Pre-reduced pellet preparation apparatus and method based on grate-rotary kiln

Patent metadata

Field	Value
Publication number	US-2024279767-A1
Application number	US-202218570627-A
Country	US
Kind code	A1
Filing date	Jun 16, 2022
Priority date	Jun 18, 2021
Publication date	Aug 22, 2024
Grant date	—

Abstract

The present disclosure provides a pre-reduced pellet preparation device and method based on grate-rotary kiln. The pre-reduced pellet preparation device comprises a grate-rotary kiln pellet oxidation system and a hydrogen-based shaft furnace reduction system. In the pre-reduced pellet preparation method, a roasting process and a reduction process for an iron-containing green pellet are organically combined, and a pellet cooling process after roasting and a heating process before pellet reduction are eliminated; physical heat of a roasted pellet is used to satisfy heat required in the heating and reduction processes; the technical problems of a low hydrogen utilization rate and high energy consumption of pellets in oxidative roasting and direct reduction processes in traditional direct reduction processes are solved; a reduced pellet having a certain metallization rate is obtained; the prepared pre-reduced pellet is used as blast furnace burden, such that blast furnace fuel consumption and carbon emission can be significantly reduced; the method is a new, low-carbon, and green pre-reduced pellet preparation process.

First claim

1 . A pre-reduced pellet preparation device, comprising a grate-rotary kiln pellet oxidation system and a hydrogen-based shaft furnace reduction system;
the grate-rotary kiln pellet oxidation system comprises a grate system, and a rotary kiln system connected to the grate system; in the grate system, iron-containing green pellets are sequentially dried and preheated to obtain preheated pellets, and in the rotary kiln system, the preheated pellets are roasted at a temperature of 1170-1300° C. to obtain roasted pellets; and the hydrogen-based shaft furnace reduction system comprises a hydrogen-based shaft furnace, a feeding system, a reducing gas system, a cooling system, and a discharging system; the feeding system is disposed at the upper part of the hydrogen-based shaft furnace, and the roasted pellets from the rotary kiln system are directly conveyed into the feeding system; the reducing gas system processes flue gas from the hydrogen-based shaft furnace, and provides reducing gas to the hydrogen-based shaft furnace; the roasted pellets from the feeding system are reduced in the hydrogen-based shaft furnace to obtain pre-reduced pellets; the cooling system cools the pre-reduced pellets in the hydrogen-based shaft furnace to obtain cooled pre-reduced pellets; and the discharging system is disposed at the bottom of the hydrogen-based shaft furnace, and discharges the cooled pre-reduced pellets; wherein the reducing gas is hydrogen gas; the reducing gas is not heated prior to entering the hydrogen-based shaft furnace.

2 . The pre-reduced pellet preparation device according to claim 1 , characterized in that the grate system is provided with a drying section I, a drying section II, a preheating section I and a preheating section II in sequence in a direction of movement of the iron-containing green pellets;
the preheating section II communicates with the rotary kiln system, and is connected with the drying section II through a first recuperation fan; the preheating section I is connected with a tubular heat exchanger of the reducing gas system, and is connected with the rotary kiln system through a combustion fan, and is connected with the drying section I through a second recuperation fan; and the drying section I and the drying section II are each connected to a bag dust collector through a main exhaust fan.

3 . The pre-reduced pellet preparation device according to claim 2 , characterized in that the feeding system comprises an upper hopper, a middle hopper and a lower hopper; valves are disposed between the upper hopper and the middle hopper, and between the middle hopper and the lower hopper; and/or
the reducing gas system comprises a tubular heat exchanger, a residual heat boiler, a first scrubber, a circulating fan, and a pressurizing fan; the tubular heat exchanger is provided with a flue gas inlet, a flue gas outlet, an air inlet and an air outlet, and the flue gas inlet is connected with a flue gas port at the top of the hydrogen-based shaft furnace, the flue gas outlet is connected with the residual heat boiler, the air inlet is connected with a fan, the air outlet is connected with the preheating section I of the grate system; an air outlet of the residual heat boiler is connected with an air inlet of the first scrubber; one end of the circulating fan is connected with an air outlet of the first scrubber, and the other end communicates with an annular tuyere in the middle part of the hydrogen-based shaft furnace; the pressurizing fan pressurizes reducing gas from the circulating fan; and/or the cooling system comprises a oxygenating combustion unit, a waste heat recovery unit, a second scrubber, and a cooling fan; the oxygenating combustion unit is connected with an air outlet at a lower part of the hydrogen-based shaft furnace; one end of the waste heat recovery unit is connected with the oxygenating combustion unit, and the other end is connected with an air inlet of the second scrubber; one end of the cooling fan is connected with an air outlet of the second scrubber, and the other end communicates with an air inlet at the lower part of the hydrogen-based shaft furnace; and the air outlet at the lower part of the hy-drogen-based shaft furnace is arranged above the air inlet at the lower part of the hydrogen-based shaft furnace.

4 . The pre-reduced pellet preparation device according to claim 3 , characterized in that the upper hopper is provided with an air duct; the middle hopper is provided with a pressure-equalizing device; and the lower hopper is provided with a universal distributor.

5 . A pre-reduced pellet preparation method, comprising preparing pre-reduced pellets by using the pre-reduced pellet preparation device according to claim 1 , roasting the pellets at a temperature of 1170-1300° C. in a grate-rotary kiln pellet oxidation system of the pre-reduced pellet preparation device to obtain roasted pellets having a temperature of 1170-1300° C., and then directly feeding the roasted pellets into a hydrogen-based shaft furnace reduction system of the pre-reduced pellet preparation device for reduction to obtain pre-reduced pellets.

6 . The pre-reduced pellet preparation method according to claim 5 , characterized in comprising the steps of:
(1) blending bentonite and finely ground limestone/slaked lime into an iron ore raw material to obtain a mixed material, then mixing water into the mixed material, and pelletizing them to obtain iron-containing green pellets; (2) distributing the iron-containing green pellets into a grate system to form a material layer of iron-containing green pellets, sequentially subjecting the material layer of iron-containing green pellets to blast drying, exhaust drying, primary preheating, and secondary preheating to obtain preheated pellets, then feeding the preheated pellets into a rotary kiln system, and performing roasting at 1170-1300° C. to obtain roasted pellets with a temperature of 1170-1300° C.; and (3) feeding the roasted pellets into a hydrogen-based shaft furnace reduction system, so that the roasted pellets undergo a reduction reaction with reducing gas, and then performing cooling treatment with cooling gas to obtain pre-reduced pellets.

7 . The pre-reduced pellet preparation method according to claim 6 , characterized in that in the step (1), the iron ore raw material is selected from one or more of magnetite, hematite and limonite; and/or
the iron ore raw material has a Blaine specific surface area of 1500 cm 2 /g or more; and/or the amount of the bentonite blended is 0.7-1.5 wt % of the iron ore raw material; and/or the mixed material has a binary alkalinity of 0.3-0.5 or 0.8-1.2; and/or the iron-containing green pellets have a particle size of 8-20 mm; and/or in the step (2), in the grate system, the material layer of iron-containing green pellets has a height of 250-400 mm; and/or the blast drying is carried out in the drying section I of the grate system at a temperature of 170-240° C. and an air speed of 0.8-1.4 m/s for 1.5-2.5 min; and/or the exhaust drying is carried out in the drying section II of the grate system at a temperature of 300-400° C. and an air speed of 0.8-1.4 m/s for 4-6 min; and/or the primary preheating is carried out in the preheating section I of the grate system at a temperature of 600-800° C. and an air speed of 0.8-1.4 m/s for 4-6 min; and/or the secondary preheating is carried out in the preheating section II of the grate system at a temperature of 900-1100° C. and an air speed of 0.8-1.4 m/s for 4-6 min; and/or the fuel used in the rotary kiln system comprises natural gas, coke oven gas, pyrolysis gas, pyrolysis oil, biomass oil, or biomass carbon; and/or the rotary kiln system uses hot air to support combustion, and the hot air is from a mixed gas composed of air and hot e

Assignees

• Baoshan Iron & Steel

Inventors

• Li Jian
• Mao Xiaoming
• Xiong Lin
• Liang Lisheng
• Jiang Linhai
• Yi Lujie
• Peng Xin
• Chen Shengfeng

Classifications

• C21B13/0033

  In fluidised bed furnaces or apparatus containing a dispersion of the material · CPC title

• C21B13/0073

  Selection or treatment of the reducing gases · CPC title

• C22B1/216

  in rotary furnaces · CPC title

• C22B1/20 Primary

  in sintering machines with movable grates · CPC title

• C21B13/0053

  On a massing grate · CPC title