Clean and rapid smelting method in an electric arc furnace with full scrap steel

Patent metadata

Field	Value
Publication number	US-10808290-B2
Application number	US-201816052629-A
Country	US
Kind code	B2
Filing date	Aug 2, 2018
Priority date	Aug 10, 2017
Publication date	Oct 20, 2020
Grant date	Oct 20, 2020

Abstract

A clean and rapid smelting method in an electric arc furnace with full scrap steel, is suitable for smelting process of 30-300 t electric arc furnace with full scrap steel. In the smelting process of the electric arc furnace with full scrap steel, different kinds of mediums are injected by an injection lance which is installed inside refractory material of sidewall at the bottom of the electric arc furnace in different stages of smelting. Carburization is utilized in molten pool to accelerate melting down and improve carbon content of the molten pool at the stage of recarburizing and fluxing. A reaction in the molten pool is intensified at the stage of high efficiency dephosphorization and deep denitrogenation, to enhance efficient dephosphorization and deep denitrification of the reaction in the molten pool, thereby accelerating the smelting speed of the electric arc furnace with full scrap steel, improving effect of dephosphorization and denitrification.

First claim

What is claimed is:

1. A clean and rapid smelting method in an electric arc furnace with full scrap steel, wherein
online dynamic switching for different mediums including a pure gas, a carrier gas A with a recarburization powder, a carrier gas B with a dephosphorization powder in an injection mode is utilized, to finish a process of blowing in turn below a molten steel level of a molten pool in different stages of smelting for the different mediums;
the process of blowing in turn comprises:
in a stage of recarburizing and fluxing, injecting the carrier gas A with the recarburization powder into the molten pool to improve a carbon content of molten steel in the molten pool, and to improve a flow velocity of the molten steel, wherein the molten steel has formed the molten pool, and accelerating a melting process of the full scrap steel by carburization, wherein the carbon content of the molten steel in the molten pool reaches 0.40%-2.0% after the melting process of the full scrap steel is completed;
in a stage of high efficiency dephosphorization, injecting the carrier gas B with the dephosphorization powder into the molten pool to improve kinetic conditions for the high efficiency dephosphorization, wherein the high efficiency dephosphorization in the electric arc furnace is achieved by systematic dephosphorization of slag particles in a molten state, to make a phosphorus content of the molten steel equal to or less than 0.010%;
in a stage of deep denitrogenation, injecting O 2 or a gas mixture of O 2 and CO 2 into the molten pool to intensify decarburization in the molten pool, and effectively removing nitrogen in the molten steel by a large number of CO bubbles produced by a metallurgical reaction in the molten pool; and
in a stage of a smelting endpoint, injecting the carrier gas B with the dephosphorization powder to prevent the molten steel from rephosphorization, then Ar into the molten pool, to homogenize compositions and a temperature of the molten pool, wherein the carbon content of the molten steel is equal to or more than 0.10%, the phosphorus content of the molten steel is equal to or less than 0.004%, and a nitrogen content of the molten steel is equal to or less than 0.005%;
wherein the online dynamic switching refers to that the switching between the mediums is controlled by a control system and is performed according to the different stages, wherein the word online in the online dynamic switching refers to that the switching between the mediums is controlled by a control system, and the word dynamic in the online dynamic switching refers to that the switching between the mediums is performed according to the different stages.

