Abstract: A virtual reality system composed of a virtual reality box, the virtual reality box mounting a smart phone or containing a similar computing device that is in a fixed position relative to a user's eyes. The smart phone or computer including one or more processors and a memory, and having front and a back. The front including a touch screen display, the back including a first camera lens and a second camera lens spaced apart from the first camera lens, and electronic sensing devices which measure the azimuth and elevation angle of the centerline of the camera located in the computing device in communication with the one or more processors and memory and receiving both visual and orientational information that is passed through the first and second camera lenses.

Abstract: Moving pictures, as exemplified by ordinary television programming, are viewed stereoscopically when viewed using a special eyewear apparatus which includes a prismatic lens construction. The three dimensional effect is produced by the design of the eyewear to redirect the visual tracking of one or both eyes away from the normal convergent angle used when viewing display screens to a wider angle, which is normally associated with viewing objects at a greater distance that the display screen. This causes the eyes to perceive two distinct views of the single picture on the screen, which are interpreted by the viewer's brain, not as two laterally displaced pictures, but as a single picture with elements of depth, or a 3D picture.

Abstract: Moving pictures, as exemplified by ordinary television programming, are viewed stereoscopically when viewed using a special eyewear apparatus which includes a prismatic lens construction. The three dimensional effect is produced by the design of the eyewear to redirect the visual tracking of one or both eyes away from the normal convergent angle used when viewing display screens to a wider angle, which is normally associated with viewing objects at a greater distance that the display screen. This causes the eyes to perceive two distinct views of the single picture on the screen, which are interpreted by the viewer's brain, not as two laterally displaced pictures, but as a single picture with elements of depth, or a 3D picture.

Abstract: Moving pictures, as may be exemplified by television programming, are viewed stereoscopically. The system preferably comprises a visual display screen upon which may be displayed a left-to-right reversed visual display. A reflecting surface is positioned opposite the visual display screen for reflecting imagery from the visual display screen toward the viewer. The reflected imagery provides a reflected left-to-right correct visual display. The visual display screen is spaced from the reflecting surface such that the viewer's perception of the visual display screen causes the viewer to focus on a point behind the reflecting surface thereby requiring the viewer to perceive laterally offset reflections of the visual display screen at the reflecting surface.

Abstract: Moving pictures, as may be exemplified by television programming, are viewed stereoscopically. The system preferably comprises a visual display screen upon which may be displayed a left-to-right reversed visual display. A reflecting surface is positioned opposite the visual display screen for reflecting imagery from the visual display screen toward the viewer. The reflected imagery provides a reflected left-to-right correct visual display. The visual display screen is spaced from the reflecting surface such that the viewer's perception of the visual display screen causes the viewer to focus on a point behind the reflecting surface thereby requiring the viewer to perceive laterally offset reflections of the visual display screen at the reflecting surface.

Abstract: A fluid contacting apparatus is constructed by coiling a ribbed, net-like material into a cylindrical core which is then placed in a retaining vessel through which fluids flow.

Abstract: A packed mass transfer tower for establishing intimate gas-liquid contact and efficient mass transfer that is less susceptible to gas or liquid channeling, gas surging and uneven distribution of gas or liquid across the cross-sectional area of the tower. In one embodiment, the packed tower includes a packing arrangement including a loosely packed bed of mobile packing material, and an adjacent, tightly packed bed of mobile packing material. The relatively tightly packed bed of mobile packing material acts as a gas distributor, as well as being a material that causes good gas-liquid contact, to provide an even flow of gas across essentially the entire cross-sectional area of the loosely packed bed of mobile packing material. In another embodiment, mobile packing elements and fixed packing elements are intermixed between the same spaced fluid-pervious grids.

