CN114004047A - Electric heating gas interconnection multi-energy system matrix operation model modeling method - Google Patents

Electric heating gas interconnection multi-energy system matrix operation model modeling method Download PDF

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CN114004047A
CN114004047A CN202111148312.3A CN202111148312A CN114004047A CN 114004047 A CN114004047 A CN 114004047A CN 202111148312 A CN202111148312 A CN 202111148312A CN 114004047 A CN114004047 A CN 114004047A
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钟永洁
李玉平
胡兵
张玮
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Nanjing SAC Automation Co Ltd
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Abstract

The invention discloses a modeling method of a matrix operation model of an electric-heating-gas interconnection multi-energy system, which is used for acquiring data information of the electric-heating-gas interconnection multi-energy system; establishing a matrixing operation model of the power system, wherein the matrixing operation model comprises a direct current power flow matrixing operation model and an alternating current power flow matrixing operation model; establishing a matrixing operation model of the thermodynamic system, wherein the matrixing operation model comprises a hydraulic model matrixing operation model, a node pressure and pressure drop matrixing operation model and a flow and temperature matrixing operation model; establishing a matrixing operation model of the natural gas system, wherein the matrixing operation model comprises a flow balance matrixing operation model and a pressure distribution matrixing operation model; and acquiring data information output by the matrixing operation models of all the electric power system, the thermodynamic system and the natural gas system. The model constructed by the invention has strong universality and wide application range, provides theoretical guidance and reference for quick topological structure analysis, quick data arrangement and induction of the electric-heating-gas interconnected multi-energy system, and saves the time, manpower and material resources of an engineering service site.

Description

Electric heating gas interconnection multi-energy system matrix operation model modeling method
Technical Field
The invention relates to a modeling method of a matrix operation model of an electric-heat-gas interconnection multi-energy system, and belongs to the technical field of electric-heat interconnection multi-energy systems.
Background
In recent years, the development of energy systems shows diversified, intelligent and informatization trends, and the combined coordinated operation of multiple or multiple energy conversion coupling devices provides abundant possibilities for operation management and control, regulation and the like of the electric-thermal-interconnection multi-energy system. The energy utilization develops towards the direction of multi-energy coordination, multi-energy complementary utilization, energy coordination deep cascade utilization and multi-source coupling integration. In order to further improve comprehensive energy efficiency grade, cultivate new energy supply and marketing mode state, reduce operation and maintenance operation economic cost, realize win-win situation, strengthen source, network, load and storage depth coordination interaction and fusion of various energy sources, the construction of the interconnected multi-energy system is one of important technical means for realizing multi-aspect interconnection and intercommunication, energy flow complementation and mutual aid and multi-type energy open interconnection of a novel energy system in the future, and the development of the modeling with strong universality and wide application range of the electric-thermal-electric-interconnection multi-energy system is a basic premise for constructing the interconnected multi-energy system.
In multiple aspects of energy production, transmission, conversion, allocation, storage, utilization, market trading and the like, the whole interconnected multi-energy system needs to be analyzed and researched by comprehensively considering the strategies and methods of coupling interconnection, unified integration, cooperative scheduling and optimized management, coupling interconnection and integration among multiple energy sources are enhanced, the coordination and complementation of multiple energy sources are promoted, and the cooperative optimization becomes the inevitable trend of the development of a novel energy system in the future. It should be noted that the heterogeneous energy interconnection system with the characteristics of multi-energy coordination and complementation becomes an effective scheme for solving the problems of high economic cost, pollution discharge and amplification, low comprehensive energy efficiency level and the like of single energy system operation. Particularly, the electricity, heat and gas interconnected energy system coordinates and complements multiple energy sources, is favorable for realizing economic and low-carbon targets, is favorable for realizing bidirectional complementary interaction and collaborative optimization of the multiple energy sources, and is one of effective means for improving the flexibility of system operation scheduling and resource coordination configuration.
However, the general modeling is complicated due to the fact that the types of the energy conversion equipment in the electric-heating-gas interconnection multi-energy system are complex and various, the coupling interconnection mode of the heterogeneous energy subsystem is complex, and the like. Therefore, it is necessary and urgent to provide a universal matrix modeling method for a multi-energy system with strong universality and wide application range in the energy subsystem level.
Disclosure of Invention
The purpose is as follows: in order to overcome the defects in the prior art, the invention provides a modeling method of a matrix operation model of an electric-heat-gas interconnected multi-energy system, which aims to realize quick topological structure analysis, quick data arrangement and induction on a system level and establish the matrix operation model with strong universality and wide application range, thereby achieving the purposes of saving engineering service site time, manpower and material resources and providing theoretical guidance and reference for modeling and operation of the electric-heat-gas interconnected multi-energy system.
The technical scheme is as follows: in order to solve the technical problems, the technical scheme adopted by the invention is as follows:
a modeling method for a matrix operation model of an electric-heating-gas interconnection multi-energy system comprises the following steps:
(1) the method comprises the steps of obtaining data information of an electric-heat-gas interconnection multi-energy system, wherein the data information comprises a coupling interconnection framework of the electric-heat-gas interconnection multi-energy system, energy conversion coupling equipment, power supplies, upper and lower limits of output power of a heat source and a natural gas source, a power system topological structure, a thermodynamic system topological structure, a natural gas system topological structure, power system circuit parameters, thermodynamic system pipeline branch parameters and natural gas system pipeline branch parameter data information.
(2) And establishing a matrixing operation model of the power system, wherein the matrixing operation model comprises a direct current power flow matrixing operation model and an alternating current power flow matrixing operation model.
(3) Establishing a matrixing operation model of the thermodynamic system, wherein the matrixing operation model comprises a hydraulic model matrixing operation model, a node pressure and pressure drop matrixing operation model and a flow and temperature matrixing operation model.
(4) And establishing a matrixing operation model of the natural gas system, wherein the matrixing operation model comprises a flow balance matrixing operation model and a pressure distribution matrixing operation model.
(5) Acquiring data information output by a matrixing operation model of all electric power systems, thermodynamic systems and natural gas systems, wherein the data information comprises power supply output of the electric power systems, node electric power, node reactive power, node voltage phase angle and node voltage data information; data information of heat source output, node mass flow, node thermal power, node pressure and pipeline pressure loss of the thermodynamic system; the natural gas system comprises the data information of gas source output, node pressure, pipeline natural gas flow, node natural gas flow, compressor consumption flow and compressor compression ratio.
Further, the step (2) of establishing a matrixing operation model of the power system comprises:
the direct current power flow matrixing operation model has the following specific expression:
Figure BDA0003286267810000021
in the formula:
Figure BDA0003286267810000022
for injecting a power vector at a time t node, where the elements
Figure BDA0003286267810000023
Here, the
Figure BDA0003286267810000024
And
Figure BDA0003286267810000025
respectively generator output and load at time t node i,
Figure BDA0003286267810000026
being a susceptance matrix, element B of the susceptance matrixij=-1/xij
Figure BDA0003286267810000027
Bij、xijRespectively the susceptance and reactance of a power network circuit or a branch circuit ij, wherein ij is the circuit or the branch circuit, and the serial numbers of the nodes at the head end and the tail end are i and j respectively;
Figure BDA0003286267810000028
is the voltage phase angle vector at time t node; subscripts i and j are numbers of different nodes of the power network.
The alternating current power flow matrixing operation model has the following specific expression:
Figure BDA0003286267810000031
in the formula: pt、QtRespectively are active power vectors and reactive power vectors of nodes in the power system at time t; u shapetIs a node voltage vector in the power system at time t; y is a node admittance matrix; re and Im are respectively the real part and the imaginary part of the vector; is an orientation quantity conjugate operation.
Further, the thermodynamic system is based on the idea of graph theory, the node numbers of the thermodynamic system are from 1 to the nodes, that is, the total number of the nodes of the thermodynamic system is the nodes; the number of the pipes or branches of the thermodynamic system is from 1 to b, i.e. the total number of branches of the thermodynamic system is b.
Further, the step (3) of establishing a matrixing operation model of the thermodynamic system comprises:
the hydraulic model matrixing operation model has the following specific expression:
Figure BDA0003286267810000032
in the formula:
Figure BDA0003286267810000033
is a complete correlation matrix related to the thermodynamic system nodes and the thermodynamic pipelines;
Figure BDA0003286267810000034
is a thermal medium mass flow vector of a thermal pipeline; 0 is a zero matrix vector;
Figure BDA0003286267810000035
a basic loop matrix related to a thermodynamic system closed loop;
Figure BDA0003286267810000036
is the thermodynamic pipeline pressure loss vector at time t;
Figure BDA0003286267810000037
is the vector of the head of the hot working medium raised by the pressure circulation pump at time t.
The node pressure and pressure drop matrixing operation model has the following specific expression:
Figure BDA0003286267810000038
wherein:
Figure BDA0003286267810000039
in the formula:
Figure BDA00032862678100000310
is a complete correlation matrix related to the thermodynamic system nodes and the thermodynamic pipelines;
Figure BDA00032862678100000311
is a node pressure vector in the thermodynamic system at time t;
Figure BDA00032862678100000312
is the thermodynamic pipeline pressure loss vector at time t;
Figure BDA00032862678100000313
is the hot working medium pressure head vector raised by the pressure circulating pump at the time t; the superscript b is the total number of branches of the thermodynamic system; superscript' is a vector transposition operation;
Figure BDA0003286267810000041
is the pressure at the node in the thermodynamic system at time t;
Figure BDA0003286267810000042
is the pressure loss in thermodynamic pipe b at time t;
Figure BDA0003286267810000043
is the head of the hot working medium raised by the pressure circulating pump in the thermodynamic system at time t.
The flow and temperature matrixing operation model has the following specific expression:
Figure BDA0003286267810000044
in the formula:
Figure BDA0003286267810000045
respectively inputting and outputting thermal power vectors of a thermal pipeline in a thermal system at time t;
Figure BDA0003286267810000046
is a node thermal load vector in the thermodynamic system at time t; cpThe specific heat capacity of the hot working medium;
Figure BDA0003286267810000047
the thermal medium mass flow vector is the thermal medium mass flow vector of the pipeline terminal node of the thermodynamic system at time t;
Figure BDA0003286267810000048
respectively are temperature vectors of an inlet port and an outlet port at a junction of the thermal pipeline and the thermal pipeline at time t;
Figure BDA0003286267810000049
respectively is a node-mass flow inflow pipeline starting point incidence matrix and a node-mass flow outflow pipeline end point incidence matrix in the thermodynamic system at time t.
Further, the natural gas system comprises a medium-pressure and high-pressure natural gas transmission system, the gas flow in the natural gas pipeline is closely related to the pressure intensity of nodes on two sides of the pipeline and the physical conditions of pipeline transmission, and the mathematical relationship is as follows:
Figure BDA00032862678100000410
in the formula: subscripts i, j and ij are a natural gas pipeline head end node, a pipeline tail end node and a pipeline number respectively;
Figure BDA00032862678100000411
respectively the natural gas pressure at the natural gas system nodes i and j at the time t;
Figure BDA00032862678100000412
is the natural gas flow direction variable of the natural gas system at time t;
Figure BDA00032862678100000413
is a pipeline characteristic constant;
Figure BDA00032862678100000414
is the amount of air flow in the duct at time t; kijIs a pipeline branch equivalent characteristic physical parameter, also called natural gas pipeline branch impedance;
Figure BDA00032862678100000415
is the square difference of the equivalent pressure at the head end and the tail end of the branch.
Numbering nodes in the topological relation of the medium-pressure and high-pressure natural gas systems based on the idea of graph theory, wherein the number of the nodes is from 1 to the node, namely the total number of the nodes is the node; numbering natural gas pipelines or topological branches, and the number of the branchesFrom 1 to b, i.e. the total number of branches is b. Then, the compression ratio of the compressor of each branch can be respectively numbered as
Figure BDA00032862678100000416
To
Figure BDA00032862678100000417
The natural gas system pipeline flow direction variables can respectively correspond to branch numbers of
Figure BDA00032862678100000418
To
Figure BDA00032862678100000419
The branch equivalent characteristic parameters can respectively correspond to branch numbers K1To Kb(ii) a The equivalent pressure square differences of the head and the tail ends of the branch can respectively correspond to the serial numbers of the branches as
Figure BDA0003286267810000051
To
Figure BDA0003286267810000052
The injected natural gas flow rate of each node can be respectively numbered as
Figure BDA0003286267810000053
To
Figure BDA0003286267810000054
The natural gas flow of each branch can be respectively numbered as
Figure BDA0003286267810000055
To
Figure BDA0003286267810000056
The natural gas flow consumed by the compressor on each branch can be respectively numbered as
Figure BDA0003286267810000057
To
Figure BDA0003286267810000058
Further, the step (4) of establishing a matrixing operation model of the natural gas system comprises the following steps: the flow balance matrixing operation model and the pressure distribution matrixing operation model comprise:
the flow balance matrixing operation model has the following specific expression:
Figure BDA0003286267810000059
wherein:
Figure BDA00032862678100000510
in the formula:
Figure BDA00032862678100000511
a natural gas system node-branch complete incidence matrix; f. oftIs the natural gas flow vector through the pipeline in the natural gas network at time t;
Figure BDA00032862678100000512
a complete starting point incidence matrix related to network nodes and pipeline branches in the natural gas network;
Figure BDA00032862678100000513
the natural gas flow vector input into the branch compressor in the natural gas network at time t; q. q.stInjecting flow vectors for nodes in the natural gas system at time t; the superscript b is the total number of the natural gas pipeline branches; subscript node is the total number of topological nodes of the natural gas system; superscript' is a vector transposition operation;
Figure BDA00032862678100000514
is the natural gas flow rate in branch b in the natural gas system at time t;
Figure BDA00032862678100000515
is the natural gas flow consumed by the compressor on time t leg b;
Figure BDA00032862678100000516
the flow of natural gas is injected at time tnode.
The pressure distribution matrixing operation model has the following specific expression:
Figure BDA00032862678100000517
wherein:
Figure BDA0003286267810000061
in the formula:
Figure BDA0003286267810000062
a complete starting point incidence matrix related to network nodes and pipeline branches in the natural gas network;
Figure BDA0003286267810000063
is a diagonal matrix relating to the compression ratio of the branch compressors in the natural gas network at time t;
Figure BDA0003286267810000064
a natural gas system node-branch complete terminal incidence matrix;
Figure BDA0003286267810000065
is the node pressure flat direction quantity in the natural gas system at time t; II typetThe equivalent pressure square error vector of the head end and the tail end of a branch in the natural gas system at the time t is shown; superscript' is a vector transposition operation;
Figure BDA0003286267810000066
the compressor compression ratio for leg b at time t;
Figure BDA0003286267810000067
is the square of the pressure at the node in the natural gas system at time t;
Figure BDA0003286267810000068
is the natural gas flow direction of branch b in the natural gas system at time t; kbIs the physical parameter of the pipeline branch b;
Figure BDA0003286267810000069
is the flow of natural gas through line b at time t.
Further, the natural gas system further comprises:
when there is no compressor in the ith branch, setting compression ratio
Figure BDA00032862678100000610
And setting the natural gas flow consumed by the compressor
Figure BDA00032862678100000611
In particular, for the electric compressor, provision is always made for
Figure BDA00032862678100000612
Secondly, the gas flow direction of the natural gas system is usually determined, and particularly in a high-pressure natural gas transmission system, the gas flow direction cannot be easily changed in various regulating valves and practical engineering application, so that the natural gas topological relation is usually determined, namely the flow direction variable of a pipeline of the natural gas system is usually a known quantity.
When the ith node is an air source node
Figure BDA00032862678100000613
When the value is positive, it is the gas load node
Figure BDA00032862678100000614
When the value is negative, as the intermediate node
Figure BDA00032862678100000615
The value is 0.
The matrixing equation of the medium-high pressure natural gas transmission system is also suitable for the low-pressure gas distribution system, and at the moment
Figure BDA00032862678100000616
Figure BDA00032862678100000617
Has the advantages that: compared with the prior art, the electric heating gas interconnection multi-energy system matrixing operation model modeling method comprehensively considers the electric heating gas heterogeneous energy subsystem at the same time, and can provide theoretical guidance for modeling and running of the multi-energy system; the invention provides a matrixing operation model of an electric power system, a thermodynamic system and a natural gas system, which has strong universality and wide application range; the invention can effectively provide theoretical guidance and reference for rapid topological structure analysis, rapid data arrangement and induction of the electric-heating-gas interconnected multi-energy system on the system level, and saves the time of engineering service site and manpower and material resources.
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FIG. 1 is a flow chart of a method of the present invention.
Detailed Description
The present invention will be further described with reference to the following examples.
Example 1:
a modeling method of a matrix operation model of an electric-heating-gas interconnection multi-energy system is shown in figure 1 and comprises the following steps:
(1) acquiring data information of electric heating and gas interconnection multi-energy system
The method comprises the steps of obtaining data information of the electric-heat-gas interconnection multi-energy system, wherein the data information comprises data such as a coupling interconnection framework of the electric-heat-gas interconnection multi-energy system, energy conversion coupling equipment, output power upper and lower limits of a power supply, a heat source and a natural gas source, a power system topological structure, a thermodynamic system topological structure, a natural gas system topological structure, power system circuit parameters, thermodynamic system pipeline branch parameters, natural gas system pipeline branch parameters and the like.
(2) Establishing a matrixing operation model of an electric power system
Establishing a direct current power flow equation for the power system, wherein a specific expression of a matrix form is as follows:
Figure BDA0003286267810000071
in the formula:
Figure BDA0003286267810000072
for injecting a power vector at a time t node, where the elements
Figure BDA0003286267810000073
Here, the
Figure BDA0003286267810000074
And
Figure BDA0003286267810000075
the output power and the load of the generator at a time t node i are respectively shown, and subscripts i and j are numbers of different nodes of the power network;
Figure BDA0003286267810000076
is a susceptance matrix in which the element Bij=-1/xij
Figure BDA0003286267810000077
B. x is susceptance and reactance of the power network circuit or branch circuit respectively, ij is the circuit or branch circuit, and the serial numbers of the nodes at the head end and the tail end of the circuit or branch circuit are i and j respectively;
Figure BDA0003286267810000078
is a vector of voltage phase angles at node t at time t.
The classical alternating current power flow model in the power system is described by a matrix form, and the mathematical model is concretely as follows:
Figure BDA0003286267810000081
in the formula: pt、QtRespectively are active power vectors and reactive power vectors of nodes in the power system at time t; u shapetIs a node voltage vector in the power system at time t; y is a node admittance matrix; re and Im are respectively the real part and the imaginary part of the vector; is an orientation quantity conjugate operation.
(3) Establishing a thermodynamic system matrixing operation model
Aiming at a thermodynamic system, based on the idea of graph theory, the node number of the thermodynamic system is from 1 to node, namely the total number of the nodes of the thermodynamic system is the node; the number of the pipes or branches of the thermodynamic system is from 1 to b, i.e. the total number of branches of the thermodynamic system is b.
The specific expression of the hydraulic model matrixing operation of the thermodynamic system is as follows:
Figure BDA0003286267810000082
in the formula:
Figure BDA0003286267810000083
is a complete correlation matrix related to the thermodynamic system nodes and the thermodynamic pipelines;
Figure BDA0003286267810000084
is a thermal medium mass flow vector of a thermal pipeline; 0 is a zero matrix vector;
Figure BDA0003286267810000085
a basic loop matrix related to a thermodynamic system closed loop;
Figure BDA0003286267810000086
is the thermodynamic pipeline pressure loss vector at time t;
Figure BDA0003286267810000087
is the vector of the head of the hot working medium raised by the pressure circulation pump at time t.
When the node pressure and the pressure drop in the thermodynamic system are subjected to matrixing operation, the specific expression is as follows:
Figure BDA0003286267810000088
wherein:
Figure BDA0003286267810000089
in the formula:
Figure BDA00032862678100000810
is a complete correlation matrix related to the thermodynamic system nodes and the thermodynamic pipelines;
Figure BDA00032862678100000811
is a node pressure vector in the thermodynamic system at time t;
Figure BDA00032862678100000812
is the thermodynamic pipeline pressure loss vector at time t;
Figure BDA00032862678100000813
is the hot working medium pressure head vector raised by the pressure circulating pump at the time t; the superscript b is the total number of branches of the thermodynamic system;
Figure BDA00032862678100000814
is the pressure at the node in the thermodynamic system at time t;
Figure BDA0003286267810000091
is the pressure loss in thermodynamic pipe b at time t;
Figure BDA0003286267810000092
is the head of the hot working medium raised by the pressure circulating pump in the thermodynamic system at time t.
The matrix operation model for expressing the flow and the temperature of the thermodynamic system by using a matrix equation set is concretely as follows:
Figure BDA0003286267810000093
in the formula:
Figure BDA0003286267810000094
respectively inputting and outputting thermal power vectors of a thermal pipeline in a thermal system at time t;
Figure BDA0003286267810000095
is a node thermal load vector in the thermodynamic system at time t; cpThe specific heat capacity of the hot working medium;
Figure BDA0003286267810000096
the thermal medium mass flow vector is the thermal medium mass flow vector of the pipeline terminal node of the thermodynamic system at time t;
Figure BDA0003286267810000097
respectively are temperature vectors of an inlet port and an outlet port at a junction of the thermal pipeline and the thermal pipeline at time t;
Figure BDA0003286267810000098
respectively is a node-mass flow inflow pipeline starting point incidence matrix and a node-mass flow outflow pipeline end point incidence matrix in the thermodynamic system at time t.
(4) Establishing a natural gas system matrixing operation model
For a medium-high pressure natural gas transmission system, the gas flow in a natural gas pipeline is closely related to the pressure of nodes on two sides of the pipeline and the physical conditions of pipeline transmission, and the mathematical relationship is as follows:
Figure BDA0003286267810000099
in the formula: subscripts i, j and ij are a natural gas pipeline head end node, a pipeline tail end node and a pipeline number respectively;
Figure BDA00032862678100000910
respectively the natural gas pressure at the natural gas system nodes i and j at the time t;
Figure BDA00032862678100000911
is the natural gas flow direction variable of the natural gas system at time t;
Figure BDA00032862678100000912
is a pipeline characteristic constant;
Figure BDA00032862678100000913
is the amount of air flow in the duct at time t; kijIs a pipeline branch equivalent characteristic physical parameter, also called natural gas pipeline branch impedance;
Figure BDA00032862678100000914
is the square difference of the equivalent pressure at the head end and the tail end of the branch.
Analyzing the topological relation of the medium and high-voltage natural gas transmission system based on the idea of graph theory, numbering topological nodes of the natural gas transmission system, and counting the number of the nodes from 1 to the node, namely counting the total number of the nodes as the node; numbering the natural gas pipelines or topological branches, wherein the number of the branches is from 1 to b, namely the total number of the branches is b. Then, the compression ratio of the compressor of each branch can be respectively numbered as
Figure BDA00032862678100000915
To
Figure BDA00032862678100000916
The natural gas system pipeline flow direction variables can respectively correspond to branch numbers of
Figure BDA00032862678100000917
To
Figure BDA00032862678100000918
The branch equivalent characteristic parameters can respectively correspond to branch numbers K1To Kb(ii) a The equivalent pressure square differences of the head and the tail ends of the branch can respectively correspond to the serial numbers of the branches as
Figure BDA0003286267810000101
To
Figure BDA0003286267810000102
The injected natural gas flow rate of each node can be respectively numbered as
Figure BDA0003286267810000103
To
Figure BDA0003286267810000104
The natural gas flow of each branch can be respectively numbered as
Figure BDA0003286267810000105
To
Figure BDA0003286267810000106
The natural gas flow consumed by the compressor on each branch can be respectively numbered as
Figure BDA0003286267810000107
To
Figure BDA0003286267810000108
The expression of the flow balance matrixing equation of the natural gas system is as follows:
Figure BDA0003286267810000109
wherein:
Figure BDA00032862678100001010
in the formula:
Figure BDA00032862678100001011
a natural gas system node-branch complete incidence matrix; f. oftFor flowing through pipes in natural gas networks at times tA natural gas flow vector;
Figure BDA00032862678100001012
a complete starting point incidence matrix related to network nodes and pipeline branches in the natural gas network;
Figure BDA00032862678100001013
the natural gas flow vector input into the branch compressor in the natural gas network at time t; q. q.stInjecting flow vectors for nodes in the natural gas system at time t; the superscript b is the total number of the natural gas pipeline branches; subscript node is the total number of topological nodes of the natural gas system; superscript' is a vector transposition operation;
Figure BDA00032862678100001014
is the natural gas flow rate in branch b in the natural gas system at time t;
Figure BDA00032862678100001015
is the natural gas flow consumed by the compressor on time t leg b;
Figure BDA00032862678100001016
the flow of natural gas is injected at time tnode.
The expression of the pressure distribution matrixing equation of the natural gas system is as follows:
Figure BDA00032862678100001017
wherein:
Figure BDA0003286267810000111
in the formula:
Figure BDA0003286267810000112
a complete starting point incidence matrix related to network nodes and pipeline branches in the natural gas network;
Figure BDA0003286267810000113
is a diagonal matrix relating to the compression ratio of the branch compressors in the natural gas network at time t;
Figure BDA0003286267810000114
a natural gas system node-branch complete terminal incidence matrix;
Figure BDA0003286267810000115
is the node pressure flat direction quantity in the natural gas system at time t; II typetThe equivalent pressure square error vector of the head end and the tail end of a branch in the natural gas system at the time t is shown; superscript' is a vector transposition operation;
Figure BDA0003286267810000116
the compressor compression ratio for leg b at time t;
Figure BDA0003286267810000117
is the square of the pressure at the node in the natural gas system at time t;
Figure BDA0003286267810000118
is the natural gas flow direction of branch b in the natural gas system at time t; kbIs the physical parameter of the pipeline branch b;
Figure BDA0003286267810000119
is the flow of natural gas through line b at time t.
The matrixing model for the natural gas system is explained as follows:
when there is no compressor in the ith branch, setting compression ratio
Figure BDA00032862678100001110
And setting the natural gas flow consumed by the compressor
Figure BDA00032862678100001111
In particular, for the electric compressor, provision is always made for
Figure BDA00032862678100001112
Secondly, the gas flow direction of the natural gas system is usually determined, and particularly in a high-pressure natural gas transmission system, the gas flow direction cannot be easily changed in various regulating valves and practical engineering application, so that the natural gas topological relation is usually determined, namely the flow direction variable of a pipeline of the natural gas system is usually a known quantity.
When the ith node is an air source node
Figure BDA00032862678100001113
When the value is positive, it is the gas load node
Figure BDA00032862678100001114
When the value is negative, as the intermediate node
Figure BDA00032862678100001115
The value is 0.
The matrixing equation of the medium-high pressure natural gas transmission system is also suitable for the low-pressure gas distribution system, and at the moment
Figure BDA00032862678100001116
Figure BDA00032862678100001117
(5) Outputting matrixed model data information
Outputting matrixing model data information including data information such as power supply output of an electric power system, node electric power, node reactive power, node voltage phase angle, node voltage and the like; data information of heat source output, node mass flow, node thermal power, node pressure, pipeline pressure loss and the like of the thermodynamic system; the natural gas system comprises data information such as gas source output, node pressure, pipeline natural gas flow, node natural gas flow, compressor consumption flow, compressor compression ratio and the like.
The above description is only of the preferred embodiments of the present invention, and it should be noted that: it will be apparent to those skilled in the art that various modifications and adaptations can be made without departing from the principles of the invention and these are intended to be within the scope of the invention.

Claims (9)

1. A modeling method for a matrix operation model of an electric-heating-gas interconnection multi-energy system is characterized by comprising the following steps of: the method comprises the following steps:
acquiring data information of an electric heating and gas interconnection multi-energy system;
establishing a matrixing operation model of the power system according to the data information, wherein the matrixing operation model comprises a direct current power flow matrixing operation model and an alternating current power flow matrixing operation model;
establishing a matrixing operation model of the thermodynamic system according to the data information, wherein the matrixing operation model comprises a hydraulic model matrixing operation model, a node pressure and pressure drop matrixing operation model and a flow and temperature matrixing operation model;
and establishing a matrixing operation model of the natural gas system according to the data information, wherein the matrixing operation model comprises a flow balance matrixing operation model and a pressure distribution matrixing operation model.
2. The modeling method of the electric-thermal-gas interconnection multi-energy system matrixing operation model of claim 1 is characterized in that: the data information of the electric-heat-gas interconnection multi-energy system comprises a coupling interconnection framework of the electric-heat-gas interconnection multi-energy system, energy conversion coupling equipment, power supplies, upper and lower limits of output power of a heat source and a natural gas source, a power system topological structure, a thermodynamic system topological structure, a natural gas system topological structure, power system circuit parameters, thermodynamic system pipeline branch parameters and natural gas system pipeline branch parameter data information.
3. The modeling method of the electric-thermal-gas interconnection multi-energy system matrixing operation model of claim 1 is characterized in that: further comprising:
acquiring data information output by a matrixing operation model of all electric power systems, thermodynamic systems and natural gas systems, wherein the data information comprises power supply output of the electric power systems, node electric power, node reactive power, node voltage phase angle and node voltage data information; data information of heat source output, node mass flow, node thermal power, node pressure and pipeline pressure loss of the thermodynamic system; the natural gas system comprises the data information of gas source output, node pressure, pipeline natural gas flow, node natural gas flow, compressor consumption flow and compressor compression ratio.
4. The modeling method of the electric-thermal-gas interconnection multi-energy system matrixing operation model according to claim 1 or 3, characterized in that: the specific expression of the direct current power flow matrixing operation model is as follows:
Figure FDA0003286267800000011
in the formula:
Figure FDA0003286267800000012
for injecting a power vector at a time t node, where the elements
Figure FDA0003286267800000013
Here, the
Figure FDA0003286267800000014
And
Figure FDA0003286267800000015
respectively generator output and load at time t node i,
Figure FDA0003286267800000016
being a susceptance matrix, element B of the susceptance matrixij=-1/xij
Figure FDA0003286267800000017
Bij、xijRespectively the susceptance and reactance of a power network line or a branch ij, wherein ij is the line or the branch, and the serial numbers of the nodes at the head end and the tail end are respectivelyi、j;
Figure FDA0003286267800000018
Is the voltage phase angle vector at time t node; subscripts i and j are numbers of different nodes of the power network;
the specific expression of the alternating current power flow matrixing operation model is as follows:
Figure FDA0003286267800000021
in the formula: pt、QtRespectively are active power vectors and reactive power vectors of nodes in the power system at time t; u shapetIs a node voltage vector in the power system at time t; y is a node admittance matrix; re and Im are respectively the real part and the imaginary part of the vector; is an orientation quantity conjugate operation.
5. The modeling method of the electric-thermal-gas interconnection multi-energy system matrixing operation model according to claim 1 or 3, characterized in that: the thermodynamic system is based on the idea of graph theory, the node number of the thermodynamic system is from 1 to the node, namely the total number of the nodes of the thermodynamic system is the node; the number of the pipes or branches of the thermodynamic system is from 1 to b, i.e. the total number of branches of the thermodynamic system is b.
6. The modeling method of the electric-thermal-gas interconnection multi-energy system matrixing operation model according to claim 5 is characterized in that: the hydraulic model matrixing operation model has the following specific expression:
Figure FDA0003286267800000022
in the formula:
Figure FDA0003286267800000023
is a complete correlation matrix related to the thermodynamic system nodes and the thermodynamic pipelines;
Figure FDA0003286267800000024
is a thermal medium mass flow vector of a thermal pipeline; 0 is a zero matrix vector;
Figure FDA0003286267800000025
a basic loop matrix related to a thermodynamic system closed loop;
Figure FDA0003286267800000026
is the thermodynamic pipeline pressure loss vector at time t;
Figure FDA0003286267800000027
is the hot working medium pressure head vector raised by the pressure circulating pump at the time t;
the node pressure and pressure drop matrixing operation model has the following specific expression:
Figure FDA0003286267800000028
wherein:
Figure FDA0003286267800000029
in the formula:
Figure FDA00032862678000000210
is a complete correlation matrix related to the thermodynamic system nodes and the thermodynamic pipelines;
Figure FDA00032862678000000211
is a node pressure vector in the thermodynamic system at time t;
Figure FDA0003286267800000031
is the thermodynamic pipeline pressure loss vector at time t;
Figure FDA0003286267800000032
is the hot working medium pressure head vector raised by the pressure circulating pump at the time t; the superscript b is the total number of branches of the thermodynamic system; superscript' is a vector transposition operation;
Figure FDA0003286267800000033
is the pressure at the node in the thermodynamic system at time t;
Figure FDA0003286267800000034
is the pressure loss in thermodynamic pipe b at time t;
Figure FDA0003286267800000035
is the head of the hot working medium raised by the pressure circulating pump in the thermodynamic system at time t.
The flow and temperature matrixing operation model has the following specific expression:
Figure FDA0003286267800000036
in the formula:
Figure FDA0003286267800000037
respectively inputting and outputting thermal power vectors of a thermal pipeline in a thermal system at time t;
Figure FDA0003286267800000038
is a node thermal load vector in the thermodynamic system at time t; cpThe specific heat capacity of the hot working medium;
Figure FDA0003286267800000039
the thermal medium mass flow vector is the thermal medium mass flow vector of the pipeline terminal node of the thermodynamic system at time t;
Figure FDA00032862678000000310
respectively at time tmoriThe temperature vectors of an inlet port and an outlet port at the junction of the pipeline and the heat distribution pipeline;
Figure FDA00032862678000000311
respectively is a node-mass flow inflow pipeline starting point incidence matrix and a node-mass flow outflow pipeline end point incidence matrix in the thermodynamic system at time t.
7. The modeling method of the electric-thermal-gas interconnection multi-energy system matrixing operation model according to claim 1 or 3, characterized in that: the natural gas system comprises a medium-pressure and high-pressure natural gas transmission system, wherein the gas flow in the natural gas pipeline is closely related to the pressure intensity of nodes on two sides of the pipeline and the physical conditions of pipeline transmission, and the mathematical relationship is as follows:
Figure FDA00032862678000000312
in the formula: subscripts i, j and ij are a natural gas pipeline head end node, a pipeline tail end node and a pipeline number respectively;
Figure FDA00032862678000000313
respectively the natural gas pressure at the natural gas system nodes i and j at the time t;
Figure FDA00032862678000000314
is the natural gas flow direction variable of the natural gas system at time t;
Figure FDA00032862678000000315
is a pipeline characteristic constant;
Figure FDA00032862678000000316
is the amount of air flow in the duct at time t; kijIs a pipeline branch equivalent characteristic physical parameter, also called natural gas pipeline branch impedance;
Figure FDA00032862678000000317
the square difference of the equivalent pressure at the head end and the tail end of the branch is taken as the pressure difference of the equivalent pressure at the head end and the tail end of the branch;
numbering nodes in the topological relation of the medium-pressure and high-pressure natural gas systems based on the idea of graph theory, wherein the number of the nodes is from 1 to the node, namely the total number of the nodes is the node; numbering natural gas pipelines or topological branches, wherein the number of the branches is from 1 to b, namely the total number of the branches is b; then, the compression ratio of the compressor of each branch can be respectively numbered as
Figure FDA0003286267800000041
To
Figure FDA0003286267800000042
The natural gas system pipeline flow direction variables can respectively correspond to branch numbers of
Figure FDA0003286267800000043
To
Figure FDA0003286267800000044
The branch equivalent characteristic parameters can respectively correspond to branch numbers K1To Kb(ii) a The equivalent pressure square differences of the head and the tail ends of the branch can respectively correspond to the serial numbers of the branches as
Figure FDA0003286267800000045
To
Figure FDA0003286267800000046
The injected natural gas flow rate of each node can be respectively numbered as
Figure FDA0003286267800000047
To
Figure FDA0003286267800000048
The natural gas flow of each branch can be respectively numbered as
Figure FDA0003286267800000049
To
Figure FDA00032862678000000410
The natural gas flow consumed by the compressor on each branch can be respectively numbered as
Figure FDA00032862678000000411
To
Figure FDA00032862678000000412
8. The modeling method of the electric-thermal-gas interconnection multi-energy system matrixing operation model of claim 7 is characterized in that: the flow balance matrixing operation model has the following specific expression:
Figure FDA00032862678000000413
wherein:
Figure FDA00032862678000000414
in the formula:
Figure FDA00032862678000000415
a natural gas system node-branch complete incidence matrix; f. oftIs the natural gas flow vector through the pipeline in the natural gas network at time t;
Figure FDA00032862678000000416
a complete starting point incidence matrix related to network nodes and pipeline branches in the natural gas network;
Figure FDA00032862678000000417
at time t daysThe natural gas flow vector input into the branch compressor in the natural gas network; q. q.stInjecting flow vectors for nodes in the natural gas system at time t; the superscript b is the total number of the natural gas pipeline branches; subscript node is the total number of topological nodes of the natural gas system; superscript' is a vector transposition operation;
Figure FDA00032862678000000418
is the natural gas flow rate in branch b in the natural gas system at time t;
Figure FDA00032862678000000419
is the natural gas flow consumed by the compressor on time t leg b;
Figure FDA00032862678000000420
is the flow of injected natural gas at time tnode;
the pressure distribution matrixing operation model has the following specific expression:
Figure FDA0003286267800000051
wherein:
Figure FDA0003286267800000052
in the formula:
Figure FDA0003286267800000053
a complete starting point incidence matrix related to network nodes and pipeline branches in the natural gas network;
Figure FDA0003286267800000054
is a diagonal matrix relating to the compression ratio of the branch compressors in the natural gas network at time t;
Figure FDA0003286267800000055
a natural gas system node-branch complete terminal incidence matrix;
Figure FDA0003286267800000056
is the node pressure flat direction quantity in the natural gas system at time t; II typetThe equivalent pressure square error vector of the head end and the tail end of a branch in the natural gas system at the time t is shown; superscript' is a vector transposition operation;
Figure FDA0003286267800000057
the compressor compression ratio for leg b at time t;
Figure FDA0003286267800000058
is the square of the pressure at the node in the natural gas system at time t;
Figure FDA0003286267800000059
is the natural gas flow direction of branch b in the natural gas system at time t; kbIs the physical parameter of the pipeline branch b;
Figure FDA00032862678000000510
is the flow of natural gas through line b at time t.
9. The modeling method of the electric-thermal-gas interconnection multi-energy system matrixing operation model of claim 7 is characterized in that: further comprising:
when no compressor is arranged in the ith branch, the compression ratio is set at the moment
Figure FDA00032862678000000511
And setting the natural gas flow consumed by the compressor
Figure FDA00032862678000000512
In particular, for the electric compressor, provision is always made for
Figure FDA00032862678000000513
The gas flow direction of a natural gas system is usually determined, particularly in a high-pressure natural gas transmission system, the gas flow direction cannot be easily changed in various regulating valves and practical engineering application, so that the natural gas topological relation is usually determined, namely the flow direction variable of a pipeline of the natural gas system is usually a known quantity;
when the ith node is an air source node
Figure FDA00032862678000000514
When the value is positive, it is the gas load node
Figure FDA00032862678000000515
When the value is negative, as the intermediate node
Figure FDA00032862678000000516
The value is 0;
the matrixing equation of the medium-high pressure natural gas transmission system is also suitable for the low-pressure gas distribution system, and at the moment
Figure FDA0003286267800000061
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