CN1073633C - Method for making pellet agglomerate used in iron-smelting - Google Patents

Abstract

The present invention relates to a method for manufacturing pellet sinter for smelting iron, which belongs to the field of the agglomeration of the pellet sinter as raw material for smelting the iron and comprises the steps of compounding, mixed pelletization, material distribution and sintering. The method adopts two times of mixed pelletization, and before the two times of mixed pelletization, lime and solid fuel are respectively added; at the time of compounding, a certain amount of lime and solid fuel are added; in the course of secondary mixed pelletization, a certain amount of lime and solid fuel are added again. The present invention can increase the production capacity of the sinter, improve the quality of the sinter, and reduce energy consumption.

Description

The manufacture method of pellet agglomerate used in iron-smelting

The invention belongs to iron-smelting raw material pellet agglomerate agglomeration field.Mainly be applicable to ironmaking mini-pellets sintering.

At present, domestic and international most of blast furnace or directly the used iron ore material of reduced ore is all served as reasons that sintering forms behind the partly or entirely thin iron concentrate pelletization.Particularly China's iron ore deposit lean ore is many, and rich ore is few, and complex ore is many, and single iron ore is few.All need be selected through fine grinding, form high-grade fine iron concentrate powder, make pellet agglomerate then, could be as raw materials such as blast furnaces.

In the prior art, the manufacture method of conventional agglomerate has ordinary sinter method and pellet sintering method.All there is following weak point in these methods: in its sintering process, form the wet band of certain thickness mistake in the bed of material, especially under the lower condition of the thick bed of material and mixture temperature, it is more remarkable to cross wet band.Owing to wetly excessively be with moisture higherly, sinter mixture or bead be very easily distortion or broken under the effect of water, forms the sposh shape when serious, cause the permeability of sintering material bed variation, make the downgrade of agglomerate, output reduces (" iron mineral powder agglomeration ", Zhongnan Polytechnic Univ compiles).Therefore, press for the wet capacitive that improves compound or bead material, reduced of the influence of wet band the ventilation property of sinter bed.

In order to improve the quality of agglomerate, the method that generally adopts is to improve the sinter bed height both at home and abroad, carries out thick bed of material operating duty.But after improving the sinter bed height, if the ventilation property of the bed of material does not improve, then agglomerate output must reduce (" iron ore powder sintering ", metallurgical industry is published, in March, 1979 the 128-130 page or leaf).For this reason, must improve solid-fuelled combustionvelocity, thereby improve vertical sintering speed, the output that prevents agglomerate reduces because of the raising of the bed of material.So there is the serious shortcoming that reduces of agglomerate output in this method.

Publication number is the manufacture method that the Chinese patent application of CN87108122A has been introduced a kind of pellet agglomerate, and this method is rolled surface at green-ball with lime and coke powder, and this green-ball cloth needs to carry out earlier drying to sinter machine, the sintering of lighting a fire then.This method weak point is that lime and coke powder all need to be processed into the powder less than 1mm.Before sintering ignition, need to be provided with the green-ball dryer section that accounts for sintering area 10%-15%.Therefore there are shortcomings such as the high and product production of production cost is low in this method.

The object of the present invention is to provide a kind of quality that can improve agglomerate output and agglomerate can reduce the manufacture method of the pellet agglomerate used in iron-smelting of sintering energy consumption again.

At above-mentioned purpose, main technical schemes of the present invention is in the manufacturing processed of pellet agglomerate, carries out mixed pelletizing twice, and lime and solid fuel successively add in the compound at twice.Promptly when batching, add lime and solid fuel, carry out mixed once and make outside the ball, when the secondary mixed pelletizing, allocate lime and solid fuel again into.

