CN113720141A - Multi-effect high-temperature overlapping type drying system - Google Patents
Multi-effect high-temperature overlapping type drying system Download PDFInfo
- Publication number
- CN113720141A CN113720141A CN202111161058.0A CN202111161058A CN113720141A CN 113720141 A CN113720141 A CN 113720141A CN 202111161058 A CN202111161058 A CN 202111161058A CN 113720141 A CN113720141 A CN 113720141A
- Authority
- CN
- China
- Prior art keywords
- drying system
- heat exchanger
- temperature
- plate heat
- temperature drying
- 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.)
- Pending
Links
Images
Classifications
-
- 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
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
- F26B21/002—Drying-air generating units, e.g. movable, independent of drying enclosure heating the drying air indirectly, i.e. using a heat exchanger
-
- 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
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
-
- 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
- F26B23/005—Heating arrangements using waste heat recovered from dryer exhaust gases using a closed cycle heat pump system ; using a heat pipe system
-
- 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
The invention discloses a multi-effect high-temperature overlapping type drying system, which consists of a high-temperature drying system, a low-temperature drying system, a four-way valve, a process water tank, two electric flow valves, a pipeline circulating water pump, a drying bin and a distilled water overflow port; the low-temperature drying systems are connected through a four-way valve, the output ends of the low-temperature drying systems are connected with a vacuum pump, the vacuum pump is connected with a process water tank, a distilled water overflow port is arranged on the process water tank and used for draining water, the high-temperature drying systems are connected with the low-temperature drying systems through pipelines, the output ends of the drying bins are connected with the high-temperature drying systems, the pipeline circulating water pump is arranged between the drying bins and the high-temperature drying systems, and electric flow valves are arranged on the pipelines connected with the high-temperature drying systems and the low-temperature drying systems; the invention can realize waste heat recovery and storage recycling in the drying process, is energy-saving, environment-friendly and free from peculiar smell, and has good market application value.
Description
Technical Field
The invention relates to the field of gas treatment of kitchen and kitchen waste, in particular to a multi-effect high-temperature overlapping type drying system.
Background
The prior kitchen waste drying technology can generate a large amount of waste heat and peculiar smell in the operation process, has overlarge energy consumption, brings great harm and pollution to the environment and the periphery and resource waste, the heat pump belongs to the most effective energy-saving scheme on the market at the present stage, but has great disadvantages for the heat pump in the negative pressure drying field, the main disadvantages are that the span of heat absorption and heat release of the heat pump is very small (for example, the condensation end of the heat pump is 95-105 ℃, the residual temperature of steam after the evaporation end is absorbed is 40-50 ℃, the evaporation temperature is high, so the service life of the heat pump system is reduced, the heat of the steam cannot be completely absorbed, the heat is wasted when the heat pump is discharged to the atmosphere, and the uncondensed gas has pungent smell when the gas is discharged), in addition, the dried material belongs to a high temperature state at the discharge stage, so the environmental temperature is increased when the material is discharged, meanwhile, high-temperature steam in the material continuously releases heat and peculiar smell to the environment in the discharging process, and the problems that the electric heating is needed to assist in temperature rise and energy consumption is too high before the equipment runs are solved, so that the purposes of environmental protection, energy conservation and emission reduction are overcome, and therefore, the prior art has defects and needs to be improved.
Disclosure of Invention
In order to solve the defects in the prior art, the invention provides a multi-effect high-temperature overlapping type drying system to solve the problems.
The invention provides a multi-effect high-temperature overlapping type drying system, which consists of a high-temperature drying system, a low-temperature drying system, a four-way valve, a process water tank, two electric flow valves, a pipeline circulating water pump, a drying bin and a distilled water overflow port; the low-temperature drying system is connected through a four-way valve, the output end of the low-temperature drying system is connected with a vacuum pump, the vacuum pump is connected with a process water tank, a distilled water overflow port is arranged on the process water tank and used for draining water, the high-temperature drying system is connected with the low-temperature drying system through a pipeline, the output end of the drying bin is connected with the high-temperature drying system, the pipeline circulating water pump is arranged between the drying bin and the high-temperature drying system, and an electric flow valve is arranged on the pipeline connected with the high-temperature drying system and the low-temperature drying system.
Preferably, the low-temperature drying system comprises a heat pump compressor I, a plate heat exchanger II, a plate heat exchanger III, a fan and a condenser; one end of the first heat pump compressor is connected with a four-way valve, the four-way valve is connected with the first plate heat exchanger, the other end of the first plate heat exchanger is connected with one end of a fan, the other end of the fan is connected with one end of the second plate heat exchanger through a pipeline, the other end of the second plate heat exchanger is connected with the third plate heat exchanger, and a port of the third plate heat exchanger is connected with a condenser.
Preferably, a throttle valve is arranged on a connecting pipeline between the fan and the second plate heat exchanger.
Preferably, the low-temperature drying system absorbs heat from air and supplies the heat to the drying system, and the fan, the plate heat exchanger II and the plate heat exchanger III are matched to realize large-temperature-difference environment work.
Preferably, the high-temperature drying system comprises a heat pump compressor II, a plate heat exchanger IV and a plate heat exchanger V; one end of the air heat pump compressor II is connected with the plate heat exchanger II, the other end of the heat pump compressor II is connected with the plate heat exchanger V, and the plate heat exchanger III is connected with the plate heat exchanger IV.
Preferably, the vacuum pump is used for pumping steam in the drying bin to generate negative pressure in the drying bin, and the pumped steam is changed into distilled water through two-stage temperature reduction and is discharged through the distilled water overflow port.
Preferably, when the high-temperature drying system converts the low heat energy of the low-temperature drying system and the steam heat in the drying bin into high heat energy, the heat is transferred into the licorice root bin through the pipeline circulating water pump, and the heat is recycled.
Preferably, the first plate heat exchanger and the second plate heat exchanger are both multi-effect evaporation and condensation, and the first plate heat exchanger and the second plate heat exchanger form a double-machine overlapping type heat recovery and reuse system.
Compared with the prior art, the invention realizes the low-temperature discharge of the evaporated distilled water without pollution and peculiar smell, can realize the drying in a low-temperature environment, the low-temperature discharge and the low-temperature discharge of the distilled water, mainly realizes the large-temperature cross-domain drying field through the multi-effect heat exchange function of a low-temperature drying system, and achieves the purposes of energy conservation and emission reduction; the waste heat recovery (excessive system heat energy caused by long-time operation of the heat pump, high temperature of circulating liquid of the drying system after drying is finished, and the dried material and the circulating liquid can be cooled to normal temperature after drying is finished) in the drying process can be realized, and the energy-saving environment-friendly drying system is energy-saving, environment-friendly and free of peculiar smell.
Drawings
FIG. 1 is a schematic view of the overall structure of the present invention;
a first plate heat exchanger 1; a fan 2; a second plate heat exchanger 3; a four-way valve 4; a first heat pump compressor 5; a third plate heat exchanger 6; a vacuum pump 7; a plate heat exchanger IV 8; a second heat pump compressor 9; a process water tank 10; a condenser 11; an electrically operated flow valve 12; a fifth plate heat exchanger 14; a pipeline circulating water pump 15; a drying bin 16; a distilled water overflow port 17.
Detailed Description
The technical features mentioned above are combined with each other to form various embodiments which are not listed above, and all of them are regarded as the scope of the present invention described in the specification; also, modifications and variations may be suggested to those skilled in the art in light of the above teachings, and it is intended to cover all such modifications and variations as fall within the true spirit and scope of the invention as defined by the appended claims.
In order to facilitate an understanding of the invention, the invention is described in more detail below with reference to the accompanying drawings and specific examples. Preferred embodiments of the present invention are shown in the drawings. This invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
It will be understood that when an element is referred to as being "secured to" another element, it can be directly on the other element or intervening elements may also be present. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or intervening elements may also be present. The terms "vertical," "horizontal," "left," "right," and the like as used herein are for descriptive purposes only.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used in the description of the invention herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention.
The present invention will be described in detail with reference to the accompanying drawings.
One embodiment as shown in fig. 1: a multi-effect high-temperature overlapping type drying system is composed of a high-temperature drying system, a low-temperature drying system, a four-way valve 4, a process water tank 10, two electric flow valves 12, a pipeline circulating water pump 15, a drying bin 16 and a distilled water overflow port 17; the low-temperature drying system is connected through a four-way valve 4, the output end of the low-temperature drying system is connected with a vacuum pump 7, the vacuum pump 7 is connected with a process water tank 10, a distilled water overflow port 17 is installed on the process water tank 10, the distilled water overflow port 17 is used for draining water, the high-temperature drying system is connected with the low-temperature drying system through a pipeline, the output end of a drying bin 16 is connected with the high-temperature drying system, a pipeline circulating water pump 15 is installed between the drying bin 16 and the high-temperature drying system, and an electric flow valve 12 is installed on the pipeline connected with the high-temperature drying system and the low-temperature drying system.
Embodiment 4 is based on embodiment 1, the low-temperature drying system absorbs heat from air and supplies the heat to the starting heat energy of the drying system, and the fan 2, the second plate heat exchanger 3 and the third plate heat exchanger 6 are used in cooperation to realize large-temperature-difference environment operation.
Embodiment 5 on the basis of embodiment 1, the high-temperature drying system includes a second heat pump compressor 9, a fourth plate heat exchanger 8, and a fifth plate heat exchanger 14; one end of the second heat pump compressor 9 is connected with the second plate heat exchanger 3, the other end of the second heat pump compressor 9 is connected with the fifth plate heat exchanger 14, and the third plate heat exchanger 6 is connected with the fourth plate heat exchanger 8.
Embodiment 7 based on embodiment 1, when the high-temperature drying system converts the low heat energy of the low-temperature drying system and the steam heat in the drying chamber 16 into high heat energy, the heat is transferred into the licorice root chamber by the pipe circulating water pump 15, so that the heat is recycled.
Embodiment 7 is based on embodiment 2, the first plate heat exchanger 1 and the second plate heat exchanger 3 are both multi-effect evaporation and condensation, and the first plate heat exchanger 1 and the second plate heat exchanger 3 form a dual-unit overlapping heat recovery and reuse system. .
The technical features mentioned above are combined with each other to form various embodiments which are not listed above, and all of them are regarded as the scope of the present invention described in the specification; also, modifications and variations may be suggested to those skilled in the art in light of the above teachings, and it is intended to cover all such modifications and variations as fall within the true spirit and scope of the invention as defined by the appended claims.
Claims (8)
1. A multi-effect high-temperature overlapping type drying system is characterized in that the drying system consists of a high-temperature drying system, a low-temperature drying system, a four-way valve, a process water tank, two electric flow valves, a pipeline circulating water pump, a drying bin and a distilled water overflow port; the low-temperature drying system is connected through a four-way valve, the output end of the low-temperature drying system is connected with a vacuum pump, the vacuum pump is connected with a process water tank, a distilled water overflow port is arranged on the process water tank and used for draining water, the high-temperature drying system is connected with the low-temperature drying system through a pipeline, the output end of the drying bin is connected with the high-temperature drying system, the pipeline circulating water pump is arranged between the drying bin and the high-temperature drying system, and an electric flow valve is arranged on the pipeline connected with the high-temperature drying system and the low-temperature drying system.
2. The multi-effect high-temperature overlapping type drying system of claim 1, wherein the low-temperature drying system comprises a first heat pump compressor, a first plate heat exchanger, a second plate heat exchanger, a third plate heat exchanger, a fan and a condenser; one end of the first heat pump compressor is connected with a four-way valve, the four-way valve is connected with the first plate heat exchanger, the other end of the first plate heat exchanger is connected with one end of a fan, the other end of the fan is connected with one end of the second plate heat exchanger through a pipeline, the other end of the second plate heat exchanger is connected with the third plate heat exchanger, and a port of the third plate heat exchanger is connected with a condenser.
3. The multi-effect high-temperature overlapping type drying system of claim 1, wherein a throttle valve is arranged on a connecting pipeline between the fan and the second plate heat exchanger.
4. The multi-effect high-temperature overlapping type drying system of claim 1, wherein the low-temperature drying system absorbs heat from air to supply starting heat energy to the drying system, and the fan, the second plate heat exchanger and the third plate heat exchanger are used in cooperation to realize large-temperature-difference environment operation.
5. The multi-effect high-temperature overlapping type drying system of claim 1, wherein the high-temperature drying system comprises a second heat pump compressor, a fourth plate heat exchanger and a fifth plate heat exchanger; one end of the second heat pump compressor is connected with the second plate heat exchanger, the other end of the second heat pump compressor is connected with the fifth plate heat exchanger, and the third plate heat exchanger is connected with the fourth plate heat exchanger.
6. The multi-effect high-temperature overlapping type drying system of claim 1, wherein the vacuum pump pumps out steam in the drying chamber to generate negative pressure in the drying chamber, and the pumped steam is cooled in two stages to become distilled water and is discharged through the distilled water overflow port.
7. The multi-effect high-temperature overlapping type drying system of claim 1, wherein when the high-temperature drying system converts low heat energy of the low-temperature drying system and steam heat in the drying chamber into high heat energy, the heat is transferred into the licorice chamber through a pipeline circulating water pump, so that the heat is recycled.
8. The multiple-effect high-temperature overlapping type drying system of claim 2, wherein both the first plate heat exchanger and the second plate heat exchanger are multiple-effect evaporation and condensation, and the first plate heat exchanger and the second plate heat exchanger form a double-machine overlapping type heat recycling system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111161058.0A CN113720141A (en) | 2021-09-30 | 2021-09-30 | Multi-effect high-temperature overlapping type drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111161058.0A CN113720141A (en) | 2021-09-30 | 2021-09-30 | Multi-effect high-temperature overlapping type drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN113720141A true CN113720141A (en) | 2021-11-30 |
Family
ID=78685577
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202111161058.0A Pending CN113720141A (en) | 2021-09-30 | 2021-09-30 | Multi-effect high-temperature overlapping type drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN113720141A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200965328Y (en) * | 2006-10-25 | 2007-10-24 | 莫少民 | Superposed type heat-exchanging central conditioner system cooling water residual heat recovery device |
| CN104596225A (en) * | 2015-01-16 | 2015-05-06 | 烟台艾格瑞环保科技有限公司 | Environment-friendly, high-efficiency and energy-saving drying system |
| CN112880313A (en) * | 2021-02-02 | 2021-06-01 | 烟台明辉热泵节能科技有限公司 | Silica gel particle ultralow-water-content high-temperature heat pump drying system and control method |
| CN214000655U (en) * | 2020-12-08 | 2021-08-20 | 格瑞环保科技(深圳)有限公司 | Solid-liquid separation kitchen garbage treatment device |
-
2021
- 2021-09-30 CN CN202111161058.0A patent/CN113720141A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200965328Y (en) * | 2006-10-25 | 2007-10-24 | 莫少民 | Superposed type heat-exchanging central conditioner system cooling water residual heat recovery device |
| CN104596225A (en) * | 2015-01-16 | 2015-05-06 | 烟台艾格瑞环保科技有限公司 | Environment-friendly, high-efficiency and energy-saving drying system |
| CN214000655U (en) * | 2020-12-08 | 2021-08-20 | 格瑞环保科技(深圳)有限公司 | Solid-liquid separation kitchen garbage treatment device |
| CN112880313A (en) * | 2021-02-02 | 2021-06-01 | 烟台明辉热泵节能科技有限公司 | Silica gel particle ultralow-water-content high-temperature heat pump drying system and control method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104771918B (en) | A kind of cold concentration systems based on wet evaporation | |
| CN109095535B (en) | Sewage evaporation concentration device and operation method thereof | |
| CN109626791B (en) | Sludge drying equipment and sludge drying method | |
| CN215062958U (en) | High-efficiency direct-current frequency-conversion cascade hot water unit | |
| CN113720141A (en) | Multi-effect high-temperature overlapping type drying system | |
| CN104713319A (en) | Heat recovery type heat pump drying machine | |
| CN208192103U (en) | A kind of tobacco humidifying machine pumped vacuum systems | |
| CN103083931A (en) | Multiple-effect forced circulation vacuum evaporation system | |
| CN108518886B (en) | White smoke-eliminating high-efficiency smoke hot water type lithium bromide absorption type cold and hot water unit | |
| CN109692490A (en) | Corrosion-resistant falling film evaporator, dilute sulfuric acid concentration systems and its technique and application | |
| CN210004496U (en) | kinds of evaporation process exhaust steam waste heat recovery utilizes system | |
| CN113418320B (en) | Device for raising low-temperature heat source temperature and application method thereof | |
| CN214436542U (en) | Heat pump type waste liquid vacuum evaporation concentration equipment | |
| CN211316644U (en) | High-efficient heating device of low temperature environment | |
| CN210624993U (en) | Ultra-low temperature frequency conversion two-combined-supply unit with refrigerant cooling function | |
| CN209989090U (en) | Heat pump device for high-salinity wastewater treatment | |
| CN109186300B (en) | Waste heat utilization system | |
| CN208860156U (en) | A kind of working medium reclaiming type Condenser Vacuum Pressure maintains and improves system | |
| CN212842498U (en) | Vacuum pulsation drying system based on air source heat pump | |
| CN111039537A (en) | Double-tank dehydration type sludge heat drying system | |
| CN109970125A (en) | Heat pump assembly is used in a kind of processing of high-salt wastewater | |
| CN206256941U (en) | A kind of condensing turbine organic working medium circulating cooling system | |
| CN218936710U (en) | Cold and hot combined supply device | |
| CN2884073Y (en) | Air sucking device used for lithium bromide absorption type air conditioner | |
| CN217781002U (en) | Waste heat recovery type sludge drying system with vortex tube |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20211130 |
|
| RJ01 | Rejection of invention patent application after publication |