Abstract: A process for removal of dissolved H.sub.2 S from condensed geothermal steam that includes the steps of cooling and oxygenating the sour steam condensate by contacting the sour condensate with air in a cooling tower; collecting the oxygenated condensate in a cooling tower collection basin and initially adding a polyvalent metal chelate catalyst, e.g., iron chelate catalyst solution, to the sour condensate at a very low concentration, e.g., about 0.1 ppm to about 10 ppm, preferably about 0.5 ppm to about 1 ppm by weight, and periodically or continuously adding, to the solution, a chelating agent for the polyvalent metal to account for chelon degradation to maintain active polyvalent metal chelate solution at a concentration of about 0.1 ppm to about 10 ppm, preferably about 0.5 ppm to about 1 ppm by weight. The dissolved H.sub.2 S is removed, by oxidation to sulfur, without the addition of polyvalent metal, e.g.

Abstract: Sour water is treated to remove dissolved hydrogen sulfide by means of an aqueous, non-chelated polyvalent metal solution in a continuous recirculating system, particularly an autocirculation system, having reaction and oxygenation zones. The solution contains a small catalytic amount of polyvalent metal, e.g., ferrous or ferric iron salts, and the dissolved hydrogen sulfide is oxidized to sulfur in the liquid phase, without chelating agent solution, by means of dissolved oxygen in the solution. The sour water feed to the reaction zone is diluted by a massive recycle of oxygenated solution from the oxygenation zone before the sour water is contacted with air or other oxidizing gas used for oxygenating the used solution. A portion of the oxygenated solution containing polyvalent metal, without added chelating agent, is removed as the sweet water product, and replacement polyvalent metal is added.

Abstract: A packed mass transfer tower for establishing intimate gas-liquid contact and efficient mass transfer that is less susceptible to gas or liquid channeling, gas surging and uneven distribution of gas or liquid across the cross-sectional area of the tower. The packed tower includes a mobile bed mass transfer stage including a packed bed of mobile packing material, such as hollow spheres.

Abstract: An apparatus and method of contacting a liquid with different gases sequentially in separate mass transfer zones within a single vessel, the mass transfer zones operatively connected in liquid communication with each other, including intimately contacting the liquid with a first process gas in cocurrent flow in a first mass transfer zone to effect mass transfer between the first liquid and the process gas, and introducing the liquid into a second mass transfer zone with a second gas, different from the first gas, in cocurrent flow with the second liquid, thereby effecting mass transfer between the second liquid and the second gas.

Abstract: A method and apparatus for removing H.sub.2 S from a process gas, including a reaction chamber between an absorption chamber and an oxidizer chamber, in the polyvalent metal redox catalyzed removal of H.sub.2 S from a process gas. The process and apparatus of the present invention inclues a first gas-liquid mass transfer zone or absorber chamber for intimately containing an H.sub.2 S-containing process gas with an oxidized polyvalent metal redox solution for absorption of the H.sub.2 S; and a reaction chamber in fluid communication with polyvalent metal redox solution exiting the absorption chamber through a valve-controlled cross-flow conduit. Cross flow of solution from the absorber chamber through a valve or other circulation control device to the reaction chamber provides controlled, continuous and sequential gas-liquid contact with two or more different gases in separate absorption, reaction and oxygenation zones within a single or multiple vessels.

Abstract: The in situ formation of a supported active metal phthalocyanine catalyst is disclosed. The supported metal phthalocyanine catalyst is useful in sweetening sour petroleum distillates containing mercaptans.

Abstract: A method and apparatus including a reaction chamber interposed in a polyvalent metal redox solution flow path between an absorber chamber and an oxygenation chamber, including one or more oxygenation stages, for contact in the reaction chamber of H.sub.2 S-laden catalytic polyvalent metal redox solution form the absorber chamber with highly oxidized polyvalent metal redox solution from the last oxygenation stage to accomplish oxidation of the dissolved H.sub.2 S species by interaction with the oxidized redox catalyst essentially in the absence of gaseous dissolved oxygen. The highly oxidized polyvalent metal redox solution, including Fe.sup.+3 or V.sup.+5, contacts the H.sub.2 S-laden solution from the absorber chamber for reoxidation of the dissolved HS.sup.-, S.sup.= and any of the polyvalent metal sulfur compounds (presumably a chelated iron sulfide or a vanadium sulfide), to avoid formation of sulfate or thiosulfate salts which reduce the yeild of sulfur and build up in the solution.

