An electrode assembly including a first electrode and a dielectric layer on the first electrode. The dielectric layer comprises a lead-containing compound of the formula PbMgV.sub.2O.sub.7, Pb.sub.2Te.sub.3O.sub.8, PbZnV.sub.2O.sub.7, Na.sub.2PbO.sub.2, PbP.sub.2O.sub.6, PbZnSiO.sub.4, Pb.sub.2In.sub.2Si.sub.2O.sub.9, Pb.sub.6(AsO.sub.4)[B(AsO.sub.4).sub.4], PbAl.sub.2Si.sub.2O.sub.8, K.sub.4PbO.sub.3, Pb.sub.2TiAs.sub.2O.sub.9, Pb.sub.4O(VO.sub.4).sub.2, Rb.sub.4PbO.sub.3, Pb.sub.2V.sub.2O.sub.7, Pb.sub.9Al.sub.8O.sub.21, Nd(Al.sub.3O.sub.6)(Pb.sub.2O.sub.2), Pb.sub.6Co.sub.9(TeO.sub.6).sub.5, Pb.sub.3(B.sub.3O.sub.7)NO.sub.3, a lead-containing oxyhalide of the formula Pb.sub.13(Cl.sub.3O.sub.5).sub.2, Pb.sub.13(Br.sub.3O.sub.5).sub.2, Pb.sub.2OF.sub.2, Pb.sub.2CO.sub.3F.sub.2, Pb(AsO.sub.2).sub.3Cl, Pb.sub.3O.sub.2(OH)Cl, Pb.sub.6(BO.sub.3).sub.3OCl, Pb.sub.2B.sub.5O.sub.9I, Pb.sub.2B.sub.5O.sub.9Br, Pb.sub.2B.sub.5O.sub.9Cl, Pb.sub.5(AsO.sub.3).sub.3Cl, Pb.sub.8Y.sub.6F.sub.32O, Pb(O.sub.2Pb.sub.3).sub.2(BO.sub.3)Br.sub.3, Pb.sub.6LaO.sub.7Cl, a lead-containing phosphate of the formula Pb.sub.2PO.sub.4I, Pb.sub.2InP.sub.3O.sub.11, Pb.sub.2MoP.sub.3O.sub.11, Pb.sub.2Ni(PO.sub.4).sub.2, Pb.sub.2VO(PO.sub.4), K.sub.2Pb(PO.sub.3).sub.4, Pb.sub.3(MoO).sub.3(PO.sub.4).sub.5, Pb.sub.4O(PO.sub.4).sub.2, RbPb(PO.sub.3).sub.3, PbVO.sub.2PO.sub.4, Pb.sub.5(PO.sub.4).sub.3F, Pb.sub.5(PO.sub.4).sub.3Cl, Pb.sub.5(PO.sub.4).sub.3I, PbP.sub.2O.sub.6, or a combination thereof. The electrode assembly can be particularly useful in various electronic devices.

The present invention relates to: a catalyst for glycerin dehydration; a preparation method therefor; and an acrolein preparation method using the catalyst. According to one embodiment of the present invention, the catalyst is used in glycerin dehydration so as to exhibit high catalytic activity, a high yield and high acrolein selectivity, and has a characteristic in which carbon is not readily deposited, thereby having a long lifetime compared with that of a conventional catalyst.

Described is a process for treatment of a fluid comprising an oxidizable contaminant selected from one or both of a sulfide and a thiol, the process comprising the step of contacting the fluid with a first complex of ferric iron and a polyphosphate to oxidize the oxidizable contaminant and generate a second complex of ferrous ion and the polyphosphate.

Disclosed are a ferrite catalyst and preparation methods thereof. The catalyst is provided with a formula below, wherein A is Mg atom, Zn atom or a mixture of both atoms at any ratio; D is one or more atoms selected from the group consisting of Ni, Co, W, Mn, Ca, Mo or V atom; Z is a catalyst carrier, which is one or more selected from the group consisting of calcium phosphate, calcium dihydrogen phosphate, aluminum phosphate, aluminum dihydrogen phosphate, ferric phosphate, magnesium phosphate, zinc phosphate, Mg—Al hydrotalcite, calcium carbonate, magnesium carbonate; a=0.01-0.6; b=0-0.30; c is a number balancing each valence; x, y represent the amounts of principal catalyst and carrier Z respectively, wherein the weight ratio y/x=0.5:1-7:1.
x(FeA.sub.aD.sub.bO.sub.c)/yZ

An improved process and catalyst composition for cracking hydrocarbons in a fluidized cracking process are disclosed. The process employs circulating inventory of a regenerated cracking having a minimal carbon content. The regenerated catalyst comprises a catalyst/additive composition which contains a pentasil zeolite, iron oxide, and a phosphorous compound. In accordance with the present disclosure, the catalyst/additive contains controlled amounts of iron oxide which is maintained in an oxidized state by maintaining low amounts of carbon on the regenerated catalyst inventory. In this manner it was discovered that the catalyst composition greatly enhances the production and selectivity of light hydrocarbons, such as propylene.

An object of the present invention is to provide a method for suppressing the corrosion of a reactor and reducing waste in the production of 2-furaldehyde from a sugar raw material containing a hexose as a constituent component, and another object of the invention is to provide an industrially advantageous method for producing 2-furaldehyde, which suppresses a decrease in the activity of a catalyst in a case of using an acid catalyst and provides a higher yield. The present invention relates to a method for producing 2-furaldehyde comprising heating a sugar raw material containing a hexose as a constituent component in an aprotic polar solvent in the presence of a solid acid catalyst.

A catalyst for converting hydrocarbon, a method of making the same, and a method of using the same are provided. Such a catalyst includes a zeotype microporous material, a binder material, and a metal phosphide, which can be in a range of from 0.01% to 10% by weight of a total weight of the catalyst. For example, such a catalyst can be used to convert light alkene or alkane into aromatic hydrocarbon such as benzene, toluene, xylenes, and a combination thereof. The alkene may be ethylene, propylene, butylene, or a combination thereof. The alkene may be supplied directly or from a stream converted from light alkane such as methane, ethane, propane, butane, or a combination thereof.

A modular device for generating hydrogen gas from a hydrogen liquid carrier may include a housing; an inlet for receiving the hydrogen liquid carrier; and at least one cartridge arranged within the housing. The cartridge may include at least one catalyst configured to cause a release of hydrogen gas when exposed to the hydrogen liquid carrier. The modular device may include a gas outlet for expelling the hydrogen gas released in the modular device and a liquid outlet for expelling spent hydrogen liquid carrier.

Methods and catalysts for producing benzyl alcohol and homologues thereof from short-chain alcohols by catalytic conversion are disclosed. The methods and catalysts develop a new route for benzyl alcohols and ethyl benzyl alcohols production through cross coupling-aromatization reaction using short-chain alcohols as reactants and provide corresponding catalysts required for the above catalytic reaction. It is emphasized on a single bed catalyst to produce benzyl alcohol and its homologues in one step, and is expected to become an important alternative route for the production of benzyl alcohol and its homologues. A route and corresponding catalysts for directly producing benzyl alcohol and ethyl benzyl alcohol through coupling-aromatization reaction starting from low carbon alcohols are provided. The selectivity of the benzyl alcohol is up to 35%, and the total selectivity of the ethyl benzyl alcohol is up to 11%.

A method for producing a lubricant base oil includes a first hydrogenation treatment step of bringing a hydrogenation treatment catalyst and a light wax into contact with each other at temperature T.sub.1, and thereby obtaining a first treated oil; a second hydrogenation treatment step of bringing the hydrogenation treatment catalyst and a heavy wax into contact with each other at temperature T.sub.2, and thereby obtaining a second treated oil; and a base oil production step of obtaining a lubricant base oil from a feedstock oil containing at least one selected from the group consisting of the first treated oil and the second treated oil, in which the hydrogenation treatment catalyst is a catalyst obtained by supporting one or more metals selected from the elements of Group 6, Group 8, Group 9, and Group 10 of the Periodic Table of Elements, on an inorganic oxide support.