CN201809170U - Production equipment of phosphoric acid adopting reflection kiln method - Google Patents
Production equipment of phosphoric acid adopting reflection kiln method Download PDFInfo
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- CN201809170U CN201809170U CN2010201371877U CN201020137187U CN201809170U CN 201809170 U CN201809170 U CN 201809170U CN 2010201371877 U CN2010201371877 U CN 2010201371877U CN 201020137187 U CN201020137187 U CN 201020137187U CN 201809170 U CN201809170 U CN 201809170U
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- phosphoric acid
- yellow phosphorus
- reverberatory
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- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 title claims abstract description 48
- 229910000147 aluminium phosphate Inorganic materials 0.000 title claims abstract description 24
- 238000000034 method Methods 0.000 title claims abstract description 19
- 238000004519 manufacturing process Methods 0.000 title claims description 24
- OBSZRRSYVTXPNB-UHFFFAOYSA-N tetraphosphorus Chemical compound P12P3P1P32 OBSZRRSYVTXPNB-UHFFFAOYSA-N 0.000 claims abstract description 13
- 230000036571 hydration Effects 0.000 claims abstract description 5
- 238000006703 hydration reaction Methods 0.000 claims abstract description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 10
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 6
- 239000011449 brick Substances 0.000 claims description 4
- 239000000377 silicon dioxide Substances 0.000 claims description 4
- 239000002893 slag Substances 0.000 claims description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 3
- 239000000395 magnesium oxide Substances 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 2
- 239000004576 sand Substances 0.000 claims description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 1
- 239000003546 flue gas Substances 0.000 claims 1
- 239000008188 pellet Substances 0.000 abstract description 19
- 238000006243 chemical reaction Methods 0.000 abstract description 15
- 238000006722 reduction reaction Methods 0.000 abstract description 13
- 238000007254 oxidation reaction Methods 0.000 abstract description 11
- 230000003647 oxidation Effects 0.000 abstract description 8
- 239000003245 coal Substances 0.000 abstract description 7
- 239000002367 phosphate rock Substances 0.000 abstract description 7
- 150000001875 compounds Chemical class 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 5
- 239000002994 raw material Substances 0.000 abstract description 3
- 229910017053 inorganic salt Inorganic materials 0.000 abstract description 2
- 238000012423 maintenance Methods 0.000 abstract description 2
- 239000002244 precipitate Substances 0.000 abstract description 2
- 229910019142 PO4 Inorganic materials 0.000 abstract 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 abstract 1
- 239000010452 phosphate Substances 0.000 abstract 1
- OJMIONKXNSYLSR-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)O OJMIONKXNSYLSR-UHFFFAOYSA-N 0.000 abstract 1
- 239000002131 composite material Substances 0.000 description 10
- 238000002485 combustion reaction Methods 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 5
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 4
- 229910052698 phosphorus Inorganic materials 0.000 description 4
- 239000011574 phosphorus Substances 0.000 description 4
- 238000007363 ring formation reaction Methods 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 229910004261 CaF 2 Inorganic materials 0.000 description 1
- 241001391944 Commicarpus scandens Species 0.000 description 1
- 208000001613 Gambling Diseases 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
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Classifications
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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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
技术领域technical field
