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Taken from the magazine Heating, Ventilation, Sanitation, Issued by the
Society of Environmental Engineering, Representative of the Czech Republic in
REHVA.
The DHW
heating curve Q2
depends on the hot water consumption VDHW over time t. The heat supply curve for DHW Q1 is dependent on the heat
supply from the heat source in the same time interval. Important prerequisites
for compiling the curves above are the following two necessary points:
1. The heat supply curve Q1 is always above the heat demand curve Q2,
2. The heat supplied by the hot water heater is
equal to the heat removed from the heater Q1p = Q2p.
Figure 1.
Example of heat supply and demand curves for DHW heating with different time
intervals of heat sources: Q1* – heat sources with
continuous operation and storage tank; Q1** – heat
sources with intermittent operation and storage tank; Q1***
– heat sources with sufficient output that are continuously controlled
according to the domestic hot water consumption without a storage tank
(flow-through heating).
The heat
supply curve must always be above the heat demand curve, otherwise there will
be a lack of energy to heat the water to the desired temperature, so that the
water temperature at the sampling point does not have the required temperature
(55°C). The delivery and heat consumption curves are not decreasing with
increasing time, as they are in principle cumulative curves that add up to
individual times of the energy supplied or withdrawn from the DHW preparation
system. The inclination of the tangent to these curves to the timeline
represents the value of instantaneous heat output. At zero power, the waveform
is horizontal with the x-axis, with the maximum curve slope being the assumed
heat output of the maximum P2max
(see Figure 1).
The volume
of the hot water tank is determined from the maximum difference between the
heat supply and demand curves as:
[l] | (1) |
In the case
of designing a DHW system with storage (DHW tank), the heat supply curve Q1 can be constructed in two
basic variants. The first case occurs when we assume that the heat supply to
the DHW cylinder is constant over a period of time (Figure 2).
This means that the heat source heats the DHW throughout the heating time
(typically 1 day). The second case occurs when we think that we will use the
heat in the tank from the previous warm water heating period, and the heat
supply will be shorter than the DHW period (Figure 2).
Figure 2.
Heat demand and supply curves with uninterrupted heat supply to the DHW storage
tank.
For heating
with a reservoir, the required heat output of the heat source is determined as:
[kW] | (2) |
where the
ratio (DQs/τ)max represents the maximum inclination of
the tangent to the time axis.
In the case
of permanent heat supply from the hot water heater during the whole period (Figure
2), DQs = Q1. In the case of intermittent operation in several
different time phases of one warming period, the maximum value is considered
for the calculation according to (2). It follows, from the above procedure,
that for a shorter supply of heat from the source to the DHW storage tank, it
is necessary to design a larger tank volume, but at the same time require a
higher heat output of the heat source than the permanent supply of heat to the
tank during the entire hot water collection period (Figure 3).
Thus, if we have a sufficiently large heat source with continuous heat output
regulation, it would be possible to design the DHW heating system without a reservoir,
i.e., in a flow-through manner.
Figure 3.
Heat demand and supply curves with heat supply to the DHW storage tank
distributed over time.
The most
common mistakes in designing the size of the DHW storage with the heat supply
and delivery curve method are the options for constructing the heat supply
curve Q1. The first
mistake is, if the designer is trying lean towards the design security side,
this then results in a significant increase in the size of the DHW storage
tank. The second mistake occurs when the possibility of changing the heat
demand curve in the non-standard behaviour of the user is not taken into account, resulting in an insufficient amount of
prepared DHW.
A typical
example of the underestimation of the heat supply curve Q1 is shown in Figure 4. The
purpose of such a design is to minimise the size of the DHW storage tank as
much as possible by copying the heat demand curve. However, if the DHW
production is increased during the DHW preparation period (one day, in this
example), this DHW set-up system will not be able to deliver enough DHW. A more
appropriate design of the same example is shown in Figure 5.
The principle of the correct design is not to create the smallest DHW tank
(i.e., the minimum difference between the heat supply and demand curve), but to
create sufficient storage space for possible non-standard DHW use. Measurements
in apartment buildings indicate that at least a 15% increase in the heat demand
over a sampling curve is required for the heat supply curve. If a significant
morning peak is expected, and if the heat source is also used for other
technologies (heating, air conditioning, etc.), it is possible to cover the
increase in the DHW consumption in the morning hours by increasing the volume
of the tank proportionally enough to allow for a longer period of time that
does not require heat to be supplied to the DHW system.
For the
examples in Figures 4 and 5, it is
interesting to compare the size of the calculated DHW storage tank and heat
demand of the heat source. The results in Table 1,
respectively Table 2 show that a heat source, for both examples,
will be required with a power of 30 kW, based on the percent ratio of the
heat to the y-axis in the graphs in Figures 4 and 5,
where 1% = 1 kWh (2). On the other hand, the storage tank is about 250
litres and about 480 litres with respect to the size of the DHW storage tank in
the example of Figure 4 and Figure 5,
respectively (1).
Figure 4
Heat demand and supply curves for an inadequately chosen charging regime of the
DHW storage tank.
Figure 5
Heat demand and supply curves with the optimised charging of the DHW storage
tank
From the
solution shown in Figure 5 it can be seen that stagnation
of the heat demand for the DHW between 8.00 and 16.20 can be expected, which is
the possibility of using the heat source for other purposes (technology) than
just DHW preparation. However, for the solution of Figure 5,
it is still necessary to include in the overall energy and cost balance of the
proposed system, both in the increase in the static heat loss of the DHW tank
and the financial costs associated with the acquisition of a larger DHW tank.
Table 1.
Sizing of the DHW storage tank and heat source according to the example in Figure 4.
Charging time | Required volume of the DHW storage VDHW [l] | The rated heating power of the DHW P1n [kW] |
6:00 to 7:00 | It is not critical for the maximum difference | 30.0 |
7:00 to 9:00 | It is not critical for the maximum difference | 7.5 |
14:00 to 14:30 | 248.4 | 20.0 |
20:00 to 22:00 | It is not critical for the maximum difference | 22.5 |
Table 2.
Sizing of the DHW storage tank and heat source according to the example in Figure 5.
Charging time | Required volume of the DHW storage VDHW [l] | The rated heating power of the DHW P1n [kW] |
6:00 to 8:00 | 477.7 | 27.5 |
16:30 to 16:50 | It is not critical for the maximum difference | 30.0 |
20:00 to 21:30 | It is not critical for the maximum difference | 23.3 |
The
advantage of preferential hot water heating is the possibility of using the
maximum heat output of the heat source, which is primarily designed for e.g.,
the heating system. If the DHW is taken from the storage tank, the water temperature
in the tDHW
tank will drop. Upon reaching the water switching temperature DHWVmin,
the heat source control preferably provides heat supply to heat the DHW. In the
case of the hydraulic connection shown in Figure 6, this
means that the heating system circulation pump is switched off and the
three-way switching valve in the direction of charging the DHW storage tank
switches. At the same time, the heat source increases the boiler water
temperature (usually a fully rated output to a maximum output temperature,
e.g., up to 80°C), and the control switches the DHW tank charging pump. When
the water temperature in the tank reaches the set (required) value, the control
switches the entire system back into the heating mode. It is, therefore,
obvious that the greater the switching difference (ΔtDHW = tDHW
– tDHWspin),
the longer the time it is to charge the tank. Switching differences are usually
selected at 5 K or 10 K depending on the type of DHW storage tank. However, the
time required to heat up the DHW tank should not be too long to interfere with
the thermal comfort in the heated area during the heat supply interruption to
the heating system. e.g., for light buildings with minimal heat accumulation,
the time required to heat the waterta
in the DHW tank should not exceed 10 minutes. For moderate and heavy buildings
with masonry storage capacity, the reheat timeta should not be longer than 20
minutes.
In order
for the above principle to work, it is necessary to meet the basic assumption that
the heat output of the boiler Qk is greater than or equal to the required power
for the preparation of the DHW QDHW. And at this point, the designer sometimes
underestimates it. If we realise the different requirements for the function of
e.g., a low-potential heat source in a passive house, it is clear that the
heating requirements will differ considerably from the requirements for the
preparation of the DHW, not only with regard to the required thermal output,
but also with regard to the time of use of the source heat. These different
requirements make it necessary to adapt the design of the DHW storage tank.