The manufacture method of pellet agglomerate used in iron-smelting of the present invention comprises following processing step: batching, mixed once are made ball, secondary mixed pelletizing, cloth and sintering.Now that each step division is as follows:

1, batching

Distribution according to the pellet agglomerate routine, with fine iron breeze, high-grad iron ore deposit powder, solid fuel, flux (Wingdale or rhombspar), lime, return mine, discharge from former feed bin and the feed bin amount of falling into a trap of returning mine respectively, form compound, enter in the lump in the mixed once pelletizer.When mixed once is made ball, lime allocate the 2-13% that weight accounts for the compound gross weight into, solid-fuelledly allocate the 1.0-3.5% that weight accounts for the compound gross weight into; For the second time during mixed pelletizing, the lime weight of allocating into accounts for the 0.5-4.0% of compound gross weight, and the solid fuel weight of allocating into accounts for the 1.5-4.0% of compound gross weight.

In above-mentioned raw materials, the granularity of fine iron breeze should be less than 0.1mm, and the granularity that accounts for 65% above high-grad iron ore deposit powder should be less than 8mm, and the granularity of lime accounts for more than 85% less than 3mm, and the granularity of return fines material is less than 6mm, and the solid fuel granularity accounts for more than 75% less than 3mm.

2, mixed once is made ball

For the first time during mixed pelletizing, the lime solid fuel of being allocated into added in the compound before compound enters the mixed once pelletizer, after compound enters the mixed once pelletizer, carry out mixed pelletizing and add an amount of water simultaneously, and control the particle diameter and the output of pelletizing by inclination angle, rotating speed and the blanking amount of regulating the mixed pelletizing machine.Requirement to the pelletizing particle diameter is the 50-90% that should account for the pelletizing total amount of 3.0-13.0mm

3, secondary mixed pelletizing

The pelletizing that comes out from the mixed once pelletizer enters secondary mixing pelletizer through travelling belt, simultaneously lime and the solid fuel of allocating into is for the second time also entered in the secondary mixing pelletizer in the lump, and the pelletizing of making ball with mixed once mixes, and continues mixed pelletizing.The pelletizing particle diameter requires to be the 70-95% that should account for the pelletizing total amount of 3.0-13.0mm.

4, cloth

The pelletizing or the compound that come out from secondary mixing pelletizer pass through distributor cloth to exhausting formula sinter machine (Dwight-Lloyd sintering machine or circular travelling sintering machine), form the mixing bed of material of certain altitude, but the sinter bed height are answered＞400mm.

The present invention can remove dryer section.

5, igniting sintering

After sinter bed cloth is good, by lighter for ignition sinter bed is carried out surface ignition, ignition temperature should be 1000-1200 ℃, 1-4 minute ignition time.Igniting back down draft sintering, sintering temperature is controlled at 1200-1350 ℃.And the employing negative-pressure operation, by regulating negative pressure, the control sintering velocity.

Sintering gained agglomerate is delivered to blast furnace hopper after crusher in crushing, screening and cooling process.

Because the present invention has allocated secondary lime during mixed pelletizing in the second time, make compound or pelletizing surface contain higher slaked lime or unslaked lime, and slaked lime or unslaked lime have very high wet capacitive, compound or pelletizing feed that all surface is wrapped with slaked lime or unslaked lime have very high humidity capacitive, this compound or pelletizing feed are crossed wet band at sinter bed and are not easy to be out of shape or fragmentation, can reduce the influence of wet band to permeability of sintering material bed.In the present invention, at secondary with addition of the solid fuel of 1.5-4%, this part solid fuel is mainly between compound or pelletizing feed top layer or material grain, because the adding of secondary slaked lime or unslaked lime, makes to be in compound or solid fuel bonding in pelletizing feed top layer is more firm.In sintering process, because CaO has katalysis to carbon burning, like this, contain too much CaO at compound or pelletizing surface, can play the effect of good carbon burning catalyzer, accelerate solid fuel ignition speed, thereby improve vertical sintering speed.In addition, there is too much CaO on compound or pelletizing feed top layer, this helps compound or pelletizing feed surface and generates more calcium ferrite, and calcium ferrite is a kind of intensity height, Well-recovered mineral substance, to the metallurgical performance that improves agglomerate, to improve sintering quality very favourable.

Compared with prior art, the present invention has following advantage:

1, the present invention adds lime and solid fuel for the second time after sinter mixture mixes and makes ball, makes compound or pelletizing surface oxidation calcium contents height, improves the wet capacitive of compound or pelletizing greatly.Excessive moistening layer can improve the ventilation property of sintered material to the granularity destruction of compound or pelletizing feed in like this can the material reducing layer.

2, because the effect of the CaO on compound or pelletizing feed surface makes that the solid fuel bonding on compound or pelletizing feed surface is firm, avoid producing the macrosegregation of solid fuel in the bed of material.

3, the lime on compound or pelletizing feed surface has katalysis to solid fuel ignition, can improve vertical sintering speed, helps improving product production.Its agglomerate output can improve 10-20%.

4, the agglomerate structure of producing by the present invention is that compound or pelletizing top layer Fe-laden acid calcium amount are higher, and this is to reducing sintering energy consumption, and it is very favourable to improve sinter quality.Its energy consumption can reduce 5-10%, and FeO content can reduce 1-4% in the agglomerate.

5, because the present invention does not establish dryer section, can reduce cost.

Embodiment

Adopt method of the present invention, be equipped with three batches of pellet agglomerate used in iron-smelting.The proportioning raw materials of agglomerate is as shown in table 1.The first time and secondary lime and solid fuel proportioning are also listed in the table 1.The granularity of each raw material and proportion thereof are as shown in table 2 in the proportioning raw materials.Carry out mixed once respectively after raw material is equipped with and make ball and secondary mixed pelletizing.Pelletizing behind the secondary mixed pelletizing and compound are lighted a fire subsequently by distributor cloth on sinter machine, and sintering.Sintering material layer thickness, ignition temperature, sintering temperature and sintering negative pressure are as shown in table 3.The technical indicator of pellet agglomerate is as shown in table 4 behind sintering.Table 1 embodiment proportioning raw materials (weight %)

Table 2 embodiment raw material granularity and proportion (weight %)

The processing parameter of table 3 embodiment The technical indicator of table 4 embodiment

Claims (3)

1, a kind of manufacture method of pellet agglomerate used in iron-smelting comprises batching, mixed pelletizing, cloth and sintering, it is characterized in that:

(1) adopts twice mixed pelletizing;

(2) when batching, lime, solid fuel are added in the compound at twice, the weight of allocating lime for the first time into accounts for the 2-13% of compound gross weight, allocates the 1.0-3.5% that solid-fuelled weight accounts for the compound gross weight for the first time into; The weight of allocating for the second time lime into accounts for the 0.5-4.0% of compound gross weight, allocates the 1.5-4.0% that solid-fuelled weight is the compound gross weight for the second time into;

(3) for the first time allocating lime, solid fuel into, is before compound enters the mixed once pelletizer, adds in the compound, enters in the lump to add water in the mixed once pelletizer and carry out mixed pelletizing; Lime of allocating into for the second time and solid fuel be at compound behind mixed once pelletizer mixed pelletizing, enter secondary mixing pelletizer before, add in the lump in the secondary mixing pelletizer with mini-pellets;

(4) granularity of the lime of being allocated into is: granularity accounts for more than 85% less than 3mm's, and the solid-fuelled granularity of being allocated into is: granularity accounts for more than 75% less than 3mm's;

(5) for the first time behind the mixed pelletizing, be the 50%-90% that should account for the pelletizing total amount of 3.0-13.0mm to the requirement of pelletizing particle diameter;

(6) behind the mixed pelletizing second time, the pelletizing particle diameter requires to be the 70-95% that should account for the pelletizing total amount of 3.0-13.0mm.

2, manufacture method according to claim 1, it is characterized in that solid fuel be in coal dust or the coke powder any.

3, manufacture method according to claim 1 is characterized in that lime can be in slaked lime or the unslaked lime any.