CN210885773U - Separated heat pump sludge low-temperature drying machine - Google Patents
Separated heat pump sludge low-temperature drying machine Download PDFInfo
- Publication number
- CN210885773U CN210885773U CN201921833101.1U CN201921833101U CN210885773U CN 210885773 U CN210885773 U CN 210885773U CN 201921833101 U CN201921833101 U CN 201921833101U CN 210885773 U CN210885773 U CN 210885773U
- Authority
- CN
- China
- Prior art keywords
- temperature
- water
- low
- air
- sludge
- 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.)
- Active
Links
Images
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a disconnect-type heat pump mud low temperature mummification machine. The sludge low-temperature drying machine comprises a closed sludge low-temperature drying machine main body, wherein a sludge drying chamber, an air heat exchange chamber and an air path circulating system are arranged in the sludge low-temperature drying machine main body; the heat pump refrigeration circulating system is arranged outside the sludge low-temperature drying machine main body and is completely isolated from the air path circulating system; the heat pump refrigeration cycle system comprises a condenser, an evaporator, a refrigeration compressor and an expansion valve; a low-temperature dehumidification surface air cooler and a high-temperature heating surface air cooler are arranged in the air heat exchange chamber; the water inlet pipe and the water outlet pipe of the high-temperature heating surface cooler are respectively connected with the water outlet pipe and the water inlet pipe of the condenser to form a water pipeline system A; the water inlet pipe and the water outlet pipe of the low-temperature dehumidification surface cooler are respectively connected with the water outlet pipe and the water inlet pipe of the evaporator to form a water pipeline system B. The separated heat pump sludge low-temperature dryer solves the problem that a heat pump refrigerating system is easy to be corroded by polluted air, can effectively prolong the service life of equipment and improve the stability of a heat pump system.
Description
Technical Field
The utility model belongs to the technical field of the sludge drying, a mud low temperature mummification machine is related to, in particular to disconnect-type heat pump mud low temperature mummification machine.
Background
A low-temperature sludge drying technology by a heat pump is a technology for drying sludge by converting low-level heat energy into high-level heat energy and converting the high-level heat energy into heat energy by means of electric energy consumption by utilizing the heat pump. As shown in fig. 1, the conventional heat pump sludge low-temperature dryer includes a closed sludge low-temperature dryer main body, and a sludge drying chamber (drying box) 15, an air heat exchange chamber 16, an air path circulation system, and a heat pump refrigeration circulation system are disposed in the closed sludge low-temperature dryer main body; a sludge drying chamber (drying box) 15 is internally provided with a conveying mesh belt 14, and the conveying mesh belt 14 carries sludge; a heat pump refrigeration cycle system (also called as a heat pump refrigeration system or a heat pump system) is arranged in the air heat exchange chamber 16; the top air outlet of the sludge drying chamber 15 is connected with the top air inlet of the air heat exchange chamber 16 through an upper ventilation pipeline or an upper ventilation chamber 1, and the bottom air outlet of the air heat exchange chamber 16 is connected with the bottom air inlet of the sludge drying chamber 15 through a lower ventilation pipeline or a lower ventilation chamber 20; the heat pump refrigerating system comprises a refrigerating compressor 2, a condenser 3, an evaporator 4, an expansion valve 5, a refrigerating pipeline and accessories; the air path circulating system comprises an air path circulating fan 13, a lower ventilating pipeline or a lower ventilating chamber 20 and an upper ventilating pipeline or an upper ventilating chamber 1; the air path circulating fan 13 is arranged in the lower ventilation pipeline or the lower ventilation chamber 20; the air circulation loop (i.e. air circulation) is formed by supplying power to the air path circulation fan 13, wherein the air flows from the air heat exchange chamber 16 to the sludge drying chamber 15 in the lower ventilation pipeline or the lower ventilation chamber 20, the air flows from the bottom to the top in the sludge drying chamber 15, the air flows from the sludge drying chamber 15 to the air heat exchange chamber 16 in the upper ventilation pipeline or the upper ventilation chamber 1, the air flows from the top to the bottom in the air heat exchange chamber 16, and the air flows from the air heat exchange chamber 16 to the sludge drying chamber 15 in the lower ventilation pipeline or the lower ventilation chamber 20. The working principle of the existing heat pump sludge low-temperature drying machine is as follows: the sludge is sent into a low-temperature drying chamber (drying box 15) through a transmission mesh belt, dry hot air is introduced into the bottom of the drying box 15 through an air path circulating fan 13, the dry hot air passes through the transmission mesh belt 14 and exchanges heat in the process of contacting with the sludge on the transmission mesh belt 14, so that the moisture in the sludge is taken away, and the sludge is dried; the wet cold air with moisture after heat exchange with the sludge comes out from the top of the drying box 15 and is conveyed to the evaporator 4 of the heat pump refrigerating system through a pipeline; the wet cold air entering the evaporator 4 is acted by the refrigerant of the evaporator 4, the water vapor is condensed into condensed water to be discharged, the wet cold air is further cooled to be dry cold air, the dry cold air enters the condenser 3, the heat is absorbed in the condenser 3 (through heat exchange with the refrigerant) to form dry hot air, and then the dry hot air is circulated to the lower part of the transmission mesh belt 14 through the pipeline and heats the sludge again; the refrigerant circulates between the evaporator 4 and the condenser 3 by the operation of the refrigeration compressor 2, and exchanges heat with air twice.
