Abstract: There is disclosed a process for selectively purifying a lithium chloride product stream from an aqueous lithium salt-containing solution, the process comprising the steps of: introducing the aqueous lithium salt-containing solution to one or more columns filled with a lithium selective sorbent; flowing the aqueous lithium salt-containing solution through the one or more columns to adsorb lithium chloride from the aqueous lithium salt-containing solution onto a sorbent and form a sorbent with a greater lithium chloride content than the sorbent prior to introducing the solution; flowing a desorbent fluid once-through the at least one or more columns to desorb lithium chloride from the sorbent into an eluate stream, wherein the desorbent fluid is flowed in a co-current direction with respect to the direction of flow of the aqueous lithium salt-containing solution, and recovering a lithium chloride product stream from the eluate stream, wherein the eluate stream has a Li:TDS ratio of 0.08 or more.

Abstract: A process for manufacturing a monocyclic aromatic compound is disclosed. The process comprises contacting an aluminosilicate catalyst with an oxygen-containing organic molecule in a reactor to produce the monocyclic aromatic compound and in situ-generated hydrogen gas, and introducing CO2 into the reactor and allowing the CO2 to react with the in situ-generated hydrogen gas to form additional monocyclic aromatic compound.

Abstract: The disclosure related to processes for the high-selectivity conversion of olefins to monocyclic aromatic compounds, such as BTX, via the introduction of a weakly coordinating compound to a dehydroaromatization catalyst. Moreover, certain embodiments relate to processes for recycling polyaromatic compounds back to a reactor to improve the yield of said monocyclic aromatic compounds. Moreover, certain embodiments relate to processes for regenerating the dehydroaromatization catalyst.

Abstract: The disclosed process relates to a process for selectively purifying a lithium product stream from an aqueous lithium salt-containing solution in a continuous mode, said process comprising the steps of: a) introducing said aqueous lithium salt-containing solution to an arrangement of three or more packed-bed columns in series each filled with a lithium selective sorbent, wherein at least two of said three or more columns are at an adsorption stage, with one at a leading lithium chloride adsorption stage and one or more at a trailing lithium chloride adsorption stage, and at least one of said three or more columns is simultaneously at a lithium chloride desorption stage; b) flowing said aqueous lithium salt-containing solution through said at least two of said three or more columns at a leading lithium chloride adsorption stage and a trailing lithium chloride adsorption stage to adsorb lithium chloride from the aqueous lithium salt-containing solution and respectively form a fully-saturated sorbent and a parti

Abstract: Processes, catalysts and systems for preparing a composition comprising aliphatic, olefinic, cyclic and/or aromatic hydrocarbons of seven or greater carbon atoms per molecule are provided.

Abstract: Methods and systems for processing a first composition of a light hydrocarbon mixture with a 100° F. vapor pressure range from 2 to 51 psia into a second composition of aromatic hydrocarbons are provided. The method comprises contacting the first composition with a reaction zone comprising three or more operating fixed bed reactors in series, each reactor containing porous solid acid catalyst, said method further comprising the step of adding a toluene feedstock to said reaction zone under conditions in which the first composition is transformed to a second composition in an amount greater and at a percentage higher in aromatics than produced via a parallel or single reactor process with the same catalyst without the toluene feedstock, and/or contacting said second composition comprising heavy aromatics with said reaction zone to further increase amount and percentage of aromatics.

Abstract: Processes, catalysts and systems for preparing a composition comprising aliphatic, olefinic, cyclic and/or aromatic hydrocarbons of seven or greater carbon atoms per molecule are provided.

Abstract: Described herein are materials and methods for improved catalytic oligomerization of an ethylene monomer and/or propylene monomer. The present disclosure teaches oligomerizing the ethylene monomer or propylene monomer to produce oligomers. Also described is a heterogeneous catalyst comprising sulfate modified nickel on titanium modified alumina and a surface modification with yttrium (Y) suitable for use in the disclosed oligomerization.

Abstract: Described herein are processes for the conversion of ethylene into CS+ olefins, naphthenics, and aromatics via a dual catalyst reaction utilizing a dearomatization catalyst.

Abstract: Described herein are processes for the conversion of ethylene into CS+ olefins, naphthenics, and aromatics via a dual catalyst reaction utilizing a dehydroaromatization catalyst.

Abstract: Described herein are processes for the conversion of ethylene into C5+ olefins, naphthenics, and aromatics via a dual catalyst reaction utilizing a dehydroaromatization catalyst.

Abstract: Described herein are processes for the conversion of ethylene into CS+ olefins, naphthenics, and aromatics via a dual catalyst reaction utilizing a dehydroaromatization catalyst.

Abstract: Described herein are materials and methods for improved catalytic oligomerization of an ethylene monomer and/or propylene monomer. The present disclosure teaches oligomerizing the ethylene monomer or propylene monomer to produce oligomers. Also described is a heterogeneous catalyst comprising sulfate modified nickel on titanium modified alumina and a surface modification with yttrium (Y) suitable for use in the disclosed oligomerization.

Abstract: Described herein are processes for the conversion of ethylene into C5+ olefins, naphthenics, and aromatics via a dual catalyst reaction utilizing a dehydroaromatization catalyst.

Abstract: A catalyst comprising palladium supported on a titania-alumina extrudate is disclosed. The extrudate comprises at least 80 wt % titania and 0.1 to 15 wt % alumina. A palladium catalyst prepared from the titania-alumina extrudate has significantly higher crush strength. Its catalytic performance in vinyl acetate production is improved.

Abstract: A method for preparing a palladium-gold catalyst containing a titania extrudate is disclosed. The titania extrudate is produced by using a carboxyalkyl cellulose and a hydroxyalkyl cellulose as extrusion aids. The titania extrudate has improved processibility and/or mechanical properties. After calcination, the extrudate is used as a carrier for the palladium-gold catalyst. The catalyst is useful in producing vinyl acetate by oxidizing ethylene with oxygen in the presence of acetic acid.

Abstract: An extrudate comprising titania, a carboxyalkyl cellulose, and a hydroxyalkyl cellulose is disclosed. The extrudates have a smooth outer surface when they exit the extruder. The extrusion processibility is improved.

Abstract: A method for preparing a palladium-gold catalyst containing a titania extrudate is disclosed. The titania extrudate is produced by using a carboxyalkyl cellulose and a hydroxyalkyl cellulose as extrusion aids. The titania extrudate has improved processibility and/or mechanical properties. After calcination, the extrudate is used as a carrier for the palladium-gold catalyst. The catalyst is useful in producing vinyl acetate by oxidizing ethylene with oxygen in the presence of acetic acid.

Abstract: A method for preparing a palladium-gold catalyst containing a titania extrudate is disclosed. The titania extrudate is produced by using a carboxyalkyl cellulose and a hydroxyalkyl cellulose as extrusion aids. The titania extrudate has improved processibility and/or mechanical properties. After calcination, the extrudate is used as a carrier for the palladium-gold catalyst. After calcination, the in producing vinyl acetate by oxidizing ethylene with oxygen in the presence of acetic acid.

Abstract: An extrudate comprising at least 50 wt % titania, 0.5 to 25 wt % tungsta, and 0.5 to 35 wt % alumina is disclosed. The extrudate has improved crush strength compared with a titania-tungsta extrudate. A palladium catalyst prepared from the extrudate has good activity in preparing an acetoxylated olefin from an olefin, oxygen, and acetic acid.