CN211823989U - Liquid-solid acceleration separator for self-cleaning fluidized bed heat exchanger and fluidized bed heat exchanger - Google Patents
Liquid-solid acceleration separator for self-cleaning fluidized bed heat exchanger and fluidized bed heat exchanger Download PDFInfo
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Abstract
The utility model relates to a self-cleaning formula is liquid solid separator and fluidized bed heat exchanger with higher speed for fluidized bed heat exchanger mainly is used for solving the technical problem that outer circulating fluidized bed heat exchanger solid particle can not fully circulate and the liquid solid knockout drum is long-pending big in the conventional art. The utility model discloses an adopt a liquid solid separator that accelerates for self-cleaning formula fluidized bed heat exchanger, including the liquid solid separating tank, be provided with rotary device in the liquid solid separating tank, rotary device includes motor, rotation axis, fixed sleeve, revolving stage and rotatory single tube, and from the top down has connected gradually fixed sleeve and revolving stage on the rotation axis, the revolving stage is equipped with the distribution hole, and rotatory single tube and revolving stage lower terminal surface be airtight connection, and with the distribution hole intercommunication; the fixing sleeve is provided with a liquid-solid mixture inlet for connecting a liquid-solid mixture pipeline, the liquid-solid separation tank is provided with a supernatant outlet for connecting a liquid pipeline, the technical scheme better solves the problem, and the fixing sleeve can be used in industrial application of a self-cleaning fluidized bed heat exchanger.
Description
Technical Field
The utility model belongs to the chemical industry field, it is concrete, belong to chemical heat transfer equipment long period operation field, relate to a self-cleaning formula liquid-solid separator and fluidized bed heat exchanger for fluidized bed heat exchanger, the wide application is in solving the problem that traditional extrinsic cycle formula fluidized bed heat exchanger solid particle can not fully circulate and influence the long period operation of device and liquid-solid knockout drum volume big in the wide application.
Background
Heat exchangers are widely used in the petroleum, chemical, energy and other industries. However, as the service life of the heat exchanger increases, the heat exchanger inevitably has a dirt adhesion phenomenon, so that the heat exchange efficiency of the heat exchanger is reduced, the resistance is increased, and the normal operation of the heat exchanger is influenced.
The fluidized bed heat exchanger is developed to replace the traditional heat exchanger, so that the heat exchange effect of the heat exchanger can be improved, and the running time of the device is effectively prolonged. Within the range of the liquid phase flow rate of the heat exchanger, whether solid particles can effectively circulate in the fluidized bed heat exchanger is a precondition for restricting the normal operation and large-scale industrial application of the fluidized bed heat exchanger. In the traditional external circulating fluidized bed heat exchanger, due to pipeline resistance and distribution, solid particles are easily sealed by a liquid column flowing in a horizontal pipe in a descending pipe in the circulating process, so that local short circuit of fluid in the descending pipe pipeline is caused, effective circulation of the solid particles is prevented, and the application of the external circulating fluidized bed heat exchanger is influenced. Document CN202709856U discloses a horizontal liquid-solid circulating fluidized bed heat exchanger using a Kenics static mixer. The fluidized bed heat exchanger has the advantages that solid particles can not be effectively circulated, and the fluidized bed heat exchanger can only be used for a horizontal heat exchanger. Document US6350928 discloses an external circulation type fluidized bed heat exchanger which is not provided with a specific solid particle circulating member and is not capable of maintaining a heat transfer effect or normally operating during an operation period. Document CN102921179 discloses an external circulation type fluidized bed heat exchanger, which adopts a reducing nozzle between a down pipe and a horizontal pipe to generate negative pressure to realize solid particle circulation.
The utility model provides a self-cleaning formula fluidized bed heat exchanger and circulation accelerating method thereof accelerates solid particle from the speed that the downcomer got into the horizontal pipe through the rotatory accelerating device of motor in the liquid-solid separating tank, realizes the effective circulation of solid particle in the heat exchanger shell row, has pointed the solution to above-mentioned problem.
SUMMERY OF THE UTILITY MODEL
The utility model discloses one of the technical problem that will solve is that outer circulating fluidized bed heat exchanger solid particle can not fully circulate and the long big technical problem of liquid-solid knockout drum volume in the traditional art, provides a liquid-solid separator with higher speed for self-cleaning formula fluidized bed heat exchanger, and this liquid-solid separator with higher speed can accelerate solid-liquid separation, and it is abundant to have solid particle circulation, and the device maintains long period operation and the small advantage of liquid-solid knockout drum volume.
The utility model discloses the technical problem that second one of the technical problem that will solve is outer circulating fluidized bed heat exchanger solid particle can not fully circulate and the big technical problem of liquid-solid knockout drum volume in the traditional art, provides a self-cleaning formula fluidized bed heat exchanger. The fluidized bed heat exchanger adopts the liquid-solid acceleration separator for solving one of the technical problems, and has the advantages of full circulation of solid particles, long-period operation of the device and small volume of the liquid-solid separation tank.
For solving one of the above technical problems, the utility model discloses the technical scheme who adopts as follows: a liquid-solid acceleration separator 4 for a self-cleaning fluidized bed heat exchanger comprises a liquid-solid separation tank 23, wherein a rotating device is arranged in the liquid-solid separation tank 23 and comprises a motor 18, a rotating shaft 19, a fixed sleeve 20, a rotating table 21 and a rotating single pipe 22, the rotating shaft 19 is sequentially connected with the fixed sleeve 20 and the rotating table 21 from top to bottom, the rotating table 21 is provided with distribution holes, and the rotating single pipe 22 is hermetically connected with the lower end face of the rotating table 21 and is communicated with the distribution holes; the fixed sleeve 20 is provided with a liquid-solid mixture inlet for connecting the liquid-solid mixture pipeline 16, and the liquid-solid separation tank 23 is provided with a supernatant outlet for connecting the liquid pipeline 17.
In the above technical solution, the rotating table 21 is preferably driven by the motor 18 through the rotating shaft 19; the rotation speed of the rotating shaft 19 is preferably 100 to 600 rpm.
In the above technical solution, the diameter of the fixed sleeve 20 is preferably the same as the diameter of the rotating table 21; the diameter of the fixed sleeve (20) is preferably 0.01 to 0.9 times of the diameter of the liquid-solid separation tank 23.
In the above technical solution, the cross section of the rotating table 21 is preferably circular; the aperture ratio of the distribution holes on the rotating table 21 is preferably 10-50%; more preferably, the distribution holes have the same shape, and more preferably, the distribution holes have a central symmetrical pattern, and most preferably, the distribution holes have a circular shape or a regular polygonal shape.
In the above technical solution, the distribution holes are preferably symmetrically distributed along the circle center of the cross section of the rotating table 21, and have the same shape and size.
In the above technical solution, the outer diameter of the rotating single tube 22 is preferably the same as the inner diameter of the distribution hole, and the inner diameter of the rotating single tube is preferably more than 3 times larger than the diameter of the solid particles to be separated, and at this time, the rotating single tube can be installed in the distribution hole in a sealing manner.
In the above technical solution, the rotating single tube 22 preferably has the same inner diameter as the inner diameter of the distribution holes; the rotating single tubes 22 are preferably symmetrically distributed along the rotating shaft 19, and the symmetrical rotating single tubes 22 are the same in shape and size; the inner diameter of the rotating single tube is preferably more than 3 times larger than the diameter of the solid particles to be separated.
In the technical scheme, the diameter of the total area of the rotating single tube 22 is preferably 0.1-0.5 times of the inner diameter of the fixed sleeve in terms of circular area; the length of the rotating single pipe 22 is preferably 0.2-1.0 time of the diameter of the cylinder of the liquid-solid separation tank; the distance from the bottom end of the rotating single tube 22 to the inner wall surface of the liquid-solid separation tank 23 is preferably 0.1-1 time of the diameter of the cylinder of the liquid-solid separation tank; the rotating single tube 22 is preferably installed in a downward inclination manner, and the included angle between the installation direction and the horizontal plane is preferably 15-75 degrees.
In the above technical solution, the liquid-solid separation tank 23 preferably comprises a cylinder and a lower end enclosure connected with the cylinder; the lower end enclosure is preferably a reducing circular truncated cone or a spherical surface, and the diameter of the upper end surface of the lower end enclosure is preferably equal to that of the cylinder; the height of the lower end socket is preferably 0.2-2 times of the diameter of the cylinder; the liquid-solid separation tank 4 is preferably provided with a particle filter plate 5 and a liquid pipeline (17), and the particle filter plate 5 is preferably positioned below, at the pipe orifice or in the pipe orifice of the liquid pipeline 17.
In the technical scheme, the diameter ratio of the aperture of the particle filter plate 5 to the solid particles to be separated is preferably 0.2-0.9.
For solving the second technical problem, the utility model discloses the technical scheme who adopts as follows: a self-cleaning fluidized bed heat exchanger comprising: a heat exchanger, a liquid-solid acceleration separator 4, a liquid storage tank 6, a liquid circulating pump 7, a downcomer 8, a horizontal pipe 10 and a solid charging tank 11 which are all described in any one of the technical solutions for solving the technical problems; the heat exchanger comprises a lower tube box 1, heat exchanger tubes 2 and an upper tube box, wherein the lower tube box 1 is connected with one end of a horizontal tube 10, and the other end of the horizontal tube 10 is connected with a liquid circulating pump 7; the liquid-solid accelerated separator 4 is connected with a horizontal pipe 10 section between the lower pipe box 1 and the liquid circulating pump 7 through a downcomer 8; a solid feeding tank is connected to the section of the horizontal pipe 10 between the downcomer 8 and the lower pipe box 1; the fixed sleeve 20 is connected with the upper pipe box 3 through a liquid-solid mixture pipeline 16, and the liquid-solid separation tank 23 is connected with the liquid storage tank 6 through a liquid pipeline 17.
In the above technical solution, the self-cleaning fluidized bed heat exchanger preferably further comprises a nozzle 9; the nozzle 9 is positioned at one side of the connection part of the horizontal pipe 10 and the downcomer 8, which is connected with the liquid circulating pump 7, in the horizontal pipe 10; or the nozzle 9 comprises a one-way valve and an inclined pipe, the one-way valve comprises an elastic sheet C, an upper baffle B and a rotating shaft A, the inclined pipe is arranged at the junction of the horizontal pipe and the descending pipe, the inclination angle of the inclined pipe and the horizontal plane is 30-90 degrees, the length of the inclined pipe extending into the horizontal pipe is 0-0.9 times of the diameter of the horizontal pipe, and the accelerated circulation is facilitated.
In the above technical solution, the downcomer 8 is preferably provided with a main valve 12, an upper metering valve 13, a lower metering valve 14 and a metering tank 15; wherein, the upper metering valve 13 and the lower metering valve 14 are arranged on branch pipelines which are connected with the downcomer 8 up and down, a metering tank 15 is connected between the upper pipeline and the lower pipeline, and the main valve 12 is arranged on the downcomer 8 between the connection points of the upper pipeline and the lower pipeline.
In the technical scheme, the upper metering valve 13 is closed, the main valve 12 is opened, solid particles are metered, the lower metering valve 14 is opened after metering is finished, and the solid particles enter the downcomer 8 to continue to finish solid particle circulation in the fluidized bed heat exchanger.
In the technical scheme, the main valve 12 and the lower metering valve 14 are closed, the upper metering valve 13 is opened, and solid particles enter the metering tank 15 to finish metering.
Among the above-mentioned technical scheme, measuring tank 15 is preferred to be made by transparent material, and measuring tank 15 inner wall has the scale according to the volume mark.
In the above technical solution, the solid particles used in the fluidized bed heat exchanger are preferably inert particles that do not react with the medium in the application system, and the bulk density of the solid particles is greater than the liquid phase density. Still more preferably one or more of zirconium silicate beads, corundum beads, porcelain beads, alumina beads, zirconium silicate, steel balls, engineering plastics, polyoxymethylene particles, polytetrafluoroethylene particles, small stones, chopped metal wires, and rubber beads, and more preferably zirconium silicate, alumina beads, and zirconium silicate beads. The average particle size of the particles is 1 mm-5 mm; the average volume solid content of the particles in the fluidized bed heat exchanger is 0.1-6%.
In the technical scheme, the operation range of the flow velocity of the circulating water in the heat exchanger tube array 2 of the fluidized bed heat exchanger is preferably 0.8-4 m/s.
The technical scheme of the utility model in to solid particle mass circulation volume comes the representation solid particle circulation effect in the metering tank 15 during stable operation in the unit interval. The mass circulation of the solid particles in the metering tank 15 is calculated in the following manner:
the solid particle mass circulation is the solid particle density x total volume of the scale portion of the measuring tank x the scale reading/time of the measuring tank.
Adopt the technical scheme of the utility model, adopt a liquid-solid acceleration separator including the rotation accelerating device that the motor that liquid-solid separating tank and interior establish drove, through the speed that motor rotation accelerating device accelerated solid granule in liquid-solid separating tank and got into the horizontal pipe from the downcomer, realize the effective circulation of solid granule in the heat exchanger tube nest, solid granule mass circulation volume can reach more than 420 grams per minute, has gained better technological effect.
Drawings
Fig. 1 is a schematic view of the flow of the fluidized bed heat exchanger of the present invention.
Fig. 2 is a schematic view of the liquid-solid acceleration separator of the present invention.
FIG. 3 is a schematic cross-sectional view of a rotary table of the rotary acceleration device.
In fig. 1, 1 is a lower pipe box; 2 is a heat exchanger tube; 3 is an upper channel box; 4 is a liquid-solid accelerated separator; 5 is a particle filter plate; 6 is a liquid storage tank; 7 is a liquid circulating pump; 8 is a down pipe; 9 is a nozzle; 10 is a horizontal tube. 11 is a feeding tank; 12 is a flow control valve of a downcomer, 13, 14 are metering valves, 15 is a metering tank, 16 is an inlet of a mixture for liquid-solid separation, 17 is an outlet of supernatant liquid for liquid-solid separation, 18 is a motor, 19 is a rotating shaft, 20 is a fixed sleeve, 21 is a rotating platform, and 22 is a rotating single pipe. And 23, a liquid-solid separation tank.
Wherein, go up the tube box 3 and connect liquid solid separator 4 with higher speed, liquid solid separator 4 with higher speed divides two tunnel, and solid phase connects the nozzle 9 that is located the junction of downcomer 8 and horizontal pipe 10 on the one hand, and another way liquid phase connects solid particle groove 6 from granule filter plate 5 upper portion, and liquid circulating pump 7 is connected to solid particle groove 6, and liquid circulating pump 7 connects horizontal pipe 10. The circulating amount of solid particles is metered by means of control valves 12, 13, 14. The liquid-solid separation mixture 16 enters the liquid-solid acceleration separator fixed sleeve 20 and then enters the rotating single pipe 22 connected to the rotating table 21. The motor 16 drives the rotating shaft 19 to rotate, and drives the rotating platform 21 and the rotating single tube 22 to rotate together and throw out to enter a reducing circular table of the liquid-solid separation tank 23 and then enter a downcomer.
In FIG. 2, 17 is a supernatant outlet for liquid-solid separation, 18 is a motor, 19 is a rotary shaft, 20 is a stationary sleeve, 21 is a rotary table, and 22 is a single rotary tube. And 23, a liquid-solid separation tank.
In FIG. 3, (a) and (b) are cross-sections of the turntable having the same diameter and the turntable having a different diameter, respectively.
The invention is further illustrated by the following examples and comparative examples, but the solution of the invention is not limited thereto.
Detailed Description
The following embodiments are further provided to explain the present invention.
[ example 1 ]
The fouling control circulating fluidized bed heat exchanger shown in FIG. 1 was used. 123 heat exchange tubes are arranged in the fluidized bed heat exchanger, each tube is 1000mm long, the tube diameter is phi 22 multiplied by 1.5mm, and the tubes are arranged in a square shape. The pipe diameter of the horizontal pipe is 50mm, and the pipe diameter of the downcomer is 25 mm. The liquid phase is water. The solid particles are zirconium silicate with the average particle diameter of 2mm, and the average volume solid content of the solid particles in the fluidized bed heat exchanger is 3 percent. The liquid phase was water and the flow rate was 2 m/s. In the liquid-solid separation accelerator system, the rotating speed of a rotating shaft is 300rpm, the diameter of a fixing sleeve is 0.2 times of that of a cylinder of a liquid-solid separation tank, the cross section of a rotating platform is a plurality of circular planes with circular holes of equal diameter, and the opening rate of the cross section of the rotating platform is 0.2. The cross section distribution circular holes are symmetrically distributed along the circle center of the cross section, the rotating single tube is a hollow tube with the same diameter as the circular hole connected with the rotating platform, the rotating single tube is symmetrically distributed along the rotating shaft, and the average diameter of the total area of the rotating single tube is 0.2 times of the inner diameter of the fixed sleeve; the length of the rotating single pipe is 0.5 times of the diameter of the cylinder of the liquid-solid separation tank; the distance from the bottom of the rotating single pipe to the liquid-solid separation tank is 0.5 times of the diameter of the cylinder of the liquid-solid separation tank. The included angle between the installation direction of the rotating single tube and the horizontal plane is 45 degrees. The height of the reducing circular truncated cone of the liquid-solid separation groove is 0.5 times of the diameter of the cylinder. The ratio of the inner diameter of the single tube to the diameter of the solid particles was 5. Under these conditions, after stable operation, the mass circulation of the solid particles in the metering tank was determined to be 422 g/min.
[ examples 2 to 10 ]
The fouling control circulating fluidized bed heat exchanger shown in FIG. 1 was used. 123 heat exchange tubes are arranged in the fluidized bed heat exchanger, each tube is 1000mm long, the tube diameter is phi 22 multiplied by 1.5mm, and the tubes are arranged in a square shape. The pipe diameter of the horizontal pipe is 50mm, and the pipe diameter of the downcomer is 25 mm. The liquid phase is water. On the basis of the embodiment 1, the rotating Speed (SP) of the rotating shaft, the ratio (L1) of the diameter of the fixed sleeve to the diameter of the liquid-solid separation tank cylinder, the shape (T) of a plurality of holes in the cross section of the rotating platform, the opening ratio (R) of the cross section of the rotating platform, the ratio (L2) of the length of the rotating single tube to the diameter of the liquid-solid separation tank cylinder, the ratio (L3) of the distance from the bottom of the rotating single tube to the liquid-solid separation tank to the diameter of the liquid-solid separation tank cylinder, the included angle (A1) of the installation direction of the rotating single tube to the horizontal plane, the ratio (L4) of the height of the diameter-reduced circular truncated cone of the liquid-solid separation tank to the diameter of the cylinder, the ratio. After stable operation, the mass circulation (MT) of the solid particles was measured and the results are given in Table 1.
TABLE 1
Comparative example 1
The fouling control circulating fluidized bed heat exchanger shown in FIG. 1 was used. 123 heat exchange tubes are arranged in the fluidized bed heat exchanger, each tube is 1000mm long, the tube diameter is phi 22 multiplied by 1.5mm, and the tubes are arranged in a square shape. The pipe diameter of the horizontal pipe is 50mm, and the pipe diameter of the downcomer is 25 mm. The liquid phase is water. In addition to example 1, no liquid-solid accelerated separator was provided. After stable operation, the mass circulation amount of the solid particles is measured to be 285g.min-1. The circulation effect is not good.
[ COMPARATIVE EXAMPLES 2 to 9 ]
The fouling control circulating fluidized bed heat exchanger shown in FIG. 1 was used. 123 heat exchange tubes are arranged in the fluidized bed heat exchanger, each tube is 1000mm long, the tube diameter is phi 22 multiplied by 1.5mm, and the tubes are arranged in a square shape. The pipe diameter of the horizontal pipe is 50mm, and the pipe diameter of the downcomer is 25 mm. The liquid phase is water. On the basis of example 1, the rotating Speed (SP) of the rotating shaft, the ratio (L1) of the diameter of the fixed sleeve to the diameter of the liquid-solid separation tank cylinder, the shape (T) of the multiple holes in the cross section of the rotating table, the opening ratio (R) of the cross section of the rotating table, the ratio (L2) of the length of the single rotating tube to the diameter of the liquid-solid separation tank cylinder, the ratio (L3) of the distance from the bottom of the single rotating tube to the liquid-solid separation tank to the diameter of the liquid-solid separation tank cylinder, the angle (a1) between the installation direction of the single rotating tube and the horizontal plane, the ratio (L4) of the height of the diameter-reduced circular truncated cone of the liquid-solid separation tank to the diameter of the cylinder, and the ratio (L5.
TABLE 2
Comparative example 10
The fouling control circulating fluidized bed heat exchanger shown in FIG. 1 was used. On the basis of example 1, the ratio of the inner diameter of the single tube to the diameter of the solid particles was set to 2. After stable operation, the single tube was found to be susceptible to plugging. The circulation effect is not good.
Claims (15)
1. A liquid-solid acceleration separator for a self-cleaning fluidized bed heat exchanger comprises a liquid-solid separation tank (23), wherein a rotating device is arranged in the liquid-solid separation tank (23), the rotating device comprises a motor (18), a rotating shaft (19), a fixed sleeve (20), a rotating table (21) and a rotating single pipe (22), the fixed sleeve (20) and the rotating table (21) are sequentially connected onto the rotating shaft (19) from top to bottom, the rotating table (21) is provided with distribution holes, and the rotating single pipe (22) is hermetically connected with the lower end face of the rotating table (21) and communicated with the distribution holes; the fixed sleeve (20) is provided with a liquid-solid mixture inlet for connecting a liquid-solid mixture pipeline (16), and the liquid-solid separation tank (23) is provided with a supernatant outlet for connecting a liquid pipeline (17).
2. The accelerated liquid-solid separator according to claim 1, characterized in that the rotating table (21) is rotated by a motor (18) through a rotating shaft (19).
3. The accelerated liquid-solid separator according to claim 2, wherein the rotating shaft (19) rotates at 100 to 600 rpm.
4. The liquid-solid accelerated separator according to claim 1, wherein the fixed sleeve (20) has the same diameter as the rotating table (21); the diameter of the fixed sleeve (20) is 0.01-0.9 times of the diameter of the liquid-solid separation tank (23).
5. The liquid-solid accelerated separator according to claim 1 or 2, wherein the rotating table (21) is circular in cross section; the aperture ratio of the distribution holes on the rotating platform (21) is 10-50%.
6. The liquid-solid accelerated separator according to claim 5, wherein the distribution holes are identical in shape.
7. The liquid-solid accelerated separator according to claim 6, wherein the distribution holes are shaped in a centrosymmetric pattern.
8. The liquid-solid accelerated separator according to claim 7, wherein the distribution holes are circular or regular polygonal in shape.
9. The accelerated liquid-solid separator according to claim 5, characterized in that said distribution holes are distributed with a symmetrical shape and size along the center of the cross section of the rotating table (21).
10. A liquid-solid accelerated separator according to claim 1 or 2, characterized in that the outer diameter of the rotating single pipe (22) is the same as the inner diameter of the distribution holes, and the inner diameter of the rotating single pipe is more than 3 times larger than the diameter of the solid particles to be separated.
11. A liquid-solid accelerated separator according to claim 1 or 2, characterized in that the rotating single pipe (22) is of equal diameter to the inner diameter of the distribution holes; the rotating single tubes (22) are symmetrically distributed along the rotating shaft (19), and the shapes and the sizes of the symmetrical rotating single tubes (22) are the same; the inner diameter of the rotating single pipe is more than 3 times larger than the diameter of the solid particles to be separated.
12. The liquid-solid accelerated separator according to claim 1 or 2, wherein the diameter of the total area of the rotating single pipes (22) in terms of circular area is 0.1 to 0.5 times the inner diameter of the fixed sleeve; the length of the rotating single pipe (22) is 0.2-1.0 time of the diameter of the cylinder of the liquid-solid separation tank; the distance from the bottom end of the rotating single pipe (22) to the inner wall surface of the liquid-solid separation tank (23) is 0.1-1 times of the diameter of the cylinder of the liquid-solid separation tank; the rotating single pipe (22) is installed in a downward inclination way, and the included angle between the installation direction and the horizontal plane is 15-75 degrees.
13. The accelerated liquid-solid separator according to claim 1 or 2, characterized in that the liquid-solid separation tank (23) consists of a cylinder and a lower head connected to the cylinder; the lower end enclosure is a reducing circular table or a spherical surface, and the diameter of the upper end surface of the lower end enclosure is equal to that of the cylinder; the height of the lower end socket is 0.2-2 times of the diameter of the cylinder; the liquid-solid separation tank (23) is internally provided with a particle filter plate (5) and a liquid pipeline (17), and the particle filter plate (5) is positioned below the orifice of the liquid pipeline (17), or in the orifice or the pipe.
14. A self-cleaning fluidized bed heat exchanger comprising: a heat exchanger, a liquid-solid accelerated separator (4) according to any one of claims 1 to 13, a liquid storage tank (6), a liquid circulating pump (7), a downcomer (8), a horizontal pipe (10) and a solid feeding tank (11); the heat exchanger comprises a lower tube box (1), heat exchanger tubes (2) and an upper tube box, wherein the lower tube box (1) is connected with one end of a horizontal tube (10), and the other end of the horizontal tube (10) is connected with a liquid circulating pump (7); the liquid-solid accelerated separator (4) is connected with a horizontal pipe (10) section between the lower pipe box (1) and the liquid circulating pump (7) through a downcomer (8); a solid feeding tank is connected to the section of the horizontal pipe (10) between the downcomer (8) and the lower pipe box (1); the fixed sleeve (20) is connected with the upper pipe box (3) through a liquid-solid mixture pipeline (16), and the liquid-solid separation tank (23) is connected with the liquid storage tank (6) through a liquid pipeline (17).
15. A self-cleaning fluidized bed heat exchanger according to claim 14, further comprising a nozzle (9); the nozzle (9) is positioned at one side of the connection part of the horizontal pipe (10) and the downcomer (8) and the horizontal pipe (10) which is connected with the liquid circulating pump (7); or the nozzle (9) comprises a one-way valve and an inclined pipe, the one-way valve comprises an elastic sheet C, an upper baffle B and a rotating shaft A, the inclined pipe is arranged at the junction of the horizontal pipe and the descending pipe, the inclination angle of the inclined pipe and the horizontal plane is 30-90 degrees, and the length of the inclined pipe extending into the horizontal pipe is 0-0.9 times of the diameter of the horizontal pipe.
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| CN201921802522.8U CN211823989U (en) | 2019-10-24 | 2019-10-24 | Liquid-solid acceleration separator for self-cleaning fluidized bed heat exchanger and fluidized bed heat exchanger |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN112710173A (en) * | 2019-10-24 | 2021-04-27 | 中国石油化工股份有限公司 | Liquid-solid separator for self-cleaning fluidized bed heat exchanger, fluidized bed heat exchanger and circulating method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN112710173A (en) * | 2019-10-24 | 2021-04-27 | 中国石油化工股份有限公司 | Liquid-solid separator for self-cleaning fluidized bed heat exchanger, fluidized bed heat exchanger and circulating method |
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