CN203657560U - High-temperature flue gas recovery device - Google Patents

High-temperature flue gas recovery device Download PDF

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Publication number
CN203657560U
CN203657560U CN201320610180.6U CN201320610180U CN203657560U CN 203657560 U CN203657560 U CN 203657560U CN 201320610180 U CN201320610180 U CN 201320610180U CN 203657560 U CN203657560 U CN 203657560U
Authority
CN
China
Prior art keywords
flue gas
heat exchanger
water tank
exchanger tube
communicated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201320610180.6U
Other languages
Chinese (zh)
Inventor
李宗华
李鲁信
邢艳磊
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
LAMBER NUMEN BOILER CO Ltd
Original Assignee
LAMBER NUMEN BOILER CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by LAMBER NUMEN BOILER CO Ltd filed Critical LAMBER NUMEN BOILER CO Ltd
Priority to CN201320610180.6U priority Critical patent/CN203657560U/en
Application granted granted Critical
Publication of CN203657560U publication Critical patent/CN203657560U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model relates to a high-temperature flue gas recovery device. The recovery device comprises a flue gas inlet, at least two heat exchange tubes, a flue gas pipeline exchange chamber, a flue gas outlet, a water tank, a water inlet and a water outlet, wherein the flue gas inlet and the flue gas outlet are arranged at upper parts of the heat exchange tubes, upper ends of part of the heat exchange tubes are communicated with the flue gas inlet, upper ends of the rest heat exchange tubes are communicated with the flue gas outlet, lower ends of the heat exchange tubes are communicated with the flue gas pipeline exchange chamber, the water inlet and the water outlet are arranged on the water tank and used for water feeding and water discharge of the water tank, and the heat exchange tubes are arranged in the water tank. The recovery device has the benefits as follows: high-temperature flue gases are treated and degraded, meanwhile, the high-temperature flue gases are recovered and utilized, and the heat energy in the flue gases is converted into the heat energy of water in the water tank.

Description

A kind of high-temperature flue gas recover
Technical field
The utility model relates to a kind of high-temperature flue gas recover.
Background technology
In a lot of industrial production, can produce high-temperature flue gas, and be also a very large difficult problem to the processing of high-temperature flue gas in prior art.The flue gas processing device in past is generally all more complicated, and the effect of degraded flue gas is also undesirable, does not also realize the recycling to high-temperature flue gas simultaneously.
Utility model content
The utility model is exactly in order to address the above problem, and overcomes high-temperature flue gas in prior art and processes existing problem, and the utility model provides a kind of high-temperature flue gas recover to satisfy the demands.
To achieve these goals, the technical solution of the utility model is as follows:
A kind of high-temperature flue gas recover, it is characterized in that, comprise into mouth, heat exchanger tube, flue switch room and outlet flue, described enter mouth and outlet flue be arranged at the top of heat exchanger tube, described heat exchanger tube comprises more than at least two, wherein the upper end of a part of heat exchanger tube with enter mouth and be communicated with, the upper end of remaining heat exchanger tube is communicated with outlet flue, the lower end of described heat exchanger tube is communicated with flue switch room, also comprise water tank and be arranged at the water inlet for water tank water intake and water outlet and the delivery port on water tank, described heat exchanger tube is arranged in water tank.
Above-mentioned a kind of high-temperature flue gas recover, is characterized in that, described water inlet is arranged at the below of water tank, and delivery port is arranged at the top of water tank.
Above-mentioned a kind of high-temperature flue gas recover, it is characterized in that, the top of described heat exchanger tube is provided with flue gas turnover case, in flue gas turnover case, be provided with and flue gas is passed in and out to space in case be divided into into smoke box and go out the baffle plate of smoke box, described enter mouth be communicated with into smoke box, wherein the upper end of a part of heat exchanger tube with enter smoke box and be communicated with, described outlet flue is communicated with smoke box, the upper end of remaining heat exchanger tube with go out smoke box and be communicated with.
Above-mentioned a kind of high-temperature flue gas recover, is characterized in that, described in enter the cleaning door being provided with in smoke box and flue switch room for clearing up the dust impurity under residual after flue gas circulation.
Above-mentioned a kind of high-temperature flue gas recover, is characterized in that, the lower end of described water tank is also provided with the sewage draining exit for clearing up water tank dirt and impurity.
Above-mentioned a kind of high-temperature flue gas recover, is characterized in that, the bottom of described flue switch room is also provided with the locator for fixing whole device.
The beneficial effects of the utility model are: not only high-temperature flue gas has been carried out processing degraded, also high-temperature flue gas has been recycled the heat energy that is Water in Water Tanks by the thermal power transfer in flue gas simultaneously.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
The specific embodiment
For technological means, creation characteristic that the utility model is realized, reach object and effect is easy to understand, below in conjunction with concrete diagram, further set forth the utility model.
Referring to Fig. 1, a kind of high-temperature flue gas recover, comprise into mouth 110, heat exchanger tube 120, flue switch room 130 and outlet flue 140, enter the top that mouth 110 and outlet flue 140 are arranged at heat exchanger tube 120, heat exchanger tube 120 comprises more than at least two, wherein the upper end of a part of heat exchanger tube 120 with enter mouth 110 and be communicated with, the upper end of remaining heat exchanger tube 120 is communicated with outlet flue 140, the lower end of heat exchanger tube 120 is communicated with flue switch room 130, also comprise water tank 200 and be arranged at water inlet 210 and the delivery port 220 for water tank 200 water inlets and water outlet on water tank 200, heat exchanger tube 120 is arranged in water tank 200.
In work time,, high-temperature flue gas enters from entering mouth 110, then by arriving the flue switch room 130 of bottom with entering the heat exchanger tube 120 that mouth 110 is communicated with, more finally discharges from outlet flue 140 through the heat exchanger tube 120 that opposite side is communicated with outlet flue 140.When high-temperature flue gas circulates in heat exchanger tube 120, the water inlet 210 that current enter water tank 200 by the pressurization of high-pressure hydraulic pump enters into water tank 200, then the heat exchanger tube 120 in water tank 200 by the thermal energy transfer of high-temperature flue gas in the current in water tank 200, thereby completed the heating to current, the current after heating flow out from delivery port.
Water inlet 210 is arranged at the below of water tank 200, and delivery port 220 is arranged at the top of water tank 200.Such design makes the in the situation that of water filling, and water is slowly to rise to tank top from the bottom of water tank 200, and the water in the process of rising in water tank 200 just can carry out thermal energy exchange with heat exchanger tube 120.If delivery port 220 is arranged on to water tank 200 belows, water inlet 210 is arranged at the top of water tank 200, and so very possible current, from water inlet 210 enters, directly just flow out, and do not carry out thermal energy exchange with heat exchanger tube 120 from the delivery port 220 of bottom.
The top of heat exchanger tube 120 is provided with flue gas turnover case 300, in flue gas turnover case 300, be provided with and flue gas is passed in and out to the interior space of case 300 be divided into into smoke box 310 and go out the baffle plate 340 of smoke box 310, entering mouth 110 is communicated with into smoke box 310, wherein the upper end of a part of heat exchanger tube 120 with enter smoke box 310 and be communicated with, outlet flue 140 is communicated with smoke box 320, the upper end of remaining heat exchanger tube 120 with go out smoke box 320 and be communicated with.
Enter the cleaning door 330 being provided with in smoke box 310 and flue switch room 130 for clearing up the dust impurity under residual after flue gas circulation.
The lower end of water tank 200 is also provided with the sewage draining exit 230 for clearing up water tank dirt and impurity.
The bottom of flue switch room 130 is also provided with the locator 400 for fixing whole device.
The beneficial effects of the utility model are: not only high-temperature flue gas has been carried out processing degraded, also high-temperature flue gas has been recycled the heat energy that is Water in Water Tanks by the thermal power transfer in flue gas simultaneously.
More than show and described basic principle of the present utility model, principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; that in above-described embodiment and description, describes just illustrates principle of the present utility model; under the prerequisite that does not depart from the utility model spirit and scope, the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.

Claims (6)

1. a high-temperature flue gas recover, it is characterized in that, comprise into mouth, heat exchanger tube, flue switch room and outlet flue, described enter mouth and outlet flue be arranged at the top of heat exchanger tube, described heat exchanger tube comprises more than at least two, wherein the upper end of a part of heat exchanger tube with enter mouth and be communicated with, the upper end of remaining heat exchanger tube is communicated with outlet flue, the lower end of described heat exchanger tube is communicated with flue switch room, also comprise water tank and be arranged at the water inlet for water tank water intake and water outlet and the delivery port on water tank, described heat exchanger tube is arranged in water tank.
2. a kind of high-temperature flue gas recover according to claim 1, is characterized in that, described water inlet is arranged at the below of water tank, and delivery port is arranged at the top of water tank.
3. according to a kind of high-temperature flue gas recover described in claim 1 or 2, it is characterized in that, the top of described heat exchanger tube is provided with flue gas turnover case, in flue gas turnover case, be provided with and flue gas is passed in and out to space in case be divided into into smoke box and go out the baffle plate of smoke box, described enter mouth be communicated with into smoke box, wherein the upper end of a part of heat exchanger tube with enter smoke box and be communicated with, described outlet flue is communicated with smoke box, the upper end of remaining heat exchanger tube with go out smoke box and be communicated with.
4. a kind of high-temperature flue gas recover according to claim 3, is characterized in that, described in enter the cleaning door being provided with in smoke box and flue switch room for clearing up the dust impurity under residual after flue gas circulation.
5. a kind of high-temperature flue gas recover according to claim 4, is characterized in that, the lower end of described water tank is also provided with the sewage draining exit for clearing up water tank dirt and impurity.
6. according to a kind of high-temperature flue gas recover described in claim 4 or 5, it is characterized in that, the bottom of described flue switch room is also provided with the locator for fixing whole device.
CN201320610180.6U 2013-09-30 2013-09-30 High-temperature flue gas recovery device Expired - Fee Related CN203657560U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320610180.6U CN203657560U (en) 2013-09-30 2013-09-30 High-temperature flue gas recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320610180.6U CN203657560U (en) 2013-09-30 2013-09-30 High-temperature flue gas recovery device

Publications (1)

Publication Number Publication Date
CN203657560U true CN203657560U (en) 2014-06-18

Family

ID=50923939

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320610180.6U Expired - Fee Related CN203657560U (en) 2013-09-30 2013-09-30 High-temperature flue gas recovery device

Country Status (1)

Country Link
CN (1) CN203657560U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106613540A (en) * 2017-03-14 2017-05-10 新疆农业科学院农业机械化研究所 Greenhouse dehumidifying warm water irrigation air heating furnace system
CN111256501A (en) * 2020-02-08 2020-06-09 刘贤方 Integrated non-sealing tank body for industrial wastewater waste heat recovery

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106613540A (en) * 2017-03-14 2017-05-10 新疆农业科学院农业机械化研究所 Greenhouse dehumidifying warm water irrigation air heating furnace system
CN111256501A (en) * 2020-02-08 2020-06-09 刘贤方 Integrated non-sealing tank body for industrial wastewater waste heat recovery

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140618

Termination date: 20150930

EXPY Termination of patent right or utility model