CN212378070U - Modular solid-liquid two-phase heat storage device - Google Patents
Modular solid-liquid two-phase heat storage device Download PDFInfo
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- CN212378070U CN212378070U CN202020673034.8U CN202020673034U CN212378070U CN 212378070 U CN212378070 U CN 212378070U CN 202020673034 U CN202020673034 U CN 202020673034U CN 212378070 U CN212378070 U CN 212378070U
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Abstract
The utility model discloses a double-phase heat-retaining device of modular solid-liquid, including the casing, along vertically installing heat storage module group in the casing, in the heat storage module group, along vertical follow top layer to bottom or from the bottom to the pipe diameter successive layer of the heat exchange tube of top layer increase progressively, every heat exchange tube that is arranged in the multilayer heat-retaining modular unit of same row connects the elbow through the reducing and establishes ties in proper order, forms the vertical parallel heat transfer medium reducing S-shaped passageway that stands side by side of multiseriate. The utility model discloses a modular heat-retaining modular unit structural design, only heat transfer pipeline all the way can make the inside heat transfer effect maximize of structure, has promoted heat storage volume and heat-retaining efficiency. The utility model discloses a heat transfer pipeline is the vertical parallel heat transfer medium reducing S-shaped passageway that stands side by side of multiseriate, through the method that changes area of contact and velocity of flow, realizes that the heat transfer volume at every turn keeps the same level.
Description
Technical Field
The utility model belongs to the heat transfer device field relates to double-phase heat-retaining device, concretely relates to double-phase heat-retaining device of modular solid-liquid.
Background
In the municipal engineering field and the industrial production field, heat supply is a constant topic and is a main aspect of energy consumption. However, the mismatch with the demand often exists in the heating process, and the mismatch is expressed in the mismatch of the demand quantity and the mismatch of the demand time, and the mismatch can cause the waste of energy. The heat storage technology is an effective method for effectively solving the problem of unbalanced heat energy supply and demand and improving the energy utilization efficiency, so that the heat storage technology is rapidly developed.
The solid-liquid two-phase heat storage can be developed because the sensible heat of the heat storage material can be used for heat storage, and the latent heat of the state in the change process can be used for heat storage, so that the solid-liquid two-phase heat storage device has the advantages of high heat storage density, small volume and the like.
In the prior art, an energy storage material is generally filled in a closed metal box body, a heat storage pipeline and a heat release pipeline are arranged in the energy storage material in a snake-shaped manner, and the final heat taking and exchanging effect is directly influenced by the arrangement density and the arrangement mode of the pipelines.
The prior art has the following defects and shortcomings:
(A) the solid-liquid conversion is not thorough, and the equipment application efficiency is low. Most of the phase heat storage materials have poor heat transfer effect, and particularly when heat is released, after the heat is converted from liquid to solid, the solid materials condensed on the heat exchange tubes influence the heat exchange between the heat exchange tubes and the liquid materials, so that the heat storage materials cannot be completely converted into a solid state, and the maximum heat storage and release cannot be realized. Therefore, a reasonable structure is required to improve the defect
(B) The heat storage device system is complicated. In the traditional heat storage device, at least two heat exchange pipelines, a heat storage medium heat exchange pipeline and a heat release medium heat exchange pipeline occupy a larger space of the heat storage device, so that the storage capacity of a heat storage material is greatly reduced, and the total heat storage capacity of the whole device is influenced.
(C) The temperature and the stress are distributed unevenly, and the reliability of the heat storage equipment is low. The heat of the existing heat accumulator is generally too concentrated at the heat exchange medium inlet section, the temperature of the heat accumulation material is higher, and the change of the physical state is quicker. Along with the heat exchange, the flowing temperature of the heat exchange medium is gradually reduced, the temperature difference between the heat exchange medium and the heat storage material is gradually reduced, the heat storage quantity at the outlet section of the device is small, the temperature of the heat storage material is low, the local overheating and temperature stratification phenomena are caused, and the effect and the service life of the heat storage device are influenced
(D) The system life and maintainability are poor. At present, most of heat storage devices mainly use a coil pipe as a main heat exchange structure, and the heat exchange coil pipe is arranged inside the heat storage device. In the long-time operation process of the heat exchange coil, once scaling and blockage occur or the pipe wall is corroded and omitted, the service performance of the whole heat storage device is reduced, even the heat storage material is leaked, and the system safety and the equipment service life are affected.
