U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Process for removing arsenic from water

Patent 5182023 Issued on January 26, 1993. Estimated Expiration Date: Icon_subject October 17, 2011. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

3171735

3436177

Wastewater treatment
Patent #: 4014787
Issued on: 03/29/1977
Inventor: Shorr

Recovery of copper from arsenic containing metallurgical waste materials
Patent #: 4149880
Issued on: 04/17/1979
Inventor: Prater ,   et al.

Process for removing arsenic from aqueous mediums
Patent #: 4201667
Issued on: 05/06/1980
Inventor: Liao

Process for the treatment of raw materials containing arsenic and metal
Patent #: 4220627
Issued on: 09/02/1980
Inventor: Fugleberg ,   et al.

Process for the recovery of arsenic as a zinc arsenate and its _utilization in the purification of zinc plant electrolytes
Patent #: 4240826
Issued on: 12/23/1980
Inventor: Kangas ,   et al.

Process for recovering metal values from materials containing arsenic
Patent #: 4244734
Issued on: 01/13/1981
Inventor: Reynolds ,   et al.

Process for recovering arsenic compounds by sodium hydroxide leaching
Patent #: 4244927
Issued on: 01/13/1981
Inventor: Reynolds ,   et al.

Membrane processes for metal recovery and pollution control in metal process industries
Patent #: 4655928
Issued on: 04/07/1987
Inventor: Milton ,   et al.

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Inventors

Assignee

Application

No. 778568 filed on 10/17/1991

US Classes:

210/652, Hyperfiltration (e.g., reverse osmosis, etc.)210/650, Filtering through membrane (e.g., ultrafiltration)210/651, Removing specified material210/661By passing through suspended bed

Examiners

Primary: Dawson, Robert A.
Assistant: Fortuna, Ana

Attorney, Agent or Firm

International Class

B01D 061/00

Abstract

A process for treating arsenic-containing aqueous waste is described wherein the aqueous waste, treated if necessary to minimize the presence of materials which reduce the efficiency of reverse osmosis membranes, is passed through an ultrafilter to remove solids followed by a chemical treatment to adjust the pH to range from about 6 to 8 and to add antiscalants and antifouling materials, then following to subject the chemically treated filtrate to a reverse osmosis process to result in a permeate stream having less than about 50 parts per billion arsenic.

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