WO2019105108A1 - 采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统 - Google Patents

采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统 Download PDF

Info

Publication number
WO2019105108A1
WO2019105108A1 PCT/CN2018/106354 CN2018106354W WO2019105108A1 WO 2019105108 A1 WO2019105108 A1 WO 2019105108A1 CN 2018106354 W CN2018106354 W CN 2018106354W WO 2019105108 A1 WO2019105108 A1 WO 2019105108A1
Authority
WO
WIPO (PCT)
Prior art keywords
suction device
ash
dust removal
valve
metal hose
Prior art date
Application number
PCT/CN2018/106354
Other languages
English (en)
French (fr)
Inventor
葛雷
Original Assignee
中冶南方工程技术有限公司
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 中冶南方工程技术有限公司 filed Critical 中冶南方工程技术有限公司
Publication of WO2019105108A1 publication Critical patent/WO2019105108A1/zh

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/04—Conveying materials in bulk pneumatically through pipes or tubes; Air slides
    • B65G53/24—Gas suction systems
    • B65G53/26—Gas suction systems operating with fluidisation of the materials
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
    • B01D46/023—Pockets filters, i.e. multiple bag filters mounted on a common frame

Definitions

  • the invention relates to the field of environmental protection equipment, and more particularly to a dry dust removal dust removal system using a ground suction device and a winch.
  • the existing main problems of the dry dust removal ash discharge system of the converter are as follows: First, the ash discharge port is far away from the ash truck, the drop is large, and it is easy to cause secondary dust; the second is that the high temperature coarse ash humidifies and generates a large amount of steam. Affect the working environment in the main building.
  • the technical problem to be solved by the present invention is to provide a dry dust removal dust-free ash discharging system using a ground suction device and a hoisting machine, which not only solves the problem of generating a large amount of steam after humidification of high-temperature coarse ash, but also solves the problem of ash discharge due to ash discharge.
  • the problem of secondary dust caused by large is to provide a dry dust removal dust-free ash discharging system using a ground suction device and a hoisting machine, which not only solves the problem of generating a large amount of steam after humidification of high-temperature coarse ash, but also solves the problem of ash discharge due to ash discharge.
  • the problem of secondary dust caused by large is to provide a dry dust removal dust-free ash discharging system using a ground suction device and a hoisting machine, which not only solves the problem of generating a large amount of steam after humidification of high-temperature coarse ash, but also solves the problem of ash discharge due to
  • the technical solution adopted by the invention to solve the technical problem is: constructing a dry dust removal dust-free ash discharging system using a ground suction device and a winch, including a coarse ash silo, an unloading ash main pipe, a telescopic metal hose, and an accident unloading Gray pipe, ground suction device, wear-resistant metal hose and nitrogen pipe;
  • the ash discharge port of the coarse ash silo and the telescopic metal hose are connected by the discharge ash main pipe, and the top of the telescopic metal hose is provided with a pulse valve, and the telescopic metal hose passes through the hoisting Lift
  • the ground suction device is connected to the coarse ash warehouse through an accidental ash discharge pipe; the nitrogen pipe is divided into two paths, one is connected with the pulse valve, and the other is connected with the air supply pipe of the ground suction device,
  • the floor suction device outlet is connected to the wear resistant metal hose.
  • a nitrogen fluidization device is disposed in the lower cone of the coarse ash silo.
  • the unloading main pipe is provided with a manual plug-in valve and a pneumatic double-layer flap valve.
  • the top of the coarse ash silo is provided with a simple bag filter and a vacuum pressure release valve.
  • the accidental ash discharge pipe is provided with an accident manual flapper valve and an accident pneumatic double-layer flapper valve.
  • the pulse valve inlet is provided with a first pneumatic ball valve
  • the ground suction device inlet is provided with a second pneumatic ball valve
  • the ground suction device is provided with an air supply valve and a discharge valve.
  • the invention eliminates the humidification and unloading ash, and no steam is generated when the ash is discharged, and the working environment in the main plant is greatly improved;
  • the gray ash silo unloading ash adopts the method of dust-free ash discharging and pneumatic conveying, and there is no dust overflow during ash discharging, which is more environmentally friendly.
  • the invention not only solves the problem of generating a large amount of steam after humidification of high-temperature coarse ash, but also solves the problem of secondary dust caused by large drop of ash discharge, and is especially suitable for a dry dust removal project of converter once, and has broad application prospects.
  • FIG. 1 is a schematic view showing the structure of a dry dust removing and dust removing system using a ground suction device and a winch according to the present invention.
