CN203469962U - Internal-reflux-type garbage removing system - Google Patents
Internal-reflux-type garbage removing system Download PDFInfo
- Publication number
- CN203469962U CN203469962U CN201320567964.5U CN201320567964U CN203469962U CN 203469962 U CN203469962 U CN 203469962U CN 201320567964 U CN201320567964 U CN 201320567964U CN 203469962 U CN203469962 U CN 203469962U
- Authority
- CN
- China
- Prior art keywords
- temperature evaporator
- garbage
- stainless steel
- particle
- removing system
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- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
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- 239000002245 particle Substances 0.000 claims abstract description 23
- 239000011261 inert gas Substances 0.000 claims abstract description 8
- 229910001220 stainless steel Inorganic materials 0.000 claims description 15
- 239000010935 stainless steel Substances 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 238000009413 insulation Methods 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 2
- 239000002994 raw material Substances 0.000 description 6
- 239000000843 powder Substances 0.000 description 5
- 238000001816 cooling Methods 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- -1 as heating source Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000004525 petroleum distillation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
Images
Abstract
The utility model discloses an internal-reflux-type garbage removing system. The internal-reflux-type garbage removing system comprises a high-temperature evaporator, wherein a crucible is arranged at the lower part of the high-temperature evaporator; an inert gas valve is arranged at the bottom of the high-temperature evaporator; a plasma gun is arranged at the upper part of the high-temperature evaporator; an opening of the high-temperature evaporator is connected with a particle controller; a cold condensing tube wraps the outer part of the particle controller; a product outlet and a garbage outlet are formed in the particle controller; the product outlet is connected with a particle collector; the garbage outlet is connected with an inlet of the high-temperature evaporator by a pipeline. Compared with the prior art, the internal-reflux-type garbage removing system has the advantages that the garbage outlet of the garbage removing system does not need to be equipped with a garbage can and a stabbing rod; garbage generated by the garbage removing system is directly conveyed into the crucible of the high-temperature evaporator, and is heated, molten and refluxed, so that utilization rate of materials is improved, and production cost is lowered.
Description
Technical field
The utility model relates to a kind of except garbage system, and specifically a kind of interior reverse-flow type is except garbage system.
Background technology
At present, aspect fine chemistry industry and petroleum distillation, especially in evaporative condenser process, due to the difference of the molten boiling point of material itself, the speed of evaporation is also different, cause certain product powder rate is low, increase the production cost of product.For avoiding blocking pipeline, most of rectifying or other equipment often adopt external reflux type design.But the equipment that the design of external reflux type needs is more, and the recycling rate of raw material is very low.
Summary of the invention
The problem existing for above-mentioned prior art, the utility model provides a kind of interior reverse-flow type except garbage system, can effectively improve the utilization rate of raw material, reduces production costs.
To achieve these goals, a kind of interior reverse-flow type of the present utility model, except garbage system, comprises high-temperature evaporator, its underpart arranges crucible, the bottom of high-temperature evaporator is provided with inert gas valve, and its top arranges plasma gun, and high-temperature evaporator opening connects particle controller; Poly-cold pipe is wrapped in the outside of particle controller, and particle controller is provided with products export and garbage outlet, and products export is connected with particle collector, and garbage outlet is connected with high-temperature evaporator entrance respectively by pipeline.
Further, poly-cold pipe comprises four layers, is followed successively by from inside to outside stay pipe, heat-insulation layer, stainless steel I and stainless steel II, between stainless steel I and stainless steel II, is provided with cold water circulating system.
Further, the carbon felt tube thickness in heat-insulation layer is no less than 1cm.
The beneficial effects of the utility model are: compared with prior art, should dustbin and tapping pin need not be set except the garbage outlet place of garbage system, the rubbish of its generation is delivered directly in the crucible of high-temperature evaporator, and heat fused refluxes, the utilization rate that has improved raw material, has reduced production cost.
Should be except in garbage system, this poly-cold pipe comprises four layers from inside to outside, wherein between two stainless steel layers, is provided with cold water circulating system, this cold water circulating system gives steam more uniform cooler environment, thereby makes the granularity of powder of cooling formation more even.
Should be except in garbage system, in poly-cold pipe, the thickness of carbon felt pipe is no less than 1cm, has increased the internal diameter size of poly-cold pipe, and better heat preservation is more easily back in high-temperature evaporator rubbish in poly-cold pipe, there will not be choking phenomenon.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of poly-cold pipe in Fig. 1.
In figure: 1, high-temperature evaporator, 2, poly-cold pipe, 3, particle controller, 4, particle collector, 5, stay pipe, 6, heat-insulation layer, 7, stainless steel I, 8, stainless steel II, 9, water inlet, 10, delivery port.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As depicted in figs. 1 and 2, a kind of interior reverse-flow type of the present utility model is except garbage system, comprise high-temperature evaporator 1, its underpart arranges crucible, and the bottom of high-temperature evaporator 1 is provided with inert gas valve, its top arranges plasma gun, high-temperature evaporator 1 opening connects particle controller 3, and poly-cold pipe 2 is wrapped in the outside of particle controller 3, and particle controller 3 is provided with products export and garbage outlet, products export is connected with particle collector 4, and garbage outlet is connected with high-temperature evaporator 1 entrance by pipeline.
