CN114139837A - Regional multi-system double-layer distributed optimization scheduling method considering double-layer carbon emission optimization distribution model - Google Patents

Regional multi-system double-layer distributed optimization scheduling method considering double-layer carbon emission optimization distribution model Download PDF

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CN114139837A
CN114139837A CN202210115359.8A CN202210115359A CN114139837A CN 114139837 A CN114139837 A CN 114139837A CN 202210115359 A CN202210115359 A CN 202210115359A CN 114139837 A CN114139837 A CN 114139837A
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power
distribution network
gas
lower layer
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CN114139837B (en
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顾海飞
刘福建
孙晓蕾
车昌盛
黄庆
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China Construction Industrial and Energy Engineering Group Co Ltd
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    • G06Q10/06312Adjustment or analysis of established resource schedule, e.g. resource or task levelling, or dynamic rescheduling
    • GPHYSICS
    • G06COMPUTING; CALCULATING OR COUNTING
    • G06QINFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES; SYSTEMS OR METHODS SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES, NOT OTHERWISE PROVIDED FOR
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    • G06QINFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES; SYSTEMS OR METHODS SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES, NOT OTHERWISE PROVIDED FOR
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Abstract

The invention provides a regional multi-system double-layer dispersion optimization scheduling method considering a double-layer carbon emission optimization distribution model, which constructs the regional multi-energy system double-layer carbon emission optimization distribution model, wherein an upper-layer multi-energy main system mainly considers a power distribution network, a gas distribution network and a heat distribution network system, real-time carbon emission constraint is formulated based on real-time environment monitoring, historical carbon emission of each multi-energy subsystem in a lower-layer region is decomposed to each multi-energy subsystem in the lower-layer region in real time, and each multi-energy subsystem in the lower-layer region needs to meet the real-time carbon emission constraint while being optimized; and finally, solving a double-layer dispersion optimization scheduling model of the multi-energy system in the region between the upper layer and the lower layer by adopting an improved target cascade analysis method. The method can reduce the total network loss of the upper distribution network system of the regional multi-energy system, reduce the operation cost of each energy subsystem in the lower region, and determine the optimal distribution scheme of the whole carbon emission of the regional multi-energy system.

Description

Regional multi-system double-layer distributed optimization scheduling method considering double-layer carbon emission optimization distribution model
Technical Field
The invention belongs to the technical field of operation management of power systems, and particularly relates to a regional multi-system double-layer distributed optimization scheduling method considering a double-layer carbon emission optimization distribution model.
Background
At present, China is still in the middle and later stages of rapid urbanization development, and the energy consumption and carbon emission of various domestic areas continue to increase every year. However, with the increasing energy demand and the worsening of ecological environment problems, regional multi-energy systems are showing new trends. The traditional multi-energy system planning and operation are limited to single energy forms of electricity, natural gas, cold, heat and the like, and complementary advantages and synergistic benefits of the multi-energy systems in regions cannot be fully exerted.
Compared with a single energy system, the regional multi-energy system mainly comprises a comprehensive energy supply and terminal use system, such as a regional power, natural gas and heat distribution system, and coordinated optimization operation of multiple types of energy can be realized by interconnecting terminals of various multi-energy subsystems. In addition, the regional multi-energy system can effectively promote the coordination and complementary operation of various urban energy sources, and fully exert the potential advantages of different types of energy subsystems. Meanwhile, various energy types are comprehensively considered, and the comprehensive energy consumption of the regional multi-energy system can be greatly reduced. Therefore, research on regional multi-energy systems is of great significance to energy conservation and emission reduction in various regions in China.
Multi-energy systems that allow for different subjects exhibit a diverse distribution across various levels and regions. Currently, many researches focus on the influence of models, strategies, demand response or comprehensive demand response mechanism designs, methods and the like on the optimized operation of regional multi-energy systems. In addition, researchers have also studied operational factors that affect carbon emissions during the optimized operation of regional multi-energy systems.
However, in recent years, each region in china has put forward a series of strict requirements for the double-carbon emission reduction policy. Although some scholars consider carbon transaction schemes or real-time energy efficiency indexes in an objective function of an economic dispatching model, low-carbon equipment such as electricity-to-gas equipment and ground source heat pumps is introduced, and low-carbon emission reduction technologies such as a given carbon emission total quota index are provided. However, in the past research, the design of a double-carbon optimal distribution mechanism of a regional multi-energy system comprising a plurality of energy subsystems and a specific distribution network model is less considered, and the influence of the double-carbon emission optimal distribution model of the specific analysis regional multi-energy system on the specific distribution network loss and the economic operation cost of each energy subsystem in the double-layer dispersion coordination optimal scheduling process is also ignored.
Disclosure of Invention
Aiming at the defects in the prior art, the invention provides a regional multi-system double-layer dispersion optimization scheduling method considering a double-layer carbon emission optimization distribution model, which effectively reduces the total network loss of an upper distribution network system of a regional multi-energy system, reduces the operation cost of each energy subsystem in a lower region and can determine the optimal distribution scheme of the whole carbon emission of the regional multi-energy system.
The present invention achieves the above-described object by the following technical means.
A regional multi-system double-layer dispersion optimization scheduling method considering a double-layer carbon emission optimization distribution model comprises the following steps:
step 1: establishing an upper-layer multi-energy main system optimization model comprising an upper-layer optimization objective function and upper-layer optimization constraint conditions;
step 2: establishing an optimization model of each multi-energy subsystem in the lower layer area, wherein the optimization model comprises a lower layer optimization objective function and a lower layer optimization constraint condition;
and step 3: establishing a double-layer carbon emission optimization distribution model between the multi-energy subsystems in the upper-layer multi-energy main system and the lower-layer area, and decomposing a total carbon emission constraint value of the area multi-energy system to the multi-energy main system of the upper-layer power distribution network, the distribution network and the heat distribution network and the multi-energy subsystems in the lower-layer area on the basis of real-time environment detection;
and 4, step 4: inputting a total carbon emission constraint value distribution parameter of the regional multi-energy system, an upper region multi-energy main system and a lower region equipment output parameter of each multi-energy subsystem; setting initial values of coupling variables of a regional multi-energy system, and parameter values and iteration initial values of various multipliers of an improved target cascade analysis method;
and 5: respectively solving the optimized scheduling problem of each multi-energy subsystem in the lower layer area, transmitting the solved coupling variable to the multi-energy main system of the power distribution network, the gas distribution network and the heat distribution network in the upper layer area for optimization, and transmitting the optimized real-time carbon emission of each multi-energy subsystem in the lower layer area to the multi-energy main system in the upper layer area so as to update and decompose the carbon emission constraint value of each multi-energy subsystem in the lower layer area;
step 6: after receiving all variables transmitted by each multi-energy subsystem in the lower layer area, the multi-energy main system of the upper layer area comprises a power distribution network, a gas distribution network and a heat distribution network, respectively solving the optimization problem of the multi-energy main system of the upper layer area, and transmitting the optimized real-time carbon emission amount of the multi-energy main system of the power distribution network, the gas distribution network and the heat distribution network to the multi-energy main system of the upper layer area so as to update the carbon emission constraint value decomposed to the multi-energy main system of the upper layer area;
and 7: checking the convergence condition of the distributed coordination optimization algorithm between the multi-energy subsystems in the upper-layer multi-energy main system and the lower-layer area, stopping iteration when the convergence criterion is met, respectively outputting the optimal scheduling results of the multi-energy subsystems in the upper-layer multi-energy main system and the lower-layer area, updating the multiplier parameter values of the improved target cascade analysis method when the convergence criterion is not met, and returning to the step 5 to continue iterative solution.
Further, in the step 1, an upper layer optimization objective function of the upper layer multi-energy-source main system is established with the goal of minimizing the network loss of the power distribution network, the gas distribution network and the heat distribution network:
Figure DEST_PATH_IMAGE001
Figure 100002_DEST_PATH_IMAGE002
Figure DEST_PATH_IMAGE003
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE004
an optimization objective function for the distribution network;
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for the distribution network
Figure 100002_DEST_PATH_IMAGE006
Time interval circuit
Figure DEST_PATH_IMAGE007
The current of (a);
Figure 100002_DEST_PATH_IMAGE008
for branch of distribution network
Figure 667126DEST_PATH_IMAGE007
The resistance of (1);
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scheduling the period of the cycle for the day ahead;
Figure 100002_DEST_PATH_IMAGE010
the number of nodes of the power distribution network;
Figure DEST_PATH_IMAGE011
the number of branches of the power distribution network;
Figure 100002_DEST_PATH_IMAGE012
an optimization objective function for the gas distribution network;
Figure DEST_PATH_IMAGE013
for distributing gas in
Figure 662895DEST_PATH_IMAGE006
Time interval pressurizer consumptionThe natural gas flow rate of (c);
Figure 100002_DEST_PATH_IMAGE014
is a natural gas pipeline
Figure 583577DEST_PATH_IMAGE006
Average flow over a period of time;
Figure DEST_PATH_IMAGE015
branch of pressurizer for gas distribution network
Figure 100002_DEST_PATH_IMAGE016
The natural gas pipeline damping coefficient of (1);
Figure DEST_PATH_IMAGE017
the number of the nodes for installing the pressurizers on the branch of the gas distribution pipe network;
Figure 100002_DEST_PATH_IMAGE018
the number of the distribution pipe network branches is;
Figure DEST_PATH_IMAGE019
an optimized objective function for the heat distribution network;
Figure 100002_DEST_PATH_IMAGE020
for heat distribution net at
Figure 529186DEST_PATH_IMAGE006
Time interval pipeline
Figure DEST_PATH_IMAGE021
The thermal power of (3);
Figure 100002_DEST_PATH_IMAGE022
for heat distribution net at
Figure 202613DEST_PATH_IMAGE006
Time interval pipeline
Figure 493917DEST_PATH_IMAGE021
Heat power transmission ofA loss coefficient of transmission;
Figure DEST_PATH_IMAGE023
the number of nodes of the heat distribution pipe network;
Figure 100002_DEST_PATH_IMAGE024
the number of branches of the heat distribution pipe network.
Further, the upper layer optimization constraints in step 1 include:
node power and voltage equality/inequality constraints of the power distribution network:
Figure DEST_PATH_IMAGE025
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE026
for the distribution network
Figure 574000DEST_PATH_IMAGE006
Time interval node
Figure DEST_PATH_IMAGE027
The active power injected;
Figure 100002_DEST_PATH_IMAGE028
for the distribution network
Figure 927227DEST_PATH_IMAGE006
Time interval circuit
Figure DEST_PATH_IMAGE029
Active power of (d);
Figure 100002_DEST_PATH_IMAGE030
for the distribution network
Figure 2631DEST_PATH_IMAGE006
Time interval node
Figure 979683DEST_PATH_IMAGE027
The reactive power injected;
Figure DEST_PATH_IMAGE031
for the distribution network
Figure 671696DEST_PATH_IMAGE006
Time interval circuit
Figure 877549DEST_PATH_IMAGE029
The reactive power of (c);
Figure 100002_DEST_PATH_IMAGE032
for the distribution network
Figure 292612DEST_PATH_IMAGE006
The time interval can be scheduled to output power of a coal-fired or diesel generator set;
Figure DEST_PATH_IMAGE033
for the distribution network
Figure 909407DEST_PATH_IMAGE006
Time interval nodes
Figure 619874DEST_PATH_IMAGE027
Active power load of (2);
Figure 100002_DEST_PATH_IMAGE034
for the electrical energy storage of the distribution network side
Figure 832681DEST_PATH_IMAGE006
A charging power of a period;
Figure DEST_PATH_IMAGE035
for the electrical energy storage of the distribution network side
Figure 444795DEST_PATH_IMAGE006
Discharge power of a time period;
Figure 100002_DEST_PATH_IMAGE036
for the distribution network
Figure 717644DEST_PATH_IMAGE006
Time period slave node
Figure 164675DEST_PATH_IMAGE027
The active power transmitted to each multi-energy subsystem of the lower layer area;
Figure DEST_PATH_IMAGE037
representing a multi-energy subsystem in an underlying region;
Figure 100002_DEST_PATH_IMAGE038
the number of each multi-energy subsystem in the lower layer area is collected;
Figure 604009DEST_PATH_IMAGE005
for the distribution network
Figure 570828DEST_PATH_IMAGE006
Segment line
Figure 811316DEST_PATH_IMAGE029
The current of (a);
Figure 496376DEST_PATH_IMAGE008
for branch of distribution network
Figure 96990DEST_PATH_IMAGE029
The resistance of (1);
Figure DEST_PATH_IMAGE039
for branch of distribution network
Figure 590419DEST_PATH_IMAGE029
A reactance of (d);
Figure 100002_DEST_PATH_IMAGE040
the voltage amplitude lower limit value of each node of the power distribution network is set;
Figure DEST_PATH_IMAGE041
the voltage amplitude upper limit value of each node of the power distribution network is obtained;
Figure 100002_DEST_PATH_IMAGE042
for branch of distribution network
Figure 421716DEST_PATH_IMAGE029
An apparent capacity upper limit value of (d);
Figure DEST_PATH_IMAGE043
the apparent capacity of the distribution network is restricted in a variation range;
Figure 100002_DEST_PATH_IMAGE044
is a node
Figure 718705DEST_PATH_IMAGE027
The square of the voltage of (c);
Figure DEST_PATH_IMAGE045
is a node
Figure 100002_DEST_PATH_IMAGE046
The square of the voltage of (c);
the capacity equality/inequality constraint of the electric energy storage equipment on the side of the power distribution network is as follows:
Figure DEST_PATH_IMAGE047
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE048
for the storage battery on the distribution network side
Figure 483530DEST_PATH_IMAGE006
A storage capacity of the time period;
Figure DEST_PATH_IMAGE049
self-discharge efficiency of the storage battery device on the distribution network side;
Figure 100002_DEST_PATH_IMAGE050
the charging efficiency of the storage battery device on the power distribution network side;
Figure DEST_PATH_IMAGE051
the discharge efficiency of the storage battery device on the distribution network side is obtained;
Figure 100002_DEST_PATH_IMAGE052
Figure DEST_PATH_IMAGE053
are binary 0-1 variables;
Figure 100002_DEST_PATH_IMAGE054
the maximum charge rate of the storage battery device is set;
Figure DEST_PATH_IMAGE055
the maximum discharge rate of the storage battery device;
Figure 100002_DEST_PATH_IMAGE056
storing energy for the accumulator means;
Figure DEST_PATH_IMAGE057
and
Figure 100002_DEST_PATH_IMAGE058
respectively the minimum rated storage capacity and the maximum rated storage capacity allowed by the storage battery device;
the power distribution network can schedule the climbing output inequality constraint of the coal/diesel engine set:
Figure DEST_PATH_IMAGE059
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE060
Figure DEST_PATH_IMAGE061
upper limit climbing force restraint system for coal-fired and diesel generator set respectivelyCounting and limiting the lower limit climbing force constraint coefficient; subscript
Figure 100002_DEST_PATH_IMAGE062
Subscript of 1 or 3 for coal-fired unit
Figure 663756DEST_PATH_IMAGE062
When the number is 2, the diesel engine group is represented;
the transmission power inequality constraints of each multi-energy subsystem in the power distribution network and the park are as follows:
Figure DEST_PATH_IMAGE063
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE064
and
Figure DEST_PATH_IMAGE065
are respectively a distribution network
Figure 603637DEST_PATH_IMAGE006
The maximum value and the minimum value of the transmission power of the tie lines between the time interval and each multi-energy subsystem in the park;
based on real-time environment detection, the carbon emission constraint of a coal-fired/diesel generator set can be scheduled by a power distribution network in the upper-layer multi-energy main system:
Figure 100002_DEST_PATH_IMAGE066
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE067
Figure 100002_DEST_PATH_IMAGE068
the carbon emission intensity coefficients of the generated energy per unit time of the coal-fired generator set and the diesel generator set are respectively;
Figure DEST_PATH_IMAGE069
Figure 100002_DEST_PATH_IMAGE070
the upper limit value of the carbon emission constraint which can be relaxed is respectively the coal-fired generator set and the diesel generator set;
Figure DEST_PATH_IMAGE071
Figure 100002_DEST_PATH_IMAGE072
respectively optimizing the carbon emission of a coal-fired generator set and a diesel generator set in real time;
Figure 997709DEST_PATH_IMAGE009
scheduling the period of the cycle for the day ahead; all superscripts
Figure DEST_PATH_IMAGE073
The numbers of the recorded data of the multi-energy main system in the upper layer area and the multi-energy subsystems in the lower layer area in the iterative optimization process are shown.
Further, the upper layer optimization constraints in step 1 include:
the power balance equality and inequality constraint of the distribution network node are as follows:
Figure 100002_DEST_PATH_IMAGE074
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE075
for distributing gas in
Figure 839327DEST_PATH_IMAGE006
The gas flow output by the natural gas source point of the time period;
Figure 100002_DEST_PATH_IMAGE076
and
Figure DEST_PATH_IMAGE077
respectively being natural gas pipelines
Figure 572928DEST_PATH_IMAGE016
In that
Figure 575388DEST_PATH_IMAGE006
Inlet gas flow and outlet gas flow for a time period;
Figure 660018DEST_PATH_IMAGE037
representing a multi-energy subsystem in an underlying region;
Figure 156859DEST_PATH_IMAGE038
the number of each multi-energy subsystem in the lower layer area is collected;
Figure 100002_DEST_PATH_IMAGE078
for distributing gas in
Figure 26857DEST_PATH_IMAGE006
Time period slave node
Figure 950951DEST_PATH_IMAGE073
Transmitting the natural gas pipeline transmission flow to each multi-energy subsystem in the lower layer region;
Figure DEST_PATH_IMAGE079
for natural gas pipeline joint
Figure 37724DEST_PATH_IMAGE073
In that
Figure 72676DEST_PATH_IMAGE006
Natural gas load flow over a period of time;
Figure 843186DEST_PATH_IMAGE013
for distributing gas in
Figure 672602DEST_PATH_IMAGE006
Natural gas flow consumed by the pressurizer over time;
Figure 100002_DEST_PATH_IMAGE080
and
Figure DEST_PATH_IMAGE081
are respectively a gas distribution net
Figure 214048DEST_PATH_IMAGE006
The upper limit value and the lower limit value of the gas flow output by the gas source point in the time interval;
the natural gas pressurizer device is constrained in an inequality way:
Figure 100002_DEST_PATH_IMAGE082
wherein the content of the first and second substances,
Figure 770800DEST_PATH_IMAGE015
branch of pressurizer for gas distribution network
Figure 333500DEST_PATH_IMAGE016
The natural gas pipeline damping coefficient of (1);
Figure 599396DEST_PATH_IMAGE014
is a natural gas pipeline
Figure 427806DEST_PATH_IMAGE006
Average flow over a period of time;
Figure DEST_PATH_IMAGE083
is a natural gas pipeline
Figure 538981DEST_PATH_IMAGE006
Time interval node
Figure 100002_DEST_PATH_IMAGE084
The pressure of (a);
Figure DEST_PATH_IMAGE085
is the compression factor of the pressurizer;
Figure 100002_DEST_PATH_IMAGE086
is a natural gas pipeline
Figure 939876DEST_PATH_IMAGE006
Time interval node
Figure 376673DEST_PATH_IMAGE073
The pressure of (a);
natural gas pipeline flow equality and inequality constraints:
Figure DEST_PATH_IMAGE087
Figure 100002_DEST_PATH_IMAGE088
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE089
is a natural gas pipe section
Figure 554364DEST_PATH_IMAGE016
In that
Figure 734809DEST_PATH_IMAGE006
Gas flow direction of the time period;
Figure 100002_DEST_PATH_IMAGE090
representing a pipe section
Figure 537680DEST_PATH_IMAGE016
In that
Figure 161691DEST_PATH_IMAGE006
Pipe constant of time interval, its value and length of pipe section
Figure DEST_PATH_IMAGE091
And diameter
Figure 100002_DEST_PATH_IMAGE092
(ii) related;
Figure DEST_PATH_IMAGE093
and
Figure 100002_DEST_PATH_IMAGE094
respectively natural gas pipe section
Figure 541856DEST_PATH_IMAGE016
In that
Figure 260414DEST_PATH_IMAGE006
A flow upper limit constraint value and a flow lower limit constraint value of a time period;
Figure DEST_PATH_IMAGE095
and
Figure 100002_DEST_PATH_IMAGE096
are respectively natural gas nodes
Figure 665594DEST_PATH_IMAGE073
Upper and lower pressure limits of (a);
Figure DEST_PATH_IMAGE097
is the natural gas flow index;
the gas network dynamic characteristic equality and inequality constraint:
Figure 100002_DEST_PATH_IMAGE098
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE099
is a natural gas pipeline
Figure 303249DEST_PATH_IMAGE016
In that
Figure 593547DEST_PATH_IMAGE006
Managing and storing time intervals;
Figure 100002_DEST_PATH_IMAGE100
and
Figure DEST_PATH_IMAGE101
are respectively pipelines
Figure 319057DEST_PATH_IMAGE016
In that
Figure 876946DEST_PATH_IMAGE006
Managing an upper limit constraint value and a lower limit constraint value of the time period;
Figure 100002_DEST_PATH_IMAGE102
is a pipe
Figure 295289DEST_PATH_IMAGE016
In that
Figure 56572DEST_PATH_IMAGE006
The initial value of the time interval is managed;
Figure DEST_PATH_IMAGE103
is a pipe
Figure 819996DEST_PATH_IMAGE016
Natural gas pipe inventory after a cycle of operation;
Figure 100002_DEST_PATH_IMAGE104
is a natural gas pipeline
Figure 701233DEST_PATH_IMAGE016
A set of (a);
Figure 821636DEST_PATH_IMAGE009
scheduling the period of the cycle for the day ahead;
the transmission power inequality constraint of the connecting lines between the gas distribution network and each multi-energy subsystem in the lower layer area is as follows:
Figure DEST_PATH_IMAGE105
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE106
and
Figure DEST_PATH_IMAGE107
are respectively a gas distribution net
Figure 758630DEST_PATH_IMAGE006
And the upper limit flow value and the lower limit flow value of the transmission flow of the communication pipeline between the time interval and each multi-energy subsystem in the lower layer area.
Further, the upper layer optimization constraints in step 1 include:
and (3) carrying out constraint of a power balance equation of the heat distribution network nodes:
Figure 100002_DEST_PATH_IMAGE108
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE109
for heat distribution net at
Figure 12894DEST_PATH_IMAGE006
Time interval node
Figure 100002_DEST_PATH_IMAGE110
The thermal power of the injection;
Figure DEST_PATH_IMAGE111
for heat distribution net at
Figure 981594DEST_PATH_IMAGE006
Time interval pipeline
Figure 538477DEST_PATH_IMAGE021
The thermal power of (3);
Figure 100002_DEST_PATH_IMAGE112
for heat distribution net at
Figure 743193DEST_PATH_IMAGE006
Time interval nodes
Figure 660203DEST_PATH_IMAGE110
Thermal power load of (2);
Figure DEST_PATH_IMAGE113
for heat distribution net at
Figure 204447DEST_PATH_IMAGE006
Time interval node
Figure 682964DEST_PATH_IMAGE110
The heating power of (a);
Figure 100002_DEST_PATH_IMAGE114
for heat distribution net at
Figure 843818DEST_PATH_IMAGE006
Transmitting power to hot water pipelines of each multi-energy subsystem in the lower layer region in a time interval;
Figure 298939DEST_PATH_IMAGE022
for heat distribution net at
Figure 291166DEST_PATH_IMAGE006
Time interval pipeline
Figure 189852DEST_PATH_IMAGE021
Thermal power transmission loss coefficient of (1);
the heat source point output power is constrained by an inequality:
Figure DEST_PATH_IMAGE115
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE116
and
Figure DEST_PATH_IMAGE117
are respectively provided with a heat distribution network
Figure 60506DEST_PATH_IMAGE006
Outputting an upper limit value and a lower limit value of thermal power by a heat source point in a time interval;
the transmission power inequality constraint of the heat distribution network pipeline is as follows:
Figure 100002_DEST_PATH_IMAGE118
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE119
and
Figure 100002_DEST_PATH_IMAGE120
are respectively provided with a heat distribution network
Figure 725842DEST_PATH_IMAGE006
Time interval circuit
Figure 838155DEST_PATH_IMAGE021
The upper limit value and the lower limit value of the thermal power flow;
the inequality constraint of the transmission power of the communication pipeline between the heat distribution network and each multi-energy subsystem in the lower layer area is as follows:
Figure DEST_PATH_IMAGE121
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE122
and
Figure DEST_PATH_IMAGE123
are respectively provided with a heat distribution network
Figure 720791DEST_PATH_IMAGE006
The time interval is respectively transmitted with the hot water pipeline between the multi-energy subsystems in the lower layer areaAn upper thermal power limit and a lower thermal power limit.
Further, in the step 2, a lower-layer optimization objective function is established for the optimization objective with the minimum economic operation cost of each multi-energy subsystem in the lower-layer region
Figure 100002_DEST_PATH_IMAGE124
Comprises the following steps:
Figure DEST_PATH_IMAGE125
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE126
is the first in the lower layer region
Figure 72882DEST_PATH_IMAGE037
The economic operating costs of the plurality of multi-energy subsystems;
Figure DEST_PATH_IMAGE127
is the first in the lower layer region
Figure 354959DEST_PATH_IMAGE037
Gas acquisition costs for micro gas turbines within the multiple energy subsystems;
Figure 100002_DEST_PATH_IMAGE128
is the first in the lower layer region
Figure 39887DEST_PATH_IMAGE037
Photovoltaic, fan, micro gas turbine, accumulator, gas storage tank, cold storage tank and heat storage tank in multiple multi-energy subsystems
Figure 14796DEST_PATH_IMAGE006
Total operating cost for a time period;
Figure 653850DEST_PATH_IMAGE038
the number of each multi-energy subsystem in the lower layer area is collected;
Figure DEST_PATH_IMAGE129
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE130
is the price of natural gas;
Figure DEST_PATH_IMAGE131
is the low calorific value of natural gas;
Figure 100002_DEST_PATH_IMAGE132
electricity production efficiency of consuming natural gas for the micro gas turbine;
Figure DEST_PATH_IMAGE133
the heat production efficiency of natural gas consumed by the boiler;
Figure 100002_DEST_PATH_IMAGE134
the number of devices for micro gas turbines;
Figure DEST_PATH_IMAGE135
is as follows
Figure 278299DEST_PATH_IMAGE037
Multiple multi-energy subsystem micro gas turbines in
Figure 365204DEST_PATH_IMAGE006
An output power of the time period;
Figure 100002_DEST_PATH_IMAGE136
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 245435DEST_PATH_IMAGE006
Thermal power input in a time period;
Figure DEST_PATH_IMAGE137
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE138
is the first in the lower layer region
Figure 542424DEST_PATH_IMAGE037
The total operating costs of the photovoltaic, the fan, the micro gas turbine and the energy storage equipment in the multiple energy subsystems;
Figure DEST_PATH_IMAGE139
Figure 100002_DEST_PATH_IMAGE140
Figure DEST_PATH_IMAGE141
Figure 100002_DEST_PATH_IMAGE142
the running costs of the photovoltaic power generation system, the fan, the micro gas turbine and the energy storage equipment are respectively calculated;
Figure DEST_PATH_IMAGE143
Figure 100002_DEST_PATH_IMAGE144
Figure DEST_PATH_IMAGE145
Figure 100002_DEST_PATH_IMAGE146
Figure DEST_PATH_IMAGE147
Figure 100002_DEST_PATH_IMAGE148
Figure DEST_PATH_IMAGE149
respectively photovoltaic, fan, micro gas turbine, storage battery, gas storage tank, cold storage tank and heat storage tankAn operating cost parameter;
Figure 100002_DEST_PATH_IMAGE150
Figure DEST_PATH_IMAGE151
respectively a photovoltaic power and a fan
Figure 992735DEST_PATH_IMAGE006
An output power of the time period;
Figure 100002_DEST_PATH_IMAGE152
Figure DEST_PATH_IMAGE153
Figure 100002_DEST_PATH_IMAGE154
Figure DEST_PATH_IMAGE155
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a heat accumulation tank
Figure 825824DEST_PATH_IMAGE006
The power of the absorbed energy of the time period;
Figure 100002_DEST_PATH_IMAGE156
Figure DEST_PATH_IMAGE157
Figure 100002_DEST_PATH_IMAGE158
Figure DEST_PATH_IMAGE159
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a heat accumulation tank
Figure 20831DEST_PATH_IMAGE006
The power of the released energy of the time period.
Further, in the step 2, the lower layer optimization constraint conditions include power balance constraints of power, natural gas, cold energy, heat energy and waste heat flue gas buses of each multi-energy subsystem in the lower layer region:
Figure 100002_DEST_PATH_IMAGE160
wherein the content of the first and second substances,
Figure 87008DEST_PATH_IMAGE150
Figure 29425DEST_PATH_IMAGE151
respectively a photovoltaic power and a fan
Figure 825342DEST_PATH_IMAGE006
An output power of the time period;
Figure DEST_PATH_IMAGE161
is as follows
Figure 47376DEST_PATH_IMAGE037
Multiple multi-energy subsystem micro gas turbines in
Figure 679477DEST_PATH_IMAGE006
An output power of the time period;
Figure 176317DEST_PATH_IMAGE134
the number of devices for micro gas turbines;
Figure 826742DEST_PATH_IMAGE156
is a storage battery device
Figure 203365DEST_PATH_IMAGE006
Power of the released energy over a period of time;
Figure 572030DEST_PATH_IMAGE152
is a storage battery device
Figure 606982DEST_PATH_IMAGE006
The power of the absorbed energy of the time period;
Figure 100002_DEST_PATH_IMAGE162
Figure DEST_PATH_IMAGE163
respectively comprises an electric heating device and an electric refrigerating device in each multi-energy subsystem in the lower layer area
Figure 62977DEST_PATH_IMAGE006
An electrical power load consumed over a period of time;
Figure 100002_DEST_PATH_IMAGE164
Figure DEST_PATH_IMAGE165
Figure 100002_DEST_PATH_IMAGE166
Figure DEST_PATH_IMAGE167
respectively distribute power, gas, heat and cold in the upper region
Figure 282606DEST_PATH_IMAGE006
Transmitting the power to each multi-energy subsystem in the lower layer region in a time interval;
Figure 100002_DEST_PATH_IMAGE168
Figure DEST_PATH_IMAGE169
Figure 100002_DEST_PATH_IMAGE170
Figure DEST_PATH_IMAGE171
respectively, the multi-energy subsystems in the lower layer area
Figure 217195DEST_PATH_IMAGE006
Electrical, gas, hot, cold power loads for a period of time;
Figure 790259DEST_PATH_IMAGE157
Figure 415276DEST_PATH_IMAGE158
Figure 681172DEST_PATH_IMAGE159
respectively comprises an air storage tank, a cold accumulation tank and a heat accumulation tank
Figure 602309DEST_PATH_IMAGE006
Power of the released energy over a period of time;
Figure 100002_DEST_PATH_IMAGE172
for each multi-energy subsystem in the lower layer region, the heat converter is arranged
Figure 713485DEST_PATH_IMAGE006
Thermal power load consumed over a period of time;
Figure DEST_PATH_IMAGE173
for the waste heat boiler in each multi-energy subsystem in the lower layer area
Figure 911117DEST_PATH_IMAGE006
The waste heat power output in time intervals;
Figure 100002_DEST_PATH_IMAGE174
Figure DEST_PATH_IMAGE175
Figure 100002_DEST_PATH_IMAGE176
Figure DEST_PATH_IMAGE177
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 177275DEST_PATH_IMAGE006
An output power of the time period;
Figure 100002_DEST_PATH_IMAGE178
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 460358DEST_PATH_IMAGE006
Thermal power output in time intervals;
Figure DEST_PATH_IMAGE179
and
Figure 100002_DEST_PATH_IMAGE180
respectively providing a conventional electric load and an adjustable electric load for each multi-energy subsystem terminal in a lower layer area;
Figure DEST_PATH_IMAGE181
Figure 100002_DEST_PATH_IMAGE182
Figure DEST_PATH_IMAGE183
adjustable power, gas and cold loads for the virtual energy output power increase participating in the comprehensive demand response plan respectively;
Figure 100002_DEST_PATH_IMAGE184
Figure DEST_PATH_IMAGE185
Figure 100002_DEST_PATH_IMAGE186
respectively outputting adjustable electricity, gas and cold loads of the power reduction for the virtual energy participating in the comprehensive demand response plan;
Figure DEST_PATH_IMAGE187
and
Figure 100002_DEST_PATH_IMAGE188
respectively a conventional gas load and an adjustable gas load;
Figure DEST_PATH_IMAGE189
and
Figure 100002_DEST_PATH_IMAGE190
respectively a conventional cold load and an adjustable cold load;
Figure DEST_PATH_IMAGE191
Figure 100002_DEST_PATH_IMAGE192
respectively a temperature control type hot air load and a flexible hot water supply type load;
Figure DEST_PATH_IMAGE193
converting factors for waste heat power generation;
Figure 100002_DEST_PATH_IMAGE194
for each multi-energy subsystem terminal in the lower layer area
Figure 77022DEST_PATH_IMAGE006
Electrical loading of the time period.
Further, in step 2, the lower optimization constraint condition includes an energy balance constraint between energy supply devices in each multi-energy subsystem in the lower zone:
Figure DEST_PATH_IMAGE195
wherein the content of the first and second substances,
Figure 102396DEST_PATH_IMAGE174
Figure 710095DEST_PATH_IMAGE175
Figure 11633DEST_PATH_IMAGE176
Figure 730190DEST_PATH_IMAGE177
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 184305DEST_PATH_IMAGE006
An output power of the time period;
Figure 100002_DEST_PATH_IMAGE196
Figure DEST_PATH_IMAGE197
respectively comprises an electric heating device and an electric refrigerating device in each multi-energy subsystem in the lower layer area
Figure 651321DEST_PATH_IMAGE006
An electrical power load consumed over a period of time;
Figure 100002_DEST_PATH_IMAGE198
is an absorption type refrigerating device in each multi-energy subsystem in the lower layer area
Figure 925307DEST_PATH_IMAGE006
An input power of the time period;
Figure DEST_PATH_IMAGE199
Figure 100002_DEST_PATH_IMAGE200
Figure DEST_PATH_IMAGE201
Figure 100002_DEST_PATH_IMAGE202
the conversion efficiency of the electric refrigeration, electric heating, absorption refrigeration and heat converter devices respectively;
Figure 788833DEST_PATH_IMAGE193
is left forThermal power generation conversion factor.
Further, in step 2, the lower optimization constraints include energy coupling constraints between energy supply devices in the multi-energy subsystems in the lower region:
Figure DEST_PATH_IMAGE203
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE204
for the micro gas turbine in each multi-energy subsystem in the lower layer area
Figure 284406DEST_PATH_IMAGE006
An output power of the time period;
Figure DEST_PATH_IMAGE205
the thermoelectric ratio of the micro gas turbine in each multi-energy subsystem in the lower layer area is obtained;
Figure 100002_DEST_PATH_IMAGE206
for the waste heat boiler in each multi-energy subsystem in the lower layer area
Figure 125585DEST_PATH_IMAGE006
The waste heat power input in time intervals;
Figure DEST_PATH_IMAGE207
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 355709DEST_PATH_IMAGE006
An output power of the time period;
Figure 100002_DEST_PATH_IMAGE208
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 665337DEST_PATH_IMAGE006
Thermal power input in a time period;
Figure DEST_PATH_IMAGE209
the efficiency of converting natural gas consumed by the micro gas turbine in each multi-energy subsystem in the lower layer area into electricity;
Figure 100002_DEST_PATH_IMAGE210
the heat conversion efficiency of the gas boilers in each multi-energy subsystem in the lower layer area is obtained;
Figure DEST_PATH_IMAGE211
the heat conversion efficiency of the waste heat boiler in each multi-energy subsystem in the lower layer area is obtained;
Figure 976933DEST_PATH_IMAGE178
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 97335DEST_PATH_IMAGE006
Thermal power output in time intervals;
Figure 100002_DEST_PATH_IMAGE212
for the waste heat boiler in each multi-energy subsystem in the lower layer area
Figure 80335DEST_PATH_IMAGE006
The waste heat power output in time intervals.
Further, in the step 2, the lower layer optimization constraint condition includes the equation and inequality constraints of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank device in each multi-energy subsystem in the lower layer region:
Figure DEST_PATH_IMAGE213
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE214
Figure DEST_PATH_IMAGE215
Figure 100002_DEST_PATH_IMAGE216
Figure DEST_PATH_IMAGE217
the self-discharge efficiency coefficients of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank device are respectively;
Figure 100002_DEST_PATH_IMAGE218
Figure DEST_PATH_IMAGE219
Figure 100002_DEST_PATH_IMAGE220
Figure DEST_PATH_IMAGE221
the charging efficiency coefficients of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank device are respectively;
Figure 100002_DEST_PATH_IMAGE222
Figure DEST_PATH_IMAGE223
Figure 100002_DEST_PATH_IMAGE224
Figure DEST_PATH_IMAGE225
energy release efficiency coefficients of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank device are respectively set;
Figure 100002_DEST_PATH_IMAGE226
Figure DEST_PATH_IMAGE227
Figure 100002_DEST_PATH_IMAGE228
Figure DEST_PATH_IMAGE229
respectively arranged on a storage battery, an air storage tank, a cold storage tank and a heat storage tank
Figure 98713DEST_PATH_IMAGE006
A storage capacity of the time period;
Figure 100002_DEST_PATH_IMAGE230
Figure DEST_PATH_IMAGE231
Figure 100002_DEST_PATH_IMAGE232
Figure DEST_PATH_IMAGE233
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a hot accumulation tank
Figure 991714DEST_PATH_IMAGE006
(ii) a charging power over a period of time;
Figure 100002_DEST_PATH_IMAGE234
Figure DEST_PATH_IMAGE235
Figure 100002_DEST_PATH_IMAGE236
Figure DEST_PATH_IMAGE237
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a hot accumulation tank
Figure 380888DEST_PATH_IMAGE006
Discharge power of a time period;
Figure 100002_DEST_PATH_IMAGE238
the maximum charge multiplying power of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank is obtained;
Figure DEST_PATH_IMAGE239
the maximum discharge multiplying power of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank is obtained;
Figure 100002_DEST_PATH_IMAGE240
Figure DEST_PATH_IMAGE241
are binary 0-1 variables;
Figure 100002_DEST_PATH_IMAGE242
is arranged in a storage battery, a gas storage tank, a cold storage tank and a heat storage tank
Figure 726550DEST_PATH_IMAGE006
A minimum stored energy for a time period;
Figure DEST_PATH_IMAGE243
is arranged in a storage battery, a gas storage tank, a cold storage tank and a heat storage tank
Figure 800816DEST_PATH_IMAGE006
Maximum stored energy for a time period;
Figure 100002_DEST_PATH_IMAGE244
is rated capacity.
