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Archive for the ‘Measurement’


Accurate flow measurement

There is a need for accurate flow measurement of numerous liquids, gases and vapors in many industries. For instance, food processing plants need to have an accurate measure of types of materials that go into the products on a large, automated scale. In the semiconductor industry, small amounts of gases have to be applied to the production process. Accurate delivery of these gases is essential to ensure the quality of the finished product.

As already mentioned, the mass flow or the volume flow are the measurements that are needed in these processes. In the case of mass flow, the Coriolis flow meter (also known as the inertial flow meter) is commonly used.

The Coriolis flow meter gets it’s name from the Coriolis effect that was first described by Gaspard-Gustave Coriolis in 1835. Coriolis worked in understanding the behaviors of objects in motion due to the various forces that applied to them. To this extent, the Coriolis mass flow meter works in this manner.

If a liquid or gas is passing through a tube it applies a force to the tube. When the tube is already moving, then the substance passing through it will change the movement or vibration of that tube. The change in the amplitude of the vibration of the tube can be used to determine the mass of a flow of the substance passing through the tube.

This is possible provided various other factors are known about the tube, such as the width, the type of material that it is made from, the vibrating frequency of the tube and it’s inertia. The flow density of the material passing through the tube is also needed.

Coriolis flowmeters are popular because they need little maintenance. By comparison to other devices that perform flow measurement they are well designed to the extent that little can go wrong with them. They do not need to be re-calibrated like other types of flow meters.

With this said, the flow meter does need to be checked from time to time, especially if the substances that pass through the tubing are hot or corrosive.

If you are using these types of substances the chances are you will have noted this when initially specifying the type of flow meter you need. Many flow meters will not be able to handle hot liquids or corrosive gases. A specially made flow meter would be required for these purposes.

When it comes to selecting a coriolis meter, you want to make sure it meets all your needs. You should also look for the best you can afford as this is a fair measure of the quality of the meter. Coriolis flow meters, and gas mass flow meters, are designed to be accurate and they’re designed to save you time and money so you will make this initial expense back on increased efficiency in the workplace

Coriolis flowmeters

Coriolis flowmeters are relatively new compared to other flowmeters. They were not seen in industrial applications until 1980’s. Coriolis meters are available in a number of different designs. A popular configuration consists of one or two U-shaped, horseshoe-shaped, or tennis-racket-shaped (generalized U-shaped) flow tube with inlet on one side and outlet on the other enclosed in a sensor housing connected to an electronics unit.

The flow is guided into the U-shaped tube. When an osillating excitation force is applied to the tube causing it to vibrate, the fluid flowing through the tube will induce a rotation or twist to the tube because of the Coriolis acceleration acting in opposite directions on either side of the applied force. For example, when the tube is moving upward during the first half of a cycle, the fluid flowing into the meter resists being forced up by pushing down on the tube. On the opposite side, the liquid flowing out of the meter resists having its vertical motion decreased by pushing up on the tube. This action causes the tube to twist. When the tube is moving downward during the second half of the vibration cycle, it twists in the opposite direction. This twist results in a phase difference (time lag) between the inlet side and the outlet side and this phase difference is directly affected by the mass passing through the tube.

A more rescent single straight tube design is available to measure some dirty and/or abrasive liquids that may clog the older U-shaped design.

An advantage of Coriolis flowmeters is that it measures the mass flow rate directly which eliminates the need to compensate for changing temperature, viscosity, and pressure conditions. Please also note that the vibration of Coriolis flowmeters has very samll amplitude, usually less than 2.5 mm (0.1 in), and the frequency is near the natural frequency of the device, usually around 80 Hz. Finally, the vibration is commonly introduced by electric coils and measured by megnetic sensors.

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Further Information

Suppose that the fluid is flowing into the U-shaped tube at velocity V and the tube is vibrating at angular velocity . Consider a small section of the fluid that is on the inlet side away from the point of flexture at distance r.

Please note that the amplitudes of the vibration and twist are extremely small compared to the size of the U-shaped tube. The above graphics are highly exaggerated for illustration purposes.

The Coriolis force on the small fluid section m is

During the down cycle, the tube applys an upward resisting force to the fluid or the fluid pushes the tube down. On the outlet side, the Coriolis force has the opposite direction.

To simply the problem, we assume that the tube has a perfect U shape with a cross section area of A. The length and width are l, d, respectively. The opposite directions of Coriolis forces on inlet and outlet sides result in a twisting moment Tc

A K factor can be introduced to compensate for the more generalized U-shape.

where Qm = AV is the mass flow rate.

The governing equation of twisting is

where Iu is the inertia of the U-shaped tube, Cu is the damping coefficient, Ku is the stiffness, is the twist angle, and t is time.

Recall that the Coriolis flowmeters are vibrating the U-shaped tube to generate the rotation, the real angular velocity is function of vibrating frequency :

Assuming that the damping term Cu is negligible, the equation of twisting becomes

The particular solution (steady-state solution) of the twist angle is

Furthermore, the velocity of the turning corners of the U-shaped tube are  and the displacement difference between these two corners is d/2. Therefore, the time lag between these two corners is

By measuring the time lag , the mass flow rate can be obtained

In vibration analysis, it is custom to use the natural frequency as a basis and normalize frequency terms against it. The natural frequency of the U-shaped tube system is (note that Iu includes the mass of the fluid in the tube)

The mass flow rate then becomes

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Common Specifications

Common specifications for commercially available Coriolis flowmeters are listed below:

Fluid Phase:

Score     Phase     Condition
Liquid      Clean
Direct Mass
Dirty
Non-Newtonian
Viscous
Slurry      Abrasive
Gas      Clean
Dirty
Liquid      Corrosive
Slurry      Fibrous
: Recommended
: Limited applicability
Line Size:     6 ~ 200 mm (0.25 ~ 8 inch)
Turndown Ratio:     100 : 1

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Pros and Cons

•     Pros:
-     Higher accuracy than most flowmeters
-     Can be used in a wide range of liquid flow conditions
-     Capable of measuring hot (e.g., molten sulphur, liquid toffee) and cold (e.g., cryogenic helium, liquid nitrogen) fluid flow
-     Low pressure drop
-     Suitable for bi-directional flow
•     Cons:
-     High initial set up cost
-     Clogging may occur and difficult to clean
-     Larger in over-all size compared to other flowmeters
-     Limited line size availability

Flowmeter Type and Its APPLICATION

So you want to measure flow? The answer would seem to be to purchase a flowmeter. With fluid flow defined as the amount of fluid that travels past a given location, this would seem to be straightforward — any flowmeter would suffice. However, consider the following equation describing the flow of a fluid in a pipe.

Q = A x v

Q is flow rate, A is the crosssectional area of the pipe, and v is the average fluid velocity in the pipe. Putting this equation into action, the flow of a fluid traveling at an average velocity of a 1 meter per second through a pipe with a 1 square meter cross-sectional area is 1 cubic meter per second. Note that Q is a volume per unit time, so Q is commonly denoted as the “volumetric” flow rate. Now consider the following equation:

W = rho x Q

Where W is flow rate (again - read on), and rho is the fluid density. Putting this equation into action, the flow rate will be 1 kilogram per second when 1 cubic meter per second of a fluid with a density of 1 kilogram per cubic meter is flowing. (The same can be done for the commonly-used “pounds”. Without getting into details — a pound is assumed to be a mass unit.) Note that W is a mass per unit time, so W is commonly denoted as the “mass” flow rate. Now — which flow do you want to measure? Not sure? In some applications, measuring the volumetric flow is the thing to do.

Consider filling a tank. Volumetric flow may be of interest to avoid overflowing a tank where liquids of differing densities can be added. (Then again, a level transmitter and high level switch/shutoff may obviate the need for a flowmeter.) Consider controlling fluid flow into a process that can only accept a limited volume per unit time. Volumetric flow measurement would seem applicable.

In other processes, mass flow is important. Consider chemical reactions where it is desirable to react substances A, B and C. Of interest is the number of molecules present (its mass), not its volume. Similarly, when buying and selling products (custody transfer) the mass is important, not its volume.

Having discovered that there are two types of flow rates (volumetric and mass), it should not be a surprise that some flowmeters measure mass (W) while other flowmeters measure volume (Q). However, it is not quite that simple. Repeating the equations from Part 1 (for convenience), it can be seen that, assuming A is constant, Q can be determined by measuring the average fluid velocity v. Further, assuming that rho is constant, W can be determined from Q.

Q = A x v  W = rho x Q

Summarizing, some flowmeters measure volumetric flow, some flowmeters measure velocity from which the volumetric flow is determined, and some flowmeters measure mass flow. In addition, when the density is known or assumed, mass flow can be determined from the volumetric flow, and the volumetric flow can be determined from the mass flow. So you just wanted to measure flow — did you now? It all seemed so logical and simple at the time. Stick around — it gets worse. Some flowmeters use other principles to infer flow. The most common of these measurements measure the velocity head (1/2 rho v x v) to infer the volumetric flow. Notice that these flowmeters do NOT measure volume, do NOT measure mass, and do NOT measure velocity — but rather measure a combination of density and the square of velocity! Would it surprise you to discover that this is a description of (commonly-applied) head flowmeters, such as orifice plates, venturis, nozzles…? Further, in many applications, the inferred volumetric flow is used to determine the mass flow. Errors can enter the measurement process during each measurement and with each assumption. Is it any surprise that plant engineers often have difficulty closing material balances in their plants?

Summarizing (again), some flowmeters measure volume, some flowmeters measure mass, some flowmeters measure velocity, and some flowmeters measure inferentially. Understand the difference, but also understand that careful attention to detail can result in an inferential measurement that is better than the others.

