CN201154253Y - A kind of filtering device of crude titanium tetrachloride - Google Patents
A kind of filtering device of crude titanium tetrachloride Download PDFInfo
- Publication number
- CN201154253Y CN201154253Y CNU2007201742748U CN200720174274U CN201154253Y CN 201154253 Y CN201154253 Y CN 201154253Y CN U2007201742748 U CNU2007201742748 U CN U2007201742748U CN 200720174274 U CN200720174274 U CN 200720174274U CN 201154253 Y CN201154253 Y CN 201154253Y
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- CN
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- Prior art keywords
- film pipe
- filter
- end cover
- discharge port
- titanium tetrachloride
- 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.)
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- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 title claims abstract description 16
- 238000001914 filtration Methods 0.000 title claims abstract description 11
- 239000000956 alloy Substances 0.000 claims abstract description 18
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 18
- 238000007789 sealing Methods 0.000 claims description 4
- 229910004349 Ti-Al Inorganic materials 0.000 claims description 2
- 229910004692 Ti—Al Inorganic materials 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims 2
- 230000000712 assembly Effects 0.000 claims 1
- 238000000429 assembly Methods 0.000 claims 1
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 239000012528 membrane Substances 0.000 abstract description 31
- 239000003795 chemical substances by application Substances 0.000 abstract description 10
- 239000002893 slag Substances 0.000 abstract description 10
- 238000011001 backwashing Methods 0.000 abstract description 7
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 8
- 239000004744 fabric Substances 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 208000027418 Wounds and injury Diseases 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 238000005660 chlorination reaction Methods 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000002006 petroleum coke Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Manufacture And Refinement Of Metals (AREA)
- Filtration Of Liquid (AREA)
Abstract
一种粗四氯化钛的过滤装置,由筒体、端盖及合金膜管组成,端盖与筒体通过法兰用螺栓紧固连接成过滤罐,合金膜管组合在一起构成过滤组件通过上下膜管固定板安装在所述过滤罐内,所述端盖上方设有出料口,端盖两侧分别设有反洗剂入口,筒体下端的一侧设有进料口、底部设有排渣口,出料口、反洗剂入口、进料口、排渣口处设有自动阀。本实用新型使粗四氯化钛过滤、反洗、排渣均处于全密封的装置中进行,可实现连续自动作业,改善工作条件,减轻工作量并降低对环境的污染。
A filter device for coarse titanium tetrachloride, which is composed of a cylinder body, an end cover and an alloy membrane tube. The end cover and the cylinder body are fastened with bolts through flanges to form a filter tank, and the alloy membrane tubes are combined to form a filter assembly. The upper and lower film tube fixing plates are installed in the filter tank, the top of the end cover is provided with a discharge port, the two sides of the end cover are respectively provided with backwashing agent inlets, the side of the lower end of the cylinder is provided with a feed port, and the bottom is provided with a There is a slag discharge port, and automatic valves are installed at the discharge port, the backwash agent inlet, the feed port, and the slag discharge port. The utility model makes crude titanium tetrachloride filtration, backwashing and slag discharge all carried out in a fully sealed device, which can realize continuous automatic operation, improve working conditions, reduce workload and reduce environmental pollution.
Description
技术领域 technical field
本实用新型涉及粗四氯化钛的过滤设备,特别涉及经氯化制取的粗四氯化钛的过滤装置。The utility model relates to a filter device for crude titanium tetrachloride, in particular to a filter device for crude titanium tetrachloride produced through chlorination.
背景技术 Background technique
目前,经沸腾氯化法制取的粗四氯化钛中含有未反应的富钛料、石油焦等较细的固体杂质,现行工艺生产中使用的是一种立式滤布过滤器,该过滤器内装有多根带孔的金属筒,金属筒外面包裹涤纶布。在过滤一段时间后要定期排出泥浆,缠绕在金属滤筒上的滤布因吸附料液内的杂质而逐渐形成滤渣饼,最终导致过滤失效。在更换滤布时,由于滤渣饼中含有大量的四氯化钛液体,在更换、清除滤布时遇到空气和水都会产生大量的白色酸性烟雾,对环境污染较大,对操作人员身体造成伤害,且这种方式属于一种间隙式作业方式,存在生产成本较高,劳动生产率低等缺点。At present, the crude titanium tetrachloride produced by boiling chlorination contains finer solid impurities such as unreacted titanium-rich materials and petroleum coke, and a vertical filter cloth filter is used in the current production process. There are many metal cylinders with holes inside, and the metal cylinders are wrapped with polyester cloth. After filtering for a period of time, the mud should be discharged regularly. The filter cloth wound on the metal filter cartridge gradually forms a filter residue cake due to the adsorption of impurities in the feed liquid, which eventually leads to filter failure. When replacing the filter cloth, since the filter residue cake contains a large amount of titanium tetrachloride liquid, a large amount of white acidic smoke will be generated when the filter cloth is replaced or removed when encountering air and water, which will pollute the environment and cause physical harm to the operator. Injury, and this method belongs to a kind of intermittent operation method, which has the disadvantages of high production cost and low labor productivity.
