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GB849140A - Cooling of vapour phase oxidation products - Google Patents

Cooling of vapour phase oxidation products

Info

Publication number
GB849140A
GB849140A GB3735157A GB3735157A GB849140A GB 849140 A GB849140 A GB 849140A GB 3735157 A GB3735157 A GB 3735157A GB 3735157 A GB3735157 A GB 3735157A GB 849140 A GB849140 A GB 849140A
Authority
GB
United Kingdom
Prior art keywords
water
slurry
passed
oxide
cooling
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
Application number
GB3735157A
Inventor
Robert William Ancrum
James Dennis Groves
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.)
British Titan Products Co Ltd
British Titan Ltd
Original Assignee
British Titan Products Co Ltd
British Titan 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 British Titan Products Co Ltd, British Titan Ltd filed Critical British Titan Products Co Ltd
Priority to GB3735157A priority Critical patent/GB849140A/en
Publication of GB849140A publication Critical patent/GB849140A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G23/00Compounds of titanium
    • C01G23/04Oxides; Hydroxides
    • C01G23/047Titanium dioxide
    • C01G23/07Producing by vapour phase processes, e.g. halide oxidation
    • C01G23/075Evacuation and cooling of the gaseous suspension containing the oxide; Desacidification and elimination of gases occluded in the separated oxide
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/113Silicon oxides; Hydrates thereof
    • C01B33/12Silica; Hydrates thereof, e.g. lepidoic silicic acid
    • C01B33/18Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof
    • C01B33/181Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof by a dry process
    • C01B33/183Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof by a dry process by oxidation or hydrolysis in the vapour phase of silicon compounds such as halides, trichlorosilane, monosilane
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • C01G49/02Oxides; Hydroxides
    • C01G49/06Ferric oxide [Fe2O3]

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Catalysts (AREA)

Abstract

In the production of oxides of metals or silicon by the vapour-phase oxidation of the corresponding chlorides, in the absence of gases which would burn to form water, the hot products of the oxidation are quenched <PICT:0849140/III/1> with water thereby cooling them so rapidly that substantially no hydrochloric acid is formed by reaction between the chlorine and the water. Cooling is normally effected to a temperature below 200 DEG C. and preferably below 100 DEG C. The oxides may be recovered as an aqueous slurry by passing the cooled gaseous suspension to a scrubbing tower where it is washed with a further quantity of water. Both quenching and scrubbing operations may be effected by a recycled aqueous slurry of the oxide. As shown in the Figure, titanium tetrachloride is reacted with oxygen to yield titanium oxide and chlorine together with excess oxygen, atmospheric gases and, if an auxiliary fuel is used, carbon dioxide; the oxide-bearing stream, at a temperature of 600-1200 DEG C., is passed into a spray cooling tower 1, supplied with a slurry of titanium dioxide in water at 85 DEG C. by pump P1. A small proportion of the oxide product is slurried in water and flows to a recirculation tank 5, whilst the cool gaseous suspension is passed to a scrubbing tower 2, also fed with oxide slurry from tank 5. The whole of the titanium oxide product is removed in tower 2 as an aqueous slurry and passed to tank 5, whilst the cool gases, now at about 85 DEG C. and saturated with water vapour are passed to a gas-cooling tower 3 where they travel counter current to cold water thereby reducing their temperatures at 25 DEG C. The so-cooled gases are exhausted and treated for the recovery of chlorine. The aqueous pigment slurry obtained in tank 5 is passed to a thickener 7 and from thence to recovery processes. The recirculated slurry is normally of a concentration up to 250 gms/litre of titanium dioxide.
GB3735157A 1957-11-29 1957-11-29 Cooling of vapour phase oxidation products Expired GB849140A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB3735157A GB849140A (en) 1957-11-29 1957-11-29 Cooling of vapour phase oxidation products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB3735157A GB849140A (en) 1957-11-29 1957-11-29 Cooling of vapour phase oxidation products

Publications (1)

Publication Number Publication Date
GB849140A true GB849140A (en) 1960-09-21

Family

ID=10395789

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3735157A Expired GB849140A (en) 1957-11-29 1957-11-29 Cooling of vapour phase oxidation products

Country Status (1)

Country Link
GB (1) GB849140A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020028169A1 (en) * 2018-08-02 2020-02-06 Corning Incorporated Methods of capturing soot
CN113307273A (en) * 2021-06-08 2021-08-27 江苏亨通智能科技有限公司 High-purity quartz sand water-quenching recycling device and method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020028169A1 (en) * 2018-08-02 2020-02-06 Corning Incorporated Methods of capturing soot
US11103825B2 (en) 2018-08-02 2021-08-31 Corning Incorporated Methods of soot capture and articles formed therefrom
JP2021532053A (en) * 2018-08-02 2021-11-25 コーニング インコーポレイテッド How to capture a suit
CN113307273A (en) * 2021-06-08 2021-08-27 江苏亨通智能科技有限公司 High-purity quartz sand water-quenching recycling device and method

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