GB1373771A - Mercury recovery process - Google Patents
Mercury recovery processInfo
- Publication number
- GB1373771A GB1373771A GB610671A GB610671A GB1373771A GB 1373771 A GB1373771 A GB 1373771A GB 610671 A GB610671 A GB 610671A GB 610671 A GB610671 A GB 610671A GB 1373771 A GB1373771 A GB 1373771A
- Authority
- GB
- United Kingdom
- Prior art keywords
- mercury
- chamber
- solutions
- vapour
- condensate
- 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
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/06—Flash distillation
- B01D3/065—Multiple-effect flash distillation (more than two traps)
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/343—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances the substance being a gas
- B01D3/346—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances the substance being a gas the gas being used for removing vapours, e.g. transport gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/38—Steam distillation
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/048—Purification of waste water by evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/70—Treatment of water, waste water, or sewage by reduction
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/06—Pressure conditions
- C02F2301/063—Underpressure, vacuum
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
1373771 Recovering mercury BP CHEMICALS Ltd 28 Feb 1972 [5 March 1971] 6106/71 Heading C7D [Also in Division B1] Aqueous solutions in which mercury is present as soluble inorganic mercury compounds are treated with a reducing agent and then flash distilled under vacuum, mercury being separated from the mixed condensate of steam and mercury vapour. Preferred reducing agents are ferrous sulphate, when the solutions have a pH greater than S, sodium borohydride, hydroxine, hydroxylamine or D-glucose when the solutions are alkaline, or iron or steel turnings or chips. Solutions containing insoluble compounds or elemental mercury must be converted to the soluble form; sodium sulphite or sulphur dioxide may be used to reduce any oxidizing agents present prior to the treatment with the preferred reductants. The process may be used to decontaminate brine from mercury cathode cells. The mixed vapour is preferably condensed on the external surfaces of internallycooled pipes or tubes; mercury is separated from the condensate by passage through a fibre pad and gravity separator or centrifuge. Distillation Apparatus, Fig.1. Aqueous solution is led in at 6 to a chamber 1 provided with a series of partitions 2; each section of the chamber includes an entrainment eliminator 3, an assembly of cooling tubes 4, a condensate collecting tray 5 and an inert gas bleed 16; reducing agent is fed in at 7. Treated solution leaves via barometric leg 8, condensates from each section are mixed and pass through a coalescing device 12 which includes fibre pads or packing pieces to a gravity separator 13 for mercury 14 and water 15, while vapour is removed by a steam ejector 9 to condensor 10 and another gravity separator, the ejector also providing the required vacuum. In one modification Fig.2 (not shown), the base of chamber 1 is stepped and includes a series of small capacity sumps from which the liquid is flash distilled, while in a further modification Fig.3 (not shown), inert gas is introduced at the base of the chamber to increase the rate of mercury vapourization.
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB610671A GB1373771A (en) | 1971-03-05 | 1971-03-05 | Mercury recovery process |
BE780222A BE780222R (en) | 1971-03-05 | 1972-03-03 | RECOVERY PROCESS |
NL7202879A NL7202879A (en) | 1971-03-05 | 1972-03-03 | |
IT21452/72A IT990501B (en) | 1971-03-05 | 1972-03-04 | PROCESS OF RECOVERY OF MERCURY |
FR7207655A FR2128648A2 (en) | 1970-12-31 | 1972-03-06 | Mercury recovery - from aq solns by treating with reducing agent and steam distilling finely divided or colloidal mercury |
DE19722210759 DE2210759A1 (en) | 1971-03-05 | 1972-03-06 | Process for the recovery of mercury |
GB24721/76A GB1530489A (en) | 1971-03-05 | 1977-06-15 | Process for the removal of mercury from aqueous solutions |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB610671A GB1373771A (en) | 1971-03-05 | 1971-03-05 | Mercury recovery process |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1373771A true GB1373771A (en) | 1974-11-13 |
Family
ID=9808495
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB610671A Expired GB1373771A (en) | 1970-12-31 | 1971-03-05 | Mercury recovery process |
Country Status (5)
Country | Link |
---|---|
BE (1) | BE780222R (en) |
DE (1) | DE2210759A1 (en) |
GB (1) | GB1373771A (en) |
IT (1) | IT990501B (en) |
NL (1) | NL7202879A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1245687A2 (en) * | 2001-03-30 | 2002-10-02 | Matsushita Electric Industrial Co., Ltd. | Method and apparatus for mercury recovery from waste fluorescent lamps |
EP2508243A1 (en) * | 2011-04-06 | 2012-10-10 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for removing mercury from waste water from hydrocarbon well stream |
WO2012104662A3 (en) * | 2011-02-02 | 2012-11-22 | Emmanuil Dermitzakis | Multi-stage desalination of low enthalpy |
ITPI20130058A1 (en) * | 2013-06-21 | 2014-12-22 | Scuola Superiore Sant Anna | REACTION TRANSPORT AND RELATED METHOD OF USE |
CN113354015A (en) * | 2021-05-06 | 2021-09-07 | 浦恩远 | Automatic change water sample mercury vapour and blow and take off enrichment facility |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5710173B2 (en) * | 1974-06-10 | 1982-02-25 | ||
DE3816282C1 (en) * | 1988-05-12 | 1989-10-05 | Gerhard Dipl.-Ing. 6940 Weinheim De Bernecker |
-
1971
- 1971-03-05 GB GB610671A patent/GB1373771A/en not_active Expired
-
1972
- 1972-03-03 NL NL7202879A patent/NL7202879A/xx unknown
- 1972-03-03 BE BE780222A patent/BE780222R/en active
- 1972-03-04 IT IT21452/72A patent/IT990501B/en active
- 1972-03-06 DE DE19722210759 patent/DE2210759A1/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1245687A2 (en) * | 2001-03-30 | 2002-10-02 | Matsushita Electric Industrial Co., Ltd. | Method and apparatus for mercury recovery from waste fluorescent lamps |
EP1245687A3 (en) * | 2001-03-30 | 2003-08-13 | Matsushita Electric Industrial Co., Ltd. | Method and apparatus for mercury recovery from waste fluorescent lamps |
US6800112B2 (en) | 2001-03-30 | 2004-10-05 | Matsushita Electric Industrial Co., Ltd. | Mercury recovery method |
US6866814B2 (en) | 2001-03-30 | 2005-03-15 | Matsushita Electric Industrial Co., Ltd. | Mercury recovery apparatus |
WO2012104662A3 (en) * | 2011-02-02 | 2012-11-22 | Emmanuil Dermitzakis | Multi-stage desalination of low enthalpy |
EP2508243A1 (en) * | 2011-04-06 | 2012-10-10 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for removing mercury from waste water from hydrocarbon well stream |
WO2012136780A1 (en) * | 2011-04-06 | 2012-10-11 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for removing mercury from waste water from hydrocarbon well stream |
AU2012238593B2 (en) * | 2011-04-06 | 2015-12-03 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for removing mercury from waste water from hydrocarbon well stream |
ITPI20130058A1 (en) * | 2013-06-21 | 2014-12-22 | Scuola Superiore Sant Anna | REACTION TRANSPORT AND RELATED METHOD OF USE |
CN113354015A (en) * | 2021-05-06 | 2021-09-07 | 浦恩远 | Automatic change water sample mercury vapour and blow and take off enrichment facility |
Also Published As
Publication number | Publication date |
---|---|
NL7202879A (en) | 1972-09-07 |
DE2210759A1 (en) | 1972-09-21 |
IT990501B (en) | 1975-07-10 |
BE780222R (en) | 1972-09-04 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |