JP5766453B2 - Hot water cleaning system and hot water cleaning method - Google Patents

Description

  The present invention relates to a warm water cleaning system and a warm water cleaning method for cleaning an object to be processed such as a used film using warm water.

  Generally, a warm water cleaning system for cleaning an object to be processed using warm water set to 90 ° C. or higher is known. Patent Document 1 listed below discloses a method of treating a used film as an object to be processed by heating a chemical solution, which is an aqueous sodium hydroxide solution to which polyethylene glycol ether is added, to 90 ° C. with a heater.

JP 2001-228594 A

In Patent Document 1, a heater is used to obtain a chemical solution at 90 ° C., but there is a warm water cleaning system using warm water heated by a boiler as shown in FIGS.
The hot water cleaning system 100 shown in FIG. 3 has a chemical distillation cooling device 101 that preheats well water, a hot water tank 103 that heats well water using a boiler and stores warm water, and a chemical solution obtained by mixing hot water and chemicals. A film cleaning device 105 for cleaning and a waste water treatment facility 107 for processing waste water after film cleaning are provided.
Well water derived from the external environment is heated from about 16 ° C. to about 30 ° C. by a chemical distillation cooling device 101 that cools the distilled chemical for use in film cleaning, and the hot water tank 103 is heated by steam obtained in the boiler. To about 95 ° C. The warm water heated to about 95 ° C. is mixed with chemicals in the film cleaning device 105 and then the film is cleaned. After the temperature is lowered to about 80 ° C., the water is discharged as waste water after cleaning. The waste water after washing at about 80 ° C. is cooled to about 30 ° C. by well water, then led to the waste water treatment facility 107 and finally discharged to the outside. Moreover, well water after cooling the drainage after washing at about 80 ° C. is also discharged to the outside.

  The hot water cleaning system 110 shown in FIG. 4 is different only in that the chemical distillation cooling device 101 of the hot water cleaning system 100 shown in FIG. 3 is omitted, and the others are the same.

However, since the hot water cleaning systems 100 and 110 shown in FIGS. 3 and 4 heat well water using a boiler, it is necessary to use a large amount of fossil fuel, and thus there is a problem that CO2 emissions are large. . In particular, when preheating using the chemical distillation cooling apparatus 101 is not performed as shown in FIG. 4, it is necessary to heat from about 16 ° C. to 95 ° C. which is the environmental temperature of the well water. Emissions increase.
In addition, although well water is used to cool the wastewater after washing after being used in the film washing apparatus 105, it is necessary to use a large amount of well water to cool from about 80 ° C to about 30 ° C. There will be a heavy environmental impact.
Furthermore, the heat of waste water after washing at about 80 ° C. is wasted to the outside, which is not preferable from the viewpoint of energy efficiency.

  This invention is made | formed in view of such a situation, Comprising: It aims at providing the warm water washing | cleaning system and warm water washing | cleaning method which can manufacture warm water efficiently while reducing the heating amount by a boiler. .

In order to solve the above problems, the hot water cleaning system and the hot water cleaning method of the present invention employ the following means.
That is, the hot water cleaning system according to the present invention cleans an object to be processed using a boiler heating unit that heats cleaning water with steam obtained from a boiler, and the heated cleaning water obtained in the boiler heating unit. A first heat exchanger that heats the cleaning water supplied to the boiler heating unit by the post-cleaning drainage discharged from the hot water cleaning device, and the first heat exchanger The second heat exchanger that heats the heat source water with the waste water after washing discharged from the exchanger, and the heat source water heated by the second heat exchanger operates as a heat source and is heated by the first heat exchanger. A heat pump for heating the cleaning water, and the cleaning water heated by the heat pump is supplied to the boiler heating unit.

The cleaning water supplied to the boiler heating unit by the waste water discharged from the hot water cleaning device is heated by the first heat exchanger, and the heat source water is secondly discharged by the waste water discharged from the first heat exchanger. It was decided to heat with a heat exchanger. Thereby, it is possible to effectively recover heat from the waste water after washing discharged from the hot water washing apparatus, and at the same time to lower the temperature of the waste water after washing. Accordingly, it is possible to reduce or eliminate as much as possible the amount of water used for cooling the waste water after washing when discharged to the outside.
Further, the heat pump is operated using the heat source water heated by the second heat exchanger as a heat source, and the cleaning water heated by the first heat exchanger is further heated. Thereby, the cleaning water can be heated to a high temperature with a high COP (coefficient of performance).
In addition, since the cleaning water is supplied to the boiler heating unit after being heated by the first heat exchanger and the heat pump, the heating amount in the boiler heating unit can be reduced. Thereby, the amount of heat supplied to the boiler can be reduced, and the fuel cost and the CO2 emission amount can be reduced.

