# US 10,865,709 B2 · Flex-fuel hydrogen reformer for IC engines and gas turbines > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 10,865,709 B2 - Document ID: US10865709B2 - Status: Granted - Kind: B2 - Application number: 15/096,219 - Filed: 2016-04-11 - Published: 2017-10-12 - Granted: 2020-12-15 - Earliest claimed: 2012-05-23 - Applicants: Herng Shinn Hwang - Inventors: Herng Shinn Hwang - Web page: https://patentgrep.com/patent/US10865709B2 ## CPC - B01J 19/2485: {Monolithic reactors} - F02C 3/20: using a special fuel, oxidant, or dilution fluid to generate the combustion products - B01J 8/001: {Controlling catalytic processes (B01J8/1809 takes precedence)} - B01J 8/0278: {Feeding reactive fluids (for solid material B01J8/0015)} - B01J 2208/00548: Flow - B01J 2208/02: with stationary particles - B01J: CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS - F02C: GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS (construction of turbines F01D; jet-propulsion plants F02K; construction of compressors or fans F04; generating combustion products of high pressure or high velocity F23R; using gas turbines in compression refrigeration plants F25B11/00) ## Abstract An on-board Flex-Fuel H2 reforming apparatus provides devices and the methods of operating these devices to produce a combustible reformate containing H2 and CO from hydrocarbons and bio-fuels. For this generator, one or more parallel autothermal reformers are used to convert the fuels into the reformate over Pt group metal catalysts, and the produced reformate is then cooled, compressed and stored in vessels at a pressure between 1 to 100 atmospheres. The reformate from the storage vessels is used either as the sole fuel or is mixed with other fuels as the fuel mixture for a lean burn engine/gas turbine. For this system, the pressure of the storage vessels and the flow control curves are used directly to control the amount of the reformers' reformate flow output. ## Claims ### Claim 1 An on-board Flex-Fuel H2 Reforming device, comprising: (a) one or more parallel autothermal reformers (ATRs) to produce a reformate comprising H2 and CO from a fuel, said fuel comprising a hydrocarbon, a bio-fuel, or combinations thereof; (b) at least one of a supported catalyst or an unsupported catalyst disposed in the ATRs, the at least one supported or unsupported catalyst including one or more of Pt, Pd, Rh, Ir, Os, and Ru; (c) an ATR reformer fuel mixture inlet in fluid communication with the one or more parallel ATRs to provide reactants thereto, said inlet comprising at least one of a liquid fuel loop, a gas fuel loop, a water supply loop, an air supply loop, a water electrolyzer loop, an exhaust gas recycle (EGR) loop, a water recycle loop and a reformate recycle loop, the reactants including i) water and/or steam, ii) an oxidant and iii) said fuel; (d) an automatic control system operably connected with the fuel mixture inlet and the one or more parallel ATRs, said automatic control system configured to maintain a selected O2/C ratio, a selected H2O/C ratio, a selected CO2/C ratio and a maximum ATR reaction temperature below 1200° C., the automatic control system including a flow control curve to regulate the reformate output, wherein a single point on the flow control curve provides a group of pre-calibrated and stored set points for a respective flow controller associated with each reactant, (e) a reformate vessel to store the reformate produced in the one or more parallel ATRs; and (f) a dry reformate storage vessel in fluid communication with the reformate vessel to store a dried form of the reformate, and wherein the flow control curve regulates a total reformate output as a function of the pressure in the dry reformate storage vessel. ### Claim 2 (depends on 1) The device of claim 1, comprising at least one of an internal combustion (IC) engine, a gas turbine and a fuel cell device in communication with said dry reformate storage vessel to receive the dry reformate for combustion the at least one of an (IC) engine, gas turbine, and fuel cell device. ### Claim 3 (depends on 2) The device of claim 2, wherein the gas turbine is configured to drive at least one of an electric generator, an automobile, a lawn mower, a fork lift truck, a diesel truck, a bus, a train and a motorcycle. ### Claim 4 (depends on 2) The device of claim 2, wherein the IC engine is configured to drive at least one of an electric