JP5737918B2 - Biological treatment-type heat pump system for wastewater treatment equipment, biological treatment-type wastewater treatment equipment provided therewith, and control method for biological treatment-type wastewater treatment equipment heat pump system - Google Patents

Description

  The present invention relates to a heat treatment system for a wastewater treatment facility by a biological treatment method that heats wastewater flowing into a biological treatment tank by a heat pump, a wastewater treatment facility by a biological treatment method provided with the same, and a wastewater treatment facility by a biological treatment method The present invention relates to a method for controlling an industrial heat pump system.

  In a wastewater treatment facility using a biological treatment system, pollutants in wastewater mainly composed of organic matter are decomposed and purified by the action of microorganisms. As the microorganism used for this biological treatment, typically, an aerobic bacterium that operates under an aerobic condition or an anaerobic bacterium that operates under anoxic conditions or almost no oxygen is used. These microorganisms such as aerobic bacteria and anaerobic bacteria are active at a predetermined temperature. Therefore, in a biological treatment tank that biologically treats wastewater, it is necessary to maintain a temperature suitable for the activity of microorganisms.

  FIG. 5 shows a general wastewater treatment facility applied to maintain the biological treatment tank at an appropriate temperature. The wastewater treatment facility 100 is treated by a heat exchanger 101 for heating that heats inflow wastewater with steam supplied from a boiler 103, a biological treatment tank 105 that decomposes pollutants in wastewater using microorganisms, and a biological treatment tank 105. A settling tank 107 for storing the drained water and precipitating sludge, and a discharge pit 109 for storing discharge water after removing the sludge in the settling tank 107 are provided.

  The inflow wastewater is guided to the heat exchanger 101 for heating, and is heated by the steam supplied from the boiler 103 so as to have a desired temperature at which microorganisms are active. The steam that has finished heating the wastewater is recovered as drain water. The waste water heated by the heating heat exchanger 101 is guided to the biological treatment tank 105, and the pollutant is decomposed by the microorganisms active in the biological treatment tank 105. After the biological treatment, the wastewater is guided to the sedimentation tank 107 and the sludge is removed, and then guided to the discharge pit 109 to be discharged into the river and the sea.

  Since this waste water treatment equipment 100 heats waste water using the boiler 103, fossil fuel is used as boiler fuel. Since fossil fuel is used, the exhaust gas after combustion is released to the atmosphere, which is not preferable from the viewpoint of global warming and environmental pollution. Further, even if heating by combustion heat is operated efficiently, the COP (coefficient of performance) does not exceed 1, which is not preferable from the viewpoint of energy saving.

  On the other hand, Patent Document 1 below discloses an invention in which waste water is heated by a heat pump. Use of a heat pump is preferable because the COP can be set to 1 or more and combustion exhaust gas is not released. FIG. 6 shows a wastewater treatment facility 110 by such heat pump heating.

  The waste water treatment facility 110 includes a heat exchanger 101 for heating, a biological treatment tank 105, a sedimentation tank 107, and a discharge pit 109, similarly to the waste water treatment equipment 100 shown in FIG. Furthermore, the waste water treatment facility 110 includes a heat pump 111 instead of the boiler. The hot heat of the heat pump 111 is output to the heating heat exchanger 101 by the hot water circulated by the hot water pump 113. The heat source of the heat pump 111 is recovered heat obtained from the discharged water by the heat recovery heat exchanger 117 provided between the settling tank 107 and the discharge pit 109. That is, chilled water is circulated by the chilled water pump 115 between the recovery heat exchanger 117 and the heat pump 111, and the recovered heat recovered by the chilled water in the heat recovery heat exchanger 117 is heat pump 111. Supplied to.

JP-A-2-214598

  Generally, a heat pump inputs a predetermined energy, recovers heat from a low-temperature heat source, and moves heat to a high temperature side, so there is a certain ratio between the heat recovery amount and the heat output. Therefore, when the temperature or flow rate of the inflow wastewater to be processed changes, the heating amount for maintaining the target heating temperature also changes, and the necessary recovered heat amount changes accordingly.

  However, in the system using the heat pump 111 shown in FIG. 6, the heat recovery is performed even though the required thermal output (heating amount) changes according to the temperature and flow rate of the wastewater flowing into the heat exchanger 101 for heating. The amount of heat recovered in the heat exchanger 117 for use depends on the temperature and flow rate of the discharged effluent, and an imbalance between the necessary heat output and the amount of heat recovered occurs. In this case, there is a problem that the inflow wastewater cannot be maintained at the target heating temperature.

  In some cases, it is desired to use the cool heat of the discharged water that has been recovered by the heat recovery heat exchanger 117 and cooled. In this case, it is necessary to maintain the discharged water cooled by the heat recovery heat exchanger 117 at the target cooling temperature. However, as described above, in the system using the heat pump 111 shown in FIG. 6, the ratio between the heat output and the heat recovery amount cannot be adjusted, so that it is impossible to achieve both the target heating temperature and the target cooling temperature. .

  The present invention has been made in view of such circumstances, and can stably maintain the target heating temperature of wastewater, and / or the target heating temperature of drainage and the target cooling temperature of discharged water. A heat treatment system for wastewater treatment equipment by a biological treatment system capable of stably maintaining both, a wastewater treatment equipment by a biological treatment system provided with the same, and a control method of a heat pump system for wastewater treatment equipment by a biological treatment system The purpose is to provide.

In order to solve the above-mentioned problems, a heat pump system for wastewater treatment equipment by a biological treatment system of the present invention, a wastewater treatment equipment by a biological treatment system provided with the same, and a control method of a heat pump system for wastewater treatment equipment by a biological treatment system Adopts the following means.
That is, the heat pump system for wastewater treatment facilities by the biological treatment system according to the present invention is treated by the heating heat exchanger that heats the wastewater flowing into the biological treatment tank that treats pollutants with microorganisms, and the biological treatment tank. A heat recovery heat exchanger that recovers heat from the discharged water discharged after the heat, and a heat pump that supplies heat to the heating heat exchanger and recovers heat by absorbing heat in the heat recovery heat exchanger A heat pump system for wastewater treatment facilities using a biological treatment system comprising: a heat recovery system connected to the heat recovery side of the heat pump so as to recover heat from another heat source different from the discharged water. A heat recovery amount of the heat recovery heat exchanger, and a heat recovery amount determined from a heating amount for obtaining a target heating temperature of the wastewater to be heated by the heating heat exchanger, and Characterized in that it comprises a control unit for determining the heat recovery amount of the serial by heat recovery system.

The heat pump system of the present invention recovers heat from the effluent after biological treatment in the heat recovery heat exchanger, operates with this recovered heat as a heat source, outputs warm heat, and before the biological treatment in the heat exchanger for heating. Heat the waste water.
The heat pump is operated so as to obtain a target heating temperature of the waste water heated by the heating heat exchanger. When the target heating temperature is determined, the heating amount that is the thermal output of the heat pump is determined, and the necessary heat recovery amount is determined at a predetermined ratio corresponding to the heating amount. Thus, if the heat output of the heat pump is determined, the amount of heat recovery corresponding to this is determined, so if the temperature or flow rate of the waste water to be heated changes, the heat output by the heat pump also changes, and the required amount of heat recovery also changes. .
Therefore, in the present invention, the heat recovery side of the heat pump is provided with another heat recovery system connected so as to recover heat from another heat source different from the discharged water so that heat can be recovered from other than the discharged water. Then, the heat recovery amount of the heat recovery heat exchanger and the heat recovery of another heat recovery system are set so that the heat recovery amount determined from the heating amount for obtaining the target heating temperature of the waste water heated by the heating heat exchanger is obtained. The amount was decided. Thereby, the heat recovery amount can be made to follow the change in the heating amount, and an appropriate heat recovery amount corresponding to the target heating temperature of the waste water can be obtained.

  Furthermore, in the heat pump system for wastewater treatment facilities according to the biological treatment system of the present invention, the separate heat source to which the separate heat recovery system is connected is a cold load.

By using a cold load as another heat source, it is possible to recover the heat from the cold load and at the same time supply the necessary cold heat to the cold load. Thereby, the load of the refrigerator for giving cold heat to the cold load can be reduced, and the efficiency of the entire system including the refrigerator is improved. Preferably, control is performed so that heat is mainly recovered from the cold load, and the shortage is recovered from the discharged water. This is because if such control is performed, the energy consumption of the refrigerator for the cold load can be reduced as much as possible.
Further, it is advantageous in that another heat source can be obtained even when there is no appropriate cooling load around the wastewater treatment facility.

  Furthermore, in the heat pump system for wastewater treatment facilities according to the biological treatment system of the present invention, the separate heat source to which the separate heat recovery system is connected is an unused natural fluid such as seawater or a river.

  By using an unused natural fluid such as seawater or a river as another heat source, it is possible to use natural energy that is originally unused, and to effectively use energy.

  In addition, the heat pump system for wastewater treatment equipment according to the biological treatment system of the present invention is processed in the heating heat exchanger that heats the wastewater flowing into the biological treatment tank that treats pollutants with microorganisms, and the biological treatment tank. A heat recovery heat exchanger that recovers heat from the discharged water discharged later, a heat pump that supplies heat to the heating heat exchanger and recovers heat by absorbing heat in the heat recovery heat exchanger; , A heat pump system for wastewater treatment facilities by a biological treatment system equipped with a heating system of the heat pump, provided with a separate heating system connected to heat another heat load different from the wastewater, After determining the heating amount for obtaining the target heating temperature of the waste water heated by the heating heat exchanger, the target cooling temperature of the discharged water cooled and recovered by the heat recovery heat exchanger is obtained. As the heating amount determined from the heat recovery amount of order, characterized in that it comprises a control unit that determines the heating amount of said another heating system.

The heat pump system of the present invention recovers heat from the effluent after biological treatment in the heat recovery heat exchanger, operates with this recovered heat as a heat source, outputs warm heat, and before the biological treatment in the heat exchanger for heating. Heat the waste water.
The heat pump is operated so as to obtain a target heating temperature of the waste water heated by the heating heat exchanger. When the target heating temperature is determined, the heating amount that is the thermal output of the heat pump is determined, and the necessary heat recovery amount is determined at a predetermined ratio corresponding to the heating amount. However, when it is desired to set the effluent water recovered and cooled by the heat recovery heat exchanger to a predetermined target cooling temperature, the heat recovery amount determined from the target cooling temperature is the heat recovery amount determined from the heating amount described above. It may be different. That is, an unbalance occurs between the heat recovery amount determined from the heating amount for obtaining the target heating temperature and the heat recovery amount for obtaining the target cooling temperature.
Therefore, in the present invention, a separate heating system connected so as to heat a separate thermal load different from the waste water is provided on the heating side of the heat pump, so that other than the waste water can be heated. And after determining the heating amount which obtains the target heating temperature of the waste water heated with the heat exchanger for heating, in order to obtain the target cooling temperature of the discharged water cooled and recovered by the heat exchanger for heat recovery The heating amount of the separate heating system was determined so as to be the heating amount determined from the heat recovery amount. Thereby, the heating amount (heat output) and heat recovery amount (cold output) of the heat pump can be balanced, and the waste water can be heated to the target heating temperature and the discharged water can be cooled to the target cooling temperature.

  Further, in the heat pump system for wastewater treatment equipment according to the biological treatment system of the present invention, a heat exchanger for cooling heat that extracts heat by exchanging heat with the effluent water cooled to the target cooling temperature by the heat recovery heat exchanger. It is characterized by having.

  Since we decided to provide a heat exchanger for cooling that takes out the cold energy by exchanging heat with the effluent water cooled to the target cooling temperature in the heat recovery heat exchanger, It can be used as cold energy for equipment. Specifically, the obtained cold energy can be used as cooling water for a compressor or a cooling air conditioning load.

  A wastewater treatment facility according to the biological treatment system of the present invention includes any one of the heat pump systems described above and a biological treatment tank into which wastewater heated by the heat pump system is guided.

  By using the heat pump system described above, wastewater having a desired target heating temperature is supplied to the biological treatment tank, so that stable biological treatment is possible.

  In addition, the control method of the heat treatment system for wastewater treatment equipment according to the biological treatment system of the present invention includes a heating heat exchanger for heating wastewater flowing into a biological treatment tank that treats pollutants with microorganisms, and the biological treatment tank. A heat recovery heat exchanger that recovers heat from the discharged water that is discharged after being treated, and supplies heat to the heating heat exchanger, and absorbs heat in the heat recovery heat exchanger to recover heat A heat pump system for a wastewater treatment facility using a biological treatment system equipped with a heat pump, wherein the heat recovery side of the heat pump is connected to recover heat from a separate heat source different from the discharged water A separate heat recovery system is provided, and the controller recovers the heat recovery amount so that the heat recovery amount is determined from the heating amount for obtaining the target heating temperature of the wastewater heated by the heating heat exchanger. Wherein the heat recovery amount of exchanger and determines the heat recovery amount of the further heat recovery system.

The heat pump system used in the control method of the present invention recovers heat from the effluent water after biological treatment in the heat recovery heat exchanger, and operates with the recovered heat as a heat source to output warm heat to the heating heat exchanger. Heat the wastewater before biological treatment.
The heat pump is operated so as to obtain a target heating temperature of the waste water heated by the heating heat exchanger. When the target heating temperature is determined, the heating amount that is the thermal output of the heat pump is determined, and the necessary heat recovery amount is determined at a predetermined ratio corresponding to the heating amount. Thus, if the heat output of the heat pump is determined, the amount of heat recovery corresponding to this is determined, so if the temperature or flow rate of the waste water to be heated changes, the heat output by the heat pump also changes, and the required amount of heat recovery also changes. .
Therefore, in the present invention, the heat recovery side of the heat pump is provided with another heat recovery system connected so as to recover heat from another heat source different from the discharged water so that heat can be recovered from other than the discharged water. Then, the heat recovery amount of the heat recovery heat exchanger and the heat recovery of another heat recovery system are set so that the heat recovery amount determined from the heating amount for obtaining the target heating temperature of the waste water heated by the heating heat exchanger is obtained. The amount was decided. Thereby, the heat recovery amount can be made to follow the change in the heating amount, and an appropriate heat recovery amount corresponding to the target heating temperature of the waste water can be obtained.

  In addition, the control method of the heat treatment system for wastewater treatment equipment according to the biological treatment system of the present invention includes a heating heat exchanger for heating wastewater flowing into a biological treatment tank that treats pollutants with microorganisms, and the biological treatment tank. A heat recovery heat exchanger that recovers heat from the discharged water that is discharged after being treated, and supplies heat to the heating heat exchanger, and absorbs heat in the heat recovery heat exchanger to recover heat A heat pump system for a wastewater treatment facility using a biological treatment system equipped with a heat pump that is connected to the heating side of the heat pump so as to heat another heat load different from the wastewater. A system is provided, and after determining a heating amount for obtaining a target heating temperature of the waste water heated by the heating heat exchanger, the effluent water cooled and recovered by the heat recovery heat exchanger So that the heating amount determined from the heat recovery amount for obtaining a target cooling temperature, characterized in that it comprises a control unit that determines the heating amount of said another heating system.

