Time (min) - ResearchGate

MICROWAVE SWING ADSORPTION
FOR VOCS ELIMINATION WITH FAU TYPE ZEOLITES AS ADSORBENTS
H. Nigar, N. Navascués, O. de la Iglesia, José L. Hueso*, R. Mallada, J. Santamaría
Department Of Chemical Engineering And Environmental Technologies, Zaragoza University, Zaragoza, Spain
Emails: [email protected]; [email protected]
INTRODUCTION
EFFECT
SOURCE VOCS
VOCs ?
SOLUTION
Desorption: Microwave heating
Adsorption
•
•
•
•
• Allows to collect for reusing VOCs
• Preconcentration of VOCs for catalytic
oxidation
Volatile Organic
Compounds
(VOCs), organic
compounds
which easily
evaporate and
enter the
atmosphere
Industries
Vehicles
Health
ABSORB MICROWAVE RADIATION
GOOD ADSORBENT
• Carcinogens
• Chronic health threats
• Harm to Liver, kidney, Immune,
nervous, and reproductive systems.
• Destruction of the ozone layer
Household Products
Perfumes
Environmental
Selective heating
Avoid heat transfer problems
Fast heating and cooling
Energy saving
FAU type Zeolite
• Narrow pore size distribution
• Catalytic activity
• High specific area=Adsorption Capacity
• Ion exchange ability
• High thermal and chemical stability.
EXPERIMENTAL
ADSORPTION – DESORPTION EXPERIMENTS
MATERIALS
PRETREATMENT
Na2O
Zeolite
Si/Al
CBV100
CBV400
CBV780
2.5
2.5
40
ADSORPTION
BASELINE
N2
100ml/min
Hexane
N2
100 ml/min 100ml/min
100ml/min
N2
100ml/min
100ml/min
T
T
MS
*MS: Mass spectrometer
MW: Microwave Heating
CH:Conventional Heating
T
DESORPTION
Hexane
N2
Cation Weight
[%]
Na+
13.0
H+
2.8
H+
0.03
SWEEPING
MS
MS
Vent
T
MS
MS
T
CH/MW
CH/MW
CHARACTERIZATION
MICROWAVE HEATING
ARGON ADSORPTION
200
CBV780
CBV400
CBV780
175
TGA
100
CBV100
160W
240
150
50
25
90
85
CBV400
80
0,002
0,004
0,006
0,008
P/P0
0,010
0,012
0,014
Pore
TGA
Surface
dp
Volume Weight
Zeolite Area
[Å] [cm3/g]
[m²/g]
loss (%)
24.3
CBV100
758
6.9 0.341
14.7
CBV400
738
7.1 0.256
12.6
CBV780
711
7.3 0.217
250
CBV400
40,7°C/min
200
180
120
CBV780
25,6°C/min
150
CBV780
120
90
Water Intensity
100
26,5°C/min
60
60
CBV100
75
0
0,000
Temperature [°C]
75
Temperature
5°C/min
180
95
Weigth Loss [%]
3
cm /gSTP
100
300
300
150
125
MICROWAVE HEATING VS CONVENTIONAL HEATING AND COOLING
Temperature [°C]
CHARACTERIZATION
50
300
30
100
200
300
400
500
Temperature [°C]
600
700
Conventional Cooling 3°C/min
Microwave Cooling 160°C/min
0
2400
800
3200
Time [s]
4000
4800
TEM
120
60
10
20
30
Time [min]
40
50
30
Runaway could take place in
zeolites that highly absorb MW,
could lead to remove the
structural water.
Water Intensity
0
20
Faster cooling
Faster heating
MW
180
Higher heating ramp is reached
by CBV100 Zeolite, which has
more water uptake.
Higher temperature could be
reached in zeolites that contain
mobile Na+
Time [min]
200W
Temperature
70°C/min
240
10
60
RESULTS
HEXANE ADSORPTION AND DESORPTION
Hexane Adsorption Capacities
180
CBV100 160W
Microwave vs. Conventional
180
CBV100 160W
CBV400
CBV780
60
CBV100 100W
CBV780 160W
60
CBV400 160W
Hexane Intensity [a.u.]
120
CBV100
120
Hexane Intensity [a.u.]
Hexane intensity [a.u.]
Hexane Desorption in MW
Hexane Desorption in Conventional Heating
Temperature [°C]
*7 different batches
Hexane Desorption in Microwave Heating
Temperature [°C]
Adsorption Capacities*
Zeolite
[mg hexane/g zeolite]
CBV100
107.3 ± 3.33
CBV400
57.6 ± 3.30
CBV780
48.9 ± 1.91
Hexane Desorption in Conventional Heating
CBV100 100W
0
530
Lower adsorption capacity
is reached by CBV 780,
which has lower micropore
volume
535
540
Time (min)
545
550
Faster desorption is obtained by CBV 780,
which has higher porous size
0
10
20
Time [min]
30
40
At the same power, desorption of CBV100 and
CBV780 are at the same time.
At the same temperature, desorption kinetic is
similar to conventional desorption
420
425
430
435
Time [min]
440
445
450
Faster desorption in microwave
heating !!!
CONCLUSIONS
• Microwave heating process in zeolites depends on the amount of water physisorbed and the type of cations in zeolite structure. Increasing the degree of hydration and mobility of cation, increase
the temperature, which favors the desorption.
• Zeolites could be instable under MW radiation.
• Adsorption capacities and kinetics for FAU type zeolites have been obtained and correlated with adsorbent properties i.e. pore size and pore volume and hydrophilicity.
• Microwave desorption provide a faster desorption than conventional desorption.
• Differences in desorption kinetics between microwave and conventional is due to different temperature reached by zeolites at the same power.
ACKNOWLEDGEMENTS
This research is supported by EU Commission ERC Advanced grant (I-2011/004 – Hector Project)
The author gratefully acknowledge financial support from the Spanish Ministry of Education for the Training of University Professors
(Formación del Profesorado Universitario – Hakan Nigar FPU12/06864)