preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium...

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Michael K. OPOKU and Bogdan Z. DLUGOGORSKI * Priority Research Centre for Energy Faculty of Engineering and Built Environment The University of Newcastle Callaghan, NSW 2308, Australia *Corresponding author. Email: [email protected] Preparation and characterisation of potassium ammonium nitrates (K x (NH 4 ) 1-x NO 3 ) The use of ammonium nitrate as an ingredient in explosives has increased significantly around the world due to demand for minerals and raw materials. Ammonium nitrate is a feedstock for making emulsion explosives as well as ammonium nitrate and fuel oil explosives, both commonly applied in open-cut mining operations. Decomposition of ammonium nitrate may release red clouds of nitrogen oxides, especially under wet-rock blasting conditions. Doping NH 4 NO 3 with potassium may decrease the amount of emitted NO x . In this contribution, we report the preparation and characterisation of co-recrystallised ammonium and potassium nitrates, for future investigations on emissions of NO x from decomposition of these materials. The results indicate the existence of solid solutions of potassium and ammonium nitrates below 1 mol % K and between 5 and 25 mol % K. 1. INTRODUCTION Ammonium nitrate (AN) constitutes a major component in industrial explosives, used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse conditions of rock type and presence of ground water, blasting of ANFO, or blends of ANFO and emulsion explosives may release substantial amounts of nitrogen oxides, especially under lean fuel oil conditions (Sapko et al. 2002). In recent years in Australia, the emissions of NO x during blasting in mining operations have come under intense scrutiny of regulatory bodies and concerned citizens, as such emissions pose environmental and health risks; in particular, when orange clouds, characteristic of high levels of NO 2 and NO, do not dissipate rapidly and drift into populated areas surrounding the mines. Thus, there is a great interest in industry for gaining improved understanding of the formation of NO x during blasting, and finding practical solutions to remedy the problem (Rowland et al. 2001; Sapko et al. 2002). Decomposition chemistry of ammonium nitrate has been studied extensively and several modes of decomposition reaction mechanisms have been proposed, as function of pressure, temperature, confinement, heating rate, samples sizes, and presence of

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Page 1: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

Michael K. OPOKU and Bogdan Z. DLUGOGORSKI*

Priority Research Centre for Energy

Faculty of Engineering and Built Environment

The University of Newcastle

Callaghan, NSW 2308, Australia

*Corresponding author. Email: [email protected]

Preparation and characterisation of potassium ammonium

nitrates (Kx(NH4)1-xNO3)

The use of ammonium nitrate as an ingredient in explosives has increased significantly

around the world due to demand for minerals and raw materials. Ammonium nitrate is a

feedstock for making emulsion explosives as well as ammonium nitrate and fuel oil explosives,

both commonly applied in open-cut mining operations. Decomposition of ammonium nitrate

may release red clouds of nitrogen oxides, especially under wet-rock blasting conditions.

Doping NH4NO3 with potassium may decrease the amount of emitted NOx. In this

contribution, we report the preparation and characterisation of co-recrystallised ammonium and

potassium nitrates, for future investigations on emissions of NOx from decomposition of these

materials. The results indicate the existence of solid solutions of potassium and ammonium

nitrates below 1 mol % K and between 5 and 25 mol % K.

1. INTRODUCTION

Ammonium nitrate (AN) constitutes a major component in industrial explosives,

used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well

as emulsion explosives. Under adverse conditions of rock type and presence of

ground water, blasting of ANFO, or blends of ANFO and emulsion explosives may

release substantial amounts of nitrogen oxides, especially under lean fuel oil

conditions (Sapko et al. 2002). In recent years in Australia, the emissions of NOx

during blasting in mining operations have come under intense scrutiny of regulatory

bodies and concerned citizens, as such emissions pose environmental and health risks;

in particular, when orange clouds, characteristic of high levels of NO2 and NO, do not

dissipate rapidly and drift into populated areas surrounding the mines. Thus, there is a

great interest in industry for gaining improved understanding of the formation of NOx

during blasting, and finding practical solutions to remedy the problem (Rowland et al.

2001; Sapko et al. 2002).

Decomposition chemistry of ammonium nitrate has been studied extensively and

several modes of decomposition reaction mechanisms have been proposed, as function

of pressure, temperature, confinement, heating rate, samples sizes, and presence of

Page 2: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

alkali and alkali earth nitrates (Gunawana and Zhang 2009; Jones et al. 1999;

Langfelderova 1982; Oxley et al. 1992; Turcotte et al. 2003). The initial step in

decomposition of AN in the condensed phase involves an endothermic proton transfer

from the ammonium ion (NH4+) to the nitrate ion (NO3

-) to form nitric acid (HNO3)

and ammonia (NH3), followed by decomposition of nitric acid itself (Eq. 1) (Brill et al.

