CN108050631A - A kind of separating antifreezing type gravity full heat recovery device and air-conditioning - Google Patents
A kind of separating antifreezing type gravity full heat recovery device and air-conditioning Download PDFInfo
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- CN108050631A CN108050631A CN201810110952.7A CN201810110952A CN108050631A CN 108050631 A CN108050631 A CN 108050631A CN 201810110952 A CN201810110952 A CN 201810110952A CN 108050631 A CN108050631 A CN 108050631A
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- accumulator tank
- liquid level
- level sensor
- exchanger rig
- heat
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- 230000005484 gravity Effects 0.000 title claims abstract description 45
- 238000011084 recovery Methods 0.000 title claims abstract description 30
- 238000004378 air conditioning Methods 0.000 title claims abstract description 11
- 239000007788 liquid Substances 0.000 claims abstract description 114
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 49
- 239000012267 brine Substances 0.000 claims abstract description 33
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims abstract description 33
- 238000009434 installation Methods 0.000 claims abstract description 19
- 238000012856 packing Methods 0.000 claims description 38
- 239000000945 filler Substances 0.000 claims description 31
- 150000003839 salts Chemical class 0.000 claims description 14
- 238000000746 purification Methods 0.000 claims description 13
- 238000012384 transportation and delivery Methods 0.000 claims description 11
- 238000004891 communication Methods 0.000 claims description 7
- 238000004064 recycling Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims 2
- 238000005265 energy consumption Methods 0.000 abstract description 10
- 238000010586 diagram Methods 0.000 description 12
- 238000001914 filtration Methods 0.000 description 5
- 230000000007 visual effect Effects 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 230000003068 static effect Effects 0.000 description 3
- 208000002925 dental caries Diseases 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000036651 mood Effects 0.000 description 2
- 238000009938 salting Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 208000034423 Delivery Diseases 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0007—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F13/00—Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
- F24F13/30—Arrangement or mounting of heat-exchangers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
- F28F25/08—Splashing boards or grids, e.g. for converting liquid sprays into liquid films; Elements or beds for increasing the area of the contact surface
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The present invention provides a kind of separating antifreezing type gravity full heat recovery device and air-conditionings, belong to field of air conditioning, including the first heat exchange structure and the second heat exchange structure, the bottom of the first V-type heat-exchanger rig is connected with the first collecting tank, and the bottom of the first collecting tank is connected with the first accumulator tank；The bottom of second V-type heat-exchanger rig is connected with the second collecting tank, the bottom of second collecting tank is connected with the second accumulator tank, first accumulator tank is connected by the first brine pump with the second V-type heat-exchanger rig, and the second accumulator tank is connected by the second brine pump with the first V-type heat-exchanger rig.Separating antifreezing type gravity full heat recovery device provided by the invention is arranged for split, it and can be horizontally disposed, the problem of band liquid, also thoroughly solves, there is stable full heat recovery device as a high efficient and reliable, the energy consumption of pump reduces, and flow increases, can offset increases the energy consumption of pump, installation can be facilitated with split again, the heat exchange of air draft air water can be higher or lower than air-supply air water heat-exchanger rig, free convenience and high-efficiency.
Description
Technical field
The present invention relates to field of air conditioning, in particular to a kind of separating antifreezing type gravity full heat recovery device and sky
It adjusts.
Background technology
Existing solution-type heat reclamation device uses straight arrangement filler, and prior art air-supply band salting liquid problem can not be kept away
Exempt from, the section blast velocity control of air and filler contact is in 1.8-2.5 meter per seconds, since filler passage has certain angle, and angle
There are many angle, match somebody with somebody the filler that forms with 75 degree with common 45 ° of angles, effective passage only have the 50% of front face area less than,
Face velocity is too high, causes band liquid inevitable, since salting liquid has severe corrosive to metal, so behind filler plus to keep off
Then water plate adds chemical industry nylon wire preventing belt liquid, but cannot avoid completely again, simply band liquid how many problem of, process is not
It is good that more serious and universal thing is reformed into liquid, corrode all facilities of metal material, blow with the heat-exchanger rig of return air only
It can integrally arrange up and down, it is impossible to split, it has not been convenient to and cost is higher.
The content of the invention
It is an object of the invention to provide a kind of separating antifreezing type gravity full heat recovery device, to improve existing air-supply
It can only integrally be arranged up and down with the heat-exchanger rig of return air, it is impossible to split, the problem of causing inconvenient and cost higher.
It, can only be upper and lower with the heat-exchanger rig for improving existing air-supply and return air it is an object of the invention to provide a kind of air-conditioning
One arrangement, it is impossible to split, the problem of causing inconvenient and cost higher.
What the present invention was realized in：
Based on the first above-mentioned purpose, the present invention provides a kind of separating antifreezing type gravity full heat recovery device, including
First heat exchange structure and the second heat exchange structure, first heat exchange structure include the first V-type heat-exchanger rig, the first collecting tank and the
One accumulator tank, the bottom of the first V-type heat-exchanger rig are connected with first collecting tank, the bottom of first collecting tank with
The first accumulator tank connection；Second heat exchange structure includes the second V-type heat-exchanger rig, the second collecting tank and the second recycling
Slot, the bottom of the second V-type heat-exchanger rig are connected with second collecting tank, the bottom of second collecting tank and described the
Two accumulator tanks connect, and first accumulator tank is connected by the first brine pump with the second V-type heat-exchanger rig, described second time
Slot is received to connect with the first V-type heat-exchanger rig by the second brine pump.
Separating antifreezing type gravity full heat recovery device provided by the invention is split arrangement, and can be horizontally disposed, band
The problem of liquid, also thoroughly solves.There is stable full heat recovery device as a high efficient and reliable, raising due to pump when horizontally disposed
Journey reduces, so the energy consumption of pump reduces, flow increases, and can offset the energy consumption for increasing pump, and can facilitate installation, air draft with split
Air water heat exchange can be higher or lower than air-supply air water heat-exchanger rig, and can lack a pump, and higher V-type heat-exchanger rig can not
If pump, brine by gravity natural back flow in relatively low air water heat-exchanger rig, free convenience and high-efficiency.
In an embodiment of the present embodiment：First collecting tank is connected by delivery pipe and first accumulator tank
Logical, first heat exchange structure further includes gravity salt water purification installation, the input terminal of the gravity salt water purification installation with it is described
Delivery pipe is connected close to one end of first collecting tank, the output terminal of the gravity salt water purification installation and the described first recycling
Slot connects.
With sundries such as particles, liquid can be filtered into the first recycling liquid after heat exchange through gravity salt water purification installation
Slot, if the filtering of gravity salt water purification installation is too late, liquid flows into the first accumulator tank by delivery pipe.
In an embodiment of the present embodiment：The first V-type heat-exchanger rig include first shell, the first cover and
First filler, first cover cap are connected to the first shell, form the first cavity, first is provided in first cover
Opening, first opening are connected with first cavity, and first filler is installed on the first shell, and described first
Filler is located in first cavity, and second accumulator tank passes through second brine pump and first open communication；Institute
Stating the second V-type heat-exchanger rig includes second shell, the second cover and the second filler, and second cover cap is connected to the second shell
Body forms the second cavity, and the second opening is provided in second cover, and second opening is connected with second cavity,
Second filler is installed on the second shell, and second filler is located in second cavity, first recycling
Slot passes through first brine pump and second open communication.
In an embodiment of the present embodiment：First filler includes frame and multiple packing sheets, the filler
Piece is corrugated, and multiple packing sheets are respectively arranged in the frame, and multiple packing sheets are arranged at intervals, the filler
The plate face of piece is arranged in parallel, and the wave height of the packing sheet is 4-10 millimeters, and the ripple width of the packing sheet is 7-25 millimeters, the side
Frame is installed on the first shell.
The packing sheet of this shape best results in use.
In an embodiment of the present embodiment：The wave height line of the packing sheet is obliquely installed with the frame, and institute
The angle between the wave height line of packing sheet and the frame is stated between 75 degree to 90 degree.
Packing sheet and frame are obliquely installed, frame can be allowed more convenient when mounted, easily controls the angle of packing sheet
Degree.
In an embodiment of the present embodiment：First accumulator tank passes through the first water-supply-pipe and second V-type
Heat-exchanger rig connects, and the one end of first water-supply-pipe away from first accumulator tank includes the first branch pipe and the second branch pipe, institute
The first branch pipe and second open communication are stated, the side wall of the second branch pipe from the second shell stretches into second cavity
Interior, first brine pump is installed on first water-supply-pipe close to one end of first accumulator tank；Second accumulator tank
Be connected by the second water-supply-pipe with the first V-type heat-exchanger rig, second water-supply-pipe away from second accumulator tank one
End includes the 3rd branch pipe and the 4th branch pipe, the 3rd branch pipe and first open communication, and the 4th branch pipe is from described the
The side wall of one housing is stretched into first cavity, and second brine pump is installed on second water-supply-pipe close to described second
One end of accumulator tank.
In an embodiment of the present embodiment：First heat exchange structure further includes automatic water compensating valve, the first high liquid
Liquid level sensor and the first low liquid level sensor in level sensor, first, the automatic water compensating valve connect with first accumulator tank
It connects, liquid level sensor and first low liquid level sensor are respectively arranged in the first high liquid level sensor, described first
First accumulator tank, and liquid level sensor and first low liquid level pass in the first high liquid level sensor, described first
Sensor is arranged at intervals along the short transverse of first accumulator tank；Second heat exchange structure further includes the second high liquid level sensing
Liquid level sensor and the second low liquid level sensor in device, second, level sensing in the second high liquid level sensor, described second
Device and second low liquid level sensor are respectively arranged in second accumulator tank, and the second high liquid level sensor, described
Liquid level sensor and second low liquid level sensor are arranged at intervals along the short transverse of second accumulator tank in second.
In an embodiment of the present embodiment：First collecting tank includes the first collection portion and the first liquid collecting portion,
The first collection portion is installed on the bottom of the first shell, and the first collection portion is obliquely installed, the first collection portion
The one end being connected with the first liquid collecting portion is less than one end that the first collection portion is connected with the first shell；Described second
Collecting tank includes the second collection portion and the second liquid collecting portion, and the second collection portion is installed on the bottom of the second shell, described
Second collection portion is obliquely installed, and one end that the second collection portion is connected with the second liquid collecting portion is less than the second collection portion
The one end being connected with the second shell.
In an embodiment of the present embodiment：Second heat exchange structure is arranged to multiple, first accumulator tank
It is connected with first the second V-type heat-exchanger rig, first second accumulator tank is filled with adjacent second V-type heat exchange
Connection is put, second accumulator tank on side is connected with the first V-type heat-exchanger rig.
Multiple second heat exchange structures can promote the effect of heat exchange and filtering.
Based on the second above-mentioned purpose, the present invention also provides a kind of air-conditioning, including separating antifreezing type as described above
Gravity full heat recovery device.
Air-conditioning provided by the invention includes above-mentioned separating antifreezing type gravity full heat recovery device, and low energy consumption for pump, row
The heat exchange of general mood water can be higher or lower than air-supply air water heat-exchanger rig, free convenience and high-efficiency.
Compared with prior art, the advantageous effect realized of the present invention is：
Separating antifreezing type gravity full heat recovery device provided by the invention is split arrangement, and can be horizontally disposed, band
The problem of liquid, also thoroughly solves.There is stable full heat recovery device as a high efficient and reliable, raising due to pump when horizontally disposed
Journey reduces, so the energy consumption of pump reduces, flow increases, and can offset the energy consumption for increasing pump, and can facilitate installation, air draft with split
Air water heat exchange can be higher or lower than air-supply air water heat-exchanger rig, and can lack a pump, and higher V-type heat-exchanger rig can not
If pump, brine by gravity natural back flow in relatively low air water heat-exchanger rig, free convenience and high-efficiency.
Description of the drawings
It, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical solution of the prior art
The attached drawing of required practicality is briefly described in embodiment or description of the prior art, it should be apparent that, it is described below attached
Figure is some embodiments of the present invention, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it can also be obtained according to these attached drawings other attached drawings.
