CN101104886A - Technique for semi-continuously producing light metal and producing device thereof - Google Patents
Technique for semi-continuously producing light metal and producing device thereof Download PDFInfo
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- CN101104886A CN101104886A CNA2006100947670A CN200610094767A CN101104886A CN 101104886 A CN101104886 A CN 101104886A CN A2006100947670 A CNA2006100947670 A CN A2006100947670A CN 200610094767 A CN200610094767 A CN 200610094767A CN 101104886 A CN101104886 A CN 101104886A
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Abstract
The invention relates to a metal production method and the production facility thereof, particularly a process for semi-continuous production of light metals and the production facility thereof. The whole process is performed in a reduction pot, raw materials are fed into the reduction pot by using a sealable preheating storage chamber fixed on the top of the vertical-type reduction pot, and the content of reaction residues inside the reduction pot is above zero when the reaction residues are discharged. The reduction pot is vertically arranged inside a heating furnace in a way that the upper and bottom ends thereof extend out of the roof and hearth of the heating furnace, and is connected with the hearth of the heating furnace via a supporter. The upper end of a discharge tube with a cooling jacket is hermetically connected with the bottom end of the reduction pot, and the lower end of the discharge tube is provided with an openable/closable discharging device that is hermetically sealed with the lower end of the discharge tube when closed. The inventive process and facility can efficiently reduce the time of the whole reduction procedure, increase the heat efficiency of the production process, and increase the production capacity of reduction pot by about one time without changing other production conditions, resulting in significant economic benefits.
Description
Technical field
The present invention relates to a kind of production technique and production unit thereof of production method and production unit thereof, particularly semi-continuously producing light metal of metal.
Background technology
Utilizing Pidgeon process to smelt light metal has at present become classical way, is example with the MAGNESIUM METAL, has the MAGNESIUM METAL more than 60% to utilize Pidgeon process to smelt.This method in the long-term production process, the problem that exists some can not be ignored.Application for a patent for invention as China Intellectual Property Office's on December 7th, 2005 disclosed " Pijiang metal refining method and equipment " by name, in application for a patent for invention, just mention some problems that exist in the present Pidgeon process smelting, disclose a kind of method that can strengthen Pidgeon process reduction jar heat transfer efficiency and creep resistance simultaneously.A kind of method of utilizing terrestrial attraction to realize Pidgeon process reduction jar automatic loading and unloading.A kind of method of the Pijiang metal reduction process being carried out the on-line continuous monitoring.The alkali-metal method of a kind of recovery reaction by-product.A kind of vertical reducing jar that utilizes above-mentioned all methods to build.A kind of Pidgeon process vertical reducing furnace that adopts above-mentioned vertical reducing jar to be built.The present invention comprises the improvement effect of skin river processing method and equipment: shortened the reduction reaction cycle, prolonged the work-ing life of reduction jar, realized automatic loading and unloading, realized on-line continuous monitoring, realized the alkali-metal recovery of reaction by-product to reduction process.But the technology of this patent application is in actual application, because a reduction jar employing is vertically mounted in the process furnace, material in the reduction jar has been full of a reduction jar inner chamber, resistance when the metallic vapor that is reduced enters crystallizer in the reduction jar increases, will cause the rate of recovery of metal to reduce, simultaneously because the temperature in the reduction jar is very high, the super heated rubber sealing-ring on the reduction jar discharge opening cover plate is very easy to inefficacy, cause reduction jar interior breaking of vacuum, the practical application of this technology is affected.
In addition, Pidgeon process is smelted in the light process of sending out metal, can't realize continuous production, its production technique: install raw material → sealing additional and vacuumize → add thermal reduction more than 10 hours → get rid of total overall reaction residue in the reduction jar in reduction tube, repeat said process then.In present production process, the temperature of charge during owing to each feeding in raw material is in room temperature state, and this just need be heated to the raw material in the reduction jar about 1200 ℃ by room temperature.Simultaneously, need the reacted material in the reduction jar is all drawn out when discharging, the temperature of reduction jar will descend rapidly like this.Will cause the calorific loss in the whole process of production very big like this.
Summary of the invention
The objective of the invention is to overcome the defective of above-mentioned prior art, a kind of production technique and the reduction apparatus that is used for this technology that can effectively improve the heat utilization efficiency in the production process and shorten the volatile metal of production of production cycle is provided.
For achieving the above object, technical scheme of the present invention is: a kind of production technique of semi-continuously producing light metal, this processing step is: feed, vacuumize, add thermal reduction, take out the reducing metal, reaction residues is discharged, it is characterized in that charging is by being fixedly mounted on the sealable preheating storage bin of vertical reducing upper end raw material to be packed in the reduction jar; The residual content of reduction jar internal reaction residue was greater than zero when reaction residues was discharged.
The residual content of above-mentioned reduction jar internal reaction material is more than or equal to 1/8 of total amount, smaller or equal to 1/3 of total amount.
The reduction apparatus that is used for the production technique of semi-continuously producing light metal, comprise the reduction jar that is vertically mounted in the process furnace, the metallic crystal device that is installed in reduction jar top, it is characterized in that the discharge port of preheating storage bin and the upper end of reduction jar fixedly link, the furnace bottom of process furnace is stretched out in the lower end of reduction jar, external stability at its extension is equipped with bracing frame, and the reduction jar links to each other with the furnace bottom of process furnace by bracing frame; The upper end of the discharge nozzle of band cooling jacket links to each other with the sealing of reduction jar lower end, but the lower end of discharge nozzle is equipped with the drawing mechanism of open and close, and this drawing mechanism is when closing and the lower end hermetic seal of discharge nozzle.
Rotating turnover panel has been connected through the hinge in the discharge port of above-mentioned preheating storage bin.
Above-mentioned drawing mechanism is by forming with discharge nozzle outside hinged outer gland sealing plate and interior blocking material plate, interior blocking material plate is hinged by hinge and discharge nozzle inwall, connect by connecting rod between outer gland sealing plate and the interior blocking material plate, the two ends of connecting rod respectively be fixedly mounted on the outer gland sealing plate and link to each other with hinge on the interior blocking material plate; When drawing mechanism is closed, outer gland sealing plate and the hermetic seal of discharge nozzle end.
On the above-mentioned outer gland sealing plate sealing member is installed, sealing part and discharge nozzle end cross-sectional match.
The lower surface and the horizontal plane of discharge nozzle acutangulate.
Be fixed with recovery tube in the above-mentioned reduction jar inner chamber, recovery tube is fixed in the reduction jar by the fixedly gusset that the inwall with its cylindrical and reduction jar links to each other, and has recovery holes on recovery tube.
The said fixing gusset is uniform two or more.
Above-mentioned recovery tube and fixedly gusset axial dimension less than the reduction jar axial dimension.
Characteristics of the present invention are: 1, owing in the upper end of reduction jar the preheating storage bin has been installed, can utilize the heat that produces in the reduction jar production process to preheat to the raw material that next batch enters in the reduction jar so on the one hand; On the other hand, absorbed a large amount of heats, just can effectively reduce the temperature of trim on the preheating storage bin, improved the work-ing life of sealing member owing to preheat raw material; The 3rd because the temperature that raw material enters when reducing jar is higher, can effectively reduce the time of heating raw in the whole reduction process.2, changed the technology of in the prior art reaction residues all being got rid of, kept a part of reaction residues in the output section of reduction jar, the speed that the temperature in the retort can be descended reduces, and has improved the thermo-efficiency of production process; Can effectively reduce the temperature of discharge port outer gland sealing plate on the other hand, improved the work-ing life of sealing member on the discharge port; 3, because the improvement of this technology and equipment, the recovery time that makes light metal was by present about 10 hours, be reduced to less than 6 hours, the ton energy consumption can reduce more than 1/5 in the production process, do not changing under other working conditions, the day throughput of the reduction jar of same specification will improve nearly one times, and the economic benefit of being brought is very significant.
