Low humidity generator

Abstract

The embodied invention is a low humidity generator which encapsulates essential piping, pressure regulator, flow regulator, and saturator in a sealed vacuum chamber. Additionally, a Stirling piston type cooler is used to cool the saturator. This eliminates atmospheric water vapor permeation and the need for thermal insulation surrounding the piping and control units. Also, the humidity generator has improved cool down characteristics, improved thermal control, and better maintenance access.

Claims

1. A humidity generator for a low dewpoint gas comprising: A. a vacuum chamber, wherein: i. a saturator, ii. a saturator pressure control valve connected to said saturator, and iii. an exit flow control valve connected to said saturator, are located within said vacuum chamber, B. a vacuum pump connected to said vacuum chamber, C. a Stirling cooler thermally connected to an upper surface or a lower surface of said saturator, and D. whereby said vacuum chamber provides thermal isolation for said saturator, E. connections for said pressure control valve and for said exit flow control valve are prevented from permeation of water into an exit gas stream.

2. The humidity generator according to claim 1, additionally comprising: A. a temperature PID control loop connected to: i. a temperature sensor located in said saturator, and ii. said Stirling cooler, B. a pressure PID control loop connected to said saturator pressure control valve, and C. a flow PID control loop connected to said exit flow control valve.

3. The humidity generator according to claim 2, wherein said saturator is connected to: A. a saturator pressure transmitter, and B. an exit pressure transmitter.

4. The humidity generator according to claim 2, wherein a blocking valve is connected between said exit pressure transmitter and said saturator.

5. The humidity generator according to claim 4, additionally comprising: A. a gas inlet connected to a shutoff valve, and B. said shutoff valve is connected to said saturator pressure control valve.

6. The humidity generator according to claim 5, additionally comprising: A. a nitrogen gas supply connected to said inlet gas connection, or B. a compressed gas supply connected to said inlet gas connection.

7. The humidity generator according to claim 6, additionally comprising a three-way solenoid valve connected to: A. a top connection to said saturator, B. a bottom connection to said saturator, and C. said saturator pressure control valve.

8. The humidity generator according to claim 7, additionally comprising a second exit flow control valve connected to said saturator.

9. The humidity generator according to claim 8, wherein said saturator comprises an assembly of multiple stacked plates.

10. The humidity generator according to claim 1, wherein a heating element that is thermally connected to: A. said Stirling cooler, B. said upper surface of said saturator, C. said lower surface of said saturator, D. said Stirling cooler and said upper surface of said saturator, or E. said Stirling cooler and said lower surface of said saturator.

11. A method of generating a low dewpoint gas in a humidity generator comprising: A. providing: a. a vacuum chamber, wherein: i. a saturator, ii. a saturator pressure control valve connected to said saturator, and iii. an exit flow control valve connected to said saturator, are located within said vacuum chamber, b. a vacuum pump connected to said vacuum chamber, c. a Stirling cooler in contact with an upper surface or a lower surface of said saturator, d. a temperature PID control loop connected to: i. a temperature sensor located in said saturator, and ii. said Stirling cooler, e. a pressure PID control loop connected to said saturator pressure control valve, f. a flow PID control loop connected to said exit flow control valve, and B. prefilling said saturator with distilled water at atmospheric pressure, C. operating said vacuum pump to create a predetermined vacuum in said vacuum chamber, D. connecting a supply gas to a gas inlet connected to said humidity generator, and E. operating: a. said temperature PID control loop, b. said pressure PID control loop, and c. said flow PID control loop, according to predetermined setpoints, and F. whereby an exit gas is generated with a dewpoint between 90° C. and 10° C.

12. The humidity generator according to claim 11, wherein said saturator is connected to: A. a saturator pressure transmitter, and B. an exit pressure transmitter.

13. The humidity generator according to claim 12, wherein a blocking valve is connected between said exit pressure transmitter and said saturator.

14. The humidity generator according to claim 13, additionally comprising: A. a gas inlet connected to a shutoff valve, and B. said shutoff valve is connected to said saturator pressure control valve.

15. The humidity generator according to claim 14, additionally comprising: A. a nitrogen gas supply connected to said inlet gas connection, or B. a compressed gas supply connected to said inlet gas connection.

