CN201109791Y - Molybdenum ore oxidation desulfurization device - Google Patents
Molybdenum ore oxidation desulfurization device Download PDFInfo
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- CN201109791Y CN201109791Y CNU2007200925510U CN200720092551U CN201109791Y CN 201109791 Y CN201109791 Y CN 201109791Y CN U2007200925510 U CNU2007200925510 U CN U2007200925510U CN 200720092551 U CN200720092551 U CN 200720092551U CN 201109791 Y CN201109791 Y CN 201109791Y
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- molybdenum ore
- ore oxidation
- ignition control
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- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 title claims abstract description 13
- 239000011733 molybdenum Substances 0.000 title claims abstract description 12
- 229910052750 molybdenum Inorganic materials 0.000 title claims abstract description 12
- 230000003647 oxidation Effects 0.000 title claims abstract description 12
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 12
- 238000006477 desulfuration reaction Methods 0.000 title abstract description 11
- 230000023556 desulfurization Effects 0.000 title abstract description 11
- 239000000463 material Substances 0.000 claims abstract description 30
- 239000000428 dust Substances 0.000 claims abstract description 11
- 238000002485 combustion reaction Methods 0.000 claims abstract description 9
- 238000005406 washing Methods 0.000 claims description 6
- 239000000446 fuel Substances 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims 1
- 230000006698 induction Effects 0.000 abstract description 5
- 239000003245 coal Substances 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000000843 powder Substances 0.000 description 9
- 238000005261 decarburization Methods 0.000 description 5
- 229910052500 inorganic mineral Inorganic materials 0.000 description 5
- 239000011707 mineral Substances 0.000 description 5
- DDTIGTPWGISMKL-UHFFFAOYSA-N molybdenum nickel Chemical compound [Ni].[Mo] DDTIGTPWGISMKL-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000005554 pickling Methods 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 229910000476 molybdenum oxide Inorganic materials 0.000 description 1
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Manufacture And Refinement Of Metals (AREA)
Abstract
一种钼矿石氧化脱硫装置,包括上料机、熟料接收室、除尘装置、引风装置,在上料机与熟料接收室之间设有预热炉和点火控制室,点火控制室内的物料通道呈蜗壳状,在熟料接收室的底部设有物料刮板和物料出口,熟料接收室底部设置的物料刮板由一个通过链轮传动的电机自动控制。本实用新型的优点是:操作简单,工人劳动强度小,可实现自动化操作;投资小,降低成本,与同等规模的反射炉比,投资仅为其十分之一,与转窑比,投资仅为其二十分之一;节约能源,可实现不外补加煤炭的方式进行燃烧;生产能力大;环保、排出的废气无污染,废气可控制在SO2浓度2-5%(V/V)以下,并可收集。
A molybdenum ore oxidation desulfurization device includes a feeder, a clinker receiving room, a dust removal device, and an air induction device. A preheating furnace and an ignition control room are arranged between the feeder and the clinker receiving room. The material channel is in the shape of a volute, and a material scraper and a material outlet are arranged at the bottom of the clinker receiving room. The material scraper set at the bottom of the clinker receiving room is automatically controlled by a motor driven by a sprocket. The utility model has the advantages of simple operation, low labor intensity of workers, automatic operation can be realized; small investment, cost reduction, compared with the reverberatory furnace of the same scale, the investment is only one tenth, and compared with the rotary kiln, the investment is only one tenth. It is one-twentieth of it; saves energy, and can realize combustion without additional coal; large production capacity; environmental protection, no pollution of exhaust gas, and exhaust gas can be controlled at SO 2 concentration of 2-5% (V/V ) below and can be collected.
Description
技术领域 technical field
本实用新型涉及一种钼矿石氧化脱硫装置,具体地说是一种用于镍钼矿与钼精粉的原生矿物氧化焙烧脱硫及脱碳装置。The utility model relates to a molybdenum ore oxidation desulfurization device, in particular to a primary mineral oxidation roasting desulfurization and decarburization device for nickel-molybdenum ore and molybdenum fine powder.
背景技术 Background technique
用镍钼矿或钼精粉生产氧化钼,现行的工艺主要使用反射炉、转窑或沸腾炉氧化焙烧进行脱硫,其反射焙烧脱硫炉属国家限制的高耗能高污染炉,生产效率低,工人劳动强度大,能耗高,产量小,污染大;转窑焙烧存在污染大、产量小、投资大、劳动效率低的缺点;沸腾焙烧存在脱硫不彻底,开机停机不方便,投资大的缺点。To produce molybdenum oxide with nickel-molybdenum ore or molybdenum powder, the current process mainly uses reverberatory furnace, rotary kiln or fluidized bed furnace for desulfurization. High labor intensity, high energy consumption, small output, and large pollution; rotary kiln roasting has the disadvantages of large pollution, small output, large investment, and low labor efficiency; boiling roasting has the disadvantages of incomplete desulfurization, inconvenient start-up and shutdown, and large investment.
