CN111336839A - Shell-and-tube heat exchanger with variable kernel spacing - Google Patents
Shell-and-tube heat exchanger with variable kernel spacing Download PDFInfo
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- CN111336839A CN111336839A CN202010050719.1A CN202010050719A CN111336839A CN 111336839 A CN111336839 A CN 111336839A CN 202010050719 A CN202010050719 A CN 202010050719A CN 111336839 A CN111336839 A CN 111336839A
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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
- F28D7/16—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 the conduits being arranged in parallel spaced relation
- F28D7/1684—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 the conduits being arranged in parallel spaced relation the conduits having a non-circular cross-section
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/18—Water-storage heaters
- F24H1/20—Water-storage heaters with immersed heating elements, e.g. electric elements or furnace tubes
- F24H1/201—Water-storage heaters with immersed heating elements, e.g. electric elements or furnace tubes using electric energy supply
- F24H1/202—Water-storage heaters with immersed heating elements, e.g. electric elements or furnace tubes using electric energy supply with resistances
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- Combustion & Propulsion (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
Abstract
The invention provides a shell-and-tube heat exchanger with variable kernel spacing, which comprises a shell, wherein end sockets are respectively arranged at two ends of the shell, tube plates are arranged at the connecting positions of the end sockets and the shell, a heat exchange tube is connected with the tube plates at the two ends, the heat exchange tube comprises an outer tube and a kernel component arranged in the outer tube, and the kernel component extends in the extending direction of the heat exchange tube; a plurality of inner core members are provided in the heat exchange tube, and the spacing between the inner core members becomes smaller from the inlet of the heat exchange tube to the outlet of the heat exchange tube. The invention further improves the heating uniformity and the heating efficiency through the change of the distance between the inner cores.
Description
The application is a divisional application aiming at 18 months 12 and 2018, application number 2018115502827 and invention name 'an electric heating tube shell-and-shell heat exchanger'.
Technical Field
The invention relates to a shell-and-tube heat exchanger, in particular to a shell-and-tube heat exchanger for generating hot water with different temperatures.
Background
At present, a shell-and-tube heat exchanger is the most widely used heat exchanger structure form in an energy engineering project, the usage of the shell-and-tube heat exchanger accounts for 70% of the usage of all heat exchangers, and the shell-and-tube heat exchanger belongs to one of dividing wall type heat exchangers. The shell-and-tube heat exchanger has the characteristics of firm structure and reliable use; the history is long, and each technical link of manufacturing and using is mature; the adaptability is higher, and the application range is wide. The shell side of the traditional shell-and-tube heat exchanger is heated by exchanging a cold source and a heat source, and generally, the temperature of one fluid is increased while the temperature of the other fluid is decreased. But cannot achieve simultaneous heating of both fluids.
In addition, in order to improve and enhance the working efficiency of the heat exchanger to achieve the purpose of energy saving and consumption reduction, the most important means is to improve the flow form of the fluid inside the heat exchanger, because the factor plays a determining role in the heat transfer performance and power consumption of the shell-and-tube heat exchanger. Because the internal heat exchange medium has various flow forms, which are mainly different from the flushing flow to the tube bundle, the flow forms can be transverse flow, longitudinal flow and spiral flow based on the flow form.
In view of the above problems, the present invention is an improvement on the basis of the previous invention, and provides a new heat exchanger, so as to solve the problem that the heat exchanger can only realize one fluid heating temperature. Meanwhile, the heating core component is arranged in the tube, and the fluid is fully heated in the heat exchange tube by setting the shape of the core component, so that the heat exchange effect is improved.
Disclosure of Invention
The invention aims to provide a heat exchanger with a novel structure, which can heat two kinds of fluid simultaneously, and is provided with an internal heating core component to achieve the effect of enhancing heat transfer.
