CN108955105A - A kind of waste heat recovering energy conserving baking oven and exhaust heat recovering method - Google Patents
A kind of waste heat recovering energy conserving baking oven and exhaust heat recovering method Download PDFInfo
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- CN108955105A CN108955105A CN201710348066.3A CN201710348066A CN108955105A CN 108955105 A CN108955105 A CN 108955105A CN 201710348066 A CN201710348066 A CN 201710348066A CN 108955105 A CN108955105 A CN 108955105A
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- China
- Prior art keywords
- dehumidifier
- baking oven
- waste heat
- reuse
- pipeline
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B9/00—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
- F26B9/06—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/08—Humidity
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/10—Temperature; Pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/001—Heating arrangements using waste heat
- F26B23/002—Heating arrangements using waste heat recovered from dryer exhaust gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Abstract
This application involves a kind of waste heat recovering energy conserving baking oven and its exhaust heat recovering methods, waste heat recovering energy conserving baking oven includes furnace body, hot blast feeding pipeline, dehumidifier blower, reuse pipeline, dehumidifier air piping, Temperature and Humidity device, automatically adjust valve, baking oven waste heat recycling system and server, it is characterized in that furnace body, which is equipped with, fills into air scoop, Temperature and Humidity device, hot blast feeding pipeline is connected to furnace body, there are several interconnected drying cavities in furnace body, each drying cavity top is equipped with dehumidifier air piping or reuse pipeline, dehumidifier blower has reuse mouth and exhaust outlet, reuse pipeline, dehumidifier air piping is connected to the reuse mouth and exhaust outlet of dehumidifier blower respectively, baking oven waste heat recycling system is mounted in dehumidifier air piping and reuse pipeline, automatic adjustment valve is mounted on the exhaust outlet of dehumidifier blower, it fills into air scoop and reuse pipeline connects Logical, server is all connected with Temperature and Humidity device, automatic adjustment valve, hot blast feeding system.The features such as compared with prior art, it is simple for structure reasonable to have, and easy to use, energy utilization rate is high by the application, at low cost.
Description
Technical field
This application involves baking oven and technical field of waste heat utilization, concretely, be related to a kind of waste heat recovering energy conserving baking oven and
Its exhaust heat recovering method.
Background technique
Glass fibre is a kind of inorganic non-metallic material haveing excellent performance, and is the warp using glass marble or post-consumer glass as raw material
The techniques such as high temperature melting, wire drawing, baking, doff are crossed to be made.Glass fibre has good insulating, heat resistance high, anticorrosive
The advantages that, it is widely used in every field.
It will use some infiltration agent emulsions during making glass fibre, in order to enable size film-forming, together
When removal draw after glass fibre in excessive moisture, need to dry the glass fibre after drawing.Existing use
What it is in drying glass fibre is single layer tunnel-type drying furnace, and the furnace body of drying oven is built-in with a drying cavity, the drying cavity
Bottom is equipped with charka track, and the charka for being loaded with glass fibre enters drying cavity from furnace body side.One on the top plate of the furnace body
As offer hot-wind inlet, the hot wind that hot blast feeding system provides is input on the drying cavity top plate by the hot-wind inlet
Hot blast feeding pipeline in, hot wind enters in cavity by the hot blast feeding pipeline on the top plate.Since hot wind enters baking
Before dry cavity, mixed in the hot blast feeding pipeline at the top of drying cavity with cold air, therefore it is logical to have a large amount of heat
The top plate for crossing furnace body is dispersed into outside air, influences the heat utilization efficiency of drying oven, and drying effect is poor.Simultaneously as existing
The cavity space of some tunnel-type drying furnaces is narrow, and hot-air cannot flow well in the cavity of drying oven after being passed through hot gas
It is dynamic, it needs to consume more heat and time just and can complete the drying to glass fibre, also further affect heat utilization
Rate and drying efficiency are unfavorable for the actual development of industrialized production.