generator, an automobile, a lawn mower, a fork lift truck, a diesel truck, a bus, a train and a motorcycle. ### Claim 5 (depends on 1) The device of claim 1, comprising at least one of a standalone distributed mobile and a stationary power station configured to receive electricity generated by the at least one of an (IC) engine, gas turbine, and fuel cell device. ### Claim 6 (depends on 1) The device of claim 1, wherein the automatic control system includes one or more of i) a flow control curve to regulate the flow rate of each reactant, and ii) a composition control curve to regulate a dry reformate composition of the dry reformate. ### Claim 7 (depends on 1) The device of claim 1, wherein an inlet fuel mixture to a selected ATR is provided at O2/C, H2O/C and CO2/C ratios according to said set points. ### Claim 8 (depends on 1) The on-board Flex-Fuel H2 Reforming device of claim 1, comprising at least one of a lean burn engine or a gas turbine as a driving device for at least one of: an electric generator, an automobile, a lawn mower, a fork lift truck, a diesel truck, a bus, a train or a motorcycle in communication with said dry reformate storage vessel to receive the dry reformate for combustion therein. ### Claim 9 (depends on 1) The on-board Flex-Fuel H2 Reforming device of claim 1, comprising at least one of a lean burn engine or a gas turbine as the driving device for an electric generator configured as an on-board electric charger for an electric vehicle, the lean burn engine or a gas turbine in communication with said dry reformate storage vessel to receive the dry reformate therefrom for combustion therein. ### Claim 10 (depends on 1) The on-board Flex-Fuel H2 Reforming device of claim 1, comprising at least one of an automobile, a lawn mower, a truck, a forklift truck, a bus, a train, a motorcycle, a portable industrial electrical equipment, a portable industrial electrical device, a portable household electrical equipment, a portable household electrical device, an electric utility vehicle, a battery charger or a backup power source in communication with said dry reformate storage vessel to receive the dry reformate therefrom for combustion therein. ### Claim 11 (depends on 1) The on-board Flex-Fuel H2 Reforming device of claim 1, comprising at least one of a mobile electric vehicle and an electric device equipped with: at least one of a solid oxide membrane fuel cell stack and a proton exchange membrane fuel cell stack in communication with said dry reformate storage vessel to receive the dry reformate therefrom for combustion therein. ### Claim 12 (depends on 1) The on-board Flex-Fuel H2 Reforming device of claim 1, wherein the at least one supported or unsupported catalyst includes a high temperature inert carrier with a catalyzed washcoat powder and a total Pt group metal loading of 0.1 to 2000 g/ft3 of a catalyst volume. ### Claim 13 (depends on 1) A method of using an on-board Flex-Fuel H2 Reforming device, comprising: providing the on-board Flex-Fuel H2 Reforming device of claim 1; providing an inlet fuel mixture to the fuel mixture inlet, said inlet fuel mixture comprising said fuel, H2O, and O2; reacting said inlet fuel mixture with at least one of said catalysts inside the one or more parallel ATRs to produce a reformate containing H2 and CO from said fuel, and simultaneously controlling at least one of an O2/C ratio, a H2O/C ratio and a CO2/C ratio of the inlet fuel mixture; maintaining a maximum ATR reaction temperature below 1200° C.; storing a dry reformate produced from the one or more parallel ATRs in the dry reformate storage vessel at a storage pressure between 1 to 100 atmospheres; using the flow control curve to regulate the reformate output; supplying said dry reformate to at least one of an internal combustion engine (IC), a gas turbine or a fuel cell device; and combusting said dry reformate in the at least one of an internal combustion engine (IC), gas turbine or fuel cell device. ### Claim 14 (depends on 13) The method of claim 13, comprising using the flow control curve to regulate at least one of a reactant flow rate, a dry reformate composition of the dry reformate, and a total reformer flow output by the storage pressure in said dry reformate storage vessel. ### Claim 15 (depends on 13) The method of claim 13, comprising: maintaining a first catalytic partial oxidation/steam reforming CPO/SR) reaction zone in the one or more parallel ATRs while maintaining at selected respective values the O2/C ratio, the H2O/C ratio and the CO2/C ratio of the inlet fuel mixture to create a reformate mixture; reacting said inlet fuel mixture over at least one of the supported and unsupported catalysts for less than a 300 millisecond residence time as calculated at standard temperature and pressure (STP) in the first CPO/SR reaction zone; reacting the fuel and the reformate mixture over at least one of the supported and unsupported catalysts for less than 5 seconds in a second steam reforming (SR) reaction zone of the one or more parallel ATRs; producing a reformate stream at a reformate temperature between 150-1200° C. and at a reformate storage pressure between 1 to 100 atmospheres, wherein said reformate stream comprises at least one of a reformate H2, a reformate CO, a reformate CO2, a reformate N2, a reformate O2 and an unconverted portion of the fuel; feeding the produced reformate stream into a water gas shift (WGS) reaction zone of the one or more parallel ATRs for less than 100 seconds; and converting a portion of the water in the inlet fuel mixture and a CO in the inlet fuel mixture into hydrogen by utilizing at least one of the supported or unsupported catalysts and a Cu/Zn oxide catalyst at a temperature between 50-500° C. ### Claim 16 (depends on 13) The method of claim 13, comprising producing a H2 reformate and a CO reformate as a reducing agent and regenerating the supported or unsupported catalyst in the one or more ATRs using the H2 and CO reformate as a reducing agent. ### Claim 17 (depends on 13) The method of claim 13, comprising: maintaining a vessel pressure of the reformate in the dry reformate storage vessel between 30 to 100 atmospheres, thereby permitting said vessel pressure to start up and shut down the on-board Flex-Fuel H2 Reforming device; and adjusting the flow output of the one or more parallel ATRs according to the flow control curve. ### Claim 18 (depends on 14) The method of claim 14, further comprising regulating the reformate pressure of the dry reformate storage vessel to regulate the reactant flow rate according to the flow control curve, and is therefore used to increase or decrease a total amount of a reformate output by the one or more parallel ATRs with a specified dry reformate composition according to said O2/C, H2O/C and CO2/C ratios of said inlet fuel mixture. ### Claim 19 (depends on 16) The method of claim 16, wherein the on-board Flex-Fuel H2 Reforming device includes at least one of an internal combustion (IC) engine, a gas turbine and a fuel cell device in communication with said dry reformate storage vessel to receive the dry reformate for combustion the at least one of an (IC) engine, gas turbine, and fuel cell device and includes an NOx trap and a catalytic converter in gaseous communication with an exhaust of the at least one of an (IC) engine, gas turbine, and fuel cell device, the method including: reducing the supported and/or unsupported catalysts; regenerating a catalyst in the catalytic converter; and removing particulates in the NOx trap using the reformate in the dry reformate storage vessel as a reducing gas. ### Claim 20 (depends on 13) The method of claim 13, comprising supplying at least one of a H2 and a H2 rich reformate to at least one of an IC engine, a gas turbine, a fuel cell device, and a catalytic combustor to supply both heat and power as an on-board Auxiliary Power Unit. ### Claim 21 (depends on 13) The method of claim 13, wherein said fuel is selected from one or more of a C1-C16 hydrocarbon, a methane, a natural gas, a methane hydrate, a LPG, a C1-C8 alcohol, a vegetable oil, a bio-ethanol, a bio-diesel, a bio-methane, an industrial waste, a vent gas containing a volatile organic compound, an agriculture biomass waste bio-fuel, an industrial biomass waste bio-fuel, and an animal biomass waste. ### Claim 22 (depends on 14) The method of claim 14, comprising: controlling the dry reformate storage vessel pressure using the flow control curve; and changing at least one of an amount of H2 production, an amount O2 production, a H2 flow rate and an O2 flow rate. ### Claim 23 (depends on 14) The method of claim 14, wherein the at least one flow control curve provides a total percentage reformate output capacity from the one or more parallel ATRs as a function of said reformate pressure in the dry reformate storage vessel.