CN101845557A - Shaft furnace, copper water bag and rotary furnace combined type fire refining process for raw red copper - Google Patents
Shaft furnace, copper water bag and rotary furnace combined type fire refining process for raw red copper Download PDFInfo
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- CN101845557A CN101845557A CN 201010200908 CN201010200908A CN101845557A CN 101845557 A CN101845557 A CN 101845557A CN 201010200908 CN201010200908 CN 201010200908 CN 201010200908 A CN201010200908 A CN 201010200908A CN 101845557 A CN101845557 A CN 101845557A
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/006—Pyrometallurgy working up of molten copper, e.g. refining
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0028—Smelting or converting
- C22B15/005—Smelting or converting in a succession of furnaces
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0028—Smelting or converting
- C22B15/0052—Reduction smelting or converting
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Abstract
The invention relates to a fire refining process for raw red copper. The process is characterized by adopting a shaft furnace, a copper water bag and at least one rotary furnace and comprising the following steps of: 1) charging the raw material of the raw red copper into the shaft furnace by using a charging machine and smelting the raw red copper in the shaft furnace into raw red copper liquid; 2) lifting and charging the raw red copper liquid smelted and produced from the shaft furnace into the rotary refining furnace by using the copper water bag to perform redox refining to obtain the refined copper liquid; and 3) allowing the refined copper liquid to directly enter a tundish through a launder to finish the subsequent procedures. According to the fire refining process, a holding furnace is saved, so the fire refining process has the advantages of high energy utilization ratio, high production continuity and good labor condition.
Description
Technical field
The present invention relates to a kind of fire refining process of purple composition brass, particularly, relate to a kind of employing shaft furnace, Tong Shuibao and at least one rotary kiln, and omit the fire refining process for raw red copper of holding furnace, belong to the non-ferrous metal metallurgy technical field.
Background technology
Purple composition brass is that copper content is not less than 90% copper scrap, claims useless red copper or useless fine copper again, is the maximum copper scrap kind of yield.Purple composition brass is purified through pyrorefining becomes refined matte.The higher refined matte liquid of purity is used for the continuous casting and rolling electrician with copper cash base (claiming copper bar, copper wire rod again), or other red copper base that is used to cast.The refined matte liquid that purity is not high is used to the positive plate of casting.
Present known fire refining process for raw red copper flow process can be divided into following 4 kinds:
1. fixed reverberatory refining technical process
Its main flow process is, purple composition brass → charging machine or hand-fed → fixed reverberatory furnace fusing, oxidation and reduction refining → refined matte liquid → chute → tundish, quantitative casting bag → be used for the continuous casting and rolling electrician to use the copper cash base, or other red copper base that is used to cast, or be used to the positive plate of casting.
2. tilting-type refining furnace refinery practice flow process
Its main flow process is, purple composition brass → charging machine → tilting-type refining furnace fusing, oxidation and reduction refining → refined matte liquid → chute → tundish, quantitative casting bag → be used for the continuous casting and rolling electrician to use the copper cash base, or other red copper base that is used to cast, or be used to the anode copper of casting.
3. shaft furnace-fixed reverberatory furnace is united the refinery practice flow process
Its main flow process is purple composition brass → charging machine → shaft furnace melting → purple composition brass liquid → chute → fixed reverberatory furnace redox refining → refined matte liquid → chute → tundish, quantitative casting bag → casting positive plate.
Paper " putting into practice of the molten process for copper of shaft furnace " (Yuan Fuping, " industrial furnace ", the 30th the 3rd phase of volume, in May, 2008) discloses the molten copper of a kind of shaft furnace-reverberatory refining integration of operation and has produced anode copper coin technology.This technology is advanced the copper material with shaft furnace, and is fused into copper water and offers reverberatory furnace, and reverberatory furnace is cast into the anode copper coin then with the redox of copper water.
4. shaft furnace-tilting-type refining furnace-holding furnace is united the refinery practice flow process
Paper " technology and the equipment of useless composition brass pyrorefining direct production glitter copper lever " (the newborn Lu Hong of Zhao, " resource recovery ", 2008 the 10th, 11 phases) discloses a kind of 1 shaft furnace-2 tilting furnace-1 holding furnace associating refinery practice.Its main flow process is that purple composition brass → charging machine → shaft furnace melting → purple composition brass liquid → chute → tilting-type refining furnace redox refining → refined matte liquid → chute → holding furnace fine setting copper liquid composition and temperature → refined matte liquid → chute → tundish → continuous casting and rolling electrician use the copper cash base.
There is following problem in existing pyrorefining technology: 1) fuel consumption of fixed reverberatory furnace and tilting-type refining furnace is big, thermo-efficiency low (energy utilization rate 15～40%), and labor condition is relatively poor; 2) the shaft furnace rate of utilization in the shaft furnace-fixed reverberatory furnace associating refinery practice is low, can't the serialization High-efficient Production; 3) holding furnace that is provided with in shaft furnace-tilting-type refining furnace-holding furnace associating refinery practice flow process has increased energy consumption.
Summary of the invention
The purpose of this invention is to provide a kind of energy utilization rate height, labor condition better, fire refining process for raw red copper that the production continuity is strong.
For this reason, the invention provides a kind of fire refining process of purple composition brass, it is characterized in that, adopt shaft furnace, Tong Shuibao and at least one rotary kiln, comprise the following steps: 1) purple composition brass raw material is by the charging machine shaft furnace of packing into, is smelted into purple composition brass liquid in shaft furnace; 2) the purple composition brass liquid of shaft furnace melting output adopts the copper water bag handling rotary refining furnace of packing into, carries out the redox refining, to obtain refined matte liquid; And 3) refined matte liquid directly enters tundish through chute, to finish subsequent handling.
Preferably, comprise at least two rotary kilns.
Preferably, comprise three rotary kilns.
Preferably, in step 3), the chute form can be movable and fixed two types combination, also can be wherein a kind of; Chute can be a multistage, also can be one section.Can directly connect subsequent handling behind the tundish, also can connect subsequent handling by the quantitative casting bag.
Preferably, subsequent handling comprises continuous casting and rolling copper cash base or casting anode copper.
Preferably, comprise two rotary kilns, these two rotary kilns are independently finished refinery process whole process, interlaced operation process separately.
Preferably, comprise a shaft furnace that is used for molten copper and two rotary kilns that are used for refined matte.
According to the present invention, the equipment of employing comprises 1 shaft furnace, Tong Shuibao, 1 to 3 rotary kiln, chute, tundish, but has omitted holding furnace.
According to one embodiment of present invention, shaft furnace of process using of the pyrorefining of purple composition brass and two rotary kiln associating refinery practice flow processs, smelt stage adopts shaft furnace to melt purple composition brass, and oxidation, reduction phase adopt two rotary refining furnaces with purple composition brass liquid refining becoming refined matte liquid.
Described shaft furnace is the sophisticated equipment of the solid-state copper of fusing, compares with fixed reverberatory furnace or tilting-type refining, and melting efficiency can improve 1～2 times, and thermosteresis can be decreased to 20～35%, and promptly energy utilization ratio can be up to 65～80%, and the production continuity is strong.
Described rotary refining furnace is to be in the large-size chemical process flow of raw material production cathode copper with ore deposit copper, and liquid blister refining is become the preferred unit of anode process for copper link, claims Rotary Anode Furnace or rotary kiln again.Compare with fixed or tilting-type reverberatory furnace, rotary refining furnace has area of dissipation little (be equivalent to reverberatory furnace about 50%), good airproof performance, thermo-efficiency height (energy utilization rate can reach 60～70%), the smoke and dust treatment difficulty is little, deslagging, put operating machine of copper level of automation height, labor condition better and the relative proven technique advantage of maximization production supporting technology.
In this embodiment of the present invention, two rotary kilns are independently finished the refinery process whole process separately, but interlaced 1/2 operation process of while.After rotary kiln is smelted and is finished, refined matte liquid directly enters tundish through chute, does not need to finely tune composition and temperature through holding furnace again, and refined matte liquid directly enters copper cash continuous-casting tandem-rolling production line or positive plate liquid filling machine, be used for continuous casting and rolling copper cash base, or be used to the positive plate of casting.
The fire refining process of purple composition brass according to the present invention has comprehensively been drawn the advantage that shaft furnace melts solid-state copper technology advantage and the liquid copper technology of rotary kiln refining.
The step of the fire refining process of purple composition brass according to another preferred embodiment is as follows:
1. the purple composition brass furnace charge of pre-treatment is removed inclusion as far as possible.
2. pack into the charging machine of truck formula or other form of furnace charge, add shaft furnace thereupon.
3. shaft furnace melting batch, the purple composition brass liquid of output.
4. crane copper water bag accesses purple composition brass liquid, and two rotary kilns are poured in handling successively into.
5. two rotary kilns are independently finished the refinery process whole process separately, but interlaced 1/2 operation process of while.Be in and access copper liquid when one, when oxidation, deslagging and reduction refining operation process, another is in the outlet temperature of control copper liquid and composition, copper operation process.When being about to out copper liquid for one, another begins copper, steadily alternately, keeps the refined matte flow quantity of inflow chute basicly stable.
6. the refined matte liquid inflow activity chute of rotary kiln output flows into fixedly chute again, finally flows into tundish, is used for the continuous casting and rolling electrician and uses the copper cash base, or be used to the positive plate of casting.
Beneficial effect according to fire refining process for raw red copper of the present invention is:
1. adopt the method for shaft furnace melting, significantly improved the melting efficiency (improving 1～2 times) and the energy utilization rate (improving 20～30 percentage points) of purple composition brass pyrorefining;
2. the operation labor condition that adopts the method for the purple composition brass of rotary kiln refining to improve deslagging, put copper;
3. a shaft furnace and two rotary kilns are united in the refinery practice, and two interlaced 1/2 refinery process processes of rotary kiln while help accessing continuously shaft furnace copper liquid, and output refined matte liquid has guaranteed the continuity of producing continuously;
4. adopt fire refining process of the present invention, helping improving with purple composition brass is maximization, mechanize and the automatic technology level of main material production copper cash base or positive plate.
Description of drawings
Fig. 1 is the fire refining process schema according to purple composition brass of the present invention.
Embodiment
Referring to accompanying drawing, the specific implementation method of technical solution of the present invention is as follows:
Among Fig. 1, purple composition brass raw material is loaded into the charging machine of truck formula or other form, adds shaft furnace thereupon; The shaft furnace melting batch, the purple composition brass liquid of output; Crane copper water bag accesses purple composition brass liquid, and two rotary kilns are poured in handling successively into, and two rotary kilns are independently finished the refinery process whole process separately, but interlaced 1/2 operation process simultaneously, and the fine copper flow quantity that keeps flowing into fixing chute is basicly stable; The fine copper liquid inflow activity chute of rotary kiln output, the tundish of finally flowing through enters copper cash continuous casting and rolling production line or positive plate liquid filling machine, is used for continuous casting and rolling copper cash base or casting positive plate.
Embodiment 1
With purple composition brass is the fire refining process flow process that raw material is produced 220000 tons of engineerings of copper cash base per year, copper water Bao Sanci handling copper liquid mode, and step is as follows:
1. the purple composition brass furnace charge of pre-treatment is removed inclusion as far as possible, and processing length or lumpiness should be fit to the truck of packing into.
2. with fork truck the purple composition brass furnace charge truck formula charging machine of packing into.
3. truck formula charging machine adds production capacity 35t/h shaft furnace to purple composition brass furnace charge.
4. production capacity 35t/h shaft furnace melting batch, the purple composition brass liquid of output accesses with nominal capacity 100t copper water bag continuously, and two nominal capacity 300t rotary kilns are poured in handling successively into.
5. first rotary kiln poured in first handling into, needs 3 times about at every turn 100t altogether.Fallen behind the 200t, entered oxidation operation.Fallen behind the 300t, entered later stage oxidation, deslagging, reduction, controlled temperature and composition refinery process, got final product copper after finishing.
6. after first rotary kiln refinery process finished during copper, second rotary kiln begins to enter and accesses copper liquid, refinery process and copper whole process.Two nominal capacity 300t rotary kilns are independently finished separately and are accessed copper liquid, oxidation, deslagging, reduction, controlled temperature and composition, copper operation whole process, but interlaced 1/2 operation process of while.When being about to out copper liquid for one, another begins copper, and steadily alternately, the refined matte flow quantity that keeps flowing into fixing chute is basicly stable.
7. the refined matte liquid of rotary kiln output is introduced fixedly chute by movable chute.
8. refined matte liquid is gone into tundish from the fixed flow concentrated flow.
9. refined matte liquid injects the continuous caster of production capacity 35t/h continuous casting and rolling production line from tundish, through continuous billet casting, roll bar, output copper cash base.
Embodiment 2
With purple composition brass is the fire refining process flow process that raw material is produced 220000 tons of engineerings of copper cash base per year, twice handling copper of copper water bag liquid mode, and step is as follows:
Step 1., 2., 3. identical with embodiment 1.
4. production capacity 35t/h shaft furnace melting batch, the purple composition brass liquid of output accesses with nominal capacity 150t copper water bag continuously, and two nominal capacity 300t rotary kilns are poured in handling successively into.
5. first rotary kiln poured in first handling into, needs 2 times about at every turn 150t altogether.Fallen behind the 300t, entered oxidation, deslagging, reduction, controlled temperature and composition refinery process, got final product copper after finishing.
Step 6., 7., 8., 9. identical with embodiment 1.
The present invention determines the rotary kiln nominal capacity by following formula:
Rotary kiln nominal capacity (t)=shaft furnace production capacity (t/h) * separate unit rotary kiln is finished and is accessed copper liquid and redox time (h)
The present invention determines that by following formula copper water Bao Zheng claims capacity:
Copper water Bao Zheng claims capacity (t)=rotary kiln nominal capacity (t) ÷ copper water bag handling number of times
Copper water bag handling number of times of the present invention should be determined according to the technical economical analysis situation.
Some specific embodiments of the present invention are more than disclosed, those skilled in the art can according to thought of the present invention carry out various improvement, perfect, replace and/or change, for example, the chute form can be movable and fixed two types combination, also can be wherein a kind of; Chute can be a multistage, also can be one section.Yet, do like this, all be included within the protection domain of claims.
Claims (8)
1. the fire refining process of a purple composition brass is characterized in that, adopts shaft furnace, Tong Shuibao and at least one rotary kiln, comprises the following steps:
1) purple composition brass raw material is smelted into purple composition brass liquid by the charging machine shaft furnace of packing in shaft furnace;
2) the purple composition brass liquid of shaft furnace melting output adopts the copper water bag handling rotary kiln of packing into, carries out the redox refining, to obtain refined matte liquid; And
3) refined matte liquid directly enters tundish through chute, to finish subsequent handling.
2. fire refining process as claimed in claim 1 is characterized in that, comprises at least two rotary kilns.
3. fire refining process as claimed in claim 2 is characterized in that, comprises three rotary kilns.
4. fire refining process as claimed in claim 1 is characterized in that, in step 3), the chute form can be movable and fixed two types combination, also can be wherein a kind of; Chute can be a multistage, also can be one section.
5. fire refining process as claimed in claim 1 is characterized in that, can directly connect subsequent handling behind the tundish, also can connect subsequent handling by the quantitative casting bag.
6. fire refining process as claimed in claim 1 is characterized in that, subsequent handling comprises continuous casting and rolling copper cash base or casting positive plate.
7. fire refining process as claimed in claim 2 is characterized in that, comprises two rotary kilns, and these two rotary kilns are independently finished refinery process whole process, interlaced operation process separately.
8. fire refining process as claimed in claim 1 is characterized in that, comprises a shaft furnace that is used for molten copper and two rotary kilns that are used for refined matte.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102009089A CN101845557B (en) | 2010-06-10 | 2010-06-10 | Shaft furnace, copper water bag and rotary furnace combined type fire refining process for raw red copper |
| PCT/CN2011/075259 WO2011153924A1 (en) | 2010-06-10 | 2011-06-03 | Method for fire refining raw red copper by combining shaft furnace, copper transferring ladle and rotary furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102009089A CN101845557B (en) | 2010-06-10 | 2010-06-10 | Shaft furnace, copper water bag and rotary furnace combined type fire refining process for raw red copper |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101845557A true CN101845557A (en) | 2010-09-29 |
| CN101845557B CN101845557B (en) | 2011-10-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2010102009089A Expired - Fee Related CN101845557B (en) | 2010-06-10 | 2010-06-10 | Shaft furnace, copper water bag and rotary furnace combined type fire refining process for raw red copper |
Country Status (2)
| Country | Link |
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| CN (1) | CN101845557B (en) |
| WO (1) | WO2011153924A1 (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011153924A1 (en) * | 2010-06-10 | 2011-12-15 | 江西稀有金属钨业控股集团有限公司 | Method for fire refining raw red copper by combining shaft furnace, copper transferring ladle and rotary furnace |
| CN104313344A (en) * | 2014-10-31 | 2015-01-28 | 宁波大学 | Environmental-friendly method for smelting and upcasting of electrical copper rod from low-grade copper |
| CN104313345A (en) * | 2014-10-31 | 2015-01-28 | 宁波大学 | Method for energy conservation of low-cost equipment for smelting of high-quality anode plate from low-grade copper |
| CN104342563A (en) * | 2014-10-31 | 2015-02-11 | 宁波大学 | Low-cost equipment energy-saving smelting method for low-grade copper raw materials |
| CN104388694A (en) * | 2014-10-31 | 2015-03-04 | 宁波大学 | Environment-friendly method for smelting high quality anode plate from low-grade copper by adopting low-cost equipment |
| CN104388693A (en) * | 2014-10-31 | 2015-03-04 | 宁波大学 | Energy-saving method for smelting high-quality positive plates by using low-quality copper |
| CN104388692A (en) * | 2014-10-31 | 2015-03-04 | 宁波大学 | Environment-friendly method for smelting high-quality anode plate from low-grade copper |
| CN113878101A (en) * | 2021-07-07 | 2022-01-04 | 浙江海亮股份有限公司 | Shaft furnace-horizontal continuous casting copper casting blank device |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111235405A (en) * | 2020-03-20 | 2020-06-05 | 四川博鑫铜业有限公司 | Low-oxygen copper rod preparation process |
| CN114350968A (en) * | 2021-12-31 | 2022-04-15 | 高诺(衡阳)产业园发展有限责任公司 | High-efficiency energy-saving copper fire refining process |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007131932A (en) * | 2005-11-11 | 2007-05-31 | Furukawa Electric Co Ltd:The | Method for melting metal |
| CN201087210Y (en) * | 2007-09-29 | 2008-07-16 | 南昌有色冶金设计研究院 | Floating smelting and immersing converting integrated continual copper smelting device |
| CN101654792A (en) * | 2008-08-23 | 2010-02-24 | 大冶有色金属公司 | Regeneration novel process adopting electrolysis residual pole pyrogenic method |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5827939A (en) * | 1981-08-13 | 1983-02-18 | Sumitomo Electric Ind Ltd | Manufacture of copper material for electric wire |
| CN101344357A (en) * | 2008-08-25 | 2009-01-14 | 中国瑞林工程技术有限公司 | Rotary kiln and technique for processing composition brass or block shaped raw copper |
