CN116832664A - A dry curing desulfurizer, preparation device and preparation method - Google Patents
A dry curing desulfurizer, preparation device and preparation method Download PDFInfo
- Publication number
- CN116832664A CN116832664A CN202310640383.8A CN202310640383A CN116832664A CN 116832664 A CN116832664 A CN 116832664A CN 202310640383 A CN202310640383 A CN 202310640383A CN 116832664 A CN116832664 A CN 116832664A
- Authority
- CN
- China
- Prior art keywords
- discharging
- butt joint
- dry curing
- mixing
- frame
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F29/00—Mixers with rotating receptacles
- B01F29/60—Mixers with rotating receptacles rotating about a horizontal or inclined axis, e.g. drum mixers
- B01F29/64—Mixers with rotating receptacles rotating about a horizontal or inclined axis, e.g. drum mixers with stirring devices moving in relation to the receptacle, e.g. rotating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/30—Driving arrangements; Transmissions; Couplings; Brakes
- B01F35/32—Driving arrangements
- B01F35/32005—Type of drive
- B01F35/3204—Motor driven, i.e. by means of an electric or IC motor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71805—Feed mechanisms characterised by the means for feeding the components to the mixer using valves, gates, orifices or openings
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/75—Discharge mechanisms
- B01F35/754—Discharge mechanisms characterised by the means for discharging the components from the mixer
- B01F35/7547—Discharge mechanisms characterised by the means for discharging the components from the mixer using valves, gates, orifices or openings
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/81—Solid phase processes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
技术领域Technical field
本发明涉及脱硫脱硝添加剂加工技术领域,特别涉及一种干法固化脱硫剂及其制备方法。The invention relates to the technical field of desulfurization and denitrification additive processing, and in particular to a dry curing desulfurization agent and a preparation method thereof.
背景技术Background technique
水泥的制备过程中,需要将生料在回转窑中利用煤炭煅烧成熟料,而煤炭在燃烧过程中会产生大量的NOX和SO2烟气污染环境,为了降低NOX和SO2的排放,现有的做法是向煤炭燃烧的烟气中添加固硫剂,但是现有的固硫剂只能固定煤炭和生料中的硫元素,不能对氮元素进行固定,这就导致现有的固硫剂对煤炭的脱硝效果较差,无法降低NOX的排放。另外,现有的固硫剂脱硫效果也差强人意,无法满足现有排放标准,需要对固硫剂的组分进行进一步改进。In the cement preparation process, raw materials need to be calcined into clinker using coal in a rotary kiln. During the combustion process , coal will produce a large amount of NO The existing method is to add sulfur-fixing agents to the flue gas of coal combustion. However, the existing sulfur-fixing agents can only fix the sulfur element in coal and raw meal, but cannot fix the nitrogen element. This results in the existing fixation agent. Sulfur agents have poor denitrification effect on coal and cannot reduce NOx emissions. In addition, the desulfurization effect of the existing sulfur-fixing agents is unsatisfactory and cannot meet the existing emission standards. The components of the sulfur-fixing agents need to be further improved.
肥皂泥和电石渣均为工业废料或副产品,如何将二者应用于固硫剂中提升脱硫效果是亟待解决的问题,将肥皂泥和电石渣应用于固硫剂中不仅可以解决工业废料的处理难题,还能够大幅减少固硫剂的制作成本。Soap sludge and carbide slag are both industrial waste or by-products. How to use them in sulfur-fixing agents to improve the desulfurization effect is an urgent problem to be solved. Applying soap sludge and carbide slag to sulfur-fixing agents can not only solve the problem of industrial waste treatment It can also significantly reduce the production cost of sulfur-fixing agents.
此外,现有技术中对于脱硫剂的制备多采用混料装置进行多组份的混合,在混料结束后,需要人工操作对接排料口进行物料的转移,并在转移后再次人工操作关闭排料口,在此过程中需要保持排料口处于位置稳定的竖直向下状态,十分不便,制约了生产效率。In addition, the preparation of desulfurizers in the prior art often uses a mixing device to mix multiple components. After the mixing is completed, it is necessary to manually operate the docking discharge port to transfer the materials, and to manually close the discharge port again after the transfer. During this process, the discharge port needs to be kept in a stable vertical downward state, which is very inconvenient and restricts production efficiency.