  • the dry dust removal dust removal system of the present invention comprises a coarse ash silo 1, an ash discharge main 5, a telescopic metal hose 8, an accidental ash discharge pipe 11, a ground suction device 14, and a wear resistant metal.
  • Hose 15 a coarse ash silo 1, an ash discharge main 5, a telescopic metal hose 8, an accidental ash discharge pipe 11, a ground suction device 14, and a wear resistant metal.
  • the ash discharge port of the coarse ash silo 1 and the telescopic metal hose 8 are connected by an unloading main pipe 5, and the unloading main pipe 5 is provided with a manual flapper valve 6 and a pneumatic double flap flapper 7.
  • the top of the coarse ash silo 1 is provided with a simple bag filter 2 and a vacuum pressure release valve 3.
  • the simple bag filter 2 is used to collect the dust discharged from the top of the coarse ash bin 1.
  • the vacuum pressure relief valve 3 serves to prevent the internal pressure of the coarse ash silo 1 from being excessively large.
  • a nitrogen fluidizing device 4 is provided in the lower cone of the coarse ash silo to reduce the coarse ash temperature, dilute the gas mixed in the coarse ash, and prevent coarse ash agglomeration.
  • a pulse valve 10 is provided on the top of the telescopic metal hose 8, and the pulse valve 10 is used to remove the coarse ash remaining in the telescopic metal hose 8.
  • the telescopic metal hose 8 is lifted and lowered by the hoisting machine 9 to reach the ash port of the ash truck 21.
  • the ground suction device 14 is connected to the coarse ash silo 1 through the accidental ash discharge pipe 11, and the accidental ash discharge pipe 11 is provided with an accident manual flapper valve 12 and an accident pneumatic double-layer flapper valve 13.
  • the accident manual flapper valve 12 and the accident pneumatic double-layer flapper valve 13 are opened, the coarse ash in the coarse ash silo 1 enters the ground suction device 14 through the accidental ash discharge pipe 11.
  • the second pneumatic ball valve 18 and the makeup valve 19 are opened, and the coarse ash in the ground suction device 14 is sent to the suction and exhaust vehicle 22 through the wear-resistant metal hose 15.
  • the nitrogen tube 16 is divided into two paths, one connected to the pulse valve 10 and the other connected to the supplemental valve 19 of the ground suction device 14.
  • the first valve of the pulse valve 10 is provided with a first pneumatic ball valve 17, and when the first pneumatic ball valve 17 is opened, the pulse valve 10 is sprayed with dust.
  • the inlet of the air supply valve 19 of the ground suction device 14 is provided with a second pneumatic ball valve 18, and the outlet of the ground suction device 14 is connected to the wear-resistant metal hose 15.
  • the process flow of the coarse dust removal of the dry dust removal and dust removal system in the present invention is as follows:
  • the coarse ash temperature in the coarse ash silo 1 is 100 ° C to 200 ° C (typically 150 ° C).
  • the nitrogen fluidization device 4 periodically sprays low-pressure nitrogen gas, which not only can reduce the temperature of the coarse ash in the coarse ash silo 1, but also dilute the gas mixed in the coarse ash, and can also fluidize the coarse ash to facilitate the ash discharge.
  • the coarse ash collected by the simple bag filter 2 can be blown back into the coarse ash bin 1 by nitrogen to ensure that the outlet of the simple bag filter 2 is up to standard.
  • the coarse gray ash discharge pipe 5, the manual insert valve 6 and the pneumatic double flap valve 7 enter the telescopic metal hose 8, and the coarse ash of the telescopic metal hose 8 is discharged to the ash truck 21 by the hoisting machine 9.
  • the hoisting machine 9 is inspected, the coarse ash is turned into the ground suction device 14 by the accidental ash discharge pipe 11, the accident manual splicing valve 12 and the accident pneumatic double slab valve 13, and the second pneumatic ball valve 18 and the supplementary valve 19 are opened, and the coarse ash is opened. It is sent to the suction and exhaust cart 22 via the wear resistant metal hose 15.
  • the outlet of the ground suction device 14 is provided with a drain valve 20, and once the wear-resistant metal hose 15 is blocked, the drain valve 20 is opened.
  • the hoisting machine 9 and the ground suction device 14 can work alternately and spare each other. When one is overhauled, the whole system can still work normally, the stability of the ash discharging system is improved, and the coarse ash is timely discharged.
  • the coarse ash of the coarse ash silo 1 is discharged to the ash transporting vehicle 21 through the telescopic metal hose 8 to solve the dusting problem caused by the large drop, and there is no dust overflow during the ash discharging, which is more environmentally friendly.
  • the nitrogen tube 16 is provided with a first pneumatic ball valve 17 and a second pneumatic ball valve 18.
  • the first pneumatic ball valve 17 is opened to close the second pneumatic ball valve 18; when the ground suction device 14 is in operation, the first pneumatic ball valve 17 is closed and the second pneumatic ball valve 18 is opened.
  • the material of the coarse ash silo 1 is stainless steel.
  • the material of the telescopic metal hose 8 is stainless steel.
  • the wear-resistant metal hose 15 is made of stainless steel.
  • the hoisting machine is equipped with an electromechanical capacity: 1.0 to 10 kW.
  • the dust-free ash discharging system of the invention is suitable for the ash discharging of the dry dust of the flue gas dry dust of the 50t-350t converter.

Abstract

一种采用地面吸料装置（14）和卷扬机（9）的干法除尘无尘卸灰系统，包括粗灰仓（1）、卸灰主管（5）、伸缩式金属软管（8）、事故卸灰管（11）、地面吸料装置（14）、耐磨金属软管（15）和氮气管（16）；该粗灰仓（1）的卸灰口和该伸缩式金属软管（8）通过该卸灰主管（5）连接，该伸缩式金属软管（8）顶部设有脉冲阀（10），该伸缩式金属软管（8）通过该卷扬机（9）升降；该地面吸料装置（14）通过事故卸灰管（11）与该粗灰仓（1）连接；该氮气管（16）分为两路，一路与该脉冲阀（10）连接，另一路与该地面吸料装置（14）的补气管连接，该地面吸料装置出口连接耐磨金属软管（15）。该系统不但解决了高温粗灰加湿后产生大量蒸汽的问题，也解决了由于卸灰落差大引起的二次扬尘的问题，尤其适合转炉一次烟气干法除尘项目，应用前景广阔。

Description

采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统 技术领域
本发明涉及环保设备领域，更具体地说，涉及一种采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统。
背景技术
随着新的环保标准不断提高，新建及改建的转炉大都采用干法除尘系统。蒸发冷却器收集的高温粗灰通过内置双链式输送机送至主厂房内的粗灰仓，加湿后由汽车外运。
现有的转炉干法除尘粗灰卸灰系统主要存在的问题：一是卸灰口离运灰车较远，落差大，容易引起二次扬尘；二是高温的粗灰加湿后产生大量蒸汽，影响主厂房内工作环境。
发明内容
本发明要解决的技术问题在于，提供一种采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统，不但解决了高温粗灰加湿后产生大量蒸汽的问题，也解决了由于卸灰落差大引起的二次扬尘的问题。
本发明解决其技术问题所采用的技术方案是：构造一种采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统，包括粗灰仓、卸灰主管、伸缩式金属软管、事故卸灰管、地面吸料装置、耐磨金属软管和氮气管；
所述粗灰仓的卸灰口和所述伸缩式金属软管通过所述卸灰主管连接，所述伸缩式金属软管顶部设有脉冲阀，所述伸缩式金属软管通过所述卷扬升降；
所述地面吸料装置通过事故卸灰管与所述粗灰仓连接；所述氮气管分为两路，一路与所述脉冲阀连接，另一路与所述地面吸料装置的补气管连接，所述地面吸料装置出口连接耐磨金属软管。
上述方案中，所述粗灰仓下锥斗内设有氮气流化装置。
上述方案中，所述卸灰主管上设有手动插板阀和气动双层翻板阀。
上述方案中，所述粗灰仓顶部设有简易布袋除尘器和真空压力释放阀。
上述方案中，所述事故卸灰管上设有事故手动插板阀和事故气动双层翻板阀。
上述方案中，所述脉冲阀入口设有第一气动球阀，所述地面吸料装置入口设有第二气动球阀。
上述方案中，所述地面吸料装置上设有补气阀和排堵阀。
实施本发明的采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统，具有以下有益效果：
1、本发明取消了加湿卸灰，卸灰时无蒸汽产生，主厂房内工作环境大大改善；
2、粗灰仓卸灰采用无尘卸灰及气力输送的方式，卸灰时无粉尘外溢，更环保。
3、本发明不但解决了高温粗灰加湿后产生大量蒸汽的问题，也解决了由于卸灰落差大引起的二次扬尘的问题，尤其适合转炉一次烟气干法除尘项目，应用前景广阔。
附图说明
下面将结合附图及实施例对本发明作进一步说明，附图中：
图1是本发明采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统的结构示意图。
具体实施方式
为了对本发明的技术特征、目的和效果有更加清楚的理解，现对照附图详细说明本发明的具体实施方式。
如图1所示，本发明的干法除尘无尘卸灰系统包括粗灰仓1、卸灰主管5、伸缩式金属软管8、事故卸灰管11、地面吸料装置14和耐磨金属软管15。
粗灰仓1的卸灰口和伸缩式金属软管8通过卸灰主管5连接，卸灰主管5上设有手动插板阀6和气动双层翻板阀7。
粗灰仓1顶部设有简易布袋除尘器2和真空压力释放阀3。简易布袋除尘器2用于收集粗灰仓1顶部排出的粉尘。真空压力释放阀3用于防止粗灰仓1内部压力过大。粗灰仓1下锥斗内设有氮气流化装置4用于降低粗灰温度、稀释粗灰中夹杂的煤气和防止粗灰结块。
伸缩式金属软管8顶部设有脉冲阀10，脉冲阀10用于清除伸缩式金属软管8内残留的粗灰。伸缩式金属软管8通过卷扬机9升降，到达运灰车21进灰口。
地面吸料装置14通过事故卸灰管11与粗灰仓1连接，事故卸灰管11上设有事故手动插板阀12和事故气动双层翻板阀13。事故手动插板阀12和事故气动双层翻板阀13开启时，粗灰仓1内的粗灰通过事故卸灰管11进入地面吸料装置14内。打开第二气动球阀18和补气阀19，地面吸料装置14内的粗灰经过耐磨金属软管15送至吸排车22内。
氮气管16分为两路，一路与脉冲阀10连接，另一路与地面吸料装置14的补气阀19连接。
脉冲阀10入口设有第一气动球阀17，第一气动球阀17开启时，脉冲阀10喷吹清灰。
地面吸料装置14的补气阀19入口设有第二气动球阀18，地面吸料装置14出口连接耐磨金属软管15。
本发明中干法除尘无尘卸灰系统粗灰卸灰的工艺流程如下：
粗灰仓1→卸灰主管5/事故卸灰管11→手动插板阀6/事故手动插板阀12→气动双层翻板阀7/事故气动双层翻板阀13→伸缩式金属软管8/地面吸料装置14→运灰车21/吸排车22。
粗灰仓1内粗灰温度100℃～200℃(一般为150℃)。氮气流化装置4周期性的喷吹低压氮气，不但可以降低粗灰仓1内粗灰的温度，也可以稀释粗灰中夹杂的煤气，还可以流化粗灰，便于卸灰。简易布袋除尘器2收集的粗灰可通过氮气反吹落至粗灰仓1内，保证简易布袋除尘器2出口排放达标。
粗灰经卸灰管5、手动插板阀6和气动双层翻板阀7进入伸缩式金属软管8，通过卷扬机9将伸缩式金属软管8的粗灰卸至运灰车21。卷扬机9检修时，粗灰经事故卸灰管11、事故手动插板阀12和事故气动双层翻板阀13进入地面吸 料装置14，第二气动球阀18和补气阀19开启，粗灰经耐磨金属软管15送至吸排车22。地面吸料装置14出口设有排堵阀20，一旦耐磨金属软管15内堵灰，打开排堵阀20。卷扬机9和地面吸料装置14可交替工作，并互为备用，其中一个检修时，整个系统仍然可以正常的工作，提高了卸灰系统的稳定性，保证了粗灰按时卸灰。
粗灰仓1的粗灰通过伸缩式金属软管8卸至运灰车21，解决了由于落差大引起的扬尘问题，卸灰时无粉尘外溢，更环保。
进一步的，氮气管16设有第一气动球阀17和第二气动球阀18。脉冲阀10喷吹时，开启第一气动球阀17，关闭第二气动球阀18；地面吸料装置14工作时，关闭第一气动球阀17，开启第二气动球阀18。
进一步的，粗灰仓1的材质为不锈钢。
进一步的，伸缩式金属软管8的材质为不锈钢。
进一步的，耐磨金属软管15的材质为不锈钢。
进一步的，卷扬机装机电容量：1.0～10kW。
本发明的无尘卸灰系统适用于50t～350t转炉一次烟气干法除尘粗灰的卸灰。
上面结合附图对本发明的实施例进行了描述，但是本发明并不局限于上述的具体实施方式，上述的具体实施方式仅仅是示意性的，而不是限制性的，本领域的普通技术人员在本发明的启示下，在不脱离本发明宗旨和权利要求所保护的范围情况下，还可做出很多形式，这些均属于本发明的保护之内。

