CN106861581B - Device for recovering nitrogen from aluminum ash - Google Patents
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- CN106861581B CN106861581B CN201710104286.1A CN201710104286A CN106861581B CN 106861581 B CN106861581 B CN 106861581B CN 201710104286 A CN201710104286 A CN 201710104286A CN 106861581 B CN106861581 B CN 106861581B
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 title claims abstract description 68
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 51
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 51
- 229910052757 nitrogen Inorganic materials 0.000 title claims abstract description 34
- 238000006243 chemical reaction Methods 0.000 claims abstract description 19
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000010521 absorption reaction Methods 0.000 claims abstract description 10
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 3
- 239000002893 slag Substances 0.000 claims description 40
- 238000003756 stirring Methods 0.000 claims description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 238000001914 filtration Methods 0.000 claims description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 5
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 229920000742 Cotton Polymers 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 2
- 239000000292 calcium oxide Substances 0.000 claims description 2
- 235000012255 calcium oxide Nutrition 0.000 claims description 2
- 239000000741 silica gel Substances 0.000 claims description 2
- 229910002027 silica gel Inorganic materials 0.000 claims description 2
- 239000002002 slurry Substances 0.000 description 15
- 238000000034 method Methods 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 230000008569 process Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 210000005069 ears Anatomy 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 229910018626 Al(OH) Inorganic materials 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- PMHQVHHXPFUNSP-UHFFFAOYSA-M copper(1+);methylsulfanylmethane;bromide Chemical compound Br[Cu].CSC PMHQVHHXPFUNSP-UHFFFAOYSA-M 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1418—Recovery of products
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/28—Methods of preparing ammonium salts in general
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Processing Of Solid Wastes (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
技术领域technical field
本公开一般涉及氮元素的回收装置,具体涉及用于回收铝灰渣中氮元素的装置。The present disclosure generally relates to a device for recovering nitrogen, and more particularly, to a device for recovering nitrogen from aluminum ash slag.
背景技术Background technique
铝灰渣(铝灰/铝渣)是铝工业中常见的废弃物,产量巨大,其主要来源为熔炼铝及铝合金生产过程中浮于铝溶体表面的不熔夹杂物、氧化物、添加剂以及与添加剂进行物理、化学反应产生的反应产物等,产生于铝发生熔融的所有生产工序。Aluminum ash slag (aluminum ash/aluminum slag) is a common waste in the aluminum industry with huge output. Its main sources are infusible inclusions, oxides, additives and Reaction products produced by physical and chemical reactions with additives, etc., are produced in all production processes in which aluminum is melted.
在铝的冶炼过程中通常要向熔炉里充氮气,加速净化与提纯,一部分氮气在蒸发时被漂浮在铝水表面的铝灰渣吸收,因此铝灰渣含氮;而氮化铝遇水生成氨气,受热易挥发,所以铝灰渣受潮即有刺激性极强的氨味,长期以来给环境稳定和人员健康带来了极大困扰。In the process of aluminum smelting, nitrogen is usually charged into the furnace to accelerate purification and purification. Part of the nitrogen is absorbed by the aluminum slag floating on the surface of the aluminum water during evaporation, so the aluminum slag contains nitrogen; and aluminum nitride is formed when it encounters water. Ammonia gas is volatile when heated, so the aluminum ash slag will have a strong irritating ammonia smell when wet, which has brought great trouble to environmental stability and personnel health for a long time.
目前针对铝灰渣中氮元素的利用方法很多,基本上停留于理论层面,而对铝灰渣中氮元素的回收利用装置极少,亟需提供一种用于回收铝灰渣中氮元素的装置。At present, there are many utilization methods for nitrogen in aluminum ash slag, which basically stay at the theoretical level, and there are very few recycling devices for nitrogen in aluminum ash slag. It is urgent to provide a method for recovering nitrogen in aluminum ash slag device.
发明内容SUMMARY OF THE INVENTION
鉴于现有技术中的上述缺陷或不足,期望提供一种用于回收铝灰渣中氮元素的装置,以最大限度的回收铝灰渣中的氮元素,避免铝灰渣(铝渣)后期加工过程对环境的污染,实现铝灰渣处理的无害化、资源化和效益化。In view of the above-mentioned defects or deficiencies in the prior art, it is desired to provide a device for recovering nitrogen elements in aluminum ash slag, so as to maximize the recovery of nitrogen elements in aluminum ash slag and avoid post-processing of aluminum ash slag (aluminum slag). The process of pollution to the environment, to achieve harmless, resourceful and efficient aluminum ash slag treatment.
