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CONFERENCE COMMITTEE
Coordinator : Yandra Arkeman, Dr. M.Eng
(Departement of Agroindustrial Technology, IPB)
Co-Coordinator: Nastiti Siswi Indrasti, Prof. Dr. Ir.
(Head of Departemen of Agroindustrial Technology, IPB)
International Experts:
1. Kenneth De Jong, Prof.
(George Mason University, Fairfax, Virginia, USA)
2. Kim Bryceson, Prof.
(School of Agriculture and Food Science , University of Queensland, Australia)
3. Haruhiro Fujita, Prof.
(Department of Information Systems, Niigata University for International and
Information Studies Japan)
4. Gajendran Kandamsany, Dr. (United Kingdom)
5. Noel Lindsay, Prof. (University of Adelaide, Australia)
Committee Members from IPB:
1. Kudang Boro Seminar, Prof.
(Departement of Mechanical & Bio-system Engineering, IPB)
2. Marimin, Prof.
(Departement of Agroindustrial Technology, IPB)
3. Endang Gumbira Said, Prof.
(Departement of Agroindustrial Technology, IPB)
4. Suprihatin, Prof.
(Secretary of Departement of Agroindustrial Technology, IPB)
5. Ono Suparno, Prof.
(Departement of Agroindustrial Technology, IPB)
6. Agus Buono, Dr.
(Head of Department of Computer Science, IPB)
PROCEEDINGS
2nd
International Conference on Adaptive and Intelligent Agroindustry (ICAIA)
September 16 – 17, 2013, IPB International Convention Center
Bogor – Indonesia
Organized by :
Departement of Agroindustrial Technology, Faculty of Agricultural Engineering and
Technology Bogor Agricultural University
George Mason University, Fairfax, Virginia, USA
Indonesian Agroindustry Association (AGRIN)
Bogor, Desember 2013
Frekwensi Terbitan : 1 Tahunan
Nomor ISSN : 2354-9041
i
WELCOMING ADDRESS
Prof. Dr. Ir. Nastiti Siswi Indrasti
Head of Agroindustrial Technology Department
Faculty of Agricultural Engineering and Technology
Bogor Agricultural University
On
Second International Conference on Adaptive and Intelligence Agroindustry (2nd
ICAIA)
Bogor, September, 16 – 17, 2013
Assalamu’alaikum Warohmatullahi Wabarokatuh
In the name of Allah, the beneficent and the merciful,
Distinguish Guest, Ladies and Gentlemen
Let me first thank you all for accepting the invitation to participate in this 2nd
International Conference on
Adaptive and Intelligence Agroindustry (ICAIA). In particular I would like to thank Rector of IPB (Institut
Pertanian Bogor/Bogor Agricultural University) Prof. Herry Suhardiyanto for supporting this event as part
of the series academic event in celebrating the 50th
Anniversary of Bogor Agricultural University.
In fact, the idea of organizing this conference was the continuation of the International Workshop on
Computational Intelligence and Supercomputing Technology for Adaptive Agroindustry held by the
Department of Agroindustrial Technology, Bogor Agricultural University last year.
Professor Kenneth A De Jong from George Mason University, US has successfully conducted joint
international research with some staff from the Department of Agroindustrial Technology and Department
of Computer Science, Bogor Agricultural University. The research aims to develop an integrated and
intelligent system (namely SMART-TIN©) for the design of adaptive agroindustrial system in order to
achieve a sustainable agroindustry that can mitigate global climate change and at the same time secure food,
water, energy and natural medicine supply.
We are certainly proud to have been able to assemble this event in IPB, Bogor. The range of participants
and audience at this conference is precisely something I would like to stress. The main goal of the
conference is to provide an effective forum for distinguished speakers, academicians, professional and
practitioners coming from universities, research institutions, government agencies and industries to share or
exchange their ideas, experience and recent progress in Adaptive and Intelligent Agroindustry.
Distinguish Guest, Ladies and Gentlement,
Global climate change is the most challenging problems for us today and in the near future. This global
change in our climate can lead to the shortage of the food, water, bioenergy and natural medicine that will
affect the quality of human life. Many studies indicate that the threat of food, water, bioenergy and natural
medicine crisis due to global climate change still worries our society. This problem can be solved by the
development of agroindustry, i.e. an interrelated value chain entities from farming, to agro-processing
industry and then to the end-customers. In fact, the design of agroindustry is complex and involves many
factors and large data bases and more importantly, needs a good intelligence to process data and
information to good decisions. Therefore, the way to design and manage agroindustry should be improved
in order to meet the design objectives.
Agroindustries consume quite significant amount of energy on one side, on the other side they generate
sizable amount of industrial wastes and its utilization as a captive energy resource is a kind of potential.
Based on our study, a plywood industry with the production capacity of 200.000 m3
/year could generate 32
percentage of solid waste. If this amount of waste used as an energy alternative, it may result on the saving
of 131.037.768.597 rupiah per month. Similar to plywood industry, sugarcane industry with the production
capacity of 480 ton per hour could generate 154 ton per hour of waste (bagasse) and this amount of waste
contribute to the saving of energy consuming by 19.250 Kwh. Recent study we conducted, indicated that
cassava starch industry may contribute to a significant amount of waste. It has also potential usage as an
energy resource. Based on our study the conversion of its waste into energy will contribute to the saving of
energy usage of 4100 liter biogas per ton material.
The three industries mentioned is only examples of how potential the role of agroindustrial waste as an
alternative resource in replacing the conventional energy resource as its presence will be significantly
ii
reduced. The new, incremental energy contributions that can be obtained from waste biomass will depend
on future government policies, on the rates of fossils fuel depletion, and on extrinsic and intrinsic economic
factors, as well as the availability of specific residues in areas where they can be collected and utilized. All
of these factors should be in detail examined to evaluate the development of the industrial waste
contribution. Hope this conference will also discuss this issue in more detail as it is an important matter for
all of us. We should no more think just how to produce high value product but it is also necessarily
important how to keep our live in good quality by understanding following old saying…” only when the
last tree has been cut, only when the last fish has been angled, and only when the last river has been
polluted, then we realized that we could not eat money”.
I do not to take up any more of your time with these opening remarks. Let me simply thank you once again
for sharing your thoughts with us. Here’s wishing every success for the conference. May Allah bless all of
us.
Thank you for your kind attention,
Wassalamu’alaikum Warohmatullahi Wabarokatuh
iii
AGENDA of
2nd
International Conference on Adaptive and Intelligent Agroindustry
(ICAIA)
Time Activities Room
Day 1 (16 September 2013)
08.00 – 09.00
(60’)
Registration
09.00 – 10.00
(60’)
Opening Ceremony
 Welcoming Address: Prof. NastitiSiswiIndrasti (Head of Dept TIN,
Fateta, IPB)
 Conference Opening: Prof. HerrySuhardiyanto(Rector of IPB)
o ABET Certification announcement and short ceremony
o Launching International Double Degree Master Program in
Innovation and Technopreneurship in Cooperation with University
of Adelaide, Australia
o Soft-launching Master in Logistik Agroindustri (Agroindustrial
Logistics)
Ballroom
10.00 – 10.45
(45’)
Opening Speeches:
Prof. IrawadiJamaran (Agroindustry Guru, IPB: 25’)
Prof. Eriyatno (Industrial and System Engineering, IPB: 20’)
Ballroom
Session 1
10.45 – 11.15
(30’)
Keynote Speech Dr. YandraArkeman (IPB) Ballroom
11.15 – 12.00
(45’)
Keynote Speech Prof. Kenneth De Jong (George Mason University, USA) Ballroom
12.00 – 13.30
(90’)
Lunch Break
Session 2
13.30 – 15.15
(105’)
Moderator: Prof. EndangGumbiraSa’id (IPB)
Invited Speakers (1-4) (4 x 20 minutes)
Discussion (25 minutes)
Tentative Schedule: Prof. Kim Bryceson (Australia), Prof. SyamsulMa’arif
(IPB), Prof. KudangBoro Seminar (IPB), Prof. HaruhiroFujita (Japan)
Ballroom
15.15 – 15.45
(30’)
Break
15.45 – 17.30
(105’)
Moderator: Prof. Marimin (IPB)
Invited Speakers (5-8) (4 x 20 minutes)
Discussion (25 minutes)
Tentative Schedule: Dr. Gajendran (UK), Prof. Noel Lindsay (University of
Adelaide), Dr. KuncoroHartoWidodo (UGM), Prof. UtomoSarjonoPutro (ITB)
Ballroom
Day 2 (17 September 2013)
08.00 – 08.30
(30’)
Registration
08.30 – 10.15
(105’)
Moderator: Prof. KudangBoro Seminar (IPB)
Invited Speakers (9-12) (4 x 20 minutes)
Discussion (25 minutes)
Prof. Egum (IPB), Prof. Marimin (IPB), Dr. AgusBuono (IPB), Dr. HeruSukoco (IPB)
10.15 – 10.30
(15’)
Coffee Break
10.30 – 12.30
(120’)
Parallel Session 1
Moderator: Prof.
Fujita
(7 paper @ 15
minutes)
Discussion (15
minutes)
Parallel Session 2
Moderator: Prof. Ono Suparno
(7 paper @ 15 minutes)
Discussion (15 minutes)
Parallel Session
Moderator: Prof. Suprihatin
(7 paper @ 15 minutes)
Discussion (15 minutes)
iv
12.30 – 13.30
(60’)
Lunch Break
13.30 – 15.00
(90’)
Open Discussion (Open Forum) with Prof. Kenneth De Jong
Topic: Foundations and Applications of Genetic/Evolutionary Algorithms
Ballroom
15.00 – 15.30
(30’)
Conference Closing Ballroom
15.30 – 17.00
(90’)
Indonesian Agroindustry Association (AGRIN) National Congress
(PIC: Prof. Suprihatin)
Ballroom
17.00 – 17.45
(45’)
Refreshment and Closing of AGRIN National Congress Ballroom
v
CONTENT LIST
Conference Committee
Welcoming Address ….………………………………………………….…………….................. i
Agenda of 2nd
ICAIA 2013.............................................................................................................. iii
Content List …………..………………………………………………......……………................. v
A.  SMART-TIN© : An Integrated And Intelligent System For The Design Of
Adaptive Agroindustry (A Conceptual Framework) (Yandra Arkeman)
1‐9.
B.  GHG  Emission  Reduction  By  Waste  Cooking  Oil  Recycling  In  Environmental 
Partnership  Program  Of  Bogor  City  (Haruhiro  Fujita,  Atsushi  Yoshimoto, 
Katsuyuki Nakano,  Koji Okuhara, Noriaki Koide, Dadang Supriatna) 
10‐16.
