A heat measurement apparatus and method for a non-invasive measurement of heat generation are provided. The method include determining a flow value of a flowing substance within a system based on a system power usage; and determining a heat energy value of a system based on a temperature difference of a first temperature of the flowing substance at an inlet of the system from a second temperature of the flowing substance at an outlet of the system and the flow value of the system.

The present invention discloses a computational distributed fiber-optic sensing method and system. The method includes: determining a signal source for modulating intensity of incident light, where the signal source is a binary sequence; using an optical pulse sequence obtained after modulation is performed using the signal source, as an incident light signal, and emitting the incident light signal to an optical fiber; acquiring, according to specified sampling frequency, a scattered light signal obtained through optical fiber scattering; determining, according to the incident light signal and the scattered light signal, a time-domain reconstructed image of a to-be-detected light signal by using a time domain-based differential ghost imaging protocol; and determining a sensing signal of the optical fiber according to the time-domain reconstructed image of the to-be-detected light signal. The computational distributed fiber-optic sensing method and system provided in the present invention feature low sampling frequency, low device complexity, and low costs.

A method for operating and/or monitoring an HVAC system (10), in which a medium circulating in a primary circuit (26) flows through at least one energy consumer (11, 12, 13), the medium entering with a volume flow () through a supply line (14) into the energy consumer (11, 12, 13) at a supply temperature (T.sub.v) and leaving the energy consumer (11, 12, 13) at a return temperature (T.sub.R) via a return line (15), and transferring heat or cooling energy to the energy consumer (11, 12, 13) in an energy flow (E). A control unit (21) adaptively operates the system by empirically determining the dependence of the energy flow (F) and/or the temperature difference T between supply temperature (T.sub.v) and return temperature (T.sub.R) on the volume flow () for the energy consumers (11, 12, 13) in a first step, and by operating and/or monitoring the HVAC system (10) according to the determined dependency or dependencies in a second step.

A method for operating and/or monitoring an HVAC system (10), in which a medium circulating in a primary circuit (26) flows through at least one energy consumer (11, 12, 13), the medium entering with a volume flow () through a supply line (14) into the energy consumer (11, 12, 13) at a supply temperature (T.sub.v) and leaving the energy consumer (11, 12, 13) at a return temperature (T.sub.R) via a return line (15), and transferring heat or cooling energy to the energy consumer (11, 12, 13) in an energy flow (E). A control unit (21) adaptively operates the system by empirically determining the dependence of the energy flow (F) and/or the temperature difference T between supply temperature (T.sub.v) and return temperature (T.sub.R) on the volume flow () for the energy consumers (11, 12, 13) in a first step, and by operating and/or monitoring the HVAC system (10) according to the determined dependency or dependencies in a second step.

A reaction calorimeter probe having an inner tube having a pumpable reaction medium flowing therethrough, and an outer tube extending coaxially of the inner tube, a sealed space between the inner and outer tube, a first temperature sensor at an inlet end of the inner tube, a second temperature sensor at an outlet end of the inner tube, at a distance from the first temperature sensor, the first and second temperature sensors are in the space and in contact with the outer surface of the inner tube for measuring an absolute temperature of the inner tube, the first and second temperature sensors enable determinations of absolute temperatures, and a calculation device connected with the first and second temperature sensors, the calculation device to determine a first absolute temperature, a second absolute temperature and to determine a temperature difference between the first and second absolute temperatures.

A reaction calorimeter probe having an inner tube having a pumpable reaction medium flowing therethrough, and an outer tube extending coaxially of the inner tube, a sealed space between the inner and outer tube, a first temperature sensor at an inlet end of the inner tube, a second temperature sensor at an outlet end of the inner tube, at a distance from the first temperature sensor, the first and second temperature sensors are in the space and in contact with the outer surface of the inner tube for measuring an absolute temperature of the inner tube, the first and second temperature sensors enable determinations of absolute temperatures, and a calculation device connected with the first and second temperature sensors, the calculation device to determine a first absolute temperature, a second absolute temperature and to determine a temperature difference between the first and second absolute temperatures.

Embodiments of the disclosure relate to systems and methods to evaluate performance of a fluid transport system. Towards this end, a performance report of the fluid transport system can be generated by estimating various performance parameters at an outlet of a heat exchanger in lieu of using sensor data obtained directly from the outlet of the heat exchanger. Specifically, in one exemplary implementation, sensor data is obtained from an inlet of the heat exchanger and an outlet of a downstream element that is coupled to the heat exchanger, for estimating the various performance parameters at the outlet of the heat exchanger. The estimated performance parameters can then be combined with empirical data and predictive data for generating the performance report of the fluid transport system.

Embodiments of the disclosure relate to systems and methods to evaluate performance of a fluid transport system. Towards this end, a performance report of the fluid transport system can be generated by estimating various performance parameters at an outlet of a heat exchanger in lieu of using sensor data obtained directly from the outlet of the heat exchanger. Specifically, in one exemplary implementation, sensor data is obtained from an inlet of the heat exchanger and an outlet of a downstream element that is coupled to the heat exchanger, for estimating the various performance parameters at the outlet of the heat exchanger. The estimated performance parameters can then be combined with empirical data and predictive data for generating the performance report of the fluid transport system.

Utility meter for measuring thermal energy delivered to a point of consumption by a fluid supplied via a supply flow and a return flow, including a flow meter unit for measuring a supply flow rate or return flow rate of the fluid; a pair of temperature sensing probes for measuring temperatures of the supply flow and the return flow, each of the temperature sensing probes including a resistive temperature device; and a calculator device configured for executing a measuring algorithm for determining an amount of thermal energy delivered to the point of consumption over a period of time based on flow rates and temperatures received from the flow meter unit and temperature sensing probes, respectively; wherein the calculator device is configured to detect the type of resistive temperature device included in the temperature sensing probes and to adapt the measuring algorithm according to the type of resistive temperature device.

A method indicates to a user the fuel consumption and/or efficiency of a heating installation having a heat pump with a thermal compressor, a heating fluid distribution circuit and radiators receiving a first quantity of energy Q1. The method includes the steps: Aof determining, over a predetermined time period a second quantity of energy Q2, corresponding to the supply of heat energy used to drive the compressor, Bof determining, over the same predetermined time period, a third quantity of energy Q3 corresponding to free energy taken from the external environment, Cof displaying the quantities Q2 and Q3, in relation to the predetermined time period, on a display screen and/or in a document for invoicing the customer.