CN1916190A - Compound deoxidizer in calcium series - Google Patents
Compound deoxidizer in calcium series Download PDFInfo
- Publication number
- CN1916190A CN1916190A CN 200610021721 CN200610021721A CN1916190A CN 1916190 A CN1916190 A CN 1916190A CN 200610021721 CN200610021721 CN 200610021721 CN 200610021721 A CN200610021721 A CN 200610021721A CN 1916190 A CN1916190 A CN 1916190A
- Authority
- CN
- China
- Prior art keywords
- calcium series
- compound deoxidizer
- calcium
- deoxidizer
- steel
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Treatment Of Steel In Its Molten State (AREA)
Abstract
This invention discloses a calcium-based composite deoxidant for molten steel deoxygenation and alloying. The calcium-based composite deoxidant comprised: Ca 35-55 wt.%, Si 15-45 wt.%, C 12-25 wt.%, Fe not higher than 12 wt.%, Al 2-5 wt.% and Ba not higher than 2 wt.%. The simultaneous actions of Ca and Al can form 12CaO .7Al2O3 with small specific surface area and low melting point. Besides, its rising speed is high, thus can reduce the quantities of impurities in molten steel and solve the problem of blockage of continuous-casting water gap. The deoxidant has good deoxidization effect, and can effectively increase the recovery rate alloy elements, modify sulfide lards, improve the processability and mechanical properties of steel, and lower the cost of steel.
Description
Technical field
The present invention relates to a kind of reductor that is used for the deoxidation of molten steel alloying technology, especially relate to the high compound deoxidizer in calcium series of the alloying element rate of recovery.
Background technology
The deoxidation of molten steel alloying technology is the important step that is related to quality product, also is indispensable technology in the STEELMAKING PRODUCTION simultaneously.At present, domestic each big steel mill adopts materials such as aluminium manganese, sial barium or Si-Al-Ba-Ca to carry out deoxidation in molten steel final deoxidation alloy process mostly.This deoxidation and alloying mode be the cost height not only, and is subjected to molten steel terminal point [C], and tapping temperature and the influence of the quantity of slag down cause Si in the molten steel, the fluctuation of Mn composition greatly, alloying element rate of recovery instability.When the reductor add-on was bigger than normal, the sour molten aluminium in the molten steel will be above to a certain degree (AlS＞0.006%), thereby causes generating solid-state Al
2O
3Bunch shape inclusion, molten steel viscosity increases, and inclusion increases and is difficult for come-up to be got rid of, water-coating port dross in finally causing, even continuous casting is disconnected waters.For reducing the STEELMAKING PRODUCTION cost, improve the rate of recovery of alloying element, solve continous casting sprue dross problem, successfully developed compound deoxidizer in calcium series through research for many years, thereby solved the problems referred to above effectively, and in suitability for industrialized production, obtained favorable economic benefit.
Summary of the invention
The object of the present invention is to provide a kind of compound deoxidizer in calcium series, this reductor not only can reduce the STEELMAKING PRODUCTION cost, improves the rate of recovery of alloying element, but also has solved the problem of continous casting sprue dross, remarkable in economical benefits.
Concrete technical scheme of the present invention is as follows:
Compound deoxidizer in calcium series is characterized in that comprising that following component forms by weight ratio:
Ca： 30～55％ Si：15～45％ C：12～25％ Fe：≤12％
Al： 2～5％ Ba：≤2％
Wherein, the preferable range value is:
Ca：32～52％ Si：20～42％ C：14～22％ Fe：≤12％
Al：2～4％ Ba：≤2％
The Ca of described compound deoxidizer in calcium series, C are by CaC
2Allocate into, Si is allocated into by Si-Fe, and Al is allocated into by aluminum shot or aluminium block.
The preparation method of compound deoxidizer in calcium series of the present invention is as follows:
Take by weighing calcium carbide, Si-Fe alloy, aluminium block or aluminum shot respectively by following weight percent, be crushed to below the 20mm, be respectively charged into 3 moistureproof small package bags of bilayer then, the double-deck moistureproof big packing bag of the 10kg that again each small package bag packed into promptly gets product:
CaC
2：30～90％ Si-Fe：10～50％ Al：1～10％
Described Si-Fe alloy can be replaced by SiC, Si-Ca, Si-Ca-Ba material.
