CN1696592A - Absorption refrigerator - Google Patents
Absorption refrigerator Download PDFInfo
- Publication number
- CN1696592A CN1696592A CNA2005100083931A CN200510008393A CN1696592A CN 1696592 A CN1696592 A CN 1696592A CN A2005100083931 A CNA2005100083931 A CN A2005100083931A CN 200510008393 A CN200510008393 A CN 200510008393A CN 1696592 A CN1696592 A CN 1696592A
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- China
- Prior art keywords
- cooling water
- frequency
- waste heat
- temperature
- supplying
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 238000010521 absorption reaction Methods 0.000 title claims abstract description 82
- 239000000498 cooling water Substances 0.000 claims abstract description 97
- 239000002918 waste heat Substances 0.000 claims abstract description 89
- 239000007788 liquid Substances 0.000 claims abstract description 57
- 239000012530 fluid Substances 0.000 claims abstract description 47
- 238000010438 heat treatment Methods 0.000 claims abstract description 20
- 239000006096 absorbing agent Substances 0.000 claims description 14
- 239000012141 concentrate Substances 0.000 claims description 14
- 238000006243 chemical reaction Methods 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims description 13
- 238000001704 evaporation Methods 0.000 claims description 13
- 230000008020 evaporation Effects 0.000 claims description 13
- 230000015654 memory Effects 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 7
- 238000005057 refrigeration Methods 0.000 claims description 7
- 238000005259 measurement Methods 0.000 claims description 6
- 230000006870 function Effects 0.000 claims description 4
- 230000001172 regenerating effect Effects 0.000 claims description 3
- 230000005144 thermotropism Effects 0.000 claims description 3
- 238000012546 transfer Methods 0.000 abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 31
- 239000003507 refrigerant Substances 0.000 description 18
- 238000013461 design Methods 0.000 description 12
- 239000007789 gas Substances 0.000 description 10
- 238000010586 diagram Methods 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 5
- 230000004087 circulation Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000008929 regeneration Effects 0.000 description 5
- 238000011069 regeneration method Methods 0.000 description 5
- 230000009471 action Effects 0.000 description 4
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 235000019628 coolness Nutrition 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000005619 thermoelectricity Effects 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Images
Classifications
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J37/00—Baking; Roasting; Grilling; Frying
- A47J37/06—Roasters; Grills; Sandwich grills
- A47J37/067—Horizontally disposed broiling griddles
-
- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J43/00—Implements for preparing or holding food, not provided for in other groups of this subclass
- A47J43/04—Machines for domestic use not covered elsewhere, e.g. for grinding, mixing, stirring, kneading, emulsifying, whipping or beating foodstuffs, e.g. power-driven
- A47J43/07—Parts or details, e.g. mixing tools, whipping tools
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
- F25B29/006—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
- Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
An absorption refrigerator, wherein the frequency (alpha Hz) of a power supply to a cooling water pump (12) is calculated based on the temperature (A) of the outlet side of a waste heat condenser of cooling water measured by a temperature detector (42), when the opening (X) of a flow control valve (13) on the side of a heat transfer pipe (3A) measured by an opening detector is in a fully opened or nearly fully opened valve-opened state at the side of the heat transfer pipe (3A) of, for example, 95% or more, the frequency (beta Hz) of the power supply to the cooling water pump (12) is calculated based on the outlet temperature (B) of waste heat fluid measured by a temperature detector (43), when alpha is not more than beta, the power supply of alpha Hz is supplied to the cooling water pump (12), when this is not the case, the power supply of beta Hz is supplied, when the opening (X) of the heat transfer pipe (3A) of the flow control valve (13) is not sufficiently large, the heating of an absorption liquid using the waste heat, and the amount of cooling water does not need to be increased. A controller (50) is preferably provided for supplying power at alpha Hz.
Description
Technical field
The present invention relates to also utilize the absorption refrigerating machine that evaporates the thermal source of the regenerator that separates cold-producing medium from the conducts such as waste heat of miscellaneous equipment supply by the heating absorption liquid.
