CN104084595B - A kind of antimony powder production system - Google Patents
A kind of antimony powder production system Download PDFInfo
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- CN104084595B CN104084595B CN201410328233.4A CN201410328233A CN104084595B CN 104084595 B CN104084595 B CN 104084595B CN 201410328233 A CN201410328233 A CN 201410328233A CN 104084595 B CN104084595 B CN 104084595B
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- antimony powder
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- smelting furnace
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Abstract
The invention discloses a kind of antimony powder production system, including: prolong device (2) in smelting furnace (1), water-cooled and antimony powder transfers pipeline (3)；Prolonging device (2) in described water-cooled and be arranged on the antimony powder exit of described smelting furnace (1), described antimony powder transfers pipeline (3) and is connected with prolonging device (2) in described water-cooled；The shape of cross section of the meal outlet prolonging device (2) in described water-cooled is ellipse, is provided with condensation layer (21) in described water-cooled is prolonged the perisporium of device (2)；Described antimony powder transfers pipeline (3) and is made up of multistage bending tube, and the junction, lower end of every two sections of bending tubes is provided with taper bucket (31).It is to prolong device in oval water-cooled by arranging shape of cross section, when antimony powder is discharged by prolonging device in this water-cooled from smelting furnace, the antimony powder of core with prolong device perisporium in water-cooled in water trough distance equal, also it is more or less the same by water trough distance in prolonging device perisporium in the antimony powder of whole outlet and water-cooled so that when antimony powder is come out of the stove, cooling is more fully and uniformly.
Description
Technical field
The present invention relates to antimony powder and produce equipment technical field, particularly to a kind of antimony powder production system.
Background technology
In antimony processing industry, it is common that refine antimony powder in high temperature melting furnace.Existing smelting furnace is to crouch to build on mill floor, offers charge door on the sidewall of smelting furnace, it is common that use the spade of belt length holding rod to be sent in smelting furnace by antimony raw material.In existing equipment, using spade to add raw material in smelting furnace has inconvenience.One is, the holding rod of spade is oversize, easily causes bending, and holding rod heats up and scalds one's hand, and brings danger to operation；Two aspects, spade at high temperature easily deliquescing, antimony raw material adition process is infiltrated iron tramp, increases antimony powder impurity content, affect antimony powder quality.
Between multiple working procedure, need transport or transfer the antimony powder of intermediate products.Existing transfer the mode each procedure of many employings after pack and be transported to next process again, or direct pipeline carries out air blast conveying.When above-mentioned employing pipeline directly carries, it is common that use straight conveyance conduit, i.e. it is erected on vehicle frame wall or connects the circular pipe between the workshop having certain distance.This erection mode easily settles one layer of dust in duct bottom, and increasingly thicker.The method removing these sedimentation dust is to offer removing window on pipeline, removes spatula at window from these and falls the dust piled up.Such reset mode to expend substantial amounts of manpower and materials, and product quality is had large effect.
Existing cooling device is divided into air-cooled and water-cooled two kinds.Wherein, air cooler, it is i.e. that the antimony powder come out of the stove is transferred at the process equipment of next process by the conveyance conduit using distance, makes the high temperature antimony powder come out of the stove cool down inside the conveying pipe of this distance.This water but mode makes antimony powder need the conveying through long-distance, adds cooling and the cost of conveying.Another kind of equipment is water cooling equipment, is arranged around a columnar antimony powder outlet at plug for outlet, is provided with condensate pipe or current separate slot in columnar outlet surrounding wall.Circular water cooling equipment, cools down not to the antimony powder of export center, even with the antimony powder inhomogeneous cooling that center is discharged around.
Therefore, how to realize the problem of the aspects such as cooling is uniform, it is smooth and easy to carry, charging is convenient in antimony powder processing, become the problem that those skilled in the art are in the urgent need to address.
Summary of the invention
In order to solve problem of the prior art, embodiments provide a kind of antimony powder production system.Described technical scheme is as follows:
Providing a kind of antimony powder production system, described system includes: prolong device in smelting furnace, water-cooled and antimony powder transfers pipeline.
Prolonging device in described water-cooled and be arranged on the antimony powder exit of described smelting furnace, described antimony powder transfers pipeline and prolongs device in described water-cooled and be connected；The shape of cross section of the meal outlet prolonging device in described water-cooled is ellipse, is provided with condensation layer in described water-cooled is prolonged the perisporium of device；Described antimony powder transfers pipeline and is made up of multistage bending tube, and the junction, lower end of every two sections of bending tubes is provided with taper bucket.
Further, described water-cooled is prolonged and on device outer wall, bottom position is provided with the water inlet pipe being connected with described condensation layer, described water-cooled is prolonged and on device outer wall, tip position is provided with the outlet pipe being connected with described condensation layer.
Further, described condensation layer is the condensate pipe being circumferentially positioned in the perisporium prolonging device in described water-cooled, and the lower port of described condensate pipe is connected with described water inlet pipe, and the upper port of described condensate pipe is connected with described outlet pipe.
Further, described system also includes the servicing unit that feeds, and described charging servicing unit is made up of installation frame, baffle plate and charging chute.Described installation frame is arranged on the charge door of antimony powder smelting furnace, and described installation frame both sides offer baffle plate guide groove, and described baffle plate guide groove is high outside and low outside inclined guide groove.Described baffle plate two ends are provided with the guide lug suitable with described baffle plate guide groove, and described guide lug is slidably mounted in described baffle plate guide groove.Described charging chute is inclined to set outside described installation frame, and described charging chute lower end is docked with arc bottom described installation frame.
The technical scheme that the embodiment of the present invention provides has the benefit that
It is to prolong device in oval water-cooled by arranging shape of cross section, when antimony powder is discharged by prolonging device in this water-cooled from smelting furnace, the antimony powder of core with prolong device perisporium in water-cooled in water trough distance equal, also it is more or less the same by water trough distance in prolonging device perisporium in the antimony powder of whole outlet and water-cooled so that when antimony powder is come out of the stove, cooling is more fully and uniformly.
Pipeline is transferred by arranging the antimony powder of bending tube and taper bucket, make this antimony powder transfer pipeline to run in straight pipeline when antimony powder carries for a long time and cause the bulk deposition of dust, even if having part to pile up also is to be deposited in inside taper bucket, it is more prone to remove sedimentating dust.
By arranging multistage bending tube, make spatially longer at a distance of the transport path of certain far and near powder of inter process up and down, the high temperature powder especially transported out from smelting furnace, the bending pipeline of these distance adds cool time, without cooling down separately, efficiently utilize the space of plant floor, save production cost.
By arranging the charging servicing unit of band baffle plate so that in smelting furnace, addition raw material is convenient simple and direct, and security performance is greatly improved.This baffle plate operationally moves, and on the one hand achieves the barrier inside and outside smelting furnace, and two aspects can facilitate raw material to enter.Charging chute is set in outer end, as long as raw material being put on this charging chute, pushing it in smelting furnace with instrument, improve convenience.
Accompanying drawing explanation
For the technical scheme being illustrated more clearly that in the embodiment of the present invention, in describing embodiment below, the required accompanying drawing used is briefly described, apparently, accompanying drawing in describing below is only some embodiments of the present invention, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the structural representation of the antimony powder production system that the embodiment of the present invention provides.
Fig. 2 is the perspective view prolonging device in the water-cooled that the embodiment of the present invention provides.
Fig. 3 is the longitudinally cutting structural representation prolonging device in the water-cooled that the embodiment of the present invention provides.
Fig. 4 is the perspective view of the charging servicing unit that the embodiment of the present invention provides.
Fig. 5 is the structural representation of the installation frame cutting later madial wall that the embodiment of the present invention provides.
Detailed description of the invention
For making the object, technical solutions and advantages of the present invention clearer, below in conjunction with accompanying drawing, embodiment of the present invention is described further in detail.
Embodiment
Present embodiments providing a kind of antimony powder production system, incorporated by reference to referring to figs. 1 to Fig. 5, this system includes: prolong device 2 in smelting furnace 1, water-cooled and antimony powder transfers pipeline 3.
Prolonging device 2 in water-cooled and be arranged on the antimony powder exit of smelting furnace 1, antimony powder transfers pipeline 3 and is connected with prolonging device 2 in water-cooled.
The shape of cross section of the meal outlet prolonging device 2 in water-cooled is ellipse, is provided with condensation layer 21 in water-cooled is prolonged the perisporium of device 2.
Antimony powder transfers pipeline 3 and is made up of multistage bending tube, and the junction, lower end of every two sections of bending tubes is provided with taper bucket 31.
Water-cooled is prolonged and on device 2 outer wall, bottom position is provided with the water inlet pipe 22 being connected with condensation layer 21, water-cooled is prolonged and on device 2 outer wall, tip position is provided with the outlet pipe 23 being connected with condensation layer 21.
Condensation layer 21 is the condensate pipe being circumferentially positioned in water-cooled in the perisporium prolonging device 2, and the lower port of condensate pipe is connected with water inlet pipe 22, and the upper port of condensate pipe is connected with outlet pipe 23.
As preferred embodiment, this system also includes the servicing unit 4 that feeds, and charging servicing unit 4 is made up of installation frame 41, baffle plate 42 and charging chute 43.
Installation frame 41 is arranged on the charge door of antimony powder smelting furnace, and installation frame 41 both sides offer baffle plate guide groove 411, and baffle plate guide groove 411 is high outside and low outside inclined guide groove.Baffle plate 42 two ends are provided with the guide lug 421 suitable with baffle plate guide groove 411, and guide lug 421 is slidably mounted in baffle plate guide groove 411.Charging chute 43 is inclined to set outside installation frame 41, and charging chute 43 lower end is docked with arc bottom installation frame 41.So, at the charge door that installation frame 41 is embedded on the sidewall of smelting furnace, raw material is by this installation frame 41 to charge door, then in smelting furnace.Baffle plate 42 is arranged on this installation frame 41, and operationally moves or rotate, and the high temperature antimony liquid being possible to prevent in smelting furnace spills outside stove.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (3)
1. an antimony powder production system, it is characterised in that described system includes: prolong device (2) in smelting furnace (1), water-cooled and antimony powder transfers pipeline (3)；
Prolonging device (2) in described water-cooled and be arranged on the antimony powder exit of described smelting furnace (1), described antimony powder transfers pipeline (3) and is connected with prolonging device (2) in described water-cooled；
The shape of cross section of the meal outlet prolonging device (2) in described water-cooled is ellipse, is provided with condensation layer (21) in described water-cooled is prolonged the perisporium of device (2)；
Described antimony powder transfers pipeline (3) and is made up of multistage bending tube, and the junction, lower end of every two sections of bending tubes is provided with taper bucket (31)；
Described system also includes the servicing unit (4) that feeds, and described charging servicing unit (4) is made up of installation frame (41), baffle plate (42) and charging chute (43)；
Described installation frame (41) is arranged on the charge door of antimony powder smelting furnace, and described installation frame (41) both sides offer baffle plate guide groove (411), and described baffle plate guide groove (411) is high outside and low outside inclined guide groove；
Described baffle plate (42) two ends are provided with the guide lug (421) suitable with described baffle plate guide groove (411), and described guide lug (421) is slidably mounted in described baffle plate guide groove (411)；
Described charging chute (43) is inclined to set in described installation frame (41) outside, and described charging chute (43) lower end is docked with described installation frame (41) bottom arc.
Antimony powder production system the most according to claim 1, it is characterized in that, described water-cooled is prolonged and on device (2) outer wall, bottom position is provided with the water inlet pipe (22) being connected with described condensation layer (21), described water-cooled is prolonged and on device (2) outer wall, tip position is provided with the outlet pipe (23) being connected with described condensation layer (21).
Antimony powder production system the most according to claim 2, it is characterized in that, described condensation layer (21) is for be circumferentially positioned at the condensate pipe in the perisporium prolonging device (2) in described water-cooled, the lower port of described condensate pipe is connected with described water inlet pipe (22), and the upper port of described condensate pipe is connected with described outlet pipe (23).