Summary of the invention
The application's aims to overcome that the above deficiencies in the existing technologies, and provide it is a kind of reasonable in design,
Convenient and practical waste heat recovering energy conserving baking oven and exhaust heat recovering method, so that lost thermal energy passes through other in drying course
Channel can be recycled preferably, under the premise of reducing energy consumption, improve the efficiency of drying.
It includes: a kind of waste heat recovering energy conserving baking oven that the present patent application, which solves technical solution used by above-mentioned technical problem,
Including furnace body, hot blast feeding pipeline, dehumidifier blower, reuse pipeline, dehumidifier air piping, Temperature and Humidity device, automatic adjustment valve,
Baking oven waste heat recycling system and server, furnace body are equipped with and fill into air scoop, Temperature and Humidity device, hot blast feeding system
It is connected to by hot blast feeding pipeline with furnace body, interior in furnace body to have several interconnected drying cavities, each drying cavity top is equipped with
Dehumidifier air piping or reuse pipeline, dehumidifier blower have reuse mouth and exhaust outlet, reuse pipeline, dehumidifier air piping respectively with dehumidifier
The reuse mouth of blower is connected to exhaust outlet, and the hot wind of reuse is sent into waste heat recovering energy conserving baking oven by reuse mouth by dehumidifier blower
In, dehumidifier blower will be discharged waste heat recovering energy conserving by baking oven waste heat recycling system treated wind by exhaust outlet and dry
Case, baking oven waste heat recycling system are mounted in dehumidifier air piping and reuse pipeline, and automatic adjustment valve is mounted on dehumidifier wind
The exhaust outlet of machine fills into air scoop and is connected to reuse pipeline, and server and Temperature and Humidity device, automatic adjustment valve, hot wind supply
System is answered to be all connected with.
The Temperature and Humidity device is mounted in dehumidifier air piping, reuse pipeline and drying cavity, is controlled and is adjusted by server
Save the supply and automatic adjustment valve aperture of heat recovery energy-saving oven.
The baking oven waste heat recycling system uses heat exchanger.
Preferably, the Temperature and Humidity device is mounted on each drying cavity, in dehumidifier air piping, and drying cavity temperature range exists
Be arranged ± 5 DEG C of technological standards, automatic adjustment valve aperture automatic adjustment, drying cavity humidity range setting technological standards ±
10%, fill into the channel regulating valve automatic adjustment of air scoop.
Preferably, the first two drying cavity is connected in the last one drying cavity of waste heat recovering energy conserving baking oven by reuse pipeline
Reuse is carried out, initial temperature is promoted.
The dehumidifier air piping is connected to by dehumidifier air piping linkage section with drying cavity, is constituted the connection of " 7 " font channel, is taken out
One conversion valve is set on wet wind tubing connection section, and conversion valve is connected to reuse pipeline, dehumidifier air piping, conversion valve
It is connect with server.
Preferably, 5~7mm of the heat-exchanger fin spacing, dehumidifier wind is by flowing 7~12m/s of wind speed, to ensure to change
Thermal effect and efficiency reach the maximum limitation of heat recovery.
The application solves technical solution used by above-mentioned technical problem further include: a kind of waste heat recovering energy conserving baking oven it is remaining
Hot reuse method, it is characterized in that the following steps are included: the hot wind in drying cavity is recycled by baking oven waste heat recycling system, warp
Hot wind after crossing baking oven waste heat recycling system is admitted to reuse pipeline if meeting reuse standard and otherwise passes through dehumidifier wind
Pipeline is discharged, the discharge of the automatic regulating valve gate heating wind configured in dehumidifier air piping.
Preferably, the hot wind after baking oven waste heat recycling system passes through the import of baking oven waste heat recycling system
Temperature and Humidity device is detected, and the temperature signal that Temperature and Humidity device detects is transferred to server, and server believes temperature
Number determined according to process set value, reuse pipeline is admitted to if meeting reuse standard otherwise passes through dehumidifier air piping and arrange
Out.
It can be seen via above technical scheme that compared with prior art, the present invention provides a kind of heat recovery sections
Energy baking oven, the energy-saving baking box have dehumidifier wind-warm syndrome humidity display and valve automatic regulation function.The temperature and humidity can effectively instruct and
Control heat source uses the channel valve mixed in the hot-air channel at the top of aperture and dehumidifier air valve and cavity with cold air
Door aperture, reduces the usage amount of heat source under the premise of temperature and humidity reaches technological standards range.The dehumidifier wind of the baking oven drying cavity
After over-heat-exchanger exchanges heat heat be recycled in drying cavity and be recycled.The hot wind of reuse is sent to last
A drying cavity promotes initial temperature.Heat energy recovery is more thorough, to reduce the consumption of the energy and improve drying efficiency.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of heat recovery of embodiment of the present invention energy-saving baking box;
Fig. 2 is another structural schematic diagram of heat recovery of embodiment of the present invention energy-saving baking box;
Fig. 3 is furnace body front elevation and hot wind flow schematic diagram in heat recovery of embodiment of the present invention energy-saving baking box.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
Fig. 1, Fig. 2 shows the structural schematic diagrams of heat recovery energy-saving baking box embodiment of the present invention, comprising: furnace body
(overall structure), hot blast feeding system 15, hot blast feeding pipeline 11, dehumidifier blower 5 and time being connected with the dehumidifier blower 5
With pipeline 3, dehumidifier air piping 4, Temperature and Humidity device 6, automatic adjustment valve 9, baking oven waste heat recycling system and service
Device 7, the furnace body, which is equipped with, fills into air scoop 14, Temperature and Humidity device 6, and hot blast feeding system 15 passes through hot blast feeding pipeline
11 are connected to the furnace body, and interior in furnace body to have several interconnected drying cavities 1, each 1 top of drying cavity is equipped with dehumidifier wind
Pipeline 4 or reuse pipeline 3, dehumidifier blower 5 have reuse mouth and exhaust outlet, reuse pipeline 3, dehumidifier air piping 4 respectively with dehumidifier
The reuse mouth of blower 5 is connected to exhaust outlet, and the hot wind of reuse is sent into waste heat recovering energy conserving baking oven by reuse mouth by dehumidifier blower 5
In, dehumidifier blower 5 will be discharged waste heat recovering energy conserving by baking oven waste heat recycling system treated wind by exhaust outlet and dry
Case, baking oven waste heat recycling system are mounted in dehumidifier air piping 4 and reuse pipeline 3, and automatic adjustment valve 9 is mounted on dehumidifier
The exhaust outlet of blower 5 fills into air scoop 14 and is connected to reuse pipeline 3, server 7 and Temperature and Humidity device 6, automatic adjustment valve
9, hot blast feeding system 15 connects.
In this heat recovery energy-saving baking box structure, including furnace body number can be one or more, this hair
The bright particular number for furnace body is not specifically limited;When being provided with multiple furnace bodies, multiple furnace bodies are sequentially connected;Fig. 1, Fig. 2
The present embodiment be a furnace body representative side section view, for hot blast feeding system 15 and dehumidifier blower 5 positional relationship not
Stringent limitation can be configured the layout of hot blast feeding pipeline 15 and dehumidifier blower 5 using existing layout type.
Have several drying cavities 1 in furnace body, be loaded with the trolley of provided with wheels in charka 12(Fig. 1 of glass fibre) it can be
Unidirectional operation in drying cavity 1, to complete the drying to glass fibre.Charka 12 is opened from right to left in Fig. 1, before the right side is, Zuo Wei
Afterwards.
Wherein, each drying cavity 1 has individual heating plant to carry out heat supply, while each drying cavity 1 is interconnected.It changes
Yan Zhi is parallelly distribute between drying cavity 1 and interconnects that centre does not separate, and is contacted with each other between charka 12,
To constitute the drying channel for going out charka 12 into charka 12 to other end from one, the drying channel i.e. hot wind are supplied
Answer pipeline 11.
The dehumidifier air piping 4 of the drying cavity 1 in the several areas in energy-saving baking box foremost is interconnected and concentrates on a reuse
In pipeline 3, the slow situation of efficiency is transported in order to avoid hot wind enters at the top of furnace body after reuse pipeline 3, so that the heat in hot wind
In a large amount of conduction to outside air of amount, dehumidifier blower 5 is installed in reuse pipeline 3, accelerates hot wind being sent into the last of baking oven
Reuse is carried out in one drying cavity 1, is circulated because accelerating hot wind using dehumidifier blower 5 in 2 outside surrounding of charka, is promoted
Drying effect, while reuse decreases the loss that thermal energy is directly brought into behind the external world by dehumidifier wind.
In order to which heat is preferably carried out reuse, one is distributed in the top dehumidifier air piping 4 of each drying cavity 1
A heat exchanger 2, heat is also pulled away while moisture is discharged to the external world by dehumidifier air piping 4, will by heat exchanger 2
Heat in moisture exchanges.And baking oven fills into air and needs through heat exchanger 2, just the heat in moisture is handed at this moment
It changes to and fills into air.The heat increased in drying cavity 1 after air uses in drying cavity 1 is filled into, to reach drying effect
It is promoted.
Further, in order to guarantee the stability of the temperature and humidity in furnace body, guarantee baked products quality and energy
The stability of consumption, further increases energy utilization rate, is arranged on 4 linkage section 41 of dehumidifier air piping that each drying cavity 1 comes out
One conversion valve 13, conversion valve 13 are connected to reuse pipeline 3, dehumidifier air piping 4, and conversion valve 13 and server 7 connect
It connects, Temperature and Humidity device 6 is distributed in the dehumidifier air piping 4 of each drying cavity 1 and shows on the server 7, in server 7
Middle setting limits up and down, once temperature and humidity is more than the range of technological standards, middle control signal feedback to heat recovery section
On the automatic adjustment valve 9 of energy baking oven, controlling opening of valve reduces temperature and humidity wave so that internal temperature and humid control are stablized
The rising of energy consumption after dynamic.When the temperature-humidity signal that the Temperature and Humidity device 6 of any dehumidifier air piping 4 detects meets reuse
When standard, 4 linkage section 41 of dehumidifier air piping is directly connected to reuse pipeline 3 by conversion valve 13, and otherwise dehumidifier air piping 4 connects
Section 41 is connected to dehumidifier air piping 4.
Certainly, increase or reduce quantity and the position of Temperature and Humidity device 6 according to the length of furnace body or drying cavity 1
It sets, the technological standards of temperature and humidity can also be required to be formulated and improved according to the control of production product, but be to ensure that
Temperature and humidity in drying cavity 1 is in a certain range.
Specifically, Fig. 1, Fig. 2 shows a kind of structural schematic diagrams of heat recovery energy-saving baking box of the invention.This field
Ordinary artisan is appreciated that can be set two or more furnaces being sequentially connected in heat recovery energy-saving baking box
Body is not specifically limited the particular number of furnace body.There are six the drying cavities being sequentially connected for the present embodiment setting in the figure
1。
Unlike the prior art, dehumidifier air piping 4 is provided with heat exchanger in heat recovery energy-saving baking box of the present invention
2, it can be seen in the drawing that the heat exchanger 2 is set to 4 top exit of dehumidifier air piping, and it is connect with total dehumidifier air piping.This
The hot wind extracted out in the heat recovery energy-saving baking box of invention is back to use in the last one drying cavity 1, can be in Fig. 1
Find out, the hot wind of two drying cavities 1 in foremost is by direct reuse.Temperature and humidity in heat recovery energy-saving baking box of the invention
Control is to be carried out automatically controlling by server 7 and adjusted the aperture of automatic adjustment valve 9, it can be seen in FIG. 1 that by warm and humid
Spend each cavity of 6 test oven of detector temperature and humidity and in being collected into server 7, for data analyze once occur
Parameter is more than that critical field is arranged in technique, i.e., can feed back to the adjusting that automatic adjustment valve 9 carries out aperture, adjust to temperature and humidity
Section, reduces unnecessary thermo-field thoery, to reduce the consumption of the energy.
Concrete operation step, when baking oven is opened, dehumidifier blower 5 can be automatically turned on, and the hot wind of oven interior also can be with Fig. 1
Route shown in ~ 3 is recycled, and fresh air can enter oven interior from air scoop 14 is filled into and be mixed with internal hot wind, is followed
The hot wind of ring can heat the yarn on charka, so that the moisture of yarn starts to evaporate.The moisture being evaporated can be taken out
The exhaust outlet (at automatic adjustment valve 9) of wet blower 5 is extracted out, and the heat of part is mixed in dehumidifier wind.It is carried out by heat exchanger 2
Heat exchange is transferred heat to fresh air and to fill into air themperature rising, reduced baking oven itself and added using steam to fresh air
The origin temp of heat, the consumption of the energy is reduced with this.
Waste heat recovering energy conserving baking oven of the present invention and existing conventional ovens items comparative situation are as shown in the table:
By taking the product L of certain glass fibre production company as an example, energy-saving baking box and conventional ovens carry out baking comparison as follows
Waste heat recovering energy conserving baking oven of the present invention | Conventional ovens | |
Heat energy recovery rate | 52% | 0% |
Dry situation | 383min | 345min |
Energy consumption situation | 352kg/ tons | 310kg/ tons |
Explain: heat energy recovery rate --- refer to the thermal energy taken away out of drying cavity by dehumidifier wind, the thermal energy ratio being back to use in baking oven again
Example;
Baking time --- refer to the time that glass fiber product is dried in an oven;
Glass film formation time --- refer to that the length of time of glass fiber precursor surface filming during baking, film formation time length are said
Bright film forming is more abundant, can shorten baking time, the energy consumption of ton silk is reduced with this;
Energy consumption situation --- refer to the steam consumption that one ton of yarn of drying needs.
Each embodiment in this specification is described in a progressive manner, the highlights of each of the examples are with other
The difference of embodiment, the same or similar parts in each embodiment may refer to each other.
The foregoing description of the disclosed embodiments enables those skilled in the art to implement or use the present invention.
Various modifications to these embodiments will be readily apparent to those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, of the invention
It is not intended to be limited to the embodiments shown herein, and is to fit to and the principles and novel features disclosed herein phase one
The widest scope of cause.
Claims (7)
1. a kind of waste heat recovering energy conserving baking oven, including furnace body, hot blast feeding pipeline, dehumidifier blower, reuse pipeline, dehumidifier air hose
Road, Temperature and Humidity device, automatic adjustment valve, baking oven waste heat recycling system and server, it is characterized in that: the furnace
Body, which is equipped with, fills into air scoop, Temperature and Humidity device, and hot blast feeding system is connected to by hot blast feeding pipeline with the furnace body,
There are several interconnected drying cavities in furnace body, each drying cavity top is equipped with dehumidifier air piping or reuse pipeline, dehumidifier wind
Machine has reuse mouth and exhaust outlet, and reuse pipeline, dehumidifier air piping are connected to the reuse mouth and exhaust outlet of dehumidifier blower respectively, takes out
The hot wind of reuse is sent into waste heat recovering energy conserving baking oven by wet blower by reuse mouth, and dehumidifier blower will be by drying by exhaust outlet
Waste heat recovering energy conserving baking oven is discharged in case waste heat recycling system treated wind, and baking oven waste heat recycling system is mounted on pumping
In wet wind pipeline and reuse pipeline, automatic adjustment valve is mounted on the exhaust outlet of dehumidifier blower, fills into air scoop and reuse pipeline
Connection, server are all connected with Temperature and Humidity device, automatic adjustment valve, hot blast feeding system.
2. waste heat recovering energy conserving baking oven according to claim 1, it is characterized in that: the Temperature and Humidity device is mounted on dehumidifier
In air piping, reuse pipeline and drying cavity, the supply of waste heat recovering energy conserving oven and automatic is controlled to adjust by server
Controlling opening of valve.
3. waste heat recovering energy conserving baking oven according to claim 1, it is characterized in that: the baking oven waste heat recycling system uses
Heat exchanger, the dehumidifier air piping are one and are connected to by dehumidifier air piping linkage section with drying cavity.
4. waste heat recovering energy conserving baking oven according to claim 1, it is characterized in that: the first two drying cavity is connected to by reuse pipeline
Reuse is carried out into the last one drying cavity of waste heat recovering energy conserving baking oven.
5. waste heat recovering energy conserving baking oven according to claim 1, it is characterized in that: the dehumidifier air piping passes through dehumidifier air piping
Linkage section is connected to drying cavity, and a conversion valve, conversion valve and reuse pipeline, dehumidifier are arranged on dehumidifier air piping linkage section
Air piping is connected to, and conversion valve is connect with server.
6. the residual heat recovery method of waste heat recovering energy conserving baking oven described in -5 any claims according to claim 1, it is characterized in that
The following steps are included: the hot wind in drying cavity is recycled by baking oven waste heat recycling system, by baking oven heat recovery
Hot wind after system, which is admitted to reuse pipeline if meeting reuse standard and otherwise passes through dehumidifier air piping, to be discharged, dehumidifier air piping
The discharge of the automatic regulating valve gate heating wind of upper configuration.
7. the residual heat recovery method of waste heat recovering energy conserving baking oven according to claim 6, it is characterized in that: being returned by baking oven waste heat
Receipts are detected using the hot wind after system by the Temperature and Humidity device of baking oven waste heat recycling system import, temperature and humidity inspection
It surveys the temperature signal that device detects and is transferred to server, server determines temperature signal according to process set value, if
Meet reuse standard and be then admitted to reuse pipeline and otherwise pass through dehumidifier air piping and is discharged.
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CN109869993A (en) * | 2019-02-14 | 2019-06-11 | 北方民族大学 | Self- propagating gradient drying box |
CN112629274A (en) * | 2020-12-24 | 2021-04-09 | 安徽省绩溪县华宇防火滤料有限公司 | Waste heat recovery system in glass fiber production process |
CN113758169A (en) * | 2021-09-27 | 2021-12-07 | 浙江哲丰新材料有限公司 | Papermaking drying cabinet |
CN114963711A (en) * | 2022-05-27 | 2022-08-30 | 扬州市江都区三和涂装设备有限公司 | Natural gas heating equipment for coating drying furnace |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109869993A (en) * | 2019-02-14 | 2019-06-11 | 北方民族大学 | Self- propagating gradient drying box |
CN109869993B (en) * | 2019-02-14 | 2023-12-05 | 北方民族大学 | Self-propagating gradient drying oven |
CN112629274A (en) * | 2020-12-24 | 2021-04-09 | 安徽省绩溪县华宇防火滤料有限公司 | Waste heat recovery system in glass fiber production process |
CN112629274B (en) * | 2020-12-24 | 2024-01-09 | 安徽省绩溪县华宇防火滤料有限公司 | Waste heat recovery system in glass fiber production process |
CN113758169A (en) * | 2021-09-27 | 2021-12-07 | 浙江哲丰新材料有限公司 | Papermaking drying cabinet |
CN114963711A (en) * | 2022-05-27 | 2022-08-30 | 扬州市江都区三和涂装设备有限公司 | Natural gas heating equipment for coating drying furnace |
CN114963711B (en) * | 2022-05-27 | 2024-02-06 | 陕西东海明珠防腐工程有限责任公司 | Natural gas heating equipment for coating drying furnace |
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