Abstract: A catalytic polyvalent metal redox solution can be recovered and re-used in a catalytic polyvalent metal redox solution H.sub.2 S-removal, sulfur production process by interposing a closed loop evaporator/condenser process and apparatus in the sulfur washing/filtering/recovery process and apparatus so that wash water used to purify the sulfur, and any polyvalent metal redox solution recovered from the sulfur melter are fed to an evaporator to concentrate the redox solution to a concentration capable of effective absorption of H.sub.2 S, and the water evaporated in the evaporator is condensed as pure water for use in washing and/or filtering the recovered sulfur.

Abstract: Sour water is treated to remove dissolved hydrogen sulfide by means of an aqueous chelated polyvalent metal solution in a continuous recirculating system, particularly an autocirculation system, having reaction and oxygenation zones. The solution contains a small catalytic amount of chelated polyvalent metal, and the dissolved hydrogen sulfide is catalytically oxidized to sulfur in the liquid phase by means of dissolved oxygen in the solution. The sour water feed to the reaction zone is diluted by a massive recycle of oxygenated solution from the oxygenation zone before the sour water is contacted with air or other oxidizing gas used for oxygenating the used solution. A portion of the oxygenated solution containing chelated polyvalent metal is removed as the sweet water product, and replacement chelated polyvalent metal is added.

Abstract: Method and apparatus for recovering sulfur from an aqueous slurry. The slurry is passed downwardly through a shell-and-tube heat exchanger having vertically arranged tubes, wherein it is heated sufficiently to melt the sulfur. The liquid mixture leaving the heat exchanger is discharged into a first separation zone, in which a phase separation between the lighter aqueous phase and the denser liquid sulfur occurs. The upper aqueous phase is then transported to an intermediate point in the height of a vertically elongated second separation zone, while the molten sulfur is transported from the lower end of the first separation zone to a point adjacent the lower end of said second separation zone, in which an interface between the phases is maintained at a point below the entry point of the aqueous liquid phase into the second separation zone. The aqueous liquid is discharged from the top of the second separation zone, while molten sulfur is discharged from the bottom of said zone.

Abstract: Apparatus for contacting a liquid reaction solution with a gas in separate reaction chambers within a single reaction vessel wherein the liquid reaction solution is continuously circulated between a first reaction chamber and a second reaction chamber within the reaction vessel but providing at least two side-by-side reaction chambers in open flow communication at their upper and lower ends with a gas supply means associated with each said chamber for introducing a gas in a finely divided form into the lower ends of each said chamber, and said gas supply means including flow control means whereby the rate of upward flow of gas in one of the chambers is greater than the rate of upward flow of gas in the other chamber so as to lower the density of the liquid reaction solution in the one chamber and provide continuous upward flow of liquid reaction solution and gas in the one chamber and downward flow of liquid reaction solution countercurrent to the flow of gas in the other chamber.

Abstract: A portable seam tester is provided for testing the seam strength, on the job site, of large sections of flexible sheet material formed by seaming together smaller size panels. The tester has a piston and cylinder mechanism carrying spaced toggle action clamping means adapted to receive and retain folded double-thickness portions of the material at opposite sides of a seam. Pressurized fluid is controllably supplied to the cylinder to force the clamping means away from each other, thereby placing the material in tension so as to impose a predetermined stress on the seam.

Abstract: Reduction of nitrogen oxide emissions from thermal incinerators is accomplished in installations for calcining solid carbonaceous materials such as petroleum coke and anthracite coal. A hot effluent gas stream containing hydrocarbon vapors and entrained carbonaceous solid particles is removed from the calciner, and means are provided to effect preliminary combustion of the hydrocarbon vapors but not the carbonaceous solid particles in the gas stream using substantially the stoichiometric amount of combustion air. The resultant gas that is substantially free of hydrocarbons and oxygen is introduced into the thermal incinerator, and combustion of the carbonaceous solid particles is effected with additional combustion air.