本发明提供的一种用于回收铝灰渣中氮元素的装置,包括反应釜和吸收塔,所述反应釜与所述吸收塔之间通过用于收集氨气的管道连通。A device for recovering nitrogen in aluminum ash slag provided by the present invention comprises a reaction kettle and an absorption tower, and the reaction kettle and the absorption tower are communicated through a pipeline for collecting ammonia gas.
与现有技术相比,本申请提供的用于回收铝灰渣中氮元素的装置,用于铝灰渣与水混合形成浆料、进行水解反应,生成氨气并经管道传输至吸收塔,进而提取氮元素。本发明提供的装置能够高效、快速地回收铝灰渣中的氮,将长期以来铝灰渣中被忽视的氮元素充分利用起来,同时能够有效地解决铝灰渣回收利用中出现的刺激性气味问题,极大地改善工作环境,保障了操作人员的生命健康。Compared with the prior art, the device for recovering nitrogen in aluminum ash slag provided by the present application is used for mixing aluminum ash slag with water to form slurry, performing hydrolysis reaction, generating ammonia gas and transferring it to an absorption tower through a pipeline, Then extract nitrogen. The device provided by the invention can efficiently and quickly recover the nitrogen in the aluminum ash slag, make full use of the neglected nitrogen element in the aluminum ash slag for a long time, and at the same time can effectively solve the irritating smell that occurs in the recycling and utilization of the aluminum ash slag problems, greatly improving the working environment and ensuring the life and health of operators.
附图说明Description of drawings
通过阅读参照以下附图所作的对非限制性实施例所作的详细描述,本申请的其它特征、目的和优点将会变得更明显:Other features, objects and advantages of the present application will become more apparent by reading the detailed description of non-limiting embodiments made with reference to the following drawings:
图1为本发明提供的用于回收铝灰渣中氮元素的装置的结构示意图;Fig. 1 is the structural representation of the device for reclaiming nitrogen element in aluminium ash slag provided by the present invention;
图2为本发明提供的用于回收铝灰渣中氮元素的装置中第一壳体的结构示意图;2 is a schematic structural diagram of a first housing in the device for recovering nitrogen in aluminum ash slag provided by the present invention;
图3为本发明提供的用于回收铝灰渣中氮元素的装置中第一壳体透视图;3 is a perspective view of the first shell in the device for recovering nitrogen in aluminum ash slag provided by the present invention;
图4为本发明提供的用于回收铝灰渣中氮元素的装置中搅拌轴与电机的连接结构示意图;4 is a schematic diagram of the connection structure of the stirring shaft and the motor in the device for recovering nitrogen in aluminum ash slag provided by the present invention;
图5为本发明提供的用于回收铝灰渣中氮元素的装置中过滤装置的结构示意图。FIG. 5 is a schematic structural diagram of a filtering device in the device for recovering nitrogen in aluminum ash slag provided by the present invention.
具体实施方式Detailed ways
下面结合附图和实施例对本申请作进一步的详细说明。可以理解的是,此处所描述的具体实施例仅仅用于解释相关发明,而非对该发明的限定。另外还需要说明的是,为了便于描述,附图中仅示出了与发明相关的部分。The present application will be further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are only used to explain the related invention, but not to limit the invention. In addition, it should be noted that, for the convenience of description, only the parts related to the invention are shown in the drawings.
