C07C1/044

Method for preparing light olefin through catalytic syngas with high selectivity by heteroatom-doped zeolite

A composite catalyst containing heteroatom-doped zeolite for preparing light olefin using direct conversion of syngas is formed by compounding component I and component II in a mechanical mixing mode. The active ingredient of component I is a metal oxide, and the component II is a heteroatom-doped zeolite. The zeolite topology is CHA or AEI, and the skeleton atoms include AlPO or SiAlPO; the heteroatoms is at least one of divalent metal Mg, Ca, Cr, Mn, Fe, Co, Ni, Cu, Zn, Sr, Zr, Mo, Cd, Ba and Ce, trivalent metal Ti and Ga, and tetravalent metal Ge. A weight ratio of the active ingredient in the component I to the component II is 0.1-20. The reaction process has high light olefin selectivity; the sum selectivity of the light olefin including ethylene, propylene and butylene can reach 50-90%, while the selectivity of a methane side product is less than 7%.

Multistage Nanoreactor Catalyst and Preparation and Application Thereof
20190092705 · 2019-03-28 ·

The present disclosure discloses a multistage nanoreactor catalyst and preparation and application thereof, belonging to the technical field of synthesis gas conversion. The catalyst consists of a core of an iron-based Fischer-Tropsch catalyst, a transition layer of a porous oxide or porous carbon material, and a shell layer of a molecular sieve having an aromatization function. The molecular sieve of the shell layer can be further modified by a metal element or a non-metal element, and the outer surface of the molecular sieve is further modified by a silicon-oxygen compound to adjust the acidic site on the outer surface and the aperture of the molecular sieve, thereby inhibiting the formation of heavy aromatic hydrocarbons. According to the disclosure, the shell layer molecular sieve with a transition layer and a shell layer containing or not containing auxiliaries, and with or without surface modification can be prepared by the iron-based Fischer-Tropsch catalyst through multiple steps. The catalyst can be used for direct preparation of aromatic compounds, especially light aromatic compounds, from synthesis gas; the selectivity of light aromatic hydrocarbons in hydrocarbons can be 75% or above, and the content in the liquid phase product is not less than 95%; and the catalyst has good stability and good industrial application prospect.

Catalyst and process for selective production of lower hydrocarbons C1—C5 from syngas with low methane and CO2 production

A catalyst composition containing cobalt manganese oxide which is modified with silicon in the form of a hydrophilic silica, the catalyst also containing at least one of lanthanum, phosphorus, Fe, Zr, and Zn, and optionally one or more basic elements selected from the group of alkali metal, alkaline earth metal, and transition metals. Also, methods for preparing and using the catalyst composition for producing aliphatic and aromatic hydrocarbons using the catalyst composition.

METHOD AND APPARATUS FOR PRODUCING A CHEMICAL COMPOUND AND THE PRODUCED CHEMICAL COMPOUND

A method and an apparatus for producing a chemical compound from biomass based raw material. The bio-mass based raw material is gasified in a gasification device for forming a gasification gas, the gasification gas is treated in the reactor which includes at least one catalyst layer including Fe-based catalyst for forming a hydrocarbon composition, at least one hydrocarbon fraction including olefins is recovered from the hydrocarbon composition, and a chemical compound is formed from the hydrocarbon fraction. Further, the invention relates to the produced chemical compound.

METHOD AND APPARATUS FOR PRODUCING A CHEMICAL COMPOUND AND THE PRODUCED CHEMICAL COMPOUND

A method and an apparatus for producing a chemical compound from biomass based raw material. The bio-mass based raw material is gasified in a gasification device for forming a gasification gas, the gasification gas is treated in the reactor which includes at least one catalyst layer including Fe-based catalyst for forming a hydrocarbon composition, at least one hydrocarbon fraction including olefins is recovered from the hydrocarbon composition, and a chemical compound is formed from the hydrocarbon fraction. Further, the invention relates to the produced chemical compound.

METHOD AND APPARATUS FOR PRODUCING A CHEMICAL COMPOUND AND THE PRODUCED CHEMICAL COMPOUND

A method and an apparatus for producing a chemical compound from biomass based raw material. The bio-mass based raw material is gasified in a gasification device for forming a gasification gas, the gasification gas is treated in the reactor which includes at least one catalyst layer including Fe-based catalyst for forming a hydrocarbon composition, at least one hydrocarbon fraction including olefins is recovered from the hydrocarbon composition, and a chemical compound is formed from the hydrocarbon fraction. Further, the invention relates to the produced chemical compound.

METHOD AND APPARATUS FOR PRODUCING A CHEMICAL COMPOUND AND THE PRODUCED CHEMICAL COMPOUND

A method and an apparatus for producing a chemical compound from biomass based raw material. The bio-mass based raw material is gasified in a gasification device for forming a gasification gas, the gasification gas is treated in the reactor which includes at least one catalyst layer including Fe-based catalyst for forming a hydrocarbon composition, at least one hydrocarbon fraction including olefins is recovered from the hydrocarbon composition, and a chemical compound is formed from the hydrocarbon fraction. Further, the invention relates to the produced chemical compound.

Methods for producing combustible gas from the electrolysis of water (HTE) or co-electrolysis with H2O/CO2 in the same chamber, and associated catalytic reactor and system

The invention relates to a novel reactor design, wherein the pressurized chamber contains both a high-temperature electrolysis (HTE) reactor with elementary electrolysis cell stacking for producing either hydrogen or a synthesis gas (syngas for a H.sub.2+CO mixture) from water vapor H.sub.2O and carbon dioxide CO.sub.2, and at least one catalyst arranged at a distance and downstream of the outlet of the electrolyzer for converting the previously produced synthesis gas into the desired combustible gas, by means of heterogeneous catalysis, the synthesis gas having being produced either directly from the electrolysis reactor or indirectly by mixing the hydrogen produced with carbon dioxide CO.sub.2 injected into the chamber.

HEAVY PETROLEUM RESIDUE DERIVED IRON INCORPORATED SP2 CARBON NANOGRANULES FOR IMPROVED SYNTHESIS OF LIGHT OLEFINS

Disclosed are sp.sup.2 carbon nanogranules with iron incorporated from heavy petroleum residue of a refinery. The nanogranules may be used for improved synthesis of light olefins (C.sub.2-C.sub.4) from syngas in a single step Fischer Tropsch synthesis to lower olefins, (FTO). The efficient iron incorporated carbon nanogranules derived from low value heavy petroleum residue are very attractive as a catalytic system for direct synthesis of light olefin (C.sub.2-C.sub.4) from syngas at CO conversion up to 30%.

HEAVY PETROLEUM RESIDUE DERIVED IRON INCORPORATED SP2 CARBON NANOGRANULES FOR IMPROVED SYNTHESIS OF LIGHT OLEFINS

Disclosed are sp.sup.2 carbon nanogranules with iron incorporated from heavy petroleum residue of a refinery. The nanogranules may be used for improved synthesis of light olefins (C.sub.2-C.sub.4) from syngas in a single step Fischer Tropsch synthesis to lower olefins, (FTO). The efficient iron incorporated carbon nanogranules derived from low value heavy petroleum residue are very attractive as a catalytic system for direct synthesis of light olefin (C.sub.2-C.sub.4) from syngas at CO conversion up to 30%.