CN102409132B - Method for producing 25CrMnB steel through converter flow - Google Patents
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Abstract
The invention discloses a method for producing 25CrMnB steel through a converter flow and belongs to the field of metallurgy. The invention aims to provide a method for enabling a continuous casting machine of small dimension to cast smoothly so as to produce 25CrMnB steel through a converter flow. The method comprises the following steps: a, carrying out converter smelting; b, adding calcium carbide during steel tapping to enable the molten steel activity to be below 0.0025; c, adding 3.5-4.5kg per ton of steel before refining and heating, and adding 0.15-0.45kg of aluminum per ton of steel during heating; stopping heating when the molten steel is heated to be 1565-1585DEG C; adding aluminum to enable the content of aluminum to be 0.011-0.016%, then adding titanium to enable the content of titanium to be 0.02-0.06%, and adding boron to enable the boron content to be 0.0005-0.003%; and d, carrying out continuous casting. The method in the invention not only is applicable to a continuous casting machine of larger dimension and can be used for casting smoothly on the continuous casting machine of small dimension.
Description
Technical field
The invention belongs to the ferrous metallurgy field, be specifically related to a kind of method of producing 25 CrMnB steel through converter flow.
Background technology
Trace B (about 0.001%) can be adsorbed on austenite grain boundary, reduce the crystal boundary energy, prevent the ferrite nucleation, improve exponentially the hardening capacity of middle low carbon steel, so the trace B of the normal interpolation 0.0005～0.003% of middle low carbon steel improves the hardening capacity of steel.But boron is one of as lively as a cricket element, can with steel in residual oxygen and nitrogen form stable inclusion, and lose beneficial effect, the boron that only exists with the solid solution form just can play useful effect.
Existing studies show that, boron and oxygen and nitrogen all have very strong avidity, and boron is easy to oxidized generation B
6O or B
2O
3, perhaps generating BN with nitrification, these all are the objectionable impuritiess that stop boron performance raising hardening capacity effect in the boron-containing steel.Therefore, improve the effect of boron-containing steel hardening capacity for guaranteeing boron, must in the smelting process of steel, at first adopt aluminium to slough the free oxygen of molten steel, and with the fixing nitrogen in the molten steel of titanium, the useful effect of guarantee adding boron.
25CrMnB is novel boracic class formation steel, can replace 23MnB to make pitch is the grip-pad of 228 above dozers or excavator, chemical composition is by weight percentage: C:0.20～0.30%, Mn:0.80～1.40%, Si:0.15～0.35%, P≤0.030%, S≤0.015%, Cr:0.30～0.60%, Ni≤0.25%, Cu≤0.30%, B:0.0005～0.0035%, generally for guaranteeing that boron improves the effect of hardening capacity, also require control Ti content more than 0.02%, Al content is more than 0.02%.For example:
The patent CN100519769C that open day is on July 29th, 2009 discloses the method that a kind of converter smelting is produced boron-containing steel, it is characterized in that adopting the explained hereafter boron-containing steel of converter smelting → ladle deoxidation, refining → boron alloy, concrete operational provisions is: at first be to add aluminium and refining slag carries out deoxidation to molten steel and slag behind converter tapping, the molten aluminium of control molten steel acid is in 0.02%～0.04% scope, then the FeO+MnO in LF stove refining controlling slag≤2.0%, and the α of molten steel
[O]≤ 10ppm adds after aluminium carries out deep deoxidation to ladle at last again, adds ferrotianium and ferro-boron and carries out alloying.Adopting the recovery rate of this technique boron high, is 69.4%～91.8%.
The patent CN101660101A that open day is on March 3rd, 2010 discloses extremely manufacture method of a kind of steel for low-carbon wear-resistant engineering machinery creeper tread, its open grip-pad is with the B that contains 0.0005～0.0035% in the steel, but its manufacture method is to adopt electrosmelting → tapping → LF external refining → VD Fruit storage, for typical electric furnace flow process, do not relate to producing 25 CrMnB steel through converter flow.And the chemical composition of CN101660101A is C:0.17～0.27%, Si:0.17～0.37%, Mn:0.85～1.20%, Cr:0.10～0.30%, Al:0.010～0.060%, Cu:0.010～0.20%, Ni:0.01～0.20%, P:0.003～0.025%, S:0.001～0.025%, Ti:0.020～0.060%, B:0.0005～0.0035%, [O]: 5～20 * 10
-6%, [N]: 40～90 * 10
-6%, remaining is Fe and inevitable impurity, can only produce the following dozer of 216 pitches or the grip-pad of excavator.This patent has also been mentioned the method that guarantees boron validity, namely requires preferably to control Al content in 0.020～0.050% scope.
