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CN201031196Y - Powder conveying and blowing device for float glass kiln - Google Patents

Powder conveying and blowing device for float glass kiln Download PDF

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Publication number
CN201031196Y
CN201031196Y CNU2007200847691U CN200720084769U CN201031196Y CN 201031196 Y CN201031196 Y CN 201031196Y CN U2007200847691 U CNU2007200847691 U CN U2007200847691U CN 200720084769 U CN200720084769 U CN 200720084769U CN 201031196 Y CN201031196 Y CN 201031196Y
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powder
pipeline
conveying
fluidized
pipe
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胡海奇
翟旭
翟兴友
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WUHAN HUAERSHUN METALLURGICAL ENGINEERING & TECHNOLOGY Co Ltd
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WUHAN HUAERSHUN METALLURGICAL ENGINEERING & TECHNOLOGY Co Ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/50Glass production, e.g. reusing waste heat during processing or shaping
    • Y02P40/57Improving the yield, e-g- reduction of reject rates

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Abstract

The utility model relates to a powder conveying blowing device for a float-glass kiln, belonging to the application in the float-glass kiln, and is characterized in that a dust feed pipeline (1) is connected with a pollen cabin (3), a fluidizer (23) is installed on the pollen cabin (3), the pollen cabin (3) is connected with a powder eccentricity screen (6) through a first blanking pipe (5), the powder eccentricity screen (6) is connected with a powder blowing tank (9) through a second blanking pipe (7), the bottom of the powder blowing tank (9) is connected with a dusting pipeline (11) through a fluidization conveyer (10), the other end of the dusting pipeline (11) is connected with a powder distributor (16), the other end of the powder distributor (16) is connected with a powder blowing pipe (17), and an outlet of the powder blowing pipe (17) is connected with a powder blow gun (18). The powder conveying system of the device is stable in blowing, the powder is evenly mixed with air and is fully burnt, the power of each blow gun is evenly distributed, and the fire-invasion length of the powder in the float-glass kiln can be adjusted.

Description

用于浮法玻璃窑的粉料输送喷吹装置 Powder conveying and blowing device for float glass kiln

技术领域technical field

本实用新型涉及平板玻璃制造领域,特别是涉及在浮法玻璃窑中的应用。The utility model relates to the field of flat glass manufacturing, in particular to the application in a float glass kiln.

背景技术Background technique

目前国内浮法玻璃窑主要是喷吹重油加热窑炉,为节能降耗,国内用户一直在寻求煤粉、石油焦粉来代替重油。喷吹粉料的设备主要采用贮粉仓、粉料喷吹罐,粉料喷吹罐下部设一螺旋给料机,用鼓风机通过喷吹管道向浮法玻璃窑内喷吹粉料,一根喷吹总管分成几根喷吹支管来分配粉料。这种工艺向浮法玻璃窑内喷吹粉料时,喷吹过程不连续、不稳定,易产生脉冲,粉料输送量大小不易控制,每支枪喷粉量分配不均匀,粉料与助燃空气不能完全混合,粉料燃烧不完全及玻璃熔窑内温度无法控制造成成品玻璃质量下降。At present, domestic float glass kilns are mainly heated by injecting heavy oil. In order to save energy and reduce consumption, domestic users have been looking for coal powder and petroleum coke powder to replace heavy oil. The equipment for blowing powder mainly adopts a powder storage bin and a powder blowing tank. A screw feeder is installed at the bottom of the powder blowing tank, and a blower is used to blow the powder into the float glass kiln through the blowing pipe. The injection main pipe is divided into several injection branch pipes to distribute the powder. When this process injects powder into the float glass kiln, the injection process is discontinuous and unstable, and it is easy to generate pulses. The air cannot be completely mixed, the powder is incompletely burned and the temperature in the glass melting furnace cannot be controlled, resulting in a decline in the quality of the finished glass.

发明内容Contents of the invention

本实用新型所要解决的技术问题是:提供一种用于浮法玻璃窑的粉料输送喷吹装置,该装置的粉料输送系统喷吹稳定、粉料与空气混合均匀、粉料燃烧充分、各喷枪粉料分配均匀且浮法玻璃窑内粉料火陷长度可调。The technical problem to be solved by the utility model is: to provide a powder conveying and blowing device for a float glass kiln, the powder conveying system of the device is stable in blowing, the powder and air are mixed evenly, the powder is fully burned, The powder distribution of each spray gun is uniform and the length of the powder fire trap in the float glass kiln is adjustable.

本实用新型的技术方案是:该装置包括输粉管道1、贮粉仓3、第一下料管5、第二下料管7、粉料喷吹罐9、喷粉管道11、喷吹支管17和粉料喷枪18,其特征在于:输粉管道1接至贮粉仓3,贮粉仓3上安有流化装置23,贮粉仓3的通过第一下料管5接至粉料偏心筛6,粉料偏心筛6通过第二下料管7接至粉料喷吹罐9,粉料喷吹罐9通过流化输送器10接至喷粉管道11,喷粉管道11的另一端接至粉料分配器16,粉料分配器16的另一端接有粉料喷吹管17,粉料喷吹管17的出口接有粉料喷枪18。The technical scheme of the utility model is: the device includes a powder delivery pipeline 1, a powder storage bin 3, a first feeding pipe 5, a second feeding pipe 7, a powder injection tank 9, a powder injection pipeline 11, and an injection branch pipe 17 and a powder spray gun 18, characterized in that: the powder delivery pipeline 1 is connected to the powder storage bin 3, and a fluidization device 23 is installed on the powder storage bin 3, and the powder storage bin 3 is connected to the powder material through the first feeding pipe 5 The eccentric sieve 6 and the powder eccentric sieve 6 are connected to the powder injection tank 9 through the second feeding pipe 7, and the powder injection tank 9 is connected to the powder injection pipeline 11 through the fluidized conveyor 10, and the other part of the powder injection pipeline 11 One end is connected to the powder material distributor 16, and the other end of the powder material distributor 16 is connected with a powder material injection pipe 17, and the outlet of the powder material injection pipe 17 is connected with a powder material spray gun 18.

该装置中,所述粉料分配器16和喷粉管道11之间接有混合器28和匀速器15。In this device, a mixer 28 and a constant velocity device 15 are connected between the powder distributor 16 and the powder injection pipeline 11 .

该装置中,所述各喷吹支管17的几何长度相等,喷吹支管17上接有火陷长度调节管道26。In this device, the geometric lengths of the injection branch pipes 17 are equal, and the injection branch pipes 17 are connected with a fire sink length adjustment pipe 26 .

与传统的浮法玻璃窑喷吹粉料的系统比较,本装置的主要优点:Compared with the traditional float glass kiln powder injection system, the main advantages of this device are:

(1)粉料采用悬浮流态化输送,粉料输送系统喷吹连续、稳定、无脉动,粉料在流化输送器内与输送介质(压缩空气或氮气)充分混合,根据喷粉量大小调节流化气体量,保证粉料与空气混合比例可调,粉料在浮法玻璃窑内燃烧性能好,粉料燃烧充分。(1) The powder is conveyed by suspension fluidization. The powder conveying system sprays continuously, stably and without pulsation. The powder is fully mixed with the conveying medium (compressed air or nitrogen) in the fluidized conveyer. Adjust the amount of fluidizing gas to ensure that the mixing ratio of powder and air can be adjusted, the powder has good combustion performance in the float glass kiln, and the powder burns fully.

(2)粉料在喷吹支管中采用加压输送,调节压缩空气流量可调节粉料在浮法玻璃窑内的燃烧火焰长度。(2) The powder is transported under pressure in the injection branch pipe, and the length of the combustion flame of the powder in the float glass kiln can be adjusted by adjusting the compressed air flow.

(3)贮粉仓锥部设流化设施,粉料下料顺畅,不起拱,不堵塞。(3) The cone of the powder storage bin is equipped with fluidization facilities, so that the powder material can be discharged smoothly without arching or clogging.

(4)贮粉仓下部设粉料偏心筛,筛除粉料中杂物,防止堵塞喷粉管道。(4) The lower part of the powder storage bin is equipped with an eccentric powder sieve to screen out impurities in the powder and prevent the powder spraying pipeline from being blocked.

(5)粉料喷吹系统采用匀速器、粉料分配器及保证各喷吹支管几何距离相等的措施,使各喷枪粉料分配喷吹均匀。(5) The powder injection system adopts a uniform speed device, a powder distributor and measures to ensure that the geometric distance of each injection branch pipe is equal, so that the powder distribution and injection of each spray gun are uniform.

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.

