YU72299A - Neprekidan, nezagađujući postupak sa tečnom fazom za dobijanje titanijum dioksida - Google Patents
Neprekidan, nezagađujući postupak sa tečnom fazom za dobijanje titanijum dioksidaInfo
- Publication number
- YU72299A YU72299A YU72299A YU72299A YU72299A YU 72299 A YU72299 A YU 72299A YU 72299 A YU72299 A YU 72299A YU 72299 A YU72299 A YU 72299A YU 72299 A YU72299 A YU 72299A
- Authority
- YU
- Yugoslavia
- Prior art keywords
- titanium dioxide
- line
- reactor
- acid
- liquid phase
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1236—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by wet processes, e.g. by leaching
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
- B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G23/00—Compounds of titanium
- C01G23/04—Oxides; Hydroxides
- C01G23/047—Titanium dioxide
- C01G23/053—Producing by wet processes, e.g. hydrolysing titanium salts
- C01G23/0532—Producing by wet processes, e.g. hydrolysing titanium salts by hydrolysing sulfate-containing salts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Opisani su postupak i aparatura za dobijanje titan dioksida iz rude ili šljake titana. Ruda ili šljaka (2) reaguje sa sumpornom kiselinom (3) u reaktoru (1) u kome se koristi topao gas (4) za mešanje. Zajedno sa izdvojenom kiselinom iz sprejnog uparivača (34) reaguje proizvod koji se preliva iz reaktora u rotirajući filter (8). Filterski kolač se ispere u rotirajućem filteru čija voda dolazi kroz liniju (14). Isprani filterski kolač se odvodi u rezervoar za rastvaranje (10). Koncentrovana kiselina zajedno sa vodom od ispiranja se vraća u reaktor kroz liniju (3). Filtrat se hidrolizuje u rezervoaru za hidrolizu (21) radi dobijanja titan dioksid hidrata koji se tada kalcinuje u fluidnom sloju kalcinera (30) radi dobijanja titan dioksida.[A process and apparatus for producing titanium dioxide from titanium ore or slag is disclosed. The ore or slag (2) is reacted with sulfuric acid (3) in a reactor (1) in which hot gas for agitation (4) is used. Makeup acid from line (6) is fed to line (3). Together with recovered acid from the spray evaporator (34) reacted product overflows from the reactor to rotary filter (8). The filter cake is washed in the rotary filter whose water comes in through line (14). The washed filter cake is delivered to dissolving tank (10). Concentrated acid together with wash water is returned to the reactor through line (3). Filtrate is hydrolized in hydrolysis tank (21) to form titanium dioxide hydrate which is then calcined in a fluid bed calciner (30) to form titanium dioxide.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US9709371 | 1997-05-30 | ||
US87623497A | 1997-06-16 | 1997-06-16 | |
US08/917,941 US6048505A (en) | 1997-06-16 | 1997-08-22 | Continuous non-polluting liquid phase titanium dioxide process and apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
YU72299A true YU72299A (sh) | 2001-09-28 |
Family
ID=47633595
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
YU72299A YU72299A (sh) | 1997-05-30 | 1998-04-01 | Neprekidan, nezagađujući postupak sa tečnom fazom za dobijanje titanijum dioksida |
Country Status (5)
Country | Link |
---|---|
CN (1) | CN1165488C (sh) |
AU (1) | AU744330B2 (sh) |
CA (1) | CA2323671A1 (sh) |
WO (1) | WO1998054095A1 (sh) |
