CN109595717A - The data processing method and data processing equipment of air-conditioner water system balance scheme - Google Patents

The data processing method and data processing equipment of air-conditioner water system balance scheme Download PDF

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CN109595717A
CN109595717A CN201811435924.9A CN201811435924A CN109595717A CN 109595717 A CN109595717 A CN 109595717A CN 201811435924 A CN201811435924 A CN 201811435924A CN 109595717 A CN109595717 A CN 109595717A
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water system
system balance
scheme
balance scheme
flow
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CN109595717B (en
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扶鑫
王鑫
钟文智
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Beijing Persagy Energy-Saving Technology Co Ltd
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Beijing Persagy Energy-Saving Technology Co Ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F5/00Air-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
    • F24F5/0003Exclusively-fluid systems
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/62Control or safety arrangements characterised by the type of control or by internal processing, e.g. using fuzzy logic, adaptive control or estimation of values
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/62Control or safety arrangements characterised by the type of control or by internal processing, e.g. using fuzzy logic, adaptive control or estimation of values
    • F24F11/63Electronic processing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F13/00Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F13/00Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
    • F24F13/02Ducting arrangements
    • GPHYSICS
    • G06COMPUTING; CALCULATING OR COUNTING
    • G06FELECTRIC DIGITAL DATA PROCESSING
    • G06F30/00Computer-aided design [CAD]
    • G06F30/10Geometric CAD
    • G06F30/17Mechanical parametric or variational design
    • GPHYSICS
    • G06COMPUTING; CALCULATING OR COUNTING
    • G06FELECTRIC DIGITAL DATA PROCESSING
    • G06F30/00Computer-aided design [CAD]
    • G06F30/20Design optimisation, verification or simulation
    • GPHYSICS
    • G06COMPUTING; CALCULATING OR COUNTING
    • G06FELECTRIC DIGITAL DATA PROCESSING
    • G06F2113/00Details relating to the application field
    • G06F2113/14Pipes
    • GPHYSICS
    • G06COMPUTING; CALCULATING OR COUNTING
    • G06FELECTRIC DIGITAL DATA PROCESSING
    • G06F2119/00Details relating to the type or aim of the analysis or the optimisation
    • G06F2119/06Power analysis or power optimisation
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02DCLIMATE CHANGE MITIGATION TECHNOLOGIES IN INFORMATION AND COMMUNICATION TECHNOLOGIES [ICT], I.E. INFORMATION AND COMMUNICATION TECHNOLOGIES AIMING AT THE REDUCTION OF THEIR OWN ENERGY USE
    • Y02D10/00Energy efficient computing, e.g. low power processors, power management or thermal management

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
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  • Theoretical Computer Science (AREA)
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  • General Physics & Mathematics (AREA)
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  • Computer Hardware Design (AREA)
  • Evolutionary Computation (AREA)
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  • Mathematical Optimization (AREA)
  • Pure & Applied Mathematics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Management, Administration, Business Operations System, And Electronic Commerce (AREA)
  • Air Conditioning Control Device (AREA)

Abstract

The embodiment of the invention discloses the data processing methods and data processing equipment of a kind of air-conditioner water system balance scheme, by calculating separately the first water system balance scheme and adjusting the calculatings total flow for multiple second water system balance schemes that the first water system balance scheme obtains according to various boundary conditions and calculate the pump selection that total pressure head determines corresponding water system balance scheme, then calculates separately and the totle drilling cost of more different water system balance schemes determines the water system balance scheme selected.The embodiment of the present invention can determine the optimal water system balance scheme of initial cost, hydraulic equilibrium effect, operation energy consumption three's resultant effect by the above method, and energy conservation is realized under the premise of guaranteeing water system hydraulic equilibrium.

Description

The data processing method and data processing equipment of air-conditioner water system balance scheme
Technical field
The present invention relates to Heating, Ventilation and Air Conditioning (HVAC) Technology fields, and in particular to a kind of data processing method of air-conditioner water system balance scheme and Data processing equipment.
Background technique
In public building, the energy consumption of central air conditioner system accounts for about the 50%-60% of building total energy consumption, and cold station energy consumption accounts for Air-conditioning energy consumption ratio is 50%-80%, and air-conditioner water system transmission & distribution energy consumption accounts for about the 10%-20% or so of cold station energy consumption, is The important component of central air conditioner system energy consumption.
The form of air-conditioner water system is divided into constant flow and variable-flow, both form designs are intended to carry out hydraulic equilibrium with full The waterpower demand of sufficient index circuit.Energize and stand in some large-scale centralizeds, will also in conjunction with operational management, by different function region, Runing time etc. divides region water system, also to accomplish mutual hydraulic equilibrium between these branches.One hydraulic equilibrium is perfect Circulation, each branch flow will not overcurrent or deficiency, system heat balance performance can also improve, and not will cause local mistake The comfort of cold, overheat, system improves.
The hydraulic equilibrium of air-conditioner water system can be by adjusting pipeline caliber or in the pipeline of end or in several ends Balanced valve is arranged on horizontal main pipe to realize.But practical investigation discovery, it installs a large amount of balanced valves additional in water system, only accounts for pair The limitation of flow, the resistance for but causing water system rises, so that water pump is run under high lift for a long time.And in several end branch On the general pipeline on road although installation balanced valve improves the degree of coupling between these ends but total supply backwater temperature difference becomes smaller.
Summary of the invention
In view of this, the present invention provides the data processing method and data processing dress of a kind of air-conditioner water system balance scheme It sets, energy conservation optimal water system balance scheme can be determined under the premise of guaranteeing water system hydraulic equilibrium.
In a first aspect, the embodiment of the invention provides a kind of data processing methods of air-conditioner water system balance scheme, comprising:
The first water system balance scheme is obtained, the first water system balance scheme is not provided with valve, and is provided with pipeline And water pump;
The theoretical total flow of each loop in the first water system balance scheme and the theoretical total pressure head of each loop are calculated, And determine the index circuit of the first water system balance scheme;
It is corresponding multiple that the first water system balance scheme acquisition various boundary conditions are adjusted according to various boundary conditions Second water system balance scheme;
Calculate separately the calculating total flow and meter of the first water system balance scheme and each second water system balance scheme Calculate total pressure head;
The water of corresponding water system balance scheme is determined according to the corresponding calculating total flow and calculating total pressure head respectively Pump type selecting;
Calculate separately the total of the totle drilling cost and each second water system balance scheme for obtaining the first water system balance scheme Cost;
Compare the totle drilling cost of different water system balance schemes to determine selected water system balance scheme.
