fine ash formation during combustion of pulverised coal–coal property impacts

9
Fine ash formation during combustion of pulverised coal–coal property impacts B.J.P. Buhre a, * , J.T. Hinkley a , R.P. Gupta a , P.F. Nelson b , T.F. Wall a a Cooperative Research Centre for Coal in Sustainable Development, Department of Chemical Engineering, University of Newcastle, Callaghan, NSW 2300, Australia b Cooperative Research Centre for Coal in Sustainable Development, Graduate School of the Environment, Macquarie University, NSW 2109, Australia Received 5 October 2004; received in revised form 24 February 2005; accepted 14 April 2005 Available online 15 September 2005 Abstract In many countries, legislation has been enacted to set guidelines for ambient concentrations and to limit the emission of fine particulates with an aerodynamic diameter less than 10 mm (PM 10 ) and less than 2.5 mm (PM 2.5 ). Ash particles are formed during the combustion of coal in pf boilers and fine ash particulates may potentially pass collection devices. The ash size fractions of legislative interest formed during coal combustion are the result of several ash formation mechanisms; however, the contribution of each of the mechanisms to the fine ash remains unclear. This study provides insight into the mechanisms and coal characteristics responsible for the formation of fine ash. Five well characterized Australian bituminous coals have been burned in a laminar flow drop tube furnace in two oxygen environments to determine the amount and composition of the fine ash (PM 10 , PM 2.5 and PM 1 ) formed. Coal characteristics have been identified that correlate with the formation of fine ash during coal combustion. The results indicate that coal selection based on (1) char characterization and (2) ash fusion temperature could play an important role in the minimization of the fine ash formed. The implications of these findings for coal selection for use in pf-fired boilers are discussed. q 2005 Elsevier Ltd. All rights reserved. Keywords: Coal combustion; Fine ash; Coal characterisation 1. Introduction The health effects of ambient fine particulates have been studied extensively and correlations have been observed between ambient fine particulate matter and human mortality rates e.g. [1]. Governments worldwide acknowledge these studies and as a result standards have been introduced to assist in reducing ambient fine particulate concentrations. In the United States, a National Ambient Air Quality Standard (NAAQS) for both ‘coarse’ particulate matter with an aerodynamic diameter less than 10 mm, PM 10 , as well as an NAAQS for PM 2.5 is currently in effect [2]. Recently in Australia, the National Environment Protection (Ambient Air Quality) Measure (NEPM) has been modified to include advisory reporting standards for PM 2.5 , the monitoring of which commenced in January 2004 [3]. PM 10 has been included in the NEPM Ambient Air Quality measures since, 1998 [4]. Around 80% of the electricity generated in Australia is generated by coal combustion [5], and coal- fired power generators are increasingly being required to monitor and characterise their emissions of fine particulate matter. Air pollution control devices (APCDs) are employed at power stations to capture the ash particulates from the flue gas. Increasing the capture efficiency of these APCDs to decrease fine ash emissions can be a costly exercise. Selecting coals which reduce the formation offine ash particulates in the first place could be a cost-effective method of minimizing fine ash emissions. This paper presents the results of a study for the coal characteristics responsible for the formation of fine ash particles. Five Australian black coals have been characterised extensively using advanced analytical techniques such as QEMSCAN, SIROQUANT, and ICP-AES on ash obtained from radio-frequency ashing technique. The coals were then burned in a drop tube furnace, which simulates the combustion in a pf fired boiler. The ash was characterised and the coal characteristics responsible for the formation of the ash size fractions of legislative interest (PM 10 , PM 2.5 , and PM 1 ) have been determined. Fuel 85 (2006) 185–193 www.fuelfirst.com 0016-2361/$ - see front matter q 2005 Elsevier Ltd. All rights reserved. doi:10.1016/j.fuel.2005.04.031 * Corresponding author. Tel.: C61 2 4921 6179; fax: C61 2 4921 6920. E-mail address: [email protected] (B.J.P. Buhre).

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Page 1: Fine ash formation during combustion of pulverised coal–coal property impacts

Fine ash formation during combustion of pulverised

coal–coal property impacts

B.J.P. Buhre a,*, J.T. Hinkley a, R.P. Gupta a, P.F. Nelson b, T.F. Wall a

a Cooperative Research Centre for Coal in Sustainable Development, Department of Chemical Engineering,

University of Newcastle, Callaghan, NSW 2300, Australiab Cooperative Research Centre for Coal in Sustainable Development, Graduate School of the Environment,

Macquarie University, NSW 2109, Australia

Received 5 October 2004; received in revised form 24 February 2005; accepted 14 April 2005

Available online 15 September 2005

Abstract

In many countries, legislation has been enacted to set guidelines for ambient concentrations and to limit the emission of fine particulates with an

aerodynamic diameter less than 10 mm (PM10) and less than 2.5 mm (PM2.5). Ash particles are formed during the combustion of coal in pf boilers

and fine ash particulates may potentially pass collection devices. The ash size fractions of legislative interest formed during coal combustion are

the result of several ash formation mechanisms; however, the contribution of each of the mechanisms to the fine ash remains unclear. This study

provides insight into the mechanisms and coal characteristics responsible for the formation of fine ash. Five well characterized Australian

bituminous coals have been burned in a laminar flow drop tube furnace in two oxygen environments to determine the amount and composition of

the fine ash (PM10, PM2.5 and PM1) formed. Coal characteristics have been identified that correlate with the formation of fine ash during coal

combustion. The results indicate that coal selection based on (1) char characterization and (2) ash fusion temperature could play an important role

in the minimization of the fine ash formed. The implications of these findings for coal selection for use in pf-fired boilers are discussed.

q 2005 Elsevier Ltd. All rights reserved.

Keywords: Coal combustion; Fine ash; Coal characterisation

1. Introduction

The health effects of ambient fine particulates have been

studied extensively and correlations have been observed

between ambient fine particulate matter and human mortality

rates e.g. [1]. Governments worldwide acknowledge these

studies and as a result standards have been introduced to

assist in reducing ambient fine particulate concentrations. In

the United States, a National Ambient Air Quality Standard

(NAAQS) for both ‘coarse’ particulate matter with an

aerodynamic diameter less than 10 mm, PM10, as well as

an NAAQS for PM2.5 is currently in effect [2]. Recently in

Australia, the National Environment Protection (Ambient Air

Quality) Measure (NEPM) has been modified to include

advisory reporting standards for PM2.5, the monitoring of

which commenced in January 2004 [3]. PM10 has been

included in the NEPM Ambient Air Quality measures since,

0016-2361/$ - see front matter q 2005 Elsevier Ltd. All rights reserved.

doi:10.1016/j.fuel.2005.04.031

* Corresponding author. Tel.: C61 2 4921 6179; fax: C61 2 4921 6920.

E-mail address: [email protected] (B.J.P. Buhre).

1998 [4]. Around 80% of the electricity generated in

Australia is generated by coal combustion [5], and coal-

fired power generators are increasingly being required to

monitor and characterise their emissions of fine particulate

matter.

Air pollution control devices (APCDs) are employed at power

stations to capture the ash particulates from the flue gas.

Increasing the capture efficiency of these APCDs to decrease

fine ash emissions can be a costly exercise. Selecting coals which

reduce the formation offine ash particulates in the first place could

be a cost-effective method of minimizing fine ash emissions.

This paper presents the results of a study for the coal

characteristics responsible for the formation of fine ash

particles. Five Australian black coals have been characterised

extensively using advanced analytical techniques such as

QEMSCAN, SIROQUANT, and ICP-AES on ash obtained

from radio-frequency ashing technique. The coals were then

burned in a drop tube furnace, which simulates the combustion

in a pf fired boiler. The ash was characterised and the coal

characteristics responsible for the formation of the ash size

fractions of legislative interest (PM10, PM2.5, and PM1) have

been determined.

Fuel 85 (2006) 185–193

www.fuelfirst.com

Page 2: Fine ash formation during combustion of pulverised coal–coal property impacts

B.J.P. Buhre et al. / Fuel 85 (2006) 185–193186

2. Experimental

Five Australian black coals have been selected to represent

the range of ash chemistry and char swelling behaviour

occurring in Australian bituminous coals; the coals were

chosen on the basis of their sulphur content, other constituents

and their vitrinite content. The coals were milled and a size cut

between 63 and 90 mm was obtained, suitable for feeding into

the drop tube furnace. The coals were subjected to proximate

and ultimate analysis, reflectogram, and QEMSCAN analyses.

QEMSCAN is a novel version of CCSEM technique that

can directly measure the coal–mineral and mineral–mineral

associations. In the technique, pulverised coal samples are

mounted in carnauba wax. The sample block is sectioned and

the surface is polished and coated with a thin layer of carbon to

ensure electrical conductivity. The particles are thus, well

separated and in random orientations with random sections

exposed. Qem*SEM (quantitative evaluation of materials by

scanning electron microscopy) is an earlier version of

QEMSCAN and has been described by Creelman and Ward

[6]. The technique is an automated image analysis system that

uses Backscattered Electron (BSE) and Energy Dispersive

X-ray (EDX) signals from a scanning electron microscope to

create pixilated images in which each pixel represents the EDX

spectrum obtained from the centre of the pixel. The light

element X-ray detectors enable the detection of organic

material, enabling a direct measurement of the coal-mineral

associations. The pixel spacing is an operator setting and

determines the resolution of the QEMSCAN images. For the

analyses used in this study, a pixel spacing of 2 mm was used.

Ash was obtained from the coal samples using a low

temperature radio frequency ashing technique [7], after which

the ash was analysed for chemical composition using ICP-

AES, and quantitative mineralogy using SIROQUANT. The

procedure applied for the ash dissolution has been described in

detail elsewhere [8]. The combination of the analytical

techniques resulted in a thorough understanding of the organic

and inorganic characteristics of the coal samples.

After characterisation, the coals were burned in the Tetlow

Model HTF375A drop tube furnace situated at the Chemical

Engineering department at the University of Newcastle in

Table 1

Considered coal characteristics for each size fraction and the ash formation mecha

Fine Ash Coal characteristic

PM10 Ash Fusion Temperature

Basic to acidic oxide ratio

Average mineral grain size

Total ash content

Char Group I content / vitrinite content

PM2.5 Ash Fusion Temperature

Ash content

Char Group I content / Vitrinite content

Sulphur content

PM1 Ash content

Char Group I content / Vitrinite content

Sulphur content

Average mineral grain size

Australia. The ash was collected using a cyclone, a cascade

impactor and subsequently a filter. The cyclone has a

theoretical d50 of 3 mm at the operating conditions applied

during the experiments. The cascade impactor is a seven stage

MRI cascade impactor, model 1503. After correction for an

assumed particle density, the d50’s of the seven impaction

plates were 17.9, 8.2, 3.2, 1.4, 0.8, 0.4, and 0.3 mm,

respectively. The experimental set-up is described elsewhere

in more detail [9,10].

After combustion, the ash was characterised for its size

distribution, morphology, and chemical composition. The ash

collected in the cyclone was suspended in ethanol and the size

distribution of the ash was determined using a Malvern

Mastersizer S with a 300 mm lens. The amounts of ash

collected on the different plates of the cascade impactor were

combined with the size distribution obtained from the Malvern

Mastersizer to obtain a complete size distribution (Table 1).

The measurement of PM10 from the ash samples was based

on the analysis results of the Mastersizer, while the PM2.5 and

PM1 was determined from the masses collected in the cascade

impactor. The amount of PM2.5 is estimated as the combined

masses of the amounts collected on the filter and on the bottom

five stages. The PM1 is calculated from the mass collected on

the filter combined with the bottom three stages. Moisture

adsorption onto the filter can significantly affect the observed

mass of the material collected onto the filter [9]. The moisture

is an artefact of the experimental procedure and should not be

considered when determining the mass of PM. Previous

publications presented PM1 measurements as the balance

mass, which does not take the effect of moisture absorption into

account [10]. The chemical compositions of the material

collected on the filters have been determined quantitatively

using a combination of Proton Induced X-Ray Emission

(PIXE) and Proton Induced Gamma Ray Emission (PIGE)

analysis. The PIXE and PIGE analysis results have been used

to calculate the mass of the elements present (converted to

oxides). This method ensures that moisture adsorbed from the

combustion gas or the atmosphere does not affect the results.

The repeatability of the experimental set-up to determine

the amount of PM1 using this technique is described elsewhere

[9,10].

nisms they could affect

Ash formation mechanism affected

Included mineral coalescence

Included mineral coalescence

Included mineral coalescence, Vaporization and condensation

Included mineral coalescence, Char fragmentation

Char fragmentation

Included Mineral Coalescence

Char Fragmentation, Included mineral coalescence

Char fragmentation

Vaporisation and condensation

Included mineral coalescence, Char fragmentation

Char fragmentation

Vaporisation and condensation

Included mineral coalescence, Vaporisation and condensation

Page 3: Fine ash formation during combustion of pulverised coal–coal property impacts

Table 2

Proximate analysis, rank and vitrinite content of the five coals used in this study (HV-Bit, high volatile bituminous; MV-Bit, medium volatile bituminous coal)

Sample ID CRC 240 CRC 272 CRC 296 CRC 297 CRC 306

Moisture (% ad) 2.14 2.47 2.09 1.27 1.64

Ash (% db) 12.96 9.18 13.81 11.93 18.77

Volatile matter (% db) 30.41 35.69 30.34 45.41 19.68

Fixed carbon (% db) (by difference) 56.63 55.13 55.85 42.66 61.55

Total sulphur content (% db) 0.60 0.96 0.61 5.07 1.72

Coal rank HV-Bit HV-Bit HV-Bit HV-Bit MV-Bit

Vitrinite content (% v/v mmf) 68.3 50.7 39.0 57.8 28.1

Ash fusion temperature (deformation

temperature, 8C)

O1600 1280 1490 1300 1240

Average mineral size (mm) 11.4 16.7 7.7 10.8 14.0

B.J.P. Buhre et al. / Fuel 85 (2006) 185–193 187

The composition of the oxidizing gas was varied during the

experiments to determine its effect on fine particle formation.