C.  Challenge  of  Indonesian  Logistics  Infrastructure  for  Perishables  Products 
(Kuncoro Hartoto Widodo, Yandra Rahardian Perdana, Joewono Soemardjito) 
17‐28.
D.  Design Of Grouping Traditional Market  Distribution Using  Fuzzy Clustering And 
Design  of  Routing  of  Packaging  Cooking  Oil  From  Distribution  Center  To 
Traditional Market  Using Traveling Salesperson Problem– Genetic Algorithm in 
Indonesia  (Case‐Jakarta)  (Teja  Primawati  Utami,  Syamsul  Maarif,  Yandra 
Arkeman, Liesbetini Hartoto) 
29‐43.
E.  Determining the degree of product rightness at the conceptual stage:A Case of 
the Low Cost Green Car (Ade Febransyah, Fransisca Tharia) 
44‐53.
F.  Co‐Composting Process Of Bagasse And Sludge From Sugarcane  Industry With 
Influence Of Difference Initial C/N Value And Aeration (Andes Ismayana, Nastiti 
Siswi Indrasti, Tori Sane) 
54‐62.
G.  Analysis Of The Competitiveness Of The Agribusiness Sector Companies Using 
Porter's Five Forces (M. Hudori) 
63‐72.
H.  Design  And  Optimization  Of  Agro‐Scm  For  Food  And  Energy  Security  In 
Indonesia (Hoetomo Lembito, Kudang Boro Seminar, Nunung Kusnadi, Yandra 
Arkeman) 
73‐83.
I.  Construction Of Patchouli Oil’s Price In West Java : A Structural Equation Model 
(Isti Surjandari, Alan Dwi Wibowo, Erlinda Muslim, Nurwan Nugraha) 
84‐90.
J.  Optimization Vehicle Routing Problem With Cross Entropy Method And Branch 
& Bound Algorithm (Iwan Aang Soenardi, Budi Marpaung) 
91‐99.
K.  Design  And  Optimization  Of  Agro‐Scm  For  Food  And  Energy  A  Remote 
Monitoring System Of Broilers’ Behavior In A Multi‐Agent Broiler Closed House 
System (K.B. Seminar, R. Afnan, M. Solahudin, Supriyanto, A.K. Wijayanto, M.Z. 
Arifin, A. Fatikunnada) 
100‐112.
L.  Artificial Neural Network Model Based Capacitance Dielectric For Crackers Self‐
Life  Prediction  (Erna  Rusliana  Muhamaad  Saleh,  Erliza  Noor,  Taufik  Djatna, 
Irzaman) 
113‐121.
M.  Characterizing  Temporal  Dynamic  Of  Weather  Variability  To  Support  Decision 
Making  On  Weed  Control  (Rizky  Mulya  Sampurno,  Kudang  B.  Seminar,  Yuli 
Suharnoto, Mohamad Solahudin) 
122‐130.
vi
N.  Risk  Management  Model  in  Dairy  Product  Transportation  With  Fuzzy  Logic 
Approach (Winnie Septiani, Yandra Arkeman) 
131‐141.
O.  Strategy  to  Increase  Institutional  Capacity  of  Farmer  Groups  to  Support  the 
Transportation System Agroindustry Products (Zulfiandri, Yandra Arkeman) 
142‐156.
P.  Adsorption Of Carotenoid From Palm Oil Methyl Ester By Using Attapulgite And 
Synthetic Silica Magnesium As Adsorbent (Sapta Raharja, Prayoga Suryadarma, 
Zuni Fitriyantini) 
157‐163.
Q.  High Accuracy Agroindustry Environment Monitoring System Based on Photonic 
Crystal Sensor Network (Mamat Rahmat, Muhamad Azis, Erus Rustami, Wenny 
Maulina, Kudang Boro Seminar, Arief Sabdo Yuwono, Husin Alatas) 
164‐174.
R.  Study  on  Effect  ofTemperatureIncrease  on  the  Productivity  of  Methanefrom 
POME Fermentation (Sarono, E. Gumbira Said, Ono Suparno, Suprihatin, Udin 
Hasanudin) 
175‐180.
S.  The Design and Implementation of Geographic Information Systems to Support 
Food  and  Energy  Security  (Arif  Purnomo  Muji  Basuki,  Yandra  Arkeman, 
Musthofa) 
181‐191.
T.  Study Of White Crystal Sugar Distribution System In Indonesia (Suripto, Yandra 
Arkeman) 
192‐199.
U.  Corncob  Biodelignification  Process  Using  White  Rot  Fungi  (Liesbetini  Hartoto, 
Purwoko, Elis Nina Herliyana, Cucu Rina Purwaningrum) 
200‐212. 
V.  Color  Stability  of  Beet  Dyes  Label  During  Heating    (Endang  Warsiki,  Asih 
Setiautami) 
213‐219.
W  Precipitation  Classification  Using  LVQ  on  Dry  Season  Base  on  Global  Climate 
Indices Case Study in Indramayu District (Indra Kelana Jaya, Agus Buono, Yandra 
Arkeman) 
220‐225.
X.  Wood Identification Type By Using Support Vector Mechine‐Based Image (A.A. 
Gede Rai Gunawan, Sri Nurdiati, Yandra Arkeman) 
226‐232.
Y.  Fuzzy  Logic  Systems  and  Applications  in  Agro‐industrial  Engineering  and 
Technology (Marimin, Mushthofa) 
233‐241.
Z.  Adaptive  Learning  Model  of  Hypergame  by  using  Genetic  Algorithm:  an 
Application of Value Co‐creation in Service System (Case Study: Airline Service) 
(Santi Novani, Utomo Sarjono Putro) 
200
Corncob Biodelignification Process Using White Rot Fungi
Liesbetini Hartoto
Dept. of Agroindustrial Technology,
Faculty of Agricultural Technology and Engineering IPB
(liesbetinihartoto@yahoo.com)
Purwoko
Dept. of Agroindustrial Technology,
Faculty of Agricultural Technology and Engineering IPB
Elis Nina Herliyana
Faculty of Forestry IPB
Cucu Rina Purwaningrum
Dept. of Agroindustrial Technology,
Faculty of Agricultural Technology and Engineering IPB
ABSTRACT
Corncob has a big potency to be converted become simple sugars which can be used as raw
materials for various products such asbioethanol and xylitol. Biodelignification is a process to
remove lignin from cellulosic materials by using microorganism like fungi, bacteria or enzyme.
Delignification need to be done because lignin is main barrier at lignocellulose hydrolysis process.
Some types of white rot fungi often applied for delignification are Schizophyllum commune,
Phanerochaete chrysosporium and Pleurotus EB9. The aims of this research is to obtain the best
type of white rot fungi,to get optimum concentration of mycelia, the bestconcentration of added
glucose and the most optimum incubation time for the chosen fungi. The results of preliminary
researchshowed that corncob delignification by fungi Phanerochaete chrysosporiumwas the best one
by decreasing of lignin content up to 26.07% andby giving degradation of dry weight up to 28.22%.
Therefore, Phanerochaete chrysosporium was chosen to be used in main research. Results of the
main research showed that optimum condition for delignification of corncob by Phanerochaete
chrysosporium wasas follows: incubation time of 24.25 days, concentration of mycelia 1.89 ml/10 g
substrate, and concentration of glucose added was 0.23 g/10 g substrate. From these conditions,the
obtained value of lignin rate ratio to holocellulose was 0.210689 g/g.
Keywords: Corncob biodelignification, Schizophyllum commune, Phanerochaete chrysosporium and
isolate Pleurotus EB9.
A. INTRODUCTION
Corncob is a byproduct of agricultural industry activity which is also the source of
lignocellulose. Indonesian dry shelled corn production reached 19.38 million tons in 2012
(BPS, 2013). Corn contains approximately 30% of corn cobs and the rest are seeds and
skins (Koswara, 1992).
According to Iswanto (2009), a corncob contains 15% of lignin, 45% of cellulose and
35% of hemicellulose. With this abundant amount of availability and the high content of
cellulose and hemicellulose in it, corncob has a great potency to be processed into high
economic products and also improved animal feeds. Corncob hydrolysis will produce
simple sugars such as glucose, xylose, mannose and arabinose. These kind of sugars can be
used as raw materials for huge variety of refined products such as carboxylic acids,
bioethanol, xylitol, amino acids or other complex products.
Prior to corncob hydrolysis process, a delignification pretreatment is required.
Delignification needs to be done because lignin is a major obstacle in the process of
cellulose hydrolysis. Lignin which protects cellulose is resistant to hydrolysis because of
the bond and the alkyl aryl ether linkage (Perez et al., 2002). There are several common
delignificationmethods, such as mechanical, chemical and semi chemical process. However,
those methods have some weaknesses such as high needs of chemicals and energy. In
201
addition, the liquid waste of delignification processwhichcontain chemicals are classified as
hazardous waste. It is toxic and tends to pollute the environment (Martina, 2002).
Several studies have been done to solve those problems by implementing biological
delignification method that known as biodelignification. White rot fungi is one of microbes
that can break down lignin selectively but just breaking down cellulose and hemicellulose
in very small amounts (Eaton and Hale, 1993). There are several types of white rot fungi
that are often be used for delignification process such as Schizophyllum commune,
Phanerochaete chrysosporium and Pleurotus EB9.
Those three types of fungi are able to do biodelignification process in wood. Realizing
that characteristic, this study observed the ability of those fungi in corncob delignification
process. In addition, this study also observe the influence of incubation time, the amount of
mycelia and the amount of additional glucose that was added to the lignin content ratio to
holocellulose. To measure biodelignification effectiveness process, the ratio of holoselulosa
to lignin content was calculated. Lowest ratio shows that these conditions are optimum
conditions for the growth of fungi.
B. METHODOLOGY
1.Preliminary Research
Preliminary research was conducted to know the characteristic of corncob and to
select the best fungi that can degrade the lignin content from corncob. There some steps
that were being taken.
a. Corncob Characterization
At this stage, corncob were being diminished up to ± 20 mesh using Hammer
Mill and followed by disc milling cutter up to ± 40 mesh. The downsizing result was
dried using oven at temperature of 50 °C (up to 10% final moisture). At this stage,
proximate tests were performed to measure moisture, ash, fat, protein, and fiber
content. In addition, fiber component analysis was also conducted, i.e. extractives,
holocellulose, cellulose, hemicellulose and lignin
b. The Best Fungi Selection
This stage aims to obtain the best white rot fungi among the three types of fungi
which are Schizophyllum commune, Phanerochaete chrysosporium and Pleurotus EB9
isolate. As its phases are:
a. Isolate Refreshment
Fungi were refreshed on Potato-Dextrose Broth (PDB) which already been
sterilized at temperature of 121o
C for 15 minutes using autoclave then followed by
incubation in room temperature for 5-10 days.
b. Culture Preparation
Materials that were used in this stage are shown at Table 1.
