CN201988203U - Titanium liquid concentration device - Google Patents
Titanium liquid concentration device Download PDFInfo
- Publication number
- CN201988203U CN201988203U CN2011201211834U CN201120121183U CN201988203U CN 201988203 U CN201988203 U CN 201988203U CN 2011201211834 U CN2011201211834 U CN 2011201211834U CN 201120121183 U CN201120121183 U CN 201120121183U CN 201988203 U CN201988203 U CN 201988203U
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- titanium liquid
- hydraulic ejector
- vacuum
- titanium
- concentration device
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Abstract
The utility model relates to a titanium liquid concentration device, a matched gas-liquid separator and a buffer tank are not required, the flow path is short and the energy consumption is low. The titanium liquid concentration device comprises a film evaporator and a hydraulic ejector, wherein the vacuum joint of the film evaporator is connected to the hydraulic ejector. When the titanium liquid concentration device is used for titanium liquid concentration, titanium liquid enters a tube nest of a concentrator from a feeding room at the bottom of the film concentrator, steam heating is conducted outside the tube nest, the concentrated titanium liquid enters a titanium liquid storage barrel through an overflow pipe, a small amount of incoagulable gas is carried along with water sprayed by the hydraulic ejector into a cooling water return pool of the hydraulic ejector through the vacuum joint, vacuum required in concentration is provided by the hydraulic ejector, one part of vacuum generates during the water spraying process, and the other part of vacuum generates by vertical falling of the sprayed water, and as the acidic incoagulable gas can not influence the use of the hydraulic ejector, a vacuum pump and the matched gas-liquid separator and buffer tank are not needed, the process flow is shortened, and the energy consumption is lowered.
Description
Technical field
The present invention relates to the titanium liquid enrichment facility in a kind of titanium dioxide process industry.
Background technology
Now the titanium liquid enrichment facility that uses in the titanium dioxide manufacturing process has two kinds: 1, titanium liquid in concentration tank by the steam indirect, water vapor in the titanium liquid, discharge from the concentration tank top, enter gas-liquid separator, the steam that the process initial gross separation is come out enters condenser from the bottom and sails against the current, cooling water descends from the condenser overhead spray, fully contact with steam, steam is outside pneumatic tube is discharged to water seal tank inflow system after the condensation, the gas that is not condensed, discharge from condenser overhead, to vacuum buffer tank, enter atmosphere through vavuum pump again through gas-liquid separation device.2, thin film concentrator: titanium liquid enters in the titanium liquid evaporimeter tubulation from the feed compartment of thin film concentrator bottom, tubulation external application Steam Heating, the steam that is evaporated in the titanium liquid rises in pipe with very high speed, titanium liquid is then pulled into film by this high velocity air, rising to the evaporimeter top in the extremely short time gushes out, concentrate good titanium liquid and enter titanium liquid storage tank through overflow pipe, the steam that is evaporated is through cyclone separator, enter then in the barometric condenser, behind the cooling water condensation by mixing, wherein a spot of incoagulable gas, discharge from condenser overhead, enter vavuum pump through gas-liquid separation device, enter vacuum buffer tank then, after enter atmosphere.
Above-mentioned titanium liquid enrichment facility all needs supporting gas-liquid separator and surge tank, long flow path, energy consumption height.
The utility model content
The utility model provides a kind of titanium liquid enrichment facility, need not supporting gas-liquid separator and surge tank, and flow process is short, and energy consumption is low.
Described titanium liquid enrichment facility comprises thin film evaporator, also comprises hydraulic ejector, and the vacuum interface of thin film evaporator is connected to hydraulic ejector.
Adopt the utility model to carry out titanium liquid when concentrating, titanium liquid enters in the inspissator tubulation from the feed compartment of thin film concentrator bottom, tubulation external application Steam Heating, the steam that is evaporated in the titanium liquid rises in pipe with very high speed, titanium liquid is then pulled into film by this high velocity air, rising to the evaporimeter top in the extremely short time gushes out, concentrate good titanium liquid and enter titanium liquid storage tank through overflow pipe, wherein a small amount of incoagulable gas is through vacuum interface, be brought into the pond that cools back of hydraulic ejector with the water under the hydraulic ejector injection, required vacuum is provided by hydraulic ejector when concentrating, wherein a part is produced by the water course of injection, another part is produced by the water vertical drop after spraying, because acid incoagulable gas can not influence the use of hydraulic ejector, thereby do not need vavuum pump and supporting gas-liquid separator and surge tank, shorten technological process, reduced energy consumption.
