CN201031196Y - Powder conveying and blowing device for float glass kiln - Google Patents
Powder conveying and blowing device for float glass kiln Download PDFInfo
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- 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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- 239000000843 powder Substances 0.000 title claims abstract description 217
- 238000007664 blowing Methods 0.000 title claims abstract description 31
- 239000005329 float glass Substances 0.000 title claims abstract description 28
- 238000005243 fluidization Methods 0.000 claims abstract description 18
- 239000000428 dust Substances 0.000 claims abstract description 9
- 238000002347 injection Methods 0.000 claims description 65
- 239000007924 injection Substances 0.000 claims description 65
- 239000000463 material Substances 0.000 claims description 37
- 238000003860 storage Methods 0.000 claims description 32
- 238000005507 spraying Methods 0.000 claims description 13
- 239000007921 spray Substances 0.000 claims description 10
- 238000010926 purge Methods 0.000 claims description 4
- 238000005303 weighing Methods 0.000 claims description 3
- 238000010410 dusting Methods 0.000 abstract 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 238000009826 distribution Methods 0.000 description 5
- 229940098458 powder spray Drugs 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002006 petroleum coke Substances 0.000 description 2
- 230000010349 pulsation Effects 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000005357 flat glass Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
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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
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
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Abstract
Description
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
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
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
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
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
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
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
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
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
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
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
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
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
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.
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Cited By (9)
| 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 |
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2007
- 2007-05-17 CN CNU2007200847691U patent/CN201031196Y/en not_active Expired - Fee Related
Cited By (11)
| 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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