1 boiler horse power is about 42,000 BTUs of INPUT
1 pound of steam is about 1,200 BTUs of INPUT fuel, and about 1,000 BTUs at the point of use, depending on the pressure of the steam
Low pressure steam is considered to be up to 15 psi; high is generally 100 psi and higher.
Superheat is a term that refers to higher temperature steam, as a result of a second special steam heat exchanger in the boiler that allows steam pressure to increase, thereby taking on more BTUs (in excess of 500 psi is typical of superheat)
Smaller boilers are generally rated in horse power; larger are generally rated in thousands of pounds of steam (500 hp and under will typically be rated in hp)
Typical boiler efficiency will be in the 75 - 85% range; new highest efficiency boilers may be near 90%; newer quick heat up types of boilers with copper heat exchangers are much more efficient, especially at startup and part load than older, heavy mass cast iron boilers
Common Boiler Types: (Click on table for larger view)
The firetube derives its name from the orientation by which heat is transferred to the fluid medium. The boiler body itself is a pressure vessel containing the fluid which is to be heated or physically altered. Within the vessel - and therefore within the fluid - are tubes which waste gases pass through. Heat is transferred from within the tube to the surrounding fluid; thus the name.
Advantages of this design are not often realized intuitively when compared to the watertube. The volume of fluid in the unit is roughly half the physical volume of the entire boiler, thus control of water levels and chemistry is much more forgiving and in need of less precision than for the typical watertube. Another advantage is found in the ease with which a unit is manufactured and serviced. The heat transfer tubes of the watertube boiler vary across the circumferential span of the drums: there may be eleven or more differing tube types to assemble in a single watertube unit. In the firetube, each heat transfer tube is identical to its counterparts. Manufacture and service are readily accomplished with a stock of a single tube type. It is this simplicity which contributes to the profound difference in life-cycle and capital cost of the firetube.
Disadvantages of the firetube are attributable only to ability. The limits of design pressure, supplemental firing rates, and capacity are realized more acutely with the firetube than with the watertube. Design pressures above 400 psig begin to move firetubes outside the realm of cost-effective design as do capacities above 80,000 lb/hr and supplemental firing temperatures above 1,600 deg F. While there are project-specific particulars which may or may not affect the overall project feasibility of the firetube design, the watertube often becomes the more reasonable option as operating parameters become more adverse.
Go to Johnston Boiler web page www.johnstonboiler.com for more information on firetube boilers.
The watertube is the most prevalent heat recovery device in industrial applications and derives its name from the orientation by which heat is transferred to the fluid medium. Flue gas passes through the boiler transferring heat into tubes placed within the gas path. Interior to the boiler tubes is the fluid medium to be heated or physically altered; thus the name "watertube".
Steam is an invisible gas that's generated by heating water to a temperature that brings it to the boiling point. When this happens, water changes its physical state and vaporizes, turning from a liquid into a gas.
Conversely, when heat energy is removed from steam, it loses its ability to retain a gaseous state and condenses back into a liquid. We refer to the resulting liquid as condensate. The temperature at which condensation takes place is known as the dew point.
When water is heated at atmospheric pressure, its temperature rises until it reaches 212°F (100°C), the highest temperature at which water can exist at this pressure. Additional heat does not raise the temperature, but converts the water to steam.
One pound of water takes 1 BTU per Degree of Temperature rise up to 212°F; to form steam, an additional 970 BTUs is required for the "Latent Heat of Vaporization". Therefore, steam has (970 + (212 - Condensate Temperature)) BTUs per pound. EXAMPLE: If the condensate temperature is 160°F, (970 + (212 - 160)) = 1,022 BTUs per pound. This clearly shows why steam has more energy content than hot water.
NOTE: These are BTUs delivered to the water; efficiency must also be factored in to determine INPUT BTU requirements.
For more information about Steam
Superheat refers to the process of increasing the temperature of steam above about 400°F and 100 psi. This feature is most common in very large power plant boilers of watertube construction. An additional heat exchanger capable of the high temperatures and pressures is required.
At least one company promotes a "direct fired" superheater, that could have some advantages for smaller sized boilers that need higher temperatures and pressures, but do not want to use a Thermal Fluid system.
According to their web site, the Cannon Superheater addresses two distinct markets, new boilers and retrofit installations. First, the addition of a Cannon Superheater allows the installation of a boiler best sized for an installation. An expensive watertube with an integral superheater could be put aside in favor of a smaller firetube with the Cannon unit. The Cannon superheater excels in the 25 HP to 1,000 HP range. Thermal oil systems, another way to achieve higher temperatures, are now less attractive. Thermal oil systems are expensive, not very flexible, and introduce environmental concerns. Simple and inexpensive steam plants with a superheater can achieve the same operating temperatures as the thermal oil system without their problems. For more information, see www.cannonboilerworks.com, Cannon Boiler's home page.
Flue gases from large boilers are typically 450 - 650°F. Stack Economizers recover some of this heat for pre-heating water. The water is most often used for boiler make-up water or some other need that coincides with boiler operation. Stack Economizers should be considered as an efficiency measure when large amounts of make-up water are used (ie: not all condensate is returned to the boiler or large amounts of live steam are used in the process so there is no condensate to return.)
The savings potential is based on the existing stack temperature, the volume of make-up water needed, and the hours of operation. Economizers are available in a wide range of sizes, from small coil-like units to very large waste heat recovery boilers.
Origin of the Problem
The most common source of corrosion in boiler systems is dissolved gas: oxygen, carbon dioxide and ammonia. Of these, oxygen is the most aggressive. The importance of eliminating oxygen as a source of pitting and iron deposition cannot be over-emphasized. Even small concentrations of this gas can cause serious corrosion problems.
Makeup water introduces appreciable amounts of oxygen into the system. Oxygen can also enter the feed water system from the condensate return system. Possible return line sources are direct air-leakage on the suction side of pumps, systems under vacuum, the breathing action of closed condensate receiving tanks, open condensate receiving tanks and leakage of nondeaerated water used for condensate pump seal and/or quench water. With all of these sources, good housekeeping is an essential part of the preventive program.
One of the most serious aspects of oxygen corrosion is that it occurs as pitting. This type of corrosion can produce failures even though only a relatively small amount of metal has been lost and the overall corrosion rate is relatively low. The degree of oxygen attack depends on the concentration of dissolved oxygen, the pH and the temperature of the water.
The influence of temperature on the corrosivity of dissolved oxygen is particularly important in closed heaters and economizers where the water temperature increases rapidly. Elevated temperature in itself does not cause corrosion. Small concentrations of oxygen at elevated temperatures do cause severe problems. This temperature rise provides the driving force that accelerates the reaction so that even small quantities of dissolved oxygen can cause serious corrosion.
The Corrosion Process
Localized attack on metal can result in a forced shutdown. The prevention of a forced shutdown is the true aim of corrosion control.
Because boiler systems are constructed primarily of carbon steel and the heat transfer medium is water, the potential for corrosion is high. Iron is carried into the boiler in various forms of chemical composition and physical state. Most of the iron found in the boiler enters as iron oxide or hydroxide. Any soluble iron in the feed water is converted to the insoluble hydroxide when exposed to the high alkalinity and temperature in the boiler.
These iron compounds are divided roughly into two types, red iron oxide (Fe2O3) and black magnetic oxide (Fe3O4). The red oxide (hematite) is formed under oxidizing conditions that exist, for example, in the condensate system or in a boiler that is out of service. The black oxides (magnetite) are formed under reducing conditions that typically exist in an operating boiler.
External treatment, as the term is applied to water prepared for use as boiler feed water, usually refers to the chemical and mechanical treatment of the water source. The goal is to improve the quality of this source prior to its use as boiler feed water, external to the operating boiler itself. Such external treatment normally includes:
Any or all of these approaches can be used in feed water or boiler water preparation.
Even after the best and most appropriate external treatment of the water source, boiler feed water (including return condensate) still contains impurities that could adversely affect boiler operation. Internal boiler water treatment is then applied to minimize the potential problems and to avoid any catastrophic failure, regardless of external treatment malfunction.
Feed Water Preparation
The basic assumption with regard to the quality of feed water is that calcium and magnesium hardness, migratory iron, migratory copper, colloidal silica and other contaminants have been reduced to a minimum, consistent with boiler design and operation parameters.
Once feed water quality has been optimized with regard to soluble and particulate contaminants, the next problem is corrosive gases. Dissolved oxygen and dissolved carbon dioxide are among the principal causes of corrosion in the boiler and pre-boiler systems. The deposition of these metallic oxides in the boiler is frequently more troublesome than the actual damage caused by the corrosion. Deposition is not only harmful in itself, but it offers an opening for further corrosion mechanisms as well.
Contaminant products in the feed water cycle up and concentrate in the boiler. As a result, deposition takes place on internal surfaces, particularly in high heat transfer areas, where it can be least tolerated. Metallic deposits act as insulators, which can cause local overheating and failure. Deposits can also restrict boiler water circulation. Reduced circulation can contribute to overheating, film boiling and accelerated deposition.
The best way to start to control pre-boiler corrosion and ultimate deposition in the boiler is to eliminate the contaminants from the feed water. Consequently, this section deals principally with the removal of oxygen, the impact of trace amounts of contaminants remaining in the feed water, and heat exchange impact.
Feed water is defined as follows:
Feed water (FW) = Makeup water (MW) + Return condensate (RC)
The above equation is a mass balance (pounds or kilograms).
Deaeration (Mechanical and Chemical)
Mechanical and chemical deaeration is an integral part of modern boiler water protection and control. Deaeration, coupled with other aspects of external treatment, provides the best and highest quality feed water for boiler use.
Simply speaking, the purposes of deaeration are:
Mechanical deaeration is the first step in eliminating oxygen and other corrosive gases from the feed water. Free carbon dioxide is also removed by deaeration, while combined carbon dioxide is released with the steam in the boiler and subsequently dissolves in the condensate. This can cause additional corrosion problems.
Because dissolved oxygen is a constant threat to boiler tube integrity, our discussion on the deaerator will be aimed at reducing the oxygen content of the feed water. The two major types of deaerators are the tray type and the spray type. In both cases, the major portion of gas removal is accomplished by spraying cold makeup water into a steam environment.
Tray Type Deaerating Heaters
Tray-type deaerating heaters release dissolved gases in the incoming water by reducing it to a fine spray as it cascades over several rows of trays. The steam that makes intimate contact with the water droplets then scrubs the dissolved gases by its counter-current flow. The steam heats the water to within 3-5 º F of the steam saturation temperature and it should remove all but the very last traces of oxygen. The deaerated water then falls to the storage space below, where a steam blanket protects it from recontamination.
Nozzles and trays should be inspected regularly to insure that they are free of deposits and are in their proper position.
Spray-Type Deaerating Heaters
Spray-type deaerating heaters work on the same general philosophy as the tray-type, but differ in their operation. Spring-loaded nozzles located in the top of the unit spray the water into a steam atmosphere that heats it. Simply stated, the steam heats the water, and at the elevated temperature the solubility of oxygen is extremely low and most of the dissolved gases are removed from the system by venting. The spray will reduce the dissolved oxygen content to 20-50 ppb, while the scrubber or trays further reduce the oxygen content to approximately 7 ppb or less.
During normal operation, the vent valve must be open to maintain a continuous plume of vented vapors and steam at least 18 inches long. If this valve is throttled too much, air and nonconclensable gases will accumulate in the deaerator. This is known as air blanketing and can be remedied by increasing the vent rate.
For optimum oxygen removal,
the water in the storage section must be heated to within 5 º F of the
temperature of the steam at saturation conditions. From inlet to outlet,
the water is deaerated in less than 10 seconds.
Deaerators and Economizers
Where economizers are installed, good deaerating heater operation is essential. Because oxygen pitting is the most common cause of economizer tube failure, this vital part of the boiler must be protected with an oxygen scavenger, usually catalyzed sodium sulfite. In order to insure complete corrosion protection of the economizer, it is common practice to maintain a sulfite residual of 5-10 ppm in the feed water and, if necessary, feed sufficient caustic soda or neutralizing amine to increase the feed water pH to between 8.0 and 9.0.
Below 900 psi excess sulfite
(up to 200 ppm) in the boiler will not be harmful. To maintain blowdown
rates, the conductivity can then be raised to compensate for the extra
solids due to the presence of the higher level of sulfite in the boiler
water. This added consideration (in protecting the economizer) is aimed
at preventing a pitting failure. Make the application of an oxygen scavenger,
such as catalyzed sulfite, a standard recommendation in all of your boiler
The foregoing discussion shows the importance of proper deaeration of boiler feed water in order to prevent oxygen corrosion. Complete oxygen removal cannot be attained by mechanical deaeration alone. Equipment manufacturers state that a properly operated deaerating heater can mechanically reduce the dissolved oxygen concentrations in the feed water to 0.005 cc per liter (7 ppb) and 0 free carbon dioxide. Typically, plant oxygen levels vary from 3 to 50 ppb. Traces of dissolved oxygen remaining in the feed water can then be chemically removed with the oxygen scavenger.
The main purpose of blowdown is to maintain the solids content of the boiler water within prescribed limits. This would be under normal steaming conditions. However, in the event contamination is introduced in the boiler, high continuous and manual blowdown rates are used to reduce the contamination as quickly as possible.
Because each boiler and plant operation is different, maximum levels should be determined on an individual basis.
By definition, bottom blowdown is intermittent and designed to remove sludge from the areas of the boiler where it settles. The frequency of bottom blowdown is a function of experience and plant operation. Bottom blowdown can be accomplished manually or electronically using automatic blowdown controllers.
Frequently used in conjunction with manual blowdown, continuous blowdown constantly removes concentrated water from the boiler. By design, it is in the area of highest boiler water concentration. This point is determined by the design of the boiler and is generally the area of greatest steam release.
Continuous blowdown allows for excellent control over boiler water solids. In addition, it can remove significant levels of suspended solids. Another advantage is that the continuous blowdown can be passed through heat recovery equipment.
Blowdown Control Summary
Proper boiler blowdown control in conjunction with proper internal boiler water treatment will provide the desired results for a boiler water program. Many modern devices can automate boiler blowdown, thereby increasing the overall efficiency of the unit.
ION EXCHANGE SYSTEMS
Ion exchange systems range from light commercial water softeners and filters to specially designed industrial equipment. Also known as deionizations (DI) systems. These systems are considered high-end where the highest quality of water treatment is needed, such as with steam turbines.
Reverse Osmosis (RO) systems are available for tap water, brackish water or seawater. These systems are considered high-end where the highest quality of water reatment is needed, such as with steam turbines.
Boiler manufacturers whos products/information are referenced above include:
Web site: www.cleaver-brooks.com
Web site: www.johnstonboiler.com
For a larger listing of manufacturers and resources, see the Vendors Section of this web site.
Sources: TechPro, DTE Energy/Bob Fegan 8/01; Johnston Boiler web site, 8/01; Armstrong International web site, 9/01; N.E.M. Business Solutions, "An Introduction to Steam Boilers and Steam Raising" at www.cip.ukcentre.com/steam.htm 9/01; economizer picture from www.e-techninc.com 9/01;