Circulating Fluidized Bed.docx

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Circulating Fluidized BedFrom Wikipedia, the free encyclopedia

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The circulating fluidized bed(CFD) is a clean process with the ability to achieve lower emission of

pollutants. By using this technology, up to 95% of pollutants[1]

will be absorbed before being emitted to the

atmosphere. At the same time, the advantages of this technology outweigh the limitations, which made it

favourable. However, the development of this technology is still at its early stages. With further R&D, this

technology is predicted to bring numerous benefits to our society.

Contents

[hide]

1 Introduction

o 1.1 Basic Fundamental

2 Range of Applications

o 2.1 Circulating Fluidized Bed Scrubber

o 2.2 Circulating Fluidized Bed Gasification System

3 Advantages and Limitations of Circulating Fluidized Bed

4 Available Design of Circulating Fluidized Bed

5 Main Process Characteristics

o 5.1 Design and Operation

6 Process Characteristics Assessments

7 Possible Heuristics to Be Used During the Design of the Process

8 New Development

o 8.1 InBed Heat Exchanger

o 8.2 U-Beam Separator Design

9 References

Introduction[edit]

Circulating fluidized bed is a relative new technology with the ability to achieve lower emission of pollutants.

Extensive research has been conducted on this technology for the past 10 years because pollution in the

world is getting more serious by the day and clean practice will be very crucial for the sustainability of the
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earth. The importance of this technology grew even more lately because of the tightened environmental

regulation for pollutant emission.

The Mercury and Air Toxic Standards (MATS) enacted in December 2011 by EPA have forced all the

countries in Europe and America to strictly adhere to this policy. This means that emissions such asmetals, acid gases, organic compound, flue gas acids and other pollutants from power plants or industrial

facilities have to meet the requirements set by EPA[2]

and upgrades have to be done for facilities that do

not meet the standards. As a result, the demand for circulating fluidized bed technology will be predicted to

go sky rocket.

Basic Fundamental[edit]

During the combustion phase, upwards jets of air will cause the solid fuels to be suspended. This is to

ensure the gas and solids will mix together turbulently for better heat transfer and chemical reactions. The

fuel will be burnt at a temperature if 1400oF to 1700oF to prevent nitrogen oxide from forming.[1]While

burning, flue gas such as sulfur dioxide will be released. At the same time, sulfur-absorbing chemical such

as limestone or dolomite will be used to mix with the fuel particles in the fluidization phase, which will

absorb almost 95% of the sulfur pollutants.

Alternatively, the sulfur absorbing chemical and fuel will be recycled to increase the efficiency of producing

a higher quality steam as well as lower the emission of pollutants. Therefore, it will be possible to use

circulating fluidized bed technology to burn fuel in a much more environmental friendly method as

compared to other conventional processes.

Range of Applications[edit]

Circulating fluidized bed technology can be implemented in many different fields ranging from oil and gas to

power stations. This technology is highly sought after due to its numerous benefits. Some of the popular

applications of circulating fluidized bed are circulating fluidized bed scrubber and circulating fluidized bed

gasification system.

Circulating Fluidized Bed Scrubber[edit]

One of the applications of a circulating fluidized bed scrubber is at power stations which utilize a dry

sorbent usually Ca(OH)2to reduce pollutants like HF, HCL, SO2and SO3in a flue gas stream.[3]

Currently,

Basin Electric Power Cooperative are the only company operating the best available circulating fluidized

bed scrubbing technology for a coal fired boiler plant near Gillette Wyoming since 2011.[4]

The three major components of the circulating fluidized bed scrubber in power plants are:

Circulating Fluidized Bed Absorber

Fabric Filter

Dry Lime Hydration System.
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In the circulating fluidized bed scrubber process, flue gas will enter the reactor from the bottom of the

vessel. Simultaneously, hydrated lime will be injected into the circulating fluidized bed absorber for reaction

to take place to convert SO2and SO3from the flue gas to calcium sulfate and calcium sulfite. Water will

also be injected at the same time to control the operation temperature for maximum absorption capacity.

The flue gas will then send to the bag house for further filtration. In the bag house, a series of air valves

across the filters, will produce compressed air bursts to ensure a more efficient solid and dust collection.

