CN207439189U - A kind of exhaust steam afterheat recycling device for aerated brick field - Google Patents
A kind of exhaust steam afterheat recycling device for aerated brick field Download PDFInfo
- Publication number
- CN207439189U CN207439189U CN201721610895.6U CN201721610895U CN207439189U CN 207439189 U CN207439189 U CN 207439189U CN 201721610895 U CN201721610895 U CN 201721610895U CN 207439189 U CN207439189 U CN 207439189U
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- Prior art keywords
- separator
- heat exchanger
- still kettle
- pipeline
- water inlet
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Abstract
The utility model discloses a kind of exhaust steam afterheat recycling device for aerated brick field, including still kettle and gas-liquid separator, the left end of the still kettle is equipped with material import and export, and steam generator is connected with by jet chimney at the top of the still kettle, and the separator wastewater outlet is connected with wastewater disposal basin by pipeline, separator waste vapour is equipped on the right side of the gas-liquid separator to export, the separator waste vapour outlet is connected by the water inlet of pipeline and the condenser pipe positioned at heat exchanger inside left, the heat exchanger right hand top is equipped with cold water inlet water tank, and the cold water inlet water tank is connected by cold water inlet and the water inlet of the heating tube positioned at heat exchanger inner right side, the water outlet of the heating tube is connected with hot-tub by utilidor.The hot waste gas heat energy recycle that the waste vapour waste-heat recovery device can discharge still kettle, simple and practicable for heating cold water, environmental protection and energy saving.
Description
Technical field
The utility model belongs to field of mechanical technique, and in particular to a kind of exhaust steam afterheat recycling device for aerated brick field.
Background technology
A large amount of remaining steam are generated in aerated bricks production process, in the still kettle of aerating brick field, existing way is
High-temperature steam directly puts idle discharge, not only waste of energy but also thermal pollution has been caused to environment, when summer temperature is higher, thermal pollution
Phenomenon is especially serious.Substantial amounts of high-temperature flue gas is given off when burning, substantial amounts of heat is not only allowed to be wasted in vain, it is also right
The environment depended on for existence causes the destruction of getting worse.The problems such as in face of environmental pollution, resource and energy shortage, it is necessary to seek
New energy development and the measure of energy-saving and emission-reduction are possible to improve efficiency of energy utilization, break through the bottleneck of economic growth, steam pressure
The exhaust steam that kettle pressure leak process excludes it is higher with certain pressure and temperature, it is necessary to condense cooling after can just be discharged into environment
In, this part exhaust steam has larger thermal energy and utility value, and traditional method is that the exhaust steam of this still kettle discharge is all
It directly discharges, causes the waste of this portion of energy;Also this useful part waste vapour heats cold water, but its profit by water pipe exchange
Low with rate, heat exchange efficiency is not also high, the method and apparatus of the hot waste vapour of above-mentioned processing still kettle discharge all there are many defects and
The recycling of problem, both unfavorable thermal energy is also unfavorable for the environmental protection of surrounding.
Utility model content
The purpose of this utility model is to provide a kind of exhaust steam afterheat recycling device for aerated brick field, to solve above-mentioned background
The problem of being proposed in technology.
To achieve the above object, the utility model provides following technical solution:A kind of waste vapour waste heat recovery of aerating brick field
Device, including still kettle and gas-liquid separator, the gas-liquid separator is located at the right side of still kettle, and the left end of the still kettle is set
There is material import and export, and steam generator is connected with by jet chimney at the top of the still kettle, the right end of the still kettle is set
There is waste vapour sewage draining exit, the waste vapour sewage draining exit is connected by pipeline and separator inlet, and the bottom of the gas-liquid separator is set
There is separator wastewater outlet, and the separator wastewater outlet is connected with wastewater disposal basin, the gas-liquid separator right side by pipeline
Exported equipped with separator waste vapour, separator waste vapour outlet by pipeline and the condenser pipe positioned at heat exchanger inside left into
The mouth of a river is connected, and the water outlet of the condenser pipe is connected by pipeline and wastewater disposal basin, and the heat exchanger right hand top is equipped with
Cold water inlet water tank, and the cold water inlet water tank passes through cold water inlet and the water inlet of the heating tube positioned at heat exchanger inner right side
It is connected, the water outlet of the heating tube is connected with hot-tub by utilidor.
