Abstract: Rocker buttons for devices such as automotive audio systems are mounted in escutcheons of the audio systems by using rocker frame members. Light dams, unitary with the rocker frame members shield lamps used to illuminate indicia in the rocker buttons so that the light is not transmitted through gaps between the rocker buttons and the edges of openings through the escutcheons which receive the rocker buttons. Trunions extend laterally from the rocker buttons and are received within bearings formed by grooves in the escutcheons. In accordance with a preferred embodiment of the invention, the rocker frames retain trunions in the bearings and in accordance with another embodiment of the invention peripheral display lenses overlie the trunions to hold the trunions in the bearings.

Abstract: A process for the liquefaction of coal wherein raw feed coal is dissolved in recycle solvent with a slurry containing recycle coal minerals in the presence of added hydrogen at elevated temperature and pressure. The highest boiling distillable dissolved liquid fraction is obtained from a vacuum distillation zone and is entirely recycled to extinction. Lower boiling distillable dissolved liquid is removed in vapor phase from the dissolver zone and passed without purification and essentially without reduction in pressure to a catalytic hydrogenation zone where it is converted to an essentially colorless liquid product boiling in the transportation fuel range.

Abstract: The relative ratio of heavy distillate to light distillate produced in a coal liquefaction process is continuously controlled by automatically and continuously controlling the ratio of heavy distillate to light distillate in a liquid solvent used to form the feed slurry to the coal liquefaction zone, and varying the weight ratio of heavy distillate to light distillate in the liquid solvent inversely with respect to the desired weight ratio of heavy distillate to light distillate in the distillate fuel oil product. The concentration of light distillate and heavy distillate in the liquid solvent is controlled by recycling predetermined amounts of light distillate and heavy distillate for admixture with feed coal to the process in accordance with the foregoing relationships.

Abstract: Normally solid dissolved coal product and a distillate liquid product are produced by continuously passing a feed slurry comprising raw feed coal and a recycle solvent oil and/or slurry together with hydrogen to a preheating-reaction zone (26, alone, or 26 together with 42), the hydrogen pressure in the preheating-reaction zone being at least 1500 psig (105 kg/cm.sup.2), reacting the slurry in the preheating-reaction zone (26, or 26 with 42) at a temperature in the range of between about 455.degree. and about 500.degree. C. to dissolve the coal to form normally liquid coal and normally solid dissolved coal. A total slurry residence time is maintained in the reaction zone ranging from a finite value from about 0 to about 0.2 hour, and reaction effluent is continuously and directly contacted with a quenching fluid (40, 68) to substantially immediately reduce the temperature of the reaction effluent to below 425.degree. C.

Abstract: Normally solid dissolved coal product and a distillate liquid product are produced by continuously passing a feed slurry comprising raw feed coal and a recycle solvent oil and/or slurry together with hydrogen to a preheating-reaction zone (26, alone, or 26 together with 42), the hydrogen pressure in the preheating-reaction zone being at least 1500 psig (105 kg/cm.sup.2), reacting the slurry in the preheating-reaction zone (26, or 26 with 42) at a temperature in the range of between about 455.degree. and about 500.degree. C. to dissolve the coal to form normally liquid coal and normally solid dissolved coal. A total slurry residence time is maintained in the reaction zone ranging from a finite value from about 0 to about 0.2 hour, and reaction effluent is continuously and directly contacted with a quenching fluid (40, 68) to substantially immediately reduce the temperature of the reaction effluent to below 425.degree. C.

Abstract: A propulsion system useful, for example, for automobiles, comprising an air compressor, a rotary engine, and a multiple stage turbine mounted upon a common shaft, and an infuser section comprising a plurality of nozzles for injecting air into the exhaust gases from the turbine to reduce the temperature and consequently the pressure of the exhaust gases prior to passage into an exhaust pipe.

Abstract: A propulsion system useful, for example, for automobiles, comprising an air compressor, a rotary engine, and a multiple stage turbine mounted upon a common shaft, and an infuser section comprising a plurality of nozzles for injecting air into the exhaust gases from the turbine to reduce the temperature and consequently the pressure of the exhaust gases prior to passage into an exhaust pipe.