Preferably, the theoretical total flow of each loop in the first water system balance scheme is all ends in respective loops The sum of the theoretical flow at end;
The theoretical total pressure head of each loop in the first water system balance scheme is least favorable end institute in respective loops In the sum of the theoretical pressure difference of all pipelines of branch.
Preferably, the calculating total flow of the first water system balance scheme and each second water system balance scheme is to correspond to The sum of the calculating total flow of all loops in scheme;
The calculating total pressure head of the first water system balance scheme and each second water system balance scheme is in corresponding scheme The calculating total pressure head of branch where least favorable end in index circuit.
Preferably, described to adjust the first water system balance scheme acquisition various boundary conditions according to various boundary conditions Corresponding multiple second water system balance schemes include:
Flow balance valve is installed to obtain in the horizontal main pipe of the non-index circuit of the first water system balance scheme Corresponding second water system balance scheme, wherein the calculating of the non-index circuit of the second water system balance scheme is always flowed Amount is equal with the theoretical total flow of non-index circuit of the first water system balance scheme, the second water system balance scheme Calculate the theoretical total pressure head phase of total pressure head with branch where least favorable end in the index circuit of the first water system balance scheme Deng.
Preferably, described to adjust the first water system balance scheme acquisition various boundary conditions according to various boundary conditions Corresponding multiple second water system balance schemes include:
Flow balance valve is installed to obtain in the end import of the non-index circuit of the first water system balance scheme Corresponding second water system balance scheme, wherein the calculating of the non-index circuit of the second water system balance scheme is always flowed Amount is equal with the theoretical total flow of non-index circuit of the first water system balance scheme, the second water system balance scheme Calculate the theoretical total pressure head phase of total pressure head with branch where least favorable end in the index circuit of the first water system balance scheme Deng.
Preferably, described to adjust the first water system balance scheme acquisition various boundary conditions according to various boundary conditions Corresponding multiple second water system balance schemes include:
Expander is carried out to obtain corresponding second water system balance scheme to the standpipe of the first water system balance scheme, Wherein, in the index circuit of the second water system balance scheme least favorable end calculating flow and the first water system balance The theoretical flow of least favorable end is equal in the index circuit of scheme, the calculating total pressure head of the second water system balance scheme Less than the theoretical total pressure head of branch where least favorable end in the index circuit of the first water system balance scheme.
Preferably, the various boundary conditions include non-index circuit horizontal main pipe installation flow balance valve, At least one of end import installation flow balance valve and expansion standpipe caliber of non-index circuit.
Second aspect, the embodiment of the invention provides a kind of data processing equipments of air-conditioner water system balance scheme, comprising:
Acquiring unit, for obtaining the first water system balance scheme, the first water system balance scheme is not provided with valve, And it is provided with pipeline and water pump;
First computing unit, for calculating the theoretical total flow of each loop in the first water system balance scheme and each The theoretical total pressure head of loop, and determine the index circuit of the first water system balance scheme;
Unit is adjusted, obtains different constraint items for adjusting the first water system balance scheme according to various boundary conditions The corresponding multiple second water system balance schemes of part;
Second computing unit, for calculating separately the first water system balance scheme and each second water system balance scheme Calculating total flow and calculate total pressure head;
Pump selection unit, for determining corresponding water according to the corresponding calculating total flow and calculating total pressure head respectively The pump selection of system balancing scheme;
Third computing unit, for calculating separately the totle drilling cost for obtaining the first water system balance scheme and each second water The totle drilling cost of system balancing scheme;
Selected unit, the totle drilling cost for more different water system balance schemes is to determine selected water system balance side Case.
The third aspect, the embodiment of the invention provides a kind of computer readable storage mediums, store computer program thereon Instruction, wherein the computer program instructions realize method as described in relation to the first aspect when being executed by processor.
Fourth aspect, the embodiment of the invention provides a kind of electronic equipment, including memory and processor, wherein described Memory is for storing one or more computer program instructions, wherein one or more computer program instructions are by institute Processor is stated to execute to realize method as described in relation to the first aspect.
The embodiment of the present invention is by calculating separately the first water system balance scheme and described in being adjusted according to various boundary conditions The calculating total flow and calculating total pressure head determination pair for multiple second water system balance schemes that first water system balance scheme obtains The pump selection for the water system balance scheme answered, then calculates separately and the totle drilling cost of more different water system balance schemes determines Selected water system balance scheme.The embodiment of the present invention can determine initial cost, hydraulic equilibrium effect, operation by the above method The optimal water system balance scheme of energy consumption three's resultant effect realizes energy conservation under the premise of guaranteeing water system hydraulic equilibrium.
Detailed description of the invention
By referring to the drawings to the description of the embodiment of the present invention, the above and other purposes of the present invention, feature and Advantage will be apparent from, in the accompanying drawings:
Fig. 1 is the flow chart of the data processing method of the air-conditioner water system balance scheme of the embodiment of the present invention;
Fig. 2 is the schematic diagram of the water system pipeline of the embodiment of the present invention;
Fig. 3 is the interpretation of result of the first water system balance scheme and each second water system balance scheme of the embodiment of the present invention Figure one;
Fig. 4 is the interpretation of result of the first water system balance scheme and each second water system balance scheme of the embodiment of the present invention Figure two;
Fig. 5 is the schematic diagram of the data processing equipment of the air-conditioner water system balance scheme of the embodiment of the present invention;
Fig. 6 is the schematic diagram of the electronic equipment of the embodiment of the present invention.
Specific embodiment
Below based on embodiment, present invention is described, but the present invention is not restricted to these embodiments.
Fig. 1 is the flow chart of the data processing method of the air-conditioner water system balance scheme of the embodiment of the present invention.Such as Fig. 1 institute Show, the data processing method includes:
S100, the first water system balance scheme is obtained.
