CA2543958A1 - Process for reduction of inorganic contaminants from waste streams - Google Patents
Process for reduction of inorganic contaminants from waste streams Download PDFInfo
- Publication number
- CA2543958A1 CA2543958A1 CA002543958A CA2543958A CA2543958A1 CA 2543958 A1 CA2543958 A1 CA 2543958A1 CA 002543958 A CA002543958 A CA 002543958A CA 2543958 A CA2543958 A CA 2543958A CA 2543958 A1 CA2543958 A1 CA 2543958A1
- Authority
- CA
- Canada
- Prior art keywords
- mercury
- liquid stream
- used alumina
- bed
- sorbent
- 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.)
- Granted
Links
Classifications
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/02—Separation 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 by adsorption, e.g. preparative gas chromatography
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
- B01J20/08—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04 comprising aluminium oxide or hydroxide; comprising bauxite
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/104—Alumina
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/60—Heavy metals or heavy metal compounds
- B01D2257/602—Mercury or mercury compounds
-
- 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
- C02F2101/103—Arsenic compounds
-
- 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
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S210/00—Liquid purification or separation
- Y10S210/902—Materials removed
- Y10S210/911—Cumulative poison
- Y10S210/912—Heavy metal
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S210/00—Liquid purification or separation
- Y10S210/902—Materials removed
- Y10S210/911—Cumulative poison
- Y10S210/912—Heavy metal
- Y10S210/914—Mercury
Abstract
The invention relates to the use of used alumina to reduce the level of inorganic contaminants, such as mercury and arsenic, from waste fluid streams.
The invention further provides a process for reducing the level of mercury or arsenic in fluid streams by contacting the fluid stream with used alumina, such as used Claus catalyst.
The invention further provides a process for reducing the level of mercury or arsenic in fluid streams by contacting the fluid stream with used alumina, such as used Claus catalyst.
Claims (16)
1. A process for reducing the level of mercury from a liquid stream comprising contacting said liquid stream with used alumina.
2. The process of claim 1, wherein the used alumina is used Claus catalyst.
3. The process of claim 1, wherein the used alumina has a sulfur concentration of at least about 0.1- 25% by weight.
4. A process for reducing the level of mercury from a liquid stream containing mercury, comprising the steps of (a) flowing the liquid stream through a bed containing a sorbent, wherein the sorbent comprises used alumina;
(b) sorbing mercury from the liquid stream onto the surface of the sorbent; and (c) allowing the mercury-depleted effluent stream to exit from the outlet of the bed.
(b) sorbing mercury from the liquid stream onto the surface of the sorbent; and (c) allowing the mercury-depleted effluent stream to exit from the outlet of the bed.
5. The process of claim 4, wherein the used alumina is used Claus catalyst.
6. The process of claim 4, wherein the used alumina has a sulfur concentration of at least about 0.1- 25% by weight.
7. The process of claim 1 or claim 4, wherein the used alumina is crushed prior to being loaded on the bed.
8. The process of claim 7, wherein the used alumina is heated to remove moisture prior to being loaded on the bed.
9. The process of claim 1 or claim 4, wherein at least about 50% of mercury is removed from said liquid stream.
10. The process of claim 1 or claim 4, wherein at least about 75% of mercury is removed from said liquid stream.
11. The process of claim 1 or claim 4, wherein at least about 90% of mercury is removed from said liquid stream.
12. The process of claim 1 or claim 4, wherein the mercury is elemental mercury.
13. The process of claim 1 or claim 4, wherein the mercury is ionic mercury.
14. A process for reducing the level of arsenic from a liquid stream comprising contacting said liquid stream with used alumina.
15. The process of claim 14, wherein the used alumina is used Claus catalyst.
16. A process for reducing the level of arsenic from a liquid stre-am containing arsenic, comprising the steps of (a) flowing the liquid stream through a bed containing a sorbent, wherein the sorbent comprises used alumina;
(b) sorbing mercury from the liquid stream onto the surface of the sorbent; and (c) allowing the arsenic-depleted effluent stream to exit from the outlet of the bed.