Background technology
As this heat absorption type refrigerator, for example as shown in Figure 5, following heat absorption type refrigerator 100X is known, this refrigerator comprises: high-temp regenerator 1, the low temperature regenerator 2 of the refrigerant vapour of supplying with from high-temperature generator 1 as the heating source of absorption liquid, with the waste heat regenerator 3 of the waste heat fluid of supplying with to miscellaneous equipments such as systems from cogeneration as heating source, wherein high-temp regenerator 1 makes it seethe with excitement to evaporate and separate the cold-producing medium send in the evaporimeter 6 by the heating absorption liquid, and as the regenerator that concentrates the regeneration absorption liquid the heating source (for example referenced patent file 1) of the combustion heat that in gas burner 1A, produces as absorption liquid.
In addition, among the figure 4 is so that the condenser that mode that the refrigerant vapour that separates from the absorption liquid evaporation in low-temperature regenerator 2 can flow into and low-temperature regenerator 2 are arranged side by side, the 5th, so that the waste heat condenser that mode that the refrigerant vapour that evaporation separates from absorption liquid in waste heat regenerator 3 can flow into and waste heat regenerator 3 are arranged side by side, the 7th, so that the absorber that mode that the refrigerant vapour of evaporation can flow in evaporimeter 6 and evaporimeter 6 are arranged side by side.The 8th, low temperature heat exchanger, the 9th, high-temperature heat exchanger, the 10th, refrigerated medium pump, 11A and 11B absorb liquid pump, the 13rd, the flow control valve of forming by triple valve, 14-17 is an open and close valve, 18-23 is the absorption liquid pipe, and 24-29 is a refrigerant pipe, the 30th, and the waste heat fluid supply line, the 31st, bypass pipe, the 32nd, cold warm water tube, the 33rd, cooling water pipe, the 34th, balance pipe, connect by pipe arrangement as shown in Figure 5, formation can make by the tube wall cooling that is arranged on the heat-transfer pipe 6A in the evaporimeter 6/or be heated to the structure of the water of predetermined temperature by the not shown heat load of cold warm water tube 32 circulation supplies.
In the absorption refrigerating machine 100X of above-mentioned formation, because the combustion heat of emitting during gas-firing in the 1A of gas burner etc. and the waste heat fluid of supplying with to other equipment such as system from cogeneration by waste heat fluid supply line 30 heat absorption liquid as thermal source, when separating the generation cold-producing medium, concentrate the regeneration absorption liquid, so thermal efficiency height by evaporation from absorption liquid.Therefore there is what is called can save resource, and can reduces the advantage of emission amount of carbon dioxide.
Patent document: the spy opens flat 8-54153 communique
Summary of the invention
Yet in patent document 1 in the disclosed absorption refrigerating machine, because be arranged on cold moving water pump on the cooling water pipe with constant-speed operation, so though the leeway of reducing kinetic energy by the revolution that reduces cooling water pump hour is arranged in heat load, but reduce because when the unsteady flow amount control of carrying out cooling water, from the waste heat fluid, absorb the heat that obtains, so do not realize that in fact (do not use in the absorption refrigerating machine of waste heat fluid, the technology of controlling the revolution of cooling water pump according to the state of the cold water of supplying with heat load from evaporimeter and cooling water is known to the control of Variable Cooling Water Flow amount in thermal source.For example the spy opens flat 8-159596 communique etc.).
Therefore be necessary by not making the heat that obtains from the waste heat fluid recovery reduce the kinetic energy that reduces cooling water pump as much as possible.And must try one's best control is realized complicatedly.
The present invention provides a kind of absorption refrigerating machine for the problem that solves above-mentioned prior art, this refrigerator uses the waste heat fluid supplied with from miscellaneous equipment by linking to each other with the waste heat supply pipe to separate cold-producing medium concentrates the thermal source of regenerating to absorption liquid part or all as the absorption liquid after the absorption refrigeration agent being carried out heating evaporation, and carry out revolution control between via the cooling water pump among the cooling water pipe of absorber and condenser pipe arrangement by frequency-conversion and speed-regulation motor, it is characterized in that: the control program described in the memory that is stored in control device is comprised: according to the state decision of refrigerating medium of supplying with by cooling back thermotropism load cycle in evaporimeter or the cooling water that flows through cooling water pipe operation to the supply frequency of frequency-conversion and speed-regulation motor supply, the operation of the supply frequency of supplying with to frequency-conversion and speed-regulation motor according to the state decision of the waste heat fluid of supplying with from miscellaneous equipment, select the operation of the high frequency in the frequency of above-mentioned decision, with the operation of supplying with the revolution of frequency-conversion and speed-regulation motor control cooling water pump by the power supply of the frequency that will select.
In absorption refrigerating machine of the present invention, because revolution according to the state control cooling water pump of refrigerating medium, cooling water and the waste heat fluid from miscellaneous equipment, supplied with, be used for the power that cooling water transports so can reduce, and just can realize above-mentioned control by simple control.
Description of drawings
Fig. 1 is the key diagram of absorption refrigerating machine of the present invention.
Fig. 2 is the key diagram that expression is stored in the basic data in the memory of controller, wherein figure (A) is a key diagram of representing waste heat condensator outlet side temperature with the relation of the supply frequency of supplying with cooling water pump of cooling water, and figure (B) is the key diagram of the relation of expression waste heat fluid outlet side temperature and the supply frequency of supplying with cooling water pump.
Fig. 3 is the key diagram that expression is stored in the control program in the memory of controller.
Fig. 4 is the key diagram that expression is stored in other control program in the controller.
Fig. 5 is the key diagram of prior art.
The specific embodiment
The invention provides a kind of absorption refrigerating machine, this refrigerator uses the waste heat fluid supplied with from miscellaneous equipment by linking to each other with the waste heat supply pipe to separate cold-producing medium concentrates the thermal source of regenerating to absorption liquid part or all as the absorption liquid after the absorption refrigeration agent being carried out heating evaporation, and carry out revolution control between via the cooling water pump between the cooling water pipe of absorber and condenser pipe arrangement by frequency-conversion and speed-regulation motor, this absorption refrigerating machine has control device, this control device is equipped with control program, and described control program comprises: the operation of supplying with the supply frequency of frequency-conversion and speed-regulation motor according to the state decision of refrigerating medium of supplying with by cooling thermotropism load cycle in evaporimeter or the cooling water that flows through cooling water pipe, the operation of the supply frequency of supplying with to frequency-conversion and speed-regulation motor according to the state decision of the waste heat fluid of supplying with from miscellaneous equipment, select the operation of the high frequency in the frequency of above-mentioned decision, with the operation of supplying with the revolution of frequency-conversion and speed-regulation motor control cooling water pump by the power supply of the frequency that will select.
Describe embodiments of the present invention in detail according to Fig. 1-Fig. 4 below.Illustrated absorption refrigerating machine 100 of the present invention makes water as cold-producing medium in Fig. 1, uses lithium bromide (LiBr) aqueous solution as absorption liquid, and is to supply with as the cold water of refrigerating medium or the absorption refrigerating machine of warm water to unshowned heat load circulation.In addition, for for the purpose of understanding easily and the part that has illustrated among all among Fig. 1 and above-mentioned Fig. 5 is had the parts of identical function, add identical symbol.
Being not difficult to find out from above-mentioned figure, is identical with the absorption refrigerating machine 100X shown in above-mentioned Fig. 5 in the connection of absorption refrigerating machine of the present invention 100 at machine shown in Fig. 1.And the latent heat cooling back the when Temperature Detector 41 with evaporimeter 6 outlet sides that can be by being arranged on cold warm water tube 32 is measured cooled dose of evaporation after tube wall and the cold-producing medium heat exchange by the heat-transfer pipe 6A in the evaporimeter 6 is from the formation of the temperature of the cold warm water of evaporimeter 6 discharges.
