|
|
Fugitive Emissions - the bad guys of the pollution world who avoid
even the toughest seals!
For many of us, the idea of a fugitive emission sounds deeply sinister and
conjures up images of dangerous, smelly chemicals skulking around behind our
backs, meaning to cause us harm. Well, not to anthropomorphasise pollutants, but
that is pretty much what these pollutants do. Mr P.J Lakhapate, a
Chemical Engineer and consultant who works in the field of fugitive emissions
helps us understand what these dangerous pollutants are and how to deal with
them.
What are fugitive emissions ?
Most fugitive emission cases are invisible to the eye. The fugitive emissions
of toxic/hazardous/corrosive substances are silent killers to human beings,
other living species, flora and fauna.
They are defined as emissions of "Any chemical or mixture of chemicals, in
any physical form, which represent an unanticipated or spurious leak, from
anywhere on an industrial site".
In other words, a fugitive emission could be that little hissing sound you
hear as you walk past an old looking valve at the dry cleaners. In reality, that
valve is releasing things into the environment that should stay in the machine -
for many reasons, not least of which that they are poisonous to you and your
environment.
Why are fugitive emissions important?
Fugitive emissions in the USA have been estimated to be in excess of 300,000
tones per year, accounting for about one third of the total organic emissions
from chemical plants. This situation is mirrored in Europe, and is probably much
worse in other parts of the world where environmental standards and levels of
policing are lower.
Volatile Organic Compounds (VOC's) emissions are of significant environmental
concern because some have the potential for Photochemical Ozone Creation
Potential (POCP), Ozone Depletion Potential (ODP), Global Warming Potential(GWP),
Summer smog, Toxicity, Carcinogenicity , Mutagenicity, Odour nuisance etc.
Apart from Safety, Health & Environment aspects fugitive emissions also
represent a huge loss of potentially valuable materials and cause of plant
efficiency.
- Visible cost
- Loss of material
- Invisible costs
- Labour to repair leaks
- Material to repair leak
- Wasted energy
- Low plant efficiency
- Environmental clean up
- Environmental fines
- Lost sale due to poor image
- Claims for personal injury
On what factors do the values of fugitive emissions depend?
Many process streams in petrochemical refineries are "light"
(containing at least 20% of substances with a vapour pressure greater than
0.3kPa at 20 °C) and at high pressure (1500- 3000 kPa) conditions which
encourage fugitive losses.
- The values of fugitive emissions depend upon
- Equipment design
- Age and Quality of equipment
- Standard of installation
- Vapour pressure of the process fluid
- Process temperature and pressure
- Number and type of sources
- Method of determination
- Inspection and maintenance routine Rate of production
How are fugitive emissions measured?
At present many end users prefer a leak-tightness result expressed in terms
of parts per million (ppm) measured by sniffing, since this is the format of the
Environmental Protection Agency (EPA) in the USA. These systems are widely used
across the world.
However ppm does not measure leakage rate, but indicates leakage severity.
Further research is being done to correlate concentration (in parts per million
- ppm) with the leakage rate.
Sources of fugitive emissions?
- Atmospheric tanks with/without breather valve
- Tank lids
- Seals of rotary equipment e.g. Pump Blower, Compressor, Turbine, Agitator
- Flange joints
- Leakage through vents & drains.
- Valve stem seals
- Sample points
Studies in various refineries indicate the following approximate distribution
of fugitive emissions:
- Valves - 60%
- Relief Valves - 15%
- Tanks - 10%
- Rotary Equipment - 10%
- Flanges - 5%
ISO-15848-1 is a standard for Measurement, Test & Qualification
procedures for Fugitive Emissions for Industrial Valves.
Studies differentiate fugitive emissions based on the type of valve. The
likelihood of leaking for the following types of valves are:
- Regulating Control Valve 70%
- Automatic Gate Valve 27
- Gate Valve 26
- Globe Valve 20
- Plug Valve 20
- Ball Valve 1
Also note that less than 1% of valves in gas/vapour service account for major
fugitive emissions in the refinery.
How fugitive emissions can be reduced
An Integrated Pollution Prevention Approach is necessary. A life cycle cost
for environmentally safe design must be evaluated at the beginning of the
project.
- For Valves:
The fugitive emissions can be substantially reduced by proper:
a) selection of type of valve (Plug or Ball instead of Gate or Globe)
b) selection of packing material based on process parameters
c) type of packing ( Diagonal interlock braided or flexible Graphite type
d) packing with bellow seal or with lantern ring
e) installation
f) maintenance
- For Control Valves:
PTFE stem gaskets are sensitive to thermal cycles at high temperature. In
the case of ordinary graphite gaskets the loading force requirement is high.