Preferably, the bottom of the still kettle is equipped with support base.
Preferably, the heat exchanger is detachable plate type heat exchanger.
Preferably, on the pipeline that separator waste vapour outlet is connected with heat exchanger, separator wastewater outlet and wastewater disposal basin
Solenoid valve is equipped on the pipeline of connection and on heat exchanger and the pipeline that is connected with wastewater disposal basin.
Preferably, the U-tube that the condenser pipe is connected for vertical arrangement, and horizontally arranged be equipped with dissipates on the condenser pipe
Hot fin.
Preferably, the ring pipe that the heating tube is connected for vertical arrangement.
The technique effect and advantage of the utility model:The exhaust steam afterheat recycling device for aerated brick field, only still kettle
Increase heat exchanger on gas exhaust piping, construction is easy, has recycled the thermal energy of hot waste vapour after still kettle cleaning systems, waste heat can heat life
Water or boiler replenishing water are applied flexibly, fuel cost is saved, reduces plant produced cost, increase economic efficiency, reduce environmental pollution,
Heat exchanger is connected with cold water pipe, and the cold water come from cold water pipe becomes hot water after heat exchanger exchanges heat, and hot water is flowed to from heat exchanger
Pond, then the place needed with hot water is transported to, the utility model structure novel, practicality, heat exchange efficiency height, environmental protection and energy saving.
Description of the drawings
Fig. 1 is the structure diagram of the utility model;
Fig. 2 is the structure diagram of the utility model heat exchanger;
Fig. 3 is the process flow chart of the utility model.
In figure:1 still kettle, 2 material import and exports, 3 steam generators, 4 waste vapour sewage draining exits, 5 separator inlets, 6 gas-liquids point
From device, 7 separator wastewater outlets, 8 wastewater disposal basins, the outlet of 9 separator waste vapour, 10 heat exchangers, 11 condenser pipes, 12 cold water inlet water tanks,
13 heating tubes, 14 hot-tubs, 15 radiating fins.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained shall fall within the protection scope of the present invention.
The utility model provides a kind of exhaust steam afterheat recycling device for aerated brick field as shown in Figs. 1-3, including steam pressure
Kettle 1 and gas-liquid separator 6, the gas-liquid separator 6 are located at the right side of still kettle 1, the left end of the still kettle 1 be equipped with material into
Outlet 2, and 1 top of the still kettle is connected with steam generator 3 by jet chimney, the right end of the still kettle 1, which is equipped with, to give up
Vapour sewage draining exit 4, the waste vapour sewage draining exit 4 are connected by pipeline and separator inlet 5, and the bottom of the gas-liquid separator 6 is set
There is separator wastewater outlet 7, and the separator wastewater outlet 7 is connected with wastewater disposal basin 8, the gas-liquid separator 6 by pipeline
Right side is equipped with separator waste vapour and exports 9, and the separator waste vapour outlet 9 is by pipeline with being located at the cold of 10 inside left of heat exchanger
The water inlet of solidifying pipe 11 is connected, and the water outlet of the condenser pipe 11 is connected by pipeline and wastewater disposal basin 8, the heat exchanger
10 right hand tops are equipped with cold water inlet water tank 12, and the cold water inlet water tank 12 is by cold water inlet and inside heat exchanger 10
The water inlet of the heating tube 13 on right side is connected, and the water outlet of the heating tube 13 is connected with hot-tub 14 by utilidor.
Specifically, the bottom of the still kettle 1 is equipped with support base.
Specifically, the heat exchanger 10 is detachable plate type heat exchanger, the heat exchange efficiency of plate heat exchanger is high and small, can
Directly it is connected with pipeline, saves cost, detachable plate type heat exchanger, disassembly, cleaning are simply easy.
Specifically, the separator waste vapour is exported on 9 pipelines being connected with heat exchanger 10, separator wastewater outlet 7 is with giving up
Solenoid valve is equipped on the pipeline that pond 8 connects and on pipeline that heat exchanger 10 and wastewater disposal basin 8 are connected.
Specifically, the condenser pipe 11 is the U-tube that is connected of vertical arrangement, and horizontally arranged on the condenser pipe 11 set
There is radiating fin 15, condense good heat dissipation effect.
Specifically, the ring pipe that the heating tube 13 is connected for vertical arrangement.
Operation principle, the exhaust steam afterheat recycling device for aerated brick field, in use, the steam of still kettle 1 is by gas-liquid point
After device 6, waste water flows into wastewater disposal basin 8 from separator wastewater outlet 7, and waste vapour is by separator waste vapour outlet 9 and heat exchanger 10
Internal condenser pipe 11 likewise enters wastewater disposal basin 8 after being condensed into water, and the cold water that heat exchanger 10 flows into is by inside heat exchanger 10
Heating tube 13 be heated to be after hot water into hot-tub 14, only increase heat exchanger 10, construction on the gas exhaust piping of still kettle 1
Easily, the thermal energy of hot waste vapour after still kettle 1 cleans has been recycled, waste heat can heat domestic water or boiler replenishing water, save combustion
Material expense reduces plant produced cost, increases economic efficiency, reduces environmental pollution.
Finally it should be noted that:The above is only the preferred embodiment of the utility model only, is not limited to this
Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it can still modify to the technical solution recorded in foregoing embodiments or to which part technical characteristic
Equivalent substitution is carried out, within the spirit and principle of the utility model, any modifications, equivalent replacements and improvements are made,
It should be included within the scope of protection of this utility model.
Claims (6)
1. a kind of exhaust steam afterheat recycling device for aerated brick field, including still kettle(1)And gas-liquid separator(6), it is characterised in that:
The gas-liquid separator(6)Positioned at still kettle(1)Right side, the still kettle(1)Left end be equipped with material import and export(2), and
The still kettle(1)Top is connected with steam generator by jet chimney(3), the still kettle(1)Right end be equipped with waste vapour
Sewage draining exit(4), the waste vapour sewage draining exit(4)Pass through pipeline and separator inlet(5)It is connected, the gas-liquid separator(6)'s
Bottom is equipped with separator wastewater outlet(7), and the separator wastewater outlet(7)Wastewater disposal basin is connected with by pipeline(8), it is described
Gas-liquid separator(6)Right side is exported equipped with separator waste vapour(9), the separator waste vapour outlet(9)It is changed by pipeline with being located at
Hot device(10)The condenser pipe of inside left(11)Water inlet be connected, and the condenser pipe(11)Water outlet by pipeline with
Wastewater disposal basin(8)It is connected, the heat exchanger(10)Right hand top is equipped with cold water inlet water tank(12), and the cold water inlet water tank(12)
By cold water inlet with being located at heat exchanger(10)The heating tube of inner right side(13)Water inlet be connected, the heating tube
(13)Water outlet hot-tub is connected with by utilidor(14).
2. a kind of exhaust steam afterheat recycling device for aerated brick field according to claim 1, it is characterised in that:The still kettle
(1)Bottom be equipped with support base.
3. a kind of exhaust steam afterheat recycling device for aerated brick field according to claim 1, it is characterised in that:The heat exchanger
(10)For detachable plate type heat exchanger.
4. a kind of exhaust steam afterheat recycling device for aerated brick field according to claim 1, it is characterised in that:The separator
Waste vapour exports(9)With heat exchanger(10)On the pipeline of connection, separator wastewater outlet(7)With wastewater disposal basin(8)On the pipeline of connection
And heat exchanger(10)With wastewater disposal basin(8)Solenoid valve is equipped on the pipeline being connected.
5. a kind of exhaust steam afterheat recycling device for aerated brick field according to claim 1, it is characterised in that:The condenser pipe
(11)To be arranged vertically the U-tube being connected, and the condenser pipe(11)It is upper horizontally arranged equipped with radiating fin(15).
6. a kind of exhaust steam afterheat recycling device for aerated brick field according to claim 1, it is characterised in that:The heating tube
(13)To be arranged vertically the ring pipe being connected.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201721610895.6U CN207439189U (en) | 2017-11-28 | 2017-11-28 | A kind of exhaust steam afterheat recycling device for aerated brick field |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201721610895.6U CN207439189U (en) | 2017-11-28 | 2017-11-28 | A kind of exhaust steam afterheat recycling device for aerated brick field |
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CN207439189U true CN207439189U (en) | 2018-06-01 |
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CN201721610895.6U Expired - Fee Related CN207439189U (en) | 2017-11-28 | 2017-11-28 | A kind of exhaust steam afterheat recycling device for aerated brick field |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110411233A (en) * | 2019-07-11 | 2019-11-05 | 曲靖翔腾建材有限公司 | A kind of method and system using steam-cured waste vapour multistage steam water separated heating waste pulp |
CN111765779A (en) * | 2020-05-29 | 2020-10-13 | 胡贤友 | Method and equipment for utilizing waste heat of steam condensate water |
CN111963882A (en) * | 2020-07-08 | 2020-11-20 | 福建省气柜设备安装有限公司 | Waste heat recovery device of steam trap |
CN112157789A (en) * | 2020-08-29 | 2021-01-01 | 上海阜阜建材有限公司 | Device and method for cascade utilization of residual pressure and residual heat of autoclaved aerated concrete block |
CN112994486A (en) * | 2021-02-06 | 2021-06-18 | 河南万贯实业有限公司 | Stable double-rectifier transformer device for graphitized electric furnace |
-
2017
- 2017-11-28 CN CN201721610895.6U patent/CN207439189U/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110411233A (en) * | 2019-07-11 | 2019-11-05 | 曲靖翔腾建材有限公司 | A kind of method and system using steam-cured waste vapour multistage steam water separated heating waste pulp |
CN111765779A (en) * | 2020-05-29 | 2020-10-13 | 胡贤友 | Method and equipment for utilizing waste heat of steam condensate water |
CN111765779B (en) * | 2020-05-29 | 2021-07-27 | 九江九宏新材料有限公司 | Method and equipment for utilizing waste heat of steam condensate water |
CN111963882A (en) * | 2020-07-08 | 2020-11-20 | 福建省气柜设备安装有限公司 | Waste heat recovery device of steam trap |
CN111963882B (en) * | 2020-07-08 | 2022-08-16 | 中琉科技有限公司 | Waste heat recovery device of steam trap |
CN112157789A (en) * | 2020-08-29 | 2021-01-01 | 上海阜阜建材有限公司 | Device and method for cascade utilization of residual pressure and residual heat of autoclaved aerated concrete block |
CN112157789B (en) * | 2020-08-29 | 2021-09-03 | 上海阜阜建材有限公司 | Device and method for cascade utilization of residual pressure and residual heat of autoclaved aerated concrete block |
CN112994486A (en) * | 2021-02-06 | 2021-06-18 | 河南万贯实业有限公司 | Stable double-rectifier transformer device for graphitized electric furnace |
CN112994486B (en) * | 2021-02-06 | 2022-06-24 | 河南万贯实业有限公司 | Stable double-rectifier transformer device for graphitized electric furnace |
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GR01 | Patent grant | ||
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CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180601 Termination date: 20201128 |
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CF01 | Termination of patent right due to non-payment of annual fee |