(b) sorbing mercury from the liquid stream onto the surface of the sorbent; and (c) allowing the arsenic-depleted effluent stream to exit from the outlet of the bed.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US51610803P | 2003-10-31 | 2003-10-31 | |
US60/516,108 | 2003-10-31 | ||
PCT/US2004/036092 WO2005042130A1 (en) | 2003-10-31 | 2004-10-29 | Process for reduction of inorganic contaminants from waste streams |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2543958A1 true CA2543958A1 (en) | 2005-05-12 |
CA2543958C CA2543958C (en) | 2012-04-10 |
Family
ID=34549488
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2543958A Expired - Fee Related CA2543958C (en) | 2003-10-31 | 2004-10-29 | Process for reduction of inorganic contaminants from waste streams |
Country Status (5)
Country | Link |
---|---|
US (3) | US7341667B2 (en) |
EP (1) | EP1682241A4 (en) |
CN (1) | CN1901982B (en) |
CA (1) | CA2543958C (en) |
WO (1) | WO2005042130A1 (en) |
Families Citing this family (24)
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US6863825B2 (en) | 2003-01-29 | 2005-03-08 | Union Oil Company Of California | Process for removing arsenic from aqueous streams |
CN1901982B (en) * | 2003-10-31 | 2010-04-21 | 金属合金回收公司 | Process for reduction of inorganic contaminants from waste streams |
US8029618B2 (en) * | 2004-09-21 | 2011-10-04 | Saudi Arabian Oil Company | Manufacture of Portland cement using spent claus catalyst |
EP1877770B1 (en) * | 2005-05-02 | 2018-09-12 | Thermo Fisher Scientific Inc. | Method and apparatus for monitoring mercury in a gas sample |
US20070092418A1 (en) * | 2005-10-17 | 2007-04-26 | Chemical Products Corporation | Sorbents for Removal of Mercury from Flue Gas |
US8066874B2 (en) | 2006-12-28 | 2011-11-29 | Molycorp Minerals, Llc | Apparatus for treating a flow of an aqueous solution containing arsenic |
US8252087B2 (en) | 2007-10-31 | 2012-08-28 | Molycorp Minerals, Llc | Process and apparatus for treating a gas containing a contaminant |
US8349764B2 (en) | 2007-10-31 | 2013-01-08 | Molycorp Minerals, Llc | Composition for treating a fluid |
US7846869B2 (en) * | 2008-04-23 | 2010-12-07 | China Petroleum & Chemical Corporation | Process for pre-treating a desulfurization sorbent |
US7906027B2 (en) * | 2008-09-26 | 2011-03-15 | Conocophillips Company | Mercury removal process |
US8535422B2 (en) | 2009-01-26 | 2013-09-17 | St. Cloud Mining Company | Metal contaminant removal compositions and methods for making and using the same |
WO2010096571A2 (en) * | 2009-02-20 | 2010-08-26 | Conocophillips Company | Selenium removal process |
AU2010270695B2 (en) * | 2009-07-06 | 2016-02-25 | Cruickshank, Cecilia A. | Media for removal of contaminants from fluid streams and method of making and using same |
US20120018384A1 (en) * | 2010-02-01 | 2012-01-26 | John Sawyer | Mercury removal from water |
US8734560B2 (en) | 2010-09-10 | 2014-05-27 | Harsco Corporation | Agricultural blend and process of forming an agricultural blend |
US20120241381A1 (en) * | 2011-03-21 | 2012-09-27 | Bruso Bruce L | Method and apparatus for removal of selenium from water |
US9233863B2 (en) | 2011-04-13 | 2016-01-12 | Molycorp Minerals, Llc | Rare earth removal of hydrated and hydroxyl species |
US8524074B2 (en) | 2011-08-17 | 2013-09-03 | Nalco Company | Removal of mercury and mercuric compounds from crude oil streams |
US20140291246A1 (en) | 2013-03-16 | 2014-10-02 | Chemica Technologies, Inc. | Selective Adsorbent Fabric for Water Purification |
EP3113859A4 (en) | 2014-03-07 | 2017-10-04 | Secure Natural Resources LLC | Cerium (iv) oxide with exceptional arsenic removal properties |
US10526215B2 (en) * | 2014-07-21 | 2020-01-07 | The Frazer And Cruickshank Living Trust | Selenium and other contaminants removal process |
US9550148B2 (en) * | 2015-06-02 | 2017-01-24 | Paragon Waste Solutions, Llc | Heavy metal removal |
US10759681B2 (en) | 2018-06-28 | 2020-09-01 | Board Of Trustees Of The University Of Arkansas | Water purification compositions and the method of producing the same |
CN113713757A (en) * | 2021-08-30 | 2021-11-30 | 华中科技大学 | Preparation method and product of high-efficiency mercury adsorbent for waste gas liquid |
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-
2004
- 2004-10-29 CN CN2004800396183A patent/CN1901982B/en not_active Expired - Fee Related
- 2004-10-29 US US10/976,519 patent/US7341667B2/en active Active
- 2004-10-29 CA CA2543958A patent/CA2543958C/en not_active Expired - Fee Related
- 2004-10-29 WO PCT/US2004/036092 patent/WO2005042130A1/en active Application Filing
- 2004-10-29 EP EP04796804A patent/EP1682241A4/en not_active Withdrawn
-
2008
- 2008-02-01 US US12/024,377 patent/US7449118B2/en active Active
- 2008-02-01 US US12/024,365 patent/US7479230B2/en active Active
Also Published As
Publication number | Publication date |
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EP1682241A1 (en) | 2006-07-26 |
EP1682241A4 (en) | 2009-07-15 |
US20080135487A1 (en) | 2008-06-12 |
CA2543958C (en) | 2012-04-10 |
US7479230B2 (en) | 2009-01-20 |
CN1901982A (en) | 2007-01-24 |
CN1901982B (en) | 2010-04-21 |
US20080135486A1 (en) | 2008-06-12 |
US7341667B2 (en) | 2008-03-11 |
US7449118B2 (en) | 2008-11-11 |
US20050194320A1 (en) | 2005-09-08 |
WO2005042130A1 (en) | 2005-05-12 |
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