A kind of asynchronous instant waste-heat recovery device of plate heat exchange of heat pipe formula
Technical field
The utility model is related to heat recovery technology field, refers in particular to a kind of asynchronous instant waste heat of plate heat exchange of heat pipe formula
Retracting device.
Background technology
Recycling to low-grade waste fluid energy, is always energy-saving field research emphasis.Bathing pool or northern school
Publilc baths concentrates the place taken a shower, and the boiler of use is generally non-pressure water tank, often asynchronous with supplement cold water using hot water,
It is synchronous with supplement cold water reheating using hot water even if some projects boiler is press-bearing water tank, because gondola water faucet quantity is more, do not know
Which gondola water faucet of road is used, and which gondola water faucet is not used, it is also difficult to accomplish waste heat recovery.At present, the spent hot water after people has taken a shower is straight
Run in.Though the heat of the waste water being discharged into waste water tank can be subsequently reclaimed with waste water source heat pump etc., due to discharge of wastewater mistake
Radiating in journey, causes a large amount of losses of heat and being greatly reduced for heat taste.The temperature of the waste water that people has just taken a shower is at 35 DEG C
Left and right, just only 25 DEG C or so of the wastewater temperature that waste water source heat pump is collected, causes heat waste, recovery value low.
At present, also there are some for reclaiming the waste-heat recovery device of waste water, but due to being limited by structure, often go out
The problem for now blocking.For example Chinese patent ZL200810244379.5 discloses a kind of high-efficiency easy-cleaning sullage heat exchanger, its by
The snakelike heat exchange tube of arrangement is exchanged heat in sewage box body.Snakelike heat exchange tube needs support, the support of snakelike heat exchange tube and snakelike
Heat exchanger tube turns into the obstacle in heat exchanger sewage runner in itself, especially easily causes hair, hair cream, dirt and blocks and deposit, clearly
Wash frequency high, clean also cumbersome, defect is fairly obvious, it is impossible to meet the demand for using.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of asynchronous instant waste heat recovery dress of plate heat exchange of heat pipe formula
Put, it avoids thermal loss and waste, reduce the energy consumption of heating devices heat running water, the flowing of its waste water is smooth, effectively prevent
Only dirt block, the phenomenon such as deposition, be easy to clean and safeguard, energy-conserving and environment-protective, and reduce the cost of shower.
In order to solve the above-mentioned technical problem, the utility model is adopted the following technical scheme that:
A kind of asynchronous instant waste-heat recovery device of plate heat exchange of heat pipe formula, including at least two mixed water assemblies, be correspondingly arranged
Plate heat exchange of heat pipe cold water inlet road connect with least two mixed water assemblies, the inlet channel that exchanges heat below mixed water assembly,
Boiler, the heater for being heated to the water in boiler that heat exchange outlet conduit is connected with heat exchange outlet conduit
And for the hot water of boiler to be delivered to the hot water effluent's pipeline of mixed water assembly;
The plate heat exchange of heat pipe includes core body, and core body includes A plates, B plates, preceding shrouding and rear shrouding;A plates are provided with some side by side
A plate deep gouges, the back side of A plate deep gouges is A plates deep gouge projection;B plates are provided with B plates deep gouge corresponding with A plate deep gouges, the back of the body of B plate deep gouges
Face is raised B plates deep gouge, and two adjacent B plate deep gouges are connected;A plate deep gouge projections are arranged in B plates deep gouge and A plate deep gouges are convex
Rise has gap and B plate deep gouges between, the raised structure that seal clearance is equipped with B plate deep gouges two ends of A plates deep gouge, A plates is sunk
Geosynclinal convex rises and forms medium runner and B plate deep gouges between;
The preceding shrouding is respectively provided with the preceding end slot and rear end slot for connecting adjacent A plates deep gouge with rear shrouding, and A plates sink
Groove, preceding end slot and rear end slot composition waste water runner;When using, waste water flows through waste water stream road;Heat exchange inlet channel and the heat exchange
Outlet conduit is connected with the medium runner respectively.
Wherein, the hot water effluent's pipeline includes house steward hot water effluent and the hot water effluent point being connected with house steward hot water effluent
Pipe, the hot water effluent is in charge of and is connected with mixed water assembly;It is described heat exchange inlet channel include heat exchange water inlet manifold and with exchange heat into
The heat exchange water inlet of supply mains's connection is in charge of, and the heat exchange water inlet is in charge of and is connected with plate heat exchange of heat pipe;
The hot water effluent is in charge of and is connected with hot water's induction installation, and the heat exchange water inlet is in charge of and is connected with throttling control
Device, when the hot water during hot water's induction installation senses that hot water effluent is in charge of flows, control device control throttling control
Device is opened.
Wherein, the heat exchange water inlet is in charge of and is connected with for the flow control apparatus for water of regulating water flow size and for showing
The current display device of water-carrying capacity.
Wherein, also including preheating water tank, the heat exchange outlet conduit is connected by preheating water tank with boiler;The preheating
Water tank is provided with high water level detection means, low water level detection means and for the pre- hot water supplying pipe supplied water in preheating water tank, this to be pre-
Hot water supplying pipe is connected with the originally water management water valve for controlling water break-make, and heat exchange outlet conduit is provided with preheating water control valve.
Wherein, the A plates deep gouge is raised and B plate deep gouges two ends are welded, and makes A plates deep gouge raised and between B plate deep gouges two ends
Gap is sealed.
Wherein, B plates are provided with the deep gouge for connecting adjacent B plates deep gouge.
Preferably, the section of the medium runner is in crescent, and the crescent section is made up of multistage curve, the multistage
Curve includes the A plate external pressures curved section for being arranged at A plates, the A plate inner pressure curves being connected with the two ends of the A plate external pressure curved sections respectively
Section, the B plates inner pressure curve section for being arranged at B plates and the B plate external pressure curved sections being connected with the two ends of B plates inner pressure curve section respectively.
Preferably, also including being covered on the cover plate of A plates, cover plate is provided with leaking hole, is provided with screen pack at leaking hole, it is described before
Shrouding is provided with the water leg for collecting the fluid flowed out in leaking hole, water leg and waste water flow passage.
Preferably, the core body is installed on cover plate by some fixture blocks.
Preferably, also including casing, the core body is installed in casing.
The beneficial effects of the utility model:
Mixed water assembly described in the utility model during practical application, mixes water assembly respective panels heat exchange of heat pipe at least provided with two
It is arranged on each and uses water spot, the multiple water spot of its composition bathing system.When people take a shower, changed in each mixed water assembly and plate pipe
Carry out using water at hot device, it is typically all asynchronous to carry out with water, plate heat exchange of heat pipe is respectively provided with to waste water with water at each
Preheating is reclaimed immediately, is used for pre- hot tap-water, it is to avoid thermal loss and waste, reduces heating devices heat running water
Energy consumption at equal temperature, its energy-conserving and environment-protective, and reduce the cost of shower.
Plate heat exchange of heat pipe compact conformation described in the utility model, can minimize, cause to install and place convenient, use
Flexibly, wide adaptation range.
Plate heat exchange of heat pipe described in the utility model, A plate deep gouges are set in A plates, and B plate deep gouges, A plates and B plates are set in B plates
The ripple struction is added to carry out enhanced heat exchange using plate, the coefficient of heat transfer is high.A plates and B plates are combined into core body, A using plate tubular construction
The overall flatness of plate deep gouge is good, and waste water flowing is smooth, effectively avoids the coefficient of heat transfer that dirt blocks, deposits and its cause
Problem is greatly lowered.
Plate heat exchange of heat pipe described in the utility model, A plates deep gouge and B plate deep gouges are set side by side with several, increase greatly
Plus the heat exchange area of waste water and running water, waste water and running water circuitous flow, running water is fully absorbed heat.
Plate heat exchange of heat pipe described in the utility model, some A plates deep gouges of A plates are connected by preceding end slot and rear end slot, are made
The corner for obtaining A plate deep gouges is Wheelchair Accessible, and its transitions smooth can be avoided the heat exchange that dirt blocks, deposits and its cause
The problem that coefficient is greatly lowered.
Plate heat exchange of heat pipe described in the utility model, carries out punching press etc. and can be obtained by corresponding deep gouge to A plates and B plates,
Its manufacture is relatively easy, lowers the cost of production.
Plate heat exchange of heat pipe described in the utility model use A plates and B plate plate tubular constructions, its Stability Analysis of Structures, long service life,
And it is easy to clean A plates deep gouge and medium runner, its maintenance cost is low.
The utility model independently reclaims waste water residual heat using plate heat exchange of heat pipe, instead of existing waste heat recovery immersion type knot
Structure, effectively avoids wastewater temperature loss, improves the efficiency of waste heat recovery.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of heater described in the utility model.
Fig. 3 is the dimensional structure diagram of plate heat exchange of heat pipe described in the utility model embodiment one.
Fig. 4 is the stereochemical structure decomposing schematic representation of plate heat exchange of heat pipe described in the utility model embodiment one.
Fig. 5 is the dimensional structure diagram of A plates described in the utility model embodiment one.
Fig. 6 is the dimensional structure diagram of B plates described in the utility model embodiment one.
Fig. 7 is the dimensional structure diagram of preceding shrouding described in the utility model embodiment one.
Fig. 8 is the dimensional structure diagram of rear shrouding described in the utility model embodiment one.
Fig. 9 is the partial structural diagram in the section of plate heat exchange of heat pipe described in the utility model embodiment one.
Figure 10 is the partial structural diagram in another section of plate heat exchange of heat pipe described in the utility model embodiment one.
Figure 11 is the dimensional structure diagram of plate heat exchange of heat pipe described in the utility model embodiment two.
Figure 12 is the stereochemical structure decomposing schematic representation of plate heat exchange of heat pipe described in the utility model embodiment two.
Figure 13 is the partial structural diagram in the section of plate heat exchange of heat pipe described in the utility model embodiment two.
Figure 14 is the dimensional structure diagram of plate heat exchange of heat pipe described in the utility model embodiment three.
Figure 15 is the stereochemical structure decomposing schematic representation of plate heat exchange of heat pipe described in the utility model embodiment three.
Figure 16 is the dimensional structure diagram of plate heat exchange of heat pipe described in the utility model example IV.
Figure 17 is the stereochemical structure decomposing schematic representation of plate heat exchange of heat pipe described in the utility model example IV.
Specific embodiment
For the ease of the understanding of those skilled in the art, further is made to the utility model with reference to embodiment and accompanying drawing
Ground explanation, the content that implementation method is referred to is not to restriction of the present utility model.
Embodiment one.
Such as Fig. 1 to Figure 10, a kind of asynchronous instant waste-heat recovery device of plate heat exchange of heat pipe formula, including at least two mixed water groups
The cold water that part 1, the plate heat exchange of heat pipe 800 for being correspondingly arranged in the lower section of mixed water assembly 1 are connected with least two mixed water assemblies 1 is intake
Pipeline 3, heat exchange inlet channel 4, heat exchange outlet conduit 5 with heat exchange outlet conduit 5 connect boiler 6, for boiler 6
The heater 7 that interior water is heated and the hot water effluent's pipeline 8 for the hot water of boiler 6 to be delivered to mixed water assembly 1;
The plate heat exchange of heat pipe 800 includes core body 20, and core body 20 includes A plates 30, B plates 40, preceding shrouding 50 and rear shrouding 70;
A plates 30 are provided with some A plates deep gouges 301 side by side, and the back side of A plates deep gouge 301 is A plate deep gouges projection 302;B plates 40 are provided with heavy with A plates
The corresponding B plates deep gouge 401 of groove 301, the back side of B plates deep gouge 401 is B plate deep gouges projection 402, two adjacent phases of B plates deep gouge 401
Connection;Between A plate deep gouges projection 302 is arranged in B plates deep gouge 401 and has between A plates deep gouge projection 302 and B plates deep gouge 401
Gap, the two ends of A plates deep gouge projection 302 and B plates deep gouge 401 are equipped with the structure of seal clearance, A plates deep gouge raised 302 is sunk with B plates
Medium runner 60 is formed between groove 401;
The preceding shrouding 50 is respectively provided with the preceding end slot 501 and rear end for connecting adjacent A plates deep gouge 301 with rear shrouding 70
Groove 701, A plates deep gouge 301, preceding end slot 501 and the composition waste water runner of rear end slot 701;When using, waste water flows through waste water stream road;Institute
State heat exchange inlet channel 4 and heat exchange outlet conduit 5 is connected with the medium runner 60 respectively.
During practical application, after the A plates 30 and the assembling of B plates 40, preceding shrouding 50 and rear shrouding 70 are respectively arranged at the He of A plates 30
The two ends of the assembly of B plates 40.As needed, can be using the two ends of various ways sealing A plates deep gouge projection 302 and B plates deep gouge 401
Gap, for example with adhesive tape sealing and welded seal etc..In the present embodiment, there is provided a kind of preferred scheme, the A plates deep gouge
The two ends welding of raised 302 and B plates deep gouge 401, during welding, can push the two ends of A plates 30 or by the two ends of B plates 40
Pressure, makes the two ends of A plates 30 and the two ends of B plates 40 carry out contact type welding, so that A plates deep gouge projection 302 and B plates deep gouge 401
The gap at two ends is sealed, and can bear larger pressure.What two adjacent B plates deep gouges 401 were connected, A plate deep gouges
Gap between raised 302 and B plates deep gouge 401 is also interconnected, and it turns into Jie for circulate running water or other media
Mass flow road 60.The section of medium runner 60 can use various shapes, such as U-shaped curved runner, circular flow channel, ellipse runner,
To adapt to various heat exchange site requirements.Adjacent A plates deep gouge 301 is mutually ganged up by preceding end slot 501 with rear end slot 701 so that if
Dry A plates deep gouge 301 and preceding end slot 501 and the composition waste water runner of rear end slot 701.The preceding end slot 501 and rear end slot 701 are preferably
U-shape so that the flowing of waste water is more smooth.
Hot water flow to mixed water assembly 1, the running water in cold water inlet road 3 by hot water effluent's pipeline 8 in boiler 6
It flow to mixed water assembly 1 to be mixed with hot water, in order to use.During shower, the waste water of generation flows into the useless of plate heat exchange of heat pipe 800
Water flow passage.At the same time, in the medium runner 60 that running water flows into plate heat exchange of heat pipe 800 from heat exchange inlet channel 4, medium runner
Running water in 60 absorbs the heat of waste water in A plates deep gouge 301, and running water carries out heat exchange with waste water, so as to reclaim waste water
Heat come pre- hot tap-water.During running water after being preheated flows to boiler 6 from heat exchange outlet conduit 5.Further, it is described
Heat exchange outlet conduit 5 can be connected with the heater 7, the running water after being preheated can flow into heater 7, by adding
Flowed into again after heat in boiler 6, by the waste water after waste heat recovery, drained from the waste water runner of plate heat exchange of heat pipe 800.Specifically
, the heater 7 can be using electric heating heating, Electromagnetic Heating, air source heat pump heating and waste water source heat pump etc., its
Existing heater can be used;The mixed water assembly 1 includes water mixing valve, can also be arranged as required to connect in water mixing valve
Gondola water faucet for connecing etc., it belongs to existing component, therefore repeats no more.
Mixed water assembly 1 described in the utility model during practical application, mixes the heat exchange of the respective panels pipe of water assembly 1 at least provided with two
Device 800 is arranged on each and uses water spot, the multiple water spot of its composition bathing system.People take a shower when, typically all it is asynchronous enter
Row water, reclaimed immediately with being respectively provided with preheating of the plate heat exchange of heat pipe 800 to waste water at water at each, it is used for preheating
Running water, it is to avoid thermal loss and waste, reduces the energy consumption under the heating running water to equal temperature of heater 7, its energy-saving ring
Protect, and reduce the cost of shower.
The compact conformation of plate heat exchange of heat pipe 800 described in the utility model, can minimize, cause to install and place convenient,
Use flexible, wide adaptation range.
Plate heat exchange of heat pipe 800 described in the utility model, A plates deep gouge 301 is set in A plates 30, and setting B plates in B plates 40 sinks
Groove 401, A plates 30 and B plates 40 add the ripple struction to carry out enhanced heat exchange using plate, and the coefficient of heat transfer is high.A plates 30 and B plates 40 are adopted
Core body 20 is combined into plate tubular construction, the overall flatness of A plates deep gouge 301 is good, waste water flowing is smooth, effectively avoids dirt
The coefficient of heat transfer for blocking, depositing and its causing is greatly lowered problem.
Plate heat exchange of heat pipe 800 described in the utility model, A plates deep gouge 301 and B plates deep gouge 401 are set side by side with some
It is individual, the heat exchange area of waste water and running water, waste water and running water circuitous flow are greatly increased, running water is fully absorbed heat.
Plate heat exchange of heat pipe 800 described in the utility model, some A plates deep gouges 301 of A plates 30 by preceding end slot 501 and after
End slot 701 is connected so that the corner of A plates deep gouge 301 is Wheelchair Accessible, and its transitions smooth can be avoided dirt and block, sinks
The problem that product and its coefficient of heat transfer for causing are greatly lowered.
Plate heat exchange of heat pipe 800 described in the utility model, carries out punching press etc. and can be obtained by accordingly to A plates 30 and B plates 40
Deep gouge, its manufacture is relatively easy, lowers the cost of production.
Plate heat exchange of heat pipe 800 described in the utility model is used using A plates 30 and the plate tubular construction of B plates 40, its Stability Analysis of Structures
Long lifespan, and be easy to clean A plates deep gouge 301 and medium runner 60, its maintenance cost is low.
The utility model independently reclaims waste water residual heat using plate heat exchange of heat pipe 800, instead of existing waste heat recovery immersion type
Structure, effectively avoids wastewater temperature loss, improves the efficiency of waste heat recovery.
In the present embodiment, the hot water effluent's pipeline 8 includes house steward hot water effluent 81 and is connected with house steward hot water effluent 81
Hot water effluent be in charge of 82, the hot water effluent is in charge of 82 and is connected with mixed water assembly 1;The heat exchange inlet channel 4 includes heat exchange
Water inlet manifold 41 and the heat exchange water inlet connected with heat exchange water inlet manifold 41 are in charge of 42, and the heat exchange water inlet is in charge of 42 and is exchanged heat with plate pipe
Device 800 is connected;Specifically, each mixed water assembly 1 draws a hot water effluent to be in charge of 82 to connect house steward hot water effluent 81, it is each
The connection of individual heat exchanger 800 is drawn a heat exchange water inlet and is in charge of 42 to connect heat exchanger 800, is easy to the supply of hot water and running water.
Further, the hot water effluent is in charge of 82 and is connected with hot water's induction installation 02, and the heat exchange water inlet is in charge of
42 are connected with throttle control device 03, when hot water's induction installation 02 senses that hot water effluent is in charge of the flowing of the hot water in 82
When, the control throttle control device 03 of control device 01 is opened.When people takes a shower, hot water effluent is in charge of 82 to its supplying hot water, works as hot water
When current induction installation 02 senses that hot water effluent is in charge of the flowing of the hot water in 82, with the corresponding section of hot water's induction installation 02
Flow control device 03 is opened, and the running water in heat exchange inlet channel 4 is entered heat exchanger 800, and its heat to waste water is
Shi Huishou.Specifically, hot water's induction installation 02 and throttle control device 03 can use existing device, water valve
Or switch etc. realizes that it is able to realize detection current and control current break-make, therefore repeats no more.
In the present embodiment, the heat exchange water inlet is in charge of 42 and is connected with flow control apparatus for water 04 for regulating water flow size
And for showing the current display device 05 of water-carrying capacity.Current display device 05 can show streamflow regime, to detect and to judge
Throttle control device 03 and flow control apparatus for water 04 it is whether faulty or damage.
As shown in Fig. 2 in the present embodiment, also including preheating water tank 9, the heat exchange outlet conduit 5 by preheating water tank 9 with
Boiler 6 is connected;The preheating water tank 9 is provided with high water level detection means 91, low water level detection means 92 and for preheating water
The pre- hot water supplying pipe 93 supplied water in case 9, the pre- hot water supplying pipe 93 is connected with the originally water management water valve 94 for controlling water break-make,
Heat exchange outlet conduit 5 is provided with preheating water control valve 51.Further, the preheating water tank 9 can be filled by pipeline with heating
Put 7 connections, the water of preheating water tank 9 can be flowed directly in boiler 6, may also flow into after heat in heater 7, it is being flowed into
In boiler 6.
When using, high water level detection means 91 and low water level detection means 92 are used for detecting water level conditions in preheating water tank 9,
When water is discontented in the display water tank of high water level detection means 91, the preheating water control valve 51 on heat exchange outlet conduit 5 is kept to open;
When water level is too low in the display water tank of low water level detection means 92, originally water management water valve 94 is opened, running water is supplied from preheating
Water pipe 93 flows into preheating water tank 9, when the water level of preheating water tank 9 rises to correct position, closes originally water management water valve 94, with
Ensure that preheating water tank 9 has water available always.
In the present embodiment, B plates 40 are provided with the deep gouge 400 for connecting adjacent B plates deep gouge 401.The deep gouge includes upper heavy
Groove 407, deep gouge 407 is located in the projection between adjacent B plates deep gouge 401 on this.As shown in figure 9, when A plate deep gouges projection 302
When bottom surface does not contact with B plates deep gouge 401, a upper deep gouge 407 is only set.As shown in Figure 10, when A plates deep gouge is raised
When 302 bottom surface contacts with B plates deep gouge 401, the deep gouge also includes lower deep gouge 408, and B plates deep gouge 401 is raised by A plates deep gouge
302 are partitioned into two parts, and adjacent B plates deep gouge 401 is connected using upper deep gouge 407 and lower deep gouge 408.So that A plates are heavy
The gap that geosynclinal convex is risen between 302 and B plates deep gouge 401 is also mutually ganged up, and the medium runner 60 for being connected, its simple structure,
Good integrity, bearing capacity is strong.Certainly, according to use demand, B plates deep gouge 401 can also be ganged up using other modes, such as adopted
Mode is ganged up with above-mentioned A plates deep gouge 301, is ganged up using closing plate structure.
In the present embodiment, preceding shrouding 50 and rear shrouding 70 are respectively arranged with preceding slot 502 and rear slot 702, A plates 30 and B
Two ends are plugged in preceding slot 502 and rear slot 702 respectively after plate 40 is assembled, and it installs simple, fixed reliable, and make some A plates
Deep gouge 301 is docked completely with preceding end slot 501 and rear end slot 701.
In the present embodiment, the core body 20 is provided with some strengthening rib strips 80, some strengthening rib strips 80 be arranged at A plates 30 and/
Or B plates 40.Specifically, strengthening rib strip 80 can be welded on A plates 30 or B plates 40, or simultaneously on A plates 30 and B plates 40 all
Welding strengthening rib strip 80 so that the Stability Analysis of Structures of core body 20, bearing capacity is strong.
As shown in figure 9, in the present embodiment, it is preferred that the section of the medium runner 60 is in crescent, larger fluid is disturbed
It is dynamic, increase the coefficient of heat transfer, strengthen the heat exchange of fluid.The crescent section is made up of multistage curve, the multistage curve bag
Buckled in the A plates for include and be arranged at the A plate external pressures curved section 305 of A plates 30, being connected with the two ends of the A plate external pressures curved section 305 respectively
Line segment 306, the B plates inner pressure curve section 405 for being arranged at B plates 40 and the B being connected with the two ends of B plates inner pressure curve section 405 respectively
Plate external pressure curved section 406.Specifically, according to the size for bearing pressure, multistage curve is set into inner pressure curve section and external pressure curve
Section, during design, is easy to calculate the thickness of A plates 30 and B plates 40, utilitarian design, rational thickness, it is to avoid produce design to lack
Fall into, and avoid the waste of material, reduce the cost of production.Medium runner 60, can using the pressure design of multistage inside or outside of curve simultaneously
The effective resistance for reducing fluid.
In the present embodiment, there is provided calculate the computing formula of A plates or B plate thickness, the thickness of the A plates or B plates is:
When being designed by external pressure
When being designed by internal pressure
Wherein, P is core body fluid design pressure;
D1nIt is A plate external pressures curved section 305 or the equivalent diameter of B plate external pressures curved section 406;
D2nIt is the equivalent diameter of A plates inner pressure curve section 306 or B plates inner pressure curve section 405;
[σ] is the tensile strength of A plate external pressures curved section 305 or the material of B plate external pressures curved section 406;
σ is the tensile strength of A plates inner pressure curve section 306 or B plates inner pressure curve 405 materials of section;
η is the safety coefficient of A plates inner pressure curve section 306 or B plates inner pressure curve section 405;
The average wall thickness of the medium runner 60 of the crescent
η3It is the tensile strength safety coefficient of the wall of medium runner 60 of crescent;The equivalent diameter of medium runner 60 of crescent
D3=L/ π;Wherein, L is the girth of the medium runner 60 of crescent;
When actually used, the thickness of the A plates or B plates takes s1n、s2n、s3In maximum, and along with safe clearance
a.The safe clearance a is the coefficient selected according to actual production demand.
Embodiment two.
As shown in Figure 11 to Figure 13, the present embodiment two is with the difference of embodiment one:The plate heat exchange of heat pipe 800
Also include being covered on the cover plate 10 of A plates 30, cover plate 10 is provided with leaking hole 101, be provided with screen pack 102 at leaking hole 101, it is described before
Shrouding 50 is provided with the water leg 503 for collecting the fluid flowed out in leaking hole 101, water leg 503 and waste water flow passage.
In the present embodiment, increase cover plate 10, the cover plate 10 is covered on A plates 30, so as to be sealed to A plates deep gouge 301.It is real
When border is applied, cover plate 10 can be with the projection contacts of the top surface of A plates 30, it is also possible to do not contact.Waste water is flowed into from leaking hole 101, is led to
After crossing the filtering of screen pack 102, it is flowed into water leg 503, waste water is flowed into A plates deep gouge 301 from water leg 503 carries out heat again
Amount is exchanged.Connection between the cover plate 10 and A plates 30, the connection between A plates 30 and B plates 40, can be according to bearing capacity
Different demands, so as to select welded seal or by adhesive tape press seal etc..In the present embodiment, the core body 20 passes through some cards
Block 90 is installed on cover plate 10.
In the present embodiment, increase cover plate 10 and A plates deep gouge 301 is sealed, screen pack 102 is filtered to waste water, can
The foreign matters such as hair removal are removed, prevents waste water runner from blocking.Core body 20 is further installed using fixture block 90, A plates 30 and B plates 40 are assembled
Afterwards, its two ends clamping of some fixture blocks 90, its is easy for installation, fixed reliable.
Embodiment three.
As shown in Figure 14 to Figure 15, the present embodiment three is with the difference of embodiment two:The plate heat exchange of heat pipe 800
Also include casing 100, the core body 20 is installed in casing 100.During practical application, when core body 20 is installed on into casing 100, casing
100 bottom surface can abut with B plates deep gouge raised 402 so that the fluid that fluid is surrounded in casing 100 and B plate deep gouges projection 402
Flowed in groove 200, as shown in figure 14.The bottom surface of casing 100 can not also abut B plate deep gouges projection 402 so that fluid is in B plates
Flowed between 40 and casing 100.On the basis of above-described embodiment two, casing 100 is further added by, waste water can be introduced fluid slot
In 200 simultaneously so that the running water in medium runner 60 absorbs the heat of waste water in fluid slot 200 and A plates deep gouge 301, its suction
Thermal effect is good, makes full use of the structure of core body 20 to carry out heat exchange.Certainly, according to the demand for using, fluid slot 200 or A
Plate deep gouge 301 can be independently matched with the heat exchange that medium runner 60 is carried out between waste water and running water.
Example IV.
As shown in Figure 16 and Figure 17, the present embodiment four is with the difference of embodiment three:The core body 20 at least sets
It is equipped with two groups.In the present embodiment, multiple core bodys 20 are combined into combination core body 700, by the combination core body 700 in casing 100.
The medium runner 60 of each core body 20 is together in parallel using the first water inlet pipe and water outlet pipe 001 and the second water inlet pipe and water outlet pipe 002, it is concentrated
Logical running water.Meanwhile, in the turnover joint 500 of the logical waste water of the connection of casing 100, waste water is led in casing 100, make combination core body 700
In running water absorb waste water heat.It is of course also possible to the medium runner 60 of each core body 20 is together in series use.This reality
In applying example, in addition to the beneficial effect in embodiment three, be applied in combination for multiple core bodys 20 by it, it is possible to increase heat exchanger is changed
Heat.
In the present embodiment, some guide plates 600 being oriented to for the flow direction to fluid are provided with the casing 100,
The core body 20 is installed on some guide plates 600.Core body 20 is fixed by guide plate 600, and guide plate 600 can be to casing
The flow direction of 100 waste water plays guide effect, it is flowed in one direction.In addition, guide plate 600 plays installation and fixed core
The effect of body 20.
Above-described embodiment is the utility model preferably implementation, and in addition, the utility model can be with other sides
Formula realizes that any obvious replacement is in protection model of the present utility model on the premise of the technical program design is not departed from
Within enclosing.