Patent Application
20210047180
The subject matter described herein relates to generating hydrogen gas and carbon products through chemical reaction, and specifically through hydrocarbon pyrolysis.
Electrical power can be produced via the combustion of hydrocarbons, such as oil and natural gas (including methane). Combustion of hydrocarbons typically generates carbon dioxide and other greenhouse gases that may be harmful to the environment. There are challenges involved with capturing and sequestering the carbon dioxide that is produced to reduce the environmental impact. Hydrogen gas can be utilized as a fuel source for powering vehicles, generating electrical power via fuel cells, engines, power plants, or the like, and powering various other loads in a “hydrogen economy.” One method for generating hydrogen gas is through hydrocarbon pyrolysis. Pyrolysis utilizes heat to break the carbon-hydrogen bonds in methane and/or other hydrocarbons to produce hydrogen gas and a solid carbon material, without producing carbon dioxide. Therefore, a significant benefit of producing hydrogen gas via hydrocarbon pyrolysis for generating electrical power, relative to conventional hydrocarbon combustion, is reduced emissions of carbon dioxide and other greenhouse gases.
One consideration with implementing hydrocarbon pyrolysis for power generation is that the hydrogen gas that is produced via pyrolysis has a lower energy content than the hydrocarbons that are reacted to produce the hydrogen. Another factor with implementing hydrocarbon pyrolysis is that the reaction is endothermic and thus requires heat to break apart the carbon-hydrogen bonds of the hydrocarbon and to prevent the reverse reaction from occurring. The treatment or disposal of the solid carbon byproduct of the reaction may represent a challenge. The carbon is typically amorphous with varying molecular and higher order structures, has relatively low value, and has limited usefulness. One conventional use for the carbon byproduct is for making soot that can be used to fill rubber in tires.
In one or more embodiments, a production system is provided that includes a first reaction chamber and a second reaction chamber. The first reaction chamber is configured to receive a first hydrocarbon stream therein through an input port and to form carbon seeds and hydrogen gas therein via hydrocarbon pyrolysis of the first hydrocarbon stream. The second reaction chamber includes a first input port and a second input port. The second reaction chamber is configured to receive the carbon seeds through the first input port and a second hydrocarbon stream through the second input port, and the second reaction chamber is configured to form carbon product elements and additional hydrogen gas in the second reaction chamber via hydrocarbon pyrolysis of the second hydrocarbon stream. The carbon product elements represent the carbon seeds with additional carbon structure grown on the carbon seeds.
In one or more embodiments, a method is provided that includes forming carbon seeds and hydrogen gas in a first reaction chamber via hydrocarbon pyrolysis of a first hydrocarbon stream. The method also includes directing the carbon seeds from the first reaction chamber to a second reaction chamber and forming carbon product elements and additional hydrogen gas in the second reaction chamber via hydrocarbon pyrolysis of a second hydrocarbon stream. The carbon product elements represent the carbon seeds with additional carbon structure grown on the carbon seeds.
In one or more embodiments, a production system is provided that includes a first reaction chamber, a second reaction chamber, and a power generation system. The first reaction chamber is configured to receive a first hydrocarbon stream therein through an input port and to form carbon seeds and hydrogen gas therein via hydrocarbon pyrolysis of the first hydrocarbon stream. The second reaction chamber has a top and a bottom that is opposite the top. The second reaction chamber includes a first input port and a first output port that are both disposed at or proximate to the top and a second input port disposed at or proximate to the bottom. The second reaction chamber is configured to receive the carbon seeds through the first input port and a second hydrocarbon stream through the second input port. The second reaction chamber is configured to form carbon product elements and additional hydrogen gas in the second reaction chamber via hydrocarbon pyrolysis of the second hydrocarbon stream. The carbon product elements represent the carbon seeds with additional carbon structure grown on the carbon seeds. The power generation system is fluidly connected to the first output port of the second reaction chamber via a duct and is configured to receive the hydrogen gas exiting the second reaction chamber for using the hydrogen gas to generate electrical power.
The present inventive subject matter will be better understood from reading the following description of non-limiting embodiments, with reference to the attached drawings, wherein below:
The embodiments described herein provide a production system and method for utilizing hydrocarbon pyrolysis to accomplish power generation. One or more embodiments in this disclosure describe a two-stage pyrolysis process for producing both hydrogen and a valuable carbon product. The hydrogen can be purified and used in H2-powered vehicles, fed to H2 fuel cells, and can also be used as fuel source in a downstream power generation system to produce electrical and/or mechanical power with significantly reduced carbon dioxide emissions. The valuable carbon product can be sold to offset the cost of energy needed to conduct the pyrolysis reaction, such as costs for providing heat sources and/or catalysts. By producing the valuable carbon product that can offset at least some of the costs associated with performing pyrolysis, the embodiments described herein can be utilized to efficiently and economically generate power without contributing to greenhouse gases. The production system and method described herein may also be able to be implemented in conjunction with other power generation systems, such as renewable sources and conventional combustion of natural gas or fossil fuels.
The carbon products described herein, such as carbon seeds, additional carbon structure, and carbon product elements, represent valuable carbon products. Valuable carbon products have solid carbon morphologies and/or molecular structures that can be utilized in various applications and/or sold to at least partially offset the cost of performing the hydrocarbon pyrolysis. For example, the carbon products may have relatively uniform molecular and/or higher order structures. Some non-limiting valuable carbon products may include graphene, graphite, carbon nanotubes, carbon fibers, semi-crystalline or graphitic carbon, and/or the like. Some non-limiting applications for these carbon products may include use in energy storage (e.g., batteries), solar panels, nuclear reactors, personal electronic devices, refractory applications (such as crucibles), and the like.
The two-stage pyrolysis process includes two different hydrocarbon pyrolysis reactions. For the first step, a first hydrocarbon stream is directed to a first reaction chamber or zone, and pyrolysis of the first hydrocarbon stream within the first reaction chamber produces hydrogen gas and small solid carbon products, or carbon seeds (of a valuable carbon product). For this reason, the first reaction chamber may also be referred to as the seeding chamber. The formation of the carbon seeds may be controlled to yield carbon seeds having desirable microstructures. For example, the carbon seeds may be graphite structures with multiple stacked layers of six-atom rings. The carbon seeds are then directed from the seeding chamber to a second reaction chamber or zone. Optionally, the hydrogen gas and residual, unreacted hydrocarbons may accompany the carbon seeds to the second reaction chamber or may be separated and sent to a power generation system instead of being directed to the second reaction chamber. A second hydrocarbon stream is directed into the second reaction chamber. The second step of the two-stage process involves performing pyrolysis of the second hydrocarbon stream and residual hydrocarbons from the first stream.
The pyrolysis reaction within the second reaction chamber produces additional hydrogen gas and causes additional carbon structures to be grown on the carbon seeds. The carbon seeds may serve as templates for the growth of additional carbon with a particular type of allotropic composition. The additional carbon structures may advantageously retain the same morphology or microstructure of the particular carbon seeds on which the additional carbon is formed. For example, if a given carbon seed has a graphite structure with multiple stacked layers of six-atom rings, then the additional carbon that bonds to that carbon seed continues the pattern and forms additional six-atom rings in the existing layers and/or in new layers stacked on the existing layers. The additional carbon bonds to the carbon seeds to produce enlarged carbon structures surrounding the seeds, and the combined structures are referred to herein as carbon product elements. Therefore, by controlling the first pyrolysis reaction in the seeding chamber to produce carbon seeds with desirable morphology characteristics, such as molecular uniformity, the carbon product elements produced in the growth chamber via the second pyrolysis reaction may have the same or at least similar morphologies as the seeds. Due to the desirable traits, the carbon product elements are sufficiently valuable to be able to collect and utilize (e.g., monetize) the carbon product elements. For example, the carbon product elements may be sold for offsetting the cost of performing the pyrolysis reactions.
The second reaction chamber may produce rapid growth of the carbon structures/products while retaining the original microstructure of the seeds. For this reason, the second reaction chamber may be referred to as a growth chamber. Alternatively, the carbon structures grown on the carbon seeds may not be the same allotropic structure as the seeds, but the combination of the seed and the growth conditions produces high value carbon. In a non-limiting example, graphene powder can be utilized as a seed, and graphite clusters can be grown on the seeds under specific growth chamber conditions. The resulting carbon product element may not have the same morphology or composition as the seed but may still have relatively high economic value. Another non-limiting example may include using nano-carbon or nano-metallic-ring structures as seeds to grow nano-tubes.
