The Effect of Moisture on Heating Values - Oak Ridge National ...
The Effect of Moisture on Heating Values - Oak Ridge National ...
The Effect of Moisture on Heating Values - Oak Ridge National ...
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<str<strong>on</strong>g>The</str<strong>on</strong>g> <str<strong>on</strong>g>Effect</str<strong>on</strong>g> <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>Moisture</str<strong>on</strong>g> <strong>on</strong> <strong>Heating</strong> <strong>Values</strong><br />
Definiti<strong>on</strong>s for heating value <str<strong>on</strong>g>of</str<strong>on</strong>g> a biomass<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> heating value <str<strong>on</strong>g>of</str<strong>on</strong>g> any fuel is the energy released per unit mass or per unit volume <str<strong>on</strong>g>of</str<strong>on</strong>g> the<br />
fuel when the fuel is completely burned (ANSI/ASABE S593.1 2011). <str<strong>on</strong>g>The</str<strong>on</strong>g> term calorific<br />
value is syn<strong>on</strong>ymous to the heating value. Typical units for expressing calorific or heating<br />
value are MJ/kg in SI units or Btu/lb in English units. <str<strong>on</strong>g>The</str<strong>on</strong>g> heating value <str<strong>on</strong>g>of</str<strong>on</strong>g> a fuel depends <strong>on</strong><br />
the assumpti<strong>on</strong> made <strong>on</strong> the c<strong>on</strong>diti<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> water molecules in the final combusti<strong>on</strong> products.<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> higher heating value (HHV) refers to a c<strong>on</strong>diti<strong>on</strong> in which the water is c<strong>on</strong>densed out <str<strong>on</strong>g>of</str<strong>on</strong>g><br />
the combusti<strong>on</strong> products. Because <str<strong>on</strong>g>of</str<strong>on</strong>g> this c<strong>on</strong>densati<strong>on</strong> all <str<strong>on</strong>g>of</str<strong>on</strong>g> the heating value <str<strong>on</strong>g>of</str<strong>on</strong>g> the fuel<br />
including sensible heat and latent heat are accounted for. <str<strong>on</strong>g>The</str<strong>on</strong>g> lower heating value (LHV), <strong>on</strong><br />
the other hand refers to the c<strong>on</strong>diti<strong>on</strong> in which water in the final combusti<strong>on</strong> products remains<br />
as vapor (or steam); i.e. the steam is not c<strong>on</strong>densed into liquid water and thus the latent heat<br />
is not accounted for. <str<strong>on</strong>g>The</str<strong>on</strong>g> term net heating value (NHV) refers to LHV (ANSI/ASABE S593.1<br />
2011). <str<strong>on</strong>g>The</str<strong>on</strong>g> term gross heating value (GHV) refers to HHV.<br />
Determinati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> heating value <str<strong>on</strong>g>of</str<strong>on</strong>g> a biomass<br />
<strong>Heating</strong> value <str<strong>on</strong>g>of</str<strong>on</strong>g> a biomass is measured experimentally in terms <str<strong>on</strong>g>of</str<strong>on</strong>g> the high heating value<br />
(HHV). <str<strong>on</strong>g>The</str<strong>on</strong>g> standard method uses a device called bomb calorimeter. <str<strong>on</strong>g>The</str<strong>on</strong>g> device burns a<br />
small mass <str<strong>on</strong>g>of</str<strong>on</strong>g> biomass in the presence <str<strong>on</strong>g>of</str<strong>on</strong>g> oxygen inside a sealed c<strong>on</strong>tainer (or bomb). <str<strong>on</strong>g>The</str<strong>on</strong>g><br />
heat released from combusti<strong>on</strong> is transferred to a mass <str<strong>on</strong>g>of</str<strong>on</strong>g> fluid (air or water) that surrounds<br />