发明内容Contents of the invention
本发明所要解决的技术问题:解决现有固硫剂在制备工艺和脱硫脱硝效果上的缺点。The technical problem to be solved by the present invention is to solve the shortcomings of the existing sulfur-fixing agent in the preparation process and desulfurization and denitrification effects.
为解决上述技术问题,本发明提供以下的技术方案:In order to solve the above technical problems, the present invention provides the following technical solutions:
一种干法固化脱硫剂的制备装置,包括工作台、混料机构、旋转动力机构、导向机构以及排料对接机构,所述混料机构借助于机架安装于工作台上并与旋转动力机构连接,所述旋转动力机构安装于机架上并用于驱动混料机构旋转,所述机架滑动连接于工作台上并能够借助于平移机构实现机架的水平移动,所述导向机构安装于排料对接机构上并用于混料机构在平移时引导混料机构上的排料机构至排料对接机构处,所述排料对接机构中的对接模组能够在排料机构平移的过程中与排料机构对接。A preparation device for dry curing desulfurization agent, including a workbench, a mixing mechanism, a rotary power mechanism, a guide mechanism and a discharge and docking mechanism. The mixing mechanism is installed on the workbench by means of a frame and is connected to the rotary power mechanism. connection, the rotary power mechanism is installed on the frame and is used to drive the mixing mechanism to rotate. The frame is slidingly connected to the workbench and can achieve horizontal movement of the frame with the help of a translation mechanism. The guide mechanism is installed on the row. On the material docking mechanism and used to guide the discharging mechanism on the mixing mechanism to the discharge docking mechanism when the mixing mechanism is translated. The docking module in the discharge docking mechanism can interact with the discharge mechanism during the translation process. Material organization docking.
优选的,所述混料机构包括混料桶、端盖、进料口以及排料机构,所述端盖安装于混料桶的两端,端盖的外端连接有驱动轴,驱动轴借助于轴承转动连接于机架上,所述进料口和排料机构均安装于混料桶的外周。Preferably, the mixing mechanism includes a mixing barrel, an end cover, a feed port and a discharging mechanism. The end covers are installed at both ends of the mixing barrel. The outer ends of the end covers are connected to a driving shaft, and the driving shaft is driven by The bearing is rotatably connected to the frame, and the feed port and the discharge mechanism are installed on the outer periphery of the mixing barrel.
优选的,所述排料机构包括排料管、电动球阀以及对接管,所述排料管固定于混料桶的外周,排料管、电动球阀以及对接管依次连接。Preferably, the discharge mechanism includes a discharge pipe, an electric ball valve and a butt pipe, the discharge pipe is fixed on the outer periphery of the mixing barrel, and the discharge pipe, the electric ball valve and the butt pipe are connected in sequence.
优选的,所述旋转动力机构包括驱动电机、主皮带轮和副皮带轮,所述驱动电机安装于机架上且其输出端连接至主皮带轮,主皮带轮借助于输送带与副皮带轮连接,副皮带轮与其中一个驱动轴连接。Preferably, the rotary power mechanism includes a drive motor, a main pulley and a auxiliary pulley. The drive motor is installed on the frame and its output end is connected to the main pulley. The main pulley is connected to the auxiliary pulley by means of a conveyor belt, and the auxiliary pulley is connected to the main pulley. One of the drive shafts is connected.
优选的,所述导向机构包括两个对称设置的导向板,导向板的一端设有与其相互垂直的延伸板,延伸板与导向板的连接处采用圆角过渡。Preferably, the guide mechanism includes two symmetrically arranged guide plates. One end of the guide plates is provided with an extension plate perpendicular to each other. The connection between the extension plate and the guide plate adopts a rounded corner transition.
优选的,所述排料对接机构包括滑台和对接模组,所述对接模组滑动连接于滑台内设置的导向面一上,对接模组的前后两侧设有滑柱,滑台的侧面设有与滑柱相配合的导向孔。Preferably, the discharge and docking mechanism includes a slide table and a docking module. The docking module is slidingly connected to a guide surface provided in the slide table. Slide columns are provided on the front and rear sides of the docking module. The slide table is There are guide holes on the side that match the sliding columns.
优选的,所述对接模组包括导向块、护板、对接部以及连接管,所述导向块借助于其上设置的导向面二滑动连接于导向面一上,所述护板固定于导向块的上端,导向块的上端还设有能够与对接管相配合的对接部,所述导向块内设有排料通道,并与对接部连通,排料通道的下端与连接管连接。Preferably, the docking module includes a guide block, a guard plate, a docking part and a connecting pipe. The guide block is slidably connected to the guide surface one by means of the guide surface two provided thereon. The guard plate is fixed to the guide block. The upper end of the guide block is also provided with a docking portion that can match the docking pipe. The guide block is provided with a discharge channel and is connected to the docking portion. The lower end of the discharge channel is connected to the connecting pipe.
优选的,所述平移机构包括伸缩油缸以及油缸座,所述伸缩油缸借助于油缸座安装于工作台上,伸缩油缸的输出端连接至机架Preferably, the translation mechanism includes a telescopic oil cylinder and a cylinder base. The telescopic oil cylinder is installed on the workbench by means of the oil cylinder base, and the output end of the telescopic oil cylinder is connected to the frame.
本发明还公开了利用所述的制备装置制备干法固化脱硫剂的方法,其特征在于,具体制备步骤如下:The invention also discloses a method for preparing dry curing desulfurizer using the preparation device, which is characterized in that the specific preparation steps are as follows:
S1.将肥皂泥与氢氧化钠和电石渣按照3:1:2的重量比混合静置2h,烘干研磨成粉得混合粉A;S1. Mix soap sludge, sodium hydroxide and carbide slag according to the weight ratio of 3:1:2 and let it stand for 2 hours, then dry and grind it into powder to obtain mixed powder A;
S2.将步骤S1中获得的混合粉A与尿素、碳酸氢钠、碳酸镁称量后投入制备装置内充分混合得混合粉B;S2. Weigh the mixed powder A obtained in step S1, urea, sodium bicarbonate, and magnesium carbonate, then put them into the preparation device and mix them thoroughly to obtain mixed powder B;
S3.通过制备装置中的排料对接机构将混合粉B转移至粉碎机内,在粉碎机内部进行研磨粉碎,达到细度的合格细粉通过气流分级机筛分出去进入旋风收集器,旋风收集器将物料收集下来通过卸料阀排出,收集到成品仓进行发运,除尘器把粉尘过滤收集,洁净空气从风机排出。S3. Transfer the mixed powder B to the pulverizer through the discharge and docking mechanism in the preparation device, and grind and pulverize it inside the pulverizer. The qualified fine powder that reaches the fineness is screened out by the air flow classifier and enters the cyclone collector. The cyclone collects it. The material is collected by the dust collector and discharged through the discharge valve, and then collected into the finished product warehouse for shipment. The dust collector filters and collects the dust, and the clean air is discharged from the fan.
本发明还公开了一种干法固化脱硫剂,采用所述的方法获得,具体由如下重量份的原料制备而成:50~80份肥皂泥、30~50份电石渣、50~70份尿素、10~20份碳酸氢钠、25~40份碳酸镁。The invention also discloses a dry solidification desulfurization agent, which is obtained by the above-mentioned method and is specifically prepared from the following raw materials by weight: 50 to 80 parts of soap sludge, 30 to 50 parts of calcium carbide slag, and 50 to 70 parts of urea. , 10 to 20 parts of sodium bicarbonate, 25 to 40 parts of magnesium carbonate.
本发明获得的有益效果:Beneficial effects obtained by the present invention:
1.本发明中通过将整个机架及混料桶设置成可平移的结构,以便于根据需要实现混料工位及排料工位的切换。1. In the present invention, the entire frame and mixing barrel are arranged into a translatable structure, so that the mixing station and the discharging station can be switched as needed.
2.本发明中设置的导向机构能够引导排料机构顺利进入到排料对接机构处并在平移的过程中实现二者的对接,从而省去了人工对接的烦恼,提高了效率。2. The guide mechanism provided in the present invention can guide the discharge mechanism to smoothly enter the discharge docking mechanism and realize docking between the two during the translation process, thereby eliminating the trouble of manual docking and improving efficiency.
