CN201208516Y - Fractionating tower capable of removing hydrogen-containing purity in germanic chloride - Google Patents

Fractionating tower capable of removing hydrogen-containing purity in germanic chloride Download PDF

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Publication number
CN201208516Y
CN201208516Y CNU2008200811656U CN200820081165U CN201208516Y CN 201208516 Y CN201208516 Y CN 201208516Y CN U2008200811656 U CNU2008200811656 U CN U2008200811656U CN 200820081165 U CN200820081165 U CN 200820081165U CN 201208516 Y CN201208516 Y CN 201208516Y
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CN
China
Prior art keywords
tower
rectifying column
pipe
hydrogen containing
containing foreign
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.)
Expired - Lifetime
Application number
CNU2008200811656U
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Chinese (zh)
Inventor
周廷熙
王少龙
钟文
晏勇
彭明清
阎建英
王瑞山
冯玉庭
张文金
张院萍
杨光玉
何斌
李雪寅
赵永波
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yunnan Chihong Zinc and Germanium Co Ltd
Original Assignee
Yunnan Chihong Zinc and Germanium Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Yunnan Chihong Zinc and Germanium Co Ltd filed Critical Yunnan Chihong Zinc and Germanium Co Ltd
Priority to CNU2008200811656U priority Critical patent/CN201208516Y/en
Application granted granted Critical
Publication of CN201208516Y publication Critical patent/CN201208516Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to a rectifying tower for removing CH impurities and HCI impurities from Germanic chloride for optical fibers, which mainly used for solving the problem of removing the CH impurities and the HCI impurities from Germanic chloride, belongs to the special equipment field, and mainly comprises a column reactor, a tower tube and a tower head. A spiral cooling water pipe, a cooling water inlet and a cooling water outlet are formed on the tower head; a gas outlet is formed at the top of the tower head; a pipeline connected with a wigwagging discharge hole is arranged on the gas outlet, and the lower part thereof is communicated with the lower end of the tower head; the bottom of the wigwagging discharge hole is communicated with the upper part of the tower tube through the pipeline; a feeding hole, a gas supplying port, a temperature monitoring port and a scrap discharge outlet are formed on the column reactor.

Description

A kind of rectifying column of removing hydrogen containing foreign in the germanium tetrachloride
Technical field the utility model relates to a kind of in producing the germanium tetrachloride for optical fibre product, removes the rectifying column of hydrogen containing foreign in the germanium tetrachloride, particularly removes the rectifying column of CH and HCl impurity.Belong to the special equipment field.
The conventional at present rectifying column of background technology can be removed metal impurities preferably, as Fe, Co, Cr, Mn, Cu etc., but can't remove hydrogen containing foreign (as CH, HCl) effectively.Adopt hydrogen chloride gas or anhydrous chlorine to come purifying germanium tetrachloride separately, can only remove arsenic and other similar impurity, and can not remove hydrogen containing foreign effectively; Though can handle germanium tetrachloride under the high temperature more than 800 ℃ by high temperature service, making hydrogen atom wherein is hydrogen chloride by chlorinated with chlorine, the final removal that realizes hydrogen containing foreign, and this technology is very high to the requirement of equipment, and complicated operation.
The summary of the invention the purpose of this utility model is to provide a kind of rectifying column of removing hydrogen containing foreign in the germanium tetrachloride, it can be lower than under 100 ℃ the temperature, remove hydrogen containing foreign in the germanium tetrachloride (CH and HCl) efficiently, easily, to satisfy the needs of producing germanium tetrachloride for optical fibre.
The technical scheme that the utility model is removed the rectifying column of hydrogen containing foreign in the germanium tetrachloride is:
This rectifying column mainly is made up of the tower still (1) of bottom, the tower head (3) at top and the tower pipe (2) of connection tower still (1) and tower head (3).
Leave charging aperture (4), gas supply mouth (5) and temperature monitoring mouth (6) at tower still (1) top, at tower still (1) middle part actinolyte (7) is arranged, in tower still (1) bottom heating tube (8) and trash discharge mouth (9) are arranged, tower pipe (2) does not have column plate, is a blank pipe.
Tower head (3) is provided with helical form water pipe (16), cooling water inlet (10) and coolant outlet (11), tower head (3) highest point has tail gas outlet (12), tower head (3) right lower quadrant is connected to fluid collection tube (14), fluid collection tube (14) is communicated with by the surplus liquid return duct of tail gas (13) with tail gas outlet (12), and be connected to yaw discharging opening (15) in fluid collection tube (14) bottom, the lower left quarter of yaw discharging opening (15) flows the upper lateral part that pipe (17) feeds tower pipe (2) once.
Actinolyte (7) is installed on the axis of tower still (1).Whole removal rectifying column is the transparent body, all adopts quartz material.
The beneficial effects of the utility model are: can intuitive and convenient ground observe whole Impurity removal process, and carry out being lower than under 100 ℃ of temperature, simple in structure, easy to operate, safe and reliable, impurity removal efficacy is higher.
Description of drawings further describes its specific embodiment below in conjunction with accompanying drawing of the present utility model.
Fig. 1 is the rectifying column schematic diagram of CH and HCl impurity in the utility model removal germanium tetrachloride.
The tower of 1-shown in figure still, 2-tower pipe, 3-tower head, the 4-charging aperture, 5-gas supply mouth, 6-temperature monitoring mouth, the 7-actinolyte, 8-heating tube, 9-trash discharge mouth, the 10-cooling water inlet, 11-coolant outlet, the outlet of 12-tail gas, the surplus liquid return duct of 13-tail gas, 14-fluid collection tube, 15-yaw discharging opening, 16-helical form water pipe, the 17-return duct
The specific embodiment
Embodiment: rectifying column is made of the tower still 1 of bottom, the tower head 3 on top and the middle part tower pipe 2 of connection tower still 1 and tower head 3, is provided with heating tube 8 and actinolyte 7 in tower still 1.Leave charging aperture 4 and gas supply mouth 5 at tower still 1 top, have temperature monitoring mouth 6, have trash discharge mouth 9 in tower still 1 bottom at tower still 1 sidepiece.
Tower head 3 is provided with helical form water pipe 16, cooling water inlet 10 and coolant outlet 11, tower head 3 highest points have tail gas outlet 12, tower head 3 right lower quadrants are connected to fluid collection tube 14, fluid collection tube 14 and tail gas outlet 12 is communicated with by the surplus liquid return duct 13 of tail gas, and be connected to yaw discharging opening 15 in fluid collection tube 14 bottoms, the lower left quarter of yaw discharging opening 15 flows the upper lateral part that pipe 17 feeds tower pipe 2 once.
Whole rectifying column is transparent, all adopts quartz material.
During use, the germanium tetrachloride that needs are purified joins in the tower still 1 by charging aperture 4, after heating, process heating tube 8 makes germanium tetrachloride boiling volatilization, the germanium tetrachloride that evaporates rises by tower pipe (2) and arrives the tower head (3) on this rectifying column top, through helical form water pipe (16) condensation, condensed germanium tetrachloride and is collected or is back in the tower still 1 by return duct (17) by control yaw discharging opening (15) in the surplus liquid return duct of tail gas (13) influent collecting pipe (14).Removal of impurity technical process of the present invention can be in this rectifying column continuous repetitive cycling, impurity content reaches the germanium tetrachloride for optical fibre standard in germanium tetrachloride, carries out formal discharging and collects qualified products from yaw discharging opening 15.
Cooling water enters the circulation back from coolant outlet 11 discharges from the cooling import 10 of helical form water pipe (16).
The real-time monitoring of running temperature and the timely heating tube of adjusting make heating-up temperature reach the required requirement of technology in 6 pairs of tower stills 1 of temperature monitoring mouth.
In heating process, according to arts demand, can feed protective gas from tower still 1 gas supply mouth 5, avoid apparatus of the present invention to be secondary polluted being used for removing hydrogen containing foreign process germanium tetrachloride.
In the removal of impurity process, need open 7 pairs of germanium tetrachlorides of actinolyte and carry out illumination.
Surplus liquid after purifying in this rectifying Tata still 1 is discharged this rectifying column by trash discharge mouth 9.
The utility model is used for germanium tetrachloride for optical fibre production and removes impurity CH and HCl, to satisfy the purity requirement of germanium tetrachloride for optical fibre product.

Claims (6)

1, a kind of rectifying column of removing hydrogen containing foreign in the germanium tetrachloride is characterized in that this rectifying column mainly is made up of the tower head (3) at the tower still (1) of bottom, top and the tower pipe (2) that connects tower still (1) and tower head (3).
2, the rectifying column of hydrogen containing foreign in the removal germanium tetrachloride according to claim 1, it is characterized in that leaving charging aperture (4), gas supply mouth (5) and temperature monitoring mouth (6) at tower still (1) top, at tower still (1) middle part actinolyte (7) is arranged, heating tube (8) and trash discharge mouth (9) are arranged in tower still (1) bottom.
3, the rectifying column of hydrogen containing foreign in the removal germanium tetrachloride according to claim 1 is characterized in that tower pipe (2) does not have column plate, is a blank pipe.
4, the rectifying column of hydrogen containing foreign in the removal germanium tetrachloride according to claim 1, it is characterized in that tower head (3) is provided with helical form water pipe (16), cooling water inlet (10) and coolant outlet (11), tower head (3) highest point has tail gas outlet (12), tower head (3) right lower quadrant is connected to fluid collection tube (14), fluid collection tube (14) is communicated with by the surplus liquid return duct of tail gas (13) with tail gas outlet (12), and be connected to yaw discharging opening (15) in fluid collection tube (14) bottom, the lower left quarter of yaw discharging opening (15) flows the upper lateral part that pipe (17) feeds tower pipe (2) once.
5, according to the rectifying column of hydrogen containing foreign in claim 1 and the 2 described removal germanium tetrachlorides, it is characterized in that actinolyte (7) is installed on the axis of tower still (1).
6, the rectifying column of hydrogen containing foreign in the removal germanium tetrachloride according to claim 1 is characterized in that whole removal rectifying column is the transparent body, all adopts quartz material.
CNU2008200811656U 2008-05-07 2008-05-07 Fractionating tower capable of removing hydrogen-containing purity in germanic chloride Expired - Lifetime CN201208516Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008200811656U CN201208516Y (en) 2008-05-07 2008-05-07 Fractionating tower capable of removing hydrogen-containing purity in germanic chloride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008200811656U CN201208516Y (en) 2008-05-07 2008-05-07 Fractionating tower capable of removing hydrogen-containing purity in germanic chloride

Publications (1)

Publication Number Publication Date
CN201208516Y true CN201208516Y (en) 2009-03-18

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103183375A (en) * 2011-12-29 2013-07-03 北京有色金属研究总院 Preparation purification method of germanium tetrachloride for optical fiber
CN106730964A (en) * 2015-11-25 2017-05-31 衡阳恒荣高纯半导体材料有限公司 A kind of distilling apparatus for producing high-purity germanium tetrachloride

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103183375A (en) * 2011-12-29 2013-07-03 北京有色金属研究总院 Preparation purification method of germanium tetrachloride for optical fiber
CN106730964A (en) * 2015-11-25 2017-05-31 衡阳恒荣高纯半导体材料有限公司 A kind of distilling apparatus for producing high-purity germanium tetrachloride

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C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20090318

Effective date of abandoning: 20080507