The hydrogen gas produced by the two pyrolysis reactions may be purified and collected for distribution or may be directed to a power generation system for using the hydrogen as a fuel source to produce power. The power generation system may be a fuel cell, a combustion engine, a gas turbine, a power plant, or the like.
The controller 112 includes one or more processors that are configured to operate based on programmed instructions. The controller 112 may include additional features or components, such as a data storage device (e.g., memory), an input/output (I/O) device, and/or a wireless communication device. The memory may store programmed instructions (i.e., software) that dictates the functioning of the one or more processors. For example, the memory may store set-up parameters and reaction parameters for operating the production system 100 to generate power and valuable carbon product elements. The controller 112 may implement the programmed instructions and manually-input commands to autonomously operate the production system 100.
An inlet duct 108A receives an incoming hydrocarbon stream 116 from a hydrocarbon source 118. The source 118 may represent a tank, a pipeline, or the like. The incoming hydrocarbon stream 116 includes one or more hydrocarbon compounds, such as methane, propane, ethane, and the like. Optionally, the stream 116 may be natural gas, which primarily includes methane but also includes smaller amounts of additional hydrocarbon compounds. Optionally, the stream 116 may be pure methane. The incoming hydrocarbon stream 116 may be fully or at least substantially in the gas phase.
The incoming hydrocarbon stream 116 is directed within a duct 108A to a splitting location 122. The hydrocarbon stream 116 is divided into a first hydrocarbon stream 124 and a second hydrocarbon stream 126 at the splitting location 122. The controller 112 may actuate one or more valves 110 at or proximate to the splitting location 122 to control how the stream 116 is distributed into the two branching hydrocarbon streams 124, 126. The first hydrocarbon stream 124 (also referred to as first stream 124) is directed to the seeding chamber 102. For example, a duct 108B is connected to the splitting location 122 and extends from the splitting location 122 to an input port 128 of the seeding chamber 102 to convey the first stream 124 directly to the seeding chamber 102. The second hydrocarbon stream 126 (also referred to as second stream 126) is directed to the growth chamber 104. The second stream 126 bypasses the seeding chamber 102. For example, a duct 108C connected to the splitting location 122 extends from the splitting location 122 to an input port 130 of the growth chamber 104 to convey the second stream 126 from the splitting location 122 to the growth chamber 104. In an embodiment, the controller 112 allocates most of the incoming hydrocarbon stream 116 to the second stream 126 that bypasses the seeding chamber 102 and proceeds directly to the growth chamber 104. For example, the valves 110 may be controlled to distribute between 5 and 45 weight percent (wt %) of the incoming hydrocarbon stream 116 to the first stream 124 and the remainder to the second stream 126.
A first pyrolysis reaction is performed on the first stream 124 within the seeding chamber 102 to produce solid carbon seeds 202 (shown in
The products of the pyrolysis reaction (e.g., the carbon seeds 202 and hydrogen gas) as well as any unreacted hydrocarbons are directed from the seeding chamber 102. In the illustrated embodiment, these materials are conveyed within a duct 108D that extends from an output port 132 of the seeding chamber 102 to an input port 131 of the growth chamber 104. In the illustrated embodiment, the output port 132 is disposed at or proximate to a bottom of the seeding chamber 102 (e.g., relative to the direction of gravity). The solid carbon seeds 202 may collect along the bottom of the seeding chamber 102 due to gravity and the density of the seeds 202. Optionally, a solid particle mover 133, such as an auger, a conveyor belt, or the like, is used to transport the carbon seeds 202 from the seeding chamber 102 towards the input port 131. For example, the mover 133 may convey the seeds 202 into and/or through the duct 108D. Optionally, the seeding chamber 102 may function as either a batch reactor or a continuous reactor. For example, as a continuous reactor, the first stream 124 is continuously supplied to the seeding chamber 102 to maintain the pyrolysis reaction. The carbon seeds 202 produced during the reaction are continuously or periodically removed from the bottom of the seeding chamber 102 via the solid particle mover 133 and fed to the input port 131 of the growth chamber 104. Alternatively, as a batch reactor, the carbon seeds 202 may be collectively moved from the bottom of the seeding chamber 102 to the growth chamber 104 after the pyrolysis reaction is completed.