2. The clean and rapid smelting method in an electric arc furnace with full scrap steel according to claim 1 , comprising the following steps:
step 1: in a time period after steel is output from the electric arc furnace and before a furnace material is added, closing a recarburization path automatic shut-off valve by the control system, opening a dephosphorization path automatic shut-off valve by the control system, through a first transmission pipeline for the high efficiency dephosphorization, injecting N 2 through a central tube and a circular seam tube of an injection lance, wherein a flow rate of the central tube is 50-500 Nm 3 /h, and a flow rate of the circular seam tube is 50-200 Nm 3 /h, to prevent the injection lance from blocking and burning;
step 2: in a feeding stage of the electric arc furnace: through the first transmission pipeline for the high efficiency dephosphorization, injecting O 2 by the central tube of the injection lance, wherein a flow rate of the central tube is 50-300 Nm 3 /h; injecting propane or natural gas by the circular seam tube, wherein a flow rate of the circular seam tube is 50-200 Nm 3 /h, to ensure a normal operation of the injection lance in the feeding stage of the electric arc furnace;
step 3: in the stage of recarburizing and fluxing: injecting carbon powder into the molten pool formed by the melting process of the full scrap steel, to improve the carbon content of the molten steel in the molten pool, and accelerate the melting process of the full scrap steel by using the carburization, wherein this step comprises the following steps:
1) in an early stage of the melting process: opening the recarburization path automatic shut-off valve by the control system, and closing the dephosphorization path automatic shut-off valve by the control system; through a second transmission pipeline for recarburization, performing a carrier gas A with recarburization powder flow mode on the central tube of the injection lance, to accelerate the carburizing and the melting process of the full scrap steel, wherein the molten pool is formed in the stage, a velocity of a powder injection is controlled to improve a carburizing efficiency, a velocity of the powder injection is 1-5 kg/min, and a flow rate of the carrier gas A is 100-300 Nm 3 /h; and injecting propane or natural gas by the circular seam tube of the injection lance, wherein a flow rate of the propane or the natural gas is 50-200 Nm 3 /h;
2) in a middle stage of the melting process: through the second transmission pipeline for the recarburization, performing the carrier gas A-recarburization powder flow mode on the central tube of the injection lance, wherein the molten pool has a depth in the middle stage of the melting process, and a velocity of the powder injection is controlled to improve the carburizing efficiency, wherein a velocity of the powder injection is 5-10 kg/min, and a flow rate of the carrier gas A is 200-500 Nm 3 /h; and injecting propane or natural gas by the circular seam tube of the injection lance, and a flow rate of the propane or the natural gas is 50-200 Nm 3 /h; and
3) in a later stage of the melting process: through the second transmission pipeline for the recarburization, performing the carrier gas A-recarburization powder flow mode on the central tube of the injection lance, wherein the molten pool is deep in the later stage of the melting process, and intensifying the carburizing and stirring in the molten pool, wherein a velocity of the powder injection is 10-20 kg/min, and a flow rate of the carrier gas A is 200-600 Nm 3 /h; and injecting propane or natural gas by the circular seam tube of the injection lance, wherein a flow rate of the propane or the natural gas is 50-200 Nm 3 /h;
step 4: in a stage of pipeline cleaning: performing pipeline cleaning by using a large flow of N 2 or CO 2 , wherein the pipe cleaning comprise the steps of: opening the recarburization path automatic shut-off valve by the control system, and closing the dephosphorization path automatic shut-off valve by the control system; through the transmission pipeline for the high efficiency dephosphorization, injecting N 2 or CO 2 by controlling the central tube of the injection lance to perform the pipeline cleaning, wherein a flow rate of the N 2 or the CO 2 is 400-600 Nm 3 /h, and a time of injecting the N 2 or the CO 2 is 20-30 s;
step 5: in the stage of the high efficiency dephosphorization: injecting high speed dephosphorization powder gas flow directly to the molten pool below the molten steel level, to effectively remove phosphorus in the molten steel, wherein this step comprises the following steps: through the first transmission pipeline for the high efficiency dephosphorization, performing a carrier gas B-dephosphorization powder flow mode on the central tube of the injection lance, and inputting the carrier gas B with the dephosphorization powder directly into the molten steel and intensifying a stirring ability of the molten pool, to dephosphorize efficiently, wherein a velocity of the powder injection is 10-50 kg/mm, and a flow rate of the carrier gas B is 100-1000 Nm 3 /h; and injecting propane or natural gas by the circular seam tube of the

Assignees

• Univ Beijing Science & Technology

Inventors

• Zhu Rong
• Wei Guangsheng
• Dong Kai
• Zhao Jingxin
• Wu Xuetao
• Tang Tianping
• Wang Xueliang
• Wu Wenhe
• Hu Shaoyan
• Wang Yun

Classifications

• C21C7/0645 Primary

  Agents used for dephosphorising or desulfurising · CPC title

• Y02P10/20

  Recycling · CPC title

• C21C7/0025

  Adding carbon material · CPC title

• C21C5/5264 Primary

  Manufacture of alloyed steels including ferro-alloys · CPC title

• C21C2005/5258

  with crater formed by down-melting of scrap or charge through electrode or lance · CPC title