Figure 6.
Example of a heat source connection in a system with priority domestic hot
water preparation: PHS – circulation pump of the
heating system; PDHW – DHW storage tank pump; EV –
expansion vessel; B – boiler; TS – remote control with internal temperature
sensor; SV – safety valve; 3V – three-way switching valve; VDHW – domestic hot water storage tank; to – outdoor temperature; ti – indoor temperature; tB – boiler water temperature; tDHW – water temperature in the domestic hot water
storage tank.
For
residential buildings, indirectly heated containers with an integrated
exchanger are most commonly used. They work on the principle of natural
buoyancy, i.e., the contents of the storage tank are heated from the bottom up.
With these systems, it is quite problematic to ensure that the entire volume of
the DHW tank is fully heated to the desired temperature. In order to calculate
the actual usable content of the container, it is expedient to include the
so-called correction factor y (Table 3)
in the calculation, which is used in German standards (e.g., DIN 4708 [5]).
Table 3.
Correction factor of heat consumption from the DHW storage tank [5]
Hot water tank | y [-] | |
t a < 20 minutes | ta < 10 minutes | |
Vertical
storage | 0.94 | 0.89 |
Horizontal
storage (up to | 0.96 | 0.91 |
Horizontal
storage (over | 0.90 | 0.85 |
The basic equation
for calculating the required warming time ta, or the size of the DHW tank volume, is the
heat supply balance of a given volume of liquid per unit time at a known
temperature difference in the form:
[W] | (3) |
The basic example
is a family house inhabited by 4 persons, with 5+1 disposition (kitchen = sink,
two bathrooms = 3x sinks, 2x showers, 1x bath). You can ignore the amount of
DHW sampling for all the sinks. From the point of view of the water supply
design values, the maximum hot water flow rate is 0.4 l/s = 24 l/min
for the bath and 0.2 l/s = 12 l/min for the shower. From the point of
mixing hot and cold water in the outflow battery, when showering and bathing is
the most common, with a mixing water temperature of between 38-40°C, the design
flow of hot water in these batteries is about 6 l/min. It means that, in a
sample family house with simultaneous bathing (running bath) and showering, it
is possible to consider the maximum flow of hot water of 12 l/min = 720 l/h.
Higher water flow rates are not designed for the water pipe.
The
“maximum” water flow rate with the simultaneous use of the shower and bathtub
is important in relation to the heat transfer capability in the heat exchanger
of the selected DHW storage tank. e.g., a 65-litre specific H65W cylinder has a
hot water flow of 438 l/h at temperature t2 = 45°C at a heat output of 18 kW on the primary
side of the heat exchanger (i.e., on the heat source side). In other words, its
steady production of hot water at 45°C, at the cold water at the inlet to the
tank of 10°C, is 438 l/h. In addition, for example, with another 120-litre
hot water tank S 120/5, the manufacturer reports a steady flow of hot water of
834 l/h at 34kW (at tK= 80°C, t2 = 45°C, t1=
10°C). Thus, if an extreme situation arises when the volume of the DHW storage
tank is depleted from previous DHW demands (i.e., tDHW = tDHWspin)
and, at the same time, the supply of heat for the collection of DHW in the form
of bathing and showering is required, it would be necessary to ensure that
requesting a heat source with a heat output of about 28 kW (based on the
flow rate of a bath and shower in the total of 720 l/h, considering the
heat exchanger surface of the exchanger in the S 120/5). This is a short, top-of-the-range
sampling of 10 to 15 minutes, but it is clear that in a classical family house,
such a heat source is not found today. Therefore, it is more appropriate to take into account the requirements of the sanitary
installation and the size of the designed reservoir to adapt these facts to the
heat source. In addition, it is clear that with the increasing number of
inhabitants (supply points) the calculation flow needs to be corrected and it
is appropriate to expect a higher proportion of discontinuity in the hot water
consumption.
Also, in
this method of preparing the DHW, setting the switching differential of the DHW
tank charger remains unavoidable in relation to the position of the sensor in
the tank (Figure 6). In the case of vertical storage, the
temperature sensor that controls the switching process of the DHW storage tank
is usually positioned from the middle of the tank up to 2/3 of the tank height.
If the sensor is placed too high (i.e., too close to the DHW outlet to the
water pipe system), a later reaction and a significant delay in charging the
DHW tank may occur, when almost the entire volume of the tank will be depleted,
and before the desired DHW temperature is reached again, the DHW temperature
drops during the DHW demand. Conversely, in cases where the sensor is located
too low (i.e., too close to the heat exchanger surface of the DHW), the heat
source can be switched frequently even with the smallest DHW consumption,
regardless of the actual desired amount of DHW taken.
Therefore,
it can be seen from the examples that although the design methods of the DHW
design can appear simple in principle, it is important to understand the link
to other professions as well. The connection is mainly related to the
profession of heating and sanitary installations in the water supply section.
The marginal conditions of the hot water system design can be summarised as
follows:
·
total
DHW demand - per unit of measurement (person, bed, shower, etc.),
·
knowledge
of the heat collection process - time distribution of the DHW in the object,
·
temperature
level of heat source for the DHW preparation,
·
heat
source operation requirements - time intervals of operation of other
technologies,
·
heat
transfer capacity of the DHW tank,
·
water
flow on drain valves.
List of nomenclature |
c specific heat capacity of water [J/(kg·K)] P1n rated heating power of the DHW [kW] P2max maximum heat output for the DHW [kW] Q1 heat supplied by the heater to the DHW [kWh] Q1p heat delivered by the heater to the DHW during the period [kWh] Q2 heat removed by the heater in the DHW [kWh] Q2p heat removed by the heater in the DHW during the period [kWh] Q2z heat lost during heating and DHW distribution during the period [kWh] Qk boiler heat output (for a common heat source for the DHW preparation) [W] QDHW heat output required to prepare the DHW [W] t1 cold water temperature [°C] t2 hot water temperature [°C] tk boiler water temperature [°C] tDHW water temperature in DHW tank [°C] tDHWspin water switching temperature in the DHW tank [°C] VDHW DHW storage volume [m³] y correction factor of heat removal from the DHW tank [-] DQmax maximum possible heat difference between Q1 and Q2 [kWh] DQs heat supplied by the heater to the DHW at time t [kWh] DtDHW switching differential for DHW heating (usually 5 to 10 K) [K] ρ density of water at medium storage temperature [kg/m³] t heat delivery time by the DHW heater [h] ta DHW retention time at the temperature difference DtDHW [s] |
The author
would like to thank Ing. Stanislav Toman for
reviewing this article.
The
labelling of some of the quantities in the article (e.g., P
power, t temperature) respects the closer and more,
used Czech habits in Latin characters, as opposed to ČSN 06 0320 (2006),
which uses the Greek alphabet (Fpower, Q temperature).
VAVŘIČKA,
R. Nejčastějšíchybypřinávrhuzásobníkuteplévody. In. Vytápění, větrání,
instalace. 2018, Vol. 27, Issue 1, pp.
16-20. ISSN 1210-1389.
[1] VAVŘIČKA, R., et al. Hot Water
Preparation.
Design Book No. 3. (in Czech).STP. Praha 2017, 182 p. ISBN 978-80-02-02713-3.
[2] ČÍHAL,
Z. Preparation of the TV and "non-hooking" of the object. (in Czech)
In. Topenářství, instalace. 2016. roč.
50, č. 5, s. 58–62. ISSN 1211-0906.
[3] ČSN EN 806-1. Vnitřnívodovod pro rozvodyvodyurčené k lidskéspotřebě – Část 1: Všeobecně. ČNI, 2002.
[4] ČSN 75 5409. Vnitřnívodovody. ÚNMZ, 2013.
[5] DIN
4708 – Zentrale Wassererwärmungsanlagen, 1994. Part 1 – Begriffe und
Berechnungsgrundlagen. Part 2 – Regeln zur Ermittlung des Wärmebedarfs zur
Erwärmung von Trinkwasser in Wohngebäuden. Part 3 – RegelnzurLeistungsprüfung
von WassererwärmernfürWohngebäude.
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