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






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.