Volumetric flow is expressed in units that reflect a volume per unit time. The example in Part 1 determines cubic meters and cubic feet per unit time to be volumetric flow units. Gallons and liters per unit time are also volumetric flow units. Mass flow is expressed in units that reflect a mass per unit time. The other example in Part 1 determines kilograms and pounds per unit time to be mass flow units. (Without getting into details — a pound is assumed to be a mass unit.) Note that the units of time are independent of whether volumetric or mass flow is measured.

Let’s have a quiz.
Are the following volumetric or mass liquid flow units?
gallons per minute
cubic feet per second
liters per minute
kilograms per hour
pounds per hour
grams per minute

Can one have a cubic foot of feathers?
yes/no

Can one have a gallon of feathers?
yes/no

Can one have a kilogram of feathers?
yes/no

If you answered volumetric to the first three questions, mass to the next three questions, and yes to the last three questions, you are on track.

Consider purchasing fuel for your car. How does a US gallon of gasoline purchased on a hot summer day in Las Vegas, Arizona compare with a US gallon of gasoline purchased on a cold winter night in Anchorage, Alaska? It was determined that a gallon is a volumetric unit, so logic would indicate that the same volume of gasoline was purchased. Yet the temperature difference would cause their densities, and hence their masses, to be different. Using this logic, more mass would be obtained by purchasing gasoline in colder weather. Thinking locally, one might conclude that it is more economical to purchase gasoline during the wee hours of the morning when the temperature is coldest.

As you might suspect, such is not the case. Gasoline pumps compensate for density variation that occurs due to temperature, and in doing so, they measure the amount (mass) of gasoline dispensed. Yet, a gallon of cold gasoline will occupy less volume than when hot. In essence, the measurement of a gallon of gasoline actually refers to its volume at a given temperature (such as 60 degF). As such, this is really a mass measurement unit because it refers to the flow of a specific substance at a given temperature, Returning to the quiz, let’s not be so hasty with the first three questions. They could be incomplete!
Part 3 discussed the use of volumetric units (such as gallons) to infer mass when the composition and temperature is known. The example given was that of purchasing a gallon of gasoline in a hot and cold climate. The assertion was that a gallon of gasoline purchased in hot and cold climates might have different sizes due to their differing temperatures, but their masses should be the same because the retail flowmeter is temperature compensated.

A number of e-mails questioning this assertion and further investigation resulted in the interesting discovery that retail gasoline flowmeters are not temperature-compensated in the United States, but are temperaturecompensated in Canada. In other words, either the measured volume (in the US) or the measured temperature-corrected volume (in Canada) is used to infer mass.

Consider the following general analysis:

1. Air temperature differences between hot and cold climates are large. In addition, air temperature fluctuations between day and night in a given location can be large.

2. There is a significant difference between ground temperatures in hot and cold climates. However, ground temperature fluctuations between day and night in a given location is very small. Ground temperature fluctuation between summer and winter in a given location is relatively small.

3. Gasoline will be warm when it leaves the refinery, but will cool in transport to the retailer’s underground tank. Given time in the tank, the temperature of the gasoline will approach the ground temperature.

4. Flowmeter calibration is performed using standard weights, implying a calibration to mass.

These statements imply that despite wide air temperature fluctuations, the temperature of the gasoline pumped through the flowmeter should be nearly the same as the ground temperature. Because the ground temperature does not fluctuate very much, the temperature variation of the gasoline will be small throughout the year, so the mass of a gallon of gasoline should not vary much throughout the year from a given tank. Following this logic, the mass of a gallon of gasoline sold in Alaska should be the same as one sold in Nevada.

Fluctuations in gasoline temperature cause gasoline density changes. The magnitude with which these changes affect measurement accuracy can be quantified by performing an uncertainty analysis to determine if temperature compensation is appropriate. An uncertainty analysis for this measurement would likely reveal a number of sources of measurement uncertainty, such as (but not limited to) the effects of ambient air temperature, gasoline temperature leaving the refinery, transport time from the refinery to the tank, ground temperature, tank level prior to filling, the volume of gasoline in the flowmeter piping, flowmeter piping temperature, frequency of use, and composition changes. As a minimum, such analysis would likely reveal that the consumer would not be advised to purchase gasoline from a tank that was just filled with warm gasoline. A detailed analysis may reveal other significant issues.

While this is perhaps more information than one would like to know about the subject, this discussion clearly illustrates the need to understand the process — and that the same process may be different in different locations. Sometimes … it’s just not so easy.

A brief review — Part 3 addressed mass flow measurement, volumetric flow measurement, and inferred mass flow measurement. The measurement of gasoline was given as an example of the inferred mass flow measurement (using volumetric units). Comments resulted in Part 3.1 that addressed some issues associated with retail gasoline measurements. This sparked a flurry of comments regarding how gasoline is measured at the pump. This issue attempts to tie the comments together, so reading this issue without having read previous issues may prove difficult.

Gasoline pumps in the USA measure volume and are calibrated using volumetric means. In other words, they are true volumetric devices — they measure volume and indicate gallons. Even the New York Times offered advice to the consumer on this one with “… buy gasoline during the coolest time of the day — early morning or late evening — while the gasoline is most dense…” (New York Times, September 24, 2001, Empowered II Smart Energy Management, A clean car is an efficient car, page 7).

Gasoline pumps in Canada measure volume. This volume is then compensated for the actual temperature to indicate the volume of the gasoline as if it were a certain temperature. The compensated volume is an implied mass measurement. I suspect (but do not know) that these pumps are calibrated using volumetric means that are temperature compensated. In other words, they are inferred mass measurement devices and are calibrated as such — they measure volume and indicate in (temperature-compensated) liters. In Canada, the inferred mass of the gasoline received should be the same (within the limitations of the equipment) regardless of gasoline temperature. Note however that composition differences (and additives) may cause the density at a given temperature to be different than its nominal value. As an example, a 1% increase in gasoline density from its nominal value does not affect the actual volume measured, but will cause the inferred mass measurement to be 1% lower than the actual mass flow.

My comments on some readers’ responses follow:

One reader questioned whether the “wee hours of the am” would be the time when the gasoline would be at its lowest temperature in an underground tank. Thermal lag for underground gasoline storage tanks is an issue, but may not be significant. For science class, my daughter measured the temperatures 1 meter above and 1 meter below grade in the fall/winter (in the New York area). I seem to remember the ground temperature changing by only 1-2 degC over a period of months. The above ground temperature changed by 20 degC (or more?) during the same period. This issue is likely to be significant for above ground storage tanks (as suggested by other readers). Note however that filling the tank may cause larger (transient) effects caused by such issues as the quantity and temperature of the gasoline prior to fill, and the quantity and temperature of gasoline added. Not being able to sell compressed natural gas measured with a Coriolis mass flowmeter in kg or lbm (pounds mass) because it was not considered ‘marketable’ to the the public illustrates resistance to change. By the way, when will gasoline be sold by the kg or lbm — or better yet, by the BTU or Joule (as suggested by another reader)? I suspect that it will not be soon.

The comments and observations about beating the measurement were amusing. Society allows people to (reasonably) operate in their own self-interest. Parting with less money for a product is clearly in the purchaser’s self-interest. (Engineers sometimes call this an “optimization problem”, but that is an issue for another day.) Comments on how to beat the system were inevitable.

The safety point regarding gasoline expansion causing explosions and fires (after topping off a gas tank in a cold climate and then parking in a warm garage) is important. Virtually everything is potentially dangerous — even a small puddle of water that turns to ice…

Liquid flow Measurement

Both gas and liquid flow can be measured in volumetric or mass flow rates (such as litres per second or kg/s). These measurements can be converted between one another if the materials density is known. The density for a liquid is almost independent of the liquids conditions, however this is not the case for a gas, whose density highly depends upon pressure and temperature.

In engineering contexts, the volumetric flow rate is usually given the symbol Q and the mass flow rate the symbol \dot m.

[edit] Gas

Due to the nature of an Ideal gas or a Real gas, the volumetric gas flow rate will differ for the same mass flow rate when at differing temperatures and pressures. As such gas volumetric flow rate is sometimes measured in “standard cubic centimeters per minute” (abbreviation sccm). This unit, although not an SI unit is sometimes used due to the additional information attached to the unit symbol, which indicates the temperature and pressure of the gas. Many other similar abbreviations are also in use, for two reasons, firstly mass flow and volumetric flow can be equated at known conditions, and secondly due to the imperial system older units such as standard cubic feet per minute or per second may still be used in some countries. It is often necessary to employ standard gas relationships (such as the ideal gas law) to convert between units of mass flow and volumetric flow.

[edit] Liquid

For liquids other units used depend on the application and industry but might include gallons (U.S. liquid or imperial) per minute, liters per second, bushels per minute and, when describing river flows, cumecs (cubic metres per second) or acre-feet per day.

[edit] Mechanical flow meters

There are several types of mechanical flow meter

[edit] Piston Meter

Because they are used for domestic water measurement, piston meters, also known as rotary piston or semi-positive displacement meters, are the most common flow measurement devices in the UK and are used for almost all meter sizes up to and including 40 mm (1 1/2″). The piston meter operates on the principle of a piston rotating within a chamber of known volume. For each rotation, an amount of water passes through the piston chamber. Through a gear mechanism and, sometimes, a magnetic drive, a needle dial and odometer type display is advanced.

[edit] Woltmann Meter

Woltman meters, commonly referred to as Helix meters are popular at larger sizes. Jet meters (single or Multi-Jet) are increasing in popularity in the UK at larger sizes and are commonplace in the EU.

[edit] Multi-jet Meter

A multi-jet meter is a velocity type meter which has an impeller which rotates horizontally on a vertical shaft. The impeller element is in a housing in which multiple inlet ports direct the fluid flow at the impeller causing it to rotate in a specific direction in proportion to the flow velocity. This meter works mechanically much like a paddle wheel meter except that the ports direct the flow at the impeller equally from several points around the circumference of the element, where a paddle wheel normally only receives flow from one offset flow stream.

