CN201686500U - A microwave rotary kiln for calcination of uranium chemical concentrate - Google Patents
A microwave rotary kiln for calcination of uranium chemical concentrate Download PDFInfo
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- CN201686500U CN201686500U CN2010201361409U CN201020136140U CN201686500U CN 201686500 U CN201686500 U CN 201686500U CN 2010201361409 U CN2010201361409 U CN 2010201361409U CN 201020136140 U CN201020136140 U CN 201020136140U CN 201686500 U CN201686500 U CN 201686500U
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- 229910052770 Uranium Inorganic materials 0.000 title claims abstract description 13
- 239000012141 concentrate Substances 0.000 title claims abstract description 13
- 239000000126 substance Substances 0.000 title claims abstract description 13
- JFALSRSLKYAFGM-UHFFFAOYSA-N uranium(0) Chemical compound [U] JFALSRSLKYAFGM-UHFFFAOYSA-N 0.000 title claims abstract description 13
- 238000001354 calcination Methods 0.000 title abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 21
- 238000001816 cooling Methods 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000007599 discharging Methods 0.000 claims abstract description 7
- 239000000779 smoke Substances 0.000 claims description 9
- 238000009413 insulation Methods 0.000 claims description 7
- 229910000838 Al alloy Inorganic materials 0.000 claims description 4
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 239000003517 fume Substances 0.000 claims 2
- 238000000034 method Methods 0.000 abstract description 7
- 238000009826 distribution Methods 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000010924 continuous production Methods 0.000 abstract 1
- 238000011031 large-scale manufacturing process Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 description 10
- 238000010438 heat treatment Methods 0.000 description 8
- 238000009529 body temperature measurement Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- UBEWDCMIDFGDOO-UHFFFAOYSA-N cobalt(2+);cobalt(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[O-2].[Co+2].[Co+3].[Co+3] UBEWDCMIDFGDOO-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- SYHPANJAVIEQQL-UHFFFAOYSA-N dicarboxy carbonate Chemical compound OC(=O)OC(=O)OC(O)=O SYHPANJAVIEQQL-UHFFFAOYSA-N 0.000 description 2
- 125000005289 uranyl group Chemical group 0.000 description 2
- MJLGNAGLHAQFHV-UHFFFAOYSA-N arsenopyrite Chemical compound [S-2].[Fe+3].[As-] MJLGNAGLHAQFHV-UHFFFAOYSA-N 0.000 description 1
- 229910052964 arsenopyrite Inorganic materials 0.000 description 1
- DVRDHUBQLOKMHZ-UHFFFAOYSA-N chalcopyrite Chemical compound [S-2].[S-2].[Fe+2].[Cu+2] DVRDHUBQLOKMHZ-UHFFFAOYSA-N 0.000 description 1
- 229910052951 chalcopyrite Inorganic materials 0.000 description 1
- 238000006880 cross-coupling reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000009768 microwave sintering Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000021715 photosynthesis, light harvesting Effects 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 230000008093 supporting effect Effects 0.000 description 1
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Abstract
本实用新型涉及一种用于铀化学浓缩物煅烧的微波回转窑。该设备主要由高位料仓,进料机构,出料机构,微波反应腔体,微波回转窑炉膛,测温仪,微波功率源,水冷系统,远程控制系统等部件组成。主要用于铀化学浓缩物煅烧。该设备不仅克服了常规煅烧设备存在的周期长,能耗高,热效率低,产品均一性差,易发生欠烧、过烧等问题,而且微波场分布均匀,设备稳定性强,是一种铀化学浓缩物煅烧工艺中大型化、连续化生产的微波设备。
The utility model relates to a microwave rotary kiln used for calcination of uranium chemical concentrates. The equipment is mainly composed of high-level silo, feeding mechanism, discharging mechanism, microwave reaction chamber, microwave rotary kiln furnace, temperature measuring instrument, microwave power source, water cooling system, remote control system and other components. It is mainly used for calcination of uranium chemical concentrates. This equipment not only overcomes the problems of long cycle, high energy consumption, low thermal efficiency, poor product uniformity, easy occurrence of under-burning and over-burning of conventional calcination equipment, but also has uniform microwave field distribution and strong equipment stability. It is a uranium chemical Microwave equipment for large-scale and continuous production in the concentrate calcination process.
Description
一、技术领域1. Technical field
本实用新型涉及一种用于铀化学浓缩物煅烧的微波回转窑,尤其是一种连续化、规模化的适宜于铀化学浓缩物煅烧的微波加热设备。The utility model relates to a microwave rotary kiln for calcination of uranium chemical concentrates, in particular to a continuous and large-scale microwave heating equipment suitable for calcination of uranium chemical concentrates.
