WO2024066378A1 - 一种改善钒钛矿冶炼高钛炉渣性能的喷吹方法 - Google Patents
一种改善钒钛矿冶炼高钛炉渣性能的喷吹方法 Download PDFInfo
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- WO2024066378A1 WO2024066378A1 PCT/CN2023/093814 CN2023093814W WO2024066378A1 WO 2024066378 A1 WO2024066378 A1 WO 2024066378A1 CN 2023093814 W CN2023093814 W CN 2023093814W WO 2024066378 A1 WO2024066378 A1 WO 2024066378A1
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- Prior art keywords
- blast furnace
- titanium
- slag
- coal
- vanadium
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- 239000002893 slag Substances 0.000 title claims abstract description 51
- 238000002347 injection Methods 0.000 title claims abstract description 38
- 239000007924 injection Substances 0.000 title claims abstract description 38
- 238000003723 Smelting Methods 0.000 title claims abstract description 30
- 239000010936 titanium Substances 0.000 title claims abstract description 27
- 229910052719 titanium Inorganic materials 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims abstract description 22
- 239000003245 coal Substances 0.000 claims abstract description 45
- 239000000843 powder Substances 0.000 claims abstract description 22
- 238000010298 pulverizing process Methods 0.000 claims abstract description 12
- 238000002156 mixing Methods 0.000 claims abstract description 8
- 239000011812 mixed powder Substances 0.000 claims abstract description 7
- 238000006243 chemical reaction Methods 0.000 claims abstract description 5
- QYHKLBKLFBZGAI-UHFFFAOYSA-N boron magnesium Chemical compound [B].[Mg] QYHKLBKLFBZGAI-UHFFFAOYSA-N 0.000 claims description 26
- GFNGCDBZVSLSFT-UHFFFAOYSA-N titanium vanadium Chemical compound [Ti].[V] GFNGCDBZVSLSFT-UHFFFAOYSA-N 0.000 claims description 20
- 239000002245 particle Substances 0.000 claims description 18
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 4
- 239000003830 anthracite Substances 0.000 claims description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 4
- 239000002802 bituminous coal Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 229910052760 oxygen Inorganic materials 0.000 claims description 4
- 239000001301 oxygen Substances 0.000 claims description 4
- 229910052681 coesite Inorganic materials 0.000 claims description 3
- 229910052906 cristobalite Inorganic materials 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- 235000012239 silicon dioxide Nutrition 0.000 claims description 3
- 229910052682 stishovite Inorganic materials 0.000 claims description 3
- 229910052905 tridymite Inorganic materials 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims 1
- 238000002844 melting Methods 0.000 abstract description 10
- 230000008018 melting Effects 0.000 abstract description 10
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 abstract description 6
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 abstract description 2
- 150000001450 anions Chemical class 0.000 abstract description 2
- 229910001424 calcium ion Inorganic materials 0.000 abstract description 2
- 230000002378 acidificating effect Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 11
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 8
- 239000010436 fluorite Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 229910001634 calcium fluoride Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/008—Composition or distribution of the charge
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/001—Injecting additional fuel or reducing agents
- C21B5/003—Injection of pulverulent coal
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/04—Making slag of special composition
Definitions
- the present invention belongs to the technical field of blast furnace ironmaking, and more specifically, relates to a blasting method for improving the performance of high-titanium slag in smelting vanadium-titanium ore.
- the general method is to add a certain proportion of block fluorite ore to the top of the blast furnace with the charge, and the proportion is generally about 0.5% of the charge, using the low melting point of fluorite ore to reduce the melting point of vanadium-titanium blast furnace slag, thereby improving the performance of vanadium-titanium slag.
- This method has a very low addition ratio, and the distribution after entering the blast furnace is extremely uneven, resulting in a large segregation of the CaF2 content in the liquid slag.
- the slag with concentrated fluorite content has good fluidity and a high CaF2 content in the slag, while the fluorite content in most areas is extremely low, and the CaF2 content in the slag is low.
- the improvement effect of the slag performance is poor, resulting in unstable and fluctuating performance of the high-titanium slag, which affects the stable production of the blast furnace.
- fluorite is added from the top of the furnace, due to its low melting point, it will cause certain erosion and scouring problems on the furnace lining after melting in the upper part of the blast furnace, reducing the service life of the lining.