1993; Brower et al. 1989; Chien et al. 2010; Oxley et al. 1989; Sinditskii et al. 2005;

Vyazovkin et al. 2001; Wu et al. 2007). Although, several reaction pathways for the

proton transfer have been proposed by different research groups, consensus exists that

the overall decomposition process of AN yields mostly H2O and N2O (Eq. 2), (Brill et

al. 1993; Brower et al. 1989; Chien et al. 2010; Oxley et al. 1989; Sinditskii et al.

2005; Vyazovkin et al. 2001; Wu et al. 2007).

NH4NO3 → NH3(g) + HNO3(g) (1)

NH4NO3 → N2O + 2H2O (2)

It is also well appreciated that fast decomposition of ammonium nitrate between 200

to 230 oC results in release of NO gas (Eq. 3) (Oommen and Jain 1999).

2 NH4NO3 → N2 + 2 NO + 4 H2O (3)

Oommen and Jain (1999) reported that AN deflagration engenders a different reaction

mechanism that yields both NO and NO2 (Eq. 4), while AN detonation follows yet

another reaction pathway (Eq. 5) that produces N2 and NO2. The presence of NO and

NO2 in decomposition gases of AN was also observed by other researchers (Brill et al.

1993).

8 NH4NO3 → 5 N2 + 4 NO + 2 NO2 + 16 H2O (4)

4 NH4NO3 → 3 N2 + 2 NO2 + 8 H2O (5)

In mining, the formation of nitrogen oxides (mainly N2O, NO, and NO2) during

thermal decomposition, deflagration or detonation of ammonium nitrate poses risks to

both people and the environment. It has been reported that addition of alkali and

alkali earth salts to AN can lower the emissions of nitrogen oxides during AN

decomposition (Kaljuvee et al. 2009; Klimova et al. 2011; Oxley et al. 2002; Rudjak

et al. 2010; Sapko et al. 2002).

Oxley et al. (Oxley et al. 2002) observed that thermal stability of AN doped with

alkali and alkali earth nitrates is related to the N2O/N2 ratio in gaseous products.

These authors ground different weight percentages of calcium, potassium, and sodium

nitrate salts together with AN, and studied the thermal decomposition of the mixtures.

The results indicated that the more stabilising the additives, the lower the N2O/N2

ratio. Unfortunately, Oxley et al. reported no measurements of concentrations of NO

and NO2. Two further observations of Oxley et al. are important. Firstly, when

calcium, potassium, and sodium nitrates were added to AN, there was almost no

Page 3: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

change in the decomposition temperatures of the mixtures compared with the

decomposition of pure AN. Secondly, a mixture containing 10 mol % potassium

nitrate exhibited a lower N2O/N2 ratio compared with that of pure AN. Likewise,

other researchers have demonstrated increased stability of AN doped with K as a

consequence of the transformation of AN from crystalline phase IV to crystalline

phase III (Li et al. 2009; Oommen and Jain 1999; Vargeese et al. 2010; Wu et al.

2008). However, the mode of decomposition of mixed nitrate crystals of AN doped

with K remains unknown, prompting the present study.

In this contribution, we investigate the effect of the presence of potassium nitrate

on the crystal structure of mixed salts for potential application in industrial explosives,

to minimise the formation of nitrogen oxides. In the first phase of the study, reported

in this contribution, we attempt to crystallise solid solutions of potassium and

ammonium nitrates, and characterise them by powder XRD (X-ray diffraction), SEM-

EDS (scanning electron microscopy – energy dispersive spectroscopy) and ICP-OES

(inductively coupled plasma – optical emission spectroscopy). We also report the

formation of two crystalline phases at low (2-4 mol %) and high (>20 mol %)

concentrations of potassium in the crystallisation solution; mol % is based only on K+

and NH4+ and does not include the solution water. The thermal and explosive

decomposition of the mixed salts will be reported in a subsequent publication.

2. EXPERIMENTAL

2.1. Materials

Pure ammonium nitrate and potassium nitrate salts were used as precursors in the

preparation of mixed salts. AN (crystalline 99.9 wt % pure (dry basis)) was supplied

by Dyno Nobel Asia Pacific Pty Ltd. Potassium nitrate salt (UNIVAR reagent 99.5

%) was purchased from Ajax Chemicals.

