NOVELTY - Recovering and recycling (M1) hydrogen from a reforming process involves: pressurizing at least one hydrogen-rich gas stream (S1) exiting at least one catalyst lock hopper (12) to desired pressure; delivering at least portion of pressurized stream (S1) to at least one predetermined location (22); maintaining desired pressure level of stream (S1) by directing at least portion of pressurized stream to device (30) for regulating desired pressure of gas; and further maintaining desired pressure of stream (S1) by controlling regulating device with a first or feed forward controller (40).    USE - For recovering and recycling of hydrogen from a reforming process (claimed), for recovery of hydrogen from hydrogen-rich gas streams in a continuous catalyst regeneration (CCR) reformer system in the petroleum and chemical refining industries, where hydrogen is used as a raw material in the refining operation.    ADVANTAGE - The process achieves more efficient recovery of hydrogen while maintaining desired stable pressures throughout the continuous catalyst regeneration reforming process in the reformer system. The recovered hydrogen from such systems can be efficiently used at its chemical value rather than being reduced to its fuel value as in the prior art processes. Such improvement is desired in reforming operations in order to retain the benefits of the reforming operations while simultaneously achieving a more efficient overall reforming operation.    DETAILED DESCRIPTION - Recovering and recycling (M1) hydrogen from a reforming process involves: pressurizing at least one hydrogen-rich gas stream (S1) exiting at least one catalyst lock hopper (12) to a desired pressure; delivering at least a portion of the pressurized stream (S1) to at least one predetermined location (22); maintaining at least the pressure of the stream (S1) in a stable condition prior to the pressurized stream is delivered to the predetermined location; maintaining the desired pressure of the stream (S1) by minimizing surges or changes in the stream (S1) exiting the catalyst lock hopper by flowing the gas stream through a surge minimizing device; further maintaining the desired pressure level of the stream (S1) by directing at least a portion of the pressurized stream to a device (30) for regulating the desired pressure of hydrogen-rich gas in the hydrogen recovery process; and further maintaining the desired pressure level of the stream (S1) by controlling the regulating device with a first, or feed forward controller (40) to keep the hydrogen-rich gas stream within previously determined parameters.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a reforming process and system for hydrogen recovery and recycling.    Catalyst lock hopper (12)    Surge drum (16)    Predetermined location (22)    Regulating device (30)    Feed forward controller (40)