The usage quantity of described compound deoxidizer in calcium series is: 1.0～5.0kg/t steel.
Product of the present invention should guard against damp, and the quality guaranteed period should not surpass 20 days, stores on-the-spot Fire Hazard Area.
The using method of compound deoxidizer in calcium series of the present invention is:
Add at tapping process, after tapping 10～15 seconds, the auxiliary chute of packed compound deoxidizer in calcium series behind the steel-making converter stove added or artificial the input, and before adding iron alloy, add all reductors.
The ultimate principle of compound deoxidizer in calcium series of the present invention is as follows:
We know, and people are by after adding the Ba element in the ferrosilicoaluminum reductor, and its deoxidizing capacity has obtained rising significantly, and as consanguinity Ca element, its deoxidation more has superiority than Ba, because of both molar mass ratio is: Ca: Ba=1: 3.426
Promptly remove a certain amount of oxygen, if need the Ca of 1kg, then Ba needs 3.24kg.And the solubleness of Ca in molten steel is very little, is 0.032% in the time of 1600 ℃, dissolving hardly in the solid steel; The vapor pressure of Ca is very big simultaneously, is 1.98 normal atmosphere in the time of 1600 ℃.Therefore, only use single Ca too big as reductor consumption, unreasonable economically, in order to improve the deoxidation efficient of Ca, need to improve the solubleness of Ca in molten steel, can promote the raising of solubleness by adding a certain amount of C, Si, Al element.And the effect of C is maximum, and every 1%C can improve one times of the solubleness of Ca.Therefore, the calcium deoxidizer main component is CaC
2Also have Si-Fe and Al, Ba etc. in addition outward.When using block Ca alloy,, reach capacity very soon in the part because the dissolution process of Ca is subjected to the frictional belt diffusional limitation, thereby can not make molten steel dissolve more Ca, major part will be evaporated, and make＜the 20mm fine granularity, can address this problem effectively.
Consider Al crystal grain thinning and the effect of fixed nitrogen minimizing timeliness in steel, also an amount of Al should be arranged during final deoxygenation, contain Al:1～1.5% in the general ferrosilicon, compound deoxidizer in calcium series is joined Al also 2～5%, and Ca and Al interaction energy generation simultaneously fusing point has only 1455 ℃ spherical 12CaO7Al like this
2O
3, having less specific surface area, ascent rate is fast, the amount of inclusion significantly reduces in the molten steel thereby make, and remains in a small amount of 12CaO7Al in the steel
2O
3Inclusion is also indeformable in rolling, can not form Al
2O
3The sort of sharp-pointed chain of inclusion distributes, and can reduce the anisotropic of steel, and good processing characteristics and mechanical property are arranged.
The invention has the advantages that:
1, compound deoxidizer in calcium series of the present invention not only has good deoxidation effect, and has also effectively improved the rate of recovery of alloying element under the situation that usage quantity reduces.
2, Ca in the compound deoxidizer in calcium series of the present invention and Al while interaction energy generates the 12CaO7Al with less specific surface area
2O
3, its ascent rate is fast, the amount of inclusion significantly reduces in the molten steel thereby make, and has solved the problem of continous casting sprue dross.
3, compound deoxidizer in calcium series of the present invention effectively reduces STEELMAKING PRODUCTION cost, remarkable in economical benefits.
4, to contain Ca amount high because of it for compound deoxidizer in calcium series of the present invention, therefore has sweetening power preferably and to the Denaturation of sulfide inclusion, can improve steel processing and mechanical property in the tapping deoxidization alloying process.