Fig. 1 shows the signal for the first separating antifreezing type gravity full heat recovery device that the embodiment of the present invention 1 provides
Figure；
Fig. 2 shows the signal for second of separating antifreezing type gravity full heat recovery device that the embodiment of the present invention 1 provides
Figure；
Fig. 3 shows schematic diagram of the first V-type heat-exchanger rig at the first visual angle of the offer of the embodiment of the present invention 1；
Fig. 4 shows schematic diagram of the first V-type heat-exchanger rig at the second visual angle of the offer of the embodiment of the present invention 1；
Fig. 5 shows the schematic diagram for the first filler that the embodiment of the present invention 1 provides；
Fig. 6 shows the schematic diagram for the first packing sheet that the embodiment of the present invention 1 provides；
Fig. 7 shows schematic diagram of the second V-type heat-exchanger rig at the first visual angle of the offer of the embodiment of the present invention 1；
Fig. 8 shows schematic diagram of the second V-type heat-exchanger rig at the second visual angle of the offer of the embodiment of the present invention 1；
Fig. 9 shows the schematic diagram for the second filler that the embodiment of the present invention 1 provides；
Figure 10 shows the schematic diagram for the second packing sheet that the embodiment of the present invention 1 provides；
Figure 11 shows the schematic diagram for the first collecting tank that the embodiment of the present invention 1 provides；
Figure 12 shows the schematic diagram for the second collecting tank that the embodiment of the present invention 1 provides；
Figure 13 shows the schematic diagram for the first water-supply-pipe that the embodiment of the present invention 1 provides；
Figure 14 shows the schematic diagram for the second water-supply-pipe that the embodiment of the present invention 1 provides.
In figure：101- the first V-type heat-exchanger rigs；The first collecting tanks of 102-；103- delivery pipes；104- gravity salt Water warfare fills
It puts；The first accumulator tanks of 105-；The first brine pumps of 106-；107- the second V-type heat-exchanger rigs；The second collecting tanks of 108-；109- pipelines；
The second accumulator tanks of 110-；The second brine pumps of 111-；112- first shells；The first covers of 113-；The first cavitys of 114-；115- first
Opening；The first fillers of 116-；117- frames；118- packing sheets；119- second shells；The second covers of 120-；The second cavitys of 121-；
122- second is open；The second fillers of 123-；The second frames of 124-；The second packing sheets of 125-；The first collections of 126- portion；127- first
Liquid collecting portion；The second collections of 128- portion；The second liquid collectings of 129- portion；130- automatic water compensating valves；131- the first high liquid level sensors；132-
Liquid level sensor in first；133 first low liquid level sensors；The first water-supply-pipes of 134-；The first branch pipes of 135-；136- second
Pipe；137- the second high liquid level sensors；Liquid level sensor in 138- second；139 second low liquid level sensors；The second water deliverys of 140-
Pipe；The 3rd branch pipes of 141-；The 4th branch pipes of 142-.
Specific embodiment
The present invention is described in further detail below through specific implementation examples and in conjunction with the accompanying drawings.
To make the purpose, technical scheme and advantage of the embodiment of the present invention clearer, above in conjunction in the embodiment of the present invention
Attached drawing, the technical solution in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is
Part of the embodiment of the present invention, instead of all the embodiments.The present invention implementation being usually described and illustrated herein in the accompanying drawings
The component of example can configure to arrange and design with a variety of.
Therefore, the detailed description of the embodiment of the present invention more than to providing in the accompanying drawings is not intended to limit claimed
The scope of the present invention, but be merely representative of the present invention selected embodiment.Based on the embodiments of the present invention, this field is common
Technical staff's all other embodiments obtained without creative efforts belong to the model that the present invention protects
It encloses.
It should be noted that：Similar label and letter represents similar terms in following attached drawing, therefore, once a certain Xiang Yi
It is defined, then it further need not be defined and explained in subsequent attached drawing in a attached drawing.
In the description of the present invention, it is to be understood that the term of indicating position or position relationship is based on shown in attached drawing
Orientation or position relationship, be for only for ease of the description present invention and simplify description rather than instruction or imply signified equipment
Or element must have specific orientation, with specific azimuth configuration and operation, therefore be not considered as limiting the invention.
In the present invention, unless otherwise clearly defined and limited, term " installation ", " connected ", " connection ", " fixation " etc.
Term should be interpreted broadly, for example, it may be being fixedly connected or integral；Can be mechanical connection or electrical connection；
It can be directly connected, can also be indirectly connected by intermediary, can be the connection inside two elements or two elements
Interaction relationship.For the ordinary skill in the art, above-mentioned term can be understood at this as the case may be
Concrete meaning in invention.
In the present invention, unless otherwise clearly defined and limited, fisrt feature can be on or below second feature
Contacted directly including the first and second features, can also include the first and second features not be contact directly but by them it
Between other characterisation contact.Moreover, fisrt feature is on second feature, top and above to include fisrt feature special second
Directly over sign and oblique upper is merely representative of fisrt feature level height higher than second feature.Fisrt feature second feature it
Under, lower section and fisrt feature included below immediately below second feature and obliquely downward or be merely representative of fisrt feature level height
Less than second feature.
