IE34646B1 - Beneficiation of ilmenite - Google Patents

Beneficiation of ilmenite

Info

Publication number
IE34646B1
IE34646B1 IE1267/70A IE126770A IE34646B1 IE 34646 B1 IE34646 B1 IE 34646B1 IE 1267/70 A IE1267/70 A IE 1267/70A IE 126770 A IE126770 A IE 126770A IE 34646 B1 IE34646 B1 IE 34646B1
Authority
IE
Ireland
Prior art keywords
leach liquor
ilmenite
hcl
leaching
content
Prior art date
Application number
IE1267/70A
Other versions
IE34646L (en
Original Assignee
Benilite Corp
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 Benilite Corp filed Critical Benilite Corp
Publication of IE34646L publication Critical patent/IE34646L/en
Publication of IE34646B1 publication Critical patent/IE34646B1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B34/00Obtaining refractory metals
    • C22B34/10Obtaining titanium, zirconium or hafnium
    • C22B34/12Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
    • C22B34/1204Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 preliminary treatment of ores or scrap to eliminate non- titanium constituents, e.g. iron, without attacking the titanium constituent
    • C22B34/1213Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 preliminary treatment of ores or scrap to eliminate non- titanium constituents, e.g. iron, without attacking the titanium constituent by wet processes, e.g. using leaching methods or flotation techniques
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

1,262,401. Benificiation of ilmenite; iron oxide. BENILITE CORP. 14 April, 1970 [15 Oct., 1969], No. 17691/70. Headings C1A and C1N. A titaniferous ore or slag, e.g. ilmenite, ilmenite magnetite, ilmenite-hematite, titaniferous magnetite, and titaniferous hematite, is benificiated 'by leaching it in a digester with hydrochloric acid leach liquor, the leaching liquor being heated during this process by feeding into the digester a vapour mixture formed by distilling an azeotropic mixture of HCl -and -water, by which means the HCl content of the leach liquor is simultaneously replenished. The leaching may be .conducted at a pressure of 20-50 p.s.i.g. and a temperature of 108‹ to 145‹ C., and the HCl content of the leach liquor may be recovered and reused in the process either as leach liquor or as the source of the vapour mixture. The preferred HCl concentration of the leach liquor is 20% by wt., and the leaching may be performed in two counter current stages. Depending on the ferrie/ferrous content of the ore, it may first be subjected to a reducing step, e.g. with coke at 815‹ to 1090‹ C. The iron content of the used leach liquor may be obtained as the oxide by hydrolysis of the chloride at high temperatures, e.g. 260-500‹ C., by direct contact with combustion gases. This simultaneously regenerates the HCl leach liquor. [GB1262401A]
IE1267/70A 1969-10-15 1970-10-01 Beneficiation of ilmenite IE34646B1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US86654869A 1969-10-15 1969-10-15

Publications (2)

Publication Number Publication Date
IE34646L IE34646L (en) 1971-04-15
IE34646B1 true IE34646B1 (en) 1975-07-09

Family

ID=25347844

Family Applications (1)

Application Number Title Priority Date Filing Date
IE1267/70A IE34646B1 (en) 1969-10-15 1970-10-01 Beneficiation of ilmenite

Country Status (12)

Country Link
JP (1) JPS558572B1 (en)
CY (1) CY748A (en)
DE (1) DE2004878C3 (en)
FR (1) FR2065775A5 (en)
GB (1) GB1262401A (en)
IE (1) IE34646B1 (en)
IL (1) IL35038A (en)
MY (1) MY7300089A (en)
NO (1) NO130392B (en)
PL (1) PL81917B1 (en)
SE (1) SE370414B (en)
ZA (1) ZA706712B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2428003A1 (en) * 1978-06-09 1980-01-04 Uop Inc Recovery of high purity titanium from ilmenite - by formation of tri:chloride and subsequent crystallisation from aq. soln.
US7008602B2 (en) 2002-04-19 2006-03-07 Millennium Inorganic Chemicals, Inc. Beneficiation of titaniferous ore with sulfuric acid
FI123884B (en) * 2011-11-08 2013-11-29 Outotec Oyj A process for dissolving a sulphidic metal concentrate
KR101323754B1 (en) * 2013-04-29 2013-10-31 한국지질자원연구원 Recovery of acid and platinum group metals from leaching solution of waste catalyst
CN109179496B (en) * 2018-09-18 2021-02-02 攀枝花中达钛业科技有限公司 High grade titanium dioxide and preparation method thereof

Also Published As

Publication number Publication date
ZA706712B (en) 1971-12-29
NO130392B (en) 1974-08-26
DE2004878C3 (en) 1975-09-18
SE370414B (en) 1974-10-14
IE34646L (en) 1971-04-15
DE2004878B2 (en) 1975-01-16
CY748A (en) 1974-06-18
GB1262401A (en) 1972-02-02
IL35038A (en) 1974-03-14
FR2065775A5 (en) 1971-08-06
MY7300089A (en) 1973-12-31
DE2004878A1 (en) 1971-05-06
JPS558572B1 (en) 1980-03-05
PL81917B1 (en) 1975-10-31
IL35038A0 (en) 1970-10-30

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