CN105087917A - Environment-friendly copper mine efficient chemical combination leaching device - Google Patents
Environment-friendly copper mine efficient chemical combination leaching device Download PDFInfo
- Publication number
- CN105087917A CN105087917A CN201510637661.XA CN201510637661A CN105087917A CN 105087917 A CN105087917 A CN 105087917A CN 201510637661 A CN201510637661 A CN 201510637661A CN 105087917 A CN105087917 A CN 105087917A
- Authority
- CN
- China
- Prior art keywords
- chemical combination
- combination leaching
- exhaust purifier
- barrel
- tail gas
- 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
Links
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
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention discloses an environment-friendly 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 inserted into the chemical combination leaching barrel after being connected with a cone cover through a hollow shaft; a blade and a liquid inlet hole are arranged in the cone cover; air inlets are uniformly distributed in the shaft periphery of the upper part of the hollow shaft; a hydraulic disc in the chemical combination leaching barrel is in shaft connection with a spiral conveyer, and is positioned on a bottom valve; a jacket is arranged outside the tail gas purifier; a middle pipe is arranged in the tail gas purifier, and is formed to a jacket structure with a spiral fin cylinder; and a cyclone is arranged in an outlet of the tail gas purifier. The device is automatic and convenient for replenishment of air (oxygen) in the chemical combination leaching barrel, is complete and sufficient in liquid flow mixing effect, is higher in chemical combination leaching effect, and is convenient, reliable and efficient in prevention of material deposition and blockage; the tail gas purifier efficiently finishes the heat transfer and the mass transfer by multiple stages, so that the gas-liquid separation effect is excellent; and the device effectively prevents the ammonia leakage, realizes the environmental protection, the automation and high efficiency of copper mine chemical combination leaching, and is important in application value.
Description
Technical field
The present invention relates to the efficient chemical combination leaching device of a kind of environmental 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), copper-amine complex can 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 air (oxygen) and ore pulp, leaching agent mix and contact insufficient, 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, not only cost of investment is high, also 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 environmental 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 environmental 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, be provided with surge dish and axle sleeve thereof in chemical combination leaching barrel, the dish that surges connects spiral conveyer by axle, and spiral conveyer is 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, exhaust purifier outlet is provided with swirler, and swirler is that axis and urceolus are formed by connecting by spinning disk.
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 spiral conveyer by axle, and axle sleeve plays dynamic support and stabilization to axle, 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 drives spiral conveyer by axle, effectively prevents 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 forces cyclone by spinning disk effect in swirler, can the effective liquid phase that wherein may carry of centrifugation, Exhaust Gas is made to realize purification, liquid phase can reflux downwards by automatic dipping wall.
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 cyclonic separation once again in swirler, 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 air (oxygen) supplementary because negative pressure sucks automatically, contact fully with slurries mixing effect, chemical combination leaching efficiency is high; The dish that surges is driven to prevent from material from depositing blocking convenient, reliable, efficient with spiral conveyer by liquid stream; 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 the three-dimensional structure schematic diagram of swirler.
Fig. 5 is helical fin bobbin mouth three-dimensional structure schematic diagram.
Fig. 6 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; C, swirler; 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, spiral conveyer; 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; 31, cone cover; 32, inlet opening; 33, blade; 34, hollow axis hole; 35, surge dish; 36, surge dish vanelets; 37, spinning disk; 38, axis; 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 copper mine of environmental type shown in Fig. 3, Fig. 4, Fig. 5 and Fig. 6, 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, be provided with surge dish 35 and axle sleeve 12 thereof in chemical combination leaching barrel 5, the dish 35 that surges connects spiral conveyer 13 by axle, and spiral conveyer 13 is 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 outlet is provided with swirler C, and swirler C is that axis 38 is formed by connecting by spinning disk 37 with urceolus.
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 spiral conveyer 13 by axle, and axle sleeve 12 pairs of axles play 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 the effect vanelets 36 surged on dish B and drives and to surge dish, and the dish B that surges drives spiral conveyer 13 by axle, effectively prevents deposition and the blocking of cone 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 acts on by spinning disk 37 and forces cyclone in swirler C, can the effective liquid phase that wherein may carry of centrifugation, Exhaust Gas is made to realize purification, liquid phase can reflux downwards by automatic dipping wall.
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 cyclonic separation once again in swirler C, 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 environmental 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, be provided with surge dish and axle sleeve thereof in chemical combination leaching barrel, the dish that surges connects spiral conveyer by axle, and spiral conveyer is 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, exhaust purifier outlet is provided with swirler, and swirler is that axis and urceolus are formed by connecting by spinning disk.