Disclosure of Invention
Not enough to prior art exists, the utility model aims to provide a double-phase heat-retaining device of modular solid-liquid solves the technical problem that equipment heat storage volume and heat-retaining efficiency remain to improve among the prior art.
In order to solve the technical problem, the utility model discloses a following technical scheme realizes:
a modularized solid-liquid two-phase heat storage device comprises a box body, wherein a heat storage module group is longitudinally arranged in the box body, the heat storage module group comprises a plurality of heat storage module units which are longitudinally arranged, the heat storage module units are in a multi-layer and multi-row array arrangement structure, a plurality of heat storage module units with the same number are transversely arranged on each layer, and a plurality of layers of heat storage module units are vertically arranged;
the heat storage module unit comprises a closed inner shell, heat exchange tubes with two ends extending out of the axial end face of the inner shell are installed in the inner shell, and a cavity between the heat exchange tubes and the inner shell is filled with heat storage materials;
in the heat storage module group, the pipe diameters of heat exchange pipes from the top layer to the bottom layer or from the bottom layer to the top layer are gradually increased layer by layer, and the heat exchange pipes in the multi-layer heat storage module units in the same row are sequentially connected in series through reducing connecting elbows to form a plurality of rows of heat exchange medium reducing S-shaped passages which are vertically parallel and parallel;
in the heat storage module group, the end parts of a plurality of heat exchange tubes with the smallest tube diameter at the top vertical layer or the bottom vertical layer are all connected with a small-diameter end water distributor through reducing connecting tubes, and the small-diameter end water distributor is connected with a small-diameter end connector of a heat exchange medium; the end parts of the plurality of heat exchange tubes with the largest tube diameter at the bottommost layer or the topmost layer are connected with a large-diameter end water distributor through connecting tubes, and the large-diameter end water distributor is connected with a large-diameter end joint of a heat exchange medium, so that a plurality of rows of parallel heat exchange medium reducing S-shaped passages are connected in parallel between the small-diameter end joint of the heat exchange medium and the large-diameter end joint of the heat exchange medium.
The utility model discloses still have following technical characteristic:
in the heat storage module group, the pipe diameter of the heat exchange pipe of the heat storage module units of two adjacent layers increases by 2-10%.
In the heat storage module group, the heat exchange tubes of the heat storage module units on the same layer have the same tube diameter.
The heat exchange tube on be provided with the multilayer along the axial and radially disperse the heat exchanger fin that sets up all around.
The axial section of the inner shell is square, and the ratio of the inner width of the inner shell to the diameter of the heat exchange plate is controlled to be (1.75-2): 1.
The inner shell is wrapped with a heat preservation layer, and the heat preservation layer is sleeved with an outer protection shell.
The plurality of heat storage module units are arranged on the support frame in a clearance fit mode, so that shrinkage gaps are formed between adjacent heat storage module units in the heat storage module group, and a multi-layer and multi-column array arrangement structure is realized.
And the longitudinal two ends of the heat storage module group are respectively provided with a positioning plate from which the heat exchange tube can extend.
The small-diameter end water distributor and the large-diameter end water distributor are both arranged outside the box body.
The reducing connecting elbow is coated with a heat-insulating layer.
Compared with the prior art, the utility model, following technological effect has:
(I) the utility model discloses a modular heat-retaining module unit structural design, only heat transfer pipeline all the way can make the inside heat transfer effect maximize of structure, has promoted heat storage volume and heat-retaining efficiency. The utility model discloses a heat transfer pipeline is the vertical parallel heat transfer medium reducing S-shaped route that stands side by side of multiseriate, high temperature heat transfer medium flows to the heat exchange tube of big pipe diameter from the heat exchange tube of little pipe diameter, low temperature heat transfer medium flows to the heat exchange tube of little pipe diameter from the heat exchange tube of big pipe diameter, heat transfer area of contact is little when heat transfer medium temperature is high, the velocity of flow is fast, heat transfer area of contact is big when heat transfer medium temperature is low, the velocity of flow is slow, through the method that changes area of contact and velocity of flow, realize that heat transfer volume at every.