the c<strong>on</strong>tainer. <str<strong>on</strong>g>The</str<strong>on</strong>g> heating value is calculated from the product <str<strong>on</strong>g>of</str<strong>on</strong>g> mass <str<strong>on</strong>g>of</str<strong>on</strong>g> fluid x specific<br />
heat <str<strong>on</strong>g>of</str<strong>on</strong>g> fluid x net temperature increase. <str<strong>on</strong>g>The</str<strong>on</strong>g> calculated heating value must be corrected for<br />
heat losses to the mass <str<strong>on</strong>g>of</str<strong>on</strong>g> c<strong>on</strong>tainer, heat c<strong>on</strong>ducti<strong>on</strong> through the c<strong>on</strong>tainer wall, and heat<br />
losses to the surrounding <str<strong>on</strong>g>of</str<strong>on</strong>g> the device. In modern calorimeters the correcti<strong>on</strong>s are made<br />
automatically using sensors and c<strong>on</strong>trollers. <str<strong>on</strong>g>The</str<strong>on</strong>g> resulting measured heating value is<br />
c<strong>on</strong>sidered gross heating value (high heating value) at c<strong>on</strong>stant volume because the<br />
biomass combusti<strong>on</strong> in the c<strong>on</strong>tainer has taken place inside the fixed volume <str<strong>on</strong>g>of</str<strong>on</strong>g> the<br />
c<strong>on</strong>tainer. <str<strong>on</strong>g>The</str<strong>on</strong>g> resulting gross heating value can be expressed based <strong>on</strong> dry mass c<strong>on</strong>tent <str<strong>on</strong>g>of</str<strong>on</strong>g><br />
the sample biomass,<br />
HHV<br />
HHVd � (Eq. 1)<br />
1 � M<br />
where HHVd is the gross heating value <str<strong>on</strong>g>of</str<strong>on</strong>g> the biomass in MJ/kg <str<strong>on</strong>g>of</str<strong>on</strong>g> b<strong>on</strong>e dry biomass, HHV is<br />
the gross heating value determined by the calorimeter. M is the moisture c<strong>on</strong>tent <str<strong>on</strong>g>of</str<strong>on</strong>g> the<br />
biomass in decimal wet mass fracti<strong>on</strong>.<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> high heating value can be estimated from the compositi<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> the fuel (Gaur and<br />
Reed 1995),<br />
HHVd � 0.<br />
35X<br />
C � 1.<br />
18X<br />
H � 0.<br />
10X<br />
S �0.<br />
02X<br />
N �0.<br />
10X<br />
O �0.<br />
02X<br />
ash (Eq. 2)<br />
where X is the mass fracti<strong>on</strong>s (percent mass dry basis) for Carb<strong>on</strong> (C), Hydrogen (H), Sulfur<br />
(S), Nitrogen (N), Oxygen (O), and ash c<strong>on</strong>tent (ash). <str<strong>on</strong>g>The</str<strong>on</strong>g> unit <str<strong>on</strong>g>of</str<strong>on</strong>g> HHV in Equati<strong>on</strong> 2 is in<br />
Biomass Energy Data Book -- 2011 -- http://cta.ornl.gov/bedb
MJ/kg dry mass. Equati<strong>on</strong> 2 shows that the elements Carb<strong>on</strong>, Hydrogen, Sulfur increase the<br />
heating value whereas the elements Nitrogen, Oxygen, and ash suppress the heating value.<br />
Net heating value <str<strong>on</strong>g>of</str<strong>on</strong>g> biomass<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> HHV or GHV for woody biomass (including bark) that is determined experimentally is<br />
around 20 MJ/kg (8600 Btu/ lb) dry mass basis and for herbaceous biomass it is around<br />
18.8 MJ/kg (8080 Btu/ lb) dry mass basis (Oberberger and <str<strong>on</strong>g>The</str<strong>on</strong>g>k 2010). For a moist fuel, the<br />
heating value decreases because a porti<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> the combusti<strong>on</strong> heat is used up to evaporate<br />
moisture in the biomass and this evaporated moisture has not been c<strong>on</strong>densed to return the<br />
heat back to the system. An estimate <str<strong>on</strong>g>of</str<strong>on</strong>g> the LHV or net heating value (NHV) is obtained from<br />
the measured HHV by subtracting the heat <str<strong>on</strong>g>of</str<strong>on</strong>g> vaporizati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> water in the products.<br />
LHV � HHV 1�<br />
M � 2.<br />
447<br />
(Eq. 3)<br />
� � M<br />
where LHV is the gross (or lower) heating value MJ/kg, M is the wet basis moisture c<strong>on</strong>tent<br />
(mass fracti<strong>on</strong> decimal). <str<strong>on</strong>g>The</str<strong>on</strong>g> c<strong>on</strong>stant 2.447 is the latent heat <str<strong>on</strong>g>of</str<strong>on</strong>g> vaporizati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> water in<br />
MJ/kg at 25 o C. A more accurate estimate <str<strong>on</strong>g>of</str<strong>on</strong>g> the net heating value from equati<strong>on</strong> 3 can be<br />
obtained by including the heat released by the combusti<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> the hydrogen c<strong>on</strong>tent <str<strong>on</strong>g>of</str<strong>on</strong>g> the<br />
biomass.<br />
High and low heating value at c<strong>on</strong>stant pressure<br />
In practice, the gases evolving from combusti<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> a biomass are expanded without much<br />
c<strong>on</strong>straints. In other words during combusti<strong>on</strong> the volume expands but the pressure in the<br />
combusti<strong>on</strong> z<strong>on</strong>e does not change much. This situati<strong>on</strong> is <str<strong>on</strong>g>of</str<strong>on</strong>g>ten present in a boiler<br />
combusti<strong>on</strong> chamber with unrestricted exhaust system. For these cases equati<strong>on</strong> 3<br />
developed from c<strong>on</strong>stant volume measurement is c<strong>on</strong>verted to heating value at c<strong>on</strong>stant<br />
pressure according to equati<strong>on</strong> 4,<br />
HHV � HHV �0.<br />
212X<br />
�0.<br />
0008 X � X<br />
(Eq. 4)<br />
p<br />
H<br />
� �<br />
where HHVp is the high heating value at c<strong>on</strong>stant pressure for dry biomass. XH, XO, and XN<br />
are the mass fracti<strong>on</strong> (percent dry mass) <str<strong>on</strong>g>of</str<strong>on</strong>g> the biomass. For wet biomass, the net heating<br />
value at c<strong>on</strong>stant pressure is calculated from<br />
� HHV 1.<br />
0 � M � 2.<br />
443<br />
(Eq. 5)<br />
LHVp, w<br />
p<br />
O<br />
� � M<br />
M is the wet basis moisture c<strong>on</strong>tent (mass fracti<strong>on</strong> decimal). LHVp,w is the net heating value<br />
<str<strong>on</strong>g>of</str<strong>on</strong>g> biomass at c<strong>on</strong>stant pressure per unit <str<strong>on</strong>g>of</str<strong>on</strong>g> wet biomass.<br />
Example <str<strong>on</strong>g>of</str<strong>on</strong>g> using equati<strong>on</strong>s 1-5<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> high heating values <str<strong>on</strong>g>of</str<strong>on</strong>g> two biomass species poplar and stover al<strong>on</strong>g with their ultimate<br />
analysis were measured. <str<strong>on</strong>g>The</str<strong>on</strong>g> moisture c<strong>on</strong>tent <str<strong>on</strong>g>of</str<strong>on</strong>g> the samples was 35% wet mass basis.<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> table below lists the measured data.<br />
Biomass Energy Data Book -- 2011 -- http://cta.ornl.gov/bedb<br />
N
Measured <str<strong>on</strong>g>Moisture</str<strong>on</strong>g>, Elements, and High <strong>Heating</strong> Value <str<strong>on</strong>g>of</str<strong>on</strong>g> Biomass<br />
M (%) Ash (%) C (%) H (%) O (%) N (%) S (%)<br />
HHVd<br />
(MJ/kg)<br />
Poplar 35 0.65 51.64 6.26 41.45 0.00 0.00 20.75<br />
Stover 35 11.27 44.80 5.35 39.55 0.38 0.01 17.33<br />
Estimati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> HHVd (c<strong>on</strong>stant volume)<br />
Equati<strong>on</strong> 2 is used to calculate high heating value<br />
HHV � 0.<br />
35X<br />
� 1.<br />
18X<br />
� 0.<br />
10X<br />
�0.<br />
02X<br />
�0.<br />
10X<br />
�0.<br />
02X<br />
d<br />
Substituting from compositi<strong>on</strong>s listed in the table above<br />
for poplar<br />
HHV d<br />
�<br />
�<br />
21.<br />
3 MJ/kg<br />
0.<br />
35(<br />
51.<br />
64 )<br />
�<br />
C<br />
1.<br />
18(<br />
6.<br />
26<br />
H<br />
S<br />
N<br />
) � 0.<br />
10(<br />
0.<br />
00 ) � 0.<br />
02(<br />
0.<br />
00 ) � 0.<br />
10(<br />
41.<br />
45 ) � 0.<br />
02(<br />
0.<br />
65 )<br />
and for stover,<br />
� 0.<br />
35(<br />
44.<br />
80 ) � 1.<br />
18(<br />
5.<br />
35 ) � 0.<br />
10(<br />
0.<br />
01)<br />
� 0.<br />
02(<br />
0.<br />
38 ) � 0.<br />
10(<br />
39.<br />
55 ) � 0.<br />
02(<br />
11.<br />
27 )<br />
HHV d<br />
�<br />
17.<br />
8<br />
MJ/kg<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> calculated HHVd for both species are slightly higher than measured HHVd in the table<br />
above.<br />
Estimati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> LHV (c<strong>on</strong>stant volume)<br />
Equati<strong>on</strong> 3 is used to calculate low heating value<br />
LHV � HHVd<br />
1�<br />
M � 2.<br />
447<br />
Substituting for HHV and moisture c<strong>on</strong>tent,<br />
for poplar,<br />
LHV � ( 20.<br />
8 ) 1 � 0.<br />
35 �<br />
and for stover,<br />
�<br />
12.<br />
7<br />
LHV �<br />
�<br />
10.<br />
4<br />
MJ/kg<br />
( 17.<br />
3<br />
MJ/kg<br />
� � M<br />
� �<br />
�1 � 0.<br />
35�<br />
)<br />
�<br />
2.<br />
447(<br />
0.<br />
35 )<br />
2.<br />
447(<br />
0.<br />
35 )<br />
Calculati<strong>on</strong>s for <str<strong>on</strong>g>of</str<strong>on</strong>g> HHVp (c<strong>on</strong>stant pressure)<br />
Equati<strong>on</strong> 3 is used to calculate low heating value (or net calorific value) at c<strong>on</strong>stant pressure<br />
HHV � HHV �0.<br />
212X<br />
�0.<br />
0008 X � X<br />
p<br />
d<br />
H<br />
O<br />
� �<br />
Substituting from the table above for HHVd (for c<strong>on</strong>stant volume) and c<strong>on</strong>centrati<strong>on</strong>s,<br />
for poplar,<br />
� ( 20.<br />
8 ) � 0.<br />
212(<br />
6.<br />
26 ) � 0.<br />
0008 41.<br />
45 � 0.<br />
00<br />
HHV p<br />
�<br />
19.<br />
4<br />
MJ/kg<br />
O<br />
N<br />
� �<br />
Biomass Energy Data Book -- 2011 -- http://cta.ornl.gov/bedb<br />
ash
and for stover,<br />
HHV p<br />
�<br />
� ( 17.<br />
3 ) � 0.<br />
212(<br />
5.<br />
35 ) � 0.<br />
0008<br />
16.<br />
1 MJ/kg<br />
Calculati<strong>on</strong>s for <str<strong>on</strong>g>of</str<strong>on</strong>g> LHVp (c<strong>on</strong>stant pressure)<br />
Equati<strong>on</strong> 5 is used to calculate low heating value,<br />
� HHV 1.<br />
0 � M<br />
�<br />
LHVp p<br />
Substituting for HHVp and moisture c<strong>on</strong>tent,<br />
for poplar,<br />
LHV � ( 19.<br />
4 ) 1 � 0.<br />
35 �<br />
and for stover,<br />
11.<br />
8<br />
LHV �<br />
�<br />
9.<br />
6<br />
MJ/kg<br />
( 16.<br />
1<br />
MJ/kg<br />
� �� 2.<br />
443M<br />
� �<br />
�1 � 0.<br />
35�<br />
)<br />
�<br />
�39. 55 � 0.<br />
38�<br />
2.<br />
443(<br />
0.<br />
35 )<br />
2.<br />
443(<br />
0.<br />
35 )<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> table below shows the applicati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> equati<strong>on</strong> 5 to calculate the net heating value<br />
<str<strong>on</strong>g>of</str<strong>on</strong>g> biomass at various levels <str<strong>on</strong>g>of</str<strong>on</strong>g> moisture c<strong>on</strong>tent. Increasing moisture c<strong>on</strong>tent diminished the<br />
