CN1019819B - Production of pellet with reveert as core - Google Patents
Production of pellet with reveert as coreInfo
- Publication number
- CN1019819B CN1019819B CN90109395A CN90109395A CN1019819B CN 1019819 B CN1019819 B CN 1019819B CN 90109395 A CN90109395 A CN 90109395A CN 90109395 A CN90109395 A CN 90109395A CN 1019819 B CN1019819 B CN 1019819B
- Authority
- CN
- China
- Prior art keywords
- ball
- pelletizing
- mine
- water
- pellet
- 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.)
- Expired
Links
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention belongs to the iron mineral powder agglomeration field, is pelletizing to be returned mine directly participate in batching, makes ball and produces pellet.The water of at first pelletizing being returned mine carries out wetting, and moisture content is 6～10%, makes the coarse particles in returning mine possess into kernel function, mixes with fine iron breeze, bentonite etc. then and makes ball; Can constantly grow up in order to guarantee to make in the ball process green-ball, the water mode of making in the ball process that adds is an atomized water, the quality of green pellets that the present invention obtains can satisfy the shaft furnace production requirement fully, can adopt the pelletizing instead of part iron ore concentrate of returning mine, not therefore the finished ball nodulizing can be and influenced, can be completely achieved pelletizing-return mine-closed cycle of pelletizing again.
Description
The invention belongs to the iron mineral powder agglomeration technical field.
At present, the pelletizing powder (5 millimeters often are called and return mine) that palletizing shaft furnace produces generally only is used for agglomerate production because granularity is thicker, if be used for producing pellet, then must can use to the fine ore granular level through ball mill etc. is levigate again.
Japanese patent application J63-130720 discloses a kind of powder material pelletizing manufacture method, be to make the ball difficult problem in order to solve special mineral fine (≤325 orders account for 80%), this method is earlier breeze to be made bead as ball (diameter is φ 4～6mm), (size φ 15～20mm) to mix the green-ball of making the granularity that meets the demands in the back with the mineral fine of same composition with this bead again, the feature of this application is through two steps with same raw material, make ball earlier, the production pellet is mixed in the back with breeze.
The objective of the invention is to obtain a kind of pelletizing can being returned mine and directly produce the method for pellet as ball.
For achieving the above object, coarse particles during the present invention is achieved in that pelletizing returned mine is as the ball of making ball, being about to above-mentioned ball in advance adds water-wet, moisture content is 6～10wt%, can make the coarse particles (〉=3 millimeters) in returning mine possess into kernel function like this, mix with iron ore concentrate, bentonite etc. then, wherein moist curing is crossed returns mine that to account for proportioning raw materials be 1～10wt%, makes ball.
Can constantly grow up for guaranteeing to make in the ball process green-ball, the water mode of making in the ball process that adds is an atomized water.
Among the present invention, its key is that the water that is at first pelletizing to be returned mine is moistening, makes it to possess into kernel function, makes ball with powdered iron ore etc. then.Coarse particles in returning mine for pelletizing, if not wetting in advance just the mixing with powdered iron ore participates in making ball, although in making the ball process, can add moisture content, the particle of returning mine still can not participate in making ball, do not possess into kernel function, therefore, people think always that pelletizing returns mine to have only to be refined to iron ore concentrate granulometric facies same level through ball milling and just can participate in making ball.The present invention is because the particle water-wet of will returning mine in advance, and water content is 6～10%, and moisture content is very few can not to reach wetting purpose, too highly then influences the whole ball process of making.The particle of returning mine is like this made in the ball process in participation, because the capillary effect of water just can combine with fine iron breeze; Can constantly grow up for guaranteeing to make in the ball process green-ball, the water mode of making in the ball process that adds is an atomized water.
Compared with the prior art, the present invention is owing to saved the levigate process of returning mine, can save facility investment, processing charges etc., the more important thing is, having overcome in the prior art pelletizing returns mine and can not participate in the prejudice of making ball directly, the available instead of part fine iron breeze of returning mine, and realized pelletizing-return mine-closed cycle of pelletizing again.
Introduce embodiments of the invention below.
Raw materials usedly in the present embodiment return mine for iron ore concentrate, bentonite, pelletizing, its size composition such as table 1 show.Balling equipment is respectively among the φ 1000mm(embodiment 2,3,4 and is laboratory test) and φ 4200mm(embodiment in 5 be industrialness production) balling disc.
It is wetting by 6%, 8%, 10% moisture content respectively in advance pelletizing to be returned mine, participate in by 5%, 10% proportioning raw materials respectively then and make ball, make that to add the water mode in the ball process be atomized water, the green-ball of making is done finished ball quality test after quality of green pellets check and the roasting respectively, result such as table 2 show.
