Polyurethane oil de-emulsification unit
View Patent ↗A process for separating an aqueous emulsion including an aqueous phase and an non-aqueous phase into separated aqueous and non-aqueous phases, to provide a recovered non-aqueous phase, and to provide a recovered aqueous phase containing an acceptable level of the non-aqueous phase. In the process, at least one body, and preferably two or more bodies, of polymeric material with a high surface area, typically a foam material or polymer chips, is used in a horizontal flow treatment system to break the emulsion and thus provide both the aqueous and non-aqueous phases as two separate flows. A wide range of polymers can be used in the system as the polymeric material including polyurethane, polypropylene, polystyrene, polyester, and polyethylene. If a very low level of non-aqueous phase in the effluent is required, for example to meet potable water standards, then a Kozlowski polyurethane, as described in U.S. Pat. No. 5,239,040, is preferred as the last Polymeric material body.
1. A process for continuously separating a flow of an aqueous emulsion including an aqueous continuous phase and a non-aqueous disperse phase to provide a flow comprising a non-aqueous phase and a further flow comprising a recovered aqueous phase containing an acceptable level of non-aqueous phase, the process comprising:
providing first and second compartments, the first compartment comprising a first enclosure occupying part of the space thereof and comprising a fixed upstream foraminous sidewall and an opposed fixed downstream foraminous sidewall, the second compartment comprising a second enclosure occupying part of the space thereof and comprising a fixed upstream foraminous sidewall and an opposed fixed downstream foraminous sidewall;
packing the first enclosure with a first body of high surface area particulate polymeric foam material;
packing the second enclosure with a second body of high surface area particulate polymeric foam material;
feeding the flow of aqueous emulsion into the first enclosure via the fixed foraminous sidewall thereof;
providing for a flow comprising a non-aqueous phase component and an aqueous phase component to flow through the opposed fixed downstream foraminous sidewall of the first enclosure into a first separation space within the first compartment for phase separation of the components;
recovering from the first separation space a non-aqueous flow comprising the non-aqueous phase component;
recovering from the first separation space a recovered aqueous flow comprising the aqueous phase component;
feeding the recovered aqueous flow into the second enclosure via the fixed foraminous sidewall thereof;
providing for a flow comprising a respective non-aqueous phase component and a respective aqueous phase component to flow through the opposed fixed downstream foraminous sidewall of the second enclosure into a second separation space within the first compartment for phase separation of the respective components;
recovering from the second separation space a non-aqueous flow comprising the respective non-aqueous phase component; and
recovering from the respective separation space a recovered aqueous flow comprising the respective aqueous phase component.
2. A process according to claim 1 further comprising:
providing a third enclosure between the first and second enclosures thereby defining a continuous flow path, the third enclosure comprising respective opposed fixed upstream and downstream foraminous sidewalls;
packing the third enclosure with a third body of high surface area particulate polymeric foam material;
feeding the recovered aqueous flow from upstream the flow path into the third enclosure;
providing for a flow comprising a further respective non-aqueous phase component and a further respective aqueous phase component to flow through the opposed fixed downstream foraminous sidewall of the third enclosure into a second separation space for phase separation of the further respective components;
recovering from the third separation space a non-aqueous flow comprising the further respective non-aqueous phase component; and
recovering from the further respective separation space a recovered aqueous flow comprising the further respective aqueous phase component for delivery downstream in the flow path.
3. A process according to claim 1 wherein for each enclosure the high surface area particulate polymeric foam material is the same.
4. A process according to claim 2 wherein for each enclosure the high surface area particulate polymeric foam material is the same.
5. A process according to claim 1 wherein the high surface area particulate polymeric foam material for each enclosure is not the same.
6. A process according to claim 2 wherein the high surface area particulate polymeric foam material for each enclosure is not the same.
7. A process according to claim 1 wherein the high surface area particulate polymeric foam material for each enclosure comprises polyurethane.
8. A process according to claim 2 wherein the high surface area particulate polymeric foam material for each enclosure comprises polyurethane.