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Expansion of the sucro-energy Industry and the new
Greenfield Projects in Brazilfrom the view of the equipment industry.
Expanded version of the paper published in
by José Luís Olivério, Fernando C. Boscariol
www.dedini.com.br
24 to 27 june, 2013, São Paulo, Brazil
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Dedini S/A Indústrias de Base Page 1 of 24
Expansion of the sucro-energy Industry and the new Greenfield Projects in Brazil from the view of the equipment industry
by José Luís Olivério, Fernando C. Boscariol
Abstract
In 2003, the sucro-energy industry in Brazil resumed its
growth cycle, which lasted until 2011. A total of 117 new
mills were installed, and today there are 441 mills in
operation. Total processed cane rose from 320 million
tonnes (2002/2003) to 620 million tonnes (2010/2011).
By analyzing such new mills, we can see a significant
evolution from the first units to those built more
recently. Brazil will face again a “boom” of new mills:
forecasts show that sugarcane harvest will rise in 2020
to 1.2 billion tonnes/crop, and 120 additional “greenfield
mills” will be built in the country. Considering the
developments that have occurred in the 117 new mills,
the following questions come to mind: what will the
future mills be like, which technologies will be used,
what will be the processing capacity, what products will
the new mills offer, the traditional sugar, ethanol and
bioelectricity, or will there be new ones, what are the
lessons learned from the recent expansions. To answer
these questions, we analyzed the design profile evolu-
tion of the 117 new mills, identified the trends to be
considered as references for the new greenfield projects,
and what are the development drivers of the new
solutions. Conclusion is that the new greenfield mills
will be designed according to five drivers of evolution
trends for products, capacities and technologies: 1)
Increased capacities and productivity of the equipment
and the mill; 2) Increased efficiencies and yields; 3)
Increased sustainability; 4) Synergy and integration; 5)
Higher value-added products from both sugarcane and
the mill. Each of these drivers is discussed, and real
examples of solutions are presented for each driver and
the reasons for the choice.
Finally, it is concluded that the equipment industry is
able and ready to meet such a huge expansion, in all
capability and competitiveness aspects.
Sumário
Em 2003, o setor sucroenergético do Brasil retomou o
seu ciclo de crescimento, que se estendeu até 2011. 117
usinas canavieiras foram então instaladas, e hoje há 441
usinas em operação no Brasil. A cana processada se
elevou de 320 milhões de toneladas(2002/2003), para
620 milhões(2010/2011). Analisando-se essas 117 usinas
recentes, verifica-se que houve sensível evolução entre
as primeiras usinas e aquelas mais recentemente
implantadas. O Brasil terá novamente um novo “boom”
de novas usinas:previsões mostram que a produção de
cana irá se elevar para 1,2 bilhões de toneladas por safra,
e 120 “greenfields” serão adicionalmente implantados
no país. Considerando-se a evolução ocorrida nas 117
novas usinas, cabem as perguntas:-Como serão essas
futuras usinas?-Que tecnologias serão utilizadas?-Qual
será a capacidade de processamento de cana?-Quais
produtos serão oferecidos pelas futuras usinas? Os
tradicionais açúcar, etanol e bioeletricidade, ou teremos
novos produtos?-Quais são as lições que a cadeia
produtiva aprendeu com a recente expansão do setor?
Para responder a essas perguntas, este trabalho analisou
a evolução das recentes 117 usinas, identificou as ten-
dências a serem consideradas como referências para os
novos “greenfields”, e quais são os direcionadores, do
desenvolvimento das novas soluções, na visão da
indústria de equipamentos.
A conclusão é que os novos “greenfields” serão projeta-
dos conforme 5 vetores de tendência de evolução
quanto a produtos, capacidades e tecnologias: 1) Au-
mento das capacidades e da produtividade dos equipa-
mentos e das usinas; 2) Aumento das eficiências e
rendimentos; 3) Aumento da sustentabilidade; 4) Maior
sinergia e integração; 5) Produtos de maior valor
agregado da cana de açúcar e da usina. Cada um desses
vetores é discutido, e exemplos reais de soluções são
apresentadas para cada vetor e os motivos para a sua
escolha. Finalmente, conclui-se que a industria de
equipamentos está capacitada para atender essa forte
expansão, em todos os aspectos da capacitação e
competitividade.
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Expansion of the sucro-energy Industry and the new Greenfield Projects in Brazil from the view of the equipment industry
Dedini S/A Indústrias de Base Page 2 of 24
Introduction The Brazilian sugarcane industry has grown
hugely in the past 40 years, as shown in Figure 1.
Starting in 1975/76 with the launch of
ProAlcohol*, there has been an impressive growth in
sugarcane production, from 68 million tonnes of cane
per crop (TCC) to 223 million TCC in 1985/86, a
milestone that we call the “1st
great leap”. The reason is
the increased ethanol demand, which jumped from 550
million litres (1975/76) to nearly 12 billion litres
(1985/86), whereas sugar production remained at 6 to 9
million tonnes. And Brazil became, at the time, the
biggest ethanol producer in the world (all data from
Datagro, 2012).
From 1985/86 to 1993/94, annual sugarcane
production remained around 220 million tonnes,
sometimes producing more ethanol, sometimes more
sugar, with inexpressive variations (ethanol: 11 to 12
billion litres; sugar: 8 to 9 million tonnes).
In 1993/94, another major expansion of the
industry took place, which continued until 2002/03, and
cane production soared from 220 million to 320 million
tonnes/crop – the “2nd
great leap”. Here, growth was
due to the increased sugar production, when the
country moved to the export market and became the
biggest sugarcane and cane sugar producer. In this
period, sugar production rose from 9 million to nearly
23 million yearly tonnes, and ethanol remained in the
range of 12 to 15 billion litres.
Today, the situation is quite different from the
previous two: both sugar and ethanol production has
grown considerably, with sugarcane harvest rising from
320 (2002/03) to 620 million tonnes (2010/11). Brazil is
now at the “3rd
great leap”, with both sugar and ethanol
contributing to this growth: ethanol production going
from 12 billion litres (2002/03) to 27 billion litres/crop
(2010/11), and sugar from 23 million tonnes (2002/03) to
38 million tonnes/crop (2010/11). The following 2011/12
crop has shown a decline in production mainly due to
climatic reasons, but demand should continue to rise in
the next years.
As a result, today we have 441 mills in
operation in Brazil, of which 324 were built before 2003,
and 117 afterwards (CNI, 2012). Such set of mills is the
reference that we will use in this paper: 324 of them we
call “old mills”, and 117 we call “new mills”.
The conditions that led to the “3rd
great leap” -
that means increased demand on ethanol for domestic
market and on sugar to export - remain until now and
should stay for the next 8-10 years, which allows us to
assume that the sucro-energy industry will continue to
have a major expansion because of three independent,
yet concurring, factors today:
ethanol – domestic market: a rise in ethanol
demand because of the commercial success of the flex-
fuel vehicles and the increase of the Brazilian fleet,
predominantly running with flex-fuel engines, and
ethanol has been the preferred fuel;
ethanol – exports: an increase in ethanol
demand as a result of the global interest on this fuel
due to its environmental qualities: ethanol is made
from biomass, a renewable feedstock, and has a high
mitigating effect on the greenhouse gases, as gasoline is
replaced in the fuels utilization;
sugar – exports: exports should also grow due
to the country’s competitiveness, the growing global
market, and the global trend to reduce agricultural
Fig 1 - Brazilian production of sugarcane, sugar and ethanol. The text in the box informs the reason why it was necessary to increase sugarcane production
BRAZIL – HISTORICAL DATA – SUGARCANE, SUGAR AND ETHANOL PRODUCTION
0
100000
200000
300000
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500000
600000
0
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10000
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Su
car
can
e P
rod
uctio
n 1
000 to
n
Su
car
(mm
to
n) a
nd
Eth
an
ol (
mm
3)
Etanol (1000 m3) Açúcar (1000 T) Cana (1000 T)
Su
gar
(1000 t
) an
deth
an
ol
(1000 m
3)
pro
du
cti
on
Ethanol Sugar Cane
1st Great
Leap
Su
garc
an
ep
rod
ucti
on
(1000 t
)
2nd Great
Leap
*
3rd Great
Leap
SOURCE:
DATAGRO
* ProAlcohol – Programa Nacional do Álcool - Brazilian Ethanol Program, a program started in 1975 with the purpose to introduce ethanol into the Brazilian Energy Matrix, in which ethanol was blended with gasoline, or replaced gasoline (100%) as a fuel in vehicles.
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Expansion of the sucro-energy Industry and the new Greenfield Projects in Brazil from the view of the equipment industry
Dedini S/A Indústrias de Base Page 3 of 24
subsidies to protect sugar production in many
countries.