[edit] Venturi Meter

Another method of measurement, known as a venturi meter, is to constrict the flow in some fashion, and measure the differential pressure (using a pressure sensor) that results across the constriction. This method is widely used to measure flow rate in the transmission of gas through pipelines, and has been used since Roman Empire times.

[edit] Dall Tube

The Dall tube is a shortened version of a Venturi meter with a lower pressure drop than an orifice plate. Both flow meters the flow rate of Dall tube is determined by measuring the pressure drop caused by restriction in the conduit. The pressure differential is measured using diaphragm pressure transducers with digital read out. Since these meters have significantly lower permanent pressure losses than the orifice meters, the Dall tubes have widely been used for measuring the flow rate of large pipeworks.

[edit] Orifice Plate

Another simple method of measurement uses an orifice plate, which is basically a plate with a hole through it. It is placed in the flow and constricts the flow. It uses the same principle as the venturi meter in that the differential pressure relates to the velocity of the fluid flow (Bernoulli’s principle).

[edit] Pitot tube

A Pitot tube is a pressure measuring instrument used to measure fluid flow velocity by determining the stagnation pressure. Bernoulli’s equation is used to calculate the dynamic pressure and thence fluid velocity.

[edit] Multi-hole Pressure Probe

Multi-hole pressure probes (also called impact probes) extend the theory of pitot tube to more than one dimension. A typical impact probe consists of three or more holes (depending on the type of probe) on the measuring tip arranged in a specific pattern. More holes allow the instrument to measure the direction of the flow velocity in addition to its magnitude (after appropriate calibration). Three-holes arranged in a line allow the pressure probes to measure the velocity vector in two dimensions. Introduction of more holes e.g., five holes arranged in a ‘plus’ formation allow measurement of the three-dimensional velocity vector.

[edit] Paddle wheel

The paddle wheel translates the mechanical action of paddles rotating in the liquid flow around an axle into a user-readable rate of flow (gpm, lpm, etc.). The paddle tends to be inserted into the flow.

[edit] Pelton wheel

The Pelton wheel turbine (better described as a radial turbine) translates the mechanical action of the Pelton wheel rotating in the liquid flow around an axis into a user-readable rate of flow (gpm, lpm, etc.). The Pelton wheel tends to have all the flow traveling around it with the inlet flow focussed on the blades by a jet. The original Pelton wheels were used for the generation of power and consisted of a radial flow turbine with “reaction cups” which not only move with the force of the water on the face but return the flow in opposite direction using this change of fluid direction to further increase the efficiency of the turbine.

[edit] Optical Flow Meters

Optical flow meters use light to determine flow rate. Small particles which accompany natural and industrial gases pass through two laser beams focused in a pipe by illuminating optics. Laser light is scattered when a particle crosses the first beam. The detecting optics collects scattered light on a photodetector, which then generates a pulse signal. If the same particle crosses the second beam, the detecting optics collect scattered light on a second photodetector, which converts the incoming light into a second electrical pulse. By measuring the time interval between these pulses, the gas velocity is calculated as V=D/T where D is the distance between the laser beams and T is the time interval.

Laser-based optical flow meters measure the actual speed of particles, a property which is not dependent on thermal conductivity of gases, variations in gas flow or composition of gases. The different operating principle enables optical laser technology to deliver highly accurate flow data, even in challenging environments which may include high temperature, low flow rates, high pressure, high humidity, pipe vibration and acoustic noise.

Optical flow meters are very stable with no moving parts and deliver a highly repeatable measurement over the life of the product. Because distance between the two laser sheets does not change, optical flow meters do not require periodic calibration after its initial commissioning. Optical flow meters require only one installation point, instead of the two installation points typically required by other types of meters. A single installation point is simpler, requires less maintenance and is less prone to errors.

Optical flow meters are capable of measuring flow from 0.1m/s to faster than 100m/s (1000:1 turn down ratio) and have been demonstrated to be effective for the measurement of flare gases, a major global contributor to the emissions associated with climate change.[1]

[edit] Turbine flow meter

The turbine flow meter (better described as an axial turbine) translates the mechanical action of the turbine rotating in the liquid flow around an axis into a user-readable rate of flow (gpm, lpm, etc.). The turbine tends to have all the flow traveling around it.

The turbine wheel is set in the part of a fluid stream. The flowing fluid impinges on the turbine blades, imparting a force to the blade surface and setting the rotor in motion. when a steady rotation speed has been reached, the speed is proportional to fluid velocity.

[edit] Open Channel Flow Measurement

[edit] Level to Flow

The level of the water is measured at a designated point behind a hydraulic structure (a weir or flume) using various means (bubblers, ultrasonic, float, and differential pressure are common methods). This depth is converted to a flow rate according to a theoretical formula of the form Q=KHX where Q is the flow rate, K is a constant, H is the water level and X is an exponent which varies with the device used, or it is converted according to empirically derived level/flow data points (a ‘flow curve’). The flow rate can then integrated over time into volumetric flow.

[edit] Area/Velocity

The cross-sectional area of the flow is calculated from a depth measurement and the average velocity of the flow is measured directly (doppler and propeller methods are common). Velocity times the cross-sectional area yields a flow rate which can be integrated into volumetric flow.

[edit] Dye Testing

A known amount of dye per unit time is added to a flow stream. After complete mixing, the concentration of the dye is measured. The dilution rate of the dye equals the flow rate.

[edit] Thermal mass flow meters

Thermal mass flow meters generally use combinations of heated elements and temperature sensors to measure the difference between static and flowing heat transfer to a fluid and infer its flow with a knowledge of the fluid’s specific heat and density. The fluid temperature is also measured and compensated for. If the density and specific heat characteristics of the fluid are constant, the meter can provide a direct mass flow readout, and does not need any additional pressure temperature compensation over their specified range.

Technological progress allows today to manufacture thermal mass flow meters on a microscopic scale as MEMS sensors, these flow devices can be used to measure flow rates in the range of nano litres or micro litres per minute.

Thermal mass flow meters are used for compressed air, nitrogen, helium, argon, oxygen, natural gas. In fact, most gases can be measured as long as they are fairly clean and

Fire Gas Detection SYstem

1: Fire Growth and Behavior
Before attempting to understand fire detection systems and automatic sprinklers, it is beneficial to possess a basic knowledge of fire development and behavior. With this information, the role and interaction of these supplemental fire safety systems in the protection process can then be better realized.

Basically, a fire is a chemical reaction in which a carbon based material (fuel), mixes with oxygen (usually as a component of air), and is heated to a point where flammable vapors are produced. These vapors can then come in contact with something that is hot enough to cause vapor ignition, and a resulting fire. In simple terms, something that can burn touches something that is hot, and a fire is produced.

Libraries, archives, museums, and historic structures frequently contain numerous fuels. These include books, manuscripts, records, artifacts, combustible interior finishes, cabinets, furnishings, and laboratory chemicals. It should be recognized that any item containing wood, plastic, paper, fabric, or combustible liquids is a potential fuel. They also contain several common, potential ignition sources including any item, action, or process which produces heat. These encompass electric lighting and power systems, heating and air conditioning equipment, heat producing conservation and maintenance activities, and electric office appliance. Flame generating construction activities such as soldering, brazing, and cutting are frequent sources of ignition. Arson is unfortunately one of the most common cultural property ignition sources, and must always be considered in fire safety planning.

When the ignition source contacts the fuel, a fire can start. Following this contact, the typical accidental fire begins as a slow growth, smoldering process which may last from a few minutes to several hours. The duration of this “incipient” period is dependent on a variety of factors including fuel type, its physical arrangement, and quantity of available oxygen. During this period heat generation increases, producing light to moderate volumes of smoke. The characteristic smell of smoke is usually the first indication that an incipient fire is underway. It is during this stage that early detection (either human or automatic), followed by a timely response by qualified fire emergency professionals, can control the fire before significant losses occur.

As the fire reaches the end of the incipient period, there is usually enough heat generation to permit the onset of open, visible flames. Once flames have appeared, the fire changes from a relatively minor situation to a serious event with rapid flame and heat growth. Ceiling temperatures can exceed 1,000° C (1,800° F) within the first minutes. These flames can ignite adjacent combustible contents within the room, and immediately endanger the lives of the room’s occupants. Within 3-5 minutes, the room ceiling acts like a broiler, raising temperatures high enough to “flash”, which simultaneously ignites all combustibles in the room. At this point, most contents will be destroyed and human survivability becomes impossible. Smoke generation in excess of several thousand cubic meters (feet) per minute will occur, obscuring visibility and impacting contents remote from the fire.

If the building is structurally sound, heat and flames will likely consume all remaining combustibles and then self extinguish (burn out). However, if wall and/or ceiling fire resistance is inadequate, (i.e. open doors, wall/ceiling breaches, combustible building construction), the fire can spread into adjacent spaces, and start the process over. If the fire remains uncontrolled, complete destruction or “burn out” of the entire building and contents may ultimately result.

Successful fire suppression is dependent on extinguishing flames before, or immediately upon, flaming combustion. Otherwise, the resulting damage may be too severe to recover from. During the incipient period, a trained person with portable fire extinguishers may be an effective first line of defense. However, should an immediate response fail or the fire grow rapidly, extinguisher capabilities can be surpassed within the first minute. More powerful suppression methods, either fire department hoses or automatic systems, then become essential.

A fire can have far reaching impact on the institution’s buildings, contents and mission. General consequences may include:

* Collections damage. Most heritage institutions house unique and irreplaceable objects. Fire generated heat and smoke can severely damage or totally destroy these items beyond repair.

* Operations and mission damage. Heritage occupancies often contain educational facilities, conservation laboratories, catalogue services, administrative/support staff offices, exhibition production, retail, food service, and a host of other activities. A fire can shut these down with adverse impact on the organization’s mission and its clientele.