With continued reference to
The seeding chamber 102 and the growth chamber 104 may be heterogeneous catalytic reaction chambers. Optionally, the growth chamber 104 may have a different size and/or may be a different type of reactor than the seeding chamber 102. For example, the growth chamber 104 may be larger than the seeding chamber 102, with a greater volume and/or capacity than the seeding chamber 102. Each of the seeding chamber 102 and the growth chamber 104 may be a respective falling packed bed reaction chamber, a fluidized bed reaction chamber, a fixed bed reaction chamber, a trickle-bed or rainfall-style reaction chamber, or the like. The seeding chamber 102 and/or the growth chamber 104 may include baffles, divider walls, flow channels, propellers, and/or the like therein to increase the molecular interactions between the reactants.
The second hydrocarbon stream 126 within the duct 108C is directed into the growth chamber 104 through the input port 130. In the illustrated embodiment, the input port 130 is separate from the input port 131. The growth chamber 104 is oriented such that the input port 130 is below the input port 131 relative to the direction of gravity. For example, the input port 130 through which the second stream 126 passes may be disposed at or proximate to a bottom 137 of the growth chamber 104, and the input port 131 through which the carbon seeds 202 pass may be at or proximate to a top 139 of the growth chamber 104. Inside the growth chamber 104, the second hydrocarbon stream 126 mixes with the carbon seeds 202, hydrogen gas, and unreacted hydrocarbons from the seed chamber 102 (unless the hydrogen and hydrocarbons have been separated from the carbon seeds 202 at the separator 135 and directed elsewhere). The second stream 126, which is a gas, entering through the port 130 may rise towards the top 139 of the growth chamber 104 as the solid carbon seeds 202 fall towards the bottom 137, providing countercurrent flow of gasses and solid carbon products. In the illustrated embodiment, the growth chamber 104 is a falling packed bed reaction chamber.
A second hydrocarbon pyrolysis reaction is performed within the growth chamber 104. The pyrolysis in the growth chamber 104 uses the second stream 126 and any unreacted hydrocarbons present from the first stream 124 to generate additional hydrogen gas and carbon product elements 302 (shown in
Although the underlying chemical reaction within the growth chamber 104 may be the same as in the seeding chamber 102, the pyrolysis performed within the growth chamber 104 may differ from the pyrolysis performed within the seeding chamber 102. For example, the growth chamber 104 may receive a greater amount or flow rate of hydrocarbons than the seeding chamber 102 due to most of the incoming stream 116 being diverted into the second stream 126. The growth chamber 104 optionally may include different catalysts and/or heat sources than the seeding chamber 102. Furthermore, the process conditions in the growth chamber 104 may differ from the process conditions in the seeding chamber 102. The process conditions may include temperature, pressure, humidity, gas flow rate, solid flow rate, and/or the like. Optionally, the process conditions in the growth chamber 104 may vary substantially from the process conditions in the seeding chamber 102, such that one or more of the process conditions in the growth chamber 104 may differ from the corresponding one or more process conditions in the seeding chamber 102 by more than a designated threshold range. The threshold range may be within 10%, 20%, 30%, or the like of the condition value of the seeding chamber 102. In a non-limiting example, the gas temperature in the seeding chamber 102 may be as high as 3000° C. to 4000° C. (the wall temperature of the seeding chamber 102 may be lower). The gas and/or wall temperature in the growth chamber 104 may be lower than the gas temperature in the seeding chamber 102, such as in the range of 1000° C. to 1500° C. The process conditions may be controlled via the selection of specific catalysts or other components within the chambers, and the controller 112 may also control the conditions by selectively operating devices such as cooling systems, heating devices, pumps, fans, and/or the like. The conditions may be specifically selected for each of the seeding chamber 102 and the growth chamber 104 based on the type of carbon production that is desired in the respective chamber (e.g., seed generation or structural growth).
Gases including hydrogen formed via the pyrolysis reaction and any unreacted hydrocarbons may exit the growth chamber 104 through an output port 141 that is located at or proximate to the top 139 of the growth chamber 104. The gases may be directed within a duct 108E. The hydrogen gas in the duct 108E may represent the combined hydrogen generated by both pyrolysis reactions. Optionally, at least one valve 110 may be located along the duct 108E or at the output port 141 to control the flow of the gases from the growth chamber 104. The solid carbon product elements 302 may exit the growth chamber 104 through an output port 142 that is located at or proximate to the bottom 137 of the chamber 104. For example, the carbon product elements 302 may settle at the bottom 137 due to gravity. Another solid particle mover 133, such as an auger, a conveyor belt, or the like, may be used to transport the carbon product elements 302 from the growth chamber 104. The carbon product elements 302 may be conveyed through a duct 108F extending from the output port 142. The growth chamber 104 may be operated as a continuous reactor that maintains the pyrolysis reaction for an extended period of time to generate streams of products, or as a batch reactor that periodically performs pyrolysis to generate hydrogen gas and carbon product elements 302 in batches.
With reference back to
Upon exiting the growth chamber 104, any gases entrenched with the carbon product elements 302 may be separated from the carbon product elements 302 within a separator device 145. The separator device 145 may be a gas-solid phase separator. The gases from the separator device 145 may be directed to the duct 108E.
The solid carbon product elements 302 may be directed from the separator device 145 to a storage container 144 for collecting the carbon product elements 302. The carbon product elements 302 collected in the storage container 144 may represent valuable carbon products that can be utilized to offset costs of performing the pyrolysis reactions, such as the costs of heating, catalysts, and/or obtaining the incoming hydrocarbon stream 116, and to offset the fact that hydrogen has a lower energy content than the incoming hydrocarbon. For example, the carbon product elements 302 may be sold to manufacturers for utilizing the carbon product elements 302 in various industrial applications, such as energy storage devices, consumer electronics, refractory applications, power generation applications, and/or the like. By selectively controlling the morphology of the carbon product elements 302 throughout the build process, including the uniformity and purity, the carbon product elements 302 may be more valuable than conventional carbon byproducts of pyrolysis reactions.
The production system 100 optionally includes a gas-gas separator device 146 along the duct 108E. The gas-gas separator device 146 may include or represent a ceramic membrane that is utilized to extract pure hydrogen from the hydrogen-methane stream within the duct 108E. For example, the gas stream entering the separator device 146 may have a range of hydrogen purity from 80-95 mol %. The pure hydrogen gas that is extracted by the separator device 146 is routed through a duct 108G and can be utilized to power vehicles, fuel cells, and other uses in a “hydrogen economy.” For example, the pure hydrogen may be stored in a tank for sale and/or later use. The remaining hydrogen, methane, and any other gases within the duct 108E may be directed to a power generation system 150 of the production system 100. The power generation system 150 utilizes the hydrogen and remaining methane as fuel to generate power, such as mechanical power or electrical power. The power generation system 150 may be located at, or represent, a power plant. The power generation system 150 may include a combustion engine, a generator, a turbine, a fuel cell, or the like. A valve 110 disposed along the duct 108E may control the flow of the gases to the power generation system 150. The carbon product elements 302 are not present in the duct 108E and are not directed to the power generation system 150.
The gases at the power generation system 150 may combust or otherwise react to produce power. For example, the hydrogen gas may react with oxygen in an exothermic reaction to produce power with a byproduct of water. In the illustrated embodiment, the power generation system 150 generates electrical power in the form of electric current (e.g., electricity) 151 that can be supplied to a power grid, an electrical storage device (e.g., one or more batteries), or directly to a load that is being powered. In an alternative embodiment, the power generation system 150 may generate mechanical power that is used to provide motive force for propelling a vehicle, such as an automobile.
In one or more embodiments, the production system 100 is configured to convert most (e.g., more than 50 mol %) of the methane and other hydrocarbons in the incoming hydrocarbon stream 116 by the pyrolysis reactions, such that the unreacted hydrocarbons present in the duct 108E may represent less than 50 mol % of the incoming hydrocarbons. For example, the production system 100 may have a conversion rate of at least 80 mol % or at least 90 mol %. As a result, the feed to the power generation system 150 may be mostly hydrogen with a small fraction of methane, such as less than 20 wt % methane or less than 10 wt % methane.
Due to the small percentage of methane in the gases supplied to the power generation system 150, the power generation system 150 may emit substantially less carbon dioxide than conventional power-generating systems that combust hydrocarbon fuels. For example, the production system 100 may reduce carbon dioxide emissions by at least 80% over known systems. In one or more embodiments, the power generation system 150 is an integrated component of the production system 100 such that the hydrogen gas generated from pyrolysis can be directly conveyed to the power generation system 150 without first storing the hydrogen and then transporting the hydrogen to a power generator. Alternatively, the hydrogen gas from the separator device 146 may be stored within a container for future use and/or sale.
The reaction of the hydrogen gas at the power generation system 150 is exothermic and generates heat. Optionally, at least some of the heat exhausted from the power generation system 150 can be used to raise the temperature of the incoming hydrocarbon stream 116 prior to entering the reaction chambers 102, 104. For example, the production system 100 may include a heat exchanger 160 that receives waste heat (e.g., hot air or other gases) exhausted by the power generation system 150 via a duct 108H and the incoming hydrocarbon stream 116. The incoming hydrocarbon stream 116 absorbs at least some of the waste heat within the heat exchanger 160 which increases the temperature of the hydrocarbon stream 116. By pre-heating the hydrocarbon stream 116, the pyrolysis reactions in the reaction chambers 102, 104 may require less external heating than if the hydrocarbon stream 116 is not pre-heated. As a result, the thermal recycling within the heat exchanger 160 may improve the efficiency of the production system 100 (and reduce costs). In addition to, or as an alternative to, the heat exchanger 160, heat may be input into seeding chamber 102 and/or the growth chamber 104 through internal combustion of fuels and/or non-contact methods such as induction or microwave heating of the carbon particles and gases.
In the illustrated embodiment, the seeding chamber 102 is discrete and spaced apart from the growth chamber 104. The duct 108D extends between the two chambers 102, 104 to convey material from the seeding chamber 102 to the growth chamber 104.
At 502, an incoming hydrocarbon stream 116 is divided into a first hydrocarbon stream 124 and a second hydrocarbon stream 126 at a splitting location 122. At 504, the first hydrocarbon stream 124 is directed from the splitting location 122 to a first reaction chamber 102 (e.g., a seeding chamber). At 506, the second hydrocarbon stream 126 is directed from the splitting location 122 to a second reaction chamber 104 (e.g., a growth chamber). The second stream 126 bypasses the first reaction chamber 102.
At 508, carbon seeds 202 and hydrogen gas are formed in the first reaction chamber 102 via pyrolysis of the first hydrocarbon stream 124. At 510, the carbon seeds 202 are directed from the first reaction chamber 102 to the second reaction chamber 104. Optionally, the hydrogen gas that is formed may also be directed to the second reaction chamber 104. At 512, carbon product elements 302 and additional hydrogen gas are formed in the second reaction chamber 104 via hydrocarbon pyrolysis of the second hydrocarbon stream 126. The carbon product elements 302 represent the carbon seeds 202 with additional carbon structure 304 grown on the carbon seeds 202. The additional carbon structure 304 grown on each of the carbon seeds 202 in the second reaction chamber 104 may have the same structural composition as the respective carbon seed 202 on which the additional carbon structure 304 is grown. Optionally, the method 500 may include controlling conditions within at least one of the first reaction chamber 102 or the second reaction chamber 104 such that the first reaction chamber 102 has a different temperature and/or a different pressure than the second reaction chamber 104.
At 514, the hydrogen gas from the second reaction chamber 104 is supplied to a power generation system 150 for using the hydrogen gas as a fuel to generate power, such as electrical power, mechanical power, or the like. At 516, waste or exhaust heat from the power generation system 150 is directed to a heat exchanger 160 disposed in a path of the incoming hydrocarbon stream 116 to transfer the heat to the hydrocarbon stream(s) prior to the first hydrocarbon stream 124 entering the first reaction chamber 102. At 518, the carbon product elements 302 are collected in a storage container 144. The collected carbon product elements 302 may be valuable such that the elements 302 can be utilized to offset operating costs of performing the method 500.
At least one technical effect of the embodiments described herein includes producing carbon products that have greater uniformity, greater purity, and/or greater value via hydrocarbon pyrolysis than known industrial applications of hydrocarbon pyrolysis. For example, by incorporating two different pyrolysis reaction zones, the first zone can be controlled to produce seed carbon with one or more structures that would offer a high value product (e.g., semi crystalline or graphitic carbon materials for energy storage applications and the like) while concurrently producing hydrogen. Then, in the downstream growth zone, the same carbon seeds and/or catalysts can be used as templates to efficiently grow additional high value carbon while producing additional hydrogen. The hydrogen can be utilized as a fuel for generating power with limited carbon emissions. The high value carbon products may be utilized in various industrial applications and/or by selling to offset costs.
In at least one embodiment, a production system is provided that includes a first reaction chamber and a second reaction chamber. The first reaction chamber is configured to receive a first hydrocarbon stream therein through an input port and to form carbon seeds and hydrogen gas therein via hydrocarbon pyrolysis of the first hydrocarbon stream. The second reaction chamber includes a first input port and a second input port. The second reaction chamber is configured to receive the carbon seeds through the first input port and a second hydrocarbon stream through the second input port, and the second reaction chamber is configured to form carbon product elements and additional hydrogen gas in the second reaction chamber via hydrocarbon pyrolysis of the second hydrocarbon stream. The carbon product elements represent the carbon seeds with additional carbon structure grown on the carbon seeds.
Optionally, the first and second reaction chambers are heterogeneous catalytic reaction chambers.
Optionally, process conditions within the second reaction chamber differ from corresponding process conditions within the first reaction chamber by more than a designated threshold range.
Optionally, the first and second input ports are spaced apart along a height of the second reaction chamber such that a top of the second reaction chamber is disposed closer to the first input port than the second input port and a bottom of the second reaction chamber is disposed closer to the second input port than the first input port. Optionally, the second reaction chamber includes a first output port disposed at or proximate to the top of the second reaction chamber, wherein at least a majority of the hydrogen gas is configured to exit the second reaction chamber through the first output port.
Optionally, each of the first reaction chamber and the second reaction chamber is a respective falling packed bed reaction chamber, fluidized bed reaction chamber, a fixed bed reaction chamber, or a trickle-bed reaction chamber.
Optionally, the production system also includes a power generation system fluidly connected to an output port of the second reaction chamber. The power generation system is configured to receive the hydrogen gas exiting the second reaction chamber for using the hydrogen gas to generate electrical power. Optionally, the power generation system includes a fuel cell, a combustion engine, a generator, and/or a turbine. Optionally, the production system also includes a heat exchanger and a duct connecting the power generation system to the heat exchanger. The heat exchanger is disposed in a path of the first and/or second hydrocarbon streams upstream of the first and second reaction chambers. The duct is configured to direct heat from the power generation system to the heat exchanger for preheating the first and/or second hydrocarbon streams.
Optionally, the production system also includes a solid particle mover configured to convey the carbon product elements from an output port of the second reaction chamber towards the first input port of the second reaction chamber to reintroduce the carbon product elements into the second reaction chamber.
Optionally, the production system also includes a solid particle mover configured to convey the carbon product elements from the second reaction chamber towards a storage container. Optionally, the production system also includes a separator device disposed between the second reaction chamber and the storage container. The separator device is configured to separate hydrogen gas that is entrained with the carbon product elements from the carbon product elements.
Optionally, the production system also includes a network of ducts and one or more valves disposed at a splitting location in the network of ducts. A first duct in the network extends from the splitting location to the input port of the first reaction chamber, and a second duct in the network extends from the splitting location to the second input port of the second reaction chamber, bypassing the first reaction chamber. The one or more valves are selectively controlled to divide an incoming hydrocarbon stream into the first hydrocarbon stream and the second hydrocarbon stream at the splitting location, direct the first hydrocarbon stream into the first duct, and direct the second hydrocarbon stream into the second duct. Optionally, the one or more valves are selectively controlled to distribute a majority of the incoming hydrocarbon stream into the second duct to form the second hydrocarbon stream.
Optionally, the additional carbon structure grown on each of the carbon seeds in the second reaction chamber has the same structural composition as the respective carbon seed on which the additional carbon structure is grown.
In at least one embodiment, a method is provided that includes forming carbon seeds and hydrogen gas in a first reaction chamber via hydrocarbon pyrolysis of a first hydrocarbon stream. The method also includes directing the carbon seeds from the first reaction chamber to a second reaction chamber and forming carbon product elements and additional hydrogen gas in the second reaction chamber via hydrocarbon pyrolysis of a second hydrocarbon stream. The carbon product elements represent the carbon seeds with additional carbon structure grown on the carbon seeds.