In order to achieve the purpose, the technical scheme of the invention is as follows:
a shell-and-tube heat exchanger comprises a shell, wherein end sockets are arranged at two ends of the shell respectively, tube plates are arranged at the connecting positions of the end sockets and the shell, a heat exchange tube is connected with the tube plates at the two ends, the heat exchange tube comprises an outer tube and an inner core part arranged in the outer tube, and the inner core part extends in the extending direction of the heat exchange tube; the electric heating element is provided in the core member, and the heating power of the electric heating element per unit length in the extending direction of the heat exchanging pipe is larger the farther from the center of the core member.
Preferably, the further away from the center of the core member, the greater and greater the magnitude of the heating power of the electric heating element per unit length in the extending direction of the heat exchange tube is increased.
Preferably, the electrical heating element is a resistance heater.
A shell-and-tube heat exchanger comprises a shell, wherein end sockets are arranged at two ends of the shell respectively, tube plates are arranged at the connecting positions of the end sockets and the shell, a heat exchange tube is connected with the tube plates at the two ends, the heat exchange tube comprises an outer tube and an inner core part arranged in the outer tube, and the inner core part extends in the extending direction of the heat exchange tube; the core component is composed of a regular quadrilateral through hole and a regular octagonal through hole, the side length of the regular quadrilateral through hole is equal to that of the regular octagonal through hole, four sides of the regular quadrilateral through hole are respectively sides of four different regular octagonal through holes, and four sides of the regular octagonal through hole, which are not connected with each other, are respectively sides of four different regular quadrilateral through holes; an electric heating element is arranged in the regular quadrilateral through hole.
Preferably, the cross section of the heat exchange tube is a regular quadrangle.
Preferably, the inner wall of the heat exchange tube is provided with a groove, and the outer end of the inner core member is arranged in the groove.
Preferably, the heat exchange tube is formed by welding a multi-stage structure, and the core member is arranged at the joint of the multi-stage structure.
Preferably, the electrical heating element is a resistance heater.
Preferably, the resistive heater fills the entire square channel.
Preferably, the core member is provided in plurality at intervals along the extending direction of the heat exchange tube.
Preferably, the further away from the inlet of the heat exchange tube, the greater the heating power per unit length of the resistance heater.
Preferably, the heating power of the resistance heater per unit length is increased by a larger and larger margin the further away the heat exchange tube inlet is.
Preferably, the center of the inner core component is a regular octagonal channel, the regular quadrilateral channel is a two-layer structure surrounding the inner core component, the outermost layer is the regular octagonal channel, and the side length of the outer tube is 8 times that of the regular quadrilateral channel.
Preferably, the heating power of each electric heating element of the first layer is W1, the heating power of each electric heating element of the second layer is W2, the length of the inner core component is L1, and the side length of the regular quadrangle is L2, so that the following requirements are met:
W2/W1= a-b LN (L1/L2); wherein a, b are parameters, 2.978< a <2.982,0.79< b < 0.81;
1.15<W2/W1<1.75；5.0<L1/L2<9.0；
the total heating power of the first layer and the second layer of the single heat exchange tube is M, and 300W < M < 500W.
Preferably, a =2.98 and b = 0.80.
Compared with the prior art, the invention has the following advantages:
1) the invention further improves the heating uniformity and the heating efficiency by setting the change of the heating power of the electric heating element in the heat exchange tube away from the center of the kernel component.
2) The invention designs a novel shell-and-tube heat exchanger with a kernel component heating structure, through the structure, hot fluid can be rapidly provided, and the shell-and-tube heat exchanger has the functions of rapid heating, uniform temperature distribution, safety and reliability, and improves the heating efficiency.
3) The invention further improves the heating uniformity and the heating efficiency by setting the change of the heating power of the electric heating element in the heat exchange tube away from the inlet of the heat exchange tube.
4) The invention designs the vertical direction interval distribution of the inner core components of the heat exchange tube, and can further improve the heating efficiency.
5) The invention designs the change of the heating power of different electric heating elements in the heat exchange tube along the length direction of the heat exchange tube, and can further improve the safety performance and the heating performance of the device.
6) The invention determines the optimal proportional relation of the electric heating powers of different layers through numerical simulation and a large number of experiments, further improves the heating uniformity and the heating efficiency, and provides an optimal reference basis for the design of the heat exchange tube with the structure.
7) According to the invention, through numerical simulation and a large number of experiments, the optimal relation of each size of the core component is determined, and the heating uniformity and the heating efficiency are further improved.
Drawings
FIG. 1 is a schematic structural view of a shell-and-tube heat exchanger of the present invention.
FIG. 2 is a schematic view of the heat exchange tube structure of the shell-and-tube heat exchanger of the present invention.
FIG. 3 is a cross-sectional view of the core member of the heat exchange tube.
FIG. 4 is a cross-sectional view of the inner core member A-A of the heat exchange tube of FIG. 3.
FIG. 5 is a schematic cross-sectional view of a heat exchange tube.
Figure 6 is a schematic view of the arrangement of the partitioning device of the present invention within a heat exchange tube.
The reference numbers are as follows: the tube-side heat exchanger comprises a front end enclosure 1, an end enclosure flange 2, a front tube plate 3, a shell 4, an inner core component 5, a heat exchange tube 6, a rear tube plate 7, an end enclosure flange 8, a rear end enclosure 9, a support 10, a support 11, a tube-side inlet tube 12, a tube-side outlet tube 13, a shell-side inlet tube 14, a shell-side outlet tube 15, an electric heating element 16, a regular quadrilateral through hole 51, a regular octagonal through hole 52 and a side 53.
Detailed Description
The following detailed description of embodiments of the invention refers to the accompanying drawings.
Herein, if not specifically stated, "/" denotes division, "×", "x" denotes multiplication, referring to formulas.
As shown in fig. 1, the shell-and-tube heat exchanger includes a shell 4, a heat exchange tube 6, a tube-side inlet tube 12, a tube-side outlet tube 13, a shell-side inlet connecting tube 14, and a shell-side outlet connecting tube 15; a heat exchange tube bundle consisting of a plurality of heat exchange tubes 6 arranged in parallel is connected on the front tube plate 3 and the rear tube plate 7; the front end of the front tube plate 3 is connected with the front seal head 1, and the rear end of the rear tube plate 7 is connected with the rear seal head 9; the tube pass inlet pipe 12 is arranged on the rear seal head 9; the tube pass outlet pipe 13 is arranged on the front seal head 1; the shell side inlet connecting pipe 14 and the shell side outlet connecting pipe 15 are both arranged on the shell 4; fluid enters from tube side inlet tube 12, exchanges heat through the heat exchange tubes, and exits from tube side outlet tube 13.
As a modification, an electric heating element 16 is provided in the heat exchange tube 6. By arranging the electric heating elements in the heat exchange tubes, the output of heating fluid with different temperatures can be ensured. The electric heating element 16 heats the fluid in the heat exchange tube 6 first, and then the heated fluid heats the fluid in the shell side through the tube wall of the heat exchange tube 6, so that the fluid with different temperatures in the tube side and the shell side is heated through the electric heating element 16, for example, the fluid with high temperature is generated in the tube side, and the heating fluid with low temperature is generated in the shell side, so as to meet different application requirements.
Preferably, the fluid is water. Further preferably, the fluid is a medicinal liquid, such as a medicinal liquid for fumigation. For example, a liquid medicine for fumigation and washing is contained in the housing.
As shown in fig. 3 to 4, an inner core member 5 is provided inside the heat exchange tube 6. The core component 5 is constructed as shown in fig. 3-4. The inner core member 5 extends in the direction in which the heat exchange tube 6 extends; the core component 5 is composed of a regular quadrilateral through hole 51 and a regular octagonal through hole 52, the side length of the regular quadrilateral through hole 51 is equal to that of the regular octagonal through hole 52, four sides 53 of the regular quadrilateral through hole are respectively sides 53 of four different regular octagonal through holes, and four sides of the regular octagonal through hole which are not connected with each other are respectively sides of four different regular quadrilateral through holes; the electric heating element 16 is arranged in the square through hole 51.