发明内容 Contents of the invention
本实用新型的目的旨在解决上述技术问题的不足,提供一种用于镍钼矿与钼精粉的原生矿物氧化焙烧脱硫及脱碳装置。The purpose of this utility model is to solve the deficiencies of the above-mentioned technical problems, and provide a primary mineral oxidation roasting desulfurization and decarburization device for nickel-molybdenum ore and molybdenum fine powder.
本实用新型为解决上述技术问题的不足,所采取的技术方案是:在充分利用镍钼矿与钼精粉中硫碳能燃烧产生热能的基础上,采用增大矿物与空气接触表面积的方法实现快速燃烧,实施设备调整矿物的细度以喷射方式,控制空气量,实现燃烧脱硫,水洗为补,其装置包括上料机、熟料接收室、除尘装置、引风装置,在上料机与熟料接收室之间设有预热炉和点火控制室,点火控制室内的物料通道呈蜗壳状,预热炉的物料通道与点火控制室相通,点火控制室的物料通道与熟料接收室相通,物料经上料机进入后研磨成200目左右的细粉并喷入预热炉,经预热炉预热后将细粉喷入点火控制室,经预热炉喷出的物料基本达到矿粉的着火点,在经可控制的点火控制室旋转一周后实现点火燃烧,并可在燃烧的瞬间实现脱硫和脱碳,在熟料接收室的底部设有物料刮板和物料出口。In order to solve the above-mentioned technical problems, the utility model adopts the technical scheme as follows: on the basis of making full use of the sulfur and carbon in nickel-molybdenum ore and molybdenum fine powder to generate heat energy through combustion, the utility model adopts the method of increasing the contact surface area of minerals and air to realize Rapid combustion, implement equipment to adjust the fineness of minerals by spraying, control air volume, realize combustion desulfurization, and wash with water as a supplement. The device includes a feeder, clinker receiving room, dust removal device, and air induction device. There is a preheating furnace and an ignition control room between the clinker receiving room. The material channel in the ignition control room is in the shape of a volute. The material channel of the preheating furnace communicates with the ignition control room. In the same way, after the material enters through the feeder, it is ground into a fine powder of about 200 meshes and sprayed into the preheating furnace. After being preheated by the preheating furnace, the fine powder is sprayed into the ignition control room. The ignition point of the ore powder can be ignited and burned after the controllable ignition control room rotates once, and desulfurization and decarburization can be realized at the moment of burning. There is a material scraper and a material outlet at the bottom of the clinker receiving room.
本实用新型,所述的熟料接收室由一个或多个串联的熟料收集器组成。In the present utility model, the clinker receiving chamber is composed of one or more clinker collectors connected in series.
本实用新型,所述的熟料接收室还设有温度控制调节器。In the present utility model, the clinker receiving chamber is also provided with a temperature control regulator.
本实用新型,熟料接收室底部设置的物料刮板由一个通过链轮传动的电机自动控制。In the utility model, the material scraper arranged at the bottom of the clinker receiving chamber is automatically controlled by a motor driven by a sprocket.
本实用新型的预热炉由燃料燃烧室和物料流通室组成,其燃料燃烧室和物料流通室相处在一个空间体内。燃料燃烧室可燃烧各种煤炭、木柴及便于燃烧的原料。The preheating furnace of the utility model is composed of a fuel combustion chamber and a material circulation chamber, and the fuel combustion chamber and the material circulation chamber are together in a space body. The fuel combustion chamber can burn various coals, firewood and raw materials that are easy to burn.
本实用新型,还设有水洗收尘系统或酸洗系统,当微量的粉尘进入细颗粒水洗收尘系统或酸洗系统,经处理后再进入风机,致使全部的物料被收集,硫和碳被除去。The utility model is also equipped with a water washing dust collection system or a pickling system. When a small amount of dust enters the fine particle water washing dust collection system or pickling system, it enters the fan after treatment, so that all the materials are collected, and the sulfur and carbon are collected. remove.
