JP2009243705A - Absorption heat pump - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an absorption heat pump for preventing crystallization of concentrated absorbing liquid caused by partial load during a heating operation. <P>SOLUTION: A heat source water pump 18 is disposed at an upstream side of a heat transfer tube 17 passing in an evaporator 4, a flow rate detecting means 19 is disposed at a downstream side, and further a refrigerant liquid temperature sensor 20 is disposed on a bottom portion of the evaporator 4. When the flow rate of the heat source water is reduced to be less than a set value, or the heat source water pump 18 is stopped, an operation is not immediately stopped, but a diluting operation of the absorbing liquid is performed to prevent crystallization of the concentrated absorbing liquid. Further when the probability of freezing of the heat source water exists, a temperature of the refrigerant liquid accumulated on the bottom portion of the evaporator 4 is measured by the refrigerant liquid temperature sensor 20, so that the diluting operation of the absorbing liquid is performed when the temperature of the refrigerant liquid is over a prescribed temperature, and the operation is stopped when the temperature becomes lower than a prescribed temperature. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

  The present invention relates to an absorption heat pump that prevents crystallization of an absorbing solution and prevents freezing of heat source water during heating operation.

  Conventionally, for example, an absorption heat pump using water as a refrigerant and a lithium bromide (LiBr) solution as an absorption liquid is known. This absorption heat pump includes, as main components, a regenerator that heats a rare absorbing liquid returned from the absorber to separate the refrigerant vapor, and a condenser that condenses and liquefies the refrigerant vapor sent from the regenerator. , The refrigerant liquid sent from this condenser is stored, the evaporator is sprayed from the spreader to the heat transfer tube and evaporated, and the refrigerant vapor sent from this evaporator is sprayed with the concentrated absorbent sent from the regenerator And the absorber that absorbs by dispersing from the container (for example, Patent Document 1).

  When using a single-effect absorption heat pump as described above for heating operation, heat source water is passed through the heat transfer tube passing through the evaporator as a secondary heat source, and is sent from the condenser and stays at the bottom of the evaporator. The refrigerant liquid to be sent is sent to the sprayer provided in the upper part of the evaporator by the refrigerant pump and sprayed on the heat transfer pipe, and when the refrigerant liquid evaporates, heat is taken from the heat source water flowing in the heat transfer pipe. When the refrigerant vapor is absorbed by the concentrated absorbent dispersed in the absorber, warm water flowing in the hot water pipe passing through the absorber (cold water returned from the load) is heated. When the hot water pipe passes through the condenser, the hot water heated by the absorber is further heated by exchanging heat with the refrigerant vapor sent from the regenerator, and then supplied to the load for heating. Used as a heat source.

  In the above case, the flow rate detecting means is provided in the outlet side heat transfer tube of the evaporator, and the flow rate of the heat source water is monitored by the flow rate detecting means. When the flow rate of the heat source water decreases and falls below the set value, a signal is input from the flow rate detection means to the control device, and a signal is output from this control device to the hot water pump provided in the inlet heat transfer pipe of the absorber. The hot water pump is stopped and the heating operation is immediately stopped.

  However, if the heating operation is stopped immediately, the absorption liquid pump that returns the rare absorption liquid stored in the absorber to the regenerator is stopped, so that the absorption liquid does not flow in the circulation path connecting the regenerator and the absorber, The concentrated absorbent stays in the pipe line from the vessel to the absorber or in the heat exchanger on the way. If the stop time is prolonged in such a state, the concentrated absorbent may cool and crystallization may occur.

  When such crystallization of the concentrated absorbent occurs, the flow of the concentrated absorbent is hindered when the operation is resumed thereafter, and normal operation immediately becomes impossible. For this reason, prior to restarting the operation, the pipe line leading from the regenerator to the absorber must be heated by a heater or the like to dissolve the crystal, which is troublesome. In particular, when crystallization occurs in a heat exchanger provided in the middle of the regenerator and the absorber, melting work by heating becomes very difficult.

