CN209138027U - A kind of waste heat recycling VOC condensate recovery system - Google Patents
A kind of waste heat recycling VOC condensate recovery system Download PDFInfo
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- CN209138027U CN209138027U CN201821779190.1U CN201821779190U CN209138027U CN 209138027 U CN209138027 U CN 209138027U CN 201821779190 U CN201821779190 U CN 201821779190U CN 209138027 U CN209138027 U CN 209138027U
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- main body
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Abstract
The utility model discloses a kind of waste heats to recycle VOC condensate recovery system, including condensing main body, the lower end outer surface of the condensation main body is provided with pedestal, the upper end outer surface of the pedestal is provided with bracket, the upper end outer surface of the bracket is provided with air blower, ventilation shaft is provided between the air blower and condensation main body, one side external surface of the condensation main body is provided with outer tank, it is provided with connection water pipe between the outer tank and condensation main body, the lower end outer surface of the outer tank is provided with outlet pipe.A kind of waste heat described in the utility model recycles VOC condensate recovery system, by being provided with outer tank and inner tank, the heat generated in VOC condensation process can be made full use of, by being provided with air blower and ventilation shaft, so that VOC gas accelerate the internal flow in condensation main body, the condensing recovery efficiency for improving VOC, brings better prospect of the application.
Description
Technical field
The utility model relates to technical field of waste gas treatment, in particular to a kind of waste heat recycles VOC condensate recovery system.
Background technique
VOC is a kind of active volatile organic matter, and with China's industrialization development to certain phase, many organises
Factory generates a large amount of VOC gas during processing, causes the serious pollution of environment, the condensation of VOC into atmosphere
Recycling is of great significance;There are certain drawbacks in existing VOC condensate recovery system, firstly, for VOC gas when in use
In heat can not recycle, be not energy-saving and environment-friendly, secondly, the flowing of gas is slower during for VOC condensing recovery,
The efficiency of condensing recovery is influenced, for this purpose, it is proposed that a kind of waste heat recycles VOC condensate recovery system.
Utility model content
The main purpose of the utility model is to provide a kind of waste heats to recycle VOC condensate recovery system, can effectively solve
Certainly the problems in background technique.
To achieve the above object, the technical solution that the utility model is taken are as follows:
The lower end outer surface of a kind of waste heat recycling VOC condensate recovery system, including condensation main body, the condensation main body is set
It is equipped with pedestal, the upper end outer surface of the pedestal is provided with bracket, and the upper end outer surface of the bracket is provided with air blower, described
Ventilation shaft is provided between air blower and condensation main body, a side external surface of the condensation main body is provided with outer tank, institute
It states and is provided with connection water pipe between outer tank and condensation main body, the lower end outer surface of the outer tank is provided with outlet pipe,
Another side external surface of the condensation main body is provided with water inlet pipe, the inside of the condensation main body relative to the side of outer tank
The position of connection water pipe is provided with inner tank, the upper end of the condensation main body is provided with gas and is discharged into pipe, the gas
The lower end for being discharged into pipe is provided with bridge piece, and the inside of the condensation main body goes out far from condensate liquid is provided with below heat exchanger tube
Mouthful.
Preferably, the lower end of the condensate outlet is provided with collecting chamber, and the collecting chamber is located at the inside of condensation main body,
The condensate outlet is provided with drain pipe through the upper end outer surface of collecting chamber, the leading exterior surface of the condensation main body,
A side external surface of the drain pipe through condensation main body and collecting chamber.
Preferably, the inside of the condensation main body is provided with heat exchanger tube below inner tank, the heat exchanger tube
Through the outer surface of the inside of condensation main body and a side external surface of outer tank, the quantity of the heat exchanger tube is several for one end
Group, the heat exchanger tube are arranged in array.
Preferably, one end of the water inlet pipe through condensation main body and inner tank a side external surface, it is described into
To be fixedly connected between water pipe and condensation main body, the bridge piece through the inside of inner tank, the connection water pipe
One end is to be fixedly connected between the inner tank and condensation main body through a side external surface of inner tank, the gas
It is discharged between pipe and bridge piece to be fixedly connected.