Forecasts for sugarcane growth in Brazil, as
developed by several official bodies and representative
entities of the sector are coinciding: all of them assume
that the industry will double cane production in the
next years, reaching 1.2 billion tonnes in 2020/21, a
considerable increase over the 2010/11 crop, (UNICA,
2012).
ethanol – domestic market + exports: from
27 to 70 billion litres, of which 80% are for the domestic
market;
sugar – domestic market + exports: from 38
to 51 million tonnes, of which 73% are for exports;
To meet such demand, in addition to the
existing mills, UNICA foresees that 120 large-size
“future mills” (“greenfield mills”) will be built in the
country by 2020.
Considering the technological progress that
have been incorporated to the 117 “new mills” in relation
to the 324 “old mills”, and the construction of 120
“future mills”, the following questions arise:
What will the “future mills” be like?
Which technologies will be used?
Which will the processing capacities be?
What products will the ”future mills” offer: the
traditional sugar, ethanol and bioelectricity, or will
there be new ones?
What are the lessons learned from the recent
expansions, and will they be used in the design and
construction of the “future mills”?
To answer these questions, we examined the
development design concepts already incorporated to
the 117 “new mills”, the advances already accomplished,
and which ones will be incorporated to the future
solutions, and then define the drivers of evolution of
the “future greenfield mills”.
The conclusion, as you will see, is that the new
greenfield plants will be designed according to five
drivers of evolution trends for the products, capacities
and technologies that will be used. This is the subject of
the present study.
Design development: from
“sugar mill” to the “sucro-energy
plant”
The typical mill
The Brazilian sugar and biofuels industry has
grown innovatively since the launch of “ProAlcohol” in
1975. Until then, the “sugar mills” in Brazil were
conventional and even technologically obsolete when
compared to other countries.
At the end of this chapter, in Table 3, we
present some performance indicators that illustrate the
technological stage then existing. Figure 2 is self-
explanatory and illustrates the typical sugar mill at the
time.
In early ProAlcohol, “Ethanol Process” plants
were incorporated and integrated to the “sugar and
alcohol mill”. It was not an innovation, but a novelty in
Fig. 2 – Traditional technology and production process: sugar and surplus bagasse.
PRODUCTION FLOWCHART – SUGAR AND SURPLUS BAGASSE
PRODUCT FLOW
HIGH ORESSURE STEAM FLOW
(DRIVING PURPOSE)
LOW PRESSURE STEAM FLOW
(THERMAL PURPOSE)
ELECTRICITY
GENERATION(TURBOGENERATOR)
CANERECEPTION/
CLEANING/
PREPARATION
EXTRACTION
SURPLUS BAGASSE
B
A
G
A
S
S
E
JUICE SUGAR
PROCESSSUGAR
MOLASSES
STEAM
GENERATION(BOILER)
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Expansion of the sucro-energy Industry and the new Greenfield Projects in Brazil from the view of the equipment industry
Dedini S/A Indústrias de Base Page 4 of 24
Brazil, since ethanol was previously produced on a
small scale and from molasses only, and then the mills
began to use molasses and/or juice (Figure 3).
Fig. 3 – Traditional technology and production process for sugar, bioethanol and surplus bagasse.
This solution was not sufficient to meet the
enormous growth in ethanol demand (the 1st
great leap,
as described in the previous section). A really
innovative approach was then implemented: a plant to
produce exclusively ethanol, resulting in a wide
reformulation of process, basic, and detailing
engineering, new equipment and process solutions, new
mass and energy balances, a full re-dimensioning of the
mill (Figure 4).
Fig. 4 – Traditional technology and production process for bioethanol and surplus bagasse.
Over time, due to the stabilized ethanol
demand and a sharp rise in sugar exports (the 2nd
great
leap), such ethanol plants evolved to incorporate and
integrate a “sugar process” plant, which was the typical
solution adopted by the “old mills” until the early
2000s. At that time, updated technologies were used for
sugar production, thus renovating the industry, which
was then in obsolete conditions.
From 2002/03, with the “3rd
great leap”, “new
mills” have been built to meet the rising demands for
sugar and ethanol. At that time, the world, and
particularly Brazil, were already in tune with the efforts
for renewable sources of energy, and there was full
awareness of the whole sugarcane energy potential, i.e.,
not just transforming cane juice into products (sugar,
ethanol), but also the cane bagasse and, more recently,
cane straw (crop residues which we named “straw”)
into new products.
Realizing that sugarcane had a major role in
the agri-energy sector, the country decided to create
institutional mechanisms to transform the bioelectricity
generated by bagasse (and straw) into a new product, a
new business.
The existing technologies were already
properly developed, so the “new mills” could
immediately use the configurations shown in Figure 5
and Figure 6; in Figure 5 the “sugar, ethanol and
bioelectricity mill”, or, as a result of the faster-growing
ethanol demand, in Figure 6, the “ethanol and
bioelectricity mill”, this last one the predominant
solution for the “new mills”.
Also in this case, innovative solutions were
developed, involving new processes, balances,
equipment, etc.
Fig. 5 – Traditional technology and production process for biosugar, bioethanol and surplus bioelectricity
*.
* To emphasize the “organic or biological origin” of the products derived from sugar cane, in this paper those products are named: bioethanol, bioelectricity and biosugar.
SURPLUS BAGASSE
PRODUCT FLOW
HIGH ORESSURE STEAM FLOW
(DRIVING PURPOSE)
LOW PRESSURE STEAM FLOW
(THERMAL PURPOSE)
ELECTRICITY
GENERATION(TURBOGENERATOR)
CANERECEPTION/
CLEANING/
PREPARATION
EXTRACTION
B
A
G
A
S
S
E
JUICE SUGAR
PROCESSSUGAR
MOLASSES
STEAM
GENERATION(BOILER)
SURPLUS BAGASSE
J
U
I
C
E BIOETHANOL
STILLAGE
BIOETHANOL
PROCESS
PRODUCTION FLOWCHART – SUGAR, BIOETHANOL AND SURPLUS BAGASSE
SURPLUS BAGASSE
PRODUCT FLOW
HIGH ORESSURE STEAM FLOW
(DRIVING PURPOSE)
LOW PRESSURE STEAM FLOW
(THERMAL PURPOSE)
ELECTRICITY
GENERATION(TURBOGENERATOR)
RECEPTION/
CLEANING/
PREPARATION
EXTRACTION
B
A
G
A
S
S
E
STEAM
GENERATION(BOILER)
SURPLUS BAGASSE
J
U
I
C
E BIOETHANOL
STILLAGE
BIOETHANOL
PROCESS
SURPLUS BAGASSE
CANE
PRODUCTION FLOWCHART – BIOETHANOL AND SURPLUS BAGASSE
B
A
G
A
S
S
E
JUICE
J
U
I
C
E
CANERECEPTION/
CLEANING/
PREPARATION
EXTRACTION
ELECTRICITY
GENERATION(TURBOGENERATION)
STEAM
GENERATION(BOILER)
BIOETHANOL
STILLAGE
SUGAR
MOLASSES
SUGAR
PROCESS
BIOETHANOL
PROCESS
BIOELECTRICITY
PRODUCT FLOW
HIGH PRESSURE STEAM
FLOW (DRIVING PURPOSE)
LOW PRESSURE STEAM FLOW
(THERMAL PURPOSE)
PRODUCTION FLOWCHART – SUGAR, BIOETHANOL AND SURPLUS BIOELECTRICITY
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Expansion of the sucro-energy Industry and the new Greenfield Projects in Brazil from the view of the equipment industry
Dedini S/A Indústrias de Base Page 5 of 24
Fig. 6 - Traditional technology and production process for bioethanol and surplus bioelectricity.
Profile of the Brazilian sugarcane mills
Before the “3rd
great leap”, 324 “old mills” were
in operation in Brazil. Over the past 10 years, 117 “new
mills” were built, as shown in Figure 7.
Fig. 7 – Number of new sugarcane mills installed in Brazil by crop. Source: (CNI, 2012)
Let’s examine the profile of these total (old
and new) plants. Figure 8 illustrates the “total mills”,
ranked by products (CNI, 2012), and Figure 9 ranks the
“new mills”.
Fig. 8 – “Total Mills” – classified by products. Source: (CNI, 2012)
Fig. 9 – “New mills” profile classified by products. Source: CNI 2012/Dedini
When we examine the graphs, we can see that
there has been a significant change in the profile of the
“new mills”, now more focused on ethanol and already
designed to produce bioelectricity, even though
partially implemented.
In “total mills”, sugar & ethanol flexible mills
predominate (60%), whereas in “new mills” ethanol
plants are in a larger number (75%);
Sugar mills are not significant (5% in “total
mills”, and with no record in “new mills”);
Regarding bioelectricity, in “total mills” is not
significant (15%), but it is now largely considered in the
“new mills” (80% designed, but 35% implemented and
in operation).
It is worth noting that the length of the milling
season has also extended significantly in the country:
from 180 overall days with 144 effective days in the end
of 80´s, to 230 overall days with 200 effective days
currently.
Figures 10 and 11 present other important
information about the Brazilian mills. Center-South is
the region in the country with the largest number of
total mills, i.e., 354 units.
Fig. 10 – Typical productivity and capacities (Source: Dedini)
B
A
G
A
S
S
E
J
U
I
C
E
CANERECEPTION/
CLEANING/
PREPARATION
EXTRACTION
ELECTRICITY
GENERATION(TURBOGENERATION)
STEAM
GENERATION(BOILER)
BIOETHANOL
STILLAGE
BIOETHANOL
PROCESS
BIOELECTRICITY
PRODUCT FLOW
HIGH PRESSURE STEAM
FLOW (DRIVING PURPOSE)
LOW PRESSURE STEAM FLOW
(THERMAL PURPOSE)
PRODUCTION FLOWCHART – BIOETHANOL AND SURPLUS BIOELECTRICITY
10
19
25
30
22
8
3
0
5
10
15
20
25
30
35
2005/06 2006/07 2007/08 2008/09 2009/10 2010/11 2011/12
SOURCE: CNI 2012
Number of new mills
100%
60%
35%
5%
15%
0%
25%
50%
75%
100%
Brazilian Total Sugarcane Mills Profile - classified by products
Total(441)
Sugar+Ethanol
Ethanol BioelectricitySugar
SOURCE: CNI 2012
100%
25%
75%
Brazilian New Mills (after 2003) Profile – classified by products
Total
(117)
Sugar+
Ethanol
Ethanol Bioelectricity
designed
80%
35%operational
SOURCE: TOTAL= CNI 2012, PROFILE = DEDINI
Center-South Typical Data
Mill Capacity
TCC
Productivity
TC/ha
Productivity
LETC
Brazil(range)
80
100
80
100 - best practices
908 mi
0,3 mi
Source: Dedini TC: Tonnes of cane TCC: Tonnes of cane per crop
LETC: Litres of ethanol per tonne of cane
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Expansion of the sucro-energy Industry and the new Greenfield Projects in Brazil from the view of the equipment industry
Dedini S/A Indústrias de Base Page 6 of 24
Fig 11 – “New mills” capacity evolution (Source: Dedini)
The productivity data (Figure 10) are self-
explanatory.
With respect to capacity, there is a great
variation between the total existing plants, ranging
from 300,000 TCC to 8 million TCC.
The “new mills” first had a typical capacity of
12,000 tonnes of cane per day (TCD) (2.4 million TCC),
but more recently such capacity has been as high as
15,000 to 20,000 TCD (3 to 4 million TCC); and the
trend is to increase even more the sugarcane processing
capacity to 20,000 to 30,000 TCD (4 to 6 million TCC),
as shown in Figure 11. Nearly all plants were designed or
considered to produce bioelectricity.
It is worth noting that due to some factors (the
2008 global financial crisis, the consolidation of the
industry into large groups through mergers and
acquisitions, the lack of investments in the renovation
of sugarcane crops, and insufficient productivity-
oriented agricultural management, followed by two
years of adverse climatic conditions), the growth cycle
has been interrupted in the past years. The last decision
for a “new mill” was made in 2007, and those units were
implemented until 2011.
The projects under consideration and
supposed to be approved after 2008 are for even larger
capacities: such future mills would have a capacity of
20,000 to 30,000 TCD (4 to 6 million of TCC), and
bioelectricity (Figure 11).
Technological evolution of the industrial area
The fast growth of the industry, which has led
to numerous investments in renovation, expansion, and
new mills, resulted in an important technological
development of equipment, processes, plants, and
complete mills.
Considering the current main products of the
Brazilian mills, we will limit our discussion to three
development routes: for sugar, ethanol and
New Mills Capacity - mi TCC / mi LEC
The First30 MW
Recent37/50 MW
Future50/75 MW
6/510
4/340
4/340
3/255
2,4/200
12.000
TCD
15.000
TCD
20.000
TCD
20.000 TCD
30.000 TCD
Source: Dedini TCC: Tonnes of cane per crop TCD: Tonnes of cane per day
mi: millions MW: Surplus power export capacity LEC: Litres of ethanol per crop
1. Dry cleaning replacing cane wash
2. High performance MCD Dedini milling
tandem or Dedini-Bosch Modular Diffuser
3. To eliminate sugar entrainment and degradation in evaporators
4. Ecoferm – Dedini-Fermentec Fermentation System with higher ethanol content and with Ecochill (absorption chiller)
5. Destiltech – Distillation system with minimum ethanol losses in stillage
6. DRD – Dedini Refinado Direto (Dedini Direct Refined)
7. DAP – Dedini Automação de Processos – Automation using intelligent
software up to MES Level – Manufacturing Execution System
8. Process sweet sorghum at the sugarcane mill
Dedini Patent ApplicationTechnological Partner Patent Application
TECHNOLOGIES FOR MAXIMUM BIOSUGAR AND BIOETHANOL PRODUCTION
Table 1 – Technologies for maximum biosugar and bioethanol production.
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Expansion of the sucro-energy Industry and the new Greenfield Projects in Brazil from the view of the equipment industry
Dedini S/A Indústrias de Base Page 7 of 24
bioelectricity production.
Sugar and ethanol – there have been
significant improvements in yields and efficiencies,
maximising the extraction of cane sugars, minimising
process losses and optimising the transformation of
juice into sugar and ethanol. There have been many
improvements in the existing processes, and numerous
innovations have been introduced, which together have
enabled optimum sugar and ethanol production per
tonne of cane.
Table 1 lists the technologies that the
equipment manufacturers in Brazil, in special Dedini,
uses when a new mill project aims at the optimal sugar
and ethanol production. Some of these technologies
will be discussed later in this paper; for an overview, see
Olivério et al., 2010a.
Bioelectricity – similarly, the industry has
experienced considerable improvements in energy
efficiency, aiming at the maximum production of
bioelectricity per tonne of cane. Maximum
bioelectricity production is attained by two kinds of
technologies designed to:
Minimum consumption of electrical and steam
energy by the mill, i.e., minimum use of energy (electric
power, steam) for cane processing and in the sugar and
ethanol production processes. As a result, we have
maximum surplus of bagasse and/or straw, i,e,,
maximum surplus biomass; and
Maximum use of the energy available in the
sugarcane and in the mil, i.e., use of the energy from
bagasse and/or straw, and biogas from vinasse with
maximum energy efficiency.
Table 2 lists the technologies, which, together,
enable maximum production of surplus bioelectricity;
for an overview of these technologies, see Olivério et al,
2010a.
With the new techno logies implemented by
the Brazilian mills since the beginning of ProAlcohol
(1975), there has been a significant increase of
productivity gains and efficiencies in sugar, ethanol and
bioelectricity production, as can be seen in Table 3 (CNI
2012).
As a reference, and to correlate the current
equipment performances with typical state-of-the-art
solutions, we included in Table 3 the products and
technologies already presented in Tables 1 and 2 and
which are commercially available from the Dedini
Company as part of their products line.
Table 2 – Technologies for maximum surplus bioelectricity production
Maximum available energy utilization Minimum energy consumption
````
1. Electric Drive to Knives/Shredder
2. Electric-Hydraulic Drive / Electro-Mechanical Drive via planetarygearbox to milling units or Dedini-Bosch Modular Diffuser
3. Multi-effect Falling Film Evaporation System
4. Regenerative Heat Exchangers
5. Ecoferm –Dedini-Fermentec Fermentation System with higher
ethanol content and with Ecochill (absorption chiller)
6. Dedini-Siemens Split Feed Distillation
7. Dedini-Vaperma Membrane Dehydration System
8. Dedini-Bosch Continuous Vacuum Pan
9. DRD – Dedini Refinado Direto (Dedini Direct Refined)
10. DCV – Dedini Stillage Concentration System
11. Maximum surplus bagasse utilization as boiler fuel (except re-start)
12. System and equipment for straw utilization as boiler fuel
13. Methax– Stillage Anaerobic Biodigestion System producing biogas/biomethane
14. Dedini AT Single Drum Multifuel Boilers –high: pressure/ temperature/ energy efficiency
15. Condensation turbine with multi-stage extraction control
16. Process sweet sorghum at sugarcane mill
17. DAP – Dedini Automação de Processos –Automation using intelligent software up to MESLevel – Manufacturing Execution System
Dedini Patent ApplicationTechnological Partner Patent Application
TECHNOLOGIES FOR MAXIMUM SURPLUS BIOELECTRICITY PRODUCTION
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Table 3 – Evolution of the technological capabilities as a function of the equipment and technology available.