When air flow (air) of the existing sealed sludge low-temperature dryer circulates in an air path system, the air flow containing corrosiveness is dehumidified and heated by a heat pump system, so that equipment of the heat pump system, such as an evaporator, a condenser, a refrigeration compressor, a refrigeration pipeline, accessories and the like, is seriously corroded, and although some surface treatment processes are adopted to prolong the service life of the accessories of the heat pump system, the effect is not ideal; in addition, dust is accumulated in the system, the surfaces of the evaporator and the condenser need to be regularly washed, and the surfaces of the evaporator and the condenser are easy to damage, corrode and leak, so that the service life of the whole equipment is seriously influenced; in addition, the existing design scheme is easy to cause frequent high-low pressure alarm of the heat pump system due to the instability of the temperature and the humidity of the air of the internal air flow during drying, so that the heat pump system is frequently started and stopped, and the dehumidification efficiency and the system stability of the heat pump system are influenced.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to overcome prior art's not enough, provide one kind and can solve the problem that heat pump refrigeration cycle system easily receives contaminated air corruption, can effectively prolong the life of equipment to improve the disconnect-type heat pump mud low temperature mummification machine of the stability of system.
The utility model aims at realizing through the following technical scheme:
a separated heat pump sludge low-temperature dryer comprises a closed sludge low-temperature dryer main body and a heat pump refrigeration cycle system; a sludge drying chamber (drying box), an air heat exchange chamber and an air path circulating system are arranged in the closed sludge low-temperature drying machine body; the heat pump refrigeration cycle system is arranged outside the sludge low-temperature dryer main body and is completely isolated from the air path circulation system; a conveying mesh belt is arranged in the sludge drying chamber (drying box), and the conveying mesh belt is loaded with sludge; the top air outlet of the sludge drying chamber is connected with the top air inlet of the air heat exchange chamber through an upper ventilation pipeline or an upper ventilation chamber, and the bottom air outlet of the air heat exchange chamber is connected with the bottom air inlet of the sludge drying chamber through a lower ventilation pipeline or a lower ventilation chamber; the air path circulating system comprises an air path circulating fan, a lower ventilating pipeline or a lower ventilating chamber, and an upper ventilating pipeline or an upper ventilating chamber; the heat pump refrigeration cycle system includes: the system comprises a refrigeration compressor, a condenser, an evaporator, an expansion valve, a refrigeration pipeline and accessories; a low-temperature dehumidification surface cooler and a high-temperature heating surface cooler are arranged in an air heat exchange chamber in the sludge low-temperature drying machine body; the water inlet pipe and the water outlet pipe of the high-temperature heating surface cooler are respectively connected with the water outlet pipe and the water inlet pipe of the condenser to form a water pipeline system A; the water inlet pipe and the water outlet pipe of the low-temperature dehumidification surface cooler are respectively connected with the water outlet pipe and the water inlet pipe of the evaporator to form a water pipeline system B; the water pipeline system A is provided with a water pump; the water pipeline system B is provided with a water pump.
Further, a plate heat exchanger is additionally arranged between the water pipeline system A and the water pipeline system B; the water outlet pipe of the low-temperature dehumidification surface cooler is connected with the water inlet pipe of the evaporator through the plate heat exchanger; the water outlet pipe of the high-temperature heating surface cooler is connected with the water inlet pipe of the condenser through the plate heat exchanger.
Furthermore, a three-way proportional valve A is arranged on a water outlet pipe of the high-temperature heating surface cooler, and is divided into two paths behind the three-way proportional valve A, wherein one path is directly connected with an inlet of the liquid storage tank A, and the other path is connected with the inlet of the liquid storage tank A through a plate heat exchanger; the outlet of the liquid storage tank A is connected with the water inlet pipe of the condenser; the liquid storage tank A is provided with an external water source control valve A; a three-way proportional valve B is arranged on a water outlet pipe of the low-temperature dehumidification surface air cooler, and is divided into two paths behind the three-way proportional valve B, wherein one path is directly connected with an inlet of the liquid storage tank B, and the other path is connected with an inlet of the liquid storage tank B through a plate heat exchanger; the outlet of the liquid storage tank B is connected with a water inlet pipe of the evaporator; the liquid storage tank B is provided with an external water source control valve B.