The first water system balance scheme is obtained according to fixed buildings.In the present embodiment, first water system balance It is provided with pipeline, water pump and end-equipment in scheme, any valve is not provided in the pipeline.In the present embodiment, The end-equipment is fan coil or air-conditioning.The water pump is set to the water inlet of cooling water pipeline or returning for chilled water At the mouth of a river, for conveying water for the air-conditioning system of fixed buildings.The water segregator of air-conditioning system passes through water system standpipe, horizon bar Pipe and each branched pipe are transported to fan coil, and perhaps air conditioning terminal is built through fan coil or air conditioning terminal air-treatment, satisfaction The environmental demand in space is built, water is pooled to water collector through water return pipeline by fan coil or air conditioning terminal.This building water system Including multiple water system loops.It should be noted that each layer of the water lines that the definition of the loop in this system is building are One loop, each loop may include at least one end-equipment, and the pipeline where each end-equipment belongs to horizontal main pipe Branch line.For example, water system pipeline as shown in Figure 2 by water segregator 4 by water system standpipe 5, horizontal main pipe 10,20, 30 and each branched pipe be transported to end, branched pipe connect (not shown) by threeway part with horizontal main pipe, through end Reason, meets the environmental demand of space, water is pooled to water collector 7 through water return pipeline 6 by end, and grey water system pipeline includes Loop 1, loop 2 and loop 3, loop 1, loop 2 and loop 3 are respectively each layer of the water lines built, and each loop includes 3 A end-equipment, the pipeline where each end-equipment belong to the branch line of corresponding horizontal main pipe 10,20,30.Loop 1 includes End 11-13, loop 2 include end 21-23, and loop 3 includes end 31-33.Certainly, the definition of loop is also possible to end Pipeline where equipment is as a loop, and in this case, each layer of building includes at least a loop.No matter using assorted The definition mode of sample, the mode of data processing are the same.Loop in the present embodiment is each layer of the water pipe with building Road is that a loop is illustrated.
S200, the theoretical total flow for calculating each loop in the first water system balance scheme and theoretical total pressure head.
In the present embodiment, the theoretical total flow of each loop be all ends in respective loops theoretical flow it With;The theoretical total pressure head of each loop is the sum of the theoretical pressure difference of all pipelines of branch where least favorable end in respective loops. Therefore, calculate the first water system balance scheme in each loop theoretical total flow and each loop theoretical total pressure head firstly the need of The theoretical pressure difference of theoretical flow needed for calculating separately each of each loop end and each pipeline, and determine described the The index circuit of one water system balance scheme.The theoretical flow of each end can carry out calculating acquisition according to formula (1), described Formula (1) are as follows:
Wherein, G1nFor the theoretical flow of each end;QnFor cold heat load, QnThe load carried according to different pipelines is not It is same to carry out selection acquisition;CpIt is chilled water in the first water system balance scheme for the specific heat of the water under return water design temperature Hold;ρ is chilled water in the first water system balance scheme for the density of the water under return water design temperature.
In the present embodiment, each pipeline includes the pipeline being directly connected to each end, the horizontal main pipe of each loop and stands The components such as pipe and elbow of pipeline threeway.The theoretical flow for the pipeline being directly connected to each end and the theoretical flow G of each end1nPhase Deng theoretical flow G of the theoretical flow of horizontal main pipe equal to each end of its branch in loop1nThe sum of.It is flat according to the first water system Trend and each pipeline of the pipeline in fixed buildings are (including pipeline, each loop being directly connected to each end in weighing apparatus scheme Horizontal main pipe and standpipe) theoretical flow G2nCalculate the caliber of each pipeline, the calculation formula of caliber are as follows:
Wherein, d1For the caliber of each pipeline;G2nFor the theoretical flow of each pipeline;ν1For the theoretical velocity of each pipeline, ν1It is ginseng It examines " practical heat supplying air conditioning design manual " and chooses acquisition.
According to the caliber value d for calculating each pipeline obtained1, to the caliber d1It is rounded, determines that the nominal of each pipeline is straight Diameter D and internal diameter of the pipeline d2.According to internal diameter of the pipeline d2Calculate the calculating flow velocity ν of each pipeline2, the calculating flow velocity ν of each pipeline2Formula Are as follows:
Wherein, ν2For the calculating flow velocity of each pipeline;G2nFor the theoretical flow of each pipeline;d2For the internal diameter of each pipeline.
The theoretical pressure difference △ P of each pipeline includes the on-way resistance △ P of each pipelineyWith local resistance △ Pj, each pipeline along journey Resistance △ PyIt can be calculated and be obtained according to formula (4):
Wherein, △ PyFor the on-way resistance of each pipeline;ν2For the calculating flow velocity of each pipeline;d2For the internal diameter of each pipeline;λ is Coefficient of frictional resistance;L is the length of each pipeline;ρ is chilled water in the first water system balance scheme for return water design temperature Under water density.
The local resistance △ P of each pipelinejRefer to the connecting components such as several elbow tee pipe fittings installed in pipeline to pipeline Caused by resistance, can according to formula (4) calculate obtain:
△Pj=∑ ξ × △ Py (5)
Wherein, △ PjThe local resistance of each pipeline;ξ is the coefficient of partial resistance of each resistance elements in each pipeline;△PyIt is each The on-way resistance of pipeline.
The theoretical pressure difference △ P of each pipeline and the resistance coefficient S of each pipeline can be calculated according to the following formula:
△Pn=△ Py+△Pj (6)
Wherein, △ P is the theoretical pressure difference of each pipeline;△PjThe local resistance of each pipeline;△PyFor being hindered along journey for each pipeline Power;S is the resistance coefficient of each pipeline;G2nFor the theoretical flow of each pipeline.
S300, the first water system balance scheme is adjusted according to various boundary conditions, and to obtain various boundary conditions corresponding Multiple second water system balance schemes.
In the present embodiment, the various boundary conditions include the horizontal main pipe installation flow equilibrium in non-index circuit Valve installs flow balance valve and expands at least one of standpipe caliber in the end import of non-index circuit.According to above-mentioned Different constraint condition adjusts available to seven the second different water system balance sides of the first water system balance scheme Case, as shown in table 1 below:
The corresponding multiple second water system balance schemes of 1 various boundary conditions of table
S400, the calculating total flow for calculating separately the first water system balance scheme and each second water system balance scheme With calculating total pressure head.
In the present embodiment, the calculating total flow of the first water system balance scheme and each second water system balance scheme For the sum of the calculating total flow of all loops in corresponding scheme, the calculating total flow of each loop is all ends in respective loops Calculate the sum of flow.The calculating total pressure head of the first water system balance scheme and each second water system balance scheme is counterparty In case in index circuit branch where least favorable end calculating total pressure head, branch where least favorable end in index circuit Calculating total pressure head be to be related to the sum of the calculating pressure difference of all pipelines of branch where least favorable end in respective loops.
