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JP5487908B2 - Electric heat supply and demand control system and electric heat supply and demand control method for distributed power supply system - Google Patents
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JP5487908B2 - Electric heat supply and demand control system and electric heat supply and demand control method for distributed power supply system - Google Patents

Electric heat supply and demand control system and electric heat supply and demand control method for distributed power supply system Download PDF

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JP5487908B2
JP5487908B2 JP2009266311A JP2009266311A JP5487908B2 JP 5487908 B2 JP5487908 B2 JP 5487908B2 JP 2009266311 A JP2009266311 A JP 2009266311A JP 2009266311 A JP2009266311 A JP 2009266311A JP 5487908 B2 JP5487908 B2 JP 5487908B2
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康治 渡辺
孝則 林
義道 奥野
靖之 星
隆之 田邊
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Meidensha Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E40/00Technologies for an efficient electrical power generation, transmission or distribution
    • Y02E40/70Smart grids as climate change mitigation technology in the energy generation sector
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y04INFORMATION OR COMMUNICATION TECHNOLOGIES HAVING AN IMPACT ON OTHER TECHNOLOGY AREAS
    • Y04SSYSTEMS INTEGRATING TECHNOLOGIES RELATED TO POWER NETWORK OPERATION, COMMUNICATION OR INFORMATION TECHNOLOGIES FOR IMPROVING THE ELECTRICAL POWER GENERATION, TRANSMISSION, DISTRIBUTION, MANAGEMENT OR USAGE, i.e. SMART GRIDS
    • Y04S10/00Systems supporting electrical power generation, transmission or distribution
    • Y04S10/12Monitoring or controlling equipment for energy generation units, e.g. distributed energy generation [DER] or load-side generation

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Description

本発明は、分散電源系統を構成する各電熱設備にそれぞれエージェントを設け、各エージェント間の情報交換によって各電熱設備の電熱需給出力を決定する分散電源系統の電熱需給制御システムおよび電熱需給制御方法に関する。   The present invention relates to an electric heat supply and demand control system and an electric heat supply and demand control method for a distributed power supply system in which an agent is provided in each electric heating facility constituting a distributed power supply system, and an electric heat supply and demand output of each electric heating facility is determined by information exchange between the agents. .

(1)電熱需給制御方式には以下の2種類がある。   (1) There are the following two types of electric heat supply and demand control methods.

(a)中央集中方式…中央集中制御装置による、発電機などの分散電源の制御方式
図3に中央集中方式を示すように、中央集中制御装置100が下位の制御装置200a〜200dから情報を受け取り、その情報を元に制御装置別の制御指令値、目標値を求め、それらを制御装置200a〜200dに送り返す。
(A) Centralized centralized system: Control system for distributed power sources such as generators by centralized centralized control device As shown in FIG. 3, the centralized centralized control device 100 receives information from the lower control devices 200a to 200d. Based on the information, the control command value and the target value for each control device are obtained, and these are sent back to the control devices 200a to 200d.

(b)自律分散方式…中央集中制御装置などの統括的な装置なしで、下位の装置による制御方式
図4に自律分散方式を示すように、下位の制御装置200a〜200dのみで構成され、他装置との情報交換を行い、自装置の制御指令値を決定する。
(B) Autonomous distributed system: Control system by lower-level devices without a central device such as a centralized control device. As shown in FIG. 4, the autonomous distributed system is configured only by lower-level control devices 200a to 200d. Exchange information with the device and determine the control command value of the device itself.

(2)分散電源系統制御への適用
上記、制御方式を分散電源系統の制御に適用すると、システム構成は以下のようになる。ただし、以下に示す、「分散電源」とはガスタービン発電機や風力発電などの自然エネルギー発電機などの基礎電源や分散電源だけでなく、ボイラー設備などの基礎熱源も含まれる。また、「負荷」については電力負荷だけでなく、熱負荷も含まれる。
(2) Application to distributed power system control When the above control method is applied to control of a distributed power system, the system configuration is as follows. However, the “distributed power source” shown below includes not only basic power sources such as gas turbine generators and natural energy generators such as wind power generators and distributed power sources but also basic heat sources such as boiler facilities. Further, “load” includes not only electric power load but also heat load.

(a)図5は中央集中方式による分散電源系統の制御処理手順図を示す。中央集中制御装置100は、下位の制御装置200a〜200dからの分散電源・負荷300a〜300dなどの出力状況の情報を受け取り、天候予測や需要予測などを考慮した制御指令値を最適化計算式で算出し、それらを下位の制御装置200a〜200dに送信する。これら制御指令値などを受け取った下位の制御装置200a〜200dは分散電源・負荷300a〜300dに対し、電熱需給制御を行う。   (A) FIG. 5 shows a control processing procedure diagram of the distributed power supply system by the centralized system. The centralized control device 100 receives output status information such as distributed power supplies / loads 300a to 300d from the lower control devices 200a to 200d and optimizes control command values in consideration of weather forecasts, demand forecasts, etc. Calculate them and send them to the lower control devices 200a to 200d. The lower-level control devices 200a to 200d that have received these control command values and the like perform electric heat supply and demand control for the distributed power supplies / loads 300a to 300d.

(b)図6は自律分散方式による分散電源系統制御方式を示す。制御装置200a〜200dは、相互に情報交換し、分散電源・負荷300a〜300dの最適化の制御指令値を算出し、その結果を元に分散電源・負荷300a〜300dを個々に電熱需給制御し、系統全体として最適化電熱需給制御を行う。   (B) FIG. 6 shows a distributed power system control system based on the autonomous distributed system. The control devices 200a to 200d exchange information with each other, calculate control command values for optimizing the distributed power sources / loads 300a to 300d, and individually control the electric power supply and demand for the distributed power sources / loads 300a to 300d based on the results. Optimize electric power supply and demand control for the entire system.

このときの制御装置200a〜200dにおける相互の情報交換は、契約ネットプロトコルによるエージェント同士で行い、この情報交換によって各設備の電熱出力を決定および制御している(例えば、特許文献1参照)。この特許文献1の情報交換処理は図7に示す処理手順S1〜S4としている。なお、各エージェントはコンピュータ資源とこれを利用して所期のアルゴリズムを実行するためのソフトウェアで構成される。   Mutual information exchange in the control devices 200a to 200d at this time is performed between agents based on the contract net protocol, and the electric heat output of each facility is determined and controlled by this information exchange (for example, see Patent Document 1). The information exchange process of this patent document 1 is made into process sequence S1-S4 shown in FIG. Each agent is composed of a computer resource and software for executing a desired algorithm using the computer resource.

(S1)エージェントAG1は他エージェントAG2〜AG4に対し、タスクを提示する。   (S1) Agent AG1 presents tasks to other agents AG2 to AG4.

(S2)タスクを受けたエージェントAG2〜AG4は制御しようとする分散電源・負荷の稼働状態を見てタスクを行うことができるか判断し、エージェントAG1に返信する。   (S2) The agents AG2 to AG4 that have received the task determine whether the task can be performed by looking at the operating state of the distributed power source / load to be controlled, and send it back to the agent AG1.

(S3)返信を受けたエージェントAG1は受け取った結果から、自身のエージェントAG1とエージェントAG2〜AG4に対するタスクの割り振りおよび出力を決定し、それを通知する。   (S3) The agent AG1 that has received the reply determines task allocation and output for its own agent AG1 and agents AG2 to AG4 from the received result, and notifies it.

(S4)自身のエージェントAG1および通知を受け取ったエージェントAG2〜AG4はタスクに従い、制御対象設備に出力指令を送る。   (S4) The agents AG1 to AG4 that have received the agent AG1 and the notification send an output command to the controlled equipment according to the task.

特開2009−100550号公報JP 2009-1000055 A

特許文献1のように、マルチエージェントシステムを用いた自律分散方式により分散電源系統の電熱需給制御を行う際、発電により発生する熱の割り当ても含めての設備の出力制御を行う必要がある。   As in Patent Document 1, when electric power supply and demand control of a distributed power supply system is performed by an autonomous distributed method using a multi-agent system, it is necessary to perform output control of equipment including allocation of heat generated by power generation.

例として、図8のような分散電源系統を考える。同図において、発電機G1はコージェネのような電力と熱を発生する設備、発電機G2は電力のみを発生するモノジェネ発電機を意味しており、発電機G1、発電機G2、商用電源ACおよび電力負荷EL1は互いに配電線で接続されている。電力負荷EL1と一体的に設備される熱負荷TL1は発電機G1と熱供給設備になるボイラー設備B1および発電機G1との間で、熱配管で接続されている。また、各設備G1、G2、AC、B1、TL1、EL1の制御装置には自律分散方式にした電熱需給制御アルゴリズムを搭載するエージェントがそれぞれ組み込まれており、それらのエージェントは他のエージェントと需給電熱量配分の協調動作を行い、制御対象設備の電熱需給制御を行う。   As an example, consider a distributed power supply system as shown in FIG. In the figure, a generator G1 means a facility that generates electric power and heat such as cogeneration, and a generator G2 means a monogenerator that generates only electric power. The generator G1, the generator G2, the commercial power supply AC, The power loads EL1 are connected to each other via a distribution line. A heat load TL1 provided integrally with the electric power load EL1 is connected by thermal piping between the generator G1 and the boiler equipment B1 and the generator G1 that serve as heat supply equipment. Each of the equipment G1, G2, AC, B1, TL1, and EL1 has a controller that incorporates an electric heat supply and demand control algorithm in an autonomous decentralized manner, and these agents communicate with other agents. Performs coordinated operation of quantity distribution and performs electric heat supply and demand control of the controlled equipment.

図8のような系統において、通常、電力負荷に関してはすべての発電機などの電力源からの電力を融通できる。しかし、発電の際に発生する熱においては輸送による熱エネルギーの損失が大きいため、熱の輸送は供給対象が近いところに限定されることがある。そのため、熱需給制御にはコージェネやボイラー設備などの熱エネルギー供給が可能な設備から熱負荷までの経路を考慮した電熱需給制御を行う必要がある。   In the system as shown in FIG. 8, normally, power from all power sources such as generators can be accommodated for the power load. However, since heat generated during power generation has a large loss of heat energy due to transportation, heat transportation may be limited to places close to the supply target. For this reason, it is necessary to perform electric power supply and demand control in consideration of a route from a facility capable of supplying thermal energy such as cogeneration and boiler equipment to a heat load.

熱の輸送経路を考慮した電熱需給制御を行うために、最も簡単に解決する方法としては各エージェントにすべての熱経路情報を静的に設定・記憶しておき、その情報を参照することで熱融通を行うことができる設備を用意する。   In order to perform electric power supply and demand control considering the heat transport route, the easiest solution is to set and store all the heat route information statically in each agent and refer to that information for heat transfer. Provide facilities that can be accommodated.

しかし、上記解決方法では、系統設備の配置や増減により各制御装置の熱経路情報を更新・修正する必要がある他に、当該熱経路による熱エネルギー損失によって効率・コスト的に不適切な熱輸送にならないかという検討が必要となり、熱経路変更に柔軟に対応した熱需給制御および適確な熱需給制御が難しくなる。特に、設備の運転状況(発電機設備が発電に際して発生する熱エネルギー量、設備がもつ蓄熱量など)が時々刻々と変化する場合にオンラインによる熱需給制御が難しくなる。   However, in the above solution, it is necessary to update / correct the heat path information of each control device due to the arrangement or increase / decrease of the system equipment, and in addition, heat transfer that is inappropriate in terms of efficiency and cost due to heat energy loss due to the heat path Therefore, it becomes difficult to carry out heat supply and demand control that responds flexibly to changes in the heat path and accurate heat supply and demand control. In particular, on-line heat supply and demand control becomes difficult when the operating status of the equipment (the amount of heat energy generated by the generator equipment, the amount of heat stored in the equipment, etc.) changes from moment to moment.

本発明の目的は、分散電源系統の電熱需給制御において、設備間の熱需給経路による熱エネルギー損失を考慮した適切な熱需給制御ができ、さらに設備の運転状況変化にオンラインで対応できる熱需給制御ができる分散電源系統の電熱需給制御システムおよび電熱需給制御方法を提供することにある。   An object of the present invention is to provide an appropriate heat supply and demand control in consideration of a heat energy loss due to a heat supply and demand route between facilities in an electric heat supply and demand control of a distributed power supply system, and further capable of responding to a change in the operation status of the facility online. An object is to provide an electric heat supply and demand control system and an electric heat supply and demand control method for a distributed power system.

本発明は、前記の課題を解決するため、各エージェントは熱エネルギーを需給できる設備間を接続する熱配管情報およびこれら設備の運転状況の情報を取得し、各設備間の熱需給経路の熱エネルギー損失および設備の運転状況の変化を含めて、当該設備間で電熱需給する価値があるかどうかを判断する指標になるエネルギー価値を求め、このエネルギー価値を基に電熱需給する設備およびその出力を決定するようにしたものであり、以下の電熱需給制御システムおよび電熱需給制御方法を特徴とする。   In order to solve the above-mentioned problems, the present invention obtains information on the heat pipes connecting between facilities capable of supplying and supplying heat energy and information on the operating status of these facilities, and heat energy in the heat supply and demand path between the facilities. The energy value, which is an index for determining whether there is value for supplying and supplying electric heat between the equipment, including losses and changes in the operating status of the equipment, is determined. Based on this energy value, the equipment to supply and supply electric power and its output are determined. The electric heat supply and demand control system and the electric heat supply and demand control method are characterized as follows.

(システムの発明)
(1)電力のみを発生または電力と熱を発生できる電熱供給側設備と、電力のみが供給または電力と熱が供給される電熱負荷側設備との間を配電線および/または熱配管で接続した分散電源系統における各設備間の電熱需給制御に、各設備に設けたエージェント間の情報交換によって各設備の電熱需給出力を決定する分散電源系統の電熱需給制御システムであって、
前記エージェントのうちの1つのエージェントは、他のエージェントとの情報交換によって熱エネルギーを需給できる設備間を接続する熱配管情報およびこれら設備の運転状況の情報を取得し、各設備間の熱需給経路の熱エネルギー損失および設備の運転状況の変化を含めて、当該設備間で電熱需給する価値があるかどうかを判断する指標になるエネルギー価値を求め、このエネルギー価値を基に電熱需給する設備およびその出力を決定する手段を備えたことを特徴とする。
(Invention of the system)
(1) A distribution line and / or a heat pipe connected between an electric heat supply side facility capable of generating only electric power or electric power and heat and an electric heat load side facility supplied only with electric power or supplied with electric power and heat. An electric heat supply and demand control system for a distributed power supply system that determines an electric heat supply and demand output of each facility by exchanging information between agents provided in each facility for electric heat supply and demand control between each facility in the distributed power supply system,
One of the agents obtains heat piping information connecting between facilities capable of supplying and supplying thermal energy by exchanging information with other agents, and information on the operating status of these facilities, and a heat supply and demand route between the facilities. The energy value, which is an index for judging whether there is value for supplying and supplying electric heat between the equipment, including the loss of thermal energy and the change in the operating status of the equipment, and the equipment that supplies and supplies electric heat based on this energy value and its A means for determining an output is provided.

(2)前記1つのエージェントは、
他のエージェントとの情報交換により、各設備での電力経路ごとの電力負荷量を算定、および熱経路ごとの熱負荷量を算定する手段と、
電熱供給側設備が前記電力負荷量の発電に必要なコストを基に、この発電に伴い発生する熱エネルギーも含めて第1のエネルギー価値として算定する手段と、
電熱供給側設備が供給する電力を商用電源で賄ったときの電力価格と、熱を熱供給設備で賄ったときの熱量価格とに換算して第2のエネルギー価値として算定する手段と、
前記第1と第2のエネルギー価値の差を求める手段と、
前記エネルギー価値の差が同程度以上の場合は当該電熱供給側設備のエネルギー価値の差が最も大きい電熱供給側設備を運転し、前記第1のエネルギー価値が第2のエネルギー価値よりも低い場合は当該電熱供給側設備を止める、または運転することなく商用電源と熱供給設備からの電熱供給とする手段と、
前記電力負荷量、熱負荷量から前記電熱供給側設備または商用電源と熱供給設備に割り当てた発電出力またはそれに対する熱出力を差し引いて、残りの電力負荷量および熱負荷量を算出する手段と、
前記残りの電力負荷量がある場合、残りの電力負荷量が無くなるまで、前記エネルギー価値を基にして他の設備を電熱供給設備として割り当てる処理に戻る手段と、
前記エネルギー価値差が低い場合、商用電源から購入した電力出力、および熱供給設備からの熱出力を決定する手段と、
を備えたことを特徴とする。
(2) The one agent is
By exchanging information with other agents, calculating the power load for each power path in each facility, and calculating the heat load for each heat path;
A means for calculating the first energy value including the thermal energy generated by the power generation on the basis of the cost required for the power generation by the electric heat supply side facility;
Means for calculating the second energy value by converting the electricity price supplied by the electric heat supply side facility with a commercial power source and the heat price when the heat is supplied by the heat supply facility;
Means for determining a difference between the first and second energy values;
When the difference in energy value is equal to or greater than that, the electric heat supply side facility having the largest difference in energy value of the electric heat supply side facility is operated, and the first energy value is lower than the second energy value. Means for supplying electric heat from the commercial power source and the heat supply facility without stopping or operating the electric heat supply side facility;
Means for subtracting the power generation output assigned to the electric heat supply side facility or the commercial power source and the heat supply facility or the heat output corresponding thereto from the power load amount and heat load amount, and calculating the remaining power load amount and heat load amount;
Means for returning to the process of allocating other equipment as electric heat supply equipment based on the energy value until there is no remaining power load, if there is the remaining power load;
If the energy value difference is low, means for determining the power output purchased from the commercial power source and the heat output from the heat supply facility;
It is provided with.