YU (1) | YU72299A (sh) |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10332530A1 (de) | 2003-07-17 | 2005-02-10 | Kerr-Mcgee Pigments Gmbh | Verfahren zur Reduktion des löslichen Chromatgehaltes in Zement sowie eine Zubereitung aus Zement und wasserlöslichen Metallsulfaten |
CN101553585B (zh) * | 2006-09-06 | 2012-05-30 | Bhp比利顿创新公司 | 硫酸盐法 |
WO2010034083A1 (en) * | 2008-09-29 | 2010-04-01 | Bhp Billiton Innovation Pty Ltd | A sulfate process |
CN101723448B (zh) * | 2009-12-29 | 2013-11-06 | 攀钢集团研究院有限公司 | 制备含钛溶液的方法 |
CN101898791B (zh) * | 2010-06-25 | 2012-10-03 | 四川龙蟒钛业股份有限公司 | 一种利用新流程钛渣制备金红石钛白粉的方法 |
CN102560117A (zh) * | 2011-11-23 | 2012-07-11 | 王景峰 | 多层电容废料回收二氧化钛、硫酸镍的方法 |
EP2623564A1 (en) * | 2012-02-03 | 2013-08-07 | Omya International AG | Installation for the purification of minerals, pigments and/or fillers and/or the preparation of precipitated earth alkali carbonate |
CN103145181B (zh) * | 2013-04-02 | 2014-12-03 | 宜宾天原集团股份有限公司 | 盐酸浸取法制备金红石用三相流态化连续反应装置 |
EP3257816A1 (de) * | 2016-06-14 | 2017-12-20 | Kronos International, Inc. | Herstellung von nano-partikulärem titandioxid |
WO2018158492A1 (en) * | 2017-03-02 | 2018-09-07 | Outotec (Finland) Oy | Method of treating titanium-containing slag |
CN107649089A (zh) * | 2017-10-26 | 2018-02-02 | 攀钢集团攀枝花钢铁研究院有限公司 | 用于过程强化连续酸解反应生产硫酸钛化物的反应器 |
CN112321889A (zh) * | 2020-11-04 | 2021-02-05 | 沪本新材料科技(上海)有限公司 | Pvc塑料生产用液体钛白的制作工艺 |
CN112624189B (zh) * | 2021-01-14 | 2023-03-28 | 上海安赐环保科技股份有限公司 | 一种硫酸法钛白粉的废酸与白水的回用方法及系统 |
CN115367795B (zh) * | 2022-09-01 | 2024-02-20 | 山东东佳集团股份有限公司 | 催化剂钛白粉水洗液回用于制酸尾气系统制备硫酸铵的新工艺 |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2774650A (en) * | 1953-05-01 | 1956-12-18 | Nat Lead Co | Method for decomposition of titaniferous ores |
US4038363A (en) * | 1975-10-21 | 1977-07-26 | Quebec Iron & Titanium Corporation-Fer Et Titane Due Quebec, Inc. | Upgrading sorelslag for production of synthetic rutile |
US4288418A (en) * | 1979-08-10 | 1981-09-08 | Nl Industries, Inc. | Process for manufacturing titanium dioxide |
US4505886A (en) * | 1983-07-01 | 1985-03-19 | Nl Industries, Inc. | Process for preparing high quality titanium dioxide |
DE3343256A1 (de) * | 1983-11-30 | 1985-06-05 | Bayer Ag, 5090 Leverkusen | Verfahren zur herstellung von titandioxid |
US4552730A (en) * | 1984-08-27 | 1985-11-12 | The United States Of America As Represented By The Secretary Of The Interior | Recovery of titanium from perovskite using sulfuric acid leaching |
DE3524053A1 (de) * | 1985-07-05 | 1987-01-08 | Bayer Antwerpen Nv | Verfahren zur herstellung von hochwertigem titandioxid nach dem sulfatverfahren |
US5591506A (en) * | 1995-05-10 | 1997-01-07 | Kemicraft Overseas Limited | Non-polluting alkali-metal bisulfate system for producing titanium dioxide pigment |
US5618331A (en) * | 1995-12-04 | 1997-04-08 | Kemicraft Overseas Limited | Vapor phase fluidized bed sulfation of titaniferous materials |
-
1998
- 1998-04-01 YU YU72299A patent/YU72299A/sh unknown
- 1998-04-01 CN CNB988077345A patent/CN1165488C/zh not_active Expired - Fee Related
- 1998-04-01 WO PCT/US1998/006499 patent/WO1998054095A1/en active IP Right Grant
- 1998-04-01 CA CA002323671A patent/CA2323671A1/en not_active Abandoned
- 1998-04-01 AU AU67944/98A patent/AU744330B2/en not_active Ceased
Also Published As
Publication number | Publication date |
---|---|
AU6794498A (en) | 1998-12-30 |
CA2323671A1 (en) | 1998-12-03 |
WO1998054095A1 (en) | 1998-12-03 |
CN1265635A (zh) | 2000-09-06 |
AU744330B2 (en) | 2002-02-21 |
CN1165488C (zh) | 2004-09-08 |
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