net heat value <str<strong>on</strong>g>of</str<strong>on</strong>g> biomass to the point that at slightly higher than 80% moisture c<strong>on</strong>tent, much<br />
<str<strong>on</strong>g>of</str<strong>on</strong>g> the heat c<strong>on</strong>tent <str<strong>on</strong>g>of</str<strong>on</strong>g> the biomass is used up to evaporate its moisture.<br />
<str<strong>on</strong>g>Effect</str<strong>on</strong>g> <str<strong>on</strong>g>of</str<strong>on</strong>g> <str<strong>on</strong>g>Moisture</str<strong>on</strong>g> C<strong>on</strong>tent <strong>on</strong> the Net <strong>Heating</strong> Value <str<strong>on</strong>g>of</str<strong>on</strong>g> Biomass at<br />
C<strong>on</strong>stant Pressure<br />
<str<strong>on</strong>g>Moisture</str<strong>on</strong>g> c<strong>on</strong>tent percent wet mass basis<br />
Biomass<br />
0 10 20 30 40 50 60 70 80<br />
Poplar 19.4 17.3 15.1 12.9 10.7 8.5 6.3 4.1 1.9<br />
Stover 16.1 14.3 12.4 10.6 8.7 6.8 5.0 3.1 1.3<br />
Biomass Energy Data Book -- 2011 -- http://cta.ornl.gov/bedb
List and Definiti<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> Symbols<br />
Symbol Definiti<strong>on</strong><br />
LHV Lower heating value<br />
HHV Higher heating value<br />
GHV Gross heating value<br />
NHV<br />
HHVp<br />
Net heating value<br />
High heating value at c<strong>on</strong>stant pressure<br />
HHVd<br />
B<strong>on</strong>e dry gross heating value <str<strong>on</strong>g>of</str<strong>on</strong>g> the biomass<br />
M <str<strong>on</strong>g>Moisture</str<strong>on</strong>g> c<strong>on</strong>tent wet mass basis<br />
X<br />
Subscripts<br />
Mass fracti<strong>on</strong> percent dry mass basis<br />
ash Ash<br />
C Carb<strong>on</strong><br />
d Dry mass basis<br />
H Hydrogen<br />
N Nitrogen<br />
O Oxygen<br />
p C<strong>on</strong>stant pressure<br />
w<br />
Units<br />
Moist biomass<br />
Btu British thermal unit<br />
°C Degrees Celsius<br />
MJ Mega (10 6 ) Joule (SI unit)<br />
kg Kilogram<br />
lb Pound mass<br />
References<br />
ASABE Standards. 2011. American Society for Agricultural & Biological Engineers, St.<br />
Joseph, MI: ASABE.<br />
ASTM E870 - 82(2006) Standard Test Methods for Analysis <str<strong>on</strong>g>of</str<strong>on</strong>g> Wood Fuels.<br />
http://www.astm.org/Standards/E870.htm<br />
Gaur, S., T. Reed. 1995. An atlas <str<strong>on</strong>g>of</str<strong>on</strong>g> thermal data for biomass and other fuels. NREL/TB-<br />
433-7965, UC Category: 1310, DE95009212, Nati<strong>on</strong>al Renewable laboratory, Golden<br />
Colorado, USA.<br />
Obenberger, I. and G. <str<strong>on</strong>g>The</str<strong>on</strong>g>k. 2010. <str<strong>on</strong>g>The</str<strong>on</strong>g> Pellet Handbook. IEA Bioenergy. Earthscan LLC,<br />
Washingt<strong>on</strong>, DC.<br />
SIS-CENéTS14918:2005. Solid bi<str<strong>on</strong>g>of</str<strong>on</strong>g>uels. Method <str<strong>on</strong>g>of</str<strong>on</strong>g> determinati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> calorific value.<br />
http://www.biomassenergycentre.org.uk/portal/page?_pageid=77,19836&_dad=portal&_sc<br />
hema=PORTAL<br />
Sjaak, Van Loo, Jaap Koppejan. 2008. <str<strong>on</strong>g>The</str<strong>on</strong>g> handbook <str<strong>on</strong>g>of</str<strong>on</strong>g> biomass combusti<strong>on</strong> and co-firing.<br />
Earthsacn, Washingt<strong>on</strong>, DC.<br />
TAPPI Gross heating value <str<strong>on</strong>g>of</str<strong>on</strong>g> black liquor, Test Method T 684 om-<br />
11http://www.tappi.org/Bookstore/Standards--TIPs/Standards.aspx<br />
Written by Shahab Sokhansanj, <strong>Oak</strong> <strong>Ridge</strong> Nati<strong>on</strong>al Laboratory, September 2011.<br />
Biomass Energy Data Book -- 2011 -- http://cta.ornl.gov/bedb