Claims (7)

  1. 一种采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统，其特征在于，包括粗灰仓(1)、卸灰主管(5)、伸缩式金属软管(8)、事故卸灰管(11)、地面吸料装置(14)、耐磨金属软管(15)和氮气管(16)；
    所述粗灰仓(1)的卸灰口和所述伸缩式金属软管(8)通过所述卸灰主管(5)连接，所述伸缩式金属软管(8)顶部设有脉冲阀(10)，所述伸缩式金属软管(8)通过所述卷扬(9)升降；
    所述地面吸料装置(14)通过事故卸灰管(11)与所述粗灰仓(1)连接；所述氮气管(16)分为两路，一路与所述脉冲阀(10)连接，另一路与所述地面吸料装置(14)的补气管连接，所述地面吸料装置(14)出口连接耐磨金属软管(15)。
  2. 根据权利要求1所述的采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统，其特征在于，所述粗灰仓(1)下锥斗内设有氮气流化装置(4)。
  3. 根据权利要求1所述的采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统，其特征在于，所述卸灰主管(5)上设有手动插板阀(6)和气动双层翻板阀(7)。
  4. 根据权利要求1所述的采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统，其特征在于，所述粗灰仓(1)顶部设有简易布袋除尘器(2)和真空压力释放阀(3)。
  5. 根据权利要求1所述的采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统，其特征在于，所述事故卸灰管(11)上设有事故手动插板阀(12)和事故气动双层翻板阀(13)。
  6. 根据权利要求1所述的采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统，其特征在于，所述脉冲阀(10)入口设有第一气动球阀(17)，所述地面吸料装置(14)入口设有第二气动球阀(18)。
  7. 根据权利要求1所述的采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统，其特征在于，所述地面吸料装置(14)上设有补气阀(19)和排堵阀(20)。
PCT/CN2018/106354 2017-11-28 2018-09-19 采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统 WO2019105108A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201711211386.0A CN107826768A (zh) 2017-11-28 2017-11-28 采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统
CN201711211386.0 2017-11-28

Publications (1)

Publication Number Publication Date
WO2019105108A1 true WO2019105108A1 (zh) 2019-06-06

Family

ID=61646220

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2018/106354 WO2019105108A1 (zh) 2017-11-28 2018-09-19 采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统

Country Status (2)

Country Link
CN (1) CN107826768A (zh)
WO (1) WO2019105108A1 (zh)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107826768A (zh) * 2017-11-28 2018-03-23 中冶南方工程技术有限公司 采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统
CN107841590A (zh) * 2017-11-28 2018-03-27 中冶南方工程技术有限公司 干法除尘无尘卸灰方法
CN107760815A (zh) * 2017-11-28 2018-03-06 中冶南方工程技术有限公司 干法粉尘无尘卸灰系统
CN109230654A (zh) * 2018-09-29 2019-01-18 四川德胜集团钒钛有限公司 运用于钒铁生产中的除尘放灰系统
CN112520328A (zh) * 2020-11-30 2021-03-19 中冶南方工程技术有限公司 无尘卸灰系统及转炉烟气处理系统
CN112359162A (zh) * 2020-11-30 2021-02-12 中冶南方工程技术有限公司 干灰无尘卸灰系统及转炉烟气处理系统

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005226145A (ja) * 2004-02-16 2005-08-25 Jfe Steel Kk 転炉排ガスの除塵装置とそのダスト付着防止方法
CN201454313U (zh) * 2009-08-14 2010-05-12 重庆钢铁(集团)有限责任公司 一种防尘排灰装置
CN203048966U (zh) * 2013-01-15 2013-07-10 刘芳 高炉排料自动除尘排灰装置
CN203728203U (zh) * 2014-02-24 2014-07-23 鞍钢集团工程技术有限公司 一种正压卸灰装置
CN104073581A (zh) * 2014-06-18 2014-10-01 鞍钢集团工程技术有限公司 强制回收高炉放散煤气的工艺方法及装置
CN205170896U (zh) * 2015-06-30 2016-04-20 中冶南方工程技术有限公司 一种转炉干法除尘粗灰气力输送系统
CN107826768A (zh) * 2017-11-28 2018-03-23 中冶南方工程技术有限公司 采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统
CN107841590A (zh) * 2017-11-28 2018-03-27 中冶南方工程技术有限公司 干法除尘无尘卸灰方法