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| CN201410328233.4A CN104084595B (en) | 2014-07-11 | 2014-07-11 | A kind of antimony powder production system |
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| CN201410328233.4A CN104084595B (en) | 2014-07-11 | 2014-07-11 | A kind of antimony powder production system |
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| CN104084595A CN104084595A (en) | 2014-10-08 |
| CN104084595B true CN104084595B (en) | 2016-08-24 |
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| CN106756109A (en) * | 2016-11-30 | 2017-05-31 | 湖南娄底华星锑业有限公司 | A kind of antimony powder converting furnace |
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| CN1199711A (en) * | 1997-05-20 | 1998-11-25 | 魏诗照 | Technical process of preparing high-purity superfine diantimony trioxide |
| CN2303833Y (en) * | 1997-08-01 | 1999-01-13 | 广东省丰顺县龙山贸易开发公司 | Cooling device for use on stibium trioxide powder production line |
| CN2332979Y (en) * | 1997-07-18 | 1999-08-11 | 广东省丰顺县龙山贸易开发公司 | Stibium trioxide smelting furnace |
| US6379419B1 (en) * | 1998-08-18 | 2002-04-30 | Noranda Inc. | Method and transferred arc plasma system for production of fine and ultrafine powders |
| CN101565781A (en) * | 2008-12-10 | 2009-10-28 | 株洲科迪亚实业有限公司 | Method and device for producing high-purity antimony |
| CN202492376U (en) * | 2012-04-05 | 2012-10-17 | 广西华锑科技有限公司 | Antimony white furnace gaseous phase cooling crystallization device |
| CN102787246A (en) * | 2012-07-18 | 2012-11-21 | 开美化学科技(南通)有限公司 | Smelting production method and device of antimony trioxide |
| CN202808392U (en) * | 2012-07-20 | 2013-03-20 | 湖南娄底华星锑业有限公司 | Upward continuation device of water-cooled antimony white furnace |
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2014
- 2014-07-11 CN CN201410328233.4A patent/CN104084595B/en active Active
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3759500A (en) * | 1970-05-29 | 1973-09-18 | Ammi Spa | Plant for the treatment and the oxidation of antimony minerals |
| CN87204984U (en) * | 1987-03-30 | 1988-02-24 | 葫芦岛锌厂 | Device for producing indirect process zinc oxide |
| CN1199711A (en) * | 1997-05-20 | 1998-11-25 | 魏诗照 | Technical process of preparing high-purity superfine diantimony trioxide |
| CN2332979Y (en) * | 1997-07-18 | 1999-08-11 | 广东省丰顺县龙山贸易开发公司 | Stibium trioxide smelting furnace |
| CN2303833Y (en) * | 1997-08-01 | 1999-01-13 | 广东省丰顺县龙山贸易开发公司 | Cooling device for use on stibium trioxide powder production line |
| US6379419B1 (en) * | 1998-08-18 | 2002-04-30 | Noranda Inc. | Method and transferred arc plasma system for production of fine and ultrafine powders |
| CN101565781A (en) * | 2008-12-10 | 2009-10-28 | 株洲科迪亚实业有限公司 | Method and device for producing high-purity antimony |
| CN202492376U (en) * | 2012-04-05 | 2012-10-17 | 广西华锑科技有限公司 | Antimony white furnace gaseous phase cooling crystallization device |
| CN102787246A (en) * | 2012-07-18 | 2012-11-21 | 开美化学科技(南通)有限公司 | Smelting production method and device of antimony trioxide |
| CN202808392U (en) * | 2012-07-20 | 2013-03-20 | 湖南娄底华星锑业有限公司 | Upward continuation device of water-cooled antimony white furnace |
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| CN104084595A (en) | 2014-10-08 |
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Effective date of registration: 20180417 Address after: 557801 Cen Gong County Industrial Park, Qiandongnan Miao and Dong Autonomous Prefecture, Guizhou Patentee after: Guizhou Huaxing Metallurgy Co., Ltd. Address before: 417600 dragon village, Xinhua County, Loudi City, Hunan Province Patentee before: Hunan Loudi Huaxing Antimony Industry Co., Ltd. |