CN111854498A - High-temperature gas cooler - Google Patents
High-temperature gas cooler Download PDFInfo
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- CN111854498A CN111854498A CN202010489024.3A CN202010489024A CN111854498A CN 111854498 A CN111854498 A CN 111854498A CN 202010489024 A CN202010489024 A CN 202010489024A CN 111854498 A CN111854498 A CN 111854498A
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- 238000009826 distribution Methods 0.000 claims abstract description 114
- 239000002826 coolant Substances 0.000 claims abstract description 51
- 230000005540 biological transmission Effects 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims description 191
- 230000008602 contraction Effects 0.000 claims description 13
- 238000003466 welding Methods 0.000 claims description 12
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 230000002035 prolonged effect Effects 0.000 abstract description 3
- 238000001816 cooling Methods 0.000 description 9
- 239000002184 metal Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000012360 testing method Methods 0.000 description 4
- 238000004088 simulation Methods 0.000 description 3
- 230000007547 defect Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0021—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for aircrafts or cosmonautics
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0026—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for combustion engines, e.g. for gas turbines or for Stirling engines
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a high-temperature gas cooler, wherein a heat exchange tube is arranged in the high-temperature gas cooler, the heat exchange tube is a straight tube and is arranged along the direction vertical to the transmission direction of high-temperature gas, a cooling medium flows in the heat exchange tube, and the high-temperature gas enters the high-temperature gas cooler and then exchanges heat with the cooling medium in the heat exchange tube; the high-temperature gas cooler comprises a high-temperature section and a low-temperature section, wherein high-temperature gas firstly enters the high-temperature section and then enters the low-temperature section, and the temperature is gradually reduced through twice heat exchange; the distribution disc is arranged in the flow guide section of the high-temperature section and used for dispersing high-temperature gas flowing in the flow guide section, so that the high-temperature gas is uniformly distributed in the same plane perpendicular to the axis of the shell when entering the high-temperature section shell, the influence caused by uneven distribution of the high-temperature gas due to the inertia of the air flow is reduced, and the heat exchange efficiency of the high-temperature gas cooler is improved. The high-temperature gas cooler provided by the invention has the advantages that the heat exchange efficiency is improved, the service life is prolonged, and the manufacturing difficulty is reduced.
Description
Technical Field
The invention relates to the technical field of high-temperature gas cooling, in particular to a high-temperature gas cooler.
Background
An aeroengine high-altitude simulation test bed (high-altitude platform for short) is system equipment for simulating the flying condition and environment of an aircraft engine in the air on the ground and carrying out high-altitude simulation tests on the whole engine and parts of the engine; the exhaust cooling device for the high-altitude simulation test bed of the aircraft engine has the advantages that the temperature of exhaust gas of the engine in a high-altitude cabin test is very high and is as high as 1800 ℃, so the exhaust gas can be exhausted into the atmosphere only after being cooled to about 40 ℃ by a high-temperature gas cooler.
The retrieved Chinese patent publication No. CN101943529.A discloses a high-temperature gas dry cooling device and a method, wherein heat exchange between high-temperature gas and cooling water in a heat exchange tube is realized in the shell pass of a tube bundle type cooler, and the purpose of cooling is realized under the condition that gas components and flow are not increased; however, the heat exchange tubes in the patent are all in an annular layout form, that is, the heat exchange tubes are all coil tubes, the flow of a cooling medium in the coil tubes is relatively long, if the flowing speed is slow, the temperature outside the heat exchange tubes, that is, the temperature of high-temperature gas, is too high, so that the cooling medium in the heat exchange tubes is easily evaporated, the heat exchange tubes are dried, and the service life of the high-temperature heat exchanger is greatly reduced; in addition, the difficulty of rolling the finned tube into a coil is higher; therefore, the high-temperature gas dry cooling device provided by the patent not only has short service life and is easy to damage, but also has high manufacturing difficulty.
Disclosure of Invention
In order to overcome the defects in the prior art, the invention provides the high-temperature gas cooler, which improves the heat exchange efficiency, prolongs the service life and reduces the manufacturing difficulty.
In order to achieve the purpose, the invention adopts the following technical scheme that:
the utility model provides a high temperature gas cooler, the inside heat exchange tube that is equipped with of high temperature gas cooler, the heat exchange tube is the straight tube, and lays along the perpendicular to high temperature gas transmission direction, and coolant is in flow in the heat exchange tube, high temperature gas get into behind the high temperature gas cooler with coolant in the heat exchange tube carries out the heat transfer.
The high-temperature gas cooler comprises a high-temperature section and a low-temperature section, and high-temperature gas firstly enters the high-temperature section to perform primary heat exchange to reduce the temperature and then enters the low-temperature section to perform secondary heat exchange to further reduce the temperature; wherein,
the high temperature section includes: a flow guide section and a high-temperature section shell;
the flow guide section is in a circular truncated cone shape, one end with a smaller radius of the flow guide section is an air inlet end of high-temperature gas, one end with a larger radius of the flow guide section is an air outlet end, and the air outlet end of the flow guide section is correspondingly connected with the air inlet end of the high-temperature section shell;
the high-temperature gas is transmitted in the high-temperature section shell along the axial direction of the high-temperature section shell;
A high-temperature section tube bundle unit is arranged in the high-temperature section shell; the high-temperature section tube bundle unit comprises: the high-temperature section lower tube box, the high-temperature section heat exchange tube and the high-temperature section upper tube box are sequentially connected from bottom to top;
the high-temperature section heat exchange tubes are arranged along the vertical direction perpendicular to the axis of the high-temperature section shell.
The high-temperature section lower pipe box is arranged on the lower half part of the inner wall of the high-temperature section shell along the circumferential direction of the high-temperature section shell; the high-temperature section upper pipe box is arranged on the upper half part of the inner wall of the high-temperature section shell along the circumferential direction of the high-temperature section shell; the high-temperature section lower tube box and the high-temperature section upper tube box are arranged independently of each other and are communicated only through the high-temperature section heat exchange tube.
In the high-temperature section tube bundle unit: a plurality of high-temperature section heat exchange tubes are uniformly distributed in the same plane vertical to the axis of the high-temperature section shell, the plurality of high-temperature section heat exchange tubes uniformly distributed in the same plane vertical to the axis of the high-temperature section shell are called a row of high-temperature section heat exchange tube group, and a plurality of rows of high-temperature section heat exchange tube groups are distributed along the direction of the axis of the high-temperature section shell;
the rows of high-temperature section heat exchange tube sets are connected with the same high-temperature section upper tube box and the same high-temperature section lower tube box.
A high-temperature section cooling medium connecting pipe is also arranged in the high-temperature section shell; the high temperature section cooling medium connecting pipe comprises: a high-temperature section liquid inlet connecting pipe and a high-temperature section liquid outlet connecting pipe; wherein,
high temperature section feed liquor is taken over and is distributed in the latter half space of high temperature section casing, includes: the high-temperature section liquid inlet pipe, the high-temperature section liquid inlet and collection pipe and the high-temperature section liquid inlet and distribution pipe are connected in sequence; the high-temperature section liquid inlet and distribution pipe is connected with the high-temperature section lower pipe box;
the high temperature section goes out liquid takeover and distributes in the first half space of high temperature section casing, includes: the high-temperature section liquid outlet pipe, the high-temperature section liquid outlet and collection pipe and the high-temperature section liquid outlet and distribution pipe are connected in sequence; the high-temperature section liquid outlet and distribution pipe is connected with the high-temperature section upper pipe box;
cooling medium flows into the high-temperature section liquid inlet and collecting pipe from an inlet of the high-temperature section liquid inlet pipe and flows into the high-temperature section lower pipe box through the high-temperature section liquid inlet and distributing pipe, the cooling medium flows into the high-temperature section heat exchange pipe from the high-temperature section lower pipe box and flows into the high-temperature section upper pipe box through the high-temperature section heat exchange pipe, and the cooling medium in the high-temperature section upper pipe box sequentially flows into the high-temperature section liquid outlet and collecting pipe and the high-temperature section liquid outlet pipe through the high-temperature section liquid outlet and distributing pipe and finally flows out of an outlet of the high;
The high-temperature section liquid inlet and collection pipe is connected with a plurality of high-temperature section liquid inlet and distribution pipes, and the plurality of high-temperature section liquid inlet and distribution pipes are respectively connected with different high-temperature section lower pipe boxes, namely, one high-temperature section liquid inlet and collection pipe corresponds to the plurality of high-temperature section lower pipe boxes; a high temperature section goes out the collector tube and connects a plurality of high temperature section and goes out the liquid distribution pipe, and this a plurality of high temperature section go out the liquid distribution pipe and connect different high temperature section and go up the pipe case respectively, promptly, a high temperature section goes out the collector tube and corresponds a plurality of high temperature section and go up the pipe case.
The low temperature section includes: a low-temperature section shell and a contraction section;
the air outlet end of the high-temperature section shell is connected with the air inlet end of the low-temperature section shell; the contraction section is in a round table shape, the gas outlet end of the low-temperature section shell is correspondingly connected with the end with the larger radius of the contraction section, and the end with the smaller radius of the contraction section is the gas outlet end of high-temperature gas; the high-temperature gas is transmitted in the low-temperature section shell along the axial direction of the low-temperature section shell;
the components and the distribution structure of the components in the low-temperature section shell are the same as those in the high-temperature section shell;
the high-temperature section heat exchange tube is a light tube; the low-temperature section heat exchange tube is a finned tube.
High-temperature section jackets are uniformly distributed on the outer wall of the high-temperature section shell and the outer wall of the flow guide section along the circumferential direction; the high-temperature section jacket is formed by welding pipes with semicircular sections on the outer walls of the high-temperature section shell and the flow guide section along the circumferential direction of the high-temperature section shell and the flow guide section in a distributed manner.
A distribution disc is arranged in the flow guide section; the distribution disc is used for dispersing high-temperature gas flowing in the flow guide section.
The distribution disc is wholly cylindrical and comprises: the side shell, the left circular plate and the right circular plate which are vertical to the high-temperature gas transmission direction are arranged on a plurality of pipelines with different inner diameters in the distribution disc; wherein,
the pipeline is used for transmitting high-temperature gas; the transmission direction of the pipeline, namely the transmission direction of the high-temperature gas is consistent with the axial direction of the distribution disc;
the left circular plate and the right circular plate of the distribution disc are respectively provided with a plurality of through holes with different diameters, and the through holes on the left circular plate and the right circular plate are in one-to-one correspondence;
the pipeline is inserted into the distribution disc through corresponding through holes on the left circular plate and the right circular plate; the diameter of the through hole positioned at the central positions of the left circular plate and the right circular plate is the smallest, the through hole extends along the radial direction of the circular plates, and the diameter of the through hole is gradually increased; correspondingly, the pipe diameter of the pipeline inserted in the central positions of the left circular plate and the right circular plate is minimum, and the pipe diameter of the pipeline is gradually increased along the radial extension of the circular plates.
A distribution disc liquid inlet pipe and a distribution disc liquid outlet pipe are fixedly connected to the side shell of the distribution disc;
one port of the distribution disc liquid inlet pipe is fixedly connected below the lateral shell, the other port of the distribution disc liquid inlet pipe downwards penetrates through the shell of the flow guide section and is fixedly connected with the shell of the flow guide section in a welding mode, and the downward port is used as an inlet of a cooling medium;
One port of the distribution disc liquid outlet pipe is fixedly connected above the side shell, the other port of the distribution disc liquid outlet pipe upwards penetrates through the shell of the flow guide section and is fixedly connected with the shell of the flow guide section in a welding mode, and the upwards port is used as an outlet of a cooling medium;
and the cooling medium flows into the shell of the distribution disc from the liquid inlet pipe of the distribution disc and then flows out from the liquid outlet pipe of the distribution disc.
The invention has the advantages that:
(1) the heat exchange tube of the high-temperature gas cooler is a straight tube, the flow of the cooling medium in the heat exchange tube is short, the cooling medium in the heat exchange tube cannot be evaporated by the high-temperature gas outside the tube, the heat exchange tube does not have the dry burning phenomenon, the service life of the equipment is prolonged, and the manufacturing difficulty of the equipment is reduced.
(2) The high-temperature gas cooler is divided into a high-temperature section and a low-temperature section, and the temperature is reduced to the temperature which can be discharged into the atmosphere through twice temperature reduction; in addition, divide into high temperature section and low temperature section and can conveniently carry out the high-temperature gas after once cooling to heat reclamation plant and recycle through the high temperature section to further discharge after cooling down with remaining another part gas.
(3) If the number of the tube boxes on the inner wall of the high-temperature gas cooler is too large, the welding workload is large, the number of welding seams is large, the probability of defects of the welding seams is increased, and the probability of leakage of a cooling medium in the tube boxes into high-temperature gas flow is increased. The cooling medium leaks into the high-temperature air flow, and the composition and flow rate of the cooled medium are increased, so that the heat load is increased. According to the invention, every 2 rows or more than 2 rows of high-temperature section/low-temperature section heat exchange tube sets are connected with the same high-temperature section/low-temperature section upper tube box and the same high-temperature section/low-temperature section lower tube box, so that the number of the high-temperature section/low-temperature section upper tube boxes and the high-temperature section/low-temperature section lower tube boxes in the high-temperature gas cooler is reduced.
(4) According to the invention, one high-temperature section/low-temperature section liquid inlet and collection pipe corresponds to a plurality of high-temperature section/low-temperature section lower pipe boxes, and one high-temperature section/low-temperature section liquid outlet and collection pipe corresponds to a plurality of high-temperature section/low-temperature section upper pipe boxes, so that the number of high-temperature section/low-temperature section liquid inlet and collection pipes and high-temperature section/low-temperature section liquid outlet and collection pipes in the high-temperature gas cooler is reduced. A high-temperature section/low-temperature section liquid inlet and collection pipe corresponds to a high-temperature section/low-temperature section liquid inlet pipe, and a high-temperature section/low-temperature section liquid outlet and collection pipe corresponds to a high-temperature section/low-temperature section liquid outlet pipe. The reduction of the number of liquid inlet and outlet pipes of the high-temperature section/low-temperature section reduces the number of liquid inlet and outlet pipes of the high-temperature section/low-temperature section, namely the number of connecting pipes on the shell of the high-temperature gas cooler is reduced. If the number of the connecting pipes on the shell of the high-temperature gas cooler is too large, that is, the holes are too many, the strength of the shell of the high-temperature gas cooler is weakened, and the wall thickness of the shell of the high-temperature gas cooler needs to be increased, which in turn increases the material cost.
(5) The high-temperature gas cooler is operated under micro negative pressure, and the reinforcing ring is arranged on the outer wall of the shell of the high-temperature gas cooler, so that the structural stability of the high-temperature gas cooler is improved.
(6) The low-temperature section heat exchange tube is a finned tube, and because the temperature of high-temperature gas at the high-temperature section is very high, the fin can be burnt if the finned tube is used, the high-temperature section heat exchange tube is a light tube, and the high-temperature gas enters the low-temperature section after the temperature of the high-temperature section heat exchange high-temperature gas is reduced, and the finned tube is used for strengthening heat exchange.
(7) The high-temperature section jackets are uniformly distributed on the outer wall of the high-temperature section shell and the outer wall of the flow guide section along the circumferential direction, and the metal temperature is rapidly increased when the incoming high-temperature gas is radiated to the metal wall surfaces of the high-temperature section shell and the flow guide section, especially the metal temperature of the flow guide section.
(8) The diameter of a front end pipeline connected with the high-temperature gas cooler is generally relatively small, the flow velocity of the high-temperature gas is large, the diameter of a flow channel is increased under the action of inertia, and high-temperature gas flow beams cannot be rapidly diffused, so that the high-temperature gas is concentrated near the axis position of the high-temperature gas cooler, uneven heat exchange is easily caused, and the heat exchange efficiency is greatly reduced.
(9) The design of the pipeline for transmitting the high-temperature gas on the distribution disc ensures that the resistance at the central position of the circular plate is large when the high-temperature gas flows through the distribution disc, and the resistance is gradually reduced along the radial extension of the circular plate, so that the high-temperature gas flows along the radial direction of the circular plate, and the phenomenon that the high-temperature gas is gathered at the central position of the circular plate 183 due to inertia is avoided.
(10) The distribution plate liquid inlet pipe and the distribution plate liquid outlet pipe are used as an inlet and an outlet of a cooling medium on one hand, and play a certain role in cooling incoming high-temperature gas; and on the other hand, provides support and fixation for the distribution plate.
Drawings
Fig. 1 is a horizontal sectional view of a high temperature gas cooler of the present invention.
Fig. 2 is a cross-sectional view taken along the Z-Z direction of the high-temperature gas cooler.
Fig. 3 is a horizontal cross-sectional view of the distributor disk of the present invention.
Fig. 4 is a cross-sectional view of the distributor disk of the present invention taken along direction B.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
As shown in fig. 1, a high-temperature gas cooler of the present invention includes: high-temperature gas firstly enters the high-temperature section to carry out primary heat exchange to reduce the temperature, and then enters the low-temperature section to carry out secondary heat exchange to further reduce the temperature so as to reduce the temperature to the required temperature.
As shown in fig. 1, the high temperature section has a structure including: the device comprises a flow guide section 1, a high-temperature section shell 2A, a high-temperature section tube bundle unit, a high-temperature section cooling medium connecting tube and a high-temperature section jacket 13.
The high-temperature section shell 2A is cylindrical; the flow guide section 1 is in a circular truncated cone shape; the larger one end of radius of water conservancy diversion section 1 with the inlet end of high temperature section casing 2A is connected, water conservancy diversion section 1 is used for being connected between high temperature section casing 2A and the front end pipeline.
The high-temperature section tube bundle unit comprises: a high-temperature section lower tube box 5A, a high-temperature section upper tube box 11A and a high-temperature section heat exchange tube 6A.
A semicircular pipe is welded on the inner wall of the high-temperature section shell 2A along the circumferential direction of the high-temperature section shell 2A, a partition plate 14 is arranged in the semicircular pipe in the horizontal direction perpendicular to the axis of the high-temperature section shell 2A, and the semicircular pipe is divided into an upper part and a lower part which are equal in size and are not communicated with each other by the partition plate 14; the closed space formed by the upper part of the semicircular pipe and the inner wall of the high-temperature section shell 2A forms the high-temperature section upper pipe box 11A, and the closed space formed by the lower part of the semicircular pipe and the inner wall of the high-temperature section shell 2A forms the high-temperature section lower pipe box 5A.
The high-temperature section heat exchange tube 6A adopts a light tube.
The high-temperature section cooling medium connecting pipe comprises: a high-temperature section liquid inlet connecting pipe and a high-temperature section liquid outlet connecting pipe. Wherein, high temperature section feed liquor takeover includes: a high-temperature section liquid inlet pipe 4A, a high-temperature section liquid inlet and collection pipe 8A and a high-temperature section liquid inlet and distribution pipe 7A; the high temperature section goes out liquid takeover includes: a high-temperature section liquid outlet pipe 12A, a high-temperature section liquid outlet and collection pipe 9A and a high-temperature section liquid outlet and distribution pipe 10A.
High temperature section feed liquor is taken over and is distributed in the latter half of high temperature section casing 2A, the high temperature section goes out the liquid takeover and distributes in the first half of high temperature section casing 2A, just the high temperature section feed liquor take over with the high temperature section goes out the liquid takeover and is the longitudinal symmetry along high temperature section casing 2A axis and distributes.
The high-temperature section liquid inlet pipe 4A is positioned below the high-temperature section shell 2A, and the high-temperature section liquid outlet pipe 12A is positioned above the high-temperature section shell 2A.
As shown in fig. 1, the high-temperature section heat exchange tubes 6A are arranged in a vertical direction perpendicular to the axis of the high-temperature section shell 2A, and a cooling medium flows in the high-temperature section heat exchange tubes 6A from bottom to top.
As shown in fig. 1 and 2, the high-temperature section liquid inlet pipe 4A and the high-temperature section liquid outlet pipe 12A are arranged in a vertical direction perpendicular to the axis of the high-temperature section housing 2A; the downward port of the high-temperature section liquid inlet pipe 4A is a cooling medium inlet, and the upward port of the high-temperature section liquid outlet pipe 12A is a cooling medium outlet.
As shown in fig. 1 and 2, the other port of the high-temperature section liquid inlet pipe 4A is connected to one port of the high-temperature section liquid inlet and collection pipe 8A, the other port of the high-temperature section liquid inlet and collection pipe 8A is connected to one port of the high-temperature section liquid inlet and distribution pipe 7A, and the other port of the high-temperature section liquid inlet and distribution pipe 7A is connected to one port of the high-temperature section lower tube box 5A; the other port of the high-temperature section lower tube box 5A is connected with one port of a high-temperature section heat exchange tube 6A, and the other port of the high-temperature section heat exchange tube 6A is connected with one port of a high-temperature section upper tube box 11A; the other port of the high-temperature section upper tube box 11A is connected with one port of the high-temperature section liquid outlet and distribution tube 10A, the other port of the high-temperature section liquid outlet and distribution tube 10A is connected with one port of the high-temperature section liquid outlet and collection tube 9A, the other port of the high-temperature section liquid outlet and collection tube 9A is connected with one port of the high-temperature section liquid outlet tube 12A, and the other port of the high-temperature section liquid outlet tube 12A faces upwards, namely the outlet faces upwards.
The cooling medium flows into the high-temperature liquid inlet and collecting pipe 8A from a downward port of the high-temperature liquid inlet pipe 4A and flows into the high-temperature lower pipe box 5A through the high-temperature liquid inlet and distributing pipe 7A, the cooling medium exchanges heat with incoming high-temperature gas through the high-temperature heat exchange pipe 6A, the cooling medium flows in the high-temperature heat exchange pipe 6A from bottom to top and then flows into the high-temperature upper pipe box 11A after being heated, and the cooling medium in the high-temperature upper pipe box 11A sequentially flows into the high-temperature liquid outlet and collecting pipe 9A and the high-temperature liquid outlet pipe 12A through the high-temperature liquid outlet and distributing pipe 10A and flows out from an upward port of the high-temperature liquid outlet pipe 12A.
As shown in fig. 2, the high-temperature section liquid inlet and outlet pipes 8A and 9A are arranged in the horizontal direction perpendicular to the axis of the high-temperature section casing 2A, and both ends of the high-temperature section liquid inlet and outlet pipes 8A and 9A are welded to the high-temperature section casing 2A, and since the flow rate of the cooling medium stored in the high-temperature section liquid inlet and outlet pipes 8A and 9A is large, in order to prevent the damage of the high-temperature section liquid inlet and outlet pipes 8A and 9A, each of the high-temperature section liquid inlet and outlet pipes 8A and 9A is supported by two support rods 16.
As shown in fig. 2, in the high-temperature section tube bundle unit: the high-temperature section heat exchange tubes 6A are arranged along the vertical direction perpendicular to the axis of the high-temperature section shell 2A, a plurality of high-temperature section heat exchange tubes 6A are uniformly arranged in the same plane perpendicular to the axis of the high-temperature section shell 2A, the plurality of high-temperature section heat exchange tubes 6A uniformly arranged in the same plane perpendicular to the axis of the high-temperature section shell 2A are called a row of high-temperature section heat exchange tube group, and a plurality of rows of high-temperature section heat exchange tube groups are distributed along the direction of the axis of the high-temperature section shell 2A. Because the rows of the high-temperature section heat exchange tube groups distributed in the high-temperature section shell 2A are more, the invention selects a plurality of rows of high-temperature section heat exchange tube groups belonging to the same high-temperature section tube bundle unit to be connected with the same high-temperature section upper tube box 11A and the same high-temperature section lower tube box 5A together. In this embodiment, each high-temperature-section tube bundle unit includes 3 rows of high-temperature-section heat exchange tube sets, and the 3 rows of high-temperature-section heat exchange tube sets are commonly connected to the same high-temperature-section upper tube box 11A and the same high-temperature-section lower tube box 5A; in this embodiment, along high temperature section casing 2A axis direction, it is equipped with to lay in high temperature section casing 2A: 4 high-temperature section tube bundle units, namely 4 high-temperature section upper tube boxes 11A and 4 high-temperature section lower tube boxes 5A which are vertically corresponding to each other are arranged, and 3 rows of high-temperature section heat exchange tube sets are connected to one corresponding high-temperature section upper tube box 11A and one corresponding high-temperature section lower tube box 5A, namely 12 rows of high-temperature section heat exchange tube sets are arranged in the high-temperature section shell 2A; the number of the high-temperature section upper tube boxes 11A and the high-temperature section lower tube boxes 5A in the high-temperature section shell 2A is reduced.
As shown in fig. 1, one high-temperature section liquid inlet and collecting pipe 8A is connected to two high-temperature section liquid inlet and distribution pipes 7A, and the two high-temperature section liquid inlet and distribution pipes 7A are respectively connected to two high-temperature section lower pipe boxes 5A adjacent to each other on the left and right; the high-temperature section liquid outlet and collection pipe 9A is connected with two high-temperature section liquid outlet and distribution pipes 10A, and the two high-temperature section liquid outlet and distribution pipes 10A are respectively connected with two high-temperature section upper pipe boxes 11A adjacent to the left and the right; the invention reduces the number of the high-temperature section liquid inlet and collecting pipes 8A and the high-temperature section liquid outlet and collecting pipes 9A in the high-temperature section shell 2A. A high-temperature section liquid inlet and collection pipe 8A corresponds to a high-temperature section liquid inlet pipe 4A, and a high-temperature section liquid outlet and collection pipe 9A corresponds to a high-temperature section liquid outlet pipe 12A. The reduction of high temperature section liquid inlet and collection pipe 8A and high temperature section liquid outlet and collection pipe 9A quantity makes high temperature section liquid inlet pipe 4A and high temperature section liquid outlet pipe 12A quantity reduce, takes over quantity reduction on high temperature section casing 2A promptly, also namely trompil reduction on high temperature section casing 2A.
As shown in fig. 1, high-temperature section jackets 13 are uniformly distributed on the outer wall of the high-temperature section shell 2A and the outer wall of the flow guide section 1 along the circumferential direction; the high-temperature section jacket 13 is formed by welding semicircular pipes on the outer walls of the high-temperature section shell 2A and the flow guide section 1 in a distributed manner along the circumferential direction of the high-temperature section shell 2A and the flow guide section 1. Because the high-temperature gas temperature of the incoming flow is high, when the high-temperature gas radiates to the metal wall surfaces of the high-temperature section shell 2A and the flow guide section 1, the metal temperature rises rapidly, especially the metal temperature of the flow guide section 1, and therefore the high-temperature section jacket 13 is arranged on the outer walls of the high-temperature section shell 2A and the flow guide section 1 to reduce the metal temperature, the design temperature of equipment is further reduced, steel is saved, and the service life is prolonged.
As shown in fig. 1, a distribution disc 18 is arranged in the flow guide section 1, and the distribution disc 18 is used for dispersing high-temperature gas flowing from the flow guide section 1, so that the high-temperature gas is uniformly distributed in the same plane perpendicular to the axis of the shell when entering the high-temperature section shell 2A, the influence caused by uneven distribution of the high-temperature gas due to the inertia of the gas flow is reduced, and the heat exchange efficiency of the high-temperature gas cooler is improved.
As shown in fig. 3 and 4, the distribution plate 18 is generally cylindrical and includes: a side shell 181, a left circular plate 183, a right circular plate 183 and a plurality of pipelines 184 which are uniformly distributed and have different diameters. Wherein,
the pipeline 184 is used for transmitting high-temperature gas; the conveying direction of the pipeline 184, i.e. the conveying direction of the high-temperature gas, is consistent with the axial direction of the distribution disc 18;
the left circular plate 183 and the right circular plate 183 of the distribution disc 18 are respectively provided with a plurality of through holes which are uniformly distributed and have different diameters, and the through holes on the left circular plate 183 and the through holes on the right circular plate 183 are in one-to-one correspondence; the pipeline 184 is inserted into the distribution disk 18 through corresponding through holes on the left circular plate 183 and the right circular plate 183;
the pipelines 184 with uniform distribution and different diameters are used for dispersing the high-temperature gas of the incoming flow; the diameter of the through hole at the center positions of the left and right circular plates 183 of the distribution disk 18 is smallest, and the diameter of the through hole extending in the radial direction of the circular plate 183 is gradually increased, and correspondingly, the pipe diameter of the pipe 184 inserted at the center positions of the left and right circular plates 183 of the distribution disk 18 is smallest, and the pipe diameter of the pipe 184 extending in the radial direction of the circular plate 183 is gradually increased; when the high-temperature gas flows through the distribution disk 18, the resistance at the center position of the circular plate 183 is ensured to be large, and the resistance extending along the radial direction of the circular plate 183 is gradually reduced, so that the high-temperature gas flows along the radial direction of the circular plate 183, and the phenomenon that the high-temperature gas is gathered at the center position of the circular plate 183 due to inertia is avoided.
The side shell 181 of the distribution disk 18 is provided with: distribution plate liquid inlet pipe 185, distribution plate liquid outlet pipe 182;
one port of the distribution plate liquid inlet pipe 185 is fixedly connected to the side shell 181, and the other port of the distribution plate liquid inlet pipe penetrates through the shell of the flow guide section 1 and is fixedly connected with the shell of the flow guide section 1 in a welding mode; the distribution disc liquid inlet pipe 185 is arranged below the side shell 181, and a downward port of the distribution disc liquid inlet pipe 185 penetrates through a port of the flow guide section 1 to serve as an inlet of a cooling medium;
one port of the distribution disc liquid outlet pipe 182 is fixedly connected to the side shell 181, and the other port of the distribution disc liquid outlet pipe passes through the shell of the flow guide section 1 and is fixedly connected with the shell of the flow guide section 1 in a welding mode; the distribution tray liquid outlet pipe 182 is arranged above the side shell 181, and an upward port of the distribution tray liquid outlet pipe 182 passes through the port of the flow guide section 1 to serve as an outlet of the cooling medium;
the cooling medium flows into the shell of the distribution plate 18 from the distribution plate liquid inlet pipe 185 and then flows out from the distribution plate liquid outlet pipe 182; distribution plate liquid inlet pipe 185 and distribution plate liquid outlet pipe 182 serve as an inlet and an outlet for the cooling medium on the one hand and provide a supporting and fixing function for distribution plate 18 on the other hand;
in this embodiment, 2 distribution tray liquid outlet pipes 182 and 1 distribution tray liquid inlet pipe 185 are uniformly distributed along the side shell 181, the 1 distribution tray liquid inlet pipe 185 is located right below the side shell 181, and the 2 distribution tray liquid outlet pipes 182 are respectively located on the left and right oblique upper sides of the side shell.
In the invention, the number of the distribution discs 18 is determined according to the flow rate of the high-temperature gas, if the flow rate is larger, a plurality of distribution discs 18 can be arranged along the transmission direction of the high-temperature gas, and the size of the plurality of distribution discs 18 is matched with the structural size of the flow guide section 1; if the flow rate is small, only one distribution disc 18 can be arranged; after the high-speed high-temperature gas of the incoming flow passes through one or more distribution discs 18 in the flow guide section 1, the high-temperature gas is uniformly distributed. In this embodiment, two distribution disks are provided along the high-temperature gas transfer direction.
As shown in fig. 1, the low temperature section includes: the low-temperature section shell 2B, the contraction section 3, the low-temperature section tube bundle unit and the low-temperature section cooling medium connecting pipe;
the low-temperature section shell 2B is cylindrical; the contraction section 3 is in a circular truncated cone shape; the contraction section 3 is used for connecting the air outlet end of the low-temperature section shell 2B with the rear end pipeline, the larger radius end of the contraction section 3 is connected with the air outlet end of the low-temperature section shell 2B, and the air inlet end of the low-temperature section shell 2B is connected with the air outlet end of the high-temperature section shell 2A.
The low-temperature section tube bundle unit comprises: a low-temperature section lower tube box 5B, a low-temperature section upper tube box 11B and a low-temperature section heat exchange tube 6B;
the structures of the low-temperature section lower tube box 5B and the low-temperature section upper tube box 11B are the same as the structures of the high-temperature section lower tube box 5A and the high-temperature section upper tube box 11A.
The low-temperature section heat exchange tube 6B adopts a finned tube, and the arrangement of the low-temperature section heat exchange tube 6B is the same as that of the high-temperature section heat exchange tube 6A; in the low-temperature section tube bundle unit, a plurality of low-temperature section heat exchange tubes 6B are uniformly distributed in the same plane vertical to the axis of the low-temperature section shell 2B, the plurality of low-temperature section heat exchange tubes 6B uniformly distributed in the same plane vertical to the axis of the low-temperature section shell 2B are called a row of low-temperature section heat exchange tube group, and a plurality of rows of low-temperature section heat exchange tube groups are distributed along the direction of the axis of the low-temperature section shell 2B.
The low-temperature section cooling medium connecting pipe comprises: a low-temperature section liquid inlet connecting pipe and a low-temperature section liquid outlet connecting pipe. Wherein, low temperature section feed liquor takeover includes: a low-temperature section liquid inlet pipe 4B, a low-temperature section liquid inlet and collection pipe 8B and a low-temperature section liquid inlet and distribution pipe 7B; the low temperature section goes out liquid takeover includes: a low-temperature section liquid outlet pipe 12B, a low-temperature section liquid outlet and collection pipe 9B and a low-temperature section liquid outlet and distribution pipe 10B.
The structures of the low-temperature section liquid inlet connecting pipe and the low-temperature section liquid outlet connecting pipe are the same as those of the high-temperature section liquid inlet connecting pipe and the high-temperature section liquid outlet connecting pipe; namely, the structures of the low-temperature section liquid inlet pipe 4B, the low-temperature section liquid inlet and collecting pipe 8B and the low-temperature section liquid inlet and distributing pipe 7B are the same as the structures of the high-temperature section liquid inlet pipe 4A, the high-temperature section liquid inlet and collecting pipe 8A and the high-temperature section liquid inlet and distributing pipe 7A; the structures of the low-temperature section liquid outlet pipe 12B, the low-temperature section liquid outlet and collection pipe 9B and the low-temperature section liquid outlet and distribution pipe 10B are the same as the structures of the high-temperature section liquid outlet pipe 12A, the high-temperature section liquid outlet and collection pipe 9A and the high-temperature section liquid outlet and distribution pipe 10A.
The cooling medium flows from bottom to top in the low-temperature section heat exchange tube 6B, and the flow mode of the cooling medium in the low-temperature section along the low-temperature section liquid inlet connecting tube, the low-temperature section lower tube box 5B, the low-temperature section heat exchange tube 6B, the low-temperature section upper tube box 11B and the low-temperature section liquid outlet connecting tube is consistent with the flow mode of the cooling medium in the high-temperature section along the high-temperature section liquid inlet connecting tube, the high-temperature section lower tube box 5A, the high-temperature section heat exchange tube 6A, the high-temperature section upper tube box 11A and the high-temperature.
In this embodiment, along low temperature section casing 2B axis direction, it is equipped with to lay in low temperature section casing 2B: 2 low-temperature section pipe bundle units, namely 2 low-temperature section upper pipe boxes 11B and 2 low-temperature section lower pipe boxes 5B which are vertically corresponding to each other are arranged, and 3 rows of low-temperature section heat exchange pipe sets are connected to one corresponding low-temperature section upper pipe box 11B and one corresponding low-temperature section lower pipe box 5B, namely 6 rows of high-temperature section heat exchange pipe sets are arranged in the low-temperature section shell 2B; the number of the low-temperature section upper tube boxes 11B and the low-temperature section lower tube boxes 5B in the low-temperature section shell 2B is reduced.
In this embodiment, one low-temperature-section liquid inlet and collecting pipe 8B is connected to two low-temperature-section liquid inlet and distribution pipes 7B, and the two low-temperature-section liquid inlet and distribution pipes 7B are respectively connected to two low-temperature-section lower pipe boxes 5B adjacent to each other on the left and right; the low-temperature section liquid outlet and collection pipe 9B is connected with two low-temperature section liquid outlet and distribution pipes 10B, and the two low-temperature section liquid outlet and distribution pipes 10B are respectively connected with two low-temperature section upper pipe boxes 11B adjacent to the left and the right; the invention reduces the number of the low-temperature section liquid inlet and collecting pipes 8B and the low-temperature section liquid outlet and collecting pipes 9B in the low-temperature section shell 2B. One low-temperature section liquid inlet and collecting pipe 8B corresponds to one low-temperature section liquid inlet pipe 4B, and one low-temperature section liquid outlet and collecting pipe 9B corresponds to one low-temperature section liquid outlet pipe 12B. The reduction of low temperature section liquid inlet and collection pipe 8B and low temperature section liquid outlet and collection pipe 9B quantity makes low temperature section liquid inlet pipe 4B and low temperature section liquid outlet pipe 12B quantity reduce, takes over quantity reduction on low temperature section casing 2B promptly, also namely trompil reduction on low temperature section casing 2B.
The high-temperature gas of the front-end pipeline flows into the high-temperature section from the flow guide section 1, the temperature is reduced through heat exchange with the cooling medium in the high-temperature section heat exchange tube 6A, then flows into the low-temperature section, the temperature is further reduced through heat exchange with the cooling medium in the low-temperature section heat exchange tube 6B, and then the high-temperature gas is discharged from the contraction section 3 and flows into the rear-end pipeline.
As shown in fig. 1 and 2, the high-temperature stage casing 2A and the low-temperature stage casing 2B are each supported by saddles 15, and the number of saddles 15 is set according to the lengths of the high-temperature stage casing 2A and the low-temperature stage casing 2B.
As shown in fig. 1 and 2, the high temperature section casing 2A and the low temperature section casing 2B are operated by micro negative pressure, so that the reinforcing rings 17 can be disposed on the outer walls of the high temperature section casing 2A and the low temperature section casing 2B, thereby improving the structural stability of the high temperature section casing 2A and the low temperature section casing 2B.
In this embodiment, the low temperature section casing 2B and the high temperature section casing 2A are connected to each other to form a whole, that is, the high temperature section and the low temperature section share the same cylindrical casing. In addition to this mode, the high-temperature section and the low-temperature section can be separated, after the incoming high-temperature gas is cooled to a certain target temperature through the high-temperature section, a part of the gas can be conveyed to the heat recovery device for reuse, and the other part of the gas is conveyed to the low-temperature section for further cooling and then is discharged.
In the invention, the cooling medium is all water, the cooling medium is led out from the water pump, flows into the high-temperature gas cooler through each inlet of the high-temperature gas cooler and flows out from each outlet of the high-temperature gas cooler, and the cooling medium can flow from bottom to top in the high-temperature gas cooler because the water pump provides larger water flow power.
The invention is not to be considered as limited to the specific embodiments shown and described, but is to be understood to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined by the appended claims.
Claims (10)
1. The high-temperature gas cooler is characterized in that a heat exchange tube is arranged inside the high-temperature gas cooler, the heat exchange tube is a straight tube and is arranged along the transmission direction of high-temperature gas, a cooling medium flows in the heat exchange tube, and the high-temperature gas enters the high-temperature gas cooler and then exchanges heat with the cooling medium in the heat exchange tube.
2. The high-temperature gas cooler according to claim 1, wherein the high-temperature gas cooler comprises a high-temperature section and a low-temperature section, and the high-temperature gas firstly enters the high-temperature section to perform primary heat exchange to reduce the temperature and then enters the low-temperature section to perform secondary heat exchange to further reduce the temperature; wherein,
The high temperature section includes: a flow guide section (1) and a high-temperature section shell (2A);
the flow guide section (1) is in a circular truncated cone shape, the end with the smaller radius of the flow guide section (1) is an air inlet end of high-temperature gas, the end with the larger radius of the flow guide section (1) is an air outlet end, and the air outlet end of the flow guide section (1) is correspondingly connected with the air inlet end of the high-temperature section shell (2A);
the high-temperature gas is transmitted in the high-temperature section shell (2A) along the axial direction of the high-temperature section shell (2A);
a high-temperature section tube bundle unit is arranged in the high-temperature section shell (2A); the high-temperature section tube bundle unit comprises: a high-temperature section lower tube box (5A), a high-temperature section heat exchange tube (6A) and a high-temperature section upper tube box (11A) which are connected in sequence from bottom to top;
the high-temperature section heat exchange tubes (6A) are arranged along the vertical direction perpendicular to the axis of the high-temperature section shell (2A).
3. A high-temperature gas cooler according to claim 2, wherein said high-temperature-stage lower header tank (5A) is provided on a lower half portion of an inner wall of the high-temperature-stage casing (2A) in a circumferential direction of the high-temperature-stage casing (2A); the high-temperature section upper pipe box (11A) is arranged on the upper half part of the inner wall of the high-temperature section shell (2A) along the circumferential direction of the high-temperature section shell (2A); the high-temperature section lower tube box (5A) and the high-temperature section upper tube box (11A) are arranged independently of each other and are communicated only through the high-temperature section heat exchange tubes (6A).
4. A high temperature gas cooler according to claim 3, wherein in the high temperature section tube bundle unit: a plurality of high-temperature section heat exchange tubes (6A) are uniformly distributed in the same plane vertical to the axis of the high-temperature section shell (2A), the plurality of high-temperature section heat exchange tubes (6A) which are uniformly distributed in the same plane vertical to the axis of the high-temperature section shell (2A) are called a row of high-temperature section heat exchange tube group, and a plurality of rows of high-temperature section heat exchange tube groups are distributed along the direction of the axis of the high-temperature section shell (2A);
the rows of high-temperature section heat exchange tube sets are connected with the same high-temperature section upper tube box (11A) and the same high-temperature section lower tube box (5A).
5. A high-temperature gas cooler according to claim 2, wherein a high-temperature section cooling medium connecting pipe is further arranged in the high-temperature section shell (2A); the high temperature section cooling medium connecting pipe comprises: a high-temperature section liquid inlet connecting pipe and a high-temperature section liquid outlet connecting pipe; wherein,
high temperature section feed liquor is taken over and is distributed in the latter half space of high temperature section casing (2A), includes: a high-temperature section liquid inlet pipe (4A), a high-temperature section liquid inlet and collection pipe (8A) and a high-temperature section liquid inlet and distribution pipe (7A) which are connected in sequence; the high-temperature section liquid inlet and distribution pipe (7A) is connected with the high-temperature section lower pipe box (5A);
The high temperature section goes out liquid takeover and distributes in the first half space of high temperature section casing (2A), includes: a high-temperature section liquid outlet pipe (12A), a high-temperature section liquid outlet and collection pipe (9A) and a high-temperature section liquid outlet and distribution pipe (10A) which are connected in sequence; the high-temperature section liquid outlet and distribution pipe (10A) is connected with a high-temperature section upper pipe box (11A);
cooling medium flows into a high-temperature section liquid inlet collecting pipe (8A) from an inlet of a high-temperature section liquid inlet pipe (4A), flows into a high-temperature section lower pipe box (5A) through a high-temperature section liquid inlet distributing pipe (7A), flows into a high-temperature section heat exchange pipe (6A) from the high-temperature section lower pipe box (5A), flows into a high-temperature section upper pipe box (11A) through the high-temperature section heat exchange pipe (6A), flows into a high-temperature section liquid outlet collecting pipe (9A) and a high-temperature section liquid outlet pipe (12A) sequentially through a high-temperature section liquid outlet distributing pipe (10A) from the high-temperature section upper pipe box (11A), and finally flows out from an outlet of a high-temperature section liquid outlet pipe (12A);
the high-temperature section liquid inlet and collection pipe (8A) is connected with a plurality of high-temperature section liquid inlet and distribution pipes (7A), the plurality of high-temperature section liquid inlet and distribution pipes (7A) are respectively connected with different high-temperature section lower pipe boxes (5A), namely, one high-temperature section liquid inlet and collection pipe (8A) corresponds to the plurality of high-temperature section lower pipe boxes (5A); a high temperature section goes out collector tube (9A) and connects a plurality of high temperature section and goes out liquid distribution pipe (10A), and this a plurality of high temperature section goes out liquid distribution pipe (10A) and connects different high temperature section upper tube case (11A) respectively, promptly, a high temperature section goes out collector tube (9A) and corresponds a plurality of high temperature section upper tube case (11A).
6. A high-temperature gas cooler according to any one of claims 2 to 5,
the low temperature section includes: a low-temperature section shell (2B) and a contraction section (3);
the air outlet end of the high-temperature section shell (2A) is connected with the air inlet end of the low-temperature section shell (2B); the contraction section (3) is in a round table shape, the air outlet end of the low-temperature section shell (2B) is correspondingly connected with the end with the larger radius of the contraction section (3), and the end with the smaller radius of the contraction section (3) is the air outlet end of high-temperature gas; the high-temperature gas is transmitted in the low-temperature section shell (2B) along the axial direction of the low-temperature section shell (2B);
the components and the distribution structure in the low-temperature section shell (2B) are the same as those in the high-temperature section shell (2A);
the high-temperature section heat exchange tube (6A) is a light tube; the low-temperature section heat exchange tube (6B) is a finned tube.
7. A high-temperature gas cooler according to claim 2, wherein the outer wall of the high-temperature section shell (2A) and the outer wall of the flow guide section (1) are uniformly provided with high-temperature section jackets (13) along the circumferential direction; the high-temperature section jacket (13) is formed by welding pipes with semicircular sections on the outer walls of the high-temperature section shell (2A) and the flow guide section (1) in a distributed manner along the circumferential direction of the high-temperature section shell (2A) and the flow guide section (1).
8. A hot gas cooler according to claim 2, characterized in that a distribution plate (18) is arranged in the flow guiding section (1); the distribution disc (18) is used for dispersing high-temperature gas flowing in the flow guide section (1).
9. A hot gas cooler according to claim 8, characterized in that the distribution plate (18) is generally cylindrical and comprises: the side shell (181), the left circular plate (183) and the right circular plate (183) which are vertical to the high-temperature gas transmission direction, and a plurality of pipelines (184) with different inner diameters which are arranged on the distribution disc (18); wherein,
the pipeline (184) is used for transmitting high-temperature gas; the transmission direction of the pipeline (184), namely the transmission direction of the high-temperature gas, is consistent with the axial direction of the distribution disc (18);
the left circular plate (183) and the right circular plate (183) of the distribution disc (18) are respectively provided with a plurality of through holes with different diameters, and the through holes on the left circular plate (183) and the right circular plate (183) are in one-to-one correspondence;
the pipeline (184) is inserted into the distribution disc (18) through corresponding through holes on the left circular plate (183) and the right circular plate (183); the diameter of the through hole positioned at the central positions of the left circular plate (183) and the right circular plate (183) is the smallest, the diameter of the through hole extends along the radial direction of the circular plate (183), and the diameter of the through hole is gradually increased; correspondingly, the pipe diameter of the pipeline (184) inserted in the central positions of the left circular plate (183) and the right circular plate (183) is minimum, and the pipe diameter of the pipeline (184) is gradually increased along the radial extension of the circular plates (183).
10. A hot gas cooler according to claim 9, characterized in that a distribution plate inlet pipe (185), a distribution plate outlet pipe (182) are fixedly connected to the side shell (181) of the distribution plate (18);
one port of the distribution disc liquid inlet pipe (185) is fixedly connected below the side shell (181), the other port of the distribution disc liquid inlet pipe (185) downwards penetrates through the shell of the flow guide section (1) and is fixedly connected with the shell of the flow guide section (1) in a welding mode, and the downwards port is used as an inlet of a cooling medium;
one port of the distribution disc liquid outlet pipe (182) is fixedly connected above the side shell (181), the other port of the distribution disc liquid outlet pipe (182) upwards penetrates through the shell of the flow guide section (1) and is fixedly connected with the shell of the flow guide section (1) in a welding mode, and the upwards port is used as an outlet of a cooling medium;
the cooling medium flows into the shell of the distribution plate (18) from the distribution plate liquid inlet pipe (185) and then flows out from the distribution plate liquid outlet pipe (182).
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| CN114413657A (en) * | 2021-12-23 | 2022-04-29 | 合肥通用机械研究院有限公司 | Matrix type high-temperature gas cooler |
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| US4220200A (en) * | 1976-11-12 | 1980-09-02 | Sulzer Brothers Limited | Heat exchanger system |
| JP2001031982A (en) * | 1999-07-19 | 2001-02-06 | Japan Gas Association | Heat exchanger and coal-gasification apparatus using this |
| CN2539121Y (en) * | 2002-04-19 | 2003-03-05 | 中国人民解放军第二炮兵第一研究所 | Modular step cooler for tail gas from diesel electric generator |
| CN2854478Y (en) * | 2005-08-05 | 2007-01-03 | 上海化工装备有限公司 | High-efficient gas cooler |
| CN101943529A (en) * | 2010-09-29 | 2011-01-12 | 西安航天华威化工生物工程有限公司 | Dry cooling device and method for high-temperature gas |
| CN208382956U (en) * | 2018-05-07 | 2019-01-15 | 华南理工大学 | A kind of spiral plate type thermochemical high temperature energy storing-releasing reaction unit |
| CN208382948U (en) * | 2018-07-03 | 2019-01-15 | 德兴市惠康节能环保有限公司 | A kind of novel plant waste heat recycling heating device |
| CN209069064U (en) * | 2018-10-31 | 2019-07-05 | 陆飞浩 | A kind of gas-gas heat exchanger |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114413657A (en) * | 2021-12-23 | 2022-04-29 | 合肥通用机械研究院有限公司 | Matrix type high-temperature gas cooler |
Also Published As
| Publication number | Publication date |
|---|---|
| CN114152112A (en) | 2022-03-08 |
| CN111854498B (en) | 2021-12-28 |
| CN114152112B (en) | 2023-09-22 |
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