DEDINI PRODUCTS
Beginning PROALCOHOL
Today State of the Art
1. Production/equipment capacities increase
Crushing Capacity (TCD) - 6x78” Vert. Shredder/ Milling Tandem
5 500 15 000
Fermentation Time (h) Batch/Cont. Ferm. 24 6 - 8
Beer Ethanol Content (°GL) Ecoferm 6.5 Up to 16
2. Efficiency/yields increase
Extraction Yield (%Sugar) - 6 Mill Units Milling Tandem/ Modular Diffuser
93 97/ 98
Fermentation Yield (%) Ecoferm 80 92
Distillation Yield (%) Destiltech 98 99.5
3. Optimising energy consumption/efficiency
Total Steam Consumption (kg Steam/t cane)
DEDINI Technology 600 320
Steam Consumption Anhydrous. (kg steam /Litre)
Split Feed+ Mem-brane/Mol. Sieve
4.5 2.0
Boiler – Efficiency (% LHV) Capac.(t/h) /Press.(Bar) / Temper.(ºC)
AZ/ AT/ Single Drum
66 89
60 / 21 / 300 400 / 120/ 540
Biomethane from Stillage (Nm3/litre of
Bioethanol) Methax - 0.1
4. Global parameters
Total Yield (Litre Hydr. Bioeth./t cane) DEDINI Technology 66 87
Surplus Bagasse (%) - Bioethanol Mill DEDINI Technology Up to 8 Up to 78
Surplus Bioelectricity to the Grid, Bioeth-anol Mill, 12 000 TCD (fuel: bagasse) (MW)
DEDINI Technology - 50.7
Surplus bioelectricity to the grid – Bioetha-nol mill, 12 000 TCD (bagasse + 50%/100% straw) – (MW)
DEDINI Technology - 84/112
Stillage Production (litre stillage/litre Bio-eth.)
Ecoferm/ DCV 13 5.0/ 0.8
Intake Water Consumption (litre Wa-ter/litre Bioeth.)
Water Mill 187 (-) 3.7
TCD = tones of processed cane per day; LHV = based on
bagasse Low Heat Value;
Capac. = Boiler Steam Production; Press. = Pressure; Temp.
= Temperature;
Bioeth.= Bioethanol; Cont. Ferm.= Continuous Fermenta-
tion system;
Vert. = Vertical; Ecoferm = Ethanol fermentation system up
to 16ºGL;
Destiltech = Ethanol distillation Plant with flegma recircula-
tion;
Mol. Sieve = Dehydration by Molecular Sieve System;
AZ/AT/Single Drum = Boilers models and types;
Methax = Stillage Biodigestion Plant producing biogas
and/or biomethane;
DCV = Evaporative Stillage Concentration Plant
Hydr: Hydrated
RESULTS OF INDUSTRIAL TECHNOLOGICAL EVOLUTION IN THE SUCROENERGY SECTOR – 2011
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Table 3 is self-explanatory, but we highlight
the development in processing capacity: six 78” milling
units processed 5500 TCD in 1975; in 1985 the
processing capacity was 10,000 TCD (Giannetti, 1985);
in 2002 it reached 13,000 TCD (Olivério, 2002); in 2006,
14,000 TCD (Olivério, 2006); and from 2010 to now the
milling tandem can process 15,000 TCD (Olivério et al.,
2010a, CNI 2012). We consider this evolution in various
steps very interesting, and appropriate to illustrate how
continuous improvements, with small incremental
increases, can reach a very significant final result. And,
in parallel, extraction process yields increased from 93%
(1975) to 97% (2011).
The profile of the Brazilian “new mills”
As already shown in this study, 117 “new mills”
were built in Brazil in the past ten years. A common
characteristic of the recent and current Brazilian mills
market is that each solution is individually defined; so,
as a whole, you will find unique solutions in each of the
mills. From the project design to equipment and
installation definitions, the mill is customized to suit
the goals and interests of the investors and/or their
consultants, engineering companies and equipment
manufacturers. This was not always so: in early
ProAlcohol, the manufacturers used to offer standard
ethanol plants, and also complete turnkey mills.
Thus, we have today almost 117 different
solutions in the 117 “new mills” installed. Therefore, to
determine the profile of the new recent mills, a long
and detailed survey and an evaluation of the different
solutions adopted would be necessary, which is not the
purpose of the present study. Our interest is to define a
profile that can be used as a reference for the
development trends of the future “greenfields” to be
built in Brazil.
According to the characteristics and solutions
adopted, we will use for this purpose the most recent
“new mill” in Brazil – the Água Emendada Mill in Goiás,
of the ETH/Brenco Group, which started operations in
November/2011.
This mill was part of a package of four new
mills implemented by ETH/Brenco, with similar, not
identical, solutions, and Dedini supplied all process
mechanical equipment and half of the bagasse boilers,
as well as the so-called “process islands”, i.e., “sugarcane
reception and processing”, “fermentation”, “distillation”,
and “boiler”.
These are the new mills: Morro
Vermelho, GO, (started operations in 2010), Alto
Taquari, MT (2010), Costa Rica, MS (2011) and Água
Emendada, GO (2011). All of them produce ethanol and
bioelectricity, with a capacity of 18,000 TCD, 3.6 million
of TCC. Figure 12 gives an overall view of the Água
Emendada Mill, with indication of its main sectors.
Figures 13, 14 and 15 show in details the sugarcane
processing sectors, bioelectricity production,
bioethanol production, and the tanking area.
Fig. 12 – Typical profile of the recent Brazilian new greenfield mills – overall view – Odebrecht (ETH/Brenco) Água Emendada Mill.
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Fig. 13 – Typical profile of the recent Brazilian new greenfield mills – view of sugarcane processing and bioelectricity production – Odebrecht (ETH/Brenco) Água Emendada Mill.
Fig. 14 – Typical profile of the recent Brazilian new greenfield mills – view of bioethanol production – Odebrecht (ETH/Brenco) Água Emendada Mill.
Fig. 15 – Typical profile of the recent Brazilian new greenfield mills – view of the ethanol tanking area – Odebrecht (ETH/Brenco) Água Emendada Mill.
The ETH/Brenco mills do not produce sugar,
but schematically, as a way of illustration, Figure 16
shows what would be a sugar, ethanol, and
bioelectricity-producing mill.
Fig. 16 – Typical profile of the recent Brazilian new greenfield mills – biosugar + bioethanol + bioelectricity mill – overall view
Drivers of development trends of products, capacities, and technolo-gies
Advancements in the mills and in overall
performances have been impressive from early
ProAlcohol to now.
Part of such evolution followed some trends
that can be easily identified when we examine the
progress of such performance in a sequence. Earlier
studies (Olivério 2002, Olivério 2006, CNI 2012)
identified models of the technological development
that the industry has experienced, namely:
▪ Equipment and plant capacity and productivity
increases;
▪ Efficiency and yield increases;
▪ Better use of sugarcane energy;
▪ Diversification of products and by-products
from sugarcane increase;
▪ The mill defined as an energy-and-foods-
producing unit.
By analysing the stages of this model, having
as reference the existing mills, particularly the “new
mills”, we can see that some stages can still be
considered as drivers that will direct the development
trends of the “future mills” – the greenfields. Others
remain with some adjustments, while some have been
changed into more specific drivers, losing the generic
characteristic that they used to have.
But new drivers have also emerged, as a result
of new concepts, requirements, and even the
development of the earlier stages. Thus, we believe that
the considerable expansion of the Brazilian sucro-
energy industry, from 600 million TCC to 1.2 TCC, and
expected to have 120 additional greenfields, will be
attained by using the five drivers that will govern the
evolution trends of products, capacities, and
technologies:
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1. Equipment and plant capacity and
productivity increases;
2. Efficiency and yield increases;
3. Sustainability increase;
4. Synergy and integration;
5. Higher value-added products from sugarcane
and the sugarcane mill.
Following we will discuss each of these drivers,
in some cases presenting possible technological
improvements to be developed, but mainly the real
solutions already existing, in operation or available
waiting for a pioneer commercial use. These examples
aim to support the central thesis of this study, i.e., that
the new “greenfields” may continue to be customized,
but that the “future mill” should consider in its basic
project the developments already resulting from these
five drivers.
Driver 1: Equipment and plant ca-pacity and productivity increases
This driver defines that the trend is of larger
and more productive equipment and mills.
