An exemplary embodiment of the regenerative electrochemical cell system comprises: a fuel cell module comprising a fuel cell oxygen inlet in fluid communication a water storage device, and a fuel cell hydrogen inlet in fluid communication with both an oxygen source and with a gaseous portion of an water phase separation device; an electrolysis module comprising an electrolysis water inlet in fluid communication with the water storage device via a fuel cell oxygen outlet, and an electrolysis water outlet in fluid communication with the fuel cell hydrogen.
One of the embodiments for operating a regenerative electrochemical cell system disclosed herein, comprises: introducing feed hydrogen from a hydrogen storage system to a fuel cell hydrogen electrode and introducing feed oxygen from an oxygen/water phase separation device to a fuel cell oxygen electrode; reacting hydrogen ions with the oxygen to generate electricity and water; once the fuel cell has attained operating conditions, ceasing the feed oxygen from the oxygen/water phase separation device, and introducing second oxygen from a surrounding atmosphere module to the fuel cell oxygen electrode; directing the water to a water storage device; introducing water to an electrolysis water electrode and power to an electrolysis module, to produce refuel hydrogen and oxygen; and directing the refuel hydrogen to the hydrogen storage device.
Drawings
Claims67
A regenerative electrochemical cell system, comprising:
a fuel cell module comprising a fuel cell hydrogen inlet in fluid communication a hydrogen storage system, and a fuel cell oxygen inlet in fluid communication with both a first oxygen source and a second oxygen source, wherein the first oxygen source is from a surrounding atmosphere and the second oxygen source is from a gaseous portion of an oxygen/water phase separation device;
and
an electrolysis module in fluid communication with the fuel cell module.
A method for operating a regenerative electrochemical cell system, comprising:
starting up a fuel cell module by introducing feed hydrogen from a hydrogen storage system to a fuel cell hydrogen electrode and introducing feed oxygen from an oxygen/water phase separation device to a fuel cell oxygen electrode, and reacting hydrogen ions with the feed oxygen to generate electricity and fuel cell water;
once the fuel cell has attained operating conditions, ceasing the introduction of the feed oxygen, and introducing second oxygen from a surrounding atmosphere to the fuel cell oxygen electrode;
directing the fuel cell water to a water storage device;
introducing electrolysis water to an electrolysis water electrode, and introducing power to an electrolysis module, to produce refuel hydrogen and refuel oxygen;
and
directing the refuel hydrogen to the hydrogen storage system.
3 more elements
A method for operating a regenerative electrochemical cell system, comprising:
maintaining a fuel cell such that the fuel cell attains an operating temperature in less than or equal to about 1 minute;
introducing hydrogen to a fuel cell hydrogen electrode and oxygen to a fuel cell oxygen electrode;
forming hydrogen ions and electrons at the fuel cell hydrogen electrodes;
passing the electrodes electrons through an external load to the fuel cell oxygen electrode;
and
reacting the hydrogen ions with the oxygen at the fuel cell oxygen electrode to form water.
3 more elements
A method for operating a regenerative electrochemical cell system, comprising:
introducing feed hydrogen from a hydrogen storage device to a fuel cell hydrogen electrode and introducing feed oxygen to a fuel cell oxygen electrode;
reacting hydrogen ions with the oxygen to produce water;
introducing an oxygen/water stream from the fuel cell oxygen electrode through a vortex tube to produce a hot stream and a cool stream, wherein the hot stream has a higher temperature than the cool stream;
introducing the cool stream to a phase separation device.
1 more element
An electrochemical regenerative cell system comprising:
a first conduit in fluid communication with a hydrogen storage device and a dryer;
a first pressure regulator disposed in the first conduit between the hydrogen storage device and the dryer, the pressure regulator capable of reducing a pressure of a gas stream discharged from the hydrogen storage device to the dryer;
a second conduit in fluid communication with the fuel cell module and at least one of the hydrogen storage device and the dryer;
and
a second pressure regulator disposed in the second conduit, wherein a pressure rating for the first pressure regulator is equal to or greater than a pressure rating for the second pressure regulator.
2 more elements
A method for operating a regenerative electrochemical cell system, comprising:
introducing water to an electrolysis water electrode and power to an electrolysis module, to produce refuel hydrogen and electrolysis oxygen;
directing the refuel hydrogen through a hydrogen storage system consisting essentially of a hydrogen/water phase separation device and an inverted hydrogen storage device, wherein the refuel hydrogen passes from the electrolysis module, through the hydrogen/water phase separation device, past a shut off valve, and into the inverted hydrogen storage device as dried hydrogen;
hydrating and fueling a fuel cell module by directing the dried hydrogen and inverted storage device water from the inverted hydrogen storage device through the hydrogen/water phase separation device, and to a fuel cell hydrogen electrode;
introducing feed oxygen to a fuel cell oxygen electrode;
and
producing water and electricity.