- the present invention designs a method to improve the vanadium-titanium ore smelting high titanium furnace Slag injection method.
- a vanadium-titanium ore injection method for improving the performance of high-titanium slag in smelting comprising: adding boron-magnesium ore and injection coal together into a blast furnace pulverizing coal injection system for pulverizing and fully mixing, and then allowing the mixed powder to enter the blast furnace coal powder injection system and be injected into the blast furnace through the tuyere of the blast furnace to participate in the slag-making reaction.
- the amount of the injected coal is 90-98% by mass, and the amount of the boron-magnesium ore is 2-10% by mass.
- the PCI coal includes anthracite, bituminous coal and a mixture thereof.
- a blast furnace coal pulverizing system includes a coal mill.
- the content of B 2 O 3 in the boron-magnesium ore is 10-15%, the content of MgO is 45-55%, and the content of SiO 2 is 8-10% by mass.
- the particle size of the PCI coal used is less than 40 mm.
- the boron-magnesium ore is in the form of a lump with a particle size greater than 10 mm that is crushed to a powder with a particle size less than 5 mm, or in the form of a powder with a particle size less than 10 mm.
- the proportion of the powder having a particle size less than 0.074 mm after powder making and mixing is more than 60%.
- the mixed powder is distributed to each tuyere of the blast furnace through a coal injection distributor, and is sprayed into the furnace of the blast furnace through a tuyere coal injection gun.
- the conditions for blast furnace smelting are that the hot air temperature is 1150-1250° C. and the oxygen enrichment rate is 3-8%.
- the present invention has the following advantages compared with the prior art:
- the present invention mainly utilizes boron -magnesium ore powder and blast furnace injection coal powder to be sprayed into the blast furnace at the same time. Because B2O3 in the boron-magnesium ore is used as an acid anion in the slag and its ability to combine with calcium ions is greater than that of TiO2-3 ions, the B2O3 component in the boron-magnesium ore can reduce the amount of perovskite with a high melting point. The reduction in the amount of perovskite can further reduce the viscosity and melting temperature of high-titanium blast furnace slag, thereby improving the smelting performance of high-titanium slag. At the same time, the MgO content in the boron-magnesium ore is also relatively high, and the increase in the MgO content Adding is also beneficial to improve the performance of slag.
- An embodiment of the present invention provides a vanadium-titanium ore smelting high-titanium slag injection method, which specifically comprises: adding boron-magnesium ore and injection coal together into a blast furnace pulverizing coal injection system for pulverizing and fully mixing, and then allowing the mixed powder to enter the blast furnace coal powder injection system and be sprayed into the blast furnace through the tuyere of the blast furnace to participate in the slag-making reaction.
- the viscosity and melting temperature of high-titanium blast furnace slag can be reduced, thereby improving the smelting performance of high-titanium blast furnace slag.
- the amount of injected coal is 90-98wt%, and the amount of boron-magnesium ore is 2-10wt%.
- the pulverized coal includes anthracite, bituminous coal and a mixture of the two.
- the blast furnace coal pulverizing system is preferably a coal mill.
- the content of B 2 O 3 in the boron-magnesium ore is 10-15wt%
- the content of MgO is 45-55wt%
- the content of SiO 2 is 8-10wt%.
- the particle size of the pulverized coal used is less than 40mm, and the boron-magnesium ore uses lumps with a particle size greater than 10mm that are crushed to a powder with a particle size less than 5mm or uses powder with a particle size less than 10mm.
- the proportion of the powder having a particle size less than 0.074 mm after powder making and mixing is more than 60%.
- the mixed powder is distributed to each tuyere of the blast furnace through the coal injection distributor, and is sprayed into the furnace of the blast furnace through the tuyere coal injection gun.
- the conditions for blast furnace smelting are hot air temperature of 1150-1250°C, oxygen-enriched The rate is 3 to 8%.
- the boron-magnesium ore and the injection coal are added to the coal mill for pulverization, and are fully mixed in the coal mill. Then, the two mixed materials are injected into the blast furnace through the blast furnace coal powder injection system through the blast furnace tuyere for slag-making reaction.