In addition, has the formation that to measure the outlet temperature of the cooling water of from waste heat condenser 5, discharging after in absorber 7, condenser 4, waste heat condenser 5, finishing cooling effect respectively by the Temperature Detector on waste heat condenser 5 outlet sides that are arranged on cooling water pipe 33 42.
In addition, can measure by separating by waste heat regenerator 3 heating absorption liquid evacuator bodies behind the cold-producing mediums by being arranged on Temperature Detector 43 on the waste heat fluid supply line 30 by concentrate waste heat fluid that absorption liquid discharges and constituting from waste heat regenerator 3 via the outlet temperature of the waste heat fluid of the waste heat fluid interflow back outflow of bypass pipe 31.
In addition, have and to measure the constituting of temperature that separates the absorption liquid that concentrates behind the cold-producing medium by gas burner A heating evaporation by being arranged on Temperature Detector 44 on the high-temp regenerator 1.
In addition, also be provided for control gas burner 1A such as temperature, the controller 50 of refrigerated medium pump 10, absorption liquid pump 11A and 11B, cooling water pump 12 and flow control valve 13 etc. according to Temperature Detector 41-44.
In the absorption refrigerating machine 100 of above-mentioned formation, under switch valve 14-17 closing state, with cooling-water drain in cooling water pipe 33, natural gas etc. is burnt in gas burner 1A, make on one side simultaneously by waste heat fluid supply line 30 high temperature from supplies such as thermoelectricity series connection feed systems, the steam of high pressure, waste heat fluids such as high-temperature water are discharged among the heat-transfer pipe 3A that is arranged in the waste heat regenerator 3, absorb liquid pump 11A by making on one side, the 11B operation, will be in absorber 7 absorption refrigeration agent and accumulate in the absorption liquid that absorption liquid accumulates the place and flow to waste heat regenerator 3, again when waste heat regenerator 3 flows to high-temp regenerator 1, the absorption liquid that absorption liquid concentration uprises after just obtaining evaporation separates from absorption liquid refrigerant vapour and separate refrigerant vapour in waste heat regenerator 3 and high-temp regenerator 1.
The high temperature refrigerant steam that generates in high-temp regenerator 1 enters low-temperature regenerator 2 by refrigerant pipe 24, heating is concentrated the back and is entered absorption liquid in the low-temperature regenerator 2 by absorption liquid pipe 20 via high-temperature heat exchanger 9 at high-temp regenerator 1, enter condenser 4 after the heat release condensation.
In addition, the refrigerant vapour that separates from absorption liquid by the heating in low-temperature regenerator 2 enters condenser 4 and the cooling water heat exchange back condensation liquefaction that flows through in the cooling water pipe 33, enters evaporimeter 6 with the cold-producing medium of supplying with after refrigerant pipe 24 condensations by refrigerant pipe 26.
The high temperature refrigerant steam that generates in residual evaporator 3 also enters waste heat condenser 5, and enters evaporimeter 6 by refrigerant pipe 27,26 behind cooling water heat exchange in the cooling water pipe 33 of flowing through and the condensation liquefaction.
Enter the refrigerant liquid that remains in the refrigerant liquid place of retaining behind the evaporimeter 6 and spray on the heat-transfer pipe 6 that is connected with cold warm water tube 32, carry out the flow through water of inside of heat-transfer pipe 6A of heat exchange and evaporative cooling with the water of supplying with by cold warm water tube 32 circulations by the operation of refrigerated medium pump 10.
Then, the cold-producing medium of evaporation enters absorber 7 in evaporimeter 6, the concentration that makes absorption liquid after by low-temperature regenerator 2 heating the cold-producing medium evaporation being separated is the absorption liquid of regeneration further with improving, promptly supplies with via low temperature heat exchanger 8 by absorption liquid pipe 21 and absorbs from the concentrated absorption solution of top distribution.
The thinning absorption liquid of concentration after the absorption refrigeration agent in absorber 7, be that rare absorption liquid flows to waste heat regenerator 3 by the operation that absorbs liquid pump 11A via low temperature heat exchanger 8, such as mentioned above, after the residual heat stream evacuator body separation cold-producing medium of being supplied with from waste heat fluid hose 30 concentrates, flow to high-temp regenerator 1 by the operation that absorbs liquid pump 11B.
When moving as described above,, move so can carry out the cooling of cold air etc. because the cold water of cooled dose heat of gasification cooling can be by the not shown heat load of cold warm water tube 32 circulation supplies among the heat-transfer pipe 6A in evaporimeter 6.
In addition, supply with to the waste heat fluid of heat-transfer pipe 3A, have precedence over the burning of natural gas in gas burner 1A etc. from waste heat fluid supply line 30.That is to say, in the unshowned memory in controller 50, at first control flow control valve 13 and set for example 7 ℃ of temperature so that the temperature of the measured cold warm water of Temperature Detector 41 is reduced to, even the amount of the waste heat fluid in flowing to biography pipe 3A reaches maximum, when the temperature of the cold warm water that Temperature Detector 41 is measured does not still drop to 7 ℃ of design temperatures, just utilize gas burner 1A that absorption liquid is heated.And control, so that in high-temp regenerator 1, also carry out the generation of refrigerant vapour and the concentrated regeneration of absorption liquid, make the temperature that is discharged to the cold warm water in the cold warm water tube 32 after evaporimeter 6 cooling become 7 ℃ of the temperature of setting, even the heat that adds that utilizes gas burner 1A is reduced to minimum, the temperature of the cold warm water of measuring as Temperature Detector 41 still rises less than 7 ℃ of design temperatures, then just stop to utilize the heating of gas burner 1A, and storage is used for reducing to the quantity delivered of the waste heat fluid of heat-transfer pipe 3A and the temperature that is discharged to the cold warm water of cold warm water tube 32 after making by evaporimeter 6 coolings reaches the control program of 7 ℃ of design temperatures by control flow control valve 13.
In addition, for example storing in controller 50 in the unshowned memory, the relational expression shown in Fig. 2 (A) (can adopt function, the method that table etc. is fit to) and the relational expression shown in for example Fig. 2 (B) (can adopt function, the method that table etc. are fit to), wherein the relational expression shown in Fig. 2 (A) is that the waste heat condensator outlet side temperature of the cooling water measured at Temperature Detector 42 just increases cooling water flow by the frequency that improves to the power supply of cooling water pump 12 supplies when higher than design temperature (for example 37.5 ℃), and when lower, just reduce cooling water flow by the frequency that reduces the power supply of supplying with to cooling water pump 12 than above-mentioned design temperature, so that make the waste heat condensator outlet side temperature of cooling water certain, and the relational expression shown in Fig. 2 (B) is the temperature of measuring at Temperature Detector 43, just increase cooling water flow to the frequency of the power supply of cooling water pump 12 supplies when promptly the temperature by being separated the waste heat fluid that concentrates waste heat fluid that absorption liquid discharges behind the cold-producing mediums and flow via the back, waste heat fluid interflow of bypass pipe 31 from waste heat regenerator 3 by the evaporation of waste heat regenerator 3 heating absorption liquids is higher than design temperature (for example 80 ℃) by raising, and when lower, just reduce cooling water inflow by the frequency that reduces the power supply of supplying with to cooling water pump 12 than above-mentioned design temperature, so that make waste heat fluid outlet side temperature keep certain.
In addition, the also control program shown in the storage map 3 in controller 50 unshowned memories.Thereby measure the waste heat condensator outlet side temperature (A) (step S1) of cooling waters the in service of absorption refrigerating machine 100 by Temperature Detector 42, calculate frequency (α Hz) (step S2) to the power supply of cooling water pump 12 supplies according to the waste heat condensator outlet side temperature (A) of measured cooling water and the relational expression shown in Fig. 2 (A).
In addition, by the heat-transfer pipe 3A side aperture (X) (step S3) of unshowned aperture detectors measure flow control valve 13, judge that whether measured aperture (X) is at for example (step S4) more than 95%.
In step S4 YES, the aperture that is the heat-transfer pipe 3A side of flow control valve 13 be standard-sized sheet or near standard-sized sheet open the valve state time, just transfer to step S5, measure the outlet side temperature (B) of waste heat fluid by Temperature Detector 43, according to the outlet side temperature (B) of measured waste heat fluid and the relational expression shown in Fig. 2 (B), calculate the frequency (β Hz) (step S6) of the power supply of supplying with to cooling water pump 12.
Then in step S7, compare frequency (α Hz) that in step S2, calculates and the frequency (β Hz) that in step S6, calculates, when α 〉=β, just transfer to step S8, supply with the power supply of α Hz to cooling water pump 12, when not being such, just transfer to step S10, supply with the power supply of β Hz to cooling water pump 12.
In addition, in step S4 NO, promptly when the aperture of the heat-transfer pipe 3A of flow control valve 13 side is very not big, because there is no need and to utilize the heating of the absorption liquid of waste heat fluid to be increased to more than the currency, so also there is no need to make cooling water inflow to increase.Therefore, even, safety coefficient is estimated power supply at the interior α Hz that calculates in step S2 so can supply with to cooling water pump 12 owing to the frequency of the power supply of obtaining according to the state of waste heat fluid of supplying with to cooling water pump 12 is become minimum also passable.
Thereby, in absorption refrigerating machine 100 of the present invention, for example stop to utilize the heating of gas burner 1A and when the concentrated regeneration of the generation of cold-producing medium and absorption liquid is carried out in the heating of only using the waste heat fluid of supplying with to heat-transfer pipe 3A by waste heat fluid supply line 30 because of heat load is little, the cold water temperature that is back to evaporimeter 6 from heat load by cold warm water tube 32 rises also few, because of cooled dose heat of gasification in heat-transfer pipe 6A cools off the temperature that is discharged to the cooling water in the cold warm water tube 32 is also descended.
Therefore, because Temperature Detector 41 is measured than 7 ℃ of low temperature of design temperature, suppress to drop into the heat of giving waste heat regenerator 3 so can pass through controller 50.That is to say, the aperture of the heat-transfer pipe 3A side of flow control valve 13 is reduced to less than 95%, the residual heat stream scale of construction by bypass pipe 31 is increased.
Because when above-mentioned low load, work and make the temperature of the cooling water that flows through cooling water pipe 33 through the cooling of absorber 7, condenser 4, waste heat condenser 5, be that the waste heat condensator outlet side temperature (A) that Temperature Detector 42 is measured also reduces, so also reduce according to the frequency alpha Hz to the power supply of cooling water pump 12 supplies of waste heat condensator outlet temperature (A) decision of this cooling water.
In addition, because the power supply of supplying with the low α Hz of frequency to cooling water pump 12 by control program as shown in Figure 3 drives, so can reduce the electrical power that cooling water pump 12 is consumed.
And, because supply with according to the supply frequency (α Hz) of waste heat condensator outlet side temperature (A) decision of cooling water and be the power supply of the big frequency in the supply frequency (β Hz) that determines according to the outlet side temperature (B) of waste heat fluid during 95% or more and at heat-transfer pipe 3A side standard-sized sheet or near full-gear in the aperture of the heat-transfer pipe 3A of flow control valve 13 side to cooling water pump 12, and being less than 95% and the heating that do not need to utilize the absorption liquid of waste heat fluid, the aperture of the heat-transfer pipe 3A side of flow control valve 13 is increased to more than the currency, and when not needing to make cooling water inflow to increase yet, supply with according to because of the amount temperature of the supplying with abundant necessity also supply frequency (α Hz) of waste heat condensator outlet side temperature (A) decision of the cooling water of step-down, so the waste heat condensator outlet side temperature (A) of cooling water and waste heat fluid outlet side temperature (B) can not become than design temperature height to cooling water pump 12.