Description of drawings
Fig. 1 is the structural representation of embodiment 1 described titanium liquid enrichment facility.
The specific embodiment
As shown in Figure 1, described titanium liquid enrichment facility comprises thin film evaporator 1 and hydraulic ejector 2, and the vacuum interface 3 of thin film evaporator 1 is connected to hydraulic ejector 2.
Adopt above-mentioned titanium liquid enrichment facility to carry out titanium liquid when concentrating, titanium liquid enters in the inspissator tubulation from the feed compartment of thin film concentrator 1 bottom, tubulation external application Steam Heating, concentrate good titanium liquid and enter titanium liquid storage tank through overflow pipe, what the water under wherein a small amount of incoagulable gas sprays through vacuum interface 3, with hydraulic ejector was brought into hydraulic ejector cools back pond 4, required vacuum is provided by hydraulic ejector 2 when concentrating, wherein a part is produced by the water course of injection, and another part is produced by the water vertical drop after spraying.
Claims (1)
1. a titanium liquid enrichment facility comprises thin film evaporator, it is characterized in that, also comprise hydraulic ejector, the vacuum interface of thin film evaporator is connected to hydraulic ejector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201211834U CN201988203U (en) | 2011-04-22 | 2011-04-22 | Titanium liquid concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201211834U CN201988203U (en) | 2011-04-22 | 2011-04-22 | Titanium liquid concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201988203U true CN201988203U (en) | 2011-09-28 |
Family
ID=44664708
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201211834U Expired - Fee Related CN201988203U (en) | 2011-04-22 | 2011-04-22 | Titanium liquid concentration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201988203U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2644264A1 (en) * | 2012-03-28 | 2013-10-02 | Aurotec GmbH | Pressure-controlled multi-reactor system |
| CN107715492A (en) * | 2017-11-13 | 2018-02-23 | 广西华银铝业有限公司 | Evaporator group incoagulable gas collects injection energy-saving device |
| CN108744562A (en) * | 2018-05-02 | 2018-11-06 | 杭州安永环保科技有限公司 | A kind of method and its device of material Multi-effect concentration |
| CN114681935A (en) * | 2020-12-28 | 2022-07-01 | 攀枝花恒通钛业有限公司 | Automatic control process for concentration of low-concentration titanium liquid |
-
2011
- 2011-04-22 CN CN2011201211834U patent/CN201988203U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2644264A1 (en) * | 2012-03-28 | 2013-10-02 | Aurotec GmbH | Pressure-controlled multi-reactor system |
| WO2013143922A1 (en) | 2012-03-28 | 2013-10-03 | Aurotec Gmbh | Pressure regulated multi-reactor system |
| CN104284717A (en) * | 2012-03-28 | 2015-01-14 | 奥若泰克股份有限公司 | Pressure regulated multi-reactor system |
| CN104284717B (en) * | 2012-03-28 | 2017-04-05 | 奥若泰克股份有限公司 | Pressure controlled multiple reactor system |
| US10913048B2 (en) | 2012-03-28 | 2021-02-09 | Aurotec Gmbh | Pressure-regulated multi-reactor system |
| CN107715492A (en) * | 2017-11-13 | 2018-02-23 | 广西华银铝业有限公司 | Evaporator group incoagulable gas collects injection energy-saving device |
| CN108744562A (en) * | 2018-05-02 | 2018-11-06 | 杭州安永环保科技有限公司 | A kind of method and its device of material Multi-effect concentration |
| CN108744562B (en) * | 2018-05-02 | 2021-03-19 | 杭州安永环保科技有限公司 | Method and device for multi-effect concentration of materials |
| CN114681935A (en) * | 2020-12-28 | 2022-07-01 | 攀枝花恒通钛业有限公司 | Automatic control process for concentration of low-concentration titanium liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110928 Termination date: 20160422 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |