HUNGARIAN JOURNAL OF
INDUSTRY AND CHEMISTRY
Vol. 50 pp. 57–65 (2022)
hjic.mk.uni-pannon.hu
DOI: 10.33927/hjic-2022-09

DEVELOPING PLANT MODELS OF REDUCED COMPLEXITY BY CHEMI-
CAL PROCESS ENGINEERING WAY OF THINKING

MÓNIKA VARGA1

1Hungarian University of Agriculture and Life Sciences, Kaposvár Campus, Guba Sándor u. 40, Kaposvár,
7400, HUNGARY

Given the increasing complexity of agricultural systems within the broader context of the bio-based circular economy,
simplified and unified plant models are needed that represent the primary biomass production by solar-driven carbon-
dioxide sequestration. Utilizing experiences from process systems engineering, which was originally inspired by chemical
engineering, a suitable plant model is proposed. The structure of the model is generated from the process net of the
underlying state and transition elements. Two special-state elements are introduced for the short-term storage of the
supplied biomass to be distributed and of the uptake of nutrient-containing water, necessary for evapotranspiration and
photosynthesis. The transition-oriented description of functionalities follows the essential causalities and balances of
natural self-control. Implementation of the model is illustrated by a simple example.

Keywords: plant model, reduced complexity, stoichiometric processes, process network, supply/demand lo-
gistics, natural self-control

1. Introduction

The bio-based circular economy is crucial to secure the
supply of food and materials for mankind given the
burden of depleting non-renewable resources and finite
reservoirs. The replacement of open process systems with
circular ones needs conscious engineering planning and
operations while systemically overviewing the underly-
ing processes. Multisectoral process networks require the
coupling of sub-models from various disciplines on dif-
ferent scales. In the bio-based circular economy, the pho-
tosynthetic biosystems (plants) represent biomass pro-
duction from solar energy, i.e. from the only external,
unlimited energy resource for our planet. Accordingly,
the model-based analysis, planning and operation of cul-
tivated and natural plants plays an important role.

Recently, motivated also by the increasingly inte-
grated engineering of natural and man-made systems, in-
tensive bidirectional learning has commenced between
the computational modeling of natural and man-made
processes whereby:

• the principles of more sustainable and resilient natu-
ral ecosystems can be applied in the design and con-
trol of man-made systems on the one hand, while

Recieved: 26 May 2022; Revised: 7 June 2022; Accepted: 7 June 2022
Correspondence: varga.monika@uni-mate.hu

• the experiences of industrial systems designed by
engineers can be taken into account with regard to
the model-based analysis, planning and operation of
agricultural cultivation on the other.

Although systems of chemical process engineering
played a unique role in this knowledge transfer because
the underlying multidisciplinary processes were complex
enough to represent various features, they were not too
complex for the application of formerly applied com-
putational tools. The lessons learnt from chemical pro-
cess systems are still clearly important in terms of the
rapidly developing model-supported problem-solving of
complex agri-food and agro-environmental process sys-
tems. This paper shows how chemical process engineer-
ing can be used to develop plant (crop) models of limited
complexity.

First, some available plant models will be overviewed
in brief. Two different approaches are available, namely
(i) empirical (statistical) models to calculate various spe-
cific sources of biomass production and (ii) the mecha-
nistic (biophysical) models that describe the underlying
physical, chemical and biological processes, representing
causalities and balances. This overview focuses on the
mechanistic crop models.

Physiological models are important to further our
understanding of metabolism, growth and how plants
respond to environmental conditions, e.g. climate
change [1]. The detailed dynamic modeling of physio-
logical processes is not a novel endeavor, in fact it was

https://doi.org/10.33927/hjic-2022-09
mailto:varga.monika@uni-mate.hu


58 VARGA

already applied at the end of the previous century [2–5].
However, because of the increasing complexity of Water-
Energy-Food-Ecosystems Nexus [6–8], besides detailed
biophysical models, the systemic coupling of these bio-
physical models from various disciplines is also neces-
sary, which also requires flexible models to couple eco-
nomic considerations [9].

Regarding the level of detail, the improved under-
standing of physiological characteristics and the expected
response to environmental changes require mechanistic
models at both the cellular and organ level [10]. How-
ever, their practical applicability, considering the avail-
able data and knowledge, also requires the development
of advanced coupling models.

Various complex crop models are available. In a re-
cent paper, eight kinds of crop models are classified and
compared [11], the most important of which are as fol-
lows:

Agricultural Production Systems sIMulator (APSIM)
is an actively evolving tool for the modeling and simu-
lation of a wide range of agricultural systems, includ-
ing plants, animals and soil, which also takes into con-
sideration management actions and climatic effects [12].
The crop-related parts contain the detailed biophysical
description concerning the phenology, biomass accumu-
lation and distribution of newly synthesized biomass as
well as the uptake of water and components by taking
into account the related limitations and dependencies on
environmental conditions.

STICS is a detailed biophysical modeling tool that
considers water, carbon as well as thermal and radia-
tion energy balances for many (ca. 20) different crops
([13, 14]). It also clearly represents the phenological
stages and the most important biophysical processes, e.g.
light interception, transpiration, uptake of water and nu-
trients, etc.