The coals were burned at 1400 8C in 21% O2 (air) and in 50%

O2. The elevated oxygen concentration results in higher char

combustion temperatures. Simulations and literature indicated

that by increasing the oxygen content from 21 to 50%, the

temperature of the burning char particles increase from

approximately 2030–2530 8C [11].

3. Results

The coal compositions are provided in Tables 2 and 3.

Table 2 provides the proximate analysis, coal rank, vitrinite

content as determined from the reflectogram [12], and the

deformation temperature as determined during the ash fusion

test in a reducing environment [13] for all five coals. For

mineral analysis, the coals have been ashed using a low

temperature radio frequency ashing technique [7]. Table 3

provides the ash elemental composition, together with total

sulfur and chlorine content.

Tables 4 and 5 provide the total ash recovered, the PM10,

PM2.5, and PM1 formed during the combustion experiments

Table 3

Elemental composition of the low-temperature ash obtained from the five coals

measured by ICP-AES, results presented in elemental wt%

LTA ash elemen-

tal composition %

CRC 240 CRC 272 CRC 296 CRC 297 CRC 306

Si 20.8 18.3 32.2 10.7 15.6

Al 16.0 11.1 7.9 9.9 6.8

Fe 1.1 5.0 0.3 3.5 9.7

Ca 0.2 4.5 0.3 9.1 9.1

Mg 0.1 0.2 0.1 2.0 1.2

Na 0.1 0.1 0.02 0.2 0.1

K 0.8 0.2 1.3 0.1 0.6

Ti 0.80 1.08 0.63 0.70 0.48

Mn 0.005 0.05 0.004 0.12 0.13

Sa(db) 0.60 0.96 0.61 5.07 1.72

P 0.07 0.3 0.1 0.2 0.2

Ba 0.03 0.06 0.03 0.03 0.04

Sr 0.02 0.05 0.02 0.10 0.04

Clb(db) 0.03 0.07 0.01 !0.01 0.05

The remainder of the ash includes oxygen, water of constitution, and carbon

present as carbonates.a Sulfur as determined by [33].b Chlorine as determined by [34].

together with the total ash collected during the experiments.

The amounts are reported as percentage of the ash generated

during combustion. The proportion of the ash larger than

10 mm was typically much larger in size than 10 mm and

displayed a mean size in the order of tens of micrometers.

4. Ash formation mechanisms

During coal combustion, ash particles are formed from the

inorganic matter present in coal. The mechanisms of ash

formation have been studied extensively in the literature, and

are affected by the combustion conditions and the coal

characteristics [14–17]. Two important coal characteristics

influencing the ash formation process are

† The mode of occurrence of the inorganic matter and

† The combustion behaviour of coal particles containing both

organic and inorganic matter.

The majority of inorganic matter present in black coals

occurs in the form of minerals of various types and sizes. These

minerals can be closely associated with the organic matter

(included minerals), or they occur excluded from the organic

matter (excluded minerals). The majority of ash particles are

formed from four formation mechanisms, shown in Fig. 1:

† Included mineral coalescence,

† Char fragmentation,

† Excluded mineral fragmentation, and

† Vaporization and subsequent condensation of inorganic

matter.

Table 4

Total ash collected, PM10, PM2.5, and PM1 generated during combustion in

21% O2 at 1400 8C

PM10, PM2.5, and PM1 as % of ash generated during combustion in 21% O2

21% O2 CRC 240 CRC 272 CRC 296 CRC 297 CRC 306

PM10 0.9 6.1 10.7 3.2 3.8

PM2.5 0.15 0.53 0.49 0.78 0.40

PM1 (dry) 0.08 0.30 0.20 0.58 0.11

Total ash

collected

81.9 82.8 91.6 72.4 73.3

PM10 determined from Malvern Mastersizer, PM2.5 and PM1 determined from

weight collected in cascade impactor. Results presented as % of ash generated.

Page 4: Fine ash formation during combustion of pulverised coal–coal property impacts

Table 5

Total ash collected, PM10, PM2.5, and PM1 generated during combustion in

50% oxygen at 1400 8C

PM10, PM2.5, and PM1 as % of ash generated during combustion in 50% O2

50% O2 CRC 240 CRC 272 CRC 296 CRC 297 CRC 306

PM10 19.8 11.7 17.4 13.3 13.3

PM2.5 0.72 1.41 1.06 1.60 0.44

PM1 (dry) 0.34 0.44 0.39 0.85 0.19

Total ash

collected

66.7 86.1 90.0 77.5 84.0

PM10 determined from Malvern Mastersizer, PM2.5 and PM1 determined from

weight collected in cascade impactor. Results presented as % of ash generated.

Fig. 1. Schematic of ash formation mechanisms during pulverised coal

combustion.

B.J.P. Buhre et al. / Fuel 85 (2006) 185–193188

Typically, ash particles are characteristic in size for the

mechanism via which they are formed. The first mechanism is

believed to be responsible for the bulk of the supermicron ash

particles formed [16]. The formation of ash particles from the

fragmentation of thin-walled cenospherical char particles (i.e.

the second mechanism) contributes to ash particles of only a

few micrometer in size [18–20]. Excluded mineral fragmenta-

tion contributes mainly to supermicron-sized ash particles, and

the last formation mechanism contributes mainly to submicron

sized ash particles [14].

Coal characteristics play an important role in the extent to

which the three ash formation mechanisms contribute to the

total ash formed. A summary of the main characteristics

affecting the formation mechanisms is provided below.

4.1. Included mineral coalescence

When char particles do not fragment, the ash formed from

included mineral coalescence is affected by the type, size and

distribution of included minerals. The high temperatures

occurring inside burning char particles cause included minerals

to turn viscous and coalesce. The ash fusion temperature is a

standard test done on coal ashes to characterise the various

stages of melting [13]. Although the ash fusion test does not

differentiate between included and excluded minerals, the test

indicates the melting behaviour of the inorganic matter upon

heating. The results in this paper suggest that this melting

behaviour could indicate the affinity of minerals to coalesce

during combustion. The ratio of basic oxides to acidic oxides is

often used in the literature as an indicator of ash slag viscosity

at high temperatures (e.g. [21]). If the ash fusion temperature

could be used as an indicator, this ratio is likely have a similar

relationship with the extent of mineral coalescence during coal

combustion.

4.2. Char fragmentation

The extent of char fragmentation depends on the char

swelling behaviour during combustion [20]. If the char

fragments are large and contain large minerals, the minerals

inside these fragments will coalesce and form large ash

particles. However, if the char swells extensively, the char will

fragment into small pieces and minerals inside these small

fragments will result in small ash particles. The two

mechanisms shown in Fig. 1 are extreme cases and ash formed

from coal combustion is a combination of the two.

Monroe suggested a mathematical model to predict the

coalescence behaviour of minerals as a function of cenosphere

shell thickness, coal particle size, mineral grain size, and

mineral volume fraction [22]. Yan validated this model by

determining the char swelling behaviour of several Australian

coals and its effect on the ash formation [17]. He modelled the

char fragmentation based on a char classification scheme, in

which the char is classified in three classes based on their

swelling behaviour. Char Group I particles are defined as char

particles that are highly porous and have low densities.

The combustion of these thin-walled cenospherical char

particles can result in more extensive fragmentation during

combustion, resulting in fine ash formation. Benfell showed

that the amount of Char Group I particles of Australian coals

could be estimated from the coal vitrinite content and the

pressure at which the char was formed [23,24]:

Char Group I ðnumber%Þ

Z 0:994!Pressure ðatmÞC0:621 ðVitrinite; v=v% mmfÞ

C29:87

This correlation is an updated version of a correlation

published earlier by the same research group [25,26]. The

updated version is based on a more extensive coal database but

produces similar results as the earlier correlation [24].

4.3. Excluded mineral fragmentation

The amount, size, and type of excluded minerals determine

the extent of excluded mineral fragmentation. The main

fragmenting mineral types in Australian black coals are calcite

and pyrite [27]. Although extensive fragmentation of these

Page 5: Fine ash formation during combustion of pulverised coal–coal property impacts

20.0

25.0

cted

)

LT

B.J.P. Buhre et al. / Fuel 85 (2006) 185–193 189

minerals has been noted, the bulk of the newly formed ash

particles are generally supermicron in size [27,28].

0.0

5.0

10.0

15.0

1000 1200 1400 1600 1800

Ash deformation temperature,°C

PM

10 (%

of a

sh c

olle HT

Fig. 2. PM10 correlation with ash fusion temperature for the five coals (LT, low

temperature; HT, high temperature experiments).

4.4. Vaporization and condensation

The extent of vaporization of inorganic matter during coal

combustion depends on (a) the temperature inside the burning

char particle, and (b) the occurrence of readily vaporised

material such as alkalis, sulphur, and phosphorus [14,29]. The

vaporization of refractory oxides from included minerals has

also been suggested to depend on the size distribution of

included minerals containing refractory oxides [14,30,31].

Summarizing, the size fractions of legislative interest are the

result of several ash formation mechanisms. Several coal

characteristics affect the extent to which the formation

mechanisms result in fine ash. This study aims at determining

the dominating coal characteristics that correlates with the

amounts of fine ash formed. Table 1 shows the coal

characteristics considered for three size fractions (PM10,

PM2.5 and PM1), together with the ash formation mechanism

they could affect.

Fig. 3. Typical SEM image of ash from CRC 240 generated in 21% oxygen.

5. Discussion

5.1. PM10

The amounts of PM10 have been compared with the coal

characteristics indicated in Table 1. The PM10 showed no

correlation with average mineral size, ash content, or Char

Group I content. The ratio of basic to acidic oxides showed

moderate correlation with the amounts of PM10, and a good

correlation was observed between PM10 and the ash fusion

temperature. In literature, the ratio of basic to acidic oxides is

frequently used to predict the slagging behaviour of ash [21].

The observed correlation between PM10 and ash fusion

temperature (and to a lesser extent the correlation with the

ratio of basic to acidic oxides) suggests that the heating

characteristics of the ash are indicative of the fine ash formed

from the coalescence of included minerals.

PM10 is formed from (a) the coalescence of very small

included minerals, which combined result in particles smaller

than 10 mm or (b) the shedding of small minerals (!10 mm)

from the burning char surface. If small included minerals are

not released from the surface by shedding, these minerals

adhere to the char surface and coalesce with other minerals

inside the burning char particle to form large ash particles. The

ash fusion temperature is a bulk ash characteristic and does not

directly relate to small included minerals inside the coal.

However, if we assume that the melting behaviour of the

minerals is independent of size, the ash fusion temperature

could indicate the likelihood of coalescence of the minerals

during combustion; a high ash fusion temperature indicates that

minerals originally present in the coal are less likely to

coalesce during combustion. If included minerals are less likely

to coalesce, they can form individual ash particles, smaller than

mineral agglomerates, resulting in elevated PM10 levels. Fig. 2

shows how the amounts of PM10 measured during the

experiments correlate with the ash deformation temperatures.

The PM10 of the different coals in 50% O2 correlate well

with the ash deformation temperatures of the five coals, as

indicated for the high temperature (HT) experiments in the

figure. The amounts of PM10 formed during the low

temperature experiments show one significant outlier: CRC

240. This outlier can be explained by the morphology of the ash

particles formed from this particular coal. The Malvern

Mastersizer calculates the size distribution of a sample in

suspension based on the diffraction of a laser light through the

sample. In its analysis, it assumes that all particles are dense

spheres. CRC 240 displays the highest ash deformation

temperature, which results in non-spherical ash particles,

indicated in Figs. 3 and 4.

The amount of PM10 formed in 50% O2 (high temperature

experiments) is significantly higher than the amount formed in

21% O2 (low temperature experiments). The gas temperature

during both temperatures was held constant, and the volatile

matter release (and thus, possible coal fragmentation during its

release) should not be affected significantly by the change in

oxygen concentration. However, at low temperatures, the burning

char surface recedes at a pace at which included minerals have

enough time to coalesce, while at high temperatures, it appears

that there may be more shedding from the fast receding surface.

This increased shedding could result in increased fine ash particle

formation. Literature has shown that coal combustion at higher

Page 6: Fine ash formation during combustion of pulverised coal–coal property impacts

Fig. 4. Typical SEM image of ash from CRC 240 generated in 50% oxygen.

0.0

0.5

1.0

1.5

2.0

0 20 40 60 80 100

Group I char (number %)

PM

2.5

(% o

f ash

gene

rate

d)

LTHT

Fig. 5. Amount of PM2.5 as a function of Char Group I content of the five coals

(LT, low temperature; HT, high temperature experiments).

B.J.P. Buhre et al. / Fuel 85 (2006) 185–193190

temperatures results in finer ash and elevated PM10 levels [32]. In

that study, the higher combustion temperatures were achieved by

elevating the gas temperatures from 1100 to 1300 8C, which

could have affected the extent of coal fragmentation during

volatile matter release. In this study, the elevated levels of PM10

are thought to be resulting from the decrease in time for

coalescence of included minerals during the char combustion.

