Abstract: A process for the alkylation of isobutane is disclosed wherein isobutane is fed to two separate alkylation systems. The effluent from the first alkylation system is fed to an interim debutanizer where the C4's are separated from the alkylate product. The overhead C4 product is then fed to the second alkylation system to provide the isobutane. The effluent from the second alkylation system is fed to a traditional deisobutanizer to prevent any build up of normal butanes in the system.

Abstract: A process for the conversion of tertiary butyl alcohol to ethyl tertiary butyl ether, including: dehydrating tertiary butyl alcohol to form a product stream comprising isobutylene and water; separating the product stream to form an isobutylene-rich fraction and a water-rich fraction; separating the water-rich fraction to recover a hydrocarbon fraction and a water fraction having less than 1 ppm hydrocarbon content; reacting isobutylene in the isobutylene-rich fraction with ethanol to form a reaction product comprising ethyl tertiary butyl ether; separating the reaction product to recover unreacted ethanol and an ethyl tertiary butyl ether stream; and recycling at least a portion of the unreacted ethanol to the reacting; wherein the ethyl tertiary butyl ether stream comprises at least 99 weight percent ethyl tertiary butyl ether.

Abstract: A process for the production of dialkyl ether, the process including: feeding a stream comprising an alkyl alcohol to a distillation column reactor system; concurrently in the distillation column reactor system: i) contacting the alkyl alcohol with a catalytic distillation structure in a distillation reaction zone thereby catalytically reacting at least a portion of the alkyl alcohol to form a corresponding dialkyl ether and water; and ii) fractionating the resulting dialkyl ether from the water; operating the distillation column reactor system to obtain substantially complete conversion of the alkyl alcohol to form the corresponding dialkyl ether and water; recovering the dialkyl ether from the distillation column reactor as an overheads fraction; recovering the water from the distillation column reactor as a bottoms fraction.

Abstract: A user access control system comprising a workstation coupled to a computer network and operable to receive a request for an authenticated access to the computer network, and to prompt for and receive one or more credentials associated with the request, a gating authentication server coupled to the computer network and operable to receive the one or more credentials and to provide as a gating factor an authenticated credential, and a public key infrastructure server coupled to the computer network and operable to generate private/public key pairs associated with the authenticated credential, wherein the private/public key pairs are either generated after a request for access to the computer system has been received at the workstation and the gating authentication server has authenticated the one or more credentials provided through the workstation, or the private/public key pairs are retrieved from a previously generated virtual smart card based on the authentication credential.

Abstract: A public key authentication system and method for use in a computer system having a plurality of users. The system includes a virtual smart card server, storage connected to the virtual smart card server, and a virtual smart card agent connected to the virtual smart card server. The storage includes a plurality of virtual smart cards, wherein each virtual smart card is associated with a user and wherein each smart card includes a private key. The virtual smart card agent authenticates the user and accesses the authenticated user's virtual smart card to obtain the user's private key.

Abstract: Disclosed is a portable table top mountable on a rail. The portable table top has a planar member defining a top portion and a bottom portion, and a fastening mechanism to removably attach the planar member to the rail. The fastening mechanism comprises a clip and a support member. The clip is securely attached to the bottom portion of the planar member. The clip has a slot for receiving a portion of the rail therein. The support member has a support plate and a securing mechanism. The securing mechanism abuttingly couples a first end of the support plate to the rail and enables a second end of the support plate to support the bottom portion of the planar member.

Abstract: A process for the alkylation of isobutane is disclosed wherein isobutane is fed to two separate alkylation systems. The effluent from the first alkylation system is fed to an interim debutanizer where the C4's are separated from the alkylate product. The overhead C4 product is then fed to the second alkylation system to provide the isobutane. The effluent from the second alkylation system is fed to a traditional deisobutanizer to prevent any build up of normal butanes in the system.

Abstract: A discharge device has i.) a body having a hollow interior; ii.) a liquid inlet; and iii.) a liquid outlet having a first end and a second end. The first end has a button. The liquid outlet has a stem. The liquid outlet has an orifice having an orifice surface area. The valve system has a rib and a valve guide having a valve system surface area. The stem passes through the valve guide. The valve system surface area and the orifice surface area have a ratio of less than about 35%.

Abstract: A discharge device which has a body with a hollow interior. The discharge device has i.) a liquid inlet having liquid inlet surface area and ii.) a liquid outlet wherein the liquid outlet has a hollow interior. The hollow interior has i.) a stem and ii.) a valve guide having a top valve guide, a bottom valve guide, and a valve guide surface area. The stem passes through the valve guide and the bottom of the valve guide is above the liquid inlet.

Abstract: A gravity discharge device for liquids, especially concentrated liquid detergents, comprises a valve guide system whose surface area optimizes liquid flow. The discharge is especially useful with concentrated (“2×”) liquid detergents, whose viscosities tend to unacceptably slow their flow rate from home-use containers, especially when the containers progressively empty after multiple uses.

Abstract: A discharge device having a liquid outlet with a hollow interior. The valve system is located inside the hollow interior of the liquid inlet. The valve guide system has a valve guide and a first rib. The valve guide system has a valve guide having a valve guide width. The valve guide width is at less than about 1.15 mm. The first rib has a first rib width having a first rib width. The width of the first rib is less than about 2.5 mm wide.

Abstract: In one embodiment, a method for handling privileged events in a virtual machine environment includes detecting an occurrence of a privileged event, determining which one of multiple virtual machine monitors (VMMs) is to handle the privileged event, and transitioning control to this VMM.

Abstract: A fabric article treating apparatus for dispensing a benefit composition through a nozzle that directs the benefit composition as droplets or particles into the chamber of the fabric article drying appliance. The droplets or particles provide benefits to the fabric articles within the drying appliance. The treating apparatus includes one or more safety features, and/or it includes beneficial control concepts that enhance the effects of the benefit composition being dispensed through the nozzle.

Abstract: An apparatus and method are provided for sensing infrared radiation. The apparatus includes a sensor element that is positioned in a magnetic field during operation to ensure a ? shaped relationship between specific heat and temperature adjacent the Curie temperature of the ferroelectric material comprising the sensor element. The apparatus is operated by inducing a magnetic field on the ferroelectric material to reduce surface charge on the element during its operation.

Abstract: Acetylenes and dienes in a stream containing hydrogen, methane, C2-C6 olefins and paraffins, C2-C6 acetylenes and dienes, benzene, toluene, xylenes, and other C6+ components are hydrogenated in a downflow boiling point reactor wherein the heat of reaction is absorbed by the liquid in the reactor which produces a vapor. Besides the feed to the reactor there is a recirculating stream which is fed at a rate sufficient to ensure that the catalyst particles within the reactor are wetted. A third stream, which is provided from a second downstream liquid/vapor separator from partially condensed vapor from the first downstream liquid/vapor separator corresponding to the mass evaporated in the reactor, is fed to the reactor. The composition of the third stream controls the steady state composition of the liquid flowing through the reactor.

Abstract: Acetylenes and dienes in a stream containing hydrogen, methane, C2-C6 olefins and paraffins, C2-C6 acetylenes and dienes, benzene, toluene, xylenes, and other C6+ components are hydrogenated in a downflow boiling point reactor wherein the heat of reaction is absorbed by the liquid in the reactor which produces a vapor. Besides the feed to the reactor there is a recirculating stream which is fed at a rate sufficient to ensure that the catalyst particles within the reactor are wetted. A third stream, which is taken from a downstream distillation column, is fed to provide the make up mass corresponding to the mass evaporated in the reactor. The composition of the this third stream controls the steady state composition of the liquid flowing through the reactor.

Abstract: A method and apparatus for applying indicia to a curved surface, including a compound curved surface having multiple axes of curvature. The curved surface is deformed to eliminate one axis of curvature. The invention is usable with hourglass or barrel shaped surfaces, as occur with containers, and to apply labels and other indicia to these surfaces.

Abstract: A process for concurrently fractionating and treating a full range naphtha stream. The full boiling range naphtha stream is first subjected to simultaneous thioetherification and splitting into a light boiling range naphtha, an intermediate boiling range naphtha and a heavy boiling range naphtha. The intermediate boiling range naphtha containing thiophene and thiophene boiling range mercaptans is passed on to a polishing hydrodesulfurization reactor where a low sulfur, low olefin gas oil is concurrently fed to the polishing reactor to insure that a liquid phase is present.