Cropping Systems Simulation Model [15] is also a
frequently used simulation model that takes into con-
sideration the soil water budget, soil-plant nitrogen bud-
get, crop-canopy and root growth, dry matter produc-
tion, yield, residue production and decomposition as well
as several management options, e.g. cultivar selection,
crop rotation, irrigation, fertilization, tillage operations,
residue management, etc.

Recently, the rediscovery of advantages regarding the
coupling of tree and crop systems by combining their
models has also come to the fore. Both APSIM and
STICS follow this direction. A few validated tree mod-
els are available that are integrated in APSIM to be used
in combination with plants [12]. On the other hand, a
STICS crop model is embedded in the Hi-sAFe agro-
forestry tool [16].

2. Challenges and objective

Plant models for well-defined important crops and trees
are available. These detailed, specific models require a

considerable set of parameters to be identified, more-
over, the increasing design space of the bio-based circular
economy needs simplified, approximate, unified, flexible,
extensible and connectible plant models.

The objective of this paper is to introduce the con-
ceptual framework and experimental implementation of
a unified plant model of reduced complexity. To develop
the model, the following chemical process engineering-
based principles were applied:

• generalized unit operations;
• specific stoichiometric composition of pseudo-

components and other entities;
• stoichiometric conservation processes based on the

model-specific conservation laws, e.g. conservation
of atoms in chemistry; and

• demand-supply chain-like representation of material
flows driven by the underlying push or pull logistics.

3. Materials and methods

3.1 Data and calculation formulae for a typical
example of a plant to be modelled

As an illustrative example of a man-made and operational
plant ecosystem, a cultivated field of maize was modeled,
where 9600 individual plants were cultivated over an area
of 1600 m2. The maize-related specific data were derived
from the literature [17–19].

Within the contours of the outlined system, this cul-
tivated field was associated with the connected layers of
soil and the compartment of air. The environmental con-
ditions were taken into consideration in accordance with
the data from the respective meteorological database.

The initial data of the plants refer to the stage fol-
lowing the sowing of the seeds when the initial biomass
of the plants is contained within the seeds and sprouting
has not yet occurred. The initial conditions of the seed
biomass (based on estimations by experts) and its com-
ponents [20, 21] are the following:

Biomass = 0.0003 kg/plant
C = 0.03747 kmol/kg
H = 0.06999 kmol/kg
O = 0.02846 kmol/kg
N = 0.00154 kmol/kg
P = 0.00011 kmol/kg
X = 0 kmol/kg
H2O = 0.118 kmol/kg
O2 = 0.00066 kmol/kg

Germination is an event-driven process that occurs af-
ter the time-driven sowing. Sowing, which is a manage-
ment process, is modelled by putting the seeds into down-
flow material storage. Afterwards, in the event of the ap-
propriate environmental (meteorological and hydrologi-
cal) conditions, the seeds germinate resulting in the re-
lease of these stored materials in accordance with the fol-
lowing parameters (based on estimations by experts):

Seed biomass = 0.0001 kg/pc

Hungarian Journal of Industry and Chemistry



DEVELOPING PLANT MODELS OF REDUCED COMPLEXITY 59

Seed rate = 6.579 × 10−7 kg/h
Proportion of leaves = 0.853
Proportion of roots = 0.147
Surface area ratio of leaves = 6.667 m2/kg
Surface area ratio of roots = 3.003 m2/kg

In our example model, the germination period is from
April 20th until May 9th.

After the leaves and roots appear, resulting from the
event-driven process of germination, the life processes of
plants, that is, photosynthesis, growth, respiration, evap-
otranspiration and uptake, start.

The rate of photosynthesis is calculated by the follow-
ing simplified equations [19]:

∆BiomassDry =
Num Rad Ft Et

ρ
DT (1)

where
∆BiomassDry = biomass produced, kg,
Num = number of plants, pc.
Rad = radiation, W/mJ2

Ft = proportion of radiation absorbed by the plants
Et = radiation-use efficiency,

kgdry matter/Wabsorbed radiation
ρ = density, number of plants/m2, where

Ft = 1 − e−ktLAIact (2)

LAIact =
LeavesSurf Num

Aact
(3)

Aact = LAIratio LandSurf (4)

ρ =
Num

Aact
(5)

LandSurf = surface area of land, m2

LAIratio = 1 m2 area of leaf / m2 area of land
kt = 0.8 - light extinction coefficient [19]
Et = 0.01409 kg/MJ, radiation-use efficiency [19]

The process of evapotranspiration is calculated from
the reference evapotranspiration (ET0, mm/day), deter-
mined from meteorological data according to the well-
known Penman-Monteith combination equation [22].
Based on this equation, the evaporation from the land and
plants during a time step are calculated separately based
on the following equations:

ETland = Ke ETM LandSurf DT (6)
ETplants = Kcb ETM Surf Num DT (7)

where
ETM = reference evapotranspiration,

recalculated from ET0 / kmol/h
ETland = land-related evapotranspiration, kmol
ETplant = plant-related evapotranspiration, kmol
LandSurf = surface area of the land, m2

Surf = surface area of the leaves, m2

Num = number of plants, pc
Ke = 1 m−2, soil-related part of the dual crop

coefficient [22]
Kcb = 1 m−2, basal plant-related part of the dual crop

coefficient [22]
DT = the time step in hours, distinguished for the

changing actual daylight or night period

Growth is calculated after germination and is inter-
preted as the distribution of the photosynthetic biomass
between the parts of the plants. Before the time- or event-
driven appearance of the product, the following ratios are
applied in line with estimations by experts:

Proportion of leaves = 0.853,
Proportion of roots = 0.147.
Afterwards:
Proportion of leaves = 0.637,
Proportion of products = 0.253,
Proportion of roots = 0.110.

Respiration is calculated for the individual parts of the
plants. For all the parts, two kinds of respiration is sim-
ulated: one as a given proportion of the biomass synthe-
sized and the other as a given proportion of the already
existing biomass. The applied equations are the follow-
ing:

Rleaves = K DMleaves + C Mleaves Num DT (8)
Rprod = K DMprod + C Mprod Num DT (9)
Rroot = K DMroots + C Mroots Num DT (10)

where
Rleaves = respired biomass of leaves, kg
Rprod = respired biomass of product, kg
Rroot = respired biomass of roots, kg
DMleaves = synthesized biomass of leaves, kg
DMprod = synthesized biomass of product, kg
DMroots = synthesized biomass of roots, kg
Mleaves = existing biomass of leaves, kg
Mprod = existing biomass of product, kg
Mroots = existing biomass of roots, kg
K = the constant of 0.1 h−1 [22]
C = the constant of 0.0001 h−1 [22]
Num = number of plants, pc.
DT = the time step in hours, distinguished for the

changing actual daylight or night period

The uptake of water, nitrogen and phosphorus (or of
other optional elements) is calculated as the minimum
amount:

• required for evapotranspiration and photosynthesis
together and

• available in the soil.

50 pp. 57–65 (2022)



60 VARGA

3.2 Non-conventional methodology of Pro-
grammable Process Structures

Programmable Process Structures (PPS, [23–26]) have
developed from its antecedent, that is, Direct Computer
Mapping [27]. PPS offers automatic generation of easily
extensible, connectible and combined dynamic balance-
and rule-based models for the analysis, planning and op-
eration of complex process systems, even beyond indus-
tries that apply CIM (Chemical Integrated Manufactur-
ing). These models consist of unified state and transition
elements, transition-oriented representations of structures
as well as locally programmable functional prototypes.

The main sources of inspiration behind PPS are: 1)
the general functional definition of process systems in
Kalman’s State Space Model [28]; 2) the structural rep-
resentation of General Net Theory [29]; 3) the concept of
communicating autonomous programs in terms of Agent-
Based Modeling [30].

Accordingly, PPS models are derived from two gen-
eral (state and transition) "meta-agents," namely the
structure of the generated state and transition elements
form a net structure, moreover, the locally programmed
state and transition prototypes represent the distributed
functionalities in terms of Kalman’s model. In addition,
PPS can consciously make a distinction between model-
specific conservation laws based on additive measures
and signals.

In fact, PPS models can be generated from two gen-
eral meta-prototypes and from the corresponding descrip-
tion of the process net. The local program containing
prototype elements (that are responsible for the case-
specific calculations), are also derived from the same
meta-prototypes. The simulation can be executed accord-
ing to the connections between the actual state and tran-
sition elements, accompanied by the data transfer be-
tween the actual elements and their calculated prototypes.
This architecture and its AI programming language-based
(SWI-Prolog to be exact) implementation strongly sup-
port the integration of various field- and task-specific
models.

4. Results and discussion

4.1 Chemical process engineering-inspired
principles and hypotheses of plant mod-
els

Natural and cultivated plants, including crops, vegetables,
herbs, grasses and bushes, trees, etc. in a broader context,
cover a wide variety of biological species embedded in
a naturally occurring and partly human-controlled pro-
cess system. Since many different species exist, at first
glance this resembles the early stages of chemical en-
gineering when individual technologies were interpreted
as a system of various case-specific reactors, separators,
etc. The essential invariant elements were later general-
ized according to the concept of unit operations. Simi-
larly, the unified, essential features of agricultural models

can be formulated as “biological engineering unit opera-
tions” within the complex system of the connected agro-
technological, ecological and environmental systems.

Considering the need for unified and simplified bi-
ological, ecological and environmental engineering pro-
cess units, these systems must be represented by the nec-
essary and sufficient types as well as numbers of state and
transition elements calculated by a limited set of gener-
ally usable program prototypes.

The coherent and connectible set of the underlying
‘first principles’-based mechanistic (physical, chemical
and biological) models must be based on causally correct,
model-specific conservation laws-based material and en-
ergy balances. Considering the numerous biochemical
compounds and biological objects, that is, organs, etc.,
synthesized from these compounds, the various typical
biological units can be characterized by their specific sto-
ichiometric composition that facilitates the representation
of balances in accordance with the conservation of atoms
and in line with chemical principles.

