Lectures on Heat (3)

Thermal Expansion and the Gas Law

Coefficients of Expansion
Almost all materials expand on heating—the most famous exception being water, which contracts as it is warmed from 0 degrees Celsius to 4 degrees. This is actually a good thing, because as freezing weather sets in, the coldest water, which is about to freeze, is less dense than slightly warmer water, so rises to the top of a lake and the ice begins to form there. For almost all other liquids, solidification on cooling begins at the bottom of the container. So, since water behaves in this weird way, ice skating is possible! Also, as a matter of fact, life in lakes is possible—the ice layer that forms insulates the rest of the lake water from very cold air, so fish can make it through the winter.
Linear Expansion
The coefficient of linear expansion α of a given material, for example a bar of copper, at a given temperature is defined as the fractional increase in length that takes place on heating through one degree:

Of course, α might vary with temperature (it does for water, as we just mentioned) but in fact for most materials it stays close to constant over wide temperature ranges.

Volume Expansion
For liquids and gases, the natural measure of expansion is the coefficient of volume expansion,β.

Of course, on heating a bar of copper, clearly the volume as well as the length increases—the bar expands by an equal fraction in all directions (this could be experimentally verified, or you could just imagine a cube of copper, in which case all directions look the same).
The volume of a cube of copper of side L is V = L3. Suppose we heat it through one degree. Putting together the definitions of ,αβabove,

Gas Pressure Increase with Temperature

In 1702, Amontons discovered a linear increase of P with T for air, and found P to increase about 33% from the freezing point of water to the boiling point of water.
That is to say, he discovered that if a container of air were to be sealed at 0°C, at ordinary atmospheric pressure of 15 pounds per square inch, and then heated to 100°C but kept at the same volume, the air would now exert a pressure of about 20 pounds per square inch on the sides of the container. (Of course, strictly speaking, the container will also have increased in size, that would lower the effect—but it’s a tiny correction, about ½% for copper, even less for steel and glass.)
Remarkably, Amontons discovered, if the gas were initially at a pressure of thirty pounds per square inch at 0°C, on heating to 100°C the pressure would go to about 40 pounds per square inch—so the percentage increase in pressure was the same for any initial pressure: on heating through 100°C, the pressure would always increase by about 33%.
Furthermore, the result turned out to be the same for different gases!

Finding a Natural Temperature Scale
In class, we plotted air pressure as a function of temperature for a fixed volume of air, by making several measurements as the air was slowly heated (to give it a chance to all be at the same temperature at each stage). We found a straight line. On the graph, we extended the line backwards, to see how the pressure would presumably drop on cooling the air. We found the remarkable prediction that the pressure should drop to zero at a temperature of about −273°C.
In fact, if we’d done the cooling experiment, we would have found that air doesn’t actually follow the line all the way down, but condenses to a liquid at around −200°C. However, helium gas stays a gas almost to −270°C, and follows the line closely.

We shall discuss the physics of gases, and the interpretation of this, much more fully in a couple of lectures. For now, the important point is that this suggests a much more natural temperature scale than the Celsius one: we should take −273°C as the zero of temperature! For one thing, if we do that, the pressure/temperature relationship for a gas becomes beautifully simple:
P  ∝  T
This temperature scale, in which the degrees have the same size as in Celsius, is called the Kelvin or absolute scale. Temperatures are written 300K. To get from Celsius to Kelvin, just add 273 (strictly speaking, 273.15).
An Ideal Gas
Physicists at this point introduce the concept of an “Ideal Gas”. This is like the idea of a frictionless surface: it doesn’t exist in nature, but it is a very handy approximation to some real systems, and makes problems much easier to handle mathematically. The ideal gas is one for which for all temperatures, so helium is close to ideal over a very wide range, and air is close to ideal at ordinary atmospheric temperatures and above.

Lectures on Heat (2)