Embodiment
Embodiment 1
A kind of compound deoxidizer in calcium series is characterized in that comprising that following component forms by weight ratio:
Ca：30％ Si：31.5％ C：18％
Fe：10.5％ Al：10％
The preparation method of compound deoxidizer in calcium series of the present invention is as follows:
Take by weighing calcium carbide, Si-Fe alloy, aluminium block respectively by following weight percent, be crushed to below the 20mm, be respectively charged into 3 moistureproof small package bags of bilayer then, the double-deck moistureproof big packing bag of the 10kg that again each small package bag packed into promptly gets product:
CaC
2：48％ Si-Fe：42％ Al：10％
The usage quantity of described compound deoxidizer in calcium series is: 1.0～5.0kg/t steel.
The using method of compound deoxidizer in calcium series of the present invention is:
After tapping 10～15 seconds, the auxiliary chute of packed compound deoxidizer in calcium series behind the steel-making converter stove added, and before adding iron alloy, add all reductors.
Embodiment 2
A kind of compound deoxidizer in calcium series is characterized in that comprising that following component forms by weight ratio:
Ca：55％ Si：8％ C：30％
Al：5％ Ba：2％
The preparation method of compound deoxidizer in calcium series of the present invention is as follows:
Take by weighing calcium carbide, Si-Ca-Ba, aluminum shot respectively by following weight percent, be crushed to below the 20mm, be respectively charged into 3 moistureproof small package bags of bilayer then, the double-deck moistureproof big packing bag of the 10kg that again each small package bag packed into promptly gets product:
CaC
2：80％ Si-Ca-Ba：15％ Al：5％
The usage quantity of described compound deoxidizer in calcium series is: 1.0～5.0kg/t steel.
The using method of compound deoxidizer in calcium series of the present invention is:
After tapping 10～15 seconds, the auxiliary chute of packed compound deoxidizer in calcium series behind the steel-making converter stove manually dropped into, and before adding iron alloy, add all reductors.
Embodiment 3
A kind of compound deoxidizer in calcium series is characterized in that comprising that following component forms by weight ratio:
Ca：40％ Si：23％ C：33％ Al：4％
The preparation method of compound deoxidizer in calcium series of the present invention is as follows:
Take by weighing calcium carbide, SiC, aluminum shot respectively by following weight percent, be crushed to below the 20mm, be respectively charged into 3 moistureproof small package bags of bilayer then, the double-deck moistureproof big packing bag of the 10kg that again each small package bag packed into promptly gets product:
CaC
2：65％ SiC：31％ Al：4％
The usage quantity of described compound deoxidizer in calcium series is: 1.0～5.0kg/t steel.
The using method of compound deoxidizer in calcium series of the present invention is:
After tapping 10～15 seconds, the auxiliary chute of packed compound deoxidizer in calcium series behind the steel-making converter stove manually dropped into, and before adding iron alloy, add all reductors.
Embodiment 4
A kind of compound deoxidizer in calcium series is characterized in that comprising that following component forms by weight ratio:
Ca：45％ Si：25％ C：20％ Al：4％ Fe：6％
The preparation method of compound deoxidizer in calcium series of the present invention is as follows:
Take by weighing calcium carbide, Si-Ca, aluminum shot respectively by following weight percent, be crushed to below the 20mm, be respectively charged into 3 moistureproof small package bags of bilayer then, the double-deck moistureproof big packing bag of the 10kg that again each small package bag packed into promptly gets product:
CaC
2：55％ Si-Ca：41％ Al：4％
The usage quantity of described compound deoxidizer in calcium series is: 1.0～5.0kg/t steel.
The using method of compound deoxidizer in calcium series of the present invention is:
After tapping 10～15 seconds, the auxiliary chute of packed compound deoxidizer in calcium series behind the steel-making converter stove manually dropped into, and before adding iron alloy, add all reductors.
Embodiment 5
A kind of compound deoxidizer in calcium series is characterized in that comprising that following component forms by weight ratio:
Ca：30％ Si：30％ C：21％ Al：10％ Fe：9％
The preparation method of compound deoxidizer in calcium series of the present invention is as follows:
Take by weighing calcium carbide, Si-Ca, aluminium flake respectively by following weight percent, be crushed to below the 20mm, be respectively charged into 3 moistureproof small package bags of bilayer then, the double-deck moistureproof big packing bag of the 10kg that again each small package bag packed into promptly gets product:
CaC
2：30％ Si-Ca 50％ Al：10％
The usage quantity of described compound deoxidizer in calcium series is: 1.0～5.0kg/t steel.