Further, in step 2, the lower optimization constraint condition includes inequality constraints of each energy supply device in each multi-energy subsystem in the lower zone:
Figure DEST_PATH_IMAGE245
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE246
and
Figure DEST_PATH_IMAGE247
respectively a micro gas turbine in each multi-energy subsystem in the lower layer area
Figure 279814DEST_PATH_IMAGE006
An upper limit value and a lower limit value of output power of a time period;
Figure 100002_DEST_PATH_IMAGE248
and
Figure DEST_PATH_IMAGE249
respectively an upper limit climbing force constraint coefficient and a lower limit climbing force constraint coefficient of the micro gas turbine;
Figure 100002_DEST_PATH_IMAGE250
Figure DEST_PATH_IMAGE251
Figure 100002_DEST_PATH_IMAGE252
Figure DEST_PATH_IMAGE253
respectively comprises a waste heat boiler, a gas boiler, a photovoltaic device and a wind power device in each multi-energy subsystem in the lower layer area
Figure 86228DEST_PATH_IMAGE006
An upper limit value of output power of the time period;
Figure 100002_DEST_PATH_IMAGE254
Figure DEST_PATH_IMAGE255
Figure 100002_DEST_PATH_IMAGE256
Figure DEST_PATH_IMAGE257
respectively comprises a waste heat boiler, a gas boiler, a photovoltaic device and a wind power device in each multi-energy subsystem in the lower layer area
Figure 371715DEST_PATH_IMAGE006
A lower limit value of the output power of the period.
Further, in step 2, the lower layer optimization constraint condition includes inequality constraints of energy conversion devices in the multi-energy subsystems in the lower layer region:
Figure 100002_DEST_PATH_IMAGE258
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE259
Figure 100002_DEST_PATH_IMAGE260
Figure DEST_PATH_IMAGE261
Figure 100002_DEST_PATH_IMAGE262
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 936425DEST_PATH_IMAGE006
An upper limit value of the period output power;
Figure DEST_PATH_IMAGE263
Figure 100002_DEST_PATH_IMAGE264
Figure DEST_PATH_IMAGE265
Figure 100002_DEST_PATH_IMAGE266
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 758013DEST_PATH_IMAGE006
A lower limit value of the period output power.
Further, in the step 2, the lower-layer optimization constraint condition includes inequality constraint of tie line transmission power between each multi-energy subsystem in the lower-layer region and each distribution network in the upper-layer region:
Figure DEST_PATH_IMAGE267
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE268
Figure DEST_PATH_IMAGE269
Figure 100002_DEST_PATH_IMAGE270
Figure DEST_PATH_IMAGE271
respectively, the multi-energy subsystems in the lower layer area
Figure 997977DEST_PATH_IMAGE006
And the upper limit of the transmission power of the connecting line between the time interval and the distribution network, the heat distribution network and the cold distribution network in the upper layer area.
Further, in step 2, the lower layer optimization constraint condition includes a carbon emission constraint of each multi-energy subsystem in the lower layer region, which is obtained based on real-time environment detection:
Figure 100002_DEST_PATH_IMAGE272
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE273
the comprehensive energy supply carbon emission intensity coefficient of the micro gas turbine, the waste heat boiler and the gas boiler device in each multi-energy subsystem in the lower layer area in unit time is obtained;
Figure 100002_DEST_PATH_IMAGE274
is as follows
Figure 567498DEST_PATH_IMAGE037
Multiple multi-energy subsystem micro gas turbines in
Figure 577043DEST_PATH_IMAGE006
An output power of the time period;
Figure 174508DEST_PATH_IMAGE134
the number of devices for micro gas turbines;
Figure 509675DEST_PATH_IMAGE009
scheduling the period of the cycle for the day ahead;
Figure DEST_PATH_IMAGE275
for the waste heat boiler in each multi-energy subsystem in the lower layer area
Figure 910700DEST_PATH_IMAGE006
The waste heat power input in time intervals;
Figure 100002_DEST_PATH_IMAGE276
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 442044DEST_PATH_IMAGE006
Thermal power output in time intervals;
Figure DEST_PATH_IMAGE277
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 834629DEST_PATH_IMAGE006
Thermal power input in a time period; all superscripts
Figure 809539DEST_PATH_IMAGE073
Both show the iterative optimization of the multi-energy main system in the upper layer area and each multi-energy subsystem in the lower layer areaThe reference numbers of the data recorded during the process,
Figure 100002_DEST_PATH_IMAGE278
the upper limit value of the total carbon emission quota of each multi-energy subsystem in the lower layer area is restricted,
Figure DEST_PATH_IMAGE279
optimizing real-time carbon emissions for operation of the various multi-energy subsystems in the lower region, wherein the subscripts
Figure 100002_DEST_PATH_IMAGE280
Indicating that the lower zone region has 3 multi-energy subsystems; and the third line and the fourth line respectively represent that the real-time carbon emission of each multi-energy subsystem in the lower layer area is calculated uniformly after optimization, and the total carbon emission quota constraint upper limit value of each multi-energy subsystem in the lower layer area is transmitted to the upper layer area.
Further, in step 2, the lower-layer optimization constraint conditions include constraints of movable electrical, gas and cold loads of each multi-energy subsystem terminal in the lower-layer region:
Figure DEST_PATH_IMAGE281
wherein the content of the first and second substances,
Figure 884811DEST_PATH_IMAGE009
scheduling the period of the cycle for the day ahead;
Figure 100002_DEST_PATH_IMAGE282
/
Figure 455732DEST_PATH_IMAGE282
Figure DEST_PATH_IMAGE283
/
Figure 100002_DEST_PATH_IMAGE284
Figure DEST_PATH_IMAGE285
/
Figure 100002_DEST_PATH_IMAGE286
the maximum change power allowed by movable electric, gas and cold loads of each multi-energy subsystem terminal in the lower layer area is respectively;
Figure DEST_PATH_IMAGE287
Figure 100002_DEST_PATH_IMAGE288
Figure DEST_PATH_IMAGE289
Figure 100002_DEST_PATH_IMAGE290
Figure DEST_PATH_IMAGE291
Figure 100002_DEST_PATH_IMAGE292
are binary variables from 0 to 1.
Further, in step 2, the lower layer optimization constraint condition includes constraint of a flexible indoor air conditioning power equivalent model of each multi-energy subsystem terminal user in the lower layer region:
Figure DEST_PATH_IMAGE293
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE294
is composed of
Figure 821598DEST_PATH_IMAGE006
Predicted cold/heat load demand power at a time;
Figure DEST_PATH_IMAGE295
for each multiple energy source in the lower zoneIs sub-system in
Figure 186982DEST_PATH_IMAGE006
Cold or hot power supplied to the end user at any time;
Figure 100002_DEST_PATH_IMAGE296
is composed of
Figure 828179DEST_PATH_IMAGE006
The comfortable temperature of the indoor of each multi-energy subsystem terminal user in the lower layer area is measured at the moment;
Figure DEST_PATH_IMAGE297
and
Figure 100002_DEST_PATH_IMAGE298
the indoor and outdoor air temperature of each multi-energy subsystem terminal user in the lower layer area is measured;
Figure DEST_PATH_IMAGE299
equivalent thermal resistance of a building where each multi-energy subsystem terminal user is located in a lower layer area;
Figure 100002_DEST_PATH_IMAGE300
and
Figure DEST_PATH_IMAGE301
respectively obtaining the minimum value and the maximum value allowed by the indoor temperature fluctuation change of the building where each multi-energy subsystem terminal user is located in the lower layer area;
Figure 100002_DEST_PATH_IMAGE302
Figure DEST_PATH_IMAGE303
respectively are the fluctuation parameters of the cold load and the heat load;
Figure 974428DEST_PATH_IMAGE009
the period of the cycle is scheduled for the day ahead.
Further, in the step 2, the lower-layer optimization constraint condition includes constraint of an indoor flexible hot water supply type load power equivalent model of the building where the terminal users of each multi-energy subsystem in the lower-layer region are located:
Figure 100002_DEST_PATH_IMAGE304
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE305
demand power for the predicted hot water load;
Figure 100002_DEST_PATH_IMAGE306
is a hot water parameter;
Figure DEST_PATH_IMAGE307
is composed of
Figure 479621DEST_PATH_IMAGE006
The cold water storage capacity at the moment;
Figure 100002_DEST_PATH_IMAGE308
is composed of
Figure 780021DEST_PATH_IMAGE006
The storage temperature of the hot water at any moment;
Figure DEST_PATH_IMAGE309
is composed of
Figure 642935DEST_PATH_IMAGE006
The temperature of cold water replacing hot water at any moment;
Figure 100002_DEST_PATH_IMAGE310
is composed of
Figure 818308DEST_PATH_IMAGE006
The hot water quantity required to be provided by each multi-energy subsystem terminal user in the lower layer area at any time;
Figure DEST_PATH_IMAGE311
and
Figure 100002_DEST_PATH_IMAGE312
all are hot water load fluctuation coefficients;
Figure DEST_PATH_IMAGE313
is composed of
Figure 270018DEST_PATH_IMAGE006
The hot water comfort temperature value of the indoor of the building where each multi-energy subsystem terminal user is located in the lower layer area at the moment;
Figure 100002_DEST_PATH_IMAGE314
and
Figure DEST_PATH_IMAGE315
are respectively as
Figure 914888DEST_PATH_IMAGE006
Minimum and maximum allowable hot water storage temperatures;
Figure 796256DEST_PATH_IMAGE009
the period of the cycle is scheduled for the day ahead.
Further, the specific process of step 3 is as follows:
Figure 100002_DEST_PATH_IMAGE316
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE317
the constraint value is a total carbon emission constraint value of the regional multi-energy system, and the constraint value is iteratively updated according to the actual carbon emission optimized by each multi-energy subsystem in the lower region and the power distribution network system in the upper region multi-energy main system in the double-layer optimization process;
Figure 100002_DEST_PATH_IMAGE318
for each multi-energy subsystem in the lower region
Figure 948889DEST_PATH_IMAGE037
Figure DEST_PATH_IMAGE319
) A total carbon emission allowance constraint upper limit value;
Figure 100002_DEST_PATH_IMAGE320
Figure DEST_PATH_IMAGE321
respectively determining the upper limit value of carbon emission constraint of a power distribution network system in the upper-layer multi-energy main system and each multi-energy subsystem in the lower-layer area for the whole area;
Figure 962762DEST_PATH_IMAGE038
the number of each multi-energy subsystem in the lower layer area is collected.
Further, a specific method for solving the complex regional multi-energy system double-layer dispersion coordination optimization scheduling model by adopting the improved target cascade analysis method is as follows:
respectively converting the objective functions of the upper-layer power distribution network, the gas distribution network and the heat distribution network system into the following forms:
Figure 100002_DEST_PATH_IMAGE322
Figure DEST_PATH_IMAGE323
Figure 100002_DEST_PATH_IMAGE324
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE325
Figure 100002_DEST_PATH_IMAGE326
Figure DEST_PATH_IMAGE327
respectively taking the transformed target functions of the distribution network, the distribution network and the heat distribution network system in the upper layer area;
Figure 965484DEST_PATH_IMAGE004
Figure 334149DEST_PATH_IMAGE012
Figure 821631DEST_PATH_IMAGE019
respectively as target functions of the upper power distribution network, the gas distribution network and the heat distribution network system;
Figure 100002_DEST_PATH_IMAGE328
Figure DEST_PATH_IMAGE329
Figure 100002_DEST_PATH_IMAGE330
respectively, the multi-energy subsystems in the lower layer area
Figure 949731DEST_PATH_IMAGE006
Connecting lines among a power distribution network, a gas distribution network and a heat distribution network system in the multi-energy main system in the time interval and the upper region transmit power auxiliary coupling variables;
Figure DEST_PATH_IMAGE331
Figure 100002_DEST_PATH_IMAGE332
Figure DEST_PATH_IMAGE333
the system of a power distribution network, a gas distribution network and a heat distribution network in the multi-energy main system of the upper layer respectively is arranged
Figure 700518DEST_PATH_IMAGE006
Connecting lines between the time interval and each multi-energy subsystem in the lower layer region transmit power coupling variables;
Figure 100002_DEST_PATH_IMAGE334
Figure DEST_PATH_IMAGE335
Figure 100002_DEST_PATH_IMAGE336
the target functions of the power distribution network, the gas distribution network and the heat distribution network are respectively
Figure 713735DEST_PATH_IMAGE006
A first order multiplier of a period lagrange penalty function;
Figure DEST_PATH_IMAGE337
Figure 100002_DEST_PATH_IMAGE338
Figure DEST_PATH_IMAGE339
the target functions of the power distribution network, the gas distribution network and the heat distribution network are respectively
Figure 411433DEST_PATH_IMAGE006
A quadratic multiplier of a period lagrange penalty function;
converting the objective function of each multi-energy subsystem in the lower zone area into the following form:
Figure 100002_DEST_PATH_IMAGE340
wherein the content of the first and second substances,
Figure 536251DEST_PATH_IMAGE037
representing a multi-energy subsystem in an underlying region;
Figure 802147DEST_PATH_IMAGE038
is the lower layer regionThe number of each multi-energy subsystem is integrated;
Figure 879825DEST_PATH_IMAGE009
the period of the cycle is scheduled for the day ahead.
Further, in step 7, as a convergence condition, whether the difference between the coupling variable optimized by the upper/lower layer system and the objective function in the iterative optimization process meets the precision requirement is specifically as follows:
Figure DEST_PATH_IMAGE341
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE342
Figure DEST_PATH_IMAGE343
Figure 100002_DEST_PATH_IMAGE344
respectively representing the convergence precision of the coupling variable difference and the target function difference between the multi-energy main system in the upper layer area and each multi-energy subsystem in the lower layer area; all superscripts
Figure 69629DEST_PATH_IMAGE073
The marks of the recorded data of the multi-energy main system in the upper layer area and the multi-energy subsystems in the lower layer area in the iterative optimization process are both represented;
Figure 549152DEST_PATH_IMAGE037
representing a multi-energy subsystem in an underlying region;
when the convergence criterion is not met, updating each multiplier parameter value of the improved target cascade analysis method according to the following formula, namely updating the quadratic term multiplier parameter value of the Lagrange penalty function:
Figure DEST_PATH_IMAGE345
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE346
the value is 2.5; the value of the lagrange penalty function multiplier is uniformly set to 1.5.
The invention has the following beneficial effects:
the invention constructs a regional multi-energy system double-layer carbon emission optimization distribution model for the first time, an upper region multi-energy main system mainly considers a power distribution network, a gas distribution network and a heat distribution network system, real-time carbon emission constraints are formulated based on real-time environment monitoring, historical carbon emission of each multi-energy subsystem in a lower region is decomposed in real time to each multi-energy subsystem in the lower region, and each multi-energy subsystem in the lower region needs to meet the real-time carbon emission constraints while being optimized; and finally, solving a double-layer dispersion optimization scheduling model of the multi-energy system in the region between the upper layer and the lower layer by adopting an improved target cascade analysis method. The method can reduce the total network loss of the upper distribution network system of the regional multi-energy system, reduce the operation cost of each energy subsystem in the lower region, and determine the optimal distribution scheme of the whole carbon emission of the regional multi-energy system.
Drawings
Fig. 1 is a flowchart of a regional multi-system double-layer decentralized optimization scheduling method considering a double-layer carbon emission optimization distribution model.
Detailed Description
The invention will be further described with reference to the following figures and specific examples, but the scope of the invention is not limited thereto.
The regional multi-system double-layer distributed optimal scheduling method considering the double-layer carbon emission optimal allocation model is shown in fig. 1 and specifically comprises the following steps:
step 1: establishing an upper-layer multi-energy main system optimization model, wherein the upper-layer multi-energy main system optimization model comprises an upper-layer optimization objective function and an upper-layer optimization constraint condition;
the minimum network loss of a power distribution network, a gas distribution network and a heat distribution network is considered as a target, so that three upper-layer optimization objective functions of the upper-layer multi-energy-source main system are respectively as follows:
the power distribution network optimization objective function is as follows:
Figure 100002_DEST_PATH_IMAGE348
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE350
an optimization objective function for the distribution network;
Figure 100002_DEST_PATH_IMAGE352
for the distribution network
Figure 100002_DEST_PATH_IMAGE354
Time interval circuit
Figure 100002_DEST_PATH_IMAGE356
Current in units of a;
Figure 100002_DEST_PATH_IMAGE358
for branch of distribution network
Figure 655123DEST_PATH_IMAGE356
Resistance in units ofohms
Figure 100002_DEST_PATH_IMAGE360
The period of the scheduling cycle is day ahead, and the unit ish
Figure 100002_DEST_PATH_IMAGE362
The number of nodes of the power distribution network;
Figure 100002_DEST_PATH_IMAGE364
the number of branches of the power distribution network;
the optimization objective function of the gas distribution network is as follows:
Figure 100002_DEST_PATH_IMAGE366
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE368
an optimization objective function for the gas distribution network;
Figure 100002_DEST_PATH_IMAGE370
for distributing gas in
Figure 298725DEST_PATH_IMAGE354
Natural gas flow rate in m consumed by the time interval pressurizer3/h;
Figure 100002_DEST_PATH_IMAGE372
Is a natural gas pipeline
Figure 948013DEST_PATH_IMAGE354
Average flow rate in m of time interval3/h;
Figure 100002_DEST_PATH_IMAGE374
Branch of pressurizer for gas distribution network
Figure 100002_DEST_PATH_IMAGE376
The damping coefficient of the natural gas pipeline is usually 0.06-0.10;
Figure 100002_DEST_PATH_IMAGE378
the number of the nodes for installing the pressurizers on the branch of the gas distribution pipe network;
Figure 100002_DEST_PATH_IMAGE380
the number of the distribution pipe network branches is;
the optimization objective function of the heat distribution network is as follows:
Figure 100002_DEST_PATH_IMAGE382
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE384
an optimized objective function for the heat distribution network;
Figure 100002_DEST_PATH_IMAGE386
for heat distribution net at
Figure 301283DEST_PATH_IMAGE354
Time interval pipeline
Figure 100002_DEST_PATH_IMAGE388
The unit of the thermal power of (A) is kW;
Figure 100002_DEST_PATH_IMAGE390
for heat distribution net at
Figure 597398DEST_PATH_IMAGE354
Time interval pipeline
Figure 384088DEST_PATH_IMAGE388
The thermal power transmission loss coefficient is 95% in unit;
Figure 100002_DEST_PATH_IMAGE392
the number of nodes of the heat distribution pipe network;
Figure 100002_DEST_PATH_IMAGE394
the number of branches of the heat distribution pipe network.