Preferably, to be fixedly connected between the outer tank and condensation main body, the connection water pipe is through external water
The upper end outer surface of case, the outlet pipe through the lower end outer surface of outer tank, the outer tank with connect water pipe with
It and is to be fixedly connected between outlet pipe.
Preferably, be to be fixedly connected between the pedestal and condensation main body and bracket, the air blower and bracket it
Between to be fixedly connected, the input port of the air blower and the output port of condensation main body are electrically connected, the ventilation shaft
Quantity be two groups, the ventilation shaft through air blower and condense main body inside.
Compared with prior art, the utility model has the following beneficial effects: the waste heat recycles VOC condensing recovery system
System, by being provided with outer tank and inner tank, water is added in inner tank user from water inlet pipe, and water is again by connection water
Pipe enters in outer tank, mating connection bend pipe, when VOC gas, which are discharged into pipe from gas, to be entered from bridge piece, heat with
Water in inner tank swaps, and when VOC gas continue to run at heat exchanger tube, heat exchanger tube condenses VOC, heat exchanger tube
In heat be further transferred in outer tank, the water in outer tank with heat exchange tubular heat exchange, it is cold to take full advantage of VOC
The heat generated during solidifying, by being provided with air blower and ventilation shaft, air blower operating is made cold by two groups of ventilation shafts
The position air flow faster of the close lower end of solidifying body interior, so that VOC gas accelerate the inside stream in condensation main body
It is dynamic, the condensing recovery efficiency of VOC is improved, a kind of entire waste heat recycling VOC condensate recovery system is compact-sized, the effect used
It is more preferable relative to traditional approach.
Detailed description of the invention
Fig. 1 is the overall structure diagram that a kind of waste heat of the utility model recycles VOC condensate recovery system.
Fig. 2 is the positive cross-sectional view that a kind of waste heat of the utility model recycles VOC condensate recovery system.
Fig. 3 is the partial view that a kind of waste heat of the utility model recycles VOC condensate recovery system.
Fig. 4 is the enlarged drawing that a kind of waste heat of the utility model recycles A in Fig. 2 of VOC condensate recovery system.
In figure: 1, condensing main body;2, pedestal;3, bracket;4, air blower;5, ventilation shaft;6, outer tank;7, water is connected
Pipe;8, outlet pipe;9, water inlet pipe;10, inner tank;11, gas is discharged into pipe;12, bridge piece;13, heat exchanger tube;14, it condenses
Liquid outlet;15, collecting chamber;16, drain pipe.
Specific embodiment
To be easy to understand the technical means, creative features, achievement of purpose, and effectiveness of the utility model, below
In conjunction with specific embodiment, the utility model is further described.
As shown in Figs 1-4, a kind of waste heat recycles VOC condensate recovery system, including condensation main body 1, condenses under main body 1
End outer surface is provided with pedestal 2, and the upper end outer surface of pedestal 2 is provided with bracket 3, and the upper end outer surface of bracket 3 is provided with air blast
Machine 4, is provided with ventilation shaft 5 between air blower 4 and condensation main body 1, a side external surface of condensation main body 1 is provided with outer tank
6, connection water pipe 7 is provided between outer tank 6 and condensation main body 1, the lower end outer surface of outer tank 6 is provided with outlet pipe 8,
Another side external surface for condensing main body 1 is provided with water inlet pipe 9 relative to the side of outer tank 6, and the inside for condensing main body 1 is close
The position of connection water pipe 7 is provided with inner tank 10, and the upper end of condensation main body 1 is provided with gas and is discharged into pipe 11, and gas is discharged into pipe
11 lower end is provided with bridge piece 12, and the inside of condensation main body 1 is provided with condensate outlet 14 far from the lower section of heat exchanger tube 13.
