CN115823856A - Energy-saving constant-humidity adjusting method for production device and modular constant-humidity-discharging heat recovery device - Google Patents
Energy-saving constant-humidity adjusting method for production device and modular constant-humidity-discharging heat recovery device Download PDFInfo
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Abstract
The invention relates to an energy-saving constant-humidity adjusting method of a production device and a modularized constant-humidity-discharging heat recovery device, wherein the device and the adjusting method control the power supply frequency of an air exhaust fan through the detection and comparison results of humidity and air volume and adjust the air volume of air exhaust; the power supply frequency of the air supply fan is automatically controlled through static pressure detection and comparison results, and the air supply quantity is adjusted; further utilizes the proportion control adjustment between the air exhaust volume and the air supply volume to reduce the air exhaust volume and the air supply volume as much as possible. On the premise of ensuring the required maximum moisture exhaust amount, the invention reduces air exhaust and air supply as much as possible, reduces the operation energy consumption and further realizes the energy optimization configuration on the premise of meeting the requirements of the production process.
Description
Technical Field
The invention relates to an energy-saving constant humidity adjusting method for a production device and a modular constant humidity-discharging heat recovery device adopting the method, in particular to a method for automatically adjusting air exhaust and air supply quantity by utilizing a humidity value and a static pressure value to realize energy-saving constant humidity adjustment of the production device and the modular constant humidity-discharging heat recovery device.
Background
In the production process of coating the battery pole piece, the drying of the pole piece is one of the key processes, in the process of drying the pole piece, the humidity in the air can be gradually increased, the quality of drying the battery pole piece greatly depends on the factors such as the humidity and the temperature in the coating box, and the change of the temperature and the humidity in the air can cause the change of the air heat to influence the drying effect. Therefore, the moisture removing effect of the oven is one of the key tasks in the drying system of the coating machine. In order to achieve a high moisture removal effect, some manufacturers simply increase the air exhaust volume and the air supply volume, so that the energy consumption is greatly increased, the concept of environmental protection and energy conservation is contradicted, the air exhaust volume and the air supply volume cannot be reasonably controlled, the humidity and the heat in the coating box are unstable, the drying effect of the battery pole piece is not facilitated, and the production consistency of the battery is poor.
Disclosure of Invention
In view of the problems that the prior art cannot realize the requirement of reducing energy consumption to the maximum extent on the premise that a production device meets constant humidity, and cannot realize reasonable control of air exhaust and air supplement to cause unstable humidity and heat in the production device, the invention mainly aims to provide a method for realizing reasonable air supply and exhaust configuration of the production device to achieve constant humidity and energy-saving effects and a modular heat recovery device.
In order to achieve the above object, the present invention provides, in a first aspect, an energy-saving constant humidity adjustment method for a production apparatus, including an air supply step and an air exhaust step, wherein the air exhaust step includes an air exhaust volume adjustment step of:
i) Detecting the air humidity of the production device to obtain a humidity value in the production device;
ii) a step of comparing the humidity value in the production apparatus with a humidity value standard;
iii) And (iii) according to the comparison result in the step ii), carrying out air exhaust air volume regulation according to the following logic:
when the detected exhaust air humidity is smaller than the humidity value standard, if the detected exhaust air volume is smaller than the lowest value of the exhaust air volume, the current air volume is maintained to operate; if the air volume of the exhaust air is detected to be larger than the minimum value of the air volume of the exhaust air, the air volume of the exhaust air is reduced; when the detected exhaust air humidity is larger than the humidity value standard, the exhaust air is increased; and if the detected exhaust air humidity is equal to or basically equal to the humidity value standard, maintaining the current exhaust air volume.
Preferably, the air supply step further comprises an air supply volume adjusting step, and the air supply volume adjusting step controls the air supply volume in proportion according to the air exhaust volume.
Preferably, the air supply step further includes an air supply volume adjusting step, and the air supply volume adjusting step includes:
iv) detecting the static pressure in the production device to obtain the static pressure value in the production device;
v) a step of comparing said static pressure value with said static pressure standard value parameter;
vi) performing air volume regulation according to the comparison result in the step v) according to the following logic:
when the detected static pressure value is smaller than the static pressure standard value parameter, increasing the air supply quantity; when the detected static pressure value is larger than the static pressure standard value parameter, reducing the air supply volume; when the detected static pressure value is equal to or basically equal to the static pressure standard value parameter, the current air quantity operation is maintained.
