CN105074356A - Heat source system, and device and method for controlling same - Google Patents
Heat source system, and device and method for controlling same Download PDFInfo
- Publication number
- CN105074356A CN105074356A CN201480010573.0A CN201480010573A CN105074356A CN 105074356 A CN105074356 A CN 105074356A CN 201480010573 A CN201480010573 A CN 201480010573A CN 105074356 A CN105074356 A CN 105074356A
- Authority
- CN
- China
- Prior art keywords
- heat source
- heat
- load factor
- source machine
- section
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 82
- 230000008569 process Effects 0.000 claims description 33
- 230000008859 change Effects 0.000 claims description 17
- 230000000052 comparative effect Effects 0.000 claims description 9
- 230000003247 decreasing effect Effects 0.000 abstract description 2
- 239000010865 sewage Substances 0.000 abstract 2
- 230000007423 decrease Effects 0.000 description 33
- 108010075226 adenovirus factor PL Proteins 0.000 description 22
- 238000010438 heat treatment Methods 0.000 description 18
- 239000003507 refrigerant Substances 0.000 description 14
- 239000003795 chemical substances by application Substances 0.000 description 11
- 238000011068 loading method Methods 0.000 description 8
- 230000008901 benefit Effects 0.000 description 4
- 239000002826 coolant Substances 0.000 description 4
- 230000014509 gene expression Effects 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000006870 function Effects 0.000 description 2
- YLOCGHYTXIINAI-XKUOMLDTSA-N (2s)-2-amino-3-(4-hydroxyphenyl)propanoic acid;(2s)-2-aminopentanedioic acid;(2s)-2-aminopropanoic acid;(2s)-2,6-diaminohexanoic acid Chemical compound C[C@H](N)C(O)=O.NCCCC[C@H](N)C(O)=O.OC(=O)[C@@H](N)CCC(O)=O.OC(=O)[C@@H](N)CC1=CC=C(O)C=C1 YLOCGHYTXIINAI-XKUOMLDTSA-N 0.000 description 1
- 102000016726 Coat Protein Complex I Human genes 0.000 description 1
- 108010092897 Coat Protein Complex I Proteins 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 230000004069 differentiation Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000010010 raising Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000002349 well water Substances 0.000 description 1
- 235000020681 well water Nutrition 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H4/00—Fluid heaters characterised by the use of heat pumps
- F24H4/02—Water heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D19/00—Details
- F24D19/10—Arrangement or mounting of control or safety devices
- F24D19/1006—Arrangement or mounting of control or safety devices for water heating systems
- F24D19/1009—Arrangement or mounting of control or safety devices for water heating systems for central heating
- F24D19/1039—Arrangement or mounting of control or safety devices for water heating systems for central heating the system uses a heat pump
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D19/00—Details
- F24D19/10—Arrangement or mounting of control or safety devices
- F24D19/1006—Arrangement or mounting of control or safety devices for water heating systems
- F24D19/1009—Arrangement or mounting of control or safety devices for water heating systems for central heating
- F24D19/1048—Counting of energy consumption
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D3/00—Hot-water central heating systems
- F24D3/18—Hot-water central heating systems using heat pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0096—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater combined with domestic apparatus
-
- 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
- F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
- F25B25/005—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00 using primary and secondary systems
-
- 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
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2200/00—Heat sources or energy sources
- F24D2200/12—Heat pump
- F24D2200/123—Compression type heat pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2200/00—Heat sources or energy sources
- F24D2200/16—Waste heat
- F24D2200/20—Sewage water
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2220/00—Components of central heating installations excluding heat sources
- F24D2220/04—Sensors
- F24D2220/042—Temperature sensors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2220/00—Components of central heating installations excluding heat sources
- F24D2220/04—Sensors
- F24D2220/044—Flow sensors
-
- 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
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
- F25B2339/047—Water-cooled condensers
-
- 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
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/06—Several compression cycles arranged in parallel
-
- 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
- Y02B10/00—Integration of renewable energy sources in buildings
- Y02B10/70—Hybrid systems, e.g. uninterruptible or back-up power supplies integrating renewable energies
-
- 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]
- Y02B30/12—Hot water central heating systems using heat pumps
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Air Conditioning Control Device (AREA)
- Other Air-Conditioning Systems (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The objective is to achieve stable output from a heat source system that includes heat source machines which utilize unused heat from sewage water or the like as the heat collection source, while using the unused heat as much as possible as the heat collection source. This heat source system is equipped with: first heat source machines, which utilize unused heat from sewage water or the like as the heat collection source; second heat source machines, which utilize a heat collection source other than unused heat; and a control device (10). The control device (10) calculates the maximum amount of heat that can be output by the first heat source machines, and the maximum load rate that can be output by the first heat source machines, and in accordance with the result of those calculations, the control device changes the increased/decreased-quantity priority and the increased/decreased-quantity load rate threshold value for the heat source machines, and controls the increasing/decreasing of the quantity of the heat source machines.
Description
Technical field
The present invention relates to and a kind ofly possess utilization and do not utilize heat energy as adopting the heat source system of heat source machine of thermal source and control device thereof and control method, particularly relate to heat that a kind of basis do not utilize heat energy to have and come the heat source system of control of heat source system increase and decrease section and control device thereof and control method.
Background technology
In recent years, there has been proposed such as utilize lower water etc. not utilize heat energy as the thermal source (such as, referenced patent document 1) of the heat source machines such as heat pump.
Prior art document
Patent document
Patent document 1: Japanese Patent Laid-Open 2003-4262 publication
Summary of the invention
The technical problem solved
But, use and do not utilize heat energy, when especially using lower water etc. as thermal source, because violent variation occurs for the flow of lower water and temperature, therefore descend adopting heat and also violent variation occurring of water.And during from lower hydromining heat, the performance for carrying out the heat exchanger of heat exchange with lower water is subject to the impact of dirt in lower water and significantly declines at short notice, the impact being subject to this heat exchanger performance comes from adopting heat violent variation occurring of lower water.So in the heat source machine not utilizing heat energy, just cannot realize stable output.Therefore having utilization does not utilize heat energy as adopting in the heat source system of heat source machine of thermal source, needs to consider that the heat not utilizing heat energy to have carries out operation and controls.
Compared with not utilizing heat energy and using the heat source machine of conventional air cooler etc., heat source machine can be used expeditiously and reduce operating cost, therefore preferably utilizing these not utilize heat energy to run heat source machine as far as possible.
The object of the present invention is to provide a kind of heat source system and control device thereof and control method, it does not utilize in the heat source system of heat energy as the heat source machine of thermal source comprising water etc. under utilization, do not utilize heat energy as thermal source as far as possible, and stable output can be realized.
Technical scheme
1st mode of the present invention is a kind of control device of heat source system, and described heat source system possesses: the 1st heat source machine, and it uses lower water etc. not utilize heat energy as adopting thermal source; And, the 2nd heat source machine, it utilizes different from not utilizing heat energy adopts thermal source, and wherein, the control device of described heat source system possesses: memory cell, and it preserves increasing section order about each described heat source machine and increasing section load factor threshold value; 1st arithmetic element, it calculates the maximum exportable heat of described 1st heat source machine; 2nd arithmetic element, it calculates the maximum exportable load factor of described 1st heat source machine; Changing unit, it uses the operation result of described 1st arithmetic element and described 2nd arithmetic element, changes in described memory cell the increasing section order of each described heat source machine preserved and increases section load factor threshold value; And increase section control unit, it is according to the increasing section order of preserving in described memory cell and increase section load factor threshold value, controls the increasing section of each described heat source machine.
