Patent classifications
B01J35/77
METHOD OF SYNTHESIZING MANGANESE OXIDE NANOCORALS
A method of synthesizing manganese oxide nanocorals comprises the steps of a) heating a potassium permanganate solution; (b) providing manganese sulfate in a basic solution; (c) combining the manganese sulfate basic solution drop-wise with the heated potassium permanganate solution until a brown precipitate is formed; (d) stirring the brown precipitate for a period of about 12 hours at a temperature greater than 300 K; (e) isolating the precipitate; and (f) drying the precipitate inside an oven at a temperature greater than 300 K to provide manganese oxide nanocorals. The manganese oxide nanocorals include nanowires having a diameter typically ranging from about 20 nm to about 40 nm.
Catalyst for low temperature slurry bed Fischer-Tropsch synthesis
A method for controllably producing a hematite-containing Fischer-Tropsch catalyst by combining an iron nitrate solution with a precipitating agent solution at a precipitating temperature and over a precipitation time to form a precipitate comprising iron phases; holding the precipitate from at a hold temperature for a hold time to provide a hematite containing precipitate; and washing the hematite containing precipitate via contact with a wash solution and filtering, to provide a washed hematite containing catalyst. The method may further comprise promoting the washed hematite containing catalyst with a chemical promoter; spray drying the promoted hematite containing catalyst; and calcining the spray dried hematite containing catalyst to provide a calcined hematite-containing Fischer-Tropsch catalyst.
METAL DOPED CERIUM OXIDE COMPOSITIONS
The present invention concerns a process for the production of metal doped cerium compositions comprising a cerium oxide and a metal oxide by precipitation. The invention also concerns metal doped cerium compositions providing high crystallites size and exhibiting high thermal stabilities, which may be used as a catalytic support or for polishing applications.
PRODUCTION METHOD OF OXYGEN STORAGE MATERIAL, AND OXYGEN STORAGE MATERIAL
A production method comprising: adding a hydroxycarboxylic acid to an aqueous solution containing a Ce salt, a Zr salt, an Al salt, and at least one selected from a La salt, an Mg salt, and a Ca salt, to produce a gel, heating the gel to obtain a solid product by decomposition of the salts, firing the solid product to obtain a fired product containing a ceria-zirconia-based regular array phase precursor and an aluminate-based composite oxide precursor, performing a reducing heat treatment of the fired product to obtain a first composite having mutually dispersed therein a pyrochlore phase and an aluminate-based composite oxide, and performing an oxidizing heat treatment of the first composite to obtain a second composite in which at least part of the pyrochlore phase is transformed into a phase; and an oxygen storage material having mutually dispersed therein the composite oxide and the regular array phase.
MOLYBDENUM-VANADIUM-BERYLLIUM-BASED OXIDATIVE DEHYDROGENATION CATALYST MATERIALS
This document relates to oxidative dehydrogenation catalyst materials that include molybdenum, vanadium, beryllium, oxygen, and optionally aluminum.
CATALYST FOR HYDROGENATION REACTION AND METHOD FOR PRODUCING SAME
The present invention relates to a catalyst for a hydrogenation reaction and a method for producing the same, and more specifically, to a catalyst for a hydrogenation reaction, wherein the catalyst includes nickel oxide as an active ingredient and copper oxide and sulfur oxide as a promoter, and especially, can control a reduction degree value according to whether or not a passivation layer of a nickel metal is removed.
Nano size crystal ZSM-5 and its preparation and applications thereof
The present invention provides a novel, cost-effective and simple synthetic process for preparing a nano ZSM-5 catalyst which is further utilized in fluid catalytic cracking of feedstock oil containing organic compounds. The nano-ZSM-5 catalyst shows higher selectivity towards olefines and low selectivity towards LCO and bottoms.
CATALYST FOR TREATING EXHAUST GAS
Provided is a method for reducing N.sub.2O emissions in an exhaust gas comprising contacting an exhaust gas containing NH.sub.3 and an inlet NO concentration with an SCR catalyst composition containing small pore zeolite having an SAR of about 3 to about 15 and having about 1-5 wt. % of an exchanged transition metal.
COMPOSITE PHOTOCATALYST, MANUFACTURING METHOD THEREOF, KITS CONTAINING COMPOSITE PHOTOCATALYST, AND BACTERICIDE PHOTOCATALYST
A composite photocatalyst, a manufacturing method thereof, the kits including the composite photocatalyst, and a bactericide photocatalyst. A composite photocatalyst includes photocatalyst nanocrystals and platinum nanocrystals. The photocatalyst nanocrystals include a compound represented by the following chemical formula (1):
A.sup.2+(B.sup.3+).sub.2X.sub.4chemical formula (1), wherein A.sup.2+ represents Zn.sup.2+, Cu.sup.2+, Fe.sup.2+, Mn.sup.2+, Ni.sup.2+, Co.sup.2+ or Ag.sub.2.sup.2+; B.sup.3+ represents Fe.sup.3+, Mn.sup.3+ or Cr.sup.3+; and X represents O.sup.2.
Catalytic cracking catalyst having a rare earth-containing Y zeolite and a preparation process thereof
The present invention relates to a catalytic cracking catalyst and a preparation process thereof, the catalytic cracking catalyst has a cracking active component, an optional mesoporous aluminosilicate material, a clay and a binder, wherein said cracking active component comprises, substantially consists of or consists of: a rare earth-containing Y zeolite, an optional other Y zeolite, and an optional MFI-structured zeolite, said rare earth-containing Y zeolite has a rare earth content as rare earth oxide of 10-25 wt %, e.g. 11-23 wt %; a unit cell size of 2.440-2.472 nm, e.g. 2.450-2.470 nm; a crystallinity of 35-65%, e.g. 40-60%; a Si/Al atom ratio in the skeleton of 2.5-5.0; and a product of the ratio of the strength I.sub.1 of the peak at 2=11.80.1 to the strength I.sub.2 of the peak at 2=12.30.1 in the X-ray diffraction spectrogram of the zeolite and the weight percent of rare earth as rare earth oxide in the zeolite of higher than 48, e.g. higher than 55.