2.2. Crystallisation

A total of 4.0 g of AN and KNO3 salts were dissolved in 1 mL of de-ionised water

to form a supersaturated solution. The concentration of KNO3 in the mixture was

varied from 1 to 25 mol %. The supersaturated solution was placed in hot water bath

at 80 oC while the solution was agitated every 15 min intermittently for complete

dissolution. After heating the solutions for 1 h at 80 oC, the solutions were quenched

in ice-cold water bath at 1 oC to effect nucleation, growth, and precipitation of mixed

nitrate salts. Precipitated salts were filtered immediately. All precipitated samples

were stored in a desiccator for at least 48 h before characterisation.

Page 4: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

2.3. Structural analysis

Structural characterisation of NH4NO3, KNO3, and NH4NO3/KNO3 mixtures were

analysed by Philips X’pert-MPD X-ray Diffraction system using Cu Kα1. XRD

characterisations of samples were conducted under conditions of room temperature

and atmospheric pressure. Samples were scanned from 10 o to 70

o for a total duration

of 20 min with a step size of 0.008 o at 40 kV and 40 mA operating power.

2.4. Morphological analysis

Recrystallised nitrate salts were imaged using Philips XL30 SEM coupled with

Oxford ISIS EDS for elemental analyses. Nitrate salts were carbon coated using SPI

Carbon Coating Unit prior to imaging. SEM images and EDS spectra of the nitrate

salts were obtained by scanning samples at 15 kV.

2.5. ICP analysis

The concentration of metal cations in potassium nitrate and mixed nitrate salts

were quantified using Varian 715-ES ICP Optical Emission Spectrometer. Amounts

of 250 mg of nitrate salts were dissolved in 500 ml of de-ionised water. Sample

solutions were transferred via Varian SPS 3 sample preparation system for analyses in

ICP-OES. High-Purity Standards ICP multi element standard solution containing

eight metal cations in 2.0 % HNO3 was used for calibration.

3. RESULTS AND DISCUSSION

X-ray powder diffraction (XRD) pattern of recrystallised AN is shown in Fig. 1.

At 2θ of 28.9 o, the 100 % peak, which corresponds to (111) surface and d-spacing

3.085 Å, matched very well with crystalline AN phase IV salt as can be seen in Fig. 1.

It was also observed that all other peaks characteristic of AN phase IV also matched

with those displayed by this sample. AN phase IV has orthorhombic structure that is

stable between -18 and 55 oC when dry or between -18 and 32

oC in the presence of

moisture (Dellien 1981; Oommen and Jain 1999).

Addition of 1 mol % KNO3 to AN during co-recrystallisation shows no visible

modification of the XRD pattern compared with pure AN phase IV. This amount of

KNO3 is probably at the detection limit of the XRD analysis. However, it stands to

reason to suggest that the crystal lattice of AN could accommodate 1 mol % content of

K+ ions as the ionic radius of K

+ (0.133 nm) is only slightly smaller than that NH4

+

(0.143 nm). Hence, NH4+ could undergo substitution by minor amount of K

+ in the

crystal structure without much distortion. Usually small inclusions in pure phase

cause peak broadening in XRD pattern of the main component due to stress in the

crystal structure which is observed as a small shift in the d-spacing. This is because a

number of parallel planes of small inclusions may prevent diffraction to occur at

Page 5: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

Position [°2Theta] (Copper (Cu))

20 30 40 50 60

Counts

0

10000

20000

30000

40000 ANF

Figure 1. XRD patterns of recrystallised AN salt.

Position [°2Theta] (Copper (Cu))

20 30 40 50 60

Counts

0

20000

40000

KA1F

Figure 2. XRD patterns of recrystallised AN containing 1 mol % KNO3.

precise angles. However, there was no visible shift of the XRD peaks of this sample

compared with pure AN phase IV. Further analysis of a co-recrystallised sample

containing 1 mol % KNO3 and 99 mol % AN by EDS indicated the presence of K in

Position [°2Theta] (Copper (Cu))

20 30 40 50 60

Counts

0

20000

40000

KA1F

Figure 27: XRD patterns of 1 mol% KNO3-AN.

Position [°2Theta] (Copper (Cu))

20 30 40 50 60

Counts

0

20000

40000

KA1F

Page 6: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

the sample. In addition, ICP-OES measurements of this sample confirmed the

presence of K. This led us to a conclusion that co-recrystallisation of 1 mol % KNO3

and 99 mol % AN probably resulted in a complete solid solution of potassium

ammonium nitrate without much distortion of the AN phase IV crystal structure.