  Furthermore, the hot water cleaning system of the present invention includes a third heat exchanger that heats the cleaning water before being supplied to the first heat exchanger by the post-cleaning drainage discharged from the second heat exchanger, Washing water heated by the third heat exchanger is supplied to the first heat exchanger.

Since the cleaning water is heated by the third heat exchanger by the waste water discharged from the second heat exchanger, the temperature of the waste water after cleaning can be further reduced, and the amount of cooling water used can be further increased. It can be reduced or eliminated.
Further, since the cleaning water heated by the third heat exchanger is supplied to the first heat exchanger, it can be used for hot water cleaning even when the temperature of the cleaning water is low.

  Moreover, the hot water cleaning method of the present invention cleans an object to be processed using a boiler heating unit that heats cleaning water with steam obtained from a boiler, and the cleaning water that is heated in the boiler heating unit. In the hot water cleaning method by the hot water cleaning system comprising a hot water cleaning device, the hot water cleaning system heats cleaning water supplied to the boiler heating unit by post-cleaning drainage discharged from the hot water cleaning device. A heat exchanger, a second heat exchanger that heats the heat source water with the waste water after washing discharged from the first heat exchanger, and the heat source water heated by the second heat exchanger operates as a heat source, A heat pump for heating the cleaning water heated by the first heat exchanger, and supplying the cleaning water heated by the heat pump to the boiler heating unit.

The cleaning water supplied to the boiler heating unit by the waste water discharged from the hot water cleaning device is heated by the first heat exchanger, and the heat source water is secondly discharged by the waste water discharged from the first heat exchanger. It was decided to heat with a heat exchanger. Thereby, it is possible to effectively recover heat from the waste water after washing discharged from the hot water washing apparatus, and at the same time to lower the temperature of the waste water after washing. Accordingly, it is possible to reduce or eliminate as much as possible the amount of water used for cooling the waste water after washing when discharged to the outside.
Further, the heat pump is operated using the heat source water heated by the second heat exchanger as a heat source, and the cleaning water heated by the first heat exchanger is further heated. Thereby, the cleaning water can be heated to a high temperature with a high COP (coefficient of performance).
In addition, since the cleaning water is supplied to the boiler heating unit after being heated by the first heat exchanger and the heat pump, the heating amount in the boiler heating unit can be reduced. Thereby, the amount of heat supplied to the boiler can be reduced, and the fuel cost and the CO2 emission amount can be reduced.

  Furthermore, in the warm water cleaning method of the present invention, the warm water cleaning system heats the cleaning water before being supplied to the first heat exchanger by the post-cleaning drainage discharged from the second heat exchanger. A heat exchanger is provided, and cleaning water heated by the third heat exchanger is supplied to the first heat exchanger.

Since the cleaning water is heated by the third heat exchanger by the waste water discharged from the second heat exchanger, the temperature of the waste water after cleaning can be further reduced, and the amount of cooling water used can be further increased. It can be reduced or eliminated.
Further, since the cleaning water heated by the third heat exchanger is supplied to the first heat exchanger, it can be used for hot water cleaning even when the temperature of the cleaning water is low.

According to the present invention, heat is recovered from the waste water after washing by the first heat exchanger and the washing water is heated, and the heat pump is heated using the heat source water that is recovered from the waste water after washing by the second heat exchanger and heated. Since the cleaning water is further heated by operating, the thermal efficiency can be improved. Further, the heat recovery and heating by the heat pump can reduce the amount of heat supplied to the boiler, and the boiler fuel cost and CO2 emission can be reduced.
Moreover, since the waste water after washing can be cooled by the first heat exchanger and the second heat exchanger, the amount of water used for cooling the waste water after washing can be reduced or eliminated as much as possible.
Furthermore, since the cleaning water is heated by the third heat exchanger by the waste water discharged from the second heat exchanger, the temperature of the waste water after cleaning can be further reduced, and the amount of water used for cooling is reduced. Can be further reduced or eliminated.
Further, since the cleaning water heated by the third heat exchanger is supplied to the first heat exchanger, it can be used for hot water cleaning even when the temperature of the cleaning water is low.