图中标号说明:1.输粉管道,2.仓顶过滤除尘器,3.贮粉仓,4.贮粉仓流化管道,5.第一下料管,6.粉料偏心筛,7.第二下料管,8.橡胶补偿器,9.粉料喷吹罐,10.流化输送器,11.喷粉管道,12.充压管道,13.流化管道,14.放散管道,15.匀速器,16.粉料分配器,17.喷吹支管,18.粉料喷枪,19.放散过滤器,20.流化嘴,23.流化装置,24.称重传感器,25.吹扫管道,26.火陷长度调节管道,27.安全阀过滤器,28混合器,32浮法玻璃窑。Explanation of symbols in the figure: 1. Powder conveying pipeline, 2. Dust collector on top of warehouse, 3. Powder storage bin, 4. Fluidization pipeline of powder storage bin, 5. First feeding pipe, 6. Powder eccentric screen, 7 .Second feeding pipe, 8. Rubber compensator, 9. Powder injection tank, 10. Fluidizing conveyor, 11. Powder spraying pipeline, 12. Pressurizing pipeline, 13. Fluidizing pipeline, 14. Discharging pipeline , 15. Uniform speed device, 16. Powder distributor, 17. Injection branch pipe, 18. Powder spray gun, 19. Diffuse filter, 20. Fluidizing nozzle, 23. Fluidizing device, 24. Load cell, 25 .Purge pipeline, 26. Fire sink length adjustment pipeline, 27. Safety valve filter, 28 Mixer, 32 Float glass kiln.

图2为上出料流化输送结构示意图。Figure 2 is a schematic diagram of the upper discharge fluidized conveying structure.

图3为下出料流化输送结构示意图。Fig. 3 is a schematic diagram of the fluidized conveying structure of the bottom discharge.

图4为混合器28结构示意图。FIG. 4 is a schematic structural diagram of the mixer 28 .

具体实施方式Detailed ways

用于浮法玻璃窑的粉料输送喷吹装置的结构特征:Structural features of powder conveying and blowing device for float glass kiln:

如图1所示,该装置包括输粉管道1、贮粉仓3、第一下料管5、第二下料管7、粉料喷吹罐9、喷粉管道11、喷吹支管17和粉料喷枪18,其特征在于:输粉管道1接至贮粉仓3,贮粉仓3上安有流化装置23,贮粉仓3的通过第一下料管5接至粉料偏心筛6,粉料偏心筛6通过第二下料管7接至粉料喷吹罐9,粉料喷吹罐9通过流化输送器10接至喷粉管道11,喷粉管道11的另一端接至粉料分配器16,粉料分配器16的另一端接有粉料喷吹管17,粉料喷吹管17的出口接有粉料喷枪18。As shown in Figure 1, the device includes a powder delivery pipeline 1, a powder storage bin 3, a first feeding pipe 5, a second feeding pipe 7, a powder injection tank 9, a powder injection pipeline 11, an injection branch pipe 17 and The powder spray gun 18 is characterized in that: the powder delivery pipeline 1 is connected to the powder storage bin 3, a fluidization device 23 is installed on the powder storage bin 3, and the powder storage bin 3 is connected to the powder eccentric sieve through the first feeding pipe 5 6. The powder eccentric sieve 6 is connected to the powder injection tank 9 through the second feeding pipe 7, the powder injection tank 9 is connected to the powder injection pipeline 11 through the fluidized conveyor 10, and the other end of the powder injection pipeline 11 is connected to To the powder material distributor 16, the other end of the powder material distributor 16 is connected with a powder material injection pipe 17, and the outlet of the powder material injection pipe 17 is connected with a powder material spray gun 18.

该装置中各设备的说明:Description of each device in the installation:

贮粉仓3,采用钢结构制作,内壁光滑,上部设安全防爆阀接口和检修入孔。The powder storage bin 3 is made of a steel structure with a smooth inner wall, and the upper part is provided with a safety explosion-proof valve interface and an inspection hole.

流化装置23安装在贮粉仓3的下锥部,流化装置23的作用是使粉料呈流化状态,有利于粉料从贮粉仓3落到粉料喷吹罐9中。流化管4的两个端口分别接至流化装置23和贮粉仓3的底部。流化管4的主要作用是消除贮粉仓棚煤。The fluidization device 23 is installed on the lower cone of the powder storage bin 3. The function of the fluidization device 23 is to make the powder in a fluidized state, which is beneficial for the powder to fall from the powder storage bin 3 into the powder injection tank 9. The two ports of the fluidizing pipe 4 are respectively connected to the bottom of the fluidizing device 23 and the powder storage bin 3 . The main effect of fluidization pipe 4 is to eliminate coal in the powder storage bin shed.