The upper-layer optimization constraint condition comprises equality and inequality constraints of a power distribution network system in the upper-layer multi-energy main system, and the equality and inequality constraints of the power distribution network system in the upper-layer multi-energy main system comprise: node power and voltage equality/inequality constraint of a power distribution network, capacity equality/inequality constraint of electric energy storage equipment at the side of the power distribution network, gradable power-saving/power-saving unit climbing output inequality constraint of the power distribution network, junctor transmission power inequality constraint between the power distribution network and each multi-energy subsystem in a park and scalable power-saving/power-saving unit carbon emission constraint of the power distribution network;
the node power and voltage equality/inequality constraints of the power distribution network are as follows:
Figure 100002_DEST_PATH_IMAGE396
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE398
for the distribution network
Figure 709503DEST_PATH_IMAGE354
Time interval node
Figure 100002_DEST_PATH_IMAGE400
The unit of the active power is kW;
Figure 100002_DEST_PATH_IMAGE402
for the distribution network
Figure 350568DEST_PATH_IMAGE354
Time interval circuit
Figure 100002_DEST_PATH_IMAGE404
Active power of (a) in kW;
Figure 100002_DEST_PATH_IMAGE406
for the distribution network
Figure 20846DEST_PATH_IMAGE354
Time interval node
Figure 294833DEST_PATH_IMAGE400
The unit of the injected reactive power is kW;
Figure 100002_DEST_PATH_IMAGE408
for the distribution network
Figure 285923DEST_PATH_IMAGE354
Time interval circuit
Figure 109391DEST_PATH_IMAGE404
The unit of the reactive power of (a) is kW;
Figure 100002_DEST_PATH_IMAGE410
for the distribution network
Figure 527734DEST_PATH_IMAGE354
The output power of the coal-fired or diesel generating set which can be dispatched in time intervals is kW;
Figure 100002_DEST_PATH_IMAGE412
for the distribution network
Figure 765381DEST_PATH_IMAGE354
Time interval nodes
Figure 825741DEST_PATH_IMAGE400
The unit of active power load of (a) is kW;
Figure 100002_DEST_PATH_IMAGE414
for the electrical energy storage of the distribution network side
Figure 175820DEST_PATH_IMAGE354
The unit of charging power of a time interval is kW;
Figure 100002_DEST_PATH_IMAGE416
for the electrical energy storage of the distribution network side
Figure 765064DEST_PATH_IMAGE354
The discharge power of the time period is kW;
Figure 100002_DEST_PATH_IMAGE418
for the distribution network
Figure 498796DEST_PATH_IMAGE354
Time period slave node
Figure 362847DEST_PATH_IMAGE400
The unit of active power transmitted to each multi-energy subsystem of the lower layer area is kW;
Figure 100002_DEST_PATH_IMAGE420
the number of each multi-energy subsystem in the lower layer area is collected;
Figure 100002_DEST_PATH_IMAGE422
for branch of distribution network
Figure 833011DEST_PATH_IMAGE404
Reactance in ohms;
Figure 100002_DEST_PATH_IMAGE424
the unit is the lower limit value of the voltage amplitude of each node of the power distribution network and is kV;
Figure 100002_DEST_PATH_IMAGE426
the unit is the upper limit value of the voltage amplitude of each node of the power distribution network and is kV;
Figure 100002_DEST_PATH_IMAGE428
for branch of distribution network
Figure 481905DEST_PATH_IMAGE404
The apparent capacity upper limit value of (1) in kVA;
Figure 100002_DEST_PATH_IMAGE430
the apparent capacity of the distribution network is restricted in a variation range;
Figure 100002_DEST_PATH_IMAGE432
is a node
Figure 404730DEST_PATH_IMAGE400
The square of the voltage of (c);
Figure 100002_DEST_PATH_IMAGE434
is a node
Figure 100002_DEST_PATH_IMAGE436
Square of the voltage of (c).
The electrical energy storage equipment capacity equality/inequality constraint on the distribution network side is as follows:
Figure 100002_DEST_PATH_IMAGE438
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE440
for the storage battery on the distribution network side
Figure 432992DEST_PATH_IMAGE354
Storage capacity of a time period in kWh;
Figure 100002_DEST_PATH_IMAGE442
the unit of the energy stored by the accumulator device is kWh;
Figure 100002_DEST_PATH_IMAGE444
and
Figure 100002_DEST_PATH_IMAGE446
respectively the minimum rated storage capacity and the maximum rated storage capacity allowed by the storage battery device, wherein the unit is kWh;
Figure 100002_DEST_PATH_IMAGE448
self-discharge efficiency of the storage battery device on the distribution network side;
Figure 100002_DEST_PATH_IMAGE450
the charging efficiency of the storage battery device on the power distribution network side;
Figure 100002_DEST_PATH_IMAGE452
the discharge efficiency of the storage battery device on the distribution network side is obtained;
Figure 100002_DEST_PATH_IMAGE454
Figure 100002_DEST_PATH_IMAGE456
both binary 0-1 variables are used for representing the charging and discharging states of the storage battery device;
Figure 100002_DEST_PATH_IMAGE458
the maximum charge rate of the storage battery device is set;
Figure 100002_DEST_PATH_IMAGE460
the maximum discharge rate of the storage battery device.
The power distribution network dispatchable coal/diesel engine unit climbing output inequality constraint is as follows:
Figure 100002_DEST_PATH_IMAGE462
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE464
Figure 100002_DEST_PATH_IMAGE466
the upper limit climbing output constraint coefficient and the lower limit climbing output constraint coefficient of the coal-fired and diesel generator sets are respectively, and the unit is kW/min; when subscript
Figure 100002_DEST_PATH_IMAGE468
When 1 or 3, represents a coal-fired unit, subscript
Figure 75106DEST_PATH_IMAGE468
When the number is 2, the diesel engine group is represented.
The inequality constraint of the transmission power of the tie line between the power distribution network and each multi-energy subsystem in the park is as follows:
Figure 100002_DEST_PATH_IMAGE470
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE472
and
Figure 100002_DEST_PATH_IMAGE474
are respectively prepared asIn the electric network
Figure 144169DEST_PATH_IMAGE354
The maximum value and the minimum value of the transmission power of the tie lines between the time interval and each multi-energy subsystem in the park are kW.
Based on real-time environment detection, the carbon emission constraint of the power distribution network in the upper-layer multi-energy main system capable of scheduling coal-fired/diesel generator sets is as follows:
Figure 100002_DEST_PATH_IMAGE476
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE478
Figure 100002_DEST_PATH_IMAGE480
the carbon emission intensity coefficients of the generated energy per unit time of the coal-fired generator set and the diesel generator set are respectively, and the unit is t/kWh;
Figure 100002_DEST_PATH_IMAGE482
Figure 100002_DEST_PATH_IMAGE484
the upper limit values of the carbon emission constraint which can be relaxed of the coal-fired generator set and the diesel generator set are respectively, and the unit is t;
Figure 100002_DEST_PATH_IMAGE486
Figure 100002_DEST_PATH_IMAGE488
the carbon emission is respectively the real-time optimized carbon emission of a coal-fired power generator set and a diesel power generator set, and the unit is t/h. The third line and the fourth line of the constraint formula are respectively a coal-fired unit and a diesel unit which can be dispatched by a power distribution network in the upper-layer multi-energy main system, and the real-time carbon emission amount of the coal-fired unit and the diesel unit is calculated and transmitted to the upper-layer multi-energy main system after optimization. All superscripts in this example
Figure 100002_DEST_PATH_IMAGE490
The numbers of the recorded data of the multi-energy main system in the upper layer area and the multi-energy subsystems in the lower layer area in the iterative optimization process are shown.
The upper-layer optimization constraint condition further comprises equality and inequality constraints of the gas distribution network system in the upper-layer multi-energy-source main system, and the equality and inequality constraints of the gas distribution network system in the upper-layer multi-energy-source main system comprise: the system comprises a gas distribution network node power balance equality and inequality constraint, a natural gas pressurizer device inequality constraint, a natural gas pipeline flow equality and inequality constraint, a gas network dynamic characteristic equality and inequality constraint, and a connecting line transmission power inequality constraint between a gas distribution network and each multi-energy subsystem in a lower layer region;
the power balance equation and inequality constraint of the distribution network node are as follows:
Figure 100002_DEST_PATH_IMAGE492
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE494
for distributing gas in
Figure 39444DEST_PATH_IMAGE354
The unit of the gas flow output by the natural gas source point of the time interval is m3/h;
Figure 100002_DEST_PATH_IMAGE496
For natural gas pipeline joint
Figure 979718DEST_PATH_IMAGE490
In that
Figure 971945DEST_PATH_IMAGE354
Natural gas load flow rate in m3/h;
Figure 100002_DEST_PATH_IMAGE498
And
Figure 100002_DEST_PATH_IMAGE500
respectively being natural gas pipelines
Figure 511378DEST_PATH_IMAGE376
In that
Figure 471112DEST_PATH_IMAGE354
The gas flow at the inlet and the gas flow at the outlet of the time interval are both m3/h;
Figure 100002_DEST_PATH_IMAGE502
For distributing gas in
Figure 949498DEST_PATH_IMAGE354
Time period slave node
Figure 61811DEST_PATH_IMAGE490
The unit of the transmission flow of the natural gas pipeline transmitted to each multi-energy subsystem in the lower layer area is m3/h;
Figure 100002_DEST_PATH_IMAGE504
And
Figure 100002_DEST_PATH_IMAGE506
are respectively a gas distribution net
Figure 819813DEST_PATH_IMAGE354
The upper limit value and the lower limit value of the output gas flow of the gas source point in the time interval are m3/h。
The natural gas pressurizer device has inequality constraints as follows:
Figure 100002_DEST_PATH_IMAGE508
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE510
is a natural gas pipeline
Figure 938948DEST_PATH_IMAGE354
Time interval node
Figure 100002_DEST_PATH_IMAGE512
Pressure of (d) in bar;
Figure 100002_DEST_PATH_IMAGE514
the compression coefficient of the pressurizer, namely the boosting proportion of the pressurizer, is 1.2;
Figure 100002_DEST_PATH_IMAGE516
is a natural gas pipeline
Figure 375352DEST_PATH_IMAGE354
Time interval node
Figure 76592DEST_PATH_IMAGE490
The pressure of (2) is in bar.
The natural gas pipeline flow equality and inequality constraints are as follows:
Figure 100002_DEST_PATH_IMAGE518
Figure 100002_DEST_PATH_IMAGE520
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE522
representing a pipe section
Figure 926867DEST_PATH_IMAGE376
In that
Figure 346347DEST_PATH_IMAGE354
The pipe constant of the time interval, the value of the parameter and the length of the pipe section
Figure 100002_DEST_PATH_IMAGE524
(in m) and diameter
Figure 100002_DEST_PATH_IMAGE526
(in mm) are related;
Figure 100002_DEST_PATH_IMAGE528
and
Figure 100002_DEST_PATH_IMAGE530
respectively natural gas pipe section
Figure 556749DEST_PATH_IMAGE376
In that
Figure 131736DEST_PATH_IMAGE354
The unit of the upper limit of flow and the lower limit of flow of the time interval is m3/h;
Figure 100002_DEST_PATH_IMAGE532
Is a natural gas pipe section
Figure 11968DEST_PATH_IMAGE376
In that
Figure 918744DEST_PATH_IMAGE354
The gas flow direction of the time interval, the invention fixes the flow direction of the gas in the pipeline by fixing the pressure difference of the nodes in the optimization process;
Figure 100002_DEST_PATH_IMAGE534
the natural gas flow index is approximately 2 in a low-pressure pipe network;
Figure 100002_DEST_PATH_IMAGE536
and
Figure 100002_DEST_PATH_IMAGE538
are respectively natural gas nodes
Figure 729574DEST_PATH_IMAGE490
The upper and lower pressure limits of (2) are in bar.
The gas network dynamic characteristic equality and inequality constraint is as follows:
Figure 100002_DEST_PATH_IMAGE540
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE542
is a natural gas pipeline
Figure 297084DEST_PATH_IMAGE376
In that
Figure 128642DEST_PATH_IMAGE354
Time period in m3/h;
Figure 100002_DEST_PATH_IMAGE544
Is a pipe
Figure 991556DEST_PATH_IMAGE376
In that
Figure 684706DEST_PATH_IMAGE354
The time interval has an upper limit constraint value in m3/h;
Figure 100002_DEST_PATH_IMAGE546
Is a pipe
Figure 962847DEST_PATH_IMAGE376
In that
Figure 450460DEST_PATH_IMAGE354
A lower bound value in m for the period of time3/h;
Figure 100002_DEST_PATH_IMAGE548
Is a pipe
Figure 253200DEST_PATH_IMAGE376
In that
Figure 15620DEST_PATH_IMAGE354
The initial value of the time interval is stored in m3/h;
Figure 100002_DEST_PATH_IMAGE550
Is a pipe
Figure 88880DEST_PATH_IMAGE376
Natural gas tube inventory after a cycle of operation in m3/h;
Figure 100002_DEST_PATH_IMAGE552
Is a natural gas pipeline
Figure 481815DEST_PATH_IMAGE376
A collection of (a).
The inequality constraint of the junctor transmission power between the gas distribution network and each multi-energy subsystem in the lower layer area is as follows:
Figure 100002_DEST_PATH_IMAGE554
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE556
and
Figure 100002_DEST_PATH_IMAGE558
are respectively a gas distribution net
Figure 240693DEST_PATH_IMAGE354
The upper limit flow value and the lower limit flow value of the transmission flow of the communication pipeline between the multi-energy subsystems in the time interval and the lower layer area are m3/h。
The upper-layer optimization constraint condition further includes the equation and inequality constraint of the heat distribution network in the upper-layer multi-energy-source main system, and the equation and inequality constraint of the heat distribution network in the upper-layer multi-energy-source main system further includes: the heat distribution network node power balance equality constraint, the heat source point output power inequality constraint, the heat distribution network pipeline transmission power inequality constraint and the connection pipeline transmission power inequality constraint between the heat distribution network and each multi-energy subsystem in the lower layer area;
the power balance equality constraint of the heat distribution network node is as follows:
Figure 100002_DEST_PATH_IMAGE560
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE562
for heat distribution net at
Figure 220850DEST_PATH_IMAGE354
Time interval node
Figure 100002_DEST_PATH_IMAGE564
The unit of the injected thermal power is kW;
Figure 100002_DEST_PATH_IMAGE566
for heat distribution net at
Figure 178311DEST_PATH_IMAGE354
Time interval nodes
Figure 273306DEST_PATH_IMAGE564
The unit of thermal power load of (a) is kW;
Figure 100002_DEST_PATH_IMAGE568
for heat distribution net at
Figure 83261DEST_PATH_IMAGE354
Time interval node
Figure 921904DEST_PATH_IMAGE564
If the heating power is higher than
Figure 100002_DEST_PATH_IMAGE570
Is the upper level heatPower injected into the distribution network by the network;
Figure 100002_DEST_PATH_IMAGE572
for heat distribution net at
Figure 937134DEST_PATH_IMAGE354
The hot water pipeline transmission power of each multi-energy subsystem in the lower layer region is transmitted in a time period, and the unit is kW.
The inequality constraint of the heat source point output power is as follows:
Figure 100002_DEST_PATH_IMAGE574
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE576
and
Figure 100002_DEST_PATH_IMAGE578
are respectively provided with a heat distribution network
Figure 622937DEST_PATH_IMAGE354
The upper limit value and the lower limit value of the thermal power output by the heat source point in the time period are both kW.
The inequality constraint of the transmission power of the heat distribution network pipeline is as follows:
Figure 100002_DEST_PATH_IMAGE580
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE582
and
Figure 100002_DEST_PATH_IMAGE584
are respectively provided with a heat distribution network
Figure 356406DEST_PATH_IMAGE354
Time interval circuit
Figure 100002_DEST_PATH_IMAGE586
The unit of the upper limit value and the lower limit value of the thermal power flow is kW.
The inequality constraint of the transmission power of the communication pipeline between the heat distribution network and each multi-energy subsystem in the lower layer area is as follows:
Figure 100002_DEST_PATH_IMAGE588
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE590
and
Figure 100002_DEST_PATH_IMAGE592
are respectively provided with a heat distribution network
Figure 562522DEST_PATH_IMAGE354
The time interval is respectively connected with the upper limit value and the lower limit value of the thermal power transmitted by the hot water pipeline between the multi-energy subsystems in the lower layer area, and the unit is kW.
Step 2: establishing optimization models of all multi-energy subsystems in the lower layer area, wherein the optimization models of all multi-energy subsystems in the lower layer area comprise a lower layer optimization objective function and a lower layer optimization constraint condition;
minimizing the economic operating cost of each multi-energy subsystem in the lower layer area is an optimization objective, and therefore, the lower layer optimization objective function
Figure 100002_DEST_PATH_IMAGE594
Comprises the following steps:
Figure 100002_DEST_PATH_IMAGE596
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE598
is the first in the lower layer region
Figure 100002_DEST_PATH_IMAGE600
The economic operating costs of the plurality of multi-energy subsystems;
Figure 100002_DEST_PATH_IMAGE602
is the first in the lower layer region
Figure 389182DEST_PATH_IMAGE600
Gas acquisition costs for micro gas turbines within the multiple energy subsystems;
Figure 100002_DEST_PATH_IMAGE604
is the first in the lower layer region
Figure 560401DEST_PATH_IMAGE600
Photovoltaic, fan, micro gas turbine, accumulator, gas storage tank, cold storage tank and heat storage tank in multiple multi-energy subsystems
Figure 374642DEST_PATH_IMAGE354
Total operating cost for a time period;
Figure 100002_DEST_PATH_IMAGE606
wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE608
is the price of natural gas in units of [/m ]3
Figure 100002_DEST_PATH_IMAGE610
Is the low calorific value of natural gas and has the unit of kWh/m3
Figure 100002_DEST_PATH_IMAGE612
Electricity production efficiency of consuming natural gas for the micro gas turbine;
Figure 100002_DEST_PATH_IMAGE614
the heat production efficiency of natural gas consumed by the boiler;
Figure 100002_DEST_PATH_IMAGE616
the number of devices for micro gas turbines;
Figure 100002_DEST_PATH_IMAGE618
is as follows
Figure 836978DEST_PATH_IMAGE600
Multiple multi-energy subsystem micro gas turbines in
Figure 374270DEST_PATH_IMAGE354
The output power of the time period is in kW.
Figure 100002_DEST_PATH_IMAGE620
Wherein the content of the first and second substances,
Figure 100002_DEST_PATH_IMAGE622
is the first in the lower layer region
Figure 933034DEST_PATH_IMAGE600
The total operating costs of the photovoltaic, the fan, the micro gas turbine and the energy storage equipment in the multiple energy subsystems;
Figure 100002_DEST_PATH_IMAGE624
Figure 100002_DEST_PATH_IMAGE626
Figure 100002_DEST_PATH_IMAGE628
Figure 100002_DEST_PATH_IMAGE630
the running costs of the photovoltaic power generation system, the fan, the micro gas turbine and the energy storage equipment are respectively calculated;
Figure 100002_DEST_PATH_IMAGE632
Figure 100002_DEST_PATH_IMAGE634
Figure 100002_DEST_PATH_IMAGE636
Figure 100002_DEST_PATH_IMAGE638
Figure 100002_DEST_PATH_IMAGE640
Figure 100002_DEST_PATH_IMAGE642
Figure 100002_DEST_PATH_IMAGE644
the running cost parameters of photovoltaic equipment, a fan equipment, a micro gas turbine equipment, a storage battery equipment, a gas storage tank equipment, a cold storage tank equipment and a heat storage tank equipment are respectively expressed in units of WrH;
Figure 100002_DEST_PATH_IMAGE646
Figure 100002_DEST_PATH_IMAGE648
respectively a photovoltaic power and a fan
Figure 766996DEST_PATH_IMAGE354
The output power of the time interval is kW.
Figure 100002_DEST_PATH_IMAGE650
Figure 100002_DEST_PATH_IMAGE652
Figure 100002_DEST_PATH_IMAGE654
Figure 100002_DEST_PATH_IMAGE656
Respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a heat accumulation tank
Figure 141346DEST_PATH_IMAGE354
The unit of the power of the absorbed energy in the time period is kW;
Figure 100002_DEST_PATH_IMAGE658
Figure 100002_DEST_PATH_IMAGE660
Figure 100002_DEST_PATH_IMAGE662
Figure 100002_DEST_PATH_IMAGE664
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a heat accumulation tank
Figure 408510DEST_PATH_IMAGE354
The power of the released energy of the time period is in kW.
The lower layer optimization constraint conditions in the optimization model of each multi-energy subsystem in the lower layer area comprise power balance constraints of electric power, natural gas, cold energy, heat energy and waste heat flue gas buses of each multi-energy subsystem in the lower layer area, and the method specifically comprises the following steps:
Figure 100002_DEST_PATH_IMAGE666
the first row to the fifth row are respectively constrained by an active power balance equation of the power bus, the natural gas bus, the cold energy bus, the heat energy bus and the waste heat flue gas bus.
Figure 100002_DEST_PATH_IMAGE668
Figure 100002_DEST_PATH_IMAGE670
Figure 100002_DEST_PATH_IMAGE672
Figure 100002_DEST_PATH_IMAGE674
Respectively in the upper regionDistribution, gas, heat and cold net
Figure 544700DEST_PATH_IMAGE354
The power transmitted to each multi-energy subsystem in the lower layer region in time intervals is kW;
Figure 100002_DEST_PATH_IMAGE676
Figure 100002_DEST_PATH_IMAGE678
Figure 100002_DEST_PATH_IMAGE680
Figure 100002_DEST_PATH_IMAGE682
respectively, the multi-energy subsystems in the lower layer area
Figure 162894DEST_PATH_IMAGE354
The unit of electric, gas, hot and cold power load of the time period is kW;
Figure 100002_DEST_PATH_IMAGE684
Figure 100002_DEST_PATH_IMAGE686
respectively comprises an electric heating device and an electric refrigerating device in each multi-energy subsystem in the lower layer area
Figure 622825DEST_PATH_IMAGE354
The unit of electric power load consumed in time intervals is kW;
Figure 100002_DEST_PATH_IMAGE688
for each multi-energy subsystem in the lower layer region, the heat converter is arranged
Figure 915135DEST_PATH_IMAGE354
The thermal power load consumed in a time period is in kW.
Figure 100002_DEST_PATH_IMAGE690
And
Figure 100002_DEST_PATH_IMAGE692
the conventional electric load and the adjustable electric load of each multi-energy subsystem terminal in the lower layer area are respectively the kW;
Figure DEST_PATH_IMAGE694
and
Figure DEST_PATH_IMAGE696
respectively a conventional gas load and an adjustable gas load;
Figure DEST_PATH_IMAGE698
and
Figure DEST_PATH_IMAGE700
the unit is kW respectively for conventional cooling load and adjustable cooling load.
Figure DEST_PATH_IMAGE702
Converting factors for waste heat power generation;
Figure DEST_PATH_IMAGE704
for each multi-energy subsystem terminal in the lower layer area
Figure 821561DEST_PATH_IMAGE354
Electrical loading of the time period.
Figure DEST_PATH_IMAGE706
Figure DEST_PATH_IMAGE708
Figure DEST_PATH_IMAGE710
Respectively outputting adjustable electricity, gas and cold loads for increasing power for virtual energy participating in a comprehensive demand response plan, wherein the unit is kW;
Figure DEST_PATH_IMAGE712
Figure DEST_PATH_IMAGE714
Figure DEST_PATH_IMAGE716
the unit is kW for adjustable electricity, gas and cold loads of virtual energy output power reduction participating in the comprehensive demand response plan.
Figure DEST_PATH_IMAGE718
Figure DEST_PATH_IMAGE720
Respectively are temperature control type hot air load and flexible hot water supply type load, and the unit is kW.
The lower layer optimization constraint conditions in the optimization model of each multi-energy subsystem in the lower layer region further include energy coupling constraints among energy supply devices in each multi-energy subsystem in the lower layer region, and the specific conditions are as follows:
Figure DEST_PATH_IMAGE722
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE724
for the micro gas turbine in each multi-energy subsystem in the lower layer area
Figure 550221DEST_PATH_IMAGE354
The output power of the time period is kW;
Figure DEST_PATH_IMAGE726
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 531952DEST_PATH_IMAGE354
The output power of the time period is in kW.
Figure DEST_PATH_IMAGE728
Is as followsThe waste heat boilers in the multi-energy subsystems in the layer area are
Figure 429501DEST_PATH_IMAGE354
The unit of waste heat power input in a time period is kW;
Figure DEST_PATH_IMAGE730
for the waste heat boiler in each multi-energy subsystem in the lower layer area
Figure 35057DEST_PATH_IMAGE354
The unit of the waste heat power output in a time period is kW;
Figure DEST_PATH_IMAGE732
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 752477DEST_PATH_IMAGE354
The unit of thermal power input in a time period is kW;
Figure DEST_PATH_IMAGE734
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 537899DEST_PATH_IMAGE354
The unit of thermal power output in a time period is kW;
Figure DEST_PATH_IMAGE736
the efficiency of converting natural gas consumed by the micro gas turbine in each multi-energy subsystem in the lower layer area into electricity;
Figure DEST_PATH_IMAGE738
the heat conversion efficiency of the gas boilers in each multi-energy subsystem in the lower layer area is obtained;
Figure DEST_PATH_IMAGE740
the heat conversion efficiency of the waste heat boiler in each multi-energy subsystem in the lower layer area is obtained;
Figure DEST_PATH_IMAGE742
the thermoelectric ratio of the micro gas turbine in each multi-energy subsystem in the lower layer area.
The lower layer optimization constraint conditions in the optimization model of each multi-energy subsystem in the lower layer region further include energy balance constraints among energy supply equipment in each multi-energy subsystem in the lower layer region, and the specific conditions are as follows:
Figure DEST_PATH_IMAGE744
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE746
Figure DEST_PATH_IMAGE748
Figure DEST_PATH_IMAGE750
Figure DEST_PATH_IMAGE752
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 48210DEST_PATH_IMAGE354
The unit of input power of the time interval is kW;
Figure DEST_PATH_IMAGE754
Figure DEST_PATH_IMAGE756
Figure DEST_PATH_IMAGE758
Figure DEST_PATH_IMAGE760
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 667410DEST_PATH_IMAGE354
The unit of the output power of the time interval is kW;
Figure DEST_PATH_IMAGE762
Figure DEST_PATH_IMAGE764
Figure DEST_PATH_IMAGE766
Figure DEST_PATH_IMAGE768
the conversion efficiency of the electric refrigeration, electric heating, absorption refrigeration and heat converter device is respectively.
The lower layer optimization constraint conditions in the optimization model of each multi-energy subsystem in the lower layer region further comprise equality and inequality constraints of storage batteries, gas storage tanks, cold storage tanks and heat storage tank equipment in each multi-energy subsystem in the lower layer region, and the lower layer optimization constraint conditions are as follows:
Figure DEST_PATH_IMAGE770
the first to fourth rows are respectively the change relations of the stored energy change of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank with the stored energy charging/discharging efficiency, the charging/discharging power, the self-discharging efficiency and the duration.
Figure DEST_PATH_IMAGE772
Figure DEST_PATH_IMAGE774
Figure DEST_PATH_IMAGE776
Figure DEST_PATH_IMAGE778
The charging efficiency coefficients of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank device are respectively;
Figure DEST_PATH_IMAGE780
Figure DEST_PATH_IMAGE782
Figure DEST_PATH_IMAGE784
Figure DEST_PATH_IMAGE786
the energy release efficiency coefficients of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank device are respectively.
Figure DEST_PATH_IMAGE788
Figure DEST_PATH_IMAGE790
Figure DEST_PATH_IMAGE792
Figure DEST_PATH_IMAGE794
The self-discharge efficiency coefficients of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank device are respectively.
Figure DEST_PATH_IMAGE796
Figure DEST_PATH_IMAGE798
Figure DEST_PATH_IMAGE800
Figure DEST_PATH_IMAGE802
Respectively arranged on a storage battery, an air storage tank, a cold storage tank and a heat storage tank
Figure 983378DEST_PATH_IMAGE354
The storage capacity of the time interval is kWh;
Figure DEST_PATH_IMAGE804
Figure DEST_PATH_IMAGE806
Figure DEST_PATH_IMAGE808
Figure DEST_PATH_IMAGE810
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a hot accumulation tank
Figure 277218DEST_PATH_IMAGE354
The unit of the charging power of the time interval is kW;
Figure DEST_PATH_IMAGE812
Figure DEST_PATH_IMAGE814
Figure DEST_PATH_IMAGE816
Figure DEST_PATH_IMAGE818
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a hot accumulation tank
Figure 490637DEST_PATH_IMAGE354
The energy discharge power of the time period is kW.
Figure DEST_PATH_IMAGE820
The maximum charge multiplying power of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank is obtained;
Figure DEST_PATH_IMAGE822
the maximum discharge rate of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank.
Figure DEST_PATH_IMAGE824
Figure DEST_PATH_IMAGE826
Are all binary 0-1 variables;
Figure DEST_PATH_IMAGE828
Is arranged in a storage battery, a gas storage tank, a cold storage tank and a heat storage tank
Figure 15160DEST_PATH_IMAGE354
Minimum energy storage in time interval, rated capacity
Figure DEST_PATH_IMAGE830
0.2 times of (A), in kWh;
Figure DEST_PATH_IMAGE832
is arranged in a storage battery, a gas storage tank, a cold storage tank and a heat storage tank
Figure 192325DEST_PATH_IMAGE354
Maximum energy storage in time interval, taking rated capacity
Figure DEST_PATH_IMAGE834
0.92 times of (a) in kWh.
The lower layer optimization constraint conditions in the optimization model of each multi-energy subsystem in the lower layer region further include inequality constraints of each energy supply device in each multi-energy subsystem in the lower layer region, and the method specifically comprises the following steps:
Figure DEST_PATH_IMAGE836
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE838
and
Figure DEST_PATH_IMAGE840
respectively a micro gas turbine in each multi-energy subsystem in the lower layer area
Figure 522813DEST_PATH_IMAGE354
Upper and lower limits of output power for a time periodThe unit is kW.
Figure DEST_PATH_IMAGE842
And
Figure DEST_PATH_IMAGE844
the upper limit climbing force constraint coefficient and the lower limit climbing force constraint coefficient of the micro gas turbine are respectively.
Figure DEST_PATH_IMAGE846
Figure DEST_PATH_IMAGE848
Figure DEST_PATH_IMAGE850
Figure DEST_PATH_IMAGE852
Respectively comprises a waste heat boiler, a gas boiler, a photovoltaic device and a wind power device in each multi-energy subsystem in the lower layer area
Figure 811579DEST_PATH_IMAGE354
The unit of the upper limit value of the output power of the time period is kW;
Figure DEST_PATH_IMAGE854
Figure DEST_PATH_IMAGE856
Figure DEST_PATH_IMAGE858
Figure DEST_PATH_IMAGE860
respectively comprises a waste heat boiler, a gas boiler, a photovoltaic device and a wind power device in each multi-energy subsystem in the lower layer area
Figure 585631DEST_PATH_IMAGE354
The lower limit value of the output power of the time interval is kW.
The lower layer optimization constraint conditions in the optimization model of each multi-energy subsystem in the lower layer region further include inequality constraints of each energy conversion device in each multi-energy subsystem in the lower layer region, and the method specifically comprises the following steps:
Figure DEST_PATH_IMAGE862
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE864
Figure DEST_PATH_IMAGE866
Figure DEST_PATH_IMAGE868
Figure DEST_PATH_IMAGE870
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 591371DEST_PATH_IMAGE354
The unit of the upper limit value of the time interval output power is kW.
Figure DEST_PATH_IMAGE872
Figure DEST_PATH_IMAGE874
Figure DEST_PATH_IMAGE876
Figure DEST_PATH_IMAGE878
The devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 679543DEST_PATH_IMAGE354
The lower limit value of the time interval output power is kW.
The lower layer optimization constraint conditions in the optimization model of each multi-energy subsystem in the lower layer region further comprise inequality constraints of junctor transmission power between each multi-energy subsystem in the lower layer region and each distribution network in the upper layer region, and the inequality constraints are as follows:
Figure DEST_PATH_IMAGE880
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE882
Figure DEST_PATH_IMAGE884
Figure DEST_PATH_IMAGE886
Figure DEST_PATH_IMAGE888
respectively, the multi-energy subsystems in the lower layer area
Figure 607835DEST_PATH_IMAGE354
And the upper limit of the transmission power of the connecting lines among the distribution network, the heat distribution network and the cold distribution network in the time interval and the upper layer area is kW.
The lower layer optimization constraint conditions in the optimization models of the multiple energy subsystems in the lower layer region further include carbon emission constraints of the multiple energy subsystems in the lower layer region obtained based on real-time environment detection, and the carbon emission constraints are as follows:
Figure DEST_PATH_IMAGE890
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE892
the comprehensive energy supply carbon emission intensity coefficient of the micro gas turbine, the waste heat boiler and the gas boiler device in each multi-energy subsystem in the lower layer area in unit time is t/kWh;
Figure DEST_PATH_IMAGE894
the total carbon emission quota constraint upper limit value of each multi-energy subsystem in the lower layer area is t;
Figure DEST_PATH_IMAGE896
optimizing the real-time carbon emission of operation of each multi-energy subsystem in the lower layer area, wherein the unit is t/h; wherein the subscript
Figure DEST_PATH_IMAGE898
Showing that there are 3 multi-energy subsystems in the lower zone. The third line and the fourth line respectively represent the real-time carbon emission of each multi-energy subsystem in the lower layer area after optimization (
Figure DEST_PATH_IMAGE900
Figure DEST_PATH_IMAGE902
Figure DEST_PATH_IMAGE904
Respectively, the real-time carbon emission amount of the 3 multi-energy subsystems in the lower layer region), and transmitting the total carbon emission quota constraint upper limit value of each multi-energy subsystem in the lower layer region to the upper layer region.
The lower layer optimization constraint conditions in the optimization models of the multiple energy subsystems in the lower layer region further include constraints of movable electricity, gas and cold loads of the multiple energy subsystems in the lower layer region, and the constraints are as follows:
Figure DEST_PATH_IMAGE906
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE908
/
Figure DEST_PATH_IMAGE910
Figure DEST_PATH_IMAGE912
/
Figure DEST_PATH_IMAGE914
Figure DEST_PATH_IMAGE916
/
Figure DEST_PATH_IMAGE918
the maximum variable power allowed by the movable electric, gas and cold loads of each multi-energy subsystem terminal in the lower layer area is respectively.
Figure DEST_PATH_IMAGE920
Figure DEST_PATH_IMAGE922
Figure DEST_PATH_IMAGE924
Figure DEST_PATH_IMAGE926
Figure DEST_PATH_IMAGE928
Figure DEST_PATH_IMAGE930
All are binary variables of 0-1.
The lower layer optimization constraint conditions in the optimization models of the multiple energy subsystems in the lower layer region further comprise constraint of the flexible indoor air conditioning power equivalent models of terminal users of the multiple energy subsystems in the lower layer region, and the constraint conditions are as follows:
Figure DEST_PATH_IMAGE932
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE934
is composed of
Figure 129952DEST_PATH_IMAGE354
The predicted cold/heat load demand power at that moment is in kW.
Figure DEST_PATH_IMAGE936
For each multi-energy subsystem in the lower layer region
Figure 311404DEST_PATH_IMAGE354
The cold or hot power, in kW, is supplied to the end user at the moment.
Figure DEST_PATH_IMAGE938
Is composed of
Figure 327901DEST_PATH_IMAGE354
And (3) the indoor comfortable temperature of each multi-energy subsystem terminal user in the lower layer area at the time is in the unit of o C.
Figure DEST_PATH_IMAGE940
And
Figure DEST_PATH_IMAGE942
the indoor and outdoor air temperature of each multi-energy subsystem terminal user in the lower layer area is represented by the unit of o C.
Figure DEST_PATH_IMAGE944
The equivalent thermal resistance of the building where each multi-energy subsystem terminal user is located in the lower layer area is represented by the unit of degree C/kW.
Figure DEST_PATH_IMAGE946
And
Figure DEST_PATH_IMAGE948
the minimum value and the maximum value allowed by the indoor temperature fluctuation change of the building where each multi-energy subsystem terminal user is located in the lower layer area are respectively in the unit of C. The third line and the fourth line in the formula represent that the indoor cold power and the indoor heat power of the building where each multi-energy subsystem terminal user in the lower layer area is located can be flexibly adjusted according to the monitored outdoor air temperature of the building.
Figure DEST_PATH_IMAGE950
Figure DEST_PATH_IMAGE952
The fluctuation parameters of the cold load and the heat load are respectively.
The lower layer optimization constraint conditions in the optimization models of the multiple energy subsystems in the lower layer region further comprise indoor flexible hot water supply type load power equivalent model constraints of buildings where terminal users of the multiple energy subsystems in the lower layer region are located, and the lower layer optimization constraint conditions are as follows:
Figure DEST_PATH_IMAGE954
the constraint condition of the first row is that the indoor flexible hot water supply requirement of the building where the terminal users of each multi-energy subsystem in the lower layer area are located can be predicted to keep the optimal water storage temperature for the users.
Figure DEST_PATH_IMAGE956
The unit is kWh/(L.degree C) as a hot water parameter;
Figure DEST_PATH_IMAGE958
is composed of
Figure 397183DEST_PATH_IMAGE354
The cold water storage capacity at that time is in units of L.
Figure DEST_PATH_IMAGE960
Is composed of
Figure 355780DEST_PATH_IMAGE354
The temperature of cold water replacing hot water at the moment is in the unit of DEG C.
Figure DEST_PATH_IMAGE962
Is composed of
Figure 244102DEST_PATH_IMAGE354
The storage temperature of the hot water at the moment is in the unit of C;
Figure DEST_PATH_IMAGE964
is composed of
Figure 812093DEST_PATH_IMAGE354
And the unit of the hot water comfortable temperature value in the indoor of the building where each multi-energy subsystem terminal user is located in the lower layer area at one time is C.
Figure DEST_PATH_IMAGE966
The predicted hot water load demand power is in kW.
Figure DEST_PATH_IMAGE968
Is composed of
Figure 85949DEST_PATH_IMAGE354
The unit of the hot water quantity required to be provided by each multi-energy subsystem terminal user in the lower layer area at any time is kW.
Figure DEST_PATH_IMAGE970
And
Figure DEST_PATH_IMAGE972
all are hot water load fluctuation coefficients.
Figure DEST_PATH_IMAGE974
And
Figure DEST_PATH_IMAGE976
is composed of
Figure 123437DEST_PATH_IMAGE354
The minimum and maximum hot water storage temperatures allowed at the moment are in the unit of ℃ C.
And step 3: establishing a double-layer carbon emission optimization distribution model between the multi-energy subsystems in the upper-layer multi-energy main system and the lower-layer area, and decomposing the total carbon emission constraint value of the regional multi-energy system to the multi-energy main system of the upper-layer power distribution network, the gas distribution network and the heat distribution network and the multi-energy subsystems in the lower-layer area on the basis of real-time environment detection, wherein the method specifically comprises the following steps:
Figure DEST_PATH_IMAGE978
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE980
the constraint value is a total carbon emission constraint value of the regional multi-energy system, the unit is t, and the constraint value is iteratively updated according to the actual carbon emission optimized by each multi-energy subsystem in the lower region and the power distribution network system in the upper region multi-energy subsystem in the double-layer optimization process;
Figure DEST_PATH_IMAGE982
Figure DEST_PATH_IMAGE984
Figure DEST_PATH_IMAGE986
respectively responsible for decomposing the region into 3 multi-energy subsystems in the lower region
Figure DEST_PATH_IMAGE988
Figure DEST_PATH_IMAGE990
) The carbon emission constraint upper limit value of (a), in units of t;
Figure DEST_PATH_IMAGE992
Figure DEST_PATH_IMAGE994
and respectively determining the upper limit value of the carbon emission constraint of each multi-energy subsystem in the upper-layer multi-energy main system and the lower-layer multi-energy subsystem in the unit of t for the whole region. The constraint value may be calculated with reference to historical cumulative carbon emissions data for each main/sub-system in the region (e.g., with reference to a historical method using historical carbon emissions intensity as a reference).
And 4, step 4: inputting a total carbon emission constraint value distribution parameter of the regional multi-energy system, an upper region multi-energy main system and a lower region equipment output parameter of each multi-energy subsystem; setting an initial value of a coupling variable of a regional multi-energy system, and a parameter value and an iteration initial value of each multiplier of an improved target cascade analysis method.
And 5: and respectively solving the optimized scheduling problem of each multi-energy subsystem in the lower layer area, transmitting the solved coupling variable to the multi-energy main system of the power distribution network, the gas distribution network and the heat distribution network in the upper layer area for optimization, and transmitting the optimized real-time carbon emission of each multi-energy subsystem in the lower layer area to the multi-energy main system in the upper layer area so as to update the carbon emission constraint value of each multi-energy subsystem in the lower layer area by the whole decomposition of the area.
Step 6: after the multi-energy main system of the upper-layer power distribution network, the gas distribution network and the heat distribution network receives all variables transmitted by each multi-energy sub-system in the lower-layer area, the optimization problem of the multi-energy main system of the upper-layer area is solved respectively, real-time carbon emission amount after optimization of the multi-energy main system of the power distribution network, the gas distribution network and the heat distribution network is transmitted to the multi-energy main system of the upper-layer area, and therefore the carbon emission constraint value of the multi-energy main system of the upper-layer area, which is decomposed in the whole area, is updated.
In the invention, an improved target cascade analysis method is adopted to solve a complex regional multi-energy system double-layer dispersion coordination optimization scheduling model, which specifically comprises the following steps:
respectively converting the objective functions of the upper-layer power distribution network, the gas distribution network and the heat distribution network system into the following forms:
Figure DEST_PATH_IMAGE996
Figure DEST_PATH_IMAGE998
Figure DEST_PATH_IMAGE1000
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE1002
Figure DEST_PATH_IMAGE1004
Figure DEST_PATH_IMAGE1006
respectively taking the transformed target functions of the distribution network, the distribution network and the heat distribution network system in the upper layer area;
Figure DEST_PATH_IMAGE1008
Figure DEST_PATH_IMAGE1010
Figure DEST_PATH_IMAGE1012
respectively, the multi-energy subsystems in the lower layer area
Figure 393662DEST_PATH_IMAGE354
And connecting lines between the time interval and a power distribution network, a gas distribution network and a heat distribution network system in the upper-layer multi-energy-source main system transmit power auxiliary coupling variables, wherein the units are kW.
Converting the objective function of each multi-energy subsystem in the lower zone area into the following form:
Figure DEST_PATH_IMAGE1014
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE1016
Figure DEST_PATH_IMAGE1018
Figure DEST_PATH_IMAGE1020
the system of a power distribution network, a gas distribution network and a heat distribution network in the multi-energy main system of the upper layer respectively is arranged
Figure 906290DEST_PATH_IMAGE354
The unit of the tie line transmission power coupling variable between the time interval and each multi-energy subsystem in the lower layer area is kW;
Figure DEST_PATH_IMAGE1022
Figure DEST_PATH_IMAGE1024
Figure DEST_PATH_IMAGE1026
the target functions of the power distribution network, the gas distribution network and the heat distribution network are respectively
Figure 723067DEST_PATH_IMAGE354
A first order multiplier of a period lagrange penalty function;
Figure DEST_PATH_IMAGE1028
Figure DEST_PATH_IMAGE1030
Figure DEST_PATH_IMAGE1032
the target functions of the power distribution network, the gas distribution network and the heat distribution network are respectively
Figure 226730DEST_PATH_IMAGE354
The quadratic multiplier of the period lagrange penalty function.
And 7: checking the convergence condition of a distributed coordination optimization algorithm between the multi-energy main system in the upper layer area and each multi-energy subsystem in the lower layer area, and taking whether the coupling variable optimized by the upper/lower layer system and the difference value of the target function meet the precision requirement in the iterative optimization process as the convergence condition, wherein the method specifically comprises the following steps:
Figure DEST_PATH_IMAGE1034
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE1036
Figure DEST_PATH_IMAGE1038
Figure DEST_PATH_IMAGE1040
respectively representing the convergence precision of the coupling variable difference and the target function difference between the multi-energy main system in the upper layer area and each multi-energy subsystem in the lower layer area;
if the convergence criterion is met, stopping the iteration of the algorithm, and respectively outputting the optimal scheduling results of the multi-energy main system in the upper layer area and the multi-energy subsystems in the lower layer area; if the convergence criterion is not met, updating each multiplier parameter value of the improved target cascade analysis method, and returning to the step 5 to continue iterative solution;
specifically, when the convergence criterion is not satisfied, updating each multiplier parameter value of the improved target cascade analysis method according to the following formula, namely updating a quadratic term multiplier parameter value of the lagrangian penalty function:
Figure DEST_PATH_IMAGE1042
wherein, in order to accelerate the convergence speed of the algorithm,
Figure DEST_PATH_IMAGE1044
the value is 2.5; the value of the lagrange penalty function multiplier is uniformly set to 1.5.
The present invention is not limited to the above-described embodiments, and any obvious improvements, substitutions or modifications can be made by those skilled in the art without departing from the spirit of the present invention.

Claims (20)

1. A regional multisystem double-layer dispersion optimization scheduling method considering a double-layer carbon emission optimization distribution model is characterized by comprising the following steps:
step 1: establishing an upper-layer multi-energy main system optimization model comprising an upper-layer optimization objective function and upper-layer optimization constraint conditions;
step 2: establishing an optimization model of each multi-energy subsystem in the lower layer area, wherein the optimization model comprises a lower layer optimization objective function and a lower layer optimization constraint condition;
and step 3: establishing a double-layer carbon emission optimization distribution model between the multi-energy subsystems in the upper-layer multi-energy main system and the lower-layer area, and decomposing a total carbon emission constraint value of the area multi-energy system to the multi-energy main system of the upper-layer power distribution network, the distribution network and the heat distribution network and the multi-energy subsystems in the lower-layer area on the basis of real-time environment detection;
and 4, step 4: inputting a total carbon emission constraint value distribution parameter of the regional multi-energy system, an upper region multi-energy main system and a lower region equipment output parameter of each multi-energy subsystem; setting initial values of coupling variables of a regional multi-energy system, and parameter values and iteration initial values of various multipliers of an improved target cascade analysis method;
and 5: respectively solving the optimized scheduling problem of each multi-energy subsystem in the lower layer area, transmitting the solved coupling variable to the multi-energy main system of the power distribution network, the gas distribution network and the heat distribution network in the upper layer area for optimization, and transmitting the optimized real-time carbon emission of each multi-energy subsystem in the lower layer area to the multi-energy main system in the upper layer area so as to update and decompose the carbon emission constraint value of each multi-energy subsystem in the lower layer area;
step 6: after receiving all variables transmitted by each multi-energy subsystem in the lower layer area, the multi-energy main system of the upper layer area comprises a power distribution network, a gas distribution network and a heat distribution network, respectively solving the optimization problem of the multi-energy main system of the upper layer area, and transmitting the optimized real-time carbon emission amount of the multi-energy main system of the power distribution network, the gas distribution network and the heat distribution network to the multi-energy main system of the upper layer area so as to update the carbon emission constraint value decomposed to the multi-energy main system of the upper layer area;
and 7: checking the convergence condition of the distributed coordination optimization algorithm between the multi-energy subsystems in the upper-layer multi-energy main system and the lower-layer area, stopping iteration when the convergence criterion is met, respectively outputting the optimal scheduling results of the multi-energy subsystems in the upper-layer multi-energy main system and the lower-layer area, updating the multiplier parameter values of the improved target cascade analysis method when the convergence criterion is not met, and returning to the step 5 to continue iterative solution.
2. The regional multi-system double-layer decentralized optimization scheduling method considering the double-layer carbon emission optimization distribution model according to claim 1, wherein in the step 1, an upper-layer optimization objective function of an upper-layer multi-energy-source main system is established with a goal of minimizing network loss of a power distribution network, a gas distribution network and a heat distribution network:
Figure DEST_PATH_IMAGE002
Figure DEST_PATH_IMAGE004
Figure DEST_PATH_IMAGE006
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE008
an optimization objective function for the distribution network;
Figure DEST_PATH_IMAGE010
for the distribution network
Figure DEST_PATH_IMAGE012
Time interval circuit
Figure DEST_PATH_IMAGE014
The current of (a);
Figure DEST_PATH_IMAGE016
for branch of distribution network
Figure 728481DEST_PATH_IMAGE014
The resistance of (1);
Figure DEST_PATH_IMAGE018
scheduling the period of the cycle for the day ahead;
Figure DEST_PATH_IMAGE020
the number of nodes of the power distribution network;
Figure DEST_PATH_IMAGE022
the number of branches of the power distribution network;
Figure DEST_PATH_IMAGE024
an optimization objective function for the gas distribution network;
Figure DEST_PATH_IMAGE026
for distributing gas in
Figure 328178DEST_PATH_IMAGE012
Natural gas flow consumed by the pressurizer over time;
Figure DEST_PATH_IMAGE028
is a natural gas pipeline
Figure 170232DEST_PATH_IMAGE012
Average flow over a period of time;
Figure DEST_PATH_IMAGE030
branch of pressurizer for gas distribution network
Figure DEST_PATH_IMAGE032
The natural gas pipeline damping coefficient of (1);
Figure DEST_PATH_IMAGE034
the number of the nodes for installing the pressurizers on the branch of the gas distribution pipe network;
Figure DEST_PATH_IMAGE036
the number of the distribution pipe network branches is;
Figure DEST_PATH_IMAGE038
an optimized objective function for the heat distribution network;
Figure DEST_PATH_IMAGE040
for heat distribution net at
Figure 988278DEST_PATH_IMAGE012
Time interval pipeline
Figure DEST_PATH_IMAGE042
The thermal power of (3);
Figure DEST_PATH_IMAGE044
for heat distribution net at
Figure 599388DEST_PATH_IMAGE012
Time interval pipeline
Figure 749746DEST_PATH_IMAGE042
Thermal power transmission loss coefficient of (1);
Figure DEST_PATH_IMAGE046
the number of nodes of the heat distribution pipe network;
Figure DEST_PATH_IMAGE048
the number of branches of the heat distribution pipe network.
3. The regional multi-system two-tier decentralized optimization scheduling method considering two-tier carbon emission optimization distribution model according to claim 1, wherein the upper-tier optimization constraint condition in step 1 includes:
node power and voltage equality/inequality constraints of the power distribution network:
Figure DEST_PATH_IMAGE050
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE052
for the distribution network
Figure 377299DEST_PATH_IMAGE012
Time interval node
Figure DEST_PATH_IMAGE054
The active power injected;
Figure DEST_PATH_IMAGE056
for the distribution network
Figure 231991DEST_PATH_IMAGE012
Time interval circuit
Figure DEST_PATH_IMAGE058
Active power of (d);
Figure DEST_PATH_IMAGE060
for the distribution network
Figure 933493DEST_PATH_IMAGE012
Time interval node
Figure 520332DEST_PATH_IMAGE054
The reactive power injected;
Figure DEST_PATH_IMAGE062
for the distribution network
Figure 336979DEST_PATH_IMAGE012
Time interval circuit
Figure 542832DEST_PATH_IMAGE058
The reactive power of (c);
Figure DEST_PATH_IMAGE064
for the distribution network
Figure 394113DEST_PATH_IMAGE012
The time interval can be scheduled to output power of a coal-fired or diesel generator set;
Figure DEST_PATH_IMAGE066
for the distribution network
Figure 116301DEST_PATH_IMAGE012
Time interval nodes
Figure 92347DEST_PATH_IMAGE054
Active power load of (2);
Figure DEST_PATH_IMAGE068
for the electrical energy storage of the distribution network side
Figure 429788DEST_PATH_IMAGE012
A charging power of a period;
Figure DEST_PATH_IMAGE070
for the electrical energy storage of the distribution network side
Figure 135575DEST_PATH_IMAGE012
Discharge power of a time period;
Figure DEST_PATH_IMAGE072
for the distribution network
Figure 533059DEST_PATH_IMAGE012
Time period slave node
Figure 356921DEST_PATH_IMAGE054
The active power transmitted to each multi-energy subsystem of the lower layer area;
Figure DEST_PATH_IMAGE074
representing a multi-energy subsystem in an underlying region;
Figure DEST_PATH_IMAGE076
the number of each multi-energy subsystem in the lower layer area is collected;
Figure 966893DEST_PATH_IMAGE010
for the distribution network
Figure 323925DEST_PATH_IMAGE012
Segment line
Figure 564414DEST_PATH_IMAGE058
The current of (a);
Figure 108528DEST_PATH_IMAGE016
for branch of distribution network
Figure 459875DEST_PATH_IMAGE058
The resistance of (1);
Figure DEST_PATH_IMAGE078
for branch of distribution network
Figure 376140DEST_PATH_IMAGE058
A reactance of (d);
Figure DEST_PATH_IMAGE080
the voltage amplitude lower limit value of each node of the power distribution network is set;
Figure DEST_PATH_IMAGE082
the voltage amplitude upper limit value of each node of the power distribution network is obtained;
Figure DEST_PATH_IMAGE084
for branch of distribution network
Figure 443322DEST_PATH_IMAGE058
An apparent capacity upper limit value of (d);
Figure DEST_PATH_IMAGE086
the apparent capacity of the distribution network is restricted in a variation range;
Figure DEST_PATH_IMAGE088
is a node
Figure 38514DEST_PATH_IMAGE054
The square of the voltage of (c);
Figure DEST_PATH_IMAGE090
is a node
Figure DEST_PATH_IMAGE092
The square of the voltage of (c);
the capacity equality/inequality constraint of the electric energy storage equipment on the side of the power distribution network is as follows:
Figure DEST_PATH_IMAGE094
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE096
for the storage battery on the distribution network side
Figure 787027DEST_PATH_IMAGE012
A storage capacity of the time period;
Figure DEST_PATH_IMAGE098
self-discharge efficiency of the storage battery device on the distribution network side;
Figure DEST_PATH_IMAGE100
the charging efficiency of the storage battery device on the power distribution network side;
Figure DEST_PATH_IMAGE102
the discharge efficiency of the storage battery device on the distribution network side is obtained;
Figure DEST_PATH_IMAGE104
Figure DEST_PATH_IMAGE106
are binary 0-1 variables;
Figure DEST_PATH_IMAGE108
the maximum charge rate of the storage battery device is set;
Figure DEST_PATH_IMAGE110
the maximum discharge rate of the storage battery device;
Figure DEST_PATH_IMAGE112
storing energy for the accumulator means;
Figure DEST_PATH_IMAGE114
and
Figure DEST_PATH_IMAGE116
respectively the minimum rated storage capacity and the maximum rated storage capacity allowed by the storage battery device;
the power distribution network can schedule the climbing output inequality constraint of the coal/diesel engine set:
Figure DEST_PATH_IMAGE118
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE120
Figure DEST_PATH_IMAGE122
the upper limit climbing output constraint coefficient and the lower limit climbing output constraint coefficient of the coal-fired and diesel generator sets are respectively; subscript
Figure DEST_PATH_IMAGE124
Subscript of 1 or 3 for coal-fired unit
Figure 692885DEST_PATH_IMAGE124
When the number is 2, the diesel engine group is represented;
the transmission power inequality constraints of each multi-energy subsystem in the power distribution network and the park are as follows:
Figure DEST_PATH_IMAGE126
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE128
and
Figure DEST_PATH_IMAGE130
are respectively a distribution network
Figure 196548DEST_PATH_IMAGE012
The maximum value and the minimum value of the transmission power of the tie lines between the time interval and each multi-energy subsystem in the park;
based on real-time environment detection, the carbon emission constraint of a coal-fired/diesel generator set can be scheduled by a power distribution network in the upper-layer multi-energy main system:
Figure DEST_PATH_IMAGE132
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE134
Figure DEST_PATH_IMAGE136
the carbon emission intensity coefficients of the generated energy per unit time of the coal-fired generator set and the diesel generator set are respectively;
Figure DEST_PATH_IMAGE138
Figure DEST_PATH_IMAGE140
the upper limit value of the carbon emission constraint which can be relaxed is respectively the coal-fired generator set and the diesel generator set;
Figure DEST_PATH_IMAGE142
Figure DEST_PATH_IMAGE144
respectively optimizing the carbon emission of a coal-fired generator set and a diesel generator set in real time;
Figure 872511DEST_PATH_IMAGE018
scheduling the period of the cycle for the day ahead; all superscripts
Figure DEST_PATH_IMAGE146
The numbers of the recorded data of the multi-energy main system in the upper layer area and the multi-energy subsystems in the lower layer area in the iterative optimization process are shown.
4. The regional multi-system two-tier decentralized optimization scheduling method considering two-tier carbon emission optimization distribution model according to claim 1, wherein the upper-tier optimization constraint condition in step 1 includes:
the power balance equality and inequality constraint of the distribution network node are as follows:
Figure DEST_PATH_IMAGE148
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE150
for distributing gas in
Figure 722918DEST_PATH_IMAGE012
The gas flow output by the natural gas source point of the time period;
Figure DEST_PATH_IMAGE152
and
Figure DEST_PATH_IMAGE154
respectively being natural gas pipelines
Figure 581152DEST_PATH_IMAGE032
In that
Figure 458978DEST_PATH_IMAGE012
Inlet gas flow and outlet gas flow for a time period;
Figure 340347DEST_PATH_IMAGE074
representing a multi-energy subsystem in an underlying region;
Figure 480864DEST_PATH_IMAGE076
the number of each multi-energy subsystem in the lower layer area is collected;
Figure DEST_PATH_IMAGE156
for distributing gas in
Figure 724763DEST_PATH_IMAGE012
Time period slave node
Figure 648857DEST_PATH_IMAGE146
Transmitting the natural gas pipeline transmission flow to each multi-energy subsystem in the lower layer region;
Figure DEST_PATH_IMAGE158
for natural gas pipeline joint
Figure 610997DEST_PATH_IMAGE146
In that
Figure 770583DEST_PATH_IMAGE012
Natural gas load flow over a period of time;
Figure 541093DEST_PATH_IMAGE026
for distributing gas in
Figure 996607DEST_PATH_IMAGE012
Natural gas flow consumed by the pressurizer over time;
Figure DEST_PATH_IMAGE160
and
Figure DEST_PATH_IMAGE162
are respectively a gas distribution net
Figure 914884DEST_PATH_IMAGE012
The upper limit value and the lower limit value of the gas flow output by the gas source point in the time interval;
the natural gas pressurizer device is constrained in an inequality way:
Figure DEST_PATH_IMAGE164
wherein the content of the first and second substances,
Figure 347003DEST_PATH_IMAGE030
branch of pressurizer for gas distribution network
Figure 831074DEST_PATH_IMAGE032
The natural gas pipeline damping coefficient of (1);
Figure 96970DEST_PATH_IMAGE028
is a natural gas pipeline
Figure 535167DEST_PATH_IMAGE012
Average flow over a period of time;
Figure DEST_PATH_IMAGE166
is a natural gas pipeline
Figure 36555DEST_PATH_IMAGE012
Time interval node
Figure DEST_PATH_IMAGE168
The pressure of (a);
Figure DEST_PATH_IMAGE170
is the compression factor of the pressurizer;
Figure DEST_PATH_IMAGE172
is a natural gas pipeline
Figure 171870DEST_PATH_IMAGE012
Time interval node
Figure 608668DEST_PATH_IMAGE146
The pressure of (a);
natural gas pipeline flow equality and inequality constraints:
Figure DEST_PATH_IMAGE174
Figure DEST_PATH_IMAGE176
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE178
is a natural gas pipe section
Figure 924374DEST_PATH_IMAGE032
In that
Figure 370399DEST_PATH_IMAGE012
Gas flow direction of the time period;
Figure DEST_PATH_IMAGE180
representing a pipe section
Figure 297903DEST_PATH_IMAGE032
In that
Figure 905602DEST_PATH_IMAGE012
Pipe constant of time interval, its value and length of pipe section
Figure DEST_PATH_IMAGE182
And diameter
Figure DEST_PATH_IMAGE184
(ii) related;
Figure DEST_PATH_IMAGE186
and
Figure DEST_PATH_IMAGE188
respectively natural gas pipe section
Figure 968324DEST_PATH_IMAGE032
In that
Figure 686882DEST_PATH_IMAGE012
A flow upper limit constraint value and a flow lower limit constraint value of a time period;
Figure DEST_PATH_IMAGE190
and
Figure DEST_PATH_IMAGE192
are respectively natural gas nodes
Figure 829412DEST_PATH_IMAGE146
Upper and lower pressure limits of (a);
Figure DEST_PATH_IMAGE194
is the natural gas flow index;
the gas network dynamic characteristic equality and inequality constraint:
Figure DEST_PATH_IMAGE196
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE198
is a natural gas pipeline
Figure 263805DEST_PATH_IMAGE032
In that
Figure 68950DEST_PATH_IMAGE012
Managing and storing time intervals;
Figure DEST_PATH_IMAGE200
and
Figure DEST_PATH_IMAGE202
are respectively pipelines
Figure 653515DEST_PATH_IMAGE032
In that
Figure 588235DEST_PATH_IMAGE012
Managing an upper limit constraint value and a lower limit constraint value of the time period;
Figure DEST_PATH_IMAGE204
is a pipe
Figure 131212DEST_PATH_IMAGE032
In that
Figure 892494DEST_PATH_IMAGE012
The initial value of the time interval is managed;
Figure DEST_PATH_IMAGE206
is a pipe
Figure 811909DEST_PATH_IMAGE032
Natural gas pipe inventory after a cycle of operation;
Figure DEST_PATH_IMAGE208
is a natural gas pipeline
Figure 568512DEST_PATH_IMAGE032
A set of (a);
Figure 315014DEST_PATH_IMAGE018
scheduling the period of the cycle for the day ahead;
the transmission power inequality constraint of the connecting lines between the gas distribution network and each multi-energy subsystem in the lower layer area is as follows:
Figure DEST_PATH_IMAGE210
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE212
and
Figure DEST_PATH_IMAGE214
are respectively a gas distribution net
Figure 750543DEST_PATH_IMAGE012
And the upper limit flow value and the lower limit flow value of the transmission flow of the communication pipeline between the time interval and each multi-energy subsystem in the lower layer area.
5. The regional multi-system two-tier decentralized optimization scheduling method considering two-tier carbon emission optimization distribution model according to claim 1, wherein the upper-tier optimization constraint condition in step 1 includes:
and (3) carrying out constraint of a power balance equation of the heat distribution network nodes:
Figure DEST_PATH_IMAGE216
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE218
for heat distribution net at
Figure 676911DEST_PATH_IMAGE012
Time interval node
Figure DEST_PATH_IMAGE220
The thermal power of the injection;
Figure DEST_PATH_IMAGE222
for heat distribution net at
Figure 518047DEST_PATH_IMAGE012
Time interval pipeline
Figure 199564DEST_PATH_IMAGE042
The thermal power of (3);
Figure DEST_PATH_IMAGE224
for heat distribution net at
Figure 528914DEST_PATH_IMAGE012
Time interval nodes
Figure 196656DEST_PATH_IMAGE220
Thermal power load of (2);
Figure DEST_PATH_IMAGE226
for heat distribution net at
Figure 662272DEST_PATH_IMAGE012
Time interval node
Figure 16155DEST_PATH_IMAGE220
The heating power of (a);
Figure DEST_PATH_IMAGE228
for heat distribution net at
Figure 98381DEST_PATH_IMAGE012
Transmitting power to hot water pipelines of each multi-energy subsystem in the lower layer region in a time interval;
Figure 304234DEST_PATH_IMAGE044
for heat distribution net at
Figure 421095DEST_PATH_IMAGE012
Time interval pipeline
Figure 319781DEST_PATH_IMAGE042
Thermal power transmission loss coefficient of (1);
the heat source point output power is constrained by an inequality:
Figure DEST_PATH_IMAGE230
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE232
and
Figure DEST_PATH_IMAGE234
are respectively provided with a heat distribution network
Figure 921926DEST_PATH_IMAGE012
Heat output from heat source point of time intervalAn upper power limit and a lower power limit;
the transmission power inequality constraint of the heat distribution network pipeline is as follows:
Figure DEST_PATH_IMAGE236
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE238
and
Figure DEST_PATH_IMAGE240
are respectively provided with a heat distribution network
Figure 852841DEST_PATH_IMAGE012
Time interval circuit
Figure 965154DEST_PATH_IMAGE042
The upper limit value and the lower limit value of the thermal power flow;
the inequality constraint of the transmission power of the communication pipeline between the heat distribution network and each multi-energy subsystem in the lower layer area is as follows:
Figure DEST_PATH_IMAGE242
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE244
and
Figure DEST_PATH_IMAGE246
are respectively provided with a heat distribution network
Figure 926419DEST_PATH_IMAGE012
And the time interval is respectively connected with the upper limit value and the lower limit value of the thermal power transmitted by the hot water pipeline between the multi-energy subsystems in the lower layer area.
6. According to the claimsSolving 1 the regional multi-system double-layer decentralized optimization scheduling method considering the double-layer carbon emission optimization distribution model is characterized in that in the step 2, a lower-layer optimization objective function is established as an optimization objective by minimizing the economic operation cost of each multi-energy subsystem in the lower layer region
Figure DEST_PATH_IMAGE248
Comprises the following steps:
Figure DEST_PATH_IMAGE250
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE252
is the first in the lower layer region
Figure 779974DEST_PATH_IMAGE074
The economic operating costs of the plurality of multi-energy subsystems;
Figure DEST_PATH_IMAGE254
is the first in the lower layer region
Figure 921106DEST_PATH_IMAGE074
Gas acquisition costs for micro gas turbines within the multiple energy subsystems;
Figure DEST_PATH_IMAGE256
is the first in the lower layer region
Figure 977005DEST_PATH_IMAGE074
Photovoltaic, fan, micro gas turbine, accumulator, gas storage tank, cold storage tank and heat storage tank in multiple multi-energy subsystems
Figure 76548DEST_PATH_IMAGE012
Total operating cost for a time period;
Figure 761608DEST_PATH_IMAGE076
the number of each multi-energy subsystem in the lower layer area is collected;
Figure DEST_PATH_IMAGE258
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE260
is the price of natural gas;
Figure DEST_PATH_IMAGE262
is the low calorific value of natural gas;
Figure DEST_PATH_IMAGE264
electricity production efficiency of consuming natural gas for the micro gas turbine;
Figure DEST_PATH_IMAGE266
the heat production efficiency of natural gas consumed by the boiler;
Figure DEST_PATH_IMAGE268
the number of devices for micro gas turbines;
Figure DEST_PATH_IMAGE270
is as follows
Figure 394845DEST_PATH_IMAGE074
Multiple multi-energy subsystem micro gas turbines in
Figure 340805DEST_PATH_IMAGE012
An output power of the time period;
Figure DEST_PATH_IMAGE272
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 611249DEST_PATH_IMAGE012
Thermal power input in a time period;
Figure DEST_PATH_IMAGE274
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE276
is the first in the lower layer region
Figure 81807DEST_PATH_IMAGE074
The total operating costs of the photovoltaic, the fan, the micro gas turbine and the energy storage equipment in the multiple energy subsystems;
Figure DEST_PATH_IMAGE278
Figure DEST_PATH_IMAGE280
Figure DEST_PATH_IMAGE282
Figure DEST_PATH_IMAGE284
the running costs of the photovoltaic power generation system, the fan, the micro gas turbine and the energy storage equipment are respectively calculated;
Figure DEST_PATH_IMAGE286
Figure DEST_PATH_IMAGE288
Figure DEST_PATH_IMAGE290
Figure DEST_PATH_IMAGE292
Figure DEST_PATH_IMAGE294
Figure DEST_PATH_IMAGE296
Figure DEST_PATH_IMAGE298
respectively setting running cost parameters of photovoltaic equipment, a fan, a micro gas turbine, a storage battery, a gas storage tank, a cold storage tank and a heat storage tank equipment;
Figure DEST_PATH_IMAGE300
Figure DEST_PATH_IMAGE302
respectively a photovoltaic power and a fan
Figure 705686DEST_PATH_IMAGE012
An output power of the time period;
Figure DEST_PATH_IMAGE304
Figure DEST_PATH_IMAGE306
Figure DEST_PATH_IMAGE308
Figure DEST_PATH_IMAGE310
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a heat accumulation tank
Figure 556354DEST_PATH_IMAGE012
The power of the absorbed energy of the time period;
Figure DEST_PATH_IMAGE312
Figure DEST_PATH_IMAGE314
Figure DEST_PATH_IMAGE316
Figure DEST_PATH_IMAGE318
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a heat accumulation tank
Figure 623798DEST_PATH_IMAGE012
The power of the released energy of the time period.
7. The regional multi-system double-layer decentralized optimization scheduling method according to claim 1, wherein in the step 2, the lower-layer optimization constraint condition includes a power balance constraint of power, natural gas, cold energy, heat energy and waste heat flue gas buses of each multi-energy subsystem in the lower-layer region:
Figure DEST_PATH_IMAGE320
wherein the content of the first and second substances,
Figure 752291DEST_PATH_IMAGE300
Figure 304495DEST_PATH_IMAGE302
respectively a photovoltaic power and a fan
Figure 365992DEST_PATH_IMAGE012
An output power of the time period;
Figure DEST_PATH_IMAGE322
is as follows
Figure 712659DEST_PATH_IMAGE074
Multiple multi-energy subsystem micro gas turbines in
Figure 718662DEST_PATH_IMAGE012
An output power of the time period;
Figure 949923DEST_PATH_IMAGE268
the number of devices for micro gas turbines;
Figure 226446DEST_PATH_IMAGE312
is a storage battery device
Figure 150539DEST_PATH_IMAGE012
Power of the released energy over a period of time;
Figure 643838DEST_PATH_IMAGE304
is a storage battery device
Figure 678790DEST_PATH_IMAGE012
The power of the absorbed energy of the time period;
Figure DEST_PATH_IMAGE324
Figure DEST_PATH_IMAGE326
respectively comprises an electric heating device and an electric refrigerating device in each multi-energy subsystem in the lower layer area
Figure 636250DEST_PATH_IMAGE012
An electrical power load consumed over a period of time;
Figure DEST_PATH_IMAGE328
Figure DEST_PATH_IMAGE330
Figure DEST_PATH_IMAGE332
Figure DEST_PATH_IMAGE334
respectively distribute power, gas, heat and cold in the upper region
Figure 357344DEST_PATH_IMAGE012
Transmitting the power to each multi-energy subsystem in the lower layer region in a time interval;
Figure DEST_PATH_IMAGE336
Figure DEST_PATH_IMAGE338
Figure DEST_PATH_IMAGE340
Figure DEST_PATH_IMAGE342
respectively, the multi-energy subsystems in the lower layer area
Figure 692598DEST_PATH_IMAGE012
Electrical, gas, hot, cold power loads for a period of time;
Figure 531241DEST_PATH_IMAGE314
Figure 280891DEST_PATH_IMAGE316
Figure 546788DEST_PATH_IMAGE318
respectively comprises an air storage tank, a cold accumulation tank and a heat accumulation tank
Figure 749099DEST_PATH_IMAGE012
Power of the released energy over a period of time;
Figure DEST_PATH_IMAGE344
for each multi-energy subsystem in the lower layer region, the heat converter is arranged
Figure 984908DEST_PATH_IMAGE012
Thermal power load consumed over a period of time;
Figure DEST_PATH_IMAGE346
for the waste heat boiler in each multi-energy subsystem in the lower layer area
Figure 559371DEST_PATH_IMAGE012
The waste heat power output in time intervals;
Figure DEST_PATH_IMAGE348
Figure DEST_PATH_IMAGE350
Figure DEST_PATH_IMAGE352
Figure DEST_PATH_IMAGE354
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 386382DEST_PATH_IMAGE012
An output power of the time period;
Figure DEST_PATH_IMAGE356
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 544831DEST_PATH_IMAGE012
Thermal power output in time intervals;
Figure DEST_PATH_IMAGE358
and
Figure DEST_PATH_IMAGE360
respectively a terminal of each multi-energy subsystem in the lower layer areaRegular and adjustable electrical loads;
Figure DEST_PATH_IMAGE362
Figure DEST_PATH_IMAGE364
Figure DEST_PATH_IMAGE366
adjustable power, gas and cold loads for the virtual energy output power increase participating in the comprehensive demand response plan respectively;
Figure DEST_PATH_IMAGE368
Figure DEST_PATH_IMAGE370
Figure DEST_PATH_IMAGE372
respectively outputting adjustable electricity, gas and cold loads of the power reduction for the virtual energy participating in the comprehensive demand response plan;
Figure DEST_PATH_IMAGE374
and
Figure DEST_PATH_IMAGE376
respectively a conventional gas load and an adjustable gas load;
Figure DEST_PATH_IMAGE378
and
Figure DEST_PATH_IMAGE380
respectively a conventional cold load and an adjustable cold load;
Figure DEST_PATH_IMAGE382
Figure DEST_PATH_IMAGE384
respectively a temperature control type hot air load and a flexible hot water supply type load;
Figure DEST_PATH_IMAGE386
converting factors for waste heat power generation;
Figure DEST_PATH_IMAGE388
for each multi-energy subsystem terminal in the lower layer area
Figure 492320DEST_PATH_IMAGE012
Electrical loading of the time period.
8. The regional multi-system double-layer decentralized optimization scheduling method according to claim 1, wherein in the step 2, the lower-layer optimization constraint condition includes an energy balance constraint between energy supply devices in each multi-energy subsystem in the lower-layer region:
Figure DEST_PATH_IMAGE390
wherein the content of the first and second substances,
Figure 181010DEST_PATH_IMAGE348
Figure 788709DEST_PATH_IMAGE350
Figure 965612DEST_PATH_IMAGE352
Figure 684169DEST_PATH_IMAGE354
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 262918DEST_PATH_IMAGE012
Time periodThe output power of (d);
Figure DEST_PATH_IMAGE392
Figure DEST_PATH_IMAGE394
respectively comprises an electric heating device and an electric refrigerating device in each multi-energy subsystem in the lower layer area
Figure 103835DEST_PATH_IMAGE012
An electrical power load consumed over a period of time;
Figure DEST_PATH_IMAGE396
is an absorption type refrigerating device in each multi-energy subsystem in the lower layer area
Figure 3920DEST_PATH_IMAGE012
An input power of the time period;
Figure DEST_PATH_IMAGE398
Figure DEST_PATH_IMAGE400
Figure DEST_PATH_IMAGE402
Figure DEST_PATH_IMAGE404
the conversion efficiency of the electric refrigeration, electric heating, absorption refrigeration and heat converter devices respectively;
Figure 775436DEST_PATH_IMAGE386
is a conversion factor of waste heat power generation.
9. The regional multi-system double-layer decentralized optimization scheduling method considering the double-layer carbon emission optimization distribution model according to claim 1, wherein in the step 2, the lower-layer optimization constraint condition includes an energy coupling constraint between energy supply devices in each multi-energy subsystem in the lower-layer region:
Figure DEST_PATH_IMAGE406
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE408
for the micro gas turbine in each multi-energy subsystem in the lower layer area
Figure 913419DEST_PATH_IMAGE012
An output power of the time period;
Figure DEST_PATH_IMAGE410
the thermoelectric ratio of the micro gas turbine in each multi-energy subsystem in the lower layer area is obtained;
Figure DEST_PATH_IMAGE412
for the waste heat boiler in each multi-energy subsystem in the lower layer area
Figure 925237DEST_PATH_IMAGE012
The waste heat power input in time intervals;
Figure DEST_PATH_IMAGE414
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 279995DEST_PATH_IMAGE012
An output power of the time period;
Figure DEST_PATH_IMAGE416
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 199409DEST_PATH_IMAGE012
Thermal power input in a time period;
Figure DEST_PATH_IMAGE418
the efficiency of converting natural gas consumed by the micro gas turbine in each multi-energy subsystem in the lower layer area into electricity;
Figure DEST_PATH_IMAGE420
the heat conversion efficiency of the gas boilers in each multi-energy subsystem in the lower layer area is obtained;
Figure DEST_PATH_IMAGE422
the heat conversion efficiency of the waste heat boiler in each multi-energy subsystem in the lower layer area is obtained;
Figure 785374DEST_PATH_IMAGE356
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 764831DEST_PATH_IMAGE012
Thermal power output in time intervals;
Figure DEST_PATH_IMAGE424
for the waste heat boiler in each multi-energy subsystem in the lower layer area
Figure 872464DEST_PATH_IMAGE012
The waste heat power output in time intervals.
10. The regional multi-system double-layer decentralized optimization scheduling method considering the double-layer carbon emission optimization distribution model according to claim 1, wherein in the step 2, the lower-layer optimization constraint condition includes an equality constraint and an inequality constraint of storage batteries, air storage tanks, cold storage tanks and heat storage tank devices in each multi-energy subsystem in the lower-layer region:
Figure DEST_PATH_IMAGE426
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE428
Figure DEST_PATH_IMAGE430
Figure DEST_PATH_IMAGE432
Figure DEST_PATH_IMAGE434
the self-discharge efficiency coefficients of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank device are respectively;
Figure DEST_PATH_IMAGE436
Figure DEST_PATH_IMAGE438
Figure DEST_PATH_IMAGE440
Figure DEST_PATH_IMAGE442
the charging efficiency coefficients of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank device are respectively;
Figure DEST_PATH_IMAGE444
Figure DEST_PATH_IMAGE446
Figure DEST_PATH_IMAGE448
Figure DEST_PATH_IMAGE450
energy release efficiency coefficients of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank device are respectively set;
Figure DEST_PATH_IMAGE452
Figure DEST_PATH_IMAGE454
Figure DEST_PATH_IMAGE456
Figure DEST_PATH_IMAGE458
respectively arranged on a storage battery, an air storage tank, a cold storage tank and a heat storage tank
Figure 592640DEST_PATH_IMAGE012
A storage capacity of the time period;
Figure DEST_PATH_IMAGE460
Figure DEST_PATH_IMAGE462
Figure DEST_PATH_IMAGE464
Figure DEST_PATH_IMAGE466
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a hot accumulation tank
Figure 734909DEST_PATH_IMAGE012
(ii) a charging power over a period of time;
Figure DEST_PATH_IMAGE468
Figure DEST_PATH_IMAGE470
Figure DEST_PATH_IMAGE472
Figure DEST_PATH_IMAGE474
respectively comprises a storage battery, a gas storage tank, a cold accumulation tank and a hot accumulation tank
Figure 183470DEST_PATH_IMAGE012
Discharge power of a time period;
Figure DEST_PATH_IMAGE476
the maximum charge multiplying power of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank is obtained;
Figure DEST_PATH_IMAGE478
the maximum discharge multiplying power of the storage battery, the gas storage tank, the cold storage tank and the heat storage tank is obtained;
Figure DEST_PATH_IMAGE480
Figure DEST_PATH_IMAGE482
are binary 0-1 variables;
Figure DEST_PATH_IMAGE484
is arranged in a storage battery, a gas storage tank, a cold storage tank and a heat storage tank
Figure 903033DEST_PATH_IMAGE012
A minimum stored energy for a time period;
Figure DEST_PATH_IMAGE486
is arranged in a storage battery, a gas storage tank, a cold storage tank and a heat storage tank
Figure 417714DEST_PATH_IMAGE012
Maximum stored energy for a time period;
Figure DEST_PATH_IMAGE488
is rated capacity.
11. The regional multi-system double-layer decentralized optimization scheduling method according to claim 1, wherein in step 2, the lower-layer optimization constraint condition includes an inequality constraint of each energy supply device in each multi-energy subsystem in the lower-layer region:
Figure DEST_PATH_IMAGE490
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE492
and
Figure DEST_PATH_IMAGE494
respectively a micro gas turbine in each multi-energy subsystem in the lower layer area
Figure 945647DEST_PATH_IMAGE012
An upper limit value and a lower limit value of output power of a time period;
Figure DEST_PATH_IMAGE496
and
Figure DEST_PATH_IMAGE498
respectively an upper limit climbing force constraint coefficient and a lower limit climbing force constraint coefficient of the micro gas turbine;
Figure DEST_PATH_IMAGE500
Figure DEST_PATH_IMAGE502
Figure DEST_PATH_IMAGE504
Figure DEST_PATH_IMAGE506
respectively a waste heat boiler, a gas boiler, a photovoltaic system and a wind power system in each multi-energy subsystem in the lower layer areaThe equipment is at
Figure 486481DEST_PATH_IMAGE012
An upper limit value of output power of the time period;
Figure DEST_PATH_IMAGE508
Figure DEST_PATH_IMAGE510
Figure DEST_PATH_IMAGE512
Figure DEST_PATH_IMAGE514
respectively comprises a waste heat boiler, a gas boiler, a photovoltaic device and a wind power device in each multi-energy subsystem in the lower layer area
Figure 70171DEST_PATH_IMAGE012
A lower limit value of the output power of the period.
12. The regional multi-system double-layer decentralized optimization scheduling method according to claim 1, wherein in step 2, the lower-layer optimization constraint condition includes inequality constraints of energy conversion devices in multi-energy subsystems in the lower-layer region:
Figure DEST_PATH_IMAGE516
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE518
Figure DEST_PATH_IMAGE520
Figure DEST_PATH_IMAGE522
Figure DEST_PATH_IMAGE524
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 259713DEST_PATH_IMAGE012
An upper limit value of the period output power;
Figure DEST_PATH_IMAGE526
Figure DEST_PATH_IMAGE528
Figure DEST_PATH_IMAGE530
Figure DEST_PATH_IMAGE532
the devices of the electric refrigeration, the electric heating, the absorption refrigeration and the heat converter in each multi-energy subsystem in the lower layer area are respectively arranged
Figure 2672DEST_PATH_IMAGE012
A lower limit value of the period output power.
13. The regional multi-system double-layer decentralized optimization scheduling method according to claim 1, wherein in step 2, the lower-layer optimization constraint condition includes an inequality constraint on link transmission power between each multi-energy subsystem in the lower-layer region and each distribution network in the upper-layer region:
Figure DEST_PATH_IMAGE534
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE536
Figure DEST_PATH_IMAGE538
Figure DEST_PATH_IMAGE540
Figure DEST_PATH_IMAGE542
respectively, the multi-energy subsystems in the lower layer area
Figure 849493DEST_PATH_IMAGE012
And the upper limit of the transmission power of the connecting line between the time interval and the distribution network, the heat distribution network and the cold distribution network in the upper layer area.
14. The regional multi-system double-layer decentralized optimization scheduling method according to claim 1, wherein in step 2, the lower-layer optimization constraint condition includes a carbon emission constraint of each multi-energy subsystem in the lower-layer region based on real-time environment detection:
Figure DEST_PATH_IMAGE544
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE546
the comprehensive energy supply carbon emission intensity coefficient of the micro gas turbine, the waste heat boiler and the gas boiler device in each multi-energy subsystem in the lower layer area in unit time is obtained;
Figure DEST_PATH_IMAGE548
is as follows
Figure 481332DEST_PATH_IMAGE074
Multiple multi-energy subsystem micro gas turbines in
Figure 490876DEST_PATH_IMAGE012
An output power of the time period;
Figure 963708DEST_PATH_IMAGE268
the number of devices for micro gas turbines;
Figure 33295DEST_PATH_IMAGE018
scheduling the period of the cycle for the day ahead;
Figure DEST_PATH_IMAGE550
for the waste heat boiler in each multi-energy subsystem in the lower layer area
Figure 558955DEST_PATH_IMAGE012
The waste heat power input in time intervals;
Figure DEST_PATH_IMAGE552
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 965665DEST_PATH_IMAGE012
Thermal power output in time intervals;
Figure DEST_PATH_IMAGE554
for each multi-energy subsystem in the lower layer region, the gas boiler is arranged
Figure 791539DEST_PATH_IMAGE012
Thermal power input in a time period; all superscripts
Figure 766448DEST_PATH_IMAGE146
Both represent the number of the recorded data of the multi-energy main system in the upper layer area and each multi-energy subsystem in the lower layer area in the iterative optimization process,
Figure DEST_PATH_IMAGE556
in the lower layer regionThe total carbon emission quota of each multi-energy subsystem constrains an upper limit value,
Figure DEST_PATH_IMAGE558
optimizing real-time carbon emissions for operation of the various multi-energy subsystems in the lower region, wherein the subscripts
Figure DEST_PATH_IMAGE560
Indicating that the lower zone region has 3 multi-energy subsystems; and the third line and the fourth line respectively represent that the real-time carbon emission of each multi-energy subsystem in the lower layer area is calculated uniformly after optimization, and the total carbon emission quota constraint upper limit value of each multi-energy subsystem in the lower layer area is transmitted to the upper layer area.
15. The regional multi-system two-tier decentralized optimization scheduling method according to claim 1, wherein in step 2, the lower-tier optimization constraints include constraints of mobile electric, gas and cold loads of each multi-energy subsystem terminal in the lower-tier region:
Figure DEST_PATH_IMAGE562
wherein the content of the first and second substances,
Figure 202240DEST_PATH_IMAGE018
scheduling the period of the cycle for the day ahead;
Figure DEST_PATH_IMAGE564
/
Figure 147062DEST_PATH_IMAGE564
Figure DEST_PATH_IMAGE566
/
Figure DEST_PATH_IMAGE568
Figure DEST_PATH_IMAGE570
/
Figure DEST_PATH_IMAGE572
the maximum change power allowed by movable electric, gas and cold loads of each multi-energy subsystem terminal in the lower layer area is respectively;
Figure DEST_PATH_IMAGE574
Figure DEST_PATH_IMAGE576
Figure DEST_PATH_IMAGE578
Figure DEST_PATH_IMAGE580
Figure DEST_PATH_IMAGE582
Figure DEST_PATH_IMAGE584
are binary variables from 0 to 1.
16. The regional multi-system double-layer decentralized optimization scheduling method according to claim 1, wherein in step 2, the lower layer optimization constraint condition includes constraint of a flexible indoor air conditioning power equivalent model for each multi-energy subsystem terminal user in the lower layer region:
Figure DEST_PATH_IMAGE586
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE588
is composed of
Figure 604938DEST_PATH_IMAGE012
Predicted cold/heat load demand power at a time;
Figure DEST_PATH_IMAGE590
for each multi-energy subsystem in the lower layer region
Figure 609803DEST_PATH_IMAGE012
Cold or hot power supplied to the end user at any time;
Figure DEST_PATH_IMAGE592
is composed of
Figure 110055DEST_PATH_IMAGE012
The comfortable temperature of the indoor of each multi-energy subsystem terminal user in the lower layer area is measured at the moment;
Figure DEST_PATH_IMAGE594
and
Figure DEST_PATH_IMAGE596
the indoor and outdoor air temperature of each multi-energy subsystem terminal user in the lower layer area is measured;
Figure DEST_PATH_IMAGE598
equivalent thermal resistance of a building where each multi-energy subsystem terminal user is located in a lower layer area;
Figure DEST_PATH_IMAGE600
and
Figure DEST_PATH_IMAGE602
respectively obtaining the minimum value and the maximum value allowed by the indoor temperature fluctuation change of the building where each multi-energy subsystem terminal user is located in the lower layer area;
Figure DEST_PATH_IMAGE604
Figure DEST_PATH_IMAGE606
respectively are the fluctuation parameters of the cold load and the heat load;
Figure 812563DEST_PATH_IMAGE018
the period of the cycle is scheduled for the day ahead.
17. The regional multi-system double-layer decentralized optimization scheduling method according to claim 1, wherein in step 2, the lower-layer optimization constraint condition includes an indoor flexible hot water supply type load power equivalent model constraint of a building where each multi-energy subsystem terminal user is located in the lower-layer region:
Figure DEST_PATH_IMAGE608
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE610
demand power for the predicted hot water load;
Figure DEST_PATH_IMAGE612
is a hot water parameter;
Figure DEST_PATH_IMAGE614
is composed of
Figure 114493DEST_PATH_IMAGE012
The cold water storage capacity at the moment;
Figure DEST_PATH_IMAGE616
is composed of
Figure 555839DEST_PATH_IMAGE012
The storage temperature of the hot water at any moment;
Figure DEST_PATH_IMAGE618
is composed of
Figure 543387DEST_PATH_IMAGE012
The temperature of cold water replacing hot water at any moment;
Figure DEST_PATH_IMAGE620
is composed of
Figure 331476DEST_PATH_IMAGE012
The hot water quantity required to be provided by each multi-energy subsystem terminal user in the lower layer area at any time;
Figure DEST_PATH_IMAGE622
and
Figure DEST_PATH_IMAGE624
all are hot water load fluctuation coefficients;
Figure DEST_PATH_IMAGE626
is composed of
Figure 48765DEST_PATH_IMAGE012
The hot water comfort temperature value of the indoor of the building where each multi-energy subsystem terminal user is located in the lower layer area at the moment;
Figure DEST_PATH_IMAGE628
and
Figure DEST_PATH_IMAGE630
are respectively as
Figure 598695DEST_PATH_IMAGE012
Minimum and maximum allowable hot water storage temperatures;
Figure 834724DEST_PATH_IMAGE018
scheduling periods for the day aheadA period of time.
18. The regional multi-system double-layer decentralized optimization scheduling method considering the double-layer carbon emission optimization distribution model according to claim 1, wherein the specific process of the step 3 is as follows:
Figure DEST_PATH_IMAGE632
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE634
the constraint value is a total carbon emission constraint value of the regional multi-energy system, and the constraint value is iteratively updated according to the actual carbon emission optimized by each multi-energy subsystem in the lower region and the power distribution network system in the upper region multi-energy main system in the double-layer optimization process;
Figure DEST_PATH_IMAGE636
for each multi-energy subsystem in the lower region
Figure 987356DEST_PATH_IMAGE074
Figure DEST_PATH_IMAGE638
) A total carbon emission allowance constraint upper limit value;
Figure DEST_PATH_IMAGE640
Figure DEST_PATH_IMAGE642
respectively determining the upper limit value of carbon emission constraint of a power distribution network system in the upper-layer multi-energy main system and each multi-energy subsystem in the lower-layer area for the whole area;
Figure 795038DEST_PATH_IMAGE076
the number of each multi-energy subsystem in the lower layer area is collected.
19. The regional multi-system double-layer decentralized optimization scheduling method considering the double-layer carbon emission optimization distribution model according to claim 1, wherein a specific method for solving the complex regional multi-energy system double-layer decentralized coordination optimization scheduling model by using the improved target cascade analysis method is as follows:
respectively converting the objective functions of the upper-layer power distribution network, the gas distribution network and the heat distribution network system into the following forms:
Figure DEST_PATH_IMAGE644
Figure DEST_PATH_IMAGE646
Figure DEST_PATH_IMAGE648
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE650
Figure DEST_PATH_IMAGE652
Figure DEST_PATH_IMAGE654
respectively taking the transformed target functions of the distribution network, the distribution network and the heat distribution network system in the upper layer area;
Figure 171661DEST_PATH_IMAGE008
Figure 166424DEST_PATH_IMAGE024
Figure 201376DEST_PATH_IMAGE038
respectively as target functions of the upper power distribution network, the gas distribution network and the heat distribution network system;
Figure DEST_PATH_IMAGE656
Figure DEST_PATH_IMAGE658
Figure DEST_PATH_IMAGE660
respectively, the multi-energy subsystems in the lower layer area
Figure 627679DEST_PATH_IMAGE012
Connecting lines among a power distribution network, a gas distribution network and a heat distribution network system in the multi-energy main system in the time interval and the upper region transmit power auxiliary coupling variables;
Figure DEST_PATH_IMAGE662
Figure DEST_PATH_IMAGE664
Figure DEST_PATH_IMAGE666
the system of a power distribution network, a gas distribution network and a heat distribution network in the multi-energy main system of the upper layer respectively is arranged
Figure 879931DEST_PATH_IMAGE012
Connecting lines between the time interval and each multi-energy subsystem in the lower layer region transmit power coupling variables;
Figure DEST_PATH_IMAGE668
Figure DEST_PATH_IMAGE670
Figure DEST_PATH_IMAGE672
the target functions of the power distribution network, the gas distribution network and the heat distribution network are respectively
Figure 860525DEST_PATH_IMAGE012
A first order multiplier of a period lagrange penalty function;
Figure DEST_PATH_IMAGE674
Figure DEST_PATH_IMAGE676
Figure DEST_PATH_IMAGE678
the target functions of the power distribution network, the gas distribution network and the heat distribution network are respectively
Figure 139582DEST_PATH_IMAGE012
A quadratic multiplier of a period lagrange penalty function;
converting the objective function of each multi-energy subsystem in the lower zone area into the following form:
Figure DEST_PATH_IMAGE680
wherein the content of the first and second substances,
Figure 358074DEST_PATH_IMAGE074
representing a multi-energy subsystem in an underlying region;
Figure 623970DEST_PATH_IMAGE076
the number of each multi-energy subsystem in the lower layer area is collected;
Figure 826282DEST_PATH_IMAGE018
the period of the cycle is scheduled for the day ahead.
20. The regional multi-system double-layer decentralized optimization scheduling method according to claim 19, wherein in step 7, whether the difference between the coupling variables and the objective function of the upper/lower layer system optimization in the iterative optimization process meets the accuracy requirement is used as a convergence condition, which is specifically as follows:
Figure DEST_PATH_IMAGE682
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE684
Figure DEST_PATH_IMAGE686
Figure DEST_PATH_IMAGE688
respectively representing the convergence precision of the coupling variable difference and the target function difference between the multi-energy main system in the upper layer area and each multi-energy subsystem in the lower layer area; all superscripts
Figure 157031DEST_PATH_IMAGE146
The marks of the recorded data of the multi-energy main system in the upper layer area and the multi-energy subsystems in the lower layer area in the iterative optimization process are both represented;
Figure 495609DEST_PATH_IMAGE074
representing a multi-energy subsystem in an underlying region;
when the convergence criterion is not met, updating each multiplier parameter value of the improved target cascade analysis method according to the following formula, namely updating the quadratic term multiplier parameter value of the Lagrange penalty function:
Figure DEST_PATH_IMAGE690
wherein the content of the first and second substances,
Figure DEST_PATH_IMAGE692
the value is 2.5; the value of the lagrange penalty function multiplier is uniformly set to 1.5.
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