Patent classifications
B01D21/08
Dehydrator system and methods of using the same
Dehydrator systems having a core dehydrator and a mixing unit are described herein and methods of using the same. The core dehydrator comprises a turbulent flow mixing compartment the turbulent flow mixing compartment with plate openings having a turbulent flow transition zone where linear speed of fluid flow is reduced, a clarifying sediment chamber, where fluid flow is substantially laminar) comprising a plurality of small deflector plaques and a plurality of large deflector plaques and a flocculation pipe. In the turbulent flow transition zone, fluid flow transitions from turbulent flow to laminar flow. The mixing unit comprises a plurality of vertical flocculators. The mixing unit further comprises a rapid mixing manifold. The rapid mixing manifold contains drilling fluids and flocculant polymers.
Dehydrator system and methods of using the same
Dehydrator systems having a core dehydrator and a mixing unit are described herein and methods of using the same. The core dehydrator comprises a turbulent flow mixing compartment the turbulent flow mixing compartment with plate openings having a turbulent flow transition zone where linear speed of fluid flow is reduced, a clarifying sediment chamber, where fluid flow is substantially laminar) comprising a plurality of small deflector plaques and a plurality of large deflector plaques and a flocculation pipe. In the turbulent flow transition zone, fluid flow transitions from turbulent flow to laminar flow. The mixing unit comprises a plurality of vertical flocculators. The mixing unit further comprises a rapid mixing manifold. The rapid mixing manifold contains drilling fluids and flocculant polymers.
FLOTATION CELL
THIS invention relates to froth flotation, and more specifically to a froth flotation cell and an internal sand removal arrangement for the froth flotation cell. The froth flotation cell included a tank having an operatively lower zone, an intermediate zone and an operatively upper zone, and a central dispersing chamber disposed in the intermediate zone of the tank. A slurry inlet is located in the operatively lower zone of the tank, and a slurry outlet conduit extends from the operatively upper zone of the tank towards a slurry outlet. The froth flotation cell is characterised in that the operatively lower zone is also selectively in flow communication with the slurry outlet of the tank, in order for slurry located in the operatively lower zone of the tank selectively to be displaceable into the slurry outlet.
Algae separation system
An algae separation system can comprise a tank comprising an algae separation chamber. The system can comprise a first inlet to supply algae-containing water to a mixing region of the algae separation chamber. The system can comprise a second inlet to supply gas-containing water comprising dissolved gas to the mixing region of the algae separation chamber. The system can comprise a bubble generator in fluid communication with the second inlet, the bubble generator configured to generate a plurality of bubbles from the gas-containing water and to supply the plurality of bubbles to the mixing region to mix with the algae-containing water.
Algae separation system
An algae separation system can comprise a tank comprising an algae separation chamber. The system can comprise a first inlet to supply algae-containing water to a mixing region of the algae separation chamber. The system can comprise a second inlet to supply gas-containing water comprising dissolved gas to the mixing region of the algae separation chamber. The system can comprise a bubble generator in fluid communication with the second inlet, the bubble generator configured to generate a plurality of bubbles from the gas-containing water and to supply the plurality of bubbles to the mixing region to mix with the algae-containing water.
System And Method For Wastewater Treatment Including Use of Microporous Media Beds
The invention provides water treatment for a municipal wastewater source by removal of contaminants including nutrient contaminants, FOG, total suspended solids, pathogenic bacteria, viruses and metal contaminates. Pathogenic bacteria and viruses are removed without the use of chlorine contact, ultraviolet treatment or reverse osmosis treatment. The treatment steps may include: oxygenation by single cell algae, electrocoagulation, precipitation of solids, absorption and flocculation, de-aeration, metered amounts of an anionic or cationic flocculant added for further coagulation and precipitation of coagulated material; mixing and subsequent clarification; sand filtration; and removal of remaining contaminants by containers housing microporous media beds or ion-exchange beds. The treatment steps may be used in various combinations and sub-combinations in order to focus treatment on prevalent contaminants in the wastewater to be treated. The invention further includes embodiments of the media bed containers and a non-transitory computer-readable medium to execute a method for conducting treatment of a wastewater stream.
System And Method For Wastewater Treatment Including Use of Microporous Media Beds
The invention provides water treatment for a municipal wastewater source by removal of contaminants including nutrient contaminants, FOG, total suspended solids, pathogenic bacteria, viruses and metal contaminates. Pathogenic bacteria and viruses are removed without the use of chlorine contact, ultraviolet treatment or reverse osmosis treatment. The treatment steps may include: oxygenation by single cell algae, electrocoagulation, precipitation of solids, absorption and flocculation, de-aeration, metered amounts of an anionic or cationic flocculant added for further coagulation and precipitation of coagulated material; mixing and subsequent clarification; sand filtration; and removal of remaining contaminants by containers housing microporous media beds or ion-exchange beds. The treatment steps may be used in various combinations and sub-combinations in order to focus treatment on prevalent contaminants in the wastewater to be treated. The invention further includes embodiments of the media bed containers and a non-transitory computer-readable medium to execute a method for conducting treatment of a wastewater stream.
Transportable multi-chamber water filtration systems
A transportable multi-chamber water filtration system useable at construction sites with sources of contaminated water is disclosed. The transportable multi-chamber water filtration system removes sediment and contaminants from contaminated water by combined processes of gravitational settling, filtration and coagulation of sediment by the use of flocculants. The system provides efficient removal of sediment and contaminants from the water around various sized sites.
Transportable multi-chamber water filtration systems
A transportable multi-chamber water filtration system useable at construction sites with sources of contaminated water is disclosed. The transportable multi-chamber water filtration system removes sediment and contaminants from contaminated water by combined processes of gravitational settling, filtration and coagulation of sediment by the use of flocculants. The system provides efficient removal of sediment and contaminants from the water around various sized sites.
Method for measuring a degree of homogeneity of oils using back titration and measuring apparatus using the same
The present disclosure relates to an apparatus and a method for measuring miscibility in oil using back titration. The apparatus includes: a flocculation solution storage unit; a flow cell including a UV transmitting member; a dissolving agent storage unit; a UV irradiation unit; and a measurement unit, wherein: a flocculation solution is stored in the flocculation solution storage unit; the flocculation solution circulates between the flocculation solution storage unit and the flow cell; the measurement unit measures the UV transmittance of the flocculation solution while the dissolving agent in the dissolving agent storage unit is supplied to the flocculation solution storage unit; the miscibility in the oil is calculated from the amount of dissolving agent supplied and a change in the UV transmittance measured by the measurement unit; and the miscibility is calculated based on a time point when the slope of increase in the UV transmittance changes.