A deep sludge dewatering method using electroosmosis with filter bags, including (1) placing a filter bag on a slope on which a cathode electrode is arranged; (2) injecting sludge into the filter bag, and after the filter bag is filled with the sludge, closing an inlet of the filter bag; and (3) laying an anode electrode on the filter bag filled with the sludge, and connecting the cathode electrode and the anode electrode to a DC power supply via an electric wire, and carrying out energization for electroosmosis so that water flows down the slope. The present invention can be used for recycling of the sludge produced in underground and tunnel excavation projects, and has the advantages of large processing capacity, simple process, good treatment effect and available resource recycling.

A foundation (1) for a structure such as an off-shore wind turbine. The foundation (1) comprises a body (4) having a lateral surface (8,9) and a distal end (5) for insertion into a soil (2). At least a region of the lateral surface (8,9) forms a first electrode. A second electrode (7) is provided on the lateral surface (8,9) of the body (4) and is electrically insulated from the first electrode. The body (4) further comprises a spacing formation (6) for forming a gap (11) between the second electrode (7) and the soil (2) when the body (4) is inserted into the soil (2). In use, an electric potential may be established between the electrodes to induce electro-osmosis in the soil for allowing the foundation to be installed more easily. The polarity of the electric potential may also be reversed for stabilising the foundation.

Various examples are provided for electrokinetic dewatering of e.g., phosphatic clay suspensions. In one example, among others, a system includes a separation chamber including an anode and a cathode extending ends of the separation chamber and a power supply configured to energize the anode and the cathode to establish an electric field. An inlet at one end of the separation chamber can supply a dilute feed suspension and an outlet at another end of the separation chamber can remove supernatant water. The electric field can consolidate solids in the dilute feed suspension. Consolidated solids may be removed by a removal mechanism. In another example, a method includes supplying a dilute feed suspension including suspended solids, establishing an electric field to consolidate solids, and removing supernatant water.

Various examples are provided for electrokinetic dewatering of e.g., phosphatic clay suspensions. In one example, among others, a system includes a separation chamber including an anode and a cathode extending ends of the separation chamber and a power supply configured to energize the anode and the cathode to establish an electric field. An inlet at one end of the separation chamber can supply a dilute feed suspension and an outlet at another end of the separation chamber can remove supernatant water. The electric field can consolidate solids in the dilute feed suspension. Consolidated solids may be removed by a removal mechanism. In another example, a method includes supplying a dilute feed suspension including suspended solids, establishing an electric field to consolidate solids, and removing supernatant water.

Various methods and systems are provided for electrokinetic dewatering of suspensions such as, e.g., phosphatic clay. In one example, among others, a system for continuous dewatering includes a cake formation zone including a first anode and a first cathode each extending across a first portion of a separation chamber; a cake dewatering zone including a second anode and a second cathode; an inlet configured to supply a dilute feed suspension comprising solids suspended in water to the cake formation zone; and a conveying belt extending between the first anode and the first cathode and between the second anode and the second cathode. A first electric field between the first anode and the first cathode forms a cake on the conveying belt by consolidating the solids, and a second electric field between the second anode and the second cathode dewaters the cake on the conveying belt.

Various methods and systems are provided for electrokinetic dewatering of suspensions such as, e.g., phosphatic clay. In one example, among others, a system for continuous dewatering includes a cake formation zone including a first anode and a first cathode each extending across a first portion of a separation chamber; a cake dewatering zone including a second anode and a second cathode; an inlet configured to supply a dilute feed suspension comprising solids suspended in water to the cake formation zone; and a conveying belt extending between the first anode and the first cathode and between the second anode and the second cathode. A first electric field between the first anode and the first cathode forms a cake on the conveying belt by consolidating the solids, and a second electric field between the second anode and the second cathode dewaters the cake on the conveying belt.

A porous membrane for use in an electroosmotic pump for pumping a fluid by electroosmotic transport, the porous membrane comprising: first and second opposite surfaces and a net fluid flow direction extending in the porous membrane between said opposite surfaces, wherein when a given amount of charge flows through the porous membrane from the first to the second opposite surface more electroosmotic transport of the fluid will occur than when the same amount of charge flows through the porous membrane from the second to the first, opposite surface.

A porous membrane for use in an electroosmotic pump for pumping a fluid by electroosmotic transport, the porous membrane comprising: first and second opposite surfaces and a net fluid flow direction extending in the porous membrane between said opposite surfaces, wherein when a given amount of charge flows through the porous membrane from the first to the second opposite surface more electroosmotic transport of the fluid will occur than when the same amount of charge flows through the porous membrane from the second to the first, opposite surface.

Capacitive electrokinetic densification, decontamination and dewatering of suspensions and soils can be performed while controlling and/or preventing chemical and pH changes in the densified material and extracted water. High electrical capacitance electrodes or Electric Double Layer Capacitor (EDLC) electrodes are used which can operate without redox reactions occurring on their surfaces until their developed voltage reaches the standard electrode potential of the electrode. Water-retaining, flexible covers for the EDLC electrodes have drainage and filtering capabilities and are made of a fabric which allows the passage of ions, water and electricity therethrough and facilitate continuous electrical contact between the EDLC electrode and the surrounding suspension.

Capacitive electrokinetic densification, decontamination and dewatering of suspensions and soils can be performed while controlling and/or preventing chemical and pH changes in the densified material and extracted water. High electrical capacitance electrodes or Electric Double Layer Capacitor (EDLC) electrodes are used which can operate without redox reactions occurring on their surfaces until their developed voltage reaches the standard electrode potential of the electrode. Water-retaining, flexible covers for the EDLC electrodes have drainage and filtering capabilities and are made of a fabric which allows the passage of ions, water and electricity therethrough and facilitate continuous electrical contact between the EDLC electrode and the surrounding suspension.