CN202606053U - Totally-closed static pipeline continuous precipitation system for rear earth precipitation and transformation - Google Patents
Totally-closed static pipeline continuous precipitation system for rear earth precipitation and transformation Download PDFInfo
- Publication number
- CN202606053U CN202606053U CN 201220251860 CN201220251860U CN202606053U CN 202606053 U CN202606053 U CN 202606053U CN 201220251860 CN201220251860 CN 201220251860 CN 201220251860 U CN201220251860 U CN 201220251860U CN 202606053 U CN202606053 U CN 202606053U
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- Prior art keywords
- pipeline
- static
- totally
- precipitation
- discharging opening
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- 230000003068 static Effects 0.000 title claims abstract description 42
- 238000001556 precipitation Methods 0.000 title claims abstract description 27
- 230000001131 transforming Effects 0.000 title abstract 3
- 238000007599 discharging Methods 0.000 claims abstract description 28
- 239000000463 material Substances 0.000 claims abstract description 11
- 229910052761 rare earth metal Inorganic materials 0.000 claims description 17
- 150000002910 rare earth metals Chemical class 0.000 claims description 17
- 239000007788 liquid Substances 0.000 claims description 12
- 238000001816 cooling Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000003153 chemical reaction reagent Substances 0.000 claims description 4
- 230000001376 precipitating Effects 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 abstract description 12
- 238000002156 mixing Methods 0.000 abstract description 9
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 239000003814 drug Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 9
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 230000005591 charge neutralization Effects 0.000 description 1
- 238000005039 chemical industry Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000001264 neutralization Effects 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000000505 pernicious Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
Abstract
The utility model relates to a totally-closed static pipeline continuous precipitation system for rear earth precipitation and transformation and belongs to the field of chemical devices. A discharging port is arranged on the lower portion of a feed tank, the discharging port is connected with a feeding port which is arranged on a circulating pump through a conveying pipe, a discharging port on the circulating pump is connected a feeding port of static pipeline mixers through the conveying pipe, a discharging port of the static pipeline mixers is connected with a pipeline gas distribution bag through a pipeline, and a medicine adding port on at least one static pipeline mixer is connected with a discharging port on a precipitation agent tank through a conveying pipeline. By the aid of the system, best conditions such as the mixing efficiency, the reaction temperature and the time in a totally-closed device are achieved. Best reaction environment is provided for a rear earth precipitation and transformation reaction, the reaction rate of materials is improved, the gas generated from chemical reactions enters an exhaust gas treatment system through the gas distribution bag and is used intensively, the use rate of resources is improved, the pollution to the environment is reduced to the lowest, the system uses small devices such as pumps and pipelines, and the occupied area of devices is reduced greatly.
Description
Technical field
The utility model relates to a kind of totally-enclosed static pipeline continuous precipitation system that is used for rare-earth precipitation transition, is specially adapted to the rare-earth precipitation environment protection energy-saving equipment of transition, belongs to the chemical industry equipment field.
Background technology
The at present domestic deposition mixing apparatus that is used for rare-earth precipitation transition is general to adopt common uncovered retort to be equipped with propeller mixer, turbine agitator or anchor agitator; Common shortcoming below these deposition mixing apparatus all exist: 1) mixed area is big; Mixing efficiency is low, and the rare-earth precipitation rate is low; 2) reaction time long, production stability is poor, energy consumption is big; 3) floor space is big; 4) operation expense is high; 5) the fixed investment cost is bigger; 6) manipulation strength is high.And these deposition mixing apparatus all adopt open operation, and the pernicious gas that produces in the production process has greatly destroyed production environment, and simultaneously above mixing apparatus all belongs to the formation that the point type implement is unfavorable for the streamlined operation.
Summary of the invention
The purpose of the utility model is to provide that a kind of rare earth mixing efficiency is high, settling velocity is fast, environmental protection, energy-conservation a kind of totally-enclosed static pipeline continuous precipitation system that is used for rare-earth precipitation transition.
Technical solution
The utility model comprises material liquid tank; The material liquid tank bottom is provided with discharging opening; Discharging opening connects through the charging aperture on the conveying pipeline circulating pump; Discharging opening on the circulating pump is connected with static pipe-line mixer charging aperture through conveying pipeline, and static pipe-line mixer discharging opening divides gas bag to be connected through pipeline and pipeline, and the dosing mouth at least one static pipe-line mixer passes through feeding pipe and is connected with the discharging opening of precipitating reagent jar.
At least three series connection of said static pipe-line mixer become the one-level array.
The said static pipe-line mixer array of one-level that on the conveying pipeline of material liquid tank discharging opening, is provided with at least.
Said static pipe-line mixer discharging opening divides gas bag to be connected through cooling or heating muff with pipeline.
Discharging opening conveying pipeline on the utility model circulating pump and pipeline divide gas bag to be provided with static pipe-line mixer; Rare earth feed liquid is mixed in static pipeline with precipitating reagent; The mixing efficiency 3-5 times of rare-earth precipitation rate that can improve material is increased to more than 98%; Reaction time foreshortens to about 3 minutes and has realized that serialization production has improved production stability and cut down the consumption of energy about 80% simultaneously; Reduce occupation area of equipment more than 80%, reduce about 20% of fixed investment to former basis, adopt totally enclosed type production procedure realization unmanned streamlined complete operation not have gas and overflow.
The utility model is an a kind of totally-enclosed static pipeline continuous precipitation system; Taking system decomposition is recycle feed, successive reaction two-part structure; Divide at static pipe-line mixer and pipeline and to be provided with cooling or heating muff between the gas bag; Make and realize conditions such as The Best Mixed efficient, reaction temperature, time in the full closeding equipment, be the rare-earth precipitation reactivity that transition, reaction provided the optimum response environment to improve material, the gas that chemical reaction is generated gets into the exhaust treatment system focus utilization through dividing gas bag; Improved the utilization rate of resource; The pollution of environment has been dropped to minimum, total system all adopts mini-plants such as pump and pipeline, has greatly reduced the floor space of equipment.
Description of drawings
Fig. 1 is the utility model structural representation.
The specific embodiment
The utility model material liquid tank 1 bottom is provided with discharging opening; Discharging opening is connected with charging aperture on the one-level circulating pump 3 through one-level conveying pipeline 2; Discharging opening on the one-level circulating pump 3 is connected through the charging aperture flange of first static pipe-line mixer in the static pipe-line mixer array 5 of one-level of secondary conveying pipeline 4 and three static pipe-line mixer series connection formation; The discharging opening of last the static pipe-line mixer in the static pipe-line mixer array 5 of one-level divides gas bag 7 to be connected through cooling or heating muff 6 with pipeline, and pipeline divides gas bag 7 discharging openings to be connected to plate and frame filter press 8 imports; Pipeline divides the exhaust outlet of gas bag 7 to be connected to exhaust gas recovery system; Dosing mouth at least one the static pipe-line mixer in the static pipe-line mixer array 5 of one-level is connected with the discharging opening of precipitating reagent jar 9 through three grades of feeding pipes.
The course of work:
Rare earth feed liquid in the material liquid tank gets into one-level circulating pump 3 through defeated batch can 1; Get in first static pipe-line mixer in the static pipe-line mixer array 5 of one-level through 3 dischargings of one-level circulating pump, defeated batch can 1; Rare earth feed liquid is through the abundant mixing of the static pipe-line mixer array 5 of one-level; Getting into pipeline through cooling or heating muff 6 divides gas bag 7 to connect; Divide gas bag 7 discharging openings to deliver to plate and frame filter press 8 imports through pipeline, the utility model rare earth feed liquid has realized that through uninterrupted entering reaction system serialization production has improved usage ratio of equipment.Pipeline divides the exhaust outlet of gas bag 7 to be connected to exhaust gas recovery system; The gas that reaction in the mixed process is generated is concentrated and is recycled to the recycling that neutralization that exhaust treatment system is used for acid gas has realized resource to greatest extent, has eliminated reaction and has generated the pollution of gas to production environment.
The static pipe-line mixer array of the utility model 5 needs according to production product expand to static pipe-line mixer array more than the secondary, and last of each array static pipe-line mixer discharging opening and pipeline divide gas bag 7 to be connected to form totally-enclosed static pipeline continuous precipitation system.
Claims (4)
1. totally-enclosed static pipeline continuous precipitation system that is used for rare-earth precipitation transition; Comprise material liquid tank, it is characterized in that the material liquid tank bottom is provided with discharging opening; Discharging opening connects through the charging aperture on the conveying pipeline circulating pump; Discharging opening on the circulating pump is connected with static pipe-line mixer charging aperture through conveying pipeline, and static pipe-line mixer discharging opening divides gas bag to be connected through pipeline and pipeline, and the dosing mouth at least one static pipe-line mixer passes through feeding pipe and is connected with the discharging opening of precipitating reagent jar.
2. a kind of totally-enclosed static pipeline continuous precipitation system that is used for rare-earth precipitation transition according to claim 1 is characterized in that at least three series connection of static pipe-line mixer become the one-level array.
3. a kind of totally-enclosed static pipeline continuous precipitation system that is used for rare-earth precipitation transition according to claim 1 is characterized in that, the static pipe-line mixer array of one-level is set on the conveying pipeline of material liquid tank discharging opening at least.
4. a kind of totally-enclosed static pipeline continuous precipitation system that is used for rare-earth precipitation transition according to claim 1 is characterized in that said static pipe-line mixer discharging opening divides gas bag to be connected through cooling or heating muff with pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220251860 CN202606053U (en) | 2012-05-20 | 2012-05-20 | Totally-closed static pipeline continuous precipitation system for rear earth precipitation and transformation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220251860 CN202606053U (en) | 2012-05-20 | 2012-05-20 | Totally-closed static pipeline continuous precipitation system for rear earth precipitation and transformation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202606053U true CN202606053U (en) | 2012-12-19 |
Family
ID=47339786
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220251860 Expired - Fee Related CN202606053U (en) | 2012-05-20 | 2012-05-20 | Totally-closed static pipeline continuous precipitation system for rear earth precipitation and transformation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202606053U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110306041A (en) * | 2018-07-26 | 2019-10-08 | 安徽金三隆再生资源有限公司 | A kind of continuous device for making of rare earth compound precipitating |
| CN113213520A (en) * | 2021-05-10 | 2021-08-06 | 清华大学 | Method and system for continuously preparing nano barium sulfate |
-
2012
- 2012-05-20 CN CN 201220251860 patent/CN202606053U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110306041A (en) * | 2018-07-26 | 2019-10-08 | 安徽金三隆再生资源有限公司 | A kind of continuous device for making of rare earth compound precipitating |
| CN113213520A (en) * | 2021-05-10 | 2021-08-06 | 清华大学 | Method and system for continuously preparing nano barium sulfate |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121219 Termination date: 20160520 |