliminating medium with coal dust.10 tons of batching Intake Quantitys, 2 tons of steel scraps, 8 tons of molten iron increase by 1.5 tons of steel scrap consumptions, and scrap ratio is 20%.
Hot metal composition is: 4.0%C, 0.6～0.8%Si, 0.06%P, 0.05%S.Adopting fixed carbon is 83%, and sulphur content is 0.37% coal dust, 21.4 kilograms in ton steel consumption coal, and the Coal powder spray flow is 10 kilograms/minute, and bottom blowing coal oxygen (weight) is than being 0.9, and end oxygen supply intensity is 0.93 mark rice
3/ minute ton, top blast oxygen supply intensity are 3.2 mark rice
3/ minute ton.
Duration of blast 20 minutes.The terminal point tapping temperature is 1710 ℃.Carbon content 0.08% in the steel, sulphur content 0.020%, P content 0.010%; FeO content is 11% in the slag.
Embodiment two
Adopt the equipment and identical raw material of embodiment one.4 tons of adding amount of scrap steel, 6 tons of molten iron add 3.5 tons of steel scrap amounts, steel scrap 40%.40 kilograms in ton steel consumption coal.The Coal powder spray flow is 20 kilograms/minute, and the top oxygen supply intensity is 3.2 mark rice
3/ minute ton, end oxygen supply intensity are 1.6 mark rice
3/ minute ton, coal oxygen (weight) is than being 1.0.
The terminal point tapping temperature is 1630 ℃, and carbon content 0.03% in the terminal point steel, sulphur content 0.03%, and FeO is 12% in the slag.Duration of blast 20 minutes.
Claims (10)
1, a kind of coal oxygen injection lance by installing in the converter bottom, top-blown converter steelmaking composite blow technology to molten bath coal injection and oxygen, it is characterized in that in whole smelting process, passing through from start to finish this spray gun simultaneously to bath coal injection and oxygen, top blow oxygen lance adopts multihole lance (comprising the double flow duct spray gun), " soft blow " technology that top blowing oxygen adopts high rifle position, big oxygen to press and disperse oxygen supply.
2, composite blow technology according to claim 1 is characterized in that the pulverized coal flow Gs of bottom blowing coal oxygen determines by following formula:
Gs=W/6.5(1+2B) (%C) the t(kilogram/minute)
T is a duration of blast in the formula, (%C) is fixed carbon content in the coal, and W compares the steel scrap amount that increases of requiring during with Coal powder spray not, and B is the post-combustion rate of furnace gas,
P
Co, P
Co2Be respectively CO in the furnace gas, CO
2Dividing potential drop.
3, composite blow technology according to claim 1 is characterized in that the BOTTOM OXYGEN amount is 15～30% of a top blowing oxygen amount.
4, composite blow technology according to claim 1 is characterized in that the weight ratio of bottom blowing coal oxygen should be controlled in 0.4～1.2 scope.
5, composite blow technology according to claim 1, it is characterized in that the coal dust at bottom blowing coal oxygen lance spraying mouth place and the powder to air ratio (weight ratio of coal dust and its carrier gases such as nitrogen) that carrier gases (as nitrogen) two phase fluid is carried should be controlled in 5～25 scopes, outlet two phase fluid apparent velocity correspondingly is controlled at 200～80 meter per seconds.
6, composite blow technology according to claim 5 is characterized in that the volume flow ratio of BOTTOM OXYGEN nitrogen should be greater than 5.0 when adopting nitrogen to do the carrier gas of delivery coal dust.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN87100551.4A CN1004707B (en) | 1987-02-12 | 1987-02-12 | Coal-oxygen composite blowing process for oxygen converter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN87100551.4A CN1004707B (en) | 1987-02-12 | 1987-02-12 | Coal-oxygen composite blowing process for oxygen converter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN87100551A CN87100551A (en) | 1988-08-31 |
| CN1004707B true CN1004707B (en) | 1989-07-05 |
Family
ID=4812926
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN87100551.4A Expired CN1004707B (en) | 1987-02-12 | 1987-02-12 | Coal-oxygen composite blowing process for oxygen converter |
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| Country | Link |
|---|---|
| CN (1) | CN1004707B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102399932B (en) * | 2010-09-16 | 2013-07-03 | 鞍钢股份有限公司 | Method for reducing converter hot metal single consumption |
| CN102787201A (en) * | 2012-08-31 | 2012-11-21 | 首钢京唐钢铁联合有限责任公司 | Application of coal serving as steelmaking slag pressing agent and method for inhibiting steel slag bubbles |
| CN113355477B (en) * | 2021-05-18 | 2022-07-05 | 北京科技大学 | Method for realizing high scrap ratio smelting of converter by bottom blowing hydrogen |
| CN115652017A (en) * | 2022-12-26 | 2023-01-31 | 北京科技大学 | Converter high-cold-material-ratio low-carbon smelting device and smelting method |
-
1987
- 1987-02-12 CN CN87100551.4A patent/CN1004707B/en not_active Expired
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| Publication number | Publication date |
|---|---|
| CN87100551A (en) | 1988-08-31 |
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