In the manner, do not utilize heat energy as adopting the maximum exportable heat of the 1st heat source machine of thermal source and maximum exportable load factor according to using, change and increase section order and increase section load factor threshold value, therefore, it is possible to set corresponding to the heat that can never utilize heat energy to gather, suitable increasing section order and increase section load factor threshold value.So just can realize as far as possible effectively utilization and not utilize the operation of the heat source machine of heat energy.
In the control device of above-mentioned heat source system, described changing unit is possessed the requirement heat of specifying, the 1st load factor of specifying and value is set to the information of the 2nd load factor of specifying being less than the 1st load factor, according to the described comparative result requiring the comparative result of heat and described maximum exportable heat and described maximum exportable load factor and described 1st load factor or described 2nd load factor, the increasing section order of each described heat source machine preserved can be changed in described storage part and increases section load factor threshold value.
In the control device of above-mentioned heat source system, the maximum exportable heat of described 1st heat source machine be described require more than heat and described maximum exportable load factor is more than described 1st load factor time, described changing unit can make the increasing section load factor threshold value of described 1st heat source machine increase.
The maximum exportable heat of the 1st heat source machine for require more than heat and maximum exportable load factor is more than 1st load factor time, be derived from do not utilize heat energy to adopt heat many, heat energy can not utilized more energetically.Therefore by making the increasing section load factor threshold value of the 1st heat source machine increase, postponing the increasing section opportunity of the 2nd heat source machine, maintaining the operation only using the 1st heat source machine as far as possible.
In the control device of above-mentioned heat source system, the maximum exportable heat of described 1st heat source machine be less than described require heat and described maximum exportable load factor is more than described 2nd load factor time, described changing unit can make the increasing section load factor threshold value of described 1st heat source machine reduce.
The maximum exportable heat of the 1st heat source machine be less than requirement heat and maximum exportable load factor is more than 2nd load factor time, be derived from do not utilize heat energy to adopt heat little, not too can not utilize heat energy energetically.Therefore in this case, by making the increasing section load factor threshold value of the 1st heat source machine reduce, being adjusted to the 2nd heat source machine and starting as early as possible.
In the control device of above-mentioned heat source system, the maximum exportable heat of described 1st heat source machine be less than described require heat and described maximum exportable load factor is less than described 2nd load factor time, described changing unit can reduce the increasing section order of described 1st heat source machine, and the increasing section load factor threshold value of described 2nd heat source machine is increased.
The maximum exportable heat of the 1st heat source machine be less than requirement heat and maximum exportable load factor is less than the 2nd load factor time, the heat of heat energy collection never can be utilized obviously to diminish, not too can obtain the advantage that use does not utilize heat energy.Therefore in this case, the increasing section of the 1st heat source machine order need be reduced to lower than the 2nd heat source machine, and the increasing section load factor threshold value of the 2nd heat source machine is increased.So, just preferentially can utilize the 2nd heat source machine, and the increasing section opportunity of the 1st heat source machine can be postponed.
2nd mode of the present invention is a kind of control device of heat source system, and described heat source system possesses: the 1st heat source machine, and it uses lower water etc. not utilize heat energy as adopting thermal source; And, the 2nd heat source machine, it utilizes different from not utilizing heat energy adopts thermal source, and wherein, the control device of described heat source system possesses: memory cell, its preserve about each described heat source machine the section of subtracting sequentially and the section of subtracting load factor threshold value; 1st arithmetic element, it calculates the maximum exportable heat of described 1st heat source machine; 2nd arithmetic element, it calculates the maximum exportable load factor of described 1st heat source machine; Changing unit, it uses the operation result of described 1st arithmetic element and described 2nd arithmetic element, changes in described memory cell the section of subtracting order and the section of the subtracting load factor threshold value of each described heat source machine preserved; And the section of subtracting control unit, it, according to the section of the subtracting order of preserving in described memory cell and the section of subtracting load factor threshold value, controls the section of subtracting of each described heat source machine.
In the manner, do not utilize heat energy as adopting the maximum exportable heat of the 1st heat source machine of thermal source and maximum exportable load factor according to using, the change section of subtracting order and the section of subtracting load factor threshold value, therefore, it is possible to set corresponding to never utilizing the heat of heat energy collection, the suitable section of subtracting order and the section of subtracting load factor threshold value.So just can realize as far as possible effectively utilization and not utilize the operation of the heat source machine of heat energy.
In the control device of above-mentioned heat source system, described changing unit is possessed the requirement heat of specifying, the 3rd load factor of specifying and value is set to the information of the 4th load factor of specifying being less than the 3rd load factor, according to the described comparative result requiring the comparative result of heat and described maximum exportable heat and described maximum exportable load factor and described 3rd load factor or described 4th load factor, the section of subtracting order and the section of the subtracting load factor threshold value of each described heat source machine preserved can be changed in described storage part.
In the control device of above-mentioned heat source system, the maximum exportable heat of described 1st heat source machine be greater than described require heat and described maximum exportable load factor is more than described 3rd load factor time, described changing unit can make the section of the subtracting load factor threshold value of described 2nd heat source machine increase.
The maximum exportable heat of the 1st heat source machine be greater than requirement heat and maximum exportable load factor is more than 3rd load factor time, be derived from do not utilize heat energy to adopt heat many, heat energy can not utilized energetically.Therefore by making the section of the subtracting load factor threshold value of the 2nd heat source machine increase, the section of the subtracting opportunity of the 2nd heat source machine ahead of time.So just can utilize the 1st heat source machine as far as possible energetically.
In the control device of above-mentioned heat source system, the maximum exportable heat of described 1st heat source machine be less than described require heat and described maximum exportable load factor is more than described 4th load factor time, described changing unit can make the section of the subtracting load factor threshold value of described 2nd heat source machine reduce.
The maximum exportable heat of the 1st heat source machine be less than requirement heat and maximum exportable load factor is more than 4th load factor time, be derived from do not utilize heat energy to adopt heat little, not too can not utilize heat energy energetically.Therefore in this case, the section of the subtracting load factor threshold value of the 2nd heat source machine is reduced, the start-up time of the 2nd heat source machine is kept longer as far as possible.So, just can postpone the section of the subtracting opportunity of the 2nd heat source machine, and use the 2nd heat source machine and the 1st heat source machine as far as possible simultaneously, stable output can be realized.
In the control device of above-mentioned heat source system, the maximum exportable heat of described 1st heat source machine be less than described require heat and described maximum exportable load factor is less than described 4th load factor time, the section of subtracting of described 1st heat source machine order can be elevated to the section of the subtracting order higher than described 2nd heat source machine by described changing unit, and the section of the subtracting load factor threshold value of described 1st heat source machine is increased.
The maximum exportable heat of the 1st heat source machine be less than requirement heat and maximum exportable load factor is less than the 4th load factor time, the heat of heat energy collection never can be utilized obviously to diminish, not too can obtain the advantage that use does not utilize heat energy.Therefore in this case, the section of subtracting of the 1st heat source machine order is elevated to higher than the 2nd heat source machine, and the section of the subtracting load factor threshold value of the 1st heat source machine is increased.So, just preferentially can utilize the 2nd heat source machine, and the section of the subtracting opportunity of the 1st heat source machine can be done sth. in advance.
In the control device of above-mentioned heat source system, described 1st arithmetic element can use the heat exchange performance relevant parameter for not utilizing heat energy to adopt the heat exchanger of heat, calculates the maximum exportable heat of described 1st heat source machine.
The heat of heat energy collection can be never utilized to depend on the heat exchange performance of the heat exchanger for not utilizing heat energy heat exchange.Therefore being used for not utilizing heat energy to adopt the heat exchange performance relevant parameter of the heat exchanger of heat by using, calculating the maximum exportable heat of the 1st heat source machine, just can improve the computational accuracy of the maximum exportable heat of the 1st heat source machine.
3rd mode of the present invention is a kind of heat source system, and it possesses: the 1st heat source machine, and it uses lower water etc. not utilize heat energy as adopting thermal source; 2nd heat source machine, what its utilization was different from not utilizing heat energy adopts thermal source; And, the control device of above-mentioned heat source system.
4th mode of the present invention is a kind of control method of heat source system, and described heat source system possesses: the 1st heat source machine, and it uses lower water etc. not utilize heat energy as adopting thermal source; And, the 2nd heat source machine, what its utilization was different from not utilizing heat energy adopts thermal source, and wherein, the control method of described heat source system comprises: the increasing section order of input about each described heat source machine and the process of increasing section load factor threshold value; Calculate the process of the maximum exportable heat of described 1st heat source machine; Calculate the process of the maximum exportable load factor of described 1st heat source machine; Use the maximum exportable heat of described 1st heat source machine and maximum exportable load factor, change the increasing section order of each described heat source machine of input and increase the process of section load factor threshold value; And, according to up-to-date increasing section order and the increasing section load factor threshold value of input, control the process of the increasing section of each described heat source machine.
5th mode of the present invention is a kind of control method of heat source system, and described heat source system possesses: the 1st heat source machine, and it uses lower water etc. not utilize heat energy as adopting thermal source; And, the 2nd heat source machine, what its utilization was different from not utilizing heat energy adopts thermal source, and wherein, the control method of described heat source system comprises: the section of the subtracting order of the relevant each described heat source machine of input and the process of the section of subtracting load factor threshold value; Calculate the process of the maximum exportable heat of described 1st heat source machine; Calculate the process of the maximum exportable load factor of described 1st heat source machine; Use the maximum exportable heat of described 1st heat source machine and maximum exportable load factor, change the section of the subtracting order of each described heat source machine of input and the process of the section of subtracting load factor threshold value; And, according to the up-to-date section of subtracting order and the section of the subtracting load factor threshold value of input, control the process of the section of subtracting of each described heat source machine.
Beneficial effect
The present invention can obtain and heat energy can not utilized as far as possible as adopting thermal source, and realizes the stable effect exported.
Accompanying drawing explanation
Fig. 1 is the summary pie graph of the present invention's wherein heat source system described in an embodiment.
Fig. 2 is the figure representing that the 1st heat source machine shown in Fig. 1 and periphery summary thereof are formed.
Fig. 3 be represent control device possess the functional block diagram that the increase and decrease of heat source machine in various function section controls relevant staple.
Fig. 4 represents the increasing section order of preserving in storage part shown in Fig. 3, the figure increasing section load factor threshold value, the section of subtracting order, the section of subtracting a load factor threshold value wherein example.
Fig. 5 represents the present invention's wherein section of increasing order described in an embodiment and increase the figure of setting process flow process of section load factor threshold value.
Fig. 6 is the figure of setting process flow process representing the present invention wherein section of subtracting order and the section of subtracting load factor threshold value described in an embodiment.
Detailed description of the invention
Below with reference to accompanying drawing, to the present invention, wherein heat source system described in an embodiment and control device thereof and control method are described.
Fig. 1 is the summary pie graph of the present invention's wherein heat source system described in an embodiment.Heat source system described in present embodiment is the heat source system 1 of heating use, and the heating medium for heating that temperature after being used in external loading reduces is supplied to external loading again by it after assigned temperature.
As shown in Figure 1, heat source system 1 possesses 4 heat source machine 2a ~ 2d.Wherein 2 heat source machines 2a, 2b are that the following water of example, rivers and creeks water, underground water, well water, seawater or lake water etc. do not utilize heat energy as adopting thermal source, and exportable heat is according to the heat source machine not utilizing the state of heat energy change.Such as, do not utilize the exportable heat of heat energy can according to temperature and flow change, when similar lower water etc. comprise dirt, also can according to changes such as the heat exchange performances of heat exchanger.Fig. 1 illustrates and uses lower water as the situation not utilizing heat energy in addition.
Heat source machine 2c, 2d use such as air etc. from the thermal source not utilizing heat energy different as the heat source machine adopting thermal source, are the heat source machines that can realize comparatively stablizing output.Fig. 1 illustrates and utilizes air as the situation of adopting thermal source.
So, described in present embodiment, heat source system 1 possesses: at least 1 heat source machine 2a, 2b, and it does not utilize heat energy as adopting thermal source; And at least 1 heat source machine 2c, 2d, it uses the non-heat energy that do not utilize as adopting thermal source, compensates comparatively stable output.When following basis adopts the difference differentiation heat source machine of thermal source, heat source machine 2a, 2b are called the 1st heat source machine 2a, 2b, heat source machine 2c, 2d are called the 2nd heat source machine 2c, 2d.Fig. 1 illustrates the situation possessing 2 the 1st heat source machines 2a, 2b and 2 the 2nd heat source machines 2c, 2d, but number of units is not limited thereto.
Heat source machine 2a, 2b possess respectively: evaporimeter 4, and it carries out heat exchange between refrigerant and heat source water; Compressor 5, its compression refrigerant; Condenser 6, carries out heat exchange between its heating agent (such as, warm water) supplied at refrigerant and external loading 9; And refrigerant loop 3, it is provided with expansion valve 7 as main composition.
In this heat source machine 2a, 2b, after utilizing the heat source water of the heat heating of lower water to carry out heat exchange with refrigerant in evaporimeter 4, heating refrigerant.In evaporimeter 4, be introduced into compressor 5 by the low-voltage high-temperature gas coolant heated, after making the gas coolant of high pressure-temperature, be sent to condenser 6.In condenser 6, by carrying out heat exchange between the refrigerant of pressure high temperature hot gas refrigerant and heating agent (warm water) and heat heating agent making, then the heating agent after heating up is supplied to external loading 9.After the aqueous refrigerant of high pressure low temperature cooled under almost isobaric condition after carrying out heat exchange with heating agent is expanded under isenthalpic conditions by expansion valve 7, be introduced into evaporimeter 4, and evaporate after again carrying out heat exchange between heat source water, become the gas coolant of low-voltage high-temperature, be then introduced into compressor 4.
