Innovative Energy & Research
Open Access

It has always been a goal to increase the energy transfer efficiency, within practical financial limits and operating specifications, of systems, which involve heat transfer [1]. Examples of such systems include: steam boilers which typically burn fossil fuel to convert water to steam for use in heating, cooling, process manufacturing, or the driving of turbines to produce electricity [2-4]; oil refinery furnaces which burn fossil fuel to heat crude oil to produce various petroleum products; and food processing systems which use fossil fuel to heat vegetable oil to produce a variety of products. Many of these systems burn millions of dollars of fuel per year, and thus small changes in efficiency can translate into large monetary savings [2,5,6]. Therefore, it is essential to conduct a thorough investigation on boiler equipment, particularly on its type, characteristics, maintenance and fuel consumption to ensure better boiler efficiency [7]. Boiler efficiency, in general, can be described as the difference between the input and output energy [8,9]. A conventional boiler would require immense initial capital expenditure on fuel usage alone per year. Therefore, slight improvement in boiler efficiency between units could provide significant amount of savings [3,10].

The preheating of feed water in boilers is one of the most effective methods for increasing the efficiency of steam boilers [11]. If the temperature of feed water increase to above 100 degree Celsius, then less firing rate is needed for reaching to a specific horsepower therefore, a significant saving in fuel consumption is achieved and the efficiency be improved [5,12]. The normal temperature of fuel gases in large boilers usually ranged from 230°C to 350°C. The heat produced from preheating of water can be recovered by using Stack economizers that are available in a various sizes [13,14]. Boiler stack economizer in general is a form of heat exchangers that separates between hot fuel gas and water [15-18]. Figure 1 shows the structure of economizer in fire-tube steam that allows the recycle usage of excess heat from exhaust [19].

Figure 1: Economizer in Fire Tube Steam Boiler.

The present paper focused on the effect of using economizer on the reduction of heat losses and increasing the efficiency of fire tube steam boiler. As well, it is aimed to determine the various types of losses and calculating the exact amount of efficiency before and after using economizer in examined fire tube boilers. The experiments provided the information needed to simulate influences of important parameters that are more effective on efficiency by using MATLAB software. The main purpose of this study is to demonstrate the importance of using an economizer to increase fuel saving during the life time of fire tube steam boiler, which is the most widely used boiler.

Efficiency in steam boiler

The efficiency in steam boilers is calculated by two methods, Direct Method (Input-Output method) and Indirect Method (Heat Loss Method) [20]. The Direct Method is assumed by measuring through instrumentation and the calculated data obtained will be utilized to calculate the fuel-to-steam efficiency [21-23]. The Indirect Method can be measured by considering the temporal losses totally. Therefore, the values obtained can be used to calculate the heat balance efficiency [10,24,25]. The main benefit of this method is that the errors in measurement do not make a major change in efficiency.

Performance test

The capacity of examined steam boilers are 6600 pounds (3000 kg of steam production per hour), this boilers were designed according to following standards of British Standard (BS) 2790, and ASME sec VIII and ISIRI 4231 [26-28]. The design pressure is 16 bar, the operation pressure is 10 bar, the pneumatic test pressure is 5 bar, and the hydro static test pressure is 16.5 bar. In first stage the steam boiler without using any equipment for increasing the efficiency (such as economizer) tested, the parameters were measured then the efficiency of the examined steam boiler will be calculated. In this study this boiler is called “Boiler 1”. Another steam boiler has been made with the same specification as “Boiler 1” but this steam boiler is equipped with economizer in the exhaust; in this study this boiler be named “Boiler 2”. The boiler was started and same parameters as before measured, according the results that collected from the experiment the efficiency of this boiler is calculated. Table 1 shows the ultimate analysis and flue gas analysis in “Boiler 1” and “Boiler 2”.

Table 1: Ultimate Analysis and Flue Gas Analysis in “Boiler 1” and “Boiler 2”.

The calculations for efficiency in these experiments by using indirect method show big differences between two boilers. In this stage the analysis of these discrepancies shows in Table 2 most of the difference in losses between the “Boiler 1” and “Boiler 2” is related to dry flue gas loss that is in “Boiler 1” more than 2 times bigger than “Boiler 2” and the main reason is because of reducing in flue gas temperature that is declined around 103 degree Celsius. The following losses that related to the hydrogen and moisture in fuel do not show big gap between twotested boilers because these losses are mainly related to the specification of fuel and the fuel that used in these boilers is exactly the same (diesel), by using diesel as fuel in these experiments the losses due to fly ash (carbon) and bottom ash (carbon) do not exist that loss due to partial combustion is zero in two examined boilers.

Efficiency and fuel’s GCV

One of the key factors that affect the efficiency is the fuel specification. The exchange of water phases in the combustion process uses energy and having higher water vapor loss during fuel firing

Table 2: The Efficiency and Losses in “Boiler 1” and “Boiler 2”.

would result in lower efficiency [29,30]. One of the most important parameters of the fuel is Gross Calorific Value (GCV) that shows the amount of heat made by the inflammation under steady and standard conditions [31,32].

The fuel that used in current experiments is diesel with the gross calorific value (GCV) of 10000 kCal/kg. By placing different fuel’s GCV in the efficiency equations by MATLAB software for the both of boilers, Figure 2 be obtained. The point that mentioned in the curves belong to the current fuel (diesel); as can be seen the type of fuel is more effective on the “Boiler 1” compare to “Boiler 2”; the difference between highest efficiency and lowest efficiency in “Boiler 1”is 45 percent, while this difference in “Boiler 2” is 30 percent, which indicates that the lower efficient boilers are more sensitive to fuel type.

Figure 2: Efficiency in Different GCV of Fuel in “Boiler 1” and “Boiler 2”.

one important point about these figures is that these efficiencies are not match with actual conditions because the efficiency by solid fuels (wood wastes with GCV’s from 2500 to 3850) have effected by some other parameters such as fly ash and bottom ash, that resulted different efficiency compare to these figures but this simulation is still beneficial for analysis the effect of GCV’s on the efficiency.

Efficiency and flue gas temperature

Flue gas or stack temperature determined as the combustion gases temperature in the exhaust of the boiler. The flue gas temperature has an important effect on the efficiency [33-35]. Figure 3 shows the effect of different flue gas temperature on efficiency of “Boiler 1” and “Boiler 2”. These figures show that the efficiency and flue gas temperature has a linear relationship. In both the boilers reducing the flue gas temperature has a same effect on efficiency and the slope is same in both the graphs, because this temperature has a fundamental role in all the losses especially on dry flue gas loss.

Figure 3: Efficiency by Different Flue Gas Temperature in “Boiler 1” and “Boiler 2”.

The difference of flue gas temperature of these boilers is due to the use of additional equipment in “Boiler 2”. The economizer decline the flue gas temperature to about 100°C and has a remarkable effect on improving the efficiency of “Boiler 2” about 7 percent compare to the efficiency of “Boiler 1” that is 77.23.

It has been proven that the initial cost of a boiler is a small part of total cost of boiler during its lifetime. The major costs resulting from the fuel costs. Therefore it is important to use a high efficient steam boiler that consume lower rate of fuel, for this purpose some equipment can be used in steam boilers that one of them used in this project that is economizer. The highest heat losses in boilers is related to dry flue gas that is around 12% of the total heat lost through the exhaust that resulting in efficiency equal to 77.2293% for “Boiler 1”, since the type of fuel and ambient temperature is the same in both boilers; therefore, using economizer concludes in a significant reduction of 103 °C in flue gas temperature. It shows the flue gas temperature of “Boiler 2” equal to 123 °C, and this declining the flue gas temperature declines the dry flue gas loss up to around 6 percent and it increases the efficiency of “Boiler 2” up to 84.5462%, which is a 7.3169% improvement in efficiency. It is found that the method of heat recovery from flue gas by economizer is one of the effective ways to save energy in fire tube boilers.

The authors would like to be obliged to Universiti Putra Malaysia and Nirou Boiler Company for providing facilities and financial assistance.