GAS
Heat Terms and units:
Method of heat transfer:(For Specific Heat, Thermal conductivity,
Calorie, Calorific Value (both Higher or Gross calorific value and Lower or Net
calorific value), Ignition point, Combustion efficiency, Conduction, Convection
and Radiation, please refer previous notes on Fuels in catering industry)
LPG and its properties: LPG is synthesised by refining crude petroleum or
"wet" natural gas, and is almost entirely derived from fossil fuel
sources, being manufactured during the refining of petroleum (crude oil), or
extracted from petroleum or natural gas streams as they emerge from the ground.
LPG
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Advantages
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Disadvantages
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High efficiency and heating
rate
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Faint odours
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High calorific value 27800
kcal/m3
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Leakage
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No smoke, complete
combustion
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Fire hazard
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Clean, easy to use,
portable, cheap
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Accident prone
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Residue & oil
contamination is small
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Explosion
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Liquefied Petroleum Gas is a predominant
mixture of Propane and Butane with a small percentage of unsaturates (Propylene and Butylene). LPG may be defined as those
hydrocarbons, which are gaseous at normal atmospheric pressure, but may be
condensed to the liquid state at normal temperature, by the application of
moderate pressures. Although they are normally
used as gases, they are stored and transported
as liquids under pressure for convenience and ease
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of handling. Liquid LPG evaporates to produce about 250 times
volume of gas. To aid in the detection of atmospheric leaks, all LPG’s are
required to be odorized. For identification of gas leakage, LPG is mixed with
an obnoxious smelling gas dehydrated desulphurised traces of organic sulphites.
LPG vapour is denser than air: butane is about twice as heavy as air and
propane about one and a half times as heavy as air. Consequently, the vapour
may flow
along the ground and into drains sinking to
the lowest level of the surroundings and be ignited at a considerable distance
from the source of leakage. In still air, vapour will disperse slowly. Escape
of even small quantities of the liquefied gas can give rise to large volumes of
vapour / air mixture and thus cause considerable hazard. There should be
adequate ground level ventilation where LPG isstored. For this very reason LPG
cylinders should not be stored in cellars or basements, which have no
ventilation at ground level.
Storage Requirements
All gas cylinders:
§ Shall not be stored in exits or egress routes.
§ Shall be stored within a well-ventilated area.
§ Shall not be stored in damp areas, near salt or corrosive chemicals,
fumes, heat or exposed to the weather.
§ Shall be stored in an upright position.
§ Shall be secured with a chain or appropriate belt above the midpoint,
but below the shoulder.
§ Shall be capped when not in use or attached to a system (if the
cylinder will accept a cap).
§ Shall be kept at least 20 ft. away from all flammable, combustible or
incompatible substances. Storage areas that have a noncombustible wall at least
5 ft. in height and with a fire resistance rating of at least 30 minutes may be
used to segregate gases of different hazard classes in close proximity to each
other.
§ Shall be stored so that cylinders are used in the order in which they
are received.
§ Shall be stored so that gases with the same hazard class are stored in
the same area. Inert gases are compatible with all other gases and may be
stored together.
§ Shall not be stored longer than one year without use.
§ Shall be stored so that full cylinders remain separate from empty
cylinders.
COMPRESSED AND LIQUEFIED GAS USE
The
general “good practice” guidelines to follow when using gas cylinders and
compressed gases are:
General Requirements:
Ensure that regulator pressure control valve is relieved (i.e. closed)
before attaching to gas tanks.
Close valves on gas cylinders when a system is not in use.
Remove all pressure from regulators not currently used (by opening
equipment valves downstream after the regulators are closed).
Shut-off valves must not be installed between pressure relief devices
and the equipment they are to protect.
Use pressure relief valves in downstream lines to prevent high pressure
buildup in the event that a regulator valve does not seat properly and a tank
valve is left on.
Relief valves should be vented to prevent potential buildup of
explosive or toxic gases.
Never allow flames or concentrated heat sources to come in contact with
a gas cylinder.
Never allow a gas cylinder to become part of an electrical circuit.
Never partially open a tank valve to remove dust or debris from the
cylinder inlet.
Never use cylinder gas as compressed air.
Pressurize regulators slowly and ensure that valve outlets and
regulators are pointed away from all personnel when cylinder valves are opened.
Cylinders that require a wrench to open the main valve shall have the
wrench left in place on the cylinder valve while it is open. Use adequately
sized wrenches (12” long) to minimize ergonomic stress when turning tight tank
valves. Never apply excessive force when trying to open valves. Cylinders with
“stuck” valves should be returned to suppliers to have valves repaired.
Do not attempt to open a corroded valve; it may be impossible to
reseal.
Valves should only be opened to the point where gas can flow into the
system at the necessary pressure. This will allow for quicker shutoff in the
event of a failure or emergency.
Use a cylinder cap hook to loosen tight cylinder caps. Never apply
excessive force or pry off caps. Return to supplier to remove “stuck” caps.
Keep piping, regulators and other apparatus gas tight to prevent gas
leakage.
Confirm gas tightness by using leak test solutions (e.g., soap and
water) or leak test instruments.
Release pressure from systems before connections are tightened or
loosened and before any repairs.
Do not use Teflon tape on compressed gas fittings where the seal is
made by metal-to-metal contact. Use of Teflon tape causes the threads to
spread and weaken, increasing the likelihood of leaks.
Never use adapters or exchange fittings between tanks and regulators.
Fluorescent light can be used to check for grease or oil in regulators
and valves.
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Operation
of gas burner:
To operate LPG gas cylinder, the cylinder valve is first opened and then the
appliance valve opened and lighted match / lighter applied to the burner head
simultaneously. The gas ignites instantly and flame can be adjusted by the
control knob. When not in use the cylinder valve is to be kept closed to ensure
safety.
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Low-And
High-Pressure Gas Burners. The important thing in all gas-burning devices is a correct
air-and-gas mixture at the burner tip as shown above in the figure. Low-pressure
burners using gas at a pressure less than 0.15 kg/ cm2 (2
psi),are usually of the multi-jet type, in which gas from a manifold is
supplied to a number of small single jets, or circular rows of small jets,
centered in or discharging around the inner circumference of circular air
openings in a block of some heat-resisting material. The whole is encased in a
rectangular cast-iron box, built into the boiler setting and having louver
doors front to regulate the air supply. Draft may be natural, induced, or
forced.
In a high-pressure gas mixer, the
energy of the gas jet draws air into the mixing chamber and delivers a
correctly proportioned mixture to the burner. When the regulating valve is
opened, gas flows through a small nozzle into a venturi tube (a tube with a
contracted section). Entrainment of air with high-velocity gas in the narrow
venturi section draws air in through large openings in the end. The gas-air
mixture is piped to a burner. The gas-burner tip may be in a variety of forms.
In a sealed-in tip type, the proper gas-air mixture is piped to the burner, and
no additional air is drawn in around the burner tip. Size of the air openings
in the venturi tube end is increased or decreased by turning a revolving shutter,
which can be locked in any desired position. Excess air levels in natural gas
burner is in the order of 5%.
Draft System
The function of draft in a combustion system is to
exhaust the products of combustion into the atmosphere. The draft can be classified
into two types namely Natural and Mechanical Draft.
Natural Draft
It is the draft
produced by a chimney alone. It is caused by the difference in weight between
the column of hot gas inside the chimney and column of outside air of the same
height and cross section. Being much lighter than outside air, chimney flue gas
tends to rise, and the heavier outside air flows in through the ash pit to take
its place. It is usually controlled by hand-operated dampers in the chimney and
breeching connecting the boiler to the chimney. Here no fans or blowers are
used. The products of combustion are discharged at such a height that it will
not be a nuisance to the surrounding community.
Mechanical Draft
It is draft
artificially produced by fans. Three basic types of drafts that are applied are
:
Balanced Draft: Forced-draft (F-D) fan (blower) pushes
air into the furnace and an induced-draft (I-D) fan draws gases into the
chimney thereby providing draft to remove the gases from the boiler. Here the
pressure is maintained between 0.05 to 0.10 in. of water gauge below
atmospheric pressure in the case of boilers and slightly positive for reheating
and heat treatment furnaces.
Induced Draft: An induced-draft fan draws enough draft for flow
into the furnace, causing the products of combustion to discharge to
atmosphere. Here the furnace is kept at a slight negative pressure below the
atmospheric pressure so that combustion air flows through the system.
Forced Draft: The Forced draft system uses a fan to deliver the air to the furnace, forcing combustion products to flow
through the unit and up the stack.
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Manifold:
Gas manifolds provide a safe, cost-effective way of
connecting and changing out compressed gas cylinders by simply eliminating the
need to repeatedly handle the regulator during a cycle change-out. You can save
yourself both time and money by using these manifolds. You will also be able to
significantly reduce accidents caused by human error in changing out tanks. A
gas manifold is a great way to increase your productivity, eliminate error, and
enhance your gas delivery system.
1. An accessory system of piping to a main piping
system (or another conductor) that serves to divide a flow into several parts,
to combine several flows into one, or to reroute a flow to any one of several
possible destinations.
2. A pipe fitting with several side outlets to
connect it with other pipes.
A continuous supply manifold uses a pressure
reducing regulator with diaphragm valves to create a compact gas delivery
system that provides continuous gas flow. It uses two different gas sources, so
when one source empties, it automatically draws from the second source. The
first source can then be changed without interruption of the outlet pressure.
A header manifold provides a cost-effective
way to connect multiple high-pressure gas cylinders to the same gas supply
line. This design in gas manifolds can increase both gas storage capacity and
flow rate, and also provides a means for a continuous supply of gas
A high-pressure inlet manifold is ideal for
applications where gas consumption warrants one or two cylinders. It provided a
safe, cost-effective means of connecting and changing out cylinders by
eliminating the need to repeatedly handle the regulator.
Manifold configurations
To make the user use most of the allotted space for the system, two basic configurations are available-single row and double row.
To make the user use most of the allotted space for the system, two basic configurations are available-single row and double row.
Single row configuration: Here all the connections to the
manifold of cylinder is done in a continuous straight line.
Double row configuration: Here the connections to the manifold
occur on either side of the common line. It has two equal rows of cylinders
with a common pipe running between the two rows. It requires support from
either the ground up or suspended from above.
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