In a reactor for partial oxidation of feedstock employing a hot oxygen stream that is generated by a suitable burner, the same burner that generates and provides the hot oxygen stream in full-scale partial oxidation operation can be employed in the starting-up of the partial oxidation reactor by suitable control of the characteristics of the feed to the burner, or of the pressures.

A method of decomposing a pre-heated feedstock includes flowing a stream of the pre-heated feedstock and injecting an oxidant into the flowing stream of pre-heated feedstock. The oxidant mixes with the pre-heated feedstock and, in response to the mixing, at least a first portion of the pre-heated feedstock auto-ignites and causes at least a second portion of the pre-heated feedstock to decompose into one or more products by pyrolysis.

A plant and process for producing a hydrogen rich gas are provided, the process including the steps of: reforming a hydrocarbon feed in a reforming step thereby obtaining a synthesis gas including CH.sub.4, CO, CO.sub.2, H.sub.2 and H.sub.2O; shifting the synthesis gas in a shift configuration including a high temperature shift step; removal of CO.sub.2 upstream hydrogen purification unit, such as a pressure swing adsorption unit (PSA), and recycling off-gas from hydrogen purification unit and mix it with natural gas upstream prereformer feed preheater, prereformer, reformer feed preheater or ATR or shift as feed for the process.

Provided is a method for preparing synthesis gas and aromatic hydrocarbons, and more particularly, a method for preparing synthesis gas and aromatic hydrocarbons including: supplying a pyrolysis fuel oil (PFO) stream containing PFO and a pyrolysis gas oil (PGO) stream containing PGO to a distillation tower as a feed stream (S10), the PFO stream and the PGO stream being discharged in a naphtha cracking center (NCC) process; and supplying a lower discharge stream from the distillation tower to a combustion chamber for a gasification process and supplying an upper discharge stream from the distillation tower to a BTX preparation process (S20).

The disclosure relates to systems and methods to produce hydrogen (H.sub.2) gas from hydrogen sulfide (H.sub.2S). H.sub.2S is contacted with a catalyst to form H.sub.2 gas and sulfur adsorbed to the catalyst. The adsorbed sulfur is contacted with oxygen (O.sub.2) gas to convert the adsorbed sulfur to sulfur dioxide (SO.sub.2) and regenerate the catalyst.

A plant and process for producing a hydrogen rich gas are provided, the process including the steps of: reforming a hydrocarbon feed in a reforming step thereby obtaining a synthesis gas including CH4, CO, CO2, H2 and H2O; shifting the synthesis gas in a shift configuration including a high temperature shift step; removal of CO2 upstream hydrogen purification unit, such as a pressure swing adsorption unit (PSA), and recycling off-gas from hydrogen purification unit and mix it with natural gas upstream prereformer feed preheater, prereformer, reformer feed preheater or ATR or shift as feed for the process.

A gas reforming system, which serves as an environmental energy solution, is proposed. More specifically, a gas reforming system utilizing plasma is proposed. A gas reforming system according to an embodiment may include a pre-treatment unit including a desulfurization process module and a first gas separation module, a plasma reforming unit including a discharge tube, an RF generation unit, an antenna structure, and an additional reaction module, and a post-treatment unit including a gas conversion module and a second gas separation module.

The present invention relates to a method and device for producing hydrogen by dissociating the water molecule through thermochemical reactions, using a small amount of active material. The thermochemical reactions are induced by solar energy with a moderate concentration of up to 50 suns, which can be achieved through linear or parabolic concentrators.

A hydrogen generation system with controlled water distribution is disclosed. The system comprises a reaction chamber containing a hydrogen-producing fuel, a liquid distribution mechanism, and a control system. The liquid distribution mechanism includes a rotating arm with liquid injection ports that move vertically through the fuel chamber. This allows for precise and efficient liquid delivery to unreacted fuel, optimizing hydrogen production. A proprietary fuel blend utilizes chemicals that store significant amounts of hydrogen in a solid-state form. A feature of the device is the arm's controlled vertical movement, achieved through a screw mechanism that adjusts the arm's height as it rotates, creating a spiral liquid distribution pattern. The control system regulates liquid injection rates, arm rotation speed, and vertical movement to optimize hydrogen production based on demand. The system can also operate at low pressures and be scaled to different sizes in a safer, more efficient, on-demand manner.

A control method of a fuel cell system according to the present disclosure uses a fuel cell system including a raw material supply system configured to supply a raw material, a water vapor supply system configured to supply water vapor to the raw material supply system, a fuel cell configured to generate electric energy from hydrogen generated from the raw material and an oxidizing agent, and a recycle gas system configured to circulate a recycle gas, which is at least a part of an anode off-gas discharged from an anode of the fuel cell, to the raw material supply system. A flow rate of water vapor flowing through the water vapor supply system is controlled in accordance with a flow rate of carbon dioxide contained in the recycle gas flowing through the recycle gas system.