- the boron-magnesium ore powder is evenly injected into the blast furnace from the blast furnace circumferential tuyere, participates in slag-making, thereby improving the slag performance, realizing uniform improvement of the slag performance, and is beneficial to the smelting of the blast furnace.
- the amount of PCI is 90-98wt%, and the amount of boron-magnesium ore is 2-10wt%.
- PCI includes anthracite, bituminous coal and a mixture of the two.
- the content of B2O3 in the boron-magnesium ore is 12%, the content of MgO is 50%, and the content of SiO2 is 8%.
- the particle size of the PCI is about 30mm, and the particle size of the boron-magnesium ore is about 4mm.
- the proportion of the particle size of the powder after powdering and mixing is less than 0.074mm is 80%.
- the conditions for blast furnace smelting are hot air temperature of 1200°C and oxygen enrichment rate of 8%.
- the slag properties were investigated by considering the changes in the coal injection ratio (kg/tFe) (the amount of coal injected) and the proportion of boron and magnesium ore:
- the proportion of boron-magnesium ore can be changed according to the change of proportion.
- the B 2 O 3 content and MgO content in slag will also change.
- the B 2 O 3 content in slag increases, the ternary basicity R3 also increases, and the melting temperature of slag decreases, thereby improving the performance of slag.
- the iron content in slag decreases, the blast furnace utilization coefficient increases, and the smelting of vanadium-titanium ore blast furnace is effectively strengthened.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Iron (AREA)
Abstract
本发明涉及一种改善钒钛矿冶炼高钛炉渣性能的喷吹方法，包括：将硼镁矿石与喷吹煤一起加入到高炉喷吹煤制粉系统中进行制粉并充分混匀，然后使混匀后的粉体进入高炉煤粉喷吹系统并经过高炉的风口喷入到高炉内参与造渣反应。本发明主要利用硼镁矿粉与高炉喷吹煤粉同时喷入高炉，因硼镁矿中B2O3在炉渣中作为酸性阴离子，并且与钙离子结合的能力大于TiO2