2. the efficient chemical combination leaching device of environmental 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 environmental 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 |
|---|---|---|---|
| CN201510637661.XA CN105087917B (en) | 2015-10-07 | 2015-10-07 | The efficient chemical combination leaching device of environmental type copper mine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510637661.XA CN105087917B (en) | 2015-10-07 | 2015-10-07 | The efficient chemical combination leaching device of environmental type copper mine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105087917A true CN105087917A (en) | 2015-11-25 |
| CN105087917B CN105087917B (en) | 2017-03-29 |
Family
ID=54569239
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510637661.XA Active CN105087917B (en) | 2015-10-07 | 2015-10-07 | The efficient chemical combination leaching device of environmental type copper mine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105087917B (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2187567C1 (en) * | 2001-08-22 | 2002-08-20 | Общество с ограниченной ответственностью "МАГОЛОС" | Apparatus for electrochemical leaching of precious metals from sludge and concentrates |
| CN201520793U (en) * | 2009-08-27 | 2010-07-07 | 浙江华友钴业股份有限公司 | NPT ammonia leached copper device |
| CN201598320U (en) * | 2010-01-08 | 2010-10-06 | 厦门紫金矿冶技术有限公司 | Gold-containing copper pyrite reaction device |
| CN203075926U (en) * | 2013-02-26 | 2013-07-24 | 长春黄金研究院 | Impeller stirred reactor with self-suction function |
| 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 CN201510637661.XA patent/CN105087917B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2187567C1 (en) * | 2001-08-22 | 2002-08-20 | Общество с ограниченной ответственностью "МАГОЛОС" | Apparatus for electrochemical leaching of precious metals from sludge and concentrates |
| CN201520793U (en) * | 2009-08-27 | 2010-07-07 | 浙江华友钴业股份有限公司 | NPT ammonia leached copper device |
| CN201598320U (en) * | 2010-01-08 | 2010-10-06 | 厦门紫金矿冶技术有限公司 | Gold-containing copper pyrite reaction device |
| CN203075926U (en) * | 2013-02-26 | 2013-07-24 | 长春黄金研究院 | Impeller stirred reactor with self-suction function |
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105087917B (en) | 2017-03-29 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104971553B (en) | A kind of multistage composite type high efficiency air liquid separation device | |
| CN208694292U (en) | A kind of liquid separation water seal integrated tank | |
| CN105214428A (en) | Be applicable to the dust arrester of high temperature dust tail gas recycle | |
| CN105087917A (en) | Environment-friendly copper mine efficient chemical combination leaching device | |
| CN105087928A (en) | Total-ammonia recovery type copper mine efficient chemical combination leaching device | |
| CN105087281A (en) | Efficient kiwi fruit wine fermentation device capable of realizing total aroma recovery | |
| CN105087920A (en) | Environment-friendly efficient copper mine combination leaching device with reverse-cone sieve disc | |
| CN110270125A (en) | Fixed gas removal device and method, evaporation crystallization equipment | |
| CN105087923A (en) | Cyclone separation environment-friendly copper mine efficient chemical combination leaching device | |
| CN105087918A (en) | Non-ammonia-leakage type copper mine efficient chemical combination leaching device | |
| CN105087282A (en) | Efficient kiwi fruit wine fermentation device capable of preventing aroma leakage | |
| CN206881536U (en) | A kind of agitator | |
| CN105087922A (en) | Cyclone separation ammonia total-recycle-type copper mine efficient chemical combination leaching device | |
| CN105087921A (en) | Effective counter-cone sieve plate ammonia full-recycling type copper mine combined leaching device | |
| CN105087919A (en) | Cyclone separation ammonia-leakage-free type copper mine efficient chemical combination leaching device | |
| CN105112653A (en) | Reverse cone sieve disk ammonia leakage-free efficient chemical combination leaching device of copper ore | |
| CN208771188U (en) | High gravity desulfurization system | |
| CN206463975U (en) | Chemical reaction pot waste gas negative pressure recovering device with spraying function | |
| CN105087283B (en) | Efficient fermentation device for full-aroma kiwi fruit wine | |
| CN108889108A (en) | High gravity desulfurization system | |
| CN105214429B (en) | Cyclone dust removal device for recycling of high-temperature dust-containing tail gas | |
| CN101288502B (en) | Drying device | |
| CN201586440U (en) | Reverse cooing, deoiling and drying integrated joint liquid-gas separating equipment | |
| CN212680953U (en) | Powder material feeding system | |
| CN106754187A (en) | One kind steams wine equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20191106 Address after: 314100 Room 204, No.158 Yaozhuang Avenue, Yaozhuang Town, Jiashan County, Jiaxing City, Zhejiang Province Patentee after: Jiashan Yaozhuang modern service industry comprehensive development Co., Ltd Address before: 416000 Hunan, Xiangxi Tujia and Miao Autonomous Prefecture, Jishou City People's road, No. 120 Patentee before: Jishou University |
|
| TR01 | Transfer of patent right |