Scheme 1 is the first water system balance scheme: being not provided on the non-index circuit of the first water system balance scheme Any valve does not also carry out expander to standpipe.The water pump of this scheme needs to meet in index circuit least when choosing The theoretical flow G of sharp end10, and as the theoretical flow G for meeting least favorable end in index circuit10When, the super stream in other ends It measures (i.e. the calculating flow of remaining end is respectively greater than the theoretical flow of end itself).Therefore, the first water system balance scheme Calculate total flow are as follows:
G1=G10+∑G3n (8)
Wherein, G1For the calculating total flow of the first water system balance scheme, G10For least favorable end in index circuit Theoretical flow, G3nFor remaining end in the first water system balance scheme calculating flow (do not include in index circuit least Sharp end).
First water system balance scheme calculates the calculating that total pressure head is branch where least favorable end in index circuit Total pressure head, the calculating total pressure head of branch where least favorable end is to be related to least favorable end in index circuit in index circuit The sum of the calculating pressure difference of all pipelines of branch where end.According to formula (4) it is found that the internal diameter of the pressure difference of each pipeline and each pipeline d2Correlation, since internal diameter of the pipeline is constant, in the calculating total pressure head △ P1 and index circuit of the first water system balance scheme The theoretical total pressure head of branch is equal where least favorable end, i.e. the calculating total pressure head △ P1 and first of the first water system balance scheme The theoretical total pressure head of the index circuit of water system balance scheme is equal.
Scheme 2: it is flat only to install dynamic flow additional on the horizontal main pipe of the non-index circuit of the first water system balance scheme Weigh valve.At this point, the theory of the non-index circuit of the calculating total flow of non-index circuit and the first water system balance scheme is total Flow is equal;The Resistance Value S value for calculating total pressure head, index circuit of index circuit is and in the first water system balance scheme Theoretical total pressure head, the resistance coefficient S of index circuit of index circuit are equal.
The calculating total flow of the water system balance scheme of this programme be all non-index circuits calculating total flow and The sum of calculating total flow of index circuit.In the present solution, the calculating total flow and the first water system of non-index circuit are flat The theoretical total flow of the non-index circuit of weighing apparatus scheme is equal, the calculating flow and the first water of least favorable end in index circuit The theoretical flow of least favorable end is equal in index circuit in system balancing scheme, the super stream in other ends in index circuit It measures (i.e. the calculating flow of remaining end is respectively greater than the theoretical flow of end itself)., therefore, the water system balance side of this programme The calculating total flow of case is the sum of the theoretical flow of each end, it may be assumed that
G2=G10+∑G1n+∑G4n (9)
Wherein, G2The calculating total flow of the water system balance scheme of this programme;G10For least favorable end in index circuit Theoretical flow;G1nFor the theoretical flow of each end in non-index circuit in the first water system balance scheme;G4nFor least favorable The calculating flow (not including the least favorable end in index circuit) of remaining end in loop.
Due to the index circuit of the water system balance scheme of this programme and the least favorable ring of the first water system balance scheme Road is identical, therefore the calculating total pressure head △ P2 of the water system balance scheme of this programme and the calculating of the first water system balance scheme are total Pressure difference △ P1 is equal, i.e. the theoretical stagnation pressure with branch where least favorable end in the index circuit of the first water system balance scheme Difference is equal.
Scheme 3: dynamic flow balance valve only is installed additional in the end import of non-index circuit.At this point, non-index circuit Calculating total flow it is equal with the theoretical total flow of non-index circuit of the first water system balance scheme;The meter of index circuit Calculate total pressure head, index circuit Resistance Value S value with the theoretical total pressure head of index circuit in the first water system balance scheme, The resistance coefficient S of index circuit is equal.The calculating flow of least favorable end and the first water system balance side in index circuit The theoretical flow of least favorable end is equal in index circuit in case, the super flow in other ends in index circuit (i.e. remaining The calculating flow of end is respectively greater than the theoretical flow of end itself).
The calculating that dynamic flow balance valve makes each end in non-index circuit is installed additional in the end of non-index circuit Flow is identical as the theoretical flow of each end in non-index circuit in the first water system balance scheme, at this point, the water of this programme The calculating total flow of system balancing scheme are as follows:
G3=G10+∑G1n+∑G4n (10)
Wherein, G3For the calculating total flow of the water system balance scheme of this programme;G10For least favorable end in index circuit The theoretical flow at end;G1nFor the theoretical flow of each end in non-index circuit in the first water system balance scheme;G4nFor least The calculating flow (not including the least favorable end in index circuit) of remaining end in sharp loop.
Due to the index circuit of the water system balance scheme of this programme and the least favorable ring of the first water system balance scheme Road is identical, therefore the calculating total pressure head △ P3 of the water system balance scheme of this programme and the calculating of the first water system balance scheme are total Pressure difference △ P1 is equal, i.e. the theoretical stagnation pressure with branch where least favorable end in the index circuit of the first water system balance scheme Difference is equal.
Scheme 4: dynamic flow balancing is installed additional on the horizontal main pipe of the non-index circuit of the first water system balance scheme Dynamic flow balance valve is installed in the end import of valve, non-index circuit additional, and pipe of not being antagonistic carries out expander.At this point, non-least favorable The calculating total flow of loop is equal with the theoretical total flow of non-index circuit of the first water system balance scheme;Index circuit To calculate total pressure head, the Resistance Value S value of index circuit total with the theory of index circuit in the first water system balance scheme Pressure difference, the resistance coefficient S of index circuit are equal.The calculating flow of least favorable end and the first water system are flat in index circuit The theoretical flow of least favorable end is equal in index circuit in weighing apparatus scheme, and the super flow in other ends in index circuit is (i.e. The calculating flow of remaining end is respectively greater than the theoretical flow of end itself).
On the horizontal main pipe of non-index circuit and end installs dynamic flow balance valve additional and makes non-index circuit In each end calculating flow it is identical as the theoretical flow of each end in non-index circuit in the first water system balance scheme, this When, the calculating total flow of the water system balance scheme of this programme are as follows:
G4=G10+∑G1n+∑G4n (11)
Wherein, G4For the calculating total flow of the water system balance scheme of this programme;G10For least favorable end in index circuit The theoretical flow at end;G1nFor the theoretical flow of each end in non-index circuit in the first water system balance scheme;G4nFor least The calculating flow (not including the least favorable end in index circuit) of remaining end in sharp loop.
Due to the index circuit of the water system balance scheme of this programme and the least favorable ring of the first water system balance scheme Road is identical, therefore the calculating total pressure head △ P4 of the water system balance scheme of this programme and the calculating of the first water system balance scheme are total Pressure difference △ P1 is equal, i.e. the theoretical stagnation pressure with branch where least favorable end in the index circuit of the first water system balance scheme Difference is equal.
