CN201455265U - Combined zinc-powder production condensing device - Google Patents
Combined zinc-powder production condensing device Download PDFInfo
- Publication number
- CN201455265U CN201455265U CN2009201114004U CN200920111400U CN201455265U CN 201455265 U CN201455265 U CN 201455265U CN 2009201114004 U CN2009201114004 U CN 2009201114004U CN 200920111400 U CN200920111400 U CN 200920111400U CN 201455265 U CN201455265 U CN 201455265U
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- Prior art keywords
- condenser
- water
- pipe
- parallel
- cold
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- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title claims abstract description 42
- 238000004519 manufacturing process Methods 0.000 title abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 238000001816 cooling Methods 0.000 claims abstract description 20
- 239000011701 zinc Substances 0.000 claims description 12
- 229910052725 zinc Inorganic materials 0.000 claims description 12
- 239000003517 fume Substances 0.000 claims description 11
- 239000000498 cooling water Substances 0.000 claims description 6
- 238000007789 sealing Methods 0.000 claims description 6
- 241000005139 Lycium andersonii Species 0.000 claims description 3
- 238000004891 communication Methods 0.000 claims description 3
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000002425 crystallisation Methods 0.000 description 12
- 230000008025 crystallization Effects 0.000 description 6
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000010010 raising Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
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Abstract
The utility model discloses a combined zinc-powder production condensing device comprising a zinc-powder steam inlet pipe (2), a condenser (3), a parallel water segregator (4), an outer circulation water cooling system (7) and a zinc-powder collection excluder (8), wherein the condenser (3) is provided with a water-sleeve type cold wall (9), a seal cold roof (11) is arranged in the condenser (3), the top of the seal cold roof (11) is provided with the parallel water segregator (4), the parallel water segregator (4) is communicated with the outer circulation water cooling system (7) through a circulation water inlet pipe (5) and a circulation water return pipe (6), a cold roof seal pipe (10) and a seal cover (14) are sealed by cold water and are communicated with the seal cold roof (11), and condensing pipes (13) are connected in parallel with a combined condensing pipe array. The internal-circulation condensing pipe array structure of the utility model shortens a condensing route and improves a condensing and crystallizing environmental condition in a condensing and crystallizing area, and the circulating and cooling efficiency is improved by 10 times in the same cold surface area and within the same time. The combined zinc-powder production condensing device has compact structure, even temperature distribution and high direct yield and is safe and reliable to maintain and replace, and the produced zinc powder is not easy to reunite.
Description
Technical field
The utility model belongs to chemical metallurgy condensing plant technical field, particularly relates to a kind of combined type zinc powder and produces condensing unit.
Background technology
At present, the zinc powder condenser of prior art is established the shell-and-tube cooler of disc type cooling tube in being mostly, and condenser shell surface contact with the high temperature zinc fume, when exchange heat energy is realized lowering the temperature, gets rid of behind the crystallization generation solid zinc powder.The intercooler of this condenser is connected with series system with outer cooling water circulation of cooling off between the pond to be realized.Because it is very high to enter the zinc fume temperature of condenser, although strengthened the condensation area and the quantity of circulating water of condenser, but the long path structure of condenser pipe, cause producing in the condenser phenomenon uneven in temperature, prolonged the time of zinc powder crystallization, zinc powder often occurs and reunite, influenced the quality and the rate of recovery of zinc powder, reduced system-wide operating efficiency.For this reason, the design people has developed a kind of combined type zinc powder and has produced condensing unit through long term test research, has overcome the deficiencies in the prior art.Evidence, effect is good.
The utility model content
The purpose of this utility model is to provide a kind of condensation-crystallization district variations in temperature little, and it is quick and convenient that temperature is adjusted, and does not have cold and hot point, and the combined type zinc powder that helps to increase the zinc fume phase driving force produces condensing unit.
The purpose of this utility model is achieved in that and comprises zinc powder vapour inlet pipe, condenser, water knockout drum in parallel, outer circulation water cooling system and zinc powder are collected ejector, described condenser is provided with the zinc fume inlet tube, condenser is provided with the cold wall of water-jacket typ, the cold top of tank seal is set in the condenser, tank seal Leng Ding top is provided with water knockout drum in parallel, water knockout drum in parallel passes through circulating water inlet, the recirculated water return pipe is communicated with the outer circulation water-cooling apparatus, water knockout drum in parallel by distributive pipe with make up that feed pipe links in the condenser pipe, the combination condenser pipe is arranged in parallel into combination condenser pipe array, and interior circulating condensing pipe top seals cold top by seal closure and condenser tank and is connected by tank seal.
Because circulating condensing pipe array architecture in the utility model adopts has shortened the condensation path, has improved the condensation-crystallization environmental condition the condensation-crystallization district in, at identical cold surface in long-pending and time, tens of times of circulation cooling effectiveness raisings; Have compact conformation, uniformity of temperature profile, crystallization kinetics and trickle crystal forming process tend to be reasonable, and the zinc powder of production is difficult for reuniting the direct yield height; Safeguard and change, safe and reliable.
