초록 ▼

A cyclic adsorption process is provided having pressurization and depressurization steps and driven by one or more centrifugal machines operating under acceleration and deceleration conditions wherein the deceleration rate of the machine is controlled to minimize power consumption and maximize the e

A cyclic adsorption process is provided having pressurization and depressurization steps and driven by one or more centrifugal machines operating under acceleration and deceleration conditions wherein the deceleration rate of the machine is controlled to minimize power consumption and maximize the efficiency of the process. The operating speed of the centrifugal machine during deceleration is matched to the measured ratio pressure conditions so that the centrifugal machine arrives at its minimum operating speed near the point required to begin acceleration.

대표청구항 ▼

1. In a cyclic adsorption process comprising: at least one adsorber vessel containing at least one adsorber bed undergoing the steps of pressurization and depressurization and driven by at least one centrifugal machine,the centrifugal machine undergoing the steps of acceleration and deceleration in

1. In a cyclic adsorption process comprising: at least one adsorber vessel containing at least one adsorber bed undergoing the steps of pressurization and depressurization and driven by at least one centrifugal machine,the centrifugal machine undergoing the steps of acceleration and deceleration in accordance with the requirements of the cyclic adsorption process, anda controller for receiving data signals for the process conditions and sending instructions to the centrifugal machine in response to the conditions;the improvement comprising measuring the pressure ratio conditions during deceleration and matching the deceleration rate of the centrifugal machine to the decreasing pressure ratio conditions during deceleration so that the centrifugal machine arrives at its minimum operating speed near the point required to begin acceleration. 2. The process of claim 1 wherein the centrifugal machine accelerates along its best efficiency line. 3. The process of claim 1 wherein the operating speed of the centrifugal machine during deceleration is maintained at a value above the minimum speed permitted by the requirements of the process for a time of less than eight (8) percent of the total cycle time. 4. The process of claim 3 wherein the process is a PSA, VSA, or VPSA process and the time of less than, eight (8) percent of the total cycle time is less than 3 seconds. 5. The process of claim 1 wherein the deceleration rate of the centrifugal machine is matched with the decreasing pressure ratio conditions by the controller; receiving data signals indicating the pressure ratio conditions during deceleration,comparing the decreasing pressure ratio conditions to the deceleration rate of the centrifugal machine, andcommunicating to the centrifugal machine in response to the decreasing pressure ratio conditions, instructions to a control system which matches the deceleration rate to the decreasing pressure ratio conditions so that the centrifugal machine reaches the final deceleration point at the same time as the point required to begin acceleration. 6. The process of claim 5 wherein the control system is one or more flow control valves which can be operated to control the mass flow of the process gas as required to reduce the deceleration rate of the centrifugal machine. 7. The process of claim 6 wherein the flow control valves are operated by the controller which receives data signals indicating pressure ratio conditions in the system and communicates instructions to the valves in response to the pressure ratio conditions thereby controlling the deceleration rate to reach the final deceleration point near the point required to begin acceleration. 8. The process of claim 7 wherein the deceleration rate is matched to the pressures ratio conditions so that the idle time is less than eight (8) percent of the total cycle time. 9. The process of claim 1 wherein the process is a VPSA, VSA, or PSA process. 10. The process of claim 9 wherein the process is a VPSA process for the separation of oxygen from air. 11. A cyclic adsorption process comprising (i) pressurizing a feed gas and passing the feed gas through an adsorbent bed which adsorbs at least one readily adsorbed gas while passing through at least one less adsorbed gas as a product gas and (ii) depressurizing the adsorbent bed containing the at least one more readily adsorbed gas to desorb the adsorbed gas from the adsorbent bed; wherein the process further comprises: passing the feed gas or the product gas through at least one centrifugal machine for the pressurization and depressurization steps, the at least one centrifugal machine undergoing acceleration and deceleration conditions,measuring the pressure ratio conditions during the deceleration conditions and sending a signal to a controller for receiving data signals with the pressure ratio conditions data,having the controller convert the data signals to instructions using a predetermined algorithm designed to instruct the centrifugal machine to arrive at the minimum operating speed at the point required to begin acceleration along the best efficiency line, andsending the instructions from the controller to at least one flow control valve which moves in response to the instructions to move to adjust the mass flow of the adsorbed gas to vary the rate of deceleration of the centrifugal machine so as to obtain its lowest operating speed at the point required to begin acceleration. 12. The process of claim 11 wherein the flow control valve closes to reduce the mass flow of the process gas to slow the rate of deceleration of the centrifugal machine. 13. The process of claim 11 wherein the rate of deceleration of the centrifugal machine is reduced to obtain the centrifugal machine's lowest operating speed within 1 seconds of obtaining the minimum pressure ratio across the machine. 14. The process of claim 11 wherein the centrifugal machine obtains its lowest operating speed at substantially the same point in time as the minimum pressure ratio is achieved. 15. The process of claim 11 wherein the cyclic adsorption process is the production of oxygen from air. 16. The process of claim 14 wherein the process is a VPSA process. 17. In a cyclic adsorption process for separating air comprising: at least one adsorber vessel containing at least one adsorber bed undergoing the steps of pressurization and depressurization and driven by at least one centrifugal machine, the centrifugal machine undergoing the steps of acceleration and deceleration in accordance with the requirements of the cyclic adsorption process, anda controller for receiving data signals for the process conditions and sending instructions in response to the conditions; andwherein the adsorber bed is pressurized to a desired pressure and nitrogen is readily adsorbed by the adsorbent as the feed air is passed across the bed; oxygen is produced as the nitrogen in the feed air is adsorbed; and nitrogen is desorbed from the adsorbent in the adsorber bed;the improvement comprising using a control system to control the deceleration rate of the centrifugal machine in response to decreasing pressure ratio process conditions occurring during deceleration so that the centrifugal machine arrives at its minimum operating speed near the point required to begin acceleration. 18. The process of claim 17 wherein the data signals about the process conditions include pressure ratio conditions measured during deceleration by a pressure measuring device. 19. The process of claim 17 wherein the control system is selected from the group consisting of a dynamic braking system, a regenerative braking system and an aerodynamic braking system. 20. The process of claim 19 wherein the control system is an aerodynamic braking system. 21. The process of claim 20 wherein the control system comprises one or more flow control valves operated on response to instructions from the controller to control the mass flow of the process gases. 22. The process of claim 20 wherein the one or more flow control valves increase or decrease the feed gas mass flow to the centrifugal machine upon instructions received from the controller. 23. The process of claim 17 wherein the power to the centrifugal machine is disengaged during deceleration and reengaged at the point required to begin acceleration along its best efficiency line.