A heat balance for bottom sediment underlying a water element i can be written as
()
where Ts,i = the temperature of the bottom sediment below element i [oC], Js,i = the sediment-water heat flux [cal/(cm2 d)], ?s = the density of the sediments [g/cm3], Cps = the specific heat of the sediments [cal/(g oC)], and Hsed,i = the effective thickness of the sediment layer [cm].
The flux from the sediments to the water can be computed as
()
where ?s = the sediment thermal diffusivity [cm2/s].
The thermal properties of some natural sediments along with its components are summarized in Table . Note that soft, gelatinous sediments found in the deposition zones of lakes are very porous and approach the values for water. Some very slow, impounded rivers may approach such a state. However, rivers tend to have coarser sediments with significant fractions of sands, gravels and stones. Upland streams can have bottoms that are dominated by boulders and rock substrates.
Table Thermal properties for natural sediments and the materials that comprise natural sediments.
Inspection of the component properties of Table suggests that the presence of solid material in stream sediments leads to a higher coefficient of thermal diffusivity than that for water or porous lake sediments. In Q2K, we suggest a default value of 0.005 cm2/s for this quantity.
In addition, specific heat tends to decrease with density. Thus, the product of these two quantities tends to be more constant than the multiplicands. Nevertheless, it appears that the presence of solid material in stream sediments leads to a lower product than that for water or gelatinous lake sediments. In Q2K, we suggest default values of ?s = 1.6 g/cm3 and Cps = 0.4 cal/(g oC). This corresponds to a product of 0.64 cal/(cm3 oC) for this quantity. Finally, as derived in Appendix C, the sediment thickness is set by default to 10 cm in order to capture the effect of the sediments on the diel heat budget for the water.
CONSTITUENT MODEL
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The model constituents are listed in Table .
Table Model state variables
Variable
|
Symbol
|
Units*
|
|
Conductivity
|
s
|
?mhos
|
Inorganic suspended solids
|
mi
|
mgD/L
|
Dissolved oxygen
|
o
|
mgO2/L
|
Slowly reacting CBOD
|
cs
|
mgO2/L
|
Fast reacting CBOD
|
cf
|
mgO2/L
|
Organic nitrogen
|
no
|
?gN/L
|
Ammonia nitrogen
|
na
|
?gN/L
|
Nitrate nitrogen
|
nn
|
?gN/L
|
Organic phosphorus
|
po
|
?gP/L
|
Inorganic phosphorus
|
pi
|
?gP/L
|
Phytoplankton
|
ap
|
?gA/L
|
Phytoplankton nitrogen
|
INp
|
?gN/L
|
Phytoplankton phosphorus
|
IPp
|
?gP/L
|
Detritus
|
mo
|
mgD/L
|
Pathogen
|
X
|
cfu/100 mL
|
Alkalinity
|
Alk
|
mgCaCO3/L
|
Total inorganic carbon
|
cT
|
mole/L
|
Bottom algae biomass
|
ab
|
mgA/m2
|
Bottom algae nitrogen
|
INb
|
mgN/m2
|
Bottom algae phosphorus
|
IPb
|
mgP/m2
|
Constituent i
|
|
|
Constituent ii
|
|
|
Constituent iii
|
|
|
* mg/L ? g/m3; In addition, the terms D, C, N, P, and A refer to dry weight, carbon, nitrogen, phosphorus, and chlorophyll a, respectively. The term cfu stands for colony forming unit which is a measure of viable bacterial numbers.
For all but the bottom algae variables, a general mass balance for a constituent in an element is written as (Figure )
()
where Wi = the external loading of the constituent to element i [g/d or mg/d], and Si = sources and sinks of the constituent due to reactions and mass transfer mechanisms [g/m3/d or mg/m3/d].
Figure Mass balance.
The external load is computed as (recall Eq. 2),
()
where cps,i,j is the jth point source concentration for element i [mg/L or ?g/L], and cnps,i,j is the jth non-point source concentration for element i [mg/L or ?g/L].
For bottom algae, the transport and loading terms are omitted,
()
()
()
where Sb,i = sources and sinks of bottom algae biomass due to reactions [mgA/m2/d], SbN,i = sources and sinks of bottom algae nitrogen due to reactions [mgN/m2/d], and SbP,i = sources and sinks of bottom algae phosphorus due to reactions [mgP/m2/d].
The sources and sinks for the state variables are depicted in Figure (note that the internal levels of nitrogen and phosphorus in the bottom algae are not depicted). The mathematical representations of these processes are presented in the following sections.
Figure Model kinetics and mass transfer processes. The state variables are defined in Table . Kinetic processes are dissolution (ds), hydrolysis (h), oxidation (ox), nitrification (n), denitrification (dn), photosynthesis (p), respiration (r), excretion (e), death (d), respiration/excretion (rx). Mass transfer processes are reaeration (re), settling (s), sediment oxygen demand (SOD), sediment exchange (se), and sediment inorganic carbon flux (cf).
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