JP-A-8-233391

  The present invention is made to eliminate the disadvantages of the conventional absorption heat pump, and provides an absorption heat pump that prevents crystallization of concentrated absorbent when the flow rate of heat source water decreases during heating operation. The purpose is to do.

  As means for achieving the above-mentioned object, claim 1 of the present invention comprises a regenerator for heating the rare absorbent returned from the absorber to separate the refrigerant vapor, and condensing the refrigerant vapor sent from the regenerator. A condenser for liquefying, an evaporator for evaporating the refrigerant liquid sent from the condenser, and the absorber for absorbing refrigerant vapor sent from the evaporator, and passing through the evaporator during heating operation. When the flow rate of the heat source water flowing through the heat pipe decreases below the set value, or when the heat source water pump provided in the heat transfer pipe upstream of the evaporator stops, the operation of diluting the absorption liquid without stopping immediately The gist of the present invention is an absorption heat pump.

  According to a second aspect of the present invention, in the absorption heat pump according to the first aspect, a flow rate detecting means is provided in a heat transfer tube downstream of the evaporator, and the flow rate of the heat source water flowing in the heat transfer tube through the flow rate detecting means is set. In addition to adjusting, when the flow rate of the heat source water decreases below a set value, the detection signal is input to the control device.

  According to a third aspect of the present invention, in the absorption heat pump according to the first aspect, when the heat source water is likely to freeze, the temperature of the refrigerant liquid accumulated at the bottom of the evaporator is measured, and the temperature of the refrigerant liquid is measured. When the temperature exceeds a predetermined temperature, the absorption liquid is diluted, and when the temperature falls below the predetermined temperature, the operation is stopped.

  According to a fourth aspect of the present invention, in the absorption heat pump according to the third aspect, a temperature sensor is provided at the bottom of the evaporator, and the temperature sensor detects the temperature of the refrigerant liquid accumulated at the bottom of the evaporator. A signal is input to the control device.

  According to the first aspect of the invention, when heating the absorption heat pump, when the flow rate of the heat source water falls below the set value or when the heat source water pump provided in the heat transfer pipe upstream from the evaporator is stopped. Since the absorption liquid is diluted without immediately stopping the operation, the concentrated absorption liquid is not left in a state where the absorption liquid is accumulated in the conduit from the regenerator to the absorber. For this reason, crystallization of the concentrated absorbent can be suppressed, and when the operation is restarted, the flow of the concentrated absorbent is not hindered, and normal operation can be immediately performed. Further, prior to restarting the operation, the conventional troublesome work of warming the pipe line and dissolving the crystals of the concentrated absorbent is not required.

  According to the second aspect of the present invention, when the flow rate of the heat source water is reduced below the set value by providing the flow rate detection means in the heat transfer pipe downstream of the evaporator, the detection signal is input to the control device. Thus, the dilution operation signal can be reliably output from the control device.

  According to the third aspect of the present invention, when there is a possibility that the heat source water is frozen, the temperature of the refrigerant liquid accumulated at the bottom of the evaporator is measured, and the temperature of the refrigerant liquid exceeds a predetermined temperature. The crystallization of the concentrated absorbent can be prevented by performing a dilution operation of the absorbent. Further, when the temperature of the refrigerant liquid becomes equal to or lower than a predetermined temperature, it is possible to suppress freezing of the heat source water in the heat transfer tube in the evaporator as much as possible by stopping the operation.

  According to the fourth aspect of the present invention, the temperature sensor is provided at the bottom of the evaporator, and the temperature of the refrigerant liquid collected at the bottom of the evaporator is detected by the temperature sensor so that the heat source water is not frozen. can do. In addition, by inputting a detection signal from the temperature sensor to the control device, an operation stop signal can be output when the temperature of the refrigerant liquid becomes a predetermined temperature or lower.

Hereinafter, an embodiment of an absorption heat pump according to the present invention will be described with reference to the accompanying drawings.
FIG. 1 is a configuration diagram showing a main part of an absorption heat pump according to the present invention. In this figure, 1 is a regenerator, 2 is a condenser, these are accommodated in the upper trunk | drum 3, and the lower part is partitioned off by the partition plate 3a. Reference numeral 4 denotes an evaporator, and 5 denotes an absorber. These are accommodated in the lower body 6 and the lower part is partitioned in an inclined state by a partition plate 6a.

  Reference numeral 7 denotes a drive heat source pipe through which a drive heat source (main heat source) circulates, and is piped to pass through the regenerator 1, and a flow rate control valve 8 is provided upstream from the regenerator 1. As the driving heat source, steam, hot water, or the like can be used. For example, the driving heat source is supplied from a supply source such as a boiler or an engine.

  In the regenerator 1, a low-concentration absorption liquid (hereinafter referred to as a rare absorption liquid) supplied from the absorber 5 via the absorption liquid pump 9 and the rare absorption liquid pipe 10 is driven through the drive heat source pipe 7. The refrigerant vapor is separated by heating with a heat source.

  The refrigerant vapor separated from the rare absorbing liquid in the regenerator 1 flows into the adjacent condenser 2 and is cooled, and becomes refrigerant liquid and accumulates at the bottom of the condenser 2. In this condenser 2, piping is provided so that the hot water pipe 11 passes through, and the hot water pipe 11 passes through the condenser 2 after passing through the absorber 5. Further, a hot water pump 12 is provided upstream of the absorber 5 in the hot water pipe 11, and a hot water outlet temperature sensor 13 is provided downstream of the condenser 2. Based on the temperature detection by the hot water outlet temperature sensor 13, the on-off valve of the flow rate control valve 8 is controlled to adjust the drive heat source supplied to the regenerator 1.

  The refrigerant liquid collected at the bottom of the condenser 2 is supplied by flowing down into the evaporator 4 through the refrigerant liquid supply pipe 14, and is collected at the bottom of the evaporator 4, and at the refrigerant liquid pump 15 through the refrigerant liquid pipe 16. Then, it is supplied to the spreader 4a provided on the upper part of the evaporator 4 and spread. The evaporator 4 is piped so that the heat transfer pipe 17 through which the heat source water (sub heat source) flows, and a heat source water pump 18 is provided upstream of the evaporator 4 in the heat transfer pipe 17. A flow rate detection means 19 is provided on the downstream side of 4. For example, a flow switch can be used as the flow rate detection means 19. A refrigerant liquid temperature sensor 20 is provided outside the bottom of the evaporator 4.

  Absorbing liquid (hereinafter, concentrated absorbing liquid) having a high concentration as a result of separation of the refrigerant vapor in the regenerator 1 is supplied by flowing down to the absorber 5 through an absorbing liquid supply pipe 21 and is provided above the absorber 5. It spreads from the spreader 5a. A heat exchanger 22 is provided in the middle of the absorption liquid supply pipe 21, and the rare absorption liquid pipe 10 passes through the heat exchanger 22, so that a high-temperature concentrated absorption liquid and a low-temperature rare absorption liquid are formed. Exchange heat.

  A control device 23 is connected to the flow rate detection means 19 and the refrigerant liquid temperature sensor 20 and is connected to the heat source water pump 18, the refrigerant liquid pump 15, the absorption liquid pump 9, the hot water pump 12, and the flow rate control valve 8. Has been. The flow control valve 8 is connected to the hot water temperature sensor 13.

  The absorption heat pump according to the present invention configured as described above can perform a heating operation by supplying a drive heat source to the drive heat source tube 7 and supplying a sub heat source to the heat transfer tube 17. As the auxiliary heat source, for example, heat source water pumped from the underground can be used.

  During the heating operation, for example, water vapor is supplied to the drive heat source pipe 7 to heat the rare absorbent in the regenerator 1 and to separate the refrigerant vapor. The refrigerant vapor separated by the regenerator 1 flows into the condenser 2, dissipates heat to the hot water flowing through the hot water pipe 11 in the condenser 2, condenses, and accumulates at the bottom of the condenser 2 as a refrigerant liquid.

  The refrigerant liquid collected at the bottom of the condenser 2 is supplied to the evaporator 4 through the refrigerant liquid supply pipe 14 and is sent to the spreader 4a through the refrigerant liquid pipe 16 by the refrigerant liquid pump 15 and is supplied to the heat transfer pipe 17. It is sprayed toward. The dispersed refrigerant liquid takes heat from the heat source water flowing through the heat transfer pipe 17 in the evaporator 4 and evaporates, and flows into the absorber 5 as refrigerant vapor.

  The refrigerant vapor that has flowed into the absorber 5 is supplied from the regenerator 1 to the absorber 5 through the absorption liquid supply pipe 21 and is absorbed by the concentrated absorption liquid sprayed from the spreader 5a to become a rare absorption liquid. And accumulates at the bottom of the absorber 5. Then, the rare absorbent stored at the bottom of the absorber 5 passes through the rare absorbent pipe 10 by the absorbent pump 9 and is heated by the heat exchanger 22 and then supplied to the regenerator 1.

  In this way, the refrigerant and the absorption liquid circulate, and the hot water passing through the hot water pipe 11 is heated by heat exchange with the refrigerant vapor when passing through the absorber 5, and then when passing through the condenser 2. It is reheated by exchanging heat with steam, supplied to a load (not shown), and used as a heat source for heating. The hot water whose temperature has decreased due to heat dissipation by the load is returned to the inlet side of the hot water pipe 11 through a pipe (not shown) and supplied to the hot water pipe 11 by the hot water pump 12.

  When the flow rate of the heat source water supplied to the heat transfer tube 17 decreases, the flow rate detection means 19 of the heat source water detects a flow rate below the set value, or the heat source water pump 18 stops, the operation is not immediately stopped. Dilute operation at.

  In this dilution operation, the flow rate control valve 8 is closed to stop the supply of water vapor to the regenerator 1, and the absorbent pump 9 is operated to return the diluted absorbent from the absorber 5 to the regenerator 1. The refrigerant liquid pump 15 is operated to supply the refrigerant vapor from the evaporator 4 to the absorber 5 and the hot water pump 12 is operated to supply the hot water to the load.

  By this dilution operation, the regenerator 1 is supplied with the rare absorbent from the absorber 5, so that the concentration of the absorbent in the regenerator 1 becomes thin, and the regenerator 1 receives water vapor from the drive heat source pipe 7. Since it is not supplied, the refrigerant vapor is hardly separated in the regenerator 1.

  The absorbing liquid whose concentration has been diluted by the regenerator 1 is supplied to the absorber 5 through the absorbing liquid supply pipe 21. Conventionally, since the operation was stopped immediately in the event of an abnormality, the concentrated absorbent does not flow from the regenerator 1 to the absorber 5 but stays in the absorbent supply pipe 21 or the heat exchanger 22 and remains in that state. When prolonged, it cooled and the concentrated absorbent crystallized. In the case of the present invention, since the dilution operation is continued without immediately stopping the operation as described above, it is possible to prevent the conventional crystallization of the absorbing solution. Conventionally, prior to resuming operation, it was necessary to perform heating with a heater or the like to dissolve the crystals, but in the case of the present invention, the absorption liquid does not crystallize, so such melting work is unnecessary. is there.

  In the present invention, in order to prevent freezing of the heat source water, the operation of diluting the absorbing liquid is performed when the temperature of the refrigerant liquid accumulated at the bottom of the evaporator 4 exceeds a predetermined temperature, and the operation is performed when the temperature is lower than the predetermined temperature. Stop.

  As shown in FIG. 2, when the flow rate of the heat source water decreases or an abnormality of the interlock occurs in the heat source water pump 18 in step S1, a signal for starting the dilution operation is output from the control device 23 in step S2. In step S3, the flow rate control valve 8 is closed. In step S4, when the refrigerant liquid temperature is 7 ° C. or higher, the hot water pump 12, the absorption liquid pump 9, and the refrigerant liquid pump 15 are respectively operated in steps S5 to S7. Dilute operation by doing.

  In step S8, it is determined whether or not the dilution is completed. If NO, the process returns to step S4 and the dilution operation is repeated. Whether or not the dilution is complete can be determined by, for example, a timer.

  In step S4, when the refrigerant liquid temperature is 7 ° C. or lower, the process proceeds to steps S9 to S11, and the hot water pump 12, the absorption liquid pump 9, and the refrigerant liquid pump 15 are stopped to stop the operation. Thereby, when the temperature of the refrigerant liquid exceeds a predetermined temperature, crystallization of the concentrated absorbent can be prevented by performing the dilution operation of the absorbent. Further, when the temperature of the refrigerant liquid becomes equal to or lower than a predetermined temperature, it is possible to suppress freezing of the heat source water in the heat transfer tube 17 in the evaporator 4 as much as possible by stopping the operation. FIG. 3 shows the time chart.

  INDUSTRIAL APPLICABILITY The present invention can be effectively applied as a means for preventing crystallization of an absorbing liquid caused by a partial load when heating operation is performed with an absorption heat pump.

It is a schematic block diagram in the case of heating operation with the absorption heat pump which concerns on this invention. It is a flowchart at the time of abnormality in heating operation with the absorption heat pump which concerns on this invention. Similarly, it is a time chart at the time of abnormality.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Regenerator 2 Condenser 4 Evaporator 5 Absorber 7 Drive heat source pipe 8 Flow control valve 9 Absorption liquid pump 10 Rare absorption liquid pipe 11 Hot water pipe 12 Hot water pump 13 Hot water outlet temperature sensor 14 Refrigerant liquid supply pipe 15 Refrigerant liquid pump 16 Refrigerant liquid pipe 17 Heat transfer pipe 18 Heat source water pump 19 Flow rate detecting means 20 Refrigerant liquid temperature sensor 21 Absorbing liquid supply pipe 22 Heat exchanger 23 Controller

Claims (4)

  A regenerator that separates the refrigerant vapor by heating the rare absorbing liquid returned from the absorber, a condenser that condenses and liquefies the refrigerant vapor sent from the regenerator, and evaporates the refrigerant liquid sent from the condenser An evaporator, and the absorber that absorbs the refrigerant vapor sent from the evaporator, and when the flow rate of the heat source water flowing in the heat transfer pipe passing through the evaporator is reduced to a set value or less during heating operation, or An absorption heat pump characterized in that when the heat source water pump provided in the heat transfer tube upstream of the evaporator is stopped, the absorption liquid is diluted without immediately stopping the operation.   When the flow rate detection means is provided in the heat transfer pipe downstream from the evaporator, the flow rate of the heat source water flowing through the heat transfer pipe is adjusted via the flow rate detection means, and when the flow rate of the heat source water decreases below a set value. The absorption heat pump according to claim 1, wherein the detection signal is input to a control device.   When the heat source water is likely to freeze, the temperature of the refrigerant liquid collected at the bottom of the evaporator is measured. If the temperature of the refrigerant liquid exceeds a predetermined temperature, the absorption liquid is diluted, The absorption heat pump according to claim 1, wherein the operation is stopped when the temperature becomes lower than the temperature.   The temperature sensor is provided at the bottom of the evaporator, and the temperature of the refrigerant liquid accumulated at the bottom of the evaporator is detected by the temperature sensor, and the detection signal is input to the control device. Absorption heat pump.

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