Besides the conservation-based balances, the causally
determined (driving force-based) transformations and
transportations are the second pillar of process engineer-
ing models. In this regard, plant-like biological process
units represent a special case because the major driving
force is solar radiation originating from beyond the con-
tours of the system. This feature determines the unique
position of plants in the bio-based circular carbon econ-
omy.

In fact, solar radiation-driven photosynthesis pro-
duces a stoichiometric composition of biomass that sup-
plies biomass in the various state elements of plants
through downflow transporting short-term storage. More-
over, the forces of solar radiation-driven evapotranspi-
ration result in the uptake of water and dissolved nutri-
ents through upflow transporting short-term storage that
supplies the additional resources required for photosyn-
thesis as well as removes the by-products of the energy-
producing respiration.

Accordingly, the essential self-control of plant life is
organized by the solar radiation-driven push logistics of
downflow as well as by the solar radiation-driven pull
logistics of upflow. The daily and seasonal changes in
plant behavior are determined by the temporally changing
environmental functionalities, while human intervention
can be taken into consideration by the respective manage-
rial events.

The hypotheses for the simplified and unified plant
model can be summarized as follows:

• The state elements are described by the specific
biomass (or mass); the stoichiometric amounts of C,
H, O, N, P and optional X atoms; as well as those
originating from H2O, O2 and CO2.

• The transition elements, e.g. photosynthesis,
growth, respiration, evapotranspiration, uptake,
etc., determine the functionalities resulting in stoi-
chiometric changes in the aforementioned sources

Hungarian Journal of Industry and Chemistry

https://www.swi-prolog.org/


DEVELOPING PLANT MODELS OF REDUCED COMPLEXITY 61

of biomass, mass, atoms and components in the
respective state elements.

• The life processes of plants as self-controlled liv-
ing systems can be characterized by (i) the supply
logistics of the photosynthesis-driven utilization of
CO2 from air and H2O, N, P, etc. (from top soil) to
produce O2 which is emitted into the atmosphere in
addition to stoichiometric pools of C, H, O, N and P
that is incorporated into downflow material storage,
as well as by (ii) the demand logistics of the solar
energy-driven evapotranspiration-controlled uptake
of H2O, N and P from the soil and the emission of
CO2 and H2O into the air.

4.2 Structure of the investigated process sys-
tem

The process net structure of the simplified plant model,
embedded in its natural environment and extended with
human managerial interventions, is illustrated in Fig. 1.
In the net model, the dots and bars represent the state and
transition elements, respectively. The state and transition
elements of the simplified plant model are the following:

Plant-related model elements:
• State elements:

– roots (responsible for the water uptake, trans-
portation of dissolved nutrients and long-term
biomass storage that is also capable of gener-
ating useful products);

– leaves (including stems which are responsible
for solar radiation-driven photosynthesis and
evapotranspiration);

– products (which facilitate the storage of
biomass for reproduction that also generates
useful products);

– downflow of material (short-term storage of
photosynthesized biomass to be distributed
amongst the roots, leaves and products);

– upflow of material (short-term storage of up-
taken water and nutrients as well as of respired
components to be distributed between evapo-
transpiration and photosynthesis).

• Transition elements:
– photosynthesis: utilizes solar radiation to syn-

thesize biomass from atmospheric carbon
dioxide, uptaken water and dissolved compo-
nents, e.g. nitrogen, phosphorus, etc.;

– growth: distributes the photosynthesized
biomass between the parts of the plant ac-
cording to the phenological phase-specific
stoichiometry;

– respiration: creates energy to synthesize tis-
sues from already synthesized biomass and in
part maintain existing plant biomass;

– evapotranspiration: which is determined by the
atmospheric conditions, i.e. level of solar en-
ergy, generates the driving force for the uptake

of water and dissolved nutrients from the soil
as well as releases the CO2 and H2O produced
by respiration;

– uptake: supplies the necessary water and dis-
solved nutrients from the soil.

Soil-related model elements:
• State elements:

– residue (only in the topsoil): contains organic
residues, e.g. from leaf littering or the plough-
ing of roots;

– humus (only in the topsoil): transformed or-
ganic biomass in the soil;

– solution containing water and dissolved com-
ponents;

– inorganic solid phase.
• Transition elements:

– transform (only in the topsoil): describes the
production of humus and dissolved nutrients
from the residues;

– air_land (only in the topsoil): calculates the
levels of precipitation and nitrogen fixation
from the atmosphere into the soil as well as
those of evaporation and CO2 emission from
the soil into the atmosphere;

– miner_deminer: determines the degrees of
mineralization and demineralization of dis-
solved components in the soil;

– seepage: calculates the vertical downflow of
water and dissolved components between the
layers of soil.

Human interventions in terms of cultivation:
• Typical state elements: manure, seeds, harvested

products, etc.
• Typical time- and/or event-driven transition ele-

ments: manuring, sowing, harvesting, ploughing,
etc.

Other environmental state elements: the atmosphere
(air), solar radiation-related meteorology, ground layer
below the soil that absorbs water and nutrients.

