CN204699694U - Hydrometallurgy horizontal multi-stage reactor - Google Patents
Hydrometallurgy horizontal multi-stage reactor Download PDFInfo
- Publication number
- CN204699694U CN204699694U CN201520198485.XU CN201520198485U CN204699694U CN 204699694 U CN204699694 U CN 204699694U CN 201520198485 U CN201520198485 U CN 201520198485U CN 204699694 U CN204699694 U CN 204699694U
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- China
- Prior art keywords
- cylindrical shell
- upper plate
- chin spoiler
- inner barrel
- deflector group
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Abstract
Hydrometallurgy horizontal multi-stage reactor, comprises cylindrical shell, and described cylindrical shell side is provided with charging aperture, opposite side is provided with discharging opening, both sides, outside are also provided with end socket, and top is provided with multiple equally distributed agitating device, and agitating device runs through cylindrical shell upper surface and stretches into inner barrel; Be provided with deflector group between two agitating devices, be uniformly distributed between each deflector group; Described deflector group comprises preceding baffle upper plate and posterior chin spoiler; Described baffle upper plate is while be connected with periphery in inner barrel is vertical, another side opening, described chin spoiler is connected with periphery under inner barrel is vertical, another side opening, therebetween be S-typely interspersed, length is all greater than cylindrical shell radius and is less than barrel diameter.The utility model has the advantages that: the setting of deflector group makes to form multiple bin in reactor, and be both convenient to material and evenly, be fully stirred, be heated, react, and be convenient to again material and flow between bin, there is not reaction dead zone, reaction effect is good.
Description
Technical field
The utility model relates to a kind of reactor, specifically a kind of hydrometallurgy horizontal multi-stage reactor.
Background technology
Early stage reactor, also exist material stirring be heated uneven, react insufficient and material flow moment, respond the problems such as dead band, cause manufacturing the process-cycle long, cost of investment is high, effective rate of utilization and year running rate low.
Traditional hydrometallurgy process, is adopt flame direct-fired mode, not only cost is high, fuel consume is large, cause the wasting of resources, and produce a large amount of chemical wastewater, serious environment pollution.
Utility model content
For the deficiency that above-mentioned technical problem exists, the purpose of this utility model is to provide a kind of hydrometallurgy horizontal multi-stage reactor.
The technical solution of the utility model is: hydrometallurgy horizontal multi-stage reactor, comprise cylindrical shell, described cylindrical shell side is provided with charging aperture, and opposite side is provided with discharging opening, described cylindrical shell top is provided with multiple equally distributed agitating device, and agitating device runs through cylindrical shell upper surface and stretches into inner barrel; Be provided with deflector group between described inner barrel two agitating devices, be uniformly distributed between each deflector group; Described deflector group comprises baffle upper plate and chin spoiler, and baffle upper plate is front, and chin spoiler is rear; Described baffle upper plate is while be connected with periphery in inner barrel is vertical, another side opening, and described chin spoiler is connected with periphery under inner barrel is vertical, another side opening, S-typely between baffle upper plate and chin spoiler is interspersed.
Further, the length of described baffle upper plate and chin spoiler is all greater than cylindrical shell radius and is less than barrel diameter.
Further, outside described cylindrical shell, both sides are also provided with end socket.
Adopt above technical scheme, compared with prior art, the utility model has the advantages that: between inner barrel two agitating devices, deflector group is set, baffle upper plate is front, chin spoiler, rear, to be S-typely interspersed, and material can either be made fully to be stirred, to be heated, to react, be convenient to again material flow between deflector, there is not reaction dead zone; Adopt multiple agitating device and deflector group, repeatedly can stir material, heat, material is fully stirred further, is heated, reacts; Being uniformly distributed of agitating device and deflector group, material mean allocation can be ensured, to sum up state, the setting of deflector group makes to form multiple bin in reactor, by the mode of coupling, shortens the process-cycle, reduce cost of investment, improve effective rate of utilization and year running rate, expand treatment scale, achieve continuous seepage.In addition, in reactor, complete metallurgical process, cost is low, fuel consume is little, chemical wastewater can recycling, both economizes on resources, free from environmental pollution again, environmental protection.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is side structure schematic diagram of the present utility model.
Wherein: 1, cylindrical shell, 2, agitating device, 3, charging aperture, 4, discharging opening, 5, baffle upper plate, 6, chin spoiler, 7, end socket.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
As shown in drawings, hydrometallurgy horizontal multi-stage reactor of the present utility model, comprise cylindrical shell 1, described cylindrical shell 1 side is provided with charging aperture 3, opposite side is provided with discharging opening 4, described cylindrical shell 1 top is provided with multiple equally distributed agitating device 2, and agitating device 2 runs through cylindrical shell 1 upper surface and stretches into cylindrical shell 1 inside; Be provided with deflector group between inner two agitating devices 2 of described cylindrical shell 1, be uniformly distributed between each deflector group; Described deflector group comprises baffle upper plate 5 and chin spoiler 6, and baffle upper plate 5 is front, and chin spoiler 6 is rear; Described baffle upper plate 5 while upper periphery is vertical is connected with cylindrical shell 1 inside, another side opening, described chin spoiler 6 is connected with in cylindrical shell 1, subordinate's periphery is vertical, another side opening, S-typely between baffle upper plate 5 and lower water conservancy diversion 6 is interspersed; The length of described baffle upper plate 5 and chin spoiler 6 is all greater than cylindrical shell 1 radius and is less than cylindrical shell 1 diameter; Outside described cylindrical shell 1, both sides are also provided with end socket 7.
The course of work of the present utility model is: under at reactor heat energy being delivered to indirectly the prerequisite in cylindrical shell 1, material enters from charging aperture 3, and the part entered at first is stirred by the agitating device 2 in first region, is fully heated, reacts; Along with material continue enter, insufficient space in first region, because baffle upper plate 5 at front, chin spoiler 6 rear, S-typely to be interspersed, be in first region inner bottom part, be fully stirred material by thermal response, can only be overflowed by the gap between baffle upper plate 5 and chin spoiler 6, from the top of chin spoiler 6 out, fall in next region, continue to be stirred by the agitating device 2 in next region, be fully heated, react.The like, this part material constantly repeats identical process, be stirred, be heated, react, overflow, enter next region, be stirred again, be heated, react, overflow, enter next region, until enter last region, after stirring, heat, reacting, from discharging opening 4 out.
And having arrived next region due to the part entered at first, bottom just fallen by the material above in first region, stirred, is fully heated, reacts by the agitating device 2 in this region; Along with material continue enter, also can only be overflowed by gap between baffle upper plate 5 and chin spoiler 6, from the top of chin spoiler 6 out, fall in next region, continue to be stirred by the agitating device 2 in next region, be fully heated, react.As can be seen here, the material that every part is come in all will constantly repeat identical process, namely the material vacating space of bottom is positioned at before waiting in this region, just can fall bottom, be stirred, be heated, react, overflow and step down, enter next region, the material vacating space of bottom is positioned at, until out before again waiting in this region.
Claims (3)
1. hydrometallurgy horizontal multi-stage reactor, comprise cylindrical shell, described cylindrical shell side is provided with charging aperture, opposite side is provided with discharging opening, described cylindrical shell top is provided with multiple equally distributed agitating device, and agitating device runs through cylindrical shell upper surface and stretches into inner barrel, it is characterized in that, be provided with deflector group between described inner barrel two agitating devices, be uniformly distributed between each deflector group; Described deflector group comprises baffle upper plate and chin spoiler, and baffle upper plate is front, and chin spoiler is rear; Described baffle upper plate is while be connected with periphery in inner barrel is vertical, another side opening, and described chin spoiler is connected with periphery under inner barrel is vertical, another side opening, S-typely between baffle upper plate and chin spoiler is interspersed.
2. hydrometallurgy horizontal multi-stage reactor according to claim 1, is characterized in that, the length of described baffle upper plate and chin spoiler is all greater than cylindrical shell radius and is less than barrel diameter.
3. hydrometallurgy horizontal multi-stage reactor according to claim 1, it is characterized in that, outside described cylindrical shell, both sides are also provided with end socket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520198485.XU CN204699694U (en) | 2015-04-03 | 2015-04-03 | Hydrometallurgy horizontal multi-stage reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520198485.XU CN204699694U (en) | 2015-04-03 | 2015-04-03 | Hydrometallurgy horizontal multi-stage reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204699694U true CN204699694U (en) | 2015-10-14 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520198485.XU Expired - Fee Related CN204699694U (en) | 2015-04-03 | 2015-04-03 | Hydrometallurgy horizontal multi-stage reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204699694U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111411225A (en) * | 2020-04-29 | 2020-07-14 | 沈阳工业大学 | Method for leaching laterite-nickel ore and separating nickel |
| CN111498882A (en) * | 2020-04-29 | 2020-08-07 | 沈阳工业大学 | Method for preparing coarse-particle aluminum hydroxide from aluminum ammonium sulfate solution |
-
2015
- 2015-04-03 CN CN201520198485.XU patent/CN204699694U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111411225A (en) * | 2020-04-29 | 2020-07-14 | 沈阳工业大学 | Method for leaching laterite-nickel ore and separating nickel |
| CN111498882A (en) * | 2020-04-29 | 2020-08-07 | 沈阳工业大学 | Method for preparing coarse-particle aluminum hydroxide from aluminum ammonium sulfate solution |
| CN111411225B (en) * | 2020-04-29 | 2022-06-24 | 沈阳工业大学 | Method for leaching and separating nickel from laterite-nickel ore |
| CN111498882B (en) * | 2020-04-29 | 2022-10-25 | 沈阳工业大学 | Method for preparing coarse-particle aluminum hydroxide from aluminum ammonium sulfate solution |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151014 Termination date: 20170403 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |