B01J29/60

Novel method to produce acrylic acid with acetaldehyde as the main by-product

Described herein are solid acid catalysts and the methods for catalytically preparing ,-unsaturated carboxylic acids and/or esters thereof. In one aspect, a zeolite catalyst may be used. The catalyst may, in certain embodiments, be modified to improve the selectivity and/or conversion of a reaction. For instance, a catalyst may be modified by ion exchange to achieve a desirable acidity profile in order to achieve high level of conversion of reactants and selectivity for desirable products of the catalytic reaction. In another aspect, a variety of feed stocks (e.g., starting compositions) may be used including an -hydroxycarboxylic acid, an -hydroxycarboxylic acid ester, a -hydroxycarboxylic acid, a -hydroxycarboxylic acid ester, cyclic esters thereof (e.g., lactide), and combinations thereof.

Catalytic cracking catalyst for high-efficiency conversion of heavy oil and preparation method thereof

The present invention provides a catalytic cracking catalyst for heavy oil and preparation methods thereof. The catalyst comprises 2 to 50% by weight of a phosphorus-containing ultrastable rare earth Y-type molecular sieve, 0.5 to 30% by weight of one or more other molecular sieves, 0.5 to 70% by weight of clay, 1.0 to 65% by weight of high-temperature-resistant inorganic oxides, and 0.01 to 12.5% by weight of a rare earth oxide. The phosphorus-containing ultra-stable rare earth Y-type molecular sieve uses a NaY molecular sieve as a raw material. The raw material is subjected to a rare-earth exchange and a dispersing pre-exchange; the molecular sieve slurry is then filtered, washed with water and subjected to a first calcination to obtain a rare earth sodium Y molecular sieve which has been subjected to such first-exchange first-calcination, wherein the steps of rare earth exchange and dispersing pre-exchange are not restricted in sequence; and then the rare earth sodium Y molecular sieve which has been subjected to one-exchange one-calcination is subjected to second exchange and second calcination including ammonium exchange and a phosphorus modification, wherein the steps of the ammonium exchange and the phosphorus modification are not restricted in sequence. The steps of the ammonium exchange and the phosphorus modification can be conducted continuously or non-continuously, the second calcination is conducted after the ammonium exchange for reducing sodium, the phosphorus modification can be conducted before or after the second calcination. The catalyst provided by the invention has the characteristics of high heavy oil conversion capacity, high total liquid yield, and high yield of light oil.

PROCESS FOR REMOVING OXYGENATES FROM NAPHTHA

A process is presented for the removal of contaminants like oxygenates from hydrocarbons. The contaminant oxygenates are removed from hydrocarbons that may be feed to cracking units. A crude feed stream is fed to a water wash column along with water to remove oxygenates and is subsequently treated with an adsorbent to effectively remove all the oxygenates from the crude hydrocarbon. A regenerant medium from a naphtha hydrotreating unit is used to regenerate the adsorbent.

Process for Obtaining a Catalyst Composite
20180044259 · 2018-02-15 ·

A process for obtaining a catalyst composite comprising the following steps: a). selecting a molecular sieve having pores of 10-or more-membered rings b). contacting the molecular sieve with a metal silicate different from said molecular sieve comprising at least one alkaline earth metal and one or more of the following metals: Ga, Al, Ce, In, Cs, Sc, Sn, Li, Zn, Co, Mo, Mn, Ni, Fe, Cu, Cr, Ti and V, such that the composite comprises at least 0.1 wt % of silicate.

Process for Obtaining a Catalyst Composite
20180044259 · 2018-02-15 ·

A process for obtaining a catalyst composite comprising the following steps: a). selecting a molecular sieve having pores of 10-or more-membered rings b). contacting the molecular sieve with a metal silicate different from said molecular sieve comprising at least one alkaline earth metal and one or more of the following metals: Ga, Al, Ce, In, Cs, Sc, Sn, Li, Zn, Co, Mo, Mn, Ni, Fe, Cu, Cr, Ti and V, such that the composite comprises at least 0.1 wt % of silicate.

Zeolite core/silica zeolite shell composite, preparing method of the same, and catalyst including the same

The present disclosure relates to a preparing method of a zeolite core/silica zeolite shell composite, which includes adding a zeolite seed crystal into a gel solution containing a silicon-source compound, a structure directing agent and a fluorine anion-source compound, and then, crystallizing the gel solution for growing a silica zeolite shell containing a crystal structure which is coherent with that of the zeolite seed crystal; a zeolite core/silica zeolite shell composite prepared by the preparing method above; and catalytic use of the zeolite core/silica zeolite shell composite.

Zeolite core/silica zeolite shell composite, preparing method of the same, and catalyst including the same

The present disclosure relates to a preparing method of a zeolite core/silica zeolite shell composite, which includes adding a zeolite seed crystal into a gel solution containing a silicon-source compound, a structure directing agent and a fluorine anion-source compound, and then, crystallizing the gel solution for growing a silica zeolite shell containing a crystal structure which is coherent with that of the zeolite seed crystal; a zeolite core/silica zeolite shell composite prepared by the preparing method above; and catalytic use of the zeolite core/silica zeolite shell composite.

DEHYDRATION OF LACTIC ACID IN THE LIQUID PHASE
20240417360 · 2024-12-19 ·

The catalytic dehydration of lactic acid to acrylic acid has traditionally occurred in the gas phase. The disclosure provides a process occurring in the liquid phase over a catalyst. The process includes pressuring a feedstream, contacting the feedstream with a catalyst, converting the feedstream into a product stream, and recovering acrylic acid, alkyl acrylate, or a cation-balanced acrylate from the product stream.

DEHYDRATION OF LACTIC ACID IN THE LIQUID PHASE
20240417360 · 2024-12-19 ·

The catalytic dehydration of lactic acid to acrylic acid has traditionally occurred in the gas phase. The disclosure provides a process occurring in the liquid phase over a catalyst. The process includes pressuring a feedstream, contacting the feedstream with a catalyst, converting the feedstream into a product stream, and recovering acrylic acid, alkyl acrylate, or a cation-balanced acrylate from the product stream.

Method for making functional structural body

A method for making a functional structural body includes a skeletal body of a porous structure composed of a zeolite-type compound, and at least one type of metallic nanoparticles present in the skeletal body, the skeletal body having channels connecting with each other, the metallic nanoparticles being present at least in the channels of the skeletal body.