Adsorbent fractionators with electronic sequence timer cycle control and process

Claim 2

A gas fractionating apparatus comprising as the essential components at least one sorbent bed adapted for alternate periodic stagewise cyclic adsorption and regeneration; at least one solenoid valve movable between positions permitting and closing off the gas flow through the bed or beds during the stages of the adsorption and regeneration cycle; a driver for the solenoid valve; and an electronic sequence timer that times the cycling of the bed for adsorption and regeneration in a series of fixed time intervals that are the same for each cycle in sequence and are determined electronically and comprise, in combination, digital integrated circuitry including a time delay oscillator generating electric impulses at selected time intervals; a binary counter receiving and counting the electric pulses from the oscillator and storing information therein in multiples of the time intervals; and a logic module having a plurality of logic gates interpreting and responding to selected output combinations from the counter corresponding to desired fixed time intervals for the stages of the adsorption and regeneration cycle of the gas fractionating apparatus, the logic module being in operative connection with the driver for the solenoid valve, and controlling the gas flow through the adsorbent gas fractionator system according to said electronically determined fixed cycling time intervals.

Claim 3

A gas fractionating apparatus according to claim 1 in which the sorbent is a desiccant.

Claim 4

A gas fractionating apparatus according to claim 1 comprising a pair of sorbent beds, disposed in separate vessels, and interconnected for alternating reception of influent gas to be fractionated, and delivery of effluent fractionated gas, and for alternating regeneration.

Claim 5

An apparatus according to claim 3 comprising a means for reducing pressure in the sorbent bed during regeneration.

Claim 6

An apparatus according to claim 3 comprising valve means for cycling the flow of influent gas between the beds and for receiving the flow of effluent gas therefrom.

Claim 7

An apparatus according to claim 3 comprising valve means for diverting a portion of the dried effluent gas as purge through the bed being regenerated.

Claim 8

An apparatus according to claim 6 in which the purge flow is in counterflow.

Claim 9

An apparatus according to claim 1 in which the timer is set for a fixed cycling time at which under the operating conditions the concentration front has not broken out of the bed.

Claim 10

An apparatus according to claim 1 in which the time delay oscillator generates electric impulses at selected short time intervals.

Claim 11

An apparatus according to claim 9 in which the oscillator is a self-excited electronic circuit whose output is a periodic function of time.

Claim 12

An apparatus according to claim 9 in which the timer oscillator utilizes a self-triggering free-running multivibrator circuit having an external capacitor that charges through one set of resistors, and discharges through another set, so that the timing interval can be varied within a desired range by varying the impedance of these two sets of resistors or the capacitance of the external capacitor.

Claim 13

An apparatus according to claim 1 in which the binary digital counter comprises a plurality of stages which in combination store information on the number of pulses at multiples of the time intervals.

Claim 14

An aparatus according to claim 12 in which each counter stage is a static master-slave flip-flop, and the counter is advanced one count on the negative going transition of each input pulse.

Claim 15

An apparatus according to claim 1 in which the binary counter is a ripple-carry binary digital counter having ripple-carry counter stages that multiply the timing interval from one stage to the next.

Claim 16

A process for reducing the concentration of one or more first gases in a mixture thereof with a second gas to below a limiting maximum concentration thereof in the second gas, by passing the mixture in contact with and from one end to another end of one of two beds of a sorbent having a preferential affinity for the first gas, adsorbing first gas thereon to form a gaseous effluent having a concentration thereof below the maximum, and forming a concentration gradient of first gas in the bed progressively decreasing from one end to the other end as the adsorption continues and an increasing concentration of first gas in the bed defining a concentration front progressively advancing in the bed from the one end to the other end as sorbent capacity therefor decreases; and then while passing a purge flow of gaseous effluent through the other of the two beds of sorbent to desorb first gas adsorbed thereon, and reverse the advance of the concentration front of first gas in the bed, regenerating the other bed for another cycle of adsorption; periodically interchanging the beds so that alternately one bed is on regeneration and the other on the adsorption portions of the cycle; timing the cycling in fixed timing intervals that are the same for each cycle in sequence and are determined electronically by a combination of digital integrated circuitry including a time delay oscillator generating electric impulses at selected time intervals; a binary counter receiving and counting the electric pulses from the oscillator and storing information therein in multiples of the time intervals; and a logic module having a plurality of logic gates interpreting and responding to selected output combinations from the counter corresponding to desired fixed time intervals for the stages of the adsorption and regeneration cycle of the gas fractionating apparatus, and controlling cycling time at a period not shorter than the regeneration time; and switching the sorbent beds at the end of such cycling time.

Claim 17

A process for reducing the concentration of one or more first gases in a mixture thereof with a second gas to below a limiting maximum concentration thereof in the second gas, by passing the mixture in contact with and from one end to another end of one of two beds of a sorbent having a preferential affinity for the first gas, adsorbing first gas thereon to form a gaseous effluent having a concentration thereof below the maximum, and forming a concentration gradient of first gas in the bed progressively decreasing from one end to the other end as the adsorption continues and an increasing concentration of first gas in the bed defining a concentration front progressively advancing in the bed from the one end to the other end as sorbent capacity therefor decreases; and then while passing a purge flow of gaseous effluent through the other of the two beds of sorbent to desorb first gas adsorbed thereon, and reverse the advance of the concentration front of first gas in the bed, regenerating the other bed for another cycle of adsorption; periodically interchanging the beds so that alternately one bed is on regeneration and the other on the adsorption portions of the cycle; timing the cycling in fixed timing intervals that are the same for each cycle in sequence and are determined electronically by a combination of digital integrated circuitry including a time delay oscillator generating electric impulses at selected time intervals; a binary counter receiving and counting the electric pulses from the oscillator and storing information therein in multiples of the time intervals; and a logic module having a plurality of logic gates interpreting and responding to selected output combinations from the counter corresponding to desired fixed time intervals for the stages of the adsorption and regeneration cycle of the gas fractionating apparatus, and controlling cycling time at a period not shorter than the regeneration time; and switching the sorbent beds at the end of such cycling time.

Claim 18

A process in accordance with claim 15 in which the first gas is water vapor.

Claim 19

A process in accordance with claim 15 in which the sorbent is silica gel.

Claim 20

A process in accordance with claim 15 wherein the purge flow is of effluent gas from the bed sorbing the first gas.

Claim 21

A process in accordance with claim 15 which comprises removing sorbed gas at a reduced pressure relative to the pressure of adsorption.