CN2458280Y - Device for pumping titanium tetrachloride back into furnace - Google Patents

Device for pumping titanium tetrachloride back into furnace Download PDF

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Publication number
CN2458280Y
CN2458280Y CN 00252776 CN00252776U CN2458280Y CN 2458280 Y CN2458280 Y CN 2458280Y CN 00252776 CN00252776 CN 00252776 CN 00252776 U CN00252776 U CN 00252776U CN 2458280 Y CN2458280 Y CN 2458280Y
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CN
China
Prior art keywords
furnace
valve
material feeding
material loading
chlorination
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
CN 00252776
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Chinese (zh)
Inventor
刘长河
张清
刘希福
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.)
CITIC Jinzhou Ferroalloy Co Ltd
Original Assignee
TITANIUM WHITE FACTORY JINZHU
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.)
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Publication date
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Priority to CN 00252776 priority Critical patent/CN2458280Y/en
Application granted granted Critical
Publication of CN2458280Y publication Critical patent/CN2458280Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to a device of slurry returning to a chlorination furnace through a fused salt chlorination procedure in chlorination process rutile type titanium dioxide production. The inner side of a slurry tank is provided with a stirrer and a slurry pump, wherein, the slurry pump is connected with a material feeding pipe passage; the other end of the material feeding pipe passage is connected with a material feeding valve and a return valve; the material feeding valve is connected with an ejector; the return valve is connected with a slurry tank through a return pipe passage; the slurry tank is arranged on the lower side of a leaching tower; the ejector is arranged on the top part of the chlorination furnace. The utility model can prevent a leaching system from clogging and ensure a furnace temperature within a control range.

Description

Titanium tetrachloride mud returns furnace apparatus
The utility model belongs to the halogenide oxidation style and produces titanium dioxide, and particularly fused salt chlorimation system crude titanic chloride mud returns furnace apparatus in the chlorination process Rutile type Titanium Dioxide production process.
The mechanism of fused salt chlorimation reaction is that (main component is TiO with titanium slag or rutile 2) issue biochemical reaction generation titanium tetrachloride and other product with chlorine in the activated carbon effect at a certain temperature.This process belongs to thermopositive reaction.Because the plasticity-of fused salt chlorimation stove throughput is very big, surpass design load easily, be that 65t/ days fused salt chlorimation stove can be produced 130t/ days now as the our factory designed capacity.Intrinsic like this heat balance system is broken, and causes furnace temperature to raise, and the muriatic vapour pressure of various high boiling points in the stove is raise, and enter elution circuit, causes that solid content increases in the washing lotion, is easy to cause elution circuit to stop up and leads to a disaster.
The purpose of this utility model provides a kind of device that can as required mud be led back chlorination furnace, with control reaction in furnace temperature, draws unnecessary heat, prevents that elution circuit from stopping up, and avoids accident to take place.
To achieve these goals, following technical scheme is proposed.
A kind of titanium tetrachloride mud returns furnace apparatus, it is characterized in that agitator and slush pump are installed in the mud tank, slush pump links to each other with the material loading pipeline, and the other end of material loading pipeline connects material loading valve and return valve, the material loading valve connects injector, and return valve links to each other with mud tank by return line.Mud tank places below the eluting column, has a drip washing pump that washing lotion is drawn, and carries out heat exchange by double pipe cooler, sprays in the eluting column after the reduction temperature again.Injector is installed in the top of chlorination furnace.
Because agitator and slush pump are installed in mud tank, mud is back and forth flowed in pipeline, avoid elution circuit to stop up, and the open degree that can regulate material loading valve and return valve as required, control mud returns, sprays into chlorination furnace.Because the furnace high-temperature effect make liquid phase titanium tetrachloride heat absorption back gasification enter smoke processing system again, and mud falls into fused salt in the stove, together discharges with abraum salt.Absorb a large amount of heat energy more than needed when becoming gas phase by liquid phase, make the interior temperature of stove be in normal range of operation owing to titanium tetrachloride.When in the stove during temperature subnormal temperature, the aperture of material loading valve need be turned down, simultaneously the aperture of return valve be transferred big respective degrees, to reduce to spray into the mud amount of chlorination furnace, increase the mud amount that flows in the mud tank, guarantee that temperature is in normal range of operation in the chlorination furnace.
Description of drawings
Accompanying drawing is the structural representation of embodiment.
Narrate embodiment with reference to the accompanying drawings
Slush pump 2 and agitator 3 are installed in mud tank 1, and slush pump 2 links to each other with material loading pipeline 6, and the other end of material loading pipeline 6 connects material loading valve 8 and return valve 7, and material loading valve 8 connects injector 9, and return valve 7 links to each other with mud tank 1 by return line 5.Mud tank 1 places below the eluting column, and injector 9 is installed in the top of chlorination furnace 10.
Temperature is enough low in stove, when not needing to return mud in chlorination furnace, can open valve 7, makes mud directly return mud tank.
Eliminated the eluting column latch up phenomenon after using this device, guaranteed that furnace temperature fluctuates in span of control, system is normally moved.