Description of drawings
Accompanying drawing 1 is structural representation of the present invention;
The structural representation that accompanying drawing 2 reduces jar for the present invention;
Accompanying drawing 3 is the A-A cut-away view of this accompanying drawing 2.
Embodiment
Present embodiment is that example describes with the production MAGNESIUM METAL.As shown in Figure 1, the upper and lower part that is vertically mounted on the reduction jar 3 in the process furnace stretches out at the bottom of process furnace furnace roof 4 and the heating-furnace 6 respectively, and the middle portion of reduction jar is in the process furnace and is heated.In reduction jar 3 upper ends preheating storage bin 2 is installed, the discharge port of preheating storage bin links with the upper end sealing and fixing of reduction jar 3, on the reduction jar between preheating storage bin 2 and the process furnace furnace roof 4, be installed with MAGNESIUM METAL crystallizer 17, on MAGNESIUM METAL crystallizer 17, be fixed with the Link Port 18 that links to each other with vaccum-pumping equipment.The external stability of the lower end extension of reduction jar 3 is equipped with bracing frame 16, and the reduction jar links to each other with the furnace bottom 6 of process furnace by bracing frame 16; The upper end of the discharge nozzle 8 of band cooling jacket links to each other with a reduction jar lower end sealing, but the lower end of discharge nozzle 8 is equipped with the drawing mechanism of open and close, this device is by forming by hinge 15 hinged outer gland sealing plate 12 and interior blocking material plate 9 with discharge nozzle 8 is outside, interior blocking material plate 9 is hinged by hinge 14 and discharge nozzle 8 inwalls, interconnects by being fixedly mounted on hinge on outer gland sealing plate and the interior blocking material plate and the connecting rod 13 that links to each other with two hinges respectively between outer gland sealing plate 12 and the interior blocking material plate 9.
The turnover panel 19 that discharge port is opened and closed is installed in the discharge port of preheating storage bin 2, and turnover panel 19 is connected through the hinge at the discharge port inwall.Turnover panel 19 is in vertical unlocking position as shown in Figure 1, and during dotted line position among Fig. 1, material enters in the reduction jar by the preheating storage bin.When material installs to design flow, turnover panel 19 is turned to horizontal closed position, then with opening for feed sealing plate 1 and opening for feed sealing and fixing.
During reaction, the outer gland sealing plate 12 of reduction jar lower end passes through sealing member 10 hermetic seals with the end of discharge nozzle 8, and blocking material plate 9 is in horizontal closed position shown in Figure 1 in the while.The reduction jar vacuumizes by Link Port 18, makes the reduction jar carry out reduction reaction under vacuum.Shown in Fig. 2,3, owing to be fixed with metallic vapor recovery tube 3-1 in the inner chamber of reduction jars 3, recovery tube 3-1 is fixed in the reduction jar by fixing gusset 3-2, has to be used to make the metal that is reduced out to enter the recovery holes 3-3 of recovery tube on recovery tube.Fixedly the quantity of gusset 3-2 can design according to the size of throughput.The quantity of the fixedly gusset of present embodiment is 3, and the inner chamber that so just will reduce jar is divided into three relatively independent chamber 3-4.Because after the outer wall of reduction jar heated by process furnace, heat rapidly to a reduction jar internal delivery, also can rise the temperature of charge in reduction jar interior centre by fixing gusset rapidly, can effectively reduce the heat-up time of material.After the MAGNESIUM METAL steam that is reduced overflows, enter by recovery holes 3-3 among the recovery tube 3-1 at reduction jar lumen centers position, enter in the crystallizer in the reduction jar by recovery tube and carry out crystallization.Because the existence of recovery tube, can effectively reduce the MAGNESIUM METAL steam and enter resistance in the crystallizer, improved the rate of recovery and the crystallization time of reduction jar.
Reaction is opened the outer gland sealing plate by the handle 11 that is fixed on the outer gland sealing plate after finishing, because the effect of connecting rod 13, interior blocking material plate is opened simultaneously in company with the outer gland sealing plate, and reacted waste residue flows out the discharge port of reduction jar bottom along interior blocking material plate.Because the effect of blocking material plate, the waste residue that has a certain temperature not with the outer gland sealing plate on contact with the discharge nozzle end cross-sectional sealing member 10 that matches, prolonged the work-ing life of sealing member.
In order further to reduce the drop temperature of waste residue, cooling jacket 7 is installed on discharge nozzle 8.
When discharging, not that reaction residues is all got rid of, but kept a part of reaction residues in the discharge nozzle of reduction jar.According to the character and the processing condition of reducing metal, the amount that keeps reaction residues is more than or equal to 1/8 of the material total amount of adorning in the reduction jar, smaller or equal to 1/3 of total amount, decrease of temperature speed slowed down.
After discharging finishes, with the outer gland sealing plate 12 of reduction jar lower end and the end hermetic seal of discharge nozzle 8, the turnover panel 19 that will be fixed on then on the discharge port of preheating storage bin 2 of reduction jar upper end is opened, be contained in the interior material of preheating storage bin and enter in the reduction jar, because the material in the reduction jar heats the material in the preheating storage bin when reacting, after this material enters the reduction jar, by the process furnace heating, can reach the temperature of reduction reaction soon, saved the heating-up time and the required energy of heating.The heating energy source of process furnace can be coal, combustion gas, electric energy equal energy source.
The lower surface and the horizontal plane of discharge nozzle acutangulate, and this acute angle is preferably 30-48 °.
Claims (10)
1. the production technique of a semi-continuously producing light metal, this processing step is: feed, vacuumize, add thermal reduction, take out the reducing metal, reaction residues is discharged, it is characterized in that charging is by being fixedly mounted on the sealable preheating storage bin of vertical reducing upper end raw material to be packed in the reduction jar; The residual content of reduction jar internal reaction residue was greater than zero when reaction residues was discharged.
2. the production technique of a kind of semi-continuously producing light metal according to claim 1, the residual content that it is characterized in that above-mentioned reduction jar internal reaction material is more than or equal to 1/8 of total amount, smaller or equal to 1/3 of total amount.
3. the reduction apparatus that is used for the production technique of the described semi-continuously producing light metal of production claim 1, comprise the reduction jar that is vertically mounted in the process furnace, the MAGNESIUM METAL crystallizer that is installed in reduction jar top, it is characterized in that the discharge port of preheating storage bin (2) and the upper end of reduction jar (3) fixedly link, the furnace bottom (6) of process furnace is stretched out in the lower end of reduction jar (3), external stability at its extension is equipped with bracing frame (16), and reduction jar (3) links to each other with the furnace bottom (6) of process furnace by bracing frame (16); The upper end of the discharge nozzle (8) of band cooling jacket links to each other with the sealing of reduction jar lower end, discharge nozzle (8) but the lower end drawing mechanism of open and close is installed, this drawing mechanism is when closing and the lower end hermetic seal of discharge nozzle (8).
4. a kind of reduction apparatus according to claim 3 is characterized in that the rotating turnover panel (19) that has been connected through the hinge in the discharge port of above-mentioned preheating storage bin (2).
5. according to claim 3 or 4 described a kind of reduction apparatuss, it is characterized in that above-mentioned drawing mechanism is by forming with discharge nozzle (8) outside hinged outer gland sealing plate (12) and interior blocking material plate (9), interior blocking material plate (9) is hinged by hinge (14) and discharge nozzle (8) inwall, connect by connecting rod (13) between outer gland sealing plate (12) and the interior blocking material plate (9), the two ends of connecting rod (13) respectively be fixedly mounted on outer gland sealing plate (12) and link to each other with hinge on the interior blocking material plate (9); At drawing mechanism when closing, outer gland sealing plate (12) and discharge nozzle (8) end hermetic seal.
6. a kind of reduction apparatus according to claim 5 is characterized in that being equipped with sealing member (10) on above-mentioned outer gland sealing plate (12), sealing part and discharge nozzle (8) end cross-sectional matches.
7. a kind of reduction apparatus according to claim 6 is characterized in that the lower surface and the horizontal plane of discharge nozzle (8) acutangulates.
8. a kind of reduction apparatus according to claim 3 is characterized in that above-mentioned reduction jar (3) inner chamber gusset (3-2) is fixed with recovery tube (3-1), has recovery holes (3-3) on recovery tube (3-1).
9. a kind of reduction apparatus according to claim 8 is characterized in that said fixing gusset (3-2) is uniform two or more.
10. according to Claim 8 or 9 described a kind of reduction apparatuss, it is characterized in that above-mentioned recovery tube (3-1) and fixedly the axial dimension of gusset (3-2) less than the axial dimension of reduction jar.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2006100947670A CN101104886A (en) | 2006-07-13 | 2006-07-13 | Technique for semi-continuously producing light metal and producing device thereof |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2006100947670A CN101104886A (en) | 2006-07-13 | 2006-07-13 | Technique for semi-continuously producing light metal and producing device thereof |
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| CN101104886A true CN101104886A (en) | 2008-01-16 |
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| CNA2006100947670A Pending CN101104886A (en) | 2006-07-13 | 2006-07-13 | Technique for semi-continuously producing light metal and producing device thereof |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102080160A (en) * | 2011-01-25 | 2011-06-01 | 吕天文 | Reduction device for manufacturing magnesium and production process thereof |
| CN101676419B (en) * | 2008-05-13 | 2011-06-15 | 辛卫亚 | Semi-continuous production metal vacuum smelting reduction device |
| CN101314816B (en) * | 2008-05-13 | 2012-01-04 | 辛卫亚 | Liquid crystallizer |
| CN102534252A (en) * | 2012-03-16 | 2012-07-04 | 五台云海镁业有限公司 | Magnesium smelting method capable of shortening reduction period |
| CN102692129A (en) * | 2012-03-19 | 2012-09-26 | 沈阳鑫博工业技术发展有限公司 | Magnesium metal continuous production equipment and process method |
| CN106191014A (en) * | 2016-07-12 | 2016-12-07 | 广州华缘食品科技有限公司 | A kind of enzyme preparation with de-painstaking effort energy and its preparation method and application |
| CN114774716A (en) * | 2022-06-06 | 2022-07-22 | 陕西秦龙电力股份有限公司 | Pidgeon process magnesium metal reduction device |
-
2006
- 2006-07-13 CN CNA2006100947670A patent/CN101104886A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101676419B (en) * | 2008-05-13 | 2011-06-15 | 辛卫亚 | Semi-continuous production metal vacuum smelting reduction device |
| CN101314816B (en) * | 2008-05-13 | 2012-01-04 | 辛卫亚 | Liquid crystallizer |
| CN102080160A (en) * | 2011-01-25 | 2011-06-01 | 吕天文 | Reduction device for manufacturing magnesium and production process thereof |
| CN102534252A (en) * | 2012-03-16 | 2012-07-04 | 五台云海镁业有限公司 | Magnesium smelting method capable of shortening reduction period |
| CN102534252B (en) * | 2012-03-16 | 2013-06-26 | 五台云海镁业有限公司 | Magnesium smelting method capable of shortening reduction period |
| CN102692129A (en) * | 2012-03-19 | 2012-09-26 | 沈阳鑫博工业技术发展有限公司 | Magnesium metal continuous production equipment and process method |
| CN106191014A (en) * | 2016-07-12 | 2016-12-07 | 广州华缘食品科技有限公司 | A kind of enzyme preparation with de-painstaking effort energy and its preparation method and application |
| CN106191014B (en) * | 2016-07-12 | 2019-12-31 | 广州华缘食品科技有限公司 | Enzyme preparation with debitterizing function and preparation method and application thereof |
| CN114774716A (en) * | 2022-06-06 | 2022-07-22 | 陕西秦龙电力股份有限公司 | Pidgeon process magnesium metal reduction device |
| CN114774716B (en) * | 2022-06-06 | 2024-05-03 | 陕西秦龙电力股份有限公司 | Pidgeon method magnesium metal reduction device |
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Open date: 20080116 |