Further, the air exhaust volume adjusting step and the air supply volume adjusting step can be adjusted synchronously or asynchronously.
Preferably, the exhaust air volume adjusting step further includes a step of setting a humidity value standard and an exhaust air volume minimum parameter.
Preferably, the air volume adjusting step further includes a step of setting a ratio of an air volume of the exhaust air to an air volume of the supply air.
Preferably, the step of adjusting the air supply volume further comprises the step of setting a standard value parameter of static pressure in the production device.
Further, the energy-saving constant-humidity adjusting method of the production device further comprises the step of exchanging heat of the air supply and the air exhaust.
The invention provides a modular constant humidity-discharging heat recovery device in a second aspect, which comprises an air supply outlet and an air exhaust outlet which are hermetically connected with a gas inlet and a gas outlet of a production device,
the heat exchanger exchanges heat between the air supply and the air exhaust;
an air supply fan;
an exhaust fan, an automatic air volume regulator of the exhaust fan;
a humidity sensor;
the humidity sensor is connected with the exhaust fan through the automatic air volume regulator of the exhaust fan, so that the humidity sensor, the automatic air volume regulator of the exhaust fan and the exhaust fan execute the exhaust air volume regulating steps.
Furthermore, the modularized constant dehumidifying and heat recovering device further comprises an automatic air supply fan adjuster, wherein the air supply fan is connected with the air exhaust fan through the automatic air supply fan adjuster and the automatic air exhaust fan adjuster, so that the automatic air supply fan adjuster and the air supply fan execute the air supply volume adjusting step.
Furthermore, the modularized constant dehumidifying and heat recovering device further comprises a static pressure sensor and an air supply fan air quantity automatic regulator, wherein the static pressure sensor is connected with the air supply fan through the air supply fan air quantity automatic regulator, so that the static pressure sensor, the air supply fan air quantity automatic regulator and the air supply fan execute the air supply air quantity regulating steps.
Optionally, the heat exchanger is a two-way corrugated plate heat exchanger, a heat pipe heat exchanger or a rotary wheel heat exchanger.
Preferably, the number of the heat exchangers is at least two, and the heat exchangers are used in series.
Furthermore, the modularized constant humidity-discharging heat recovery device further comprises a fresh air filter.
Preferably, the air supply fan and/or the air exhaust fan are variable frequency fans.
Based on the design, the invention has the beneficial effects that: the power supply frequency of the air exhaust fan is controlled through the humidity detection and comparison result, so that the air exhaust can be reduced as much as possible on the premise of ensuring the required maximum moisture exhaust amount, and the operation energy consumption is reduced; in addition, the air supply volume adjusting step can proportionally control the air supply volume according to the air exhaust volume, and can also control the power supply frequency of an air supply fan through a static pressure detection and comparison result so as to adjust the air supply volume, on the premise of meeting the humidity elimination, the air supply volume can be reduced as much as possible through different air supply logics, and the energy optimization configuration and the process requirements in the production device are further realized; in addition, the humidity value standard, the lowest value parameter of the air exhaust volume and the standard value parameter of the static pressure in the production device can be set according to the external environment and the actual process requirements, so that the use efficiency and the use effect of the device under different conditions are optimized; on the other hand, the modularized constant humidity-discharging heat recovery device provided by the invention combines the heat exchange component, the constant humidity control component and logic operation with each other, further reduces the energy consumption of the device and the method, can prepare corresponding modularized products according to different production devices, is beneficial to standardization and expanded production, and realizes organic combination of energy conservation, environmental protection and economic benefits.
Drawings
Fig. 1 is a schematic diagram illustrating the principle and structure of a modular constant-humidity heat recovery device and an energy-saving constant-humidity adjustment method according to a first embodiment of the present invention;
FIG. 2 is a schematic diagram of the venting logic of the first embodiment of the present invention;
FIG. 3 is a schematic diagram of the principle and structure of a modular constant humidity exhaust heat recovery device and a second embodiment of the energy-saving constant humidity adjustment method of the present invention;
FIG. 4 is a schematic diagram of a second embodiment of the present invention;
FIG. 5 is a schematic diagram of the principle and structure of a modular constant humidity discharging heat recovery device and an energy-saving constant humidity adjusting method according to a third embodiment of the present invention;
description of the reference numerals
100. Coating machine drying oven; 200. the anode modularization constant humidity-discharging heat recovery device; 201. a heat exchanger; 202. an air supply fan; 203. a frequency converter of the air supply fan; 204. an automatic air supply volume regulator; 205. a static pressure sensor; 206. an exhaust air humidity sensor; 207. an exhaust fan; 208. an exhaust fan frequency converter; 209. an automatic air exhaust volume regulator; 210. a fresh air filter; 211. and (5) draining and sealing.
Detailed Description
In order to make those skilled in the art better understand the technical solution of the present invention, the technical solution in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments shown in the drawings. It should be noted that these embodiments are not intended to limit the present invention, and those skilled in the art should be able to make functional, methodical, or structural equivalents or substitutions according to these embodiments without departing from the scope of the present invention.
Meanwhile, in the present specification, descriptions related to orientations such as up, down, left, right, front, rear, inner, outer, longitudinal, lateral, vertical, horizontal, etc., indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the referred device or element must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention.
In the description of the present specification, unless otherwise specifically stated or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, a fixed connection, a detachable connection, or an integral connection, a mechanical connection, an electrical connection, a direct connection, an indirect connection through an intermediate medium, or a communication between two elements. To those skilled in the art, the specific meanings of the above terms in the present invention can be understood according to specific situations, and the present invention should not be construed as being limited thereto.
For convenience of description, in the preferred embodiments of the present invention, the coater anode oven is selected as a production device, and the principle of moisture and energy saving between the coater anode oven and the constant moisture and energy saving processing module box is mainly explained, but it should be understood that the production device described in the present invention should not be limited to the coater electrode oven, and any production device requiring air supply, air exhaust and moisture removal in production, such as: production devices in the fields of the paper industry, the solar photovoltaic cell production process, the automobile coating flash drying chamber, the semiconductor manufacturing industry, the pharmacy industry, the food production industry and the like can be used in combination with the modular constant moisture and heat removal device of the invention, and the coater electrode oven should not be construed as limiting the production device in the claims.
Fig. 1 is a schematic diagram illustrating the principle and structure of a modular constant humidity discharging heat recovery device and an energy-saving constant humidity adjusting method according to a first embodiment of the present invention, including: a coater oven 100 and an anode modular constant moisture and heat removal and recovery device 200; the gas inlet and outlet of the coater oven 100 are hermetically connected with the air supply outlet and the air exhaust outlet of the anode modular constant moisture and heat recovery device 200 correspondingly, so that the waste gas in the coater oven 100 is guided into the anode modular constant moisture and heat recovery device 200 through the air exhaust outlet, and the outside fresh air is guided into the coater oven 100 through the air supply outlet; the anode modular constant humidity and heat recovery device 200 at least comprises a heat exchanger 201, an air supply fan 202, an exhaust fan 207, an exhaust air volume automatic regulator 209 and a humidity sensor 206, wherein the heat exchanger 201 divides the inside of the anode modular constant humidity and heat recovery device 200 into an air supply air channel and an air exhaust air channel, the air supply fan 202 and the exhaust fan 207 are respectively and correspondingly arranged in the air supply air channel and the air exhaust air channel and are used for introducing fresh air into the coater oven 100 and leading exhaust gas out of the coater oven 100, and because the exhaust gas exhausted from the coater oven 100 has high temperature (usually about 100 ℃), the fresh air entering the coater oven from the outside air has low temperature and needs to be heated for drying, the heat exchanger 201 can exchange heat between the fresh air and the exhaust gas, on one hand, the heat quantity of the exhaust gas exhausted into the outside air can be reduced, on the other hand, the fresh air can be preheated, the energy consumption of a system required for reheating to a specified temperature is reduced, and the effects of energy saving and efficiency increasing are achieved. The heat exchanger 201 of the present invention is preferably a two-way corrugated plate heat exchanger, and is disposed in a diamond shape, but any other heat exchangers capable of performing heat exchange, such as heat pipe heat exchanger, heat wheel heat exchanger, and other various air-to-air heat exchangers and their adaptive fixing and mounting methods, are all covered by the scope of the present invention.
In this embodiment, the humidity sensor 206 is disposed in the exhaust air duct and is configured to detect a humidity value of an air flow inside the oven 100; the anode modularized constant humidity-discharging heat-recovering device 200 further comprises an exhaust air volume automatic regulator 209, wherein an input end of the exhaust air volume automatic regulator 209 is electrically connected with the humidity sensor 206 for receiving a humidity value detected by the humidity sensor 206, and in a preferred scheme, the humidity value standard can be set additionally according to experience of a user, and/or external environment, and/or drying process requirements; the output end of the exhaust air volume automatic regulator 209 is connected with the exhaust fan 207 to regulate the exhaust volume of the exhaust fan 207 according to the following exhaust logic: as shown in fig. 2, when the detected exhaust air humidity is smaller than the humidity value standard, if the detected exhaust air volume is smaller than the lowest value of the exhaust air volume, the current air volume is maintained to operate; if the air volume of the exhaust air is detected to be larger than the minimum value of the air volume of the exhaust air, the air volume of the exhaust air is reduced; when the detected exhaust air humidity is larger than the humidity value standard, the exhaust air is increased; and if the detected exhaust air humidity is equal to or basically equal to the humidity value standard, maintaining the current air volume. The power supply frequency of the air exhaust fan is controlled through the humidity detection and comparison result, so that the air exhaust can be reduced as much as possible on the premise of ensuring the required maximum moisture exhaust amount, and the operation energy consumption is reduced.
In this embodiment, the air volume of the air supply fan 202 may automatically supply air according to a certain ratio between the air volume of the exhaust air and the air volume of the supply air. The automatic exhaust air volume regulator 209 is in signal connection with the automatic supply air volume regulator 204, and the exhaust air volume and the supply air volume automatically supply air according to a certain proportion. Preferably, the ratio can be specifically set according to the experience of the user and the process requirements. Specifically, the exhaust air volume and the supply air volume are in a ratio of 1: setting a ratio of 0.9-0.95, when the humidity sensor 206 detects that the air humidity in the oven is 33.0g/kg (more than 25g/kg of humidity value standard), indicating that the air humidity in the oven is increased, enlarging the air exhaust volume to 70000m for cultivation/h, and correspondingly automatically adjusting the air supply volume to 63000 m for cultivation/h according to the set ratio of the air exhaust volume to the air supply volume; when the humidity sensor 206 detects that the air humidity in the oven is 25.2 g/kg (the humidity value standard is 25g/kg, and the humidity value is +/-2 from the humidity value standard and is regarded as being basically equal to the humidity value standard), the air humidity in the oven can meet the process requirements, the air exhaust amount is not required to be increased at the moment, only the current air exhaust amount is required to be maintained, and the air supply amount is automatically maintained according to the set proportion of the air exhaust amount to the air supply amount correspondingly; when the air humidity in the oven of the humidity sensor 206 is 21g/kg (less than the humidity value standard of 25 g/kg), it is indicated that the air in the oven is very dry and can completely meet the drying requirement, and at the moment, the process level can be met only by keeping the air exhaust air quantity as small as possible, so that the energy consumption of the system is reduced, namely: if detecting that the exhaust air volume is smaller than the minimum exhaust air volume value of 45000m through labor/hour, maintaining the current air volume operation, and correspondingly, automatically maintaining the air volume according to the set ratio of the exhaust air volume to the air volume; if the exhaust air volume is detected to be larger than the minimum exhaust air volume, the exhaust air volume is reduced to the minimum exhaust air volume, and correspondingly, the supply air volume is automatically reduced to the corresponding minimum value according to the set ratio of the exhaust air volume to the supply air volume. The embodiment can automatically adjust the air supply volume according to the air exhaust volume in a proportion adjusting mode, and reduces the energy consumption of the system on the premise of meeting the humidity elimination requirement.
Preferably, in order to further optimize the system performance of the anode modular constant humidity-discharging heat recovery device 200, a plurality of sets of devices may be further added, for example: a fresh air filter 210 is additionally arranged to strictly filter fresh air led into the coating machine drying oven 100 so as to meet the drying process requirement and prevent dust and the like from polluting electrode plates in the drying process; set up exhaust fan 207 as the frequency conversion fan, specifically do: the exhaust fan frequency converter 208 is combined with the form of the exhaust fan 207 to adjust the exhaust air quantity by changing the power frequency, so that the air quantity adjustment is more convenient; and a water seal 211 for draining the condensed liquid after heat exchange out of the system in time to prevent the condensed water from accumulating in the system; preferably, in the embodiment, the humidity value standard and the minimum exhaust air quantity parameter can be specifically set according to the external environment and the actual process requirements, so that the efficiency effect of the device used under different conditions is optimized, and the use range of the device under different conditions is widened; although the above groups of devices are shown in embodiment 1, it should be understood that they are only preferred embodiments for implementing functions of the system, and are not the lowest configuration requirements for implementing functions of the system, and should not be construed as limiting the scope of the claims.
Fig. 3 is a schematic diagram of the principle and structure of a second embodiment of the modularized constant humidity-discharging heat-recovering device and the energy-saving constant humidity adjusting method of the present invention, and compared with the first embodiment, the main difference of this embodiment lies in the change of the air supply logic, in this embodiment, a static pressure sensor 205 for detecting the static pressure value in the oven is arranged in the coater oven 100, the air supply logic is executed according to the static pressure value in the oven detected by the static pressure sensor 205, and the air supply amount of the air supply fan 202 is adjusted by the automatic air supply amount adjuster 204.
The specific air supply logic is as follows: when the static pressure value detected by the static pressure sensor 205 is smaller than the static pressure standard value parameter, the air supply volume needs to be increased; when the detected static pressure value is larger than the static pressure standard value parameter, reducing the air supply volume; when the detected static pressure value is equal to or basically equal to the static pressure standard value parameter, the current air quantity operation is maintained. Specifically, when humidity sensor 206 detects that the humidity of the air in the oven is 33.0g/kg (greater than the humidity value standard of 25 g/kg), which indicates that the humidity of the air in the oven is increased, the air discharge amount needs to be increased to 70000m for carrying out the year/h, the static pressure value detected by static pressure sensor 205 is smaller than the static pressure standard value parameter of-10 Pa, and the air supply amount needs to be automatically increased to 63000 m for carrying out the year/h; when the humidity sensor 206 detects that the humidity of the air in the oven is 26g/kg (for example, the humidity value is 25g/kg, the humidity value is plus or minus 2 from the humidity value standard and is regarded as being substantially equal to the humidity value standard), it indicates that the humidity of the air in the oven can meet the process requirements, at this time, the air discharge amount does not need to be increased, and only the current air discharge amount needs to be maintained, and at this time, the static pressure value detected by the static pressure sensor 205 is also equal to or substantially equal to the static pressure standard value parameter (the static pressure standard value is-10 Pa, and the static pressure value is plus or minus 5Pa from the static pressure standard value and is regarded as being substantially equal to the static pressure standard value), so that the current air volume operation is maintained; when the air humidity in the humidity sensor 206 oven is 21g/kg (less than 25g/kg of humidity value standard), it is described that the air in the oven is very dry, and the drying requirement can be completely met, and at the moment, the process level can be met only by keeping the air exhaust air quantity as small as possible, so that the energy consumption of the system is reduced, namely: and if detecting that the exhaust air volume is smaller than the minimum exhaust air volume value of 45000 m/h, maintaining the current air volume operation, and correspondingly, reducing the air supply volume to 43000m for cultivation/h when the detected static pressure value is larger than the static pressure standard value parameter.
Preferably, the air supply fan 202 in this embodiment is also preferably a variable frequency fan, specifically: the air supply fan frequency converter 203 is combined with the air supply fan 202 to adjust the air exhaust quantity by changing the power supply frequency, so that the air quantity adjustment is more convenient; in this embodiment, the exhaust air volume adjusting step and the supply air volume adjusting step may be adjusted synchronously or asynchronously, that is: the air exhaust volume adjusting step and the air supply volume adjusting step may be performed simultaneously, or the air exhaust volume adjusting step may be performed prior to or subsequent to the air supply volume adjusting step; preferably, in this embodiment, the static pressure standard value parameter in the oven can also be specifically set according to the external environment and the actual process requirements, so that the efficiency and the effect of the device used under different conditions are optimized, and the use range of the device under different conditions is widened.
In the embodiment, the power supply frequency of the air exhaust fan is controlled through the humidity and air volume detection and comparison results, so that the air exhaust can be reduced as much as possible on the premise of ensuring the required maximum moisture exhaust amount, and the operation energy consumption is reduced; the power supply frequency of the air supply fan is automatically controlled through the static pressure detection and comparison results, and the air exhaust and air supply air quantity is reduced as much as possible by utilizing the proportional control adjustment between the static pressure detection and comparison results, so that the energy source optimal configuration is further realized on the premise of meeting the production process requirements.
Fig. 5 is a schematic diagram of the principle and structure of a third embodiment of the modular constant humidity discharging and heat recovering device and the energy-saving constant humidity adjusting method of the present invention, compared with the second embodiment, the main difference of this embodiment is that a heat exchanger 201 can be configured to be used in series with two heat exchangers, and the heat exchangers are preferably plate heat exchangers and arranged in a diamond shape. It should be understood that the type, number and arrangement of the heat exchangers 201 can be adjusted by those skilled in the art according to actual needs.
More than two heat exchangers are arranged, so that the heat exchange efficiency and effect can be further improved, taking the two heat exchangers 201 as an example, the temperature of high-temperature waste gas is reduced by about 30% compared with that of one heat exchanger after two-stage heat exchange, and the emission standard is met; and the outside new trend is through two-stage heat exchange, compares in a heat exchanger, and the temperature can increase about 30%, only needs to add slightly the heating and can accord with the needs of stoving temperature. Compared with single-stage heat exchange, the multi-stage heat exchange has more sufficient heat exchange and lower energy consumption, and better meets the requirement of production energy conservation.
It should be understood that although the specification describes embodiments, not every embodiment includes only a single embodiment, and such description is for clarity purposes only, and it will be appreciated by those skilled in the art that the specification as a whole may be appropriately combined to form other embodiments as will be apparent to those skilled in the art.
The above-listed detailed description is merely a detailed description of possible embodiments of the present invention, and it is not intended to limit the scope of the invention, and equivalent embodiments or modifications made without departing from the technical spirit of the present invention are intended to be included within the scope of the present invention.
Claims (15)
1. The energy-saving constant-humidity adjusting method of the production device is characterized by comprising an air supply step and an air exhaust step, wherein the air exhaust step comprises the following air exhaust volume adjusting step:
i) Detecting the air humidity of the production device to obtain a humidity value in the production device;
ii) a step of comparing the humidity value in the production apparatus with a humidity value standard;
iii) And (ii) performing air exhaust volume regulation according to the comparison result in the step ii) according to the following logic:
when the detected exhaust air humidity is smaller than the humidity value standard, if the detected exhaust air volume is smaller than the lowest value of the exhaust air volume, the current air volume is maintained to operate; if the air volume of the exhaust air is detected to be larger than the minimum value of the air volume of the exhaust air, the air volume of the exhaust air is reduced; when the detected exhaust air humidity is larger than the humidity value standard, the exhaust air is increased; and if the detected exhaust air humidity is equal to or basically equal to the humidity value standard, maintaining the current exhaust air volume.
2. The energy-saving constant-humidity adjusting method of the production device as claimed in claim 1, characterized in that: the air supply step also comprises an air supply volume adjusting step, and the air supply volume adjusting step controls the air supply volume according to the air exhaust volume in proportion.
3. The energy-saving constant-humidity adjusting method of the production device as claimed in claim 1, characterized in that: the air supply step further comprises an air supply volume adjusting step, and the air supply volume adjusting step comprises:
iv) detecting the static pressure in the production device to obtain the static pressure value in the production device;
v) a step of comparing said static pressure value with said static pressure standard value parameter;
vi) according to the comparison result in the step v), carrying out air supply quantity regulation according to the following logic:
when the detected static pressure value is smaller than the static pressure standard value parameter, increasing the air supply quantity; when the detected static pressure value is larger than the static pressure standard value parameter, reducing the air supply volume; and when the detected static pressure value is equal to or basically equal to the static pressure standard value parameter, maintaining the current air flow operation.
4. The energy-saving constant-humidity adjusting method of the production device as claimed in claim 3, characterized in that: the air exhaust volume adjusting step and the air supply volume adjusting step can be synchronously or asynchronously adjusted.
5. The energy-saving constant-humidity adjusting method of the production device as claimed in claim 1, characterized in that: the air exhaust quantity adjusting step also comprises the step of setting a humidity value standard and an air exhaust quantity minimum parameter.
6. The energy-saving constant-humidity adjusting method of the production device as claimed in claim 2, characterized in that: the air supply quantity adjusting step also comprises the step of setting the proportion of the air exhaust quantity and the air supply quantity.
7. The energy-saving constant-humidity adjusting method of the production device as claimed in claim 3, characterized in that: the air supply volume adjusting step also comprises the step of setting a static pressure standard value parameter in the production device.
8. The energy-saving constant-humidity adjusting method of the production device according to any one of claims 1 to 7, characterized in that: also comprises a step of exchanging heat between the air supply and the air exhaust.
9. The utility model provides a invariable hydrofuge heat reclamation device of modularization, includes supply-air outlet and the air exit that corresponds airtight connection with the gaseous import of apparatus for producing and export, its characterized in that:
the heat exchanger exchanges heat between the air supply and the air exhaust;
an air supply fan;
an exhaust fan, an automatic air volume regulator of the exhaust fan;
a humidity sensor;
the humidity sensor is connected with the exhaust fan through the automatic air volume regulator of the exhaust fan, so that the humidity sensor, the automatic air volume regulator of the exhaust fan and the exhaust fan execute the exhaust air volume regulating step as claimed in claim 1, 5 or 8.
10. The modular constant extraction moisture heat recovery unit of claim 9, further comprising: and the air supply fan is connected with the exhaust fan through the air supply fan automatic regulator and the exhaust fan automatic regulator, so that the air supply fan automatic regulator and the air supply fan execute the air supply volume adjusting step as claimed in claim 2 or 6.
11. The modular constant extraction moisture heat recovery device of claim 9, wherein: further comprising: the static pressure sensor is connected with the air supply fan through the automatic air supply fan volume regulator, so that the static pressure sensor, the automatic air supply fan volume regulator and the air supply fan can execute the air supply volume regulating steps as claimed in claim 3, 4 or 7.
12. The modular constant extraction moisture heat recovery device of claim 9, wherein: the heat exchanger is a bidirectional corrugated plate type heat exchanger, a heat pipe type heat exchanger or a rotary wheel type heat exchanger.
13. The modular constant extraction moisture heat recovery device of claim 9 or 12, wherein: the number of the heat exchangers is at least two, and the heat exchangers are used in series.
14. The modular constant extraction moisture heat recovery device of claim 9, wherein: also comprises a fresh air filter.
15. The modular constant extraction moisture heat recovery device of claim 9, wherein: the air supply fan and/or the air exhaust fan are variable frequency fans.
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Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61268161A (en) * | 1985-05-22 | 1986-11-27 | Furuta Denki Kk | Method for drying laver |
CN201740352U (en) * | 2010-08-20 | 2011-02-09 | 昆明理工大学 | Tunnel-type drying device |
CN105066666A (en) * | 2015-07-22 | 2015-11-18 | 合肥淘能环境科技有限公司 | Heat pump drying device with humidity and temperature adjusting function |
CN105571308A (en) * | 2014-10-15 | 2016-05-11 | 中联重科股份有限公司 | Control system, method and device of dry-mixed mortar drying system |
CN206136869U (en) * | 2016-10-09 | 2017-05-03 | 南京农业大学淮安研究院 | Supplementary exhaust device of beasts and birds house |
CN206469594U (en) * | 2016-12-20 | 2017-09-05 | 珠海格力电器股份有限公司 | A kind of heat pump dryer |
CN107449266A (en) * | 2017-07-01 | 2017-12-08 | 烟台明辉热泵节能科技有限公司 | A kind of tunnel drying system and furnace drying method |
CN206919556U (en) * | 2017-06-29 | 2018-01-23 | 颜厥电 | A kind of dryer |
CN207214766U (en) * | 2017-09-05 | 2018-04-10 | 中国电力工程顾问集团华北电力设计院有限公司 | Ultrahigh-temperature waste heat recovery wet down unit |
CN109520275A (en) * | 2018-12-19 | 2019-03-26 | 宝莲华新能源技术(上海)股份有限公司 | A kind of four-way intelligence dryer |
CN109579455A (en) * | 2018-12-19 | 2019-04-05 | 重庆奇甫机械有限责任公司 | Rotary drying formula auto parts and components drying system |
CN209524736U (en) * | 2019-01-10 | 2019-10-22 | 上海粹好科技有限公司 | A kind of agricultural and sideline product bakery hydrofuge waste-heat recovery device |
CN110469927A (en) * | 2019-02-22 | 2019-11-19 | 秦文选 | Self coupling heat exchange and cold and heat recovery fresh air dehumidification air conditioner |
JP2020008251A (en) * | 2018-07-11 | 2020-01-16 | ダイキン工業株式会社 | Ventilation device |
CN111780509A (en) * | 2020-07-15 | 2020-10-16 | 昆明飞泉环保科技有限公司 | Intelligent temperature-control electric heating tobacco curing barn and control method |
-
2021
- 2021-09-17 CN CN202111090706.8A patent/CN115823856A/en active Pending
Patent Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61268161A (en) * | 1985-05-22 | 1986-11-27 | Furuta Denki Kk | Method for drying laver |
CN201740352U (en) * | 2010-08-20 | 2011-02-09 | 昆明理工大学 | Tunnel-type drying device |
CN105571308A (en) * | 2014-10-15 | 2016-05-11 | 中联重科股份有限公司 | Control system, method and device of dry-mixed mortar drying system |
CN105066666A (en) * | 2015-07-22 | 2015-11-18 | 合肥淘能环境科技有限公司 | Heat pump drying device with humidity and temperature adjusting function |
CN206136869U (en) * | 2016-10-09 | 2017-05-03 | 南京农业大学淮安研究院 | Supplementary exhaust device of beasts and birds house |
CN206469594U (en) * | 2016-12-20 | 2017-09-05 | 珠海格力电器股份有限公司 | A kind of heat pump dryer |
CN206919556U (en) * | 2017-06-29 | 2018-01-23 | 颜厥电 | A kind of dryer |
CN107449266A (en) * | 2017-07-01 | 2017-12-08 | 烟台明辉热泵节能科技有限公司 | A kind of tunnel drying system and furnace drying method |
CN207214766U (en) * | 2017-09-05 | 2018-04-10 | 中国电力工程顾问集团华北电力设计院有限公司 | Ultrahigh-temperature waste heat recovery wet down unit |
JP2020008251A (en) * | 2018-07-11 | 2020-01-16 | ダイキン工業株式会社 | Ventilation device |
CN109520275A (en) * | 2018-12-19 | 2019-03-26 | 宝莲华新能源技术(上海)股份有限公司 | A kind of four-way intelligence dryer |
CN109579455A (en) * | 2018-12-19 | 2019-04-05 | 重庆奇甫机械有限责任公司 | Rotary drying formula auto parts and components drying system |
CN209524736U (en) * | 2019-01-10 | 2019-10-22 | 上海粹好科技有限公司 | A kind of agricultural and sideline product bakery hydrofuge waste-heat recovery device |
CN110469927A (en) * | 2019-02-22 | 2019-11-19 | 秦文选 | Self coupling heat exchange and cold and heat recovery fresh air dehumidification air conditioner |
CN111780509A (en) * | 2020-07-15 | 2020-10-16 | 昆明飞泉环保科技有限公司 | Intelligent temperature-control electric heating tobacco curing barn and control method |
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