The heat pump system used in the control method of the present invention recovers heat from the effluent water after biological treatment in the heat recovery heat exchanger, and operates with the recovered heat as a heat source to output warm heat to the heating heat exchanger. Heat the wastewater before biological treatment.
The heat pump is operated so as to obtain a target heating temperature of the waste water heated by the heating heat exchanger. When the target heating temperature is determined, the heating amount that is the thermal output of the heat pump is determined, and the necessary heat recovery amount is determined at a predetermined ratio corresponding to the heating amount. However, when it is desired to set the effluent water recovered and cooled by the heat recovery heat exchanger to a predetermined target cooling temperature, the heat recovery amount determined from the target cooling temperature is the heat recovery amount determined from the heating amount described above. It may be different. That is, an unbalance occurs between the heat recovery amount determined from the heating amount for obtaining the target heating temperature and the heat recovery amount for obtaining the target cooling temperature.
Therefore, in the present invention, a separate heating system connected so as to heat a separate thermal load different from the waste water is provided on the heating side of the heat pump, so that other than the waste water can be heated. And after determining the heating amount which obtains the target heating temperature of the waste water heated with the heat exchanger for heating, in order to obtain the target cooling temperature of the discharged water cooled and recovered by the heat exchanger for heat recovery The heating amount of the separate heating system was determined so as to be the heating amount determined from the heat recovery amount. Thereby, the heating amount (heat output) and heat recovery amount (cold output) of the heat pump can be balanced, and the waste water can be heated to the target heating temperature and the discharged water can be cooled to the target cooling temperature.

  According to the present invention, the heat recovery side of the heat pump is provided with another heat recovery system connected so as to recover heat from another heat source different from the discharged water, so that heat can be recovered from other than the discharged water. Because the heat recovery amount of the heat exchanger for heat recovery and the heat recovery amount of the separate heat recovery system are determined so that the heat recovery amount is determined from the target heating temperature of the waste water heated by the heat exchanger. By making the heat recovery amount follow the change in the amount, the target heating temperature of the wastewater can be stably maintained.

  Also, on the heating side of the heat pump, a separate heating system connected to heat a separate thermal load different from the waste water is provided so that other than the waste water can be heated, so that the waste water heated by the heating heat exchanger can be heated. After determining the heating amount to obtain the target heating temperature, the heating amount of the separate heating system is set so that the heating amount is determined from the target cooling temperature of the effluent water recovered and cooled by the heat recovery heat exchanger. Since it was decided, the target heating temperature of the waste water and the target cooling temperature of the discharged water can be stably maintained by balancing the heating amount (heat output) and heat recovery amount (cold output) of the heat pump. it can.

It is the schematic block diagram which showed the waste water treatment facility concerning 1st Embodiment of this invention. It is the control block diagram which showed control of the heat pump of FIG. It is the schematic block diagram which showed the waste water treatment facility concerning 2nd Embodiment of this invention. It is the schematic block diagram which showed the waste water treatment facility concerning 3rd Embodiment of this invention. It is the schematic block diagram which showed the waste water treatment facility using the conventional boiler. It is the schematic block diagram which showed the waste water treatment facility using the conventional heat pump.

Embodiments according to the present invention will be described below with reference to the drawings.
[First Embodiment]
Hereinafter, a first embodiment of the present invention will be described with reference to FIGS. 1 and 2.
FIG. 1 shows a wastewater treatment facility 1A using a biological treatment system according to the present embodiment.

  The wastewater treatment facility 1 </ b> A stores the heat exchanger 3 for heating the inflowing wastewater, the biological treatment tank 5 for decomposing pollutants (organic substances) in the wastewater by microorganisms, and the wastewater treated by the biological treatment tank 5. A settling tank 7 for precipitating sludge and a discharge pit 9 for storing the discharged water after removing the sludge in the settling tank 7. In addition, a heat recovery heat exchanger 11 that recovers heat from the discharged water from the settling tank 7 is provided between the settling tank 7 and the discharge pit 9.

  The heating heat exchanger 3 exchanges heat between the inflow waste water and hot water heated by the heat pump 13 described later. The heating heat exchanger 3 includes a hot water heat transfer tube 3a, and warm water passing through the hot water heat transfer tube 3a and waste water flowing in contact with the outer surface of the hot water heat transfer tube 3a exchange heat. .

  The biological treatment tank 5 decomposes pollutants in the wastewater by microorganisms such as aerobic bacteria that are active under aerobic conditions or anaerobic bacteria that are active under anoxic or almost no oxygen. The inside of the biological treatment tank 5 is maintained at an oxygen concentration required for aerobic bacteria or anaerobic bacteria. Moreover, it is maintained at a temperature suitable for the activity of microorganisms such as aerobic bacteria and anaerobic bacteria. As will be described later, this temperature is obtained by heating the wastewater in the heat exchanger 3 for heating by the heat pump 13.

The sedimentation tank 7 stores the wastewater treated by the biological treatment tank 5 and precipitates sludge. The precipitated sludge is pulled out from below and discharged out of the system. The water present above the settling tank 7 is led to the heat recovery heat exchanger 11 as discharge water.
In addition, in this invention including this embodiment, the thing before processing with the sedimentation tank 7 is called drainage, and what was processed with the sedimentation tank 7 is called discharge water.

  The heat recovery heat exchanger 11 exchanges heat between the discharged water guided from the settling tank 7 and cold water cooled by the heat pump 13 described later. The heat recovery heat exchanger 11 includes a cold water heat transfer tube 11a, and the cold water passing through the inside of the cold water heat transfer tube 11a and the discharged water flowing in contact with the outer surface of the cold water heat transfer tube 11a exchange heat. I do.

  The discharge pit 9 temporarily stores the discharged water after being recovered by the heat recovery heat exchanger 11 and cooled. The discharged water that has flowed out of the discharge pit 9 is discharged into a river or the sea.

Between the heat exchanger 3 for heating and the heat exchanger 11 for heat recovery, a heat pump 13 is provided that exchanges heat with the heat exchangers 3 and 11. With this heat pump 13, heat is recovered by the heat recovery heat exchanger 11, and the heat is output to the heating heat exchanger 3.
The heat pump 13 is a turbo refrigerator. Although not shown, the turbo refrigerator includes a turbo compressor that compresses the refrigerant, a condenser that condenses the refrigerant compressed by the turbo compressor, an expansion valve that expands the condensed liquid refrigerant, and an expanded refrigerant. And an evaporator for evaporating.
The heat pump 13 typically includes a turbo refrigerator using a turbo compressor as in the present embodiment, but other vapor compression heat pumps using a screw type or scroll type compressor. Alternatively, other types such as an absorption refrigerator and an adsorption refrigerator may be used.

  The hot water flowing from the hot water inlet nozzle 13a is heated by the condensation heat that dissipates heat when the refrigerant condenses in the condenser. The heated warm water flows out from the warm water outlet nozzle 13 b, passes through the warm water forward pipe 17, and is led to the warm water heat transfer tube 3 a installed in the heating heat exchanger 3. A warm water return pipe 19 is connected to the downstream side of the heat transfer pipe 3a for warm water, and the warm water after heat exchange is returned to the warm water inlet nozzle 13a. The warm water return pipe 19 is provided with a warm water pump 15, whereby the warm water is circulated between the heat pump 13 and the heating heat exchanger 3.

  A warm water bypass pipe 21 and a warm water bypass valve 23 are provided between the warm water forward pipe 17 and the warm water return pipe 19. The opening degree of the hot water bypass valve 23 is adjusted by the control unit 30. The heating heat exchanger 3 is heated by adjusting the opening degree of the hot water bypass valve 23 and bypassing a part of the hot water from the heat pump 13 from the heating heat exchanger 3 and flowing it to the hot water return pipe 19. The target heating temperature of drainage is adjusted.

  The cold water flowing from the cold water inlet nozzle 13c is cooled by the evaporation heat that absorbs heat when the refrigerant evaporates in the evaporator. The cooled cold water flows out from the cold water outlet nozzle 13d, passes through the cold water forward pipe 25, and is led to the cold water heat transfer tube 11a installed in the heat recovery heat exchanger 11. A chilled water return pipe 27 is connected to the downstream side of the chilled water heat transfer pipe 11a, and the chilled water after heat exchange is returned to the chilled water inlet nozzle 13c. The cold water return pipe 27 is provided with a cold water pump 29, whereby the cold water is circulated between the heat pump 13 and the heat recovery heat exchanger 11.

The cold water forward pipe 25 is provided with a cold water three-way valve 31 for guiding the cold water to the cold load 33. The opening degree of the cold water three-way valve 31 is adjusted by the control unit 30. By adjusting the opening degree of the cold water three-way valve 31, the cold water guided from the heat pump 13 is distributed to the heat recovery heat exchanger 11 side and the cold load 33 side. The cold water branched to the cold load 33 side by the cold water three-way valve 31 passes through the cold load forward pipe 35 and is guided to the cold water forward header 37. The cold water three-way valve 31 may be configured by combining two normal control valves (two-way valves) instead of the three-way valve.
The cooling load 33 is, for example, air conditioning for cooling or cooling water of a compressor, and obtains cooling heat by the cooling water led from the cooling water flow header 37. The cold water after the cold heat is applied to the cold load 33 is guided to the cold water return header 39. The cold heat header 37 and the cold heat return header 39 are connected to a heat source machine (refrigerator) 41 for cold output provided separately, and cold water is circulated by the cold water pump 43 therebetween.
A cold load return pipe 45 is connected to the cold water return header 39, and the cold water joins the cold water return pipe 27 through the cold load return pipe 45 and is guided to the heat pump 13 side.

  Thus, the system for supplying and recovering cold water to the cold load 33, that is, the cold load forward pipe 35 and the cold load return pipe 45 are different from the system for recovering heat from the wastewater by the heat recovery heat exchanger 11. It is a separate heat recovery system.

  The control part 30 performs control which heats inflow wastewater to target heating temperature based on various input data. The control unit 30 includes an inflow drainage temperature Ti and an inflow drainage flow rate Fi before being heated by the heating heat exchanger 3, and a discharge water temperature before flowing out from the settling tank 7 and into the heat recovery heat exchanger 11. To, the cold water temperature (separate heat source temperature) T1 before joining the cold water return pipe 27 through the cold load return pipe 45, and various measurement values of the heat pump 13 such as the heat pump hot water inlet / outlet temperature and the cold water inlet / outlet temperature are input. . The control unit 30 sets the hot water outlet temperature of the heat pump 13 (the temperature of the hot water flowing out from the hot water outlet nozzle 13b) so that the target heating temperature of the waste water is obtained, and the hot water bypass valve 23 and the cold water three-way valve 31 are set. Control the opening.

  FIG. 2 shows a specific configuration of the control unit 30. As shown in the figure, the control unit 30 performs a predetermined calculation with a storage unit 51 in which various characteristics of the heat pump 13 such as output and efficiency according to the cooling water temperature for cooling the condenser of the centrifugal chiller are recorded. Based on the result obtained by the calculation part 53 and the calculation part 53 to perform, the control instruction | indication part 55 which outputs an opening degree command value to the hot water bypass valve 23 and the cold water three-way valve 31, and outputs a warm water outlet preset temperature to the heat pump 13 And.

The calculation unit 53 performs a predetermined calculation based on the data stored in the storage unit 51 and each input value described above. Specifically, necessary heat amount calculation, necessary cooling (heat recovery) amount calculation, heat pump heat output calculation, heat pump cooling output calculation, and the like are performed.
The required heat quantity calculation is performed using the inflow / drainage temperature Ti, the inflow / drainage flow rate Fi, and the target heating temperature of the wastewater. The target heating temperature of the waste water is set as a temperature necessary for maintaining an appropriate temperature in the biological treatment tank 5.
The required cooling (heat recovery) amount calculation is performed to obtain the heat recovery amount necessary for obtaining the necessary heat amount obtained by the required heat amount calculation, and various characteristics of the heat pump stored in the storage unit 51 and the calculation unit 53. It is performed based on the measurement values of the heat pump input to.
In the heat pump heat output calculation, the heat output of the heat pump for outputting the necessary heat amount obtained by the necessary heat amount calculation is calculated.
In the heat pump cooling output calculation, a heat pump cooling output (cold output) corresponding to a heat recovery amount necessary for obtaining the heat pump heat output obtained by the heat pump heat output calculation is calculated.
Based on the results of these calculations, the opening degree of the hot water bypass valve 23 and the heat pump hot water outlet set temperature are obtained.
Moreover, in the calculating part 53, the effluent water temperature To before flowing out from the sedimentation tank 7 and flowing into the heat recovery heat exchanger 11 and the chilled water temperature before joining the chilled water return pipe 27 through the cold load return pipe 45 ( Based on the separate heat source temperature T1, the cold water distribution amount between the heat recovery heat exchanger 11 side and the cold load 33 side is calculated. Based on the calculation result, the opening degree of the cold water three-way valve 31 is determined.

Next, an operation method of the wastewater treatment facility 1A having the above configuration will be described.
The inflow wastewater is guided to the heat exchanger 3 for heating, and the target temperature is set so that the microorganisms in the biological treatment tank 5 are activated by the hot water supplied from the heat pump 13 in the heat exchanger 3 for heating. Heated to heating temperature. At this time, the heat pump 13 outputs a heating amount (heat output) that provides a target heating temperature based on a command from the control unit 30. That is, the heat output of the heat pump 13 is controlled so as to output a heating amount corresponding to the inflow / drainage temperature Ti and the inflow / drainage flow rate Fi. Further, the control unit 30 controls the temperature of the hot water led to the heating heat exchanger 3 by adjusting the opening degree of the hot water bypass valve 23. Specifically, when the hot water temperature is increased, the opening degree of the hot water bypass valve 23 is reduced, and a large amount of hot water is allowed to flow to the heating heat exchanger 3, and when the hot water temperature is decreased, the hot water bypass valve 23 is opened. The degree of bypass is increased to increase the amount of bypass of hot water, and the flow rate of hot water led to the heat exchanger 3 for heating is decreased.

The waste water heated by the heating heat exchanger 3 is guided to the biological treatment tank 5, and the pollutant is decomposed by the microorganisms active in the biological treatment tank 105. The wastewater that has undergone the biological treatment is guided to the settling tank 107, and the precipitated sludge is removed.
The waste water from which the sludge has been removed is guided to the heat recovery heat exchanger 11, cooled by the cold water guided from the heat pump 13, and recovered.

  The heat recovery according to the present embodiment is also performed mainly from the cold load 33, although it is also performed from the heat recovery heat exchanger 11 through which discharged water flows. That is, the chilled water branched by the chilled water three-way valve 31 is led to the chilled load 33 through the chilled load outgoing pipe 35, and is recovered by a separate heat recovery system that is returned to the heat pump 13 through the chilled load return pipe 45. Mainly done. The distribution of the cold water to the heat recovery heat exchanger 11 side and the cold load 33 side is performed by adjusting the opening degree of the cold water three-way valve 31 controlled by the control unit 30. Specifically, the discharge water temperature To before flowing out from the settling tank 7 and flowing into the heat recovery heat exchanger 11 and the cold water temperature before joining the cold water return pipe 27 through the cold load return pipe 45 (another heat source) (Temperature) T1. This calculation mainly recovers heat from the cold load 33 so as to cover the necessary heat recovery amount (necessary cooling output) of the heat pump 13 corresponding to the necessary thermal output (necessary heating amount) output by the heat pump 13, and heats the shortage. The heat is recovered from the recovery heat exchanger 11. Thereby, it can drive | operate so that the energy consumption of the heat-source equipment 41 for cold-heat output may be suppressed to the minimum.

  The discharged water after the heat is recovered and cooled by the heat recovery heat exchanger 11 is guided to the discharge pit 9 and discharged to the river and the sea.

As described above, according to the present embodiment, the following operational effects are obtained.
On the heat recovery side of the heat pump 13, a separate heat recovery system (cold load forward pipe 35 and cold return pipe 45) connected so as to recover heat from the cold load 33, which is a separate heat source different from the discharged water, is provided and discharged. Heat recovery was possible from other than water. Then, the heat recovery amount of the heat recovery heat exchanger 11 and the heat of the separate heat recovery system on the cold load 33 side are set so that the heat recovery amount determined from the target heating temperature of the waste water heated by the heating heat exchanger 3 is obtained. The recovery amount was decided. Thereby, the heat recovery amount can be made to follow the change in the heating amount, and an appropriate heat recovery amount corresponding to the target heating temperature of the waste water can be obtained.

  In addition, by using the cooling load 33 as another heat source, it is possible to recover the heat from the cooling load 33 and at the same time supply necessary cooling heat to the cooling load 33. Thereby, the load of the heat source device 41 for giving cold heat to the cold heat load can be reduced, and the efficiency of the entire system including the heat source device 41 is improved. Furthermore, since heat recovery is mainly performed from the cold load 33 and the shortage is recovered from the discharged water, the energy consumption of the heat source unit 41 can be minimized.

[Second Embodiment]
Next, a second embodiment of the present invention will be described with reference to FIG.
The present embodiment differs from the first embodiment in that the cold load 33 (see FIG. 1) is used as a separate heat source, whereas unused energy such as rivers and seawater is used as a separate heat source. Accordingly, since the other points are the same, the same reference numerals are given and the description thereof is omitted.
As shown in FIG. 3, the wastewater treatment facility 1 </ b> B is connected to a separate heat source forward pipe 36 connected to the cold water three-way valve 31 and a river or the like so as to use natural unused energy such as a river or the sea as a heat source. And a separate heat source return pipe 46 for returning the recovered cold water. The opening degree of the chilled water three-way valve 31 is controlled by the control unit 30 and distributes the chilled water to the heat recovery heat exchanger 11 side and the river side so that the necessary heat recovery amount can be obtained.

As described above, in this embodiment, as in the first embodiment, the heat recovery is performed from another heat source. Therefore, the heat recovery amount can be made to follow the change in the heating amount of the influent wastewater, An appropriate heat recovery amount according to the target heating temperature can be obtained.
In addition, since natural energy that is originally unused such as rivers can be used, energy can be effectively used.
Further, it is advantageous in that a separate heat source can be obtained even when there is no appropriate cooling load 33 around the wastewater treatment facility 1B.

[Third Embodiment]
Next, a third embodiment of the present invention will be described with reference to FIG.
In addition to the first embodiment, the present embodiment is intended to further effectively use the cold energy obtained by the heat recovery heat exchanger 11. Therefore, the same components as those in the first embodiment are denoted by the same reference numerals and the description thereof is omitted.

  As shown in FIG. 4, in the wastewater treatment facility 1 </ b> C of the present embodiment, a warm water three-way valve 50 is provided in the warm water forward pipe 17, and the thermal load forward pipe 52 is branched. A thermal load 54 is connected to the thermal load outgoing pipe 52. Connected to the thermal load 54 is a thermal load return pipe 56 through which hot water is supplied after the thermal heat is supplied by the thermal load. The downstream end of the thermal load return pipe 56 is connected to the hot water return pipe 19 so that the joined hot water is guided to the heat pump 13.

  The opening degree of the hot water three-way valve 50 is controlled by the control unit 30. By controlling the opening degree of the hot water three-way valve 50, the heating heat exchanger 3 is configured to supply the heating load 54 with a heating temperature that exceeds the heating amount required.

  On the downstream side of the heat recovery heat exchanger 11, a cold heat exchanger 58 for obtaining the cold heat of the discharged water is provided. A chilled water heat transfer tube 58 is provided in the chilled heat exchanger 58, and the chilled water flowing in the chilled water heat transfer tube 58a and the effluent water guided from the heat recovery heat exchanger 11 exchange heat. It is like that. The cold water cooled by the discharged water is guided to the cold load 60, and after giving cold heat to the cold load 60, it is returned to the cold heat exchanger 58 again. Examples of the cooling load 60 include compressor cooling water and cooling air conditioning, as in the first embodiment.

  A chilled water bypass pipe 26 and a chilled water bypass valve 28 are provided between the chilled water outgoing pipe 25 that circulates the chilled water between the heat recovery heat exchanger 11 and the cold water return pipe 27. The controller 30 adjusts the opening degree of the cold water bypass valve 28 to control the discharge water temperature T2 flowing out from the heat recovery heat exchanger 11 to the target cooling temperature. Specifically, when the discharge water temperature T2 is lowered, the cold water bypass valve 28 is throttled so that a large amount of cold water flows to the heat recovery heat exchanger 11, and when the discharge water temperature T2 is raised, the cold water bypass valve And the flow rate of cold water flowing to the heat recovery heat exchanger 11 is reduced.

  On the other hand, the operation of the heat pump 13 is controlled by the control unit 30 so that a cooling output (heat recovery amount) that requires the cooling load 60 is obtained. In other words, the heat pump 13 is operated mainly by the cold output to be output to the cold load 60, not by the hot output necessary for heating the waste water. Therefore, when the heat output corresponding to the cold heat output exceeds the heating amount of the waste water, the hot water three-way valve 50 is controlled by an instruction from the control unit 30 so that the hot water flowing to the heat load 54 is increased to adjust the heat output. To.