Scheme 5: reasonable expander only is carried out to the standpipe of the first water system balance scheme.At this point, in index circuit least The calculating flow of sharp end is equal with the theoretical flow of least favorable end in index circuit in the first water system balance scheme, most The super flow in other ends (i.e. the calculating flow of remaining end is respectively greater than the theoretical flow of end itself) in unfavorable loop.By It changes in the caliber of standpipe, the calculating total pressure head △ P of branch where least favorable end in the index circuit of this programmewIt can To recalculate acquisition according to formula (4), (5), (6), by calculating least favorable end in the index circuit for knowing this programme The calculating total pressure head △ P of place branchwLess than branch where least favorable end in index circuit in the first water system balance scheme The calculating total pressure head on road.
The end import of non-index circuit and horizontal main pipe do not install dynamic flow balance valve additional, at this time non-least favorable The resistance coefficient S of the resistance coefficient S of each pipeline of loop pipeline corresponding with the first water system balance schemenIt is identical, non-least favorable ring The calculating total pressure head △ P for calculating branch where least favorable end in pressure difference and index circuit of each pipeline in roadwIt is identical, it is non-at this time The calculating flow of each end of index circuit are as follows:
Wherein, Gn5For the calculating flow of each end of the non-index circuit of this programme;△PwFor in index circuit least The calculating total pressure head of branch where sharp end;SnFor the resistance coefficient of each pipeline in the non-index circuit of this programme.
It follows that the calculating total flow of the water system balance scheme of this programme are as follows:
G5=G10+∑G4n+∑Gn5 (13)
Wherein, G5The calculating total flow of the water system balance scheme of this programme;G10For least favorable end in index circuit Theoretical flow;G4nIt (does not include the least favorable end in index circuit for the calculating flow of remaining end in index circuit End);Gn5For the calculating flow of each end in non-index circuit.
It is propped up where least favorable end in the calculating total pressure head △ P5 and index circuit of the water system balance scheme of this programme The equal calculating total pressure head on road is △ Pw.The calculating total pressure head △ P5 of the water system balance scheme of this programme is less than the first water system The calculating total pressure head △ P1 of system balance scheme, i.e., less than least favorable end institute in the index circuit of the first water system balance scheme In the theoretical total pressure head of branch.
Scheme 6: dynamic flow balancing is installed additional on the horizontal main pipe of the non-index circuit of the first water system balance scheme Valve, the end import of non-index circuit rationally widen standpipe withouyt dynamic flow balance valve.At this point, non-least favorable ring The calculating total flow on road is equal with the theoretical total flow of non-index circuit of the first water system balance scheme;In index circuit The theoretical flow phase of the calculating flow and least favorable end in the index circuit of the first water system balance scheme of least favorable end Together, (i.e. the calculating flow of remaining end is respectively greater than the theoretical stream of end itself to the super flow in other ends in index circuit Amount).
Since the caliber of standpipe changes, the calculating of branch is total where least favorable end in the index circuit of this programme Pressure difference △ PwAcquisition can be recalculated according to formula (4), (5), (6), by calculating in the index circuit for knowing this programme The calculating total pressure head △ P of branch where least favorable endwLess than least favorable in index circuit in the first water system balance scheme The calculating total pressure head of branch where end.
The calculating total flow of the water system balance scheme of this programme are as follows:
G6=G10+∑G1n+∑G4n (14)
Wherein, G6The calculating total flow of the water system balance scheme of this programme;G10For least favorable end in index circuit Theoretical flow;G1nFor the theoretical flow of each end in non-index circuit in the first water system balance scheme;G4nFor least favorable The calculating flow (not including the least favorable end in index circuit) of remaining end in loop.
It is propped up where least favorable end in the calculating total pressure head △ P6 and index circuit of the water system balance scheme of this programme The equal calculating total pressure head on road is △ Pw.The calculating total pressure head △ P6 of the water system balance scheme of this programme is less than the first water system The calculating total pressure head △ P1 of system balance scheme, i.e., less than least favorable end institute in the index circuit of the first water system balance scheme In the theoretical total pressure head of branch.
Scheme 7: flat withouyt dynamic flow on the horizontal main pipe of the non-index circuit of the first water system balance scheme Weigh valve, and dynamic flow balance valve is installed in the end import of non-index circuit additional, and rationally widens standpipe.At this point, index circuit The theoretical flow of least favorable end in the index circuit for calculating flow and the first water system balance scheme of middle least favorable end Identical, (i.e. the calculating flow of remaining end is respectively greater than the theory of end itself to the super flow in other ends in index circuit Flow).
Since the caliber of standpipe changes, the calculating of branch is total where least favorable end in the index circuit of this programme Pressure difference △ PwAcquisition can be recalculated according to formula (4), (5), (6), by calculating in the index circuit for knowing this programme The calculating total pressure head △ P of branch where least favorable endwLess than least favorable in index circuit in the first water system balance scheme The theoretical total pressure head of branch where end.
The calculating that dynamic flow balance valve makes each end in non-index circuit is installed additional in the end of non-index circuit Flow is identical as the theoretical flow of each end in non-index circuit in the first water system balance scheme, at this point, the water of this programme The calculating total flow of system balancing scheme are as follows:
G7=G10+∑G1n+∑G4n (15)
Wherein, G7For the calculating total flow of the water system balance scheme of this programme;G10For least favorable end in index circuit The theoretical flow at end;G1nFor the theoretical flow of each end in non-index circuit in the first water system balance scheme;G4nFor least The calculating flow (not including the least favorable end in index circuit) of remaining end in sharp loop.
It is propped up where least favorable end in the calculating total pressure head △ P7 and index circuit of the water system balance scheme of this programme The equal calculating total pressure head on road is △ Pw.The calculating total pressure head △ P7 of the water system balance scheme of this programme is less than the first water system The calculating total pressure head △ P1 of system balance scheme, i.e., less than least favorable end institute in the index circuit of the first water system balance scheme In the theoretical total pressure head of branch.
Scheme 8: dynamic flow balancing is installed additional on the horizontal main pipe of the non-index circuit of the first water system balance scheme Dynamic flow balance valve is installed in the end import of valve, non-index circuit additional, and rationally widens standpipe.At this point, in index circuit The flow of least favorable end is identical as the theoretical flow of least favorable end in the index circuit of the first water system balance scheme, most The super flow in other ends (i.e. the calculating flow of remaining end is respectively greater than the theoretical flow of end itself) in unfavorable loop.