本实用新型的优点是:The utility model has the advantages of:
1、操作简单,工人劳动强度小,可实现自动化操作;1. The operation is simple, the labor intensity of the workers is small, and the automatic operation can be realized;
2、投资小,降低成本,与同等规模的反射炉比,投资仅为其十分之一,与转窑比,投资仅为其二十分之一;2. Small investment and cost reduction. Compared with reverberatory furnaces of the same scale, the investment is only one tenth, and compared with rotary kilns, the investment is only one twentieth;
3、节约能源,可实现不外补加煤炭的方式进行燃烧;3. Energy saving, can realize burning without additional coal;
4、生产能力大;4. Large production capacity;
5、环保、排出的废气无污染,废气可控制在SO2浓度2-5%(V/V)以下,并可收集。5. Environmental protection, the discharged exhaust gas is non-polluting, and the exhaust gas can be controlled below the SO 2 concentration of 2-5% (V/V), and can be collected.
附图说明 Description of drawings
图1是本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;
图2是本实用新型的点火控制室结构示意图。Fig. 2 is a structural schematic diagram of the ignition control chamber of the present invention.
图中标记:1、上料机,2、预热炉,3、点火控制室,4、熟料接收室,5、物料刮板,6、除尘装置,7、引风装置,8、水洗收尘系统,9、电机,10、出料口,11、电机。Marks in the figure: 1. Loading machine, 2. Preheating furnace, 3. Ignition control room, 4. Clinker receiving room, 5. Material scraper, 6. Dust removal device, 7. Air induction device, 8. Washing and collecting Dust system, 9, motor, 10, discharge port, 11, motor.
具体实施方式 Detailed ways
由图1可知,本实用新型设有上料机1、熟料接收室4、除尘装置6,在上料机1与熟料接收室4之间设有预热炉2和点火控制室3,物料经上料机1进入后研磨成200目左右的细粉并喷入预热炉2,经预热炉2预热后将细粉喷入点火控制室3,经预热炉2喷出的物料基本达到矿粉的着火点,在经可控制的点火控制室3旋转一周后实现点火燃烧,在燃烧的同时喷入熟料接收室4,并在燃烧的瞬间实现脱硫和脱碳,在熟料接收室4的底部设有物料刮板5和物料出口11,当燃烧后的物料落入熟料接收室4的底部后,由设置的物料刮板5自动将其送入出料口10出料。燃烧充分的物料在熟料接收室4中收集,微量的粉尘进入细颗粒水洗收尘系统8,经水洗后进入引风装置7,由于物料与空气是按配比加入,可控制进入引风装置7的SO2气体浓度。As can be seen from Figure 1, the utility model is provided with a feeder 1, a
本实用新型,还适应于其它的原生矿物氧化焙烧脱硫及脱碳。The utility model is also suitable for oxidation roasting desulfurization and decarburization of other primary minerals.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200925510U CN201109791Y (en) | 2007-10-25 | 2007-10-25 | Molybdenum ore oxidation desulfurization device |
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|---|---|---|---|
| CNU2007200925510U CN201109791Y (en) | 2007-10-25 | 2007-10-25 | Molybdenum ore oxidation desulfurization device |
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| CN201109791Y true CN201109791Y (en) | 2008-09-03 |
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| CNU2007200925510U Expired - Fee Related CN201109791Y (en) | 2007-10-25 | 2007-10-25 | Molybdenum ore oxidation desulfurization device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102268538A (en) * | 2011-07-27 | 2011-12-07 | 中南大学 | Boiling furnace device used for roasting nickel-molybdenum concentrate and method for roasting nickel-molybdenum concentrate |
| CN103103342A (en) * | 2013-02-27 | 2013-05-15 | 伍耀明 | Rectangular vertical vacuum furnace for treating arsenic-containing gold mine |
| CN106269206A (en) * | 2016-08-22 | 2017-01-04 | 中国地质科学院矿产综合利用研究所 | Method for comprehensively recovering low-grade molybdenum from copper concentrate containing organic carbon |
-
2007
- 2007-10-25 CN CNU2007200925510U patent/CN201109791Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102268538A (en) * | 2011-07-27 | 2011-12-07 | 中南大学 | Boiling furnace device used for roasting nickel-molybdenum concentrate and method for roasting nickel-molybdenum concentrate |
| CN103103342A (en) * | 2013-02-27 | 2013-05-15 | 伍耀明 | Rectangular vertical vacuum furnace for treating arsenic-containing gold mine |
| CN103103342B (en) * | 2013-02-27 | 2014-03-19 | 伍耀明 | Rectangular vertical vacuum furnace for treating arsenic-containing gold mine |
| CN106269206A (en) * | 2016-08-22 | 2017-01-04 | 中国地质科学院矿产综合利用研究所 | Method for comprehensively recovering low-grade molybdenum from copper concentrate containing organic carbon |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080903 Termination date: 20111025 |