Comprehensive above-mentioned public technology improves the effect of hardening capacity for guaranteeing boron, must have the aluminium more than 0.02% in the steel, and guarantee adds the useful effect of boron.Find according to production practice, the control aluminium that CN100519769C and CN101660101A mention or sour molten aluminium are not less than 0.02%, have certain limitation.Be specially aluminium or sour molten aluminium greater than 0.02% molten steel, in casting cycle, can produce a certain amount of Al
2O
3, these Al
2O
3Affecting continuous casting thereby the conticaster crystallizer mouth of a river is diminished, even stop up the conticaster crystallizer mouth of a river, is particularly serious on 200 * 200mm or the continuous caster below 200 * 200mm at section particularly, and the small dimension continuous caster can't be cast.
Summary of the invention
That technical problem to be solved by this invention provides is a kind of when guaranteeing boron-containing steel hardening capacity, make the method for the producing 25 CrMnB steel through converter flow that the small dimension continuous caster can cast smoothly.
The technical solution adopted for the present invention to solve the technical problems is:
A kind of method of producing 25 CrMnB steel through converter flow comprises the steps:
A, in converter, add molten iron smelting;
B, molten steel are tapped to ladle, add calcium carbide during tapping and make the molten steel oxygen activity below 0.0025%;
C, ladle move into the refining of LF stove, molten steel per ton adds calcium carbide 3.5～4.5kg before the refining heating, molten steel per ton adds metallic aluminium 0.15～0.45kg in the heat-processed, stopped heating when liquid steel temperature is heated to 1565～1585 ℃, in molten steel, add aluminium, make in the molten steel sour molten aluminium weight percent content 0.011～0.016%, add again titanium and make in the molten steel titanium weight percent content 0.02～0.06%, add boron and make in the molten steel boron weight percent content 0.0005～0.003%;
Carry out continuous casting after d, the refining.
Wherein, also add steel scrap when adding molten iron in the converter among the aforesaid method step a, the weight of steel scrap is no more than 15% of weight of molten iron.
Further, when just refining of molten steel composition to C by weight percentage is 0.05%～0.15%, in the ladle of molten steel being tapped when P≤0.015% and S≤0.015%.
Wherein, among the aforesaid method step b, it is foundation that the calcium carbide add-on is just refined endpoint carbon content according to converter, when converter terminal carbon weight percent drops into by molten steel 3.5～4.5kg per ton when following 0.10%; When converter terminal carbon weight percent drops into by molten steel 2.5～3.5kg per ton greater than 0.10%, less than 0.15% the time; When converter terminal carbon weight percent drops into by molten steel 1.5～2.5kg per ton when above 0.15%.
Also add when wherein, adding calcium carbide among the aforesaid method step b ferrosilicon make in the molten steel silicon weight percent content 0.15～0.35%, add ferromanganese make in the molten steel manganese weight percent content 0.80～1.10%, add ferrochrome make in the molten steel weight of chromium degree 0.30～0.60%, add carburelant and make the carbon weight percent content 0.20～0.30%.
Described carburelant mainly refer to contain fixed carbon more than 98% asphalt adhesive or contain the hard coal of fixed carbon more than 92%.
Wherein, molten steel adding calcium carbide 3.8～4.2kg per ton before the refining heating among the aforesaid method step c, molten steel per ton adds metallic aluminium 0.2～0.4kg in the heat-processed.
Wherein, the mode that adds titanium among the aforesaid method step c is the cored-wire with feeding wire machine feeding titaniferous, and the mode that adds boron is the cored-wire with feeding wire machine feeding boracic.
Wherein, in the aforesaid method during steps d continuous casting in the continuous caster bag temperature be 1530 ± 20 ℃.
Wherein, calcium carbide contains CaC described in the aforesaid method
2More than 70%.