Since the caliber of standpipe changes, the calculating of branch is total where least favorable end in the index circuit of this programme Pressure difference △ PwAcquisition can be recalculated according to formula (4), (5), (6), by calculating in the index circuit for knowing this programme The calculating total pressure head △ P of branch where least favorable endwLess than least favorable in index circuit in the first water system balance scheme The calculating total pressure head of branch where end.
On the horizontal main pipe of non-index circuit and end installs dynamic flow balance valve additional and makes non-index circuit In each end calculating flow it is identical as the theoretical flow of each end in non-index circuit in the first water system balance scheme, this When, the calculating total flow of the water system balance scheme of this programme are as follows:
G8=G10+∑G1n+∑G4n (16)
Wherein, G8For the calculating total flow of the water system balance scheme of this programme;G10For least favorable end in index circuit The theoretical flow at end;G1nFor the theoretical flow of each end in non-index circuit in the first water system balance scheme;G4nFor least The calculating flow (not including the least favorable end in index circuit) of remaining end in sharp loop.
It is propped up where least favorable end in the calculating total pressure head △ P8 and index circuit of the water system balance scheme of this programme The equal calculating total pressure head on road is △ Pw.The calculating total pressure head △ P8 of the water system balance scheme of this programme is less than the first water system The calculating total pressure head △ P1 of system balance scheme, i.e., less than least favorable end institute in the index circuit of the first water system balance scheme In the theoretical total pressure head of branch.
S500, respectively according to the corresponding calculating total flow and calculate total pressure head determine corresponding water system balance scheme Pump selection.
The first water system balance scheme that obtains is calculated separately according to step S400 and seven the second different water systems are flat The calculating total flow and calculating total pressure head of weighing apparatus scheme, can determine the first water system balance scheme and seven the second different water The pump selection of system balancing scheme.
S600, the totle drilling cost and each second water system balance scheme for obtaining the first water system balance scheme are calculated separately Totle drilling cost.
The totle drilling cost of the first water system balance scheme and the totle drilling cost of each second water system balance scheme are calculated separately, In, totle drilling cost includes hardware cost, annual operating cost and investment payback time.Hardware cost includes the peace of pipeline, valve and water pump Dress investment.
S700, the different water system balance schemes of comparison totle drilling cost to determine selected water system balance scheme.
The totle drilling cost for comparing different water system balance schemes can determine selected water system balance scheme.Totle drilling cost packet Include hardware cost, annual operating cost and investment payback time.Hardware cost includes the installation investment of pipeline, valve and water pump.It is preferred that Ground can determine the higher scheme of economy by comparing the totle drilling cost of different water system balance schemes.The embodiment of the present invention can Effectively to realize that air-conditioner water system hydraulic equilibrium rationally reduces pipe network while guaranteeing that assignment of traffic meets each end demand Resistance saves initial cost, and realizes the control of transmission & distribution energy consumption in lower level.
In embodiments of the present invention, the data processing method of above-mentioned air-conditioner water system balance scheme is respectively applied to Beijing In certain newly-built office tower and Hefei large scale business building complex.As can be seen from FIG. 3, by above-mentioned air-conditioner water system balance side When the data processing method of case is applied in the newly-built office tower in Beijing, the annual operating cost of scheme 1 is 13.9 ten thousand;Scheme 2 annual operating cost is 10.9 ten thousand, and the initial cost relative to scheme 1 increases 8.4 ten thousand, and the investment payback time is 2.8 years;Scheme 3 Annual operating cost be 9.6 ten thousand, the initial cost relative to scheme 1 increases 2.7 ten thousand, and the investment payback time is 0.6 year;Scheme 4 Annual operating cost is 9.6 ten thousand, and the initial cost relative to scheme 1 increases 11.1 ten thousand, and the investment payback time is 2.6 years;The year of scheme 5 Operating cost is 8.9 ten thousand, and the initial cost relative to scheme 1 reduces 1.5 ten thousand, the investment payback time 0;The annual running cost of scheme 6 With being 8.2 ten thousand, the initial cost relative to scheme 1 increases 6.9 ten thousand, and the investment payback time is 1.2 years;The annual operating cost of scheme 7 It is 7.2 ten thousand, the initial cost relative to scheme 1 increases 1.2 ten thousand, and the investment payback time is 0.2 year;The annual operating cost of scheme 8 is 7.2 ten thousand, the initial cost relative to scheme 1 increases 9.6 ten thousand, and the investment payback time is 1.4 years.By the annual running cost of above-mentioned each scheme Being compared with, initial cost and investment payback time can determine that scheme 5 is the highest scheme of economy, and standpipe is expanded by DN300 To DN350, pump head can be down to 25m by 32m.It as can be seen from FIG. 4, will be at the data of above-mentioned air-conditioner water system balance scheme When reason method is applied in Hefei large scale business building complex, the annual operating cost of scheme 1 is 22.7 ten thousand;The year of scheme 2 transports Row expense is 17.7 ten thousand, and the initial cost relative to scheme 1 reduces 42.1 ten thousand, and the investment payback time is 0 year;The year of scheme 3 runs Expense is 15.6 ten thousand, and the initial cost relative to scheme 1 reduces 28.1 ten thousand, and the investment payback time is 0 year;The annual running cost of scheme 4 With being 15.6 ten thousand, initial cost is constant, and the investment payback time is 0 year;The annual operating cost of scheme 5 is 14.4 ten thousand, relative to scheme 1 Initial cost reduces 510,000, the investment payback time 0;The annual operating cost of scheme 6 is 13.3 ten thousand, the initial cost relative to scheme 1 Reduce 22.9 ten thousand, the investment payback time is 0 year;The annual operating cost of scheme 7 is 11.7 ten thousand, and the initial cost relative to scheme 1 subtracts Lack 90,000, the investment payback time is 0 year;The annual operating cost of scheme 8 is 11.7 ten thousand, and the initial cost relative to scheme 1 increases 19.1 ten thousand, the investment payback time is 1.8 years.Annual operating cost, initial cost and the investment payback time of above-mentioned each scheme are compared Compared with that can determine that scheme 5 is the highest scheme of economy, standpipe is widened a model under existing design scheme and is calculated, water pump Lift is down to 32m by former 47m.
Fig. 5 is the schematic diagram of the data processing equipment of the air-conditioner water system balance scheme of the embodiment of the present invention.Such as Fig. 5 institute Show, the data processing equipment of the present embodiment includes acquiring unit 41, the first computing unit 42, adjusts the calculating list of unit 43, second Member 44, pump selection unit 45, third computing unit 46 and selected unit 47.Acquiring unit 41 is flat for obtaining the first water system Weighing apparatus scheme wherein the first water system balance scheme is not provided with valve, and is provided with pipeline and water pump.First computing unit 42 For calculating the theoretical total flow and theory total pressure head of each loop in the first water system balance scheme.Unit 43 is adjusted to use Corresponding multiple second water of various boundary conditions are obtained in adjusting the first water system balance scheme according to various boundary conditions System balancing scheme.Second computing unit 44 is flat for calculating separately the first water system balance scheme and each second water system The calculating total flow and calculating total pressure head of weighing apparatus scheme.Pump selection unit 45 is used for respectively according to the corresponding calculating total flow The pump selection of corresponding water system balance scheme is determined with calculating total pressure head.Third computing unit 46.It is obtained for calculating separately Obtain the totle drilling cost of the first water system balance scheme and the totle drilling cost of each second water system balance scheme.Selected unit 47 is used for Compare the totle drilling cost of different water system balance schemes to determine selected water system balance scheme.
Fig. 6 is the schematic diagram of the electronic equipment of the embodiment of the present invention.Electronic equipment shown in fig. 6 is general data processing dress It sets comprising general computer hardware structure includes at least processor 51 and memory 52.Processor 51 and memory 52 It is connected by bus 53.Memory 52 is suitable for the instruction or program that storage processor 51 can be performed.Processor 51 can be independence Microprocessor, be also possible to one or more microprocessor set.Processor 51 is deposited by executing memory 52 as a result, The instruction of storage is realized thereby executing the method flow of embodiment present invention as described above for the processing of data and for other The control of device.Bus 53 links together above-mentioned multiple components, while said modules are connected to 54 He of display controller Display device and input/output (I/O) device 55.Input/output (I/O) device 55 can be mouse, keyboard, modulation /demodulation Device, network interface, touch-control input device, body-sensing input unit, printer and other devices well known in the art.Typically, Input/output device 55 is connected by input/output (I/O) controller 56 with system.Preferably, the electronic equipment of the present embodiment For server.
Meanwhile as skilled in the art will be aware of, the various aspects of the embodiment of the present invention may be implemented as be System, method or computer program product.Therefore, the various aspects of the embodiment of the present invention can take following form: complete hardware Embodiment, complete software embodiment (including firmware, resident software, microcode etc.) usually can all claim herein For the embodiment for combining software aspects with hardware aspect of circuit, " module " or " system ".In addition, side of the invention Face can take following form: the computer program product realized in one or more computer-readable medium, computer can Reading medium has the computer readable program code realized on it.
It can use any combination of one or more computer-readable mediums.Computer-readable medium can be computer Readable signal medium or computer readable storage medium.Computer readable storage medium can be such as (but not limited to) electronics, Magnetic, optical, electromagnetism, infrared or semiconductor system, device or any suitable combination above-mentioned.Meter The more specific example (exhaustive to enumerate) of calculation machine readable storage medium storing program for executing will include the following terms: with one or more electric wire Electrical connection, hard disk, random access memory (RAM), read-only memory (ROM), erasable is compiled portable computer diskette Journey read-only memory (EPROM or flash memory), optical fiber, portable optic disk read-only storage (CD-ROM), light storage device, Magnetic memory apparatus or any suitable combination above-mentioned.In the context of the embodiment of the present invention, computer readable storage medium It can be that can include or store the program used by instruction execution system, device or combine instruction execution system, set Any tangible medium for the program that standby or device uses.
Computer-readable signal media may include the data-signal propagated, and the data-signal of the propagation has wherein The computer readable program code realized such as a part in a base band or as carrier wave.The signal of such propagation can use Any form in diversified forms, including but not limited to: electromagnetism, optical or its any combination appropriate.It is computer-readable Signal media can be following any computer-readable medium: not be computer readable storage medium, and can be to by instructing Program that is that execution system, device use or combining instruction execution system, device to use is communicated, is propagated Or transmission.
Including but not limited to wireless, wired, fiber optic cables, RF etc. or above-mentioned any appropriately combined any can be used Suitable medium transmits the program code realized on a computer-readable medium.
Computer program code for executing the operation for being directed to various aspects of the present invention can be with one or more programming languages Any combination of speech is write, and the programming language includes: programming language such as Java, Smalltalk, C++ of object-oriented etc.; And conventional process programming language such as " C " programming language or similar programming language.Program code can be used as independent software package Fully on the user computer, partly execute on the user computer;Partly exist on the user computer and partly It is executed on remote computer;Or it fully executes on a remote computer or server.It in the latter case, can will be remote Journey computer by include local area network (LAN) or wide area network (WAN) any type of network connection to subscriber computer, or (such as internet by using ISP) can be attached with outer computer.
It is above-mentioned according to the method for the embodiment of the present invention, the flow chart legend of equipment (system) and computer program product and/ Or block diagram describes various aspects of the invention.It will be appreciated that each of flow chart legend and/or block diagram piece and process The combination of block in figure legend and/or block diagram can be realized by computer program instructions.These computer program instructions can be with It is provided to the processor of general purpose computer, special purpose computer or other programmable data processing devices, to generate machine, so that (being executed via computer or the processor of other programmable data processing devices) instruction creation for realizing flow chart and/or The device for the function action specified in block diagram or block.
These computer program instructions can also be stored in can instruct computer, other programmable data processing devices Or in the computer-readable medium that runs in a specific way of other devices, so that the instruction stored in computer-readable medium produces Raw includes the product for realizing the instruction for the function action specified in flowchart and or block diagram block or block.
Computer program instructions can also be loaded on computer, other programmable data processing devices or other devices On so that executed on computer, other programmable devices or other devices it is a series of can operating procedure come generate computer reality Existing process, so that the instruction executed on computer or other programmable devices is provided for realizing in flow chart and/or frame The process for the function action specified in segment or block.
The embodiment of the invention discloses the data processing method and data processing equipment of a kind of air-conditioner water system balance scheme, It is obtained by calculating separately the first water system balance scheme and adjusting the first water system balance scheme according to various boundary conditions The calculating total flow and calculating total pressure head of the multiple second water system balance schemes taken determine corresponding water system balance scheme Pump selection, then calculates separately and the totle drilling cost of more different water system balance schemes determines selected water system balance side Case.The embodiment of the present invention can determine initial cost, hydraulic equilibrium effect, operation energy consumption three resultant effect most by the above method Excellent water system balance scheme realizes energy conservation under the premise of guaranteeing water system hydraulic equilibrium.
The above description is only a preferred embodiment of the present invention, is not intended to restrict the invention, for those skilled in the art For, the invention can have various changes and changes.All any modifications made within the spirit and principles of the present invention are equal Replacement, improvement etc., should all be included in the protection scope of the present invention.

Claims (10)

1. a kind of data processing method of air-conditioner water system balance scheme, comprising:
The first water system balance scheme is obtained, the first water system balance scheme is not provided with valve, and is provided with pipeline and water Pump;
The theoretical total flow of each loop in the first water system balance scheme and the theoretical total pressure head of each loop are calculated, and really The index circuit of the fixed first water system balance scheme;
The first water system balance scheme, which is adjusted, according to various boundary conditions obtains various boundary conditions corresponding multiple second Water system balance scheme;
It calculates separately the calculating total flow of the first water system balance scheme and each second water system balance scheme and calculates total Pressure difference;
Determine that the water pump of corresponding water system balance scheme selects according to corresponding total flow and the calculating total pressure head of calculating respectively Type;
Calculate separately the totle drilling cost of the totle drilling cost and each second water system balance scheme that obtain the first water system balance scheme;
Compare the totle drilling cost of different water system balance schemes to determine selected water system balance scheme.
2. data processing method according to claim 1, which is characterized in that each in the first water system balance scheme The theoretical total flow of loop is the sum of the theoretical flow of all ends in respective loops;
The theoretical total pressure head of each loop in the first water system balance scheme is branch where least favorable end in respective loops The sum of the theoretical pressure difference of all pipelines on road.
3. data processing method according to claim 1, which is characterized in that the first water system balance scheme and Ge The calculating total flow of two water system balance schemes is the sum of the calculating total flow of all loops in corresponding scheme;
The calculating total pressure head of the first water system balance scheme and each second water system balance scheme be in corresponding scheme least The calculating total pressure head of branch where least favorable end in sharp loop.
4. data processing method according to claim 1, which is characterized in that it is described adjusted according to various boundary conditions described in First water system balance scheme obtains the corresponding multiple second water system balance schemes of various boundary conditions
Flow balance valve is installed to obtain correspondence in the horizontal main pipe of the non-index circuit of the first water system balance scheme The second water system balance scheme, wherein the calculating total flow of the non-index circuit of the second water system balance scheme with The theoretical total flow of the non-index circuit of first water system balance scheme is equal, the calculating of the second water system balance scheme Total pressure head is equal with the theoretical total pressure head of branch where least favorable end in the index circuit of the first water system balance scheme.
5. data processing method according to claim 1, which is characterized in that it is described adjusted according to various boundary conditions described in First water system balance scheme obtains the corresponding multiple second water system balance schemes of various boundary conditions
Flow balance valve is installed to obtain correspondence in the end import of the non-index circuit of the first water system balance scheme The second water system balance scheme, wherein the calculating total flow of the non-index circuit of the second water system balance scheme with The theoretical total flow of the non-index circuit of first water system balance scheme is equal, the calculating of the second water system balance scheme Total pressure head is equal with the theoretical total pressure head of branch where least favorable end in the index circuit of the first water system balance scheme.
6. data processing method according to claim 1, which is characterized in that it is described adjusted according to various boundary conditions described in First water system balance scheme obtains the corresponding multiple second water system balance schemes of various boundary conditions
Expander is carried out to obtain corresponding second water system balance scheme to the standpipe of the first water system balance scheme, In, the calculating flow of least favorable end and the first water system balance side in the index circuit of the second water system balance scheme The theoretical flow of least favorable end is equal in the index circuit of case, and the calculating total pressure head of the second water system balance scheme is small The theoretical total pressure head of branch where least favorable end in the index circuit of the first water system balance scheme.
7. data processing method according to claim 1, which is characterized in that the various boundary conditions be included in it is non-least The horizontal main pipe installation flow balance valve of sharp loop is stood in the end import installation flow balance valve of non-index circuit and expansion At least one of pipe caliber.
8. a kind of data processing equipment of air-conditioner water system balance scheme, comprising:
Acquiring unit, for obtaining the first water system balance scheme, the first water system balance scheme is not provided with valve, and sets It is equipped with pipeline and water pump;
First computing unit, for calculate each loop in the first water system balance scheme theoretical total flow and each loop Theoretical total pressure head, and determine the index circuit of the first water system balance scheme;
Unit is adjusted, obtains various boundary conditions pair for adjusting the first water system balance scheme according to various boundary conditions The multiple second water system balance schemes answered;
Second computing unit, by calculating separately based on the first water system balance scheme and each second water system balance scheme It calculates total flow and calculates total pressure head;
Pump selection unit, for determining corresponding water system according to the corresponding calculating total flow and calculating total pressure head respectively The pump selection of balance scheme;
Third computing unit, for calculating separately the totle drilling cost and each second water system that obtain the first water system balance scheme The totle drilling cost of balance scheme;
Selected unit, the totle drilling cost for more different water system balance schemes is to determine selected water system balance scheme.
9. a kind of computer readable storage medium, stores computer program instructions thereon, which is characterized in that the computer program Such as method of any of claims 1-7 is realized in instruction when being executed by processor.
10. a kind of electronic equipment, including memory and processor, which is characterized in that the memory is for storing one or more Computer program instructions, wherein one or more computer program instructions are executed by the processor to realize such as power Benefit requires method described in any one of 1-7.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1619276A (en) * 2004-09-24 2005-05-25 曹琦 Method of calculating central air conditioning waterway system resistance
DE102010022763A1 (en) * 2010-06-05 2011-12-08 Oventrop Gmbh & Co. Kg Method for automatic hydraulic balancing in fluid-carrying systems
CN205481597U (en) * 2016-01-07 2016-08-17 上海龙万机电设备有限公司 Air conditioning water balance system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1619276A (en) * 2004-09-24 2005-05-25 曹琦 Method of calculating central air conditioning waterway system resistance
DE102010022763A1 (en) * 2010-06-05 2011-12-08 Oventrop Gmbh & Co. Kg Method for automatic hydraulic balancing in fluid-carrying systems
CN205481597U (en) * 2016-01-07 2016-08-17 上海龙万机电设备有限公司 Air conditioning water balance system

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
张会琴: "《空调水系统的平衡方法研究》", 《中国优秀硕士学位论文全文数据库社会科学II辑》 *
荆有印等: "《暖通空调设计及系统分析》", 31 January 2010, 中国电力出版社 *

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