Combined Power and Heat (CHP) refers to the simultaneous production
of electric power and usable high enthalpy steam for industrial
processes and/or heat exchangers for district heating. District
heating is a system for distributing heat usually for residential and
commercial requirements such as heating systems and water heating. A
typical layout consists of centralized heat generation, usually
composed of heat boilers and co-generation plants in parallel, and a
heat-isolated distribution pipeline network. CHP and district heating
is an efficient form of energy production that can produce significant
cost savings and reduce carbon emissions (it is also awarded by low
carbon footprints).
The CHP dispatch problem consists of finding the optimal levels of
electricity output considering heat requirements. It is sometimes
referred to as a multi-objective optimization problem. In the
simulation cost model, heat and power are related by the feasible
region of the CHP generators and fuel costs are minimized. In a
competitive model (i.e. when Market
objects are defined), heat is represented by a simplified linear
approximation and profit maximization becomes the objective function.
The following article describes both models and shows some numerical
examples of the various alternatives.
Fundamentals of CHP modelling:
Two types of CHP generators can be defined:
In the former option, special features of co-generation units can be
defined in detail whereas in the latter a simplified linear model for
waste heat can be supplied to a generic market if prices are
competitive enough. Co-generation plants in district heating (first
option) can be defined as a simplified power-to-heat linear constant
relationship or, a more complex option, as an operating area where the
unit has the ability to deliver both electrical and heat output.
CHP are defined as instances of the Generator
class. A CHP can consist of one co-generation power plant with an
optional auxiliary boiler (often called stand-alone ancillary boiler).
Tri-generation and other modern forms also belong to the CHP class and
can be modelled in the same way as described in the following
sections. Generator are recognized
as CHP type when certain properties are defined.
This is a simplified version of the operational region of the unit.
It is useful when complete operational zone data are not available.
However, reported power-to-heat
ratio efficiencies are easier to find from different vendors and
statistical communities. CHP units can deliver pure electrical (often
referred to as 'condense mode'), power and heat (referred to as 'CHP
mode') and pure heat (usually by its ancillary boiler). Figure 1
illustrates the schematic equivalent of this mode.
In Condense mode, the Fuel
Offtake function is given by:
In Condense mode, the Fuel
Offtake function is given by:
F(cond) = Heat Rate x E(cond)
In CHP mode, the Fuel Offtake function is given by:
F(chp) = CHP Electric Heat Rate Incr × E(chp)
The unit can thus operate in a mixed mode, condense and CHP modes,
like in the following expression:
F = F(cond) + F(chp)
F = Heat Rate × E(cond) + CHP Electric Heat Rate Incr * E(chp)
F = Heat Rate × (E - E(chp)) + CHP Electric Heat Rate Incr * E(chp)
Since:
E(chp)= Power-to-Heat Ratio × H
and:
E = E(cond) + E(chp)
it results:
F = Heat Rate × E + ( CHP Electric Heat Rate Incr - Heat Rate ) ×
Power to Heat Ratio × H
Auxiliary boiler produces heat according to the following expression:
F(aux) = Boiler Heat Rate Incr × I
Notes:
In this model, CHP units are represented by a feasible piecewise representation of the thermal characteristics of the boiler. This is an acceptably accurate representation of many commercial co-generation power plants currently in use. The quadrilateral area in Figure 2 defines the feasible operating region of the CHP units.
Figure 2: Fuel Offtake Domain
The boundaries of the feasible region are defined by:
Usually refers to the electro-mechanical limits of the steam the turbine.
Isothermal limits of the boiler. Not that the Min Stable Level in CHP mode is defined by the minimum fuel input of the unit (i.e. flame stability).
This value is defined by E > Power to Heat Ratio x H
Table 1 lists all properties related to CHP.
Property | Type | Observations |
---|---|---|
Power to Heat Ratio | Key | Defines CHP unit |
CHP Electric Heat Rate Incr | Key | Required for heat production |
Heat Rate Incr | Optional | Efficiency for condense mode |
Boiler Heat Rate Incr | Optional | Ancillary boiler heat production |
CHP Heat Surrogate Heat Rate Incr | Optional | Notional value for heat fuel offtake estimation. This property is only used for CHP Heat Surrogate Fuel Offtake at the solution |
CHP offtake representation can be a non-linear 2nd order polynomial expression. The optimization problem can be solved using QP or MIQP. According to CHP specialized references the fuel offtake function has the following generic non-linear form [1]:
F = ∑_i[c_i (p_i)]+∑_j[c_j (p_i,h_j ) ]+∑_k[c_k (h_k)]
Where ci, ck and cj are the coefficients for Condense mode only units i, CHP units j and pure heat producers k (ancillary boilers), respectively. Note that the term ∑_j[c_j (p_i,h_j ) ] could be any non-linear function of electricity and heat production. In [2], a test system for Combined Heat a Power is developed and analyzed in details. Numerical examples for CHP units have the following form:
F_i = c_(0,i )+c_(1,i ) p_i+c_(2,i ) p_i^2+c_(3,i ) h_i+c_(4,i ) h_i^2+c_(5,i ) p_i h_i
Table 3: Suggested values for the 2nd order polynomial[2]
Coefficient | Unit 1 [247MW] | Unit 2 [125MW] |
---|---|---|
C0 | 2650 | 1250 |
C1 | 14.5 | 36 |
C2 | 0.0345 | 0.0435 |
C3 | 4.2 | 0.6 |
C4 | 0.034 | 0.027 |
C5 | 0.031 | 0.011 |
Currently, the non-linear coefficients C4 and C5 are not supported. The following values are supported:
Table 4: Modelling non-linear CHP functions
Coefficient | Property |
C0 | Heat Rate Base |
C1 | Heat Rate Incr |
C2 | Heat Rate Incr 2 |
C3 | (CHP Electric Heat Rate Incr-Heat Rate Incr) x Power to Heat Ratio |
C4 | - |
C5 | - |
Multi-fuel definition is supported. There is an important limitation
that has to be considered. Since CHP mode efficiency and auxiliary
boiler are defined as Generator
properties, the fuel offtake function has to also be defined as a Generator property. If the heat rate
function (in any of its modalities as explained in the Heat
Rate Modelling article) is defined in the Generator Fuels
collection, they have to be identical across all fuels. If they
differ, a warning will be issued. Fuel Offtake for heat production is:
F = AHR × E + ( CHP
Electric Heat Rate Incr - AHR ) × Power
to Heat Ratio × H
With:
AHR = ∑(Heat Rate) / N
Where N is the number of defined fuels. The user can still create
diversity and scale total cost functions using Transport
Charge and/or Shadow Price.
This model applies to CHP units with defined active Market objects. Waste heat is modelled as a linear proportion of the energy loss, which is defined by the difference between the unit's electrical output energy and the fuel input energy. In order to define this proportion, it is required to define the property Heat Generators Conversion Rate in the respective membership. Figure 4 shows the simplified market model where "HR" is the Generator Heat Rate value and 'k' is the linear proportion of fuel heat input for the external market Conversion Rate. When the user defines Heat Rate in multiple bands, the Conversion Rate must be defined using the same number of bands as Load Point. Generators can participate in more than one Market.
Figure 4: Waste heat market schemeWhen using waste heat market model, CHP key properties are ignored. Fuel 'Isothermal' limits are still considered though. The Fuel Offtake function is defined by the offtake for electricity production, as waste heat is produced only if electricity is also delivered to the node(s). The natural objective function, as with any other market model, is profit maximization. The solution will show the optimal trade-off between electricity and heat production, according to the heat waste market prices.
In this example, a simple CHP generator is defined using the key properties Power to Heat Ratio and CHP Electric Heat Rate Incr. Figure 5 shows the system modelled. The data for the CHP unit is presented in Table 5.
Table 5: Power to Heat Ratio Numerical
Property | Value | Units |
---|---|---|
Max Capacity | 200 | MW |
Min Stable Level | 50 | MW |
Heat Rate | 13 | GJ/MWh |
Heat Load | 50 | GJ |
Power to Heat Ratio | 3.8 | - |
CHP Electric Heat Rate Incr | 15 | GJ/MWh |
Boiler Heat Rate Incr | 1.2 | GJ/GJ |
Max Boiler Heat | 15 | GJ |
In this example, there is a constant heat load of 50 GJ which can be
supplied by the cogeneration of electricity and heat or in combination
with the ancillary boiler (as it is defined by the last two properties
in the table above). The simulator will understand that the generator
has an auxiliary boiler when the property Boiler
Heat Rate Incr is defined. For the electrical system load
demand, the optimal solution solves the decision problem of optimal
electrical dispatch of the CHP unit and its auxiliary boiler in order
to meet the heat load demand. The Fuel
Offtake function (F) of the CHP unit is:
F = 13 × P + (15-13) × (3.8 / 3.6) × H = 13 × P + 2.111 × H
Feasible operating region of the CHP unit is showed in the Figure 6:
The red dot in the figure shows the results of the economical dispatch of CHP. The rationale for the dispatch solution lies in that the CHP unit for electricity production is more expensive than its alternatives CCGT and Hydro units. So the operation of CHP in this case is bounded at its lower electricity production range (50 MW). The high efficiency auxiliary boiler is required at the optimal solution. The heat load demand is then satisfied from 15 GJ (max capacity of ancillary boiler) and 35 GJ from the co-generation plant.
Pricing AnalysisFrom the optimal solution, an increment in the heat load demand will
affect the electrical and heat dispatch of the co-generation plant and
will also affect the other unit's dispatch. The shadow price of the
heat balance constraint (i.e. the dual variable of (2 4)) is 33.77
$/GJ. Since no other constraints would bind in this simple linear
model, an easy exercise can show that an increase of 1 GJ of heat load
would increase the total system cost.
This is:
∂Fo/∂H≈(ΔTotal Cost)/ΔH=(Fo(51GJ)-F(50GJ))/((51-50))
Following the same numerical example, this leads to:
∂Fo/∂H≈19104-19070.22=33.77
The explanation comes from the gradient of the Lagrangian function at
the optimal solution. Assuming μ the Lagrange multipliers and Q the
set of active constraints and assuming in advance that the heat load
constraint is active:
μ=16*2.111=33.777 In practical terms, the heat price 33.77 $/GJ is the competitive price of heat production considering the electrical system and the co-generation capabilities of the power plants.
This case is an extension of the previous example. In this case the CCGT waste heat is assumed to be also connected to the district heating system.
Figure 8: District Heating ProblemIn order to model this feature, the following changes are required:
Table 6: CCGT Power to Heat Ratio Required data
Property | Value | Units |
---|---|---|
Heat Rate | 6 | GJ/MWh |
Power to Heat Ratio | 1 | - |
CHP Electric Heat Rate Incr | 11 | GJ/MWh |
The following Constraint"Compete-Heat"
is required:
Table 7: Compete-Heat Constraint
Collection | Property | Value |
---|---|---|
Compete-Heat | Sense | = |
Compete-Heat | RHS | 50 |
Constraint(Compete-Heat).Generators(cogen) | Heat Production Coefficient | 1 |
Constraint(Compete Heat). Generators(cogen) | Heat Production Coefficient | 1 |
The optimal 'electrical' dispatch is:
Generator | Property | Value | Units |
---|---|---|---|
CCGT | Generation | 200 | MW |
Cogen | Generation | 0 | MW |
Hydro | Generation | 300 | MW |
The co-optimization of heat and power also leads to the following heat dispatch solution:
Generator | Property | Value | Units |
---|---|---|---|
CCGT | Heat Production | 50 | GJ |
Cogen | Heat Production | 0 | GJ |
Even though results may look trivial, the formulation can be extended. Co-optimization is extended to complex transmission-constrained power systems, ancillary requirements, etc. Any number of co-generation plants can be defined for the same district heating system. CHP units or any other co-generation plant may have the option to supply its own 'fixed' heat load and additional waste heat can participate in complex district heating networks.
Suppose that there exists an external heat waste competitive market and cogen plant can offer its waste heat. In this case the dispatch problem of cogen solves the trade-off between generating electricity where it is not competitive and may even have losses compared with a demand response function of the heat market. The solution should maximize the profits considering the revenue from electricity and heat markets. The properties related to the Market "Heat" are shown in Table 8.
Table 8: Market for Heat
Collection | Property | Value | Units |
---|---|---|---|
Generator | Heat Rate | 8.5 | GJ/MWh |
Market Heat Generators | Conversion Rate | 0.29 | GJ/GJ |
In this example the generator has a constant Heat Rate of 8.5 GJ/MWh. This is an equivalent efficiency of 3.6 / 8.5 = 42%. Here, 3.6 is the constant [MWh/GJ] energy conversion value. Thus the gross waste heat is 58%. Assuming that half of this is lost before it can be used in heating the Conversion Rate to usable heat is 0.5 0.58 = 0.29.
CHP plant can be configured with heat storage. In addition, dedicated electric boilers can also be modelled. See the separate article Heat Storage.
1. Guo,T., Henwood, M.I., van Ooijen,M. "An Algorithm for Combined
Heat and Power Economic Dispatch". ''IEEE Transactions on Power
Systems''. Vol. 11 No. 4. November 1996.
2. Algie,C., Wong,K.,P. "A Test System for Combined Heat and Power
Economic Dispatch Problems". ''2004 IEEE International Conference on
Electric Utility Deregulation, Restructuring and Power Technologies''.
(DRPT2004). April 2004. Hong Kong.
3. "Combined Heat and Power (CHP) and Statistics". ''Joint
IEA/Eurostat Annual Questionnaire Training Workshop''. IEA, Paris 29 -
31 October 2001.