需要说明的是,在不冲突的情况下,本申请中的实施例及实施例中的特征可以相互组合。下面将参考附图并结合实施例来详细说明本申请。It should be noted that the embodiments in the present application and the features of the embodiments may be combined with each other in the case of no conflict. The present application will be described in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
如图1至图5所示,本申请提供的一种用于回收铝灰渣中氮元素的装置,包括:反应釜1和吸收塔2,反应釜1与吸收塔2之间通过用于收集氨气的管道3连通。As shown in Figures 1 to 5, a device for recovering nitrogen elements in aluminum ash slag provided by the present application includes: a reaction kettle 1 and an
进一步地,反应釜1包括反应釜壳体,反应釜壳体内水平安装有搅拌轴5且搅拌轴5与位于反应釜壳体外的电机4相连,搅拌轴5外侧安装有搅拌叶片6。Further, the reaction kettle 1 includes a reaction kettle shell, a stirring
如图4所示,搅拌轴5与反应釜壳体之间通过滚珠轴承10连接。搅拌轴5与反应釜壳体之间转动连接,通过第一通孔111可向反应釜的腔室内倒入铝灰渣并加入水形成浆料;由于反应釜壳体与搅拌轴之间转动连接,待反应釜内的浆料反应完全后,转动反应釜壳体使得第一通孔位于下方,第一通孔可充当出料口将混合物倒出。本申请中反应釜壳体上的第一通孔集入料口、入水口及出料口的功能于一体,极大的简化装置的结构。As shown in FIG. 4 , the
搅拌轴5与电机4之间齿轮传动,搅拌轴5的一端伸出反应釜壳体且该端安装有第一齿轮;搅拌轴5的一端连接一连接端并伸出反应釜壳体,且连接端安装有第一齿轮。如图4所示,第一电机4的电机轴的一端安装有第二齿轮41,第一齿轮51与第二齿轮41相互啮合,搅拌轴在电机的驱动下转动,搅拌轴的转动速度优选为5r/min~30r/min,便于将浆料搅拌均匀、高效挥发出氨气。Gear transmission between the
进一步地,反应釜壳体包括通过法兰连接的第一壳体11和第二壳体12,第一壳体11和第二壳体12之间的法兰连接面为第一平面,第一平面沿竖直方向分布,第一壳体的上方设有第一通孔111和出气孔112,出气孔112与管道3相连接。Further, the reactor shell includes a first shell 11 and a
进一步地,第一壳体11和第二壳体12均为半球形结构;第一壳体的内壁与第二壳体的内壁均设有多个凸起的挡流板7,挡流板7偏离反应釜壳体的水平轴线所经过的平面。本申请中反应釜壳体为球形结构,搅拌轴位于反应釜壳体的水平轴线上;通过设置挡流板,使得铝灰渣与水混合形成的浆料在被搅拌的过程中,部分浆料落入挡流板且在重力的作用下沿挡流板滑动,相对于仅有叶片转动的情况,在一定程度上增加流延行程和料体外部滞留时间,使浆料的反应更充分,料液混合更均匀,搅拌效率更高;同时加速气体的释放进程,便于更快速的将反应生成的氨气带出。Further, the first shell 11 and the
进一步地,第一壳体的内壁上的挡流板和第二壳体的内壁上的挡流板关于第一平面对称分布;第一壳体的内壁上的挡流板均匀分布。Further, the baffles on the inner wall of the first casing and the baffles on the inner wall of the second casing are symmetrically distributed with respect to the first plane; the baffles on the inner wall of the first casing are evenly distributed.
进一步地,在第一壳体的内壁上挡流板自远离第一平面的一侧向第一平面所在的一侧延伸,挡流板与第一平面成30°~60°。如图3所示,以某一挡流板7a为例,第一平面I与挡流板所在的平面II之间的夹角α成30°~60°。这样的设置确保搅拌轴搅拌浆料的过程中,浆料能够在挡流板上滞留一段时间。Further, on the inner wall of the first housing, the baffle plate extends from the side away from the first plane to the side where the first plane is located, and the baffle plate and the first plane are at an angle of 30°˜60°. As shown in FIG. 3 , taking a
进一步地,用于回收铝灰渣中氮元素的装置还包括支架20,反应釜壳体设于支架上;在反应釜壳体的下方且位于第一平面所在方向上,支架设有一凹槽部,第一壳体与第二壳体的法兰连接部与凹槽部相嵌合;在垂直于第一平面的方向上,法兰连接部上设有第一圆孔,凹槽部上设有第二圆孔,第一圆孔和第二圆孔之间通过插销21相连接。支架包括两支撑耳朵,两支撑耳朵上分别设有圆孔,搅拌轴与圆孔之间通过滚动轴承连接,反应釜内铝灰渣与水发生反应时,将插销21插上,第一通孔111位于第一壳体的上方;反应完后拔下插销21,翻转反应釜壳体180°,通过第一通孔111将浆料倒出。在垂直于第一平面的宽度方向上,第一通孔111和出气孔112的位置与凹槽部的位置错开,在翻转反应釜壳体180°时,第一通孔111和出气孔112与凹槽部互不影响。电机部分由相应的支座进行支撑,图中未示出。Further, the device for recovering nitrogen in the aluminum ash slag also includes a
进一步地,管道上还设有过滤装置,过滤装置包括用于过滤铝灰颗粒的第一过滤装置,过滤装置还包括用于过滤水汽的第二过滤装置。Further, a filter device is also provided on the pipeline, the filter device includes a first filter device for filtering aluminum ash particles, and the filter device further includes a second filter device for filtering water vapor.