* Structure damage. Buildings provide the “shell” that safeguards collections, operations and occupants from weather, pollution, vandalism and numerous other environmental elements. A fire can destroy walls, floors, ceiling/roof assemblies and structural support, as well as systems that illuminate, control temperature and humidity, and supply electrical power. This can in turn lead to content harm, and expensive relocation activities.

* Knowledge loss. Books, manuscripts, photographs, films, recordings and other archival collections contain a vast wealth of information that can be destroyed by fire.

* Injury or loss of life. The lives of staff and visitors can be endangered.

* Public relations impact. Staff and visitors expect safe conditions in heritage buildings. Those who donate or loan collections presume these items will be safeguarded. A severe fire could shake public confidence and cause a devastating public relations impact.

* Building security. A fire represents the single greatest security threat! Given the same amount of time, an accidental or intentionally set fire can cause far greater harm to collections than the most accomplished thieves. Immense volumes of smoke and toxic gases can cause confusion and panic, thereby creating the ideal opportunity for unlawful entry and theft. Unrestricted firefighting operations will be necessary, adding to the security risk. Arson fires set to conceal a crime are common.

To minimize fire risk and its impact, heritage institutions should develop and implement comprehensive and objective fire protection programs. Program elements should include fire prevention efforts, building construction improvements, methods to detect a developing fire and alert emergency personnel, and means to effectively extinguish a fire. Each component is important toward overall accomplishment of the institution’s fire safety goal. It is important for management to outline desired protection objectives during a fire and establish a program that addresses these goals. Therefore, the basic question to be asked by the property’s managers is, “What maximum fire size and loss can the institution accept?” With this information, goal oriented protection can be implemented.

2: Fire Detection and Alarm Systems
2.1: Introduction
A key aspect of fire protection is to identify a developing fire emergency in a timely manner, and to alert the building’s occupants and fire emergency organizations. This is the role of fire detection and alarm systems. Depending on the anticipated fire scenario, building and use type, number and type of occupants, and criticality of contents and mission, these systems can provide several main functions. First they provide a means to identify a developing fire through either manual or automatic methods and second, they alert building occupants to a fire condition and the need to evacuate. Another common function is the transmission of an alarm notification signal to the fire department or other emergency response organization. They may also shut down electrical, air handling equipment or special process operations, and they may be used to initiate automatic suppression systems. This section will describe the basic aspects of fire detection and alarm systems.

2.2: Control Panels
The control panel is the “brain” of the fire detection and alarm system. It is responsible for monitoring the various alarm “input” devices such as manual and automatic detection components, and then activating alarm “output” devices such as horns, bells, warning lights, emergency telephone dialers, and building controls. Control panels may range from simple units with a single input and output zone, to complex computer driven systems that monitor several buildings over an entire campus. There are two main control panel arrangements, conventional and addressable, which will be discussed below.

Conventional or “point wired” fire detection and alarm systems were for many years the standard method for providing emergency signaling. In a conventional system one or more circuits are routed through the protected space or building. Along each circuit, one or more detection devices are placed. Selection and placement of these detectors is dependent upon a variety of factors including the need for automatic or manual initiation, ambient temperature and environmental conditions, the anticipated type of fire, and the desired speed of response. One or more device types are commonly located along a circuit to address a variety of needs and concerns.

Upon fire occurrence, one or more detectors will operate. This action closes the circuit, which the fire control panel recognizes as an emergency condition. The panel will then activate one or more signaling circuits to sound building alarms and summon emergency help. The panel may also send the signal to another alarm panel so that it can be monitored from a remote point.

In order to help insure that the system is functioning properly, these systems monitor the condition of each circuit by sending a small current through the wires. Should a fault occur, such as due to a wiring break, this current cannot proceed and is registered as a “trouble” condition. The indication is a need for service somewhere along the respective circuit.

In a conventional alarm system, all alarm initiating and signaling is accomplished by the system’s hardware which includes multiple sets of wire, various closing and opening relays, and assorted diodes. Because of this arrangement, these systems are actually monitoring and controlling circuits, and not individual devices.

To further explain this, assume that a building’s fire alarm system has 5 circuits, zones A through E, and that each circuit has 10 smoke detectors and 2 manual stations located in various rooms of each zone. A fire ignition in one of the rooms monitored by zone “A” causes a smoke detector to go into alarm. This will be reported by the fire alarm control panel as a fire in circuit or zone “A”. It will not indicate the specific detector type nor location within this zone. Emergency responding personnel may need to search the entire zone to determine where the device is reporting a fire. Where zones have several rooms, or concealed spaces, this response can be time consuming and wasteful of valuable response opportunity.

The advantage of conventional systems is that they are relatively simple for small to intermediate size buildings. Servicing does not require a large amount of specialized training.

A disadvantage is that for large buildings, they can be expensive to install because of the extensive amounts of wire that are necessary to accurately monitor initiating devices.

Conventional systems may also be inherently labor intensive and expensive to maintain. Each detection device may require some form of operational test to verify it is in working condition. Smoke detectors must be periodically removed, cleaned, and recalibrated to prevent improper operation. With a conventional system, there is no accurate way of determining which detectors are in need of servicing. Consequently, each detector must be removed and serviced, which can be a time consuming, labor intensive, and costly endeavor. If a fault occurs, the “trouble” indication only states that the circuit has failed, but does not specifically state where the problem is occurring. Subsequently, technicians must survey the entire circuit to identify the problem.

Addressable or “intelligent” systems represent the current state-of-the-art in fire detection and alarm technology. Unlike conventional alarm methods, these systems monitor and control the capabilities of each alarm initiating and signaling device through microprocessors and system software. In effect, each intelligent fire alarm system is a small computer overseeing and operating a series of input and output devices.

Like a conventional system, the address system consists of one or more circuits that radiate throughout the space or building. Also, like standard systems, one or more alarm initiating devices may be located along these circuits. The major difference between system types involves the way in which each device is monitored. In an addressable system, each initiating device (automatic detector, manual station, sprinkler waterflow switch, etc.) is given a specific identification or “address”. This address is correspondingly programmed into the control panel’s memory with information such as the type of device, its location, and specific response details such as which alarm devices are to be activated.

The control panel’s microprocessor sends a constant interrogation signal over each circuit, in which each initiating device is contacted to inquire its status (normal or emergency). This active monitoring process occurs in rapid succession, providing system updates every 5 to 10 seconds.

The addressable system also monitors the condition of each circuit, identifying any faults which may occur. One of the advancements offered by these systems is their ability to specifically identify where a fault has developed. Therefore, instead of merely showing a fault along a wire, they will indicate the location of the problem. This permits faster diagnosis of the trouble, and allows a quicker repair and return to normal.

Advantages provided by addressable alarm systems include stability, enhanced maintenance, and ease of modification. Stability is achieved by the system software. If a detector recognizes a condition which could be indicative of a fire, the control panel will first attempt a quick reset. For most spurious situations such as insects, dust, or breezes, the incident will often remedy itself during this reset procedure, thereby reducing the probability of false alarm. If a genuine smoke or fire condition exists, the detector will reenter the alarm mode immediately after the reset attempt. The control panel will now regard this as a fire condition, and will enter its alarm mode.

With respect to maintenance, these systems offer several key advantages over conventional ones. First of all, they are able to monitor the status of each detector. As a detector becomes dirty, the microprocessor recognizes a decreased capability, and provides a maintenance alert. This feature, known as Listed Integral Sensitivity Testing, allows facilities personnel to service only those detectors that need attention, rather than requiring a labor and time consuming cleaning of all units.

Advanced systems, such as the FCI 7200 incorporate another maintenance feature known as drift compensation. This software procedure adjusts the detector’s sensitivity to compensate for minor dust conditions. This avoids the ultra sensitive or “hot” detector condition which often results as debris obscures the detector’s optics. When the detector has been compensated to its limit, the control panel alerts maintenance personnel so that servicing can be performed.

Modifying these systems, such as to add or delete a detector, involves connecting or removing the respective device from the addressable circuit, and changing the appropriate memory section. This memory change is accomplished either at the panel or on a personal computer, with the information downloaded into the panel’s microprocessor.

The main disadvantage of addressable systems is that each system has its own unique operating characteristics. Therefore, service technicians must be trained for the respective system. The training program is usually a 3-4 day course at the respective manufacturer’s facility. Periodic update training may be necessary as new service methods are developed.

2.3: Fire Detectors
When present, humans can be excellent fire detectors. The healthy person is able to sense multiple aspects of a fire including the heat, flames, smoke, and odors. For this reason, most fire alarm systems are designed with one or more manual alarm activation devices to be used by the person who discovers a fire. Unfortunately, a person can also be an unreliable detection method since they may not be present when a fire starts, may not raise an alarm in an effective manner, or may not be in perfect heath to recognize fire signatures. It is for this reason that a variety of automatic fire detectors have been developed. Automatic detectors are meant to imitate one or more of the human senses of touch, smell or sight. Thermal detectors are similar to our ability to identify high temperatures, smoke detectors replicate the sense of smell, and flame detectors are electronic eyes. The properly selected and installed automatic detector can be a highly reliable fire sensor.

Manual fire detection is the oldest method of detection. In the simplest form, a person yelling can provide fire warning. In buildings, however, a person’s voice may not always transmit throughout the structure. For this reason, manual alarm stations are installed. The general design philosophy is to place stations within reach along paths of escape. It is for this reason that they can usually be found near exit doors in corridors and large rooms.

The advantage of manual alarm stations is that, upon discovering the fire, they provide occupants with a readily identifiable means to activate the building fire alarm system. The alarm system can then serve in lieu of the shouting person’s voice. They are simple devices, and can be highly reliable when the building is occupied. The key disadvantage of manual stations is that they will not work when the building is unoccupied. They may also be used for malicious alarm activations. Nonetheless, they are an important component in any fire alarm system.