本实用新型属于无机盐工业的磷酸生产技术领域,是一种以中低品位磷矿石为原料、采取还原氧化法制成磷酸的工艺技术。 The utility model belongs to the technical field of phosphoric acid production in the inorganic salt industry, and relates to a process technology for preparing phosphoric acid by using medium and low-grade phosphate rocks as raw materials and adopting a reduction-oxidation method. the
背景技术Background technique
我国能源短缺的形势相当严峻,节省能源已成为我们面临的迫切任务。其中,磷矿资源经过数十年的开采,高品位的矿石已经很少,国内可以直接用于湿法磷酸生产的矿石已经所剩无几;剩下的绝大部分是高杂质含量的中、低品位磷矿,开采和利用都非常的困难,特别是对于磷酸行业。 The situation of energy shortage in our country is quite severe, and saving energy has become an urgent task we are facing. Among them, after decades of mining of phosphate rock resources, there are very few high-grade ores, and there are very few ores that can be directly used in the production of wet-process phosphoric acid in China; It is very difficult to mine and utilize high-grade phosphate rock, especially for the phosphoric acid industry. the
因此,上世纪80年代,美国西方石油研究公司开发了一种制备工业磷酸的新工艺——窑法磷酸,但这项研究由于存在反应工程技术问题一直未实现工业化。国内技术人员在国外的研究基础上,开发出很多新的窑法磷酸生产方法: Therefore, in the 1980s, the Western Petroleum Research Corporation of the United States developed a new process for preparing industrial phosphoric acid - kiln phosphoric acid, but this research has not been industrialized due to the problems of reaction engineering technology. On the basis of foreign research, domestic technicians have developed many new kiln phosphoric acid production methods:
1、回转窑:这是一种重载、大扭矩、多支点、筒状中空窑炉运行系统,球状物料在窑内随着窑体的旋转而运动;磷的还原在还原区进行,P4的氧化在氧化区进行,还原区和氧化区都在窑体内,燃料在窑内燃烧直接供热。该技术有很多不足之处:未考虑氧化区与还原区的分隔,物料中的还原炭容易被氧化而出现早然现象,因此炭用量大,同时影响磷的还原;此外回转窑窑内结圈现象严重,影响窑的正常运转而难以实现工业化生产。 1. Rotary kiln: This is a heavy-duty, high-torque, multi-fulcrum, cylindrical hollow kiln operating system. The spherical material moves in the kiln with the rotation of the kiln body; the reduction of phosphorus is carried out in the reduction zone, P 4 The oxidation of the furnace is carried out in the oxidation zone, the reduction zone and the oxidation zone are both in the kiln body, and the fuel is burned in the kiln for direct heating. This technology has many deficiencies: the separation of the oxidation zone and the reduction zone is not considered, and the reduced carbon in the material is easily oxidized and prematurely occurs, so the amount of carbon used is large, and the reduction of phosphorus is affected at the same time; in addition, ring formation in the rotary kiln The phenomenon is serious, which affects the normal operation of the kiln and is difficult to realize industrialized production.
2、隧道窑:这是一条长的直线型隧道,其两侧及顶部有固定的墙壁及拱(平)顶,底部铺设的轨道上运行着窑车,燃烧设备设在隧道窑的中部两侧;采用隔烟或明焰烧成物料放在窑车上,经过预热带、高温带和冷却带;该技术虽然解决了物料在窑内的翻滚破碎和结圈等问题,但还存在氧化区和还原区有效隔离的问题,同时也存在设备体积庞大、机械化程度低,生产过程复杂、还原反应时间长,还原率低,难实现大型工业化生产的问题。 2. Tunnel kiln: This is a long linear tunnel with fixed walls and arched (flat) roofs on both sides and the top. The kiln car is running on the track laid at the bottom, and the combustion equipment is located on both sides of the middle of the tunnel kiln. ;Using smoke insulation or open flame firing materials are placed on the kiln car, passing through the preheating zone, high temperature zone and cooling zone; although this technology solves the problems of tumbling, crushing and ring formation of materials in the kiln, there are still oxidation zones The problem of effective isolation from the reduction area, but also the problems of bulky equipment, low degree of mechanization, complex production process, long reduction reaction time, low reduction rate, and difficulty in realizing large-scale industrial production. the
3、锟道窑:这是隧道窑技术的的一种改进,相对于隧道窑虽然磷矿反应时间缩短,自动化程度提高,但仍然存在体积庞大,成产过程复杂的问题。 3. Kundao kiln: This is an improvement of tunnel kiln technology. Compared with tunnel kiln, although the reaction time of phosphate rock is shortened and the degree of automation is improved, there are still problems of large volume and complicated production process. the
4、环底窑:环底窑结构复杂,操作繁琐,高温下容易发生赌赛现象。 4. Ring-bottom kiln: Ring-bottom kiln has complex structure and cumbersome operation, and it is prone to gambling under high temperature. the