(II) the channel-changing type flow channel design of the utility model improves the heat release balance of the whole heat storage device; compared with the heat storage device with the same volume, the heat storage quantity is improved.
(III) the utility model provides a heat-retaining equipment structure of optimization for heat-retaining equipment can increase or change the heat-retaining module according to actual conditions, has reduced use and maintenance cost.
Drawings
Fig. 1 is the internal structure schematic diagram of the modular solid-liquid two-phase heat storage device of the present invention.
Fig. 2 is a schematic diagram of the overall structure of the heat storage module group of the present invention.
Fig. 3 is a schematic structural diagram of the reducing connecting pipe.
Fig. 4 is a schematic structural view of the heat storage module unit.
Fig. 5 is a schematic diagram of the overall structure of a multi-operation mode solid-liquid two-phase heat storage system.
The meaning of the individual reference symbols in the figures is: 1-a heat storage device, 2-a user side circulation pipeline, 3-a system side multi-operation mode circulation pipeline and 4-a heat exchanger;
101-a box body, 102-a heat storage module group, 103-a heat storage module unit, 104-a reducing connecting elbow, 105-a reducing connecting pipe, 106-a small-diameter end water distributor, 107-a heat exchange medium small-diameter end connector, 108-a connecting pipe, 109-a large-diameter end water distributor, 110-a heat exchange medium large-diameter end connector, 111-a support frame, 112-a contraction gap and 113-a positioning plate;
10301-inner shell, 10302-heat exchange tube, 10303-heat storage material, 10304-heat exchange sheet, 10305-heat insulation layer, 10306-outer protective shell;
201-user side circulation pump, 202-end user;
301-system side circulation pump, 302-first valve, 303-heat source, 304-second valve, 305-third valve, 306-fourth valve, 307-fifth valve, 308-sixth valve, 309-seventh valve;
401-user side heat exchange tube, 402-system side heat exchange tube.
The following examples are provided to explain the present invention in further detail.
Detailed Description
The utility model discloses the main technical problem who solves includes: the problems that the heat storage device in the prior art is uneven in heat distribution, layered in temperature and incomplete in change of the physical state of part of the heat storage material are solved; the structural form of the equipment is improved, and the problem that the heat storage capacity of the existing equipment needs to be improved is solved; the feasibility of equipment inspection and maintenance is improved, and the stability of equipment operation and maintenance is improved; the running cost of the system is reduced.
It is to be noted that all the components and materials of the present invention are known in the art, and the components and materials are not specifically described.
It should be noted that, the pipe diameter of the heat exchange pipe in the present invention is the inner diameter of the heat exchange pipe.
It should be noted that, in the present invention, the inner housing is axial, i.e. longitudinal.
The following embodiments of the present invention are given, and it should be noted that the present invention is not limited to the following embodiments, and all the equivalent transformations made on the basis of the technical solution of the present application all fall into the protection scope of the present invention.
Example 1:
the embodiment provides a modularized solid-liquid two-phase heat storage device, as shown in fig. 1 to 4, which includes a box 101, a heat storage module group 102 is installed in the box 101 along a longitudinal direction, the heat storage module group 102 includes a plurality of heat storage module units 103 arranged longitudinally, the plurality of heat storage module units 103 are in a multi-layer and multi-row array arrangement structure, a plurality of heat storage module units 103 with the same number are transversely arranged in each layer, and a plurality of layers of heat storage module units 103 are vertically arranged;
the heat storage module unit 103 comprises a closed inner shell 10301, a heat exchange tube 10302 with two ends extending out of the axial end face of the inner shell 10301 is arranged in the inner shell 10301, and a cavity between the heat exchange tube 10302 and the inner shell 10301 is filled with a heat storage material 10303;
in the heat storage module group 102, the pipe diameters of the heat exchange pipes 10302 from the top layer to the bottom layer or from the bottom layer to the top layer are gradually increased layer by layer, and the heat exchange pipes 10302 in the multiple layers of heat storage module units 103 in the same row are sequentially connected in series through the reducing connecting elbows 104 to form multiple rows of heat exchange medium reducing S-shaped passages which are vertically parallel and parallel;
in the heat storage module group 102, the end portions of the plurality of heat exchange tubes 10302 having the smallest tube diameter at the top vertical layer or the bottom vertical layer are connected to the small-diameter-end water distributor 106 through the reducing connection tube 105, and the small-diameter-end water distributor 106 is connected to the heat exchange medium small-diameter-end connector 107; the end parts of the plurality of heat exchange tubes 10302 with the largest tube diameter at the bottom layer or the top layer are connected with a large-diameter end water distributor 109 through connecting tubes 108, and the large-diameter end water distributor 109 is connected with a heat exchange medium large-diameter end joint 110, so that a plurality of rows of parallel heat exchange medium reducing S-shaped passages are connected in parallel between the heat exchange medium small-diameter end joint 107 and the heat exchange medium large-diameter end joint 110.