Thermal detectors are the oldest type of automatic detection device, having origin in the mid 1800’s, with several styles still in production today. The most common units are fixed temperature devices that operate when the room reaches a predetermined temperature (usually in the 135°-165°F/57°-74°C). The second most common type of thermal sensor is the rate-of-rise detector, which identifies an abnormally fast temperature climb over a short time period. Both of these units are “spot type” detectors, which means that they are periodically spaced along a ceiling or high on a wall. The third detector type is the fixed temperature line type detector, which consists of two cables and an insulated sheathing that is designed to breakdown when exposed to heat. The advantage of line type over spot detection is that thermal sensing density can be increased at lower cost.

Thermal detectors are highly reliable and have good resistance to operation from nonhostile sources. They are also very easy and inexpensive to maintain. On the down side, they do not function until room temperatures have reached a substantial temperature, at which point the fire is well underway and damage is growing exponentially. Subsequently, thermal detectors are usually not permitted in life safety applications. They are also not recommended in locations where there is a desire to identify a fire before substantial flames occur, such as spaces where high value thermal sensitive contents are housed.

Smoke detectors are a much newer technology, having gained wide usage during the 1970’s and 1980’s in residential and life safety applications. As the name implies, these devices are designed to identify a fire while in its smoldering or early flame stages, replicating the human sense of smell. The most common smoke detectors are spot type units, that are placed along ceilings or high on walls in a manner similar to spot thermal units. They operate on either an ionization or photoelectric principle, with each type having advantages in different applications. For large open spaces such as galleries and atria, a frequently used smoke detector is a projected beam unit. This detector consists of two components, a light transmitter and a receiver, that are mounted at some distance (up to 300 ft/100m) apart. As smoke migrates between the two components, the transmitted light beam becomes obstructed and the receiver is no longer able to see the full beam intensity. This is interpreted as a smoke condition, and the alarm activation signal is transmitted to the fire alarm panel.

A third type of smoke detector, which has become widely used in extremely sensitive applications, is the air aspirating system. This device consists of two main components: a cotrol unit that houses the detection chamber, an aspiration fan and operation circuitry; and a network of sampling tubes or pipes. Along the pipes are a series of ports that are designed to permit air to enter the tubes and be transported to the detector. Under normal conditions, the detector constantly draws an air sample into the detection chamber, via the pipe network. The sample is analyzed for the existence of smoke, and then returned to atmosphere. If smoke becomes present in the sample, it is detected and an alarm signal is transmitted to the main fire alarm control panel. Air aspirating detectors are extremely sensitive and are typically the fastest responding automatic detection method. Many high technology organizations, such as telephone companies, have standardized on aspiration systems. In cultural properties they are used for areas such as collections storage vaults and highly valuable rooms. These are also frequently used in aesthetically sensitive applications since components are often easier to conceal, when compared to other detection methods.

The key advantage of smoke detectors is their ability to identify a fire while it is still in its incipient. As such, they provide added opportunity for emergency personnel to respond and control the developing fire before severe damage occurs. They are usually the preferred detection method in life safety and high content value applications. The disadvantage of smoke detectors is that they are usually more expensive to install, when compared to thermal sensors, and are more resistant to inadvertent alarms. However, when properly selected and designed, they can be highly reliable with a very low probability of false alarm.

Flame detectors represent the third major type of automatic detection method, and imitate the human sense of sight. They are line of sight devices that operate on either an infrared, ultraviolet or combination principle. As radiant energy in the approximate 4,000 to 7,700 angstroms range occurs, as indicative of a flaming condition, their sensing equipment recognizes the fire signature and sends a signal to the fire alarm panel.

The advantage of flame detection is that it is extremely reliable in a hostile environment. They are usually used in high value energy and transportation applications where other detectors would be subject to spurious activation. Common uses include locomotive and aircraft maintenance facilities, refineries and fuel loading platforms, and mines. A disadvantage is that they can be very expensive and labor intensive to maintain. Flame detectors must be looking directly at the fire source, unlike thermal and smoke detectors which can identify migrating fire signatures. Their use in cultural properties is extremely limited.

2.4: Alarm Output Devices
Upon receiving an alarm notification, the fire alarm control panel must now tell someone that an emergency is underway. This is the primary function of the alarm output aspect of a system. Occupant signaling components include various audible and visual alerting components, and are the primary alarm output devices. Bells are the most common and familiar alarm sounding device, and are appropriate for most building applications. Horns are another option, and are especially well suited to areas where a loud signal is needed such as library stacks, and architecturally sensitive buildings where devices need partial concealment. Chimes may be used where a soft alarm tone is preferred, such as health care facilities and theaters. Speakers are the fourth alarm sounding option, which sound a reproducible signal such as a recorded voice message. They are often ideally suited for large, multistory or other similar buildings where phased evacuation is preferred. Speakers also offer the added flexibility of emergency public address announcements. With respect to visual alert, there are a number of strobe and flashing light devices. Visual alerting is required in spaces where ambient noise levels are high enough to preclude hearing sounding equipment, and where hearing impaired occupants may be found. Standards such as the Americans with Disabilities Act (ADA) mandate visual devices in numerous museum, library, and historic building applications.

Another key function of the output function is emergency response notification. The most common arrangement is an automatic telephone or radio signal that is communicated to a constantly staffed monitoring center. Upon receiving the alert, the center will then contact the appropriate fire department, providing information about the location of alarm. In some instances, the monitoring station may be the police or fire departments, or a 911 center. In other instances it will be a private monitoring company that is under contract to the organization. In many cultural properties, the building’s inhouse security service may serve as the monitoring center.

Other output functions include shutting down electrical equipment such as computers, shutting off air handling fans to prevent smoke migration, and shutting down operations such as chemical movement through piping in the alarmed area. They may also activate fans to extract smoke, which is a common function in large atria spaces. These systems can also activate discharge of gaseous fire extinguishing systems, or preaction sprinkler systems.

2.5: Summary
In summary, there are several options for a building’s fire detection and alarm system. The ultimate system type, and selected components, will be dependent upon the building construction and value, its use or uses, the type of occupants, mandated standards, content value, and mission sensitivity. Contacting a fire engineer or other appropriate professional who understands fire problems and the different alarm and detection options is usually a preferred first step to find the best system.

3: Fire Sprinklers
3.1: Introduction
For most fires, water represents the ideal extinguishing agent. Fire sprinklers utilize water by direct application onto flames and heat, which causes cooling of the combustion process and prevents ignition of adjacent combustibles. They are most effective during the fire’s initial flame growth stage, while the fire is relatively easy to control. A properly selected sprinkler will detect the fire’s heat, initiate alarm, and begin suppression within moments after flames appear. In most instances sprinklers will control fire advancement within a few minutes of their activation, which will in turn result in significantly less damage than otherwise would happen without sprinklers.

Among the potential benefits of sprinklers are the following:

* Immediate identification and control of a developing fire. Sprinkler systems respond at all times, including periods of low occupancy. Control is generally instantaneous.

* Immediate alert. In conjunction with the building fire alarm system, automatic sprinkler systems will notify occupants and emergency response personnel of the developing fire.

* Reduced heat and smoke damage. Significantly less heat and smoke will be generated when the fire is extinguished at an early stage.

* Enhanced life safety. Staff, visitors and fire fighters will be subject to less danger when fire growth is checked.

* Design flexibility. Egress route and fire/smoke barrier placement becomes less restrictive since early fire control minimizes demand on these systems. Many fire and building codes will permit design and operations flexibility based on the presence of a fire sprinkler system.

* Enhanced security. A sprinkler controlled fire can reduce demand on security forces by minimizing intrusion and theft opportunities.

* Decreased insurance expenditure. Sprinkler controlled fires are less damaging than fires in nonsprinklered buildings. Insurance underwriters may offer reduced premiums in sprinkler protected properties.

These benefits should be considered when deciding on the selection of automatic fire sprinkler protection.

3.2: Sprinkler System Components and Operation
Sprinkler systems are essentially a series of water pipes that are supplied by a reliable water supply. At selected intervals along these pipes are independent, heat activated valves known as sprinkler heads. It is the sprinkler that is responsible for water distribution onto the fire. Most sprinkler systems also include an alarm to alert occupants and emergency forces when sprinkler activation (fire) occurs.

During the incipient fire stage, the heat output is relatively low and is unable to cause sprinkler operation. However, as the fire intensity increases, the sprinkler’s sensing elements become exposed to elevated temperatures (typically in excess of 57-107°C (135-225°F), and begin to deform. Assuming temperatures remain high, as they would during an increasing fire, the element will fatigue after an approximate 30 to 120 second period. This releases the sprinkler’s seals allowing water to discharge onto the fire and begin the suppression action. In most situations less than 2 sprinklers are needed to control the fire. In fast growing fire scenarios, however, such as a flammable liquid spill, up to 12 sprinklers may be required.

In addition to normal fire control efforts, sprinkler operation may be interconnected to initiate building and fire department alarms, shutdown electrical and mechanical equipment, close fire doors and dampers, and suspend some processes.

As fire fighters arrive their efforts will focus on ensuring that the system has contained the fire, and, when satisfied, shut off the water flow to minimize water damage. It is at this point that staff will normally be permitted to enter the damaged space and perform salvage duties.

3.3: System Components and Types
The basic components of a sprinkler system are the sprinklers, system piping, and a dependable water source. Most systems also require an alarm, system control valves, and means to test the equipment.

The sprinkler itself is the spray nozzle, which distributes water over a defined fire hazard area (typically 14-21 m2/150-225 ft2) with each sprinkler operating by actuation of its own temperature linkage. The typical sprinkler consists of a frame, thermal operated linkage, cap, orifice, and deflector. Styles of each component may vary but the basic principles of each remain the same.

