Abstract: A wall panel system attaches to a wall. The wall panel system has an attachment clip, a panel perimeter, and a wall panel. The attachment clip is secured to the wall. The panel perimeter has two legs. One leg is held between the attachment clip and the wall. The wall panel is attached to the other leg.

Abstract: A catalytic cracking process is disclosed in which cracking is performed in a riser reactor, catalytically cracked product is substantially separated from the catalyst in a gross-cut separator downstream of the riser reactor, and the cracked product is quenched with an anhydrous quench liquid at a location immediately downstream of the oil outlet of the gross-cut separator.

Abstract: Effective quenching is provided in a catalytic cracking unit to increase product yield and decrease thermal cracking. For increased benefits, the quench is injected at special locations. In the illustrated embodiment, the quench is injected into the oil product immediately downstream of an external gross cut separator before the product enters a disengaging vessel.

Abstract: Effective quenching is provided in a catalytic cracking process to increase product yield and decrease thermal cracking. To this end, the quench is injected at special locations and a special quench is used. In the illustrated embodiment, the quench is injected into the oil product immediately downstream of an external gross cut separator before the product enters a disengaging vessel and the quench comprises cycle oil.

Abstract: Isomerization process for petroleum light hydrocarbons with a boiling point within the range of from about 100.degree. F. (38.degree. C.) to about 210.degree. F. (99.degree. C.) wherein said process comprises contacting said hydrocarbons with a catalyst consisting essentially of an ultrastable, large pore crystalline zeolite aluminosilicate material containing less than 1 (wt)% alkali metal and characterized by well-defined hydroxyl infra-red bands and a maximum unit cubic cell dimension of 24.55 A and a metal component selected from the metals, oxides or sulfides of the Group VIII elements of the Periodic Table, under suitable isomerization conditions.

Abstract: A method for catalytically cracking an isolated reactant feed, 80-100 volume percent of which is a substantially mono-aromatic hydrocarbon fraction boiling in the boiling range of heavy gasoline and the remainder of which is a vaporizable hydrocarbon fraction, under effective cracking conditions of cracking temperature, catalyst composition, catalyst activity, catalyst-to-feed weight ratio, and weight hourly space velocity, to produce an isolated product having increased low molecular weight olefin and low molecular weight mono-aromatic contents and a reduced sulfur content and having a high octane rating.