Abstract: An air data probe includes a probe head defining a longitudinal axis between a forward tip and aft base. A port opening is defined in a side of the probe head and opening at an angle with respect to the longitudinal axis. A bulkhead within the probe head has a chamber in fluid communication with the port opening. The chamber includes a single chamber inlet having an elongated cross-sectional shape. The single elongated chamber inlet is in fluid communication with two downstream pressure conduits to provide redundancy in case one of the two pressure conduits is blocked.

Abstract: New sensors and methods for qualitative and quantitative analysis of multiple gaseous substances simultaneously with both high selectivity and high sensitivity are provided. The new sensors rely on a characteristic difference in energy between the interaction of a particular substance with a catalyst coated heat transfer device (HTD) and a non-catalyst coated (or one coated with a different catalyst) reference HTD. Molecular detection is achieved by an exothermic or endothermic chemical or physical reaction between the catalytic surface of the sensor and the molecule, tending to induce a temperature change of the sensor. Both high temperature and non-destructive low temperature detection are possible. The magnitude and rate of endothermic or exothermic heat transfer from a specific molecule-catalyst interaction is related to molecular concentration.

Abstract: An apparatus, system, and method are disclosed for determining a catalyst bed temperature. The method may include receiving a current fluid mass flow within an exhaust pipe and a total amount of unburned fuel available for catalytic combustion. The method may further include determining a plurality of fluid enthalpy values corresponding to various locations within the exhaust pipe. The method may continue with calculating an amount of fuel burned on an upstream catalyst based on the plurality of fluid enthalpy values, and determining an amount of fuel remaining that is available for combustion on a downstream catalyst. The method may determine a combustion efficiency of the downstream catalyst based on the temperature rise across the downstream catalyst, and an amount of heat generated within the downstream catalyst based on the combustion efficiency and the amount of fuel remaining that is available for combustion on the downstream catalyst.

Abstract: A system for attaching in situ thermal management equipment, such as a heat exchanger, to a high pressure gas storage tank in a manner which fixes the in situ equipment in the interior of the tank, to the tank, but does not constrain the axial location of the in situ equipment, thereby allowing a small amount of longitudinal displacement or axial rotation between the heat exchanger and the tank. A degree of longitudinal movement along the axis of the tank and a degree of rotation is effected, both singularly at either end of the in situ device or dually at each end of the in situ device positioned within the tank.

Abstract: An energy content meter can spectroscopically quantify oxidation products after oxidation of a combustible mixture. The measured oxidation product concentrations or mole fractions can be converted to an energy content of the un-oxidized combustible mixture using a conversion factor that relates oxygen consumption during oxidation of the combustible mixture to the energy content of the combustible mixture.

Abstract: An embodiment of the invention is disclosed that relates to a mechanism for passing a rigid medium under an image-forming mechanism. The mechanism includes a conveyor belt and a number of rollers. The rigid medium travels on the conveyor belt under the image-forming mechanism, for image formation on the rigid medium. The rollers move the conveyor belt.

Abstract: The invention concerns a device (10) for measuring exchanges of amounts of heat in non-stationary operational conditions, including an elongated housing (11) having one measuring end (12) closed and one connecting end (13) and a central cavity (14). The central cavity (14) contains a measuring cell (15) and electrical connection members (13). The housing (11) is extended by a hollow finger (17) which contains partly at least the measuring cell (15) which consists of a sensitive heat flux measuring element (18) sandwiched between a first heat conducting component (19) and a second heat conducting component (20). The first heat conducting component (19) is in contact with at the least one surface of the said housing (11), and in the second heat conducting component (20) is insulated from the housing and constitutes a constant heat capacity.

Abstract: A clinical tester has been described that includes a probe to aspirate a fluid. The probe is washed between aspirations to reduce carryover. The wash operation includes both an internal and an external wash, where the internal wash operation is terminated prior to terminating the external wash. In one embodiment, the probe wash can be implemented on an integrated clinical chemistry/immunoassay tester.

Abstract: The proposed method allows to determine by dielectrometry the variation of the glass-transition temperature (Tg) of a polymer material used in the presence of fluids (water/organic compound/gas), pure or in admixture. More precisely, the invention is based on the use of dielectric sensors whose geometry is such that they allow to follow, in a sensitive and reproducible way, the frequency and/or temperature dependence of the dielectric permittivity characteristics of a polymer material in the presence of fluids without disturbing permeation/desorption of the solute during transient and unsteady states, these dielectric measurements (real and/or imaginary part) being connected with the plasticized state of the material, which determines the performances thereof during use.

Abstract: A low-cost, accurate enthalpy sensor is described. The invention provides an on/off output which reflects the result of a comparison between the enthalpy level of a space and a predetermined setpoint. The sensor combines a signal representative of humidity with a signal representative of temperature to create a signal representative of enthalpy. The signal representative of enthalpy is compared with a predetermined setpoint to determine if the enthalpy level is above or below the setpoint. An output is then produced which indicates whether the output representative of enthalpy is above or below the predetermined setpoint.

Abstract: An improved monitoring of the quality and heat value of a flow of condensable vapor. A small side stream of representative vapor sample is tapped from the flow in the vapor main by utilizing the difference between the dynamic pressure of the vapor at a sample intake point and the suction pressure of the vapor at a sample return point. The sample stream passes through a superheater-calorimeter to completely vaporize any liquid entrained in the sample stream and superheat the vaporized sample, and then through a mass flowmeter before being returned to the vapor main. The quality and the heat value of the sample stream are determined by a heat balance around the superheater-calorimeter using correlations relating thermodynamic properties of the vapor to pressures and temperatures. The invention also monitors the enthalpy and the mass-flow rate of said vapor flow.

Abstract: A high temperature gas meter provides a liquid injection means, at least one temperature sensing means located upstream from the liquid injection means and a liquid flow measuring means. Alternatively, a second temperature sensing means may be employed downstream from the liquid injection means. The meter uses the change in temperature of a gas flowing through a conduit recorded at temperature sensing means before and after injection into the gas stream of a liquid of known quantity and temperature. The flow of the gas is inversely proportional to the change in temperature recorded prior to liquid injection and after liquid injection.

Abstract: An enthalpy calculator unit outputs a value of enthalpy directly from two measured parameters, such as dry bulb temperature and relative humidity, and includes a humidity sensor 17 for converting a measured relative humidity into an electrical signal; temperature sensors for converting a measured temperature into electrical signals; and arithmetic units for calculating the enthalpy and for outputting electrical signal corresponding thereto after performiing a calculation based on the signals input by the sensors in accordance with the following equation:i=(ae.sup.bt -c)(t+d).psi.+mt+nwherea, b, c, d, m, and n are constants, and:t: dry bulb temperature (.degree.C.).psi.: relative humidity (%),and a, b, c, d, m, and n are selected so that .vertline.i-i.sub.0 .vertline..ltoreq.0.5 within a fixed temperture range if:i.sub.0 =0.240t+(597.3+0.441t)xx=0.622.multidot..psi..multidot.h/(P-.psi..multidot.h)whereP: atmospheric pressureh: saturated vapor pressure under the atomspheric pressure P.

Abstract: Energy transmitted to a load in a fluid medium is measured utilizing a probe having an elongate heat transmitter that includes a sensing tip at one end, a heat exchanger at its opposite end, a thermal impedance forming at least a segment of the heat transmitter, and temperature sensors spaced apart along the impedance. The temperature of the sensing tip is maintained different from that of the sensed fluid. A read-out is responsive to the temperature sensors and it is calibrated in terms of the energy content of the fluid flowing in the sensed passage. Corrections for various factors of error are incorporated in the read-out. A relative simple yet reasonably accurate measure is made of the energy in steam, where the heat exchanger of the probe is a passive heat dissipator.

Abstract: An enthalpy measuring arrangement for measuring the heat content of a substance which may in the liquid phase, vapor phase or a mixed phase of liquid and vapor, comprises a first enthalpy calculating module for calculating the enthalpy of the substance when in a two-phase condition utilizing a plurality of discrete function blocks. The specific volumes of the overall mixture is calculated using a density transmitter which measures the density of the substance. Tables are utilized to obtain the specific volumes of the gas and vapor part of the substance on the basis of a measured temperature for the substance. These values are in turn used to obtain a quality value which is multiplied by a value representing the difference between the enthalpys of the vapor and liquid components of the substance to obtain the overall enthalpy of the mixture. Another module with a plurality of function blocks generates the enthalpy of the substance when it is superheated or entirely in the vapor phase.

Abstract: A laser calorimeter which operates by absorbing the energy of a laser beam directed through a lens at the front of the calorimeter. The calorimeter contains a absorbing medium with high absorbance characteristics at the laser wavelength in question. The absorbed laser energy is converted to heat. The device has a means for measuring the changes in temperature of the absorbing medium as well as a means for measuring the changes in pressure inside the calorimeter chamber. The absorbing medium is typically a liquid which also demonstrates preferable heat transfer characteristics. This in turn affords greater precision and a faster response time of the calorimeter when measuring the laser energy. A typical medium for such a device is a dimethylformamide solution which has extremely good absorbance characteristics for an optical path length of 0.015 inches at a laser wavelength of 1.064 microns.