3 more elements
A method for operating a regenerative electrochemical cell system, comprising:
introducing feed water to an electrolysis water electrode and power to an electrolysis module, to produce refuel hydrogen and electrolysis oxygen;
directing the refuel hydrogen through a hydrogen/water phase separation device and a dryer and into a hydrogen storage device at a pressure, wherein the dryer removes dryer water from the refuel hydrogen to form a dryer hydrogen;
hydrating and fueling a fuel cell module by reducing the pressure of the dryer hydrogen to a reduced pressure, passing the dryer hydrogen through the dryer, and removing dryer water from the dryer to form a hydrated hydrogen;
directing the hydrated hydrogen to a fuel cell hydrogen electrode of the fuel cell module;
introducing feed oxygen to a fuel cell oxygen electrode;
and
producing water and electricity.
4 more elements
A regenerative electrochemical cell system, comprising:
a fuel cell module comprising a fuel cell hydrogen inlet in fluid communication a hydrogen storage system, and a fuel cell oxygen inlet in fluid communication with both an oxygen source and with a gaseous portion of an oxygen/water phase separation device;
an electrolysis module comprising an electrolysis water inlet in fluid communication with a first water storage device via the fuel cell module, and an electrolysis water outlet in fluid communication with a second water storage device;
and a heat exchanger disposed in fluid communication with the fuel cell module and the electrolysis water inlet, such that at least a portion of the water passing from the fuel cell module would pass through the heat exchanger prior to entering the electrolysis water inlet.
A regenerative electrochemical cell system, comprising:
a fuel cell module comprising a fuel cell hydrogen inlet in fluid communication a hydrogen storage system, and a fuel cell oxygen inlet in fluid communication with both an oxygen source and with a gaseous portion of an oxygen/water phase separation device, wherein the fuel cell oxygen inlet is capable of fluid communication with the oxygen source independent of fluid communication with the oxygen/water phase separation device;
and
an electrolysis module comprising an electrolysis water inlet in fluid communication with a first water storage device via the fuel cell module.
A regenerative electrochemical cell system, comprising:
a fuel cell module comprising a fuel cell hydrogen inlet in fluid communication a hydrogen storage system, and a fuel cell oxygen inlet in fluid communication with both a first oxygen source and second oxygen source, wherein the fuel cell oxygen inlet is capable of fluid communication with the first oxygen source independent fluid of communication with the second oxygen source;
and
an electrolysis module comprising an electrolysis water inlet in fluid communication with a first water storage device via the fuel cell module, and an electrolysis water outlet in fluid communication with a second water storage device.
A method for operating a regenerative electrochemical cell system, comprising:
starting up a fuel cell module by heating the fuel cell module;
and introducing feed hydrogen from a hydrogen storage system to a fuel cell hydrogen electrode and introducing feed oxygen from an oxygen/water phase separation device to a fuel cell oxygen electrode when the fuel cell module is not producing electricity, wherein the feed oxygen comprises a feed oxygen concentration greater than a surrounding atmosphere concentration of oxygen;
and reacting hydrogen ions with the feed oxygen to generate electricity and fuel cell water;
and
once the fuel cell has attained operating conditions, ceasing the introduction of the feed oxygen, and introducing second oxygen from the surrounding atmosphere to the fuel cell oxygen electrode.
09/966,727Filed 28 Sep 2001 · us provisional application
Priority
28 Sep 2000
Published
US 2002/0051898 A12 May 2002
Granted
3 May 2005
Term ended
4 Dec 2022Estimated · howhide20 years from earliest known nonprovisional domestic filing plus recorded patent term adjustment, including 432 days of adjustment. Maintenance-fee lapses, terminal disclaimers and statutory extensions have not been checked. The continuity chain may be incomplete; this is not an enforceability determination.
Operating or servicing cells: supplying or removing reactants or electrolytes; Regeneration of electrolytes
Life of this patent
Term ended 4 Dec 2022 (estimated)
Priority28 Sep 2000
Filed28 Sep 2001
Granted3 May 2005
Term ended4 Dec 2022
Priority28 Sep 2000
Granted3 May 2005
Term ended4 Dec 2022
Priority claimedParent application 60/236,278
Application filedUS 09/966,727
Assigned to Proton Energy Systems, Inc.assignment of assignor's interest
PublishedUS 2002/0051898 A1
GrantedUS 6,887,601 B2
Assigned to Perseus Partners Vii, L.P.security agreement
Assigned to Proton Energy Systems, Inc.assignment of assignor's interest
Assigned to Proton Energy Systems, Inc.release of security interest
Term endedEstimated, includes 432 days of adjustment
Description8,428 words
Summary1,564 words
#This disclosure relates generally to electrochemical cell systems, and especially relates to regenerative electrochemical cell systems.