1 is a schematic configuration diagram illustrating a hot water cleaning system according to a first embodiment of the present invention. It is the schematic block diagram which showed the hot water washing | cleaning system concerning 2nd Embodiment of this invention. It is the schematic block diagram which showed the warm water washing | cleaning system which is a related technique of this invention. It is the schematic block diagram which showed the hot water washing | cleaning system which is the other related technique of this invention.

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 FIG.
In the present embodiment, a hot water cleaning system 1 for cleaning a used film will be described as an example. The hot water washing system 1 is a chemical distillation cooling device 3 that preheats well water, a warm water tank (boiler heating unit) 5 that heats well water with a boiler and stores warm water, and a chemical solution that mixes warm water and chemicals. A film cleaning device (hot water cleaning device) 7 for cleaning and a waste water treatment facility 9 for processing waste water after film cleaning are provided.

Further, a first heat exchanger 11 and a second heat exchanger 12 are provided between the film cleaning device 7 and the waste water treatment facility 9 for recovering heat from the post-cleaning waste water discharged from the film cleaning device 7. ing.
In the first heat exchanger 11, the washed waste water discharged from the film cleaning device 7 and the cleaning water guided from the chemical distillation cooling device 3 by the pressure pump 15 are heat-exchanged. In the second heat exchanger 12, the washed waste water that has flowed out of the first heat exchanger 11 and the heat source water of the heat pump 17 described later are heat-exchanged.

Furthermore, the hot water cleaning system 1 of the present embodiment includes a heat pump 17 for heating the cleaning water. The heat pump 17 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. As the turbo compressor, an electric turbo compressor driven by an electric motor supplied with electric power from an inverter device and having a variable rotation frequency is preferable.
The heat pump 17 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 may be used.

  The heat source water recovered by the second heat exchanger 12 is supplied to the heat source side of the heat pump 17. The heat source water is circulated between the second heat exchanger 12 and the evaporator of the heat pump 17 by the heat source water pump 19. A three-way valve 21 is provided on the upstream side of the heat source water pump 19, and the heat source water temperature guided to the heat pump 17 by adjusting the flow rate flowing through the heat source water bypass passage 23 that bypasses the second heat exchanger 12. Is to control. Instead of the three-way valve 21, two two-way valves may be combined.

  Washing water that has been subjected to heat exchange in the first heat exchanger 11 is guided to the hot water side that is the heat output side of the heat pump 17. The washing water is guided from the first heat exchanger 11 to the condenser of the heat pump 17 by the hot water pump 25 and is heated by the heat pump 17. A three-way valve 27 is provided on the upstream side of the hot water pump 25. The three-way valve 27 adjusts the flow rate through the hot water bypass passage 29 that returns a part of the cleaning water heated by the heat pump 17 to the heat pump 17 without being guided to the hot water tank 5. The temperature of the cleaning water led to the hot water tank 5 is controlled to a desired value by adjusting the flow rate flowing through the hot water bypass passage 29 by the three-way valve 27. Instead of the three-way valve 27, two two-way valves may be combined.

  A cooling heat exchanger 31 is provided between the second heat exchanger 12 and the waste water treatment facility 9 for cooling the waste water after washing with well water. The waste water after washing cooled to a desired temperature by the cooling heat exchanger 31 is guided to the waste water treatment facility 9.

The hot water cleaning system 1 having the above configuration is operated as follows.
First, well water used as cleaning water is taken from the external environment and guided to the chemical distillation cooling device 3. In the chemical distillation cooling device 3, cleaning water (well water) is heated from about 16 ° C. to about 30 ° C. by cooling the distilled chemical for use in film cleaning. The cleaning water heated to about 30 ° C. is guided to the first heat exchanger 11 by the pressurizing pump 15.
In the first heat exchanger 11, the cleaning water is heated from about 30 ° C. to about 70 ° C. by the post-cleaning waste water after the film cleaning is completed by the film cleaning device 7. Along with this, the temperature of the waste water after washing is reduced from about 80 ° C. to about 40 ° C. in the first heat exchanger 11.

The washing water heated to about 70 ° C. in the first heat exchanger 11 is guided to the condenser of the heat pump 17 by the hot water pump 25. In the heat pump 17, the temperature of the cleaning water is raised to about 80 ° C. The opening degree of the three-way valve 27 is adjusted so as to maintain the heating temperature of the cleaning water at a predetermined value (about 80 ° C.). The cleaning water heated by the heat pump 17 is guided to the hot water tank 5.
On the other hand, the heat source water heat-exchanged by the second heat exchanger 12 is guided to the evaporator on the heat source side of the heat pump 17. In the second heat exchanger 12, the waste water after washing that has been subjected to heat exchange in the first heat exchanger 11 and reduced in temperature to about 40 ° C. and the heat source water are configured to exchange heat. After washing, the temperature of the waste water is reduced to about 33 ° C., and the heat source water recovers heat corresponding to the heat quantity. The heat source water is circulated between the second heat exchanger 12 and the evaporator of the heat pump 17 by the heat source water pump 19, and is adjusted to a desired temperature (about 25 ° C.) by adjusting the opening of the three-way valve 21. Heat source water is supplied to the evaporator of the heat pump 17.
Thus, the heat pump 17 is used so as to heat the cleaning water using the temperature recovered by the second heat exchanger 12 as a heat source.

The cleaning water heated to about 80 ° C. by the heat pump 17 is led to the hot water tank 5 and then heated to about 95 ° C. by the steam obtained in the boiler. That is, the temperature rise range heated by the boiler is only about 15 ° C. from about 80 ° C. to about 95 ° C.
The cleaning water heated to about 95 ° C. is guided to the film cleaning device 7 and mixed with chemicals to clean the film. After the temperature is reduced to about 80 ° C., the cleaning water is discharged as waste water after cleaning. As described above, the waste water after washing is reduced in temperature from about 80 ° C. to about 40 ° C. in the first heat exchanger 11 and further reduced in temperature from about 40 ° C. to about 33 ° C. in the second heat exchanger 12. Is done.
The waste water after washing, which has been reduced to about 33 ° C. in the second heat exchanger 12, is reduced to about 30 ° C. by the well water introduced from the outside in the cooling heat exchanger 31, and then the waste water treatment facility 9 leads to. The well water after cooling the drainage after washing is discharged to the outside.
The waste water after washing guided to the waste water treatment facility 9 is discharged to the outside after the contained chemical substances and SS (suspended substance) are removed by coagulation sedimentation or the like.

As described above, according to the hot water cleaning system 1 of the present embodiment, the following operational effects can be obtained.
The cleaning water supplied to the hot water tank 5 by the waste water discharged from the film cleaning device 7 is heated by the first heat exchanger 11, and the heat source water is discharged by the waste water discharged from the first heat exchanger 11. Was heated by the second heat exchanger 12. As a result, it is possible to effectively recover heat from the waste water after washing discharged from the film cleaning device 7 and at the same time to lower the temperature of the waste water after washing. Therefore, it is possible to reduce as much as possible the amount of well water used for cooling the drainage after washing when discharging to the outside.
Further, the heat pump 17 is operated using the heat source water heated by the second heat exchanger 12 as a heat source, and the cleaning water heated by the first heat exchanger 11 is further heated. Accordingly, the cleaning water can be heated to a high temperature (about 80 ° C.) with a high COP (coefficient of performance).
Further, since the cleaning water is supplied to the hot water tank 5 and heated by the boiler after being heated by the first heat exchanger 11 and the heat pump 17, as shown in FIG. Compared with the case where 30 ° C. cleaning water is heated to about 95 ° C., the amount of heating by the boiler can be reduced (in this embodiment, the heating amount from about 80 ° C. to about 95 ° C. is sufficient). Thereby, the amount of heat supplied to the boiler can be reduced, and the fuel cost and the CO2 emission amount can be reduced.

[Second Embodiment]
Next, a second embodiment of the present invention will be described with reference to FIG. This embodiment is suitable when used for preheating the cleaning water by the chemical distillation cooling device 3 as in the first embodiment. The present embodiment is different from the first embodiment in that the chemical distillation cooling device is omitted and a third heat exchanger 13 is added, and the others are the same. Therefore, the same components as those in the first embodiment are denoted by the same reference numerals and the description thereof is omitted.

The hot water cleaning system 10 of this embodiment includes a third heat exchanger 13 between the second heat exchanger 12 and the cooling heat exchanger 31. In the third heat exchanger 13, the well water (cleaning water) taken from the outside and the washed waste water discharged from the second heat exchanger 12 are heat-exchanged, and the well water has a water intake temperature of about 16 The temperature is raised from about 30 ° C. to about 30 ° C., and the waste water after washing is reduced from about 33 ° C. to about 19 ° C.
The cleaning wastewater (well water) that has been heated and preheated in the third heat exchanger 13 is guided to the first heat exchanger 11. The processes after the first heat exchanger 11 are the same as those in the first embodiment.
The post-cleaning waste water whose temperature has been reduced by the third heat exchanger 13 is about 19 ° C. and is sufficiently cooled, and therefore cooling by the cooling heat exchanger 31 is not required. Therefore, the well water is not passed through the cooling heat exchanger 31, and the washed waste water is guided to the waste water treatment facility 9 without performing heat exchange in the cooling heat exchanger 31. Therefore, in the case of this embodiment, it is good also as a structure which abbreviate | omitted the heat exchanger 31 for cooling.

As described above, according to the hot water cleaning system 10 of the present embodiment, the following operational effects can be obtained.
Since the cleaning water is heated by the third heat exchanger 13 using the waste water discharged from the second heat exchanger 12, the temperature of the waste water after cleaning can be further reduced, and the amount of water used for cooling is reduced. Can be further reduced or eliminated.
Further, since the cleaning water heated by the third heat exchanger 13 is supplied to the first heat exchanger 11, there is no preheating means for the cleaning water as shown in FIG. 4, and the temperature of the cleaning water is low. However, it can be used for washing with warm water.

In each of the above-described embodiments, a hot water cleaning system for cleaning a used film has been described as an example. However, the present invention is not limited to this, and equipment for cleaning an object to be processed using hot water. If so, it can be applied.
Moreover, in each embodiment mentioned above, although temperature was mentioned and demonstrated as a specific example, this invention is not limited to these temperatures.

1,10 Warm water cleaning system 5 Warm water tank (boiler heating section)
7 Film cleaning device (hot water cleaning device)
11 1st heat exchanger 12 2nd heat exchanger 13 3rd heat exchanger 17 Heat pump

Claims (4)

A boiler heating unit that heats cleaning water with steam obtained from the boiler;
A hot water cleaning device for cleaning an object to be processed using the cleaning water after heating obtained in the boiler heating unit;
In the hot water cleaning system with
A first heat exchanger that heats cleaning water supplied to the boiler heating unit by post-cleaning drainage discharged from the hot water cleaning device;
A second heat exchanger for heating the heat source water by the waste water after washing discharged from the first heat exchanger;
A heat pump that operates using the heat source water heated by the second heat exchanger as a heat source, and heats the cleaning water heated by the first heat exchanger;
With
A hot water cleaning system, wherein cleaning water heated by the heat pump is supplied to the boiler heating section. A third heat exchanger that heats the cleaning water before being supplied to the first heat exchanger by the post-cleaning waste water that has flowed out of the second heat exchanger;
The hot water cleaning system according to claim 1, wherein the cleaning water heated by the third heat exchanger is supplied to the first heat exchanger. A boiler heating unit that heats cleaning water with steam obtained from the boiler;
A hot water cleaning device for cleaning an object to be processed using the cleaning water after heating obtained in the boiler heating unit;
In the hot water cleaning method by the hot water cleaning system equipped with
The warm water cleaning system includes a first heat exchanger that heats cleaning water supplied to the boiler heating unit by post-cleaning drainage discharged from the warm water cleaning device;
A second heat exchanger for heating the heat source water by the waste water after washing discharged from the first heat exchanger;
A heat pump that operates using the heat source water heated by the second heat exchanger as a heat source, and heats the cleaning water heated by the first heat exchanger;
With
A hot water cleaning method, comprising supplying cleaning water heated by the heat pump to the boiler heating section. The warm water cleaning system includes a third heat exchanger that heats the cleaning water before being supplied to the first heat exchanger by the post-cleaning drainage discharged from the second heat exchanger,
The hot water cleaning method according to claim 3, wherein cleaning water heated by the third heat exchanger is supplied to the first heat exchanger.

Images