Lastly, clean flue gas will then be directed to the stack with the minimum pollutants in the flue gas

stream.[4]

The schematic diagram of the process is shown in Figure 1.

Circulating Fluidized Bed Gasification System[edit]

Gasification is the process of converting biodegradable waste materials into synthetic gas without

combustion. This process is first used at the Gussing power plant in Austria[5]

based on the steam

gasification of biomass in the internally circulating fluidized bed.

In the gasification process, fuel will be gasifies at 850oC

[5]in the presence of steam to produce a nitrogen-

free and clean synthetic gas. Charcoal with be burnt with air in the

Figure 2: Showing Gasification Process Schematic Diagram

combustion chamber to provide the heating for the gasification process as it is an endothermic process.

Thermal transfer will take place between the gasification and combustion chamber. The illustrated

gasification process is presented in Figure 2.

The chemical reaction that takes place in the gasification as shown in equation [1] and [2] whereas the

reaction in combustion chamber is represent in equation [3].

Gasification;

C + H2O = CO + H2 [1]

C + CO2= 2CO [2]

Combustion;
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C + O2= CO [3]

Dolomite lime or limestone can also be used to increase the hydrogen concentration by absorbing carbon

dioxide to increase the combustion process.

Advantages and Limitations of Circulating Fluidized Bed[edit]

Before, wet flue gas desulfurization (Wet FGD) had been used to capture the pollutants gas. However, this

machinery is expensive to be built, hard to be maintained and take a lot of space in chemical plant. Wet

FGD uses lot of water, however only marginal metals like mercury and acid gases such as HCl, HF and

SO3 can be captured.[6]

Hence, new technology of circulating fluidized bed scrubber (CFBS) was introduced circa 1984 to improve

performance. The turbulator wall design will ensure a perfect mixing and the ability to capture various

pollutants. The used of alloy metals had been replaced with a carbon steel design, reducing the installation

cost. It also comes in a compact size hence the capital costs could be reduced. The water usage also can

be reduced with the design of plug-free water spray nozzles.[7]

Besides that, the CFBS can undergo self-

cleaning process, which reduces the cost of maintenance. The operating temperature is also low thus the

production of the nitrogen oxides, which is one of the greenhouse gases, can be minimized.[8]

Despite of all the advantages, the CFBS that is higher than 400 MW will require more than one unit. The

limestone used in the CFBS is more expensive and must be kept either in a concrete or steel silo rather

than a pile[8]. Besides that, this machinery also produces a by-product, for instance CaCl that do not have

many uses due to its properties.[8]

Another type of CFB is circulating fluidized bed gasification (CFBG), which is more preferable compared to

other type of gasifiers. CFBG has a high mass and heat transfer rate as well as high efficient gas-solid

contacting. At low operating temperature of CFBG, a longer residence time of solid can be achieved

leading to a higher gasification yield.[9]

CFBG process is more energy efficient as it is an endothermic

process. Only the required heat will be generated to maintain the process at the optimum

temperature.[9]

Practically, all the heat produced will be utilized throughout all the processes, as it is an

adiabatic and isothermal process.[9]

Even though, the CBFG process is able to manage huge range of fuels but high gasification yield cannot

be achieved for the fuels that are less reactive such as anthracite and pet coke because of the low

operating temperature. The flow is also multiphase complex and every distinct particles need to be scale-

up in a different way[10]

Available Design of Circulating Fluidized Bed[edit]

Nowadays, several designs had been invented for CFBS for example the CFBS develop by Clyde

Bergemann Power Group namely Circulating Dry Scrubbers (CDS). This type of CFBS is consisted of three

distinct feedback control loops which are for temperature, pressure drop and sulphur dioxide emission.[11]

In
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order to minimized erosion, it injection was designed to be above the ventures . Not only that, the CDS

contains less moving parts compared to other type of CFBS. This design will lead to a lower maintenance

cost. Major components of the CDS are shown in Figure 3.