The using method of compound deoxidizer in calcium series of the present invention is:
After tapping 10～15 seconds, the auxiliary chute of packed compound deoxidizer in calcium series behind the steel-making converter stove manually dropped into, and before adding iron alloy, add all reductors.
Embodiment 7: compound deoxidizer in calcium series application test of the present invention
1, tests condition and method
1.1 test steel grade: B level steel, 25MnV-1
1.2 test method:
Aluminium block and CaBaAlSi are adopted in former converter tapping deoxidation, and the every stove of CaBaAlSi adds 240kg (3.0Kg/t steel); Aluminium block and compound deoxidizer in calcium series are adopted in deoxidation during test, and the aluminium block add-on is with using CaBaAlSi.Every stove adds 200Kg (2.5Kg/t steel) compound deoxidizer in calcium series, compound deoxidizer in calcium series in tapping process by in the artificial adding bag.
2, test-results
2.1 deoxidation effect
2.1.1 oxygen activity
The deoxidation effect of reductor uses the equilibrium oxygen activity that is reached after the clearance of oxygen activity before and after the deoxidation and the deoxidation to estimate usually.When the test compound deoxidizer in calcium series, 80t converter tapping process adds compound deoxidizer in calcium series, has measured the part heat respectively into and out of the station oxygen activity of molten steel at the LF stove, and experimental result sees Table 1.
Table 1 uses the molten steel oxygen activity (ppm) behind the compound deoxidizer in calcium series
| Heat (batch) number | Steel grade | LF enters the station | The LF station of setting off |
| 06303790 | B | 1.3 | 3.8 |
| 06303791 | B | 2.0 | 5.0 |
| 06303803 | 25MnV-1 | 2.0 | 3.9 |
| 06303804 | 25MnV-1 | 11.0 | 2.7 |
| 06303805 | 25MnV-1 | 3.9 | 4.3 |
| 06303806 | 25MnV-1 | 3.0 | 2.2 |
| 06303807 | 25MnV-1 | 14.7 | 3.5 |
| 06303828 | B | 2.6 | 2.7 |
| 06303829 | B | 2.0 | 4.3 |
| 06303830 | B | 19.2 | 4.3 |
| 06303831 | B | 22.2 | 2.7 |
| 06303832 | B | 2.3 | 5.0 |
| 06303833 | B | 2.4 | 3.0 |
| 06303834 | B | 1.6 | 3.7 |
| 06303835 | B | 2.7 | 5.0 |
| Scope | 1.3～22.2 | 2.2～5.0 | |
| On average | 6.2 | 3.8 |
As seen from the above table, after in molten steel, adding compound deoxidizer in calcium series, no matter produce B level steel and still produce oxygen activity after oil casing steel (25MnV-1) deoxidation, and most below 5ppm all less than 25ppm, after the LF stove is concise in the steel dissolved oxygen all in 5ppm.Molten steel oxygen activity after 1 stove that duration of test is measured uses the deoxidation of CaBaAlSi reductor is 3.3ppm simultaneously.Therefore, oxygen activity from steel after the deoxidation, the deoxidation effect of compound deoxidizer in calcium series is good, in existing deoxidation scheme, use 200Kg (2.5Kg/t steel) compound deoxidizer in calcium series to substitute 240Kg (3.0Kg/t steel) reductor, can guarantee that deoxidation of molten steel is good, satisfy the production requirement of each tube blank steel.
2.1.2 strand gas content
T[O in the steel] for dissolved oxygen be mingled with the oxygen sum.Reductor is to dissolved oxygen in the steel and to be mingled with oxygen all influential, and good reductor not only can be deviate from dissolved oxygen in the steel, and the deoxidation products that the generates discharge of can in time floating, thereby T[O in the steel] little.In order further to investigate the deoxidation effect of compound deoxidizer in calcium series, the continuously cast bloom of having got 5 stove compound deoxidizer in calcium series deoxidations and 2 stove CaBaAlSi reductor deoxidations has respectively carried out T[O] and the analysis of N, it the results are shown in Table 2
Table 2 strand T[O] and N content
| Heat (batch) number | Steel grade | T[O] and N content (ppm) | |||
| Compound deoxidizer in calcium series | The CaBaAlSi reductor | ||||
| T[O] | N | T[O] | N | ||
| 6303784 | B | 35 | 58 | ||
| 6303837 | B | 55 | 52 | ||
| 6303790 | B | 33 | 81 | ||
| 6303791 | B | 38 | 49 | ||
| 6303803 | 25MnV-1 | 33 | 89 | ||
| 6303805 | 25MnV-1 | 35 | 85 | ||
| 6303828 | B | 48 | 65 | ||
Can see by table 2, use the T[O of compound deoxidizer in calcium series strand] a little less than the T[O that uses CaBaAlSi reductor strand].
In sum, use the deoxidation effect of compound deoxidizer in calcium series to be not less than use CaBaAlSi reductor, can satisfy the production requirement of each tube blank steel fully.
2.2 strand is mingled with
Above-mentioned strand is carried out T[O] when analyzing, and carried out being mingled with the analysis of total amount and component, it the results are shown in Table 3.
Table 3 strand is mingled with content (%)
| Heat (batch) number | Reductor | Be mingled with content | ||||
| Total amount | Al 2O 3 | SiO 2 | FeO | MnO | ||
| 6303784 | CaBaAlSi | 0.0165 | 0.0045 | 0.0032 | 0.0030 | 0.0001 |
| 6303837 | 0.0095 | 0.0023 | 0.0025 | 0.0016 | 0.0001 | |
| 6303790 | Ca system | 0.0100 | 0.0025 | 0.0030 | 0.0008 | 0.0001 |
| 6303791 | 0.0115 | 0.0023 | 0.0032 | 0.0031 | 0.0001 | |
| 6303803 | 0.0090 | 0.0021 | 0.0025 | 0.0018 | 0.0002 | |
| 6303805 | 0.0090 | 0.0020 | 0.0025 | 0.0003 | 0.0001 | |
| 6303828 | 0.0095 | 0.0025 | 0.0025 | 0.0016 | 0.0001 | |
Can see that by table 3 that uses the compound deoxidizer in calcium series strand is mingled with content a little less than the content that is mingled with that uses CaBaAlSi reductor strand.The T[O of this and strand] content is consistent.
In sum, use compound deoxidizer in calcium series suitable with use CaBaAlSi reductor to the removal effect of inclusion.
2.3 influence to the slag composition
Test heat converter finishing slag and the LF slag specimen composition that enters the station sees Table 4.
The slag specimen composition (%) of table 4 test heat
| Title | SiO | AlO | CaO | MgO | S | FeO | MnO | TFe |
| Converter terminal | 7.88 | 1.43 | 47.60 | 6.75 | 0.192 | 3.55 | 18.55 | |
| LF enters the station | 13.52 | 18.8 | 54.44 | 5.88 | 0.75 | 1.27 | 0.8 |
By table 4 as seen, the oxidisability from converter terminal to the LF slag reduces behind deoxidation alloying significantly, the enter the station FeO average out to 1.27 of slag specimen of LF, and 50% above heat is lower than 1.0 (seeing Table 1).Show thus, because the modifying function that compound deoxidizer in calcium series has certain ladle slag, in the refining of LF stove, help forming rapidly the white slag refining, favourable to being mingled with, improving the molten steel purity in the removal steel, refining finishes T[O in the steel of back] in 20～55 (ppm) scope, average out to 34.3ppm.
2.4 influence to sulphur in the steel
After adding compound deoxidizer in calcium series in the test, converter terminal to LF concise before, promptly the reduced rate of [S] is 14.28～19.23% in tapping process, average out to 16.78%.Illustrate and use compound deoxidizer in calcium series that the effect that promotes LF stokehold phase desulfurization is arranged.
3, the analysis of economic benefit
The direct economic benefit of compound deoxidizer in calcium series is mainly reflected in the benefit of deoxidation lament price variance and usage quantity generation:
J1＝W2×3.0/1000-W1×2.5/1000
In the formula: the economic benefit that the J1-price variance produces, unit/ton steel
The price of W1-compound deoxidizer in calcium series, unit/ton
The price of W2-CaBaAlSi reductor, unit/ton
By the price of present CaBaAlSi: 7800.00 yuan/ton, the price of compound deoxidizer in calcium series: 6700.00 yuan of/ton calculating as can be known: the latter reduces cost than the former: 6.65 yuan/ton.
4, conclusion
1, deoxidation effect: test shows that compound deoxidizer in calcium series has good deoxidation effect, uses the deoxidation effect of compound deoxidizer in calcium series to be not less than use CaBaAlSi reductor.
2, strand is mingled with: use the compound deoxidizer in calcium series strand be mingled with content with use CaBaAlSi reductor strand to be mingled with content suitable.
3, use compound deoxidizer in calcium series can improve the alloying element recovery rate, reduce the reductor add-on, can reduce by 6.65 yuan/ton of STEELMAKING PRODUCTION costs, therefore, have present direct economic benefit.
4, sweetening effectiveness: after adopting compound deoxidizer in calcium series, because of its calcium content height, so in the tapping deoxidization alloying process, have deoxidizing capacity preferably; Because of it has the characteristic of diffusive deoxidation, so help reducing fast the sweetening power in early stage of the oxidisability in the first slag, the slagging of quickening refining furnace and raising refining slag.
Claims (7)
1, compound deoxidizer in calcium series is characterized in that comprising that following component forms by weight ratio:
Ca：30～55％ Si：15～45％ C：12～25％ Fe：≤12％
Al：2～5％ Ba：≤2％。
2, compound deoxidizer in calcium series according to claim 1 is characterized in that comprising that following component forms by weight ratio:
Ca：32～52％ Si：20～42％ C：14～22％ Fe：≤12％
Al：2～4％ Ba：≤2％。
3, according to the described compound deoxidizer in calcium series of claim 1, the Ca, the C that it is characterized in that described compound deoxidizer in calcium series are by CaC
2Allocate into, Si is allocated into by Si-Fe, and Al is allocated into by aluminum shot or aluminium block.
4, compound deoxidizer in calcium series according to claim 1 and 2 is characterized in that the preparation method is as follows:
Take by weighing calcium carbide, Si-Fe alloy, aluminium block or aluminum shot respectively by following weight percent, be crushed to below the 20mm, be respectively charged into 3 moistureproof small package bags of bilayer then, the double-deck moistureproof big packing bag of the 10kg that again each small package bag packed into promptly gets product:
CaC
2：30～90％ Si-Fe：10～50％ Al：1～10％。
5, compound deoxidizer in calcium series according to claim 4 is characterized in that described Si-Fe alloy is replaced by SiC, Si-Ca, Si-Ca-Ba material.
6, compound deoxidizer in calcium series according to claim 1 is characterized in that the usage quantity of described compound deoxidizer in calcium series is: 1.0～5.0kg/t steel.
7, compound deoxidizer in calcium series according to claim 1, the using method that it is characterized in that described compound deoxidizer in calcium series is: add in tapping process, after tapping 10～15 seconds, the auxiliary chute of packed compound deoxidizer in calcium series behind the steel-making converter stove added or artificial the input, and before adding iron alloy, add all reductors.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100217216A CN100398670C (en) | 2006-08-31 | 2006-08-31 | Compound deoxidizer in calcium series |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100217216A CN100398670C (en) | 2006-08-31 | 2006-08-31 | Compound deoxidizer in calcium series |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1916190A true CN1916190A (en) | 2007-02-21 |
| CN100398670C CN100398670C (en) | 2008-07-02 |
Family
ID=37737253
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100217216A Expired - Fee Related CN100398670C (en) | 2006-08-31 | 2006-08-31 | Compound deoxidizer in calcium series |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100398670C (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102220454A (en) * | 2010-04-19 | 2011-10-19 | 广东延能新材料科技有限公司 | Steelmaking method of microalloy steel with added vanadium nitride alloy in steel |
| CN102776321A (en) * | 2011-05-11 | 2012-11-14 | 宝钢集团新疆八一钢铁有限公司 | Novel calcium-adding method for preventing nozzle clogging of steel furnace continuous casting |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU990832A1 (en) * | 1981-10-28 | 1983-01-23 | Предприятие П/Я М-5481 | Method for making steel |
| JPS6333514A (en) * | 1986-07-24 | 1988-02-13 | Nippon Steel Corp | Manufacture of molten steel containing calcium by refining |
| CN1027701C (en) * | 1989-08-07 | 1995-02-22 | 冶金工业部攀枝花钢铁公司钢铁研究院 | Deoxidising agent for manufacture of steel with converters |
| CN100343398C (en) * | 2005-12-16 | 2007-10-17 | 安阳市龙泉华贯冶金厂 | Method for preparing silicon aluminium calcium composite deoxidant |
-
2006
- 2006-08-31 CN CNB2006100217216A patent/CN100398670C/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102220454A (en) * | 2010-04-19 | 2011-10-19 | 广东延能新材料科技有限公司 | Steelmaking method of microalloy steel with added vanadium nitride alloy in steel |
| CN102220454B (en) * | 2010-04-19 | 2013-04-10 | 蔡惜辉 | Steelmaking method of microalloy steel with added vanadium nitride alloy in steel |
| CN102776321A (en) * | 2011-05-11 | 2012-11-14 | 宝钢集团新疆八一钢铁有限公司 | Novel calcium-adding method for preventing nozzle clogging of steel furnace continuous casting |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100398670C (en) | 2008-07-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1056415C (en) | Aluminium-contained premelting slag and preparation method therefor, and molten steel desulfurizer and purifier containing same | |
| CN1818093A (en) | High-efficient metallurgical refiner and preparation thereof | |
| CN1209479C (en) | Multielement high-chromium wear-resisting cast-iron sieve-plate and production thereof | |
| CN101665858A (en) | Steel ladle slag modifier for external refining | |
| CN1916190A (en) | Compound deoxidizer in calcium series | |
| CN1850996A (en) | Method for direct making iron and steel by converter using waste iron and steel furnace burden | |
| CN1327007C (en) | Al-Mg-Ca-Fe alloy contg. micro-carbon, low silicon, low phosphorous, low-sulphur used for steelmaking | |
| CN1818094A (en) | Steel liquid cleaner for steel smelting | |
| CN1912148A (en) | Iron and steel metallurgical compound refining agent | |
| RU2515709C2 (en) | Charge to produce vanadium cast iron | |
| CN101121952A (en) | Micro-carbon, low-silicon, low-phosphor and low-sulphur aluminum-magnesium-calcium-iron alloy used for smelting steel and deoxidizing | |
| CN1218060C (en) | High-strength low alloy steel micro alloying by using rich-nitrogen and vanadium-containing alloy and its smelting method | |
| CN1626682A (en) | Converter refined slaging medium and slagging technique | |
| CN1023572C (en) | Compound spheroidizing inoculant | |
| CN1209471C (en) | Composite metallurgical refining agent | |
| CN105624365B (en) | A kind of alkaline earth oxide is combined molten steel refining agent and preparation method thereof | |
| CN1150338C (en) | Al-Mg alloy for deoxidizing and desulfurizing in smelting steel | |
| CN110453040A (en) | A kind of alumal deoxidier and its deoxidation in steel making method | |
| RU2456349C1 (en) | Procedure for out-of-furnace treatment of iron-carbon melt | |
| CN1033292A (en) | Cast steel | |
| CN1050746A (en) | Spheroidal graphite cast iron | |
| CN1215086A (en) | Agent for refining and heat-insulating of molten steel surface and its preparation process | |
| CN1818092A (en) | Preparation of steel-smelting carburant | |
| JP2008266768A (en) | Steel ingot for forging | |
| JP2004346402A (en) | Method of refining steel material for spring |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080702 Termination date: 20150831 |
|
| EXPY | Termination of patent right or utility model |