According to this embodiment mentioned above, there exist the following effects.
On the heating side of the heat pump 13, a separate heating system (the thermal load forward pipe 52 and the thermal load return pipe 56) connected to heat the thermal load 54 different from the waste water is provided so that heat other than the waste water can be heated. . And after determining and ensuring the heating amount which obtains the target heating temperature of the waste_water | drain which heats with the heat exchanger 3 for heating, the target cooling of the discharge water cooled and cooled by the heat exchanger 11 for heat recovery It was decided to determine the flow rate of warm water flowing to the separate heating system so that the heating amount determined from the heat recovery amount for obtaining the temperature. Thereby, the heating amount (heat output) and heat recovery amount (cold output) of the heat pump 13 can be balanced, and the waste water can be heated to the target heating temperature and the discharged water can be cooled to the target cooling temperature. .
In addition, since the heat exchanger 58 for cooling that takes out the cold by exchanging heat with the discharged water cooled to the target cooling temperature by the heat exchanger 11 for heat recovery is provided, the heat exchanger 58 for cooling is obtained. The generated cold energy can be used for the cold load 60.

1A, 1B, 1C Wastewater treatment equipment 3 by biological treatment system Heating heat exchanger 5 Biological treatment tank 7 Precipitation tank 11 Heat recovery heat exchanger 13 Heat pump 30 Control unit 33 Cooling load 35 Cooling load forward piping (separate heat recovery system )
45 Cold load return piping (separate heat recovery system)
52 Outward piping for thermal load (separate heating system)
56 Thermal load return piping (separate heating system)
58 Heat exchanger for cold energy

Claims (8)

A heating heat exchanger for heating wastewater flowing into a biological treatment tank that treats pollutants with microorganisms;
A heat exchanger for heat recovery that recovers heat from the discharged water discharged after being treated in the biological treatment tank;
A heat pump that supplies heat to the heat exchanger for heating and recovers heat by absorbing heat in the heat exchanger for heat recovery;
A heat pump system for wastewater treatment facilities by a biological treatment system equipped with
The heat recovery side of the heat pump is provided with another heat recovery system connected to recover heat from another heat source different from the discharged water,
The heat recovery amount of the heat recovery heat exchanger and the heat of the separate heat recovery system so that the heat recovery amount is determined from the heating amount for obtaining the target heating temperature of the wastewater heated by the heating heat exchanger. A heat pump system for wastewater treatment facilities using a biological treatment system, comprising a control unit for determining a recovery amount.   The heat pump system for wastewater treatment equipment according to claim 1, wherein the separate heat source to which the separate heat recovery system is connected is a cold load.   The heat pump system for wastewater treatment equipment according to claim 1, wherein the separate heat source to which the separate heat recovery system is connected is an unused natural fluid such as seawater or a river. A heating heat exchanger for heating wastewater flowing into a biological treatment tank that treats pollutants with microorganisms;
A heat exchanger for heat recovery that recovers heat from the discharged water discharged after being treated in the biological treatment tank;
A heat pump that supplies heat to the heat exchanger for heating and recovers heat by absorbing heat in the heat exchanger for heat recovery;
A heat pump system for wastewater treatment facilities by a biological treatment system equipped with
The heating side of the heat pump is provided with another heating system connected to heat another temperature load different from the waste water,
In order to obtain the target cooling temperature of the discharged water cooled and recovered by the heat recovery heat exchanger after determining the amount of heating to obtain the target heating temperature of the waste water heated by the heating heat exchanger A heat pump system for wastewater treatment facilities using a biological treatment system, comprising a control unit that determines a heating amount of the separate heating system so as to be a heating amount determined from a heat recovery amount of the biological treatment system.   5. The biological treatment system according to claim 4, further comprising a cold heat exchanger that exchanges heat with the effluent water that has been cooled to the target cooling temperature in the heat recovery heat exchanger to extract cold heat. Heat pump system for wastewater treatment equipment. A heat pump system according to any one of claims 1 to 5,
A biological treatment tank to which waste water heated by the heat pump system is guided;
A wastewater treatment facility using a biological treatment system. A heating heat exchanger for heating wastewater flowing into a biological treatment tank that treats pollutants with microorganisms;
A heat exchanger for heat recovery that recovers heat from the discharged water discharged after being treated in the biological treatment tank;
A heat pump that supplies heat to the heat exchanger for heating and recovers heat by absorbing heat in the heat exchanger for heat recovery;
A method for controlling a heat pump system for wastewater treatment facilities by a biological treatment system comprising:
The heat recovery side of the heat pump is provided with another heat recovery system connected to recover heat from another heat source different from the discharged water,
The heat recovery amount of the heat recovery heat exchanger and the separate heat are set such that the control unit obtains a heat recovery amount determined from the heating amount for obtaining the target heating temperature of the wastewater heated by the heating heat exchanger. A control method for a heat pump system for wastewater treatment facilities by a biological treatment system, wherein the heat recovery amount of a recovery system is determined. A heating heat exchanger for heating wastewater flowing into a biological treatment tank that treats pollutants with microorganisms;
A heat exchanger for heat recovery that recovers heat from the discharged water discharged after being treated in the biological treatment tank;
A heat pump that supplies heat to the heat exchanger for heating and recovers heat by absorbing heat in the heat exchanger for heat recovery;
A method for controlling a heat pump system for wastewater treatment facilities by a biological treatment system comprising:
The heating side of the heat pump is provided with another heating system connected to heat another temperature load different from the waste water,
In order to obtain the target cooling temperature of the discharged water cooled and recovered by the heat recovery heat exchanger after determining the amount of heating to obtain the target heating temperature of the waste water heated by the heating heat exchanger A control method for a heat pump system for wastewater treatment facilities by a biological treatment system, comprising a control unit for determining a heating amount of the separate heating system so as to be a heating amount determined from a heat recovery amount of the biological treatment system.

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