CN105087922A - Cyclone separation ammonia total-recycle-type copper mine efficient chemical combination leaching device - Google Patents
Cyclone separation ammonia total-recycle-type copper mine efficient chemical combination leaching device Download PDFInfo
- Publication number
- CN105087922A CN105087922A CN201510637669.6A CN201510637669A CN105087922A CN 105087922 A CN105087922 A CN 105087922A CN 201510637669 A CN201510637669 A CN 201510637669A CN 105087922 A CN105087922 A CN 105087922A
- Authority
- CN
- China
- Prior art keywords
- chemical combination
- combination leaching
- barrel
- tubular shaft
- exhaust purifier
- Prior art date
- 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.)
- Granted
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- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 62
- 239000000126 substance Substances 0.000 title claims abstract description 52
- 238000002386 leaching Methods 0.000 title claims abstract description 51
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 31
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 19
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 19
- 239000010949 copper Substances 0.000 title claims abstract description 19
- 238000000926 separation method Methods 0.000 title claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 46
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 239000007791 liquid phase Substances 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 11
- 238000011084 recovery Methods 0.000 claims description 9
- 239000002826 coolant Substances 0.000 claims description 5
- 238000012856 packing Methods 0.000 claims description 5
- 239000003507 refrigerant Substances 0.000 claims description 5
- 238000009827 uniform distribution Methods 0.000 claims description 5
- 238000003466 welding Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 38
- 238000012546 transfer Methods 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 8
- 239000000463 material Substances 0.000 abstract description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 5
- 239000001301 oxygen Substances 0.000 abstract description 5
- 229910052760 oxygen Inorganic materials 0.000 abstract description 5
- 238000002156 mixing Methods 0.000 abstract description 4
- 238000003756 stirring Methods 0.000 abstract description 3
- 238000004062 sedimentation Methods 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 6
- 239000012071 phase Substances 0.000 description 6
- BWFPGXWASODCHM-UHFFFAOYSA-N copper monosulfide Chemical compound [Cu]=S BWFPGXWASODCHM-UHFFFAOYSA-N 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 230000000903 blocking effect Effects 0.000 description 4
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 238000000151 deposition Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 239000011229 interlayer Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 230000001174 ascending effect Effects 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 238000005202 decontamination Methods 0.000 description 2
- 230000003588 decontaminative effect Effects 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 235000019633 pungent taste Nutrition 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Abstract
The invention discloses a cyclone separation ammonia total-recycle-type copper mine efficient chemical combination leaching device. A chemical combination leaching barrel and a tail gas purifier are connected through a flange. A stirring motor is connected with a conical cover through a hollow shaft and then is inserted in the chemical combination leaching barrel. The conical cover is internally provided with blades and liquid inflow holes. Gas inlets which are evenly formed in the axial circumference are formed in the upper portion of the hollow shaft. After being connected with the hollow pipe shaft, a hydraulic plate arranged in the chemical combination leaching barrel is located on a bottom valve. A jacket is arranged outside the tail gas purifier; a middle pipe and a spiral fin barrel are arranged in the tail gas purifier so that a jacket structure can be formed; and a tail gas purifier outlet is provided with a cyclone separator. Air (oxygen) in the chemical combination leaching barrel is automatically and conveniently supplemented, the liquid flow mixing effect is complete and sufficient, and chemical combination leaching efficiency is very high; material sedimentation and blockage are prevented, and the cyclone separation ammonia total-recycle-type copper mine efficient chemical combination leaching device is convenient to use, reliable and efficient; the tail gas purifier efficiently completes heat transfer and mass transfer in a multi-stage manner, the gas and liquid separation effect is particularly good, ammonia leakage is effectively prevented, copper mine chemical combination leaching can be environment-friendly, automatic and efficient, and important application value is achieved.
Description
Technical field
The present invention relates to the efficient chemical combination leaching device of a kind of cyclonic separation ammonia full recovery type copper mine.
Background technology
The copper mine of occurring in nature has quite a few to be exist with the form of cupric sulfide, cupric sulfide is in the ammonia solution of applicable concentration, enough air are had to blast (mainly oxygen participates in reaction), can complex compound be formed and dissolve, complete chemical combination and after leaching and dissolving, then carry out solid-liquid separation and just can carry out next step operation.
Therefore, the chemical combination leaching device of copper mine is the requisite key equipment of process for copper processed, but existing copper mine chemical combination leaching device exists two large defects, thus constrains the development of copper technology processed.One to be that air blasts insufficient and inconvenient, and the chemical combination leaching velocity of cupric sulfide is slow, efficiency is low, needs to increase special air and blasts equipment, increase equipment investment, also cause unnecessary trouble; Two is that ammonia easily leaks, because ammonia has high pungency, volatile toxic and harmful, thus very large to environmental influence, also very large to the loss of ammonia, if but adopt Sealing Arrangement to react, then the easy security incident such as explosion caused.
Therefore, if the efficient chemical combination leaching device of copper mine that a kind of air automatically conveniently blasts, ammonia is not easy to leak, be not again pressurized vessel can be designed, then there is important actual application value.
Summary of the invention
The technical problem to be solved in the present invention overcomes the deficiencies in the prior art exactly, provides a kind of simple and practical, the efficient chemical combination leaching device of cyclonic separation ammonia full recovery type copper mine that air is automatically convenient to be blasted, ammonia is not easy to leak, be not again pressurized vessel.
For overcoming the deficiencies in the prior art, the present invention takes following technical scheme:
The efficient chemical combination leaching device of a kind of cyclonic separation ammonia full recovery type copper mine, comprise chemical combination leaching barrel and exhaust purifier, it is characterized in that: the intervalve of chemical combination leaching barrel and exhaust purifier is removably connected by flange, exhaust purifier is by upflow tube and return liquid inclined tube and to be linked back chemical combination leaching barrel; Chemical combination leaching barrel is provided with manhole, liquid feed valve and heating jacket, agitator motor inserts in chemical combination leaching barrel after connecting cone cover by tubular shaft, blade and inlet opening is provided with in cone cover, the inlet mouth that tubular shaft top has axle circumference uniform distribution to open, tubular shaft bottom has axle sleeve to play dynamic state limit and stable support function, being provided with the dish that surges in chemical combination leaching barrel and connecting hollow tubular shaft, hollow tubular shaft is provided with axle sleeve and on bottom valve; Exhaust purifier outside is provided with chuck and leads to water coolant or refrigerated water, inside is provided with open intervalve and forms jacket structured with the helical fin cylinder closed, helical fin cylinder is that inwall welding helical fin forms, the gap of helical fin cylinder and exhaust purifier inwall is provided with packing layer, emptying after exhaust purifier outlet connects cyclonic separator, cyclonic separator liquid-phase outlet converges with time liquid inclined tube.
Described heating jacket is provided with heat medium enter hose and goes out pipe.
Described tail gas recycle device chuck is provided with refrigerant inlet pipe and goes out pipe.
The core of the design is exactly that chemical combination leaching barrel and exhaust purifier are removably connected by flange.
Chemical combination leaching barrel has heating jacket, operate certain liquid level, the solid-phase materials such as copper-sulphide ores are added by the removable cover opening manhole, the liquid phase materials such as ammonia control to add by liquid feed valve, agitator motor connects impeller cone cover by tubular shaft, the inlet mouth that tubular shaft top has axle circumference uniform distribution to open, bottom has axle sleeve to play dynamic state limit and stable support function.The dish that surges connects hollow tubular shaft, and axle sleeve starts state to hollow tubular shaft and supports and stabilization, and bottom valve plays discharge control action kou.
Impeller cone cover connects tubular shaft by driven by motor high speed rotating, inlet opening feed liquor is accelerated centrifugal by blade, move along cone cover inner surface, thrown away by cone shroud rim, high velocity liquid stream can be produced in upper speed cone cover like this and then produce vacuum, such large quantity of air is drawn in mixed solution stream along tubular shaft by vacuum by inlet mouth, is thrown away by cone shroud rim, realizes gas liquid high-efficiency mixing and air (oxygen) supply.In addition, liquid flows through vanelets that effect surges on dish and drives and to surge dish, and the dish that surges connects hollow tubular shaft, and impeller cone cover high speed rotating produces parital vacuum, and hollow tubular shaft also just has suction function, effectively can prevent deposition and the blocking of cone substrate material.
Heating jacket leads to steam or hot water realizes heat temperature raising, also can lead to cold water and lower the temperature, overflow liquid level gas can carry water vapour simultaneously, ammonia becomes tail gas, gas mixture by exhaust purifier realize reclaim and tail gas clean-up, avoid the leakage of ammonia.
Exhaust purifier has chuck can lead to water coolant or refrigerated water, intervalve and helical fin cylinder form jacket structured, overflow gas and rise to top again by the downward water conservancy diversion of helical fin cylinder by intervalve, owing to having helical fin in helical fin cylinder, can realize guiding to gas in interlayer and rotate, produce downward helical air flow path, overflow by edge under helical fin cylinder and pass packing layer, overflow from liquid level and rise, air-flow can the effective liquid phase that wherein may carry of centrifugation at cyclonic separator, Exhaust Gas is made to realize purification, chemical combination leaching barrel is back to after liquid phase and time liquid inclined tube converge.
The decontamination effect improving of exhaust purifier depends on the heat and mass transport overcoming difficulties and carry out, the wherein controlled upflow tube position of liquid level, rear upflow tube meeting overflow that phlegma is many, returning liquid inclined tube can effectively prevent return slag from blocking, in chuck, in refrigerated water and exhaust purifier, liquid phase has very high overall heat transfer coefficient, in exhaust purifier, liquid can produce good automatic stirring convection circulation due to temperature and gas overflowing, helical fin cylinder has larger gas phase side heat interchanging area, simultaneously subsurface liquid phase can efficient heat transfer, cooling ammonia condensing is realized to gas phase in cylinder, ullage divides and is realized gas phase precooling in cylinder by the cryogenic gas overflowed, in helical fin cylinder, swirling eddy can promote heat and mass transfer by effective disturbance air film, carry out one-level cooling, condensation, gas-liquid separation, the heat and mass transfer that secondary directly contacts is realized again through filler liquid phase layer, realize ammonia efficiently to catch, ascending vapor finally realizes once again being separated in cyclonic separator, makes emission reach purification requirement.
The design adopts basic closed interlayer pot chemical combination leaching system, more supporting tail gas recycle ammonia, when air capacity is larger, realizes condensation and the efficient recovery of ammonia, completes tail gas clean-up discharge simultaneously.When non-condensable gases exists in a large number and has a strong impact on condensing interface heat and mass transport state, the high-efficiency condensation achieving ammonia catches.
Compared with prior art, beneficial effect of the present invention is also:
In chemical combination leaching barrel, supplementary convenient, the liquid stream mixing effect automatically of air (oxygen) is improved fully, and chemical combination leaching efficiency is very high; Drive the dish that surges to aspirate material with vacuum driven hollow tubular shaft by liquid stream to prevent from depositing and block, convenient especially, reliable, efficient; Exhaust purifier is multistage, it is good especially efficiently to complete heat transfer, mass transfer, gas-liquid separation effect, effectively prevents the leakage of ammonia.
The present invention by above Integration ofTechnology, achieves environmental protection that copper mine chemical combination leaches and automatical and efficient, has important using value.
Accompanying drawing explanation
Fig. 1 is two dimensional structure schematic diagram of the present invention
Fig. 2 is the three-dimensional structure schematic diagram of impeller cone cover.
Fig. 3 is the three-dimensional structure schematic diagram coiled that surges.
Fig. 4 is helical fin bobbin mouth three-dimensional structure schematic diagram.
Fig. 5 is that three-dimensional structure schematic diagram analysed and observe by helical fin cylinder.
In figure, each label represents:
A, impeller cone cover; B, surge dish; D, helical fin cylinder; 1, agitator motor; 2, inlet mouth; 3, manhole; 4, liquid feed valve; 5, chemical combination leaching barrel; 6, tubular shaft; 7, liquid level in chemical combination leaching barrel; 8, heat medium enter hose; 9, heating jacket; 10, tubular shaft axle sleeve; 11, heat medium produce hose; 12, surge dish axle sleeve; 13, hollow tubular shaft; 14, bottom valve; 15, liquid inclined tube is returned; 21, exhaust purifier; 22, refrigerant goes out pipe; 23, exhaust purifier liquid level; 24, upflow tube; 25, freezing chuck; 26, flow spiral path; 27, filler; 28, intervalve; 29, refrigerant inlet pipe; 30, cyclonic separator; 31, cone cover; 32, inlet opening; 33, blade; 34, hollow axis hole; 35, surge dish; 36, surge dish vanelets; 39, urceolus; 40, helical fin.
Embodiment
Now by reference to the accompanying drawings, the present invention is illustrated further.
As shown in Figure 1, Figure 2, the efficient chemical combination leaching device of the ammonia of cyclonic separation shown in Fig. 3, Fig. 4 and Fig. 5 full recovery type copper mine, comprise chemical combination leaching barrel 5 and exhaust purifier 21, the intervalve 28 of chemical combination leaching barrel 5 and exhaust purifier 21 is removably connected by flange, and exhaust purifier 21 is by upflow tube 24 and return liquid inclined tube 15 and to be linked back chemical combination leaching barrel 5; Chemical combination leaching barrel 5 is provided with manhole 3, liquid feed valve 4 and heating jacket 9, agitator motor 1 inserts in chemical combination leaching barrel 5 after connecting cone cover 31 by tubular shaft 6, blade 33 and inlet opening 32 is provided with in cone cover 31, the inlet mouth 2 that tubular shaft 6 top has axle circumference uniform distribution to open, axle sleeve 10 dynamic state limits and stable support function are arranged at tubular shaft 6 bottom, being provided with the dish B that surges in chemical combination leaching barrel 5 and connecting hollow tubular shaft 13, hollow tubular shaft 13 is provided with axle sleeve 12 and on bottom valve 14; Exhaust purifier 21 outside is provided with chuck 25 and leads to water coolant or refrigerated water, inside is provided with open intervalve 28 and forms jacket structured with the helical fin cylinder D closed, helical fin cylinder D is that inwall welding helical fin 40 forms, the gap of helical fin cylinder D and exhaust purifier 21 inwall is provided with packing layer 27, exhaust purifier 21 is emptying after exporting and connecting cyclonic separator 30, and cyclonic separator 30 liquid-phase outlet converges with time liquid inclined tube 15.
Described heating jacket 9 is provided with heat medium enter hose 8 and goes out pipe 11.
Described tail gas recycle device chuck is provided with refrigerant inlet pipe 29 and goes out pipe 22.
The core of the design is exactly that chemical combination leaching barrel 5 is removably connected by flange with exhaust purifier 21.
Chemical combination leaching barrel 5 has heating jacket 9, liquid level is 7, the solid-phase materials such as copper-sulphide ores are added by the removable cover opening manhole 3, the liquid phase materials such as ammonia control to add by liquid feed valve 4, agitator motor 1 connects impeller cone cover A by tubular shaft 6, the inlet mouth 2 that tubular shaft 6 top has axle circumference uniform distribution to open, axle sleeve 10 dynamic state limits and stable support function are arranged at bottom.The dish B that surges connects hollow tubular shaft 13, axle sleeve 12 pairs of hollow tubular shaft 13 dynamic support and stabilization, bottom valve 14 discharge control action kous.
Impeller cone cover A connects tubular shaft 6 and drives high speed rotating by motor 1, inlet opening 32 feed liquor is accelerated centrifugal by blade 33, along cone cover 31 inner surface movement, thrown away by cone cover 31 edge, high velocity liquid stream can be produced in upper speed cone cover 31 like this and then produce vacuum, such large quantity of air is drawn in mixed solution stream along tubular shaft 6 by vacuum by inlet mouth 2, is thrown away by cone cover 31 edge, realizes gas liquid high-efficiency mixing and air (oxygen) supply.In addition, liquid flows through surge vanelets 36 on dish 35 of effect and drives the dish 35 that surges, and the dish B that surges connects hollow tubular shaft 13, and impeller cone cover A high speed rotating produces parital vacuum, hollow tubular shaft 13 also just has suction function, effectively can prevent deposition and the blocking of boring substrate material.
Heating jacket 9 leads to steam or hot water realizes heat temperature raising, also can lead to cold water and lower the temperature, overflow liquid level gas can carry water vapour simultaneously, ammonia becomes tail gas, gas mixture by exhaust purifier 21 realize reclaim and tail gas clean-up, avoid the leakage of ammonia.
Exhaust purifier 21 has chuck 25 can lead to water coolant or refrigerated water, intervalve 28 and helical fin cylinder D form jacket structured, overflow gas and rise to top again by the downward water conservancy diversion of helical fin cylinder D by intervalve 28, owing to having helical fin 40 in helical fin cylinder D, can realize guiding to gas in interlayer and rotate, produce downward helical air flow path 26, overflow by edge under helical fin cylinder D and pass packing layer 27, overflow from liquid level 23 and rise, air-flow can the effective liquid phase that wherein may carry of centrifugation at cyclonic separator 30, Exhaust Gas is made to realize purification, chemical combination leaching barrel 5 is back to after liquid phase and time liquid inclined tube 15 converge.
The decontamination effect improving of exhaust purifier 21 depends on the heat and mass transport overcoming difficulties and carry out, wherein liquid level 23 controlled upflow tube 24 position, rear upflow tube 24 meeting overflow that phlegma is many, returning liquid inclined tube 15 can effectively prevent return slag from blocking, in chuck 25, in refrigerated water and exhaust purifier, liquid phase has very high overall heat transfer coefficient, in exhaust purifier, liquid can produce good automatic stirring convection circulation due to temperature and gas overflowing, helical fin cylinder D has larger gas phase side heat interchanging area, liquid phase simultaneously under liquid level 23 can efficient heat transfer, cooling ammonia condensing is realized to gas phase in cylinder, liquid level 23 upper part is realized gas phase precooling in cylinder by the cryogenic gas overflowed, in helical fin cylinder D, swirling eddy can promote heat and mass transfer by effective disturbance air film, carry out one-level cooling, condensation, gas-liquid separation, the heat and mass transfer that secondary directly contacts is realized again through filler 27 liquid phase layer, realize ammonia efficiently to catch, ascending vapor finally realizes once again being separated in cyclonic separator 30, makes emission reach purification requirement.
Above-mentioned just preferred embodiment of the present invention, not does any pro forma restriction to the present invention.Any those of ordinary skill in the art, when not departing from technical solution of the present invention scope, can utilize the technology contents of above-mentioned announcement to make many possible variations and modification to technical solution of the present invention, or being revised as the Equivalent embodiments of equivalent variations.Therefore, every content not departing from technical solution of the present invention, according to the technology of the present invention essence to any simple modification made for any of the above embodiments, equivalent variations and modification, all should drop in the scope of technical solution of the present invention protection.
Claims (3)
1. the efficient chemical combination leaching device of cyclonic separation ammonia full recovery type copper mine, comprise chemical combination leaching barrel and exhaust purifier, it is characterized in that: the intervalve of chemical combination leaching barrel and exhaust purifier is removably connected by flange, exhaust purifier is by upflow tube and return liquid inclined tube and to be linked back chemical combination leaching barrel; Chemical combination leaching barrel is provided with manhole, liquid feed valve and heating jacket, agitator motor inserts in chemical combination leaching barrel after connecting cone cover by tubular shaft, blade and inlet opening is provided with in cone cover, the inlet mouth that tubular shaft top has axle circumference uniform distribution to open, tubular shaft bottom has axle sleeve to play dynamic state limit and stable support function, being provided with the dish that surges in chemical combination leaching barrel and connecting hollow tubular shaft, hollow tubular shaft is provided with axle sleeve and on bottom valve; Exhaust purifier outside is provided with chuck and leads to water coolant or refrigerated water, inside is provided with open intervalve and forms jacket structured with the helical fin cylinder closed, helical fin cylinder is that inwall welding helical fin forms, the gap of helical fin cylinder and exhaust purifier inwall is provided with packing layer, emptying after exhaust purifier outlet connects cyclonic separator, cyclonic separator liquid-phase outlet converges with time liquid inclined tube.
2. the efficient chemical combination leaching device of cyclonic separation ammonia full recovery type copper mine according to claim 1, is characterized in that: described heating jacket is provided with heat medium enter hose and goes out pipe.
3. the efficient chemical combination leaching device of cyclonic separation ammonia full recovery type copper mine according to claim 1 or 2, is characterized in that: described tail gas recycle device chuck is provided with refrigerant inlet pipe and goes out pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510637669.6A CN105087922B (en) | 2015-10-07 | 2015-10-07 | The efficient chemical combination leaching device of the full recovery type copper mine of cyclonic separation ammonia |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510637669.6A CN105087922B (en) | 2015-10-07 | 2015-10-07 | The efficient chemical combination leaching device of the full recovery type copper mine of cyclonic separation ammonia |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105087922A true CN105087922A (en) | 2015-11-25 |
| CN105087922B CN105087922B (en) | 2017-06-06 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510637669.6A Active CN105087922B (en) | 2015-10-07 | 2015-10-07 | The efficient chemical combination leaching device of the full recovery type copper mine of cyclonic separation ammonia |
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| Country | Link |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2064330C1 (en) * | 1981-07-17 | 1996-07-27 | Красноармейский Научно-Исследовательский Институт Механизации | Mixer |
| CN2815487Y (en) * | 2005-08-12 | 2006-09-13 | 周凤举 | Internal back streaming tower fluidized_bed reactor with habyrinth helical fin diversion baffle |
| CN103657471A (en) * | 2013-11-27 | 2014-03-26 | 江苏浩特隆搅拌设备有限公司 | Special stirring machine for garbage fermentation |
| CN203990638U (en) * | 2014-08-20 | 2014-12-10 | 潍坊科技学院 | Cathode electrophoresis dope reaction unit |
-
2015
- 2015-10-07 CN CN201510637669.6A patent/CN105087922B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2064330C1 (en) * | 1981-07-17 | 1996-07-27 | Красноармейский Научно-Исследовательский Институт Механизации | Mixer |
| CN2815487Y (en) * | 2005-08-12 | 2006-09-13 | 周凤举 | Internal back streaming tower fluidized_bed reactor with habyrinth helical fin diversion baffle |
| CN103657471A (en) * | 2013-11-27 | 2014-03-26 | 江苏浩特隆搅拌设备有限公司 | Special stirring machine for garbage fermentation |
| CN203990638U (en) * | 2014-08-20 | 2014-12-10 | 潍坊科技学院 | Cathode electrophoresis dope reaction unit |
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| Publication number | Publication date |
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| CN105087922B (en) | 2017-06-06 |
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Inventor after: Liu Xiang Inventor before: Yin Yongzhong Inventor before: Liu Zhixiong |
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Effective date of registration: 20170508 Address after: 362100, Fujian Province, Quanzhou County, Yongchun province reached 15 village, two floor, Po Town Applicant after: YONGCHUN HONGMING FURNITURE Co.,Ltd. Address before: 510000 unit 2414-2416, building, No. five, No. 371, Tianhe District, Guangdong, China Applicant before: GUANGDONG GAOHANG INTELLECTUAL PROPERTY OPERATION Co.,Ltd. Effective date of registration: 20170508 Address after: 510000 unit 2414-2416, building, No. five, No. 371, Tianhe District, Guangdong, China Applicant after: GUANGDONG GAOHANG INTELLECTUAL PROPERTY OPERATION Co.,Ltd. Address before: 416000 Hunan, Xiangxi Tujia and Miao Autonomous Prefecture, Jishou City People's road, No. 120 Applicant before: Jishou University |
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