CN102923718A - High-temperature gasification reaction pipe of quartz sand purifying device - Google Patents
High-temperature gasification reaction pipe of quartz sand purifying device Download PDFInfo
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- CN102923718A CN102923718A CN2012103726410A CN201210372641A CN102923718A CN 102923718 A CN102923718 A CN 102923718A CN 2012103726410 A CN2012103726410 A CN 2012103726410A CN 201210372641 A CN201210372641 A CN 201210372641A CN 102923718 A CN102923718 A CN 102923718A
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- reaction tubes
- temperature gasification
- quartz sand
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- reaction pipe
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Abstract
The invention provides a high-temperature gasification reaction pipe of a quartz sand purifying device. The high-temperature gasification reaction pipe is a horizontal reaction pipe. One end of the reaction pipe is provided with a shrinking gas inlet, the pipe wall of the reaction pipe, which is close to the gas inlet, is provided with at least one discharging hole, and the gas inlet is positioned in the center axial line of the reaction pipe. The other end of the reaction pipe is provided with a shrinking feeding hole, and the feeding hole is arranged in the center axial line of the reaction pipe. The horizontal reaction pipe is adopted without enabling the pipe body to reach an integrally filling state, thus the problem that the reaction pipe is broken due to phase change and volume expansion of quartz under a high temperature condition. The whole pipe body realizes that materials continuously overturn in a rotating process to ensure that the reaction is carried out more fully and the reaction efficiency is high as well as the problems of hardening, adhering and the like cannot be easily caused.
Description
Technical field
The present invention relates to a kind of high-temperature gasification reaction tubes of purification device for quartz sand, particularly a kind of physical chemistry purification techniques of at high temperature removing element impurity in the quartz sand.
Background technology
Glass sand is high-purity nonmetalliferous ore raw material of being produced through purification techniques series of physical and chemistry by the natural quartz mineral, internationally recognized glass sand is to be higher than U.S. You Niming (UNIMIN) IOTA-CG of company standard, the content of 13 kinds of element impurity (comprising Al, K, Na, Li, Ti, Ca, Mg, Fe, Mn, Cu, Cr, Ni and B) is less than 22ppm, and wherein the content of each basic metal (K, Na and Li) is respectively less than the high-tech product of 1ppm.
Glass sand is the main raw material(s) of producing purity quartz glass pipe for high/rod and quartz glass crucibles, and silica glass is widely used in high-end electric light source, reaches in the industries such as super large-scale integration, solar cell, optical fiber, laser, space flight, military affairs on a large scale with its good physics and chemistry performance.
The raw ore of glass sand is the natural quartz ore, in the quartz mine except quartz, usually contain the plurality of impurities mineral, common impure mineral has mica, feldspar, iron titanium oxide etc., quartzy itself often contain some metal or non-metallic element impurity because of crystal structure defects or microfissure, and fluid impurity.Can most of Impurity removal be fallen by means such as flotation, magnetic separation, gravity treatment, acidleach, calcinings, but be difficult to accomplish some element in the glass sand is reduced to requirement less than 1ppm.
The shortcoming of the employed high-temperature gasification reaction tubes of quartz sand high-temperature gasification purifying plant of the prior art is that the residence time of quartz sand in reaction tubes is short, react insufficient, yield poorly, and easily leak poisonous chemical treatment gas, environment and the person are caused higher threat.
Summary of the invention
For problems of the prior art, the invention provides the high-temperature gasification reaction tubes of purification device for quartz sand, one end of this reaction tubes has the inlet mouth of contraction, has at least one discharge port at the tube wall near inlet mouth one end, described inlet mouth is positioned on the central axis of this reaction tubes, and the other end of this reaction tubes has opening for feed.Has the angle theta between the water flat wall that is connected straight line and reaction tubes between water flat wall limit end and the air intake ports of reaction tubes of inlet mouth one end
1Satisfy 90 °≤θ
1<180 °.More than the little 20mm of internal diameter of the internal diameter of described inlet mouth than reaction tubes.Described opening for feed is positioned on the central axis of this reaction tubes, more than the little 20mm of internal diameter of the internal diameter of this opening for feed than reaction tubes.Has the angle theta between the water flat wall that is connected straight line and reaction tubes between water flat wall limit end and the opening for feed port of reaction tubes of opening for feed one end
2Satisfy 90 °≤θ
2<180 °.
Described opening for feed is positioned on the central axis of this reaction tubes, and the internal diameter of this opening for feed equates with the internal diameter of this reaction tubes.The total flux area of described discharge port is 25mm
2~400mm
2Described high-temperature gasification reaction tubes adopting quartz glass pipe, its working temperature is 1000 ℃ ~ 1400 ℃.
