Differential pressure detection

Figure 1. Differential Pressure Detection of Fluid Viscosity.

Using pitot tube as a differential pressure detection device, it need to consider factors that affect measurement accuracy, including the pitot tube coefficient, air density, temperature, pressure, thermal expansion coefficient, kinematic viscosity, and installation locations. 

Figure 14.6 Flow determination with differential pressure detection, horizontal tube with orifice...

Quednau J and Schneider G M 1989 A new high-pressure cell for differential pressure-jump experiments using optical detection Rev. Sc/. Instnim. 60 3685-7... 

Closed Vessels. Liquid level can be measured by the static pressure method also at non atmospheric pressures. However, ia such cases the pressure above the Hquid must be subtracted from the total head measurement. Differential pressure measuriag instmments that measure only the difference ia pressure between the pressure tap at the bottom of the tank and the pressure ia the vapor space are used for this purpose. At each tap, the pressure detected equals the Hquid head pressure plus the vapor pressure above the Hquid. Siace the pressure above the Hquid is identical ia both cases, it cancels out. Therefore, the change ia differential pressure measured by the instmment is due only to the change ia head of Hquid ia the vessel. It is iadependent of the pressure within the tank and is an accurate measure of the level. 

Monitoring The differential pressure across the arrester element can be monitored to determine the possible need for cleaning. The pressure taps must not create a flame path around the arrester. It can be important to provide temperature sensors, such as thermocouples, at the arrester to detect flame arrival and stabilization. Since arrester function may involve damage to the arrester, the event of successful function (flame arrival) may be used to initiate inspection of the element for damage. If the piping is such that flame stabihzation on the element is a realistic concern, action must be taken immediately upon indication of such stabihzation (see also Endurance Burn ). Such action may involve valve closure to shut off gas flow. 

Abnormal Formation Pressure Detection from Kicks. The kicks, or flow of formation fluids into the borehole, are the ultimate indication that the well has encountered an overpressured zone. Kick detection during drilling usually is achieved by use of a pit-volume indicator and/or a flow indicator. The usual pit-volume alert is 10 barrels drilling fluid volume increase. A differential mud flow indicator can also be used to detect kicks more quickly. 

Electrons spontaneously flow from the zinc to the copper electrode because copper has a greater afflnity for electrons than does zinc. We will discuss a procedure for quantifying these affinities in a few pages. At this point, we recognize that each reactant has a characteristic affinity and that this difference in affinity creates an electron pressure differential across the wire. This differential is detected as a voltage. 

Where it is possible for flammable or toxic gas or vapor released within a hazardous area to migrate to the inlets for HVAC systems serving nonhazardous enclosed areas such as control rooms, detection systems should be installed in those HVAC inlets or connecting ductwork. Detection should be provided in HVAC system intakes if the building, room, or enclosure served is not electrically classified and a flammable (or toxic) gas or vapor could feasibly be drawn into the area, either by mechanical ventilation systems or by differential pressures. The detection system should alarm and automatically shutdown the HVAC to prevent gas or vapor concentration in the protected space from reaching the flammable or toxic range. 

Earlier experiments involved the collection of SEC effluent aliquots to measure solution viscosity in batches with the very time consuming Ubbelohde drop-time type viscometers. A continuous capillary type viscometer was first proposed for SEC by Ouano. Basically, as shown in Figure 1, a single capillary tube with a differential pressure transducer was used to monitor the viscosity of SEC effluent at the exit of the SEC column. As liquid continuously flows through the capillary (but not through the pressure transducer), the detected pressure drop (AP) across the capillary provides the measure for the fluid viscosity (h) according to the Poiseuille s viscosity law ... 

Figure 14 illustrates a typical steam generator level detection arrangement. The AP detector measures actual differential pressure. A separate pressure detector measures the pressure of the saturated steam. Since saturation pressure is proportional to saturation temperature, a pressure signal can be used to correct the differential pressure for density. An electronic circuit uses the pressure signal to compensate for the difference in density between the reference leg water and the steam generator fluid. 

Figure 11 Differential Pressure Flow Detection Block Diagram 17...

The pitot tube, illustrated in Figure 5, is another primary flow element used to produce a differential pressure for flow detection. In its simplest form, it consists of a tube with an opening at the end. The small hole in the end is positioned such that it faces the flowing fluid. The velocity of the fluid at the opening of the tube decreases to zero. This provides for the high pressure input to a differential pressure detector. A pressure tap provides the low pressure input. 

Figure 11 shows a block diagram of a typical differential pressure flow detection circuit. The DP transmitter operation is dependent on the pressure difference across an orifice, venturi, or flow tube. This differential pressure is used to position a mechanical device such as a bellows. The bellows acts against spring pressure to reposition the core of a differential transformer. The transformer s output voltage on each of two secondary windings varies with a change in flow. 

The density of the fluid, ambient temperature, and humidity are the three factors which can affect the accuracy and reliability of flow sensing instrumentation. The purpose of each block of a typical differential pressure flow detection circuit is summarized below. 

H. Sato (JAEA) presented a paper discussing detection methods and system behaviour assessments for a tube rupture of the intermediate heat exchanger (IHX) for a sulphur-iodine based nuclear hydrogen plant. A rupture could be detected by monitoring the secondary helium gas supply using a control system that monitors the differential pressure between the primary and secondary helium gas supply. Isolation valves would be used to reduce the helium flow between the primary and secondary cooling systems. The study showed that the maximum temperature of the reactor core does not exceed its initial value and that system behaviour did not exceed acceptance criteria. 

Monitoring differential pressure between the primary and secondary cooling systems would be one of the candidates for detecting the heat transfer tube rupture. Meanwhile, the pressure varies even at normal operation and therefore there is a concern of malfunction of CV isolation valves. In case of primary helium gas recovery flow rate, primary helium pressure control system only covers the rated operation since the system activates when the primary coolant pressure reaches about 3.95 MPa. On the other hand, the primary-secondary differential pressure control system covers start-up, shutdown and rated operations. The control system keeps supplying helium gas to the secondary cooling system during the scenario. Thus, monitoring the entire secondary helium gas supply would be an effective way to detect the tube rupture. 

Head-type flowmeters include orifice plates, venturi tubes, weirs, flumes, and many others. They change the velocity or direction of the flow, creating a measurable differential pressure, or "pressure head," in the fluid. Head metering is one of the most ancient of flow detection techniques. There is evidence that the Egyptians used weirs for measurement of irrigation water flows in the days of the Pharaohs and that the Romans used orifices to meter water to households in Caesar s time. In the 18th century, Bernoulli established the basic relationship between the pressure head and velocity head, and Venturi published on the flow tube bearing his name. 

The detection of pressure drop across a restriction is undoubtedly the most widely used method of industrial flow measurement. If the density is constant, the pressure drop can be interpreted as a reading of the flow. In larger pipes or ducts, the yearly energy operating cost of differential-pressure (d/p)-type flowmeters can exceed the purchase price of the meter. The permanent pressure loss through a flowmeter is usually expressed in units of velocity heads, v2/2 g, where v is the flowing velocity, and g is the gravitational acceleration (9.819 m/s2, or 32.215 ft/s2, at 60° latitude). 

The operation of this sensor requires the blowing of an air (or some other gas) jet through a nozzle and detecting the deflection of this jet caused by the velocity of the process gas in the duct. This deflection causes an increase in pressure at the downstream receiver port and a decrease at the upstream one. Therefore, the process flow is related to the pressure difference between the two receiver ports (Figure 3.66). When there is no flow in the process pipe or duct, the jet is centered between these receiver ports, and the differential pressure is zero. As the process gases start flowing, the jet is deflected, and this deflection is converted into flow. 

When detecting the interface between two liquids, electrical conductivity, thermal conductivity, opacity, or sonic transmittance of the liquids can be used. Interface-level switches are usually of the sonic, optical, capacitance, displacer, conductivity, thermal, microwave, or radiation types. Differential pressure transmitters can continuously detect the interface, but, if their density differential is small relative to the span, the error will be high. On clean services, float- and displacer-type sensors can also be used as interface-level detectors. In specialized cases, such as the continuous detection of the interface between the ash and coal layers in fluidized bed combustion chambers, the best choice is to use the nuclear radiation sensors. 

The proposed optimization strategy will replace the traditional method of controlling the release of Oz. Today, the rate of 02 released is controlled to maintain the d/p between the electrolyte chambers in order to limit the force that the separation diaphragm has to withstand. When the pressure differential is detected and controlled by conventional d/p cells, the measurement cannot be sensitive or accurate therefore, the diaphragm has to be strong, and the electrolyzer (or fuel cell) must be bulky and heavy. In this optimized design (if a liquid electrolyte design is selected), differential level control (ALC-12) will be used, which can control minute differentials. 

Periodically or on demand, the computer simultiineously closes SVl and SV2. Liquid then flows from 7] to V<2, displacing gas from V2 to the process. However, differential pressure of the liquid is not detected by the APT until the falling liquid-level reaches the open end of tube Ti, inside of V. Thereafter, the differential pressure increases steadily until the liquid level reaches the open end of tube T2, at which point the differential again becomes steady. 

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