3.本发明使用多种工业副产品和下脚料,相互作用,实现固硫和减少NOX排放,同时实现资源综合利用,本粉体固硫剂无毒,在生产、储存、运输及使用过程中无安全隐患,添加到煤炭中,还具有部分降低煤耗,减少二氧化碳排放、减少环境污染的优点。3. The present invention uses a variety of industrial by-products and scraps to interact with each other to achieve sulfur fixation and reduce NO There is no safety hazard, and when added to coal, it also has the advantages of partially reducing coal consumption, reducing carbon dioxide emissions, and reducing environmental pollution.
附图说明Description of the drawings
图1为本发明中制备装置的结构示意图。Figure 1 is a schematic structural diagram of the preparation device in the present invention.
图2为图1的主视图。Figure 2 is a front view of Figure 1.
图3为排料对接机构的结构示意图。Figure 3 is a schematic structural diagram of the discharge and docking mechanism.
图4为图3的俯视图。FIG. 4 is a top view of FIG. 3 .
图5为图4中沿A-A方向的剖视图。FIG. 5 is a cross-sectional view along the A-A direction in FIG. 4 .
其中,1工作台,10滑轨,2混料机构,20混料桶,21端盖,22进料口,23排料机构,230排料管,231电动球阀,232对接管,24驱动轴,3旋转动力机构,30驱动电机,31主皮带轮,32副皮带轮,33输送带,4导向机构,40导向板,41延伸板,5排料对接机构,50滑台,500导向面一,501导向孔,51对接模组,510导向块,511护板,512对接部,513连接管,514滑柱,515排料通道,516导向面二,7平移机构,70伸缩油缸,71油缸座,8机架。Among them, 1 workbench, 10 slide rails, 2 mixing mechanism, 20 mixing barrel, 21 end cover, 22 feed port, 23 discharge mechanism, 230 discharge pipe, 231 electric ball valve, 232 butt pipe, 24 drive shaft , 3 rotating power mechanism, 30 drive motor, 31 main pulley, 32 auxiliary pulley, 33 conveyor belt, 4 guide mechanism, 40 guide plate, 41 extension plate, 5 discharge docking mechanism, 50 slide table, 500 guide surface one, 501 Guide hole, 51 docking module, 510 guide block, 511 guard plate, 512 docking part, 513 connecting pipe, 514 sliding column, 515 discharge channel, 516 guide surface two, 7 translation mechanism, 70 telescopic cylinder, 71 cylinder seat, 8 racks.
具体实施方式Detailed ways
下面通过对实施例的描述,对本发明的具体实施方式作进一步详细的说明,以帮助本领域的技术人员对本发明的发明构思、技术方案有更完整、准确和深入的理解。The specific implementation modes of the present invention will be further described in detail through the description of the examples below to help those skilled in the art have a more complete, accurate and in-depth understanding of the inventive concepts and technical solutions of the present invention.
一种干法固化脱硫剂的制备装置,包括工作台1、混料机构2、旋转动力机构3、导向机构4以及排料对接机构5;A preparation device for dry curing desulfurization agent, including a workbench 1, a mixing mechanism 2, a rotating power mechanism 3, a guide mechanism 4 and a discharge and docking mechanism 5;
所述混料机构2借助于机架8安装于工作台1上并与旋转动力机构3连接,所述混料机构2包括混料桶20、端盖21、进料口22以及排料机构23,所述端盖21安装于混料桶20的两端,端盖21的外端连接有驱动轴24,驱动轴24借助于轴承转动连接于机架8上,所述进料口22和排料机构23均安装于混料桶20的外周。The mixing mechanism 2 is installed on the workbench 1 by means of the frame 8 and is connected to the rotating power mechanism 3. The mixing mechanism 2 includes a mixing barrel 20, an end cover 21, a feed port 22 and a discharge mechanism 23. , the end caps 21 are installed at both ends of the mixing barrel 20, the outer ends of the end caps 21 are connected to a drive shaft 24, the drive shaft 24 is rotationally connected to the frame 8 by means of bearings, the feed port 22 and the discharge The material mechanism 23 is installed on the outer periphery of the mixing barrel 20 .
所述排料机构23包括排料管230、电动球阀231以及对接管232,所述排料管230固定于混料桶20的外周,排料管230、电动球阀231以及对接管232依次连接。The discharge mechanism 23 includes a discharge pipe 230, an electric ball valve 231 and a connecting pipe 232. The discharge pipe 230 is fixed on the outer periphery of the mixing barrel 20. The discharge pipe 230, the electric ball valve 231 and the connecting pipe 232 are connected in sequence.
所述旋转动力机构3安装于机架8上并用于驱动混料机构2旋转,所述旋转动力机构3包括驱动电机30、主皮带轮31和副皮带轮32,所述驱动电机30安装于机架8上且其输出端连接至主皮带轮31,主皮带轮31借助于输送带33与副皮带轮32连接,副皮带轮32与其中一个驱动轴24连接。The rotary power mechanism 3 is installed on the frame 8 and is used to drive the mixing mechanism 2 to rotate. The rotary power mechanism 3 includes a drive motor 30, a main pulley 31 and an auxiliary pulley 32. The drive motor 30 is installed on the frame 8. and its output end is connected to the main pulley 31. The main pulley 31 is connected to the auxiliary pulley 32 by means of the conveyor belt 33. The auxiliary pulley 32 is connected to one of the drive shafts 24.
所述机架8滑动连接于工作台1上(如借助于滑轨10)并能够借助于平移机构7实现机架8的水平移动,所述平移机构7包括伸缩油缸70以及油缸座71,所述伸缩油缸70借助于油缸座71安装于工作台1上,伸缩油缸70的输出端连接至机架8。The frame 8 is slidingly connected to the workbench 1 (such as by means of the slide rail 10) and can achieve horizontal movement of the frame 8 with the help of a translation mechanism 7. The translation mechanism 7 includes a telescopic cylinder 70 and a cylinder base 71, so The telescopic oil cylinder 70 is installed on the workbench 1 by means of the oil cylinder seat 71 , and the output end of the telescopic oil cylinder 70 is connected to the frame 8 .
所述导向机构4安装于排料对接机构5上并用于混料机构2在平移时引导混料机构2上的排料机构23至排料对接机构5处,所述排料对接机构5中的对接模组51能够在排料机构23平移的过程中与排料机构23对接,所述导向机构4包括两个对称设置的导向板40,导向板40安装于滑台50上,导向板40的一端设有与其相互垂直的延伸板41,延伸板41与导向板40的连接处采用圆角过渡,所述排料对接机构5包括滑台50和对接模组51,所述对接模组51滑动连接于滑台50内设置的导向面一500上,对接模组51的前后两侧设有滑柱514,滑台50的侧面设有与滑柱514相配合的导向孔501;The guide mechanism 4 is installed on the discharge docking mechanism 5 and is used to guide the discharge mechanism 23 on the mixing mechanism 2 to the discharge docking mechanism 5 when the mixing mechanism 2 is translated. The docking module 51 can dock with the discharging mechanism 23 during the translation process of the discharging mechanism 23. The guide mechanism 4 includes two symmetrically arranged guide plates 40. The guide plates 40 are installed on the sliding table 50. The guide plates 40 are One end is provided with an extension plate 41 that is perpendicular to each other. The connection between the extension plate 41 and the guide plate 40 adopts a rounded corner transition. The discharge docking mechanism 5 includes a sliding table 50 and a docking module 51. The docking module 51 slides Connected to the guide surface 500 provided in the slide table 50, the docking module 51 is provided with sliding columns 514 on the front and rear sides, and the side of the slide table 50 is provided with guide holes 501 that match the sliding columns 514;
所述对接模组51包括导向块510、护板511、对接部512以及连接管513,所述导向块510借助于其上设置的导向面二516滑动连接于导向面一500上,所述护板511固定于导向块510的上端,导向块510的上端还设有能够与对接管232相配合的对接部512,所述导向块510内设有排料通道515,并与对接部512连通,排料通道515的下端与连接管513连接。The docking module 51 includes a guide block 510, a guard plate 511, a docking portion 512 and a connecting pipe 513. The guide block 510 is slidably connected to the guide surface 500 by means of the guide surface 516 provided thereon. The plate 511 is fixed on the upper end of the guide block 510. The upper end of the guide block 510 is also provided with a docking portion 512 that can cooperate with the docking pipe 232. The guide block 510 is provided with a discharge channel 515 and is connected with the docking portion 512. The lower end of the discharge channel 515 is connected to the connecting pipe 513 .