The advantage that the present invention has is:
1, the present invention adopts the horizontal reacting pipe, need not body and reaches the state that integral body is filled up, and avoids the problem of breaking because of quartz undergoes phase transition under hot conditions, volumetric expansion causes reaction tubes.
2, whole body is realized the continuous rolling of material in rotation process, makes reaction more abundant, and reaction efficiency is high, is not easy to harden, the problem such as adhesion.
3, the two ends of reaction tubes (inlet mouth and opening for feed) adopts contraction mouth, can keep material that the long residence time is arranged in reaction tubes, and the chemical reaction between element impurity and the reactant gases is more complete, can reach best impurity elimination effect.
Description of drawings
Fig. 1 is the structural representation of the high-temperature gasification reaction tubes of the purification device for quartz sand that proposes of the present invention.
Fig. 2 is the another kind of structural representation of the high-temperature gasification reaction tubes of the purification device for quartz sand that proposes of the present invention.
Among the figure: the 1-quartz glass tube; The 2-opening for feed; The 3-discharge port; The 4-inlet mouth.
Embodiment
The invention will be further described below in conjunction with the drawings and specific embodiments, can be implemented so that those skilled in the art can better understand the present invention also, but illustrated embodiment is not as a limitation of the invention.
The present invention proposes a kind of high-temperature gasification reaction tubes of purification device for quartz sand, is used for removing element impurity, particularly basic metal and the transition metal impurity of quartz sand.The purity quartz glass pipe for high 1 that high-temperature gasification reaction tubes 1 adopts glass sand to make among the present invention, working temperature is 1000 ℃ ~ 1400 ℃.One end of this reaction tubes has the inlet mouth 4 that is shunk by the reaction tubes end, as shown in Figure 1, described inlet mouth 4 is positioned on the central axis of this reaction tubes, and this inlet mouth 4 can directly be shunk by the reaction tubes end and form, and namely the reaction tubes end has an internal diameter less than the inlet mouth 4 of reaction tubes caliber; Also can be formed to the outside contraction by the reaction tubes end, can shrink with taper, also can shrink with vertical wall first, shrink with taper or other forms again.The angle theta of described reaction tubes between the water flat wall that is connected straight line and reaction tubes between the port of the reaction tubes water flat wall limit end with inlet mouth end and inlet mouth 4
1Satisfy 90 °≤θ
1<180 °.The port internal diameter of this inlet mouth 4 is than more than the little 20mm of high-temperature gasification tube inner diameter.Have at least one discharge port 3 near the tube wall of inlet mouth 4 one sides, described discharge port 3 different can be circle, the different shape such as square, and the total flux area of all discharge ports 3 is 25mm
2~400mm
2The other end of this reaction tubes has opening for feed 2, and this opening for feed 2 is positioned on the central axis of high-temperature gasification reaction tubes, and the internal diameter of this opening for feed 2 is identical with the internal diameter of high-temperature gasification reaction tubes, is straight shape mouth.Opening for feed 2 also can be selected contraction mouth, and shrink form is not limit, and can be bell, the angle theta of described reaction tubes between the water flat wall that is connected straight line and reaction tubes between the port of the reaction tubes water flat wall limit end with feed inlet end and opening for feed 2
2Satisfy 90 °≤θ
2<180 °.As shown in Figure 2, more than the little 20mm of internal diameter of the internal diameter of opening for feed 2 than high-temperature gasification reaction tubes, better than the refining effect of straight shape mouth when opening for feed 2 is chosen as contraction mouth.
The high-temperature gasification reaction tubes is placed horizontal electric furnace, tilted to discharge port 3 directions by opening for feed 2.Obtain to support and power by transmission mechanism, in electric furnace, rotate.By vibratory feeder material is sent into from opening for feed 2, imported chemical reaction gas from inlet mouth 4.By heating by electric cooker, working temperature is 1000 ℃-1400 ℃.Material is constantly counter-rotating in the high-temperature gasification reaction tubes of rotation, dynamically with reactant gases generation hot conditions under physics-chemical reaction, remove the impurity element in the quartz sand, and obtain power to discharge port 3 motions, from discharge port 3 outflows.
The above embodiment is the preferred embodiment that proves absolutely that the present invention lifts, and protection scope of the present invention is not limited to this.Being equal to that those skilled in the art do on basis of the present invention substitutes or conversion, all within protection scope of the present invention.Protection scope of the present invention is as the criterion with claims.
Claims (8)
1. the high-temperature gasification reaction tubes of a purification device for quartz sand, this high-temperature gasification reaction tubes is the horizontal reacting pipe, it is characterized in that, one end of this reaction tubes has the inlet mouth of contraction, has at least one discharge port at the tube wall near inlet mouth one end, described inlet mouth is positioned on the central axis of this reaction tubes, and the other end of this reaction tubes has opening for feed.