A good example is the increased capacity of
the six 78” milling units, as already seen, which jumped
from 5,500 to 10,000 TCD, then 13,000 TCD, and today
15,000 TCD, mainly because of higher productivity
rates.
This occurred first from adjustments in
equipment engineering to meet a national super
crushing demand, as a result of pressure put on the
mills to crush more and more cane to produce larger
ethanol volumes (due to ProAlcohol), along with the
lack of financial resources to expand the mills. As a
consequence, the existing equipment were used to the
their limits and improved with the use of materials,
accessories, new components, and design modifications
that have been introduced to attain higher
performances. Then, when such possibilities were
exhausted, in a second stage there were changes in
geometry, in dimensioning, and use of more advanced
devices, resulting in a new rise in productivity for this
same set of 78” crushers.
Further productivity increases for this same
crusher are increasingly difficult to obtain, but the need
for increased capacities remains, i.e., this driver will
continue to influence the design of the future mills,
which will have as limitations to daily crushing
capacities the technical and economic feasibility of the
maximum amount of cane that could be supplied to the
plant. It is known that cane supply from long distances
may be unviable. But, in Brazil, the future mills will be
built mainly at the new agricultural frontiers, where
there are more contiguous lands available for cane
crops. Thus, large areas in hectares of cultivation will
have short average distances for the transportation of
sugarcane to the plant during harvest, which will make
viable the increase of the yearly/daily crushing volume.
Thus, the new projects requirements will be
for even larger cane processing capacities, and the best
economic solution is a single processing line, i.e., a
single crushing tandem or a single high-capacity
diffusion plant.
Regarding crushers, productivities are close to
their limits; an increase in cane processing will be
achieved mainly by means of capacity increases, using
larger equipment, i.e., 90”, 100”, 110”, and 120” crushers.
In the case of diffusers, the traditional chain
diffusers have design and mechanical complexities that
are not easy to be overcome in so large capacities. Thus,
we believe that increased capacities will be attained by
chainless modular diffusers, which are expansible in
their own conception (Olivério, 2011).
Another possibility is the evolution of the
diffusion systems by the incorporation of new
technologies, reducing the time of cane in the
equipment (e.g., use of vacuum for the intake of
imbibition juice).
Some equipment and solutions already found
in “new mills” (see Figures 17 to 23) support our belief
that this driver will be very important for designing
“future greenfields”.
Figure 17 shows the world’s biggest capacity
diffuser 21 000 TCD, and Figure 18 the same for the
milling tandem, 31 200 TCD.
Figure 19 is an example of the same trend
expressed by driver 1 in steam generation, two boilers
with capacity of 320 tonnes of steam per hour each.
Figure 20 demonstrates the capacity increase
driver impact on juice treatment and concentration
stages: the world’s biggest short retention time clarifier,
and a high capacity five effect falling film evaporators.
Also, driver 1 impact is shown on ethanol
process: Figure 21 presents a fermentation plant using
the world’s biggest feed-batch fermentation vessel
utilising yeast recycle process: 2000 m³; Figure 22
presents big capacities on distillation plants to produce:
hydrated ethanol, (total of 2 700 000 litres/day,
composed of three installations of 900 000 litres/day
each), and anhydrous ethanol (molecular sieve plant of
1 000 000 litres/day capacity).
The correspondent impact of driver 1 on sugar
process is presented in Figure 23.
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Fig. 17 – Trend: increased diffusers capaci-ty/productivity – Raízen Jataí Mill –high capacity chainless modular diffuser
Fig. 18 – Trend: increased milling units/milling tandem capacity – US Sugar Mill –high capacity milling unit/tandem
Fig. 19 – Trend: increased boilers capacity/productivity – Raízen Barra Mill –high capacity bagasse boiler
Fig. 20 – Trend: increased juice treat-ment/concentration equipment and systems capaci-ty/productivity – high capacity solutions: Raízen Jataí clarifier/ Bunge Santa Juliana Mill evaporators
Fig. 21 – Trend: Larger fermentation vessels and in-creased plants capacity/productivity – Odebrecht (ETH) Agua Emendada Mill – high capacity Fermenta-tion Plant
Fig. 22 – Trend: increased distillation and dehydration capacity/productivity – high capacity plant: Santa Luzia Mill distillation plant/ Rio Brilhante Mill dehydration plant.
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Fig. 23 – Trend: increased sugar equipment and plant capacity/productivity – Clealcool Mill sugar plant.
More information regarding these
equipment/solutions can be seen in Figures 17 and 18,
Olivério 2011; Figure 19, Olivério and Ferreira 2010.
The driver “increased capacity and
productivity” is one of the most effective trend of the
new greenfields because the investments in equipment,
plants, and the mill itself are very sensitive to
economies of scale, having a positive effect on CAPEX
(Capital Expenditure), and, therefore, usually large-
scale solutions result in specific low-cost investments,
i.e., the larger the scale the lower the investment
expenditures per tonne of processed cane per crop
(TCC).
Driver 2: Efficiency and yield in-creases
It is natural that this driver should influence
the future greenfields design because in essence this
means producing more with less. Solutions resulting in
a larger amount of products per tonne of cane are
usually more competitive, with lower costs, thus
enabling larger sales volume.
The industry has advanced considerably in
sugar production, where losses are relatively small, but
still there is room for further developments in the
ethanol process (in fermentation there is great potential
of improvements), and mainly in bioelectricity
production.
With respect to energy, sugarcane has not ben
used to its full potential in Brazil. There are wastes in
the mills processes, as well as an effective low use of the
energy available in bagasse, especially in straw (crop
residues). Table 3 illustrates the state-of-the-art
technology for potential bioelectricity to be exported to
the grid: a state-of-the-art mill of 12,000 TCD can
provide 50.7 MW of surplus power while few “old mills”
have the capacity to produce surplus electricity. Even
the “new mills” are not optimised, producing surplus
power not over 30/35 MW. By using the energy from
straw, Table 3 shows that a potential surplus is even
more representative: 84MW from bagasse plus 50%
straw, and 112 MW from bagasse plus 100% straw
(Olivério and Ferreira, 2010). These figures confirm our
premise that bioelectricity production and the full use
of sugarcane are the greatest potential area for
evolution when targeting efficiencies and yields.
The most competitive future greenfields and
which will deliver more profits to the stockholders and
investors are those with the highest efficiencies and
yields in the production of sugar, ethanol, and
bioelectricty per tonne of cane.
A large number of “new mills” have already
incorporated solutions (equipment, plants) related to
this development driver, as can be seen in Figures 24 to
28, which we present to show that good solutions
already exist, have already been implemented, and
should be improved and used in the “future
greenfields”.
Fig. 24 – Trend: increased efficiency and yield – cane and straw dry cleaning and separation plant, allowing energy production from straw and minimum sugar losses by replacing cane wash
Fig. 25 – Trend: increased efficiency and yield– Fluid-ized bed boiler allowing flexibility on fuel utilization: new bagasse (because of mechanical harvesting + bagasse from diffuser + straw utilization + higher moisture + “sulphur traces” + “chlorine traces”), con-centrated stillage, other solid recovered fuel, operating at a higher energy efficiency.
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Fig. 26 – Trend: increased efficiency and yield – Eco-ferm: higher fermentation yield, lower stillage volume, energy optimisation.
Fig. 27 – Trend: increased efficiency and yield – sugar losses reduction and lower steam/energy consumption – Bunge Santa Juliana Mill Evaporators, Laginha Mill split feed distillation, Distillation/Dehydration Dedini membrane Demo Plant at São Martinho Mill.
Fig. 28 – Trend: increased efficiency and yield – stillage concentration plant with energy integration reducing energy/steam consumption (Gabardo, 2011; Ferreira, 2012)
More information regarding these
equipment/solutions can be seen in Figure 24, Gurgel
2012; Figure 25, Faiad and Acenso 2011; Figure 26,
Olivério et al. 2010b, and Amorim and Olivério 2010;
Figure 27, Moura 2006, Moura and Medeiros 2007 and
Olivério et al. 2010c; Figure 28 Gabardo 2011 and
Ferreira 2012.
This driver, “increased efficiencies and yields”
is crucial to the business economic results because it
means more products for the same, or less, inputs. It
has a positive impact on OPEX (Operational
Expenditure), by reducing direct costs or variable costs
per unit produced and, thus, allowing higher
operational profits.
Driver 3: Sustainability increase
Today, sustainability is mandatory in all
human activities. Pressures of society, scientific facts,
governments, laws, and even the consumers awareness
are demanding more and more sustainable solutions
and practices, including, and particularly, in industrial
activities.
The sucro-energy mill is no exception; on the
contrary, in mills, the need to comply with
sustainability concepts is even greater, because their
products are food (sugar) and energy (ethanol and
bioelectricity) for which the whole world today
demands sustainable solutions.
