The Allam Cycle or Allam-Fetvedt Cycle is a process for converting carbonaceous fuels [1] into thermal energy, while capturing the generated carbon dioxide and water.
The inventors are English engineer Rodney John Allam, American engineer Jeremy Eron Fetvedt, American scientist Dr. Miles R Palmer, and American businessperson and innovator G. William Brown, Jr. [2] [3] [4] [5] [6] [7] [8] [9] The Allam-Fetvedt Cycle was recognized by MIT Technology Review on the 2018 list of 10 Breakthrough Technologies. [10]
This cycle was validated at a 50 MWth natural gas fed test facility in La Porte, Texas in May 2018.
The Allam-Fetvedt Cycle is a recuperated, high-pressure, Brayton cycle employing a transcritical CO2 working fluid with an oxy-fuel combustion regime. This cycle begins by burning a gaseous fuel with oxygen and a hot, high-pressure, recycled supercritical CO2 working fluid in a combustor. The recycled CO2 stream serves the dual purpose of lowering the combustion flame temperature to a manageable level and diluting the combustion products such that the cycle working fluid is predominantly CO2. The pressure in the combustor can be as high as approximately 30 MPa. The combustion feedstock consists of approximately 95% recycled CO2 by mass.
The combustor provides high-pressure exhaust that can be supplied to a turbine expander operating at a pressure ratio between 6 and 12. The expander discharge leaves as a subcritical CO2 mixture predominantly commingled with combustion derived water. This fluid enters an economizer heat exchanger, which cools the expander discharge to below 65 °C against the stream of CO2 that is recycled to the combustor. Upon exiting the economizer heat exchanger, the expander exhaust is further cooled to near ambient temperature by a central cooling system, enabling liquid water to be removed from the working fluid and recycled for beneficial use.
The remaining working fluid of nearly pure CO2 then enters a compression and pumping stage. The compression system consists of a conventional inter-cooled centrifugal compressor with an inlet pressure below the CO2 critical pressure. The CO2 working fluid is compressed and then cooled to near ambient temperature in the compressor after-cooler. At this point, the combination of compressing and cooling the working fluid permits it to achieve a density in excess of 500 kg/m3. In this condition, the CO2 stream can be pumped to the high combustion pressure required using a multi-stage centrifugal pump. Finally, the high-pressure working fluid is sent back through the economizer heat exchanger to be reheated and returned to the combustor.
The net CO2 product derived from the addition of fuel and oxygen in the combustor is removed from the high-pressure stream; at this point, the CO2 product is high-pressure and high purity, ready for sequestration or utilization without requiring further compression. [11] [12] [13] [14]
Stage of the cycle | Oxygen | Natural gas | Water (H2O) | Carbon dioxide (CO2) | |
Combustion Inlet | 4.75% | 1.25% | – | 94% (hot, high pressure) | |
Turbine Inlet | – | – | 2.75% (very hot steam) | 97.25% (very hot) | |
Heat Exchanger Inlet (Exhaust) | – | – | 2.75% (hot steam) | 97.25% (hot, low pressure) | |
Heat Exchanger Outlet (Exhaust) | – | – | 2.75% (steam condensed) | 97.25% (to compressor-pump) | |
Compressor-Pump Outlet | – | – | 94% (to heat exchanger) | 3.25% (CCS/CCUS) | |
Heat Exchanger Inlet (Recycle) | – | – | 94% (compressed) | ||
Heat Exchanger Outlet (Recycle) | – | – | 94% (hot, compressed, to be recycled) |
In order for the system to achieve high thermal efficiency, a close temperature approach is needed on the high-temperature side of the primary heat exchanger. Due to the cooling process employed at the compression and pumping stage, a large energy imbalance would typically exist in the cycle between the cooling expander exhaust flow and the reheating CO2 recycle flow.