Figure 3 shows an XRD spectrum of a co-recrystallised sample containing 2 mol

% KNO3 in balance of AN. The spectrum illustrates two crystalline phases of AN;

that is, AN phase IV with a small trace of AN phase III. AN phase III has an

orthorhombic structure which is stable between 32–84 oC but is less dense, by about

3.84 %, than AN phase IV (Oommen and Jain 1999). Co-recrystallisation of 2 mol %

KNO3 and 98 mol % AN commences to change the crystal structure of AN from phase

IV to III in order to accommodate the increased modal concentration of K+

ions. This

is evident in the XRD pattern at 2θ of 22.7 o (60 % peak), and 27.7

o (100 % peak)

which correspond to (111) and (021) planes of AN phase III as shown magnified in

the inset to Fig. 3.

Position [°2Theta] (Copper (Cu))

20 30 40 50 60

Counts

0

10000

20000

30000

40000

KA2F

Figure 3. XRD patterns of co-recrystallised AN containing 2 mol % KNO3 showing phase III

(red) and phase IV (blue).

In Fig. 4, the XRD spectrum of recrystallised samples confirms that increasing

KNO3 concentration to 3 mol % in balance of AN elevates the content of phase III in

the multi-phase AN. When modal composition of KNO3 increases to 5 mol %, the

XRD peak at 2θ of 27.7 o matches well the (210) surface that corresponds to 100 %

peak of K0.05(NH4)0.95NO3. K0.05(NH4)0.95NO3 displays orthorhombic structure similar

to phase III of AN. Further increment in KNO3 concentration from 5 to 20 mol %,

Position [°2Theta] (Copper (Cu))

20 30 40 50 60

Counts

0

10000

20000

30000

40000

KA2F

Page 7: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

during preparation, reveals single phase Kx(NH4)1-xNO3 with no separate phase of

potassium nitrate, according to the XRD results as presented in Fig. 5 and Table 1.

From the overlaid spectra of Fig. 5, the largest peak at 2θ of 34.2 o corresponds to d-

spacing of 2.617 Å in samples containing 10, 15 and 20 mol % K. However, crystals

obtained from the solution of 25 mol % KNO3 and 75 mol % AN reveal the presence

of pure KNO3 phase, as indicated by the peak at 2θ of 26.9 o in the XRD

measurement. This demonstrates that 25 mol % substitution of NH4+ by K

+ exceeds

the solid solubility limit of AN crystal structure, causing the precipitation of pure

KNO3, when co-recrystallised with AN.

Position [°2Theta] (Copper (Cu))

20 30 40 50 60

Counts

0

5000

10000

15000

KA3F

Figure 4. XRD patterns of co-recrystallised AN containing 3 mol % KNO3 showing phase III

(red) and phase IV (blue).

Recrystallisation of pure AN from hot saturated solution by direct quenching in

ice-cold water bath at 1 oC resulted in plate and needle-like shapes, consistently with

the results of other researchers (Vargeese et al. 2009). SEM images could not be

taken at magnification higher than 10,000×. The samples seemed to evaporate at

higher magnification even if the voltage was set as low as 5 kV. The SEM images of

recrystallised pure AN displayed sheet-like surfaces with a few embedded needle-like

crystals, as shown in Fig. 6. However, the morphology of samples of AN containing

KNO3 exhibited fused crystals with numerous cracks along the crystals boundaries, as

illustrated in Figs. 6-8. It appears that increasing concentration of K in solid solutions

induces the formation of more distinct crystals with micro tree-like cracks in addition

to crystal boundaries. This demonstrates the effect of rising stress on the crystal

structure at increasing concentration of K, leading to separation of the material into

two phases, once modal content of K reaches 25 mol %.

Position [°2Theta] (Copper (Cu))

20 30 40 50 60

Counts

0

5000

10000

15000

KA3F

Page 8: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

EDS analyses of single crystals of nitrate salts were not possible, but bulk

qualitative EDS of recrystallised nitrate salts indicated the presence of potassium in all

the potassium ammonium nitrate salts. Figures 9-11 illustrate the characteristic peaks

Kα1 and Kβ1 of potassium, which appear at 3.314 and 3.590 keV respectively. As

expected, the intensities of the characteristics potassium peaks of Kα1 and Kβ1 increase

with increasing concentration of KNO3 in the co-recrystallised salts.

Table 1. Summary of powder XRD results of co-recrystallisation of KNO3 and AN salts.

mol % KNO3* mol % KNO3** Phase(s) Present XRD Comments

0.00 1.06 ± 0.01 AN phase IV Single phase

1.00 1.91 ± 0.03 AN phase IV Single phase

2.00 2.57 ± 0.01 AN phase III and IV Multi-phase of AN

3.00 3.43 ± 0.03 AN phase III and IV Multi-phase of AN

4.00 4.24 ± 0.05 AN phase III and IV Multi-phase of AN

5.00 11.77 ± 0.09 K0.05(NH4)0.95NO3 Single phase

10.00 17.06 ± 0.18 Kx (NH4)1-xNO3 Single phase

15.00 23.58 ± 0.23 Kx (NH4)1-xNO3 Single phase

20.00 27.74 ± 0.21 Kx (NH4)1-xNO3 Single phase

25.00 97.57 ± 1.66 Kx(NH4)1-xNO3 and

KNO3

Multi-phase of KNO3

and AN

* refers to mol % KNO3 in AN in crystallising solution, on water free basis

** refers to mol % KNO3 in mixed crystals as measured by ICP OES

15 20 25 30 35 40 45 50 55 60 652Theta (°)

20000

40000

60000

80000

Inte

nsity (

counts

)

Figure 5. XRD patterns of co-recrystallised AN containing 5-25 mol % KNO3.

15 20 25 30 35 40 45 50 55 60 652Theta (°)

20000

40000

60000

80000

Inte

nsity

(co

unts

)

Page 9: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

Figure 6. SEM images of pure AN (left), and 1 mol % KNO3-AN (right).

Figure 7. SEM images of 2 mol% KNO3 /AN (left), and 4 mol% KNO3 /AN (right).

Figure 8. SEM images of 10 mol % KNO3 /AN (left), and 25 mol % KNO3 /AN (right).

Page 10: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

.0 5 10 15 20

Energy (keV)

0

1

2

3

4

5

cps

KK

0 5 10 15 20Energy (keV)

0

1

2

3

4

5

6cps

K

K

Figure 9. EDS spectrums of recrystallized pure AN (left), and 4 mol % KNO3/AN (right).

0 5 10 15 20Energy (keV)

0

2

4

6

8

10

12cps

K

K

0 5 10 15 20Energy (keV)

0

5

10

15

20

cps

K

K

Figure 10. EDS spectrums of 4 mol % KNO3/AN (left), and K0.05(NH4)0.95NO3 (right).

0 5 10 15 20Energy (keV)

0

50

100

cps

K

K

0 5 10 15 20Energy (keV)

0

50

100

150

cps

K

K

Figure 11. EDS spectrums of K0.10(NH4)0.90NO3 (left), and K0.20(NH4)0.80NO3 (right).

Page 11: Preparation and characterisation of potassium ammonium ... · used mainly in formulating ammonium nitrate and fuel oil (ANFO) explosives, as well as emulsion explosives. Under adverse

4. CONCLUSION

Attempts were made to prepare mixed potassium ammonium nitrate salts for

potential application to minimise the formation of NOx during detonation of AN

explosives. Co-recrystallised mixed nitrate salts were prepared from pure ammonium

and potassium nitrate precursors. Powder XRD, SEM-EDS, and ICP-OES were used

to characterise the co-recrystallised salts. Co-recrystallisation of 1 mol % KNO3 and

AN resulted in a single phase, identified as AN phase IV. Increasing the concentration

of KNO3 to between 2 and 4 mol % resulted in the appearance of an additional AN

phase. Loadings of 5 to 20 mol % KNO3 formed solid solution of the form Kx(NH4)1-

xNO3, which has orthorhombic structure similar to pure AN phase III. Attempts to

increase KNO3 content in AN to 25 % led to the formation of two phases, solid

solution of the form Kx(NH4)1-xNO3 plus small phase precipitation of pure KNO3.

Acknowledgments

The authors are grateful to Professors Eric Kennedy and John Mackie of the

University of Newcastle and Dr Jeff Gore of Dyno Nobel Asia Pacific Pty Ltd for

their time and professional assistance. The first author would like to acknowledge the

financial support from the University of Newcastle Postgraduate Scholarships

(UNIPRS and UNRSC). We would like to thank Mr David Phelan and Ms Jennifer

Zobec of Electron Microscope/X-Ray Unit, The University of Newcastle for their

assistance with characterisation of the salts. This study was funded jointly by the

Australian Research Council and Dyno Nobel Asia Pacific Pty Ltd.

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