4.3 Solar radiation-driven “natural supply lo-
gistics” of plant biomass generation

The essential functionalities of the investigated process
system can be represented as solar energy-driven as
well as predominantly self-regulated, natural supply-and-
demand logistics. Moreover, the respective supply-and-
demand processes are causally connected that establish
a natural (basically cooperative) feedback between each
other.

Solar radiation facilitates the synthesis of biomass,
the latter is calculated according to Eqs. 1-5. The related
subprocesses of the plant model are denoted in green lines
in Fig. 1.

The synthesis of biomass is driven by solar radiation
but limited by the available amounts of water, nitrogen
and phosphorus with regard to the upflow material to be

50 pp. 57–65 (2022)



62 VARGA

Figure 1: Process network of the simplified plant model

stored. The rate of photosynthesis also depends on the
surface area of the leaves and stem. Controlled by these
conditions and limitations, the synthesis sequestrates the
calculated amount of the practically unlimited supply of
atmospheric CO2 in the biomass. Simultaneously, pho-
tosynthesis emits O2 into the atmosphere as a result of
the oxidation of uptaken water, while the associated hy-
drogen is incorporated into the synthesized biomass. The
photosynthesized biomass supplies the downflow of ma-
terial to be stored according to the plant-specific atomic
stoichiometry. In the case of the studied maize, the sto-
ichiometry of the synthesized dry matter was as fol-
lows [20, 21]:

[C, H, O, N, P, X] = [0.037, 0.062, 0.029, 0.00087,
4.8 × 10−5, 0]

The dry matter is supplied by an additional amount of
H2O, according to the average water content of the plant
(in our case 0.682).

The synthesized biomass is divided between the
leaves, roots and product state elements of the plant, ac-
cording to the plant-specific ratios that also depend on the
phenological condition of the model. Furthermore, differ-
ent stoichiometries can be used by the various parts of the
plant.

In addition to the increase in the amount of synthe-
sized biomass, a given proportion of that which is stored
in the short term is utilized to meet the energy demand
supplied by respiration for the synthesis of plant biomass
according to Eqs. 8-10.

4.4 Solar energy-driven “natural demand lo-
gistics” of water and nutrient uptake

Considering the “natural demand logistics,” the solar en-
ergy facilitates the uptake of water and dissolved nutri-
ents from the soil as well as of H2O and CO2, the by-
products of respiration. The respective evapotranspiration
is calculated according to the Penman-Monteith combi-
nation equation [22] as well by Eqs. 6-7. The related sub-
processes of the plant model are denoted in red lines in
Fig. 1.

Depending on the meteorological conditions, the H2O
and CO2 content of the uptaken material to be stored is
emitted into the atmosphere by the process of evapotran-
spiration. Simultaneously, the by-products of respiration,
namely H2O and CO2, accumulate here, moreover, the
necessary amounts of H2O as well as of dissolved nitro-
gen and phosphorus are utilized for photosynthesis from
this store. In the knowledge of the resultant actual condi-
tions with regard to the uptaken material to be stored, the
uptake is controlled by demand-determined pull actions
according to the concentration bounds and uptake rules
as follows:

Lower and upper bounds for H2O as well as N and P
atoms are known. The rule that is applied is the following:

if Actual ≤ Lower, then
Demand = min((Upper-Actual), Available),
otherwise Demand = 0, where
Actual = actual amount of uptaken material

to be stored,
Lower = lower bound,

Hungarian Journal of Industry and Chemistry



DEVELOPING PLANT MODELS OF REDUCED COMPLEXITY 63

Upper = upper bound,
Demand = quantity to be uptaken,
Available = available amount in the topsoil.

4.5 Generation and simulation of the PPS
model

The files describing the respective model are found in the
“Plant” directory of a Mendeley database [31].

The process network of the example model is defined
in the text file named Plant_N.pl. The initial conditions
(mass, biomass, components, etc.) and parameters (coef-
ficients of equations, bounds, etc.) are described in the
text file entitled Plant_D.pl, which was derived using an
appropriately configured MS Excel spreadsheet. Starting
from these case-specific files and the general definition of
state and transition meta-prototypes, the general-purpose
kernel program generates the editable graphical model
Plant_G.graphml.

In parallel, by utilizing the meta-prototypes-based
templates, modeling experts have to prepare the local
programs for the respective elements of the prototypes.
The locally executable programs of the prototypes are de-
scribed in the file entitled Plant_G_prot.graphml.

In the knowledge of the prototype elements, the sec-
ond generating algorithm of the PPS kernel prepares the
dynamic databases of the simulation, namely

• Plant_Exp.pl containing the declaration of the Pro-
log clauses describing the local programs; and

• Plant_Use.pl containing the declaration of the Pro-
log facts describing the case-specific elements of the
model along with their initial values and parameters.

The actually selected simulation results are saved in the
file named Plant_Out.csv, while the data can be visual-
ized using a case-specific MS Excel spreadsheet.

Some examples of the simulated results are illustrated
in Figs. 2-5.