As a preferable scheme of this embodiment, in the heat storage module group 102, the pipe diameter of the heat exchange pipe 10302 of the heat storage module units 103 in two adjacent layers increases by 2% to 10%. According to the temperature change of the heat exchange medium in the flowing process, the pipe diameter of the heat exchange pipe in each layer of heat exchange module unit is changed, and a pipe diameter-variable passage is designed, so that the contact area and the flow velocity of the heat exchange medium in each layer are balanced, and the phenomena of local overheating and temperature stratification in the prior art are improved. The thermal stress of equipment operation is reduced.
As a preferable scheme of this embodiment, in the heat storage module group 102, the heat exchange tubes 10302 of the heat storage module units 103 located in the same layer have the same tube diameter. Because temperature difference occurs in the heat storage and release processes, in order to improve the nonuniformity of thermal stress distribution in the heat storage and release processes and prevent the heat storage module units 103 from excessively deforming, the pipe diameters of the heat exchange pipes 10302 of the heat storage module units 103 located in the same layer are set to be equal, so that the problems can be effectively avoided.
As a preferable scheme of this embodiment, a plurality of layers of heat exchanging fins 10304 radially arranged around are axially arranged on the heat exchanging pipe 10302. Further preferably, the axial section of the inner shell 10301 is square, and the ratio of the inner width of the inner shell 10301 to the diameter of the heat exchange plate 10304 is controlled to be (1.75-2): 1. The heat exchange plates 10304 ensure uniformity of heat storage inside each heat storage module unit 103.
In this embodiment, the heat storage material 10303 can be selected from a low temperature heat storage material, a medium temperature heat storage material, or a high temperature heat storage material as needed. The heat storage material 10303 absorbs heat from the heat exchange medium in the heat exchange tube 10302 and the heat exchange fins 10304 to reach a melting point, so that the solid-state to liquid-state conversion is realized, and the heat is stored in the phase conversion process. The whole heat storage module unit 103 forms a closed space inside, and leakage does not occur in the process that the heat storage material 10303 absorbs heat and changes into a liquid state. Due to the independent sealing design of each heat storage module unit 103, other heat storage modules cannot be influenced when the heat exchange pipeline is corroded and leaked, and the operation safety of the device is ensured.
As a preferable scheme of this embodiment, the inner housing 10301 is covered by a heat insulating layer 10305, and the heat insulating layer 10305 is covered by an outer protective housing 10306. The inner housing 10301 is insulated to avoid heat loss during heat exchange. The reducing connecting elbow 104 is covered with an insulating layer to avoid heat loss in the heat exchange process. In order to reduce heat loss and improve the heat efficiency of the heat storage device, heat preservation is performed outside each elbow connecting pipeline inside the box body 101 except for the heat preservation layer designed outside each heat storage module unit 103.
As a preferable scheme of this embodiment, the plurality of heat storage module units 103 are installed on the support frame 111 in a clearance fit manner, so that in the heat storage module group 102, a contraction gap 112 is formed between adjacent heat storage module units 103, and a multi-layer and multi-column array arrangement structure is implemented. The contraction gap 112 leaves a deformation space for the deformation of the heat storage module unit 103, thereby avoiding adverse effects caused by direct stacking and extrusion of the heat storage module unit 103. The heat storage module group 102 can be realized by increasing or decreasing the number of the heat storage module units 103 according to different heat requirements.
As a preferable scheme of this embodiment, the heat storage module set 102 is provided with positioning plates 113 at two longitudinal ends thereof, respectively, where the heat exchange tubes 10302 can extend out. The positioning plate 113 aligns and positions the plurality of heat storage module units 103 in the longitudinal direction. The positioning plate 113 is openable for replacement and maintenance of each heat storage module unit 103.
As a preferable mode of this embodiment, the small-diameter-end water distributor 106 and the large-diameter-end water distributor 109 are both disposed outside the tank 101.
The utility model discloses a double-phase heat-retaining device of modular solid-liquid is when using, confirms every layer of heat-retaining modular unit 103's quantity and vertical many layers of heat-retaining modular unit 103 that set up in the heat storage module group 102 according to actual need. The heat exchange medium small-diameter end joint 107 is connected to the high-temperature side of the heat exchange medium, and the heat exchange medium large-diameter end joint 110 is connected to the low-temperature side of the heat exchange medium. During heat storage, a heat exchange medium is high in temperature, the heat exchange medium enters the small-diameter end water distributor 106 from the small-diameter end connector 107, the heat exchange medium is evenly distributed in each heat storage module unit 103 with the smallest pipe diameter at the topmost layer or the bottommost layer in the small-diameter end water distributor 106, the heat exchange medium enters the next layer or the previous layer through the reducing connection elbow 104 after heat exchange and continues to exchange heat until the heat exchange is carried out in the heat storage module unit 103 with the largest pipe diameter at the bottommost layer or the topmost layer, heat of the heat exchange medium is stored in the heat storage material, and the heat exchange medium is collected through the large-diameter end water distributor 109 after the temperature of the heat exchange medium is reduced and is discharged from the large-diameter end connector 110. During heat release, the heat exchange medium is at a low temperature, runs in the opposite direction, enters from the large-diameter end joint 110 of the heat exchange medium and is discharged from the small-diameter end joint 107 of the heat exchange medium.
Example 2:
the embodiment provides a solid-liquid two-phase heat storage system with multiple operation modes, as shown in fig. 5, which includes a user side circulation pipeline 2 with closed circulation and a system side circulation pipeline 3 with multiple operation modes with closed circulation, and is characterized in that a user side circulation pump 201, a user side heat exchange pipe 401 of a heat exchanger 4 and a tail end user 202 are sequentially connected in series on the user side circulation pipeline 2 to form a user side heat exchange medium closed circulation loop;
the system side multi-operation mode circulating pipeline 3 comprises a system side circulating pump 301, a first valve 302, a heat source 303, a second valve 304, a heat storage device 1, a third valve 305, a fourth valve 306 and a system side heat exchange medium closed circulation loop formed by system side heat exchange pipes 402 of the heat exchanger 4 which are sequentially connected in series;
a first bypass connected in parallel with the system side circulating pump 301, the first valve 302, the heat source 303 and the second valve 304 is further arranged on the system side heat exchange medium closed circulation loop, and a fifth valve 307 is arranged on the first bypass;
a second bypass connected with the first valve 302, the heat source 303 and the second valve 304 in parallel is further arranged on the system side heat exchange medium closed circulation loop, and a sixth valve 308 is arranged on the second bypass;
a third bypass connected with the second valve 304, the heat storage device 1 and the third valve 305 in parallel is further arranged on the system side heat exchange medium closed circulation loop, and a seventh valve 309 is arranged on the third bypass.
Specifically, the system side multi-operation mode circulation pipeline 3 comprises a heat storage mode circulation pipeline, a heat release mode circulation pipeline, a heat source independent heat supply mode circulation pipeline, a heat storage combined heat source heat supply mode circulation pipeline and a heat release combined heat source heat supply mode circulation pipeline;
the heat storage mode circulating pipeline is a circulating pipeline which is formed by a system side circulating pump 301, a first valve 302, a heat source 303, a seventh valve 309, a third valve 305, the heat storage device 1 and a fifth valve 307 and through which a heat exchange medium flows in sequence;
the heat release mode circulation pipeline is a circulation pipeline which is formed by a system side circulation pump 301, a sixth valve 308, a heat storage device 1, a third valve 305, a fourth valve 306 and a system side heat exchange pipe 402 of the heat exchanger 4 and through which heat exchange media sequentially flow;
the heat source independent heat supply mode circulating pipeline is a circulating pipeline formed by a system side circulating pump 301, a first valve 302, a heat source 303, a seventh valve 309 and a fourth valve 306 through which heat exchange media sequentially flow and a system side heat exchange pipe 402 of the heat exchanger 4;
the heat storage combined heat source heat supply mode circulating pipeline is a parallel circulating pipeline in which the heat storage mode circulating pipeline and the heat source independent heat supply mode circulating pipeline run simultaneously, and the heat source 303 supplies heat to the heat exchanger 4 while supplying heat and storing heat to the solid-liquid two-phase heat storage device 1; specifically, the heat storage combined heat source heat supply mode circulation pipeline comprises a main pipeline and two parallel branches, wherein one main pipeline comprises a system side circulation pump 301, a first valve 302, a heat source 303 and a seventh valve 309 through which heat exchange media sequentially flow, and one branch pipeline comprises a third valve 305, a heat storage device 1 and a fifth valve 307 through which heat exchange media sequentially flow; the other branch comprises a fourth valve 306 through which the heat exchange medium flows in sequence and a system side heat exchange pipe 402 of the heat exchanger 4.
The heat release combined heat source heat supply mode circulating pipeline is a circulating pipeline formed by a system side circulating pump 301, a first valve 302, a heat source 303, a second valve 304, a heat storage device 1, a third valve 305, a fourth valve 306 and a system side heat exchange pipe 402 of a heat exchanger 4 through which heat exchange media sequentially flow.
Specifically, the heat storage device is a modularized solid-liquid two-phase heat storage device in example 1, and the modularized solid-liquid two-phase heat storage device is provided,
the heat storage device 1 comprises a heat exchange medium reducing passage inside, one end of the heat exchange medium reducing passage is connected with a heat exchange medium large-diameter end joint 110, and the other end of the heat exchange medium reducing passage is connected with a heat exchange medium small-diameter end joint 107; the second valve 304 is connected to the heat exchange medium large-diameter end fitting 110 of the heat storage apparatus 1, and the third valve 305 is connected to the heat exchange medium small-diameter end fitting 107 of the heat storage apparatus 1. The low-temperature heat exchange medium is ensured to flow in from the heat exchange medium large-diameter end joint 110 and flow out from the heat exchange medium small-diameter end joint 107, and the high-temperature heat exchange medium flows in from the heat exchange medium small-diameter end joint 107 and flows out from the heat exchange medium large-diameter end joint 110.
As a preferable scheme of this embodiment, the heat source 303 is an electric boiler or a heat source such as a solar water heater that can be selected as needed to match with the system.
The utility model discloses a double-phase heat-retaining system of solid-liquid can switch as required under a plurality of operational mode, and the system architecture design of many operational mode has reduced the system running cost. Through different valve switching, the running time and the output of the energy storage device and the heat source can be flexibly and reasonably scheduled, and the running cost of the whole system is reduced.
The utility model discloses an energy storage system of many operational modes uses the double-phase heat-retaining device of modular solid-liquid to the system in, the two is in coordination each other, jointly increase effect, the inside of the double-phase heat-retaining device of modular solid-liquid includes heat transfer medium reducing route, the energy storage system of many operational modes can ensure that the high temperature heat transfer medium among the double-phase heat-retaining device of modular solid-liquid flows in from the tip of reducing pipeline, the tip flows, low temperature heat transfer medium flows in from the tip of reducing pipeline, the tip flows, through the method that changes contact area and velocity of flow, realize that heat transfer capacity at every turn keeps the same level.
The utility model discloses a system design of the intensification of double-phase heat-retaining system of solid-liquid reduces the configuration quantity of system side circulating pump, has reduced the investment of equipment.
The solid-liquid two-phase heat storage system with multiple operation modes comprises a heat storage mode, a heat release mode, a heat source independent heat supply mode, a heat storage combined heat source heat supply mode and a heat release combined heat source heat supply mode, and the operation process of the specific multiple operation modes is as follows;
a heat storage mode: the heat source 303 supplies heat to the heat storage device 1, and the heat storage device 1 stores heat. In this mode, the first valve 302, the seventh valve 309, the third valve 305, and the fifth valve 307 are open, and the remaining valves are closed. Starting the system side circulating pump 301, circulating the heat exchange medium in the heat storage mode circulating pipeline, and performing heat exchange in the heat storage device 1 to ensure that the heat storage material 10303 in the heat storage device 1 absorbs heat and gradually converts the heat from a solid state to a liquid state, so as to store the absorbed energy; after the temperature of the heat exchange medium after heat exchange is reduced, the heat exchange medium returns to the heat source 303 to be heated again, and the circulation is performed.