The heat source water that carry out heat exchange with refrigerant in evaporimeter 4 after, temperature reduces is sent to heat exchanger 8, is heated by carrying out heat exchange with lower water.Heat source water after heating is sent to evaporimeter 4 again.Dispel the heat after carrying out heat exchange as the lower water of thermal source in heat exchanger 8, cooled lower water returns drainage pipeline.The lower water turning back to drainage pipeline is such as sent to other system and again utilizes as thermal source.
Be provided with the air heat exchanger 4' carrying out heat exchange between refrigerant and air in heat source machine 2c, 2d and replace evaporimeter 4.So, in heat source machine 2c, 2d, the low-voltage high-temperature gas coolant heated carry out heat exchange between refrigerant and air after is introduced into compressor 5.In addition, the formation beyond air heat exchanger 4' is identical with above-mentioned heat source machine 2a, 2b, therefore detailed.
Fig. 2 is the figure representing that above-mentioned 1st heat source machine 2a and periphery summary thereof are formed.As shown in Figure 2, the heat source water heated after carrying out heat exchange with lower water in heat exchanger 8 is introduced into evaporimeter 4 by heating agent pipe arrangement 20.Be provided with near the entrance of the evaporimeter 4 of heat source water pipe arrangement 20 and measure heat source water inlet temperature T
lItemperature sensor 31.The heat source water cooled carry out heat exchange with refrigerant in evaporimeter 4 after is introduced into heat exchanger 8 by heat source water pipe arrangement 20.Be provided with near the outlet of the evaporimeter 4 of heat source water pipe arrangement 20 and measure heat source water outlet temperature T
lOtemperature sensor 32 and measure heat source water flow F
lflow sensor 33.
After using in external loading 9 (with reference to figure 1), the heating agent of cooling is introduced into condenser 6 by heating agent pipe arrangement 21.The heating agent heated carry out heat exchange with refrigerant in condenser 6 after is supplied to external loading 9 by heating agent pipe arrangement 21.Be provided with near the outlet of the condenser 6 of heating agent pipe arrangement 21 and measure heat medium outlet temperature T
hOtemperature sensor 36.
The measured value of above-mentioned each sensor is sent to control device 10 (with reference to figure 1).Control device 10 uses the exportable maximum heat of sensor measured value computing the 1st heat source machine 2a, 2b and maximum load rate, according to these operation results, the increase and decrease section order of adjustment heat source machine 2a ~ 2d and increase and decrease section load factor threshold value, make as far as possible effectively utilization not utilize heat energy, thus the increase and decrease section of carrying out according to the heat source machine 2a ~ 2d of these orders and threshold value control.
Control device 10 is such as computer, possesses: the main storage devices such as CPU (central operation treating apparatus), RAM (RandomAccessMemory), secondary storage device, by carrying out the communicator etc. of information interaction with external device communication.
Secondary storage device is the recording medium can carrying out computer reading, such as, comprise disk, photomagneto disk, CD-ROM, DVD-ROM, semiconductor memory etc.This secondary storage device preserves various program, and program reads main storage device from secondary storage device by CPU, realizes various process by performing a programme.
Fig. 3 be represent control device 10 possess heat source machine 2a ~ 2d in various function and increase and decrease the functional block diagram that section controls relevant staple.
As shown in Figure 3, control device 10 possesses storage part 11, the 1st operational part 12, the 2nd operational part 13, changing unit 14 and increase and decrease section control part 15 as main composition.
In storage part 11, each heat source machine 2a ~ 2d is preserved respectively and increase section order (boot sequence), the section of subtracting order (stopping order), increasing section load factor threshold value and the section of subtracting load factor threshold value.Herein, about increasing section load factor threshold value, be in the heat source machine of running status, when load factor exceedes the increasing section load factor threshold value of this heat source machine, the heat source machine being in next increasing section order starts.Therefore, increase section load factor threshold value higher, the startup of the heat source machine being in next increasing section order just can be made to get over backward delay.About the section of subtracting load factor threshold value, be in the heat source machine of running status, time below the section of the subtracting load factor threshold value that load factor is this heat source machine, this heat source machine stopped.Therefore, the section of subtracting load factor threshold value is lower, and this heat source machine just can be made to run more of a specified duration.
Fig. 4 represents an example of the initial value (default value) increasing section order (boot sequence), the section of subtracting order (stopping order), increasing section load factor threshold value and the section of subtracting load factor threshold value.As shown in Figure 4, increase section order and be set with the 1st heat source machine 2a, the 1st heat source machine 2b, the 2nd heat source machine 2c, the 2nd heat source machine 2d in order from high to low, increase section load factor threshold value and the 1st heat source machine 2a, 2b and the 2nd heat source machine 2c is all set as 85%.In addition, the 2nd heat source machine 2d finally section of increasing, does not therefore specially set and increases section load factor threshold value.
The section of subtracting order is set with the 2nd heat source machine 2d, the 2nd heat source machine 2c, the 1st heat source machine 2b, the 1st heat source machine 2a from high to low according to the section of subtracting order, and the 2nd heat source machine 2d, the 2nd heat source machine 2c and the 1st heat source machine 2b are all set as 40% by the section of subtracting load factor threshold value.In addition, the 1st heat source machine 2a finally section of subtracting, does not therefore specially set the section of subtracting load factor threshold value.
So, initial value is set to preferential the increase and decrease section order and the increase and decrease section load factor threshold value that use the 1st heat source machine 2a, 2b.
Herein, the initial value of increasing section order (boot sequence) shown in Fig. 4, the section of subtracting order (stopping order), increasing section load factor threshold value and the section of subtracting load factor threshold value is such as stored in not shown non-volatile memory, from non-volatile memory, read above-mentioned default value information during startup, and be saved in storage part 11.And, use aftermentioned changing unit 14 according to the lower water state of each time period, increasing section order (boot sequence) of preserving in change storage part 11, the section of subtracting order (stopping order), increasing section load factor threshold value and the section of subtracting load factor threshold value, carry out increase and decrease section according to up-to-date increase and decrease section order and increase and decrease section load factor threshold value and control.
1st operational part 12 calculates the exportable maximum heat of the 1st heat source machine 2a and maximum exportable heat Q
h.Herein, as shown in Figure 2, adopt thermal source because the 1st heat source machine 2a and the 1st heat source machine 2b shares one, therefore maximum exportable heat gets identical value.Therefore, the maximum exportable heat Q of any 1st heat source machine of computing (being the 1st heat source machine 2a in present embodiment)
hjust enough.In addition, the maximum exportable heat Q of the 1st heat source machine 2b can certainly be calculated
hreplace the 1st heat source machine 2a.
The maximum exportable heat Q of the 1st heat source machine 2a
h(kW) such as can according to Q
h=Q
l+ Q
h/ COP carries out derivation by following (1) formula and tries to achieve.
Q
H=Q
L×COP/(COP-1)(1)
(1) in formula, Q
l(kW) adopt heat for heat source water, can be derived by following (2) formula and try to achieve.
Q
L=(T
LI-T
LO)×F
L×ρ
L×C
L/3600(2)
In above-mentioned (2) formula, T
lIfor heat source water inlet temperature (DEG C), the measured value of serviceability temperature sensor 31.T
lOfor heat source water outlet temperature (DEG C), the measured value of serviceability temperature sensor 32.F
lfor heat source water flow (m
3/ h), the measured value of use traffic sensor 33.ρ
lfor the density (kg/m of heat source water
3), C
lfor thermal source specific heat of water (kJ/kgK), use the constant preset respectively.
COP (-) is by the measured value of temperature sensor 36 and heat medium outlet temperature T
hOthe measured value of (DEG C) and temperature sensor 32 and thermal source water outlet temperature T
lO(DEG C) substitutes into the well-known value of specifying and calculating in arithmetic expression.
1st operational part 12 possesses the maximum exportable heat Q calculating above-mentioned 1st heat source machine 2a
hrequired various arithmetic expressions, after the measured value being derived from each sensor is substituted into these arithmetic expressions, calculate the maximum exportable heat Q of the 1st heat source machine 2a
h.
2nd operational part 13 calculates the maximum exportable load factor PL of the 1st heat source machine 2a
h.Maximum exportable load factor PL
hfollowing (3) formula is used to calculate.In addition, maximum exportable load factor PL
hwith maximum exportable heat Q
hequally, also the value of the 1st heat source machine 2b can be used as this value.
PL
h=Q
h/ rated heat (3)
(3) in formula, Q
hit is the maximum exportable heat of the 1st heat source machine 2a calculated in the 1st operational part 12.Rated heat uses the designated value (kW) preset.Herein, rated heat according to the running status of heat source machine, such as, according to warm water outlet temperature T
hO, heat source water outlet temperature T
lOset.
So, the maximum exportable load factor PL of the 1st heat source machine 2a
hby the operation result i.e. maximum exportable heat Q of the 1st heat source machine 2a of above-mentioned 1st operational part 12
hcalculate divided by rated heat.
Changing unit 14 uses the maximum exportable heat Q of the 1st heat source machine 2a calculated by the 1st operational part 12
hand the maximum exportable load factor PL of the 1st heat source machine 2a to be calculated by the 2nd operational part 13
h, change increase and decrease section order and the increase and decrease section load factor threshold value of each heat source machine preserved in storage part 11.
Such as, changing unit 14 possess external loading 9 requirement heat Qreq, do not utilize heat energy actively to utilize load factor (the 1st load factor, the 3rd load factor) PLmax, do not utilize heat energy passiveness to utilize the information of load factor (the 2nd load factor, the 4th load factor) PLmin, heat Qreq and maximum exportable heat Q as requested
hcomparative result and maximum exportable load factor PL
hactively utilize load factor PLmax with not utilizing heat energy and do not utilize heat energy passiveness to utilize the comparative result of load factor PLmin, change increase and decrease section order and the increase and decrease section load factor threshold value of each heat source machine preserved in storage part 11.
Herein, do not utilize heat energy actively to utilize load factor PLmax and do not utilize heat energy passiveness to utilize load factor PLmin to be the value that can set arbitrarily, not utilizing heat energy passiveness to utilize load factor PLmin to be set smaller than and do not utilize heat energy actively to utilize the value of load factor PLmax.
Increase and decrease section control part 15 is according to the increase and decrease section order of preserving in storage part 11 and increase and decrease section load factor threshold value, the increase and decrease section of control of heat source machine 2a ~ 2d.In addition, when using changing unit 14 change increase and decrease section order and increase and decrease section load factor threshold value, because the information of preserving in storage part 11 upgrades to some extent, the control increasing and decreasing section therefore can be carried out according to the information after renewal.
Below with reference to Fig. 5 and Fig. 6, to the 1st operational part 12 ~ changing unit 14 possessed by above-mentioned control device 10, mainly the increase and decrease section order of execution and the setting process of increase and decrease section load factor threshold value are described.Fig. 5 increases section relevant treatment flow process, and Fig. 6 is the section of subtracting relevant treatment flow process.Below respective flow process is described.
First, the measured value (step SA1) of temperature sensor 31,32,35 and flow sensor 33 mensuration is obtained when increasing section.
Then, use each measured value, above-mentioned (1) formula and (2) formula of obtaining, calculate the maximum exportable heat Q of the 1st heat source machine 2a
h(step SA2).
Then, the maximum exportable heat Q by obtaining in step SA2
hmaximum exportable load factor PL is calculated divided by rated heat
h(step SA3).
Then, the maximum exportable heat Q will calculated in step SA2
hwith require that heat Qreq compares (step SA4).Its result, maximum exportable heat Q
hduring for requiring more than heat Qreq, the maximum exportable load factor PL calculated in determination step SA3
hwhether be do not utilize heat energy actively to utilize more than load factor PLmax (step SA5).
Its result, maximum exportable load factor PL
hwhen actively utilizing more than load factor PLmax for not utilizing heat energy, the increasing section load factor threshold value of the 1st heat source machine 2a, the 2b preserved in storage part 11 is made to increase (step SA6).Such as, in this case, be derived from lower water to adopt heat many, lower water can be utilized more energetically, therefore increasing section load factor threshold value can be changed to value (the maximum exportable load factor PL such as, calculated in step SA3 being greater than 85%
h).So, just can postpone the increasing section opportunity of the 2nd heat source machine 2c, 2d, and realize the operation only utilizing the 1st heat source machine 2a, 2b as far as possible.
In step SA5, maximum exportable load factor PL
hbe less than when not utilizing heat energy actively to utilize load factor PLmax, maintain the default value (step SA7) preserved in storage part 11.
On the other hand, in step SA4, maximum exportable heat Q
hwhen being less than requirement heat Qreq, the maximum exportable load factor PL calculated in determination step SA3
hwhether be do not utilize heat energy passiveness to utilize more than load factor PLmin (step SA8).
Its result, maximum exportable load factor PL
hwhen utilizing more than load factor PLmin for not utilizing heat energy passiveness, the increasing section load factor threshold value of the 1st heat source machine 2a, 2b is made to reduce (step SA9).Such as, in this case, be derived from lower water to adopt heat little, not too can utilize lower water energetically.Therefore, increasing section load factor threshold value is altered to value (the maximum exportable load factor PL such as, calculated by the 2nd operational part 13 being less than 85%
h), adjustment makes the 2nd heat source machine 2c, 2d start as early as possible.
In step SA8, maximum exportable load factor PL
hbe less than when not utilizing heat energy passiveness to utilize load factor PLmin, obviously can diminish from the heat of lower hydromining collection, not too can obtain the advantage using lower water.Therefore, be reduced to lower than the 2nd heat source machine 2c, 2d by the increasing section of the 1st heat source machine 2a, 2b order, change order makes the 2nd heat source machine 2c, 2d preferentially utilize, and makes the increasing section load factor threshold value of the 2nd heat source machine 2c, 2d increase (step SA10).So, just preferentially can utilize the 2nd heat source machine 2c, 2d, and the increasing section opportunity of the 1st heat source machine 2a, 2b can be postponed.