According to the invention, by arranging the shell-and-tube heat exchanger with a novel heating structure, the heating elements are uniformly distributed around the plurality of regular octagonal channels by the heating structure, so that fluid can enter the regular octagonal channels and can be uniformly heated by the heating elements.
Through the structure arrangement, hot fluids with different temperatures can be generated simultaneously, so that the shell-and-tube heat exchanger has multiple functions, and the utilization range of the shell-and-tube heat exchanger is expanded.
The invention provides a heat exchanger with a novel structure combining a novel regular quadrilateral through hole and a novel regular octagonal through hole, wherein the included angles formed by the edges of the formed regular octagonal holes are more than or equal to 90 degrees through the regular quadrilateral and the regular octagonal, so that fluid can fully flow through each position of each hole, and the short circuit of fluid flow is avoided or reduced. According to the invention, through reasonable layout, the through holes in the regular quadrangle and the regular octagon are uniformly distributed, so that the fluid on the whole cross section is uniformly divided, and the problem of nonuniform division along the circumferential direction in the prior art is avoided.
Preferably, the heat exchange tubes 6 are arranged in a horizontal direction.
Preferably, the outer tube of the heat exchange tube is the outer wall surface of the core member. Preferably, the heat exchange tube and the core member are integrally manufactured.
Preferably, the cross section of the heat exchange tube 6 is a regular quadrangle.
Preferably, the wires connecting the heating elements 16 enter through the tube side inlet tube 12 and/or the tube side outlet tube 13.
Preferably, the inner wall of the heat exchange tube 6 is provided with grooves, and the outer wall surface of the core member 5 is provided in the grooves. By such an arrangement, the firmness of the installation of the core component can be further improved.
Preferably, the heat exchange tube 6 is formed by welding a plurality of stages, and the core member 7 is provided at the joint of the plurality of stages. Through such setting, can be so that processing is convenient, save the cost.
Preferably, the electrical heating element 16 is a resistance heater.
Preferably, the resistive heater 16 fills the entire square channel. Through so setting up can guarantee the wall contact of electric heating element and regular quadrangle passageway, further improve heating efficiency.
Preferably, the farther the center of the regular quadrangular through hole is from the center of the core member 5, the larger the heating power of the resistance heater per unit length in the extending direction of the heat exchange tube. For example, in fig. 3, the heating power of the first layer is smaller than that of the second layer, but the heating power of the second layer is also different, specifically, the heating power of the four corners is larger than that of the non-corners. It has been found by numerical simulations and experiments that the further away from the centre the more heating power is required, especially in the outermost layers, because the water outside the heat exchange tubes is also heated, and therefore the more heating power per unit length in the extension direction of the heat exchange tubes is required. The invention further improves the heating uniformity and the heating efficiency by setting the change of the heating power of the electric heating element in the heat exchange tube away from the center of the kernel component.
Preferably, the heating power of the resistance heater per unit length in the extending direction of the heat exchange tube is increased by a larger and larger amount the farther the center of the regular quadrangular through hole is from the center of the core member 5. The above-mentioned variation of the heating amplitude is also obtained through a large number of numerical simulations and experiments, and is not common knowledge in the art. Through the change of above-mentioned range, can further improve heating efficiency and heating degree of consistency.
Preferably, the core component 5 is a regular octagonal central core component, and the regular octagonal through hole is located in the center of the core component. As shown in fig. 3.
Preferably, the center of the inner core component 5 is a regular octagonal channel, the regular quadrilateral channel is a two-layer structure surrounding the inner core component, the outermost layer is the regular octagonal channel, and the side length of the outer tube is 8 times that of the regular octagonal through hole.
Through a large number of numerical simulations and experiments, the purpose that the heating power of the electric heating elements on different layers can be required to be different to achieve uniform heating can be achieved, and the longer the side length of the regular quadrangle is, the larger the volume to be heated is, the larger the external space is, and the larger the heating power ratio of the inner layer to the outer layer is; the longer the length of the core member in the extending direction of the heat exchange tube, the more uniform the heating distribution because the larger the heating area over the entire length, and the smaller the heating power ratio of the inner and outer layers is required. Therefore, the invention carries out a great deal of research on the heating power of each layer, the side length and the height thereof through a great deal of numerical simulation and experiments to obtain the optimal heating power relation. For the above-described configuration of fig. 3, the ratio of the heating power of the outermost layer to the heating power of the innermost layer satisfies the following requirements:
preferably, the heating power of each electric heating element of the first layer is W1, the heating power of each electric heating element of the second layer is W2, the length of the core element is L1, and the side length of the regular quadrilateral channel is L2, so that the following requirements are met:
W2/W1= a-b LN (L1/L2); wherein a, b are parameters, 2.978< a <2.982,0.79< b < 0.81;
1.15<W2/W1<1.75；5.0<L1/L2<9.0；
the total heating power of the first layer and the second layer of the single heat exchange tube is M, and 300W < M < 500W.
Preferably, a =2.98 and b = 0.80.
Preferably, 1.3< W2/W1< 1.5; 6.9< L1/L2< 7.5;
120<B2<280mm；
8<L2<30mm；
the first and second layers are inner and outer layers, respectively.
Preferably, a is gradually reduced and b is gradually increased as L1/L2 is increased. Through so setting up can further make the heating even, improve heating efficiency.
Preferably, the tube diameter of the heat exchange tube 6 becomes continuously larger along the direction of the flow of the fluid in the heat exchange tube. The main reasons are as follows: 1) by increasing the tube diameter of the heat exchange tube 6, the resistance to fluid flow in the heat exchange tube can be reduced, so that the fluid heated in the heat exchange tube 6 continuously moves towards the direction of increasing the tube diameter, thereby further promoting the fluid flow. 2) Because the liquid is heated in the heat exchange tube 6 continuously along with the continuous flowing of the fluid, the volume of the fluid is larger and larger, and the pressure is also larger and larger, the change of the volume and the pressure of the gas which are increased continuously is met by increasing the tube diameter, and the pressure distribution is uniform on the whole.
Preferably, the heat exchange tube 6 has a tube diameter that increases progressively with increasing magnitude in the direction of fluid flow within the heat exchange tube. The amplitude change of the pipe diameter is a result obtained by a large number of experiments and numerical simulation of the applicant, and through the arrangement, the flow of the fluid can be further promoted, and the pressure is integrally uniform.
Preferably, a plurality of core members 5 are provided in the heat exchange tube 6, and the plurality of core members 5 are provided at intervals. By arranging the plurality of inner core components 5 at intervals, the fluid is heated in the inner core components and then enters the non-inner core component area for mixing, so that the uniform heating is ensured. After mixing, the mixture enters the core component to be heated.
Preferably, a plurality of core members 5 are provided in the heat exchange tube 6, and the pitch between the core members 5 becomes smaller from the inlet of the heat exchange tube 6 to the outlet of the heat exchange tube 6. Let L1 be a distance from the inlet of the heat exchange tube 6 and S, S = F be a distance between adjacent core members1(L1) that is, S is a function of the distance L1 as a variable, and S' is the first derivative of S, the following requirements are satisfied:
S’<0；
the main reason is to further enhance heat transfer. Through the arrangement, the heating power along the flowing direction of the fluid can be increased, which is similar to the countercurrent movement of a shell-and-tube heat exchanger, so that the heating temperature at the outlet of the pipeline is increased. The temperature of the heat source like the outlet of the pipe is higher and higher, so that the water is sufficiently heated.
Through the experiment, the heating is kept uniform to the greatest extent by the arrangement, and the heating effect can be improved.
It is further preferred that the distance between adjacent core members from the inlet of the heat exchange tube 6 to the outlet of the heat exchange tube 6 is increased in a larger and larger range. I.e. S "is the second derivative of S, the following requirements are met:
S”>0;
through experimental discovery, through so setting up, can further improve the heating effect. It should be noted that the above rule is a rule obtained by a large number of experiments and numerical simulations, and is not common knowledge or conventional means in the field.
Preferably, a plurality of core members 5 are provided in the heat exchange tube 6, and the different core members are longer and longer from the inlet of the heat exchange tube 6 to the outlet of the heat exchange tube 6. The length refers to a length of the inner core member extending in a direction in which the heat exchange tube extends. It is further preferred that the lengths of the different core members increase progressively from the inlet of the heat exchange tube 6 to the outlet of the heat exchange tube 6. For the same reasons as above.
Preferably, a plurality of core members are provided in the heat exchange tube 6, and the heating power of the electric heating elements arranged in each of the quadrangles of the different core members is gradually increased from the inlet of the heat exchange tube 6 to the outlet of the heat exchange tube 6. Assuming that the distance from the inlet of the heat exchange tube 6 is L1, the power of the electric heating element arranged in each regular quadrangle of the adjacent core members is W, S = F3(L1) that is, W is a function of the distance L1 as a variable, and W' is the first derivative of W, satisfies the following requirements:
W’>0;
the main reason is to further enhance heat transfer. Through the arrangement, the heating power along the flowing direction of the fluid can be increased, which is similar to the countercurrent movement of a shell-and-tube heat exchanger, so that the heating temperature at the outlet of the pipeline is increased. The temperature of the heat source like the outlet of the pipe is higher and higher, so that the water is sufficiently heated.
Through the experiment, the heating is kept uniform to the greatest extent by the arrangement, and the heating effect can be improved.
Further preferably, the electric heating elements arranged in each of the regular quadrangles of the adjacent core members become increasingly powered from the inlet of the heat exchange tube 6 to the outlet of the heat exchange tube 6. I.e., W "is the second derivative of S, the following requirement is satisfied:
W”>0；
through the experiment discovery, through so setting up, can further keep the whole even of heating, can improve the heating effect simultaneously. It should be noted that the above rule is a rule obtained by a large number of experiments and numerical simulations, and is not common knowledge or conventional means in the field.
Preferably, a plurality of inner core members are provided in the heat exchange tube 6, and the side length of the regular quadrangle becomes smaller from the inlet of the heat exchange tube 6 to the outlet of the heat exchange tube 6. The distance from the inlet of the heat exchange tube 6 was L1, the side length of the square was C, C = F2(L1), C' is the first derivative of C, satisfying the following requirements:
C’<0；
the main reason is because the smaller the side length of the regular quadrilateral, the more difficult the manufacture, but the better the uniformity of the overall heating. Because the water is heated uniformly in the whole area beyond the outlet of the heat exchange tube, and partial dry-out caused by nonuniform heating is avoided. Through the arrangement, the cost can be saved, and the best heating uniformity and hot fluid output efficiency are achieved.
Further preferably, the length of the side of the regular quadrangle is gradually increased from the inlet of the heat exchange tube 6 to the outlet of the heat exchange tube 6. C' is the second derivative of C, and meets the following requirements:
C”>0。
preferably, the distance between adjacent core components remains constant.
Through the experiment discovery, through so setting up, can further keep the whole even of heating, can improve the heating effect simultaneously. It should be noted that the above rule is a rule obtained by a large number of experiments and numerical simulations, and is not common knowledge or conventional means in the field.
Preferably, the farther the center of the regular quadrangular through hole is from the center of the core member, the larger the heating power of the resistance heater per unit length in the extending direction of the heat exchange tube.
Since it can be seen through experiments and numerical simulations that the more outward the larger the volume to be heated, especially the outermost side, the peripheral water and the water in the inner tube. The invention further improves the heating uniformity and the heating efficiency by setting the change of the heating power of the electric heating element in the heat exchange tube away from the center of the kernel component.
Preferably, the heating power of the resistance heater per unit length in the extending direction of the heat exchange tube is increased to a larger and larger extent as the regular quadrangular through-hole is farther from the center of the core member. Through such rule setting, heating degree of consistency and heating efficiency have further been improved.
Preferably, the heating power per unit length of the electrical heating element 16 is continuously increased along the direction of fluid flow within the heat exchange tubes. The main reason is to further enhance heat transfer. Through the arrangement, the heating power along the flowing direction of the fluid can be increased, which is similar to the countercurrent movement of a shell-and-tube heat exchanger, so that the heating temperature at the outlet of the pipeline is increased. The temperature of the heat source like the outlet of the pipe is higher and higher, so that the water is sufficiently heated. Through a large amount of experiments and numerical simulation, the heating efficiency can be further improved by about 10% through the change of the heating power of the heat exchange tube, and the heating time is saved.
Preferably, the magnitude of the continuous decrease in the heating power per unit length of the electric heating rod 16 is continuously increased along the height direction.
Through a large amount of experiments and numerical simulation, the heating efficiency can be further improved by 5% through the change of the heating power amplitude of the electric heating rod 16, and the heating time is further saved.
Preferably, the same electrical heater rod 16 within the same core member is divided into a plurality of sections, with different sections having different heating powers per unit length along the direction of fluid flow within the heat exchange tubes. Wherein the heating power per unit length of the different sections is continuously increased along the direction of fluid flow in the heat exchange tubes. Further preferably, the magnitude of the increase is continuously increased.
Preferably, the length of each segment is the same.
Preferably, the heating power per unit length of each segment is the same.
The specific reason is as described above.
By providing the segments, manufacturing can be further facilitated.
Through analysis and experiments, the distance between the inner core components in the extension direction of the heat exchange tube cannot be too large, the effect of hot fluid generation is poor if the distance is too large, meanwhile, the distance cannot be too small, the inner tube is easy to burn out if the distance is too small, and similarly, the side length of the regular quadrangle cannot be too large or too small, the heating is uneven if the distance is too large, the distribution of the regular quadrangle and the octagon is too dense due to the too small size, the flow resistance is increased, and the processing cost is increased. Therefore, the resistance is optimized through a large number of experiments under the condition that the hot fluid steam outlet amount is preferentially met, and the optimal relation of each parameter is arranged.
Preferably, the distance between adjacent core components is S1, the side length of a regular quadrangle is L2, the core components are regular quadrangle sections, and the side length of the regular quadrangle section of the core component is B2, so that the following requirements are met:
10*L2/B2=a-b*(S1/B2);
wherein a, b are parameters, wherein 0.95< a <0.96,0.16< b < 0.17;
120<B2<280mm；
8<L2<30mm；
29<S1<110mm。
further preferably, a =0.9562, b =0.163;
further preferably, a is larger and B is smaller as L2/B2 is increased.
Preferably, the side length L2 of the regular quadrilateral through-hole is an average of the inner side length and the outer side length of the regular quadrilateral through-hole, and the side length B2 of the regular quadrilateral cross-section of the core member is an average of the inner side length and the outer side length of the regular quadrilateral cross-section of the core member.
The distance between adjacent core elements S1 is the distance between the facing surfaces of adjacent core elements. Such as the distance between the left end face of the right core element and the right end face of the left core element.
Preferably, as B2 increases, L2 also increases. However, as B2 increased, the magnitude of the increase in L2 became smaller and smaller. The change of the rule is obtained through a large amount of numerical simulation and experiments, and the heat exchange effect and the noise are further improved and reduced through the change of the rule.
Preferably, S1 decreases as B2 increases. However, as B2 increases, the magnitude of the decrease of S1 becomes smaller and smaller. The change of the rule is obtained through a large amount of numerical simulation and experiments, and the heat exchange effect and the noise are further improved and reduced through the change of the rule.
Preferably, the length of the side of the regular quadrangular cross section of the core member is equal to the length of the side of the inner wall surface of the heat exchange tube.
The length L1 of the inner core member is preferably 50-300 mm, more preferably 100-150 mm.
Preferably, the length of the heat exchange tube is between 3000-3500 mm. More preferably, 3200-.
By optimizing the optimal geometric dimension of the formula, the optimal effect of shock absorption and noise reduction can be achieved under the condition of meeting the normal flow resistance.
For other parameters, such as the wall thickness of the pipe and the wall thickness of the shell, the parameters are set according to normal standards.
Preferably, the fluid in the heat exchange tubes is water.
For other parameters, such as the wall thickness of the pipe and the wall thickness of the shell, the parameters are set according to normal standards.
Preferably, the shell-side fluid is water.
Preferably, the flow rate of the fluid in the tube side is 3-5 m/S.
Preferably, the ratio of the length of the heat exchange tube to the shell diameter of the heat exchanger is 6 to 10.
Although the present invention has been described with reference to the preferred embodiments, it is not limited thereto. Various changes and modifications may be effected therein by one skilled in the art without departing from the spirit and scope of the invention as defined in the appended claims.
Claims (2)
1. A shell-and-tube heat exchanger with variable kernel spacing comprises a shell, wherein end sockets are respectively arranged at two ends of the shell, tube plates are arranged at the connecting positions of the end sockets and the shell, a heat exchange tube is connected with the tube plates at two ends, the heat exchange tube comprises an outer tube and a kernel component arranged in the outer tube, and the kernel component extends in the extending direction of the heat exchange tube; a plurality of inner core members are provided in the heat exchange tube, and the spacing between the inner core members becomes smaller from the inlet of the heat exchange tube to the outlet of the heat exchange tube.
2. The heat exchanger of claim 1, wherein the distance between adjacent core members increases in increasing magnitude from the inlet of the heat exchange tube to the outlet of the heat exchange tube.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202010050719.1A CN111336839B (en) | 2018-12-18 | 2018-12-18 | Shell-and-tube heat exchanger with variable kernel spacing |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201811550282.7A CN109612308B (en) | 2018-12-18 | 2018-12-18 | Shell-and-tube heat exchanger for liquid medicine used for fumigation |
| CN202010050719.1A CN111336839B (en) | 2018-12-18 | 2018-12-18 | Shell-and-tube heat exchanger with variable kernel spacing |
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| CN201811550282.7A Division CN109612308B (en) | 2018-12-18 | 2018-12-18 | Shell-and-tube heat exchanger for liquid medicine used for fumigation |
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| CN111336839B CN111336839B (en) | 2021-04-06 |
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| CN201811550282.7A Active CN109612308B (en) | 2018-12-18 | 2018-12-18 | Shell-and-tube heat exchanger for liquid medicine used for fumigation |
| CN202010050720.4A Active CN111336840B (en) | 2018-12-18 | 2018-12-18 | Shell and tube heat exchanger |
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| CN202010050720.4A Active CN111336840B (en) | 2018-12-18 | 2018-12-18 | Shell and tube heat exchanger |
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| CN206609321U (en) * | 2017-02-14 | 2017-11-03 | 湖州新奥克化工有限公司 | A kind of shell-and-tube heat exchanger |
| CN106705712A (en) * | 2017-02-14 | 2017-05-24 | 湖州新奥克化工有限公司 | Pipe shell type heat exchanger |
| CN106969652B (en) * | 2017-05-09 | 2019-03-19 | 山东大学 | A kind of condensable annular and separation device heat exchanger of length variation |
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| CN205662564U (en) * | 2016-06-15 | 2016-10-26 | 衡阳旺发锡业有限公司 | Electric heat spiral crystallizer |
| CN106679466A (en) * | 2017-02-13 | 2017-05-17 | 中国核动力研究设计院 | Porous medium two-phase flow shell-and-tube heat exchanger and stabilization device thereof |
| CN107101514A (en) * | 2017-05-09 | 2017-08-29 | 山东大学 | What a kind of spacing changed can not condensing body annular and separation device heat exchanger |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN109612308A (en) | 2019-04-12 |
| CN111336839B (en) | 2021-04-06 |
| CN111336840A (en) | 2020-06-26 |
| CN109612308B (en) | 2020-03-17 |
| CN111336840B (en) | 2021-04-06 |
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