Thermal Equilibrium and the Zeroth Law of Thermodynamics
Once the thermometer came to be widely used, more precise observations of temperature and (as we shall see) heat flow became possible. Joseph Black, a professor at the University of Edinburgh in the 1700’s, noticed that a collection of objects at different temperatures, if brought together, will all eventually reach the same temperature.
As he wrote, “By the use of these instruments [thermometers] we have learned, that if we take 1000, or more, different kinds of matter, such as metals, stones, salts, woods, cork, feathers, wool, water and a variety of other fluids, although they be all at first of different heats, let them be placed together in a room without a fire, and into which the sun does not shine, the heat will be communicated from the hotter of these bodies to the colder, during some hours, perhaps, or the course of a day, at the end of which time, if we apply a thermometer to all of them in succession, it will point to precisely the same degree.”
We say nowadays that bodies in “thermal contact” eventually come into “thermal equilibrium”—which means they finally attain the same temperature, after which no further heat flow takes place. This is equivalent to:
The Zeroth Law of Thermodynamics:
If two objects are in thermal equilibrium with a third, then they are in thermal equilibrium with each other.
The “third body” in a practical situation is just the thermometer.
It’s perhaps worth pointing out that this trivial sounding statement certainly wasn’t obvious before the invention of the thermometer. With only the sense of touch to go on, few people would agree that a piece of wool and a bar of metal, both at 0°C, were at the same temperature.
Measuring Heat Flow: a Unit of Heat
The next obvious question is, can we get more quantitative about this “flow of heat” that takes place between bodies as they move towards thermal equilibrium? For example, suppose I reproduce one of Fahrenheit’s experiments, by taking 100 ccs of water at 100°F, and 100ccs at 150°F, and mix them together in an insulated jug so little heat escapes. What is the final temperature of the mix?
Of course, it’s close to 125°F—not surprising, but it does tell us something! It tells us that the amount of heat required to raise the temperature of 100 cc of water from 100°F to 125°F is exactly the same as the amount needed to raise it from 125°F to 150°F. A series of such experiments (done by Fahrenheit, Black and others) established that it always took the same amount of heat to raise the temperature of 1 cc of water by one degree.
This makes it possible to define a unit of heat. Perhaps unfairly to Fahrenheit,
1 calorie is the heat required to raise the temperature of 1 gram of water by 1 degree Celsius.
(Celsius also lived in the early 1700’s. His scale has the freezing point of water as 0°C, the boiling point as 100°C. Fahrenheit’s scale is no longer used in science, but lives on in engineering in the US, and in the British Thermal Unit, which is the heat required to raise the temperature of one pound of water by 1°F.)
Specific Heats and Calorimetry
First, let’s define specific heat:
The specific heat of a substance is the heat required in calories to raise the temperature of 1 gram by 1 degree Celsius.
As Fahrenheit continues his measurements of heat flow, it quickly became evident that for different materials, the amount of heat needed to raise the temperature of one gram by one degree could be quite different. For example, it had been widely thought before the measurements were made, that one cc of Mercury, being a lot heavier than one cc of water, would take more heat to raise its temperature by one degree. This proved not to be the case—Fahrenheit himself made the measurement. In an insulating container, called a “calorimeter” he added 100ccs of water at 100°F to 100ccs of mercury at 150°F, and stirred so they quickly reached thermal equilibrium.
Question: what do you think the final temperature was? Approximately?
Answer: The final temperature was, surprisingly, about 120°F. 100 cc of water evidently “contained more heat” than 100 cc of mercury, despite the large difference in weight!
This technique, called calorimetry, was widely used to find the specific heats of many different substances, and at first no clear pattern emerged. It was puzzling that the specific heat of mercury was so low compared with water! As more experiments on different substances were done, it gradually became evident that heavier substances, paradoxically, had lower specific heats.
A Connection With Atomic Theory
Meanwhile, this quantitative approach to scientific observation had spread to chemistry. Towards the end of the 1700’s, Lavoisier weighed chemicals involved in reactions before and after the reaction. This involved weighing the gases involved, so had to be carried out in closed containers, so that, for example, the weight of oxygen used and the carbon dioxide, etc., produced would accounted for in studying combustion. The big discovery was that mass was neither created nor destroyed. This had not been realized before because no one had weighed the gases involved. It made the atomic theory suddenly more plausible, with the idea that maybe chemical reactions were just rearrangements of atoms into different combinations.
Lavoisier also clarified the concept of an element, an idea that was taken up in about 1800 by John Dalton, who argues that a given compound consisted of identical molecules, made up of elementary atoms in the same proportion, such as H2O (although that was thought initially to be HO). This explained why, when substances reacted chemically, such as the burning of hydrogen to form water, it took exactly eight grams of oxygen for each gram of hydrogen. (Well, you could also produce H2O2 under the right conditions, with exactly sixteen grams of oxygen to one of hydrogen, but the simple ratios of amounts of oxygen needed for the two reactions were simply explained by different molecular structures, and made the atomic hypothesis even more plausible.)
Much effort was expended carefully weighing the constituents in many chemical reactions, and constructing diagrams of the molecules. The important result of all this work was that it became possible to list the relative weights of the atoms involved. For example, the data on H2O and H2O2 led to the conclusion that an oxygen atom weighed sixteen times the weight of a hydrogen atom.
It must be emphasized, though, that these results gave no clue as to the actual weights of atoms! All that was known was that atoms were too small to see in the best microscopes. Nevertheless, knowing the relative weights of some atoms in 1820 led to an important discovery. Two professors in France, Dulong and Petit, found that for a whole series of elements the product of atomic weight and specific heat was the same!

The significance of this, as they pointed out, was that the “specific heat”, or heat capacity, of each atom was the same—a piece of lead and a piece of zinc having the same number of atoms would have the same heat capacity. So heavier atoms absorbed no more heat than lighter atoms for a given rise in temperature. This partially explained why mercury had such a surprisingly low heat capacity. Of course, having no idea how big the atoms might be, they could go no further. And, indeed, many of their colleagues didn’t believe in atoms anyway, so it was hard to convince them of the significance of this discovery.
Latent Heat
One of Black’s experiments was to set a pan of water on a steady fire and observe the temperature
as a function of time. He found it steadily increased, reflecting the supply of heat from the fire, until the water began to boil, whereupon the temperature stayed the same for a long time. The steam coming off was at the same (boiling) temperature as the water. So what was happening to the heat being supplied? Black correctly concluded that heat needed to be supplied to change water from its liquid state to its gaseous state, that is, to steam. In fact, a lot of heat had to be supplied: 540 calories per gram, as opposed to the mere 100 calories per gram needed to bring it from the freezing temperature to boiling. He also discovered that it took 80 calories per gram to melt ice into water, with no rise in temperature. This heat is released when the water freezes back to ice, so it is somehow “hidden” in the water. He called it latent heat, meaning hidden heat.

Lectures on Heat (1)

Heat

Feeling and seeing temperature changes
Within some reasonable temperature range, we can get a rough idea how warm something is by touching it. But this can be unreliable—if you put one hand in cold water, one in hot, then plunge both of them into lukewarm water, one hand will tell you it’s hot, the other will feel cold. For something too hot to touch, we can often get an impression of how hot it is by approaching and sensing the radiant heat. If the temperature increases enough, it begins to glow and we can see it’s hot!
The problem with these subjective perceptions of heat is that they may not be the same for everybody. If our two hands can’t agree on whether water is warm or cold, how likely is it that a group of people can set a uniform standard? We need to construct a device of some kind that responds to temperature in a simple, measurable way—we need a thermometer.
The first step on the road to a thermometer was taken by one Philo of Byzantium, an engineer, in the second century BC. He took a hollow lead sphere connected with a tight seal to one end of a pipe, the other end of the pipe being under water in another vessel.

 

To quote Philo: “…if you expose the sphere to the sun, part of the air enclosed in the tube will pass out when the sphere becomes hot. This will be evident because the air will descend from the tube into the water, agitating it and producing a succession of bubbles.
Now if the sphere is put back in the shade, that is, where the sun’s rays do not reach it, the water will rise and pass through the tube …”
“No matter how many times you repeat the operation, the same thing will happen.
In fact, if you heat the sphere with fire, or even if you pour hot water over it, the result will be the same.”
Notice that Philo did what a real investigative scientist should do—he checked that the experiment was reproducible, and he established that the air’s expansion was in response to heat being applied to the sphere, and was independent of the source of the heat.

Classic Dramatic Uses of Temperature-Dependent Effects

This expansion of air on heating became widely known in classical times, and was used in various dramatic devices. For example, Hero of Alexandria describes a small temple where a fire on the altar causes the doors to open

The altar is a large airtight box, with a pipe leading from it to another enclosed container filled with water. When the fire is set on top of the altar, the air in the box heats up and expands into a second container which is filled with water. This water is forced out through an overflow pipe into a bucket hung on a rope attached to the door hinges in such a way that as the bucket fills with water, it drops, turns the hinges, and opens the doors. The pipe into this bucket reaches almost to the bottom, so that when the altar fire goes out, the water is sucked back and the doors close again. (Presumably, once the fire is burning, the god behind the doors is ready to do business and the doors open…)
Still, none of these ingenious devices is a thermometer. There was no attempt (at least none recorded) by Philo or his followers to make a quantitative measurement of how hot or cold the sphere was. And the “meter” in thermometer means measurement
The First Thermometer
Galileo claimed to have invented the first thermometer. Well, actually, he called it a thermoscope, but he did try to measure “degrees of heat and cold” according to a colleague, and that qualifies it as a thermometer. (Technically, a thermoscope is a device making it possible to see a temperature change, a thermometer can measure the temperature change.) Galileo used an inverted narrow-necked bulb with a tubular neck, like a hen’s egg with a long glass tube attached at the tip.

He first heated the bulb with his hands then immediately put it into water. He recorded that the water rose in the bulb the height of “one palm”. Later, either Galileo or his colleague Santorio Santorio put a paper scale next to the tube to read off changes in the water level. This definitely made it a thermometer, but who thought of it first isn’t clear (they argued about it). And, in fact, this thermometer had problems.
Question: what problems? If you occasionally top up the water, why shouldn’t this thermometer be good for recording daily changes in temperature?
Answer: because it’s also a barometer! But—Galileo didn’t know about the atmospheric pressure.
Torricelli, one of Galileo’s pupils, was the first to realize, shortly after Galileo died, that the real driving force in suction was external atmospheric pressure, a satisfying mechanical explanation in contrast to the philosophical “nature abhors a vacuum”. In the 1640’s, Pascal pointed out that the variability of atmospheric pressure rendered the air thermometer untrustworthy.
Liquid-in-glass thermometers were used from the 1630’s, and they were of course insensitive to barometric pressure. Meteorological records were kept from this time, but there was no real uniformity of temperature measurement until Fahrenheit, almost a hundred years later.

Newton’s Anonymous Table of Temperatures
The first systematic account of a range of different temperatures, “Degrees of Heat”, was written by Newton, but published anonymously, in 1701. Presumably he felt that this project lacked the timeless significance of some of his other achievements.
Taking the freezing point of water as zero, Newton found the temperature of boiling water to be almost three times that of the human body, melting lead eight times as great (actually 327C, whereas 8x37=296, so this is pretty good!) but for higher temperatures, such as that of a wood fire, he underestimated considerably. He used a linseed oil liquid in glass thermometer up to the melting point of tin (232°C). (Linseed oil doesn’t boil until 343°C, but that is also its autoignition temperature!)
Newton tried to estimate the higher temperatures indirectly. He heated up a piece of iron in a fire, then let it cool in a steady breeze. He found that, at least at the lower temperatures where he could cross check with his thermometer, the temperature dropped in a geometric progression, that is, if it took five minutes to drop from 80° above air temperature to 40° above air temperature, it took another five minutes to drop to 20° above air, another five to drop to 10° above, and so on. He then assumed this same pattern of temperature drop was true at the high temperatures beyond the reach of his thermometer, and so estimated the temperature of the fire and of iron glowing red hot. This wasn’t very accurate—he (under)estimated the temperature of the fire to be about 600°C.
Fahrenheit’s Excellent Thermometer
The first really good thermometer, using mercury expanding from a bulb into a capillary tube, was made by Fahrenheit in the early 1720’s. He got the idea of using mercury from a colleague’s comment that one should correct a barometer reading to allow for the variation of the density of mercury with temperature. The point that has to be borne in mind in constructing thermometers, and defining temperature scales, is that not all liquids expand at uniform rates on heating—water, for example, at first contracts on heating from its freezing point, then begins to expand at around forty degrees Fahrenheit, so a water thermometer wouldn’t be very helpful on a cold day. It is also not easy to manufacture a uniform cross section capillary tube, but Fahrenheit managed to do it, and demonstrated his success by showing his thermometers agreed with each other over a whole range of temperatures. Fortunately, it turns out that mercury is well behaved in that the temperature scale defined by taking its expansion to be uniform coincides very closely with the true temperature scale, as we shall see later.
Amontons’ Air Thermometer: Pressure Increases Linearly with Temperature
A little earlier (1702) Amontons introduced an air pressure thermometer. He established that if air at atmospheric pressure (he states 30 inches of mercury) at the freezing point of water is enclosed then heated to the boiling point of water, but meanwhile kept at constant volume by increasing the pressure on it, the pressure goes up by about 10 inches of mercury. He also discovered that if he compressed the air in the first place, so that it was at a pressure of sixty inches of mercury at the temperature of melting ice, then if he raised its temperature to that of boiling water, at the same time adding mercury to the column to keep the volume of air constant, the pressure increased by 20 inches of mercury. In other words, he found that for a fixed amount of air kept in a container at constant volume, the pressure increased with temperature by about 33% from freezing to boiling, that percentage being independent of the initial pressure.

Definitions of Words and Terms Used in the Gas Processing Industry

absorber
A tower or column that provides contact between natural gas being processed and a liquid solvent.
absorption
The operation in which one or more components in the gas phase are transferred to (absorbed into) a liquid solvent.
absorption factor
A factor which is an indication of the tendency for a given gas phase component to be transferred to the liquid solvent. It is generally expressed as A = L/KV where L and V are the molar flows of liquid and vapor, and K is the average value of the vapor-liquid equilibrium constant for the component of concern.
absorption oil
A hydrocarbon liquid used to absorb and recover components from the natural gas being processed.
acid gas
The hydrogen sulfide and/or carbon dioxide contained in, or extracted from, gas or other streams.
adiabatic expansion
The expansion of a gas, vapor, or liquid stream from a higher pressure to a lower pressure in which there is no heat transfer between the gas, vapor, or liquid and the surroundings.
adsorbent
A solid substance used to remove components from natural gas being processed.
adsorption
The process by which gaseous components are adsorbed on solids because of their  molecular attraction to the solid surface.
amine (alkanolamine)
Any of several liquid compounds containing amino nitrogen generally used in water solution to remove, by reversible chemical reaction, hydrogen sulfide and/or carbon dioxide from gas and liquid hydrocarbon streams.
API Gravity
An arbitrary scale expressing the relative density of liquid petroleum products. The scale is calibrated in degrees API, calculated by the following formula:

γ = relative density
associated gas
Gaseous hydrocarbons occuring as a free-gas phase under original oil-reservoir conditions of temperature and pressure.
atmospheric pressure
The pressure exerted on the earth by the earth’s atmosphere. A pressure of 760 mm of mercury, 29.92 inches of mercury, or 14.696 psia is used as a standard for some measurements. State regulatory bodies have set other standards for use in
measuring the legal volume of gas. Atmospheric pressure may also refer to the absolute ambient pressure at any given location.
barrel
A common English-unit mesure of liquid volume which, in the petroleum industry, equals 42 U.S. liquid gallons for petroleum or natural gas liquid products measured at 60°F and equilibrium vapor pressure. One barrel equals 0.159 cubic meters, or 6.29 barrels per cubic meter .
blanket gas
A gas phase maintained in a vessel containing liquid to protect the liquid against air contamination, to reduce the hazard of explosion, or to maintain pressure of the liquid. The source of the gas is external to the vessel.
blow case
A small vessel in which liquid is accumulated and then forced from the vessel by applying gas or air pressure above the liquid level.
blowdown
The act of emptying or depressuring a vessel. This may also refer to discarded material,  such as blowdown water from a boiler or cooling tower.
boilaway test
Sometimes used to describe the GPA weathering test for LPgas. Refer to definition for "weathering test".
bottoms
The liquid or residual matter which is withdrawn from the bottom of a fractionator or other vessel during processing or while in storage.
B-P mix
A liquefied hydrocarbon product composed chiefly of butanes and propane. If it originates in a refinery, it may also contain butylenes and propylene. More specifically, it conforms to the GPA specifications for commercial B-P mixes as described in GPA Standard 2140.
breathing
The movement of vapor in or out of an atmospheric pressure storage tank because of a change of level of the stored liquid, a change in the temperature of the vapor space above the liquid, or a change of atmospheric pressure.
bs&w (basic sediment and water)
Waste that collects in the bottom of vessels and tanks containing petroleum or petroleum products.
bubble point
The temperature at a specified pressure at which the first stable  vapor forms above a liquid.
butane, commercial
A liquefied hydrocarbon consisting predominately of butane and/or butylene and which conforms to the GPA specification for commercial butane defined in GPA Standard 2140.
butane, normal
In commercial transactions, a product meeting the GPA specifications for commercial butane and, in addition, containing a minimum of 95 liquid volume percent normal butane. Chemically, normal butane is an aliphatic compound of the paraffin series having the chemical formula C4H10 and having all of its carbon atoms joined in a straight chain.
calorimeter
An apparatus which is used to determine the heating value of a combustible material.
carbonyl sulfide
A chemical compound of the aldehyde group containing a carbonyl group and sulfur (COS). Sometimes a contaminant in natural gas and NGL. It may need to be removed in order to meet sulfur specifications.
casinghead gas
Unprocessed natural gas produced from a reservoir containing oil. It contains heavier hydrocarbon vapors and is usually produced under low pressure from a casing head on the well.
charcoal test
A test standardized by the Gas Processors Association and the American Gas Association for determining the natural gasoline content of a given natural gas. The gasoline is adsorbed from the gas on activated charcoal and then recovered by distillation.
The test is prescribed in Testing Code 101-43, a joint publication of AGA and GPA.
chromatography
A technique for separating a mixture into individual components by repeated adsorption and desorption on a confined solid bed. It is used for analysis of natural gas and NGL.
Claus Process
A process to convert hydrogen sulfide into elemental sulfur by selective oxidation.
compressibility factor
A factor, usually expressed as "Z," which gives the ratio of the actual volume of gas at a given temperature and pressure to the volume of gas when calculated by the ideal gas law.
compression ratio
The ratio of the absolute discharge pressure from a compressor to the absolute intake pressure. Also applies to one cylinder of a reciprocating compressor and one or more stages of a rotating compressor.
condensate
The liquid formed by the condensation of a vapor or gas; specifically, the hydrocarbon liquid separated from natural gas because of changes in temperature and pressure when the gas
from the reservoir was delivered to the surface separators. In a steam system it may be water that is condensed and returned to the boilers.
convergence pressure
The pressure at a given temperature for a hydrocarbon system of fixed composition at which the vapor-liquid equilibrium Kvalues of the various components in the system become, or
tend to become, unity. The convergence pressure is used to adjust vapor-liquid equilibrium K-values to the particular system under consideration. (See TP-22)
copper strip test
A test using a small strip of pure copper to determine qualitatively the hydrogen sulfide corrosivity of a product. Refer to GPA LP-gas copper strip test (Copper Strip Method), ASTM D-1838 test procedure.

cricondenbar
The highest pressure at which liquid and vapor phases can exist at equilibrium in a  multicomponent system.
cricondentherm
The highest temperature at which liquid and vapor phases can exist at equilibrium in a multicomponent system.
critical density
The density of a substance at its critical temperature and critical pressure.
critical pressure
The vapor pressure of a substance at its critical temperature. critical temperature
For a pure component, the maximum temperature at which the component can exist as a liquid.
cryogenic plant
A gas processing plant which is capable of producing natural gas liquid products, including ethane, at very low operating temperatures, usually below minus 50°F.
cubic meter
A unit of volume measurement commonly used in international commerce for petroleum, petroleum products and natural gas. One cubic meter measured at 60°F = 264.172 U.S.
gallons = 6.29 barrels = 35.315 cubic feet measured at 60°F.
deaerator
An item of equipment used for removing air or other non-condensible gases from a process stream or from steam condensate or boiler feed water.
debutanizer
A fractionator designed to separate butane (and more volatile
components if present) from a hydrocarbon mixture.
dehydration
The act or process of removing water from gases or liquids.
demethanized product
A product from which essentially all methane and lighter materials
have been removed.
demethanizer
A fractionator designed to separate methane (and more volatile
components if present) from a hydrocarbon mixture.
depropanizer
A fractionator designed to separate propane (and more volatile
components if present) from a hydrocarbon mixture.
desiccant
A substance used in a dehydrator to remove water and moisture.
Also a material used to remove moisture from the air.
desulfurization
A process by which sulfur and sulfur compounds are removed
from gases or liquid hydrocarbon mixtures.
dew point
The temperature at any given pressure, or the pressure at any
given temperature, at which liquid initially condenses from a
gas or vapor. It is specifically applied to the temperature at
which water vapor starts to condense from a gas mixture
(water dew point), or at which hydrocarbons start to condense
(hydrocarbon dew point).
distillation
The process of separating materials by successively heating to
vaporize a portion and then cooling to liquefy a part of the
vapor. Materials to be separated must differ in boiling point
and/or relative volatility..
doctor test
A qualitative method for detecting hydrogen sulfide and mercaptans
in NGL. The test distinguishes between "sour" and
"sweet" products.
dry gas
(1) Gas whose water content has been reduced by a dehydration
process. (2) Gas containing little or no hydrocarbons commercially
recoverable as liquid product. Gas in this second
definition preferably should be called lean gas.
end point
The maximum temperature observed on the thermometer
during an ASTM distillation test.
EP-mix (ethane-propane mix)
A product consisting of a mixture of essentially ethane and
propane.
expansion turbine
A device which converts part of the energy content of a gas or
liquid stream into mechanical work by expanding the gas or
liquid through a turbine from which work is extracted.
extraction
The process of transferring one or more components from one
liquid phase to another by virtue of different solubility in the
two liquids. It is also used to indicate removal of one or more
constituents from a stream.
field separator
A vessel in the oil or gas field for separating gas, hydrocarbon
liquid, and water from each other.
flash point
The lowest temperature at which vapors from a hydrocarbon
liquid will ignite. See ASTM D-56.
fractionation
See definition of "distillation." Generally used to describe
separation of a mixture of hydrocarbons into individual products
based on difference in boiling point and/or relative volatility.
freeze valve
A specially constructed and calibrated valve designed and
used solely for determining the water content in propane product.
See ASTM D-2713.
gas constant (R)
The constant multiplier in the Ideal Gas Law. Numerically,
R=PV/T, if V is the volume of one mole of an ideal gas at temperature
T and pressure P.
gas hydrate
Refer to definition of "hydrate".
gas injection
The injection of natural gas into a reservoir to maintain or
increase the reservoir pressure or reduce the rate of decline of
the reservoir pressure.
gas lift
A method for bringing crude oil or water to the surface by
injecting gas into the producing well bore.
gas-oil ratio (GOR)
The ratio of gas to liquid hydrocarbon produced from a well.
This may be expressed as standard cubic feet of gas per barrel
of stock tank liquid.
gas processing
The separation of constituents from natural gas for the purpose
of making salable products and also for treating the residue
gas to meet required specifications.
gas processing plant
A plant which processes natural gas for recovery of natural
gas liquids and sometimes other substances such as sulfur.
gas-well gas
The gas produced or separated at surface conditions from the
full well stream produced from a gas reservoir.
gas-well liquids
The liquid separated at surface conditions from the full well
stream produced from a gas reservoir.
gathering system
The network of pipelines which carry gas from the wells to the
processing plant or other separation equipment.
gpm/GPM
(1) gpm (gallons per minute): The term used to describe the
rate of flowing fluid in gallons per minute. (2) GPM — Preferably
Gal/Mcf (gallons per thousand cubic feet): This term refers
to the content in natural gas of components which are
recoverable or recovered as liquid products.
heat medium (heating medium)
A material, whether flowing or static, used to transport heat
from a primary source such as combustion of fuel to another
material. Heating oil, steam, and an eutectic salt mixture are
examples of heat mediums.
heating value (heat of combustion)
The amount of heat obtained by the complete combustion of a
unit quantity of material. The gross, or higher, heating value
is the amount of heat obtained when the water produced in
the combustion is condensed. The net, or lower, heating value
is the amount of heat obtained when the water produced in
the combustion is not condensed.
heavy ends
The portion of a hydrocarbon mixture having the highest boiling
point. Usually hexanes or heptanes and all heavier hydrocarbons
are the heavy ends in a natural gas stream.
hexanes plus (or heptanes plus)
The portion of a hydrocarbon fluid mixture or the last component
of a hydrocarbon analysis which contains the hexanes (or
heptanes) and all hydrocarbons heavier than the hexanes (or
heptanes).
hydrate
A solid material resulting from the combination of a hydrocarbon
with water under pressure.
immiscible
Liquids that will not mix nor blend to give homogeneity are
said to be immiscible.
ideal gas (also called "perfect" gas)
A gas that obeys the ideal gas law expressed as PV=RT, see
Fig. 1-4.
inerts
Elements or compounds not acted upon chemically by the surrounding
environment. Nitrogen and helium are examples of
inert constituents of natural gases.
isobutane
In commercial transactions, a product meeting the GPA specification
for commercial butane and, in addition, containing a
minimum of 95 liquid volume percent isobutane. Chemically,
a hydrocarbon of the paraffin series with the formula C4H10
and having its carbon atoms branched.
jacket water
Water which fills, or is circulated through, a casing which partially
or wholly surrounds a vessel or machine element in order
to remove, add, or distribute heat in order to control the temperature
within the vessel or element.
Joule-Thomson effect
The change in gas temperature which occurs when the gas is
expanded at constant enthalpy from a higher pressure to a
lower pressure. The effect for most gases at normal pressure,
except hydrogen and helium, is a cooling of the gas.
lead acetate test
A method for detecting the presence of hydrogen sulfide by
discoloration of paper which has been moistened with lead acetate
solution. See ASTM D-2420.
lean gas
(1) The residue gas remaining after recovery of natural gas
liquids in a gas processing plant. (2) Unprocessed gas containing
little or no recoverable natural gas liquids.
lean oil
Absorption oil as purchased or recovered by the plant, or oil
from which the absorbed constituents have been removed.
lift gas
Gas used in a gas lift operation.
light ends
The low-boiling, easily evaporated components of a hydrocarbon
liquid mixture.
light hydrocarbons
The low molecular weight hydrocarbons such as methane, ethane,
propane and butanes.
LNG (liquefied natural gas)
The light hydrocarbon portion of natural gas, predominately
methane, which has been liquefied.
loading rack
A structural and piping installation alongside a railroad track
or roadway used for the purpose of filling railroad tank cars
or transport trucks.
LPG (liquefied petroleum gas)
Refer to definition of "LP-gas".
LP-gas (liquefied petroleum gas)
Predominately propane or butane, either separately or in mixtures, which is maintained in a liquid state under pressure within the confining vessel.
LRG (liquefied refinery gas)
Liquid propane or butane produced by a crude oil refinery. It may differ from LP-gas in that propylene and butylene may be present.
LTX (low temperature extraction unit)
A unit which uses the cooling of a constant enthalpy expansion to increase liquid recovery from streams produced from high pressure gas condensate reservoirs. Also called LTS (low temperature separation) unit.
Mcf
An abbreviation for one thousand cubic feet of gas.
MMcf
An abbreviation for one million cubic feet of gas.
mercaptan
Any of a homologous series of compounds of the general formula RSH. All mercaptans possess a foul odor.
miscible flood
A method of secondary recovery of fluids from a reservoir by
injection of fluids that are miscible with the reservoir fluids.

After 1000 years .. Disclosure of the secret head of the Inca people triangular

After about 1,000 years of mystery scientists have discovered Mexico City Onava way through which was showing a picture of a skull tribes of the Incas, which predicted the end of the world on December 21, 2012.

It turned out that the Incas were deliberately distorted skulls of cultural excellence door for them, and placing the baby in a triangle by clicking on the head and sealed timber after only one month of his birth.

The group affiliation of practices that have succeeded the peoples of the Incas, which pour in favor of quality scientific and practical level, development and civilization.

Well Test Description pdf

 Chapter 1 - PVT Property Correlations
PVT property correlations....................................................................................................................................................1-1
Chapter 2 - SCAL Correlations
SCAL correlations................................................................................................................................................................2-1
Chapter 3 - Pseudo variables
Chapter 4 - Analytical Models
Fully-completed vertical well................................................................................................................................................4-1
Partial completion ................................................................................................................................................................4-3
Partial completion with gas cap or aquifer ...........................................................................................................................4-5
Infinite conductivity vertical fracture.....................................................................................................................................4-7
Uniform flux vertical fracture ................................................................................................................................................4-9
Finite conductivity vertical fracture.....................................................................................................................................4-11
Horizontal well with two no-flow boundaries......................................................................................................................4-13
Horizontal well with gas cap or aquifer ..............................................................................................................................4-15
Homogeneous reservoir ....................................................................................................................................................4-17
Two-porosity reservoir .......................................................................................................................................................4-19
Radial composite reservoir ................................................................................................................................................4-21
Infinite acting ...... ..............................................................................................................................................................4-23
Single sealing fault ............................................................................................................................................................4-25
Single constant-pressure boundary...................................................................................................................................4-27
Parallel sealing faults.........................................................................................................................................................4-29
Intersecting faults ..............................................................................................................................................................4-31
Partially sealing fault..........................................................................................................................................................4-33
Closed circle ....... ..............................................................................................................................................................4-35
Constant pressure circle ....................................................................................................................................................4-37
Closed Rectangle ..............................................................................................................................................................4-39
Constant pressure and mixed-boundary rectangles..........................................................................................................4-41
Constant wellbore storage.................................................................................................................................................4-43
Variable wellbore storage ..................................................................................................................................................4-44
Chapter 5 - Selected Laplace Solutions
Introduction......... ................................................................................................................................................................5-1
Transient pressure analysis for fractured wells ...................................................................................................................5-4
Composite naturally fractured reservoirs .............................................................................................................................5-5
Chapter 6 - Non-linear Regression
Introduction......... ................................................................................................................................................................6-1
Modified Levenberg-Marquardt method...............................................................................................................................6-2
Nonlinear least squares.......................................................................................................................................................6-4
Appendix A - Unit Convention
Unit definitions .... ............................................................................................................................................................... A-1
Unit sets.............. ............................................................................................................................................................... A-5
Unit conversion factors to SI............................................................................................................................................... A-8

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Why if it is chopped earth worm does not die

Because the nervous system of the worm is widespread in all parts is represented each piece an important head of the worm cut into pieces

MPLS Traffic Engineering—Fast Reroute Link and Node Protection

Prerequisites for MPLS Traffic Engineering—Fast Reroute
Link and Node Protection

Your network must support the following Cisco IOS XE features:
• IP Cisco Express Forwarding
• Multiprotocol Label Switching (MPLS)
Your network must support at least one of the following protocols:
• Intermediate System-to-Intermediate System (IS-IS)
• Open Shortest Path First (OSPF)
Before configuring FRR link and node protection, it is assumed that you have done the following tasks but
you do not have to already have configured MPLS traffic engineering (TE) tunnels:
• Enabled MPLS TE on all relevant routers and interfaces
• Configured MPLS TE tunnels

Restrictions for MPLS Traffic Engineering—Fast Reroute Link
and Node Protection
• Interfaces must use MPLS Global Label Allocation.
• The router’s physical interface for MPLS-TE and Fast RR for Gigabit Ethernet (GE), and Packet over
SONET (POS) is supported for enabling a 50 millisecond (ms) failover. However, the GE
subinterfaces, logical interfaces and copper interface (e.g. Fast Ethernet interface) are not supported
for enabling a 50 ms failover (even though they may be configurable). Also, FRR is not configurable
on ATM interface.
• The FRR link protect mode failover time is independent of the number of prefixes pointing to the link.
• Cisco IOS-XE does not support QoS on MPLS-TE tunnels.
• Backup tunnel headend and tailend routers must implement FRR as described in draft-pan-rsvpfastreroute-
00.txt.
• Backup tunnels are not protected. If an LSP is actively using a backup tunnel and the backup tunnel
fails, the LSP is torn down.
• LSPs that are actively using backup tunnels are not considered for promotion. If an LSP is actively
using a backup tunnel and a better backup tunnel becomes available, the active LSP is not switched to
the better backup tunnel.
• You cannot enable FRR Hellos on a router that also has Resource Reservation Protocol (RSVP)
Graceful Restart enabled.
• MPLS TE LSPs that are FRR cannot be successfully recovered if the LSPs are FRR active and the
Point of Local Repair (PLR) router experiences a stateful switchover (SSO).


Fast Reroute
Fast Reroute (FRR) is a mechanism for protecting MPLS TE LSPs from link and node failures by locally
repairing the LSPs at the point of failure, allowing data to continue to flow on them while their headend
routers attempt to establish new end-to-end LSPs to replace them. FRR locally repairs the protected LSPs
by rerouting them over backup tunnels that bypass failed links or node.
Link Protection
Backup tunnels that bypass only a single link of the LSP’s path provide link protection. They protect LSPs
if a link along their path fails by rerouting the LSP’s traffic to the next hop (bypassing the failed link).
These are referred to as next-hop (NHOP) backup tunnels because they terminate at the LSP’s next hop
beyond the point of failure. The figure below illustrates an NHOP backup tunnel.

Node Protection
FRR provides node protection for LSPs. Backup tunnels that bypass next-hop nodes along LSP paths are
called next-next-hop (NNHOP) backup tunnels because they terminate at the node following the next-hop
node of the LSP paths, thereby bypassing the next-hop node. They protect LSPs if a node along their path
fails by enabling the node upstream of the failure to reroute the LSPs and their traffic around the failed
node to the next-next hop. FRR supports the use of RSVP Hellos to accelerate the detection of node
failures. NNHOP backup tunnels also provide protection from link failures, because they bypass the failed
link and the node.

The figure below illustrates an NNHOP backup tunnel.

If an LSP is using a backup tunnel and something changes so that the LSP is no longer appropriate for the
backup tunnel, the LSP is torn down. Such changes are the following:
• Backup bandwidth of the backup tunnel is reduced.
• Backup bandwidth type of backup tunnel is changed to a type that is incompatible with the primary
LSP.
• Primary LSP is modified so that FRR is disabled. (The no mpls traffic-eng fast-reroute command is
entered.)
Bandwidth Protection
NHOP and NNHOP backup tunnels can be used to provide bandwidth protection for rerouted LSPs. This is
referred to as backup bandwidth. You can associate backup bandwidth with NHOP or NNHOP backup
tunnels. This informs the router of the amount of backup bandwidth a particular backup tunnel can protect.
When a router maps LSPs to backup tunnels, bandwidth protection ensures that an LSP uses a given
backup tunnel only if there is sufficient backup bandwidth. The router selects which LSPs use which
backup tunnels in order to provide maximum bandwidth protection. That is, the router determines the best
way to map LSPs onto backup tunnels in order to maximize the number of LSPs that can be protected. For
information about mapping tunnels and assigning backup bandwidth, see the "Backup Tunnel Selection
Procedure" section.
LSPs that have the “bandwidth protection desired” bit set have a higher right to select backup tunnels that
provide bandwidth protection; that is, those LSPs can preempt other LSPs that do not have that bit set. For
more information, see the "Prioritizing Which LSPs Obtain Backup Tunnels with Bandwidth Protection"
section.
RSVP Hello Operation
RSVP Hello enables RSVP nodes to detect when a neighboring node is not reachable. This provides nodeto-
node failure detection. When such a failure is detected, it is handled in a similar manner as a link-layer
communication failure.

RSVP Hello can be used by FRR when notification of link-layer failures is not available (for example, with
Fast Ethernet), or when the failure detection mechanisms provided by the link layer are not sufficient for
the timely detection of node failures.
A node running Hello sends a Hello Request to a neighboring node every interval. If the receiving node is
running Hello, it responds with Hello Ack. If four intervals pass and the sending node has not received an
Ack or it receives a bad message, the sending node declares that the neighbor is down and notifies FRR.
There are two configurable parameters:
• Hello interval--Use the ip rsvp signalling hello refresh interval command.
• Number of acknowledgment messages that are missed before the sending node declares that the
neighbor is down--Use the ip rsvp signalling hello refresh misses command
RSVP Hello Instance
A Hello instance implements RSVP Hello for a given router interface IP address and remote IP address. A
large number of Hello requests are sent; this puts a strain on the router resources. Therefore, create a Hello
instance only when it is necessary and delete it when it is no longer needed.
There are two types of Hello instances:
• RSVP Hello Instance,
• RSVP Hello Instance,
Active Hello Instances
If a neighbor is unreachable when an LSP is ready to be fast rerouted, an active Hello instance is needed.
Create an active Hello instance for each neighbor with at least one LSP in this state.
Active Hello instances periodically send Hello Request messages, and expect Hello Ack messages in
response. If the expected Ack message is not received, the active Hello instance declares that the neighbor
(remote IP address) is unreachable (lost). LSPs traversing that neighbor may be fast rerouted.
If there is a Hello instance with no LSPs for an unreachable neighbor, do not delete the Hello instance.
Convert the active Hello instance to a passive Hello instance because there may be an active instance on the
neighboring router that is sending Hello requests to this instance.
Passive Hello Instances
Passive Hello instances respond to Hello Request messages (sending Ack messages), but do not initiate
Hello Request messages and do not cause LSPs to be fast rerouted. A router with multiple interfaces can
run multiple Hello instances to different neighbors or to the same neighbor.
A passive Hello instance is created when a Hello Request is received from a neighbor with a source IP
address/destination IP address pair in the IP header for which a Hello instance does not exist.
Delete passive instances if no Hello messages are received for this instance within 10 minutes.
Backup Tunnel Support
Backup tunnel support has the following capabilities:
Backup Tunnels Can Terminate at the Next-Next Hop to Support FRR
Backup tunnels that terminate at the next-next hop protect both the downstream link and node. This
provides protection for link and node failures. For more detailed information, see the Node Protection,
Multiple Backup Tunnels Can Protect the Same Interface
There is no limit (except memory limitations) to the number of backup tunnels that can protect a given
interface. In many topologies, support for node protection requires supporting multiple backup tunnels per
protected interface. These backup tunnels can terminate at the same destination or at different destinations.
That is, for a given protected interface, you can configure multiple NHOP or NNHOP backup tunnels. This
allows redundancy and load balancing.
In addition to being required for node protection, the protection of an interface by multiple backup tunnels
provides the following benefits:
• Redundancy--If one backup tunnel is down, other backup tunnels protect LSPs.
• Increased backup capacity--If the protected interface is a high-capacity link and no single backup path
exists with an equal capacity, multiple backup tunnels can protect that one high-capacity link. The
LSPs using this link will fail over to different backup tunnels, allowing all of the LSPs to have
adequate bandwidth protection during failure (rerouting). If bandwidth protection is not desired, the
router spreads LSPs across all available backup tunnels (that is, there is load balancing across backup
tunnels). For a more detailed explanation, see the Backup Tunnel Selection Procedure,
Backup Tunnels Provide Scalability
A backup tunnel can protect multiple LSPs. Furthermore, a backup tunnel can protect multiple interfaces.
This is called many-to-one (N:1) protection. An example of N:1 protection is when one backup tunnel
protects 5000 LSPs, each router along the backup path maintains one additional tunnel.
One-to-one protection is when a separate backup tunnel must be used for each LSP needing protection. N:1
protection has significant scalability advantages over one-to-one (1:1) protection. An example of 1:1
protection is when 5000 backup tunnels protect 5000 LSPs, each router along the backup path must
maintain state for an additional 5000 tunnels.

ICDL Module 1 (IT) lec (5)

1.8 Copyright and the Law
1.8.1 Copyright
1.8.1.1 Understand the concept of copyright when applied to software,
and also to files such as: graphics, text, audio, video. Understand
copyright issues involved in downloading information from the Internet.
Software Copyright Issues
• Most programs which you purchase are copyrighted and you must not copy them. If you
do so you may be breaking the law and if caught, you could find yourself being
prosecuted. Many people will buy a copy of a game and make a copy for their friends or
other family member. This is also normally unlawful. Even lending your program disks or
CD-ROM to other people may be breaking the law in most cases. There are numerous
organisations, such as FAST (the Federation Against Software Theft), which are
dedicated to preventing the illegal copying of software. In a business situation, if your
manager tells you to copy software, ALWAYS first make sure that you have a licence
which entitles you to copy the software, because in many countries, you will be
personally liable for damages.
• Most text which you will find on the Internet is copyrighted. Never copy text without
authority to do so and always quote your sources.
• There are many sites offering free graphics and clipart. Some are genuine and have the
authority to offer you a free download of images. Many sites however may not have this
authority. Popular examples are pictures, sound clips, or movie clips from Star Trek. If
you visit the official Star Trek site (www.startrek.com) you will see that use of images,
and even the name 'Star Trek' is protected and may not be used on 'fan sites'. Even
downloading sound clips to replace the bleeps which Microsoft Windows makes is often
illegal. Some sites even allow the 'free' download for complete films or music tracks. If
you can download a film for free before it is even officially available on video/DVD, it is a
pretty good bet that the site is unauthorised. Cover yourself. Get written permission to
used downloaded materials and 'if in doubt - don't' is the safe rule. Because CD-ROM
writers have become so widely available, it has become possible to copy entire CDROMs
which can contain software, games or data. Do not do this. Always be careful of
software which you may find advertised at very cheap prices, it may be illegally copied.
More Information: The Federation Against Software Theft http://www.fast.org.uk
What are site licences?
• Many large companies do not go out and buy a certain amount of 'shrink-wrapped'
copies of each software product which they need, instead they will buy a site licence.
These site licences are different in their small print, but generally mean that the
companies purchasing the licence can make a fixed numbers of copies available to their
staff, normally via a company network.
1.8.1.2 Understand copyright issues associated with using and
distributing materials stored on removable media such as CD’s, Zip
disks, diskettes.
Copyright Issues
• Transferring files across a LAN:
You need to be careful that you do not accidentally make copies of software via your
Local Area Network (unless of course you are authorised to make such copies).
• Downloading files from the Internet:
You need to be VERY careful when downloading files from the Internet. Just because a
site may say you are free to download materials from the site, does not necessary mean
that the owners of the Internet site have the authority to allow you to do this. It is possible
to download entire software packages from the net, even entire movie films. In many
cases however it is not legal to do so.
• Copying diskettes / CD-ROMs / DVD / ZIP disks:
If you purchase software, you may, in some cases be allowed to make a single, backup
copy of disk. You are not allowed to distribute copies to family and friends. You are
certainly not allowed to copy and re-sell commercial software.
• Freeware:
This is software which can be copied or downloaded for free. It is often fully functional.
Examples may include software developed by organisations such as Universities, where
the aim was not to profit from the software. It is very important not to confuse freeware
and shareware.
• Shareware:
This is where you can use software for a free trial period. Sometimes the shareware
versions may be fully functional, but after a time period will either start to display an
annoying message, asking you to register (i.e. pay for) your software, or in some cases it
may stop working altogether after the trial period. This 'try before you buy' method of
getting software is becoming increasing popular with the major software suppliers.
• User Licences:
If you have more than one PC, then you can either purchase a separate copy of the
software you require for each PC, or better: you can purchase a user licence. This user
licence allows you to make copies and install them on each computer. The more copies
you make the more the user licence will cost, but the cheaper the effective cost per PC.
1.8.1.3 Know how to check the Product ID number for a software
product. Understand the terms shareware, freeware, end-user licence
agreement.
How to check a software Product ID
• Normally if you click on the Help drop down menu within an application, there will be a
command such as About. Clicking on this option will often display your software product
identification number.
What is freeware?
• Some software is made freely available. Demonstration disks often come under this
category. In addition, a lot of software is produced by the educational community and is
made freely available. Always read any licences supplied with such software very
carefully before use.
What is shareware?
• Shareware is software which is freely available and is designed to let you use the
product for free, for a limited period while you decide if you like it or not. After this period,
you must legally either remove it, or pay an amount to the producers of the product.
More information: http://shareware.cnet.com
What about software which you find on the Internet
• There are some sites on the Internet run by dubious organisations which might make
copies of commercial software freely available. If you download any software from the
Internet, make sure that it is legal.
What is an end-user licence agreement?
• Normally when you install software these days there is a step within the installation
routine in which you have to agree to be bound by the end user licence agreement. This
agreement can be very large and is drawn up to protect the manufacturers of a product
from being prosecuted due to faulty software. It also defines how many copies of the
software you are entitled to. I recently printed out a Microsoft end user agreement and it
was over 15 pages long.
1.8.2 Data Protection Legislation
1.8.2.1 Know about data protection legislation or conventions in your
country. Understand the implications of data protection legislation for
data subjects and data holders. Describe some of the uses of personal
data.
Data Protection and Privacy Issues
• If your computer system holds information about individuals, then you have a moral and
legal duty to treat that information with respect. For instance if a police force computer is
used by unscrupulous people to gain unauthorised information about a person’s private
life, that would be a clear breach of trust. In the same way doctors, government
departments and credit agencies often hold vast amounts of information about the
general public, which is both sensitive and private. In a free society you have the right to
ensure that the information held about you is not abused. In many countries, this right is
enshrined under data protection laws.
Data Protection Legislation
• Listed below are the main principles of the UK Data Protection Act. This is meant as an
illustration only and should NOT be used for determining liability or operating principles.
You must read the full details of the act if you are considering legal implementation. For
more information about the UK data protection act please access the following Web
sites:
http://www.hmso.gov.uk/acts/acts1984/1984035.htm#aofs
http://www.pro.gov.uk/recordsmanagement/dp/default.htm
The information to be contained in personal data shall be obtained, and personal data
shall be processed, fairly and lawfully.
Personal data shall be held only for one or more specified and lawful purposes.
Personal data held for any purpose or purposes shall not be used or disclosed in any
manner incompatible with that purpose or those purposes.
Personal data held for any purpose or purposes shall be adequate, relevant and not
excessive in relation to that purpose or those purposes.
Personal data shall be accurate and, where necessary, kept up to date.
Personal data held for any purpose or purposes shall not be kept for longer than is
necessary for that purpose or those purposes.
An individual shall be entitled at reasonable intervals and without undue delay or
expense to be informed by any data user whether he holds personal data of which that
individual is the subject; and access to any such data held by a data user; and where
appropriate, to have such data corrected or erased.
Personal data held by data users or in respect of which services are provided by persons
carrying on computer bureau. Appropriate security measures shall be taken against
unauthorised access to, or alteration, disclosure or destruction of, personal data and
against accidental loss or destruction of personal data.