The utility model further improves, poly-cold pipe 2 comprises four layers, be followed successively by from inside to outside stay pipe 5, heat-insulation layer 6, stainless steel I 7 and stainless steel II 8, between stainless steel I 7 and stainless steel II 8, be provided with cold water circulating system, this cold water circulating system is provided with water inlet 9 and delivery port 10.This cold water circulating system gives steam more uniform cooler environment, thereby makes the granularity of powder of cooling formation more even.
The utility model further improves, carbon felt tube thickness in heat-insulation layer 6 is no less than 1cm, in this poly-cold pipe 2, the thickness of carbon felt pipe increases, increased the internal diameter size of poly-cold pipe 2, better heat preservation, rubbish in poly-cold pipe 2 is more easily back in high-temperature evaporator 1, there will not be choking phenomenon.
Embodiment: the step of nanosized copper power production and recovery rubbish:
(1) raw material joins in the crucible in high-temperature evaporator 1, after checking that reaction system air-tightness is qualified, reaction system is vacuumized, then open the inert gas valve that is arranged on high-temperature evaporator 1 bottom, reaction system is filled with to inert gas, and making reaction system internal pressure is 100-130KPa;
(2) open the plasma gun be arranged on high-temperature evaporator 1 top, using and produce high frequency plasma gas, as heating source, raw material is carried out to heating evaporation, heating raw materials is formed to steam to fluidized state;
(3) regulate the throughput of inert gas of high-temperature evaporator 1 bottom to 10-60m
3/ h, is transported in the particle controller 3 being communicated with high-temperature evaporator 1 steam evaporating with inert gas flow, under the effect of poly-cold pipe 2, in particle controller 3, steam is through constantly colliding, merge, solidify to form fine particle;
(4) these fine particles, a part is through the cooling nanometer grade powder that becomes, and the particle diameter of this powder is 600-1000nm, with air-flow, is transported in particle collector 4; Another part, through further colliding, merge, be cured as larger particle, becomes rubbish, by pipeline, is recycled to high-temperature evaporator 1 porch.
Claims (3)
- In one kind reverse-flow type except garbage system, comprise high-temperature evaporator (1), its underpart arranges crucible, the bottom of described high-temperature evaporator (1) is provided with inert gas valve, its top arranges plasma gun, described high-temperature evaporator (1) opening connects particle controller (3), it is characterized in that, also comprise poly-cold pipe (2), described poly-cold pipe (2) is wrapped in the outside of particle controller (3), described particle controller (3) is provided with products export and garbage outlet, described products export is connected with particle collector (4), described garbage outlet is connected with high-temperature evaporator (1) entrance by pipeline.
- 2. interior reverse-flow type according to claim 1 is except garbage system, it is characterized in that, described poly-cold pipe (2) comprises four layers, be followed successively by from inside to outside stay pipe (5), heat-insulation layer (6), stainless steel I (7) and stainless steel II (8), between described stainless steel I (7) and stainless steel II (8), be provided with cold water circulating system.
- 3. interior reverse-flow type according to claim 2, except garbage system, is characterized in that, the carbon felt tube thickness in described heat-insulation layer (6) is no less than 1cm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320567964.5U CN203469962U (en) | 2013-09-12 | 2013-09-12 | Internal-reflux-type garbage removing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320567964.5U CN203469962U (en) | 2013-09-12 | 2013-09-12 | Internal-reflux-type garbage removing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203469962U true CN203469962U (en) | 2014-03-12 |
Family
ID=50218380
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320567964.5U Expired - Lifetime CN203469962U (en) | 2013-09-12 | 2013-09-12 | Internal-reflux-type garbage removing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203469962U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022156224A1 (en) * | 2021-01-25 | 2022-07-28 | 钟笔 | Ultrafine powder particle aggregation and cooling tank structure and ultrafine powder particle forming method |
| WO2022156227A1 (en) * | 2021-01-25 | 2022-07-28 | 钟笔 | High-temperature-resistant liquid reflux and air outlet structure for preparing fine powder by gas-phase method |
-
2013
- 2013-09-12 CN CN201320567964.5U patent/CN203469962U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022156224A1 (en) * | 2021-01-25 | 2022-07-28 | 钟笔 | Ultrafine powder particle aggregation and cooling tank structure and ultrafine powder particle forming method |
| WO2022156227A1 (en) * | 2021-01-25 | 2022-07-28 | 钟笔 | High-temperature-resistant liquid reflux and air outlet structure for preparing fine powder by gas-phase method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 223800 Suqian province high tech Development Zone, Jiangshan Road, No. 23, No. Patentee after: JIANGSU BOQIAN NEW MATERIALS STOCK CO.,LTD. Address before: 109, Huashan Road, Suyu Economic Development Zone, Suqian, Jiangsu Patentee before: JIANGSU BOQIAN NEW MATERIALS Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140312 |