16. The humidity generator according to claim 15, additionally comprising a three-way solenoid valve connected to: A. a top connection to said saturator, B. a bottom connection to said saturator, and C. said saturator pressure control valve.

17. The humidity generator according to claim 16, additionally comprising a second exit flow control valve connected to said saturator.

18. The humidity generator according to claim 17, wherein said saturator comprises an assembly of multiple stacked plates.

19. The humidity generator according to claim 11, wherein a heating element thermally connected to: A. said Stirling cooler, B. said upper surface of said saturator, C. said lower surface of said saturator, D. said Stirling cooler and said upper surface of said saturator, or E. said Stirling cooler and said lower surface of said saturator.

Description

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWING(S)

(1) FIG. 1 shows a perspective view of the assembled humidity generator.

(2) FIG. 2 shows a right side profile of FIG. 1.

(3) FIG. 3 shows an exploded view of FIG. 1 to better see the humidity generator assembly.

(4) FIG. 4 is a detailed exploded view of FIG. 3 to better see the vacuum chamber assembly.

(5) FIG. 5 shows a perspective view of the gas pressure-control sub assembly, with arrows indicating the direction of gas flow during a normal (generator) operation.

(6) FIG. 6 shows a perspective view of the gas pressure-control sub assembly, with arrows indicating the direction of gas flow during a purge operation.

(7) FIG. 7 shows a Process and Instrumentation Diagram schematic of the humidity generator.

(8) FIG. 8 shows an electrical schematic of the saturator temperature interface to the main controller board.

(9) FIG. 9 shows an electrical power schematic of the vacuum pump and the Stirling cooler.

(10) FIG. 10 shows the main controller board interface with sensors, valve solenoids, valve controllers, a vacuum pump, and a user interface.

DETAILED DESCRIPTION OF THE INVENTION

(11) The text ‘humidity generator’ means a complete unit that receives an input gas (or carrier gas), adding a specific amount of water vapor to the input gas, and provides an exit gas flow at a designated moisture content. The text ‘humidity saturator’ or ‘saturator’ refers to a thermally controlled stacked plate unit that allows the input gas to admix with water vapor. (Note that the terms ‘humidity’, ‘moisture’, ‘dew point’, ‘frost point’, ‘water vapor’, and ‘water vapor partial pressure’ are used synonymously within the context of this document. While they may exhibit differing numeric values, they are all directly proportional and mathematically convertible to one another. They are alternate terms for expressing the concept of water vapor admixed with a carrier gas.)

(12) The embodied humidity generator follows an overall design based on NIST two pressure and two temperature principles. Utilizing these principles, a stream of gas at an elevated pressure is saturated with respect to the liquid or solid phase of water at a given saturation temperature. Here, saturation temperature is the major determining factor for the quantity of water vapor admixed with the carrier gas. Pressure within the saturator is the major determining factor for the carrier gas quantity of the mixture. The humidified gas stream is then expanded to a lower pressure and warmed to an alternate temperature. Measurements of the pressure and temperature within the saturator, and the pressure and temperature following expansion (generally at the DUT), are all that is required to determine the resulting humidity content of the gas stream.

(13) The electronic controls provide for automatic humidity generation based on desired humidity setpoints. The operator adjusts the desired exit flow rate setpoint and the desired dew point in the exit gas. The embedded computer control provides the computations needed to create the saturator temperature and saturator pressure PID control setpoints to achieve the desired gas dewpoint and flow rate. Through the use of appropriate mathematical algorithms within custom software programming, automated setpoint determination is employed to achieve and maintain any humidity value desired within the range of capability of the humidity generator. Although automatically determined by the computer, the operator may over-ride specific setpoints of temperature and pressure, allowing for customized testing functionality. The operator also has full control over the exit flow rate setpoint. While not controlled, both the temperature and pressure of the gas stream at the DUT are monitored, and appropriate adjustments are made to ensure the setpoints of saturator temperature and pressure are adjusted accordingly to maintain steady humidity control at the DUT.

(14) The embodied humidity generator has a very small footprint due to the compact FPSC Stirling cooler unit utilized for saturator cooling. A typical outlet temperature range needed from the Stirling cooler is +10° C. to as low as −90° C.

(15) Uncertainty of the pressure measurements plays an important role in the accuracy of generated humidity. The humidity in the outlet stream is based on the absolute outlet pressure and also on the ratio of saturator to outlet (DUT) pressure.

(16) The saturator input pressure is maintained to the desired value by the pressure controller. As there may be a slight pressure drop as the gas passes through the saturator, the saturator pressure used within humidity computations is measured by a pressure sensor nearest the saturator exhaust. Differences between the controlled saturator inlet pressure and the resulting saturator outlet pressure may be used to adjust the saturator inlet pressure setpoint to compensated for the pressure drop. This ensures the saturator pressure nearest the saturator outlet reaches desired saturator pressure setpoint.

(17) Uncertainty of the saturator temperature measurement is very important to the humidity in the exit gas stream. All generated humidity parameters such as dew point and frost point temperature are dependent on saturator temperature, while other values such as percent Relative Humidity are also dependent on temperature of the gas at the DUT. In the case where both the saturator and DUT temperatures are required, uncertainty of both temperatures must be considered.

(18) Saturator temperature is maintained by control of the Stirling cooler thermally connected to (i.e. in contact directly or indirectly) to either the upper or lower plates of the saturator, and by heaters thermally connected to the Stirling cooler or the upper and lower surfaces of the saturator, or both. In general, heating and cooling of the saturator is done by conduction from either the upper or the lower surface of the saturator.

(19) The humidity generator can generate any humidity level within the capabilities of the pressure and temperature ranges of the system.

(20) The exit gas is useful for calibration purposes in a wide variety of industries for:

(21) 1. Chilled Mirror Hygrometers.

(22) 2. Humidity Sensors and Electrolytic Hygrometers.

(23) 3. Environmental testing for various humidity sensors.

(24) 4. R&D humidity sensors.

(25) The equipment is used in industries that include aerospace, farming, medical, research and development, pharmacy, plastics industry, and others.

(26) The embodied invention is generally useful to control a low amount of humidity in dry nitrogen or compressed air. However, other gases could also be used.

(27) FIGS. 1-6 show different views of the humidity generator assembly. The items shown in FIGS. 1-6 are:

(28) TABLE-US-00001  1 Humidity Generator Support Frame  2a Top Free Piston Stirling Cooler  2b Alternate Bottom Free Piston Stirling Cooler  3 Vacuum Chamber  4 Saturator (Plate Stack Assembly)  5 Saturator Pressure Controller Valve  6 Saturator Exit Gas Flow Controller Valve  7 Vacuum pump  8 Vacuum chamber wall  9 Top Vacuum Flange Part A 10 Top Vacuum Flange Part B 11 Bottom Vacuum Flange 12 Flow-generator & Purge - 3 Way Valve 13 Nitrogen Inlet Pressure Regulator 14 Purge outlet valve 15 Entry On-off Valve 16a, b Optional Heaters

(29) FIG. 1 is an isometric view of the humidity generator, showing a vacuum chamber 3 that encloses the saturator 4, the saturator pressure controller valve 5, the flow-purge three-way valve 12, and the exit gas flow control valve 6. These components are surrounded by a vacuum in the vacuum chamber and have O rings, gaskets, or connections that are subject to permeation. Also, the enclosed components transfer less heat when in the vacuum chamber and provide better temperature control. Only modest vacuum level i.e. 1E-4 hPa or lower is required.

(30) A gas inlet pressure regulator 13 reduces the high cylinder supply pressure (typically dry air or nitrogen at 200 psi) to a lower pressure for improved pressure control in the saturator. Stirling cooler 2a (or alternate Stirling cooler position 2b) provides low temperature cooling to the saturator 4. The alternate lower Stirling cooler position 2b is illustrated in dashed lines. If the upper Stirling cooler position is used, the saturator is mechanically attached to and suspended from the upper Stirling cooler. If the alternate lower Stirling cooler position is used, the saturator rests upon, and is mechanically attached to the lower Stirling cooler.

(31) FIG. 2 shows a right side profile of FIG. 1, while FIG. 3 shows an exploded view of FIG. 1 to better see the humidity generator components. In another embodiment, heaters 16a,b provide heating to the saturator, but are not required to control the temperature of the saturator. The heaters preferably encircle the conducting surface of the upper and lower coolers, but may also encircle the upper and lower surfaces of the saturator, or both. FIG. 4 is an exploded view of the vacuum chamber, showing the vacuum flanges 9, 10, 11 as well as various piping and control components.

(32) FIG. 5 shows the gas flow through the piping and humidity generator components during the normal generation cycle. A gas (i.e. nitrogen) cylinder is connected (gas in) to a pressure regulator valve 13 where the gas pressure is regulated down to approximately 150 psi. The gas then follows the arrow directions through the entry on-off valve 15, to the saturator pressure control valve 5, through the three way valve 12, and enters the bottom (piping not shown) of the saturator 4. The gas then exits out of the top of the saturator, through the flow control valve 6, and exits to the downstream units (Gas Out).

(33) Similarly, FIG. 6 shows a purge cycle where the gas takes a similar entry route, except the three-way valve directs the gas into the top of the saturator 4 and then the gas exits (Gas Out) through the vent valve 14.

(34) Saturator

(35) The gas saturator assembly 4 comprises a series of vertically stacked round plates that are fused together by brazing. Each of the stacked plates incorporates an entry and exit hole for plate to plate gas flow. Each plate utilizes a machined pathway to maximize gas exposure to the liquid or frozen water residing in the pathway. The plate design directs the calibration gas around the pathway on each plate, causing the gas to admix with water vapor at the saturator pressure. Water within the pathway has a large exposed surface area to ensure high water vapor saturation efficiency into the gas stream. The water level of the pathway has adequate depth to ensure a sufficient humidity supply for a long period.

(36) In one embodiment, the plates in the saturator are made from stainless steel. The plates are then fused together in a nickel brazing operation which completely seals the saturator so that it can withstand the saturator pressures needed during operation (up to 100 psi). In a preferred embodiment, the plates are made from copper for better thermal conductivity. For corrosion protection, the copper plates are plated with a corrosion resistant metal such as nickel, silver, rhodium, or gold. Nickel is a preferred plating metal as it readily self brazes together in a vacuum oven. In alternate embodiments, the saturator plates are aluminum or nickel and plated for corrosion protection.

(37) When filling the saturator with distilled water, each stackable plate has a machined fill level point or dam which must be reached before the water spills over and down to the next plate. To fill the water channels in the saturator, a distilled water syringe (about 100 ml of water) is discharged into the top saturator plate. The initial fill is done top to bottom in the direction of gravity which is also in a direction counter to the normal gas flow through the saturator. A purge technique directs a gas flow in the same direction as the water during filling, pushing excess water from the top plate down toward the bottom plate and finally out an open vent (as mentioned in FIG. 6 description). This purge gas flow removes excess water from the saturator and may also be used to dry exit piping.

(38) Alternately, a small pump may be used to fill the saturator for applications where there is more demand for water and/or a desire to fully automate the filling process.

(39) The saturator temperature is controlled by a Stirling cooler, at the top, (or alternately at the bottom), which provides a direct contact surface to cool the top (or alternately the bottom) of the saturator assembly. The cooling is readily transferred by conduction from contact between plates in the saturator assembly. Typically, the entire saturator is cooled to the desired temperature in less than an hour. The saturator is maintained at the required saturation temperature by two sensors situated in the upper and lower portion of the saturator. A PID control loop on the Stirling cooler monitors the saturator temperature and controls the Stirling cooler. Contact heaters are also installed to heat the saturator when required. A PID control loop monitors the two saturator temperature sensors previously mentioned and controls power applied to the heating elements. For more precise temperature control, a custom algorithm is employed whereby both the heating and cooling work simultaneously and in conjunction with one another.

(40) The Stirling cooler cools the saturator by direct contact on the upper saturator surface (or alternately the lower saturator surface). The Stirling cooler is a piston style-gas expansion cooler.

(41) Typically, due to the very low need for water to saturate the incoming gas, a 100 ml quantity of water could last for months. Typical humidity amounts in the exit gas are several parts per million to several parts per billion. However, the refill timing is highly dependent on the desired humidity and flow output.

(42) The saturator is filled at atmospheric pressure and room temperature to assure a fill. It is readily understandable to those skilled in the art that a cold saturator (below 0° C.) will not fill properly due to the potential of freezing of the water while filling.

(43) Optionally, the embodied humidity generator unit is provided with a battery backup when power reliability is suspect.

(44) The embodied humidity generator will operate for days or months without any need for operator intervention.

(45) The embodied humidity generator has a very small footprint verses other designs due to the compact design of the Stirling cooler unit.

(46) The embodied humidity generator is generally described as a single exit stream from the humidity generator to an external device for use. However, a plurality of exit streams could equally be generated by utilizing multiple exit flow control valves in a parallel flow orientation.

(47) Operation of the Humidity Generator

(48) The operator sets up the humidity generator, and the electronic controls takes care of any adjustment need to maintain the exit stream humidity level with little or no intervention by the operator. The embodied invention generates a humidity by: A. Allowing the operator to select the desired output humidity in terms of dew point, frost point, parts per million, or another humidity related parameter. B. Allowing the operator to select the desired flow rate. C. The system will then measure the pressure of the output, or DUT, depending on the method of physical connection made by the user. D. The system will measure the temperature at the DUT, if needed for the selected humidity output parameter. E. Based on data from A C, and D, the system will select a suitable saturation temperature and begin control toward that temperature. F. Based on parameter measurements and setpoints established in A, C, D, and E above, the system will compute the saturation pressure setpoint required to bring about the correct humidity output. G. The system will continuously monitor all appropriate conditions, continuing to recompute setpoints for saturation temperature and saturation pressure as necessary. H. The system will continually control saturation temperature, saturation pressure, and flow rate controls to achieve the required setpoint values, resulting in proper humidity output.

(49) The humidity generator produces humidity values useful for calibrating and verifying instrumentation. The embodied humidity generator is fully capable of supply a continuous humidified gas stream, within the frost/dew point range of −90° C. to +10° C.

(50) A humidity measuring instrument is not needed to determine the amount of humidity in the exit stream. Instead, the NIST fundamental principles of two-temperature and two-pressure humidity generation techniques are used and the known amount of humidity at those parameters is presumed to be the correct output.

(51) Process Control

(52) Elements illustrated in FIG. 7:

(53) TABLE-US-00002 21 Inlet gas 22 Inlet pressure regulator 23 Inlet pressure transmitter 24 Inlet relief valve 25 Saturator on/off valve 26 Saturator pressure control valve 27 Three way valve 28 Saturator 29 Exit flow control valve 31 Exit Pressure 32 Saturator pressure transmitter (high range) 33 Blocking valve (1) 34 Exit pressure transmitter (low range) 35 blocking valve (2) 36 Water fill point 37 Water fill pump 38 Water fill tank 39 Vacuum pressure gauge 40 Vacuum pump 41 Vacuum chamber 42 Vacuum chamber over pressure valve

(54) Gas from a gas connection 21 flows to an inlet pressure regulator 22 to be reduced to approximately 150 psi. An on/off solenoid valve 25 allows the gas to go through a precise pressure regulator 26 to a three-way valve. The gas normally follows the generate path to the lower part of the saturator 28. It then goes out the top of the saturator to a flow control valve 29. Gas then exits the flow control valve and is directed to the DUT connected to the generator's outlet port 31. The saturator pressure is normally measured by a higher range saturator pressure transmitter 32. When saturation pressure is low, the saturation pressure is more accurately measured by the lower range exit pressure transmitter 34 by opening blocking solenoid valve 33 and closing blocking solenoid valve 35. In this case the exit pressure transmitter monitors both the exit pressure and saturator pressure in a ‘switching’ arrangement by toggling solenoid blocking valve 33 and solenoid blocking valve 35 on/off. The switching is for relatively short periods.

(55) A three-way solenoid valve 27 directs the gas to either a purge cycle or a generate cycle. The purge cycle is used when filling the saturator 28 with water. The purge gas flows downwardly through the saturator and clears out excess water as previously described.

(56) An over-pressure relief valve 23 is added to the vacuum chamber 41 to avoid damage to the vacuum chamber if the gas pressure regulator 26 fails open. If the vacuum camber 41 goes over pressure, then the relief valve 23 check valve will activate to relieve the pressure and prevent damage.

(57) Electrical Control

(58) In FIGS. 8-10, the following items are illustrated in the figures:

(59) TABLE-US-00003 101 Main controller board with analog and digital I/O, custom Firmware 102 Multi-channel high accuracy temperature measuring circuit 103 Vacuum Pump 104 AC input power receptacle 105a Electronic control circuit to drive 106a 105b Electronic control circuit to drive 106b 106a Free Piston Stirling Cooler (FPSC) 106b Alternate Free Piston Stirling Cooler (FPSC) 107 Vacuum chamber 108 Saturator 109a Heater Top 109b Heater Bottom 110a Saturator Temperature Sensor a (upper) 110b Saturator Temperature Sensor b (lower) 111 Saturator pressure sensor (transmitter) 112 Exit pressure sensor (transmitter) 113 gas inlet pressure sensor 114 Gas inlet valve 115 Directional valve to select gas flow path purge/generate 116 Vent valve solenoid 117 Water fill valve solenoid 118 Pressure selection valve low (Psl) 119 Pressure selection valve high (Psh) 120 Pressure controller 121 Flow 1 controller 122 Flow 2 controller - optional 123 Flow 3 controller - optional 124 Vacuum gauge sensor 125 User Interface with PC - custom programming 126 24 VDC power supply 127 48 VDC power supply 128 Power switch with integrated LED indicator

(60) A multifunction custom printed circuit board is used to control and operate the low humidity generator.

(61) In FIG. 8, temperature control of the saturator is attained by two PID control loops which use saturator temperature measurements 110a,b connected to a temperature measuring board 102 that is connected to the main controller board 101. The main controller board then directs the Stirling control driver board 105a, (alternate 105b) to control the Stirling cooler 106a, (alternate 106b) to the desired temperature. The two temperature measurements are located on the upper and lower sections of the saturator. The control temperature is typically any value between −90° C. and 10° C.

(62) The dashed lines around the lower Sterling cooler 106b and the FPSC driver board 105b indicate that it is an alternate Sterling cooler position.

(63) FIG. 9 shows the power setup to the main controller board 101 and the temperature board 102 which are based on a 24 VDC power supply 126. The Stirling cooler is powered by a 48 VDC power supply 127. A power switch 128 energizes the power supplies 126,127 and has an integral LED light.

(64) The dashed lines around the lower Sterling cooler 106b and the Electronic control circuit to drive 105b indicate that it is an alternate Sterling cooler position.

(65) FIG. 10 shows the main controller board 101 connections to various sensors 111-113, solenoids 114-119, and controllers 120-123. Also, a user interface/personal computer connection 128 is shown. The computer connection (or mobile computer device) follows a communication protocol that is common and known in the art. The vacuum gauge sensor 124 and vacuum pump control 103 also connects to the main controller board 101. All of the sensor connections and controller connections are analog, serial, parallel, or wireless, and utilize communication protocols that are common and known in the art.

(66) The main controller board 101 is customized and provides both PID loop process control and logic control for the humidity generator. (FIG. 10)

(67) A humidity generator can provide more than one exit flow. Provisions for up to three independent exit flow controllers 121-123 are illustrated. More than three can be provided.

(68) Gas Flow and Pressure Control (FIG. 7)

(69) Gas pressure in the saturator is controlled by a pressure control valve 26 equipped with integral pressure measurement used for feedback. The saturator 28 has comparatively little pressure loss for normal gas flow rates, and the water vapor is admixed with the carrier gas at the temperature and pressure of the saturator. A PID pressure control algorithm provides for even and steady state pressure control.

(70) Similarly, the exit flow rate control is provided after the saturator by a flow control valve 29 with an integral flow meter for measurement and feedback. A PID control algorithm provides for even and steady state exit gas flow.

(71) The exit gas pressure after the saturator exit flow valve 29 will vary depending upon the downstream device utilizing the gas, often called the device under test (DUT). If the DUT instrument vents to atmosphere, the generator exit pressure will be near atmospheric. If the DUT instruments use a back pressure venting valve, or utilize other flow restriction mechanisms, the generator exit pressure will be elevated based on the back pressure setpoint or the flow rate used. In either case, the exit pressure is typically very steady. The flow controller 29 will continue to maintain the desired flow rate, and the saturator pressure controller 26 will automatically adjust to maintain the desired humidity output setpoint.

(72) Operational Control (FIG. 7)

(73) In normal operation, the carrier gas (usually compressed air or nitrogen) is directed through (in order): 1. an initial mechanical pressure valve 22 to reduce the pressure to an acceptable amount. 2. a saturator on-off solenoid operated valve 25. 3. a saturator pressure control valve with integral exit pressure feedback 26. The exit pressure is the pressure of a humidity saturator (or simply ‘saturator’). 4. the saturator 28 comprised of a number of stacked plates with channels containing pure liquid water or ice laying in machined channels on the stacked plates. 5. an exit flow valve 29.

(74) For maintenance, the vacuum chamber is relatively easy to access. The humidity generator unit is turned off, air is allowed to enter the vacuum chamber, and then the vacuum chamber is disassembled. All of the gas components and electrical wiring inside the vacuum chamber are then available for service.

(75) Pressure Sensor Accuracy (FIG. 7)

(76) The accuracy of the pressure sensors in the saturator and the exit gas pressure is very important to the accuracy of the humidity level. Typical pressure sensor accuracy is 0.05% full scale. The saturator can operate to a pressure of up to 100 psi, and to as low as near ambient pressure. To improve the humidity control and measurement, both the higher range saturator pressure sensor and the exit (lower range pressure sensor) are able to monitor the saturator pressure. Due to the mathematical relationship of saturator and exit pressures in the generation of humidity, the need for increased measurement accuracy becomes important at the lower saturator pressures. To ensure accuracy while the saturator is at low pressures (near ambient), the exit range pressure transmitter 34 assumes a time-sharing measurement role. The exit pressure transmitter 34 measures the saturator 28 for a short period by closing blocking valve 35 and opening blocking valve 33. It then measures the exit or DUT pressure 31 for a short period by closing blocking valve 33 and opening blocking valve 35. This time-sharing of the exit pressure transmitter continues while the saturator pressure remains within the range of the exit pressure transmitter 34.

(77) Because the lower range exit transmitter 34 is damaged when exposed to the higher operating range of the saturator, a solenoid valve 33 blocks the lower range sensor to protect it when the saturator pressure is higher than the sensor's measuring capability. During this time, the exit pressure transmitter 34 monitors only the exit or DUT pressure 31 by closing blocking valve 33 and opening blocking valve 35. So, while the saturator pressure is above the allowable range of the low pressure sensor, the exit pressure transmitter 34 monitors the exit or DUT pressure fully and does not time-share.

(78) It is desirable to be able to check calibration of the pressure transmitters 32, 34 while running. For this purpose, a pneumatic fitting is installed at the pneumatic junction of the saturator pressure transmitter 32 and the blocking valve 33. A reference pressure may be connected to this fitting and used as a comparison measurement to the saturator pressure transmitter. In this case, blocking valve 33 will be closed. For comparison to the low range exit pressure sensor 34, blocking valve 35 will be closed and blocking valve 33 will be open.

(79) Benefits

(80) The vacuum chamber improves accuracy of generated humidity by significantly reducing the problem of higher than expected humidity output due to the problem of permeation of external water vapor into the gas stream through O-rings and other connections. Since the external portion of O-rings and connections are physically located within the vacuum environment, they are contained in a low water vapor pressure environment. And since the inside of the O-rings and joints are at a low water vapor pressure because of the generated humidity, the normally large differential water vapor pressure between inside and outside of connections is significantly reduced, thus reducing the driving force behind the permeation, and the negative effects it would otherwise impose.

(81) The vacuum chamber also provides thermal isolation. It is known that thermal losses are mostly through contact with the ambient air and conductivity on support components. The vacuum chamber eliminates these kinds of heat losses. Also, the saturator is suspended in the chamber by direct contact with the Stirling cooler, so there is no thermal warming from saturator mounting equipment. Radiant heating through the vacuum chamber is very minimal.

(82) While various embodiments of the present invention have been described, the invention may be modified and adapted to various operational methods to those skilled in the art. Therefore, this invention is not limited to the description and figure shown herein, and includes all such embodiments, changes, and modifications that are encompassed by the scope of the claims.