GB968879A - Improvements in or relating to processes for the treatment of industrial waste gases - Google Patents

Improvements in or relating to processes for the treatment of industrial waste gases

Info

Publication number
GB968879A
GB968879A GB1011861A GB1011861A GB968879A GB 968879 A GB968879 A GB 968879A GB 1011861 A GB1011861 A GB 1011861A GB 1011861 A GB1011861 A GB 1011861A GB 968879 A GB968879 A GB 968879A
Authority
GB
United Kingdom
Prior art keywords
solution
washing
ferric
compounds
cryolite
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
GB1011861A
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.)
Societe dElectro Chimie dElectro Metallurgie et des Acieries Electriques Dugine SA SECEMAU
Original Assignee
Societe dElectro Chimie dElectro Metallurgie et des Acieries Electriques Dugine SA SECEMAU
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 Societe dElectro Chimie dElectro Metallurgie et des Acieries Electriques Dugine SA SECEMAU filed Critical Societe dElectro Chimie dElectro Metallurgie et des Acieries Electriques Dugine SA SECEMAU
Publication of GB968879A publication Critical patent/GB968879A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/68Halogens or halogen compounds
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F7/00Compounds of aluminium
    • C01F7/48Halides, with or without other cations besides aluminium
    • C01F7/50Fluorides
    • C01F7/54Double compounds containing both aluminium and alkali metals or alkaline-earth metals

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Biomedical Technology (AREA)
  • Treating Waste Gases (AREA)
  • Removal Of Specific Substances (AREA)

Abstract

Cryolite is obtained by washing industrial waste gases containing fluorine with an acidified aqueous solution, then adding to the resultant acid solution ferric ion in an amount at least sufficient to form FePO4 with any phosphorus present, then raising the pH of the solution, preferably by adding ammonia, so as successively to precipitate phosphorus compounds, excess ferric ion and silica, and adding to the remaining solution a soluble salt of aluminium and a sodium salt to cause the precipitation of cryolite. The process may be applied to the gas containing fluorinated compounds derived from the treatment of natural phosphates used in the production of phosphorus, phosphoric acid or superphosphates. The washing solution may be formed by introducing into the washing apparatus water or a mixture of water and part of the solution resulting from the washing. The washing solution, which preferably has a pH of less than 5, may contain in solution compounds used at a later stage of the process, e.g. sodium or ammonium ions or a portion, or all, of the ferric compound which is used to precipitate the phosphoric anions. The desired pH in the washing apparatus is obtained by regulating the respective flows of feed. The preferred ferric compounds are the chloride, fluoride, sulphate or alum; ferric fluoride may be obtained by reacting a portion of the solution from the gas washing with an iron oxide or hydroxide or metallic iron in the presence of air. The cryolite suspension finally obtained is filtered and a portion of the filtrate which contains the regenerated ammonia and possibly an ammonium salt corresponding to the anion of the utilized ferric compound, is withdrawn to keep the working volume constant, and the remaining filtrate is recycled principally towards the stage of neutralization of the ferric acid solution and partly, if desired, to the stage of washing the gases, mixed with a portion of the acid solution from the gas washing. A flow diagram is given.
GB1011861A 1960-03-25 1961-03-20 Improvements in or relating to processes for the treatment of industrial waste gases Expired GB968879A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR822376A FR1260171A (en) 1960-03-25 1960-03-25 Fluorinated gas treatment process

Publications (1)

Publication Number Publication Date
GB968879A true GB968879A (en) 1964-09-02

Family

ID=8727870

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1011861A Expired GB968879A (en) 1960-03-25 1961-03-20 Improvements in or relating to processes for the treatment of industrial waste gases

Country Status (6)

Country Link
BE (1) BE600509A (en)
CH (1) CH401924A (en)
DE (1) DE1190449B (en)
FR (1) FR1260171A (en)
GB (1) GB968879A (en)
NL (1) NL262471A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109851132A (en) * 2019-03-22 2019-06-07 盛隆资源再生(无锡)有限公司 A method of recycling ice crystal, fluorite and ammonium sulfate from the high ammonia nitrogen acid waste water of high fluorine

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2750943A1 (en) * 1977-11-15 1979-05-17 Bayer Ag METHOD FOR PURIFYING AMMONIUM FLUORIDE SOLUTIONS
CN112850680B (en) * 2021-02-26 2022-11-22 桂林理工大学 Method for preparing anhydrous iron phosphate by ferrate self-reduction reaction

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109851132A (en) * 2019-03-22 2019-06-07 盛隆资源再生(无锡)有限公司 A method of recycling ice crystal, fluorite and ammonium sulfate from the high ammonia nitrogen acid waste water of high fluorine

Also Published As

Publication number Publication date
NL262471A (en)
DE1190449B (en) 1965-04-08
FR1260171A (en) 1961-05-05
CH401924A (en) 1965-11-15
BE600509A (en) 1961-06-16

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