Abstract: A method for controlling an operation of an industrial machine that includes authenticating control commands remotely issued by command issuers through a network. The control commands each describe a modifying action to the operation of the industrial machine. The method includes: providing a jump host as a communication buffer between a unit controller of the industrial machine and the network; maintaining within a memory of the jump host whitelisted commands, the whitelisted commands including a list of the approved control commands; receiving, at the jump host, a first control command via the network; determining, at the jump host, whether the first control command is contained within the whitelisted commands; in response to an affirmative determination that the first control command is contained within the whitelisted commands, deeming the first control command as being authenticated; and transmitting the first control command to the unit controller of the industrial machine.

Abstract: A method for controlling an operation of an industrial machine that includes authenticating control commands remotely issued by command issuers through a network. The control commands each describe a modifying action to the operation of the industrial machine. The method includes: providing a jump host as a communication buffer between a unit controller of the industrial machine and the network; maintaining within a memory of the jump host whitelisted commands, the whitelisted commands including a list of the approved control commands; receiving, at the jump host, a first control command via the network; determining, at the jump host, whether the first control command is contained within the whitelisted commands; in response to an affirmative determination that the first control command is contained within the whitelisted commands, deeming the first control command as being authenticated; and transmitting the first control command to the unit controller of the industrial machine.

Abstract: A process for the selective hydrogenation of dienes and acetylenes in a mixed hydrocarbon stream from a pyrolysis steam cracker in which a front end a one step acetylene hydrogenation is carried out using catalyst comprising (A) 1 to 30 wt. % based on the total weight of the catalyst of a catalytic component of nickel only or nickel and one or more elements selected from the group consisting of copper, rhenium, palladium, zinc, gold, silver, magnesium, molybdenum, calcium and bismuth deposited on (B) a support having the a BET surface area of from 1 to about 100 m2/gram, total nitrogen pore volume of from 0.2 to about 0.9 cc/gram and an average pore diameter of from about 110 to 450 ? under conditions of temperature and pressure to selectively hydrogenate acetylenes and dienes. The process hydrogenates the dienes and acetylenes to olefins without loss of ethylene and propylene in the light and heavy products which eliminates the need for further processing of the heavier stream.

Abstract: Improved Ni catalysts for hydrogenation reactions are disclosed. The catalysts are useful for hydrogenation such as selective hydrogenation of acetylenic impurities in crude olefin and diolefin streams. The catalysts are prepared by depositing nickel on a porous support which has the following specific physical properties; BET surface area of from 30 to about 100 m2/g, total nitrogen pore volume of from 0.4 to about 0.9 cc/g, and an average pore diameter of from about 110 to 450 ? with or without modifiers of one or more elements selected from the group consisting of Cu, Re, Pd, Zn, Mg, Mo, Ca and Bi.

Abstract: Improved Ni catalysts for hydrogenation reactions are disclosed. The catalysts are useful for hydrogenation such as selective hydrogenation of acetylenic impurities in crude olefin and diolefin streams. The catalysts are prepared by depositing nickel on a porous support which has the following specific physical properties; BET surface area of from 30 to about 100 m2/g, total nitrogen pore volume of from 0.4 to about 0.9 cc/g, and an average pore diameter of from about 110 to 450 ? with or without modifiers of one or more elements selected from the group consisting of Cu, Re, Pd, Zn, Mg, Mo, Ca and Bi.

Abstract: Improved Ni catalysts for hydrogenation reactions are disclosed. The catalysts are useful for hydrogenation such as selective hydrogenation of acetylenic impurities in crude olefin and diolefin streams. The catalysts are prepared by depositing nickel on a porous support which has the following specific physical properties; BET surface area of from 30 to about 100 m2/g, total nitrogen pore volume of from 0.4 to about 0.9 cc/g, and an average pore diameter of from about 110 to 450 ? with or without modifiers of one or more elements selected from the group consisting of Cu, Re, Pd, Zn, Mg, Mo, Ca and Bi.