When the heat storage device 1 is a modular solid-liquid two-phase heat storage device, the heat exchange medium flows in from the heat exchange medium small-diameter end joint 107 of the modular solid-liquid two-phase heat storage device, and flows out from the heat exchange medium large-diameter end joint 110 of the modular solid-liquid two-phase heat storage device.
Heat release pattern: the heat storage device 1 independently supplies heat to the heat exchanger 4. In this mode, the heat source 303 stops supplying heat, the sixth valve 308, the third valve 305, and the fourth valve 306 are opened, and the remaining valves are closed. The system side circulating pump 301 is started, the heat exchange medium circularly flows in the heat release mode circulating pipeline, the heat exchange medium carries out heat exchange in the heat storage device 1, the temperature of the heat exchange medium is increased after the heat exchange medium absorbs heat stored in the heat storage material 10303 in the heat storage device 1, the heat exchange medium is conveyed into the heat exchanger 4 under the action of the system side circulating pump 301 to carry out heat exchange, the heat is transferred to the heat exchanger 4, the heat is transferred to the heat transfer medium in the user side circulating pipeline 2 through the heat exchange, and the heat is supplied to the end user 202 under the driving of the user side circulating pump 201. The heat storage material 10303 in the heat storage device 1 gradually changes from a liquid state to a solid state again due to release of latent heat and sensible heat, and thus the heat release and supply mode is completed. The mode is mainly operated at the peak of electricity price or the peak of load, so as to reduce peak load and reduce the peak operation cost.
When the heat storage device 1 is a modular solid-liquid two-phase heat storage device, the heat exchange medium flows in from the heat exchange medium large-diameter end joint 110 of the modular solid-liquid two-phase heat storage device, and flows out from the heat exchange medium small-diameter end joint 107 of the modular solid-liquid two-phase heat storage device.
The heat source independent heating mode comprises the following steps: heat is independently supplied to the heat exchanger 4 by the heat source 303. In this mode, the heat storage device 1 stops operating, the first valve 302, the seventh valve 309, and the fourth valve 306 are opened, and the remaining valves are closed. The system side circulating pump 301 is started, the heat exchange medium circularly flows in the heat source independent heat supply mode circulating pipeline, and is conveyed to the heat exchanger 4 under the action of the system side circulating pump 301 to exchange heat, the heat is transferred to the heat exchanger 4, the heat is transferred to the heat transfer medium in the user side circulating pipeline 2 through the heat exchange, and the heat is supplied to the end user 202 under the driving of the user side circulating pump 201.
The heat storage combined heat source heating mode comprises the following steps: the heat source 303 supplies heat to the heat storage device 1 and also supplies heat to the heat exchanger 4, and because the heat storage mode circulation pipeline and the heat source independent heat supply mode circulation pipeline are connected in parallel, the heat storage mode circulation pipeline and the heat source independent heat supply mode circulation pipeline can be simultaneously operated, namely, two operation modes of a heat source independent heat supply mode and a heat storage mode are simultaneously operated, and the heat source 303 supplies heat to the two modes at the same time.
The heat release is combined with the heat source to supply heat mode: heat is simultaneously supplied to the heat exchanger 4 by the heat source 303 and the heat storage device 1. In this mode, the first valve 302, the second valve 304, the third valve 305, and the fourth valve 306 are open, and the remaining valves are closed. And starting the system side circulating pump 301, and circulating the heat exchange medium in the heat release combined heat source heat supply mode circulating pipeline. In the mode, the heat source 303 can reduce the load, reduce the water outlet temperature, and achieve stable heat supply after being lifted again by the heat storage device 1. The power consumption of the heat source is reduced, and the operation cost is saved.
Claims (10)
1. A modularized solid-liquid two-phase heat storage device comprises a box body (101), and is characterized in that a heat storage module group (102) is longitudinally arranged in the box body (101), the heat storage module group (102) comprises a plurality of heat storage module units (103) which are longitudinally arranged, the heat storage module units (103) are in a multi-layer and multi-row array arrangement structure, a plurality of heat storage module units (103) with the same number are transversely arranged on each layer, and a plurality of layers of heat storage module units (103) are vertically arranged;
the heat storage module unit (103) comprises a closed inner shell (10301), a heat exchange tube (10302) with two ends extending out of the axial end face of the inner shell (10301) is installed in the inner shell (10301), and a cavity between the heat exchange tube (10302) and the inner shell (10301) is filled with a heat storage material (10303);
in the heat storage module group (102), the pipe diameters of heat exchange pipes (10302) from the top layer to the bottom layer or from the bottom layer to the top layer are gradually increased layer by layer, and the heat exchange pipes (10302) in the heat storage module units (103) in the same row are sequentially connected in series through reducing connecting elbows (104) to form a plurality of rows of heat exchange medium reducing S-shaped passages which are vertically parallel and parallel;
in the heat storage module group (102), the end parts of a plurality of heat exchange tubes (10302) with the smallest tube diameter at the top vertical layer or the bottom vertical layer are connected with a small-diameter end water distributor (106) through reducing connecting tubes (105), and the small-diameter end water distributor (106) is connected with a heat exchange medium small-diameter end connector (107); the end parts of a plurality of heat exchange tubes (10302) with the largest tube diameter at the bottommost layer or the topmost layer are connected with a large-diameter end water distributor (109) through connecting tubes (108), and the large-diameter end water distributor (109) is connected with a heat exchange medium large-diameter end connector (110), so that a plurality of rows of parallel heat exchange medium reducing S-shaped passages are connected in parallel between the heat exchange medium small-diameter end connector (107) and the heat exchange medium large-diameter end connector (110).
2. The modular solid-liquid two-phase heat storage device as claimed in claim 1, wherein in the heat storage module group (102), the heat exchange tubes (10302) of the heat storage module units (103) in two adjacent layers have tube diameters increasing by 2-10%.
3. The modular solid-liquid two-phase heat storage device as claimed in claim 1, wherein in the heat storage module group (102), the heat exchange tubes (10302) of the heat storage module units (103) in the same layer have the same tube diameter.
4. The modular solid-liquid two-phase heat storage device as claimed in claim 1, characterised in that the heat exchange tubes (10302) are provided with a plurality of layers of heat exchanger fins (10304) radially arranged around in an axial direction.
5. The modular solid-liquid two-phase heat storage device as claimed in claim 4, characterized in that the axial cross section of the inner shell (10301) is square, and the ratio of the inner width of the inner shell (10301) to the diameter of the heat exchanger fin (10304) is controlled to be (1.75-2): 1.
6. The modular solid-liquid two-phase heat storage device as claimed in claim 1, characterized in that the inner housing (10301) is coated with a layer of insulating layer (10305), and the insulating layer (10305) is coated with an outer protective housing (10306).
7. The modular solid-liquid two-phase heat storage device as claimed in claim 1, wherein the plurality of heat storage module units (103) are installed on the support frame (111) in a clearance fit manner, so that in the heat storage module group (102), contraction gaps (112) are formed between adjacent heat storage module units (103), and a multi-layer and multi-row array arrangement structure is realized.
8. The modular solid-liquid two-phase heat storage device as claimed in claim 1, wherein the heat storage module group (102) is provided at its longitudinal ends with positioning plates (113) from which heat exchange tubes (10302) can extend.
9. The modular solid-liquid two-phase heat storage device as claimed in claim 1, characterized in that the small-diameter end water distributor (106) and the large-diameter end water distributor (109) are both arranged outside the tank (101).
10. The modular solid-liquid two-phase heat storage device as claimed in claim 1, characterized in that the reducing connecting bend (104) is coated with a heat insulating layer.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111503713A (en) * | 2020-04-27 | 2020-08-07 | 西安联创分布式可再生能源研究院有限公司 | Modular solid-liquid two-phase heat storage device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111503713A (en) * | 2020-04-27 | 2020-08-07 | 西安联创分布式可再生能源研究院有限公司 | Modular solid-liquid two-phase heat storage device |
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