The present invention specifically can implement in the following manner: a kind of method of producing 25 CrMnB steel through converter flow comprises the steps:
A, add molten iron and scrap smelting in the converter, the weight of steel scrap is no more than 15% of weight of molten iron, when just refining of molten steel composition to C by weight percentage is 0.05%～0.15%, in the ladle of molten steel being tapped when P≤0.015% and S≤0.015%;
B, molten steel are tapped to ladle, add during tapping and contain CaC
270% calcium carbide makes the molten steel oxygen activity below 0.0025%, and it is foundation that the calcium carbide add-on is just refined endpoint carbon content according to converter, when converter terminal carbon weight percent drops into by molten steel 3.5～4.5kg per ton when following 0.10%; When converter terminal carbon weight percent drops into by molten steel 2.5～3.5kg per ton greater than 0.10%, less than 0.15% the time; When converter terminal carbon weight percent drops into by molten steel 1.5～2.5kg per ton when above 0.15%; Also add when adding calcium carbide ferrosilicon make in the molten steel silicon weight percent content 0.15～0.35%, add ferromanganese make in the molten steel manganese weight percent content 0.80～1.10%, add ferrochrome make in the molten steel weight of chromium degree 0.30～0.60%, add carburelant and make the carbon weight percent content 0.20～0.30%;
C, ladle move into the refining of LF stove, and molten steel per ton adds and contains CaC before the refining heating
2Calcium carbide 3.8～4.2kg of 70%, molten steel per ton adds metallic aluminium 0.2～0.4kg in the heat-processed, stopped heating when liquid steel temperature is heated to 1565～1585 ℃, in molten steel, add aluminium, make in the molten steel sour molten aluminium weight percent content 0.011～0.016%, make in the molten steel titanium weight percent content 0.02～0.06% with the cored-wire of feeding wire machine feeding titaniferous again, make in the molten steel boron weight percent content 0.0005～0.003% with the cored-wire of feeding wire machine feeding boracic;
Carry out continuous casting after d, the refining, wrapping temperature in the continuous caster during continuous casting is 1530 ± 20 ℃.
The invention has the beneficial effects as follows: continuous caster mold gap in casting cycle stops up, owing to aluminium too high levels in the molten steel causes, according to practical condition, if the strand size is less than 200 * 200mm, and casting is to contain the molten steel of aluminium more than 0.02%, just might make the conticaster crystallizer nozzle clogging, cause continuous caster to cast.But in order to guarantee that boron in the boron-containing steel improves the effect of hardening capacity, boron-containing steel must at first adopt aluminium to slough the free oxygen of molten steel in the smelting process of steel usually, and with the fixing nitrogen in the molten steel of titanium, the useful effect of guarantee adding boron.Analyze boron-containing steel production key point, aluminium more than 0.02% is just in order to slough as much as possible the free oxygen in the molten steel, the tapping process of the inventive method after just refining of molten steel is complete do not adopt aluminium to carry out pre-deoxidation, and the employing calcium carbide, be generally again the relation of a constant according to carbon in the converter steelmaking process and equilibrium oxygen, the technology of the present invention has been taked according to the different end point carbons of converter, and the way of the different calcium carbide quantity of corresponding adding is carried out pre-deoxidation, after the above-mentioned pre-deoxidation of molten steel process, molten steel oxygen activity α
[O]Can be controlled in below 0.0025%.Ladle moves on to the LF refining furnace molten steel is carried out refining, further deoxidation, and the front adding of heating calcium carbide adds metallic aluminium and strengthens diffusive deoxidation effect adding calcium carbide replacement part aluminium before the heating of LF stove to reach, thereby reduces acid-soluble aluminum content in the molten steel in the heat-processed.The calcium carbide and the metallic aluminium light specific gravity that add can not enter molten steel, molten steel α after the diffusive deoxidation
[O]Can be controlled in below 0.0015%, slag oxidisability FeO+MnO can be controlled in below 1.5%.Iff using calcium carbide, slag oxidisability FeO+MnO is difficult to be controlled at below 1.5%, can only reach 1.5～2.0% level at LF stove refinery practice, and the metal aluminum shot that molten steel therefore per ton adds 0.2～0.4kg is very necessary.Stopped heating when liquid steel temperature is heated to 1565～1585 ℃ adds aluminium in molten steel, make that sour molten aluminium weight percent content is to consider that rear portion continuous casting steel machine process has part Als and is oxidized to Al 0.011～0.016% in the molten steel
2O
3Phenomenon, learn that through a large amount of practices the continuous casting steel machine process has 0.006～0.011% Als to be oxidized to Al
2O
3, this operation must add aluminium and control sour molten aluminium 0.011～0.016%, also has 0.005～0.010% sour molten aluminium with the molten steel that guarantees final casting.The aluminium that molten steel adds after complete deoxidation all forms AlN basically, and the effect of fixed nitrogen is arranged, and can reduce the titanium usage quantity, avoids bulk TiN to be mingled with appearance, and in addition, AlN is also useful to the crystal grain of refinement steel.The inventive method has guaranteed that the free oxygen of molten steel is removed, and the boron recovery rate is high, and the 25CrMnB steel hardenability is good, and don't as for making the aluminium in the molten steel too high.Therefore, the inventive method not only can be applicable to the continuous caster of large specification, and is applicable to the following small dimension continuous caster of 200 * 200mm, and assurance small dimension continuous caster can be cast smoothly.
