[0001] This invention relates to a gas-fired central-heating (CH) boiler with a provision
for supplying hot sanitary water, according to the preamble of claim 1. Such a boiler
is known from FR-A-2672113.
[0002] Such so-called combined boilers are well known and comprise a gas burner, a heat
exchanger arranged in the path of the flue gases and included in a closed CH water
circuit with a delivery pipe to radiators or other space heating elements and a return
pipe, the sanitary water provision being adapted for the indirect uptake, by way of
the heated CH water, of heat generated by the burner.
[0003] With regard to the manner of heating the sanitary water, a distinction is made between
the through-flow principle and the storage principle. In a combined boiler according
to the through-flow principle, a sanitary water coil, connected at one end to the
water mains and at whose other end hot water can be tapped for household use, extends
through a vessel entirely filled with water from the closed CH water circuit. With
a combined boiler according to the storage principle, an amount of water for household
use is stored in a vessel through which extends a coil-shaped part of the delivery
CH water pipe.
[0004] In both cases, sanitary water is indirectly heated by CH water heated in the heat
exchanger of the boiler.
[0005] The present invention concerns a combined boiler according to the storage principle.
In combined boilers, the supply of hot sanitary water takes priority over the space
heating function, i.e. upon a demand for sanitary water, the circulation of heated
CH water is short-circuited over the CH water coil in the storage vessel, so that
the heat produced by the burner is exclusively used for the benefit of sanitary water.
Upon a demand for space heating, however, heated CH water always flows through the
storage vessel. This makes it impossible to prevent a situation where, in winter for
instance, when in the morning the temperature in the house is to be raised from 15°
to 20° and the heat demand on the CH installation persists for a long period, too
much heat is supplied to the sanitary water supply, i.e. the temperature in the storage
vessel exceeds the set value (60-80°C). This leads to the switch-off of the burner
and stagnation of the space heating process.
[0006] The object of the present invention is to provide a combined boiler which does not
have this drawback. A boiler according to the invention is characterized by the characterizing
part of claim 1. The invention is based on the insight that if the burner is switched
off by the thermostat of the sanitary water vessel, at least as long as the circulation
pump works, CH water that no longer receives heat from the boiler heat exchanger can
draw heat from the storage vessel functioning as a heat accumulator, until the temperature
in the storage vessel has fallen to the extent where where the burner is switched
on again.
[0007] It is true that this also occurs in known combined boilers according to the storage
principle, where a coil forms part of the CH water supply to radators, but it occurs
in a little effective manner. The fact is a coil-shaped pipe section through which
flows a large amount of CH water of a temperature of, for instance, 80-90°C, may be
sufficient for bringing a relatively small amount of samitary water in the storage
vessel to a temperature of 60°C, but, conversely, the amount of heat that can be drawn
from the sanitary water in the storage vessel is inadequate for an effective heat
transfer by way of the coil to the much larger amount of CH water flowing through.
[0008] The effect contemplated, viz. the transfer of heat accumulated in the storage vessel
filled with sanitary water, to a sufficient extent to meet the demand for space heating
as long as the burner is switched off by the thermostat of the storage vessel, can
be realized in that, in a combined boiler which is equipped with a burner and a heat
exchanger for transferring heat of flue gases to CH water (CH heat exchanger), as
well as with a storage vessel for sanitary water, according to the invention, the
CH heat exchanger is at least partly immersed in sanitary water and is adapted for
direct heat exchange between passing flue gases, passing CH water and sanitary water
in the storage vessel.
[0009] The most important improvement over the prior art achieved through these features
is that heat transfer from flue gas to sanitary water and to CH water takes place
directly in the same heat exchanger, which, by virtue of the greater heat-transfer
capacity present, can take place more effectively than indirectly by way of CH water
being passed through a coil in a storage vessel.
[0010] Further, it is an advantage that, using the same heat exchanger, sanitary water can
be rapidly heated, directly by flue gas, and thereby the contents of the storage vessel
can be better maintained at the required temperature. Also, in the off-condition of
the burner, heat can be better transferred from the sanitary water to CH water.
[0011] In further elaboration of the invention, in order to ensure a good heat transfer
from flue gases both to the CH water and to sanitary water, the heat exchanger may
comprise a flue gas passage bounded on one side by a CH water channel and on the other
by a wall portion in direct contact with sanitary water present in the storage vessel,
this wall portion being at least locally in heat-transmissive contact with the CH
water passage.
[0012] In further elaboration of the invention, the heat-transmissive contact between the
wall portion in contact with sanitary water on the one hand and the CH water channel
on the other can be provided by heating surface-enlarging elements which extend in
the flue gas passage and are in direct communication both with a CH water passage
and with the wall portion referred to.
[0013] When the burner is in operation, hot flue gases flow along the heating surface-enlarging
elements and heat is transferred both to CH water flowing through the water passage
and to sanitary water present on the other side of the wall portion referred to.
[0014] Thus a demand for space heating can be met while at the same time sanitary water
in the storage vessel is maintained at the required temperature. Upon a demand for
sanitary water, as soon as the temperature in the storage vessel has fallen below
a set value, the CH water circuit is short-circuited, so that all of the heat produced
by the burner is used for the benefit of the sanitary water.
[0015] If, however, the demand for CH water persists for a long time, whereby the flue gases
produced by the burner give off heat not only to the CH water but at the same time
to the sanitary water in the storage vessel as well, so that the temperature in that
vessel exceeds the set maximum value, the burner is switched off. Then the CH water
flowing through the heat exchanger can for some time withdraw heat from the sanitary
water vessel by way of the heating surface-enlarging elements referred to, until the
temperature of the sanitary water vessel has decreased to the extent where the burner
switches on again.
[0016] When a demand for space heating arises only after a long period of time, it may even
suffice initially to operate exclusively the circulation pump of the CH system, allowing
CH water to withdraw heat from the sanitary water in the storage vessel, until the
temperature thereof has fallen to the point where the burner switches on and both
CH water and sanitary water are heated by flue gases.
[0017] In a preferred embodiment of the invention, the heat exchanger, made from light metal,
may form part of a premix gas/air burner in a housing with a sidewall and a closed
end wall, the burner being arrranged centrally within the sidewall with the combustion
space facing the end wall, the flue gas duct, in which extend the heating surface-enlarging
elements, being bounded by the above-mentioned sidewall of the housing and the CH
water passage arranged substantially coaxially between the burner and the sidewall.
[0018] In this way a burner/heat exchanger unit is obtained which has a housing part, bounded
by a closed end wall, extending only partly into a storage vessel for sanitary water,
i.e. only that portion of the housing where the combustion chamber is located and
the flue gases have their highest temperature, is located within the storage vessel,
and the part of the housing where the flue gases leave the housing is located outside
the storage vessel. In the part of the housing located outside the storage vessel,
egressing flue gases can no longer be heated by hot water in the storage vessel and
they move in countercurrent with return CH water flowing in the water passage. In
the process, the flue gases can give off their residual heat to the return CH water
and be cooled to 60-70°C. The part of the burner/heat exchanger unit located outside
the storage vessel thus operates as an economizer in that the flue gases present therein
condense, thereby further giving off heat, and the boiler can therefore be qualified
as a High-Efficiency boiler.
[0019] Depending on the depth to which the housing is inserted into the storage vessel,
the capacity of the boiler can be varied form 5 kW to 25 kW. This means that with
a single appliance, the greater part of the market with regard to households can be
covered.
[0020] The boiler according to the invention can be manufactured in similar sizes to known
combined boilers of the storage principle, at lower cost and providing more convenience
in use than comparable combined boilers. In fact, by virtue of the direct heating
of the sanitary water in the storage vessel by the flue gases, a more rapid heating
can be obtained, so that sanitary water is practically always available. Further,
the burner may be made of modulating design.
[0021] To clarify the invention, one exemplary embodiment of the High-Efficiency combined
boiler will be described with reference to the accompanying drawings.
Fig. 1 is a diagrammatic longitudinal elevation of the boiler;
Fig. 1A shows the course of the water in the CH water passage in the heat exchanger
according to Fig. 1; and
Fig. 2 shows an exemplary embodiment of a control diagram of the boiler according
to Fig. 1.
[0022] According to the drawings, in particular Fig. 1, a burner/heat exchanger assembly
1 extends partly into a storage vessel 2 for sanitary water. The depth of insertion
is variable, i.e. the assembly 1 projects outside the vessel 2 over a variable distance
a.
[0023] The vessel 2 comprises an inlet 3 for cold sanitary water S and a tap 4 for hot sanitary
water. Indicated by 5 is a sensor having the function of a maximum-thermostat, control
thermostat and priority thermostat.
[0024] The burner/heat exchanger assembly 1 comprises a housing, for instance cylindrical,
with a sidewall 6 and a closed end wall 7. Arranged substantially coaxially within
the housing 6, 7 are a burner 8 with a combustion chamber 9 and a CH water passage
10 with an inlet 11 for return CH water and a discharge 12 for heated CH water, connected
with a space heater, such as a radiator 13 (see Fig. 2).
[0025] The burner 8 is of the premix type, with a mixing chamber 14 which is supplied with
air by a fan 15 and with gas through a pipe 16.
[0026] The CH water passage 10, together with the sidewall 6 of the housing 6, 7, bounds
a flue gas duct 17 communicating with the combustion chamber 9 near the closed end
wall 7 of the housing 6, 7. The flue gas passage 17 ends in a discharge 18, connectible
to, for instance, a flue.
[0027] The course of the water in the CH water passage 10 is indicated diagrammatically
in Fig. 1A, i.e. return CH water enters at 11 and flows upwards following an interrupted
helical path to a discharge 12 extending straight down.
[0028] The CH water passage 10 is directly connected with the housing sidewall 6 through
heating surface-enlarging projections 19 extending transversly through the flue gas
duct 17.
[0029] The combined boiler operates as follows:
[0030] The storage vessel 2, made of stainless steel or enamelled on the inside in view
of the storage of drinking water, is filled by way of the inlet 3 and supplemented
when hot water is withdrawn from the vessel through the tap 4.
[0031] Flue gas flows from the combustion chamber 9 along the inside of the housing end
wall 7 into the flue gas duct 17 to the discharge 18. In the process, the flue gas,
which may have a temperature of 1400°C in the combustion chamber 9, gives off heat
directly to the light metal-cast CH water passage 10 and to the housing sidewall 6,
and indirectly by way of the projections 19. Thus the CH water flowing in the passage
10 substantially in countercurrent with the flue gases, as well as the sanitary water
S in the vessel 2 are heated. In the process, the housing sidewall 6 will assume a
temperature 10-15°C higher than the temperature of the sanitary water in the vessel
2. Before leaving the unit 1, flue gas flows through the part of the housing where
the mixing chamber 14 of the burner is located and the part of the housing which projects
outside the vessel 2 over a distance
a. In the last-mentioned paths, the flue gas is further cooled through heat release
to combustible mixture in the mixing chamber and to incoming return CH water which
only has a temperature of about 20°C, so that the flue gas entering the flue has only
a temperature of about 60°C. In this last path, the flue gases condense, so that condensation
heat is used as well, which makes the boiler a High-Efficiency boiler.
[0032] When upon prolonged demand for space heating - whereby the burner is in operation
for a long time and during that time gives off heat not only to the CH water but also
to sanitary water in the vessel 2 - the temperature in the vessel 2 may rise to such
an extent that the burner is switched off by the maximum thermostat sensor 5.
[0033] Outgoing CH water can nevertheless be heated, viz. by transfer, through the projections
19, of accumulated heat from the vessel 2, until the temperature in the vessel 2 has
fallen to the extent where the sensor 5 controls the ignition of the burner.
[0034] As shown in Fig. 2, the combined boiler 1 may be equipped with a standard circulation
pump 20, a standard DC fan 15 and a standard three-way valve 21 for short-circuiting
the CH circuit. Instead of using a three-way valve, it is also possible to switch
the pump 20 in the case where the radiators in a space to be heated are provided with
thermostat valves.
[0035] Included in the gas supply duct 12 is a gas valve 22 suitable for use with an electrical
(spark or heater plug) ignition.
[0036] The pump can be driven so as to continue operating for a specified time after switch-off.
[0037] Three NTCs (resistive temperature sensors) 23 or other thermostats provide for the
observation of the temperature, on the basis of which the maximum-limitation is implemented,
the control thermostat is controlled, the preferred control for hot sanitary water
and similar functions are controlled.
1. A combined boiler, which is equipped with a burner (8) and a heat exchanger (10,19,6)
for transferring heat of flue gases to central-heating (CH) water, and with a storage
vessel (2) for sanitary water (S), wherein the heat exchanger (10,19,6) is at least
partly immersed in sanitary water (S) and is adapted for direct heat exchange between
through-flowing flue gases, through-flowing CH water, and sanitary water in the storage
vessel (2), characterized in that the burner (8) and the heat exchanger (10,19,6)
are combined in an assembly (1) which enters the storage vessel (2) from one side,
whereby in use the flue gases leave the assembly near the side from which the assembly
is entered in the vessel.
2. A boiler according to claim 1, characterized in that the heat exchanger (10, 19, 6)
comprises a flue gas passage (17) which is bounded on one side by a CH water channel
(10) and on the other by a wall portion (6) which is in direct contact with sanitary
water (S) present in the storage vessel (2), said wall portion being at least locally
in heat-transmissive contact with the CH water channel (10).
3. A boiler according to claim 2, characterized in that heating surface-enlarging elements
(19) extend in the flue gas passage (17) and are in direct communication both with
a CH water passage (10) and with said wall portion (6).
4. A boiler according to claim 3, characterized in that the heat exchanger (10, 19, 6),
made of light metal, forms part of a premix gas/air burner (8) in a housing (6, 7)
with a sidewall (6) and a closed end wall (7), the burner (8) being arranged centrally
within the sidewall (6) with the combustion space (9) facing the end wall (7), the
flue gas duct (17) in which extend the heating surface-enlarging elements (19) being
bounded by said sidewall (6) of the housing (6, 7) and the CH water passage (10) arranged
substantially coaxially between the burner (8) and the sidewall (6).
5. A boiler according to any one of the preceeding claims, characterized in that the
depth to which the assembly (1) is inserted into the storage vessel (2) is adjustable,
such that the capacity of the boiler can be varied.
1. Kombinierter Kessel, der mit einem Brenner (8) und einem Wärmeaustauscher (10, 19,
6) zum Übertragen von Wärme von Verbrennungsgasen an Wasser einer Zentralheizung (CH)
und mit einem Speicherkessel (2) für Sanitärwasser (S) ausgestattet ist, wobei der
Wärmeaustauscher (10, 19, 6) zumindest teilweise in Sanitärwasser (S) eingetaucht
ist und für einen direkten Wärmeaustausch zwischen hindurchströmenden Verbrennungsgasen,
hindurchströmendem CH-Wasser und Sanitärwasser in dem Speicherkessel (2) angepaßt
ist,
dadurch gekennzeichnet, daß
der Brenner (8) und der Wärmeaustauscher (10, 19, 6) in einer Baueinheit (1) kombiniert
sind, welche in den Speicherkessel (2) von einer Seite eintritt, wodurch die Verbrennungsgase
die Baueinheit bei Gebrauch in der Nähe der Seite verlassen, von der die Baueinheit
in den Kessel eingesetzt wird.
2. Kessel gemäß Anspruch 1, dadurch gekennzeichnet, daß der Wärmeaustauscher (10, 19,
6) einen Durchgang (17) für das Verbrennungsgas aufweist, der auf einer Seite durch
einen CH-Wasserkanal (10) und auf der anderen Seite durch einen Wandabschnitt (6)
begrenzt wird, der mit dem in dem Speicherkessel (2) befindlichen Sanitärwasser (S)
in direktem Kontakt steht, wobei der Wandabschnitt zumindest lokal in Wärmeübergangs-Kontakt
mit dem CH-Wasserkanal (10) steht.
3. Kessel gemäß Anspruch 2, dadurch gekennzeichnet, daß Heizflächen vergrößernde Elemente
(19) in den Durchgang (17) für das Verbrennungsgas ragen und in direkter Verbindung
sowohl mit einem CH-Wasserdurchgang (10) und mit dem Wandabschnitt (6) stehen.
4. Kessel gemäß Anspruch 3, dadurch gekennzeichnet, daß der aus Leichtmetall hergestellte
Wärmeaustauscher (10, 19, 6) einen Teil eines Gas/Luftbrenners (8) mit Vormischung
in einem Gehäuse (6, 7) mit einer Seitenwand (6) und einer geschlossenen Endwand (7)
bildet, wobei der Brenner (8) zentral innerhalb der Seitenwand (6) mit dem der Endwand
(7) gegenüberliegenden Verbrennungsraum (9) angeordnet ist, die Leitung (17) für das
Verbrennungsgas, in welche die die Heizflächen vergrößernden Elemente (19) ragen,
durch die Seitenwand (6) des Gehäuses (6, 7) begrenzt wird und wobei der CH-Wasserdurchgang
(10) im wesentlichen koaxial zwischen dem Brenner (8) und der Seitenwand (6) angeordnet
ist.
5. Kessel gemäß einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß die Tiefe,
bis zu der die Baueinheit (1) in den Speicherkessel (2) eingesetzt wird, einstellbar
ist, so daß die Kapazität des Kessels verändert werden kann.
1. Une chaudière combinée ou mixte, qui est équipée d'un brûleur (8) et d'un échangeur
de chaleur (10, 19, 6) pour transférer la chaleur de gaz brûlés à de l'eau de chauffage
central (CH), et d'un récipient de stockage (2) pour de l'eau sanitaire (S), dans
laquelle l'échangeur de chaleur (10, 19, 6) est au moins partiellement immergé dans
l'eau sanitaire (S) et est apte à l'échange de chaleur direct entre les gaz brûlés
s'écoulant à travers, l'eau de chauffage central s'écoulant à travers, et l'eau sanitaire
dans le récipient de stockage (2), caractérisée en ce que le brûleur (8) et l'échangeur
de chaleur (10, 19, 6) sont combinés en un ensemble (1) qui pénètre dans le récipient
de stockage (2) d'un côté, de telle manière qu'en service les gaz brûlés quittent
l'ensemble à proximité de la face à partir de laquelle l'ensemble a pénétré dans le
récipient.
2. Une chaudière selon la revendication 1, caractérisée en ce que l'échangeur de chaleur
(10, 19, 6) comporte un passage de gaz brûlés (17) qui est délimité d'un côté par
un canal (10) d'eau de chauffage central et de l'autre côté par une partie de paroi
(6) qui est en contact direct avec l'eau sanitaire (S) présente dans le récipient
de stockage (2), ladite partie de paroi étant au moins localement en contact de transmission
de chaleur avec le canal (10) d'eau de chauffage central.
3. Une chaudière selon la revendication 2, caractérisée en ce que des éléments (19) d'augmentation
de la surface de chauffage s'étendent dans le passage de gaz brûlés (17) et sont en
communication directe à la fois avec un passage d'eau de chauffage central (10) et
avec ladite partie de paroi (6).
4. Une chaudière selon la revendication 3, caractérisée en ce que l'échangeur de chaleur
(10, 19, 6), réalisé en métal léger, forme une partie d'un brûleur à prémélange gaz/air
(8) dans un boîtier (6, 7) muni d'une paroi latérale (6) et d'une paroi d'extrémité
fermée (7), le brûleur (8) étant disposé au centre, à l'intérieur de la paroi latérale
(6) avec l'espace de combustion (9) faisant face à la paroi d'extrémité (7), le conduit
de gaz brûlés (17) dans lequel s'étendent les éléments (19) d'augmentation de la surface
de chauffage étant délimité par ladite paroi latérale (6) du boîtier (6, 7), et par
le passage (10) d'eau de chauffage central, disposé de façon sensiblement coaxiale
entre le brûleur (8) et la paroi latérale (6).
5. Une chaudière selon l'une quelconque des revendications précédentes, caractérisée
en ce que la profondeur d'insertion de l'ensemble (1) dans le récipient de stockage
(2) est réglable, de telle façon que l'on puisse faire varier la capacité de la chaudière.