发明内容 Contents of the invention
本实用新型的目的是提供一种粗四氯化钛的过滤装置,以解决现行工艺过滤设备造成的环境污染及劳动生产率低的问题,实现过滤工序的自动化控制。该过滤装置由筒体、端盖及合金膜管组成,端盖与筒体通过法兰用螺栓紧固连接成过滤罐,合金膜管组合在一起构成过滤组件,固定安装在所述过滤罐内,所述端盖上方设有出料口,端盖两侧分别设有反洗剂入口,筒体下端的一侧设有进料口、底部设有排渣口。所述出料口、反洗剂入口、进料口和排渣口处分别设有自动阀。The purpose of this utility model is to provide a filter device for coarse titanium tetrachloride, to solve the problems of environmental pollution and low labor productivity caused by the current process filter equipment, and to realize the automatic control of the filter process. The filter device is composed of a cylinder body, an end cover and an alloy membrane tube. The end cover and the cylinder body are fastened with bolts through flanges to form a filter tank. The alloy membrane tubes are combined to form a filter assembly, which is fixedly installed in the filter tank. , the top of the end cover is provided with a discharge port, the two sides of the end cover are respectively provided with backwash agent inlets, one side of the lower end of the cylinder is provided with a feed port, and the bottom is provided with a slag discharge port. Automatic valves are respectively provided at the discharge port, the backwash agent inlet, the feed port and the slag discharge port.
过滤罐内设有膜管上固定板及膜管下固定板,膜管上固定板上设有密封垫,膜管下固定板悬于过滤罐内,膜管上固定板和膜管下固定板通过双头螺杆拉紧,所述各合金膜管通过螺钉和调节螺杆夹持固定在膜管上固定板和膜管下固定板之间。The filter tank is equipped with the upper fixing plate of the membrane tube and the lower fixing plate of the membrane tube. The upper fixing plate of the membrane tube is provided with a sealing gasket. The lower fixing plate of the membrane tube is suspended in the filter tank. The alloy membrane tubes are clamped and fixed between the upper fixing plate of the membrane tube and the lower fixing plate of the membrane tube through the screw and the adjusting screw.
本实用新型在使用中,使过滤、反洗、排渣过程都处于全密封的系统内完成,反洗时,不会引入新的杂质成分,能实现连续自动作业,减轻了人工劳动量,解决了环保污染问题。When the utility model is in use, the processes of filtration, backwashing and slag discharge are all completed in a fully sealed system. During backwashing, no new impurity components will be introduced, and continuous automatic operation can be realized, which reduces the amount of manual labor and solves the problem of environmental pollution issues.
附图说明 Description of drawings
图1为本实用新型粗四氯化钛的过滤装置结构示意图;Fig. 1 is the filter device structural representation of the thick titanium tetrachloride of the present utility model;
图2为图1中I处放大图;Fig. 2 is an enlarged view at I place in Fig. 1;
图3为图1中II处放大图。Fig. 3 is an enlarged view of II in Fig. 1 .
图中:1-筒体、2-端盖、3-出料口、4-反洗剂入口、5-支座、6-进料口、7-排渣口、8-双头螺杆、9-合金膜管、10-螺钉、11-密封垫、12-膜管上固定板、13-膜管下固定板、14-调节螺杆。In the figure: 1-cylinder, 2-end cover, 3-outlet, 4-backwashing agent inlet, 5-support, 6-feed inlet, 7-slagging outlet, 8-double-headed screw, 9 -alloy membrane tube, 10-screw, 11-sealing gasket, 12-upper fixing plate of membrane tube, 13-lower fixing plate of membrane tube, 14-adjusting screw.
具体实施方式: Detailed ways:
下面结合附图对本实用新型作进一步说明。Below in conjunction with accompanying drawing, the utility model is further described.
本实用新型的一种粗四氯化钛的过滤装置,主要由筒体1、端盖2、及合金膜管9组成,端盖2与筒体1通过法兰用螺栓紧固连接成过滤罐,在端盖2上方设有出料口3,端盖2两侧分别设有两个反洗剂入口4,在筒体1上设有支座5,筒体1靠下的一侧设有进料口6,最下端设有排渣口7,在过滤罐内设有由多根合金膜管9组合在一起构成的过滤组件及膜管上固定板12、膜管下固定板13,膜管上固定板12设于筒体1与端盖2之间,并在膜管上固定板12上设有密封垫11,膜管下固定板13悬于过滤罐内,膜管上固定板12和膜管下固定板13利用多根双头螺杆8拉紧,各合金膜管9通过螺钉10和调节螺杆14夹持固定在膜管上固定板12和膜管下固定板13之间。A filter device for coarse titanium tetrachloride of the utility model is mainly composed of a cylinder body 1, an end cover 2, and an
本实用新型还可在出料口3、反洗剂入口4、进料口6和排渣口7处分别设置自动阀,以实现过滤过程的自动化。In the utility model, automatic valves can also be respectively arranged at the discharge port 3, the backwash agent inlet 4, the feed port 6 and the slag discharge port 7, so as to realize the automation of the filtering process.
为提高本实用新型的耐腐蚀性及延长合金膜管9的使用寿命,合金膜管最好采用Ti-Al合金。In order to improve the corrosion resistance of the utility model and prolong the service life of the
利用本实用新型进行粗四氯化钛过滤时,关闭好底部排渣接口阀门,粗四氯化钛从进料口6加入,透过合金膜管9后由出料口3流出;在过滤过程中按照设定的时间反洗时,关闭出料口3和进料口6处的自动阀,打开反洗剂入口4和排渣口7处的自动阀,加入反洗剂可将附着在合金膜管外表面上的过滤物吹脱,并通过排渣口排入浓密机中。When the utility model is used for crude titanium tetrachloride filtration, close the slag discharge interface valve at the bottom, the crude titanium tetrachloride is added from the feed port 6, and flows out from the discharge port 3 after passing through the
上述反洗剂可以采用氩气或过滤清液或氩气与过滤清液混合物等。The above-mentioned backwashing agent can be argon or filtered clear liquid or a mixture of argon and filtered clear liquid.
本实用新型在生产应用过程中,滤液固含量均完全合格,膜透过率良好,有效地改善了环境质量,且实现了密闭、连续生产,极大地提高了生产效率。During the production and application process of the utility model, the solid content of the filtrate is completely qualified, the membrane permeability is good, the environmental quality is effectively improved, and the airtight and continuous production is realized, which greatly improves the production efficiency.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201742748U CN201154253Y (en) | 2007-12-15 | 2007-12-15 | A kind of filtering device of crude titanium tetrachloride |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201742748U CN201154253Y (en) | 2007-12-15 | 2007-12-15 | A kind of filtering device of crude titanium tetrachloride |
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| CN201154253Y true CN201154253Y (en) | 2008-11-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201742748U Expired - Fee Related CN201154253Y (en) | 2007-12-15 | 2007-12-15 | A kind of filtering device of crude titanium tetrachloride |
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| CN (1) | CN201154253Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104645692A (en) * | 2013-11-20 | 2015-05-27 | 沈阳工业大学 | Zinc oxide solution filtering pot |
| CN104874211A (en) * | 2015-04-29 | 2015-09-02 | 南京梅山冶金发展有限公司 | Anti-blocking method used for diameter-height-ratio thickener |
| CN105923844A (en) * | 2016-06-27 | 2016-09-07 | 重庆市欣荣城机电有限公司 | Comprehensive treatment, filtration and recovery device for mud sewage |
-
2007
- 2007-12-15 CN CNU2007201742748U patent/CN201154253Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104645692A (en) * | 2013-11-20 | 2015-05-27 | 沈阳工业大学 | Zinc oxide solution filtering pot |
| CN104874211A (en) * | 2015-04-29 | 2015-09-02 | 南京梅山冶金发展有限公司 | Anti-blocking method used for diameter-height-ratio thickener |
| CN105923844A (en) * | 2016-06-27 | 2016-09-07 | 重庆市欣荣城机电有限公司 | Comprehensive treatment, filtration and recovery device for mud sewage |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081126 Termination date: 20111215 |