[0001] The presently disclosed subject matter relates to the boiler included in heating
system, especially designed for membrane heating of chemical reactors, in which liquid
metal is used as a heat carrier between boiler and heater.
[0002] In scientific and patent literature liquid metal as heat carrier appears practically
exclusively as a working medium intermediating in heat exchange process between nuclear
fast reactor and generating electric power steam turbine system, and recently also
in processor cooling systems. In power systems nuclear reactor plays a role of boiler
and steam generator - a role of heat sink. Dozens descriptions of various structural
solutions of such arrangements for heat transfer can be found in patent literature,
as for example
US 4515109,
US 6904754,
US 2865827,
US 3033538,
US 4324617.
[0003] In heating systems of chemical reactors there is, however, technological need of
their periodical tuning on and turning off, which is giving rise to completely different
problems, associated with phase transition of a heat carrier from solid state to liquid
and inversely. Technical problem connected with stress changes in fitting points of
heat exchangers pipes in false bottoms is rather hardly recognized in case of chemical
reactor heating pot. Only in few publications, as for example
US 3336974, this problem is mentioned in some scope.
[0004] Process of delivery of large amounts of heat at relatively small temperature gradient
between working fluid and reaction mixture and at high process temperature, excluding
using any organic fluids as heat carriers, requires using liquid salts or liquid metal,
as for example in patent
PL205686. Eutectic alloys, characterized with possibly low melting temperature, are mostly
useful for this goal, if boiler design ensures sufficient strength for bimetallic
stresses and enables intensive heat transfer from flue gas to metallic heat carrier
flowing through boiler in its whole volume. It is also important to carry out the
heating process using possibly small amount of heat carrier in the circuit due to
its high price.
[0005] On the basis of tests of heating system of chemical reactor for depolymerization
process of plastic waste material carried out in industrial conditions the design
of boiler for heating of liquid metal has been developed and realized. This design
is a subject matter of presently disclosed invention.
[0006] Body of boiler for liquid metal heating in heating systems especially of chemical
reactors, is built from a bundle of pipe couples of "pipe in pipe" type and possess
at least two liquid metal chambers created between perforated bottoms connected with
this bundle of pipe couples, where at least one of liquid metal chamber or flue gas
chamber is equipped with elongation compensator and chambers are supported in such
way, that they can freely and independently displace on supporting beds, and the whole
boiler can displace on rolls mounted under support feet. Moreover, the boiler is characterized
with it, that elongation compensator is built-in almost one liquid metal chamber,
and if compensator is built-in one of flue gas chambers it works effectively for compression.
The jacket of the boiler separating one of heating media from surroundings is built
from many separate surfaces. The boiler has a stock chamber, connected freely with
heating circuit of the boiler, with capacity greater than the capacity of heating
circuit apart from the boiler. Liquid metal is transferred between chambers connected
with bundle of pipes of "pipe in pipe" type in spaces between flue gas pipes and jacket
pipes, where boiler design enables exchanging the route of those heating media.
[0007] The boiler has at least two chambers for liquid metal, connected with bundle of pipes
of "pipe in pipe" type, where each outer pipe is a separate boiler jacket separating
one of heating media from the surroundings, thus creating from the sum of external
surfaces of pipes of that bundle a multi-surface boiler jacket. Those chambers are
confined with even number of perforated bottoms and with surfaces perpendicular to
them, with compensating components built-in some of them. External perforated bottoms
of liquid metal chambers are connected with flue gas pipes passing favourably inside
bundle pipes, where it is also possible to lead flue gas in the section between a
couple of pipes from the bundle and leading the liquid metal in the internal pipe.
Metal flows in favourable way between liquid metal chambers in areas of annular or
close to annular shape between jacket pipes and flue gas pipes. Chambers are also
provided with connector pipes for outflow and inflow of the metal to and from heating
circuit. The whole boiler is supported loosely on support beds and supports are founded
on rolls enabling rolling displacement of the structure. Boiler is also provided with
storage chamber enabling accumulation of whole circulating metal in the boiler during
turning off the installation, connecting pipe for protective atmosphere and overflow
connection for short circulation during boiler start-up.
[0008] Boiler design according to the present invention provides very well conditions for
heat transfer from flue gas to liquid metal and simultaneously eliminates all stresses
which could destroy boiler structure, especially during start-up and turning off the
boiler. These features are completed by very small capacity of heat exchanger part
of the boiler, liquid metal is forced through, thus enabling increase of multiplicity
of liquid metal circulation and increase of its linear velocity, providing also much
greater heat flux delivered to heaters.
[0009] The presently disclosed subject matter is depicted in example of embodiment in following
Figures, where longitudinal section of mostly typical solution of boiler design is
depicted in Fig. 1 and its transverse section in Fig.2, whereas Fig. 3 presents the
scheme of solution with exchanged flue gas and liquid metal circulations. Such a solution
is possible, however due to worse conditions for uniform leading of flue gas and hotter
medium at multi-surface jacket of the boiler, it is less advantageous.
[0010] Boiler according to the present invention is provided with four perforated bottoms
1, 2, 3 and 4, of which external ones 1 and 4 are connected by means of flue gas pipes
6 and internal perforated bottoms 2 and 3 are connected by means of pipes of greater
diameter, constituting multi-surface jacket 8 of the boiler. Perforated bottoms are
closed, in pairs with cylindrical surfaces 16; moreover between bottoms 1 and 2 a
circular compensator 7 is built-in. A tube 15 equipped with a valve is welded into
cylindrical surface connecting perforated bottoms 1 and 2, used for venting this liquid
metal chamber during filling up of heating circuit with liquid metal. A support screen
5 preventing deformation of hot pipes in the course of long-term operation of the
boiler is mounted in a half of the lengths of jacket pipes 8. Liquid metal chamber
created between perforated bottoms 1 and 2 is equipped with connector pipe 10 leading
liquid metal from heating circuit to the boiler, and chamber between perforated bottoms
3 and 4 is provided with connector pipe 9 to which liquid metal circulating pump is
connected.
[0011] On the top of liquid metal chamber, between perforated bottoms 3 and 4 a storage
chamber 11 is added of capacity required for storage of metal from the whole given
heating circuit. This chamber is provided with overflow connection 12 for short circulation
of liquid metal used during boiler start-up and connection pipe 14 for connecting
protective atmosphere protecting liquid metal against oxidation. Chamber 11 has also
a charging hole closed with cover 13. Mobile flange 17 connects the boiler with furnace
chamber. Boiler rests freely on beds 19 of supports 18 and these supports have rolls
facilitating displacement of the whole structure, mounted under their surfaces 20.
Rolls facilitating displacement at beds 19 are also foreseen for greater weights of
the boiler.
[0012] After turning the burner on with properly selected small power, flue gas is heating
at first perforated bottoms 4, pipes 6 and perforated bottom 1. After obtaining at
mentioned above boiler components temperature higher by 10 - 15 °C than melting temperature
of used eutectic metal alloy, very thin layer of it is melted, eliminating bimetallic
stresses caused by different linear expansion of eutectic alloy and structural material
of the boiler. Up to this moment those stresses are taken over by compensator 7 and
elastic deformations of thinner perforated bottoms 1 and 4. After melting the entire
metal in the boiler burners' power is increased and temperature of liquid metal is
being raised. Due to different length of pipes 6 and 8 they expand unequally, what
is taken over by compensator 7. Expansion of pipes 6 and 8 causes that liquid metal
chambers, included between perforated bottoms 1 and 2 and also 3 and 4, move away
each other. To avoid stresses in boiler structure caused by this reason, both chambers
have freedom of displacement on beds 19 of supports 18. Full independence of moves
of the whole boiler is provided by rolls located under feet 20 of supports 18. The
boiler is connected with flue gas pipe by means of standard longitudinal compensator
working for compression. Each liquid metal chamber of the boiler has one connector
pipe for connection to serviced heating installation. Lower connector pipe 9 is connected
to liquid metal pump and other connector 10 works as an inlet of liquid metal returning
from the heating system. On the top of one of liquid metal chambers a storage chamber
11 is added, capacity of which enables to store of liquid metal required for filling
the whole heating circuit. In case of shutting off the installation it enables withdrawing
almost whole liquid metal from heaters to the boiler, which radically facilitates
another start-up. Depending on needs it is possible to install such stock chambers
in the larger amount than one. It is also possible design of the boiler based on the
same structural principles, but with circulation of heating media as shown in Fig.3.
1. Boiler for liquid metal heating in heating systems, especially chemical reactors,
characterized in that the body of said boiler is built of a bundle of pipe couples "pipe in pipe" type
8 and 6, and comprises at least two liquid metal chambers created between perforated bottoms
1 and 2 as well as 3 and 4 connected with this bundle of pipe couples, where at least one of liquid metal chambers
or fumes gas chamber is equipped with elongations compensator and chambers are supported
in such a way, that they can freely and independently displace on beds 19 of supports 18, and the whole boiler can displace on rolls mounted under support feet 20.
2. Boiler according to claim 1, characterized in that a circular compensator 7 of thermal expansions working for tension is built-in at least in one liquid metal
chamber.
3. Boiler according to claim 1, characterized in that jacket pipes 8 separating one of heating media from the surroundings is built of many separate surfaces.
4. Boiler according to claim 1, characterized in that it has a storage chamber 11. Freely connected to heating circuit of the boiler, capacity of which is greater
than the capacity of heating circuit out of the boiler.
5. Boiler according to claim 1, characterized in that liquid metal is transferred between chambers connected with a bundle of pipe couples
of "pipe in pipe" type in the space between flue gas pipes 6 and jacket pipes 8, whereas boiler design enables exchanging the route of those heating media according
to the scheme shown in Fig. 3.