* Frame. The frame provides the main structural component which holds the sprinkler together. Water supply piping is connected to the sprinkler at the base of the frame. The frame holds the thermal linkage and cap in place, and supports the deflector during discharge. Frame styles include standard and low profile, flush, and concealed mount. Some are designed for extended spray coverage, beyond the range of normal sprinklers. Standard finishes include brass, chrome, black, and white, while custom finishes are available for aesthetically sensitive spaces. Special coatings are available for areas subject to high corrosive effect. Selection of a specific frame style is dependent on the size and type of area to be covered, anticipated hazard, visual impact features, and atmospheric conditions.

* Thermal linkage. The thermal linkage is the component that controls water release. Under normal conditions the linkage holds the cap in place and prevents water flow. As the link is exposed to heat, however, it weakens and releases the cap. Common linkage styles include soldered metal levers, frangible glass bulbs, and solder pellets. Each link style is equally dependable.

Upon reaching the desired operating temperature, an approximate 30 second to 4 minute time lag will follow. This lag is the time required for linkage fatigue and is largely controlled by the link materials and mass. Standard responding sprinklers operate closer to the 3-4 minute mark while quick response (QR) sprinklers operate in significantly shorter periods. Selection of a sprinkler response characteristic is dependent upon the existing risk, acceptable loss level, and desired response action.

In heritage applications the advantage of quick response sprinklers often becomes apparent. The faster a sprinkler reacts to a fire, the sooner the suppression activity is initiated, and the lower the potential damage level. This is particularly beneficial in high value or life safety applications where the earliest possible extinguishment is a fire protection goal. It is important to understand that response time is independent of response temperature. A quicker responding sprinkler will not activate at a lower temperature than a comparable standard head.

* Cap. The cap provides the water tight seal which is located over the sprinkler orifice. It is held in place by the thermal linkage, and falls from position after linkage heating to permit water flow. Caps are constructed solely of metal or a metal with a teflon disk.

* Orifice. The machined opening at the base of the sprinkler frame is the orifice from which extinguishing water flows. Most orifice openings are 15 mm (1/2 inch) diameter with smaller bores available for residential applications and larger openings for higher hazards.

* Deflector. The deflector is mounted on the frame opposite the orifice. Its purpose is to break up the water stream discharging from the orifice into a more efficient extinguishing pattern. Deflector styles determine how the sprinkler is mounted, with common sprinkler mounting styles known as upright (mounted above the pipe), pendent (mounted below the pipe, i.e. under ceilings), and sidewall sprinklers which discharge water in a lateral position from a wall. The sprinkler must be mounted as designed to ensure proper action. Selection of a particular style is often dependent upon physical building constraints.

A sprinkler that has received wide spread interest for museum applications is the on/off sprinkler. The principle behind these products is that as a fire occurs, water discharge and extinguishing action will happen similar to standard sprinklers. As the room temperature is cooled to a safer level, a bimetallic snap disk on the sprinkler closes and water flow ceases. Should the fire reignite, operation will once again occur. The advantage of on/off sprinklers is their ability to shut off, which theoretically can reduce the quantity of water distributed and resultant damage levels. The problem, however, is the long time period that may pass before room temperatures are sufficiently cooled to the sprinkler’s shut off point. In most heritage applications, the building’s construction will retain heat and prevent the desired sprinkler shut down. Frequently, fire emergency response forces will have arrived and will be able to close sprinkler zone control valves before the automatic shut down feature has functioned.

On-off sprinklers typically cost 8-10 times more than the average sprinkler, which is only justifiable when assurance can be made that these products will perform as intended. Therefore, on/off sprinkler use in heritage facilities should remain limited.

Selection of specific sprinklers is based on: risk characteristics, ambient room temperature, desired response time, hazard criticality and aesthetic factors. Several sprinkler types may be used in a heritage facility.

All sprinkler systems require a reliable water source. In urban areas, a piped public service is the most common supply, while rural areas generally utilize private tanks, reservoirs, lakes, or rivers. Where a high degree of reliability is desired, or a single source is undependable, multiple supplies may be utilized.

Basic water source criteria include:

* The source must be available at all times. Fires can happen at any time and therefore, the water supply must be in a constant state of readiness. Supplies must be evaluated for resistance to pipe failure, pressure loss, droughts, and other issues that may impact availability.

* The system must provide adequate sprinkler supply and pressure. A sprinkler system will create a hydraulic demand, in terms of flow and pressure, on the water supply. The supply must be capable of meeting this demand. Otherwise, supplemental components such as a fire pump or standby tank must be added to the system.

* The supply must provide water for the anticipated fire duration. Depending of the fire hazard, suppression may take several minutes to over an hour. The selected source must be capable of providing sprinklers with water until suppression has been achieved.

* The system must provide water for fire department hoses operating in tandem with the sprinkler system. Most fire department procedures involve the use of fire attack hoses to supplement sprinklers. The water supply must be capable of handling this additional demand without adverse impact on sprinkler performance.

Sprinkler water is transported to fire via a system of fixed pipes and fittings. Piping material options include various steel alloys, copper, and fire resistant plastics. Steel is the traditional material with copper and plastics utilized in many sensitive applications.

Primary considerations for selection of pipe materials include:

* Ease of installation. The easier the material is installed, the less disruption is imposed on the institution’s operations and mission. The ability to install a system with the least amount of disturbance is an important consideration, especially in sprinkler retrofit applications where building use will continue during construction.

* Cost of material versus cost of protected area. Piping typically represents the greatest single cost item in a sprinkler system. Often there is a temptation to reduce costs by utilizing less expensive piping materials that may be perfectly acceptable in certain instances, i.e. office or commercial environs. However, in heritage applications where the value of contents may be far beyond sprinkler costs, appropriateness of the piping rather than cost should be the deciding factor.

* Contractor familiarity with materials. A mistake to be avoided is one in which the contractor and pipe materials have been selected, only to find out that the contractor is inexperienced with the pipe. This can lead to installation difficulties, added expense, and increased failure potential. A contractor must demonstrate familiarity with the desired material before selection.

* Prefabrication requirements or other installation constraints. In some instances, such as in fine art vaults, requirements may be imposed to limit the amount of work time in the space. This will often require extensive prefabrication work outside of the work area. Some materials are easily adapted to prefabrication.

* Material cleanliness. Some pipe materials are cleaner to install than others. This will reduce the potential for soiling collections, displays, or building finishes during installation. Various materials are also resistant to accumulation in the system water, which could discharge onto collections. Cleanliness of installation and discharge should be a consideration.

* Labor requirements. Some pipe materials are heavier or more cumbersome to work with than others. Consequently additional workers are needed to install pipes, which can add to installation costs. If the number of construction workers allowed into the building is a factor, lighter materials may be beneficial.

The benefits and disadvantages of each material should be evaluated prior to selection of pipe materials.

Other major sprinkler system components include:

* Control valves. A sprinkler system must be capable of shut down after the fire has been controlled, and for periodic maintenance and modification. In the simplest system a single shutoff valve may be located at the point where the water supply enters the building. In larger buildings the sprinkler system may consist of multiple zones with a control valve for each. Control valves should be located in readily identified locations to assist responded emergency personnel.

* Alarms. Alarms alert building occupants and emergency forces when a sprinkler water flow occurs. The simplest alarms are water driven gongs supplied by the sprinkler system. Electrical flow and pressure switches, connected to a building fire alarm system, are more common in large buildings. Alarms are also provided to alert building management when a sprinkler valve is closed.

* Drain and test connections. Most sprinkler systems have provisions to drain pipes during system maintenance. Drains should be properly installed to remove all water from the sprinkler system, and prevent water from leakage onto protected spaces, when piping service is necessary. It is advisable to install drains at a remote location from the supply, thereby permitting effective system flushing to remove debris. Test connections are usually provided to simulate the flow of a sprinkler, thereby verifying the working condition of alarms. Test connections should be operated every 6 months.

* Specialty valves. Drypipe and preaction sprinkler systems require complex, special control valves that are designed to hold water from the system piping until needed. These control valves also include air pressure maintenance equipment and emergency operation/release systems.

* Fire Hose Connections. Fire fighters will often supplement sprinkler systems with hoses. Firefighting tasks are enhanced by installing hose connections to sprinkler system piping. The additional water demand imposed by these hoses must be factored into the overall sprinkler design in order to prevent adverse system performance.

3.4: System Types
There are three basic types of sprinkler systems: wet pipe, dry pipe and preaction, with each having applicability, depending on a variety of conditions such as potential fire severity, anticipated fire growth rates, content water sensitivity, ambient conditions, and desired response. In large multifunction facilities, such as a major museum or library, two or more system types may be employed.

Wet pipe systems are the most common sprinkler system. As the name implies, a wet pipe system is one in which water is constantly maintained within the sprinkler piping. When a sprinkler activates this water is immediately discharged onto the fire.

Wet pipe system advantages include:

* System simplicity and reliability. Wet pipe sprinkler systems have the least number of components and therefore, the lowest number of items to malfunction. This produces unexcelled reliability, which is important since sprinklers may be asked to sit in waiting for many years before they are needed. This simplicity aspect also becomes important in facilities where system maintenance may not be performed with the desired frequency.

* Relative low installation and maintenance expense. Due to their overall simplicity, wet pipe sprinklers require the least amount of installation time and capital. Maintenance cost savings are also realized since less service time is generally required, compared to other system types. These savings become important when maintenance budgets are shrinking.

* Ease of modification. Heritage institutions are often dynamic with respect to exhibition and operation spaces. Wet pipe systems are advantageous since modifications involve shutting down the water supply, draining pipes, and making alterations. Following the work, the system is pressure tested and restored. Additional work for detection and special control equipment is avoided, which again saves time and expense.

* Short term down time following a fire. Wet pipe sprinkler systems require the least amount of effort to restore. In most instances, sprinkler protection is reinstated by replacing the fused sprinklers and turning the water supply back on. Preaction and drypipe systems may require additional effort to reset control equipment.

The main disadvantage of these systems is that they are not suited for subfreezing environments. There also may be concern where piping is subject to severe impact damage, such as some warehouses.

The advantages of wet systems make them highly desirable for use in most heritage applications, and with limited exception, they represent the system of choice for museum, library and historic building protection.

The next system type, a dry pipe sprinkler system, is one in which pipes are filled with pressurized air or nitrogen, rather than water. This air holds a remote valve, known as a dry pipe valve, in a closed position. The drypipe valve is located in a heated area and prevents water from entering the pipe until a fire causes one or more sprinklers to operate. Once this happens, the air escapes and the dry pipe valve releases. Water then enters the pipe, flowing through open sprinklers onto the fire.

The main advantage of dry pipe sprinkler systems is their ability to provide automatic protection in spaces where freezing is possible. Typical dry pipe installations include unheated warehouses and attics, outside exposed loading docks and within commercial freezers.

Many heritage managers view dry pipe sprinklers as advantageous for protection of collections and other water sensitive areas, with a perceived benefit that a physically damaged wet pipe system will leak while dry pipe systems will not. In these situations, however, dry pipe systems will generally not offer any advantage over wet pipe systems. Should impact damage happen, there will only be a mild discharge delay, i.e. 1 minute, while air in the piping is released before water flow.

Dry pipe systems have some disadvantages that must be evaluated before selecting this equipment. These include:

* Increased complexity. Dry pipe systems require additional control equipment and air pressure supply components, which increases system complexity. Without proper maintenance this equipment may be less reliable than a comparable wet pipe system.

* Higher installation and maintenance costs. The added complexity impacts the overall drypipe installation cost. This complexity also increases maintenance expenditure, primarily due to added service labor costs.

* Lower design flexibility. There are strict requirements regarding the maximum permitted size (typically 750 gallons) of individual drypipe systems. These limitations may impact the ability of an owner to make system additions.

* Increased fire response time. Up to 60 seconds may pass from the time a sprinkler opens until water is discharged onto the fire. This will delay fire extinguishing actions, which may produce increased content damage.

* Increased corrosion potential. Following operation, drypipe sprinkler systems must be completely drained and dried. Otherwise, remaining water may cause pipe corrosion and premature failure. This is not a problem with wet pipe systems where water is constantly maintained in piping.

With the exception of unheated building spaces and freezer rooms, dry pipe systems do not offer any significant advantages over wet pipe systems and their use in heritage buildings is generally not recommended.

The third sprinkler system type, preaction, employs the basic concept of a dry pipe system in that water is not normally contained within the pipes. The difference, however, is that water is held from piping by an electrically operated valve, known as a preaction valve. The operation of this valve is controlled by independent flame, heat, or smoke detection. Two separate events must happen to initiate sprinkler discharge. First, the detection system must identify a developing fire and then open the preaction valve. This allows water to flow into system piping, which effectively creates a wet pipe sprinkler system. Second, individual sprinkler heads must release to permit water flow onto the fire.

In some instances, the preaction system may be set up with an interlock feature in which pressurized air or nitrogen is added to system piping. The purpose of this feature is twofold: first to monitor piping for leaks and second to hold water from system piping in the event of inadvertent detector operation. The most common application for this system type is in freezer warehouses.

The primary advantage of a preaction system is the dual action required for water release: the preaction valve must operate and sprinkler heads must fuse. This provides an added level of protection against inadvertent discharge, and for this reason, these systems are frequently employed in water sensitive environments such as archival vaults, fine art storage rooms, rare book libraries and computer centers.

There are some disadvantages to preaction systems. These include:

* Higher installation and maintenance costs. Preaction systems are more complex with several additional components, notably a fire detection system. This adds to the overall system cost.

* Modification difficulties. As with drypipe systems, preaction sprinkler systems have specific size limitations which may impact future system modifications. In addition, system modifications must incorporate changes to the fire detection and control system to ensure proper operation.

* Potential decreased reliability. The higher level of complexity associated with preaction systems creates an increased chance that something may not work when needed. Regular maintenance is essential to ensure reliability. Therefore, if the facility’s management decides to install preaction sprinkler protection, they must remain committed to installing the highest quality equipment, and to maintaining these systems as required by manufacturer’s recommendations.

Provided the application is appropriate, preaction systems have a place in heritage buildings, especially in water sensitive spaces.

A slight variation of preaction sprinklers is the deluge system, which is basically a preaction system using open sprinklers. Operation of the fire detection system releases a deluge valve, which in turn produces immediate water flow through all sprinklers in a given area. Typical deluge systems applications are found in specialized industrial situations, i.e. aircraft hangers and chemical plants, where high velocity suppression is necessary to prevent fire spread. Use of deluge systems in heritage facilities is rare and typically not recommended.

Another preaction system variation is the on/off system which utilizes the basic arrangement of a preaction system, with the addition of a thermal detector and nonlatching alarm panel. The system functions similar to any other preaction sprinkler system, except that as the fire is extinguished, a thermal device cools to allow the control panel to shut off water flow. If the fire should reignite, the system will turn back on. In certain applications on/off systems can be effective. Care, however, must be exercised when selecting this equipment to ensure that it functions as desired. In most urban areas, it is likely that the fire department will arrive before the system has shut itself down, thereby defeating any actual benefits.

3.5: Sprinkler Concerns
Several common misconceptions about sprinkler systems exist. Consequently, heritage building owners and operators are often reluctant to provide this protection, especially for collections storage and other water sensitive spaces. Typical misunderstandings include:

* When one sprinkler operates, all will activate. With the exception of deluge systems (discussed later in this leaflet), only those sprinklers in direct contact with the fire’s heat will react. Statistically, approximately 61% of all sprinkler controlled fires are stopped by two or less sprinklers.

* Sprinklers operate when exposed to smoke. Sprinklers function by thermal impact against their sensing elements. The presence of smoke alone will not cause activation without high heat.

* Sprinkler systems are prone to leakage or inadvertent operation. Insurance statistics indicate a failure rate of approximately 1 head failure per 16,000,000 sprinklers installed per year. Sprinkler components and systems are among the most tested systems in an average building. Failure of a proper system is very remote.

Where failures do occur, they are usually the result of improper design, installation, or maintenance. Therefore, to avoid problems, the institution should carefully select those who will be responsible for the installation and be committed to proper system maintenance.

* Sprinkler activation will cause excessive water damage to contents and structure. Water damage will occur when a sprinkler activates. This issue becomes relative, however, when compared to alternative suppression methods. The typical sprinklerwill discharge approximately 25 gallons per minute (GPM) while the typical fire department hose delivers 100-250 GPM. Sprinklers are significantly less damaging than hoses. Since sprinklers usually operate before the fire becomes large, the overall water quantity required for control is lower than situations where the fire continues to increase until firefighters arrive.

The table below shows approximate comparative water application rates for various manual and automatic suppression methods.
< TR>
Table 31: Fire Suppression Water Application Rates.

Delivery Method
Liters/min.

Gallons/min.
Portable Fire Extinguisher/Appliance
10

2.5
Occupant Use Fire Hose
380

100
Sprinkler (1)
95

25
Sprinkler (2)
180

47
Sprinkler (3)
260

72
Fire Department, Single 1.5″ Hose
380

100
Fire Department, Double 1.5″ Hose
760

200
Fire Department, Single 2.5″ Hose
950

250
Fire Department, Double 2.5″ Hose
1900

500

One final point to consider is that the water damage is usually capable of repair and restoration. Burned out contents, however, are often beyond mend.

* Sprinkler systems look bad and will harm the building’s appearance. This concern has usually resulted from someone who has observed a less than ideal appearing system, and admittedly there are some poorly designed systems out there. Sprinkler systems can be designed and installed with almost no aesthetic impact.

To ensure proper design, the institution and design team should take an active role in the selection of visible components. Sprinkler piping should be placed, either concealed or in a decorative arrangement, to minimize visual impact. Only sprinklers with high quality finishes should be used. Often sprinkler manufacturers will use customer provided paints to match finish colors, while maintaining the sprinkler’s listing. The selected sprinkler contractor must understand the role of aesthetics.

To help ensure overall success, the sprinkler system designer should understand the institution’s protection objectives, operations, and fire risks. This individual should be knowledgeable about system requirements and flexible to implement unique, thought-out solutions for those areas where special aesthetic or operations concerns exist. The designer should be experienced in the design of systems in architecturally sensitive applications.

Ideally, the sprinkler contractor should be experienced working in heritage applications. However, an option is to select a contractor experienced in water sensitive applications such as telecommunications, pharmaceuticals, clean rooms, or high tech manufacturing. Companies including AT&T, Bristol Meyers Squibb, and IBM have very stringent sprinkler installation requirements. If a sprinkler contractor has demonstrated success with these type of organizations, then they will be capable of performing satisfactorily in a heritage site.

The selected sprinkler components should be provided by a reputable manufacturer, experienced in special, water sensitive hazards. The cost differential between average and the highest quality components is minimal. The long term benefit, however, is substantial. When considering the value of a facility and its contents, the extra investment is worth while.

With proper attention to selection, design, and maintenance, sprinkler systems will serve the institution without adverse impact. If the institution or design team does not possess the experience to ensure the system is proper, a fire protection engineer experienced in heritage applications can be a great advantage.

3.6: Water Mist
One of the most promising automatic extinguishing technologies is the recently available fine water droplet, or mist systems. This technology represents another tool that can provide automatic fire suppression in some cultural property applications. Potential uses include locations where reliable water supplies do not exist, where even sprinkler water discharges are too high, or where building construction and aesthetics impact the use of standard sprinkler pipe dimensions. Mist systems may also be an appropriate solution to the protection void left by the environmental concerns, and subsequent demise, of Halon 1301 gas.

Mist technology was originally developed for offshore uses such as on board ships and oil drilling platforms. For both of these applications, there is a need to control severe fires while limiting the amount of extinguishing water, which could impact vessel stability. These systems have been extensively approved by a number of domestic and international marine organizations, and have been a protection standard for the past 8-10 years. They have a solid track record dealing with maritime fires. These systems have also been used in several land based applications, and have a number of listings, primarily in Europe, where their effectiveness has been recognized. Some systems have recently received approvals for North American land based uses.

Mist systems discharge limited water quantities at higher pressures than sprinkler systems. These pressures range from approximately 100 to 1,000 psi, with the higher pressure systems generally producing larger volumes of fine sprays. The produced droplets are usually in the 50 to 200 micron diameter range (compared to 600-1,000 microns for standard sprinklers), resulting in exceptionally high efficiency cooling and fire control, with significantly little water. In most situations, fires are controlled with approximately 10-25% of the water normally associated with sprinklers. Water saturation that is often associated with standard firefighting procedures is decreased. Other benefits include lower aesthetic impact and known environmental safety.

Typical water mist systems consist of the following components:

* Water supply: Water for a system may be provided by either the piped building system or a dedicated tank arrangement. In some instances, lower pressure systems may use existing sprinkler piping. For most, however, supplemental pumps will be required. Other options include dedicated water/nitrogen storage cylinders, which can deliver a limited duration supply.

* Piping and nozzles: Piping can be greatly reduced when compared to sprinklers. For low pressure systems, pipes are generally 25-50% smaller than comparable sprinkler piping. For high pressure systems, piping is even smaller with the 0.50-0.75 inch diameters as the norm. Like sprinklers, nozzles are individually activated by the fire’s heat, and are selected to cover a certain size hazard. Their sizes are comparable to a low profile sprinkler.

* Detection and control equipment. In some instances, mist discharge can be controlled by selected, high reliability intelligent detectors or by an advanced technology VESDA smoke detection system. These systems represent the premier, stateoftheart, fire detection technology that can provide very early warning of a developing fire, as well as reduce the probability of inadvertent discharge.

At this point, one of the main drawbacks to mist systems is their higher cost, which can be 50-100% greater than standard sprinklers. This cost, however, may be reduced due to possible installation labor savings. In rural applications, where reliable sprinkler water supplies can be expensive, mist systems may be comparable or less than standard sprinklers. Another problem is that these systems do not have the variety of approvals and listings commonly associated with sprinklers. As such, they may not be as recognized by fire and building authorities. In addition, the number of contractors who are familiar with the technology is limited. These concerns are diminishing, however, as use of these systems becomes more widespread.

3.7: Summary:
In summary, automatic sprinklers often represent one of the most important fire protection options for most heritage applications. The successful application of sprinklers is dependent upon careful design and installation of high quality components by capable engineers and contractors. A properly selected, designed and installed system will offer unexcelled reliability. Sprinkler system components should be selected for compliance with the institution’s objectives. Wet pipe systems offer the greatest degree of reliability and are the most appropriate system type for most heritage fire risks. With the exception of spaces subject to freezing conditions, dry pipe systems do not offer advantages over wet pipe systems in heritage buildings. Preaction sprinkler systems are beneficial in areas of highest water sensitivity. Their success is dependent upon selection of proper suppression and detection components and management’s commitment to properly maintain systems. Water mist represents a very promising alternative to gaseous agent systems.

Ultraviolet ANSWER

Ultraviolet (UV) light has shorter wavelengths than visible light. Though these waves are invisible to the human eye, some insects, like bumblebees, can see them! (Image of the bumblebee is courtesty of Mark Cassino.)     An image of a bumblebee.

Scientists have divided the ultraviolet part of the spectrum into three regions: the near ultraviolet, the far ultraviolet, and the extreme ultraviolet. The three regions are distinguished by how energetic the ultraviolet radiation is, and by the “wavelength” of the ultraviolet light, which is related to energy.

The near ultraviolet, abbreviated NUV, is the light closest to optical or visible light. The extreme ultraviolet, abbreviated EUV, is the ultraviolet light closest to X-rays, and is the most energetic of the three types. The far ultraviolet, abbreviated FUV, lies between the near and extreme ultraviolet regions. It is the least explored of the three regions.

The Extreme Ultraviolet Sun.     Our Sun emits light at all the different wavelengths in electromagnetic spectrum, but it is ultraviolet waves that are responsible for causing our sunburns. To the left is an image of the Sun taken at an Extreme Ultraviolet wavelength - 171 Angstroms to be exact. (An Angstrom is a unit length equal to 10-10 meters.) This image was taken by a satellite named SOHO and it shows what the Sun looked like on April 24, 2000.

Though some ultraviolet waves from the Sun penetrate Earth’s atmosphere, most of them are blocked from entering by various gases like Ozone. Some days, more ultraviolet waves get through our atmosphere. Scientists have developed a UV index to help people protect themselves from these harmful ultraviolet waves.

How do we “see” using Ultraviolet light?

It is good for humans that we are protected from getting too much ultraviolet radiation, but it is bad for scientists! Astronomers have to put ultraviolet telescopes on satellites to measure the ultraviolet light from stars and galaxies - and even closer things like the Sun!

There are many different satellites that help us study ultraviolet astronomy. Many of them only detect a small portion of UV light. For example, the Hubble Space Telescope observes stars and galaxies mostly in near ultraviolet light. NASA’s Extreme Ultraviolet Explorer satellite is currently exploring the extreme ultraviolet universe. The International Ultraviolet Explorer (IUE) satellite has observed in the far and near ultraviolet regions for over 17 years.     The International Ultraviolet Explorer

What does Ultraviolet light show us?

We can study stars and galaxies by studying the UV light they give off - but did you know we can even study the Earth? Below is an unusual image - it is a picture of Earth taken from a lunar observatory! This false-color picture shows how the Earth glows in ultraviolet (UV) light.

The Far UV Camera/Spectrograph deployed and left on the Moon by the crew of Apollo 16 took this picture. The part of the Earth facing the Sun reflects much UV light. Even more interesting is the side facing away from the Sun. Here, bands of UV emission are also apparent. These bands are the result of aurora caused by charged particles given off by the Sun. They spiral towards the Earth along Earth’s magnetic field lines.     The UV Earth D

Many scientists are interested in studying the invisible universe of ultraviolet light, since the hottest and the most active objects in the cosmos give off large amounts of ultraviolet energy.

The image below shows three different galaxies taken in visible light (bottom three images) and ultraviolet light (top row) taken by NASA’s Ultraviolet Imaging Telescope (UIT) on the Astro-2 mission.

UV and Visible images of 3 galaxiesD

The difference in how the galaxies appear is due to which type of stars shine brightest in the optical and ultraviolet wavelengths. Pictures of galaxies like the ones below show mainly clouds of gas containing newly formed stars many times more massive than the sun, which glow strongly in ultraviolet light. In contrast, visible light pictures of galaxies show mostly the yellow and red light of older stars. By comparing these types of data, astronomers can learn about the structure and evolution of galaxies.

Ultrasonic Flowmeter Worldwide Outlook

8/6/2008
Ultrasonic Flowmeter Market to Reach $590 Million by 2012
Propelled by strong growth in the oil & gas industry, the worldwide market for ultrasonic flowmeters is expected to grow at a compounded annual growth rate (CAGR) of 9.9% over the next five years.  The market was $367 million in 2007 and is forecasted to be over $589 million in 2012, according to a new ARC Advisory Group study.

UltrasonicUltrasonic flowmeters, once limited to use in niche applications, have become the fastest growing flow technology, particularly in the hydrocarbon industries.  While ultrasonic flowmeter technology has been available for decades, it has only in recent years begun to see more widespread adoption.  “Ultrasonic meters offer a compelling value proposition to users, and stand poised for widespread adoption in the process industries.  Given its smaller market size relative to other flow technologies, sustained growth of the hydrocarbon industries, and a large installed base of obsolete and maintenance-heavy mechanical metering technologies ripe for replacement, ARC expects the ultrasonic market to continue to grow at near double-digit rates in coming years,” according to Analyst Allen Avery, the principal author of ARC’s “Ultrasonic Flowmeter Worldwide Outlook”.

Custody Transfer Segment Sees Strong Growth
Almost all of the growth of the process ultrasonic market in recent years has been due to increased shipments to the oil & gas industry, which nearly doubled over previous levels.  It appears that the custody transfer market for natural gas has taken shape, thanks to adoption of the AGA9 custody transfer standard, and the use of ultrasonic meters for liquid custody transfer is increasing.  The oil & gas industry has set aside its conservative stance on field device technology and has begun to embrace ultrasonic metering, particularly in new projects that allow the design of an infrastructure appropriate to achieve the best meter performance.

Smart Meters Provide Diagnostic Information
Fieldbus enabled smart meters will see strong growth, as flowmeters are installed as part of overall control systems.  Communication via fieldbus networks allows users to remotely configure, monitor, and control their ultrasonic flowmeters.  Meters that use digital communications protocols can also provide users with a wealth of diagnostic information about the health of not only the meter, but also the process.  With sophisticated electronics embedded in ultrasonic flowmeters and visualization software, users can monitor flow profiles, the effects of flow conditioning, and detect potential line blockages.  Armed with this data, users can optimize their meter calibration and maintenance practices.

Asia, Middle East Lead Growth
The largest growth will occur in Asia and EMEA regions.  China and India are expected to make robust investment in basic infrastructure and new manufacturing plants.  As energy-poor China seeks fuel for its rapid economic growth, it will ramp up its oil & gas infrastructure.  The Middle East will continue to be fertile ground for ultrasonic meter suppliers, due to its role in oil & gas production. Growth in North America will be relatively modest, but still healthy due to investment in oil & gas infrastructure.

RTD Advantage Disadvantages

Resistance Temperature Detectors: Theory and Standards

With these general guidelines to the basic function, performance, and recognized standards for RTD’s, anyone can specify the right de