The lower end of condensate outlet 14 is provided with collecting chamber 15, and collecting chamber 15 is located at the inside of condensation main body 1, and condensate liquid goes out
Mouth 14 is through the upper end outer surface of collecting chamber 15, and the leading exterior surface for condensing main body 1 is provided with drain pipe 16, and drain pipe 16 passes through
It is through at a side external surface of condensation main body 1 and collecting chamber 15, it is ensured that drain pipe 16 can return the VOC liquid in collecting chamber 15
It receives;The inside for condensing main body 1 is provided with heat exchanger tube 13 close to the lower section of inner tank 10, and one end of heat exchanger tube 13 is through condensation
The quantity of the outer surface of the inside of main body 1 and a side external surface of outer tank 6, heat exchanger tube 13 is several groups, and heat exchanger tube 13 is in
Array arrangement, several groups heat exchanger tube 13 ensure the abundant condensation of VOC gas;One end of water inlet pipe 9 through condensation main body 1 and
One side external surface of inner tank 10, to be fixedly connected between water inlet pipe 9 and condensation main body 1, bridge piece 12 is through inside
The inside of water tank 10 connects one end of water pipe 7 through a side external surface of inner tank 10, inner tank 10 and condensation main body
To be fixedly connected between 1, gas is discharged between pipe 11 and bridge piece 12 to be fixedly connected, and bridge piece 12 ensures VOC gas
In heat heat carried out by tube wall and water body as far as possible exchange;To be fixedly connected between outer tank 6 and condensation main body 1,
Water pipe 7 is connected through the upper end outer surface of outer tank 6, outlet pipe 8 is external through the lower end outer surface of outer tank 6
It is to be fixedly connected between water tank 6 and connection water pipe 7 and outlet pipe 8, outer tank 6 ensures the utilization again of part of waste heat;
It is to be fixedly connected between pedestal 2 and condensation main body 1 and bracket 3, is fixedly connected between air blower 4 and bracket 3, air blower
4 input port and the output port of condensation main body 1 are electrically connected, and the quantity of ventilation shaft 5 is two groups, and ventilation shaft 5 runs through
In air blower 4 and the inside of condensation main body 1, it is ensured that air blower 4 can make the sky for condensing the close end portion inside main body 1
Flow of air is accelerated.
It should be noted that the utility model is that a kind of waste heat recycles VOC condensate recovery system, when in use, use
Water is added in inner tank 10 person from water inlet pipe 9, and water is entered in outer tank 6 by connection water pipe 7 again, using by VOC gas
Body is discharged into from pipe 11 from gas to be injected, when VOC gas, which are discharged into pipe 11 from gas, to be entered from bridge piece 12, heat and internal water
Water in case 10 swaps, and when VOC gas continue to run at heat exchanger tube 13, heat exchanger tube 13 condenses VOC, heat exchanger tube
Heat in 13 is further transferred in outer tank 6, and the water in outer tank 6 is exchanged with 13 heat of heat exchanger tube, is made full use of
The heat generated in VOC condensation process, the water of heating are finally discharged by outlet pipe 8, are used for other processings, together
When air blower 4 operating, by two groups of ventilation shafts 5 make condense main body 1 inside close lower end position air flow faster,
So that VOC gas are accelerated to improve the condensing recovery efficiency of VOC, the liquid condensed in the internal flow of condensation main body 1
It is entered in collecting chamber 15 by condensate outlet 14, end user can collect liquid from drain pipe 16, more practical.
The basic principles and main features of the present invention and the advantages of the present invention have been shown and described above.Current row
The technical staff of industry is described in above embodiments and description it should be appreciated that the present utility model is not limited to the above embodiments
Only illustrate the principles of the present invention, on the premise of not departing from the spirit and scope of the utility model, the utility model is also
It will have various changes and improvements, these various changes and improvements fall within the scope of the claimed invention.The utility model
Claimed range is defined by the appending claims and its equivalent thereof.
Claims (6)
1. a kind of waste heat recycles VOC condensate recovery system, including condensation main body (1), it is characterised in that: the condensation main body
(1) lower end outer surface is provided with pedestal (2), and the upper end outer surface of the pedestal (2) is provided with bracket (3), the bracket (3)
Upper end outer surface be provided with air blower (4), the air blower (4) and condensation main body (1) between be provided with ventilation shaft (5),
One side external surface of condensation main body (1) is provided with outer tank (6), between the outer tank (6) and condensation main body (1)
It is provided with connection water pipe (7), the lower end outer surface of the outer tank (6) is provided with outlet pipe (8), the condensation main body (1)
Another side external surface be provided with water inlet pipe (9) relative to the side of outer tank (6), it is described condensation main body (1) inside lean on
The position of nearly connection water pipe (7) is provided with inner tank (10), and the upper end of condensation main body (1) is provided with gas and is discharged into pipe
(11), the lower end that the gas is discharged into pipe (11) is provided with bridge piece (12), and the inside of condensation main body (1) is far from heat exchange
Condensate outlet (14) are provided with below pipe (13).