The result shows that the not low original split pellet quality level of the pellet quality that adopts the technology of the present invention to obtain satisfies the blast furnace production requirement fully.Simultaneously, adopt the technology of the present invention then can cancel the pelletizing regrinding process of returning mine, whenever utilize one ton of pelletizing to return mine to save 50 yuan, the remarkable in economical benefits of bringing.
Table 1 raw material granularity is formed (%)
≥3mm ＞20 -20 -40 -60 -80 -100 -120 -140 -160 -180 -200
Pelletizing returns mine 15.3 17 7.7 4 1.8 85 0.2 4.4 0.8 5.2 30.4
Fine iron breeze 0.2 3.5 3.4 0.5 7.7 7.9 0.2 7.8 2.5 11 55.5
Bentonite 0.2 0.4 2 0.2 2.2 22 91
Table 2 experimental result
Original technology embodiment of the invention
Sequence number 12345 ※ ※
Do not grind proportioning (%) 10 ※ 55 10 10 that return mine
Mill does not return mine wetting 6 10 88
Moisture content (%)
Ultimate compression strength 14.3 11.1 14.7 14.3 14.2
Give birth to (newton /)
Ball dropping strength 4.4 3.8 3.9 4.0 4.8
Matter (inferior /)
Amount burst temperature＞800＞800＞800＞800＞800
（℃）
Ultimate compression strength 1,781 2,705 3,193 3,028 1797
Become
(newton /)
Product
Barrate strength 84.9 85.9
Ball
（%）
Matter
Screening index 2.4 2.4
Amount
（%）
※ is pelletizing return mine (200, account for 60%) after ball mill is regrinded.
※ ※ is the industrial production actual result.
Claims (2)
1, a kind of production of pellet with reveert as core is iron ore concentrate, moisture and ball to be mixed to participate in make the ball process, and it is characterized in that: described ball is the coarse particles during pelletizing is returned mine, and in advance this ball is added water-wet, and moisture is 6～10wt%.
2, production of pellet with reveert as core according to claim 1 is characterized in that: the water mode that adds in making the ball process is an atomized water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN90109395A CN1019819B (en) | 1990-11-27 | 1990-11-27 | Production of pellet with reveert as core |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN90109395A CN1019819B (en) | 1990-11-27 | 1990-11-27 | Production of pellet with reveert as core |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1051759A CN1051759A (en) | 1991-05-29 |
| CN1019819B true CN1019819B (en) | 1992-12-30 |
Family
ID=4881410
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN90109395A Expired CN1019819B (en) | 1990-11-27 | 1990-11-27 | Production of pellet with reveert as core |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1019819B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1055092C (en) * | 1998-01-20 | 2000-08-02 | 张永正 | Preparation of gluconic acid by hydrogen peroxide oxidizing process |
| CN1319930C (en) * | 2004-07-11 | 2007-06-06 | 昆明贵金属研究所 | Preparation method of gluconic acid and its salt |
| CN104073627B (en) * | 2013-03-27 | 2016-11-23 | 鞍钢股份有限公司 | A kind of production method of fluxed composite briquette ore |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103074485B (en) * | 2013-02-06 | 2015-03-04 | 武汉科技大学 | Preparation method of oxidized pellets with coarse-grain hematite as main raw material |
| CN104975169B (en) * | 2014-04-10 | 2017-05-24 | 鞍钢股份有限公司 | Method of improving breathability of sintering mixture |
| CN105441669B (en) * | 2016-01-13 | 2017-09-01 | 山西太钢不锈钢股份有限公司 | It is a kind of to improve the method for full fine powder permeability of sintering material bed |
| CN113789440A (en) * | 2021-09-28 | 2021-12-14 | 攀钢集团攀枝花钢铁研究院有限公司 | Preparation method of vanadium-titanium pellet ore |
-
1990
- 1990-11-27 CN CN90109395A patent/CN1019819B/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1055092C (en) * | 1998-01-20 | 2000-08-02 | 张永正 | Preparation of gluconic acid by hydrogen peroxide oxidizing process |
| CN1319930C (en) * | 2004-07-11 | 2007-06-06 | 昆明贵金属研究所 | Preparation method of gluconic acid and its salt |
| CN104073627B (en) * | 2013-03-27 | 2016-11-23 | 鞍钢股份有限公司 | A kind of production method of fluxed composite briquette ore |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1051759A (en) | 1991-05-29 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C13 | Decision | ||
| GR02 | Examined patent application |