ES250525A1 - Recovery of mercury - Google Patents
Recovery of mercuryInfo
- Publication number
- ES250525A1 ES250525A1 ES0250525A ES250525A ES250525A1 ES 250525 A1 ES250525 A1 ES 250525A1 ES 0250525 A ES0250525 A ES 0250525A ES 250525 A ES250525 A ES 250525A ES 250525 A1 ES250525 A1 ES 250525A1
- Authority
- ES
- Spain
- Prior art keywords
- mercury
- brine
- exchange material
- chloride
- recovery
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D3/00—Halides of sodium, potassium or alkali metals in general
- C01D3/14—Purification
- C01D3/145—Purification by solid ion-exchangers or solid chelating agents
-
- 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
- C22B43/00—Obtaining mercury
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Inorganic Chemistry (AREA)
- Treatment Of Water By Ion Exchange (AREA)
- Removal Of Specific Substances (AREA)
Abstract
Mercury present as dissolved mercury compounds is recovered from a brine having a pH between 0.1 and 10.5, by passing the brine through a bed of anion-exchange material, which adzorbs the mercury as complex anions of mercury, and then eluting the mercury from the exchange material by washing it with a solution of sulphuric acid or phosphoric acid. The brine may be an aqueous solution of sodium chloride, potassium chloride or calcium chloride, which has been circulated through an electrolytic cell having a mercury cathode. The mercury concentration in the brine may be between 0.1 and 1000 parts per million. Examples are given.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA754920 | 1958-07-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
ES250525A1 true ES250525A1 (en) | 1959-11-16 |
Family
ID=38531111
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES0250525A Expired ES250525A1 (en) | 1958-07-11 | 1959-07-04 | Recovery of mercury |
Country Status (5)
Country | Link |
---|---|
AT (1) | AT215438B (en) |
BE (1) | BE580509A (en) |
ES (1) | ES250525A1 (en) |
FR (1) | FR1231944A (en) |
GB (1) | GB872985A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3701764A1 (en) * | 1987-01-22 | 1988-08-04 | Norddeutsche Affinerie | METHOD FOR DEPOSITING GASEOUS METAL MERCURY FROM GASES |
-
1959
- 1959-06-17 GB GB2075659A patent/GB872985A/en not_active Expired
- 1959-07-04 ES ES0250525A patent/ES250525A1/en not_active Expired
- 1959-07-08 BE BE580509A patent/BE580509A/en unknown
- 1959-07-09 AT AT500459A patent/AT215438B/en active
- 1959-07-11 FR FR800033A patent/FR1231944A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
FR1231944A (en) | 1960-10-04 |
BE580509A (en) | 1960-01-08 |
AT215438B (en) | 1961-06-12 |
GB872985A (en) | 1961-07-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
ES250525A1 (en) | Recovery of mercury | |
GB898392A (en) | Improvements in or relating to a process for the production of electrolytic products by the electrolysis of brine and to apparatus therefor | |
GB1286142A (en) | Manfacture of sodium carbonate | |
GB592767A (en) | Improvements relating to the treatment of aqueous liquors containing thiocyanate | |
GB751855A (en) | Improvements in ion-exchange processes | |
ES390572A1 (en) | Process for hydrodimerizing acrylonitrile | |
GB772226A (en) | Process for recovering purified mercury from impure mercury containing alloying metal impurities | |
GB882263A (en) | A method for the production of citric acid | |
ES434722A1 (en) | Process for recovery of cyanuric acid from treated chlorinated mother liquor | |
GB751856A (en) | Improvements in the recovery of acids from effluents using ion-exchange materials | |
SU390902A1 (en) | ||
ES290583A1 (en) | Process for obtaining chlorine, sodium hydroxide and hydrogen by the electrolysis of sodium chloride in mercury cells | |
Grandi et al. | Polarographic determination of mercury in brines and industrial waters | |
GB916866A (en) | Treatment of brine | |
SU150822A1 (en) | Method of electrochemical concentration of substances | |
ES254078A1 (en) | Therapeutically active product | |
ES355745A1 (en) | Sodium chloride deposition procedure. (Machine-translation by Google Translate, not legally binding) | |
GB744059A (en) | Method of recovering ammonia from dilute aqueous solutions containing ammonium ions | |
GB1382540A (en) | Electrolytic treatment of waste water containing cyanide | |
ES414725A1 (en) | Improvements introduced in a procedure to produce magnesium dioxide. (Machine-translation by Google Translate, not legally binding) | |
GB1170436A (en) | Process for Producing Adiponitrile | |
GB1045681A (en) | Improved method of operating a brine supply system for electrolysis | |
GB914918A (en) | Process for the recovery of mercury from brines | |
GB1375656A (en) | ||
ES240952A1 (en) | A procedure to separate the ions k and mg from a double salt that contains them, eventually mixed with sodium salts (Machine-translation by Google Translate, not legally binding) |