#Electrochemical cells are energy conversion devices, usually classified as either electrolysis cells or fuel cells. A proton exchange membrane electrolysis cell can function as a hydrogen generator by electrolytically decomposing water to produce hydrogen and oxygen gas, and can function as a fuel cell by electrochemically reacting hydrogen with oxygen to generate electricity. Referring to FIG. 1, which is a partial section of a typical anode feed electrolysis cell 100, process water 102 is fed into cell 100 on the side of an oxygen electrode (anode) 116 to form oxygen gas 104, electrons, and hydrogen ions (protons) 106. The reaction is facilitated by the positive terminal of a power source 120 electrically connected to anode 116 and the negative terminal of power source 120 connected to a hydrogen electrode (cathode) 114. The oxygen gas 104, and a portion of the process water 108, exit cell 100, while protons 106 and water 110 migrate across a proton exchange membrane 118 to cathode 114 where hydrogen gas 112 is formed. The hydrogen gas 112 and the migrated water 110 exit cell 100 from the cathode side of the cell 100.
#Another typical water electrolysis cell using the same configuration as is shown in FIG. 1 is a cathode feed cell, wherein process water is fed on the side of the hydrogen electrode. A portion of the water migrates from the cathode across the membrane to the anode where hydrogen ions and oxygen gas are formed due to the reaction facilitated by connection with a power source across the anode and cathode. A portion of the process water exits the cell at the cathode side without passing through the membrane, while some excess water, as well as oxygen gas, exit the cell at the anode side.
Brief description of the drawings3 figures
#Referring now to the drawings, which are meant to be exemplary and not limiting, and wherein like elements are numbered alike:
#FIG. 1 is a schematic diagram illustrating a prior art electrochemical cell;
#FIG. 2 is a schematic diagram representing a regenerative electrochemical cell system; and
Detailed description6,806 words
#A regenerative electrochemical cell system (herein also referred to as “regen-system”) is described, comprising an electrolysis module and a fuel cell module. This regen-system can maintain an uninterrupted power supply to numerous applications, including residential and commercial. Some possible commercial applications include telecommunications industry (e.g., outside plants, cell towers, and the like), computers (e.g., individual computers, a network of computers, and the like) individual businesses, office parks, cable (e.g., telephone, internet, and the like), the power grid, and the like. Some possible residential uses include individual homes, neighborhoods, villages, and the like. This regen-system can also be employed to enable peak-shaving, i.e., during peak usage times, various units can be engaged to supply power to a given area (home, community, commercial entity/group, etc.), such that the grid power can be re-directed to other areas needing additional power. For example, a telecommunication company can sell power from their cell tower back-up regen-system to the power company, thereby supplying the neighborhood located near the cell tower. Since the cell tower back-up regen-system typically remains idle (e.g., the regen-system is idle for greater than 98% of the time the regen-system is at the cell tower site), the power company is assisted with local power, the consumers avoid blackouts/brownouts, and the telecommunication company generates revenue from an otherwise idle system.
#Use of the regen-system in a peak-shaving mode would entail operable communications between the regen-system (e.g., the owners/operators of the regen-system, and/or directly in operable communication with the regen-system) and the power grid, operable communication between the grid operators and the regen-system, and other various centralized or distributed utility control and monitoring systems. The regen-system may also be connected to utility systems responsible for metering and billing functions for the purpose of revenue reconciliation. Peak-shaving may be performed as a method to assist the main power source in time of high demand or, alternately, may be advantageously used more often whenever the cost of peak versus non-peak energy will provide the regen-system owner with a net-positive revenue source. In operation, the operator would engage (turn on), remotely or manually, the regen-system such that electricity would be supplied from the regen-system to a desired area, for a desired period of time or until regeneration the of the regen-system is needed to replenish various reactants (e.g., hydrogen). Note, regeneration during electricity production is also possible.
#During operation of the regen-system, i.e., when power is desired, hydrogen gas (e.g., from a hydrogen storage) and oxygen gas (e.g., from the surrounding atmosphere, from the oxygen/water storage device, or from an oxygen storage, as well as from combinations comprising at least one of the foregoing oxygen sources) are supplied to the fuel cell module. Within the fuel cell, hydrogen ions, formed at the anode, migrate across the electrolyte to the cathode where they react with oxygen to form water. Meanwhile the electrons, released during the hydrogen ion formation, pass through an external load, producing electricity (i.e., power). The water produced at the cathode, can be vented to the atmosphere or passed through a phase separator to recover the water, prior to venting the oxygen, nitrogen, and any other gases, to the atmosphere. The recovered water can be directed to a water storage device. Power generation will continue until the hydrogen source is exhausted or the power is no longer required. Reasons for ending power generation may include, for example, the restoration of the grid power, restoration of renewable energy sources (such as solar, wind, wave power, or the like), or the determination that peak-shaving is no longer cost effective or no longer required.