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instrument. Monitoring intervals depend on component type and periodic leak rate but are
typically weekly, monthly, quarterly, and yearly.
1.2.4. Repairing components
Components have to be repair as soon as possible after the leak is detected. The following
practices can be applied:
- Tightening bonnet bolts.
- Replacing bonnet bolts.
- Tightening packing gland nuts.
- Injecting lubricant into lubricated packing.
If the repair of any component is technically infeasible without a process unit shutdown, the
component may be placed on the Delay of Repair list.
1.2.5. Record keeping
For each regulated process, a list of ID number for all equipment subject, detailed schematics,
equipment design specifications, piping and instrumentation diagrams and results of
performance testing and leak detection monitoring must be maintain.
For leaking equipment, records, instrument and operator ID numbers and the date the leak
was detected must be maintained. The dates of each repair attempt and an explanation of the
attempted repair method is noted. Dates of successful repairs and results
of monitoring tests to
determine if the repair was successful are included.
2. Flue gases from process heaters and boilers
1,5,6,7,8,13
Fuel combustion in process heaters and boilers is an important pollutants and greenhouse
gases emission source. Carbon dioxide (CO
2
) is the principal gas released but nitrogen and
sulfur oxides (NOx and SOx), carbon monoxide (CO), organic compounds and particulate
matters (PM) are also released in non negligible quantities. In order to reduce the overall air
emissions of a refinery or a petrochemical plant, these emissions must be taken into account.
Several technologies exist to reduce these emissions. The present report synthesizes them.
2.1. General
In process heaters and boilers in refineries and petrochemical plants,
two major types of fuel
are burned by combustion sources: fuel gas and fuel oil.
Refinery fuel gas is a collection of light gases generated in a number of processing units in the
refinery. It contains principally hydrogen and methane and variable amounts of light
hydrocarbons such as ethane, ethylene or propane. It can also contain hydrogen sulfide in
trace amounts.
Fuel oil is a fraction obtained from petroleum distillation. It can be divided in two categories:
distillate oils and residual oils, further distinguished by grade numbers with 1 and 2 being
distillate oils and 5 and 6 being residual oils:
- Grade 1: Light domestic fuel oil-distillate.
- Grade 2: Medium domestic fuel oil-distillate.
- Grade 3: Heavy domestic fuel oil-distillate.
- Grade 4: Light industrial fuel oil.
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- Grade 5: Medium industrial fuel oil.
- Grade 6: Heavy industrial fuel oil.
There are four major types of boilers used in industrial applications: watertube, firetube, cast
iron and tubeless design. Boilers design and size, orientation of
heat transfer surfaces and
burner configuration are factors that influence strongly emissions and the potential for
controlling emissions.
Emissions depend also on type and composition of the fuel. Because the combustion
characteristics are different, their combustion can produce significantly different emissions.
Among these emissions can be found:
- Particulate emissions, filterable or condensable, which depends on the completeness of
combustion and the initial fuel ash content.
- Nitrogen oxides emissions, due either to thermal fixation of atmospheric nitrogen in the
combustion air (thermal NOx), or to the conversion of chemically
bound nitrogen in the fuel
(fuel NOx).
- Sulfur oxides emissions, that are generated during combustion from the oxidation of sulfur
contained in the fuel.
- Carbon monoxide and organic compounds emissions, which depends on the combustion
efficiency of the fuel.
- Trace metals emissions, which depend on the initial fuel metals content.
All these emissions can be estimated thanks to emission factors available in EPA literature.
Control techniques for the reduction of NOx, SOx and particulate matters are described and
compared below as these three types of emission are the most relevant.
2.2. Control techniques for NOx emissions reduction
NOx reduction in boilers and process heaters can be achieved with
combustion modification
and flue gas treatment or a combination of these. The choice of the technique depends on the
type and size of the boiler or heater, the fuel characteristics and the flexibility for
modifications. Practically, NOx reductions consist in
thermal NOx* reduction and
fuel NOx**
reduction. When fuel with low nitrogen content is used, such as fuel gas or distillate oil,
thermal NOx is the only component that can be controlled.
* Thermal NOx is produced by combination at high flame
temperature of nitrogen and
oxygen contained in the combustion air supply. It is produced during the combustion of both
fuel gases and fuel oils.
** Fuel NOx is produced by combination of nitrogen contained in the fuel with excess
oxygen contained in the combustion air. It is only a problem with fuel oils containing bound
nitrogen.
Combustion control involves consequently three main strategies:
- Reducing peak temperatures in the combustion zone.
- Reducing the gas residence time in the high-temperature zone.
- Reducing oxygen concentrations in the combustion zone.
5
These changes can be achieved with process modifications or operating conditions
modifications.
Finally, the flue gas treatment allows reducing NOx emissions.
Here below different technologies are generally and shortly described. The table synthesized
information available concerning efficiency and applicability of these technologies on process
heaters or boilers in petroleum industry, using fuel oil or fuel gas. Only methods that have
been used for industrial process heaters or boilers are considered here but many others
techniques exist.
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