Abstract: An information processing apparatus comprises a first heat generation circuit, a second heat generation circuit, a blocking assembly, and a processor. The blocking assembly performs a first operation of blocking air flowing from the first heat generation circuit toward the second heat generation circuit or a second operation of passing the air, and the processor is configure to instruct the blocking assembly to perform the first operation in a case where a temperature of the air is higher than a predetermined value, and instruct the blocking assembly to perform the second operation in a case where the temperature of the air is lower than the predetermined value.

Abstract: The problem to be solved by the present invention is to provide an oxygen storage and release material comprising a ceria-zirconia-based complex oxide improved in ability to remove HC and NOx and a three-way catalyst able to reduce an amount of NOx emission. Further, to solve this problem, an oxygen storage and release material comprising a ceria-zirconia-based complex oxide containing Gd2O3 in 0.1 mol % or more and less than 20 mol % and having an ion conductivity of 2×10?5 S/cm or more at 400° C. is provided. Further, in addition to the above, an oxygen storage and release material having a molar ratio of cerium and zirconium of 0.2 or more and 0.6 or less by cerium/(cerium+zirconium) and an speed of oxygen storage and release “?t50” of 20.0 seconds or more or amount of oxygen storage and release of 300 ?mol-O2/g or more etc. was obtained.

Abstract: The problem to be solved by the present invention is to provide an oxygen storage and release material comprising a ceria-zirconia-based complex oxide improved in ability to remove HC and NOx and a three-way catalyst able to reduce an amount of NOx emission. Further, to solve this problem, an oxygen storage and release material comprising a ceria-zirconia-based complex oxide containing Gd2O3 in 0.1 mol % or more and less than 20 mol % and having an ion conductivity of 2×10?5 S/cm or more at 400° C. is provided. Further, in addition to the above, an oxygen storage and release material having a molar ratio of cerium and zirconium of 0.2 or more and 0.6 or less by cerium/(cerium+zirconium) and an speed of oxygen storage and release “?t50” of 20.0 seconds or more or amount of oxygen storage and release of 300 ?mol-O2/g or more etc. was obtained.

Abstract: Provided is a hydrogen station that supplies hydrogen, including: a shaft power generation unit that generates shaft power and heat; a reactor that obtains hydrogen by causing a reaction in a raw material using the heat supplied from the shaft power generation unit; and a compressor that compresses the hydrogen obtained by the reactor, wherein the shaft power generation unit drives the other devices and drives the compressor by applying the shaft power thereto.

Abstract: An apparatus connected to a first and second buses, the apparatus having a first controller that transforms first form data into second form data, transforms second form data into first form data, and outputs the transformed data, a second controller that transforms first form data into second form data, transforms second form data into first form data, and outputs the transformed data, a first distributing unit connected to the first and second controllers, the first distributing unit distributing first form data to the first and second controllers, respectively, a first selector that selects one of the second form data, and outputs the selected data, a second distributing unit connected to the first and the second controllers, the second distributing unit distributing second form data to the first and second controllers, respectively, and a second selector that selects one of the first form data, and outputs the selected data

Abstract: A process of the present invention for producing a hydrotreated gas oil has a step for obtaining a product oil having a total aromatic content of 3% by volume or less by hydrogenating a hydrotreated oil including 95% by volume or more of fraction having a boiling point range of 150-380° C., a sulfur content of 2-15 ppm by mass, a total aromatic content of 10-25% by volume, and a naphthene of 20-60% by volume in the presence of a hydrogenation catalyst; and a step for obtaining, by hydrogenating the above-described product oil in the presence of a hydrogenation catalyst containing a crystalline molecular sieve component, a product oil satisfying the conditions that the content of petroleum fraction having a boiling point range of lower than 150° C. is 16% by volume or less, and the sum of the total aromatic content and the total naphthene content is 80% or less relative to the sum of these in the hydrotreated oil.

Abstract: The present invention provides a process of desulfurizing a heavy oil, which comprises diluting the heavy oil with a dilution medium to 90 percent by mass or less and cracking the diluted heavy oil at a cracking rate of 10 percent or less thereby prolonging the lifetime of a catalyst for desulfurizing a heavy oil.

Abstract: A process for producing a high-octane gasoline blending stock in high yield from hydrocarbons having 4 carbon atoms and/or hydrocarbons having 5 carbon atoms recovered as by-products from a catalytic cracking unit or a thermal cracking unit, characterized in that a hydrocarbon mixture containing 50 percent by weight or more of hydrocarbon having 4 carbon atoms and/or hydrocarbons having 5 carbon atoms is brought into contact with a zeolite catalyst so as to be reformed under such reaction conditions that the reformed fraction having 5 or more carbon atoms has: (1) a content of olefins having 5 or more carbon atoms of 5 to 90 percent by weight; (2) an aromatic content of 10 to 90 percent by weight; (3) a benzene content of the aromatics of 10 percent by mass or less; and (4) a content of aromatics having 8 carbon atoms of the aromatics of 30 percent by mass, and the reformed fraction having 5 or more carbon atoms has a research octane number of 95 or higher and is produced at a yield of 60 percent by mass or m

Abstract: A catalyst is provided for hydrocracking paraffinic hydrocarbons which simultaneously the three requirements of high cracking activity and high selectivity of middle distillates as well as the low pour point of the resulting gas oil; and a process is provided for producing liquid hydrocarbons using the catalyst. The catalyst is characterized in that it comprises (a) a crystalline aluminosilicate and (b) an amorphous aluminosilicate at a weight ratio of 0.01<(a)/(b)<1.0. Furthermore, the catalyst is characterized in that it further comprises a group VIb metal and/or a group VIII metal.