Optionally, the method also includes collecting the carbon product elements in a storage container.
Optionally, the carbon product elements are directed to the second reaction chamber through a first input port of the second reaction chamber. The method also includes supplying the second hydrocarbon stream to the second reaction chamber through a second input port of the second reaction chamber. The first input port is disposed closer to a top of the second reaction chamber than the second input port (e.g., the distance between the first input port and the top is less than the distance between the second input port and the top).
Optionally, the method also includes supplying the hydrogen gas from the second reaction chamber to a power generation system through a duct. The power generation system is configured for using the hydrogen gas to generate electrical power.
Optionally, the method also includes dividing an incoming hydrocarbon stream into the first hydrocarbon stream and the second hydrocarbon stream at a splitting location, directing the first hydrocarbon stream from the splitting location to the first reaction chamber, and directing the second hydrocarbon stream from the splitting location to the second reaction chamber, bypassing the first reaction chamber.
Optionally, directing the carbon seeds from the first reaction chamber to the second reaction chamber includes controlling a solid particle mover to convey the carbon product elements from a bottom of the first reaction chamber out of the first reaction chamber through an output port towards a first input port of the second reaction chamber.
In at least one embodiment, a production system is provided that includes a first reaction chamber, a second reaction chamber, and a power generation system. The first reaction chamber is configured to receive a first hydrocarbon stream therein through an input port and to form carbon seeds and hydrogen gas therein via hydrocarbon pyrolysis of the first hydrocarbon stream. The second reaction chamber has a top and a bottom that is opposite the top. The second reaction chamber includes a first input port and a first output port that are both disposed at or proximate to the top and a second input port disposed at or proximate to the bottom. The second reaction chamber is configured to receive the carbon seeds through the first input port and a second hydrocarbon stream through the second input port. The second reaction chamber is configured to form carbon product elements and additional hydrogen gas in the second reaction chamber via hydrocarbon pyrolysis of the second hydrocarbon stream. The carbon product elements represent the carbon seeds with additional carbon structure grown on the carbon seeds. The power generation system is fluidly connected to the first output port of the second reaction chamber via a duct and is configured to receive the hydrogen gas exiting the second reaction chamber for using the hydrogen gas to generate electrical power.
As used herein, an element or step recited in the singular and proceeded with the word “a” or “an” should be understood as not excluding plural of said elements or steps, unless such exclusion is explicitly stated. Furthermore, references to “one embodiment” of the presently described subject matter are not intended to be interpreted as excluding the existence of additional embodiments that also incorporate the recited features. Moreover, unless explicitly stated to the contrary, embodiments “comprising” or “having” an element or a plurality of elements having a particular property may include additional such elements not having that property.
The above description is illustrative and not restrictive. For example, the above-described embodiments (and/or aspects thereof) may be used in combination with each other. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the subject matter set forth herein without departing from its scope. While the dimensions and types of materials described herein are intended to define the parameters of the disclosed subject matter, they are by no means limiting and are example embodiments. Many other embodiments will be apparent to those of ordinary skill in the art upon reviewing the above description. The scope of the subject matter described herein should, therefore, be determined with reference to the appended claims, along with the full scope of equivalents to which such claims are entitled. In the appended claims, the terms “including” and “in which” are used as the plain-English equivalents of the respective terms “comprising” and “wherein.” Moreover, in the following claims, the terms “first,” “second,” and “third,” etc. are used merely as labels, and are not intended to impose numerical requirements on their objects. Further, the limitations of the following claims are not written in means-plus-function format and are not intended to be interpreted based on 35 U.S.C. § 112(f), unless and until such claim limitations expressly use the phrase “means for” followed by a statement of function void of further structure.
This written description uses examples to disclose several embodiments of the subject matter set forth herein, including the best mode, and also to enable a person of ordinary skill in the art to practice the embodiments of disclosed subject matter, including making and using the devices or systems and performing the methods. The patentable scope of the subject matter described herein is defined by the claims, and may include other examples that occur to those of ordinary skill in the art. Such other examples are intended to be within the scope of the claims if they have structural elements that do not differ from the literal language of the claims, or if they include equivalent structural elements with insubstantial differences from the literal languages of the claims.