Description of drawings
The utility model is described in further detail below in conjunction with accompanying drawing, but never in any form the utility model is limited.
Fig. 1 partly cuts open schematic diagram for the utility model overall structure.
Fig. 2 is that the AA of Fig. 1 is to view.
Among the figure: 1-zinc evaporimeter, 2-zinc fume inlet tube, 3-condenser, 4-water knockout drum in parallel, the 5-circulating water inlet, 6-recirculated water return pipe, 7-outer circulation water-cooling apparatus, the 8-zinc powder is collected ejector, the cold wall of 9-water-jacket typ, 10-tank seal pipe, 11 water tank types seal cold top; Periodical feeding pipe in the 12-, 13-condenser pipe, 14-condenser pipe seal closure.
The specific embodiment
As Fig. 1, shown in Figure 2, the utility model comprises zinc powder vapour inlet pipe 2, condenser 3, water knockout drum 4 in parallel, outer circulation water cooling system 7 and zinc powder are collected ejector 8, described condenser 3 is provided with zinc fume inlet tube 2, condenser 3 is provided with the cold wall 9 of water-jacket typ, water tank type is set in the condenser 3 seals cold top 11, water tank type seals 11 tops, cold top water knockout drum 4 in parallel is set, water knockout drum 4 in parallel is by circulating water inlet 5, recirculated water return pipe 6 is communicated with outer circulation water-cooling apparatus 7, condenser 3 bottoms are provided with zinc powder and collect ejector 8, tank seal pipe 10 is tightly connected by the cooling water that water tank type seals in the cold top 11 with condenser pipe seal closure 14, and condenser pipe 13 is arranged in parallel into combination condenser pipe array.
Combination can with outer circulation water-cooling apparatus 7 separate connection or multitube parallel be connected described condenser pipe, or the multitube series-parallel connection connects.
The operation principle of the present utility model and the course of work:
The high temperature zinc fume directly enters by condenser tank from zinc fume inlet tube 2 and seals the zinc powder condensation-crystallization district that cold top 11, the cold wall 9 of water jacket and condenser pipe array constitute, under the effect of pressure and temperature, high temperature zinc fume stream is by combination condenser pipe array, each condensation, through overheated transmission, heat radiation, thermal convection current heat-shift, heat is taken out of by inside and outside recirculated cooling water immediately, quickened the zinc fume fast cooling, the solid zinc powder that crystallization is good is discharged collection after sedimentation is collected ejector by zinc powder.Described seal closure 14 had both played the sealing function of condenser pipe, the explosion relief valve when also being the rising of condenser internal pressure.
On the described water tank sealed tube is arranged, both as the cold top of condenser, the water seal of conduct combination condenser pipe again was again as the water seal of condenser explosion-proof pressure for water tank.By one or one group of water knockout drum in parallel and each combination condenser pipe parallel connection, the recirculated water return pipe is concentrated to be returned outside the outer circulation water-cooling apparatus from sealing cold top from the water of outer circulation water-cooling apparatus.
Characteristics of the present utility model:
1, compare with prior art shell-and-tube coil pipe zinc powder condenser, the utility model has shortened the path of condenser pipe greatly, and in long-pending and time, circulating cooling efficient is than the high several times of prior art, and even decades of times at identical cold surface; Leaf has improved the condensation-crystallization environmental condition in the condensation-crystallization district simultaneously.
2, have simple in structure, compactness, variations in temperature is little and be evenly distributed, and has region-wide fast cold mechanism and cooling trend from the bottom to top, crystallization kinetics and trickle Crystallization process tend to be reasonable, zinc powder is difficult for reuniting the direct yield height.
3, the combination condenser pipe maintains easily replacing, and the sealing means of combination condenser pipe and condenser can be opened, automatically for condenser provides extra safety measure when the condenser internal pressure raises.
Claims (3)
1. a combined type zinc powder is produced condensing unit, comprise zinc powder steam inlet tube (2), condenser (3), water knockout drum (4) in parallel, outer circulation water cooling system (7) and zinc powder are collected ejector (8), described condenser (3) is provided with zinc fume inlet tube (2), condenser (3) bottom is provided with zinc powder and collects ejector (8), it is characterized in that: condenser (3) is provided with the cold wall of water-jacket typ (9), sealing cold top (11) is set in the condenser (3), seal top, cold top (11) water knockout drum in parallel (4) is set, water knockout drum in parallel (4) is by circulating water inlet (5), recirculated water return pipe (6) is communicated with outer circulation water-cooling apparatus (7), cold top sealed tube (10) seals the cold top of communication seals (11) with seal closure (14) by cooling water, the condenser pipe array of condenser pipe (13) combination in parallel.
2. combined type zinc powder as claimed in claim 1 is produced condensing unit, it is characterized in that: described condenser pipe combination comprises: interior periodical feeding pipe (12) and condenser pipe (13), interior periodical feeding pipe (12) top is communicated with water knockout drum in parallel (4), interior periodical feeding pipe (12) bottom extend into condenser pipe (13) bottom, condenser pipe (13) top is communicated with condenser pipe seal closure (14), and cold top sealed tube (10) is by the cooling water sealing cold top of communication seals (11).
3. combined type zinc powder as claimed in claim 1 is produced condensing unit, it is characterized in that: combination can with outer circulation water-cooling apparatus (7) separate connection or multitube parallel be connected each condenser pipe as required, or the multitube series-parallel connection connects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201114004U CN201455265U (en) | 2009-05-19 | 2009-05-19 | Combined zinc-powder production condensing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201114004U CN201455265U (en) | 2009-05-19 | 2009-05-19 | Combined zinc-powder production condensing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201455265U true CN201455265U (en) | 2010-05-12 |
Family
ID=42382615
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009201114004U Expired - Fee Related CN201455265U (en) | 2009-05-19 | 2009-05-19 | Combined zinc-powder production condensing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201455265U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105372874A (en) * | 2015-11-14 | 2016-03-02 | 合肥骇虫信息科技有限公司 | Liquid crystal module set with uniformed brightness |
| CN107218809A (en) * | 2016-12-30 | 2017-09-29 | 郴州万墨环保科技有限公司 | A kind of many metal distillation temperature control condensed components evaporate single crude product vacuum drying oven |
| CN107964487A (en) * | 2016-10-19 | 2018-04-27 | 南京九溪生物科技有限公司 | A kind of circulating cooling type brewing device |
| CN114918419A (en) * | 2022-04-26 | 2022-08-19 | 广东长信精密设备有限公司 | Circulating cooling structure of sublimation furnace condenser and cooling method thereof |
| CN115028182A (en) * | 2022-06-23 | 2022-09-09 | 多氟多（昆明）科技开发有限公司 | Production facility based on electrolytic aluminum fluorine-containing waste residue manufacturing and processing cryolite |
-
2009
- 2009-05-19 CN CN2009201114004U patent/CN201455265U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105372874A (en) * | 2015-11-14 | 2016-03-02 | 合肥骇虫信息科技有限公司 | Liquid crystal module set with uniformed brightness |
| CN107964487A (en) * | 2016-10-19 | 2018-04-27 | 南京九溪生物科技有限公司 | A kind of circulating cooling type brewing device |
| CN107218809A (en) * | 2016-12-30 | 2017-09-29 | 郴州万墨环保科技有限公司 | A kind of many metal distillation temperature control condensed components evaporate single crude product vacuum drying oven |
| CN114918419A (en) * | 2022-04-26 | 2022-08-19 | 广东长信精密设备有限公司 | Circulating cooling structure of sublimation furnace condenser and cooling method thereof |
| CN114918419B (en) * | 2022-04-26 | 2024-03-26 | 广东长信精密设备有限公司 | Circulation cooling structure of sublimation furnace condenser and cooling method thereof |
| CN115028182A (en) * | 2022-06-23 | 2022-09-09 | 多氟多（昆明）科技开发有限公司 | Production facility based on electrolytic aluminum fluorine-containing waste residue manufacturing and processing cryolite |
| CN115028182B (en) * | 2022-06-23 | 2022-11-25 | 多氟多（昆明）科技开发有限公司 | Production facility based on electrolytic aluminum fluorine-containing waste residue manufacturing and processing cryolite |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Qiaojia Xin Xin Resources Recycling Co., Ltd. Assignor: Fang Xi|Peng Bo Contract record no.: 2010530000053 Denomination of utility model: Combined zinc-powder production condensing device Granted publication date: 20100512 License type: Exclusive License Record date: 20101008 |
|
| EM01 | Change of recordation of patent licensing contract |
Change date: 20101021 Contract record no.: 2010530000053 Assignee after: Qiaojia Aoxin Resource Recycling Co., Ltd. Assignee before: Qiaojia Xin Xin Resources Recycling Co., Ltd. |
|
| ASS | Succession or assignment of patent right |
Free format text: FORMER OWNER: PENG BO Effective date: 20120926 Owner name: YUNNAN CHUANGXIN ENVIRONMENTAL RESOURCE TECHNOLOGY Free format text: FORMER OWNER: FANG XI Effective date: 20120926 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20120926 Address after: 650041 No. 229 Dongfeng Dongfeng Road, Yunnan, 3, attached to Kunming Patentee after: Yunnan Chuangxin environment resource science and Technology Co Ltd Address before: Kunming City, Yunnan province 650041 Dongfeng East Road, No. 229 Boye metallurgy chemical engineering company Patentee before: Fang Xi Patentee before: Peng Bo |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100512 Termination date: 20150519 |
|
| EXPY | Termination of patent right or utility model |