实施例1:Example 1:
本实施例公开了一种干法固化脱硫剂,采用所述的方法获得,具体由如下重量份的原料制备而成:45重量份肥皂泥、30重量份氢氧化钠、30重量份电石渣、50重量份尿素、10重量份碳酸氢钠、25重量份碳酸镁。This embodiment discloses a dry curing desulfurization agent, which is obtained by the method described above and is specifically prepared from the following raw materials by weight: 45 parts by weight of soap sludge, 30 parts by weight of sodium hydroxide, 30 parts by weight of calcium carbide slag, 50 parts by weight of urea, 10 parts by weight of sodium bicarbonate, and 25 parts by weight of magnesium carbonate.
按如下方法制备干法固化脱硫剂:Prepare dry curing desulfurizer as follows:
S1.将肥皂泥与氢氧化钠和电石渣按照3:1:2的重量比混合静置2h,烘干研磨成粉得混合粉A;S1. Mix soap sludge, sodium hydroxide and carbide slag according to the weight ratio of 3:1:2 and let it stand for 2 hours, then dry and grind it into powder to obtain mixed powder A;
S2.将步骤S1中获得的混合粉A与尿素、碳酸氢钠、碳酸镁称量后投入制备装置内充分混合得混合粉B;S2. Weigh the mixed powder A obtained in step S1, urea, sodium bicarbonate, and magnesium carbonate, then put them into the preparation device and mix them thoroughly to obtain mixed powder B;
S3.通过制备装置中的排料对接机构将混合粉B转移至粉碎机内,在粉碎机内部进行研磨粉碎,达到细度的合格细粉通过气流分级机筛分出去进入旋风收集器,旋风收集器将物料收集下来通过卸料阀排出,收集到成品仓进行发运,除尘器把粉尘过滤收集,洁净空气从风机排出。S3. Transfer the mixed powder B to the pulverizer through the discharge and docking mechanism in the preparation device, and grind and pulverize it inside the pulverizer. The qualified fine powder that reaches the fineness is screened out by the air flow classifier and enters the cyclone collector. The cyclone collects it. The material is collected by the dust collector and discharged through the discharge valve, and then collected into the finished product warehouse for shipment. The dust collector filters and collects the dust, and the clean air is discharged from the fan.
实施例2:其余均与实施例1相同,不同之处在于:Embodiment 2: The rest are the same as Embodiment 1, except that:
原料配比为:60重量份肥皂泥、15重量份氢氧化钠、40重量份电石渣、60重量份尿素、15重量份碳酸氢钠、30重量份碳酸镁。The raw material ratio is: 60 parts by weight of soap sludge, 15 parts by weight of sodium hydroxide, 40 parts by weight of carbide slag, 60 parts by weight of urea, 15 parts by weight of sodium bicarbonate, and 30 parts by weight of magnesium carbonate.
实施例3:其余均与实施例1相同,不同之处在于:Embodiment 3: The rest are the same as Embodiment 1, except that:
原料配比为75重量份肥皂泥、20重量份氢氧化钠、50重量份电石渣、70重量份尿素、20重量份碳酸氢钠、40重量份碳酸镁。The raw material ratio is 75 parts by weight of soap sludge, 20 parts by weight of sodium hydroxide, 50 parts by weight of carbide slag, 70 parts by weight of urea, 20 parts by weight of sodium bicarbonate, and 40 parts by weight of magnesium carbonate.
将实施例中制备的干法固化脱硫剂或促燃固硫剂粉末按煤炭量的3.0wt%掺混进入煤炭燃烧后烟气中,燃烧后测定排出废气中的NOx和SO2降低比例,计算公式为:The dry curing desulfurization agent or combustion-promoting sulfur-fixing agent powder prepared in the example is blended into the flue gas after coal combustion at 3.0wt% of the coal amount. After combustion, the NOx and SO2 reduction ratio in the exhaust gas are measured and calculated. The formula is:
脱硫/脱硝比例=(C0-Cx)/C0*100%,其中,CX为添加了干法固化脱硫剂或促燃固硫剂的煤炭燃烧废气中NOx或SO2的含量;C0为未添加干法固化脱硫剂或促燃固硫剂的煤炭燃烧废气中NOx或SO2的含量。Desulfurization/denitrification ratio = (C 0 -C x )/C 0 *100%, where C 0 is the NOx or SO 2 content in the coal combustion exhaust gas without the addition of dry-curing desulfurizer or combustion-promoting sulfur-fixing agent.
市售脱硫剂由由微晶高岭土、方镁石、电石渣、赤泥、炉渣和蛭石制成。本发明用于煤炭燃烧废气的脱硫脱硝时,用量较少且效果较好,当用等量的市售脱硫剂掺入煤炭时,由于用量较少,不能达到最佳用量,使得脱硫效果明显降低。Commercially available desulfurizers are made of microcrystalline kaolin, periclase, carbide slag, red mud, slag and vermiculite. When the present invention is used for desulfurization and denitrification of coal combustion exhaust gas, the dosage is small and the effect is better. When the same amount of commercially available desulfurizer is used to mix coal, the optimal dosage cannot be achieved due to the small dosage, resulting in a significant reduction in the desulfurization effect. .
上述制备装置的工作过程如下:The working process of the above preparation device is as follows:
待步骤S1中获得的混合粉A与尿素、碳酸氢钠、碳酸镁称量后投入制备装置内混合完成后,关闭驱动电机30,直至混料桶20平稳下来,接着启动伸缩油缸70,驱动机架8向油缸座71方向水平移动,在引导机构的作用下,对接管232沿着导向板40移动至护板511处,接着驱动导向块510同步水平移动,在导向面一500的作用下,导向块510水平移动的同时会不断上升,直至导向块510上端的对接部512插入到对接管232内,即可完成排料机构23与对接模组51的连接,开启电动球阀231,开始排料。After the mixed powder A obtained in step S1, urea, sodium bicarbonate, and magnesium carbonate are weighed and put into the preparation device, the driving motor 30 is turned off until the mixing barrel 20 stabilizes, and then the telescopic cylinder 70 is started to drive the machine. The frame 8 moves horizontally toward the direction of the cylinder base 71. Under the action of the guide mechanism, the docking pipe 232 moves along the guide plate 40 to the guard plate 511, and then the guide block 510 is driven to move horizontally synchronously. Under the action of the guide surface 500, The guide block 510 will continue to rise while moving horizontally until the docking portion 512 at the upper end of the guide block 510 is inserted into the docking pipe 232. The connection between the discharging mechanism 23 and the docking module 51 is completed. The electric ball valve 231 is opened to start discharging. .
排料完成后,关闭电动球阀231,伸缩油缸70驱动机架8复位,对接模组51也随之复位。After the discharge is completed, the electric ball valve 231 is closed, the telescopic cylinder 70 drives the frame 8 to reset, and the docking module 51 is also reset.
以上实施例仅为说明本发明的技术思想,不能以此限定本发明的保护范围,凡是按照本发明提出的技术思想,在技术方案基础上所做的任何改动,均落入本发明保护范围之内;本发明未涉及的技术均可通过现有技术加以实现。The above embodiments are only for illustrating the technical ideas of the present invention and cannot limit the protection scope of the present invention. Any changes made based on the technical solutions based on the technical ideas proposed by the present invention will fall within the protection scope of the present invention. Within; technologies not involved in the present invention can be implemented through existing technologies.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310640383.8A CN116832664B (en) | 2023-06-01 | 2023-06-01 | A dry solidification desulfurizer, preparation device and preparation method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310640383.8A CN116832664B (en) | 2023-06-01 | 2023-06-01 | A dry solidification desulfurizer, preparation device and preparation method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN116832664A true CN116832664A (en) | 2023-10-03 |
| CN116832664B CN116832664B (en) | 2025-09-30 |
Family
ID=88158483
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202310640383.8A Active CN116832664B (en) | 2023-06-01 | 2023-06-01 | A dry solidification desulfurizer, preparation device and preparation method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN116832664B (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4792234A (en) * | 1986-01-06 | 1988-12-20 | Port-A-Pour, Inc. | Portable concrete batch plant |
| CN208406821U (en) * | 2018-06-29 | 2019-01-22 | 北京慧农生物科技有限公司 | A kind of rotary drum mixer |
| CN212417738U (en) * | 2020-05-09 | 2021-01-29 | 永康市彩发颜料有限公司 | Blendor convenient to remove |
| JP6847345B1 (en) * | 2019-11-27 | 2021-03-24 | 青島軍平減震科技有限公司 | Rice storage can with the function of dividing rice into fixed quantities |
| CN113739574A (en) * | 2021-09-07 | 2021-12-03 | 山东恒瑞磁电科技有限公司 | Slurry sintering device for producing soft magnetic ferrite particles |
| CN217048718U (en) * | 2022-02-25 | 2022-07-26 | 辽宁华唯环球生物科技有限公司 | Quick transfer device is used in feed processing |
| CN114917734A (en) * | 2022-05-23 | 2022-08-19 | 安徽海萃工业制剂有限公司 | Dry-process curing desulfurizer and preparation method thereof |
-
2023
- 2023-06-01 CN CN202310640383.8A patent/CN116832664B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4792234A (en) * | 1986-01-06 | 1988-12-20 | Port-A-Pour, Inc. | Portable concrete batch plant |
| CN208406821U (en) * | 2018-06-29 | 2019-01-22 | 北京慧农生物科技有限公司 | A kind of rotary drum mixer |
| JP6847345B1 (en) * | 2019-11-27 | 2021-03-24 | 青島軍平減震科技有限公司 | Rice storage can with the function of dividing rice into fixed quantities |
| CN212417738U (en) * | 2020-05-09 | 2021-01-29 | 永康市彩发颜料有限公司 | Blendor convenient to remove |
| CN113739574A (en) * | 2021-09-07 | 2021-12-03 | 山东恒瑞磁电科技有限公司 | Slurry sintering device for producing soft magnetic ferrite particles |
| CN217048718U (en) * | 2022-02-25 | 2022-07-26 | 辽宁华唯环球生物科技有限公司 | Quick transfer device is used in feed processing |
| CN114917734A (en) * | 2022-05-23 | 2022-08-19 | 安徽海萃工业制剂有限公司 | Dry-process curing desulfurizer and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN116832664B (en) | 2025-09-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110274463A (en) | A kind of pure sintering system and method based on fuel formulations and roasting control | |
| CN113244832A (en) | Chemical industry filler smashes agitating unit | |
| CN116832664A (en) | A dry curing desulfurizer, preparation device and preparation method | |
| CN111362603A (en) | Cement clinker calcining and cooling process | |
| CN114917734A (en) | Dry-process curing desulfurizer and preparation method thereof | |
| CN211302725U (en) | High-efficient magnesite board double-shaft mixer | |
| CN213918983U (en) | Fly ash slag concrete filter equipment | |
| CN216181646U (en) | Admixture mixing arrangement that can react fast for concrete processing | |
| CN213171487U (en) | Device for producing aluminum oxide by using high-alumina fly ash | |
| CN215848924U (en) | Aerated concrete raw material mixing device with dust fall function | |
| CN215390683U (en) | Deslagging and screening device for production of aluminum oxide powder | |
| CN116423668A (en) | A dust-free automatic feeding system for a mixing station | |
| CN112872008B (en) | A kind of equipment and method for co-processing and repairing cement kiln in industrial site polluted by organochlorine pesticides | |
| CN213238386U (en) | Energy-saving rotary kiln capable of improving oxygen supply capacity | |
| CN209501595U (en) | A kind of more chutes intersection mixing system of active carbon | |
| CN208553636U (en) | Production waste gas purification apparatus is electroplated | |
| CN211590713U (en) | Dustless mixing arrangement of high strength concrete | |
| CN211189756U (en) | Novel high-efficient low temperature denitration desulfurization device of boiler | |
| CN215901842U (en) | Gypsum product reutilization recovery mill | |
| CN215909060U (en) | Cement kiln is dealt with domestic waste dore furnace in coordination | |
| CN210584465U (en) | Lime kiln flue gas desulfurization device | |
| CN220026837U (en) | Automatic refractory material batching equipment with dust removing device | |
| CN116283010B (en) | Carbonization process of solid waste recycled concrete aggregate for concrete | |
| CN218834377U (en) | A kind of forage mixing device | |
| CN221520879U (en) | Feeding conveyer belt for cement stirring |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant |