The invention relates to petroleum sludge or other wastes recycle treatment system, which comprises a pre-treatment operation facility for a treated matter to be treated as a raw material. A feeding unit is arranged to feed the raw material into at least one gasification reactor with a push rod or a screw for pyrolysis gasification. The upper half of the at least one gasification reactor is provided with a syngas collecting pipe which can be connected with a gas collecting pump, and the lower half is provided with a liquid petroleum output pipe and an ash residue outlet, in which the ash residue outlet can be provided with a spiral pipe to draw the ash residue out. The petroleum sludge and other wastes in a dense fluid state are transported from a raw material tank to the at least one gasification reactor end which is bent upward through at least one pipe body, and the feeding mode of pyrolysis gasification of the raw material from below to upper of the gasification reactor is adopted. The top of the at least one gasification reactor is provided with a syngas collecting pipe, and the other side is provided with an ash residue accumulation chamber. The ash residue can be centralized and discharged through the lower buffer chamber and the slag discharge chamber, so as to convert the petroleum sludge or other wastes into more energy-efficient syngas providing human beings as users of electric or thermal energy.

An apparatus is disclosed for the pre-capture of carbon from natural gas and/or other light gaseous hydrocarbons and oils, and for co-firing the resulting hydrogen and any remaining hydrocarbons with higher carbon ratio fuels, such as coal and heavy oils and even lower carbon ratio natural gas, in a steam electric generator and/or other boilers, processes, reactors, power plants, engines and combustion turbines, and combined cycle units, to reduce their carbon dioxide production and emissions to the environment, and for co-processing the syngas with other feed materials to react them in a separate vessel and produce a desired outcome.

An apparatus is disclosed for the pre-capture of carbon from natural gas and/or other light gaseous hydrocarbons and oils, and for co-firing the resulting hydrogen and any remaining hydrocarbons with higher carbon ratio fuels, such as coal and heavy oils and even lower carbon ratio natural gas, in a steam electric generator and/or other boilers, processes, reactors, power plants, engines and combustion turbines, and combined cycle units, to reduce their carbon dioxide production and emissions to the environment, and for co-processing the syngas with other feed materials to react them in a separate vessel and produce a desired outcome.

The present invention provides for a pressure swing adsorption (PSA) process for the substantial removal of H.sub.2O and CO.sub.2 from a synthesis gas to obtain a multicomponent product gas substantially free of H.sub.2O and CO.sub.2 with high recovery of the product gas. Further, the present invention provides an integrated process that achieves sufficiently high H.sub.2 and CO recoveries such that compression and recycling of the syngas purification PSA tailgas is not necessary to be economically advantageous compared to the conventional processes.

The present invention provides for a pressure swing adsorption (PSA) process for the substantial removal of H.sub.2O and CO.sub.2 from a synthesis gas to obtain a multicomponent product gas substantially free of H.sub.2O and CO.sub.2 with high recovery of the product gas. Further, the present invention provides an integrated process that achieves sufficiently high H.sub.2 and CO recoveries such that compression and recycling of the syngas purification PSA tailgas is not necessary to be economically advantageous compared to the conventional processes.

The present invention relates to a process for the production of high value chemicals, preferably including at least ethylene and propylene, by steam cracking a mixture of non-cyclic paraffin stream (A) comprising at least 90% of components having at least 12 carbon atoms, with either a mixture of hydrocarbons having from 3 to 4 carbon atoms or a mixture of hydrocarbons comprising at least 90% of components having a boiling point ranging from 15° C. to 200° C.

The present invention relates to a process for the production of high value chemicals, preferably including at least ethylene and propylene, by steam cracking a mixture of non-cyclic paraffin stream (A) comprising at least 90% of components having at least 12 carbon atoms, with either a mixture of hydrocarbons having from 3 to 4 carbon atoms or a mixture of hydrocarbons comprising at least 90% of components having a boiling point ranging from 15° C. to 200° C.

Embodiments include a method for converting renewable energy source electricity and a hydrocarbon feedstock into a liquid fuel by providing a source of renewable electrical energy in communication with a synthesis gas generation unit and an air separation unit. Oxygen from the air separation unit and a hydrocarbon feedstock is provided to the synthesis gas generation unit, thereby causing partial oxidation reactions in the synthesis gas generation unit in a process that converts the hydrocarbon feedstock into synthesis gas. The synthesis gas is then converted into a liquid fuel.

Embodiments include a method for converting renewable energy source electricity and a hydrocarbon feedstock into a liquid fuel by providing a source of renewable electrical energy in communication with a synthesis gas generation unit and an air separation unit. Oxygen from the air separation unit and a hydrocarbon feedstock is provided to the synthesis gas generation unit, thereby causing partial oxidation reactions in the synthesis gas generation unit in a process that converts the hydrocarbon feedstock into synthesis gas. The synthesis gas is then converted into a liquid fuel.

Process and plant for producing hydrocarbon products from a feedstock originating from a renewable source, where a hydrogen-rich stream and on off-gas stream comprising hydrocarbons is formed. A portion of the hydrogen-rich stream is used as a recycle gas stream in a hydroprocessing stage for the production of said hydrocarbon products, and another portion may be used for hydrogen production, while the off-gas stream is treated to remove its H.sub.2S content and used as a recycle gas stream in the hydrogen producing unit, from which the hydrogen produced i.e. make-up hydrogen, is used in the hydroprocessing stage. The invention enables minimizing natural gas consumption in the hydrogen producing unit as well as steam reformer size.