Further, the condenser is a shell-and-tube or double-tube condenser (heat exchanger).
Further, the evaporator is a shell-and-tube or double-tube evaporator (heat exchanger).
Furthermore, the low-temperature dehumidifying surface air cooler and the high-temperature heating surface air cooler are made of corrosion-resistant 316 stainless steel.
Further, the water pipeline system A is provided with a high-temperature water pump; the high-temperature water pump is arranged on a water outlet pipe of the condenser.
Further, the water pipeline system B is provided with a low-temperature water pump; the low-temperature water pump is arranged on a water outlet pipe of the evaporator.
Further, the air path circulating fan is arranged in the lower ventilation pipeline or the lower ventilation chamber.
Furthermore, the peripheral side walls of the sludge drying chamber and the air heat exchange chamber are provided with heat insulation layers.
Further, the sludge drying chamber and the air heat exchange chamber can be connected or not connected.
The utility model discloses a disconnect-type heat pump mud low temperature mummification machine, the theory of operation of its mud low temperature mummification part and wind path circulation part is the same with the theory of operation of current heat pump mud low temperature mummification machine, and the theory of operation of its heat pump refrigeration and air heat transfer part is different with current, and the difference lies in: the heat pump refrigeration cycle system is isolated (separated) from the air path circulation system of the low-temperature sludge drying, a shell-and-tube heat exchanger or a sleeve-type heat exchanger is adopted as a heat exchanger (a condenser and an evaporator) of the heat pump refrigeration cycle system, a refrigerant is adopted to carry out heat exchange with water, then the water is sent into surface coolers (a low-temperature dehumidification surface cooler and a high-temperature heating surface cooler) in an air heat exchange chamber of the main body of the low-temperature sludge drying machine through a water pump and a water pipe, and then the heat exchange is carried out with the air through the surface coolers, so that the purposes of heating and dehumidifying the circulating air in.
The utility model has the advantages that:
the utility model discloses a disconnect-type heat pump mud low temperature mummification machine, heat pump refrigeration cycle system set up outside the mud low temperature mummification machine main part, and wind path circulation system sets up within the mud low temperature mummification machine main part, and heat pump refrigeration cycle system keeps apart with the wind path circulation system of mud low temperature mummification machine completely, has solved the problem that heat pump refrigeration cycle system easily receives contaminated air corruption from this, can effectively prolong the life of heat pump system equipment to improve heat pump system's stability.
Compared with the prior art, the utility model, have following advantage:
1. separating the heat pump refrigeration circulation system from the sludge low-temperature drying machine body, placing the heat pump refrigeration circulation system in other space outside the sludge low-temperature drying machine body, isolating the heat pump refrigeration circulation system from the air path circulation system for low-temperature drying of the sludge, completely isolating the heat pump refrigeration circulation system from the polluted air in the sludge low-temperature drying machine body, and transmitting cold and heat energy into a built-in stainless steel surface cooler (in an air heat exchange chamber) of the sludge low-temperature drying machine body through a water pipe; therefore, the problem that the heat pump refrigeration cycle system is corroded by polluted air is thoroughly solved, and the service life of the heat pump refrigeration system equipment is greatly prolonged.
2. The heat pump refrigeration circulating system is externally arranged, and supplies heat and radiates heat (heat exchange is carried out between the refrigerant and water) for the heat pump refrigeration system through the water supply pipeline circulating system, so that the heat pump refrigeration system is more stable and reliable than supplying heat and radiating heat (heat exchange is carried out between the refrigerant and air) for the heat pump refrigeration system through air airflow in the drying box; thereby improving the stability of the heat pump system.
3. The system is more convenient to overhaul and maintain.
Drawings
FIG. 1 is a schematic structural diagram of a conventional heat pump sludge low-temperature dryer;
FIG. 2 is a schematic structural diagram of a separated heat pump sludge low-temperature drying machine according to embodiment 1 of the present invention;
FIG. 3 is a schematic structural diagram of a separated heat pump sludge low-temperature drying machine according to embodiment 2 of the present invention;
fig. 4 is a schematic structural diagram of a separated heat pump sludge low-temperature drying machine according to embodiment 3 of the present invention.
In the figure: 1. an upper ventilation pipeline or an upper ventilation chamber 2, a refrigeration compressor 3, a condenser 4, an evaporator 5, an expansion valve 6, a plate heat exchanger 7, a high-temperature heating surface cooler 8, a low-temperature dehumidification surface cooler 9, a high-temperature water pump 10, a low-temperature water pump 11, a water pipeline system A12, a water pipeline system B13, an air path circulating fan 14, a conveying mesh belt 15, a sludge drying chamber (drying box) 16, an air heat exchange chamber 17, a heat insulation layer 18, an outer wall 19 close to the inner side of the sludge drying chamber, an outer wall 20 close to the inner side of the air heat exchange chamber, a lower ventilation pipeline or a lower ventilation chamber 21, a three-way proportional valve A22, a three-way proportional valve B23, a liquid storage tank A24, a liquid storage tank B25, an external water
Detailed Description
The present invention will be further described with reference to the accompanying drawings and examples.
Example 1
As shown in fig. 2, the utility model relates to a separated heat pump sludge low-temperature dryer, which comprises a closed sludge low-temperature dryer main body and a heat pump refrigeration cycle system arranged outside the sludge low-temperature dryer main body; a sludge drying chamber (drying box) 15, an air heat exchange chamber 16 and an air path circulating system are arranged in the closed sludge low-temperature drying machine body; the heat pump refrigeration cycle system is arranged outside the sludge low-temperature dryer main body and is completely isolated from the air path circulation system; a sludge drying chamber (drying box) 15 is internally provided with a conveying mesh belt 14, and the conveying mesh belt 14 carries sludge; the top air outlet of the sludge drying chamber 15 is connected with the top air inlet of the air heat exchange chamber 16 through the upper ventilation chamber 1, and the bottom air outlet of the air heat exchange chamber 16 is connected with the bottom air inlet of the sludge drying chamber 15 through the lower ventilation chamber 20; the air path circulating system comprises an upper ventilating chamber 1, a lower ventilating chamber 20 and an air path circulating fan 13; the air path circulating fan 13 is arranged in the lower ventilation pipeline or the lower ventilation chamber 20; the air circulation loop (i.e. air path circulation) is formed by the air flowing from the air heat exchange chamber 16 to the sludge drying chamber 15 in the lower ventilation chamber 20, the air flowing from the bottom to the top in the sludge drying chamber 15, the air flowing from the sludge drying chamber 15 to the air heat exchange chamber 16 in the upper ventilation chamber 1, the air flowing from the top to the bottom in the air heat exchange chamber 16 and the air flowing from the air heat exchange chamber 16 to the sludge drying chamber 15 in the lower ventilation chamber 20 by the power of the air path circulation fan 13. The heat pump refrigeration cycle system includes: the system comprises a refrigeration compressor 2, a condenser 3, an evaporator 4, an expansion valve 5, a refrigeration pipeline and accessories; an air heat exchange chamber 16 in the sludge low-temperature drying machine body is provided with a high-temperature heating surface cooler 7 and a low-temperature dehumidifying surface cooler 8; the water inlet pipe and the water outlet pipe of the high-temperature heating surface cooler 7 are respectively connected with the water outlet pipe and the water inlet pipe of the condenser to form a water pipeline system A11; the water inlet pipe and the water outlet pipe of the low-temperature dehumidification surface cooler are respectively connected with the water outlet pipe and the water inlet pipe of the evaporator to form a water pipeline system B12.
A plate heat exchanger 6 is additionally arranged between the water pipeline system A11 and the water pipeline system B12; the water outlet pipe of the low-temperature dehumidification surface cooler 8 is connected with the water inlet pipe of the evaporator 4 through the plate heat exchanger 6; the water outlet pipe of the high-temperature heating surface cooler 7 is connected with the water inlet pipe of the condenser 3 through the plate heat exchanger 6.
The water pipeline system A11 is provided with a high-temperature water pump 9, and the high-temperature water pump 9 is arranged on a water outlet pipe of the condenser 3; the water pipeline system B12 is provided with a low-temperature water pump 10, and the low-temperature water pump 10 is arranged on a water outlet pipe of the evaporator 4.
The low-temperature dehumidification surface air cooler 8 and the high-temperature heating surface air cooler 7 are made of corrosion-resistant materials 316 stainless steel.
The condenser 3 is a shell-and-tube condenser (heat exchanger). The evaporator 4 is a shell-and-tube evaporator (heat exchanger).
The peripheral side walls of the sludge drying chamber 15 and the air heat exchange chamber 16 are provided with insulating layers 17.
The sludge drying chamber 15 is connected with the air heat exchange chamber 16 (namely, the outer wall 18 close to the inner side of the sludge drying chamber is attached with the outer wall 19 close to the inner side of the air heat exchange chamber).
The utility model discloses a disconnect-type heat pump mud low temperature mummification machine, the concrete implementation method is as follows:
1. moving the heat pump refrigeration cycle system out of the air path cycle system; the heat pump refrigeration cycle system includes: the system comprises an evaporator 4, a condenser 3, a refrigeration compressor 2, an expansion valve 5, a refrigeration pipeline and accessories;
2. a pair of or more than one water-cooled surface air coolers (a low-temperature dehumidification surface air cooler 8 and a high-temperature heating surface air cooler 7) are arranged in an air path circulating system of the sludge low-temperature drying machine; the surface cooler is made of a corrosion-resistant material 316 stainless steel; a heat exchange water pipeline system of the high-temperature heating surface cooler 7 is communicated with a heat exchange water pipeline system of the condenser 3 to form a water pipeline system A; the heat exchange water pipeline system of the low-temperature dehumidification surface cooler 8 is communicated with the heat exchange water pipeline system of the evaporator 4 to form a water pipeline system B;
3. the condenser of the heat pump refrigeration cycle system is cooled by cold water, and can be a shell-tube heat exchanger or a sleeve-tube heat exchanger, the temperature of the cold water rises while the condenser (heat exchanger) is cooled, the cold water is changed into high-temperature water, the high-temperature water enters a high-temperature heating surface cooler of a sludge low-temperature dryer through a water pipeline system A, and the high-temperature water is changed into cold water after heat exchange and cooling and flows back to the condenser;
4. the evaporator of the heat pump refrigeration circulating system adopts hot water for heat supply, and can be a shell-and-tube heat exchanger or a sleeve-type heat exchanger, when the hot water transfers heat to the evaporator (the heat exchanger), the water temperature is reduced to become low-temperature water, the low-temperature water enters a low-temperature dehumidification surface air cooler of the sludge low-temperature dryer through the other water pipeline system B, and the low-temperature dehumidification surface air cooler is changed into hot water after heat exchange and temperature rise and then flows back to the evaporator;
5. a plate heat exchanger is additionally arranged between the water pipeline system A and the water pipeline system B: before the hot water pipeline system A flows back to the condenser, the water is cooled through the plate heat exchanger; before the water returns to the evaporator through the water pipeline system B, the temperature of the water is raised through the plate heat exchanger.
6. Under the action of the refrigeration compressor 2, the refrigerant circulates between the evaporator 4 and the condenser 3 and exchanges heat with water twice (the refrigerant enters the evaporator 4 after coming out of the refrigeration compressor 2, and after the refrigerant exchanges heat with hot water in the evaporator 4 for the first time, the temperature of the refrigerant rises, enters the condenser 3 through the expansion valve 5, and after the refrigerant exchanges heat with cold water in the condenser 3 for the second time, the temperature of the refrigerant is reduced, and the refrigerant returns to the refrigeration compressor 2. the circulation is carried out).
The utility model discloses a disconnect-type heat pump mud low temperature mummification machine, the theory of operation of its mud low temperature mummification part and wind path circulation part is the same with the theory of operation of current heat pump mud low temperature mummification machine, and the theory of operation of its heat pump refrigeration and air heat transfer part is different with current, and the difference lies in: the heat pump refrigeration cycle system is isolated (separated) from the air path circulation system of the sludge low-temperature drying, a shell-and-tube heat exchanger or a sleeve-type heat exchanger is adopted as a heat exchanger (an evaporator 4 and a condenser 3) of the heat pump refrigeration cycle system, heat exchange is carried out between a refrigerant and water, then the water is sent into surface air coolers (a low-temperature dehumidification surface air cooler 8 and a high-temperature heating surface air cooler 7) in an air heat exchange chamber of the heat pump sludge low-temperature drying machine main body through a water pump and a water pipe, and heat exchange is carried out between the water and the air through the surface air coolers, so that the purposes of heating and dehumidifying.
The utility model discloses a disconnect-type heat pump mud low temperature mummification machine, heat pump refrigeration cycle system set up outside the mud low temperature mummification machine main part, and wind path circulation system sets up within the mud low temperature mummification machine main part, and heat pump refrigeration cycle system keeps apart with the wind path circulation system of mud low temperature mummification machine completely, has solved the problem that heat pump refrigeration cycle system easily receives contaminated air corruption from this, can effectively prolong the life of equipment to improve system's stability.
The utility model discloses a disconnect-type heat pump mud low temperature mummification machine compares with current heat pump mud low temperature mummification machine, has following advantage:
1. separating the heat pump refrigeration circulation system from the sludge low-temperature drying machine body, placing the heat pump refrigeration circulation system in other space outside the sludge low-temperature drying machine body, isolating the heat pump refrigeration circulation system from the air path circulation system for low-temperature drying of the sludge, completely isolating the heat pump refrigeration circulation system from the polluted air in the sludge low-temperature drying machine body, and transmitting cold and heat energy into a built-in stainless steel surface cooler (in an air heat exchange chamber) of the sludge low-temperature drying machine body through a water pipe; therefore, the problem that the heat pump refrigeration cycle system is corroded by polluted air is thoroughly solved, and the service life of the heat pump refrigeration system equipment is greatly prolonged.
2. The system is more convenient to overhaul and maintain.
Example 2
As shown in fig. 3, the low-temperature drying machine for separated heat pump sludge of this embodiment is basically the same as the low-temperature drying machine for separated heat pump sludge of embodiment 1, except that:
a three-way proportional valve A21 is additionally arranged on a water outlet pipe of the high-temperature heating surface cooler 7, and is divided into two paths behind the three-way proportional valve A21, wherein one path is directly connected with an inlet of a liquid storage tank A23, and the other path is connected with an inlet of the liquid storage tank A23 through a plate heat exchanger 6; the outlet of the liquid storage tank A23 is connected with the water inlet pipe of the condenser 3; the liquid storage tank A23 is provided with an external water source control valve A25; a three-way proportional valve B22 is additionally arranged on a water outlet pipe of the low-temperature dehumidification surface air cooler 8, the water outlet pipe is divided into two paths behind the three-way proportional valve B22, one path is directly connected with an inlet of a liquid storage tank B24, and the other path is connected with the inlet of the liquid storage tank B24 through a plate heat exchanger 6; the outlet of the liquid storage tank B24 is connected with the water inlet pipe of the evaporator 4; the liquid storage tank B24 is provided with an external water source control valve B26.
The water flow entering the plate heat exchanger 6 is controlled by a three-way proportional valve A21 in a hot water pipeline system A, and is cooled by the plate heat exchanger 6 before converging to a main water pipe, and then enters a liquid storage tank A23; the water flow entering the plate heat exchanger 6 is controlled by a three-way proportional valve B22 in the water pipeline system B, and the water is heated by the plate heat exchanger 6 before converging to a main water pipe and then enters a liquid storage tank B24; by adjusting the water flow entering the plate heat exchanger 6, the water temperature entering the evaporator 4 and the condenser 3 can be effectively controlled, thereby improving the heat efficiency and the stability of the heat pump system.
The utility model discloses a disconnect-type heat pump mud low temperature mummification machine compares with current heat pump mud low temperature mummification machine, has following advantage:
1. separating the heat pump refrigeration circulation system from the sludge low-temperature drying machine body, placing the heat pump refrigeration circulation system in other space outside the sludge low-temperature drying machine body, isolating the heat pump refrigeration circulation system from the air path circulation system for low-temperature drying of the sludge, completely isolating the heat pump refrigeration circulation system from the polluted air in the sludge low-temperature drying machine body, and transmitting cold and heat energy into a built-in stainless steel surface cooler (in an air heat exchange chamber) of the sludge low-temperature drying machine body through a water pipe; therefore, the problem that the heat pump refrigeration cycle system is corroded by polluted air is thoroughly solved, and the service life of the heat pump refrigeration system equipment is greatly prolonged.
2. The heat pump refrigeration circulating system is externally arranged, and supplies heat and radiates heat (heat exchange is carried out between the refrigerant and water) to the refrigeration system through the water supply pipeline circulating system, so that the heat pump refrigeration circulating system is more stable and reliable than supplying heat and radiating heat (heat exchange is carried out between the refrigerant and air) to the refrigeration system through airflow air in the drying box; thereby improving the stability of the heat pump system.
3. The thermal efficiency is improved.
4. The system is more convenient to overhaul and maintain.
Example 3
As shown in fig. 4, the low-temperature drying machine for separated heat pump sludge of this embodiment is basically the same as the low-temperature drying machine for separated heat pump sludge of embodiment 1, except that:
the sludge drying chamber 15 is not connected with the air heat exchange chamber 16 (namely, a gap is left between the outer wall 18 close to the inner side of the sludge drying chamber and the outer wall 19 close to the inner side of the air heat exchange chamber, and the gaps are not attached); the top air outlet of the sludge drying chamber 15 is connected with the top air inlet of the air heat exchange chamber 16 through an upper ventilation pipeline 1 (gaps are reserved between the upper ventilation pipeline 1 and the top of the sludge drying chamber 15 and between the upper ventilation pipeline 1 and the top of the air heat exchange chamber 16); the bottom air outlet of the air heat exchange chamber 16 is connected with the bottom air inlet of the sludge drying chamber 15 through a lower ventilation pipeline 20 (gaps are reserved between the lower ventilation pipeline 20 and the top of the sludge drying chamber 15 and between the lower ventilation pipeline 20 and the top of the air heat exchange chamber 16); the air path circulating system comprises an upper ventilating pipeline 1, a lower ventilating pipeline 20 and an air path circulating fan 13; the air path circulating fan 13 is arranged in the lower ventilation pipeline 20; an air circulation loop is formed by supplying power through the air path circulating fan 13, wherein air flowing from the air heat exchange chamber 16 to the sludge drying chamber 15 in the lower ventilation pipeline 20, air flowing from the bottom to the top in the sludge drying chamber 15, air flowing from the sludge drying chamber 15 to the air heat exchange chamber 16 in the upper ventilation pipeline 1, air flowing from the top to the bottom in the air heat exchange chamber 16 and air flowing from the air heat exchange chamber 16 to the sludge drying chamber 15 in the lower ventilation pipeline 20. The condenser 3 is a double-pipe condenser (heat exchanger); the evaporator 4 is a double pipe evaporator (heat exchanger).
Claims (10)
1. A separated heat pump sludge low-temperature dryer is characterized by comprising a closed sludge low-temperature dryer main body and a heat pump refrigeration cycle system; a sludge drying chamber, an air heat exchange chamber and an air path circulating system are arranged in the closed sludge low-temperature drying machine body; the heat pump refrigeration cycle system is arranged outside the sludge low-temperature dryer main body and is completely isolated from the air path circulation system; a conveying mesh belt is arranged in the sludge drying chamber, and sludge is loaded on the conveying mesh belt; the top air outlet of the sludge drying chamber is connected with the top air inlet of the air heat exchange chamber through an upper ventilation pipeline or an upper ventilation chamber, and the bottom air outlet of the air heat exchange chamber is connected with the bottom air inlet of the sludge drying chamber through a lower ventilation pipeline or a lower ventilation chamber; the air path circulating system comprises an air path circulating fan, a lower ventilating pipeline or a lower ventilating chamber, and an upper ventilating pipeline or an upper ventilating chamber; the heat pump refrigeration cycle system includes: the system comprises a refrigeration compressor, a condenser, an evaporator, an expansion valve, a refrigeration pipeline and accessories; a low-temperature dehumidification surface cooler and a high-temperature heating surface cooler are arranged in an air heat exchange chamber in the sludge low-temperature drying machine; the water inlet pipe and the water outlet pipe of the high-temperature heating surface cooler are respectively connected with the water outlet pipe and the water inlet pipe of the condenser to form a water pipeline system A; the water inlet pipe and the water outlet pipe of the low-temperature dehumidification surface cooler are respectively connected with the water outlet pipe and the water inlet pipe of the evaporator to form a water pipeline system B; the water pipeline system A is provided with a water pump; the water pipeline system B is provided with a water pump.
2. The separated heat pump sludge low-temperature drying machine according to claim 1, wherein a plate heat exchanger is additionally arranged between the water pipeline system A and the water pipeline system B; the water outlet pipe of the low-temperature dehumidification surface cooler is connected with the water inlet pipe of the evaporator through the plate heat exchanger; the water outlet pipe of the high-temperature heating surface cooler is connected with the water inlet pipe of the condenser through the plate heat exchanger.
3. The separated heat pump sludge low-temperature dryer as claimed in claim 2, wherein a three-way proportional valve A is arranged on a water outlet pipe of the high-temperature heating surface cooler, and is divided into two paths after the three-way proportional valve A, wherein one path is directly connected with an inlet of the liquid storage tank A, and the other path is connected with the inlet of the liquid storage tank A through the plate heat exchanger; the outlet of the liquid storage tank A is connected with the water inlet pipe of the condenser; the liquid storage tank A is provided with an external water source control valve A; a three-way proportional valve B is arranged on a water outlet pipe of the low-temperature dehumidification surface air cooler, and is divided into two paths behind the three-way proportional valve B, wherein one path is directly connected with an inlet of the liquid storage tank B, and the other path is connected with an inlet of the liquid storage tank B through a plate heat exchanger; the outlet of the liquid storage tank B is connected with a water inlet pipe of the evaporator; the liquid storage tank B is provided with an external water source control valve B.
4. The separated heat pump sludge low-temperature drying machine according to claim 1, 2 or 3, wherein the condenser is a shell-and-tube or double-tube heat exchanger; the evaporator is a shell-and-tube or double-tube heat exchanger.
5. The separated heat pump sludge low-temperature drying machine as claimed in claim 1, 2 or 3, wherein the low-temperature dehumidifying surface cooler and the high-temperature heating surface cooler are made of corrosion-resistant 316 stainless steel.
6. The separated heat pump sludge low-temperature drying machine according to claim 1, 2 or 3, wherein the water pipeline system A is provided with a high-temperature water pump; the high-temperature water pump is arranged on a water outlet pipe of the condenser.
7. The separated heat pump sludge low-temperature drying machine according to claim 1, 2 or 3, wherein the water pipeline system B is provided with a low-temperature water pump; the low-temperature water pump is arranged on a water outlet pipe of the evaporator.
8. The separated heat pump sludge low-temperature drying machine as claimed in claim 1, 2 or 3, wherein the air path circulating fan is arranged in the lower ventilation pipeline or the lower ventilation chamber.
9. The separated heat pump sludge low-temperature dryer as claimed in claim 1, 2 or 3, wherein the peripheral side walls of the sludge drying chamber and the air heat exchange chamber are provided with insulating layers.
10. The separated heat pump sludge low-temperature dryer as claimed in claim 1, 2 or 3, wherein the sludge drying chamber is connected or not connected with the air heat exchange chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921833101.1U CN210885773U (en) | 2019-10-29 | 2019-10-29 | Separated heat pump sludge low-temperature drying machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921833101.1U CN210885773U (en) | 2019-10-29 | 2019-10-29 | Separated heat pump sludge low-temperature drying machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210885773U true CN210885773U (en) | 2020-06-30 |
Family
ID=71320686
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921833101.1U Active CN210885773U (en) | 2019-10-29 | 2019-10-29 | Separated heat pump sludge low-temperature drying machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210885773U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110590116A (en) * | 2019-10-29 | 2019-12-20 | 上海同臣环保有限公司 | Separated heat pump sludge low-temperature drying machine |
-
2019
- 2019-10-29 CN CN201921833101.1U patent/CN210885773U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110590116A (en) * | 2019-10-29 | 2019-12-20 | 上海同臣环保有限公司 | Separated heat pump sludge low-temperature drying machine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110590116A (en) | Separated heat pump sludge low-temperature drying machine | |
| CN103900184A (en) | Water cooling medium three-pipe refrigerating and heating air-conditioning system | |
| CN105546876A (en) | Drying dehumidifier | |
| CN103983013A (en) | Novel frostless air source heat pump water heater | |
| CN105135739A (en) | Multifunctional heat pump type evaporative condensing air-conditioning unit | |
| CN210885773U (en) | Separated heat pump sludge low-temperature drying machine | |
| CN102908879B (en) | A kind of energy-efficient air dehumidification system | |
| CN102777989A (en) | Heat pump air-conditioning unit system suitable for high-humidity low-temperature environment of underground hydropower station cavern | |
| CN212253005U (en) | Anti-freezing type indirect evaporative cooling air conditioning unit | |
| CN111594962B (en) | Energy-saving indirect evaporative cooling air conditioning unit with fluorine pump and control method | |
| CN212253004U (en) | Two-stage indirect evaporative cooling air conditioning unit | |
| CN210292562U (en) | Air-source heat pump closed-loop dehumidification drying unit | |
| CN205980700U (en) | Responsibility is dodged all to heat of high -efficient heat recovery | |
| CN207515080U (en) | A kind of dehumidification device with heat pump | |
| CN105859093B (en) | A kind of low-power consumption sludge method of vacuum freeze drying that energy regenerating utilizes | |
| CN102734973A (en) | Special dual-temperature high efficiency water source heat pump unit for capillary radiation air conditioning system | |
| CN214308097U (en) | Integral vacuum type heat pump drying energy-saving device | |
| CN109186245A (en) | A kind of high-temperature dry air circulation energy-saving system | |
| CN211112813U (en) | Heat pump clothes dryer | |
| CN213514206U (en) | Energy-saving indirect evaporative cooling air conditioning unit with fluorine pump | |
| CN210220562U (en) | Tunnel type composite heat pump dehumidification drying system with heat pipe heat recovery function | |
| CN209857691U (en) | Intelligent control compact dry-wet combined evaporation type air cooler | |
| CN210717915U (en) | Industrial air cooler | |
| CN210220227U (en) | Embedded dryer and drying room with secondary waste heat recovery function | |
| CN206522889U (en) | Binary integrated combined-type refrigerated air-conditioning system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |