1. Technical Field
This invention relates to battery systems, and more specifically, to reduction-oxidation (redox) flow batteries with a hydrogen rebalance cell.
2. Discussion of Related Art
Redox flow batteries store electrical energy in a chemical form and subsequently dispense the stored energy in an electrical form via a spontaneous reverse redox reaction. Conversion between chemical and electrical energy occurs in a reactor cell.
Electrolyte can be flowed through a reactor cell where the electrochemical reaction takes place. Externally stored electrolytes can be flowed through the battery system by pumping, gravity feed, or by any other method of moving fluid through the system. The electrolyte can be charged and discharged through many cycles. However, over time the electrolyte degrades, at least partially as a result of loss of hydrogen from the electrolyte. Hydrogen gas is emitted as a byproduct of the electrochemical charge and discharge reactions that the electrolyte undergoes.
Redox flow batteries have a wide application. Examples include use as uninterruptible power supplies for mission critical devices and services, storage and distribution of green energy, and electric automobiles.
There is, therefore, a need to provide an efficient and simplified way to maintain balance of the electrolyte and enhance overall capacity, lifetime, and performance of the battery system.
Consistent with embodiments of the present invention, a redox flow cell system having a rebalance cell and a venturi pump, and providing enhanced capacity and performance of the flow battery is presented.
A redox flow cell system according to the present invention can include at least one flow cell; a pumping system that pumps a first electrolyte from a first storage tank through a first half cell of the at least one flow cell; a rebalance cell coupled to receive a second electrolyte from a second storage tank; and a venturi pump in the pumping system, the venturi pump further coupled to receive gasses that flow from the first storage tank and through the rebalance cell.
A method for circulating hydrogen gas in a redox flow cell system consistent with embodiments of the present invention includes flowing a first electrolyte via a pumping system from a first storage tank through a first half cell of at least one flow cell; receiving a second electrolyte into a rebalance cell coupled to receive the second electrolyte; and drawing hydrogen gas from the first storage tank through the rebalance cell using a venturi pump coupled to the pumping system and further coupled to draw hydrogen gas from the first storage tank through the rebalance cell.
A method of rebalancing a redox flow cell system consistent with embodiments of the present invention includes flowing a first electrolyte via a pumping system from a first storage tank through a first half cell of at least one flow cell; receiving a second electrolyte into a rebalance cell coupled to receive the second electrolyte; and drawing hydrogen gas from the first storage tank through the rebalance cell using a venturi pump coupled to the pumping system and further coupled to draw hydrogen gas from the first storage tank through the rebalance cell.
These and other embodiments of the present invention are further described below with reference to the following figures.
In order to more fully understand the present invention, reference is made to the accompanying drawings, with the understanding that these drawings are not intended to limit the scope of the invention.
In the figures, elements having the same designation have the same or similar function. The figures are illustrative only and relative sizes and distances depicted in the figures are for convenience of illustration only and have no further meaning.
This description is explicative of certain embodiments of the invention and should not be considered to be limiting. The apparatus components and method steps are represented here by appropriate conventional symbols in the drawings, showing only those specific details that are pertinent to understanding the embodiments of the present invention so as not to obscure the disclosure with details that will be readily apparent to those of ordinary skill in the art having the benefit of the description herein.
Consistent with the embodiments of the present invention, a reduction-oxidation (redox) flow battery with active hydrogen circulation without the need for any externally powered pump is proposed.
A redox flow battery according to the present invention can include a simple, no moving parts pump, based on the Venturi principle. The pump may be fitted to an electrolyte return line and employed to circulate hydrogen gas using reverse suction.
A method of providing active hydrogen circulation consistent with embodiments of the present invention includes enhanced performance of the rebalance cell by providing a suitable transfer of hydrogen into the rebalance cell.
There are different electrolyte solutions which in turn contain differing dissolved electro-active chemicals. For example, in an exemplary embodiment of a redox system using electro-active chromium and ferrous chemicals, the anolyte may be comprised of an aqueous solution of hydrochloric acid and chromium chloride and the catholyte may be comprised of an aqueous solution of hydrochloric acid and iron chloride. In some other embodiments of the redox system using electro-active chromium and ferrous chemicals, both the anolyte and catholyte may be comprised of an aqueous solution of hydrochloric acid combined with chromium chloride and iron chloride.
The electro-chemical capacity of the electrolytes is a function of the amount of active material contained in the solution of the electrolytes and the oxidation state or charge of the electrolytes. The system is “in balance” when the anolyte and the catholyte have an equivalent amount of active material and charge. However, over time an electrochemical imbalance of the electrolytes may occur due to side reactions causing the system to become unbalanced due to differing charges between the anolyte and catholyte. Such imbalance reduces the output capacity of the battery. It is therefore desirable to maintain a balance of active material in the electrolyte solutions in order to maximize capacity and efficiency.
When electrolyte is flowed through a reactor cell an electrochemical reaction takes place in the reactor cell:
Cathodic reaction in half cell 120: Fe3+ +e-→Fe2+
Anodic reaction in half cell 118: Cr2+→Cr3+ +e-
In addition, a secondary reaction takes places where hydrogen gas (H2) is emitted in an electrolysis reaction:
2HCL→H2+2Cl−
The H2 is emitted as gas and the Cl— is a scavenger. The H2 and Cl must be recombined to maintain system balance.
The function of rebalance cell 202 may be significantly enhanced if the hydrogen gas is actively circulated as opposed to being “dead headed”. Under dead heading, the only driving force is partial pressure which results in very slow transfer of the hydrogen gas into rebalance cell 202. The use of normal gas pumps present problems in terms of both cost and reliability. One solution is to take advantage of the circulating electrolyte from anolyte chamber 104 to provide the driving force to circulate hydrogen gas 224 present at the top of anolyte chamber 206. The present invention provides that a venturi pump 214 may be coupled to electrolyte return pathway 212. Venturi pump 214 causes hydrogen gas (H2) 224 to be drawn from H2 tap 218 of electrolyte chamber 104 to produce an active flow of H2 through rebalance cell 202. A check-valve 204 can be incorporated into H2 return line 220 to prevent any backflow from entering the rebalance cell.
An embodiment of pump 214 is shown in
While preferred embodiments of the present invention have been shown and described herein, it will be obvious to those skilled in the art that such embodiments are provided by way of example only. Numerous variations, changes, and substitutions will now occur to those skilled in the art without departing from the invention. As those of ordinary skill in the art will readily appreciate, for example, the present invention may circulate and recombine other gasses such as. It should be understood that various alternatives to the embodiments of the invention described herein may be employed in practicing the invention.
It is intended that the following claims define the scope of the invention and that methods and structures within the scope of these claims are their equivalents be covered thereby.
The present application claims benefit under 35 U.S.C. §119(e) of U.S. Provisional Application No. 61/104,596 filed on Oct. 10, 2008, entitled “Venturi Pumping System In A Hydrogen Gas Circulation Of A Flow Battery,” the content of which is hereby incorporated by reference in its entirety.
Number | Date | Country | |
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61104596 | Oct 2008 | US |