贮粉仓3的顶部可设置除尘过滤器2,除尘过滤器2包括壳体、脉冲喷吹阀、除尘滤布、龙骨及配管。除尘过滤器2能够有效地清除粉料的尘埃。The top of powder storage bin 3 can be provided with dust removal filter 2, and dust removal filter 2 comprises housing, pulse injection valve, dust removal filter cloth, keel and piping. The dust filter 2 can effectively remove the dust of the powder.

粉料偏心筛6,包括壳体、筛网、偏心轴、传动装置及手孔。主要作用是清除粉料中的木屑等杂物,防止喷粉管道堵塞。The powder eccentric screen 6 includes a housing, a screen, an eccentric shaft, a transmission device and a hand hole. The main function is to remove sawdust and other sundries in the powder to prevent the powder spraying pipeline from being blocked.

第二下料管7和粉料喷吹罐9之间可接橡胶补偿器8,橡胶补偿器8能消除管道盲板力,以保证称量准确。A rubber compensator 8 can be connected between the second feeding pipe 7 and the powder injection tank 9, and the rubber compensator 8 can eliminate the blind plate force of the pipeline to ensure accurate weighing.

粉料喷吹罐9属压力容器,罐体上部安有充压管道12、放散过滤器19、安全阀过滤器27,粉料喷吹罐9的下锥部安有流化嘴20,流化嘴20与流化管道13相连。流化气体通过流化管道13输送进流化嘴20,使粉料喷吹罐9内的粉料处于悬浮状态,有利于粉料的输送。放散过滤器19上部通过放散管道14和贮粉仓3相连。安全阀过滤器27、放散过滤器19的作用是减少排放气体中粉料的含量,有利于环境保护。粉料喷吹罐9的罐体上边缘还安有称重传感器24。The powder injection tank 9 is a pressure vessel, and the upper part of the tank body is equipped with a pressurization pipeline 12, a release filter 19, a safety valve filter 27, and a fluidization nozzle 20 is installed on the lower cone of the powder injection tank 9 to fluidize The nozzle 20 is connected to the fluidizing conduit 13 . The fluidization gas is transported into the fluidization nozzle 20 through the fluidization pipeline 13, so that the powder in the powder injection tank 9 is in a suspended state, which is beneficial to the transportation of the powder. The upper part of the release filter 19 is connected to the powder storage bin 3 through the release pipeline 14 . The effects of the safety valve filter 27 and the release filter 19 are to reduce the powder content in the discharge gas, which is beneficial to environmental protection. The tank body upper edge of powder injection tank 9 is also equipped with weighing sensor 24.

流化输送器10,包括粉料流化床、气体分配装置及配管。流化输送器的主要作用是使粉料形成悬浮状态,有助于顺利喷吹粉料,另外,流化输送器10根据结构形式不同,又分为上出料和下出料两种流化输送的结构:上出料流化输送的结构如图2所示,流化输送器罐体21的上部接口29与粉料喷吹罐9底部相连,流化输送器罐体21的中部或上部安有粉料出口30,粉料出口30与喷粉管道11相连,流化输送器罐体21的下部安有压缩空气入口31,压缩空气入口31与流化输送管13相连;下出料输送的结构如图3所示,流化输送器罐体21的上部接口29与粉料喷吹罐9底部相连,流化输送器罐体22的底部安有粉料出口30,粉料出口30与喷粉管道11相连,流化输送器罐体22的中部安有压缩空气入口31,压缩空气入口31与流化输送管13相连。The fluidized conveyor 10 includes a powder fluidized bed, a gas distribution device and piping. The main function of the fluidized conveyor is to make the powder form a suspended state, which helps to spray the powder smoothly. In addition, the fluidized conveyor 10 is divided into two kinds of fluidized fluidized conveyors: upper discharge and lower discharge according to different structural forms. The structure of conveying: the structure of upper discharge fluidized conveying is shown in Figure 2. The upper interface 29 of the fluidized conveyor tank 21 is connected to the bottom of the powder injection tank 9, and the middle or upper part of the fluidized conveyor tank 21 A powder outlet 30 is installed, and the powder outlet 30 is connected with the powder spraying pipeline 11. The lower part of the fluidized conveyor tank 21 is equipped with a compressed air inlet 31, and the compressed air inlet 31 is connected with the fluidized conveying pipe 13; As shown in Figure 3, the upper interface 29 of the fluidized conveyor tank 21 is connected to the bottom of the powder injection tank 9, and the bottom of the fluidized conveyor tank 22 is equipped with a powder outlet 30, and the powder outlet 30 is connected to the bottom of the fluidized conveyor tank 22. The powder spraying pipeline 11 is connected to each other, and a compressed air inlet 31 is installed in the middle of the tank body 22 of the fluidized conveyor, and the compressed air inlet 31 is connected to the fluidized conveying pipe 13 .

上出料流化输送的结构具有输粉顺畅,输送浓度高等优点,但设备高度相对较高,对布置空间有一定的要求;下出料流化输送的结构所采用的设备较简单,占用空间小,易于布置,但输粉稳定性稍差,可采用辅助手段解决。粉料在流化输送器10内与输送介质(压缩空气或氮气)充分混合,根据喷粉量大小调节流化气体量,保证粉料与空气混合比例可调,粉料在浮法玻璃窑内燃烧性能好,粉料燃烧充分。The upper discharge fluidized conveying structure has the advantages of smooth powder delivery and high conveying concentration, but the height of the equipment is relatively high, and there are certain requirements for the layout space; the lower discharging fluidized conveying structure adopts relatively simple equipment and takes up a lot of space. Small and easy to arrange, but the stability of powder delivery is slightly poor, which can be solved by auxiliary means. The powder is fully mixed with the conveying medium (compressed air or nitrogen) in the fluidized conveyor 10, and the amount of fluidized gas is adjusted according to the amount of powder sprayed to ensure that the mixing ratio of the powder and air can be adjusted. The powder is in the float glass kiln The combustion performance is good, and the powder is fully burned.

吹扫管道25接在喷粉管道11上,吹扫管道25的主要作用是防止输粉管道堵塞或消除管道堵塞。采用的气源是压缩空气或氮气。The purge pipeline 25 is connected on the powder injection pipeline 11, and the main function of the purge pipeline 25 is to prevent the powder delivery pipeline from clogging or to eliminate pipeline clogging. The gas source used is compressed air or nitrogen.

粉料分配器16,采用耐磨材质制作,内部设有粉料均匀分配锥、上部安装陶瓷耐磨管,保证各喷吹支管的分配精度,分配误差≤±5%。The powder material distributor 16 is made of wear-resistant material. The inside is equipped with a cone for evenly distributing powder material, and ceramic wear-resistant pipes are installed on the upper part to ensure the distribution accuracy of each injection branch pipe, and the distribution error is ≤±5%.

喷粉管道11和粉料分配器16之间可接混合器28与匀速器15,混合器28能够促进粉料的充分混合,匀速器15能改善粉料流动状态,有利于均匀喷吹,消除脉动。混合器28的结构如图4所示。混合器28设有进料口33、出料口34和进气口35,混合器28内部设有流化气室,起到二次混合作用,并可控制喷粉流量。The mixer 28 and the uniform speed device 15 can be connected between the powder injection pipeline 11 and the powder material distributor 16. The mixer 28 can promote the sufficient mixing of the powder material, and the uniform speed device 15 can improve the flow state of the powder material, which is conducive to uniform spraying and eliminates pulsation. The structure of the mixer 28 is shown in FIG. 4 . The mixer 28 is provided with a material inlet 33, a material outlet 34 and an air inlet 35. The mixer 28 is provided with a fluidizing air chamber inside, which plays a role of secondary mixing and can control the flow rate of powder spraying.

火陷长度调节管道26和喷吹支管17直接连接,压缩空气通过火焰长度调节管道26进入喷吹支管17。粉料在喷吹支管17中采用加压输送,通过调节压缩空气的流量可调节粉料在浮法玻璃窑内的燃烧火焰长度。所有喷吹支管17的几何长度相等。The flame length adjustment pipe 26 is directly connected to the injection branch pipe 17, and the compressed air enters the injection branch pipe 17 through the flame length adjustment pipe 26. The powder is transported under pressure in the injection branch pipe 17, and the combustion flame length of the powder in the float glass kiln can be adjusted by adjusting the flow rate of the compressed air. The geometric lengths of all injection branches 17 are equal.

粉料喷枪18:采用高炉喷粉用的耐磨陶瓷喷枪或不锈钢管喷枪。Powder spray gun 18: a wear-resistant ceramic spray gun or a stainless steel tube spray gun for blast furnace powder spraying.

工作原理:working principle:

如图1所示,煤粉通过输粉管道1输送粉料到贮粉仓3,输送气通过仓顶过滤除尘器2排出。贮粉仓3中的粉料被贮粉仓锥部流化装置流化后,通过第一下料管5排到粉料偏心筛6,粉料经过粉料偏心筛6过滤后通过第二下料管7和橡胶补偿器8排到粉料喷吹罐9,粉料喷吹罐9中的粉料经充压管道12充压及通过其底部的流化输送器10流化后,再通过喷粉管道11及其上的混合器28、匀速器15输送到粉料分配器16,粉料分配器16将粉料均匀分配给各喷吹支管17,各喷吹支管17长度相同。然后粉料通过喷吹支管17和粉料喷枪18喷到浮法玻璃窑32内,每罐粉料喷吹20分钟。喷吹完毕后,粉料喷吹罐通过放散管道14泄压,泄压完毕后再装料、充压、等待、喷吹,系统循环连续作业。粉料为石油焦粉时的工作原理与粉料的情况完全相同。As shown in Figure 1, the pulverized coal is transported to the powder storage bin 3 through the powder delivery pipeline 1, and the conveyed gas is discharged through the dust collector 2 on the top of the bin. After the powder in the powder storage bin 3 is fluidized by the cone fluidization device of the powder storage bin, it is discharged to the powder eccentric sieve 6 through the first feeding pipe 5, and the powder is filtered through the powder eccentric sieve 6 and then passed through the second The material pipe 7 and the rubber compensator 8 are discharged to the powder injection tank 9, and the powder in the powder injection tank 9 is pressurized through the pressure-charging pipeline 12 and fluidized through the fluidized conveyor 10 at the bottom, and then passed through the Powder spraying pipe 11 and the mixer 28 on it and the constant speed device 15 are delivered to the powder material distributor 16, and the powder material distributor 16 is evenly distributed to each injection branch pipe 17, and each injection branch pipe 17 has the same length. Then the powder is sprayed into the float glass kiln 32 by the injection branch pipe 17 and the powder spray gun 18, and every can of powder is sprayed for 20 minutes. After the blowing is completed, the powder blowing tank releases the pressure through the release pipe 14, and after the pressure release is completed, the material is loaded, pressurized, waited, and blown, and the system circulates and operates continuously. The working principle when the powder is petroleum coke powder is exactly the same as that of the powder.

该系统采用封闭的贮粉仓和粉料喷吹罐,从粉料输送到喷吹系统粉料始终在密闭的环境中,贮粉仓上仓顶过滤除尘器排放浓度小于30mg/m3,系统可采用氮气或压缩空气喷吹,生产中无其他有害气体排入大气中,环境保护效果好。The system adopts a closed powder storage bin and a powder injection tank. The powder is always in a closed environment from the powder delivery to the injection system . Nitrogen or compressed air can be used for blowing, no other harmful gases are discharged into the atmosphere during production, and the environmental protection effect is good.

Claims (10)