2. a kind of waste heat according to claim 1 recycles VOC condensate recovery system, it is characterised in that: the condensate liquid
The lower end of outlet (14) is provided with collecting chamber (15), and the collecting chamber (15) is located at the inside of condensation main body (1), the condensate liquid
(14) are exported through the upper end outer surface of collecting chamber (15), the leading exterior surface of condensation main body (1) is provided with drain pipe
(16), a side external surface of the drain pipe (16) through condensation main body (1) and collecting chamber (15).
3. a kind of waste heat according to claim 1 recycles VOC condensate recovery system, it is characterised in that: the condensation master
The inside of body (1) is provided with heat exchanger tube (13) below inner tank (10), one end of the heat exchanger tube (13) through
The outer surface of the inside of main body (1) and a side external surface of outer tank (6) are condensed, the quantity of the heat exchanger tube (13) is several
Group, the heat exchanger tube (13) are arranged in array.
4. a kind of waste heat according to claim 1 recycles VOC condensate recovery system, it is characterised in that: the water inlet pipe
(9) it is led through condensation main body (1) and a side external surface of inner tank (10), the water inlet pipe (9) and condensation one end
To be fixedly connected between body (1), inside of the bridge piece (12) through inner tank (10), the connection water pipe (7)
One end through inner tank (10) a side external surface, the inner tank (10) and condensation main body (1) between be fixed
Connection, the gas are discharged between pipe (11) and bridge piece (12) to be fixedly connected.
5. a kind of waste heat according to claim 1 recycles VOC condensate recovery system, it is characterised in that: the external water
To be fixedly connected between case (6) and condensation main body (1), upper end appearance of connection water pipe (7) through outer tank (6)
Face, the outlet pipe (8) through the lower end outer surface of outer tank (6), the outer tank (6) with connect water pipe (7) with
It and between outlet pipe (8) is to be fixedly connected.
6. a kind of waste heat according to claim 1 recycles VOC condensate recovery system, it is characterised in that: the pedestal (2)
It is to be fixedly connected between condensation main body (1) and bracket (3), is fixed company between the air blower (4) and bracket (3)
It connects, the input port of the air blower (4) and the output port of condensation main body (1) are electrically connected, the number of the ventilation shaft (5)
Amount be two groups, the ventilation shaft (5) through air blower (4) and condense main body (1) inside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201821779190.1U CN209138027U (en) | 2018-10-30 | 2018-10-30 | A kind of waste heat recycling VOC condensate recovery system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201821779190.1U CN209138027U (en) | 2018-10-30 | 2018-10-30 | A kind of waste heat recycling VOC condensate recovery system |
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Publication Number | Publication Date |
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CN209138027U true CN209138027U (en) | 2019-07-23 |
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CN201821779190.1U Expired - Fee Related CN209138027U (en) | 2018-10-30 | 2018-10-30 | A kind of waste heat recycling VOC condensate recovery system |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113352447A (en) * | 2021-06-22 | 2021-09-07 | 宁国华滋筑友建材科技有限公司 | Still kettle waste heat recovery device and method for producing autoclaved aerated concrete slab AAC-S |
-
2018
- 2018-10-30 CN CN201821779190.1U patent/CN209138027U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113352447A (en) * | 2021-06-22 | 2021-09-07 | 宁国华滋筑友建材科技有限公司 | Still kettle waste heat recovery device and method for producing autoclaved aerated concrete slab AAC-S |
CN113352447B (en) * | 2021-06-22 | 2022-08-19 | 宁国华滋筑友建材科技有限公司 | Still kettle waste heat recovery device and method for producing autoclaved aerated concrete slab AAC-S |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190723 Termination date: 20191030 |
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CF01 | Termination of patent right due to non-payment of annual fee |