Similar to CFBS, there are several designs available with specific specification to fulfill various industrialdemands. One of the types is the CFBG, developed by the Phoenix BioEnergy. This type of CFBG

combines several technologies and implement the auger gasifier into one design. The large diameter of the

auger will be placed horizontally on top of the fluidized bed. This configuration will increase the gasification

efficiency, which will assist in the heat transferral over the suspended aggregate into the biofuel.[12]

Full

design of this CFBG is shown in Figure 4.

Main Process Characteristics[edit]

The circulating fluidized bed reactors have been widely used in various industrial processes such as

gasification and coal combustion.[13]

Though the circulating fluidized beds are used widely, the CFD, which

can be, describe by non-uniformity flow patterns and a thorough back mixing still possess significant radial

gradients in the particle density and a lower solid holdup inside the riser interior compared to the wall of the

reactor. These events will then result in low contact efficiency.[14]

For the case of catalytic gas-phase reaction process, gas back mixing should be avoided thus the reacted

product is the gas phase. Another characteristic of the circulating fluidized bed is, as it required promoting

the small contact time of gas and solid catalyst and plug flow, a significant high gas velocity in the riser is

needed.[14]

The significant high gas velocity in the riser is also desired to fulfill the necessity in the catalytic

gas-phase reaction.

Design and Operation[edit]

The circulating fluidized bed involves basically two balancing characteristics of the gas-solid system, which

are the design and the operation characteristics.

Design: Recirculating loop of particles occurred when entrained particles, which possess a substantial

amount of flux, are separated efficiently and externally to the reactor from a giant core reactor (riser) from

its carrying fluid and will then be circulated back to the bottommost of the riser. The carrying fluid will

circulate around this loop only once however the particle will pass through several times before finally

leaving the system[15]

The schematic diagram of a typical circulating fluidized bed can be seen in Figure 5

below.

Operational: The system is usually operated under high particle flux and high superficial gas velocity, which

are typically (101000 kg/m2s), and (212 m/s) respectively.

[15]This operational condition is chosen to

avoid a distinct interface between the dilute region and the dense bed inside the riser. Thus gas velocities

above the bubbling point is chosen for contacting.[15]

The standard operating conditions for the circulating

fluidized bed can be seen in Table 1 below.

Parameters Accepted Values
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Superficial Gas Velocity (m/s) 2 - 12

Net Solids Flux Through The Riser (kg/m2s) 10 - 1000

Temperature (C) 20 - 950

Pressure (kPa) 100 - 2000

Mean Particle Diameter (m) 50 - 500Overall Riser height (m) 15 - 40

Table 1:Typical operational condition for circulating fluidized bed in commercial use

Process Characteristics Assessments[edit]

The circulating fluidized bed (CFB) use high fluid velocity to provide better gas-solid contact by providing

more intense mixing of the fluid so that better quality of product can be obtained. However, the high gas

velocities and the recirculation of solids may make the CFB system much more expensive in term of power

requirement and investment compared to conventional f luidized bed reactors.[16]

CFBs have been widely

used in the field of solid catalyzed gas phase reactions in two situations below.[17]

1. Continuous regeneration of catalyst, which deactivates rapidly. The solid is maintained in constant

circulation where catalyst is continuously regenerated and return to the reactor.

2. Heat must be brought in or removed from a reactor. A continuous circulation of solids between

vessels can efficiently transport heat from one vessel to another since solids have relatively large

heat capacity compared to gases.

One important factor of circulating system is the ability to control the feed circulation rate. The feed

circulation rate is control by the gas velocity in the bed which determines the flow regime and density of

bed. All the circulating systems can be characterized either by the solid circulation rate, kg/s and the

transfer ratio of the suspended materials being exchanged between vessels .[17]

For circulating fluidized bed in coal combustion, the beds need to use a greater fluidizing speed, so the

particles will remained constant in the flue gases, before moving across the combustion chamber and into

the cyclone. During combustion, a dense bed is required to mix the fuel eventhough the solids are

dispersed evenly all over the unit. The bigger particles are extracted and returned to combustion chamber

for further process, which required relatively longer particle residence time. . If the total carbon conversion

efficiencies gets over 98% it shows good separation process that leaves simply a minor proportion of

unburned char in the residues.[18]

During the whole process, the operating conditions are relatively uniform

for the combustor.

