Method for controlling gas generation

Abstract

A method is disclosed for controlling the generation of gas occurring in a generator via a filtering membrane (M). The filtering membrane (M) is fed at the entry with a gas pushed by a compressor (C), and is capable of separating gaseous components of the gas at the exit. The method has the steps of detecting the gas pressure at a detection point (SP1) at the membrane entry and/or at the exit (M); adjusting the regime of the compressor (C) so that the detected pressure is maintained at a reference pressure, here called Pref]. Advantages: less wear out for the compressor and extended life cycle.

Claims

1. A method for controlling the generation of nitrogen or oxygen occurring in a generator by filtering a gas via a filtering membrane, the filtering membrane having an entry and an exit, the filtering membrane being fed at the entry with the gas pushed by a compressor running with a regimen and being capable of separating gaseous components of the gas at the exit, the gas being ambient air, the method comprising the steps of: detecting the gas pressure at a detection point (SP1) at the entry of the filtering membrane and/or at the exit of the filtering membrane; and adjusting the regimen of the compressor so that the detected pressure is maintained at a reference pressure, wherein the gas pressure is also detected at the exit of the filtering membrane downstream of the detection point and the gas pressure is regulated downstream of the detection point at a pressure value which is smaller than the reference pressure.

2. The method according to claim 1, wherein the filtering membrane consists of a pack of parallel tubes along which the gas at the entry of the filtering membrane is made to flow.

3. The method according to claim 1, wherein a value of the reference pressure is calculated or adjusted to determine a degree of purity of the gas exiting the filtering membrane, and the pressure value is calculated or adjusted to obtain a desired pressure of the gas delivered by the generator.

4. The method according to claim 1, wherein the gas flow-rate is measured at the exit of the filtering membrane and, depending on the measured flow-rate, the pressure of the gas entering the filtering membrane or the regiment of the compressor is adjusted.

5. The method according to claim 1, wherein the filtering membrane is fed with a gas flow-rate higher than required at an exit of the generator and a gas excess is accumulated in a tank.

6. A gas generator comprising: a filtering membrane having an entry and an exit, the filtering membrane capable of separating at the exit gaseous components of a gas at the entry, the gas being ambient air and the components of the gas being nitrogen or oxygen; a compressor running with a regimen and operative to feed the entry of the filtering membrane with a gas flow; a first pressure sensor for detecting the gas pressure at a detection point at the entry and/or the exit of the filtering membrane; an electronic circuit connected to the first sensor and to the compressor to regulate the regimen of the compressor so that the pressure detected by the first sensor is maintained at a reference pressure; a second sensor of gas pressure at the exit of the filtering membrane, located downstream of the first pressure sensor and connected to the electronic circuit; and a pressure regulator element located downstream of the second pressure sensor and connected to the electronic circuit, the electronic circuit being configured to monitor the second sensor and to drive the regulator element so that the pressure of the gas downstream of the second sensor is maintained at a pressure value which is lower than reference pressure.

7. The gas generator according to claim 6, wherein the compressor comprises: a motor, and a power inverter, through which the electronic circuit can control the regimen of the compressor.

8. The gas generator according to claim 6, further comprising: a tank for accumulating an excess of gas at the exit of the filtering membrane, and the electronic circuit is configured to supply the filtering membrane with a gas flow-rate greater than that required by an exit of the generator so as to generate an excess of gas to be stored in the tank.

9. The method according to claim 3, wherein the gas flow-rate is measured at the exit of the filtering membrane and, depending on the measured flow-rate, the pressure of the gas entering the filtering membrane or the regimen of the compressor is adjusted.

10. The method according to claim 1, wherein the gas pressure is regulated downstream of the detection point at a pressure value that is lower than the reference pressure by controlling a valve inserted in the path of the gas.

11. The method according to claim 3, wherein the gas pressure is regulated downstream of the detection point at a pressure value that is lower than the reference pressure by controlling a valve inserted in the path of the gas.

12. The method according to claim 4, wherein the gas pressure is regulated downstream of the detection point at a pressure value that is lower than the reference pressure by controlling a valve inserted in the path of the gas.

13. The method according to claim 9, wherein the gas pressure is regulated downstream of the detection point at a pressure value that is lower than the reference pressure by controlling a valve inserted in the path of the gas.

14. The gas generator according to claim 6, wherein the compressor is a scroll compressor.

15. The gas generator according to claim 6, wherein the pressure regulator element comprises or consists of a valve inserted into the gas path.

16. The gas generator according to claim 6, wherein the electronic circuit is configured to calculate or adjust the reference pressure to determine a purity level of the gas at the exit of the filtering membrane, and calculate or adjust the pressure value to get a desired gas pressure delivered by the generator.

17. The gas generator according to claim 6, further comprising a gas flow rate meter at the exit of the filtering membrane and the electronic circuit is configured for adjusting, depending on the measured flow rate, the regimen of the compressor and/or the gas pressure at the entry of the filtering membrane.

Description

(1) The advantages of the invention will be clearer from the following description of a preferred embodiment of a gas generator, with reference to the attached drawing in which

(2) FIG. 1 shows a diagram of a gas generator apparatus,

(3) FIG. 2 shows a variation of the scheme for the gas generator apparatus.