This increases the stem friction and affects stem movement. These problems
can be solved by perfluoroelastomer packing (Perfluoroelastomers are
polymerized from TFE and several other monomers including perfluoromethyl
vinyl ether).
- For Relief Valves:
It is difficult to reduce emissions through the relief valves since in most
of the cases these are linked with upsets in process conditions. However the
following guidelines can be used.
a) Keep an adequate margin between the operating pressure and set pressure.
b) For VOC emissions connect to a flare header
(If possible provide voc recovery system)
- For Rotary Equipment
Rotary equipment include Pumps, Compressors, Blowers, Turbines, Agitators,
Mixers, Blenders etc.
The fugitive emissions for rotary equipment depend upon
Design - Process Parameters, Speed, Seal selection,
Installation - Fixing with base plate, Piping connection forces, Shaft &
Casing alignment, Coupling alignment, Balancing of shaft & impeller
Commissioning - Poor priming
Operation - Beyond performance range
Maintenance - Inadequate
An approximate leakage rate for various sealing options are given below
-
|
gm/hr |
ppm |
| Gland Packing |
>1 |
>1000 |
| Single Mech . Seal |
0.01 - 1.0 |
10 - 1000 |
| Double Mech . Seal |
< 0.01 |
< 10 |
| Sealless |
0 |
0 |
- For Bolted Flanged Connections:
The factors affecting the leakages are
a) Non parallel flanges
b) Non smooth surfaces
c) Surface waviness
d) Quality of gasket
e) Type of gasket (Non metallic, Semi -metallic, Metallic)
f) Form of gasket (Plane Sheet, Rectangular, Spiral wound)
g) Type of joint involved ( flat, tongue & groove)
h) Process parameters (Pressure, Temperature)
i) Fluid handled
j) No. of Bolts
k) Installation Procedure (placement of gasket, tightening of bolts)
l) Maintenance
- A study conducted by the Pressure Vessel Research Council (PVRC) in the
USA indicated that most flange joint failures resulting in leaks were due to
a) Improper installation - 26%
b) Flange Damage - 25%
c) Gasket - 22%
d) Loose Bolts - 15%
e) Flange Misalignment - 12%
What are the statutory regulations/requirements?
- The 1990 Clean Air Act Ammendments (CAAA) lists 189 volatile hazardous air
pollutants(VHAP) including 150 volatile organic compounds(VOC). If process
contains 5% (or more) by weight of one or more VHAP it comes under CAAA
legislation.
- In April 1997, the CAAA incorporated Quality Improvement Program (QIP)
with earlier Leak Detection and Repair (LDAR) concept.
- If greater than 2% of tested valves are leaking (more than 500 ppm),
monthly inspections are required for all the valves or the the facility
stays at a quarterly inspection frequency by committing to a QIP programme.
- Further leaking valves must be repaired within 5 days, repaired and
retested within 15 days or identified for repair during the next shutdown.
Inspection timing intervals can be reduced to quarterly if leaking valves
are less than 2%, semiannually if leaking valves are less than 1% or
annually if less than 0.5% of the total no. of valves.
- A large refinery or petrochemical complex may have more than 100,000
components on various monitoring schedules for compliance with Environmental
Regulations. This is a major task for the maintenance team if implemented in
the right spirit.
- What is the path forward? Elimination is better than minimization. This
requires thinking out of the box.
- A few examples are given below:
- An excess flow valve (spring loaded valve) does not have a stem hence
there are no fugitive emissions. This automatic recirculation valve is
already being used in recirculation lines of centrifugal pumps. Thus
wherever possible this valve can be used instead of a control valve.
- If the line or equipment is kept under shade, then a thermal relief valve
for solar exposure can be eliminated.
- If the line is above 8m height then external fire case can be eliminated
for the liquid trapped between two isolation valves.
- If possible design the equipment for higher pressure rating and eliminate
the requirement of thermal relief valve.
- If possible select a low pressure process so that total emission can be
reduced substantially.
- Seal less pumps ( eg a Peristaltic Pump) are better than pumps with seals
as far as fugitive emissions are considered. However we need to improve the
efficiency of these pump.
- Use of a monobloc pump also eliminates seal requirement.
Inherent environmentally safe designs are the key for future survival.
More information:
About
Author: Mr P.J. Lakhapate is a Chemical Engr. from UDCT (Mumbai). He has 31
years of industrial experience and currently consults in the field. He has
published more than 30 articles. Contact information Phone:
91-22-27702655. Email: plakhapate@rediffmail.com.
Related articles:
Fuel cells - powering your home, your car tomorrow?
|