Embodiment
The specific embodiment of the invention is as follows: a kind of method of producing 25 CrMnB steel through converter flow comprises the steps:
A, in converter, add molten iron smelting;
B, molten steel are tapped to ladle, add calcium carbide during tapping and make the molten steel oxygen activity below 0.0025%;
C, ladle move into the refining of LF stove, molten steel per ton adds calcium carbide 3.5～4.5kg before the refining heating, molten steel per ton adds metallic aluminium 0.15～0.45kg in the heat-processed, stopped heating when liquid steel temperature is heated to 1565～1585 ℃, in molten steel, add aluminium, make in the molten steel sour molten aluminium weight percent content 0.011～0.016%, add again titanium and make in the molten steel titanium weight percent content 0.02～0.06%, add boron and make in the molten steel boron weight percent content 0.0005～0.003%;
Carry out continuous casting after d, the refining.
Preferably, also add steel scrap when adding molten iron in the converter among the aforesaid method step a, the weight of steel scrap is no more than 15% of weight of molten iron.Steel scrap can derive from salvage station, also can derive from steel mill inside.Converter steelmaking is originated without external heat, all rely on carbon in the oxidation molten iron, and a small amount of silicon and manganese emit heat, thereby molten steel is heated, with respect to molten iron, the steel scrap carbon content is generally very low, and the steel scrap that adds in the converter smelting can play the effect that reduces temperature.Simultaneously in order to economize on resources, and produce qualified Finished Steel, because remaining Ni and Cu in the steel scrap are uncontrollable, can cause the Ni＞0.25% in the molten steel, the phenomenon of Cu＞0.30% to occur for fear of excessive adding steel scrap, the weight of steel scrap can not surpass 15% of weight of molten iron.
Further, when just refining of molten steel composition to C by weight percentage is 0.05%～0.15%, in the ladle of molten steel being tapped when P≤0.015% and S≤0.015%.In fact steelmaking process is exactly initial oxidation, and then the process of reduction during converter steelmaking, is only carried out oxidizing reaction in converter, and reduction reaction is carried out in ladle.When C is 0.05%～0.15%, illustrate that oxidizing reaction is through with, should tap and carry out reduction reaction.
Preferably, among the aforesaid method step b, it is foundation that the calcium carbide add-on is just refined endpoint carbon content according to converter, when converter terminal carbon weight percent drops into by molten steel 3.5～4.5kg per ton when following 0.10%; When converter terminal carbon weight percent drops into by molten steel 2.5～3.5kg per ton greater than 0.10%, less than 0.15% the time; When converter terminal carbon weight percent drops into by molten steel 1.5～2.5kg per ton when above 0.15%.The tapping process of the inventive method after just refining of molten steel is complete do not adopt aluminium to carry out pre-deoxidation, and the employing calcium carbide, be generally again the relation of a constant according to carbon in the converter steelmaking process and equilibrium oxygen, the technology of the present invention has been taked according to the different end point carbons of converter, the way of the different calcium carbide quantity of corresponding adding is carried out pre-deoxidation, can play the effect of deoxidation, can avoid again carbon to exceed standard, carbon is controlled in the suitable scope.After the above-mentioned pre-deoxidation of molten steel process, molten steel oxygen activity α
[O]Can be controlled in below 0.0025%, guaranteed that the inventive method finally can access qualified 25CrMnB steel, the molten aluminium of acid can be controlled at smaller scope again, the small dimension continuous caster can be cast smoothly.
In order to produce qualified 25CrMnB steel, also add when adding calcium carbide among the aforesaid method step b ferrosilicon make in the molten steel silicon weight percent content 0.15～0.35%, add ferromanganese make in the molten steel manganese weight percent content 0.80～1.10%, add ferrochrome make in the molten steel weight of chromium degree 0.30～0.60%, add carburelant and make the carbon weight percent content 0.20～0.30%.
Preferably, molten steel adding calcium carbide 3.8～4.2kg per ton before the refining heating among the aforesaid method step c, molten steel per ton adds metallic aluminium 0.2～0.4kg in the heat-processed.Add calcium carbide before the heating, add metallic aluminium in the heat-processed to reach the effect of strengthening the diffusive deoxidation effect, the calcium carbide of adding and metallic aluminium light specific gravity can not enter molten steel, molten steel α after the diffusive deoxidation
[O]Can be controlled in below 0.0015%, guarantee boron-containing steel hardening capacity, slag oxidisability FeO+MnO can be controlled in below 1.5%.At LF stove refinery practice iff using calcium carbide, slag oxidisability FeO+MnO is difficult to be controlled at below 1.5%, can only reach 1.5～2.0% level, the metal aluminum shot that molten steel therefore per ton adds 0.2～0.4kg is very necessary, can not just add calcium carbide.
Preferably, the mode that adds titanium among the aforesaid method step c is the cored-wire with feeding wire machine feeding titaniferous, and the mode that adds boron is the cored-wire with feeding wire machine feeding boracic.
Preferably, in the aforesaid method during steps d continuous casting in the continuous caster bag temperature be 1530 ± 20 ℃.The 25CrMnB liquidus temperature is 1500 ℃, and the superheating temperature that control is wrapped in the continuous caster is 30 ± 20 ℃, and therefore, the bag temperature is 1530 ± 20 ℃ in the control continuous caster, and this temperature is that the electrically heated by front LF stove realizes.
Preferably, calcium carbide contains CaC described in the aforesaid method
2More than 70%.With handled easily with avoid adding too much impurity.
The invention will be further described below by embodiment, but therefore do not limit the present invention among the scope of description of embodiment.
Embodiment one
Adopt the technology of the present invention to produce the 25CrMnB steel at 120 tons of nominal capacities, the actual tap bof process in 120～140 tons of scopes, production technique is that 120 tons of converters are just made steel water → 120 ton LF stove refined molten steel → 6 machines, 6 stream billet casters and are cast into 280mm * 380mm strand.
At first in converter, add 130 tons of molten iron and 10 tons of steel scraps, utilize Converter Oxigen Blowing to take off the function of C, molten iron and steel scrap just are smelt molten steel, tap when the C of just refining of molten steel composition to 0.05%, 0.015% P, 0.015% S, 0.01% Si and 0.05% Mn in the ladle, this moment actual tap be 133 tons, in the converter steelmaking process approximately 5% raw material by scaling loss.Add calcium carbide 530kg in the tapping process in the molten steel and (contain CaC
275%), and adding simultaneously FeSi, FeMn, FeCr alloy and hard coal, to carry out Si, Mn, Cr and C element alloyed, Si content is 74% in the FeSi alloy that wherein adds, Mn content is 82% in the FeMn alloy, Cr content is 52% in the FeCr alloy, fixation of C is 92% in the hard coal, and Si content is 0.16% in the control molten steel, Mn content is 1.40%, Cr content is that 0.31%, C content is 0.20%.Gone out that to measure molten steel oxygen activity α [O] with apparatus for determination of oxygen behind the steel be 0.0025%.
After molten steel arrives the LF stove, at first add before the heating and contain CaC
2Then calcium carbide 530kg more than 70% begins heating, heats to add 26kg metal aluminum shot after 3 minutes.Stopped heating when liquid steel temperature is heated to 1565 ℃, aluminum steel 22kg with feeding wire machine feeding φ 10 in the ladle, the recovery rate that feed aluminum steel aluminium this moment is about 60%, and then the feeding φ 12 contain Ti cored-wire 90kg (this moment 90kg be core grain weight amount, do not comprise the outer field iron sheet weight of cored-wire, the core powder all is FeTi40, namely contain Ti and be 40% iron alloy), and φ 12 contain B cored-wire 10kg (this moment 10kg be core grain weight amount, do not comprise the outer field iron sheet weight of cored-wire, the core powder all is FeB23, namely contain B and be 23% iron alloy), having fed and having measured molten steel oxygen activity α [O] behind the line is 0.0012%, and slag oxidisability FeO+MnO is 1.3%.The chemical composition Als that measures in addition molten steel is that 0.011%, Ti is that 0.02%, B is 0.0014%, and this moment, the recovery rate of B was 80%.
Become 280mm * 380mm strand in the 6 stream billet caster top castings of 6 machines at last, tundish temperature is 1520 ℃ during continuous casting, bag sampling analysis molten steel chemical composition is 0.20% C, 0.15% Si, 1.40% Mn, 0.015% P, 0.014% S, 0.35% Cr, 0.06% Ni, 0.10% Cu, 0.0012% B in continuous caster, and the Als of 0.02% Ti and 0.005% (Als scaling loss 0.006% in the casting cycle), all the other are Fe and inevitable other impurity.
Embodiment two
Adopt the technology of the present invention to produce the 25CrMnB steel at 120 tons of nominal capacities, the actual tap bof process in 120～140 tons of scopes, production technique is that 120 tons of converters are just made steel water → 120 ton LF stove refined molten steel → 6 machines, 6 stream billet casters and are cast into 200mm * 200mm strand.
At first in converter, add 120 tons of molten iron and 20 tons of steel scraps, utilize Converter Oxigen Blowing to take off the function of C, molten iron and steel scrap just are smelt molten steel, tap when the C of just refining of molten steel composition to 0.15%, 0.015% P, 0.010% S, 0.01% Si and 0.05% Mn in the ladle, this moment actual tap be 133 tons, in the converter steelmaking process approximately 5% raw material by scaling loss.Add calcium carbide 400kg in the tapping process in the molten steel and (contain CaC
275%), and adding simultaneously FeSi, FeMn, FeCr alloy and hard coal, to carry out Si, Mn, Cr and C element alloyed, Si content is 74% in the FeSi alloy that wherein adds, Mn content is 82% in the FeMn alloy, Cr content is 52% in the FeCr alloy, fixation of C is 92% in the hard coal, and Si content is 0.35% in the control molten steel, Mn content is 0.80%, Cr content is 0.45%, C content is 0.30%.Gone out that to measure molten steel oxygen activity α [O] with apparatus for determination of oxygen behind the steel be 0.0020%.
After molten steel arrives the LF stove, at first add before the heating and contain CaC
2Then calcium carbide 530kg more than 70% begins heating, heats to add 40kg metal aluminum shot after 3 minutes.Stopped heating when liquid steel temperature is heated to 1585 ℃, aluminum steel 33kg (recovery rate that feed aluminum steel aluminium this moment is about 60%) with feeding wire machine feeding φ 10 in the ladle, and then the feeding φ 12 contain Ti cored-wire 130kg (this moment 130kg be core grain weight amount, do not comprise the outer field iron sheet weight of cored-wire, the core powder all is FeTi40, namely contain Ti and be 40% iron alloy), and φ 12 contain B cored-wire 15kg (this moment 15kg be core grain weight amount, do not comprise the outer field iron sheet weight of cored-wire, the core powder all is FeB23, namely contain B and be 23% iron alloy), having fed and having measured molten steel oxygen activity α [O] behind the line is 0.0014%, and slag oxidisability FeO+MnO is 1.0%.The chemical composition Als that measures in addition molten steel is that 0.015%, Ti is that 0.03%, B is 0.0020%, and this moment, the recovery rate of B was 75%.
Become 200mm * 200mm strand in the 6 stream billet caster top castings of 6 machines at last, tundish temperature is 1550 ℃ during continuous casting, bag sampling analysis molten steel chemical composition is 0.30% C, 0.35% Si, 0.81% Mn, 0.015% P, 0.009% S, 0.45% Cr, 0.06% Ni, 0.16% Cu, 0.0020% B in continuous caster, and the Als of 0.03% Ti and 0.009% (Als scaling loss 0.006% in the casting cycle), all the other are Fe and inevitable other impurity.
Embodiment three
Adopt the technology of the present invention to produce the 25CrMnB steel at 80 tons of nominal capacities, the actual tap bof process in 80～82 tons of scopes, production technique is that 80 tons of converters are just made steel water → 80 ton LF stove refined molten steel → 5 machines, 5 stream billet casters and are cast into 150mm * 150mm strand.
At first in converter, add 84 tons of molten iron, utilize Converter Oxigen Blowing to take off the function of C, molten iron just is smelt molten steel, tap when the C of just refining of molten steel composition to 0.10%, 0.012% P, 0.009% S, 0.01% Si and 0.05% Mn in the ladle, this moment actual tap be 80 tons, in the converter steelmaking process approximately 5% raw material by scaling loss.Add calcium carbide 320kg in the tapping process in the molten steel and (contain CaC
275%), and adding simultaneously FeSi, FeMn, FeCr alloy and hard coal, to carry out Si, Mn, Cr and C element alloyed, wherein Si content is 74% in the FeSi alloy, Mn content is 82% in the FeMn alloy, Cr content is 52% in the FeCr alloy, fixation of C is 92% in the hard coal, and Si content is 0.25% in the control molten steel, Mn content is 1.01%, Cr content is 0.60%, C content is 0.23%, has gone out that to measure molten steel oxygen activity α [O] with apparatus for determination of oxygen behind the steel be 0.0024%.
After molten steel arrives the LF stove, at first add before the heating and contain CaC
2Then calcium carbide 320kg more than 70% begins heating, heats to add 32kg metal aluminum shot after 3 minutes.Stopped heating when liquid steel temperature is heated to 1570 ℃, aluminum steel 20kg (recovery rate that feed aluminum steel aluminium this moment is about 60%) with feeding wire machine feeding φ 10 in the ladle, and then the feeding φ 12 contain Ti cored-wire 145kg (this moment 145kg be core grain weight amount, do not comprise the outer field iron sheet weight of cored-wire, the core powder all is FeTi40, namely contain Ti and be 40% iron alloy), and φ 12 contain B cored-wire 10kg (this moment 10kg be core grain weight amount, do not comprise the outer field iron sheet weight of cored-wire, the core powder all is FeB23, namely contain B and be 23% iron alloy), having fed and having measured molten steel oxygen activity α [O] behind the line is 0.0011%, and slag oxidisability FeO+MnO is 1.4%.The chemical composition Als that measures in addition molten steel is that 0.015%, Ti is that 0.06%, B is 0.0019%, and this moment, the recovery rate of B was 65%.
Become 150mm * 150mm strand in the 5 stream billet caster top castings of 5 machines at last, tundish temperature is 1530 ℃ during continuous casting, bag sampling analysis molten steel chemical composition is 0.23% C, 0.25% Si, 1.09% Mn, 0.013% P, 0.009% S, 0.60% Cr, 0.06% Ni, 0.05% Cu, 0.0019% B in continuous caster, and the Als of 0.06% Ti and 0.006% (Als scaling loss 0.009% in the casting cycle), all the other are Fe and inevitable other impurity.
The comparative example
Adopt the technology of the present invention to produce the 25CrMnB steel at 80 tons of nominal capacities, the actual tap bof process in 80～82 tons of scopes, production technique is that 80 tons of converters are just made steel water → 80 ton LF stove refined molten steel → 5 machines, 5 stream billet casters and are cast into 150mm * 150mm strand.
At first in converter, add 84 tons of molten iron, utilize Converter Oxigen Blowing to take off the function of C, molten iron just is smelt molten steel, tap when the C of just refining of molten steel composition to 0.10%, 0.012% P, 0.009% S, 0.01% Si and 0.05% Mn in the ladle, this moment actual tap be 80 tons, in the converter steelmaking process approximately 5% raw material by scaling loss.Add FeAl 167kg in the tapping process in the molten steel and (contain Al 40%, all the other are Fe), and add simultaneously FeSi, FeMn, FeCr alloy and hard coal carry out Si, Mn, Cr and C are element alloyed, wherein Si content is 74% in the FeSi alloy, Mn content is 82% in the FeMn alloy, Cr content is 52% in the FeCr alloy, fixation of C is 92% in the hard coal, Si content is 0.25% in the control molten steel, Mn content is 1.01%, Cr content is 0.60%, C content is 0.23%, gone out that to measure molten steel oxygen activity α [O] with apparatus for determination of oxygen behind the steel be 0.0021%, the Als of sample examination molten steel is 0.05% (recovery rate is 60%).
Molten steel begins heating after arriving the LF stove, and stopped heating when liquid steel temperature is heated to 1570 ℃, the Als of sample examination molten steel are 0.025%, and this moment is not owing to carrying out deoxidation to slag, the Als of scaling loss 0.025% in the molten steel.In ladle, feed the aluminum steel 22kg of φ 10 (because slag does not carry out deoxidation with feeding wire machine, the feeding aluminum steel need pass the higher slag blanket of oxidisability, the recovery rate of aluminium is lower than 60% of the technology of the present invention, be about 55%), and then the feeding φ 12 contain Ti cored-wire 145kg (this moment 145kg be core grain weight amount, do not comprise the outer field iron sheet weight of cored-wire, the core powder all is FeTi40, namely contain Ti and be 40% iron alloy), and φ 12 contain B cored-wire 10kg (this moment 10kg be core grain weight amount, do not comprise the outer field iron sheet weight of cored-wire, the core powder all is FeB23, namely contains B and be 23% iron alloy), having fed the chemical composition molten aluminium of acid (Als) of measuring molten steel behind the line is 0.040%, Ti is that 0.06%, B is 0.0019%, and this moment, the recovery rate of B was 65%.
Become 150mm * 150mm strand in the 5 stream billet caster top castings of 5 machines at last, tundish temperature is 1530 ℃ during continuous casting, bag sampling analysis molten steel chemical composition is 0.23% C, 0.25% Si, 1.09% Mn, 0.013% P, 0.009% S, 0.60% Cr, 0.06% Ni, 0.05% Cu, 0.0019% B in continuous caster, and the Als of 0.06% Ti and 0.030% (Als scaling loss 0.010% in the casting cycle), all the other are Fe and inevitable other impurity.The the 1st and the 4th flows out existing serious unsteady flow (be the continuous caster mouth of a river diminish phenomenon) in the molten steel casting, all stops up afterwards in 12 minutes, and all the other runners also have the unsteady flow phenomenon.
Above-described embodiment explanation adopts the technology of the present invention to produce the 25CrMnB steel, whole process control effectively to molten steel oxygen activity and acid-soluble aluminum content, tapping process does not adopt aluminium to carry out pre-deoxidation, and the employing calcium carbide, and carry out strong diffusive deoxidation at the LF stove, replace part aluminium with calcium carbide, reduce acid-soluble aluminum content in the molten steel, the recovery rate of boron is more than 65% behind the adding ferro-boron, both guaranteed the effect that boron improves hardening capacity, in casting 200mm * 200mm and 150mm * 150mm square billet process, the phenomenon of having avoided the continuous caster mouth of a river to diminish is cast smoothly again.Therefore, the inventive method not only can be applicable to the continuous caster of large specification, and is applicable to the following small dimension continuous caster of 200 * 200mm, and assurance small dimension continuous caster can be cast smoothly.
Claims (9)
1. the method for a producing 25 CrMnB steel through converter flow is characterized in that comprising the steps:
A, in converter, add molten iron smelting;
B, molten steel are tapped to ladle, add calcium carbide during tapping and make the molten steel oxygen activity below 0.0025%;
C, ladle move into the refining of LF stove, molten steel per ton adds calcium carbide 3.5～4.5kg before the refining heating, molten steel per ton adds metallic aluminium 0.15～0.45kg in the heat-processed, stopped heating when liquid steel temperature is heated to 1565～1585 ℃, in molten steel, add aluminium, make in the molten steel sour molten aluminium weight percent content 0.011～0.016%, add again titanium and make in the molten steel titanium weight percent content 0.02～0.06%, add boron and make in the molten steel boron weight percent content 0.0005～0.003%;
Carry out continuous casting after d, the refining.
2. the method for producing 25 CrMnB steel through converter flow according to claim 1 is characterized in that: also add steel scrap when adding molten iron in the converter among the step a, the weight of steel scrap is no more than 15% of weight of molten iron.
3. the method for producing 25 CrMnB steel through converter flow according to claim 2 is characterized in that: when just refining of molten steel composition to C by weight percentage is 0.05%～0.15%, in the ladle of molten steel being tapped when P≤0.015% and S≤0.015%.
4. the method for producing 25 CrMnB steel through converter flow according to claim 1, it is characterized in that: among the step b, the calcium carbide add-on is foundation according to endpoint carbon content of converter, when converter terminal carbon weight percent drops into by molten steel 3.5～4.5kg per ton when following 0.10%; When converter terminal carbon weight percent drops into by molten steel 2.5～3.5kg per ton greater than 0.10%, less than 0.15% the time; When converter terminal carbon weight percent drops into by molten steel 1.5～2.5kg per ton when above 0.15%.
5. the method for producing 25 CrMnB steel through converter flow according to claim 1 is characterized in that: also add when adding calcium carbide among the step b ferrosilicon make in the molten steel silicon weight percent content 0.15～0.35%, add ferromanganese make in the molten steel manganese weight percent content 0.80～1.10%, add ferrochrome make in the molten steel weight of chromium degree 0.30～0.60%, add carburelant and make the carbon weight percent content 0.20～0.30%.
6. the method for producing 25 CrMnB steel through converter flow according to claim 1 is characterized in that: molten steel adding calcium carbide 3.8～4.2kg per ton before the refining heating among the step c, molten steel adding metallic aluminium 0.2～0.4kg per ton in the heat-processed.
7. the method for producing 25 CrMnB steel through converter flow according to claim 1 is characterized in that: the mode that adds titanium among the step c is the cored-wire with feeding wire machine feeding titaniferous, and the mode that adds boron is the cored-wire with feeding wire machine feeding boracic.
8. the method for producing 25 CrMnB steel through converter flow according to claim 1 is characterized in that: during the steps d continuous casting in the continuous caster bag temperature be 1530 ± 20 ℃.
9. the method for producing 25 CrMnB steel through converter flow according to claim 1, it is characterized in that: described calcium carbide contains CaC
2More than 70%.
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| CN101045948A (en) * | 2007-04-29 | 2007-10-03 | 攀钢集团攀枝花钢铁研究院 | Method for producing boron steel by smelting in converter |
| CN101343714A (en) * | 2008-08-21 | 2009-01-14 | 攀钢集团成都钢铁有限责任公司 | 30CrMnSiB steel, weldless steel tube for cylinder and method of manufacturing the same |
| CN101358323A (en) * | 2008-08-26 | 2009-02-04 | 攀钢集团成都钢铁有限责任公司 | Seamless steel tube for 27SiMnB steel, cylinder and production method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101045948A (en) * | 2007-04-29 | 2007-10-03 | 攀钢集团攀枝花钢铁研究院 | Method for producing boron steel by smelting in converter |
| CN101343714A (en) * | 2008-08-21 | 2009-01-14 | 攀钢集团成都钢铁有限责任公司 | 30CrMnSiB steel, weldless steel tube for cylinder and method of manufacturing the same |
| CN101358323A (en) * | 2008-08-26 | 2009-02-04 | 攀钢集团成都钢铁有限责任公司 | Seamless steel tube for 27SiMnB steel, cylinder and production method thereof |
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