In addition, such demand is even stricter,
since ethanol and bioelectricity are presented as
“green”, clean, renewable energy from biomass, with
optimum energy balance, and are beneficial to people
and the environment because of the improved air
quality, decreased pollution, and the mitigating effect
of the greenhouse gases; additionally, from its
production processes solid wastes and effluents can be
recycled, and, at the same time, replace fossil inputs.
Both ethanol and bioelectricity are considered
sustainable products and, therefore, it would be
inconsistent if they were produced using unsustainable
resources, and technologies. For that alone, this driver
would be important to influence the future greenfield
projects.
Furthermore, the full use of sugarcane still has
a huge potential to further improve the favorable
balance that the industry has attained with respect to
sustainability.
As a result, we understand that this will be one
of the most important drivers of technological
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development to be considered in the expansion of the
sugarcane industry in Brazil. In fact, some sugarcane
mills have already been submitted to an evaluation
from specialized auditing companies which are
internationally qualified to certify those mills that
comply with sustainability criteria and systems, such as
Bonsucro EU, ISCC International Sustainability and
Carbon Certifications, etc (CNI 2012).
Following, we highlight some of the solutions
for sustainability that have already been employed.
Vinasse, an effluent from ethanol production,
is sent back to the cane field, thus making use of its
fertilizing and salvage irrigation qualities and
eliminating its potential polluting potential when
discarded into water courses;
Concentrated vinasse, which enables its
application in more distant crops, eliminating the use
of sacrificial areas near the mill and the consequential
risk of becoming saturated with salts that would
ultimately contaminate the groundwater.
The use of process residues as fertilizers, such
as boiler ashes and soot, and filter cake, replace
chemical fertilizers and prevent them to become
polluting agents; and
Reduced water consumption in the industry,
which has been obtained over the years, is a major goal
of new projects currently. Table 4 next illustrates such
evolution, and it is worth noting that some mills
already have achieved better results, lower than l tonne
of water/tonne of cane.
Table 4: Evolution of water consumption in the mills
a) Better rates of “clean energy output” per
”fossil energy input” are the result of the increasingly
use of bagasse and straw to produce bioelectricity,
raising the rates from 7 to over 10. (CNI 2012; Seabra
and Macedo, 2008).
But in order that “sustainability increase”
could be considered a driver, the development of a
systemic approach was necessary, which would be used
to produce sustainable projects.
As a result, to meet the new world demands
for sustained solutions in the economic, environmental,
and social aspects, Dedini has developed the DSM –
Dedini Sustainable Mill (Olivério et al., 2010a). It is a
product in continuous development and was
commercially available in 2008 in its first commercial
stage.
The innovative feature of DSM is that it is a
physical system, comprising of, for example, machines,
tubes, tanks, and sustainability is more evident in the
operational management. The question then is: How
can a set of physical items contribute to sustainability?
This question is briefly answered in Figure 29, that also
describes the concepts of “increased sustainability” as
employed in the DSM design.
What is DSM – Dedini Sustainable Mill? The
following text explains what is DSM, considering a
higher focus on environmental issues, for simplification
reasons.
To conceive the DSM, the mill needed to be
seen as a “macro-machine”, designed to meet the
optimum criteria of sustainability, with emphasis on
the environment. Therefore, DSM was conceived to
enhance the environmental qualities of ethanol without
neglecting the business economic results and social
aspects.
In the DSM, developed technologies enable
the production of 6 bioproducts: biosugar, bioethanol,
bioelectricity, biodiesel, biofertilizer and biowater in a
single, integrated design, aiming to minimize emissions
while maximizing the contribution of sugarcane
ethanol to the mitigation of GHG-greenhouse gases.
The DSM can be implemented gradually, as it is the
case of the Barralcoool Mill in Barra do Bugres, MT,
which has been producing the first 4 Bios since 2006,
with a pioneering biodiesel plant supplied by Dedini
and integrated to the mill (Figure 38).
If you compare the DSM with a traditional
mill, you will find the following benefits:
Typical intake water consumption to produce ethanol
Year m³ water/t canel water
/l ethanol(4)
1975(3) 15.00 187
1990(1) 5.60 70
1997(2) 5.07 63
2005(3) 1.83 23
(1) PERH – Plano Estadual de Recursos Hídricos (State Plan for Water
Resources), 1994/95
(2) CTC – Research with 34 mills in São Paulo State, 1997
(3) CTC/Unica – 2005
(4) Assuming 80 litres ethanol/t cane
NOTE: Some mills consumption < 1m3 water/t cane
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b) It optimises the production processes by
increasing yields and efficiencies and allowing the
maximum production of biosugar and bioethanol per
tonne of cane. Therefore, much more gasoline can be
replaced by ethanol, thus reducing GHG emissions even
further;
c) It optimises the use of the sugarcane energy
by producing the maximum bioelectricity to be
supplied to the grid, also by using sugarcane “straw” as
a source of energy. With a greater supply of energy
from renewable sources, the use of fossil fuels can be
avoided, thus diminishing emissions;
d) It includes the integrated production of
biodiesel in the mill with agricultural integration (e.g.,
soybean production in rotation with sugarcane) and
industrial integration (biodiesel plant added to the mill,
with the use of vegetable oil from soybean and the
renewable bioenergy from bagasse and bioethanol, thus
enabling a 100% green biodiesel, in substitution for
methanol from fossil origin, which is traditionally used
as the second feedstock). So, ethyl biodiesel is
produced to fuel the crop fleet and to be sold to third
parties as a new business, in both cases replacing fossil
diesel and avoiding emissions;
e) It uses all process wastes as feedstock for
the production of BIOFOM – Organomineral
biofertilizer, which replaces at least 70% of the
chemical fertilizers and also contributes to mitigate
emissions;
f) The mill becomes water self-sufficient,
using, saving and recycling only the water contained in
the sugarcane and without requiring water uptake from
natural sources, also producing surplus water to be
exported: the biowater. It should be noted that a typical
mill requires 23 litres of water per litre of ethanol
produced, while the DSM exports 3.7 litres.
g) The DSM incorporates the most advanced
concepts of occupational hygiene and safety.
Considering all items mentioned above, higher
economic results would be obtained, as well as an
optimised accomplishment of the three sustainability
pillars: economic, social and environmental.
As a final result, the DSM attains two
concepts: optimisation and zero concepts. In the
optimization concept, the goal is to use the minimal
amount of feedstock and inputs to obtain maximum
products per tonne of cane: maximum biosugar,
bioethanol, bioelectricity, and integrated biodiesel
production. The DSM also meets the zero concept,
whereby the goal is the zero use and zero
contamination of the natural resources and maximum
environmental preservation, allowing: zero wastes /
Fig. 29 – Sustainable development characteristics of the DSM - Dedini Sustainable Mill
ENVIRONMENTAL
DSM solutions include the
commitment of not wasting (also
minimizing consumption) and not
polluting the environment and
the natural resources, mainly air,
water, energy, materials/raw
materials, biodiversity, and
minimum or zero generation of
emissions, effluents, residues,
and odors.
DSM complies with the standards
and regulations, reducing/
eliminating environmental
impacts, and contributes to
agricultural sustainability
DSM contributes to, and makes it
easier, the management system
ISO 14001
ECONOMIC
DSM is competitive in a free
market, without subsidies
SOCIAL In DSM, the equipment, processes,
materials, installations need to be located, to move, to operate,complying with the best practices and regulations to provide comfort hygienic and safe conditions, and good health in the workplace
Using ergonomics concepts, DSM provides appropriate man-machine interactions, requiring minimum physical efforts from workers.
DSM uses automation through integrated and intelligent software, MES level, linked and integrated to ERP System
DSM contributes and makes it easier the management system SA 8000
DSM - DEDINI SUSTAINABLE MILL
DRIVER: SUSTAINABILITY INCREASE
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zero effluents / zero odors / zero water from natural
sources /minimum CO2 emissions. It is noteworthy
that the bioethanol produced by the DSM has a
mitigating greenhouse effect as significant as 112% (132%
when using 50% of the straw as energy source), while
the ethanol produced by the traditional mill represents
89% of mitigation (Olivério et al., 2010a). Finally, the
DSM enhances the sustainability of the sugarcane
industry and may contribute significantly to the
mitigation of climate changes caused by the global
warming.
The DSM is the result of the integration of
various technologies under the focus of sustainability,
some of them developed by DEDINI itself or with
partnerships, resulting in eleven patent applications,
eight filed by Dedini, some of them already granted.