二、背景技术2. Background technology
目前,众知的铀化学浓缩物煅烧通常采用以滚筒为代表的半动态电热煅烧窑。其特征是通过传导、对流、辐射等方式使热量从物料外部向内部传递。由于该设备在同一截面上存在温度分布不均匀,从而导致该生产方法存在周期长,能耗高,热效率低,产品均一性差,易发生欠烧、过烧等现象,给后续工序带来加工困难;而且更为关键的是电热窑煅烧三碳酸铀酰铵加工工艺时间长会导致核辐射威胁几率增大。如专利CN1319848A提供的煅烧三碳酸铀酰铵制备八氧化三铀工艺过程中,需以300-500℃/小时由室温升至700-900℃,同时保温时间长达2-6小时。因此,开发一种快速、安全、低能耗的新型煅烧设备显得极为重要。At present, the known calcining of uranium chemical concentrates usually adopts a semi-dynamic electric calcining kiln represented by a drum. It is characterized in that heat is transferred from the outside to the inside of the material through conduction, convection, radiation, etc. Due to the uneven temperature distribution on the same section of the equipment, the production method has a long cycle, high energy consumption, low thermal efficiency, poor product uniformity, and prone to under-burning and over-burning, which will bring processing difficulties to subsequent processes. ; and more critically, the electric kiln calcining ammonium uranyl tricarbonate for a long time will lead to an increase in the threat of nuclear radiation. For example, in the process of preparing U3O8 by calcining ammonium uranyl tricarbonate provided by the patent CN1319848A, it needs to be raised from room temperature to 700-900°C at 300-500°C/hour, and the holding time is as long as 2-6 hours. Therefore, it is extremely important to develop a new type of calcination equipment that is fast, safe, and low in energy consumption.
微波作为一种绿色高效的加热方法,可以通过在物料内部的能量耗散选择性加热物料,具有加热均匀、热效率高、清洁无污染等常规加热方式无法比拟的优点。然而,公知的微波设备中,经改装的家用微波炉属间歇式加热,功率密度低、重复性差,无法进行规模化作业;对于大功率高温微波设备,尽管国内外均开展了这方面的研究,如英国EA技术公司建立了微波高温烧结设备,加拿大的EMR微波技术公司建立了黄铜矿和砷黄铁矿的微波预处理装置,但均存在微波场分布不均匀,设备密闭性不好等问题。如专利CN1718790A提供的微波烧结设备,尽管能满足四氧化三钴的制备,但存在密闭性差,反应器内温度场分布单一,无法实现铀化学浓缩物的移植性煅烧。因此,目前能够用于煅烧铀化学浓缩物的连续化、规模化的高温微波设备仍然是空白。另外,由于目前微波反应器功率源系统多采用自然风冷或强制风冷方式冷却,然不论是自然风冷还是强制风冷均存在冷却效率低,冷却效果差,从而导致设备稳定性差、使用寿命短。As a green and efficient heating method, microwave can selectively heat materials through energy dissipation inside the materials. It has the advantages of uniform heating, high thermal efficiency, clean and pollution-free, etc. that cannot be compared with conventional heating methods. However, among the known microwave equipment, the refitted household microwave oven belongs to intermittent heating, has low power density and poor repeatability, and cannot carry out large-scale operations; for high-power high-temperature microwave equipment, although researches in this area have been carried out both at home and abroad, such as British EA Technology Company has established microwave high-temperature sintering equipment, and Canadian EMR Microwave Technology Company has established microwave pretreatment devices for chalcopyrite and arsenopyrite, but there are problems such as uneven distribution of microwave fields and poor airtightness of equipment. For example, the microwave sintering equipment provided by the patent CN1718790A, although it can meet the preparation of tricobalt tetroxide, has poor airtightness, single temperature field distribution in the reactor, and cannot realize the implantable calcination of uranium chemical concentrates. Therefore, the continuous and large-scale high-temperature microwave equipment that can be used for calcining uranium chemical concentrates is still blank. In addition, since the current microwave reactor power source system is mostly cooled by natural air cooling or forced air cooling, both natural air cooling and forced air cooling have low cooling efficiency and poor cooling effect, resulting in poor equipment stability and long service life. short.