And after above-mentioned process performed repeatedly with the time interval of specifying, can adopt heat according to what be derived from water under each time period, setting reasonably increases section opportunity and increases section order.And, according to the increasing section opportunity after so changing and increase the increasing section that section order carries out heat source machine 2a ~ 2d and control, the operation of the heat source machine 2a ~ 2d as far as possible effectively using lower hydromining heat just can be realized.
Then, during the section of subtracting in the step SB1 of Fig. 6 ~ SB4, the process of step SA1 ~ SA4 in flow process when carrying out above-mentioned increasing section equally.In step SB4, maximum exportable heat Q
hduring for requiring more than heat Qreq, the maximum exportable load factor PL calculated in determination step SB3
hwhether be do not utilize heat energy actively to utilize more than load factor PLmax (step SB5).
Its result, maximum exportable load factor PL
hwhen actively utilizing more than load factor PLmax for not utilizing heat energy, the section of the subtracting load factor threshold value of the 2nd heat source machine 2c, the 2d preserved in storage part 11 is made to increase (step SB6).Such as, in this case, be derived from lower water to adopt heat many, lower water can be utilized energetically.Therefore, the section of the subtracting load factor threshold value of the 2nd heat source machine 2c, 2d is changed to the value (such as, 50% etc.) being greater than 40%, ahead of time the section of the subtracting opportunity of the 2nd heat source machine 2c, 2d.So just can utilize the 1st heat source machine 2a, 2b as far as possible energetically.
In step SB5, maximum exportable load factor PL
hbe less than when not utilizing heat energy actively to utilize load factor PLmax, maintain the default value (step SB7) preserved in storage part 11.
On the other hand, in step SB4, maximum exportable heat Q
hwhen being less than requirement heat Qreq, the maximum exportable load factor PL calculated in determination step SB3
hwhether be do not utilize heat energy passiveness to utilize more than load factor PLmin (step SB8).
Its result, maximum exportable load factor PL
hwhen utilizing more than load factor PLmin for not utilizing heat energy passiveness, the section of the subtracting load factor threshold value of the 2nd heat source machine 2c, 2d is made to reduce (step SB9).Such as, in this case, be derived from lower water to adopt heat little, not too can utilize lower water energetically.Therefore, the section of the subtracting load factor threshold value of the 2nd heat source machine 2c, 2d is changed to the value (such as, 35% etc.) being less than 40%, the start-up time of the 2nd heat source machine 2c, 2d is kept longer as far as possible.So, just can postpone the section of the subtracting opportunity of the 2nd heat source machine 2c, 2d, and use the 2nd heat source machine 2c, 2d and the 1st heat source machine 2a, 2b as far as possible simultaneously, thus realize stable output.
In step SB8, maximum exportable load factor PL
hbe less than when not utilizing heat energy passiveness to utilize load factor PLmin, obviously can diminish from the heat of lower hydromining collection, not too can obtain the advantage using lower water.Therefore in this case, the section of subtracting of the 1st heat source machine 2a, 2b order is elevated to higher than the 2nd heat source machine 2c, 2d, and makes the section of the subtracting load factor threshold value of the 1st heat source machine 2a, 2b increase (step SB10).So, just preferentially can utilize the 2nd heat source machine 2c, 2d, and the section of the subtracting opportunity of the 1st heat source machine 2a, 2b can be done sth. in advance.
And after above-mentioned process performed repeatedly with the time interval of specifying, can adopt heat according to what be derived from water under each time period, setting is the section of subtracting opportunity and the section of subtracting order reasonably.And the section of subtracting of carrying out heat source machine 2a ~ 2d according to the section of the subtracting opportunity after like this change and the section of subtracting order controls, the operation of the heat source machine 2a ~ 2d of the lower hydromining heat of as far as possible effectively utilization just can be realized.
Above, in heat source system described in present embodiment 1 and control device 10 and control method thereof, calculate use and do not utilize heat energy as the exportable maximum heat Q of the 1st heat source machine 2a, 2b adopting thermal source
hwith maximum load rate PL
h, according to this maximum exportable heat Q
hand maximum exportable load factor PL
h, change increase and decrease section order and increase and decrease section load factor threshold value, therefore, it is possible to set corresponding to the heat that can never utilize heat energy to gather, suitable increase and decrease section order and increase and decrease section load factor threshold value.So just can realize the operation of the heat source machine 2a ~ 2d as far as possible effectively using lower hydromining heat.
In addition, present embodiment is when increasing the Duan Shiyu section of subtracting, use general not utilizing heat energy actively to utilize load factor PLmax and do not utilize heat energy passiveness to utilize load factor PLmin, but also can make not utilize heat energy actively to utilize load factor PLmax and do not utilize heat energy passiveness to utilize the value of load factor PLmin when increasing the Duan Shiyu section of subtracting different.
Present embodiment uses heat source water inlet temperature T
lI, heat source water outlet temperature T
lO, and heat source water flow F
l, what calculate the heat source water of the 1st heat source machine 2a, 2b adopts heat Q
l, and use calculate heat source water adopt heat Q
l, the maximum exportable heat Q of computing the 1st heat source machine 2a, 2b
h, but such as, when the 1st heat source machine 2a, 2b stops etc. for a long time, the heat exchange of heat source water and lower water can stop, and may occur the situation that lower hydromining heat cannot be reflected to heat source water temperature.Therefore in this case, such as, when dwell time exceedes the designated duration preset, the initial value of increase and decrease section order and increase and decrease section load factor threshold value can be read storage part 11, and this initial value can be used to carry out the control of increase and decrease section.
What present embodiment used (2) formula computing heat source water adopts heat Q
l, but the arithmetic expression of the heat exchange performance relevant parameter of temperature and flow and the heat exchanger 8 comprising and do not utilize heat energy can also be used to replace (2) formula, what calculate heat source water adopts heat Q
l.
As the heat exchange performance relevant parameter of heat exchanger 8, such as can exemplify to after the washing and cleaning operation of heat exchanger 8 through the parameter that number of days (elapsed time) is relevant, and to after the rainy day surges through parameter that number of days (elapsed time) is relevant.More through number of days after the washing and cleaning operation of heat exchanger 8, then accumulation of mud is more, and heat exchange performance decreases.After raining, lower water increases, and utilize this effect to clean the rear all raisings of heat exchange performance of heat exchanger 8, therefore the rainy day surges and also can obtain the effect identical with the washing and cleaning operation of heat exchanger 8.So, use the temperature of heat source water and the heat exchange performance relevant parameter of flow and heat exchanger 8, what calculate heat source water adopts heat Q
l, the mensuration utilizing above-mentioned flow sensor and temperature sensor to carry out can be omitted, and then can System's composition be simplified.
Above to the present invention wherein an embodiment be illustrated, but scope of the present invention is not limited to above-mentioned embodiment, not departing from the scope of INVENTION IN GENERAL, can implement various distortion.
Description of reference numerals
1 heat source system
2a, 2b the 1st heat source machine
2c, 2d the 2nd heat source machine
4 evaporimeters
5 compressors
6 condensers
7 expansion valves
8 heat exchangers
9 external loadings
10 control device
11 storage parts
12 the 1st operational parts
13 the 2nd operational parts
14 changing units
15 increase and decrease section control parts
Claims (14)
1. a control device for heat source system, described heat source system possesses: the 1st heat source machine, and it uses lower water etc. not utilize heat energy as adopting thermal source; And, the 2nd heat source machine, what its utilization was different from not utilizing heat energy adopts thermal source,
The control device of described heat source system possesses: memory cell, its preserve about each described heat source machine increasing section order and increase section load factor threshold value;
1st arithmetic element, it calculates the maximum exportable heat of described 1st heat source machine;
2nd arithmetic element, it calculates the maximum exportable load factor of described 1st heat source machine;
Changing unit, it uses the operation result of described 1st arithmetic element and described 2nd arithmetic element, changes in described memory cell the increasing section order of each described heat source machine preserved and increases section load factor threshold value; And,
Increase section control unit, it is according to the increasing section order of preserving in described memory cell and increase section load factor threshold value, controls the increasing section of each described heat source machine.
2. the control device of heat source system according to claim 1, wherein, described changing unit is possessed appointment and is required heat, specifies the 1st load factor and setting value to be less than the information of appointment the 2nd load factor of described 1st load factor, according to the described comparative result requiring the comparative result of heat and described maximum exportable heat and described maximum exportable load factor and described 1st load factor or described 2nd load factor, change in described memory cell the increasing section order of each described heat source machine preserved and increase section load factor threshold value.
3. the control device of heat source system according to claim 2, wherein, the maximum exportable heat of described 1st heat source machine be described require more than heat and described maximum exportable load factor is more than described 1st load factor time, described changing unit increases the increasing section load factor threshold value of described 1st heat source machine.
4. according to the control device of claim 2 or heat source system according to claim 3, wherein, the maximum exportable heat of described 1st heat source machine be less than described require heat and described maximum exportable load factor is more than described 2nd load factor time, described changing unit reduces the increasing section load factor threshold value of described 1st heat source machine.
5. the control device of the heat source system according to any one of claim 2 to claim 4, wherein, the maximum exportable heat of described 1st heat source machine be less than described require heat and described maximum exportable load factor is less than described 2nd load factor time, described changing unit reduces the increasing section order of described 1st heat source machine, and increases the increasing section load factor threshold value of described 2nd heat source machine.
6. a control device for heat source system, described heat source system possesses: the 1st heat source machine, and it uses lower water etc. not utilize heat energy as adopting thermal source; And, the 2nd heat source machine, what its utilization was different from not utilizing heat energy adopts thermal source,
The control device of described heat source system possesses: memory cell, its preserve about each described heat source machine the section of subtracting order and the section of subtracting load factor threshold value;
1st arithmetic element, it calculates the maximum exportable heat of described 1st heat source machine;
2nd arithmetic element, it calculates the maximum exportable load factor of described 1st heat source machine;
Changing unit, it uses the operation result of described 1st arithmetic element and described 2nd arithmetic element, changes in described memory cell the section of subtracting order and the section of the subtracting load factor threshold value of each described heat source machine preserved;
The section of subtracting control unit, it, according to the section of the subtracting order of preserving in described memory cell and the section of subtracting load factor threshold value, controls the section of subtracting of each described heat source machine.
7. the control device of heat source system according to claim 6, wherein, described changing unit is possessed appointment and is required heat, specifies the 3rd load factor and setting value to be less than the information of appointment the 4th load factor of described 3rd load factor, according to the described comparative result requiring the comparative result of heat and described maximum exportable heat and described maximum exportable load factor and described 3rd load factor or described 4th load factor, change in described storage part the section of subtracting order and the section of the subtracting load factor threshold value of each described heat source machine preserved.
8. the control device of heat source system according to claim 7, wherein, the maximum exportable heat of described 1st heat source machine be greater than described require heat and described maximum exportable load factor is more than described 3rd load factor time, described changing unit increases the section of the subtracting load factor threshold value of described 2nd heat source machine.
9. according to the control device of claim 7 or heat source system according to claim 8, wherein, the maximum exportable heat of described 1st heat source machine be less than described require heat and described maximum exportable load factor is more than described 4th load factor time, described changing unit reduces the section of the subtracting load factor threshold value of described 2nd heat source machine.
10. the control device of the heat source system according to any one of claim 7 to claim 9, wherein, the maximum exportable heat of described 1st heat source machine be less than described require heat and described maximum exportable load factor is less than described 4th load factor time, the section of the subtracting order that described changing unit improves described 1st heat source machine makes its order of section of subtracting higher than described 2nd heat source machine, and increases the section of the subtracting load factor threshold value of described 1st heat source machine.
The control device of 11. heat source systems according to any one of claim 1 to claim 10, wherein, described 1st arithmetic element uses and does not utilize heat energy to adopt the heat exchange performance relevant parameter of heat heat exchanger, calculates the maximum exportable heat of described 1st heat source machine.
12. 1 kinds of heat source systems, it possesses: the 1st heat source machine, and it uses lower water etc. not utilize heat energy as adopting thermal source;
2nd heat source machine, what its utilization was different from not utilizing heat energy adopts thermal source; And,
The control device of the heat source system according to any one of claim 1 to claim 11.
The control method of 13. 1 kinds of heat source systems, described heat source system possesses: the 1st heat source machine, and it uses lower water etc. not utilize heat energy as adopting thermal source; And, the 2nd heat source machine, what its utilization was different from not utilizing heat energy adopts thermal source,
The control method of described heat source system comprises: the increasing section order of registration about each described heat source machine and the process of increasing section load factor threshold value;
Calculate the process of the maximum exportable heat of described 1st heat source machine;
Calculate the process of the maximum exportable load factor of described 1st heat source machine;
Use the maximum exportable heat of described 1st heat source machine and maximum exportable load factor, to the process that increasing section order and the increasing section load factor threshold value of registered each described heat source machine change; And,
According to the most newly-increased section order and the increasing section load factor threshold value of registration, control the process of the increasing section of each described heat source machine.