-3离子，由此利用硼镁矿中的B2O3成分可以减少高熔点的钙钛矿生成量，钙钛矿生成量的减少进而可以导致高钛型高炉渣粘度和熔化性温度降低，从而改善高钛炉渣的冶炼性能；同时硼镁矿中的MgO含量也较高，MgO含量的增加也有利于改善炉渣的性能。
Description
本发明属于高炉炼铁技术领域，并且更具体地，涉及一种改善钒钛矿冶炼高钛炉渣性能的喷吹方法。
目前，冶炼高钛型钒钛磁铁矿时，由于炉渣TiO2含量高，炉渣中TiO2发生过还原反应后生成低价Ti(C,N)，由此会导致炉渣性能变差，使炉渣熔化性温度上升，炉渣粘度上升，渣铁分离也困难，严重影响钒钛磁铁矿高炉的冶炼。通常为了改善高钛炉渣的性能，一般采用的方法是在高炉的炉顶随着炉料加入一定比例的块状萤石矿石，其比例一般为加入炉料的0.5％左右，利用萤石矿石的熔点较低的特性来降低钒钛高炉渣的熔点，从而改善钒钛炉渣的性能。这种方法由于加入的比例很低，进入高炉后分布极不均匀，造成了液态炉渣中CaF2含量的偏析很大，萤石含量集中部位的炉渣流动性好，炉渣中CaF2含量较高，而大部份区域的萤石含量极低，炉渣中CaF2含量低，炉渣性能的改善效果较差，造成了高钛炉渣的性能不稳定，波动大，影响了高炉的稳定生产。同时，萤石从炉顶加入后，因萤石熔点较低在高炉上部熔化后对炉衬将产生一定的侵蚀及冲刷问题，降低了内衬的使用寿命。
因此，上述现有技术有待改进。
发明内容
为了解决现有的技术问题，本发明设计了一种改善钒钛矿冶炼高钛炉
渣性能的喷吹方法。
根据本发明的方面，提供一种改善钒钛矿冶炼高钛炉渣性能的喷吹方法，包括：将硼镁矿石与喷吹煤一起加入到高炉喷吹煤制粉系统中进行制粉并充分混匀，然后使混匀后的粉体进入高炉煤粉喷吹系统并经过高炉的风口喷入到高炉内参与造渣反应。
在本发明的一个实施例中，按照质量百分比计，喷吹煤的用量为90～98％，硼镁矿石的用量为2～10％。
在本发明的一个实施例中，喷吹煤包括无烟煤、烟煤及两者混合物。
在本发明的一个实施例中，高炉喷吹煤制粉系统包括磨煤机。
在本发明的一个实施例中，按照质量百分比计，硼镁矿石中B2O3的含量为10～15％，MgO的含量为45～55％，SiO2的含量为8～10％。
在本发明的一个实施例中，使用的喷吹煤的粒度小于40mm。
在本发明的一个实施例中，硼镁矿石使用粒度大于10mm的块状物经破碎至粒度小于5mm后的粉状物或使用粒度小于10mm的粉状物。
在本发明的一个实施例中，制粉混匀后的粉体的粒度小于0.074mm的比例在60％以上。
在本发明的一个实施例中，混匀后的粉体通过喷煤分配器分配到高炉的各个风口，并通过风口喷煤枪喷入高炉的炉缸内。
在本发明的一个实施例中，高炉冶炼的条件是热风温度为1150～1250℃，富氧率为3～8％。
由于采用以上技术方案，本发明与现有技术相比具有如下优点：
本发明主要利用硼镁矿粉与高炉喷吹煤粉同时喷入高炉，因硼镁矿中B2O3在炉渣中作为酸性阴离子，并且与钙离子结合的能力大于TiO2
-3离子，由此利用硼镁矿中的B2O3成分可以减少高熔点的钙钛矿生成量，钙钛矿生成量的减少进而可以导致高钛型高炉渣粘度和熔化性温度降低，从而改善高钛炉渣的冶炼性能；同时硼镁矿中的MgO含量也较高，MgO含量的增
加也有利于改善炉渣的性能。
为了使本发明的目的、技术方案及优点更加清楚明白，下面结合实施例，对本发明进行进一步详细说明。应当理解，此处所描述的具体实施例仅用以解释本发明，并不用于限定本发明。
本发明的实施例中提供了一种改善钒钛矿冶炼高钛炉渣性能的喷吹方法，该方法具体为：将硼镁矿石与喷吹煤一起加入到高炉喷吹煤制粉系统中进行制粉并充分混匀，然后使混匀后的粉体进入高炉煤粉喷吹系统并经过高炉的风口喷入到高炉内参与造渣反应。
通过本发明的方法，本发明可以导致高钛型高炉渣粘度和熔化性温度降低，从而改善高钛炉渣的冶炼性能。
在上述技术方案中，喷吹煤的用量为90～98wt％，硼镁矿石的用量为2～10wt％。
在上述技术方案中，喷吹煤包括无烟煤、烟煤及两者混合物。
在上述技术方案中，高炉喷吹煤制粉系统优选磨煤机。
在上述技术方案中，硼镁矿石中B2O3的含量为10～15wt％，MgO的含量为45～55wt％，SiO2的含量为8～10wt％。
在上述技术方案中，使用的喷吹煤的粒度小于40mm，硼镁矿石使用粒度大于10mm的块状物经破碎至粒度小于5mm后的粉状物或使用粒度小于10mm的粉状物。
在上述技术方案中，制粉混匀后的粉体的粒度小于0.074mm的比例在60％以上。
在上述技术方案中，混匀后的粉体通过喷煤分配器分配到高炉的各个风口，并通过风口喷煤枪喷入高炉的炉缸内。
在上述技术方案中，高炉冶炼的条件是热风温度为1150～1250℃，富氧
率为3～8％。
下面结合具体实施例以及实验数据来对本申请的上述技术方案进行详细说明。
本发明实施例中改善钒钛矿冶炼高钛炉渣性能的喷吹方法具体如下：
将硼镁矿石与喷吹煤一起加入磨煤机进行制粉，并在磨煤机内进行充分地混匀，然后混匀后的两者一起通过高炉煤粉喷吹系统，经过高炉的风口喷入高炉内进行造渣反应。硼镁矿粉从高炉圆周风口均匀喷入高炉，参与造渣从而改善了炉渣性能，实现了炉渣性能的均匀改善，有利于高炉的冶炼。
在上述实施例中，喷吹煤的用量为90～98wt％，硼镁矿石的用量为2～10wt％。喷吹煤包括无烟煤、烟煤及两者混合物。硼镁矿石中B2O3的含量为12％，MgO的含量为50％，SiO2的含量为8％。使用的喷吹煤的粒度在30mm左右，使用的硼镁矿石的粒度在4mm左右。制粉混匀后的粉体的粒度小于0.074mm的比例为80％。高炉冶炼的条件是热风温度为1200℃，富氧率为8％。
通过考虑喷煤比(kg/tFe)(喷吹煤的用量)和硼镁矿石配比用量的变化来考察炉渣性能：
具体执行实施例1-4的高炉冶炼效果的结果见下表1所示。
表1实施例1-4的高炉冶炼效果
注：表中的三元碱度R3为炉渣中(CaO+MgO)/SiO2
注：表中的三元碱度R3为炉渣中(CaO+MgO)/SiO2
由表1可以看出，采用高炉喷吹煤粉中添加不同比例硼镁矿石粉后，可以根据配比比例的变化来改变硼镁矿石配比，随着硼镁矿石配比的变化，炉渣中B2O3含量、MgO含量也会发生变化，例如，随着硼镁矿石配比的升高，炉渣中B2O3含量升高，三元碱度R3也升高，炉渣的熔化性温度会降低，由此炉渣性能得到改善。同时，随着硼镁矿石配比的升高，渣中带铁减少，高炉利用系数增加，有效强化了钒钛矿高炉的冶炼。
以上实施例仅表达了本发明的实施方式，其描述较为具体和详细，但并不能因此而理解为对本发明专利范围的限制。应当指出的是，对于本领域的普通技术人员来说，在不脱离本发明构思的前提下，还可以做出若干变形和改进，这些都属于本发明的保护范围。因此，本发明专利的保护范围应以所附权利要求为准。
Claims (10)
- 一种改善钒钛矿冶炼高钛炉渣性能的喷吹方法，其特征在于，包括：将硼镁矿石与喷吹煤一起加入到高炉喷吹煤制粉系统中进行制粉并充分混匀，然后使混匀后的粉体进入高炉煤粉喷吹系统并经过高炉的风口喷入到高炉内参与造渣反应。
- 根据权利要求1所述的改善钒钛矿冶炼高钛炉渣性能的喷吹方法，其特征在于，按照质量百分比计，所述喷吹煤的用量为90～98％，所述硼镁矿石的用量为2～10％。
- 根据权利要求2所述的改善钒钛矿冶炼高钛炉渣性能的喷吹方法，其特征在于，所述喷吹煤包括无烟煤、烟煤及两者混合物。
- 根据权利要求1所述的改善钒钛矿冶炼高钛炉渣性能的喷吹方法，其特征在于，所述高炉喷吹煤制粉系统包括磨煤机。
- 根据权利要求1所述的改善钒钛矿冶炼高钛炉渣性能的喷吹方法，其特征在于，按照质量百分比计，所述硼镁矿石中B2O3的含量为10～15％，MgO的含量为45～55％，SiO2的含量为8～10％。
- 根据权利要求1所述的改善钒钛矿冶炼高钛炉渣性能的喷吹方法，其特征在于，使用的所述喷吹煤的粒度小于40mm。
- 根据权利要求6所述的改善钒钛矿冶炼高钛炉渣性能的喷吹方法，其特征在于，所述硼镁矿石使用粒度大于10mm的块状物经破碎至粒度小于5mm后的粉状物或使用粒度小于10mm的粉状物。
- 根据权利要求1所述的改善钒钛矿冶炼高钛炉渣性能的喷吹方法，其特征在于，制粉混匀后的粉体的粒度小于0.074mm的比例在60％以上。
- 根据权利要求1所述的改善钒钛矿冶炼高钛炉渣性能的喷吹方法，其特征在于，混匀后的粉体通过喷煤分配器分配到高炉的各个风口，并通过风口喷煤枪喷入高炉的炉缸内。
- 根据权利要求1所述的改善钒钛矿冶炼高钛炉渣性能的喷吹方法，其 特征在于，高炉冶炼的条件是热风温度为1150～1250℃，富氧率为3～8％。
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