A direct carbon fuel cell (DCFC) has a conductive mesh between an anode and a cathode of the DCFC. The conductive mesh is positioned at a specified distance from the anode. As the DCFC is operated, a carbon/carbonate fluid flows through the conductive mesh and though the porous anode. If the rate of carbon introduced into the DCFC is greater than the amount consumed, carbon will build up on the surface on the anode. Once the carbon build-up reaches the mesh, a conductive path will be created between the mesh and anode. A controller in contact with the conductive mesh measures the resistance between the conductive mesh and the anode and when the measured resistance falls to or below a defined set-point indicating a resistance when a conductive path between the anode and conductive mesh has formed, the controller can send a carbon build-up detected signal, and/or execute mitigation actions to reduce the amount of carbon delivered to the cell.

Flow type electrochemical cells are disclosed. The electrochemical cell has an anode half-cell, a cathode half-cell, and permeable separating layer. The half-cells are bounded by side elements. Respective porous electrodes are housed in the half-cells. The permeable separating layer is disposed between the anode half-cell and the cathode half-cell. An electrolyte region connected to an electrolyte feed and an electrolyte outflow region connected to an electrolyte drain are further provided. An electrolyte inflow region and an electrolyte outflow region are disposed on opposite sides of the porous electrodes such that inflowing electrolyte flows through the porous electrode perpendicularly to the permeable separating layer.

A battery with a corrosion-resistant ion-exchange membrane system is presented. The battery has an acidic catholyte, an anode metal that is chemically reactive towards water, and an ion-exchange membrane system. Some examples of anode metals include alkali metals, alkaline earth metals, and aluminum (Al). The ion-exchange membrane system includes a solid, cation-permeable, water-impermeable first membrane adjacent to the anode, prone to decomposition upon chemical reaction with an acid, an anion-permeable second membrane adjacent to the cathode, and a buffer compartment including a solution, interposed between the first membrane and the second membrane. In response to discharging the battery, the solution in the buffer compartment accepts cations from the anode and anions from the cathode, forming a cation-anion salt solution in the buffer compartment. The second membrane prevents the transportation of protons from the catholyte to the buffer compartment, and so prevents the corrosion of the first membrane.

The present invention relates to methods and systems related to fuel cells, and in particular, to direct carbon fuel cells. The methods and systems relate to cleaning and removal of components utilized and produced during operation of the fuel cell, regeneration of components utilized during operation of the fuel cell, and generating power using the fuel cell.

In one embodiment of the present disclosure, a composition for producing a vanadium electrolyte includes a vanadium compound and an ion solution containing vanadium ions and hydrogen ions. In another embodiment, a method for producing a vanadium electrolyte includes obtaining a vanadium compound, and mixing the vanadium compound with an ion solution containing vanadium ions and hydrogen ions.

In one embodiment of the present disclosure, a composition for producing a vanadium electrolyte includes a vanadium compound and an ion solution containing vanadium ions and hydrogen ions. In another embodiment, a method for producing a vanadium electrolyte includes obtaining a vanadium compound, and mixing the vanadium compound with an ion solution containing vanadium ions and hydrogen ions.