| CN101845557B (en) * | 2010-06-10 | 2011-10-05 | 江西稀有金属钨业控股集团有限公司 | Shaft furnace, copper water bag and rotary furnace combined type fire refining process for raw red copper |
-
2010
- 2010-06-10 CN CN2010102009089A patent/CN101845557B/en not_active Expired - Fee Related
-
2011
- 2011-06-03 WO PCT/CN2011/075259 patent/WO2011153924A1/en active Application Filing
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007131932A (en) * | 2005-11-11 | 2007-05-31 | Furukawa Electric Co Ltd:The | Method for melting metal |
| CN201087210Y (en) * | 2007-09-29 | 2008-07-16 | 南昌有色冶金设计研究院 | Floating smelting and immersing converting integrated continual copper smelting device |
| CN101654792A (en) * | 2008-08-23 | 2010-02-24 | 大冶有色金属公司 | Regeneration novel process adopting electrolysis residual pole pyrogenic method |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011153924A1 (en) * | 2010-06-10 | 2011-12-15 | 江西稀有金属钨业控股集团有限公司 | Method for fire refining raw red copper by combining shaft furnace, copper transferring ladle and rotary furnace |
| CN104313344A (en) * | 2014-10-31 | 2015-01-28 | 宁波大学 | Environmental-friendly method for smelting and upcasting of electrical copper rod from low-grade copper |
| CN104313345A (en) * | 2014-10-31 | 2015-01-28 | 宁波大学 | Method for energy conservation of low-cost equipment for smelting of high-quality anode plate from low-grade copper |
| CN104342563A (en) * | 2014-10-31 | 2015-02-11 | 宁波大学 | Low-cost equipment energy-saving smelting method for low-grade copper raw materials |
| CN104388694A (en) * | 2014-10-31 | 2015-03-04 | 宁波大学 | Environment-friendly method for smelting high quality anode plate from low-grade copper by adopting low-cost equipment |
| CN104388693A (en) * | 2014-10-31 | 2015-03-04 | 宁波大学 | Energy-saving method for smelting high-quality positive plates by using low-quality copper |
| CN104388692A (en) * | 2014-10-31 | 2015-03-04 | 宁波大学 | Environment-friendly method for smelting high-quality anode plate from low-grade copper |
| CN104313344B (en) * | 2014-10-31 | 2016-05-11 | 宁波大学 | A kind of low-grade copper draws the environment protection method of electrician's copper bar on smelting |
| CN104342563B (en) * | 2014-10-31 | 2016-05-11 | 宁波大学 | A kind of energy-conservation smelting process of low cost equipment of low-grade copper raw material |
| CN104388692B (en) * | 2014-10-31 | 2016-06-08 | 宁波大学 | A kind of low-grade copper smelts the environment protection method of high-quality positive plate |
| CN104388693B (en) * | 2014-10-31 | 2016-08-31 | 宁波大学 | A kind of low-grade copper smelts the power-economizing method of high-quality positive plate |
| CN113878101A (en) * | 2021-07-07 | 2022-01-04 | 浙江海亮股份有限公司 | Shaft furnace-horizontal continuous casting copper casting blank device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101845557B (en) | 2011-10-05 |
| WO2011153924A1 (en) | 2011-12-15 |
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Address after: 330046 No. 118 West Beijing Road, Jiangxi, Nanchang Patentee after: JIANGXI TUNGSTEN HOLDING GROUP CO.,LTD. Address before: 330046 No. 118 West Beijing Road, Jiangxi, Nanchang Patentee before: JIANGXI RARE EARTH & RARE METALS TUNGSTEN GROUP HOLDING Co.,Ltd. |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220531 Address after: 341099 Jinlong Road, Ganzhou economic and Technological Development Zone, Jiangxi Province Patentee after: GANZHOU JIANGWU NEW TYPE ALLOY MATERIAL Co.,Ltd. Address before: 330046 No. 118 West Beijing Road, Jiangxi, Nanchang Patentee before: JIANGXI TUNGSTEN HOLDING GROUP CO.,LTD. |
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| 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: 20111005 |