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TRANSPORT OF WATER VAPOUR Chapter 6
1
Quantities for moist air Section 6.1
2
3 http://www.atmosedu.com/meteor/Animations/chapter23/
saturated vapor pressure
• imagine a closed container, partially filled with liquid water
vice versa, all gases have a tendency to condense
like all liquids, water has the
tendency to evaporate
the corresponding vapor pressure in the gas is called “saturated vapor pressure” (𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa])
at equilibrium Gevaporation = Gcondensation
4
saturated vapor pressure
• now increase the temperature
since the vapor pressure increases, the condensation rate increases as well
molecules have more energy to escape
from the liquid and evaporation increases
a new equilibrium is found, characterized by a higher “saturated vapor pressure” (𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa])
5
saturated vapor pressure
• how to find 𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 for a given temperature? – from charts (not sufficiently accurate) – from tables – from mathematical expressions
these three methods have a different accuracy for exercises, you can choose between tables (book) or mathematical expression
6
saturated vapor pressure
• determination of 𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 based on a chart
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 ≈ 1100 Pa
𝜃𝜃 ≈ 8.4 °C
7
For building physics applications, pv,sat lies between ≈ 100-10’000 Pa !!!
saturated vapor pressure
• determination of 𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 based on a table
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 = 1102 Pa at 8.4 °C 8
saturated vapor pressure
• determination of 𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 based on a formula
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 = 1101.8 Pa at 8.4 °C
𝜃𝜃 < 0℃
𝜃𝜃 ≥ 0℃
9
22.5273
, 610.5v satp eθθ+
=
17.27237.3
, 610.5v satp eθθ
+ =
relative humidity
• now we remove the lid of the container
since there are less molecules above the solution, the conden- sation rate decreases
evaporation will still continue
some molecules escape
the vapor pressure in the air is lower than 𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠
10
relative humidity
• relative humidity (RH) is the ratio of the vapor pressure to the saturated vapor pressure – symbol: 𝜑𝜑
– formula: 𝜑𝜑 = 𝑝𝑝𝑣𝑣𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠
– unit: dimensionless, sometimes in %
by definition, 𝜑𝜑 has to have a value between 0 and 1! so between 0% – 100%!
11
relative humidity
12
For building physics applications, pv lies between ≈ 0-10’000 Pa !!!
Warm and humid air => high pv
Cold and dry air => low pv
dew point
• the dew point is the temperature to which humid air must be cooled, at constant pressure, for vapor to condense into water – symbol: 𝜃𝜃𝑑𝑑
– unit: °C
• the dew point can be found using (i) a chart,
(ii) a table or (iii) a formula
13
relative humidity
14 Dewpoint θd
Temperature at which pv,sat(θd)= pv(θamb,RHamb)
What is the dew point at 25°C and RH = 50%?
condensation
• condensation occurs when the temperature at a certain location is equal to or below the dew point of the humid air at that location:
• condensation occurs when the vapor pressure at a certain location becomes equal to the saturated vapor pressure at that location:
dθθ ≤
satvv pp ,=15
,
100%v
v sat
pp
ϕ = =
vapor concentration
• the vapor concentration is the mass of vapor per unit volume of air – symbol: 𝜌𝜌𝑣𝑣
– formula: 𝜌𝜌𝑣𝑣 = 𝑚𝑚𝑣𝑣𝑉𝑉
• 𝜌𝜌𝑣𝑣 depends on 𝑝𝑝𝑣𝑣 and 𝑇𝑇!
– unit: kg/m3
Example: at 99% RH and 20°C
→ 𝜌𝜌𝑣𝑣 =𝑝𝑝𝑣𝑣𝑅𝑅𝑣𝑣𝑇𝑇
16 ( )
3
0.99 2337 0.0171462 20 273.15
.
v vsatv
v v a
p p Pa kgJR T R T mK
kg K
ϕρ ×= = = =
+
Also called absolute humidity
vapor ratio
• the vapor ratio is the mass of vapor per unit mass of dry air – symbol: 𝑥𝑥 – formula:
• often used in HVAC product documentation
– unit: kg/kg Example: at 99% RH and 20°C
d
v
dv
vd
d
v
d
v
pp
pRpR
mmx 62.0====
ρρ
17
3
3
0.01421.
0.0171
2
v
a
v
d
a
v
dd
m
m
kgkgx kg kg
ρρ
= = =
Amount of water vapour that can be contained in the air is small!
31.2d akgm
ρ ρ≈ = 101325d ap P Pa≈ =
Question humidity
• The air in a closed room (30°C) has an absolute humidity of 18 g/m3. When the air is cooled, how do the following parameters change: – Relative humidity – Absolute humidity – Dew point temperature
18
unit equation
Ideal gas law -
Relative humidity %
Vapor concentration kg/m³
Vapor ratio kg/kg
Air pressure Pa
overview
v v
d d
mxm
ρρ
= =
19
v vv
v
m pV R T
ρ = =
,
v
v sat
pp
ϕ =
v v vp V m R T=
a d vP p p= +
exercise
• you place some food in a box (15 x 15 x 5 cm3) in the kitchen (20°C, 50% RH). You close the lid of the box, and put the box in the fridge (2°C). – what happens? – express initial and final
state in 𝑝𝑝𝑣𝑣, 𝜑𝜑, 𝜌𝜌𝑣𝑣, 𝑥𝑥, 𝑚𝑚𝑣𝑣
(𝑅𝑅𝑣𝑣 = 462 J/(kg.K); 𝜌𝜌𝑠𝑠 = 1.2 kg/m3)
20
exercise - solution
• requested
21
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa]
𝑝𝑝𝑣𝑣 [Pa]
𝜌𝜌𝑣𝑣 [kg/m3]
𝑥𝑥 [kg/kg]
𝑚𝑚𝑣𝑣 [kg]
exercise - solution
• requested
22
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50% 100%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa] 2337 Pa 705 Pa 705 Pa
𝑝𝑝𝑣𝑣 [Pa]
𝜌𝜌𝑣𝑣 [kg/m3]
𝑥𝑥 [kg/kg]
𝑚𝑚𝑣𝑣 [kg]
exercise - solution
• requested
23
, , , 0.5 2337 Pa 1169 Pav ini ini v sat inip pϕ= = × =
( ),
, 3
1169 Pa 0.0086462 20 273.15 K
v ini vv ini
v ini a
p kgJR T m
kgK
ρ = = =+
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50% 100%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa] 2337 Pa 705 Pa 705 Pa
𝑝𝑝𝑣𝑣 [Pa] 1169 Pa
𝜌𝜌𝑣𝑣 [kg/m3] 0.0086 kg/m3
𝑥𝑥 [kg/kg]
𝑚𝑚𝑣𝑣 [kg]
exercise - solution
• requested
24
3,
3
0.00860.0072
1.2
v
v ini a v
aa a
a
kgm kgx kg kg
m
ρρ
= = =
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50% 100%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa] 2337 Pa 705 Pa 705 Pa
𝑝𝑝𝑣𝑣 [Pa] 1169 Pa 705 Pa
𝜌𝜌𝑣𝑣 [kg/m3] 0.0086 kg/m3
𝑥𝑥 [kg/kg] 0.0072 kg/kg
𝑚𝑚𝑣𝑣 [kg]
31.2d aa
a
kgm
ρ ρ≈ =
exercise - solution
• requested
25
( )3 6, 30.0086 0.15 0.15 0.05 9.71 10v
v v ini box va
kgm V m kgm
ρ −= = × × = ×
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50% 100%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa] 2337 Pa 705 Pa 705 Pa
𝑝𝑝𝑣𝑣 [Pa] 1169 Pa 705 Pa
𝜌𝜌𝑣𝑣 [kg/m3] 0.0086 kg/m3
𝑥𝑥 [kg/kg] 0.0072 kg/kg
𝑚𝑚𝑣𝑣 [kg] 9.71x10-6 kg
exercise - solution
• requested
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50% 100%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa] 2337 Pa 705 Pa 705 Pa
𝑝𝑝𝑣𝑣 [Pa] 1169 Pa 705 Pa
𝜌𝜌𝑣𝑣 [kg/m3] 0.0086 kg/m3 0.0086 kg/m3
𝑥𝑥 [kg/kg] 0.0072 kg/kg 0.0072 kg/kg
𝑚𝑚𝑣𝑣 [kg] 9.71x10-6 kg 9.71x10-6 kg
26
exercise - solution
• requested
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50% 100%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa] 2337 Pa 705 Pa 705 Pa
𝑝𝑝𝑣𝑣 [Pa] 1169 Pa 1097 Pa 705 Pa
𝜌𝜌𝑣𝑣 [kg/m3] 0.0086 kg/m3 0.0086 kg/m3
𝑥𝑥 [kg/kg] 0.0072 kg/kg 0.0072 kg/kg
𝑚𝑚𝑣𝑣 [kg] 9.71x10-6 kg 9.71x10-6 kg
27
( ),fin ,fin 30.0086 462 2 273.15K 1097vv v v fin
a
kg Jp R T Pam kgK
ρ= = + =
exercise - solution
• requested
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50% 156% 100%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa] 2337 Pa 705 Pa 705 Pa
𝑝𝑝𝑣𝑣 [Pa] 1169 Pa 1097 Pa 705 Pa
𝜌𝜌𝑣𝑣 [kg/m3] 0.0086 kg/m3 0.0086 kg/m3
𝑥𝑥 [kg/kg] 0.0072 kg/kg 0.0072 kg/kg
𝑚𝑚𝑣𝑣 [kg] 9.71x10-6 kg 9.71x10-6 kg
28
( ),fin ,fin 30.0086 462 2 273.15K 1097vv v v fin
a
kg Jp R T Pam kgK
ρ= = + =
,finfin
, ,fin
1097 156%705
v
v sat
p Pap Pa
ϕ = = = Condens until RH = 100%
exercise - solution
• requested
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50% 156% 100%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa] 2337 Pa 705 Pa 705 Pa
𝑝𝑝𝑣𝑣 [Pa] 1169 Pa 1097 Pa 705 Pa
𝜌𝜌𝑣𝑣 [kg/m3] 0.0086 kg/m3 0.0086 kg/m3
𝑥𝑥 [kg/kg] 0.0072 kg/kg 0.0072 kg/kg
𝑚𝑚𝑣𝑣 [kg] 9.71x10-6 kg 9.71x10-6 kg
29 Condens until RH = 100%
exercise - solution
• requested
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50% 156% 100%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa] 2337 Pa 705 Pa 705 Pa
𝑝𝑝𝑣𝑣 [Pa] 1169 Pa 1097 Pa 705 Pa
𝜌𝜌𝑣𝑣 [kg/m3] 0.0086 kg/m3 0.0086 kg/m3 0.0055 kg/m3
𝑥𝑥 [kg/kg] 0.0072 kg/kg 0.0072 kg/kg 0.0046 kg/kg
𝑚𝑚𝑣𝑣 [kg] 9.71x10-6 kg 9.71x10-6 kg
30
( ),cond
,cond 3
705Pa 0.0055462 2 273.15K
v vv
v fin a
p kgJR T m
kgK
ρ = = =+
,cond 0.0046v v
a a
kgxkg
ρρ
= =
exercise - solution
• requested
initial final with condens
θ [°C] 20°C 2°C 2°C
𝜑𝜑 [%] 50% 156% 100%
𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 [Pa] 2337 Pa 705 Pa 705 Pa
𝑝𝑝𝑣𝑣 [Pa] 1169 Pa 1097 Pa 705 Pa
𝜌𝜌𝑣𝑣 [kg/m3] 0.0086 kg/m3 0.0086 kg/m3 0.0055 kg/m3
𝑥𝑥 [kg/kg] 0.0072 kg/kg 0.0072 kg/kg 0.0046 kg/kg
𝑚𝑚𝑣𝑣 [kg] 9.71x10-6 kg 9.71x10-6 kg 6.24x10-6 kg
31
( )3 6, ,cond 30.0055 0.15 0.15 0.05 6.24 10v
v cond v box va
kgm V m kgm
ρ −= = × × = ×
6, , ,cond 3.46 10cond liq v ini v lm m m kg−= − = × Amount of condensed liquid water
Question humidity
• 2 cases – Winterday -10°C 90% – Summerday 25°C 40%
• On which day is the air more humid (absolute humidity)?
32
v vv
v
m pV R T
ρ = =
To remember
• Moisture quantities
• 𝑝𝑝𝑣𝑣,𝑠𝑠𝑠𝑠𝑠𝑠 from table or formula 33
Additional exercises Vapour - part 1
34
Exercise 1: quantities for moist air • Air at 34°C and 39% relative humidity?
– What is the partial vapor pressure (pv) 2073 Pa – What is the vapor concentration (ρv) 0.0146 kg/m3
– What is the vapor ratio (x) 0.0122 kg/kg – What is the dew point (θd) ≈ 18.1°C
• The air is heated to 40°C (in a closed container)
– What is the partial vapor pressure (pv) 2114 Pa – What is the relative humidity 29 % – What is the vapor concentration (ρv) 0.0146 kg/m3
– What is the vapor ratio (x) 0.0122 kg/kg
use the formula to calculate pv,sat use the table to determine dew point
35
Vapor transport Section 6.2
36
advection ↔ diffusion
advection • air moves • water vapor is transported
together with the air • driven by a pressure
difference (ΔPa)
diffusion • air is stagnant • water vapor is transported
through the air • driven by a concentration
difference (Δpv)
37 High concentration (pv >>>)
Low concentration (pv <<<)
diffusion
• Applications in this course – Diffusion through building materials/components – Interstitial condensation
38
diffusion
• imagine a closed container, consisting of two compartments
water vapor dry air
vapor concentration is different in both compartments
39
diffusion
• now take away the barrier and wait until a new equilibrium is found
water vapor dry air
this transport mechanism is called diffusion
40
vapor diffusion in air
• diffusion in air is described by
a
vvdav Dg
ρρρ ∇−=
with ρa [kg/m3] the air density ρv [kg/m3] the vapor concentration Dvd [m2/s] the binary diffusion coefficient of water vapor in dry air, given by
81.1101069.8 TDvd−⋅= (according to Schirmer)
41
vapor diffusion in air
• let’s simplify this formula
a
vvdav Dg
ρρρ ∇−=
(assume that ρa is constant) vvdv Dg ρ∇−=
(vapor behaves as an ideal gas)
TRpDgv
vvdv ∇−=
(assume that T is constant) v
v
vdv p
TRDg ∇−=
42
vapor diffusion in air
• and some further simplifications
(introduce the variable δa = vapor permeability of air)
vav pg ∇−= δ
(definition of a gradient)
vv
vdv p
TRDg ∇−=
va
v pd
g ∆=δ
s 102 10−⋅≈aδ at 20°C
43
Large vapor flux if: • Large vapor pressure difference • Large vapor permeability of air • Small thickness of (air) layer d
𝛥𝛥𝑝𝑝𝑣𝑣 𝛿𝛿𝑠𝑠
vapor diffusion in air
• the mass flow rate by diffusion in air is thus
with 𝐾𝐾𝑣𝑣𝑠𝑠 [s/m] the (vapor) diffusion permeance of air 𝛿𝛿𝑠𝑠 [s] the vapor permeability of air 𝑑𝑑 [m] the thickness of the air layer 𝐴𝐴 [m2] the frontal area of the air layer
diffusion is an extremely slow process, but since buildings have a long life-time …
44
( ),1 2 ,1 ,2aa
v v v v vG A p AK p pdδ
− = ∆ = − a avK
dδ
=
vapor diffusion in air
• … diffusion can lead to severe problems
© Marsden Property Services
45
vapor diffusion in air
• the diffusion constant 𝑁𝑁 [s-1] is the inverse of the vapor permeability of air
• 𝑁𝑁 was introduced because small quantities give the (wrong) impression that the associated phenomena are unimportant
a
Nδ1
= -19 s 105 ⋅≈N at 20°C and
46
vapor diffusion in materials
• just like (advective) air transport, also diffusive transport can take place through materials with open porosity
accessible
non-accessible
solid material
since there is only a limited number of pathways through the material, diffusion will be slower than in plain air
47
vapor diffusion in materials
• the shortest path through a material is at least as long as the material thickness, but probably much longer
48
accessible
non-accessible
solid material
this is due to the «tortuosity» of the pore system d
L
L ≥ d
vapor diffusion in materials
• the vapor resistance factor μ [-] quantifies how much slower diffusive vapor transport in a material is, compared to in air
v
a
δδµ =
with δa [s] the vapor permeability of air δv [s] the vapor permeability of the material
by definition, 1 ≤ μ < +∞
or N
av µµ
δδ 1==
49
vapor diffusion in materials material vapor resistance factor [-]
Brick 10-20
Concrete 100
Glass +∞
Gypsum board 12
Metal +∞
Mineral wool 1.5
Natural stone (sandstone) 15
Polymer >10000
Plastic foam >30
Wood (pine) 50
porous materials are more vapor open
50
vapor diffusion in materials
• the (vapor) diffusion resistance 𝑍𝑍 [m/s] was defined as
• 𝑍𝑍 is –literally– the resistance against diffusion • the higher 𝑍𝑍, the smaller the vapor flux
through the material for a given difference in partial vapor pressure
dNddZav
µδµ
δ===
51
wall ii
Z Z= ∑
vapor diffusion in materials
• material documentation – for most materials, documentation specifies the
vapor permeability δv [s] or the vapor resistance factor μ [-]
– for some materials, especially foils, it is hard to measure the thickness. For those materials, the diffusion thickness μd [m] is specified.
from any of these, the diffusion resistance Z [m/s] can be calculated
52
vapor diffusion in materials
• mass flow rate 𝐺𝐺𝑣𝑣,1
𝜙𝜙→2
[kg/s] through a layer of
open porous material from location 1 to 2:
with 𝐾𝐾𝑣𝑣𝜙𝜙 = 1
𝑍𝑍⁄ [s/m] the vapor permeance, and 𝐴𝐴 [m2] the frontal area of the open porous layer
53
𝑝𝑝𝑣𝑣,1 𝑝𝑝𝑣𝑣,2 𝐺𝐺𝑣𝑣,1
𝜙𝜙→2
𝐺𝐺𝑣𝑣,1
𝜙𝜙→2
= 𝐾𝐾𝑣𝑣𝜙𝜙𝐴𝐴 𝑝𝑝𝑣𝑣,1 − 𝑝𝑝𝑣𝑣,2
Always use same convention: Draw flow rate from point 1 -> 2 Write flow rate as 𝑝𝑝𝑣𝑣,1 − 𝑝𝑝𝑣𝑣,2
( ) vvv pAKG ∆= φ
To remember
• in air layer
• in porous layer
• in joints
• in holes
( ) vavv pAKG ∆= with 𝐾𝐾𝑣𝑣𝑠𝑠 [s/m] the vapor permeance
and 𝐴𝐴 [m2] the area of the layer
( ) vvv pLKG ∆= ψ
( ) vvv pnKG ∆= χ
with 𝐾𝐾𝑣𝑣𝜓𝜓 [s] the vapor permeance
and 𝐿𝐿 [m] the length of the joint
with 𝐾𝐾𝑣𝑣𝜒𝜒 [m.s] the vapor permeance
and 𝑛𝑛 [-] the number of holes
54
with 𝐾𝐾𝑣𝑣𝜙𝜙 [s/m] the vapor permeance
and 𝐴𝐴 [m2] the area of the layer
• Flow rate
• Vapour resistance – permeance
( ) ( ),1 ,2,1 2 ,1 ,2
v vv v v v
A p pG K A p p
Zφ
−
−= − =
To remember
55
1
v v a
d dZ N dKϕ
µ µδ δ
= = = =
Always use same convention Draw flow rate Gv,1-2 from point 1→2 Write pressure difference as (pv,1-pv,2)
9 -11 5 10 sa
Nδ
= ≈ ⋅v
a
δδµ =
• Mass balance example – Draw all flow rates towards point of interest
( ) ( ) ( )1 ,1 ,i 2 ,2 ,i 3 ,3 ,i
1 2 3
0v v v v v vA p p A p p A p pZ Z Z− − −
+ + =
To remember
56
,1vp ,2vp
,3vp
,ivp
,1 ,2 ,3 0v i v i v iG G G− − −+ + =
57
Exercises next week
• Bring slides / book / calculator or laptop
Additional exercises Vapour - part 1
58
Exercise 2: Vapour resistance • A wall consists of two material layers (from inside to outside):
– layer 1 has thickness d = 0.115 m and vapor resistance factor µ = 4 – layer 2 has thickness d = 0.50 m and vapor resistance factor µ = 2
• What is the vapour permeance Kv
φ of the wall (in s/m) (N = 5.0x109 s-1)
• What is the total vapour flux through this wall (in kg/(m2s)) for following vapor pressures at the interior and exterior: – pv,i = 2100 Pa and pv,e = 600 Pa
• What is the vapor pressure (in Pa) at the interface between layer 1 and
2?
(Hint: gv is constant throughout wall so gv,i->e =gv,i->interface
59
101.37 10vsKm
φ −= ×
722.05 10v
kggm s
−= ×
,interface 1627vp Pa=
Exercise 3: Retrofitting basement
• A basement is transformed into a disco. Above the basement, there is a heated space. Due to the new room purpose, the air temperature and RH in the basement will increase. To avoid surface condensation, the basement wall was retrofitted with insulation.
– Air temperature 25°C – Soil temperature 12°C – Relative humidity 80% – Heat transfer coefficient 8 W/m2K
60 Original basement wall (at soil temperature)
Insulation d = 80 mm λ = 0.2 W/mK
Mortar d = 35 mm λ = 0.7 W/mK
Exercise 3: Retrofitting basement
• Calculate the surface temperature on the inner surface with and without insulation.
• Is retrofitting necessary and sufficient to avoid surface condensation (calculate!)?
61 Original basement wall (at soil temperature)
Insulation d = 80 mm λ = 0.2 W/mK
Mortar d = 35 mm λ = 0.7 W/mK
θs,i,without-insul = 15.7 °C θs,i,with-insul = 22.2 °C
Yes, retrofitting is necessary