综上可知,由于缺乏安全、稳定的专用微波反应器,使微波的产业化应用范围较窄,对经济的支撑作用很不明显。因此,研发连续化、规模化的高温微波反应器对于引领未来微波在核能工业的发展具有重要的作用。To sum up, due to the lack of safe and stable dedicated microwave reactors, the scope of industrial application of microwave is narrow, and the supporting effect on the economy is not obvious. Therefore, the development of continuous and large-scale high-temperature microwave reactors plays an important role in leading the development of microwave in the nuclear energy industry in the future.
三、发明内容3. Contents of the invention
本实用新型的目的是提供一种用于铀化学浓缩物煅烧的微波回转窑。针对常规电热回转窑存在生产周期长,能耗高,产品均一性差等弊端和现有微波设备存在的微波场分布不均匀、设备稳定性差、使用寿命短等不足,依据铀化学浓缩物辐射危害大、设备密闭性要求高等特殊性,提供的这种微波回转窑是一种适宜于铀化学浓缩物煅烧,可实现多段控温的连续化、规模化的高温微波回转窑设备。The purpose of the utility model is to provide a microwave rotary kiln for calcination of uranium chemical concentrate. In view of the disadvantages of conventional electric heating rotary kiln, such as long production cycle, high energy consumption, and poor product uniformity, and the existing microwave equipment, such as uneven distribution of microwave field, poor equipment stability, and short service life, etc., according to the large radiation hazard of uranium chemical concentrates , The airtightness of the equipment requires high specificity. The microwave rotary kiln provided is a kind of high-temperature microwave rotary kiln equipment suitable for calcination of uranium chemical concentrates, which can realize continuous and large-scale multi-stage temperature control.
本实用新型按以下技术方案实施,其包括高位料仓1,进料机构2,排烟系统3,微波反应腔体4,微波回转窑炉膛5,出料机构6,远程控制系统7,微波功率源8,水冷系统9,保温层10,测温仪11。高位料仓1置于微波反应腔体4进料端,其下部与进料机构2连接,进料机构采用螺旋方式进料,进料螺旋通过链条与调速电机相连,微波反应腔体4为正五面体的反应腔体,微波功率源8配置水冷系统9布置于微波反应腔体4的四周,水冷系统9采用铝合金环形水冷器装配在微波功率源8上,微波回转窑炉膛5两端设置有钢质夹套,夹套上装配有齿轮,齿轮通过链条与调速电机连接驱动微波回转窑炉膛5转动,微波回转窑炉膛5的按装斜度为3-10度,出料机构6与微波回转窑炉膛5出料端相连接,进料机构2和出料机构6与微波回转窑炉膛5之间用石墨密封环密封,微波回转窑炉膛5外覆保温层10,微波回转窑炉膛排烟系统3,一端与进料端固定连接,另一端与排烟管连接,微波回转窑炉膛5出料端装配有测温仪11,采用独立的PID(比例-积分-微分)三段模块控温,测温热电偶采用三点组合式测温,微波回转窑通过远程控制系统7控制。The utility model is implemented according to the following technical scheme, which includes a high-
工作时将物料装入高位料仓,开启进出料开关,调节进料螺旋转速,物料通过进料螺旋连续地输送至微波反应腔体内,待物料布满微波回转窑炉膛并达到一定厚度后开启微波加热开关,调节微波输出功率,使物料由室温以一定的升温速率分别升至预定温度,物料由回转窑进料端缓慢地经过整个回转窑炉膛,经微波处理后由出料机构排出回收,烟气由排烟系统排出。When working, put the material into the high-level hopper, turn on the in-out material switch, adjust the feeding screw speed, and the material is continuously transported into the microwave reaction chamber through the feeding screw, and the microwave is turned on after the material is covered with the microwave rotary kiln and reaches a certain thickness. The heating switch adjusts the microwave output power so that the materials are raised from room temperature to the predetermined temperature at a certain heating rate. The materials pass through the entire rotary kiln chamber slowly from the feed end of the rotary kiln, and are discharged and recovered by the discharge mechanism after microwave treatment. The gas is exhausted by the smoke exhaust system.
本实用新型的优点及积极效果Advantages and positive effects of the utility model
(1)通过对微波反应腔的仿真优化,本微波反应腔体采用正五面体设计,使得微波源间交叉互耦最小,腔体内微波场更均匀;(1) Through the simulation optimization of the microwave reaction chamber, the microwave reaction chamber adopts a regular pentahedron design, so that the cross-coupling between microwave sources is minimized, and the microwave field in the cavity is more uniform;
(2)微波磁控管采用铝合金环形水冷方式,提高了设备的稳定性、延长了设备的使用寿命;(2) The microwave magnetron adopts aluminum alloy annular water cooling method, which improves the stability of the equipment and prolongs the service life of the equipment;
(3)微波反应腔体进出料机构与炉膛之间采用石墨密封环密封,保证了炉膛的密闭性;(3) The graphite sealing ring is used to seal between the microwave reaction cavity feeding and discharging mechanism and the furnace to ensure the airtightness of the furnace;
(4)基于微波“体加热”特性,使物料整体均匀受热,产品成分及粒径均匀,生产周期短;(4) Based on the characteristics of microwave "body heating", the whole material is heated evenly, the product composition and particle size are uniform, and the production cycle is short;
(5)微波反应腔体通过PLC远程控制系统控制,避免了微波泄露可能对人体造成的伤害。(5) The microwave reaction chamber is controlled by the PLC remote control system, which avoids possible damage to the human body caused by microwave leakage.
四、附图说明4. Description of drawings
图1是本实用新型组成结构图,图中,1为高位料仓,2为进料机构,3为排烟系统,4为微波反应腔体,5为微波回转窑炉膛,6为出料机构,7为远程控制系统,8为微波功率源,9为水冷系统,10为保温层,11为测温仪。Fig. 1 is a structural diagram of the utility model, in which, 1 is a high-level silo, 2 is a feeding mechanism, 3 is a smoke exhaust system, 4 is a microwave reaction chamber, 5 is a microwave rotary kiln hearth, and 6 is a discharge mechanism , 7 is a remote control system, 8 is a microwave power source, 9 is a water cooling system, 10 is an insulation layer, and 11 is a thermometer.
五、具体实施方式5. Specific implementation
按图1所示的结构,其包括高位料仓1,进料机构2,排烟系统3,微波反应腔体4,微波回转窑炉膛5,出料机构6,远程控制系统7,微波功率源8,水冷系统9,保温层10,测温仪11。高位料仓1置于微波反应腔体4进料端,其下部与进料机构2连接,进料机构采用螺旋方式进料,进料螺旋通过链条与调速电机相连,微波反应腔体4为正五面体的反应腔体,微波功率源8配置水冷系统9布置于微波反应腔体4的四周,水冷系统9采用铝合金环形水冷器装配在微波功率源8上,微波回转窑炉膛5两端设置有钢质夹套,夹套上装配有齿轮,齿轮通过链条与调速电机连接驱动微波回转窑炉膛5转动,微波回转窑炉膛5的按装斜度为3-10度,出料机构6与微波回转窑炉膛5出料端相连接,进料机构2和出料机构6与微波回转窑炉膛5之间用石墨密封环密封,微波回转窑炉膛5外覆保温层10,微波回转窑炉膛排烟系统3,一端与进料端固定连接,另一端与排烟管连接,微波回转窑炉膛5出料端装配有测温仪11,采用独立的PID(比例-积分-微分)三段模块控温,测温热电偶采用三点组合式测温,微波回转窑通过远程控制系统7控制。According to the structure shown in Figure 1, it includes a high-
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CN102419086A (en) * | 2011-12-20 | 2012-04-18 | 湖南省中晟热能科技有限公司 | Microwave and electricity hybrid heating high-temperature rotary kiln |
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CN109592714A (en) * | 2018-11-19 | 2019-04-09 | 中核二七二铀业有限责任公司 | A kind of method of uranyl nitrate thermal denitration preparation high activity orange oxide |
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CN102326858A (en) * | 2011-05-26 | 2012-01-25 | 云南昆船瑞升烟草加工新技术有限责任公司 | Roller type tobacco stalk continuous microwave expansion device |
CN102419086A (en) * | 2011-12-20 | 2012-04-18 | 湖南省中晟热能科技有限公司 | Microwave and electricity hybrid heating high-temperature rotary kiln |
CN106211405A (en) * | 2016-07-08 | 2016-12-07 | 同济大学 | A kind of tunnel type band revolute function multi-die microwave resonant chamber |
CN106211405B (en) * | 2016-07-08 | 2019-08-06 | 同济大学 | A tunnel-type multi-mode microwave resonator with gyration function |
CN109592714A (en) * | 2018-11-19 | 2019-04-09 | 中核二七二铀业有限责任公司 | A kind of method of uranyl nitrate thermal denitration preparation high activity orange oxide |
WO2020234075A1 (en) * | 2019-05-21 | 2020-11-26 | Basf Se | Process for performing endothermic reactions, and reaction vessel suitable therefore |
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