5、专利号为ZL200920081113.3的专利提供了一种竖窑法,该窑法虽然结构简单、能将氧化区和还原区有效地隔离、窑内不结圈、热量的利用比较合理,但是由于该设备是竖的,而且比较高(20米),所以很容易对成型原料造成破碎,反应率以及资源利用率因此而降低。 5. The patent No. ZL200920081113.3 provides a vertical kiln method. Although this kiln method has a simple structure, can effectively isolate the oxidation zone and the reduction zone, does not form rings in the kiln, and uses heat more reasonably, but due to The equipment is vertical and relatively high (20 meters), so it is easy to break the molding raw materials, and the reaction rate and resource utilization rate are thus reduced. the
以上方法均使用煤炭来燃烧放热,没有能更多地利用磷的燃烧放热。 The above methods all use coal to burn and release heat, and there is no combustion and release of heat that can make more use of phosphorus. the
发明内容Contents of the invention
本实用新型针对现有技术的不足,提出一种磷酸的反射窑法生产设备,用此磷酸新型生产设备生产磷酸是采用黄磷代替部分煤炭燃烧,节约能源,最大限度地实现了能源在磷酸生产中的综合利用,大大降低了生产成本。该设备反应率高,窑内不存在结圈现象,设备结构简单,体积小,投资少,操作方便。 Aiming at the deficiencies of the prior art, the utility model proposes a reverberatory kiln production equipment for phosphoric acid. The production of phosphoric acid by using this new phosphoric acid production equipment uses yellow phosphorus instead of part of the coal combustion, saves energy, and realizes energy in the production of phosphoric acid to the greatest extent. The comprehensive utilization of them greatly reduces the production cost. The equipment has a high reaction rate, no ring formation in the kiln, simple structure, small volume, low investment and convenient operation. the
本实用新型提供了一种磷酸的反射窑法生产设备,其反射窑主要结构包括1、炉门;2、加料口;3、P2O5出口;4、排渣口;5、黄磷入口;6、空气入口。窑壁采用内衬镁砖;窑顶采用拱式顶,内衬硅砖;窑底用镁铁砂烧结而成。工作原理是首先黄磷经黄磷入口5进入反射窑燃烧,热量通过窑顶、窑壁以及炽热气体反射给复合球粒,复合球粒内发生还原反应生成P4蒸气,P4蒸气从复合球粒内析出,并在窑内发生氧化反应,生成P2O5,然后经引风机引入水合塔;氧化反应产生的热量也通过窑顶、窑壁以及炽热空气反射给复合球粒;复合残球经过反应之后,体积变小,从排渣口4排出。 The utility model provides a reverberatory kiln production equipment for phosphoric acid. The main structure of the
本实用新型提供一种磷酸的反射窑法生产设备,其新生产工艺如下: The utility model provides a reverberatory kiln production equipment for phosphoric acid, and its new production process is as follows:
将磷矿石、硅石、焦炭3种原料按要求计量,然后经破碎、粉磨成通过200目的细粉,再加入粘结剂经润磨致密,然后用盘式造球机成球(直径约15mm)。同时,包裹剂(煤和熔点调整剂)也经球磨后加入粘结剂再经润磨致密,用另一台盘式造粒机包裹在上述球粒表面,制成复合球粒。复合球粒送入链篦机利用冷却残球所获的热空气进行干燥和预热,热球进入反射窑,在此球粒进行还原反应,窑内进行氧化反应。 The phosphate rock, silica, and coke are measured according to the requirements, then crushed and ground into a fine powder of 200 mesh, then added with a binder, moistened and compacted, and then formed into balls with a disc pelletizer (diameter approx. 15mm). At the same time, the wrapping agent (coal and melting point regulator) is ball-milled, then added with a binder, then moistened and compacted, and wrapped on the surface of the above-mentioned pellets by another disc granulator to make composite pellets. Composite pellets are fed into the chain grate machine to use the hot air obtained from cooling residual balls for drying and preheating, and the hot balls enter the reverberatory kiln, where the pellets undergo reduction reaction and oxidation reaction takes place in the kiln. the
反应原理如下: The reaction principle is as follows:
复合球粒内: Inside the composite pellet:
Ca10(PO4)6F2+15C+9SiO2→3/2P4+15CO+9CaO·SiO2+CaF2 (1) Ca 10 (PO 4 ) 6 F 2 +15C+9SiO 2 →3/2P 4 +15CO+9CaO·SiO 2 +CaF 2 (1)
ΔH=28006kJ/kg(P4) ΔH=28006kJ/kg(P 4 )
反射窑内: In the reflection kiln:
P4+5O2→2P2O5 (2) P 4 +5O 2 →2P 2 O 5 (2)
ΔH=-25498kJ/kg(P4) ΔH=-25498kJ/kg (P 4 )
CO+1/2O2→2CO2 (3) CO+1/2O 2 →2CO 2 (3)
ΔH=-22154kJ/kg(P4) ΔH=-22154kJ/kg (P 4 )
上述反应中,反应(2)(3)放出的热量大大地满足反应(1)所吸收的热量,故反应(1)能持续地进行。 In the above reactions, the heat released by reactions (2) and (3) largely meets the heat absorbed by reaction (1), so reaction (1) can continue. the
反射窑生成含P2O5的窑气导入水化塔,经净化等工序即得高纯度的磷酸。反应后残球粒进入链篦机鼓入空气冷却,热空气则导入干燥链篦机和反射窑使用。 The reverberatory kiln generates kiln gas containing P 2 O 5 and introduces it into the hydration tower. After purification and other processes, high-purity phosphoric acid can be obtained. After the reaction, the residual balls enter the chain grate and blow air to cool, and the hot air is introduced into the drying chain and the reverberatory kiln for use.
本实用新型采用一种磷酸的反射窑法生产设备,此生产设备将热法磷酸与窑法磷酸生产 原理相结合,其优点如下: The utility model adopts a reflective kiln production equipment for phosphoric acid. This production equipment combines the production principles of thermal phosphoric acid and kiln phosphoric acid. Its advantages are as follows:
1、本实用新型所述的反射窑内,采用黄磷代替部分煤炭燃烧,节约能源,最大限度地实现了能源在磷酸生产中的综合利用,大大降低了生产成本。 1. In the reverberatory kiln described in the utility model, yellow phosphorus is used to replace part of the coal combustion, which saves energy, realizes the comprehensive utilization of energy in the production of phosphoric acid to the greatest extent, and greatly reduces the production cost. the
2、本实用新型采用黄磷燃烧加热复合球粒,代替传统的煤燃烧加热法,实现了能源的综合利用,节约了成本,同时也保证了质量。 2. The utility model adopts yellow phosphorus combustion and heating composite pellets to replace the traditional coal combustion heating method, realizes comprehensive utilization of energy, saves cost, and ensures quality at the same time. the
3、本实用新型所述的反射窑,热量是通过反射的方式传给复合球粒,所以复合球粒受热均匀,反应完全,实现了热量的充分利用。 3. In the reverberatory kiln described in the utility model, the heat is transmitted to the composite pellets through reflection, so the composite pellets are heated evenly and react completely, realizing full utilization of heat. the
4、本实用新型所述的反射窑不转动,不存在结圈现象,同时由于投料口与窑底的距离不高,所以不存在复合球粒破碎的现象。 4. The reverberatory kiln described in the utility model does not rotate, and there is no ring formation phenomenon. At the same time, because the distance between the feeding port and the kiln bottom is not high, there is no phenomenon of composite pellets being broken. the
5、本实用新型所述的反射窑,其结构简单,体积小,操作简易,维修方便 5. The reverberatory kiln described in the utility model has simple structure, small volume, simple operation and convenient maintenance
附图说明Description of drawings
图1是本实用新型窑法磷酸生产设备一反射窑结构示意图 Fig. 1 is a structural schematic diagram of a reverberatory kiln of the utility model kiln process phosphoric acid production equipment
图2是图1的侧视图 Figure 2 is a side view of Figure 1
图3是本实用新型工艺流程图 Fig. 3 is a process flow diagram of the utility model
具体实施方式Detailed ways
实施例1 Example 1
先将磷矿(28%)、硅石、焦炭按比例10∶7∶3,经破碎、粉磨成的细粉;取200kg细粉,加入粘结剂经润磨致密,然后用盘式造球机成复合球粒,直径约15mm。用链篦机预热并送入反射窑内;黄磷燃烧器中的黄磷10kg在反射窑内自燃,使窑内温度逐步上升至1200℃左右;反应球粒在此温度下发生还原反应,并析出P4蒸气,反应时间1.5小时;反应残球经排渣口排出;P4蒸气在氧化区内迅速发生氧化反应,窑气从P2O5出口进入水合塔,后经净化等工序即得120kg高纯度的磷酸(85%),磷的收率达95%,反应过程中设备运行稳定。 First, phosphate rock (28%), silica and coke are crushed and ground into a fine powder in a ratio of 10:7:3; take 200kg of fine powder, add a binder, moisten and compact, and then use a disc pelletizer Machine into composite pellets, about 15mm in diameter. Preheat with a grate and send it into the reverberatory kiln; 10kg of yellow phosphorus in the yellow phosphorus burner spontaneously ignites in the reverberatory kiln, making the temperature in the kiln gradually rise to about 1200°C; the reaction pellets undergo a reduction reaction at this temperature, And precipitate P 4 steam, the reaction time is 1.5 hours; the reaction residual balls are discharged through the slag discharge port; the P 4 steam oxidizes rapidly in the oxidation zone, and the kiln gas enters the hydration tower from the P 2 O 5 outlet, and then undergoes purification and other processes to obtain Obtain 120kg of high-purity phosphoric acid (85%), the yield of phosphorus reaches 95%, and the equipment runs stably in the reaction process.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775677A (en) * | 2017-11-10 | 2019-05-21 | 广西越洋科技股份有限公司 | A method of production phosphoric acid is combined with shaft kiln using reverberatory furnace |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775677A (en) * | 2017-11-10 | 2019-05-21 | 广西越洋科技股份有限公司 | A method of production phosphoric acid is combined with shaft kiln using reverberatory furnace |
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