本申请中,管道3上顺次设置第一过滤装置8、第二过滤装置9。In the present application, the
进一步地,第一过滤装置8包括圆柱状的第一滤芯81以及位于第一滤芯两侧的第一硬质过滤网82,第一滤芯包括由过滤棉缠绕组成的滤体结构,滤体结构内均匀分布有活性炭颗粒;Further, the
管道上设有第一凸出部31,两第一硬质过滤网82卡合于第一凸出部31的内壁的两端,第一滤芯81与第一凸出部31的内壁无缝接触且支撑于两第一硬质过滤网82的中间。The pipe is provided with a
进一步地,第二过滤装置9包括圆柱状结构的第二滤芯91以及位于第二滤芯两侧的第二硬质过滤网92,第二滤芯的成分至少包括以下一种:生石灰、氢氧化钠和硅胶;Further, the
管道上设有第二凸出部32,两第二硬质过滤网92卡合于第二凸出部32的内壁的两端,第二滤芯91与第二凸出部32的内壁无缝接触且支撑于两第二硬质过滤网92的中间。The pipe is provided with a second protruding
本申请所提供的用于收集铝灰渣中氮元素的装置的工作原理为:The working principle of the device for collecting nitrogen in aluminum ash slag provided by this application is:
铝灰渣从第一通孔111倒入反应釜的腔室内,并且通过第一通孔111向反应釜的腔室内加入60~90℃(例如60℃、70℃、80℃、90℃)的热水以形成浆料,其中铝灰渣与水的质量比为1:1~1:3,然后关闭入料口,开启电机4带动搅拌轴5上的搅拌叶片6转动,搅拌叶片6带动浆料运动,部分浆料落入挡流板上,在重力作用下沿挡流板滑动,增加流延行程和料体外部滞留时间,以充分搅拌浆料。铝灰渣中的氮元素通常以AlN形式存在,遇水发生以下反应:AlN+3H2O=Al(OH)3+NH3,即生成NH3后脱离浆料,经过管道到达过滤装置分别进行固体颗粒及水汽的过滤,以得到更为纯净气体,最后被吸收塔用强酸吸收成铵盐,然后旋转反应釜壳体,将反应后的浆料从第一通孔111倒出。The aluminum ash slag is poured into the chamber of the reaction kettle from the first through
以上描述仅为本申请的较佳实施例以及对所运用技术原理的说明。本领域技术人员应当理解,本申请中所涉及的发明范围,并不限于上述技术特征的特定组合而成的技术方案,同时也应涵盖在不脱离所述发明构思的情况下,由上述技术特征或其等同特征进行任意组合而形成的其它技术方案。例如上述特征与本申请中公开的(但不限于)具有类似功能的技术特征进行互相替换而形成的技术方案。The above description is only a preferred embodiment of the present application and an illustration of the applied technical principles. Those skilled in the art should understand that the scope of the invention involved in this application is not limited to the technical solution formed by the specific combination of the above-mentioned technical features, and should also cover the above-mentioned technical features without departing from the inventive concept. Other technical solutions formed by any combination of its equivalent features. For example, a technical solution is formed by replacing the above-mentioned features with the technical features disclosed in this application (but not limited to) with similar functions.
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CN108117091A (en) * | 2018-01-10 | 2018-06-05 | 南通大学 | Aluminium clinker water solution denitrogenates apparatus control method |
CN108663482A (en) * | 2018-04-27 | 2018-10-16 | 南通大学 | Ammonia concentration detection method after gas concentration detection apparatus and the hydrolysis of aluminium lime-ash |
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CN204107347U (en) * | 2014-10-21 | 2015-01-21 | 武汉钢铁(集团)公司 | The anti-NH of constant temperature 3the SCR method distributing instrument of corrosion |
CN104511229A (en) * | 2013-09-29 | 2015-04-15 | 天津众邦化工有限公司 | Tail gas absorption device used in preparation of sodium pentachlorophenate |
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CN88100289A (en) * | 1987-01-20 | 1988-12-07 | 阿托化学公司 | With vinylchlorid is the mass polymerization production method of the polymkeric substance and the multipolymer of main component |
CN104511229A (en) * | 2013-09-29 | 2015-04-15 | 天津众邦化工有限公司 | Tail gas absorption device used in preparation of sodium pentachlorophenate |
CN204107347U (en) * | 2014-10-21 | 2015-01-21 | 武汉钢铁(集团)公司 | The anti-NH of constant temperature 3the SCR method distributing instrument of corrosion |
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