Figure 30 is a schematic representation of DSM
Fig. 30 – DSM – Dedini Sustainable Mill: The 6 Bio-Products, the optimisation and zero concepts, and maximum mitigation effect on GHG
Most of the technologies used in DSM design
are presented in this study, including solutions for
maximum biosugar, bioethanol, and bioelectricity
production. For biodiesel production integrated to the
mill, some information will be provided later in this
study, and more details can be found in (Olivério et al.
2007).
With respect to biowater and Biofom,
following Figures 31, 32, 33 and 34 summarize the
information relating to the production of these by-
products.
As references for biowater, we cite (Olivério et
al. 2010a, 2010d), and for Biofom (Olivério et al. 2010e).
Fig. 31 – Trend: increased sustainability – reduced water consumption in water self-sufficient mill design.
Fig. 32 – Trend: increased sustainability – The Biowater Production Mill.
Fig. 33 - Trend: increased sustainability – elimination of effluents and residues via Biofom production process.
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Fig. 34 - Trend: increased sustainability – agricultural evaluation of Biofom as a proven organic biofertilizer.
Figure 35 presents an option that is being
analysed in Brazil: to process sweet sorghum at the
sugarcane mill. Sweet sorghum is produced integrated
and in rotation with sugarcane, allowing diverse
feedstock processing, longer operation crop period,
increasing bioethanol and bioelectricity production, so,
contributing to a better return on sugarcane plant
investment.
Fig. 35 – Trend: Increased sustainability by processing sweet sorghum at the existing sugar cane mill. (Gurgel,2010)
Driver 4: Synergy and integration
The sucro-energy mills and the respective crop
areas are extremely favorable to synergy and
integration.
Some practices currently in use in Brazil are
clear evidences of this trend: intercropping of sugarcane
with other cultures in crop rotation systems, in
renovation lands, which benefit both cultures; the
energy surplus that cane provides attracts other
industries to the mill’s proximity.
Figure 36 illustrates the integrations that can
be accomplished. Having as core elements the land,
human, physical, and financial resources, as well as
systems and management, integration in the sugarcane
mill takes place in the farm, in the industry, in
management/business, and leads to economic, energy
and process integration.
Fig. 36 – Trend: synergy and integration – different solutions available at the sugarcane agribusiness.
Figures 37, 38 and 39 illustrate three real cases
of synergy and integration, of which Santa Vitória mill
is in the stage of design/implementation.
Fig. 37 – Trend: synergy and integration – Ethanol and energy mill (steam, bioelectricity); energy supplied to an edible oil producing plant near the mill (energy integration of two plants) – Coamo Mill.
ECONOMIC
INTEGRATION
ENERGY
INTEGRATION
FARM INTEGRATION
(CROP)
INDUSTRY
INTEGRATION
(MILL)
PROCESS
INTEGRATION
BUSINESS/
MANAGEMENT
RESOURCES
LAND
HUMAN
PHYSICAL
FINANCIAL
SYSTEMS
MANAGEMENT
DRIVER: SYNERGY AND INTEGRATION
ENERGY INTEGRATION IS AN OLD TOPIC
IN SUGARCANE AGRIBUSINESS
ETHANOL-AND-ENERGY PRODUCING UNIT (BIOETHANOL MILL)
1985 - DESTILARIA COAMO - CAMPO MOURÃO-PR-BRAZIL – DEDINI TURN-KEY SUPPLY
EDIBLE OIL PLANT
3 000 KVA
RECEPTIONPREPARAT./
EXTRACTIONBIOETHANOL PROCESS Bioethanol
Stillage
ELECTRICITY
GENERATION
STEAM GENERATION
BOILER: 30 BAR/350º C
Bagasse
BIOETHANOL MILL
2 500 KVA
CANE
JUICE
Electrical Power
3 000 KVA
Steam Process
DRIVER: SYNERGY AND INTEGRATION
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Fig. 39 – Trend: synergy and integration – bioetha-nol/bioenergy (steam, bioelectricity) mill x linear biopolyethylene plant integration – Santa Vitória Project.
Let’s examine the integration of biodiesel
production in the sucro-energy mill as represented in
Figure 38 (Olivério et al., 2007).
In the agricultural sector, know-how for
oleaginous grains production in rotation to sugarcane
crops is already available. A traditional practice is the
cultivation of soybean in areas of sugarcane renovation,
after 4-5 cuts. Such practice maximizes land
productivity with optimum and profitable use of the
land. It also breaks the cycle of pests and diseases and
contributes to recover the soil fertility; from soybean
can be extracted the oil to be used as feedstock for
biodiesel production.
Another synergy that benefits integration is
the shared use of farming and industrial infrastructure
and resources, allowing cost savings, optimised use of
facilities, and less investment. This includes tractors,
harvesters, trucks, machinery, agricultural implements,
steam, co-generated electrical power, water, integrated
solutions for wastewaters, agricultural and industrial
manpower, and shared use of plants, facilities and
support services. An important integration is the use of
three products from the sugarcane mill as inputs for the
biodiesel plant: anhydrous bioethanol (as the second
feedstock; the first is vegetable oil), bioelectricity and
steam. The surplus bioethanol with water, which
derives from biodiesel production, as can be seen in
Figure 38, is reprocessed in the distillery already
available at the mill and, after dehydration, bioethanol
is sent back to the biodiesel process.
The biodiesel produced can fuel the vehicles
used in the production of sugarcane and the oleaginous
grains.
Regarding management and businesses, there
are some synergies and advantages that we can point
out: a new market is created for anhydrous bioethanol
(currently methanol is used as the second feedstock),
the increase of income/profits from the new products,
PRODUCTS AND ENERGY INTEGRATION
GREEN PROJECT – DOW/MITSUI - SANTA VITÓRIA PROJECT (MG)
LINEAR
BIOPOLYETHYLENEBIOETHYLENE
STEAM ELECTRICITYETHANOL STEAM ELECTRICITYETHANOL
CANE CANE
350.000 T/YEAR
LINEAR BIOPOLYETHYLENE
6 mi to 8 mi TCC
BIOETHANOL MILL BIOETHANOL MILL
DRIVER: SYNERGY AND INTEGRATION
Biodiesel Plant integrated to Barralcool MillBarralcool Mill
AGRICULTURAL AND INDUSTRIAL INTEGRATION ( ENERGY + PRODUCTS + PROCESSES) INTEGRATION
1st GENERATION 4 BIOS MILL – BIODIESEL PRODUCTION INTEGRATED TO A SUCROENERGY MILL
Sugarcane Farm/ Refurbished Area
DEHYDRATED BIOETHANOL IN EXCESS
BIOENERGY
BIODIESEL/GLYCERINE
SOLD TO THE MARKET
SOYA OIL
DEDINI: INTRODUCTION OF THE CONCEPT TO THE WORLD MARKET AND
FIRST WORLD SUPPLY/ 1st WORLD CONTINUOUS ETHYLIC PROCESS PLANT
BARRALCOOL MILL: 1st MILL IN THE WORLD PRODUCING THE 3 BIOs:
BIOETHANOL, BIOELECTRICITY AND BIODIESEL,
PLUS BIOSUGAR = 4 BIOs MILL
BIO
DIE
SE
L -
US
ED
AT
TH
E FA
RM
This driver “Synergy and Integration” has positive effect on CAPEX, OPEX,
management/business fixed and logistic costs
DRIVER: SYNERGY AND INTEGRATION
SURPLUS BIOETHANOL + WATER
Fig. 38 – Trend: synergy and integration – Synergies between bioethanol/bioelectricity and biodiesel processes – farm, business/management, industry (process, energy), economic integrations – Barralcool Mill integrated to a biodiesel plant.
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biodiesel and glycerin, which also helps to dilute
market risks.
Biodiesel commercialization will make use of
the experience and expertise developed in the
bioethanol business, and will be made with the same
clients. The operational structure and management
systems can be shared.
When using biodiesel in the mill vehicles, the
fuel is exempt of tax, so it costs less (for being own
production), and replaces diesel, which is taxable fuel.
The Coamo Mill Figure 37 presents energy,
economic, management/business integration (Olivério
and Ribeiro, 2006), which is also seen in Dow/ Mitsui
Santa Vitoria Project, Figure 39. In addition, the
intermediate product from the latter, bioethanol, is the
feedstock for biopolymer, the end product of the
project, i.e., linear bio-polyethylene (Dow 2012), defined
as the biggest biopolymer integrated plant in the world.
It is worth noting that this driver, synergy and
integration, has a positive impact on both OPEX and
CAPEX, as well as on management and business,
including a possible reduction of fixed and logistic
costs.
Driver 5: Higher value-added prod-ucts from sugarcane and the sugar-cane mill
Today, sugarcane is processed predominantly
into three end products: sugar, ethanol, and bagasse
and bioelectricity. However, as it is a biomass
consisting of organic components, it can be the raw
material for a large number of products. Sugarcane is
basically constituted of Carbon, Hydrogen and Oxigen,
which, after been broken down and then recombined
via chemical reactions, may generate an almost infinite
variety of compounds.
But we need not go that far: in sugarcane juice,
we can find several types of sugar; in bagasse and straw,
several cellulosic and lignocellulosic materials. For
these tree inputs there already exist numerous
chemical, physical, and biological processes and their
combinations, which may be used to obtain products,
many of them with high economic value.
With the advancements of science and
technology, new processes have been introduced for
this purpose. Most of the products obtained mainly
from non-renewable fossil materials can be produced
from biomass.
As technological advancements promote cost
savings, bioproducts become more competitive, and on
this logic is based the use of cane to produce them. As a
result, the sugarcane mill design will be changed
accordingly, so that new processes, equipment, and
plants can make such new products.
This is a more sophisticated way to produce
higher value-added products from sugarcane. And we
can already find numerous examples, new real cases in
Brazil, in which the mills have promoted upgrades in
this direction.
Another way, more simple, is the processing of
cane products and by-products into higher value-added
products, by means of additional process stages.
Figures 40 and 41 are examples: Figure 40 presents an
“upgraded yeast” production plant integrated to a mill,
and Figure 41, refined sugar can be produced directly by
the mill using traditional processes (production of raw
sugar and, from this, refined sugar) or by incorporating
a new technology (production of refined sugar directly
from the juice in a single crystallization step, Olivério
and Boscariol, 2006). In Figure 42, a sodium
bicarbonate plant (having CO2 from fermentation as
feedstock) is integrated into the ethanol mill (Olivério
et al., 2010a).
Figure 43 also illustrates this new greenfields
development trend: a larger amount of products to be
made in the future mills, consisting of higher value-
added products serving profitable market niches. The
example in Figure 39 also illustrates this trend driver,
the production of linear bio-polyethylene production
using ethanol as a feedstock.
Fig. 40 – Trend: higher value-added products – use of sugarcane juice as a feedstock to produce large amounts of upgraded yeast for animal feed (export market) – Biomass to Animal Feed Plant integrated to Vale do Ivai Mill.
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Fig. 41 – Trend: Higher value added Products – Refined sugar production integrated to a sugar mill using different feedstocks: raw sugar (Vale do Paranaiba) and sugarcane juice (DRD-Dedini Direct Refined)
Fig. 42 – Trend: Higher value-added products – “green” sodium bicarbonate production using CO2 from fer-mentation as feedstock, integrated to São Carlos do Ivai Mill.
Fig. 43 – Trend: Higher value-added products –higher value bioproducts integrated to a sugarcane mill, using sugarcane components as a feedstock – the sugarcane mill will become a biorefinery.
Regarding Figure 43, there are many projects
being implemented in Brazil:
▪ In a joint venture between Amyris and the São
Martinho Group, a farnesene plant using sugar
as feedstock is being added to the São Martinho
mill (Amyris, 2012);
▪ Amyris has also partnered Paraiso mill to
produce farnesene by means of a plant
integrated to the mill (Amyris, 2012);
▪ PHB Industrial, a joint venture between Pedra
Agro Industrial and Balbo Goup, is expanding
the biodegradable plastic plant integrated to the
Usina da Pedra mill (Biocycle 2012);
▪ Granbio is integrating a 2nd
generation ethanol
plant in Usina Caeté, using bagasse as feedstock
(Graalbio, 2012);
▪ Many international companies that are investing
in the Brazilian sucro-energy sector as well as
some traditional businessman announced
partnership and investment with technological
bio-based chemistry companies, declaring future
plans to integrate new plants into a sugarcane
mill to produce bio-products from sugarcane:
Bunge and Solozyme, Rhodia and Cobalt,
Butamax a joint venture between BP and
DuPont, Total and Amyris, JB (Brazilian
Sugarcane Mill Group) and SAT (anon, 2012).
▪ Many mill groups in partnership with diverse
technology-based companies, were selected by
Brazilian Development Bank – BNDES and
Engineering and Technology Development
Agency - FINEP to be considered to be granted
with prime financing credit lines to develop new
technological routes for the production of new
bio-products, as well as second-generation
ethanol (based on enzymatic cellulose
hydrolysis) and third-generation biofuels/bio-
products (BTL - Biomass to Liquid
technologies), comprising bagasse/straw
gasification for synthesis gas production, which
in a Fischer-Tropsch type reactors are converted
into synthesis bio-products (PAISS, 2012).
All these projects, already underway in Brazil,
allow us to conclude that the BIOREFINERY integrated
to the SUGAR MILL, will be, or rather already is, a
REALITY.
DRIVER: HIGHER VALUE ADDED PRODUCTS FROM SUGARCANE AND SUGARCANE MILL
Some companies are in early commercial or in advanced stage of development: (1) Amyris, (2) Braskem, (3) PHB Industrial, (4) Rhodia, (5) GranBio
Different kind of fuels and several types of chemical specialties can be produced
from the above feedstocks, through specific fermentation processes and physical-
chemical complementary treatments.
Fuel as renewable diesel oil (1)
Jet Fuels (1)
Lubricant oils (1)
Cosmetic products (1)
Aromatics and flavors (1)
Butyl Alcohol (2)
Solvents (2)
Biodegradable Plastics (3)
Polypropylene (4)
2nd and 3rd generation products (5)
Feedstock: Sugarcane Juice, Concentrated Juice, Syrup, Sugar, Bioethanol,
Bagasse, Straw.
New technologies will be integrated to the Sugarcane Mill towards a
Biorefinery, producing higher value added products
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The new “greenfields” and the sug-
arcane mill equipment industry
The Brazilian sucro-energy industry will be in
considerable expansion, with projections of 120 “future
greenfields mills”, and doubling the processing
capacity.
This work aimed to show that such future
expansion has a large number of solutions already
underway, which means that solutions are ready to be
used in the new configurations of the “future mills”.
In order to contribute to this discussions,
aiming to foresee the trends in conceptual design of the
“future mills”, in this paper we propose a model using
five drivers that will define the evolution trends
regarding products, capacities and technologies, from
the view of the equipment industry.
As a consequence, an important question now
arises: is the equipment industry ready and able to meet
such huge expansion, not only in Brazil, but worldwide
speaking?
We know that until now the equipment
industry has succeeded in responding accordingly to
the growth of the sucro-energy business. In ProAlcohol
period, more than 300 ethanol mills were installed in 10
years (Olivério 2007), and recently 117 “new mills”
started operations.
The expansion already attained, from 68
million tonnes (1975/76) to 620 million tonnes of
processed sugarcane per crop (2010/11), was fully
achieved by the equipment industry, with almost 100%
own development and supply.
But this is the picture of the past. And what
about the future?
For a secure and reliable response, we should
review again the respective “capability” and
“competitiveness” of the equipment industry in the
light of the new challenges.
We understand that in this case “capability”
means “to meet the market needs”, i.e., to fulfill the
technological needs, having industrial, manufacturing,
and financial capabilities as well as guarantees.
Likewise, as “competitiveness” we understand
“to meet the clients’ needs”, i.e., the industry should
offer quality, delivery times and prices competitively,
according to the client’s requirements.
Taking into account the past accomplishments
and the most recent supplies, conclusion is that the
equipment industry has the necessary capabilities and
competitiveness to fully meet the market and the
clients’ demands. Figure 44 summarizes these
conclusions.
Fig. 44 – Evaluation of the equipment industry “capabil-ity” and “competitiveness” to meet the heavy expansion of the sugarcane agribusiness.
This work aimed to show that such future expansion
has solutions already underway, and that there are
processes, equipment, and plants, that means, solutions
ready to be used in the new configuration of the “future
mills”.
Our conclusion is that the equipment industry
is prepared to serve the future with updated and
innovative technologies, adequate supply capacity, and
competitive quality, delivery time, and prices.
Finally, this is a challenge that the equipment
industry accepts and is ready to meet.
THE NEW “GREENFIELDS” AND THE SUGARCANE MILL
EQUIPMENT INDUSTRY
CAPABILITY COMPETITIVENESS
ATTEND TO THE
MARKET NEEDS
ATTEND TO THE
CLIENTS NEEDS
CAPABILITY
TECHNOLOGICAL
INDUSTRIAL/MANUFACTURING
FINANCIAL/GUARANTEE
COMPETITIVENESS
QUALITY
DELIVERY TIME
PRICE
IS THE EQUIPMENT INDUSTRY PREPARED AND ABLE TO ATTEND THE NEEDED HEAVY
EXPANSION ON SUGARCANE AGRIBUSINESS?
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