In addition, in controller 50 in the unshowned memory, the also control program shown in the storage map 4, thereby, because when the temperature of the absorption liquid in the high-temp regenerator 1 that Temperature Detector 44 is measured surpasses design temperature (for example 155 ℃), cooling water pump 12 just moves with maximum revolution, cooling water flow is forced to return to 100% flow, so can avoid the frequent safety that the abnormal high temperature because of high-temp regenerator 1 causes stops (though do not describe in detail, known safety device always equipment is equipped same as before but because avoid in order to measure above design temperature at Temperature Detector 44 dangerous, even so move by cooling water flow is become 100% flow forcibly, when Temperature Detector 44 is measured height above design temperature, also can stop cooling water pump 12 safely by making known safety device action always.), so can reach above-mentioned good effect by the simple control of number of steps about 10.
In addition, because the invention is not restricted to above-mentioned embodiment, so all be possible at the embodiment of the various modification of the scope of the aim that does not exceed claims.
For example promptly use the cooling water temperature of the condensator outlet side that Temperature Detector 45 measures to replace the waste heat condensator outlet side temperature (A) of the cooling water that Temperature Detector 42 measures, with the above-mentioned frequency of similarly obtaining the power supply of supplying with to cooling water pump 12, controlling as the unsteady flow amount of the cooling water of supplying with to cooling water pump 12, also can obtain and above-mentioned same action effect then by the power supply of the frequency of this supply frequency and the decision of the supply frequency (β Hz) that calculates according to waste heat fluid outlet side temperature (B).
Also have, promptly use this cooling water heat condensator outlet side temperature (A) and the temperature difference of the cooling water temperature of the absorber entrance side of Temperature Detector 46 measurements that are arranged on the absorber entrance side to replace the waste heat condensator outlet side temperature (A) of the cooling water of Temperature Detector 42 measurements, with the above-mentioned supply frequency of supplying with to cooling water pump 12 of similarly obtaining, controlling as the unsteady flow amount of the cooling water of supplying with to cooling water pump 12, also can obtain and above-mentioned same action effect then by the power supply of the frequency of this supply frequency and the decision of the supply frequency (β Hz) that calculates according to waste heat fluid outlet side temperature (B).
In addition, promptly use the evaporator outlet side temperature of the cold warm water of measuring with Temperature Detector 41 and the temperature difference of the cold warm water temperature of the evaporator inlet side of Temperature Detector 47 measurements of the evaporator inlet side that is arranged on cold warm water tube 32, perhaps measure big or small resultant certain data wherein of and heat load of not shown circulation by cold warm water tube 32 feeding cold waters with suitable means, the waste heat condensator outlet side temperature (A) that replaces the cooling water of Temperature Detector 42 measurements, with the above-mentioned frequency of similarly obtaining the power supply of supplying with to cooling water pump 12, then also obtaining and last same action effect by the unsteady flow amount control of the power supply of the frequency of this supply frequency and supply frequency (β Hz) decision that calculates according to waste heat fluid outlet side temperature (B) as the cooling water of supplying with cooling water pump 12.
The waste heat fluid outlet side temperature (B) that the entrance side temperature of the waste heat fluid of measuring with the Temperature Detector 48 of the entrance side that is arranged on waste heat regenerator 3 replaces Temperature Detector 43 to measure also can be carried out the unsteady flow amount control of above-mentioned cooling water.
Also can carry out the unsteady flow amount control of above-mentioned cooling water with the temperature that the pressure in the high-temp regenerator of measuring with the same unshowned pressure detectors that are provided with of Temperature Detector 44 1 replaces Temperature Detector 44 to measure the absorption liquid in the high-temp regenerators 1.
Also can the absorption liquid pipe be installed by pipe arrangement, so that flowing to waste heat regenerator 3 earlier, the rare absorption liquid that reduces by the concentration by absorber 7 absorption refrigeration agent concentrates, then this absorption liquid that concentrates is flowed to low-temperature regenerator 2 and concentrate, flow to high-temp regenerator 1 at last and concentrate; Also can the absorption liquid pipe be installed by pipe arrangement, carry so that rare absorption liquid that concentration reduces by absorber 7 absorption refrigeration agent is branched off in high-temp regenerator 1 and the waste heat regenerator 3, again the absorption liquid after being concentrated by high-temp regenerator 1 and waste heat regenerator 3 is flowed to low-temperature regenerator 2 and concentrate.
Also can be arranged on the cooling tube 29 that clips open and close valve 17 between the downstream and absorber 7 of refrigerated medium pump 10 of refrigerant pipe 28.
In addition, on the branch location of the waste heat fluid supply line 30 that also can be arranged on waste heat fluid entrance side to flow control valve 13 and bypass pipe 31.
Claims (2)
1. absorption refrigerating machine, this refrigerator uses the waste heat fluid supplied with from miscellaneous equipment by linking to each other with the waste heat supply pipe to separate cold-producing medium concentrates the thermal source of regenerating to absorption liquid part or all as the absorption liquid after the absorption refrigeration agent being carried out heating evaporation, and carry out revolution control between via the cooling water pump among the cooling water pipe of absorber and condenser pipe arrangement by frequency-conversion and speed-regulation motor, it is characterized in that: control program is stored in the memory of control device, described control program comprises: the operation of the supply frequency of supplying with to frequency-conversion and speed-regulation motor according to the state decision of refrigerating medium of supplying with by cooling back thermotropism load cycle in evaporimeter or the cooling water that flows through cooling water pipe, the operation of the supply frequency of supplying with to frequency-conversion and speed-regulation motor according to the state decision of the waste heat fluid of supplying with from miscellaneous equipment, select the operation of the high frequency in the frequency of above-mentioned decision, with the operation of supplying with the revolution of frequency-conversion and speed-regulation motor control cooling water pump by the power supply of the frequency that will select.
2. absorption refrigerating machine as claimed in claim 1, it is characterized in that: be provided with and measure the interior temperature of regenerator or the device of pressure, control device has when the data of this measurement mechanism measurement reach predetermined value makes the function of cooling water pump with the maximum revolution operation by power supply from peak frequency to frequency-conversion and speed-regulation motor that supply with.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP145010/04 | 2004-05-14 | ||
| JP2004145010A JP4308076B2 (en) | 2004-05-14 | 2004-05-14 | Absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1696592A true CN1696592A (en) | 2005-11-16 |
| CN100533009C CN100533009C (en) | 2009-08-26 |
Family
ID=35349422
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100083931A Expired - Fee Related CN100533009C (en) | 2004-05-14 | 2005-02-18 | Absorption refrigerator |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JP4308076B2 (en) |
| KR (1) | KR100585354B1 (en) |
| CN (1) | CN100533009C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101900456A (en) * | 2009-05-27 | 2010-12-01 | 三洋电机株式会社 | Absorption cold-hot water machine |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5598909B2 (en) * | 2010-05-27 | 2014-10-01 | 三洋電機株式会社 | Exhaust heat absorption chiller / heater and its drain water generation prevention method |
| CN115077199B (en) * | 2022-06-28 | 2024-04-19 | 中石化节能技术服务有限公司 | Method and system for utilizing low-temperature heat and chilled water |
-
2004
- 2004-05-14 JP JP2004145010A patent/JP4308076B2/en not_active Expired - Fee Related
-
2005
- 2005-02-18 CN CNB2005100083931A patent/CN100533009C/en not_active Expired - Fee Related
- 2005-02-24 KR KR1020050015180A patent/KR100585354B1/en not_active IP Right Cessation
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101900456A (en) * | 2009-05-27 | 2010-12-01 | 三洋电机株式会社 | Absorption cold-hot water machine |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2005326088A (en) | 2005-11-24 |
| KR100585354B1 (en) | 2006-06-02 |
| KR20060045331A (en) | 2006-05-17 |
| JP4308076B2 (en) | 2009-08-05 |
| CN100533009C (en) | 2009-08-26 |
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