Wet ESPs – The Sky's the Limit
by Steven A. Jaasund P.E.
November 1, 2008
Wet electrostatic precipitation may be considered an old technology, but with new advances, it is worth another look.
As environmental requirements become tighter, the demand for
better gas cleaning technology has been rising as well. This trend has pushed
the development of a relatively old technology, the wet electrostatic
precipitator (Wet ESP).
First utilized in 1910 at a smelter in California for the
collection of sulfuric acid mist, the wet ESP led to the development of the dry
ESP, which has become the dominant version of precipitation technology used on
thousands of boilers and furnaces around the world.
Until the advent of the Clean Air Act in 1970,
wet precipitation technology has remained a mainstay for acid mist control. The
regulatory push mandated by this landmark legislation has rejuvenated interest
in wet ESPs. The result has been a number of innovative improvements in wet
ESPs that have led to opportunities in applications never anticipated.
Technical advantages
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| Figure 1: Operational concerns of fine particle control technologies. |
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The obvious distinction between dry and wet precipitation is
that wet ESPs operate on gas streams that are 100-percent saturated with water
vapor. This simple difference affords wet precipitation certain technical
advantages over dry precipitation and other non-electrostatic methods of
particulate collection.
The wet precipitation process is inherently useful on a
variety of gas-cleaning applications. This is because wet ESPs are relatively
immune to many limitations of other particulate separation alternatives,
including fabric filters, dry precipitators and even wet scrubbers. Factors
such as particulate resistivity and chemistry, while of great concern in dry
ESPs, are not a factor in wet ESPs; the particulate is collected on a wet, electrically
grounded surface. Also, temperature is normally not a concern because the gas
stream must first be quenched to the wet bulb temperature, normally below
170°F. Operation at this low temperature reduces gas volume, which allows lower
capital investment and saves energy.
Wet systems also offer several mechanical advantages over
their dry cousins. When constructed as a vertical flow, tube-type system wet
ESPs have none of the gas sneak-by issues confronting plate-type, dry ESPs.
Also they do not need to be mechanically vibrated to dislodge the collected
particulate matter. As a result, re-entrainment losses, a large part of the
inefficiency of a dry system, are not a problem.
Wet precipitators are ideal for treating gas
streams with condensable particulate matter. Such condensable matter may be in
the form of acid mist or condensed organic compounds, but cannot be collected
as particles until they form as a result of cooling. Dry ESPs and fabric
filters, limited to operating at elevated temperatures, cannot do this job.
Finally, wet ESP technology is attractive when fire is a concern and when
impediments to gas flow (e.g. plugging) must be avoided.
Recent advancements
Since the days when wet ESPs were strictly used for acid
mist control, there have been many significant developments that have enhanced
the technology. Some of the more important ones are discussed below:
Tube cooling. Most wet ESPs are
configured as vertical flow, tube-type systems, although plate-type units are
still occasionally applied. The tube design is a ready-made heat exchanger that
allows the design engineer to utilize the outside of the collecting tube for
heat transfer. This approach has two benefits. First, it encourages
condensation of water on the inside of the collecting tube, enhancing
particulate collection and making it easier to remove the collected particulate
matter. Second, it provides a source of warm air that can be used for a variety
of purposes, including purge air for the support insulator compartments, which
saves energy.
High-frequency power supplies. The
development of high-frequency power supplies has been beneficial to all
electrostatic precipitators. However, the benefits to wet ESPs may be the
greatest because of the costly materials of construction in wet units and
because of the tendency of wet units to be applied to gas streams with high
concentrations of fine particulate.
As seen in Figure 2, the high-frequency
power supply outperforms the standard 60-Hz, single-phase design. The
additional voltage means that the precipitator can be smaller for the same
efficiency or, alternatively, perform better at the same size.
Multiple, vertical stages. Multiple
electric fields in series are nothing new in dry ESPs; units with three or more
fields are the rule in coal-fired boiler applications. However, vertical fields
in series in wet ESP designs are a new development, one which has delivered
some surprising performance improvements. These multi-field installations have
shown outlet particulate concentrations that rival levels achieved by the best
fabric filtration systems. Also, field testing has shown that for a given level
of efficiency, the total required collecting area of a multi-field wet ESP is
significantly less than a single-field unit.
New materials. When Congress
passed the 1970 Clean Air Act, wet ESPs for acid mist service were made
exclusively of lead. In a few other applications, carbon and 300-series stainless
steels were used. Today, modern alloys ranging from duplex stainless steels all
the way up to high nickel alloys are commonplace. Also, fiberglass, PVC and
other polymeric construction have been employed.
New applications
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| Figure 2: High-frequency and 60-Hz waveforms. |
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Perhaps the most important new application for wet
precipitators is as a final gas-cleaning step for coal-fired utility boilers.
Presently there are five utility-scale wet ESP systems operating in North
America and several more in engineering and construction. These units are mostly
intended to control the sulfuric acid mist that is emitted downstream of a wet
flue gas desulfurization (FGD) scrubber. The need for an acid mist-control step
is further amplified by the effect of upstream selective catalytic reduction
systems designed to reduce NO X emissions. This is
because these systems tend to add SO 3 to the gas stream,
which ultimately hydrates to
H 2SO 4 in the FGD scrubber.
A related application presently being explored is directed
toward cleaning coal-fired utility boiler flue gas prior to entering a system
designed to remove CO 2. The role of the wet ESP is
critical in this process if the CO 2 is to be absorbed in
a highly alkaline liquor such as ammonia. In such a process it is extremely
important to remove the acid mist before the gas enters the
CO 2 absorber. Otherwise, the recirculated alkaline
reagent will be wasted as it reacts with the acid mist.
Another innovative application of wet ESPs has been in the
biofuels industry. In the manufacture of ethanol for fuel, the solid material
left behind from the fermentation tanks (distillers grain) is normally dried so
it can be stored and shipped as animal feed. Because the wet distillers grain
contains a significant quantity of volatile organic compounds (VOCs)
regenerative thermal oxidizers (RTOs), designed to incinerate the VOCs, are
normally required. These units can have trouble handling the wet, sticky
emissions from the dryers because of plugging and fouling. Wet ESPs are ideally
suited for pre-cleaning the gas stream prior to entering the oxidizer.
There are many ethanol and other plants in operation
throughout North America and many more are planned. The continued drive to
replace fossil fuels with green alternatives will mean a strong future for wet
ESPs in these industries.
Recently, the EPA promulgated new standards requiring the
installation of maximum achievable control technology (MACT) to be installed on
many solid-fuel fired boilers ( Ed Note: As of Sept. 2008, the present
MACT standards are being re-written by the EPA due to a recent court
decision). These regulations have significantly lowered the allowable
particulate emissions from many operating boilers and in some cases have forced
operators to install new emission control equipment. In many cases, the
technology of choice is the wet ESP.
A move to wet technology to meet MACT
requirements may, however, have a silver lining. Because of the inherent
flexibility of this technology, boilers with wet ESPs often can be fired with
alternative, low-grade fuels such as heavy oil, petroleum coke and tire-derived
fuel. These fuels are often much cheaper than higher-grade fuels.
Where can we go?
Because wet ESP technology is flexible, the array of
applications in which it can be applied is indeed very large. Here is a brief
list of some novel areas where the technology may be a good fit:
Regenerative catalytic oxidizers (RCOs).
RCOs consume less energy than RTOs. A limiting factor in their use, however, is
gas cleanliness, i.e., too much particulate can foul or poison the catalytic
media. In situations where a wet ESP is required to protect a downstream RTO,
there may still be too much particulate to allow for catalytic operation. In
these cases, if the performance of the wet ESP could be enhanced, then the RTO
could be changed into a catalytic unit with significant energy savings. As fuel
prices continue to rise, this approach could become more attractive.
Mist elimination – Wet ESPs are excellent
mist eliminators. In situations where very high mist removal efficiency is
required, a wet ESP may be an appropriate approach. Also, because they are so
efficient on relatively large water droplets, wet ESPs could be adapted for the
recovery of drift from cooling towers.
Gas separation. Research on gas
separation membrane technology continues at a fast pace in laboratories all
over the world. Application of these membranes shows a great deal of promise.
Keeping the membranes clean could be an important role for wet precipitation
technology particularly because wet ESPs are efficient and non-plugging, unlike
filters.
Nuclear waste processing. Vitrification
is the most likely fate of much of the high- and low-grade nuclear waste
generated in nuclear power plants. The challenge of the vitrication process is
cleaning the gas stream after it exits the glass furnace. Because the
particulate matter will be radioactive, an extremely high removal efficiency
will be required. However, because the amount of particulate matter will be
substantial, filters, which can plug, can be impractical. The open-flow,
high-efficiency wet ESP fits the bill.
As the first industrial wet ESP approaches its
100th anniversary, the industry is seeing more and more examples of wet
precipitation as a leading technology for particulate removal. With society
demanding more from technology to preserve the environment while providing
abundant and affordable energy Dr. Cottrell's simple and effective wet ESP may
be just beginning to come into its own. PE
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