5.2. PM2.5

PM2.5 is formed from two mechanisms: vaporisation and

condensation (the homogeneously nucleated submicron ash

particles) and the release of included minerals due to char

fragmentation. Depending on the char combustion temperature

(oxygen concentration), the submicron material accounts for

the majority of PM2.5. Several studies have suggested that the

release of small included minerals by fragmentation of

cenospherical char particles contributes to ash particles in the

size range between one and a few micrometers [18–20]. The

formation of cenospherical char particles (Char Group I

particles) has been correlated with the pressure of char

formation and the coal vitrinite content by Benfell [24].

The PM2.5 has been correlated to the coal characteristics

indicated in Table 1. No correlation was observed between the

amounts of PM2.5 and the ash fusion temperatures, the ash and

sulphur contents. A poor correlation was observed between the

PM2.5 and the Char Group I content estimated from the vitrinite

content, shown in Fig. 5.

A correlation between PM2.5 and Char Group I content

could be expected, however, the experimental results shown in

Fig. 5 provide no conclusive evidence. There are two possible

explanations for the lack of a good correlation between the two:

† During the low temperature experiments, the contribution

of PM1 to PM2.5 is significantly higher (up to 74%) than that

during the high temperature experiments. As a result, the

PM2.5 formation is dominated by the submicron ash, and

little correlation with Char Group I content is expected.

† A correlation between PM2.5 and Char Group I content is

only expected when the included minerals of all coals have

the same size distribution and are uniformly distributed

through the maceral types.

Experiments using more coals and more detailed coal

analyses could provide more insight in the coal characteristics

that correlate with PM2.5. It must be noted that the Char Group I

content is estimated from the vitrinite content, and that a

similar correlation between PM2.5 and vitrinite content and

with the mean vitrinite reflectance can be observed.

The elevated PM2.5 emissions during the experiments in

50% O2 can be attributed to:

† Increased vaporisation of elements, which increase PM1

formation and

† At high temperatures, there may be more shedding from the

fast receding surface, similar to the mechanism resulting in

elevated PM10 levels at higher temperatures.

5.3. PM1

The chemical composition of PM1 is significantly different

from the bulk chemical composition, and depends on the

combustion temperature and the mode of occurrence of

the inorganic material in the coal. The main components in

the submicron ash are sulphur, silicon, sodium, and phos-

phorus, with sulphur being the most abundant element detected

on the filters [10]. Particles collected onto the filter were

typically around 20–30 nm, much smaller than the cut-off of

the last impactor stage. Although the amount of particles

collected on the last stages were much smaller, they accounted

for a significant proportion of the mass. This makes

identification of the dominating coal characteristic correlating

with the amount of PM1 a difficult task.

The amount of PM1 has been compared with the average

mineral size, the ash and sulphur content and the Char Group I

content. No correlation was observed between PM1 and the ash

content or the average mineral grain size. Fig. 6 shows how

PM1 and the total sulphur content in the coal correlate. Fig. 7

shows the correlation between PM1 and Char Group I content.

Of the two coal characteristics correlated with the amount of

PM1, the total sulphur content is the best indicator of the

amount of PM1 formed. Sulphur is the most abundant element

detected on the filters and a similar correlation is observed

between the amount of ash collected on the filter and the coal

Page 7: Fine ash formation during combustion of pulverised coal–coal property impacts

0.0

0.2

0.4

0.6

0.8

1.0

0 20 40 60 80

Char Group I content (number %)

PM

1 (%

of a

sh c

olle

cted

)

LT

HT

Fig. 7. Amount of PM1 as a function of char group I content of the five coals

(LT, low temperature, HT, high temperature experiments).

0.0

0.2

0.4

0.6

0.8

1.0

4 620

Coal sulphur content (% db)

PM

1 (%

of a

sh c

olle

cted

)

LT

HT

Fig. 6. Amount of PM1 as a function of coal sulphur content of the five coals

(LT, low temperature, HT, high temperature experiments).

B.J.P. Buhre et al. / Fuel 85 (2006) 185–193 191

sulphur content. However, no correlation could be observed

between the Char Group I content and the amount of ash

collected on the filter. The ash collected on the filter is very fine

(around 20–30 nm) compared to the ash collected on the latter

stages of the impactor (a few hundred nanometers). The ash

collected on the last stages could be the result of char

fragmentation, while the material collected on the filter is the

result of vaporisation and condensation of inorganic material.

As a first pass, the coal sulphur content could be used as an

indicator of the amount of PM1 formed during coal

combustion; however, more experiments using higher sulphur

coals could confirm this conclusion.

The amounts of PM1 formed during the high temperature

experiments are consistently higher than the amounts formed

during the low temperature experiments. This observation is

well documented in the literature and can be attributed to

Table 6

Guidelines for black coal assessment for their potential to form fine ash

Fine ash Analysis technique Measured coal characteristic

PM10 Ash fusibility test in oxidizing

environment, [13]

Ash deformation temperature

PM2.5 Maceral analysis (e.g. reflecto-

gram [12])

Char Group I content (proporti

of coal that shows swelling beh

viour during char formation),

determined from vitrinite conte

PM1 Ultimate analysis, total sulphur

content [35]

Total amount of sulphur in the c

the enhanced vaporization of refractory oxides inside burning

char particles [14].

5.4. Coal selection guideline

This study has characterised coals using various methods

and analysis techniques and compared the results of these

techniques with the amount and characteristics of the fine ash

formed. Table 6 summarizes the analysis techniques and coal

characteristics that have been found best to assess coals for

their potential to form fine ash in this study.

The guidelines can be used to assess different coals for their

potential to form fine ash during combustion. The guideline for

PM1 is questionable, as the correlation is skewed by the PM1

formed from one coal with high sulphur content. PM1 is formed

from a wide variety of elements and the elemental mode of

occurrence in the coal, which is responsible for the occurrence

of these elements in the submicron ash is not always known.

For example, two coals show significant amount of sodium in

the submicron ash, which is not reflected in the previous

guideline [10].

6. Conclusion

The ash size fractions of legislative interest (PM10 and

PM2.5, and PM1) formed during coal combustion are the result

of several ash formation mechanisms. They are formed by a

combination of (1) included mineral coalescence (2) excluded

mineral fragmentation, (3) char fragmentation, and (4)

vaporization and subsequent condensation of inorganic matter.

Ash particles are characteristics in size for the mechanism via

which they are formed. Coal characteristics and combustion

conditions determine the extent to which the ash formation

processes contribute to the total ash formed.

Five well-characterized black coals have been selected to

represent the range of ash chemistry and char swelling

behaviour of Australian bituminous coals. Ash was generated

by combustion of the coals in a drop tube furnace, simulating

combustion in a pf boiler. The amount of fine ash was

determined and the coal characteristics responsible for its

formation have been established.

Trends observed Comments

The higher the ash fusion tem-

perature, the more PM10 (% of ash)

is formed during combustion

Combustion in 21 and 50% O2

showed similar trends, with one

outlier (Fig. 2)

on

a-

nt.

The higher the Char Group I

content, the more the char swells,

the more the PM2.5 is expected to

be formed

This correlation is expected, how-

ever, the experiments are incon-

clusive. (Fig. 5)

oal The more sulphur is detected, the

higher the amount of submicron

ash formed

Sulphur has been shown to be a

major contributor to PM1 and the

observed correlation is mainly the

result of the high sulphur presence

in CRC 297 (Fig. 6)

Page 8: Fine ash formation during combustion of pulverised coal–coal property impacts

B.J.P. Buhre et al. / Fuel 85 (2006) 185–193192

The amount of PM10 formed during the experiments

correlates with the ash fusion temperature. A high ash fusion

temperature could indicate that the minerals originally present

in the coal are less likely to coalesce. If included minerals are

less likely to coalesce, they can transform into individual ash

particles, smaller than mineral agglomerates, resulting in

elevated PM10 levels.

The amounts of PM2.5 formed would be expected to

correlate with the amount of char particles displaying swelling

behaviour, expressed as Char Group I particles. Thin-walled

cenospherical char particles can fragment during combustion,

resulting in the release of fine included minerals originally

present in these char particles, which transform to ash particles

of a few micrometers in size. This expectation could not be

confirmed conclusively from the experiments. More exper-

iments using different coals and maceral types could confirm

this expectation.

The amounts of PM1 correlate slightly with the coal sulphur

content. More experiments using higher sulphur coals could

confirm this observation. The amount of PM10, PM2.5 and PM1

increased consistently when increasing the oxygen concen-

tration in the combustion gas from 21 to 50%. The enhanced

temperatures increase the char fragmentation and vaporization

of inorganic matter. Finally, it is shown that these results can be

used a guidance for coal selection for minimization of fine

particle formation.

Acknowledgements

The authors wish to acknowledge the financial support

provided by the Cooperative Research Centre for Coal in

Sustainable Development, which is funded in part by the

Cooperative Research Centres Program of the Commonwealth

Government of Australia.

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