2. the high-temperature gasification reaction tubes of purification device for quartz sand according to claim 1 is characterized in that, has the angle theta between the water flat wall that is connected straight line and reaction tubes between water flat wall limit end and the air intake ports of reaction tubes of inlet mouth one end
1Satisfy 90 °≤θ
1<180 °.
3. the high-temperature gasification reaction tubes of purification device for quartz sand according to claim 1 is characterized in that, more than the little 20mm of internal diameter of the internal diameter of described inlet mouth than reaction tubes.
4. the high-temperature gasification reaction tubes of purification device for quartz sand according to claim 1 is characterized in that, described opening for feed is positioned on the central axis of this reaction tubes, more than the little 20mm of internal diameter of the internal diameter of this opening for feed than reaction tubes.
5. the high-temperature gasification reaction tubes of purification device for quartz sand according to claim 4 is characterized in that, has the angle theta between the water flat wall that is connected straight line and reaction tubes between water flat wall limit end and the opening for feed port of reaction tubes of opening for feed one end
2Satisfy 90 °≤θ
2<180 °.
6. the high-temperature gasification reaction tubes of purification device for quartz sand according to claim 1 is characterized in that, described opening for feed is positioned on the central axis of this reaction tubes, and the internal diameter of this opening for feed equates with the internal diameter of this reaction tubes.
7. the high-temperature gasification reaction tubes of purification device for quartz sand according to claim 1 is characterized in that, the total flux area of described discharge port is 25mm
2~400mm
2
8. the high-temperature gasification reaction tubes of purification device for quartz sand according to claim 1 is characterized in that, described high-temperature gasification reaction tubes adopting quartz glass pipe, and its working temperature is 1000 ℃ ~ 1400 ℃.
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CN2012103726410A CN102923718A (en) | 2012-09-29 | 2012-09-29 | High-temperature gasification reaction pipe of quartz sand purifying device |
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CN2012103726410A CN102923718A (en) | 2012-09-29 | 2012-09-29 | High-temperature gasification reaction pipe of quartz sand purifying device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108328920A (en) * | 2018-04-23 | 2018-07-27 | 江苏景泰玻璃有限公司 | A kind of horizontal gasification reaction tube of quartz sand purifying |
CN108439415A (en) * | 2018-04-10 | 2018-08-24 | 东海县晶盛源硅微粉有限公司 | A kind of quartz sand high-temperature gasification reaction tube |
Citations (5)
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---|---|---|---|---|
US4956059A (en) * | 1988-10-29 | 1990-09-11 | Heraeus Quarzschmelze Gmbh | Process for the purification of granular silicon dioxide |
US5637284A (en) * | 1995-04-10 | 1997-06-10 | Heraeus Quarzglas Gmbh | Process for continuous refining of quartz powder |
CN200999203Y (en) * | 2006-12-31 | 2008-01-02 | 陈士斌 | Quartz sand high-heating calcining evaporated purification apparatus |
CN201974027U (en) * | 2010-12-13 | 2011-09-14 | 安徽好思家涂料有限公司 | Rolling type quartz sand coloring heating furnace |
CN202968142U (en) * | 2012-09-29 | 2013-06-05 | 江苏太平洋石英股份有限公司 | High temperature gasification reaction tube for quartz sand purifying device |
-
2012
- 2012-09-29 CN CN2012103726410A patent/CN102923718A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4956059A (en) * | 1988-10-29 | 1990-09-11 | Heraeus Quarzschmelze Gmbh | Process for the purification of granular silicon dioxide |
US5637284A (en) * | 1995-04-10 | 1997-06-10 | Heraeus Quarzglas Gmbh | Process for continuous refining of quartz powder |
CN200999203Y (en) * | 2006-12-31 | 2008-01-02 | 陈士斌 | Quartz sand high-heating calcining evaporated purification apparatus |
CN201974027U (en) * | 2010-12-13 | 2011-09-14 | 安徽好思家涂料有限公司 | Rolling type quartz sand coloring heating furnace |
CN202968142U (en) * | 2012-09-29 | 2013-06-05 | 江苏太平洋石英股份有限公司 | High temperature gasification reaction tube for quartz sand purifying device |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108439415A (en) * | 2018-04-10 | 2018-08-24 | 东海县晶盛源硅微粉有限公司 | A kind of quartz sand high-temperature gasification reaction tube |
CN108328920A (en) * | 2018-04-23 | 2018-07-27 | 江苏景泰玻璃有限公司 | A kind of horizontal gasification reaction tube of quartz sand purifying |
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Application publication date: 20130213 |