It should be noted that in the case where there is no conflict, the feature in embodiment and embodiment in the present invention can phase
Mutually combination.
Embodiment 1
Referring to figs. 1 to Figure 14, a kind of separating antifreezing type gravity full heat recovery device is present embodiments provided, including first
Heat exchange structure and the second heat exchange structure, the first heat exchange structure include the first V-type heat-exchanger rig 101, the first collecting tank 102 and first
Accumulator tank 105, the bottom of the first V-type heat-exchanger rig 101 are connected with the first collecting tank 102, the bottom of the first collecting tank 102 and the
One accumulator tank 105 connects；Second heat exchange structure includes the second V-type heat-exchanger rig 107, the second collecting tank 108 and the second accumulator tank
110, the bottom of the second V-type heat-exchanger rig 107 is connected with the second collecting tank 108, and the bottom of the second collecting tank 110 passes through pipeline
109 connect with the second accumulator tank 110, and the first accumulator tank 105 is connected by the first brine pump 106 and the second V-type heat-exchanger rig 107
Logical, the second accumulator tank 110 is connected by the second brine pump 111 with the first V-type heat-exchanger rig 101.
Separating antifreezing type gravity full heat recovery device provided in this embodiment is split arrangement, and can be horizontally disposed,
The problem of band liquid, also thoroughly solves.There is stable full heat recovery device as a high efficient and reliable, due to pump when horizontally disposed
Lift reduces, so the energy consumption of pump reduces, flow increases, and can offset the energy consumption for increasing pump, and can facilitate installation with split, arranges
The heat exchange of general mood water can be higher or lower than air-supply air water heat-exchanger rig, and can lack a pump, and higher V-type heat-exchanger rig can be with
Pump is not set, brine is by gravity natural back flow to relatively low air water heat-exchanger rig, free convenience and high-efficiency.
First collecting tank 102 is connected by delivery pipe 103 with the first accumulator tank 105, and the first heat exchange structure further includes gravity
Salt water purification installation 104, the input terminal and delivery pipe 103 of gravity salt water purification installation 104 are close to one end of the first collecting tank 102
Connection, the output terminal of gravity salt water purification installation 104 are connected with the first accumulator tank 105.If the liquid after heat exchange is with particle etc.
Sundries, then liquid can be filtered through gravity salt water purification installation 104 enters the first accumulator tank 105, if gravity salt water purification installation
104 filterings are too late, then liquid can flow into the first accumulator tank 105 by delivery pipe 103.
First V-type heat-exchanger rig 101 includes first shell 112, the first cover 113 and the first filler 116, the first cover
113 lids are connected to first shell 112, form the first cavity 114, and the first opening 115, the first opening are provided in the first cover 113
115 connect with the first cavity 114, and the first filler 116 is installed on first shell 112, and the first filler 116 is located at the first cavity
In 114, the second accumulator tank 110 is connected by the second brine pump 111 with the first opening 115；Second V-type heat-exchanger rig 107 includes
Second shell 119, the second cover 120 and the second filler 123, the second cover 120 lid are connected to second shell 119, it is empty to form second
Chamber 121 is provided with the second opening 122 in second cover 120, and the second opening 122 is connected with the second cavity 121, the second filler 123
Second shell 119 is installed on, and the second filler 123 is located in the second cavity 121, the first accumulator tank 105 passes through the first brine pump
106 connect with the second opening 122.
First filler 116 includes frame 117 and multiple packing sheets 118, and packing sheet 118 is corrugated, multiple packing sheets 118
It is respectively arranged in frame 117, multiple packing sheets 118 are arranged at intervals, and the plate face of packing sheet 118 is arranged in parallel, packing sheet 118
Wave height is 4-10 millimeters, and the ripple width of packing sheet 118 is 7-25 millimeters, and frame 117 is installed on first shell 112.This shape
The best results in use of packing sheet 118.
Second filler 123 includes the second frame 124 and multiple second packing sheets 125, the second frame 124 and above-mentioned frame
117 is identical, and the second packing sheet 125 is identical with above-mentioned packing sheet 118.
The wave height line of packing sheet 118 is obliquely installed with frame 117, and between the wave height line of packing sheet 118 and frame 117
Angle is between 75 degree to 90 degree.Packing sheet 118 and frame 117 are obliquely installed, frame 117 can be allowed more square when mounted
Just, the angle of packing sheet 118 is easily controlled.
First accumulator tank 105 is connected by the first water-supply-pipe 134 with the second V-type heat-exchanger rig 107, the first water-supply-pipe 134
One end away from the first accumulator tank 105 includes the first branch pipe 135 and the second branch pipe 136, the first branch pipe 135 and the second opening 122
Connection, the side wall of the second branch pipe 136 from second shell 119 are stretched into the second cavity 121, and the first brine pump 106 is installed on first
Water-supply-pipe 134 is close to one end of the first accumulator tank 105；Second accumulator tank 110 is exchanged heat by the second water-supply-pipe 140 and the first V-type
Device 101 connects, and the one end of the second water-supply-pipe 140 away from the second accumulator tank 110 includes the 3rd branch pipe 141 and the 4th branch pipe 142,
3rd branch pipe 141 is connected with the first opening 115, and the side wall of the 4th branch pipe 142 from first shell 112 is stretched into the first cavity 114,
Second brine pump 111 is installed on the second water-supply-pipe 140 close to one end of the second accumulator tank 110.
First heat exchange structure further includes liquid level sensor in automatic water compensating valve 130, the first high liquid level sensor 131, first
132 and first low liquid level sensor 133, automatic water compensating valve 130 be connected with the first accumulator tank 105, the first high liquid level sensor
131st, 132 and first low liquid level sensor 133 of liquid level sensor is respectively arranged in the first accumulator tank 105 in first, and first is high
Height side of 132 and first low liquid level sensor 133 of liquid level sensor along the first accumulator tank 105 in liquid level sensor 131, first
To interval setting；It is low that second heat exchange structure further includes liquid level sensor 138 and second in the second high liquid level sensor 137, second
Liquid level sensor 139,138 and second low liquid level sensor 139 of liquid level sensor is divided in the second high liquid level sensor 137, second
The second accumulator tank 110 is not installed on, and 138 and second low liquid level of liquid level sensor passes in the second high liquid level sensor 137, second
Sensor 139 is arranged at intervals along the short transverse of the second accumulator tank 110.
Wherein, automatic water compensating valve 130 is the assembly of pressure reducing valve, filter, shut-off valve and check-valves, can keep system
Pressure is in a stationary value, and when pressure decreases, valve can automatically open, to system water supplement, after reaching setting pressure, valve from
It is dynamic to close, filter is carried in valve, can be to avoid the inflow of impurity, built-in check valve in valve can prevent heating system
Hot water return is to cold water pipeline, even if inlet pressure changes, pressure regulator can keep the stabilization of outlet pressure.In case of emergency or
Maintenance system, automatic water compensating valve 130 are equipped with hand stop valve.It horizontal or vertical can install, it is water inlet end to have arrow one side.
Liquid level sensor (static pressure liquid level meter/fluid level transmitter/liquid level sensor/water level sensor) is a kind of measurement liquid level
Pressure sensor.Static pressure throw-in type liquid transmitter (liquid level gauge) be based on the height of surveyed fluid pressure and the liquid into than
Using external advanced isolated form diffusion silicon-sensitive element or ceramic capacitive pressure sensitive sensor, static pressure is turned for the principle of example
Electric signal is changed to, using temperature-compensating and linear amendment, changes into standard electric signal (generally 4~20mA/1~5VDC).
First collecting tank 102 includes the first collection portion 126 and the first liquid collecting portion 127, and the first collection portion 126 is installed on first
The bottom of housing 112, the first collection portion 126 are obliquely installed, and the first collection portion 126 is low with the first liquid collecting portion 127 one end being connected
In one end that the first collection portion 126 is connected with first shell 112；Second collecting tank 108 includes the second collection portion 128 and the second collection
Liquid portion 129, the second collection portion 128 are installed on the bottom of second shell 119, and the second collection portion 128 is obliquely installed, the second collection portion
128 one end being connected with the second liquid collecting portion 129 are less than one end that the second collection portion 128 is connected with second shell 119.
Second heat exchange structure is arranged to multiple, and the first accumulator tank 105 is connected with first the second V-type heat-exchanger rig 107, the
One the second accumulator tank 110 is connected with the second adjacent V-type heat-exchanger rig 107, the second accumulator tank 110 and first on side
V-type heat-exchanger rig 101 connects.Multiple second heat exchange structures can promote the effect of heat exchange and filtering.