The Allam-Fetvedt Cycle corrects this imbalance through the incorporation of low-grade heat at the low-temperature end of the recuperative heat exchanger. Due to the low temperatures at the cool end of the cycle, this low-grade heat only needs to be in the range of 100 °C to 400 °C. A convenient source of this heat is the Air Separation Unit (ASU) required for the oxy-fuel combustion regime.
When burning natural gas as a fuel, this basic configuration has been modeled to achieve an efficiency up to 60% (LHV) as a power cycle net of all parasitic loads, including the energy-intensive ASU. Despite its novelty, the components required by this cycle are commercially available, with the exception of the combustion turbine package. The turbine relies on proven technologies and approaches used by existing gas and steam turbine design tools. [15] [16]
Construction began in March 2016 in La Porte, Texas on a 50 MWth industrial test facility to showcase the Allam-Fetvedt Cycle, finishing in 2017. In 2018, the Allam-Fetvedt Cycle and supporting technologies were validated, [17] allowing OEMs to certify components for use with future production plants.
On November 15, 2021, at approximately 7:40 pm EST the test facility successfully synchronized to the ERCOT grid [18] proving that the Allam Fetvedt Cycle was capable of generating power at 60 Hz.
This test facility is owned and operated by NET Power, which is owned by Constellation Energy Corporation, Occidental Petroleum (Oxy) Low Carbon Ventures, Baker Hughes and 8 Rivers Capital (the inventor of the technology).
NET Power was awarded the 2018 International Excellence in Energy Breakthrough Technological Project of the Year at the Abu Dhabi International Petroleum Exhibition and Conference (ADIPEC). [19]
Publication Number | Title | Application Date | Publication Date | Current Assignee | Legal Status & Events | Inventor Name |
---|---|---|---|---|---|---|
US20100300063A1 | Apparatus and Method for Combusting a Fuel at High Pressure and High Temperature, and Associated System and Device | 2010-02-26 | 2010-12-02 | 8 RIVERS CAPITAL, LLC | Granted Pledge Transfer | PALMER, MILES R.; ALLAM, RODNEY JOHN; BROWN, JR., GLENN WILLIAM |
US9416728B2 | Apparatus and method for combusting a fuel at high pressure and high temperature, and associated system and device | 2010-02-26 | 2016-08-16 | 8 RIVERS CAPITAL, LLC | Granted Pledge Transfer | PALMER, MILES R.; ALLAM, RODNEY JOHN; BROWN, JR., GLENN WILLIAM |
US20110179799A1 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2010-08-31 | 2011-07-28 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | ALLAM, RODNEY JOHN; PALMER, MILES; BROWN, JR., GLENN WILLIAM |
US8596075B2 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2010-08-31 | 2013-12-03 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | ALLAM, RODNEY JOHN; PALMER, MILES; BROWN, JR., GLENN WILLIAM |
US20120067056A1 | System and method for high efficiency power generation using a nitrogen gas working fluid | 2011-09-19 | 2012-03-22 | 8 RIVERS CAPITAL, LLC | Granted Pledge | PALMER, MILES; ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON |
US20120067568A1 | Method of using carbon dioxide in recovery of formation deposits | 2011-09-19 | 2012-03-22 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | PALMER, MILES; ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON; FREED, DAVID ARTHUR; BROWN, JR., GLENN WILLIAM |
US8869889B2 | Method of using carbon dioxide in recovery of formation deposits | 2011-09-19 | 2014-10-28 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | PALMER, MILES; ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON; FREED, DAVID ARTHUR; BROWN, JR., GLENN WILLIAM |
US9410481B2 | System and method for high efficiency power generation using a nitrogen gas working fluid | 2011-09-19 | 2016-08-09 | 8 RIVERS CAPITAL, LLC | Granted Pledge | PALMER, MILES; ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON |
US20130205746A1 | Partial oxidation reaction with closed cycle quench | 2013-02-11 | 2013-08-15 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON; PALMER, MILES R. |
US8776532B2 | Partial oxidation reaction with closed cycle quench | 2013-02-11 | 2014-07-15 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON; PALMER, MILES R. |
US20130199195A1 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2013-03-14 | 2013-08-08 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | ALLAM, RODNEY JOHN; PALMER, MILES R.; BROWN, JR., GLENN WILLIAM |
US9062608B2 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2013-03-14 | 2015-06-23 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | ALLAM, RODNEY JOHN; PALMER, MILES R.; BROWN, JR., GLENN WILLIAM |
US10018115B2 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2013-03-15 | 2018-07-10 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | ALLAM, RODNEY JOHN; PALMER, MILES R.; BROWN, JR., GLENN WILLIAM; FETVEDT, JEREMY ERON; FORREST, BROCK ALAN |
US20130213049A1 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2013-03-15 | 2013-08-22 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | ALLAM, RODNEY JOHN; PALMER, MILES R.; BROWN, JR., GLENN WILLIAM; FETVEDT, JEREMY ERON; FORREST, BROCK ALAN |
US20140053529A1 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2013-11-04 | 2014-02-27 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | ALLAM, RODNEY JOHN; BROWN, JR., GLENN WILLIAM; PALMER, MILES R. |
US8959887B2 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2013-11-04 | 2015-02-24 | PALMER LABS, LLC; 8 RIVERS CAPITAL, LLC | Granted Pledge | ALLAM, RODNEY JOHN; BROWN, JR., GLENN WILLIAM; PALMER, MILES R. |
US20140290263A1 | Partial oxidation reaction with closed cycle quench | 2014-06-12 | 2014-10-02 | 8 RIVERS CAPITAL, LLC; PALMER LABS, LLC | Granted | ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON; PALMER, MILES R. |
US9581082B2 | Partial oxidation reaction with closed cycle quench | 2014-06-12 | 2017-02-28 | 8 RIVERS CAPITAL, LLC; PALMER LABS, LLC | Granted | ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON; PALMER, MILES R. |
US10927679B2 | High efficiency power production methods, assemblies, and systems | 2014-07-25 | 2021-02-23 | 8 RIVERS CAPITAL, LLC | Granted | PALMER, MILES R.; FETVEDT, JEREMY ERON; ALLAM, RODNEY JOHN |
US20140331687A1 | High Efficiency Power Production Methods, Assemblies, and Systems | 2014-07-25 | 2014-11-13 | 8 RIVERS CAPITAL, LLC | Granted | PALMER, MILES R.; FETVEDT, JEREMY ERON; ALLAM, RODNEY JOHN |
US10047671B2 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2015-01-23 | 2018-08-14 | 8 RIVERS CAPITAL, LLC | Granted | ALLAM, RODNEY JOHN; BROWN, JR., GLENN WILLIAM; PALMER, MILES R. |
US20160215693A1 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2015-01-23 | 2016-07-28 | 8 RIVERS CAPITAL, LLC | Granted | ALLAM, RODNEY JOHN; BROWN, JR., GLENN WILLIAM; PALMER, MILES R. |
US20150252724A1 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2015-05-20 | 2015-09-10 | 8 RIVERS CAPITAL, LLC | Granted | ALLAM, RODNEY JOHN; PALMER, MILES R.; BROWN, JR., GLENN WILLIAM |
US9869245B2 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2015-05-20 | 2018-01-16 | 8 RIVERS CAPITAL, LLC | Granted | ALLAM, RODNEY JOHN; PALMER, MILES R.; BROWN, JR., GLENN WILLIAM |
US20160319741A1 | System and method for high efficiency power generation using a nitrogen gas working fluid | 2016-07-14 | 2016-11-03 | 8 RIVERS CAPITAL, LLC | Granted | PALMER, MILES; ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON |
US9611785B2 | System and method for high efficiency power generation using a nitrogen gas working fluid | 2016-07-14 | 2017-04-04 | 8 RIVERS CAPITAL, LLC | Granted | PALMER, MILES; ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON |
US10054046B2 | System and method for high efficiency power generation using a nitrogen gas working fluid | 2017-03-10 | 2018-08-21 | 8 RIVERS CAPITAL, LLC | Granted | PALMER, MILES; ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON |
US20180016979A1 | System and method for high efficiency power generation using a nitrogen gas working fluid | 2017-03-10 | 2018-01-18 | 8 RIVERS CAPITAL, LLC | Granted | PALMER, MILES; ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON |
US10989113B2 | System and method for power production using partial oxidation | 2017-09-13 | 2021-04-27 | 8 RIVERS CAPITAL, LLC | Granted | FORREST, BROCK ALAN; LU, XIJIA; ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON; PALMER, MILES R. |
US20180073430A1 | System and method for power production using partial oxidation | 2017-09-13 | 2018-03-15 | 8 RIVERS CAPITAL, LLC | Granted | FORREST, BROCK ALAN; LU, XIJIA; ALLAM, RODNEY JOHN; FETVEDT, JEREMY ERON; PALMER, MILES R. |
US10975766B2 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2018-06-13 | 2021-04-13 | 8 RIVERS CAPITAL, LLC | Granted | ALLAM, RODNEY JOHN; PALMER, MILES R.; BROWN, JR., GLENN WILLIAM; FETVEDT, JEREMY ERON; FORREST, BROCK ALAN |
US20180291805A1 | System and method for high efficiency power generation using a carbon dioxide circulating working fluid | 2018-06-13 | 2018-10-11 | 8 RIVERS CAPITAL, LLC | Granted | ALLAM, RODNEY JOHN; PALMER, MILES R.; BROWN, JR., GLENN WILLIAM; FETVEDT, JEREMY ERON; FORREST, BROCK ALAN |
A heat engine is a system that converts heat to usable energy, particularly mechanical energy, which can then be used to do mechanical work. While originally conceived in the context of mechanical energy, the concept of the heat engine has been applied to various other kinds of energy, particularly electrical, since at least the late 19th century. The heat engine does this by bringing a working substance from a higher state temperature to a lower state temperature. A heat source generates thermal energy that brings the working substance to the higher temperature state. The working substance generates work in the working body of the engine while transferring heat to the colder sink until it reaches a lower temperature state. During this process some of the thermal energy is converted into work by exploiting the properties of the working substance. The working substance can be any system with a non-zero heat capacity, but it usually is a gas or liquid. During this process, some heat is normally lost to the surroundings and is not converted to work. Also, some energy is unusable because of friction and drag.
Gasification is a process that converts biomass- or fossil fuel-based carbonaceous materials into gases, including as the largest fractions: nitrogen (N2), carbon monoxide (CO), hydrogen (H2), and carbon dioxide (CO2). This is achieved by reacting the feedstock material at high temperatures (typically >700 °C), without combustion, via controlling the amount of oxygen and/or steam present in the reaction. The resulting gas mixture is called syngas (from synthesis gas) or producer gas and is itself a fuel due to the flammability of the H2 and CO of which the gas is largely composed. Power can be derived from the subsequent combustion of the resultant gas, and is considered to be a source of renewable energy if the gasified compounds were obtained from biomass feedstock.
Fluidized bed combustion (FBC) is a combustion technology used to burn solid fuels.
The Brayton cycle, also known as the Joule cycle, is a thermodynamic cycle that describes the operation of certain heat engines that have air or some other gas as their working fluid. It is characterized by isentropic compression and expansion, and isobaric heat addition and rejection, though practical engines have adiabatic rather than isentropic steps.
A combined cycle power plant is an assembly of heat engines that work in tandem from the same source of heat, converting it into mechanical energy. On land, when used to make electricity the most common type is called a combined cycle gas turbine (CCGT) plant, which is a kind of gas-fired power plant. The same principle is also used for marine propulsion, where it is called a combined gas and steam (COGAS) plant. Combining two or more thermodynamic cycles improves overall efficiency, which reduces fuel costs.
The Rankine cycle is an idealized thermodynamic cycle describing the process by which certain heat engines, such as steam turbines or reciprocating steam engines, allow mechanical work to be extracted from a fluid as it moves between a heat source and heat sink. The Rankine cycle is named after William John Macquorn Rankine, a Scottish polymath professor at Glasgow University.
A supercritical fluid (SCF) is any substance at a temperature and pressure above its critical point, where distinct liquid and gas phases do not exist, but below the pressure required to compress it into a solid. It can effuse through porous solids like a gas, overcoming the mass transfer limitations that slow liquid transport through such materials. SCFs are superior to gases in their ability to dissolve materials like liquids or solids. Also, near the critical point, small changes in pressure or temperature result in large changes in density, allowing many properties of a supercritical fluid to be "fine-tuned".
A combustor is a component or area of a gas turbine, ramjet, or scramjet engine where combustion takes place. It is also known as a burner, burner can, combustion chamber or flame holder. In a gas turbine engine, the combustor or combustion chamber is fed high-pressure air by the compression system. The combustor then heats this air at constant pressure as the fuel/air mix burns. As it burns the fuel/air mix heats and rapidly expands. The burned mix is exhausted from the combustor through the nozzle guide vanes to the turbine. In the case of a ramjet or scramjet engines, the exhaust is directly fed out through the nozzle.
Supercritical carbon dioxide is a fluid state of carbon dioxide where it is held at or above its critical temperature and critical pressure.
The steam-electric power station is a power station in which the electric generator is steam driven. Water is heated, turns into steam and spins a steam turbine which drives an electrical generator. After it passes through the turbine, the steam is condensed in a condenser. The greatest variation in the design of steam-electric power plants is due to the different fuel sources.
An integrated gasification combined cycle (IGCC) is a technology using a high pressure gasifier to turn coal and other carbon based fuels into pressurized gas—synthesis gas (syngas). It can then remove impurities from the syngas prior to the electricity generation cycle. Some of these pollutants, such as sulfur, can be turned into re-usable byproducts through the Claus process. This results in lower emissions of sulfur dioxide, particulates, mercury, and in some cases carbon dioxide. With additional process equipment, a water-gas shift reaction can increase gasification efficiency and reduce carbon monoxide emissions by converting it to carbon dioxide. The resulting carbon dioxide from the shift reaction can be separated, compressed, and stored through sequestration. Excess heat from the primary combustion and syngas fired generation is then passed to a steam cycle, similar to a combined cycle gas turbine. This process results in improved thermodynamic efficiency, compared to conventional pulverized coal combustion.
Supercritical fluid chromatography (SFC) is a form of normal phase chromatography that uses a supercritical fluid such as carbon dioxide as the mobile phase. It is used for the analysis and purification of low to moderate molecular weight, thermally labile molecules and can also be used for the separation of chiral compounds. Principles are similar to those of high performance liquid chromatography (HPLC); however, SFC typically utilizes carbon dioxide as the mobile phase. Therefore, the entire chromatographic flow path must be pressurized. Because the supercritical phase represents a state whereby bulk liquid and gas properties converge, supercritical fluid chromatography is sometimes called convergence chromatography. The idea of liquid and gas properties convergence was first envisioned by Giddings.
Oxy-fuel combustion is the process of burning a fuel using pure oxygen, or a mixture of oxygen and recirculated flue gas, instead of air. Since the nitrogen component of air is not heated, fuel consumption is reduced, and higher flame temperatures are possible. Historically, the primary use of oxy-fuel combustion has been in welding and cutting of metals, especially steel, since oxy-fuel allows for higher flame temperatures than can be achieved with an air-fuel flame. It has also received a lot of attention in recent decades as a potential carbon capture and storage technology.
A transcritical cycle is a closed thermodynamic cycle where the working fluid goes through both subcritical and supercritical states. In particular, for power cycles the working fluid is kept in the liquid region during the compression phase and in vapour and/or supercritical conditions during the expansion phase. The ultrasupercritical steam Rankine cycle represents a widespread transcritical cycle in the electricity generation field from fossil fuels, where water is used as working fluid. Other typical applications of transcritical cycles to the purpose of power generation are represented by organic Rankine cycles, which are especially suitable to exploit low temperature heat sources, such as geothermal energy, heat recovery applications or waste to energy plants. With respect to subcritical cycles, the transcritical cycle exploits by definition higher pressure ratios, a feature that ultimately yields higher efficiencies for the majority of the working fluids. Considering then also supercritical cycles as a valid alternative to the transcritical ones, the latter cycles are capable of achieving higher specific works due to the limited relative importance of the work of compression work. This evidences the extreme potential of transcritical cycles to the purpose of producing the most power with the least expenditure.
A closed-cycle gas turbine is a turbine that uses a gas for the working fluid as part of a closed thermodynamic system. Heat is supplied from an external source. Such recirculating turbines follow the Brayton cycle.
The circulating fluidized bed (CFB) is a type of fluidized bed combustion that utilizes a recirculating loop for even greater efficiency of combustion. while achieving lower emission of pollutants. Reports suggest that up to 95% of pollutants can be absorbed before being emitted into the atmosphere. The technology is limited in scale however, due to its extensive use of limestone, and the fact that it produces waste byproducts.
An internal combustion engine is a heat engine in which the combustion of a fuel occurs with an oxidizer in a combustion chamber that is an integral part of the working fluid flow circuit. In an internal combustion engine, the expansion of the high-temperature and high-pressure gases produced by combustion applies direct force to some component of the engine. The force is typically applied to pistons, turbine blades, a rotor, or a nozzle. This force moves the component over a distance. This process transforms chemical energy into kinetic energy which is used to propel, move or power whatever the engine is attached to.
Lower-temperature fuel cell types such as the proton exchange membrane fuel cell, phosphoric acid fuel cell, and alkaline fuel cell require pure hydrogen as fuel, typically produced from external reforming of natural gas. However, fuels cells operating at high temperature such as the solid oxide fuel cell (SOFC) are not poisoned by carbon monoxide and carbon dioxide, and in fact can accept hydrogen, carbon monoxide, carbon dioxide, steam, and methane mixtures as fuel directly, because of their internal shift and reforming capabilities. This opens up the possibility of efficient fuel cell-based power cycles consuming solid fuels such as coal and biomass, the gasification of which results in syngas containing mostly hydrogen, carbon monoxide and methane which can be cleaned and fed directly to the SOFCs without the added cost and complexity of methane reforming, water gas shifting and hydrogen separation operations which would otherwise be needed to isolate pure hydrogen as fuel. A power cycle based on gasification of solid fuel and SOFCs is called an Integrated Gasification Fuel Cell (IGFC) cycle; the IGFC power plant is analogous to an integrated gasification combined cycle power plant, but with the gas turbine power generation unit replaced with a fuel cell power generation unit. By taking advantage of intrinsically high energy efficiency of SOFCs and process integration, exceptionally high power plant efficiencies are possible. Furthermore, SOFCs in the IGFC cycle can be operated so as to isolate a carbon dioxide-rich anodic exhaust stream, allowing efficient carbon capture to address greenhouse gas emissions concerns of coal-based power generation.
The Whitetail Clean Energy is a proposed power station in Wilton, Redcar and Cleveland, England. The generating process of the plant is listed as a "clean energy source", using natural gas and oxygen in a Allam-Fetvedt Cycle to create power. The excess carbon dioxide not used by the co-generation process is intended to be captured and stored under the North Sea, making the plant the first in the United Kingdom to utilise this type of technology, and also using carbon sequestration under the North Sea. The plant is also included in the Net Zero Teesside project. The power plant is proposed to start generating in 2025.
Supercritical carbon dioxide blend (sCO2 blend) is an homogeneous mixture of CO2 with one or more fluids (dopant fluid) where it is held at or above its critical temperature and critical pressure.