Jeffrey Gerard Peeters - Toronto, CA William A. Bonkoski - Wilmington DE, US Pierre Lucien Cote - Dundas, CA Hidayat Husain - Oakville, CA Timothy Michael Pickett - Salt Lake City UT, US
Assignee:
Zenon Technology Partnership - Wilmington DE
International Classification:
C02F 3/30
US Classification:
210615, 210617, 210630, 210631, 210150, 210914
Abstract:
A process has steps of one or more of aerobic treatment to remove COD and nitrify a waste stream, anoxic treatment to denitrify a waste stream, anoxic treatment to remove selenium and anaerobic treatment to remove heavy metals and sulphur. The process may be used to treat, for example, FGD blow down water. The process may further include one or more of (a) membrane separation of the waste stream upstream of the anoxic digestion to remove selenium, (b) dilution upstream of the biological treatment step, (c) physical/chemical pretreatment upstream of the biological processes or dilution step to remove TSS and soften the waste stream, or (d) ammonia stripping upstream of the biological treatment steps or dilutions step. These processes may be provided in a variety of suspended growth or fixed film reactors, for example a membrane bioreactor or a fixed film reactor having a GAC bed. Processes for biological treatment of inorganic compounds in a fixed medium reactor is described including steps of one or more of maintaining desired ORP levels, optionally by controlling nutrient addition, and removing solids or gas bubbles from the medium bed.
Apparatus And Method For Treating Fgd Blowdown Or Similar Liquids
Jeffrey Gerard Peeters - Toronto, CA William A. Bonkoski - Conshohocken PA, US Pierre Lucien Cote - Dundas, CA Hidayat Husain - Oakville, CA Timothy Michael Pickett - Salt Lake City UT, US
Assignee:
Zenon Technology Partnership - Wilmington DE
International Classification:
C02F 3/04
US Classification:
210615, 210150
Abstract:
A process has steps of one or more of aerobic treatment to remove COD and nitrify a waste stream, anoxic treatment to denitrify a waste stream, anoxic treatment to remove selenium and anaerobic treatment to remove heavy metals and sulphur. The process may be used to treat, for example, FGD blow down water. The process may further include one or more of (a) membrane separation of the waste stream upstream of the anoxic digestion to remove selenium, (b) dilution upstream of the biological treatment step, (c) physical/chemical pretreatment upstream of the biological processes or dilution step to remove TSS and soften the waste stream, or (d) ammonia stripping upstream of the biological treatment steps or dilutions step. These processes may be provided in a variety of suspended growth or fixed film reactors, for example a membrane bioreactor or a fixed film reactor having a GAC bed. Processes for biological treatment of inorganic compounds in a fixed medium reactor is described including steps of one or more of maintaining desired ORP levels, optionally by controlling nutrient addition, and removing solids or gas bubbles from the medium bed.
In one embodiment, a grey water treatment system includes an oxidation reactor for oxidizing grey water. The grey water treatment system also includes a biological reduction and precipitation system with microbes designed to remove one or more target components from the oxidized grey water.
Selenium Removal Using Chemical Oxidation And Biological Reduction
Timothy Michael PICKETT - Salt Lake City UT, US Yanguo Ma - Salt Lake City UT, US Jill Sonstegard - Layton UT, US
International Classification:
C02F 9/04 C02F 3/00 C02F 1/70 C02F 1/72 C02F 1/58
US Classification:
210719, 210205
Abstract:
Selenium in the form of a reduced species such as selenocyanate is oxidized to produce an oxidized selenium species such as selenate or selenite, and then a biological reduction process is used to remove selenium from the oxidized selenium species. In an example, a chemical oxidant is added to a wastewater containing selenocyanate to produce selenate and selenite. The partially treated wastewater is then fed to a reactor containing a fixed media supporting a biofilm with selenium reducing organisms. The selenium in the selenate and selenite is reduced to an insoluble form of selenium, such as elemental selenium, which precipitates from the wastewater.
Selenium Separation And Recovery From Bioreactor Sludge
Wastewater containing soluble selenium is treated in a bioreactor. Microorganisms in the reactor reduce the selenium to elemental selenium, which is insoluble. The elemental selenium is discharged from the reactor in waste sludge. The sludge is treated to recover selenium. In one method, the sludge is washed with chemicals, for example surfactants, and agitated to disrupt the adhesion of the selenium particles to the cells. The selenium particles are then separated from the cells using a physical separation process such as a centrifuge or differential filtration. In another method, the sludge is de-watered or dried to a very high solids content. The selenium particles are dissolved using an oxidizer under high pH conditions. A solids fraction is removed from the resulting slurry. A resulting selenium brine is further refined to recover the selenium.
D. Jack Adams - Park City UT Timothy M. Pickett - Salt Lake City UT
Assignee:
Weber State University - Ogden UT
International Classification:
C02F 300 C02F 334
US Classification:
210611
Abstract:
Dissolved selenium is removed from contaminated water by treating the water in a reactor containing selected endemic and other selenium reducing organisms. Microbes may be isolated from the specific water or imported from other selenium contaminated water, The microbes are then screened for ability to reduce selenium under the site specific environmental conditions. The selected microbes are optimized for selenium reduction, then established in a high density biofilm within a reactor. The selenium contaminated water is passed through the reactor with optimized nutrient mix added as needed. The elemental selenium is precipitated and removed from the water.
Fail Safe Flushing Bioreactor For Selenium Water Treatment
A biological reactor system treats concentrated contaminated water with a combination of upflow and downflow bioreactors that are downstream from a reverse osmosis or other concentrator. The system may have a fail safe configuration where flush water may be introduced to the reactors in the event of a power failure or when taking the reactors offline. Many reverse osmosis systems introduce antiscalant treatments upstream so that the reverse osmosis filters do not scale. However, such treatments result in superconcentrated conditions of the antiscalants in the contaminated water processed by the bioreactors. A flushing system may deconcentrate the bioreactors to prevent the antiscalants from precipitating and fouling the bioreactors.
Fail Safe Flushing Bioreactor For Selenium Water Treatment
A biological reactor system treats concentrated contaminated water with a combination of upflow and downflow bioreactors that are downstream from a reverse osmosis or other concentrator. The system may have a fail safe configuration where flush water may be introduced to the reactors in the event of a power failure or when taking the reactors offline. Many reverse osmosis systems introduce antiscalant treatments upstream so that the reverse osmosis filters do not scale. However, such treatments result in superconcentrated conditions of the antiscalants in the contaminated water processed by the bioreactors. A flushing system may deconcentrate the bioreactors to prevent the antiscalants from precipitating and fouling the bioreactors.
Name / Title
Company / Classification
Phones & Addresses
Timothy W. Pickett Principal
Tim Pickett LLC Business Services at Non-Commercial Site
Shive-Hattery, Inc. since Apr 2008
Mechanical Engineer EIT
NGI Apr 2007 - Apr 2008
Mechanical Engineer
BYU Capstone Sep 2006 - Apr 2007
Capstone Team Leader
Brigham Young University Jul 2005 - Apr 2007
Biomedical Research Assistant
Northwest Orthotics and Prosthetics Apr 2005 - Mar 2006
Prosthetic Technician
Education:
Brigham Young University 2003 - 2007
BS, Mechanical Engineering
Skills:
Mechanical Engineering Cad Engineering Design of Experiments R&D Heat Transfer Prototype Development Ideation and Brainstorming Testing Solidworks Instrumentation Cnc Operation 3D Printing Fluid Mechanics Ergonomics and Human Factors Intellectual Property Thermodynamics Machining Product Development Design For Manufacturing Iso 13485 Fda Qsr Ethnographic Research Microsoft Excel Project Management Camworks
Languages:
Spanish Portuguese English
Certifications:
License 8346338 Ncees and State of Utah, License 8346338 Professional Engineer Iso 13485:2016 Lead Auditor Certified Solidworks Associate (Cswa)
Utah Marijuana Org
Founder
Steward Health Care
Physician Assistant
Education:
University of Utah School of Medicine 2020 - 2020
Master of Science, Masters
University of Utah School of Medicine 2011 - 2014
Master of Science, Masters
University of Utah School of Medicine 2012 - 2014
Master of Science, Masters
Skills:
Emergency Medicine Bls Acls Medicine Family Medicine Pediatrics Internal Medicine Emr Medical Education Surgery Healthcare Public Health Hospitals Cpr Certified Ekg
Western Michigan University - Haworth College of Business 2005 - 2011
Bachelor's of Business Administration, Computer Information Systems
Skills:
VMware Infrastructure Windows Server 2003 Windows Server 2008 Cisco Switches Watchguard firewalls Windows 7 Windows XP Professional Mac OS X Dell PowerEdge Servers Dell OpenManage HP Proliant Mitel VoIP Manufacturing Management Unix Wireless Networking Fortinet Firewalls Cisco Routers iPhone iPad WAN LAN Windows Server