In use, outdoor fresh air is carried out gas-liquid heat exchange, fresh air is heated or is dropped by the first V-type heat-exchanger rig 101
Temperature；Liquid after heat exchange is with sundries such as particles, through the filtering of gravity salt water purification installation 104 into the first accumulator tank 105, when molten
When liquid measure is big, the first accumulator tank 105 is directly entered by delivery pipe 103, then liquid exchanges heat through the second V-type heat-exchanger rig 107,
Second V-type heat-exchanger rig, 107 air inlet connects indoor return air, is discharged through heat exchange, is then recycled through the second collecting tank 108, second
Slot 110, the second brine pump 111 are cycled into the first V-type heat exchanger.
Under normal circumstances, the liquid level in the first accumulator tank 105 and the second accumulator tank 110 is in middle liquid level, each liquid in system
Level sensor, water pump, water compensating valve control logic are as follows：
When liquid level is less than middle liquid level, the first automatic valve, which is opened, carries out moisturizing, when rate of water make-up is excessive or wrong, reaches
High liquid level, the first high liquid level sensor 131 close water compensating valve, simultaneously close off the second brine pump 111, etc. liquid levels decline after 10s, the
Two brine pumps 111 are opened；
When liquid level is too low, the first low sensors and the first low sensors start, at this time the first brine pump 106 and second
Brine pump 111 is closed；
When the second accumulator tank 110 reaches high liquid level, when the second high liquid level sensor 137 is opened, the first brine pump is closed
106, etc. liquid levels decline after after 3s~10s, the first brine pump 106 is opened.
Embodiment 2
The present embodiment additionally provides a kind of air-conditioning, including separating antifreezing type gravity full heat recovery device as above.
Air-conditioning provided in this embodiment includes above-mentioned separating antifreezing type gravity full heat recovery device, and low energy consumption for pump,
The heat exchange of air draft air water can be higher or lower than air-supply air water heat-exchanger rig, free convenience and high-efficiency.
The foregoing is only a preferred embodiment of the present invention, is not intended to limit the invention, for the skill of this field
For art personnel, the invention may be variously modified and varied.Within the spirit and principles of the invention, that is made any repaiies
Change, equivalent substitution, improvement etc., should all be included in the protection scope of the present invention.
Claims (10)
1. a kind of separating antifreezing type gravity full heat recovery device, which is characterized in that exchange heat including the first heat exchange structure and second
Structure, first heat exchange structure include the first V-type heat-exchanger rig, the first collecting tank and the first accumulator tank, and first V-type is changed
The bottom of thermal is connected with first collecting tank, and the bottom of first collecting tank is connected with first accumulator tank；Institute
Stating the second heat exchange structure includes the second V-type heat-exchanger rig, the second collecting tank and the second accumulator tank, the second V-type heat-exchanger rig
Bottom connected with second collecting tank, the bottom of second collecting tank is connected with second accumulator tank, described first
Accumulator tank is connected by the first brine pump with the second V-type heat-exchanger rig, second accumulator tank by the second brine pump with
The first V-type heat-exchanger rig connection.
2. separating antifreezing type gravity full heat recovery device according to claim 1, which is characterized in that first liquid collecting
Slot is connected by delivery pipe with first accumulator tank, and first heat exchange structure further includes gravity salt water purification installation, described
The input terminal of gravity salt water purification installation is connected with the delivery pipe close to one end of first collecting tank, the gravity brine
The output terminal of purifier is connected with first accumulator tank.
3. separating antifreezing type gravity full heat recovery device according to claim 1, which is characterized in that first V-type
Heat-exchanger rig includes first shell, the first cover and the first filler, and first cover cap is connected to the first shell, forms the
One cavity is provided with the first opening in first cover, and first opening is connected with first cavity, and described first fills out
Material is installed on the first shell, and first filler is located in first cavity, and second accumulator tank passes through described
Second brine pump and first open communication；The second V-type heat-exchanger rig includes second shell, the second cover and second is filled out
Material, second cover cap are connected to the second shell, form the second cavity, the second opening is provided in second cover,
Second opening is connected with second cavity, and second filler is installed on the second shell, and second filler
In second cavity, first accumulator tank passes through first brine pump and second open communication.
4. separating antifreezing type gravity full heat recovery device according to claim 3, which is characterized in that first filler
Including frame and multiple packing sheets, the packing sheet is corrugated, and multiple packing sheets are respectively arranged in the frame, more
A packing sheet is arranged at intervals, and the plate face of the packing sheet is arranged in parallel, and the wave height of the packing sheet is 4-10 millimeters, described
The ripple width of packing sheet is 7-25 millimeters, and the frame is installed on the first shell.
5. separating antifreezing type gravity full heat recovery device according to claim 4, which is characterized in that the packing sheet
Wave height line is obliquely installed with the frame, and the angle between the wave height line of the packing sheet and the frame is at 75 degree to 90 degree
Between.
6. separating antifreezing type gravity full heat recovery device according to claim 3, which is characterized in that first recycling
Slot is connected by the first water-supply-pipe with the second V-type heat-exchanger rig, and first water-supply-pipe is away from first accumulator tank
One end includes the first branch pipe and the second branch pipe, first branch pipe and second open communication, and second branch pipe is from described
The side wall of second shell is stretched into second cavity, and first brine pump is installed on first water-supply-pipe close to described
One end of one accumulator tank；Second accumulator tank is connected by the second water-supply-pipe with the first V-type heat-exchanger rig, and described second
The one end of water-supply-pipe away from second accumulator tank includes the 3rd branch pipe and the 4th branch pipe, and the 3rd branch pipe is opened with described first
Mouth connection, the side wall of the 4th branch pipe from the first shell are stretched into first cavity, the second brine pump installation
In second water-supply-pipe close to one end of second accumulator tank.
7. separating antifreezing type gravity full heat recovery device according to claim 3, which is characterized in that first heat exchange
Structure further includes liquid level sensor and the first low liquid level sensor in automatic water compensating valve, the first high liquid level sensor, first, described
Automatic water compensating valve is connected with first accumulator tank, liquid level sensor and institute in the first high liquid level sensor, described first
It states the first low liquid level sensor and is respectively arranged in first accumulator tank, and in the first high liquid level sensor, described first
Liquid level sensor and first low liquid level sensor are arranged at intervals along the short transverse of first accumulator tank；Described second changes
Heat structure further includes liquid level sensor and the second low liquid level sensor in the second high liquid level sensor, second, the second high liquid
Liquid level sensor and second low liquid level sensor are respectively arranged in second accumulator tank in level sensor, described second,
And in the second high liquid level sensor, described second liquid level sensor and second low liquid level sensor along described second time
The short transverse for receiving slot is arranged at intervals.
8. separating antifreezing type gravity full heat recovery device according to claim 3, which is characterized in that first liquid collecting
Slot includes the first collection portion and the first liquid collecting portion, and the first collection portion is installed on the bottom of the first shell, and described first
Collection portion is obliquely installed, and one end that the first collection portion is connected with the first liquid collecting portion is less than the first collection portion and institute
State one end of first shell connection；Second collecting tank includes the second collection portion and the second liquid collecting portion, the second collection portion
The bottom of the second shell is installed on, the second collection portion is obliquely installed, the second collection portion and second liquid collecting
One end of portion's connection is less than one end that the second collection portion is connected with the second shell.
9. separating antifreezing type gravity full heat recovery device according to claim 1, which is characterized in that second heat exchange
To be multiple, first accumulator tank connects structure setting with first the second V-type heat-exchanger rig, first described second time
It receives slot to connect with adjacent the second V-type heat-exchanger rig, second accumulator tank on side exchanges heat with first V-type
Device connects.
10. a kind of air-conditioning, which is characterized in that entirely hot including separating antifreezing type gravity as described in any one of claim 1 to 9
Retracting device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810110952.7A CN108050631A (en) | 2018-02-02 | 2018-02-02 | A kind of separating antifreezing type gravity full heat recovery device and air-conditioning |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810110952.7A CN108050631A (en) | 2018-02-02 | 2018-02-02 | A kind of separating antifreezing type gravity full heat recovery device and air-conditioning |
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| Publication Number | Publication Date |
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| CN108050631A true CN108050631A (en) | 2018-05-18 |
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|---|---|---|---|
| CN201810110952.7A Pending CN108050631A (en) | 2018-02-02 | 2018-02-02 | A kind of separating antifreezing type gravity full heat recovery device and air-conditioning |
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