1.用于浮法玻璃窑的粉料输送喷吹装置,包括输粉管道(1)、贮粉仓(3)、第一下料管(5)、第二下料管(7)、粉料喷吹罐(9)、喷粉管道(11)、喷吹支管(17)和粉料喷枪(18),其特征在于:输粉管道(1)接至贮粉仓(3),贮粉仓(3)上安有流化装置(23),贮粉仓(3)通过第一下料管(5)接至粉料偏心筛(6),粉料偏心筛(6)通过第二下料管(7)接至粉料喷吹罐(9),粉料喷吹罐(9)底部通过流化输送器(10)接至喷粉管道(11),喷粉管道(11)的另一端接至粉料分配器(16),粉料分配器(16)的另一端接有粉料喷吹管(17),粉料喷吹管(17)的出口接有粉料喷枪(18)。1. Powder conveying and blowing device for float glass kiln, including powder conveying pipeline (1), powder storage bin (3), first feeding pipe (5), second feeding pipe (7), powder Material injection tank (9), powder injection pipeline (11), injection branch pipe (17) and powder material spray gun (18), it is characterized in that: powder delivery pipeline (1) is connected to powder storage bin (3), powder storage The bin (3) is equipped with a fluidization device (23), the powder storage bin (3) is connected to the powder eccentric sieve (6) through the first feeding pipe (5), and the powder eccentric sieve (6) passes through the second lower The feed pipe (7) is connected to the powder injection tank (9), and the bottom of the powder injection tank (9) is connected to the powder injection pipeline (11) through the fluidized conveyor (10), and the other part of the powder injection pipeline (11) One end is connected to powder material distributor (16), and the other end of powder material distributor (16) is connected with powder material injection pipe (17), and the outlet of powder material injection pipe (17) is connected with powder material spray gun (18). 2.如权利要求1所述的用于浮法玻璃窑的粉料输送喷吹装置,其特征在于:所述的贮粉仓(3)顶部安有仓顶过滤除尘器(2)。2. The powder conveying and blowing device for a float glass kiln according to claim 1, characterized in that: the top of the powder storage bin (3) is equipped with a filter dust collector (2) on the top of the bin. 3.如权利要求1所述的用于浮法玻璃窑的粉料输送喷吹装置,其特征在于:所述的第二下料管(7)和粉料喷吹罐(9)之间接有橡胶补偿器(8)。3. The powder conveying and blowing device for a float glass kiln as claimed in claim 1, characterized in that: said second feeding pipe (7) and the powder blowing tank (9) are connected with Rubber compensator (8). 4.如权利要求1所述的用于浮法玻璃窑的粉料输送喷吹装置,其特征在于:所述流化装置(23)安装在贮粉仓(3)的下锥部,流化管(4)的两个端口分别接至流化装置(23)和贮粉仓(3)的底部。4. The powder conveying and blowing device for a float glass kiln as claimed in claim 1, characterized in that: the fluidization device (23) is installed in the lower cone of the powder storage bin (3), and fluidized The two ports of the pipe (4) are respectively connected to the bottom of the fluidization device (23) and the powder storage bin (3). 5.如权利要求1所述的用于浮法玻璃窑的粉料输送喷吹装置,其特征在于:所述的粉料喷吹罐(9)上安有充压管道(12)、放散过滤器(19)、安全阀过滤器(27)、称重传感器(24)、流化嘴20,放散过滤器(19)通过放散管道(14)接到贮粉仓(3),流化嘴(20)与流化管道(13)相连。5. The powder conveying and blowing device for a float glass kiln as claimed in claim 1, characterized in that: said powder blowing tank (9) is equipped with a pressurized pipeline (12), a release filter device (19), safety valve filter (27), weighing sensor (24), fluidizing nozzle 20, and the release filter (19) is connected to the powder storage bin (3) through the release pipeline (14), and the fluidizing nozzle ( 20) Link to each other with the fluidization pipeline (13). 6.根据权利要求1所述的用于浮法玻璃窑的粉料输送喷吹装置,其特征在于:所述粉料分配器(16)和喷粉管道(11)之间接有混合器(28)和匀速器(15)。6. The powder conveying and blowing device for a float glass kiln according to claim 1, characterized in that: a mixer (28) is connected between the powder distributor (16) and the powder spraying pipeline (11) ) and uniform speed device (15). 7.根据权利要求1所述的用于浮法玻璃窑的粉料输送喷吹装置,其特征在于:所述喷粉管道(11)上接有吹扫管道(25)。7. The powder conveying and blowing device for a float glass kiln according to claim 1, characterized in that: said powder spraying pipeline (11) is connected with a purge pipeline (25). 8.根据权利要求1所述的用于浮法玻璃窑的粉料输送喷吹装置,其特征在于:所述各喷吹支管(17)的几何长度相等,喷吹支管(17)上接有火陷长度调节管道(26)。8. The powder conveying and blowing device for a float glass kiln according to claim 1, characterized in that: the geometric lengths of each of the blowing branch pipes (17) are equal, and the blowing branch pipes (17) are connected with Fire trap length adjustment pipe (26). 9.根据权利要求1所述的用于浮法玻璃窑的粉料输送喷吹装置,其特征在于,所述流化输送器(10)采用上出料流化输送的结构,流化输送器罐体(21)的上部接口(29)与粉料喷吹罐(9)底部相连,流化输送器罐体(21)的中部或上部安有粉料出口(30),粉料出口(30)与喷粉管道(11)相连,流化输送器罐体(21)的下部安有压缩空气入口(31),压缩空气入口(31)与流化输送管(13)相连。9. The powder conveying and blowing device for a float glass kiln according to claim 1, characterized in that, the fluidized conveyor (10) adopts the structure of upper discharge fluidized conveying, and the fluidized conveyor The upper interface (29) of the tank body (21) is connected with the bottom of the powder material injection tank (9), and the middle or upper part of the fluidized conveyor tank body (21) is equipped with a powder material outlet (30), and the powder material outlet (30 ) is connected with the powder spraying pipeline (11), and the bottom of the fluidized conveyor tank body (21) is equipped with a compressed air inlet (31), and the compressed air inlet (31) is connected with the fluidized conveying pipe (13). 10.根据权利要求1所述的用于浮法玻璃窑的粉料输送喷吹装置,其特征在于,所述流化输送器(10)采用下出料流化输送的结构,流化输送器罐体(22)的上部接口(29)与粉料喷吹罐(9)底部相连,流化输送器罐体(22)的底部安有粉料出口(30),粉料出口(30)与喷粉管道(11)相连,流化输送器罐体(22)的中部安有压缩空气入口(31),压缩空气入口(31)与流化输送管(13)相连。10. The powder conveying and blowing device for float glass kiln according to claim 1, characterized in that, the fluidized conveyor (10) adopts the structure of fluidized conveying of the bottom discharge, and the fluidized conveyor The upper interface (29) of the tank body (22) links to each other with the bottom of the powder material injection tank (9), and the bottom of the fluidized conveyor tank body (22) is equipped with a powder material outlet (30), and the powder material outlet (30) is connected to the bottom of the tank body (22). The powder spraying pipeline (11) is connected to each other, and the middle part of the fluidized conveyor tank body (22) is equipped with a compressed air inlet (31), and the compressed air inlet (31) is connected to the fluidized conveying pipe (13).
CNU2007200847691U 2007-05-17 2007-05-17 Powder conveying and blowing device for float glass kiln Expired - Fee Related CN201031196Y (en)

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102140009A (en) * 2010-11-25 2011-08-03 张家港华汇特种玻璃有限公司 Powder supply device for production of float glass
CN101761934B (en) * 2010-01-08 2011-09-28 武汉华尔顺冶金工程技术有限公司 Burning method for pulverized solid fuels transferred by dilute phase pneumatic in tunnel kiln and dilute phase pneumatic transferring system
CN102398685A (en) * 2010-09-07 2012-04-04 烟台市金河保险粉厂有限公司 Method for packaging sodium hydrosulfite
CN102944007A (en) * 2012-11-28 2013-02-27 佛山市沛沣科技有限公司 Multi-temperature-zone powder combustion control system
CN103849700A (en) * 2012-11-30 2014-06-11 西林钢铁集团有限公司 Technology for long-distance direct injection of pulverized coal
CN104140860A (en) * 2014-07-15 2014-11-12 首钢总公司 Coking ash blended fuel, and preparation system, preparation method, application system and application method thereof
CN109678355A (en) * 2019-03-05 2019-04-26 南通职业大学 A kind of novel glass powder blower and its working method
CN109897923A (en) * 2019-04-10 2019-06-18 中冶赛迪技术研究中心有限公司 A kind of streaming tank, coal powder injection apparatus of blast furnace, system and control method
CN116832674A (en) * 2023-06-15 2023-10-03 湖南洪康新材料科技有限公司 Mixing device and mixing method for glass batch materials and cullet

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101761934B (en) * 2010-01-08 2011-09-28 武汉华尔顺冶金工程技术有限公司 Burning method for pulverized solid fuels transferred by dilute phase pneumatic in tunnel kiln and dilute phase pneumatic transferring system
CN102398685A (en) * 2010-09-07 2012-04-04 烟台市金河保险粉厂有限公司 Method for packaging sodium hydrosulfite
CN102140009A (en) * 2010-11-25 2011-08-03 张家港华汇特种玻璃有限公司 Powder supply device for production of float glass
CN102140009B (en) * 2010-11-25 2013-07-10 华尔润玻璃产业股份有限公司 Powder supply device for production of float glass
CN102944007A (en) * 2012-11-28 2013-02-27 佛山市沛沣科技有限公司 Multi-temperature-zone powder combustion control system
CN103849700A (en) * 2012-11-30 2014-06-11 西林钢铁集团有限公司 Technology for long-distance direct injection of pulverized coal
CN104140860A (en) * 2014-07-15 2014-11-12 首钢总公司 Coking ash blended fuel, and preparation system, preparation method, application system and application method thereof
CN109678355A (en) * 2019-03-05 2019-04-26 南通职业大学 A kind of novel glass powder blower and its working method
CN109897923A (en) * 2019-04-10 2019-06-18 中冶赛迪技术研究中心有限公司 A kind of streaming tank, coal powder injection apparatus of blast furnace, system and control method
CN109897923B (en) * 2019-04-10 2024-04-30 中冶赛迪技术研究中心有限公司 Control method of blast furnace coal injection device
CN116832674A (en) * 2023-06-15 2023-10-03 湖南洪康新材料科技有限公司 Mixing device and mixing method for glass batch materials and cullet

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