The control method of 14. 1 kinds of heat source systems, described heat source system possesses: the 1st heat source machine, and it uses lower water etc. not utilize heat energy as adopting thermal source; And, the 2nd heat source machine, what its utilization was different from not utilizing heat energy adopts thermal source,
The control method of described heat source system comprises: the section of the subtracting order of the relevant each described heat source machine of registration and the process of the section of subtracting load factor threshold value;
Calculate the process of the maximum exportable heat of described 1st heat source machine;
Calculate the process of the maximum exportable load factor of described 1st heat source machine;
Use the maximum exportable heat of described 1st heat source machine and maximum exportable load factor, to the process that the section of subtracting order and the section of the subtracting load factor threshold value of registered each described heat source machine change; And,
According to the up-to-date section of subtracting order and the section of the subtracting load factor threshold value of registration, control the process of the section of subtracting of each described heat source machine.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2013066485A JP6008772B2 (en) | 2013-03-27 | 2013-03-27 | Heat source system, control device therefor, and control method therefor |
JP2013-066485 | 2013-03-27 | ||
PCT/JP2014/057573 WO2014156895A1 (en) | 2013-03-27 | 2014-03-19 | Heat source system, and device and method for controlling same |
Publications (2)
Publication Number | Publication Date |
---|---|
CN105074356A true CN105074356A (en) | 2015-11-18 |
CN105074356B CN105074356B (en) | 2017-03-15 |
Family
ID=51623874
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201480010573.0A Expired - Fee Related CN105074356B (en) | 2013-03-27 | 2014-03-19 | Heat source system and its control device and control method |
Country Status (4)
Country | Link |
---|---|
JP (1) | JP6008772B2 (en) |
CN (1) | CN105074356B (en) |
DE (1) | DE112014001702T5 (en) |
WO (1) | WO2014156895A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106969534A (en) * | 2017-03-24 | 2017-07-21 | 张模辉 | A kind of optomagnetic converting system and method |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6663740B2 (en) * | 2016-02-16 | 2020-03-13 | 株式会社竹中工務店 | Heat utilization system |
JP6697891B2 (en) * | 2016-02-16 | 2020-05-27 | 株式会社竹中工務店 | Heat utilization system |
EP3594588B1 (en) * | 2017-03-09 | 2022-07-13 | Mitsubishi Electric Corporation | Geothermal heat pump device |
JP6470345B2 (en) * | 2017-05-08 | 2019-02-13 | 東京ガスエンジニアリングソリューションズ株式会社 | Heat source machine control device and heat source machine system |
JP7407759B2 (en) * | 2021-03-24 | 2024-01-04 | 株式会社関電エネルギーソリューション | Control device and control method |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9112482D0 (en) * | 1990-06-13 | 1991-07-31 | Solmate Inc | Intergrated heating,cooling and ventilation system |
JPH08247496A (en) * | 1995-03-14 | 1996-09-27 | Mayekawa Mfg Co Ltd | Heat pump utilizing system using underground water as heat source, and district heat supplying system incorporating the system |
JP2003262430A (en) * | 2002-03-05 | 2003-09-19 | Jmc Geothermal Engineering Co Ltd | Heat pump using underground heat |
CN102203512A (en) * | 2008-09-05 | 2011-09-28 | 阿兰·穆雷 | Heating system with optimized recovery of waste water heat |
JP5121747B2 (en) * | 2009-01-29 | 2013-01-16 | 株式会社コロナ | Geothermal heat pump device |
US20130037236A1 (en) * | 2010-04-20 | 2013-02-14 | Bsr Technologies | Geothermal facility with thermal recharging of the subsoil |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3140346B2 (en) * | 1995-09-29 | 2001-03-05 | 株式会社クボタ | Heat source side operation method of heat pump and heat source device |
JP2001165526A (en) * | 1999-09-30 | 2001-06-22 | Kubota Corp | Double heat source type heat pump device |
JP4782462B2 (en) * | 2005-04-13 | 2011-09-28 | 新日鉄エンジニアリング株式会社 | Geothermal heat pump device, geothermal heat device equipped with the same, and control method for geothermal heat pump device |
JP2009168256A (en) * | 2008-01-10 | 2009-07-30 | Kimura Kohki Co Ltd | Combination type air conditioning system |
JP5356900B2 (en) * | 2009-04-20 | 2013-12-04 | 株式会社コロナ | Geothermal heat pump device |
JP5831379B2 (en) * | 2011-07-27 | 2015-12-09 | Jfeエンジニアリング株式会社 | HEAT PUMP SYSTEM, ITS CONTROL METHOD AND PROGRAM |
-
2013
- 2013-03-27 JP JP2013066485A patent/JP6008772B2/en active Active
-
2014
- 2014-03-19 WO PCT/JP2014/057573 patent/WO2014156895A1/en active Application Filing
- 2014-03-19 DE DE112014001702.7T patent/DE112014001702T5/en not_active Withdrawn
- 2014-03-19 CN CN201480010573.0A patent/CN105074356B/en not_active Expired - Fee Related
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9112482D0 (en) * | 1990-06-13 | 1991-07-31 | Solmate Inc | Intergrated heating,cooling and ventilation system |
JPH08247496A (en) * | 1995-03-14 | 1996-09-27 | Mayekawa Mfg Co Ltd | Heat pump utilizing system using underground water as heat source, and district heat supplying system incorporating the system |
JP2003262430A (en) * | 2002-03-05 | 2003-09-19 | Jmc Geothermal Engineering Co Ltd | Heat pump using underground heat |
CN102203512A (en) * | 2008-09-05 | 2011-09-28 | 阿兰·穆雷 | Heating system with optimized recovery of waste water heat |
JP5121747B2 (en) * | 2009-01-29 | 2013-01-16 | 株式会社コロナ | Geothermal heat pump device |
US20130037236A1 (en) * | 2010-04-20 | 2013-02-14 | Bsr Technologies | Geothermal facility with thermal recharging of the subsoil |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106969534A (en) * | 2017-03-24 | 2017-07-21 | 张模辉 | A kind of optomagnetic converting system and method |
Also Published As
Publication number | Publication date |
---|---|
WO2014156895A1 (en) | 2014-10-02 |
JP6008772B2 (en) | 2016-10-19 |
CN105074356B (en) | 2017-03-15 |
JP2014190619A (en) | 2014-10-06 |
DE112014001702T5 (en) | 2015-12-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105074356A (en) | Heat source system, and device and method for controlling same | |
CN103370584B (en) | Refrigerating circulatory device and kind of refrigeration cycle control method | |
JP5524571B2 (en) | Heat pump equipment | |
CN102032704B (en) | Heat pump apparatus | |
CN204704908U (en) | Hot water apparatus | |
JP5951397B2 (en) | Air conditioner | |
CN103168204B (en) | Device for estimating flowrate of heating medium, heat source device, and method for estimating flowrate of heating medium | |
JP6413713B2 (en) | Snow and ice air conditioning system | |
JP6943797B2 (en) | Geothermal heat pump device | |
CN117321349A (en) | Computing device, computing method, program, control device, control method, and control program | |
JP2012032091A (en) | Heat pump cycle system | |
CN105378392A (en) | Air-conditioning device | |
CN100567850C (en) | Full-liquid type water-icing machine | |
KR20230044385A (en) | Water purifier with ice maker | |
CN103348196A (en) | Heat source system and control method therefor | |
US10527294B2 (en) | Control of a pump to optimize heat transfer | |
JP2011257098A (en) | Heat pump cycle device | |
KR101456878B1 (en) | Control Method of Performance Test System for Heat Pump | |
JP2012007751A (en) | Heat pump cycle device | |
JP2018170194A (en) | Fuel cell system | |
CN114517962B (en) | Method and device for humidifying air conditioner and air conditioner | |
JP6297324B2 (en) | Refrigeration system and control method thereof | |
JP4434865B2 (en) | Regenerative air conditioner and method for operating the same | |
JP5071146B2 (en) | Heat source system and operation method thereof | |
JP7068861B2 (en) | Chiller system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20170818 Address after: Tokyo, Japan, Japan Patentee after: MITSUBISHI heavy industry refrigeration air conditioning system Co Ltd Address before: Tokyo, Japan, Japan Patentee before: Mit-subishi Heavy Industries Ltd. |
|
TR01 | Transfer of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170315 Termination date: 20210319 |
|
CF01 | Termination of patent right due to non-payment of annual fee |