(4) In the figures equal numbers indicate equal parts, and in order not to crowd the drawings some parts are not marked by numbers.

(5) An apparatus MC for generating at its exit O nitrogen gas (N2) from atmospheric air is shown in FIG. 1.

(6) The apparatus MC comprises a filtering membrane M which is fed at the entry with ambient air pushed by a compressor C. The open arrows indicate a gas flow.

(7) The membrane M separates at the exit the gaseous nitrogen from the other gaseous components, which get dispersed into the environment.

(8) A pressure sensor—respectively SP1. SP1b—is arranged at the entry and/or exit of the membrane M to detect the gas pressure at the entry and/or exit of membrane M.

(9) Downstream of the sensor SP1b there is

(10) an (optional) flow sensor SF, to detect the gas flow rate exiting from membrane M, and

(11) followed by a valve V, e.g. a proportional valve.

(12) Downstream of the proportional valve V there is a pressure sensor SP2 to detect the pressure of the gas delivered at the exit O.

(13) The sensors SP1, SP1b, SP2, SF, and the V valve are mounted in series on the duct that carries the filtered gas from the membrane exit M to the exit O.

(14) An electronic control unit U is connected to the sensors SP1, SP1b, SP2, SF to read the measured values thereof, and is connected to the valve V and to the compressor C for controlling their functioning. Signal lines are indicated by solid arrows whose direction indicates the direction of the signals.

(15) Preferably the electronic control unit U is also connected to a user interface D, such as a display and/or a touch-screen. With the user interface D the operator can program the electronic control unit U to set the flow rate (pressure) of the gas exiting the generator MC and the purity of the generated gas.

(16) According to a preferred variant, the electronic control unit U detects the value of the pressure detected by the sensors SP1 and/or SP1b, and regulates the regimen of the compressor C so as to keep such value at a reference value (called Pref1).

(17) In this way the pressure Pref1 with which the membrane M is supplied is constant or almost constant, and coincides with the working pressure of the compressor.

(18) Given that Pref1 is the minimum value (without ripple) between those which guarantee the functioning of the membrane M at a certain pressure, the compressor C works at an optimal regimen, that is, the one that causes it to wear out less remaining the working pressure on the membrane M the same.

(19) According to a second preferred variant, alternative or combinable with the first variant, the electronic control unit U detects the pressure value detected by the sensor SP2 and adjusts the valve V to maintain such detected value at a reference value, called Pref2, which is lower than Pref1.

(20) In this way, the pressure Pref2 at which the gas is delivered at the exit of the generator MC is constant or almost constant.

(21) By combining the two variants an advantageous and more sophisticated control can be implemented, by setting different values for Pref1 and Pref2, .i.e. Pref1>Pref2.

(22) Through the value Pref1 one can adjust the purity of the gas coming out from the membrane M, because such purity depends approximately proportionally on the working pressure of membrane M. Through the value Pref2 one can adjust the gas pressure exiting the apparatus MC. It is Pref1>Pref2 because this is the condition for raising the purity of the gas generated at the exit O while keeping the set value Pref2 the same.

(23) Further, for any desired purity value at the exit O, the compressor C works at the minimum regimen which guarantees such purity, with the advantages said before of longevity and lower consumption.

(24) Preferably the regulation of the control unit U occurs by means of a feedback control.

(25) The flow sensor SF allows an advantageous variant of operation.

(26) The control unit U is programmed

(27) to detect, by means of the sensor SF, the gas flow rate at the exit of the membrane M and, depending on the measured flow rate,

(28) to adjust the gas pressure Pref1 at the entry and/or exit of the membrane M by adjusting the regimen of compressor C (in this way, the efficiency of membrane M, which has zero efficiency at low flow rates, is maximized. Instead, a pressure value can be set at the entry of the membrane M that guarantees a certain efficiency), and/or

(29) turn off the compressor C if the detected flow is zero or almost zero, not to waste energy.

(30) The apparatus MC2 shows, in relation to the apparatus MC, some more components, to be used alone or in any combination.

(31) There is a non-return valve VR at the exit of membrane M, to avoid backflow or back pressure.

(32) There is an optional tank T1 downstream of the valve VR, useful for nitrogen accumulation when the required output flow is lower than a certain threshold that would cause the membrane—and consequently the whole generator—to work at low energy efficiency. In this case, the control unit U is programmed to control the compressor C in order to increase the pressure inside the membrane M, e.g. with predefined thresholds, to accumulate the gas into the tank T1. while the proportional valve V is controlled by the control unit U to maintain constant pressure at exit O. Once a sufficient quantity of gas is accumulated in the tank T1, the control unit U turns off the compressor C and turns it on again once the pressure in the tank T1 falls below a threshold (for this purpose the control unit U for example monitors a pressure sensor that measures the pressure inside the tank T1).

(33) There is an optional tank T2 in parallel with the exit O, which is used for storing an excess of filtered gas when, to maximize efficiency, the membrane M works at a flow rate greater than what is delivered at the exit O. When the tank T2 is full the control unit U e.g. is programmed to switch off the compressor C, to save energy, until the tank T2, delivering gas to the exit O, is empty or no longer has sufficient pressure.

(34) Preferably the control unit U comprises a programmed microprocessor to perform the described functions. The control unit U can also be built only with discrete components to carry out the operating logic.