Fig. 2 shows the change in the total amount of
biomass produced over one hectare during consecutive
half days in the simulation. Time = 0 indicates when the
land was sowed. Biomass begins to be produced follow-
ing germination and stops at the end of the vegetation
period. Fluctuations in biomass production indicate that
its rate is higher during the daytime compared to at night-
time.

In Fig. 3, water that evaporated from the plant (blue)
and from the land (red) are illustrated. Evaporation from
the land follows the weather conditions much more
closely and dominates during the early stages of the
growing season, particularly when the leaves develop.
Similarly to the production of biomass, evaporation rates
are also higher in this simulation during the daytime.

In Fig. 4, the biomass of the parts of one plant (leaves,
stem, roots, products) can be seen. The leaves, stem and
roots begin to develop at the point of germination, while
products appear later on. Although the leaves, stem and
products are removed at harvest time, the roots are trans-
formed into residues as a result of ploughing. Of course,

Figure 2: Total amount of photosynthesized biomass per
hectare

Figure 3: Dynamic changes in the evaporation rate of H2O
from plants and the surface of the land

Figure 4: Biomass of plant parts throughout the growing
season

the stepwise increase in biomass is insignificant in this
integrated illustration.

Fig. 5 shows the sequestrated CO2 over one hectare
during consecutive half days of the simulation. The neg-
ative values refer to the reduction in its concentration in
the surrounding atmosphere.

5. Conclusion

Although detailed plant models for well-defined impor-
tant crops are available that require hundreds of parame-

50 pp. 57–65 (2022)



64 VARGA

Figure 5: Amount of sequestrated CO2

ters to be identified, the increasing complexity of agricul-
tural systems within the broader context of the bio-based
circular carbon economy requires simplified and unified
plant models, which can describe the primary production
of biomass. The suggested conceptual framework and
its experimental implementation show how the chemical
process engineering principles of process units, stoichio-
metric conservational processes, process networks, driv-
ing force-controlled functionalities and supply/demand
processes can result in a reduced, unified plant model.

The structure of the model can be generated from
the process net of the underlying state and transition ele-
ments. The model contains two special state elements for
the short-term storage of the synthesized biomass to be
distributed amongst the state elements of the plant as well
as for the short-term storage of the uptaken aqueous nutri-
ents required for evapotranspiration and photosynthesis.
These two forms of logistical storage used represent the
roles of phloem and xylem in detailed biophysical mod-
els.

The transition-related dynamic models follow the es-
sential causalities and balances of natural self-control.
Solar radiation-driven photosynthesis produces a stoi-
chiometric composition of biomass that, as a result of the
downflow of products to be stored in the short term, in-
creases the biomass in the various plant elements. More-
over, solar radiation-driven evapotranspiration forces wa-
ter and dissolved nutrients to be uptaken through the up-
flow of products to be stored in the short term, which
increases the amount of water and the additional re-
sources for photosynthesis required, as well as removes
the by-products of energy-producing respiration. The nat-
ural self-control of plant life is organized by the solar
radiation-driven push logistics of downflow as well as by
the solar radiation-driven pull logistics of upflow.

The suggested stoichiometric approach underlines the
increasing importance of elemental analysis with regard
to agriculture-related raw materials and products.

The experimental PPS implementation of a simple ex-
ample model illustrates the possible application of the re-
duced plant model prepared according to the suggested
principles inspired by process systems engineering.

Acknowledgements

This research was partly supported by the 2019-2.1.11-
TÉT-2020-00252 program. The author is especially
grateful to Béla Csukás for his valuable advice.

REFERENCES

[1] Marin, F. R.; Ribeiro, R. V.; Marchiori, P. E. R.: How
can crop modeling and plant physiology help to un-
derstand the plant responses to climate change? A
case study with sugarcane, Theor. Exp. Plant Phys-
iol., 2014, 26, 49–63 DOI: 10.1007/s40626-014-0006-2

[2] Whisler, F.; Acock, B,; Baker, D.; et al: Crop sim-
ulation models in agronomic systems, Adv. Agron.,
1986, 40, 141–208 DOI: 10.1016/S0065-2113(08)60282-5

[3] Penning de Vries, F.; Jansen, D.; Ten Berge, H.;
Bakema, A.: Simulation of ecophysiological pro-
cesses of growth in several annual crops. Wagenin-
gen: Centre for Agricultural Publishing and Docu-
mentation (Pudoc); 1989.

[4] McMaster, G. S.; Morgan, J. A.; Wilhelm, W. W.:
Simulating winter wheat spike development and
growth. Agric. For. Meteorol., 1992, 60, 193–220
DOI: 10.1016/0168-1923(92)90038-6

[5] Salminen, H.; Saarenmaa, H.; Perttunen, J.; Sievä-
nen, R.; Väkevä, J.; Nikinmaa, E.: Modelling
trees using an object-oriented scheme, Math. Com-
put. Model., 1994, 20, 49–64 DOI: 10.1016/0895-
7177(94)90230-5

[6] Garcia, D. J., You, F.: The water-energy-food
nexus and process systems engineering: A new fo-
cus, Comput. Chem. Eng., 2016, 91, 49–67 DOI:
10.1016/j.compchemeng.2016.03.003

[7] Fouladi, J.; AlNouss, A.; Al-Ansari, T.: Sus-
tainable energy-water-food nexus integration
and optimisation in eco-industrial parks, Com-
put. Chem. Eng., 2021, 146, 107229 DOI:
10.1016/j.compchemeng.2021.107229

[8] Yoon, P. R.; Lee, S-H.; Choi, J-Y.; Yoo, S-H.;
Hur, S-O.: Analysis of climate change impact on
resource intensity and carbon emission in pro-
tected farming systems using water-energy-food-
carbon nexus, SSRN Electron. J., 2022, 184, 106394
DOI: 10.2139/ssrn.4054485

[9] Henderson, J. D.; Parajuli, R.; Abt, R. C.: Biologi-
cal and market responses of pine forests in the US
Southeast to carbon fertilization, Ecol. Econ., 2020,
169, 106491 DOI: 10.1016/j.ecolecon.2019.106491

[10] Poorter, H.; Anten, N. P. R.; Marcelis, L. F. M.:
Physiological mechanisms in plant growth models:
Do we need a supra-cellular systems biology ap-
proach? Plant, Cell Environ., 2013, 36, 1673–1690
DOI: 10.1111/pce.12123

[11] Tao, F.; Palosuo, T.; Rötter, R. P.; et al. Why do crop
models diverge substantially in climate impact pro-
jections? A comprehensive analysis based on eight
barley crop models, Agric. For. Meteorol., 2020, 281,
107851 DOI: 10.1016/j.agrformet.2019.107851

Hungarian Journal of Industry and Chemistry

https://doi.org/10.1007/s40626-014-0006-2
https://doi.org/10.1016/S0065-2113(08)60282-5
https://doi.org/10.1016/0168-1923(92)90038-6
https://doi.org/10.1016/0895-7177(94)90230-5
https://doi.org/10.1016/0895-7177(94)90230-5
https://doi.org/10.1016/j.compchemeng.2016.03.003
https://doi.org/10.1016/j.compchemeng.2016.03.003
https://doi.org/10.1016/j.compchemeng.2021.107229
https://doi.org/10.1016/j.compchemeng.2021.107229
https://doi.org/10.2139/ssrn.4054485
https://doi.org/10.1016/j.ecolecon.2019.106491
https://doi.org/10.1111/pce.12123
https://doi.org/10.1016/j.agrformet.2019.107851


DEVELOPING PLANT MODELS OF REDUCED COMPLEXITY 65

[12] Holzworth, D. P.; Huth, N. I.; deVoil, P. G.;
et al. APSIM – Evolution towards a new gen-
eration of agricultural systems simulation, En-
viron. Model. Softw., 2014, 62, 327–350 DOI:
10.1016/J.ENVSOFT.2014.07.009

[13] Brisson, N.; Mary, B.; Ripoche, D.; et al. STICS: A
generic model for the simulation of crops and their
water and nitrogen balances. I. Theory and param-
eterization applied to wheat and corn, Agronomie,
1998, 18, 311–346 DOI: 10.1051/agro:19980501

[14] Brisson, N.; Launay, M.; Mary, B.; Beaudoin, N.
(Eds.): Conceptual basis, formalisations and param-
eterization of the STICS crop model (Éditions Quæ,
Versailles, France) 2009 ISBN: 978-2-7592-0290-4

[15] Stöckle, C. O.; Kemanian, A. R.; Nelson, R. L.;
Adam, J. C.; Sommer, R.; Carlson, B.: CropSyst
model evolution: From field to regional to global
scales and from research to decision support sys-
tems, Environ. Model. Softw., 2014, 62, 361–369 DOI:
10.1016/j.envsoft.2014.09.006

[16] Dupraz, C.; Wolz, K. J.; Lecomte, I.; et al.: Hi-
sAFe: A 3D agroforestry model for integrating dy-
namic tree-crop interactions, Sustain., 2019, 11(8),
2293, DOI: 10.3390/su11082293

[17] Bergez, J. E.; Raynal, H.; Launay, M.; et al.: Evo-
lution of the STICS crop model to tackle new en-
vironmental issues: New formalisms and integration
in the modelling and simulation platform RECORD,
Environ. Model. Softw., 2014, 62, 370–384 DOI:
10.1016/J.ENVSOFT.2014.07.010

[18] Varga, M.; Gyalog, G.; Raso, J.; Kucska, B.;
Csukas, B.: Programmable process structures of uni-
fied elements for model-based planning and op-
eration of complex agri-environmental processes.
In: Bochtis D. D.; Sørensen, C. G.; Fountas, S.;
Moysiadis, V.; Pardalos, P. Inf. Commun. Technol.
Agric. III Decis., (Cham.: Springer) 2022, pp. 223–
249 DOI: 10.1007/978-3-030-84152-2_11

[19] van der Werf, W.; Keesman, K.; Burgess, P.; et al.
Yield-SAFE: A parameter-sparse, process-based dy-
namic model for predicting resource capture, growth,
and production in agroforestry systems, Ecol. Eng.
2007, 29 419–433 DOI: 10.1016/j.ecoleng.2006.09.017

[20] TNO Biobased and Circular Technologies, The
Netherlands. Database for the physico-chemical
composition of (treated) lignocellulosic biomass,
micro- and macroalgae, various feedstocks for biogas

production and biochar n.d. https://phyllis.nl/ (accessed
January 4, 2022)

[21] Antal, M.; Allen, S. G.; Dai, X.; Shimizu, B.; Tam,
M. S.; Grønli, M.: Attainment of the theoretical yield
of carbon from biomass, Ind. Eng. Chem. Res., 2000,
39, 4024–4031 DOI: 10.1021/ie000511u

[22] Allen, R.; Pereira, L.; Raes, D.; Smith, M.: Crop
evapotranspiration - Guidelines for computing crop
water requirements - FAO Irrigation and drainage pa-
per 56, Chapter 2 - FAO Penman-Monteith equation,
Rome: FAO; 1998.

[23] Varga, M.; Prokop, A.; Csukas, B.: Biosystem mod-
els, generated from a complex rule/reaction/influence
network and from two functionality proto-
types, BioSystems, 2017, 152, 24–43 DOI:
10.1016/j.biosystems.2016.12.005

[24] Varga, M.; Csukas, B.: Generation of extensible
ecosystem models from a network structure and from
locally executable programs, Ecol. Modell., 2017,
364, 25–41 DOI: 10.1016/J.ECOLMODEL.2017.09.014

[25] Varga, M.; Csukas, B.; Kucska, B.: Implementation
of an easily reconfigurable dynamic simulator for re-
circulating aquaculture systems, Aquac. Eng., 2020,
90, 102073 DOI: 10.1016/J.AQUAENG.2020.102073

[26] Varga, M.; Berzi-Nagy, L.; Csukas, B.; Gyalog,
G.: Long-term dynamic simulation of environmen-
tal impacts on ecosystem-based pond aquaculture,
Environ. Model. Softw., 2020, 134, 104755 DOI:
10.1016/j.envsoft.2020.104755

[27] Csukas, B.: Simulation by direct mapping of the
structural models onto executable programs, AIChE
Annu. Meet., Miami, FL: AIChE, 1998, Paper 239/9.

[28] Kalman, R.; Falb P.; Arbib, M.: Topics in mathemat-
ical system theory (McGraw-Hill, New York, USA)
1969 ISBN: 978-0-0703-3255-3

[29] Petri, C.: Introduction to general net theory, In:
Brauer, W. (Ed.): Net Theory Appl. Lect. Notes Com-
put. Sci. (Heidelberg: Springer, Berlin, Germany),
1980, DOI: 10.1007/3-540-10001-6_21

[30] Abar, S.; Theodoropoulos, G. K.; Lemarinier, P.;
O’Hare, G. M. P.: Agent based modelling and sim-
ulation tools: A review of the state-of-art soft-
ware, Comput. Sci. Rev., 2017, 24, 13–33 DOI:
10.1016/J.COSREV.2017.03.001

[31] Varga, M.: Mendeley Data, V1, 2022, linked to this
paper DOI: 10.17632/nw3cjv75j5.1

50 pp. 57–65 (2022)

https://doi.org/10.1016/J.ENVSOFT.2014.07.009
https://doi.org/10.1016/J.ENVSOFT.2014.07.009
https://doi.org/10.1051/agro:19980501
https://doi.org/10.1016/j.envsoft.2014.09.006
https://doi.org/10.1016/j.envsoft.2014.09.006
https://doi.org/10.3390/su11082293
https://doi.org/10.1016/J.ENVSOFT.2014.07.010
https://doi.org/10.1016/J.ENVSOFT.2014.07.010
https://doi.org/10.1007/978-3-030-84152-2_11
https://doi.org/10.1016/j.ecoleng.2006.09.017
https://phyllis.nl/
https://doi.org/10.1021/ie000511u
https://doi.org/10.1016/j.biosystems.2016.12.005
https://doi.org/10.1016/j.biosystems.2016.12.005
https://doi.org/10.1016/J.ECOLMODEL.2017.09.014
https://doi.org/10.1016/J.AQUAENG.2020.102073
https://doi.org/10.1016/j.envsoft.2020.104755
https://doi.org/10.1016/j.envsoft.2020.104755
https://doi.org/10.1007/3-540-10001-6_21
https://doi.org/10.1016/J.COSREV.2017.03.001
https://doi.org/10.1016/J.COSREV.2017.03.001
https://doi.org/10.17632/nw3cjv75j5.1

	Introduction
	Challenges and objective
	Materials and methods
	Data and calculation formulae for a typical example of a plant to be modelled
	Non-conventional methodology of Programmable Process Structures

	Results and discussion
	Chemical process engineering-inspired principles and hypotheses of plant models 
	Structure of the investigated process system
	Solar radiation-driven ``natural supply logistics'' of plant biomass generation
	Solar energy-driven ``natural demand logistics'' of water and nutrient uptake
	Generation and simulation of the PPS model

	Conclusion