The present disclosure relates to a process for producing ethylene oligomers and more particularly, to a process for oligomerizing ethylene by recycling butene, hexene, and octene in an ethylene oligomerization reaction with a catalyst system including a transition metal or transition metal precursor, a ligand with a backbone structure expressed by the following Chemical Formula 1, and a co-catalyst. [Chemical Formula 1] R.sup.1OYOR.sup.2 or R.sup.1OC(O)YC(O)OR.sup.2 Herein, R.sup.1, R.sup.2 are each independently hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl, or substituted heterohydrocarbyl, and Y represents a group connecting O or C(O)O and is hydrocarbyl, substituted hydrocarbyl, hetero hydrocarbyl, or substituted heterohydrocarbyl. According to the oligomerization method of the present disclosure, in the distribution of the produced -olefins, C10-C12 -olefins care highly distributed, the produced -olefins have a remarkably high purity.

Described herein are zirconium oxychloride clusters comprising zirconium oxychloride and a basic amino acid. Oral care compositions comprising the same; and methods of making and using the same are also described.

Described herein are zirconium oxychloride clusters comprising zirconium oxychloride and a basic amino acid. Oral care compositions comprising the same; and methods of making and using the same are also described.

The present invention relates to a monolith catalyst for reforming reaction, and more particularly, to a thermally stable (i.e. thermal resistance-improved) monolith catalyst for reforming reaction having a novel construction such that any one of Group 1A to Group 5A metals are used as a barrier component in the existing catalyst particles to inhibit carbon deposition occurring during the reforming reaction in a process for formation of a reforming monolith catalyst while improving thermal durability as well as non-activation of the catalyst due to a degradation.

This invention provides an electrolyte salt for use in an electrodeposition process for depositing Zirconium metal on a thin foil substrate. The prior art electrochemical process causes a reaction between a uranium substrate and ZrF.sub.4 species in the electrolyte that causes the formation of UF.sub.x at the substrate surface that prevents the formation of a dense uniform zirconium coating. This problem is solved by using an electrolyte salt in an electrodeposition process consisting of lithium fluoride (LiF) in a concentration ranging between about 11.5 molar percent and about 61 molar percent and one or more salts selected from the group consisting of sodium fluoride (NaF), potassium fluoride (KF), cesium fluoride (CsF), or cesium chloride (CsCL). Zirconium is added to the electrolyte salt through an addition of zirconium fluoride (ZrF.sub.4) in the range of about 1 to about 5 mass percent (w/w %). The Zr coating is of at least 98% pure Zr with a density of at least 98%.

This invention provides an electrolyte salt for use in an electrodeposition process for depositing Zirconium metal on a thin foil substrate. The prior art electrochemical process causes a reaction between a uranium substrate and ZrF.sub.4 species in the electrolyte that causes the formation of UF.sub.x at the substrate surface that prevents the formation of a dense uniform zirconium coating. This problem is solved by using an electrolyte salt in an electrodeposition process consisting of lithium fluoride (LiF) in a concentration ranging between about 11.5 molar percent and about 61 molar percent and one or more salts selected from the group consisting of sodium fluoride (NaF), potassium fluoride (KF), cesium fluoride (CsF), or cesium chloride (CsCL). Zirconium is added to the electrolyte salt through an addition of zirconium fluoride (ZrF.sub.4) in the range of about 1 to about 5 mass percent (w/w %). The Zr coating is of at least 98% pure Zr with a density of at least 98%.

A method for separating zirconium oxide/hafnium oxide by pyrometallurgy. The mixture of zirconium oxide/hafnium oxide, carbon and pure bromine react one hour at 650? C., then added to molten salt mixture for rectifying separation, and then maintained two hours at rectifying tower bottom below 357? C., to get the non-target substance; and then maintained five hours at 357? C. to collect the target substance zirconium tetrabromide; the residue in the reactor is retained, then rectification separation is performed in the same device, heated to 400? C. to retain more than five hours, to get hafnium tetrabromide, then the zirconium tetrabromide and hafnium tetrabromide are substituted by magnesium to get the pure zirconium and pure hafnium.

A method for separating zirconium oxide/hafnium oxide by pyrometallurgy. The mixture of zirconium oxide/hafnium oxide, carbon and pure bromine react one hour at 650? C., then added to molten salt mixture for rectifying separation, and then maintained two hours at rectifying tower bottom below 357? C., to get the non-target substance; and then maintained five hours at 357? C. to collect the target substance zirconium tetrabromide; the residue in the reactor is retained, then rectification separation is performed in the same device, heated to 400? C. to retain more than five hours, to get hafnium tetrabromide, then the zirconium tetrabromide and hafnium tetrabromide are substituted by magnesium to get the pure zirconium and pure hafnium.

The present invention relates to the recovery of rare earths, scandium, niobium, tantalum, zirconium, hafnium, titanium, and the like from ores or concentrates containing fluorine. More specifically, the ores or concentrates are pretreated by carbochlorination to convert the rare earths and other metals into their chlorides and then subjected to dilute hydrochloric acid leaching to recover the valuable rare earths and other metals from the leachate. Niobium, tantalum, zirconium, hafnium, and titanium can be recovered as their chlorides or oxychlorides from the gaseous products of carbochlorination, or converted into their oxides while simultaneously regenerating chlorine.

The present disclosure relates to a process for producing ethylene oligomers and more particularly, to a process for oligomerizing ethylene by recycling butene, hexene, and octene in an ethylene oligomerization reaction with a catalyst system including a transition metal or transition metal precursor, a ligand with a backbone structure expressed by the following Chemical Formula 1, and a co-catalyst. [Chemical Formula 1] R.sup.1OYOR.sup.2 or R.sup.1OC(O)YC(O)OR.sup.2 Herein, R.sup.1, R.sup.2 are each independently hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl, or substituted heterohydrocarbyl, and Y represents a group connecting O or C(O)O and is hydrocarbyl, substituted hydrocarbyl, hetero hydrocarbyl, or substituted heterohydrocarbyl. According to the oligomerization method of the present disclosure, in the distribution of the produced -olefins, C10-C12 -olefins care highly distributed, the produced -olefins have a remarkably high purity.