Claims (1)

  1. A kind of titanium tetrachloride mud returns furnace apparatus, it is characterized in that agitator and slush pump are installed in the mud tank, slush pump links to each other with the material loading pipeline, and the other end of material loading pipeline connects material loading valve and return valve, the material loading valve connects injector, and return valve links to each other with mud tank by return line.
CN 00252776 2000-11-08 2000-11-08 Device for pumping titanium tetrachloride back into furnace Expired - Lifetime CN2458280Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 00252776 CN2458280Y (en) 2000-11-08 2000-11-08 Device for pumping titanium tetrachloride back into furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 00252776 CN2458280Y (en) 2000-11-08 2000-11-08 Device for pumping titanium tetrachloride back into furnace

Publications (1)

Publication Number Publication Date
CN2458280Y true CN2458280Y (en) 2001-11-07

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Application Number Title Priority Date Filing Date
CN 00252776 Expired - Lifetime CN2458280Y (en) 2000-11-08 2000-11-08 Device for pumping titanium tetrachloride back into furnace

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CN (1) CN2458280Y (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103449513A (en) * 2012-06-05 2013-12-18 沈阳铝镁设计研究院有限公司 Titanium tetrachloride spray washer and washing method
CN103626224A (en) * 2013-11-25 2014-03-12 攀钢集团攀枝花钢铁研究院有限公司 Fused salt chlorination furnace for producing titanium tetrachloride
CN106629832A (en) * 2016-10-25 2017-05-10 锦州钛业有限公司 Method for removing low-melting-point complex in elution tower for producing titanium tetrachloride through fused salt chlorination
CN107311225A (en) * 2017-08-09 2017-11-03 攀钢集团研究院有限公司 Low temperature chlorination stove returns titanium tetrachloride mud analogue experiment installation
CN109052459A (en) * 2018-08-22 2018-12-21 攀钢集团攀枝花钢铁研究院有限公司 For producing TiCl4Chlorination furnace and its method for controlling furnace temperature
CN112408468A (en) * 2020-11-13 2021-02-26 云南国钛金属股份有限公司 Slurry returning device and method for chlorination furnace

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103449513A (en) * 2012-06-05 2013-12-18 沈阳铝镁设计研究院有限公司 Titanium tetrachloride spray washer and washing method
CN103449513B (en) * 2012-06-05 2015-02-18 沈阳铝镁设计研究院有限公司 Titanium tetrachloride spray washer and washing method
CN103626224A (en) * 2013-11-25 2014-03-12 攀钢集团攀枝花钢铁研究院有限公司 Fused salt chlorination furnace for producing titanium tetrachloride
CN103626224B (en) * 2013-11-25 2015-07-22 攀钢集团攀枝花钢铁研究院有限公司 Fused salt chlorination furnace for producing titanium tetrachloride
CN106629832A (en) * 2016-10-25 2017-05-10 锦州钛业有限公司 Method for removing low-melting-point complex in elution tower for producing titanium tetrachloride through fused salt chlorination
CN106629832B (en) * 2016-10-25 2018-03-20 锦州钛业股份有限公司 The minimizing technology of low melting point complex in fused salt chlorimation production titanium tetrachloride eluting column
CN107311225A (en) * 2017-08-09 2017-11-03 攀钢集团研究院有限公司 Low temperature chlorination stove returns titanium tetrachloride mud analogue experiment installation
CN107311225B (en) * 2017-08-09 2020-02-04 攀钢集团研究院有限公司 Titanium tetrachloride slurry returning simulation experiment device for low-temperature chlorination furnace
CN109052459A (en) * 2018-08-22 2018-12-21 攀钢集团攀枝花钢铁研究院有限公司 For producing TiCl4Chlorination furnace and its method for controlling furnace temperature
CN109052459B (en) * 2018-08-22 2021-05-25 攀钢集团攀枝花钢铁研究院有限公司 For preparing TiCl4Chlorination furnace and furnace temperature control method thereof
CN112408468A (en) * 2020-11-13 2021-02-26 云南国钛金属股份有限公司 Slurry returning device and method for chlorination furnace

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: JINZHOU IRON ALLOY CO., LTD.

Free format text: FORMER NAME OR ADDRESS: TITANIUM WHITE POWDER PLANT OF JINZHOU FERROALLOY (GROUP) CO LTD, JINZHOU

CP01 Change in the name or title of a patent holder

Address after: 121005 alloy No. 59, Taihe District, Liaoning, Jinzhou

Patentee after: Jinzhou Iron Alloy (Group) Co., Ltd.

Address before: 121005 alloy No. 59, Taihe District, Liaoning, Jinzhou

Patentee before: Titanium White Power Factory, Jinzhou Ferroalloy (Group) Co., Ltd.

ASS Succession or assignment of patent right

Owner name: CITIC JINZHOU FERROALLOY CO., LTD.

Free format text: FORMER OWNER: JINZHOU IRON ALLOY CO., LTD.

Effective date: 20080815

C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20080815

Address after: Alloy 59, Taihe District, Jinzhou, Liaoning, China: 121005

Patentee after: CITIC Jinzhou Ferroalloy Co., Ltd.

Address before: Alloy 59, Taihe District, Liaoning, Jinzhou, China: 121005

Patentee before: Jinzhou Iron Alloy (Group) Co., Ltd.

C17 Cessation of patent right
CX01 Expiry of patent term

Expiration termination date: 20101108

Granted publication date: 20011107