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101544363A (zh) * 2008-03-26 2009-09-30 贵阳铝镁设计研究院 可伸缩式卸灰装置
CN202046728U (zh) * 2010-11-30 2011-11-23 中冶南方工程技术有限公司 除尘灰仓卸灰二次扬尘收尘装置
RU2535821C1 (ru) * 2013-10-31 2014-12-20 Закрытое Акционерное Общество "Твин Трейдинг Компани" Вакуумно-пневматическое устройство для транспортирования сыпучих материалов с высокой массовой концентрацией
CN204417528U (zh) * 2014-12-31 2015-06-24 江苏瑞帆环保装备股份有限公司 高炉煤气干法袋式除尘器双点流化卸灰装置
CN104909168A (zh) * 2015-04-28 2015-09-16 北京首钢国际工程技术有限公司 吸排车输灰配套装置及使用方法
CN205170899U (zh) * 2015-06-30 2016-04-20 中冶南方工程技术有限公司 一种转炉煤气干法除尘粗灰气力输送系统
CN205114513U (zh) * 2015-08-19 2016-03-30 武汉运盛特种汽车制造有限公司 吸排车用移动吸料装置
CN106429453B (zh) * 2016-09-20 2018-10-30 河南工业大学 颗粒性粮食农作物长距离管道气力螺旋推进式输送系统
CN207632118U (zh) * 2017-11-28 2018-07-20 中冶南方工程技术有限公司 采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005226145A (ja) * 2004-02-16 2005-08-25 Jfe Steel Kk 転炉排ガスの除塵装置とそのダスト付着防止方法
CN201454313U (zh) * 2009-08-14 2010-05-12 重庆钢铁(集团)有限责任公司 一种防尘排灰装置
CN203048966U (zh) * 2013-01-15 2013-07-10 刘芳 高炉排料自动除尘排灰装置
CN203728203U (zh) * 2014-02-24 2014-07-23 鞍钢集团工程技术有限公司 一种正压卸灰装置
CN104073581A (zh) * 2014-06-18 2014-10-01 鞍钢集团工程技术有限公司 强制回收高炉放散煤气的工艺方法及装置
CN205170896U (zh) * 2015-06-30 2016-04-20 中冶南方工程技术有限公司 一种转炉干法除尘粗灰气力输送系统
CN107826768A (zh) * 2017-11-28 2018-03-23 中冶南方工程技术有限公司 采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统
CN107841590A (zh) * 2017-11-28 2018-03-27 中冶南方工程技术有限公司 干法除尘无尘卸灰方法

Also Published As

Publication number Publication date
CN107826768A (zh) 2018-03-23

Similar Documents

Publication Publication Date Title
WO2019105108A1 (zh) 采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统
CN105947683A (zh) 正负压一体化气力输灰系统
CN103057862A (zh) 一种粉尘转运的储存和卸料装置及其使用方法
CN103333983A (zh) 一种转炉一次烟气干法除尘粗灰气力输送系统
WO2019105109A1 (zh) 干法除尘无尘卸灰方法
CN103333984B (zh) 转炉一次烟气干法除尘粗灰气力输送系统
CN103332493B (zh) 一种转炉煤气干法除尘粗灰气力输送方法
CN203033223U (zh) 一种粉尘转运的储存和卸料装置
WO2019105111A1 (zh) 干法粉尘无尘卸灰系统
CN203319266U (zh) 火电厂浓相气力输灰系统
CN205170896U (zh) 一种转炉干法除尘粗灰气力输送系统
CN103333985B (zh) 转炉煤气干法除尘粗灰气力输送系统
CN103333986B (zh) 一种转炉煤气干法除尘粗灰气力输送系统
CN207632118U (zh) 采用地面吸料装置和卷扬机的干法除尘无尘卸灰系统
CN207632831U (zh) 转炉干法无尘卸灰系统
CN212654859U (zh) 一种吸料口设置有清理管路的粉粒物料运输罐
CN103318648B (zh) 转炉煤气干法除尘粗灰气力输送方法
CN105858222A (zh) 正负压一体化气力输灰系统和方法
CN107723408A (zh) 转炉干法无尘卸灰方法
CN205045500U (zh) 真空提升机
CN206229088U (zh) 一种机制砂设备的气控系统
CN106520209B (zh) 一种U-Gas气化炉飞灰连续返炉控制系统及其控制方法
CN203780397U (zh) 干式颗粒、粉料自卸罐车
CN205115519U (zh) 一种提钒转炉一次除尘粗灰气力输送系统
CN213049973U (zh) 煤气尘灰处理装置

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 18883411

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 18883411

Country of ref document: EP

Kind code of ref document: A1