(3)前記電熱供給設備がガスタービン発電機の場合、前記第1のエネルギー価値の算定は、
前記電力負荷量に対しての出力可能な量Poutから、ガスタービン発電機の発電効率eを用いて電力を発生するのに必要な購入ガス熱量H(=e*Pout)を求める手段と、
前記購入ガス熱量Hと1立米当たりの熱量Hmから購入ガス体積V(=H/Hm)を求める手段と、
前記購入ガス体積Vと購入ガス単価Uから購入ガス価格Pe(=V*U)を求める手段と、
前記購入ガス価格Peとガスタービン発電機が発電する場合に必要なコストCとを合わせた値をガスタービン発電機のエネルギー価値Ee(=C+Pe)として求める手段と、
を備えたことを特徴とする。
(3) When the electric heat supply facility is a gas turbine generator, the calculation of the first energy value is as follows:
Means for obtaining a purchased gas heat quantity H (= e * Pout) necessary for generating electric power from the amount Pout that can be output with respect to the electric power load amount using the power generation efficiency e of the gas turbine generator;
Means for obtaining a purchase gas volume V (= H / Hm) from the purchase gas heat quantity H and the heat quantity Hm per 1 cubic meter;
Means for obtaining a purchase gas price Pe (= V * U) from the purchase gas volume V and purchase gas unit price U;
Means for obtaining, as the energy value Ee (= C + Pe) of the gas turbine generator, a value obtained by combining the purchased gas price Pe and the cost C required when the gas turbine generator generates electricity;
It is provided with.

(4)前記商用電源および熱供給設備に換算した前記第2のエネルギー価値の算定は、
設備の出力可能な電力量Poutに対して、時間帯によって変化する商用電源の電力単価Upを用いて商用電力価格Pu(=Pout*Up)を求める手段と、
熱負荷に対する割当量Haから、熱供給設備の効率ebを用いて購入ガス熱量Hb(=eb*Ha)を求める手段と、
前記購入ガス熱量Hbと1立米あたりの熱量Hbmから購入ガス体積Vb(=Hb/Hbm)を求める手段と、
前記購入ガス体積Vbと購入ガス単価Uから購入ガス価格Pb(=Vb*U)を求める手段と、
商用電源の電力価格Puと購入ガス価格Pbを足し合わせてエネルギー価値Eb(=Pu+Pb)を求める手段と、
を備えたことを特徴とする。
(4) The calculation of the second energy value converted into the commercial power source and the heat supply facility is as follows:
Means for obtaining a commercial power price Pu (= Pout * Up) using a power unit price Up of a commercial power source that changes with time with respect to a power amount Pout that can be output from the facility;
Means for obtaining the purchased gas heat quantity Hb (= eb * Ha) using the efficiency eb of the heat supply equipment from the assigned quantity Ha for the thermal load;
Means for obtaining a purchased gas volume Vb (= Hb / Hbm) from the purchased gas calorie Hb and the calorie Hbm per 1 cubic meter;
Means for obtaining a purchase gas price Pb (= Vb * U) from the purchase gas volume Vb and the purchase gas unit price U;
Means for obtaining the energy value Eb (= Pu + Pb) by adding the power price Pu of the commercial power supply and the purchase gas price Pb;
It is provided with.

(5)前記電熱供給設備が蓄熱槽を持つ場合の前記熱負荷量の算定は、
現在の熱負荷量H(t)と、現在の蓄熱量S(t)と、現在の時間tと、経過時間t≡から、次式によって換算熱負荷量C(t)を求め、
(5) The calculation of the heat load when the electric heat supply facility has a heat storage tank,
From the current heat load amount H (t), the current heat storage amount S (t), the current time t, and the elapsed time t≡, the converted heat load amount C (t) is obtained by the following equation:

Figure 0005487908
Figure 0005487908

この換算熱負荷量C(t)を前記熱負荷量とする手段を備えたことを特徴とする。   Means for converting the converted heat load C (t) to the heat load is provided.

(6)前記電熱供給設備の起動コストが高い場合の前記コストの算定は、
起動コストIと、予想運転時間T(t)と、経過時間t’後の熱負荷量H(t’)と、定格熱出力Wと、現在の時間tと、経過時間t≡から、次式によって換算した起動コストB(t)を求め、
(6) When the start-up cost of the electric heat supply equipment is high, the calculation of the cost is
From the start-up cost I, the expected operating time T (t), the thermal load H (t ′) after the elapsed time t ′, the rated heat output W, the current time t, and the elapsed time t≡ The starting cost B (t) converted by

Figure 0005487908
Figure 0005487908

この起動コストB(t)を前記コストに含める手段を備えたことを特徴とする。   A means for including the activation cost B (t) in the cost is provided.

(方法の発明)
(7)電力のみを発生または電力と熱を発生できる電熱供給側設備と、電力のみが供給または電力と熱が供給される電熱負荷側設備との間を配電線および/または熱配管で接続した分散電源系統における各設備間の電熱需給制御に、各設備に設けたエージェント間の情報交換によって各設備の電熱需給出力を決定する分散電源系統の電熱需給制御方法であって、
前記エージェントのうちの1つのエージェントは、他のエージェントとの情報交換によって熱エネルギーを需給できる設備間を接続する熱配管情報およびこれら設備の運転状況の情報を取得し、各設備間の熱需給経路の熱エネルギー損失および設備の運転状況の変化を含めて、当該設備間で電熱需給する価値があるかどうかを判断する指標になるエネルギー価値を求め、このエネルギー価値を基に電熱需給する設備およびその出力を決定することを特徴とする。
(Invention of method)
(7) A distribution line and / or a heat pipe connected between an electric heat supply side facility that can generate only electric power or electric power and heat, and an electric heat load side facility that is supplied only with electric power or supplied with electric power and heat An electric heat supply and demand control method for a distributed power supply system that determines an electric heat supply and demand output of each facility by exchanging information between agents provided in each facility for electric heat supply and demand control between each facility in a distributed power supply system,
One of the agents obtains heat piping information connecting between facilities capable of supplying and supplying thermal energy by exchanging information with other agents, and information on the operating status of these facilities, and a heat supply and demand route between the facilities. The energy value, which is an index for judging whether there is value for supplying and supplying electric heat between the equipment, including the loss of thermal energy and the change in the operating status of the equipment, and the equipment that supplies and supplies electric heat based on this energy value and its The output is determined.

(8)前記1つのエージェントは、
他のエージェントとの情報交換により、各設備での電力経路ごとの電力負荷量を算定、および熱経路ごとの熱負荷量を算定するステップと、
電熱供給側設備が前記電力負荷量の発電に必要なコストを基に、この発電に伴い発生する熱エネルギーも含めて第1のエネルギー価値として算定するステップと、
電熱供給側設備が供給する電力を商用電源で賄ったときの電力価格と、熱を熱供給設備で賄ったときの熱量価格とに換算して第2のエネルギー価値として算定するステップと、
前記第1と第2のエネルギー価値の差を求めるステップと、
前記エネルギー価値の差が同程度以上の場合は当該電熱供給側設備のエネルギー価値の差が最も大きい電熱供給側設備を運転し、前記第1のエネルギー価値が第2のエネルギー価値よりも低い場合は当該電熱供給側設備を止める、または運転することなく商用電源と熱供給設備からの電熱供給とするステップと、
前記電力負荷量、熱負荷量から前記電熱供給側設備または商用電源と熱供給設備に割り当てた発電出力またはそれに対する熱出力を差し引いて、残りの電力負荷量および熱負荷量を算出するステップと、
前記残りの電力負荷量がある場合、残りの電力負荷量が無くなるまで、前記エネルギー価値を基にして他の設備を電熱供給設備として割り当てる処理に戻るステップと、
前記エネルギー価値差が低い場合、商用電源から購入した電力出力、および熱供給設備からの熱出力を決定するステップと、
を有することを特徴とする。
(8) The one agent is
Calculating the amount of power load for each power path in each facility by exchanging information with other agents, and calculating the amount of heat load for each heat path;
Calculating the first energy value including the thermal energy generated by the power generation based on the cost required for power generation by the electric heat supply side facility;
A step of calculating the second energy value by converting the electric power supplied by the electric heat supply side facility to the power price when commercial power is supplied and the heat price when the heat is supplied from the heat supply facility;
Determining a difference between the first and second energy values;
When the difference in energy value is equal to or greater than that, the electric heat supply side facility having the largest difference in energy value of the electric heat supply side facility is operated, and the first energy value is lower than the second energy value. A step of setting the electric heat supply from the commercial power source and the heat supply facility without stopping or operating the electric heat supply side facility;
Subtracting the power output allocated to the electric heat supply side facility or the commercial power source and the heat supply facility or the heat output corresponding thereto from the power load amount and the heat load amount to calculate the remaining power load amount and the heat load amount; and
If there is the remaining power load, returning to the process of assigning other equipment as electric heat supply equipment based on the energy value until there is no remaining power load;
If the energy value difference is low, determining the power output purchased from the commercial power source and the heat output from the heat supply facility;
It is characterized by having.

(9)前記電熱供給設備がガスタービン発電機の場合、前記第1のエネルギー価値の算定は、
前記電力負荷量に対しての出力可能な量Poutから、ガスタービン発電機の発電効率eを用いて電力を発生するのに必要な購入ガス熱量H(=e*Pout)を求めるステップと、
前記購入ガス熱量Hと1立米当たりの熱量Hmから購入ガス体積V(=H/Hm)を求めるステップと、
前記購入ガス体積Vと購入ガス単価Uから購入ガス価格Pe(=V*U)を求めるステップと、
前記購入ガス価格Peとガスタービン発電機が発電する場合に必要なコストCとを合わせた値をガスタービン発電機のエネルギー価値Ee(=C+Pe)として求めるステップと、
を有することを特徴とする。
(9) When the electric heat supply facility is a gas turbine generator, the calculation of the first energy value is as follows:
Obtaining a purchased gas heat quantity H (= e * Pout) necessary for generating electric power from the power output amount Pout with respect to the power load amount using the power generation efficiency e of the gas turbine generator;
Obtaining a purchased gas volume V (= H / Hm) from the purchased gas calorie H and the calorie Hm per 1 rice;
Obtaining a purchase gas price Pe (= V * U) from the purchase gas volume V and purchase gas unit price U;
Obtaining a value obtained by combining the purchased gas price Pe and a cost C required when the gas turbine generator generates electricity as an energy value Ee (= C + Pe) of the gas turbine generator;
It is characterized by having.

(10)前記商用電源および熱供給設備に換算した前記第2のエネルギー価値の算定は、
設備の出力可能な電力量Poutに対して、時間帯によって変化する商用電源の電力単価Upを用いて商用電力価格Pu(=Pout*Up)を求めるステップと、
熱負荷に対する割当量Haから、熱供給設備の効率ebを用いて購入ガス熱量Hb(=eb*Ha)を求めるステップと、
前記購入ガス熱量Hbと1立米あたりの熱量Hbmから購入ガス体積Vb(=Hb/Hbm)を求めるステップと、
前記購入ガス体積Vbと購入ガス単価Uから購入ガス価格Pb(=Vb*U)を求めるステップと、
商用電源の電力価格Puと購入ガス価格Pbを足し合わせてエネルギー価値Eb(=Pu+Pb)を求めるステップと、
を有することを特徴とする。
(10) The calculation of the second energy value converted into the commercial power source and the heat supply facility is as follows:
A step of obtaining a commercial power price Pu (= Pout * Up) using a power unit price Up of a commercial power source that varies depending on a time zone with respect to a power amount Pout that can be output from the facility;
Obtaining a purchased gas heat quantity Hb (= eb * Ha) using the efficiency eb of the heat supply equipment from the assigned quantity Ha for the thermal load;
Obtaining a purchase gas volume Vb (= Hb / Hbm) from the purchase gas calorie Hb and the calorie Hbm per 1 rice;
Obtaining a purchase gas price Pb (= Vb * U) from the purchase gas volume Vb and purchase gas unit price U;
A step of obtaining an energy value Eb (= Pu + Pb) by adding the power price Pu of the commercial power supply and the purchase gas price Pb;
It is characterized by having.

(11)前記電熱供給設備が蓄熱槽を持つ場合の前記熱負荷量の算定は、
現在の熱負荷量H(t)と、現在の蓄熱量S(t)と、現在の時間tと、経過時間t≡から、次式によって換算熱負荷量C(t)を求め、
(11) Calculation of the heat load when the electric heat supply facility has a heat storage tank,
From the current heat load amount H (t), the current heat storage amount S (t), the current time t, and the elapsed time t≡, the converted heat load amount C (t) is obtained by the following equation:

Figure 0005487908
Figure 0005487908

この換算熱負荷量C(t)を前記熱負荷量とするステップを有することを特徴とする。   The conversion heat load amount C (t) is used as the heat load amount.

(12)前記電熱供給設備の起動コストが高い場合の前記コストの算定は、
起動コストIと、予想運転時間T(t)と、経過時間t’後の熱負荷量H(t’)と、定格熱出力Wと、現在の時間tと、経過時間t≡から、次式によって換算した起動コストB(t)を求め、
(12) When the start-up cost of the electric heat supply equipment is high, the calculation of the cost is as follows:
From the start-up cost I, the expected operating time T (t), the thermal load H (t ′) after the elapsed time t ′, the rated heat output W, the current time t, and the elapsed time t≡ The starting cost B (t) converted by

Figure 0005487908
Figure 0005487908

この起動コストB(t)を前記コストに含めるステップを有することを特徴とする。   It has the step which includes this starting cost B (t) in the said cost.

以上のとおり、本発明によれば、各エージェントは熱エネルギーを需給できる設備間を接続する熱配管情報およびこれら設備の運転状況の情報を有し、各設備間の熱需給経路の熱エネルギー損失および設備の運転状況の変化を含めて、当該設備間で電熱需給する価値があるかどうかを判断する指標になるエネルギー価値を求め、このエネルギー価値を基に電熱需給する設備およびその出力を決定するようにしたため、設備間の熱需給経路による熱エネルギー損失を考慮した適切な熱需給制御ができ、さらに設備の運転状況変化にオンラインで対応できる熱需給制御ができる。   As described above, according to the present invention, each agent has information on heat piping connecting between facilities capable of supplying and supplying thermal energy, and information on the operation status of these facilities, and heat energy loss in the heat supply and demand path between the facilities and To determine the energy value that will be an index for judging whether there is value for electric power supply and demand between the equipment, including changes in the operation status of the equipment, and to determine the equipment to supply and supply electric heat and its output based on this energy value Therefore, appropriate heat supply and demand control can be performed in consideration of heat energy loss through the heat supply and demand path between facilities, and further, heat supply and demand control that can respond online to changes in the operation status of the facility.

本発明の実施形態を示す分散電源系統図。The distributed power supply system diagram which shows embodiment of this invention. エネルギー価値の算出アルゴリズム。Energy value calculation algorithm. 中央集中方式の電熱需給制御システムの構成図。The block diagram of the electric power supply-and-demand control system of a centralized system. 自律分散方式の電熱需給制御システムの構成図。The block diagram of the electric-heat supply-and-demand control system of an autonomous distributed system. 中央集中方式の分散電源系統の制御処理系統図。The control processing system diagram of a centralized distributed power supply system. 自律分散方式の分散電源系統の制御処理系統図。The control processing system diagram of the distributed power supply system of an autonomous distributed system. エージェント同士の情報交換処理例。An example of information exchange processing between agents. 分散電源系統の例。An example of a distributed power system.

(1)電熱需給制御の概要
本発明の実施形態を示す分散電源系統図である。各エージェントは熱エネルギーを需給できる設備間を接続する熱配管情報およびこれら設備の運転状況の情報を取得し、各設備間の熱需給経路の熱エネルギー損失および設備の運転状況の変化を含めて、当該設備間で電熱需給する価値があるかどうかを判断する指標になるエネルギー価値を求め、このエネルギー価値を基に電熱需給する設備およびその出力を決定する点にある。
(1) Outline of Electric Heat Supply / Demand Control FIG. 1 is a distributed power system diagram showing an embodiment of the present invention. Each agent acquires information on the heat pipes connecting equipment that can supply and demand thermal energy and information on the operating status of these equipment, including heat energy loss in the heat supply and demand route between each equipment and changes in the operating status of the equipment, An energy value that is an index for determining whether or not there is value for supplying and supplying electric heat between the facilities is obtained, and the facility for supplying and supplying electric heat and its output are determined based on this energy value.

図1に示す分散電源系統では、発電機G1と熱供給設備になるボイラー設備B1が熱供給設備になり、熱負荷TL1が熱需要設備になり、これら設備間に熱配管P1を敷設した電熱需給システムの場合を示す。このシステム構成において、発電機G1とボイラー設備B1および熱負荷TL1の各エージェントには、前処理としてエージェントセットアップ時に熱配管に対する固有のIDを付け、電熱需給設備ごとにどの経路から熱が供給されるのか、どの経路で熱を供給するのかを示す情報を設定する。各エージェントのうち、任意の1つのエージェントは、他のエージェントとの情報交換で上記の熱配管情報を取得し、この情報により熱配管による熱エネルギー損失を求め、このエネルギー損失、さらには各設備の運転状況などから電熱需給のエネルギー価値を求め、このエネルギー価値を基に熱需給する設備およびその熱需給量を求め、他のエージェントに各設備での熱需給制御を指令する。   In the distributed power supply system shown in FIG. 1, the boiler equipment B1 which becomes the generator G1 and the heat supply equipment becomes the heat supply equipment, the heat load TL1 becomes the heat demand equipment, and the electric power supply and demand with the heat pipe P1 laid between these equipments Indicates the system case. In this system configuration, each of the generator G1, the boiler equipment B1, and the thermal load TL1 is given a unique ID for the heat pipe at the time of agent setup as pre-processing, and heat is supplied from which path for each electric heat supply and demand equipment. Or information indicating the route through which heat is supplied. Of each agent, any one agent acquires the above heat piping information by exchanging information with other agents, and uses this information to determine the heat energy loss due to the heat piping. The energy value of electric heat supply and demand is obtained from the operating status, etc., the equipment for supplying and supplying heat and the amount of heat supply and demand are obtained based on this energy value, and the heat supply and demand control at each equipment is commanded to other agents.

例として、図1のような分散電源系統を考えた場合、全体的な処理手順を以下のようにすることで、設備間の熱需給経路による熱エネルギー損失を考慮した適切な熱需給制御ができる。   As an example, when a distributed power supply system as shown in FIG. 1 is considered, appropriate heat supply and demand control can be performed in consideration of heat energy loss due to the heat supply and demand path between facilities by performing the overall processing procedure as follows. .

(S1)各エージェントの代表とする1つの電力負荷EL1のエージェントは、系統の各電熱需給設備にそれぞれ設けたすべてのエージェントに電熱需給制御の開始通知を行う。   (S1) The agent of one power load EL1 as a representative of each agent notifies the start of the electric heat supply and demand control to all agents provided in each electric heat supply and demand facility of the system.

(S2)上記の電熱需給制御の開始通知を受け取った電熱供給側設備になる発電機G1,G2、商用電源AC、ボイラー設備B1および熱負荷設備TL1の各エージェントは自設備の運転状況(出力情報など)や熱経路情報などの需給制御に必要な情報を電力負荷EL1のエージェントに返す。   (S2) The agents of the generators G1 and G2, the commercial power supply AC, the boiler facility B1, and the heat load facility TL1, which are the facilities for supplying electric heat that have received the notification of the start of the electric power supply and demand control, operate their own facilities (output information) Etc.) and information necessary for supply and demand control such as heat path information are returned to the agent of the power load EL1.

(S3)電力負荷EL1のエージェントは、返された情報を基に、各エージェントの制御対象設備の出力決定アルゴリズム(後に説明する)により設備運転の可否や出力を決定する。   (S3) Based on the returned information, the agent of the power load EL1 determines the availability of the facility operation and the output by the output determination algorithm (described later) of the control target facility of each agent.

(S4)電力負荷EL1のエージェントは、処理(S3)の結果を各エージェントに返信する。   (S4) The agent of the power load EL1 returns the result of the process (S3) to each agent.

(S5)処理結果を受け取った各エージェントは、それが属する各電熱需給設備の出力の指令に従い、電熱需給制御を実行する。   (S5) Each agent that receives the processing result executes electric heat supply and demand control in accordance with an output command of each electric heat supply and demand facility to which the agent belongs.

(2)電熱需給設備の出力決定アルゴリズム
前記の電熱需給制御の概要で記述したように、コージェネやモノジェネ発電機で系統が構成される場合、各設備の出力を算定する際、本実施形態における各エージェントは以下のようなアルゴリズムを用いる。このアルゴリズムは各電熱需給設備のエネルギー価値を算定し、このエネルギー価値を基に当該設備の運転の可否や出力を決定する。
(2) Output decision algorithm of electric heat supply and demand equipment As described in the outline of the electric heat supply and demand control, when a system is configured with a cogeneration system or a monogeneration generator, each output in this embodiment is calculated when calculating the output of each equipment. The agent uses the following algorithm. This algorithm calculates the energy value of each electric heat supply and demand facility, and determines the availability and output of the facility based on this energy value.

具体的な流れは図2にエネルギー価値の算出アルゴリズムを示すように、以下の手順とする。   The specific flow is as follows, as shown in FIG.

(S11)電力負荷量および熱負荷量を算定する。この処理は、前記の処理(S2)で電熱供給側設備から返された情報から各設備から電熱負荷側設備に供給される電力および熱の経路ごとの負荷量を算定する。   (S11) The power load and the heat load are calculated. In this process, the load amount for each path of power and heat supplied from each facility to the electrical heating load side facility is calculated from the information returned from the electrical heat supply side facility in the process (S2).

(S12)設備ごとのエネルギー価値を算定する。この処理は、上記処理(S11)で算出された電力負荷量を当該設備が発電する場合に必要なコストを基にエネルギー価値として算定する。ただし、電力と熱の両方を供給できる設備については、それが発電の際に発生する熱量はすべて熱負荷で消費されるとは限らず、熱負荷が満足された場合は廃棄されるが、ここでのエネルギー価値は廃棄される熱エネルギーも含めて算定されることを意味する。   (S12) The energy value for each facility is calculated. In this process, the amount of power load calculated in the above process (S11) is calculated as an energy value based on the cost required when the facility generates power. However, for equipment that can supply both electric power and heat, the amount of heat generated during power generation is not always consumed by the heat load, but is discarded if the heat load is satisfied. It means that the energy value in is calculated including the waste heat energy.

例えば、設備がガスタービン発電機の場合のエネルギー価値の算定は以下のようにして求める。   For example, the calculation of the energy value when the equipment is a gas turbine generator is obtained as follows.

(step1)電力負荷量に対しての出力可能な量Poutから、ガスタービン発電機の発電効率eを用いて電力を発生するのに必要な購入ガス熱量Hを求める。   (Step 1) From the amount Pout that can be output with respect to the amount of power load, the purchased gas heat amount H required to generate electric power is determined using the power generation efficiency e of the gas turbine generator.

H=e*Pout …(1)
(step2)上記の(step1)の結果から1立米当たりの熱量Hmを用いて、購入ガス体積Vを求める。
H = e * Pout (1)
(Step 2) The purchased gas volume V is obtained from the result of the above (step 1) using the amount of heat Hm per square meter.

V=H/Hm …(2)
(step3)購入ガス単価Uから購入ガス価格Peを求める。
V = H / Hm (2)
(Step 3) The purchase gas price Pe is obtained from the purchase gas unit price U.

Pe=V*U …(3)
(step4)ガスタービン発電機が発電する場合に必要なコストCと、購入ガス価格Peを合わせた値を設備(ガスタービン発電機)のエネルギー価値Eeとして求める。
Pe = V * U (3)
(Step 4) A value obtained by combining the cost C required when the gas turbine generator generates power and the purchased gas price Pe is obtained as the energy value Ee of the facility (gas turbine generator).

Ee=C+Pe …(4)
(S13)電熱供給側設備が供給する電力を商用電源で賄い、熱をボイラー設備で賄う場合のエネルギー価値を算定する。この処理は、上記処理(S11)で電熱供給側設備に要求された電力負荷量を商用電源で賄ったときの電力価格と、そのときに電熱供給側設備で発生する熱量が熱負荷で有効利用される熱量をボイラー設備で換算したときの熱量価格とを足し合わせ、商用電源とボイラー設備で賄った場合に換算したコストをエネルギー価値として求める。
Ee = C + Pe (4)
(S13) The energy value in the case where the electric power supplied from the electric heat supply side facility is supplied by the commercial power supply and the heat is supplied from the boiler facility is calculated. In this processing, the power price when the power load required for the electric heat supply side equipment in the above processing (S11) is covered by the commercial power supply and the amount of heat generated at the electric heat supply side equipment at that time are effectively used for the heat load. The energy value is calculated as the energy value when the amount of heat generated is added to the price of heat when converted by the boiler equipment and covered by the commercial power supply and the boiler equipment.

この商用電源とボイラー設備換算でのエネルギー価値は以下のようにして求める。   The energy value in terms of commercial power supply and boiler equipment is obtained as follows.

(step11)設備の出力可能な電力量Poutに対して、時間帯によって変化する商用電源の電力単価Upを用いて商用電力価格Puを求める。   (Step 11) The commercial power price Pu is obtained by using the power unit price Up of the commercial power source that changes depending on the time zone with respect to the power amount Pout that can be output from the facility.

Pu=Pout*Up …(11)
(step12)熱負荷に対する割当量Haから、ボイラー設備の効率ebを用いて購入ガス熱量Hbを求める。
Pu = Pout * Up (11)
(Step 12) The purchased gas heat quantity Hb is obtained from the assigned quantity Ha for the thermal load using the efficiency eb of the boiler facility.

Hb=eb*Ha …(12)
(step13)上記の(step12)の結果から1立米あたりの熱量Hbmを用いて購入ガス体積Vbを求める。
Hb = eb * Ha (12)
(Step 13) The purchased gas volume Vb is obtained from the result of the above (step 12) using the amount of heat Hbm per 1 cubic meter.

Vb=Hb/Hbm …(13)
(step14)購入ガス体積Vbと購入ガス単価Uから購入ガス価格Pbを求める。
Vb = Hb / Hbm (13)
(Step 14) The purchase gas price Pb is obtained from the purchase gas volume Vb and the purchase gas unit price U.

Pb=Vb*U …(14)
(step15)商用電源の電力価格Puと購入ガス価格Pbを足し合わせてエネルギー価値Ebを求める。
Pb = Vb * U (14)
(Step 15) The energy value Eb is obtained by adding the power price Pu of the commercial power source and the purchase gas price Pb.

Eb=Pu+Pb …(15)
(S14)エネルギー価値の差を求める。この処理は、処理(S12)、(S13)で求めた各電熱供給側設備のエネルギー価値の差を求める。
Eb = Pu + Pb (15)
(S14) The difference in energy value is obtained. This process calculates | requires the difference of the energy value of each electric-heat supply side installation calculated | required by process (S12) and (S13).

(S15)エネルギー価値の差を比較する。この処理は、経済性を重視した系統の運用であれば、当該設備のエネルギー価値差が同程度以上の場合、すなわち要求される負荷電力量を発電機G1やG2で単独運転または並列運転で賄う場合のコストが商用電源とボイラー設備で賄う場合のコストと同程度以上となるとき、発電機G1等で発電の際に発生する熱を捨てることがあったとしても発電機G1を運転する方が価値があることを意味する。逆の場合は設備(発電機G1など)を止める、または運転することなく商用電源とボイラー設備で賄った方が有効であるとして商用電源とボイラー設備からの電熱供給とする。   (S15) The difference in energy value is compared. If this process is an operation of a system with an emphasis on economy, if the difference in energy value between the facilities is about the same or higher, that is, the required load power is covered by the generators G1 and G2 by single operation or parallel operation. When the cost of the case is about the same as or more than the cost of supplying commercial power and boiler equipment, it is better to operate the generator G1 even if the heat generated by the generator G1 or the like is discarded. Means worth it. In the opposite case, it is assumed that it is more effective to supply the commercial power supply and the boiler equipment without stopping or operating the equipment (generator G1 or the like), and the electric power is supplied from the commercial power supply and the boiler equipment.

(S16)エネルギー価値差が最も大きい設備に発電出力を割り当てる。この処理は、処理(S15)の処理によりエネルギー価値が高い設備が二つ以上存在した場合にエネルギー価値が最も高い設備に発電出力を割り当て、この発電出力に伴う熱出力を熱負荷に割り当てる。   (S16) The power generation output is assigned to the equipment having the largest energy value difference. In this process, when there are two or more facilities having a high energy value by the process (S15), the power generation output is allocated to the facility having the highest energy value, and the heat output associated with the power generation output is allocated to the heat load.

(S17)残りの電力および熱負荷量を算出する。この処理は、次回以降、運転させる設備を決定するために処理(S16)で割り当てた発電出力、またそれに対する熱出力を電力負荷量、熱負荷量から差し引く。   (S17) The remaining power and heat load are calculated. In this process, the power generation output assigned in the process (S16) and the heat output corresponding thereto are subtracted from the power load amount and the heat load amount in order to determine the equipment to be operated from the next time.

(S18)電力負荷量の有無を判定する。この処理は、電熱供給側設備により電熱供給出力を差し引いても、要求される電力負荷量が残っているか否かを判定し、残っている場合には処理(S11)に戻って残りの電力負荷量が無くなるまで、エネルギー価値を基にして他の設備を電熱供給設備として割り当てる処理を繰り返す。   (S18) The presence or absence of the power load is determined. In this process, even if the electric heat supply output is subtracted by the electric heat supply side equipment, it is determined whether or not the required power load amount remains, and if it remains, the process returns to the process (S11) to return the remaining electric power load. Until the amount runs out, the process of allocating other equipment as electric heat supply equipment based on the energy value is repeated.

なお、残りの電力負荷量が無い場合はこれ以上、設備を運転することが必要ないと判断し、残りの電力負荷量はボイラー設備で賄う。これは、電力と熱を同時発生する発電機を用いて電主熱従運転を行うため、残りの電力負荷量がなし、かつ、熱負荷が余った場合は発電機を稼働させることができないため、ボイラー設備でカバーすることとする。   If there is no remaining power load, it is determined that it is no longer necessary to operate the equipment, and the remaining power load is covered by the boiler equipment. This is because the main heat follower operation is performed using a generator that generates power and heat at the same time, so there is no remaining power load and the generator cannot be operated if there is a surplus heat load. It will be covered with boiler equipment.

(S19)上記の処理(S15)の判定で、エネルギー価値差が低い場合、商用電源から購入した電力出力、およびボイラー設備からの熱出力を決定する。この処理は、残りの電力・熱負荷量を補うため、運転させる設備が存在しない場合、または、電力負荷を満足した場合、算出する。   (S19) If the energy value difference is low in the determination of the above process (S15), the power output purchased from the commercial power supply and the heat output from the boiler facility are determined. In order to compensate for the remaining power / heat load, this process is calculated when there is no equipment to be operated or when the power load is satisfied.

(3A)電熱供給設備が蓄熱槽を持つ場合の熱負荷量の算定
蓄熱槽を持ち排熱を一時的に蓄えることができる設備(例えば、蓄熱槽が付属される燃料電池発電システム)が分散電源系統に存在し、蓄熱槽の蓄熱を利用して経済性運転を行うとき、前期のように、コージェネやモノジェネ発電機で上記アルゴリズムに従って電熱需給制御を行う処理を毎回繰り返すと、蓄熱槽の蓄熱状況を考慮せずに発電することになり、蓄熱槽が蓄熱する熱エネルギーを有効利用できなくなる。
(3A) Calculation of heat load when the electric heat supply facility has a heat storage tank A facility that has a heat storage tank and can temporarily store exhaust heat (for example, a fuel cell power generation system with a heat storage tank) is a distributed power source When the economical operation using the heat storage in the heat storage tank exists in the grid, the heat storage status of the heat storage tank is repeated every time the process of controlling electric power supply and demand according to the above algorithm is repeated with a cogeneration or monogeneration generator as in the previous period Therefore, it is impossible to effectively use the heat energy stored in the heat storage tank.

この問題を解決するために、次式のように換算熱負荷量C(t)を定義する。ただし、次式において、H(t)は現在の熱負荷量、S(t)は現在の蓄熱量、tは現在の時間、t’は経過時間を意味する。   In order to solve this problem, a converted heat load C (t) is defined as in the following equation. In the following equation, H (t) represents the current heat load, S (t) represents the current heat storage amount, t represents the current time, and t ′ represents the elapsed time.

Figure 0005487908
Figure 0005487908

これを各設備の出力決定アルゴリズムの処理(S13)に実装することで、現在の熱負荷量H(t)と過去データなどから推定される将来の熱負荷量H(t’)を考慮した、設備の指令値の算定を行うことで、蓄熱状況を考慮した電熱需給制御ができる
(3B)起動コストが高い設備のコストの算定
起動コストの高い設備についてエネルギー価値を算定する場合には、前記の出力決定アルゴリズムにて選出されない可能性がある。そのため、以下の換算起動コストを設備の運転に必要なコストに含めることで、運転していない設備のエネルギー価値を上げ、運転させる設備の割合を多くする。
By implementing this in the processing (S13) of the output determination algorithm of each facility, the current heat load amount H (t) and the future heat load amount H (t ′) estimated from past data are taken into consideration. By calculating the command value of equipment, it is possible to control the supply and demand of electricity in consideration of the heat storage status. (3B) Calculation of the cost of equipment with a high start-up cost When calculating the energy value of equipment with a high start-up cost, It may not be selected by the output decision algorithm. Therefore, the following conversion start-up costs are included in the costs necessary for the operation of the equipment, thereby increasing the energy value of the equipment that is not in operation and increasing the proportion of the equipment to be operated.

Figure 0005487908
Figure 0005487908

ただし、Iは起動コスト、T(t)は予想運転時間、B(t)は換算した起動コストを意味する。また、予想運転時間T(t)は、経過時間t’後の推定される熱負荷量H(t’)と、定格熱出力Wと、現在の時間tと、経過時間t≡から求める。   However, I means start-up cost, T (t) means expected operation time, and B (t) means converted start-up cost. Further, the expected operation time T (t) is obtained from the estimated thermal load H (t ′) after the elapsed time t ′, the rated heat output W, the current time t, and the elapsed time t≡.

B1 ボイラー設備
G1 発電機(電力と熱を発生する設備)
G2 発電機(電力のみを発生する設備)
AC 交流電源
TL1 熱負荷
EL1 電力負荷
P1 熱配管
B1 boiler equipment G1 generator (equipment that generates electricity and heat)
G2 generator (equipment that generates electricity only)
AC AC power supply TL1 Thermal load EL1 Electric power load P1 Thermal piping

Claims (12)

電力のみを発生または電力と熱を発生できる電熱供給側設備と、電力のみが供給または電力と熱が供給される電熱負荷側設備との間を配電線および/または熱配管で接続した分散電源系統における各設備間の電熱需給制御に、各設備に設けたエージェント間の情報交換によって各設備の電熱需給出力を決定する分散電源系統の電熱需給制御システムであって、
前記エージェントのうちの1つのエージェントは、他のエージェントとの情報交換によって熱エネルギーを需給できる設備間を接続する熱配管情報およびこれら設備の運転状況の情報を取得し、各設備間の熱需給経路の熱エネルギー損失および設備の運転状況の変化を含めて、当該設備間で電熱需給する価値があるかどうかを判断する指標になるエネルギー価値を求め、このエネルギー価値を基に電熱需給する設備およびその出力を決定する手段を備えたことを特徴とする分散電源系統の電熱需給制御システム。
A distributed power supply system that connects power supply side equipment that can generate only power or power and heat, and power supply load side equipment that is supplied only with power or that is supplied with power and heat, using distribution lines and / or heat piping Electric power supply and demand control system of a distributed power system that determines the electric heat supply and demand output of each facility by exchanging information between agents provided in each facility,
One of the agents obtains heat piping information connecting between facilities capable of supplying and supplying thermal energy by exchanging information with other agents, and information on the operating status of these facilities, and a heat supply and demand route between the facilities. The energy value, which is an index for judging whether there is value for supplying and supplying electric heat between the equipment, including the loss of thermal energy and the change in the operating status of the equipment, and the equipment that supplies and supplies electric heat based on this energy value and its An electric heat supply and demand control system for a distributed power system, characterized by comprising means for determining an output.
前記1つのエージェントは、
他のエージェントとの情報交換により、各設備での電力経路ごとの電力負荷量を算定、および熱経路ごとの熱負荷量を算定する手段と、
電熱供給側設備が前記電力負荷量の発電に必要なコストを基に、この発電に伴い発生する熱エネルギーも含めて第1のエネルギー価値として算定する手段と、
電熱供給側設備が供給する電力を商用電源で賄ったときの電力価格と、熱を熱供給設備で賄ったときの熱量価格とに換算して第2のエネルギー価値として算定する手段と、
前記第1と第2のエネルギー価値の差を求める手段と、
前記エネルギー価値の差が同程度以上の場合は当該電熱供給側設備のエネルギー価値の差が最も大きい電熱供給側設備を運転し、前記第1のエネルギー価値が第2のエネルギー価値よりも低い場合は当該電熱供給側設備を止める、または運転することなく商用電源と熱供給設備からの電熱供給とする手段と、
前記電力負荷量、熱負荷量から前記電熱供給側設備または商用電源と熱供給設備に割り当てた発電出力またはそれに対する熱出力を差し引いて、残りの電力負荷量および熱負荷量を算出する手段と、
前記残りの電力負荷量がある場合、残りの電力負荷量が無くなるまで、前記エネルギー価値を基にして他の設備を電熱供給設備として割り当てる処理に戻る手段と、
前記エネルギー価値差が低い場合、商用電源から購入した電力出力、および熱供給設備からの熱出力を決定する手段と、
を備えたことを特徴とする請求項1に記載の分散電源系統の電熱需給制御システム。
The one agent is
By exchanging information with other agents, calculating the power load for each power path in each facility, and calculating the heat load for each heat path;
A means for calculating the first energy value including the thermal energy generated by the power generation on the basis of the cost required for the power generation by the electric heat supply side facility;
Means for calculating the second energy value by converting the electricity price supplied by the electric heat supply side facility with a commercial power source and the heat price when the heat is supplied by the heat supply facility;
Means for determining a difference between the first and second energy values;
When the difference in energy value is equal to or greater than that, the electric heat supply side facility having the largest difference in energy value of the electric heat supply side facility is operated, and the first energy value is lower than the second energy value. Means for supplying electric heat from the commercial power source and the heat supply facility without stopping or operating the electric heat supply side facility;
Means for subtracting the power generation output assigned to the electric heat supply side facility or the commercial power source and the heat supply facility or the heat output corresponding thereto from the power load amount and heat load amount, and calculating the remaining power load amount and heat load amount;
Means for returning to the process of allocating other equipment as electric heat supply equipment based on the energy value until there is no remaining power load, if there is the remaining power load;
If the energy value difference is low, means for determining the power output purchased from the commercial power source and the heat output from the heat supply facility;
The electric heat supply and demand control system for a distributed power supply system according to claim 1, comprising:
前記電熱供給設備がガスタービン発電機の場合、前記第1のエネルギー価値の算定は、
前記電力負荷量に対しての出力可能な量Poutから、ガスタービン発電機の発電効率eを用いて電力を発生するのに必要な購入ガス熱量H(=e*Pout)を求める手段と、
前記購入ガス熱量Hと1立米当たりの熱量Hmから購入ガス体積V(=H/Hm)を求める手段と、
前記購入ガス体積Vと購入ガス単価Uから購入ガス価格Pe(=V*U)を求める手段と、
前記購入ガス価格Peとガスタービン発電機が発電する場合に必要なコストCとを合わせた値をガスタービン発電機のエネルギー価値Ee(=C+Pe)として求める手段と、
を備えたことを特徴とする請求項に記載の分散電源系統の電熱需給制御システム。
When the electric heat supply facility is a gas turbine generator, the calculation of the first energy value is
Means for obtaining a purchased gas heat quantity H (= e * Pout) necessary for generating electric power from the amount Pout that can be output with respect to the electric power load amount using the power generation efficiency e of the gas turbine generator;
Means for obtaining a purchase gas volume V (= H / Hm) from the purchase gas heat quantity H and the heat quantity Hm per 1 cubic meter;
Means for obtaining a purchase gas price Pe (= V * U) from the purchase gas volume V and purchase gas unit price U;
Means for obtaining, as the energy value Ee (= C + Pe) of the gas turbine generator, a value obtained by combining the purchased gas price Pe and the cost C required when the gas turbine generator generates electricity;
The electric power supply and demand control system for a distributed power supply system according to claim 2 , comprising:
前記商用電源および熱供給設備に換算した前記第2のエネルギー価値の算定は、
設備の出力可能な電力量Poutに対して、時間帯によって変化する商用電源の電力単価Upを用いて商用電力価格Pu(=Pout*Up)を求める手段と、
熱負荷に対する割当量Haから、熱供給設備の効率ebを用いて購入ガス熱量Hb(=eb*Ha)を求める手段と、
前記購入ガス熱量Hbと1立米あたりの熱量Hbmから購入ガス体積Vb(=Hb/Hbm)を求める手段と、
前記購入ガス体積Vbと購入ガス単価Uから購入ガス価格Pb(=Vb*U)を求める手段と、
商用電源の電力価格Puと購入ガス価格Pbを足し合わせてエネルギー価値Eb(=Pu+Pb)を求める手段と、
を備えたことを特徴とする請求項2または3に記載の分散電源系統の電熱需給制御システム。
The calculation of the second energy value converted into the commercial power source and the heat supply facility is as follows:
Means for obtaining a commercial power price Pu (= Pout * Up) using a power unit price Up of a commercial power source that changes with time with respect to a power amount Pout that can be output from the facility;
Means for obtaining the purchased gas heat quantity Hb (= eb * Ha) using the efficiency eb of the heat supply equipment from the assigned quantity Ha for the thermal load;
Means for obtaining a purchased gas volume Vb (= Hb / Hbm) from the purchased gas calorie Hb and the calorie Hbm per 1 cubic meter;
Means for obtaining a purchase gas price Pb (= Vb * U) from the purchase gas volume Vb and the purchase gas unit price U;
Means for obtaining the energy value Eb (= Pu + Pb) by adding the power price Pu of the commercial power supply and the purchase gas price Pb;
The electric power supply and demand control system for a distributed power supply system according to claim 2 or 3 , characterized by comprising:
前記電熱供給設備が蓄熱槽を持つ場合の前記熱負荷量の算定は、
現在の熱負荷量H(t)と、現在の蓄熱量S(t)と、現在の時間tと、経過時間t≡から、次式によって換算熱負荷量C(t)を求め、
Figure 0005487908
この換算熱負荷量C(t)を前記熱負荷量とする手段を備えたことを特徴とする請求項1〜4のいずれか1項に記載の分散電源系統の電熱需給制御システム。
Calculation of the heat load when the electric heat supply equipment has a heat storage tank,
From the current heat load amount H (t), the current heat storage amount S (t), the current time t, and the elapsed time t≡, the converted heat load amount C (t) is obtained by the following equation:
Figure 0005487908
The electric power supply and demand control system for a distributed power system according to any one of claims 1 to 4, further comprising means for setting the converted heat load amount C (t) as the heat load amount.
前記電熱供給設備の起動コストが高い場合の前記コストの算定は、
起動コストIと、予想運転時間T(t)と、経過時間t’後の熱負荷量H(t’)と、定格熱出力Wと、現在の時間tと、経過時間t≡から、次式によって換算した起動コストB(t)を求め、
Figure 0005487908
この起動コストB(t)を前記コストに含める手段を備えたことを特徴とする請求項1〜5のいずれか1項に記載の分散電源系統の電熱需給制御システム。
When the startup cost of the electric heat supply equipment is high, the calculation of the cost is
From the start-up cost I, the expected operating time T (t), the thermal load H (t ′) after the elapsed time t ′, the rated heat output W, the current time t, and the elapsed time t≡ The starting cost B (t) converted by
Figure 0005487908
The electric power supply and demand control system for a distributed power supply system according to any one of claims 1 to 5, further comprising means for including the activation cost B (t) in the cost.
電力のみを発生または電力と熱を発生できる電熱供給側設備と、電力のみが供給または電力と熱が供給される電熱負荷側設備との間を配電線および/または熱配管で接続した分散電源系統における各設備間の電熱需給制御に、各設備に設けたエージェント間の情報交換によって各設備の電熱需給出力を決定する分散電源系統の電熱需給制御方法であって、
前記エージェントのうちの1つのエージェントは、他のエージェントとの情報交換によって熱エネルギーを需給できる設備間を接続する熱配管情報およびこれら設備の運転状況の情報を取得し、各設備間の熱需給経路の熱エネルギー損失および設備の運転状況の変化を含めて、当該設備間で電熱需給する価値があるかどうかを判断する指標になるエネルギー価値を求め、このエネルギー価値を基に電熱需給する設備およびその出力を決定することを特徴とする分散電源系統の電熱需給制御方法。
A distributed power supply system that connects power supply side equipment that can generate only power or power and heat, and power supply load side equipment that is supplied only with power or that is supplied with power and heat, using distribution lines and / or heat piping In the electric power supply and demand control method of the distributed power supply system for determining the electric heat supply and demand output of each facility by exchanging information between agents provided in each facility,
One of the agents obtains heat piping information connecting between facilities capable of supplying and supplying thermal energy by exchanging information with other agents, and information on the operating status of these facilities, and a heat supply and demand route between the facilities. The energy value, which is an index for judging whether there is value for supplying and supplying electric heat between the equipment, including the loss of thermal energy and the change in the operating status of the equipment, and the equipment that supplies and supplies electric heat based on this energy value and its An electric heat supply and demand control method for a distributed power supply system, characterized in that an output is determined.
前記1つのエージェントは、
他のエージェントとの情報交換により、各設備での電力経路ごとの電力負荷量を算定、および熱経路ごとの熱負荷量を算定するステップと、
電熱供給側設備が前記電力負荷量の発電に必要なコストを基に、この発電に伴い発生する熱エネルギーも含めて第1のエネルギー価値として算定するステップと、
電熱供給側設備が供給する電力を商用電源で賄ったときの電力価格と、熱を熱供給設備で賄ったときの熱量価格とに換算して第2のエネルギー価値として算定するステップと、
前記第1と第2のエネルギー価値の差を求めるステップと、
前記エネルギー価値の差が同程度以上の場合は当該電熱供給側設備のエネルギー価値の差が最も大きい電熱供給側設備を運転し、前記第1のエネルギー価値が第2のエネルギー価値よりも低い場合は当該電熱供給側設備を止める、または運転することなく商用電源と熱供給設備からの電熱供給とするステップと、
前記電力負荷量、熱負荷量から前記電熱供給側設備または商用電源と熱供給設備に割り当てた発電出力またはそれに対する熱出力を差し引いて、残りの電力負荷量および熱負荷量を算出するステップと、
前記残りの電力負荷量がある場合、残りの電力負荷量が無くなるまで、前記エネルギー価値を基にして他の設備を電熱供給設備として割り当てる処理に戻るステップと、
前記エネルギー価値差が低い場合、商用電源から購入した電力出力、および熱供給設備からの熱出力を決定するステップと、
を有することを特徴とする請求項7に記載の分散電源系統の電熱需給制御方法。
The one agent is
Calculating the amount of power load for each power path in each facility by exchanging information with other agents, and calculating the amount of heat load for each heat path;
Calculating the first energy value including the thermal energy generated by the power generation based on the cost required for power generation by the electric heat supply side facility;
A step of calculating the second energy value by converting the electric power supplied by the electric heat supply side facility to the power price when commercial power is supplied and the heat price when the heat is supplied from the heat supply facility;
Determining a difference between the first and second energy values;
When the difference in energy value is equal to or greater than that, the electric heat supply side facility having the largest difference in energy value of the electric heat supply side facility is operated, and the first energy value is lower than the second energy value. A step of setting the electric heat supply from the commercial power source and the heat supply facility without stopping or operating the electric heat supply side facility;
Subtracting the power output allocated to the electric heat supply side facility or the commercial power source and the heat supply facility or the heat output corresponding thereto from the power load amount and the heat load amount to calculate the remaining power load amount and the heat load amount; and
If there is the remaining power load, returning to the process of assigning other equipment as electric heat supply equipment based on the energy value until there is no remaining power load;
If the energy value difference is low, determining the power output purchased from the commercial power source and the heat output from the heat supply facility;
The electric heat supply and demand control method for a distributed power supply system according to claim 7, wherein:
前記電熱供給設備がガスタービン発電機の場合、前記第1のエネルギー価値の算定は、
前記電力負荷量に対しての出力可能な量Poutから、ガスタービン発電機の発電効率eを用いて電力を発生するのに必要な購入ガス熱量H(=e*Pout)を求めるステップと、
前記購入ガス熱量Hと1立米当たりの熱量Hmから購入ガス体積V(=H/Hm)を求めるステップと、
前記購入ガス体積Vと購入ガス単価Uから購入ガス価格Pe(=V*U)を求めるステップと、
前記購入ガス価格Peとガスタービン発電機が発電する場合に必要なコストCとを合わせた値をガスタービン発電機のエネルギー価値Ee(=C+Pe)として求めるステップと、
を有することを特徴とする請求項に記載の分散電源系統の電熱需給制御方法。
When the electric heat supply facility is a gas turbine generator, the calculation of the first energy value is
Obtaining a purchased gas heat quantity H (= e * Pout) necessary for generating electric power from the power output amount Pout with respect to the power load amount using the power generation efficiency e of the gas turbine generator;
Obtaining a purchased gas volume V (= H / Hm) from the purchased gas calorie H and the calorie Hm per 1 rice;
Obtaining a purchase gas price Pe (= V * U) from the purchase gas volume V and purchase gas unit price U;
Obtaining a value obtained by combining the purchased gas price Pe and a cost C required when the gas turbine generator generates electricity as an energy value Ee (= C + Pe) of the gas turbine generator;
The electric power supply and demand control method for a distributed power supply system according to claim 8 , wherein:
前記商用電源および熱供給設備に換算した前記第2のエネルギー価値の算定は、
設備の出力可能な電力量Poutに対して、時間帯によって変化する商用電源の電力単価Upを用いて商用電力価格Pu(=Pout*Up)を求めるステップと、
熱負荷に対する割当量Haから、熱供給設備の効率ebを用いて購入ガス熱量Hb(=eb*Ha)を求めるステップと、
前記購入ガス熱量Hbと1立米あたりの熱量Hbmから購入ガス体積Vb(=Hb/Hbm)を求めるステップと、
前記購入ガス体積Vbと購入ガス単価Uから購入ガス価格Pb(=Vb*U)を求めるステップと、
商用電源の電力価格Puと購入ガス価格Pbを足し合わせてエネルギー価値Eb(=Pu+Pb)を求めるステップと、
を有することを特徴とする請求項8または9に記載の分散電源系統の電熱需給制御方法。
The calculation of the second energy value converted into the commercial power source and the heat supply facility is as follows:
A step of obtaining a commercial power price Pu (= Pout * Up) using a power unit price Up of a commercial power source that varies depending on a time zone with respect to a power amount Pout that can be output from the facility;
Obtaining a purchased gas heat quantity Hb (= eb * Ha) using the efficiency eb of the heat supply equipment from the assigned quantity Ha for the thermal load;
Obtaining a purchase gas volume Vb (= Hb / Hbm) from the purchase gas calorie Hb and the calorie Hbm per 1 rice;
Obtaining a purchase gas price Pb (= Vb * U) from the purchase gas volume Vb and purchase gas unit price U;
A step of obtaining an energy value Eb (= Pu + Pb) by adding the power price Pu of the commercial power supply and the purchase gas price Pb;
10. The electric power supply and demand control method for a distributed power supply system according to claim 8 or 9 , characterized by comprising:
前記電熱供給設備が蓄熱槽を持つ場合の前記熱負荷量の算定は、
現在の熱負荷量H(t)と、現在の蓄熱量S(t)と、現在の時間tと、経過時間t≡から、次式によって換算熱負荷量C(t)を求め、
Figure 0005487908
この換算熱負荷量C(t)を前記熱負荷量とするステップを有することを特徴とする請求項7〜10のいずれか1項に記載の分散電源系統の電熱需給制御方法。
Calculation of the heat load when the electric heat supply equipment has a heat storage tank,
From the current heat load amount H (t), the current heat storage amount S (t), the current time t, and the elapsed time t≡, the converted heat load amount C (t) is obtained by the following equation:
Figure 0005487908
11. The electric power supply and demand control method for a distributed power system according to claim 7, further comprising a step of setting the converted heat load amount C (t) as the heat load amount.
前記電熱供給設備の起動コストが高い場合の前記コストの算定は、
起動コストIと、予想運転時間T(t)と、経過時間t’後の熱負荷量H(t’)と、定格熱出力Wと、現在の時間tと、経過時間t≡から、次式によって換算した起動コストB(t)を求め、
Figure 0005487908
この起動コストB(t)を前記コストに含めるステップを有することを特徴とする請求項7〜11のいずれか1項に記載の分散電源系統の電熱需給制御方法。
When the startup cost of the electric heat supply equipment is high, the calculation of the cost is
From the start-up cost I, the expected operating time T (t), the thermal load H (t ′) after the elapsed time t ′, the rated heat output W, the current time t, and the elapsed time t≡ The starting cost B (t) converted by
Figure 0005487908
12. The electric power supply and demand control method for a distributed power system according to any one of claims 7 to 11, further comprising a step of including the start-up cost B (t) in the cost.
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