Possible Heuristics to Be Used During the Design of the Process[edit]

In designing a circulating fluidized bed, it shows an excellent heat transfer. The reactors usually show

constant temperature distribution for either endothermic or exothermic reactions. In order to determine the

appropriate design for cooling or heating of the circulating fluidized bed reactors, a good approximation of

heat transfer rates are necessary for better control so that the reactors can change its performance for
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different operating conditions.[19]

For highly exothermic reactor, it is recommended to keep the conversion

of material low and recycle any possible cooled reactants. It is also recommended to separate the

components in order of decreasing percentage of material in feed. This will help in reducing the cost of

maintenance for the next separation process.

In many industrial processes that involved small, porous or light particle which have to be fluidized with

more viscous fluid in the present of gas, a Gas-Liquid-Solid circulating fluidized bed (GLSCFB) is more

preferred compared to conventional system because it can minimize dead zone and increase the

contacting efficiency among gas, liquid and solid phases by improving the shear stress between those

phases. Gas-Liquid-Solid circulating fluidized bed also can provide higher gas holdup, produce more

uniform bubble size, better interphase contact, and good heat and mass transfer capabilities. The flexibility

of using GLSCFB allow the fluidized bed to operate at much more higher liquid velocity than the minimum

fluidization velocity which in turn increase the fractional conversion as well as production efficiency per unit

cross-sectional area of the bed. Moreover, the deactivated catalyst used in the GLSCFB can be

regenerated continuously by using the circulating fluidized bed which in turn reduced the operating cost for

replacing the catalyst frequently.[20]

As for circulating fluidized bed scrubbers (CFBS), it is more preferred in industrial due to its ability to

produce higher purity product while avoiding the corrosion issue. The CFBS also preferred because it

requires low installation cost, high capture of metals, low maintenance required, wide fuel sulphur flexibility

and fast response to cope with changes in operating condition.[21]

Some modification is necessary at the

inlet in order to eliminate loss of solids materials at the bottom of bed during low-load operation. For better

quality of product, it is advisable to purify the feed stream if it is difficult to separate between the impurity

and the desired product if it is present in large amount.

This will enable the fluidized bed to operate at full capacity range in a stable manner. Every CFBS need to

have larger boilers that are connected to several cyclones in parallel as to remove the solids for

recirculation.[18]

CFBS also need to have heat recovery unit as some of the heat from the bottom ash can

be recovered as it is more economically feasible in term of lowering the operating cost. Ash coolers are

prone to foul the bed while the heat transfer tubes in fluidized bed are prone to erosion can be removed by

the use of some fluidizing air.

New Development[edit]

More new clean technology has to be implemented to maintain the sustainability of the earth. Bigger

reactors, with lower pollutants emission, have to be developed to meet the global demand. One of the best

clean technologies to be used is the circulating fluidized bed technology. However, circulating fluidized bed

technology is still at a very early stage. Currently circulating fluidized bed technology has only reached the

second generation and is more efficient in capturing pollutants with a simpler design as compared to the

first generation.[10]

The most significant development for this technology is the development of in-bed heat

exchanger and the U-beam separator design.
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InBed Heat Exchanger[edit]

Another major field that is currently being looked into is the further development of in-bed heat exchanger

used with circulating fluidized bed technology. With this design, the bed materials fill the in-bed heat

exchanger through the open top of the circulating fluidized bed furnace, which enables the control ofmaterials through the in-bed heat exchanger.

[22]By being able to control the materials throughput rate,

better control of heat absorption as well as bed temperature in the furnace is achievable. With further

development in this field, we will be able to fully utilize the energy required to drive the furnace with

minimum energy wastage.

U-Beam Separator Design[edit]

The U-beam separator design has been improved for better efficiency, reliability as well as maintainability

and it is now in the 4th generation of its design as shown in Figure 6.

With the improved design, this has contributes and bring numerous benefits to the circulating fluidized bed

technology. Some of the benefits are as follows:[22]

High solids collection efficiency

Controlled furnace temperature

Low auxiliary power

Smaller footprint

Minimal refractory use

Low maintenance
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