Table 1. Materials of Culture
Materials Amount
KH2PO4 7.2 g
MgSO4.7H2O 1.5 g
CaCl2.H2O 0.3 g
FeCl3.6H2O 0.045 g
ZnSO4.7H2O 0.023 g
CuSO4.5H2O 0.015 g
MnSO4.H2O 0.03 g
Aquades 150 ml
Source: Fadilah (2009)
c. Fungi Suspension Production
Fungi suspension was made by separating mycelia from its liquid media using
sterilized filtering paper. Then fungi suspension was mixed with 20 ml Tween solution
80 0.01% in a volumetric flask 50 ml and diluted with sterilized water up to 50 ml.
202
d. Media Preparation and Incubation
10 grams of 40 mesh corncob powder in a 6 cm diameter glass bottles, added
with 0.01gram of glucose and been stirred until homogeneous, followed by 15 ml
culture medium addition. The media were sterilized in an autoclave at a temperature of
121o
C for 15 minutes, cooled and inoculated by adding 2.5 ml of fungi suspension.
This media were incubated in an incubator for 30 days at a temperature of 30o
C. The
best fungi was selected based on its ability to degrade lignin.
2.Main Research
Activities undertaken in the main research include refreshment of isolates, culture
preparation, fungi suspension production, media preparation, incubation of white rot
fungi and observation of lignin degradation result.
a. Isolate Refreshment
Fungi are refreshed on Potato-Dextrose Broth (PDB) which already been
sterilized at temperature of 121o
C for 15 minutes using autoclave and followed by
shuffling using shaker during incubation in room temperature for ± 5-10 days. The
aim of shuffling was to downsize the size of mycelia so that easier to be extracted.
b. Media Preparation and Incubation of White Rot Fungi
This stage aims to provide optimum concentrations of fungi, glucose
concentration and optimum incubation time for fungi that obtained from the
preliminary research. An amount of 10 grams of 40 mesh corncob powder in a 6 cm
diameter glass bottles, was added with 0.01gram of glucose and stirred until
homogeneous. Then 15 ml culture medium was added. The media were sterilized in an
autoclave at a temperature of 121o
C for 15 minutes, cooled and inoculated by adding
fungi suspension. Then the media were incubated in an incubator for at a temperature
of 30o
C
e. Observation to Lignin Degradation Result
Parameters measured in this study were the reduction of dry weight percentage,
levels of extractive substances (TAPPI T 6m-59), levels of lignin (TAPPI T 13 os-54),
levels holosclullose (TAPPI T 9 m-54), cellulose (TAPPI T 17 m-55) and
hemicelluloses. Moreover, this study also measure the dry weight of mycelia /ml
suspension of fungi and microscopic observation to corncob structure before and after
delignification.
3.Determination of Influence Factor Against Lignin/Holocellulosa Ratio
This stage determines the influence of the amount of glucose, the amount of mycelia
that were added and the incubation time to the ratio of lignin / holocellulose. The
experimental design used in this research was factorial design 23
Full Factorial Central
Composide (CCD). This experimental design has a response equation as follows:
LHN
*
= β0+ β1x1 + β2x2 + β3x3 + β11x1
2
+ β22x2
2
+ β33x3
2
+ β12x12 + β13x13… + β23x23
LHN
*
is the ratio of lignin content to holocellulosa (g/g), x1 is the incubation time
(days), x2 is the number of mycelia that were added (ml), and x3 is the amount of glucose
added (g), while β is the coefficient. Value of these factors are shown in Table 2.
Table 2. Value of Research Treatment Factor.
Factor Extreem
Value
Minimum
Value
Average
Value
Maximum
Value
Extreem
Value
Incubation
Time (day)
3.18 10 20 30 37.8
Micelial (ml) 1 2.5 6.25 10 12.56
Glucose (g) 0.032 0.1 0.2 0.3 0.368
Code +-1.68 1 0 +1 + = +1.68
203
3. Data Analysis
Lignin content and holocellulose data that were obtained from chemical analysis
been analyzed statistically to determine the incubation time, the addition of glucose and
mycelia to the ratio of lignin/holocellulose. Analysis and determination of the best
conditions in the delignification process was done by using Statistic Analysis Software
(SAS) version 9.1. MINITAB 14 was used to provide three dimensional images of the
surface response.
C. RESULT AND DISCUSSION
1. Characterization of Corncob
a) Proximate Analysis
Proximate analysis was conducted to determine initial conditions of corncob. The
result is shown in Table 3. Initial corncob water content was 10.71%. This data
indicates the corn cob have low moisture content that cause the material more resistant
to microbial damage during storage.
Table 3. Corncob Proximate Analysis Result
Component % (w/w) %(d.w)
Water 10.71 -
Ash 1.69 1.89
Protein 0.60 0.67
Fat 2.34 2.62
Fiber 79.15 88.64
Carbohydrate (by difference) 5.51 6.18
Note: % w.w = wet weight percentage; % d.w = dry weight percentage
The ash content in corncob was about 1.69%. Ash content shows the amount of
inorganic and mineral content in a particular substance.
Protein content in corncob was very low, only 0.60 %. This shows that the corncob
in this study has not enough nutrition to be applied directly as an animal feed. This corncob
has 2.34 % of fat. Fat is an extractive substance that can be dissolved in organic solvent
such as eter, aceton, etc. (Fengel and Wegener, 1995).
The high content of fiber in the corncob (79.15%) showed that this substance is a
good carbon source which support microbial growth, especially microbe that can degrade
fiber component (ligninolyticand celullolytic).
b) Lignocellulose Content Analysis
Lignocellulose is the main component of a crop that represents the amount of organic
matter that can be renewed (Sjostrom, 1995). Lignocellulose consists of cellulose,
hemicellulose, lignin and some other extractive materials. All components of
lignocelluloses can be found in cell walls. The result of lignocelluloses analysis is shown in
Table 4.
Tabel 4. Composition of Corncob’s Lignocellulosesbefore Delignification
Component % d.w
Extractive material 4.92
Lignin 19.74
Cellulose 41.45
Hemicellulose 33.91
Note: % d.w = dry weight percentage
204
The initial corncob lignocellulose components analysis showed that corncob
has 19.74% lignin content, 41.45%cellulose content and 33.91% hemicellulose.
While the corncob that were used by Iswanto in his research (2009) has 15%lignin,
45% cellulose and 35% hemicellulose content. It shows that each corncob has
different lignocelluloses compositions. Differences in the chemical composition of
the corncob is influenced by several factors such as differences in varieties, place of
growth, weather and humidity while harvesting (Shofiyanto, 2008).
2. The Best Fungi Selection
The main parameters to select the best fungi is the ability of each fungi
which are, Schizophyllum commune,Phanerochaete chrysosporium and isolat
Pleurotus EB9 to degrade lignin during 30 days of incubation. The reduction
percentage of lignin content by each fungi is shown in Picture 1 as follows.
Figure 1 : Percentage of Reduction Corncob Lignin Content
After 30 days of incubation, corncob which was incubated with P. chrysosporium has
the highest reduction of lignin content level among the other two types of fungi (26.07 %).
This fungi has the ability to degrade lignin component of most large corncob among others.
Therefore, P. chrysosporium was selected to be used in the main research.
Decreasing lignin content by Pleurotus EB9 isolate after 30 days of incubation was
very low which was 1.66%. Different from P. chrysosporium which can produce enzyme
that can degrade components of phenolic (MnP) and non-phenolic components (lip) at once,
Pleurotus EB9 only produces one type of lignin-degrading enzymes which is laccase
enzyme. According to Kimura et al. (1990), attempts to detect the activity of the enzyme in
lignin peroxidase P.ostreatus under some culture conditions did not show positive results.
Sannia et al. (1991) found that there is laccase enzyme activity in white rot fungi Pleurotus.
Laccase is a copper-containing phenol oxidase that does not require H2O2 but oxygen
(Thurston, 1994). Laccase can oxidize non-phenolic components if there is a mediator such
as (2,2- azinobis (3-etilbenzthiazolin-6-sulfonat) or HBT (hydroxybenzotriazol)
(Bourbonnais and Paice, 1990). In fact, approximately 90% lignin structure composed of
non phenolic unit (Srebotnik et al., 1994). This caused the small decreasing lignin
percentage in substrate which incubated with Pleurotus than P. chrysosporium
Likewise Pleurotus, S. commune is known as fungi that can degrade lignin by only
producing laccase enzyme. The lower end of the weight lignin experienced by the substrate
after incubation with S. commune is mainly because the greater dry weight reduction of the
substrate.
Moreover, corncob also experienced decreasing in its dry weight. Likewise lignin
reduction content, corncob that was incubated with P. chrysosporium has the highest
reduction dry weight among the othe fungi at 28.22% (Picture 2).
Type of Fungi
ReductionofLignin
205
Figure 2 : Reduction of Corncob Dry Weight Percentage
Reduction of corncob dry weight percentage is one indicator of the existence of
biodegradation by fungi. Refer Picture 2, it can be inferred that P. chrysosporium has the
highest ability to decrease corncob’s dry weight than the other fungi in this study.
Reduction of corncob’s dry weight during incubation happened because there was enzyme
produced by the fungi that degrade corncob. According to Hatakka (2001), white-rot fungi
produce some kind of enzyme that involved in lignin degradation process, and also produce
cellulase, xilanase dan hemicellulase.
3. MAIN RESEARCH
1.Corncob Microscopic Structure
Initial fiber corncob microscopic structure and fiber corncob microscopic structure
after incubation with P. chrysosporium is shown in Picture 3. In that picture looks thread-
like structures called fibrils. Fibrils is a combination molecules of cellulose and contains
regular and less regular part. Initial corncob structure Picture 3 (a) shows fibrils structure
which still straight arrayed. However, after 30 days of incubation (Picture3 (b) ) it can be
seen that fiber structure seems more tenuous. This happened because during the incubation
there was degradation activity by enzymes released by fungi, thus causing the cell walls are
increasingly porous and produce a honeycomb structure. Cellulose fibrils lysis zones are
unprotected and loose (Fengel and Wegener, 1995).
Figure 3 : Corncob Fiber Microscopic Structure (400x of zooing): without polarized
light (a) before lignification, (b) after 30 days incubation; with polarized
light; (c) before delignification, (d) after 30 days incubation
Type of Fungi
ReductionofDryWeight(%)
206
Corncob appearance with polarized light (Picture 3 (c), (d)), there is a bluish color
that shows the structure of crystalline cellulose. On the initial corncob structure (before
delignification) appereance there is a structure of crystalline cellulose which characterized
by a bluish color. In the 30 days of incubation bluish color in polarized light become less
then before. This shows that the lignin content directly proportional with the length of
incubation time. According to Knauf and Moniruzzaman (2004), changes in the structure of
lignocellulose that has already been pretreated with separation between the cellulose and
material that protect it (hemicellulose and lignin). Changes in the structure of cellulose
which was originally shaped crystals become amorphous, makes it easy to be hydrolyzed.
2.Biodeliginification by P. chrysosporium
a.Dry Weight After Incubation
Incubation treatment P. chrysosporium on corncob has caused decreasing and
increasing its dry weight. The result of dry weight measurement of initial corncob and
post delignification corncob is shown in Picture 4.
Figure 4 : Dry weight of Corncob before (initial) and after Delignification
Degradation of lignocelluloses component is marked by decreasing of dry weight
substance. Enzyme that produced by fungi catalyzes the biochemical reactions in
lignocellulose media, so that the holocellulose and lignin can be changed into simpler
compounds. Then fungi can absorbed and metabolize these compounds (Herliyana,
1997).
However, the results obtained from this study showed an increasing dry weight in
both treatments. This increasing dry weight happened due to the fast growth of mycelia.
According to Fadilah (2009), the addition of nutrients such as glucose in the medium
has two advantages; one of them is the rapid growth of fungi on media. Because of the
addition of mycelia, there was an increase in the dry weight of the substrate after
delignification.
b.Extractive Substance Content
Extractive substance consists of several organic compounds such as acids, resins,
fatty acids, terpenes and alkaloids (Sjostrom, 1995). Extractive substances have varies
molecular weights. The substances can be found in lignocellulose contained materials
but not construct the cell wall. The ability of P. chrysosporium degrades extractive
component is influenced by the character of its extractive substance. There are some
extractive substance in corncob which are 0.7% of fat and uronat acids up to 3.36%
(Parajo et al., 2003) (Figure 5).
Sample Number
DryWeight(g)
Initial
207
Figure 5 : Extractive substance content (g/g) which dissolved in etanol:benzene (1:2)
before (initial) and after delignification
According to Rayner and Boddy (1995) the presence of wood extractive
substances can affect the growth of fungi, which acts as a carbon source, as a growth
stimulant and as an impediment to growth. Decreasing number of extractive substances
happened because it is estimated that the extractive substances contained in the corncob
are used as a carbon source by fungi.
c.Lignin Content
Figure 6 : Lignin Content (g/g) before (initial) and after Delignification by
Phanerochaete chrysosporium
The results (Figure 6) showed that the incubation time of 37.8 days (Experiment
No. 10) causes the higest decrease in lignin content from 0.187 (g/g) to 0.136 (g/g)
32.82%. From the data also found that the longer incubation time, the bigger decrease
in corncob lignin content. This shows that the fungi P. chrysosporium is an efficient
ligninolytic fungi.
d.Cellulose Content
Beside degrading lignin components, P. chrysosporium also capable to degrade
cellulose. Cellulose degradation is a work of a group of cellulolytic enzymes that work
synergistically. Fungi P. chrysosporium produces cellulase enzymes which has similar
activity with endogluconases (EGs) and exocellobiohydrolases (CBHs) depends on the
carbon source that available (Broda et al., 1996).
Cellulose content was decreasing during incubated with P. Chrysosporium
(Figure 7). This decreasing shows that during the incubation P. chrysosporium has
broken down cellulose component by using cellulolytic enzyme.
Initial
Initial
Sample Number
ExtractiveSubstanceContent(g/g)
Sample Number
LigninContent(g/g)
208
Figure 7 : Cellulose content (g/g) before (initial) and after Incubation Treatment with
Phanerochaete chrysosporium
Cellulose will be broken down into simpler compounds by fungi which then used
as nutrition for its growth. Those compounds then will be used in its metabolism cycles.
Additional sugar as nutrition is a factor that decreases cellulose degradation. The more
glucose that is added, the less rate of cellulose degradation will happen. This is because
the fungi will consume glucose first before degrade cellulose into simpler sugars
e. Hemicellulose Content
Hemicellulose is biodegraded into sugar monomer and acetic acids with the help
hemicellulase enzyme. Hemicelulase as like as many other enzyme which can
hydrolize cell wall of plant. Xylan is the main carbohydrates that develop
hemicellulose. Xylanase is also the main hemicellulase which hydrolyze β-1,4 bonds.
Fungi P. chrysosporium produced endoxylanase that plays a role in the breakdown of
xylan into oligosaccharides (Perez et al., 2002).
In Picture 8 it can be seen that some samples experienced increasing number of
hemicellulose content. Increasing in the hemicellulose content of the substrate can be
caused by miscounting of mycelia as part of the hemicellulose. This is probably
happened because in some samples mycelial growth rate higher than the rate of
degradation of lignocellulosic components. According to Chang and Miles (1989), the
average mycelial fungi have fiber content ranging at 7.4%-24.6%.
Figure 8 : Hemicellulose content (g/g) before (initial) and after incubation treatment by
Phanerochaete chrysosporium
Sample Number
CelluloseContent(g/g)
Sample Number
HemicelluloseContent(g/g)
Initial
Initial
209
3. Influence of Factor against Ratio Lignin/Holocellulose Content
Biodelignification process is influenced by some factors which are duration of
incubation, amount of nutrition and amount of additional mycelia that is added into media.
Those factors can be optimized so that can increase delignification efectivity. Increasing
delignification efectivity can be seen from degradation lignin levels by P. chrysosporium.
Ideal delignification process is happened when lignin was decomposed in large
numbers but holocellulosa components broken down in small amounts. Holocellulose
which is a part of the fiber that is free from extractive substances and lignin, consist of
all the cellulose and hemicellulose components (Chang and Alan, 1971). Therefore, the
main parameter to assess the effectiveness of delignification is decreasing lignin and
holocellulose content level.
This research measures the influence of incubation time, the amount of mycelia
that were added and the amount of glucose that is added to the ratio of
lignin/holocellulosa as well as the interaction of these three factors to the ratio of
lignin/holocelulose. Relation between factor reaction with response can be determined
through a systematic series of experiments that tested through statistical analysis.
Table 5. Influence of Linear and Quadratic Factors Against the Ratio of
Lignin/Holocellulose
Source Probability p > F Effect
X1 < 0001 Significant
X1*X2 < 0001 Significant
X2 0.8335 Not significant
X2*X2 0.7999 Not significant
X3 0.6172 Not significant
X3*X3 0.4023 Not significant
Results of statistical analysis (Table 5) showed that both the linear and quadratic
effect of incubation time gave a significant effect on the ratio of lignin / holoselulosa. Yet,
in this study the addition of mycelia (x2) in delignification process did not decrease lignin
content ratio against holocellulose. Though it appears from the graph that the lignin content
against holocellulosa ratio slightly decreased with increasing the amount of glucose that is
added, but from the linear and quadratic effects analysis it can be inferred that the amount
of glucose was not significantly affected the response (Figure 9).
Figure 9 : Influence Combination of Length of Incubation Time (day), Amount of
mycelia (ml/10 g substrate), Amount of glucose (g/10 g substrate) that
is added against ratio lignin/holocellulose
Incubation time (day)
Incubation time (day)
Incubation time (day)
Amount of Glucose
(g/10 g)
Amount of Glucose
(g/10 g)
Amount of Glucose
(g/10 g)
Ratio (g/g)
Ratio (g/g)
Ratio (g/g)
210
Interaction effect between the number of mycelia, length of incubation time and the
amount of glucose that is added to the process showed no significant effect to the value
ratio lignin/ holoselulosa. It can be seen from the shape of response surface that which
not tend to change in various combinations with other factors.It is reinforced by
opportunities value p> F that showed interaction effect was not significant (Table 6).
Table6. Interaction InfluencebetweenLength of Incubation Time, Amount of Mycelia and
Glucosethat is Added againstLignin/Holocellulose Ratio
Source* Probability p > F Effect
X1- X2 0.8117 Not Significant
X1- X3 0.6916 Not Significant
X2-X3 0.9754 Not Significant
4.THE BEST CONDITION FOR BIODELIGNIFICATION PROCESS
The result of data analysis ratio lignin/holocelluloseat various treatment
producedoptimization equation ratio lignin/holocellulose for delignification process as
follows.
LHN
*
is symbol for ratio lignin/holocellulose (g/g), x1is length of
incubationtime(day), x2is additional mycelia (ml), and x3is additional glucose (g).
The results of the canonical analysis to the response surface showed that the
response surface model is minimum. This causes the optimum value can be determined
from the response surface. Determination of the best conditions of biodelignifikasi
process using Phanerochaete chrysosporium is shown in Table 7.
Tabel 7. The Best Condition of Biodelignification Process Using Phanerochaete
chrysosporium
Factor* Code Value
X1 0.22 24.25
X2 -0.85 1.89
X3 0.18 0.23
*x1 : Length of Incubation time (day); x2 : Amount of mycelia (ml/10 g substrate) ; x3 : amount of
glucose(g/10 g substrate).
That condition is estimated giving ratio of lignin content against holoselulosaup
to0.210689 g/g. It means there is 0.210689 g of lignin in each 1g of holocellulose. This
ratio is obtained in 24.25 days length time of incubation using Phanerochaete
chrysosporium, the amount of additional mycelia is 1.89 ml/10 g substrate and the
additional glucose is 0.23 g/10 g substrate.
5. CONCLUSION
Based on its ability to degrade lignin, Phanerochaete chrysosporium isolate has
better capability than Schizophyllum commune and Pleurotus EB9 isolate. This is proven
by the decreasing value of lignin content from corncob that was incubated with P.
chrysosporium for 30 days at room temperature 26.07o
C.
Corncob biodelignification process effectiveness using P. chrysosporium can be
seen from decreasing ratio lignin/holocellulose level. The result of statistical analysis
showed that length of incubation time significantly affected the decreasing of
lignin/holocellulose ratio level. However, various additional mycelia and amount of
glucose did not significantly affect the decreasing lignin/ holocellulose ratio.
211
From the result of surface respon analysis, it can be inferred that the optimum
condition for corncob biodelignification process is determined by response equation model,
as follows.
LHN
*
= 0.314541 - 0.007922 x1- 0.000709 x2- 0.061692 x3 + 0.000168 x1
2
+ 0.000046
x2
2
+ 0.194656 x3
2
+ 0.000020 x12- 0.001181 x13 + 0.000246 x23
This equation provided decreasing value of ratio lignin/holoselulosa up to 0.210689
g/g. This ratio derived from 24.25 days of incubation using Phanerochaete chrysosporium
on the substrate of corncob with additional mycelia up to 1.89 ml/10 g substrate and the
amount of glucose is 0.23 g/10 g substrat.
6. ACKNOWLEDGEMENT
Authors thank to the Directorate General of Higher Education - Ministery of
National Education R.I for funding this research through Batch I Competitive Grants
funding in 2009.
REFERENCES
[1] [TAPPI] Technical Association of The Pulp and Paper Industry. 1996. TAPPI Test Method.
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role for laccase in lignin biodegradation. FEBS Letters. 267:99-102.
[3] Broda, P., P.R.J. Birch, P.R. Brooks dan P.F.G. Sims. 1996. Lignocellulose degradation by
Phanerochaete chrysosporium: Gene families and gene expression for a complex process.
Molecul. Microbiol. 19(5):923-932.
[4] Chang, H. M. dan G. G. Allan. 1971. Oxidation. hlm. 463-468. Di dalam K. V. Sarkanen &
C. H. Ludwig (Penyunting). Lignins: Occurance Formation, Stucture and Reactions.
JohnWiley & Sons, New York.
[5] Chang, S.T, dan P.G. Miles. 1989. Edible Mushrooms and Their Cultivation. Florida: CRC
Press, Inc. 451p.
[6] Eaton, R. A. dan M.D.C. Hale. 1993. Wood, Decay, Pest and Protection. Chapman and Hall,
London.
[7] Fadilah, S. Distantina, S. R. Dwiningsih, dan D. R. Ma’rifah. 2009. Pengaruh penambahan
glukosa dan ekstrak yeast terhadap biodelignifikasi ampas batang aren.EkuilibriumVol. 8.
No. 1: 29 –33.
[8] Fengel, D. dan G. Wegener. 1995. Kimia Kayu, Reaksi Ultrastruktur: Terjemahan
Sastrohamidjojo, H,. Gadjah Mada University Press, Yogyakarta.
[9] Hatakka, A. 2001. Biodegradation of lignin. In: Steinbüchel, A. [ed] Biopolymers. Vol 1:
Lignin, Humic Substances and Coal. Germany: Wiley VCH. pp. 129-180.
[10] Herliyana, E. N. 1997. Potensi Schizophyllum commune dan Phanerochaete chrysosporium
untuk pemutihan pulp kayu Acacia mangium dan Pinus merkusii [tesis]. Program Studi
Entomologi/Fitopatologi Program Pascasarjana IPB, Bogor.
[11] Iswanto, A. H. 2009. Fungsi Polimer Alami: Terbentuknya Dimensi Baru dalam Kimia
Lignoselulosa. Makalah: Fakultas Pertanian Univesitas Sumatera Utara.
[12] Kimura, Y., Y. Asada, dan M. Kuwahara. 1990. Screening of basidiomycetes for lignin
peroxidase genes using a DNA probe. Appl. Microbiol. Biotechnol. 32:436-442.
[13] Knauf, M. dan M. Moniruzzaman. 2004. Lignocellulosic Biomass Processing: A Perspective.
International Sugar Jurnal 106 : 147-151.
[14] Koswara, J. 1992. Budidaya Jagung. Jurusan Budidaya Pertanian, Fakultas Pertanian, IPB,
Bogor.
[15] Martina, A., N. Yuli dan M. Sutisna. 2002. Optimasi beberapa faktor fisik terhadap laju
degradasi selulosa kayu albasia (Paraserianthesfalcataria (L.)) Nielsen dan
Karboksimetilselulosa (CMC) secara enzimatik oleh fungi. Jurnal Natur Indonesia 4(2):
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[16] Parajo, J. C., Garotte, J.M. Cruz, dan H. Dominguez. 2003. Production of
Xyloligosaccharides by Autohydrolisis of Lygnocellulosic Materials. Trends in Food
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[18] Rayner, A. D. M. dan L. Boddy. 1995. Fungal Decompotition of Wood: Its Biology and
Ecology. John Wiley & Sons, Chichester.
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corncob biodelignification process using white rot fungi

  • 1.
  • 2. CONFERENCE COMMITTEE Coordinator : Yandra Arkeman, Dr. M.Eng (Departement of Agroindustrial Technology, IPB) Co-Coordinator: Nastiti Siswi Indrasti, Prof. Dr. Ir. (Head of Departemen of Agroindustrial Technology, IPB) International Experts: 1. Kenneth De Jong, Prof. (George Mason University, Fairfax, Virginia, USA) 2. Kim Bryceson, Prof. (School of Agriculture and Food Science , University of Queensland, Australia) 3. Haruhiro Fujita, Prof. (Department of Information Systems, Niigata University for International and Information Studies Japan) 4. Gajendran Kandamsany, Dr. (United Kingdom) 5. Noel Lindsay, Prof. (University of Adelaide, Australia) Committee Members from IPB: 1. Kudang Boro Seminar, Prof. (Departement of Mechanical & Bio-system Engineering, IPB) 2. Marimin, Prof. (Departement of Agroindustrial Technology, IPB) 3. Endang Gumbira Said, Prof. (Departement of Agroindustrial Technology, IPB) 4. Suprihatin, Prof. (Secretary of Departement of Agroindustrial Technology, IPB) 5. Ono Suparno, Prof. (Departement of Agroindustrial Technology, IPB) 6. Agus Buono, Dr. (Head of Department of Computer Science, IPB) PROCEEDINGS 2nd International Conference on Adaptive and Intelligent Agroindustry (ICAIA) September 16 – 17, 2013, IPB International Convention Center Bogor – Indonesia Organized by : Departement of Agroindustrial Technology, Faculty of Agricultural Engineering and Technology Bogor Agricultural University George Mason University, Fairfax, Virginia, USA Indonesian Agroindustry Association (AGRIN) Bogor, Desember 2013 Frekwensi Terbitan : 1 Tahunan Nomor ISSN : 2354-9041
  • 3. i WELCOMING ADDRESS Prof. Dr. Ir. Nastiti Siswi Indrasti Head of Agroindustrial Technology Department Faculty of Agricultural Engineering and Technology Bogor Agricultural University On Second International Conference on Adaptive and Intelligence Agroindustry (2nd ICAIA) Bogor, September, 16 – 17, 2013 Assalamu’alaikum Warohmatullahi Wabarokatuh In the name of Allah, the beneficent and the merciful, Distinguish Guest, Ladies and Gentlemen Let me first thank you all for accepting the invitation to participate in this 2nd International Conference on Adaptive and Intelligence Agroindustry (ICAIA). In particular I would like to thank Rector of IPB (Institut Pertanian Bogor/Bogor Agricultural University) Prof. Herry Suhardiyanto for supporting this event as part of the series academic event in celebrating the 50th Anniversary of Bogor Agricultural University. In fact, the idea of organizing this conference was the continuation of the International Workshop on Computational Intelligence and Supercomputing Technology for Adaptive Agroindustry held by the Department of Agroindustrial Technology, Bogor Agricultural University last year. Professor Kenneth A De Jong from George Mason University, US has successfully conducted joint international research with some staff from the Department of Agroindustrial Technology and Department of Computer Science, Bogor Agricultural University. The research aims to develop an integrated and intelligent system (namely SMART-TIN©) for the design of adaptive agroindustrial system in order to achieve a sustainable agroindustry that can mitigate global climate change and at the same time secure food, water, energy and natural medicine supply. We are certainly proud to have been able to assemble this event in IPB, Bogor. The range of participants and audience at this conference is precisely something I would like to stress. The main goal of the conference is to provide an effective forum for distinguished speakers, academicians, professional and practitioners coming from universities, research institutions, government agencies and industries to share or exchange their ideas, experience and recent progress in Adaptive and Intelligent Agroindustry. Distinguish Guest, Ladies and Gentlement, Global climate change is the most challenging problems for us today and in the near future. This global change in our climate can lead to the shortage of the food, water, bioenergy and natural medicine that will affect the quality of human life. Many studies indicate that the threat of food, water, bioenergy and natural medicine crisis due to global climate change still worries our society. This problem can be solved by the development of agroindustry, i.e. an interrelated value chain entities from farming, to agro-processing industry and then to the end-customers. In fact, the design of agroindustry is complex and involves many factors and large data bases and more importantly, needs a good intelligence to process data and information to good decisions. Therefore, the way to design and manage agroindustry should be improved in order to meet the design objectives. Agroindustries consume quite significant amount of energy on one side, on the other side they generate sizable amount of industrial wastes and its utilization as a captive energy resource is a kind of potential. Based on our study, a plywood industry with the production capacity of 200.000 m3 /year could generate 32 percentage of solid waste. If this amount of waste used as an energy alternative, it may result on the saving of 131.037.768.597 rupiah per month. Similar to plywood industry, sugarcane industry with the production capacity of 480 ton per hour could generate 154 ton per hour of waste (bagasse) and this amount of waste contribute to the saving of energy consuming by 19.250 Kwh. Recent study we conducted, indicated that cassava starch industry may contribute to a significant amount of waste. It has also potential usage as an energy resource. Based on our study the conversion of its waste into energy will contribute to the saving of energy usage of 4100 liter biogas per ton material. The three industries mentioned is only examples of how potential the role of agroindustrial waste as an alternative resource in replacing the conventional energy resource as its presence will be significantly
  • 4. ii reduced. The new, incremental energy contributions that can be obtained from waste biomass will depend on future government policies, on the rates of fossils fuel depletion, and on extrinsic and intrinsic economic factors, as well as the availability of specific residues in areas where they can be collected and utilized. All of these factors should be in detail examined to evaluate the development of the industrial waste contribution. Hope this conference will also discuss this issue in more detail as it is an important matter for all of us. We should no more think just how to produce high value product but it is also necessarily important how to keep our live in good quality by understanding following old saying…” only when the last tree has been cut, only when the last fish has been angled, and only when the last river has been polluted, then we realized that we could not eat money”. I do not to take up any more of your time with these opening remarks. Let me simply thank you once again for sharing your thoughts with us. Here’s wishing every success for the conference. May Allah bless all of us. Thank you for your kind attention, Wassalamu’alaikum Warohmatullahi Wabarokatuh
  • 5. iii AGENDA of 2nd International Conference on Adaptive and Intelligent Agroindustry (ICAIA) Time Activities Room Day 1 (16 September 2013) 08.00 – 09.00 (60’) Registration 09.00 – 10.00 (60’) Opening Ceremony  Welcoming Address: Prof. NastitiSiswiIndrasti (Head of Dept TIN, Fateta, IPB)  Conference Opening: Prof. HerrySuhardiyanto(Rector of IPB) o ABET Certification announcement and short ceremony o Launching International Double Degree Master Program in Innovation and Technopreneurship in Cooperation with University of Adelaide, Australia o Soft-launching Master in Logistik Agroindustri (Agroindustrial Logistics) Ballroom 10.00 – 10.45 (45’) Opening Speeches: Prof. IrawadiJamaran (Agroindustry Guru, IPB: 25’) Prof. Eriyatno (Industrial and System Engineering, IPB: 20’) Ballroom Session 1 10.45 – 11.15 (30’) Keynote Speech Dr. YandraArkeman (IPB) Ballroom 11.15 – 12.00 (45’) Keynote Speech Prof. Kenneth De Jong (George Mason University, USA) Ballroom 12.00 – 13.30 (90’) Lunch Break Session 2 13.30 – 15.15 (105’) Moderator: Prof. EndangGumbiraSa’id (IPB) Invited Speakers (1-4) (4 x 20 minutes) Discussion (25 minutes) Tentative Schedule: Prof. Kim Bryceson (Australia), Prof. SyamsulMa’arif (IPB), Prof. KudangBoro Seminar (IPB), Prof. HaruhiroFujita (Japan) Ballroom 15.15 – 15.45 (30’) Break 15.45 – 17.30 (105’) Moderator: Prof. Marimin (IPB) Invited Speakers (5-8) (4 x 20 minutes) Discussion (25 minutes) Tentative Schedule: Dr. Gajendran (UK), Prof. Noel Lindsay (University of Adelaide), Dr. KuncoroHartoWidodo (UGM), Prof. UtomoSarjonoPutro (ITB) Ballroom Day 2 (17 September 2013) 08.00 – 08.30 (30’) Registration 08.30 – 10.15 (105’) Moderator: Prof. KudangBoro Seminar (IPB) Invited Speakers (9-12) (4 x 20 minutes) Discussion (25 minutes) Prof. Egum (IPB), Prof. Marimin (IPB), Dr. AgusBuono (IPB), Dr. HeruSukoco (IPB) 10.15 – 10.30 (15’) Coffee Break 10.30 – 12.30 (120’) Parallel Session 1 Moderator: Prof. Fujita (7 paper @ 15 minutes) Discussion (15 minutes) Parallel Session 2 Moderator: Prof. Ono Suparno (7 paper @ 15 minutes) Discussion (15 minutes) Parallel Session Moderator: Prof. Suprihatin (7 paper @ 15 minutes) Discussion (15 minutes)
  • 6. iv 12.30 – 13.30 (60’) Lunch Break 13.30 – 15.00 (90’) Open Discussion (Open Forum) with Prof. Kenneth De Jong Topic: Foundations and Applications of Genetic/Evolutionary Algorithms Ballroom 15.00 – 15.30 (30’) Conference Closing Ballroom 15.30 – 17.00 (90’) Indonesian Agroindustry Association (AGRIN) National Congress (PIC: Prof. Suprihatin) Ballroom 17.00 – 17.45 (45’) Refreshment and Closing of AGRIN National Congress Ballroom
  • 7. v CONTENT LIST Conference Committee Welcoming Address ….………………………………………………….…………….................. i Agenda of 2nd ICAIA 2013.............................................................................................................. iii Content List …………..………………………………………………......……………................. v A.  SMART-TIN© : An Integrated And Intelligent System For The Design Of Adaptive Agroindustry (A Conceptual Framework) (Yandra Arkeman) 1‐9. B.  GHG  Emission  Reduction  By  Waste  Cooking  Oil  Recycling  In  Environmental  Partnership  Program  Of  Bogor  City  (Haruhiro  Fujita,  Atsushi  Yoshimoto,  Katsuyuki Nakano,  Koji Okuhara, Noriaki Koide, Dadang Supriatna)  10‐16. C.  Challenge  of  Indonesian  Logistics  Infrastructure  for  Perishables  Products  (Kuncoro Hartoto Widodo, Yandra Rahardian Perdana, Joewono Soemardjito)  17‐28. D.  Design Of Grouping Traditional Market  Distribution Using  Fuzzy Clustering And  Design  of  Routing  of  Packaging  Cooking  Oil  From  Distribution  Center  To  Traditional Market  Using Traveling Salesperson Problem– Genetic Algorithm in  Indonesia  (Case‐Jakarta)  (Teja  Primawati  Utami,  Syamsul  Maarif,  Yandra  Arkeman, Liesbetini Hartoto)  29‐43. E.  Determining the degree of product rightness at the conceptual stage:A Case of  the Low Cost Green Car (Ade Febransyah, Fransisca Tharia)  44‐53. F.  Co‐Composting Process Of Bagasse And Sludge From Sugarcane  Industry With  Influence Of Difference Initial C/N Value And Aeration (Andes Ismayana, Nastiti  Siswi Indrasti, Tori Sane)  54‐62. G.  Analysis Of The Competitiveness Of The Agribusiness Sector Companies Using  Porter's Five Forces (M. Hudori)  63‐72. H.  Design  And  Optimization  Of  Agro‐Scm  For  Food  And  Energy  Security  In  Indonesia (Hoetomo Lembito, Kudang Boro Seminar, Nunung Kusnadi, Yandra  Arkeman)  73‐83. I.  Construction Of Patchouli Oil’s Price In West Java : A Structural Equation Model  (Isti Surjandari, Alan Dwi Wibowo, Erlinda Muslim, Nurwan Nugraha)  84‐90. J.  Optimization Vehicle Routing Problem With Cross Entropy Method And Branch  & Bound Algorithm (Iwan Aang Soenardi, Budi Marpaung)  91‐99. K.  Design  And  Optimization  Of  Agro‐Scm  For  Food  And  Energy  A  Remote  Monitoring System Of Broilers’ Behavior In A Multi‐Agent Broiler Closed House  System (K.B. Seminar, R. Afnan, M. Solahudin, Supriyanto, A.K. Wijayanto, M.Z.  Arifin, A. Fatikunnada)  100‐112. L.  Artificial Neural Network Model Based Capacitance Dielectric For Crackers Self‐ Life  Prediction  (Erna  Rusliana  Muhamaad  Saleh,  Erliza  Noor,  Taufik  Djatna,  Irzaman)  113‐121. M.  Characterizing  Temporal  Dynamic  Of  Weather  Variability  To  Support  Decision  Making  On  Weed  Control  (Rizky  Mulya  Sampurno,  Kudang  B.  Seminar,  Yuli  Suharnoto, Mohamad Solahudin)  122‐130.
  • 8. vi N.  Risk  Management  Model  in  Dairy  Product  Transportation  With  Fuzzy  Logic  Approach (Winnie Septiani, Yandra Arkeman)  131‐141. O.  Strategy  to  Increase  Institutional  Capacity  of  Farmer  Groups  to  Support  the  Transportation System Agroindustry Products (Zulfiandri, Yandra Arkeman)  142‐156. P.  Adsorption Of Carotenoid From Palm Oil Methyl Ester By Using Attapulgite And  Synthetic Silica Magnesium As Adsorbent (Sapta Raharja, Prayoga Suryadarma,  Zuni Fitriyantini)  157‐163. Q.  High Accuracy Agroindustry Environment Monitoring System Based on Photonic  Crystal Sensor Network (Mamat Rahmat, Muhamad Azis, Erus Rustami, Wenny  Maulina, Kudang Boro Seminar, Arief Sabdo Yuwono, Husin Alatas)  164‐174. R.  Study  on  Effect  ofTemperatureIncrease  on  the  Productivity  of  Methanefrom  POME Fermentation (Sarono, E. Gumbira Said, Ono Suparno, Suprihatin, Udin  Hasanudin)  175‐180. S.  The Design and Implementation of Geographic Information Systems to Support  Food  and  Energy  Security  (Arif  Purnomo  Muji  Basuki,  Yandra  Arkeman,  Musthofa)  181‐191. T.  Study Of White Crystal Sugar Distribution System In Indonesia (Suripto, Yandra  Arkeman)  192‐199. U.  Corncob  Biodelignification  Process  Using  White  Rot  Fungi  (Liesbetini  Hartoto,  Purwoko, Elis Nina Herliyana, Cucu Rina Purwaningrum)  200‐212.  V.  Color  Stability  of  Beet  Dyes  Label  During  Heating    (Endang  Warsiki,  Asih  Setiautami)  213‐219. W  Precipitation  Classification  Using  LVQ  on  Dry  Season  Base  on  Global  Climate  Indices Case Study in Indramayu District (Indra Kelana Jaya, Agus Buono, Yandra  Arkeman)  220‐225. X.  Wood Identification Type By Using Support Vector Mechine‐Based Image (A.A.  Gede Rai Gunawan, Sri Nurdiati, Yandra Arkeman)  226‐232. Y.  Fuzzy  Logic  Systems  and  Applications  in  Agro‐industrial  Engineering  and  Technology (Marimin, Mushthofa)  233‐241. Z.  Adaptive  Learning  Model  of  Hypergame  by  using  Genetic  Algorithm:  an  Application of Value Co‐creation in Service System (Case Study: Airline Service)  (Santi Novani, Utomo Sarjono Putro) 
  • 9. 200 Corncob Biodelignification Process Using White Rot Fungi Liesbetini Hartoto Dept. of Agroindustrial Technology, Faculty of Agricultural Technology and Engineering IPB (liesbetinihartoto@yahoo.com) Purwoko Dept. of Agroindustrial Technology, Faculty of Agricultural Technology and Engineering IPB Elis Nina Herliyana Faculty of Forestry IPB Cucu Rina Purwaningrum Dept. of Agroindustrial Technology, Faculty of Agricultural Technology and Engineering IPB ABSTRACT Corncob has a big potency to be converted become simple sugars which can be used as raw materials for various products such asbioethanol and xylitol. Biodelignification is a process to remove lignin from cellulosic materials by using microorganism like fungi, bacteria or enzyme. Delignification need to be done because lignin is main barrier at lignocellulose hydrolysis process. Some types of white rot fungi often applied for delignification are Schizophyllum commune, Phanerochaete chrysosporium and Pleurotus EB9. The aims of this research is to obtain the best type of white rot fungi,to get optimum concentration of mycelia, the bestconcentration of added glucose and the most optimum incubation time for the chosen fungi. The results of preliminary researchshowed that corncob delignification by fungi Phanerochaete chrysosporiumwas the best one by decreasing of lignin content up to 26.07% andby giving degradation of dry weight up to 28.22%. Therefore, Phanerochaete chrysosporium was chosen to be used in main research. Results of the main research showed that optimum condition for delignification of corncob by Phanerochaete chrysosporium wasas follows: incubation time of 24.25 days, concentration of mycelia 1.89 ml/10 g substrate, and concentration of glucose added was 0.23 g/10 g substrate. From these conditions,the obtained value of lignin rate ratio to holocellulose was 0.210689 g/g. Keywords: Corncob biodelignification, Schizophyllum commune, Phanerochaete chrysosporium and isolate Pleurotus EB9. A. INTRODUCTION Corncob is a byproduct of agricultural industry activity which is also the source of lignocellulose. Indonesian dry shelled corn production reached 19.38 million tons in 2012 (BPS, 2013). Corn contains approximately 30% of corn cobs and the rest are seeds and skins (Koswara, 1992). According to Iswanto (2009), a corncob contains 15% of lignin, 45% of cellulose and 35% of hemicellulose. With this abundant amount of availability and the high content of cellulose and hemicellulose in it, corncob has a great potency to be processed into high economic products and also improved animal feeds. Corncob hydrolysis will produce simple sugars such as glucose, xylose, mannose and arabinose. These kind of sugars can be used as raw materials for huge variety of refined products such as carboxylic acids, bioethanol, xylitol, amino acids or other complex products. Prior to corncob hydrolysis process, a delignification pretreatment is required. Delignification needs to be done because lignin is a major obstacle in the process of cellulose hydrolysis. Lignin which protects cellulose is resistant to hydrolysis because of the bond and the alkyl aryl ether linkage (Perez et al., 2002). There are several common delignificationmethods, such as mechanical, chemical and semi chemical process. However, those methods have some weaknesses such as high needs of chemicals and energy. In
  • 10. 201 addition, the liquid waste of delignification processwhichcontain chemicals are classified as hazardous waste. It is toxic and tends to pollute the environment (Martina, 2002). Several studies have been done to solve those problems by implementing biological delignification method that known as biodelignification. White rot fungi is one of microbes that can break down lignin selectively but just breaking down cellulose and hemicellulose in very small amounts (Eaton and Hale, 1993). There are several types of white rot fungi that are often be used for delignification process such as Schizophyllum commune, Phanerochaete chrysosporium and Pleurotus EB9. Those three types of fungi are able to do biodelignification process in wood. Realizing that characteristic, this study observed the ability of those fungi in corncob delignification process. In addition, this study also observe the influence of incubation time, the amount of mycelia and the amount of additional glucose that was added to the lignin content ratio to holocellulose. To measure biodelignification effectiveness process, the ratio of holoselulosa to lignin content was calculated. Lowest ratio shows that these conditions are optimum conditions for the growth of fungi. B. METHODOLOGY 1.Preliminary Research Preliminary research was conducted to know the characteristic of corncob and to select the best fungi that can degrade the lignin content from corncob. There some steps that were being taken. a. Corncob Characterization At this stage, corncob were being diminished up to ± 20 mesh using Hammer Mill and followed by disc milling cutter up to ± 40 mesh. The downsizing result was dried using oven at temperature of 50 °C (up to 10% final moisture). At this stage, proximate tests were performed to measure moisture, ash, fat, protein, and fiber content. In addition, fiber component analysis was also conducted, i.e. extractives, holocellulose, cellulose, hemicellulose and lignin b. The Best Fungi Selection This stage aims to obtain the best white rot fungi among the three types of fungi which are Schizophyllum commune, Phanerochaete chrysosporium and Pleurotus EB9 isolate. As its phases are: a. Isolate Refreshment Fungi were refreshed on Potato-Dextrose Broth (PDB) which already been sterilized at temperature of 121o C for 15 minutes using autoclave then followed by incubation in room temperature for 5-10 days. b. Culture Preparation Materials that were used in this stage are shown at Table 1. Table 1. Materials of Culture Materials Amount KH2PO4 7.2 g MgSO4.7H2O 1.5 g CaCl2.H2O 0.3 g FeCl3.6H2O 0.045 g ZnSO4.7H2O 0.023 g CuSO4.5H2O 0.015 g MnSO4.H2O 0.03 g Aquades 150 ml Source: Fadilah (2009) c. Fungi Suspension Production Fungi suspension was made by separating mycelia from its liquid media using sterilized filtering paper. Then fungi suspension was mixed with 20 ml Tween solution 80 0.01% in a volumetric flask 50 ml and diluted with sterilized water up to 50 ml.
  • 11. 202 d. Media Preparation and Incubation 10 grams of 40 mesh corncob powder in a 6 cm diameter glass bottles, added with 0.01gram of glucose and been stirred until homogeneous, followed by 15 ml culture medium addition. The media were sterilized in an autoclave at a temperature of 121o C for 15 minutes, cooled and inoculated by adding 2.5 ml of fungi suspension. This media were incubated in an incubator for 30 days at a temperature of 30o C. The best fungi was selected based on its ability to degrade lignin. 2.Main Research Activities undertaken in the main research include refreshment of isolates, culture preparation, fungi suspension production, media preparation, incubation of white rot fungi and observation of lignin degradation result. a. Isolate Refreshment Fungi are refreshed on Potato-Dextrose Broth (PDB) which already been sterilized at temperature of 121o C for 15 minutes using autoclave and followed by shuffling using shaker during incubation in room temperature for ± 5-10 days. The aim of shuffling was to downsize the size of mycelia so that easier to be extracted. b. Media Preparation and Incubation of White Rot Fungi This stage aims to provide optimum concentrations of fungi, glucose concentration and optimum incubation time for fungi that obtained from the preliminary research. An amount of 10 grams of 40 mesh corncob powder in a 6 cm diameter glass bottles, was added with 0.01gram of glucose and stirred until homogeneous. Then 15 ml culture medium was added. The media were sterilized in an autoclave at a temperature of 121o C for 15 minutes, cooled and inoculated by adding fungi suspension. Then the media were incubated in an incubator for at a temperature of 30o C e. Observation to Lignin Degradation Result Parameters measured in this study were the reduction of dry weight percentage, levels of extractive substances (TAPPI T 6m-59), levels of lignin (TAPPI T 13 os-54), levels holosclullose (TAPPI T 9 m-54), cellulose (TAPPI T 17 m-55) and hemicelluloses. Moreover, this study also measure the dry weight of mycelia /ml suspension of fungi and microscopic observation to corncob structure before and after delignification. 3.Determination of Influence Factor Against Lignin/Holocellulosa Ratio This stage determines the influence of the amount of glucose, the amount of mycelia that were added and the incubation time to the ratio of lignin / holocellulose. The experimental design used in this research was factorial design 23 Full Factorial Central Composide (CCD). This experimental design has a response equation as follows: LHN * = β0+ β1x1 + β2x2 + β3x3 + β11x1 2 + β22x2 2 + β33x3 2 + β12x12 + β13x13… + β23x23 LHN * is the ratio of lignin content to holocellulosa (g/g), x1 is the incubation time (days), x2 is the number of mycelia that were added (ml), and x3 is the amount of glucose added (g), while β is the coefficient. Value of these factors are shown in Table 2. Table 2. Value of Research Treatment Factor. Factor Extreem Value Minimum Value Average Value Maximum Value Extreem Value Incubation Time (day) 3.18 10 20 30 37.8 Micelial (ml) 1 2.5 6.25 10 12.56 Glucose (g) 0.032 0.1 0.2 0.3 0.368 Code +-1.68 1 0 +1 + = +1.68
  • 12. 203 3. Data Analysis Lignin content and holocellulose data that were obtained from chemical analysis been analyzed statistically to determine the incubation time, the addition of glucose and mycelia to the ratio of lignin/holocellulose. Analysis and determination of the best conditions in the delignification process was done by using Statistic Analysis Software (SAS) version 9.1. MINITAB 14 was used to provide three dimensional images of the surface response. C. RESULT AND DISCUSSION 1. Characterization of Corncob a) Proximate Analysis Proximate analysis was conducted to determine initial conditions of corncob. The result is shown in Table 3. Initial corncob water content was 10.71%. This data indicates the corn cob have low moisture content that cause the material more resistant to microbial damage during storage. Table 3. Corncob Proximate Analysis Result Component % (w/w) %(d.w) Water 10.71 - Ash 1.69 1.89 Protein 0.60 0.67 Fat 2.34 2.62 Fiber 79.15 88.64 Carbohydrate (by difference) 5.51 6.18 Note: % w.w = wet weight percentage; % d.w = dry weight percentage The ash content in corncob was about 1.69%. Ash content shows the amount of inorganic and mineral content in a particular substance. Protein content in corncob was very low, only 0.60 %. This shows that the corncob in this study has not enough nutrition to be applied directly as an animal feed. This corncob has 2.34 % of fat. Fat is an extractive substance that can be dissolved in organic solvent such as eter, aceton, etc. (Fengel and Wegener, 1995). The high content of fiber in the corncob (79.15%) showed that this substance is a good carbon source which support microbial growth, especially microbe that can degrade fiber component (ligninolyticand celullolytic). b) Lignocellulose Content Analysis Lignocellulose is the main component of a crop that represents the amount of organic matter that can be renewed (Sjostrom, 1995). Lignocellulose consists of cellulose, hemicellulose, lignin and some other extractive materials. All components of lignocelluloses can be found in cell walls. The result of lignocelluloses analysis is shown in Table 4. Tabel 4. Composition of Corncob’s Lignocellulosesbefore Delignification Component % d.w Extractive material 4.92 Lignin 19.74 Cellulose 41.45 Hemicellulose 33.91 Note: % d.w = dry weight percentage
  • 13. 204 The initial corncob lignocellulose components analysis showed that corncob has 19.74% lignin content, 41.45%cellulose content and 33.91% hemicellulose. While the corncob that were used by Iswanto in his research (2009) has 15%lignin, 45% cellulose and 35% hemicellulose content. It shows that each corncob has different lignocelluloses compositions. Differences in the chemical composition of the corncob is influenced by several factors such as differences in varieties, place of growth, weather and humidity while harvesting (Shofiyanto, 2008). 2. The Best Fungi Selection The main parameters to select the best fungi is the ability of each fungi which are, Schizophyllum commune,Phanerochaete chrysosporium and isolat Pleurotus EB9 to degrade lignin during 30 days of incubation. The reduction percentage of lignin content by each fungi is shown in Picture 1 as follows. Figure 1 : Percentage of Reduction Corncob Lignin Content After 30 days of incubation, corncob which was incubated with P. chrysosporium has the highest reduction of lignin content level among the other two types of fungi (26.07 %). This fungi has the ability to degrade lignin component of most large corncob among others. Therefore, P. chrysosporium was selected to be used in the main research. Decreasing lignin content by Pleurotus EB9 isolate after 30 days of incubation was very low which was 1.66%. Different from P. chrysosporium which can produce enzyme that can degrade components of phenolic (MnP) and non-phenolic components (lip) at once, Pleurotus EB9 only produces one type of lignin-degrading enzymes which is laccase enzyme. According to Kimura et al. (1990), attempts to detect the activity of the enzyme in lignin peroxidase P.ostreatus under some culture conditions did not show positive results. Sannia et al. (1991) found that there is laccase enzyme activity in white rot fungi Pleurotus. Laccase is a copper-containing phenol oxidase that does not require H2O2 but oxygen (Thurston, 1994). Laccase can oxidize non-phenolic components if there is a mediator such as (2,2- azinobis (3-etilbenzthiazolin-6-sulfonat) or HBT (hydroxybenzotriazol) (Bourbonnais and Paice, 1990). In fact, approximately 90% lignin structure composed of non phenolic unit (Srebotnik et al., 1994). This caused the small decreasing lignin percentage in substrate which incubated with Pleurotus than P. chrysosporium Likewise Pleurotus, S. commune is known as fungi that can degrade lignin by only producing laccase enzyme. The lower end of the weight lignin experienced by the substrate after incubation with S. commune is mainly because the greater dry weight reduction of the substrate. Moreover, corncob also experienced decreasing in its dry weight. Likewise lignin reduction content, corncob that was incubated with P. chrysosporium has the highest reduction dry weight among the othe fungi at 28.22% (Picture 2). Type of Fungi ReductionofLignin
  • 14. 205 Figure 2 : Reduction of Corncob Dry Weight Percentage Reduction of corncob dry weight percentage is one indicator of the existence of biodegradation by fungi. Refer Picture 2, it can be inferred that P. chrysosporium has the highest ability to decrease corncob’s dry weight than the other fungi in this study. Reduction of corncob’s dry weight during incubation happened because there was enzyme produced by the fungi that degrade corncob. According to Hatakka (2001), white-rot fungi produce some kind of enzyme that involved in lignin degradation process, and also produce cellulase, xilanase dan hemicellulase. 3. MAIN RESEARCH 1.Corncob Microscopic Structure Initial fiber corncob microscopic structure and fiber corncob microscopic structure after incubation with P. chrysosporium is shown in Picture 3. In that picture looks thread- like structures called fibrils. Fibrils is a combination molecules of cellulose and contains regular and less regular part. Initial corncob structure Picture 3 (a) shows fibrils structure which still straight arrayed. However, after 30 days of incubation (Picture3 (b) ) it can be seen that fiber structure seems more tenuous. This happened because during the incubation there was degradation activity by enzymes released by fungi, thus causing the cell walls are increasingly porous and produce a honeycomb structure. Cellulose fibrils lysis zones are unprotected and loose (Fengel and Wegener, 1995). Figure 3 : Corncob Fiber Microscopic Structure (400x of zooing): without polarized light (a) before lignification, (b) after 30 days incubation; with polarized light; (c) before delignification, (d) after 30 days incubation Type of Fungi ReductionofDryWeight(%)
  • 15. 206 Corncob appearance with polarized light (Picture 3 (c), (d)), there is a bluish color that shows the structure of crystalline cellulose. On the initial corncob structure (before delignification) appereance there is a structure of crystalline cellulose which characterized by a bluish color. In the 30 days of incubation bluish color in polarized light become less then before. This shows that the lignin content directly proportional with the length of incubation time. According to Knauf and Moniruzzaman (2004), changes in the structure of lignocellulose that has already been pretreated with separation between the cellulose and material that protect it (hemicellulose and lignin). Changes in the structure of cellulose which was originally shaped crystals become amorphous, makes it easy to be hydrolyzed. 2.Biodeliginification by P. chrysosporium a.Dry Weight After Incubation Incubation treatment P. chrysosporium on corncob has caused decreasing and increasing its dry weight. The result of dry weight measurement of initial corncob and post delignification corncob is shown in Picture 4. Figure 4 : Dry weight of Corncob before (initial) and after Delignification Degradation of lignocelluloses component is marked by decreasing of dry weight substance. Enzyme that produced by fungi catalyzes the biochemical reactions in lignocellulose media, so that the holocellulose and lignin can be changed into simpler compounds. Then fungi can absorbed and metabolize these compounds (Herliyana, 1997). However, the results obtained from this study showed an increasing dry weight in both treatments. This increasing dry weight happened due to the fast growth of mycelia. According to Fadilah (2009), the addition of nutrients such as glucose in the medium has two advantages; one of them is the rapid growth of fungi on media. Because of the addition of mycelia, there was an increase in the dry weight of the substrate after delignification. b.Extractive Substance Content Extractive substance consists of several organic compounds such as acids, resins, fatty acids, terpenes and alkaloids (Sjostrom, 1995). Extractive substances have varies molecular weights. The substances can be found in lignocellulose contained materials but not construct the cell wall. The ability of P. chrysosporium degrades extractive component is influenced by the character of its extractive substance. There are some extractive substance in corncob which are 0.7% of fat and uronat acids up to 3.36% (Parajo et al., 2003) (Figure 5). Sample Number DryWeight(g) Initial
  • 16. 207 Figure 5 : Extractive substance content (g/g) which dissolved in etanol:benzene (1:2) before (initial) and after delignification According to Rayner and Boddy (1995) the presence of wood extractive substances can affect the growth of fungi, which acts as a carbon source, as a growth stimulant and as an impediment to growth. Decreasing number of extractive substances happened because it is estimated that the extractive substances contained in the corncob are used as a carbon source by fungi. c.Lignin Content Figure 6 : Lignin Content (g/g) before (initial) and after Delignification by Phanerochaete chrysosporium The results (Figure 6) showed that the incubation time of 37.8 days (Experiment No. 10) causes the higest decrease in lignin content from 0.187 (g/g) to 0.136 (g/g) 32.82%. From the data also found that the longer incubation time, the bigger decrease in corncob lignin content. This shows that the fungi P. chrysosporium is an efficient ligninolytic fungi. d.Cellulose Content Beside degrading lignin components, P. chrysosporium also capable to degrade cellulose. Cellulose degradation is a work of a group of cellulolytic enzymes that work synergistically. Fungi P. chrysosporium produces cellulase enzymes which has similar activity with endogluconases (EGs) and exocellobiohydrolases (CBHs) depends on the carbon source that available (Broda et al., 1996). Cellulose content was decreasing during incubated with P. Chrysosporium (Figure 7). This decreasing shows that during the incubation P. chrysosporium has broken down cellulose component by using cellulolytic enzyme. Initial Initial Sample Number ExtractiveSubstanceContent(g/g) Sample Number LigninContent(g/g)
  • 17. 208 Figure 7 : Cellulose content (g/g) before (initial) and after Incubation Treatment with Phanerochaete chrysosporium Cellulose will be broken down into simpler compounds by fungi which then used as nutrition for its growth. Those compounds then will be used in its metabolism cycles. Additional sugar as nutrition is a factor that decreases cellulose degradation. The more glucose that is added, the less rate of cellulose degradation will happen. This is because the fungi will consume glucose first before degrade cellulose into simpler sugars e. Hemicellulose Content Hemicellulose is biodegraded into sugar monomer and acetic acids with the help hemicellulase enzyme. Hemicelulase as like as many other enzyme which can hydrolize cell wall of plant. Xylan is the main carbohydrates that develop hemicellulose. Xylanase is also the main hemicellulase which hydrolyze β-1,4 bonds. Fungi P. chrysosporium produced endoxylanase that plays a role in the breakdown of xylan into oligosaccharides (Perez et al., 2002). In Picture 8 it can be seen that some samples experienced increasing number of hemicellulose content. Increasing in the hemicellulose content of the substrate can be caused by miscounting of mycelia as part of the hemicellulose. This is probably happened because in some samples mycelial growth rate higher than the rate of degradation of lignocellulosic components. According to Chang and Miles (1989), the average mycelial fungi have fiber content ranging at 7.4%-24.6%. Figure 8 : Hemicellulose content (g/g) before (initial) and after incubation treatment by Phanerochaete chrysosporium Sample Number CelluloseContent(g/g) Sample Number HemicelluloseContent(g/g) Initial Initial
  • 18. 209 3. Influence of Factor against Ratio Lignin/Holocellulose Content Biodelignification process is influenced by some factors which are duration of incubation, amount of nutrition and amount of additional mycelia that is added into media. Those factors can be optimized so that can increase delignification efectivity. Increasing delignification efectivity can be seen from degradation lignin levels by P. chrysosporium. Ideal delignification process is happened when lignin was decomposed in large numbers but holocellulosa components broken down in small amounts. Holocellulose which is a part of the fiber that is free from extractive substances and lignin, consist of all the cellulose and hemicellulose components (Chang and Alan, 1971). Therefore, the main parameter to assess the effectiveness of delignification is decreasing lignin and holocellulose content level. This research measures the influence of incubation time, the amount of mycelia that were added and the amount of glucose that is added to the ratio of lignin/holocellulosa as well as the interaction of these three factors to the ratio of lignin/holocelulose. Relation between factor reaction with response can be determined through a systematic series of experiments that tested through statistical analysis. Table 5. Influence of Linear and Quadratic Factors Against the Ratio of Lignin/Holocellulose Source Probability p > F Effect X1 < 0001 Significant X1*X2 < 0001 Significant X2 0.8335 Not significant X2*X2 0.7999 Not significant X3 0.6172 Not significant X3*X3 0.4023 Not significant Results of statistical analysis (Table 5) showed that both the linear and quadratic effect of incubation time gave a significant effect on the ratio of lignin / holoselulosa. Yet, in this study the addition of mycelia (x2) in delignification process did not decrease lignin content ratio against holocellulose. Though it appears from the graph that the lignin content against holocellulosa ratio slightly decreased with increasing the amount of glucose that is added, but from the linear and quadratic effects analysis it can be inferred that the amount of glucose was not significantly affected the response (Figure 9). Figure 9 : Influence Combination of Length of Incubation Time (day), Amount of mycelia (ml/10 g substrate), Amount of glucose (g/10 g substrate) that is added against ratio lignin/holocellulose Incubation time (day) Incubation time (day) Incubation time (day) Amount of Glucose (g/10 g) Amount of Glucose (g/10 g) Amount of Glucose (g/10 g) Ratio (g/g) Ratio (g/g) Ratio (g/g)
  • 19. 210 Interaction effect between the number of mycelia, length of incubation time and the amount of glucose that is added to the process showed no significant effect to the value ratio lignin/ holoselulosa. It can be seen from the shape of response surface that which not tend to change in various combinations with other factors.It is reinforced by opportunities value p> F that showed interaction effect was not significant (Table 6). Table6. Interaction InfluencebetweenLength of Incubation Time, Amount of Mycelia and Glucosethat is Added againstLignin/Holocellulose Ratio Source* Probability p > F Effect X1- X2 0.8117 Not Significant X1- X3 0.6916 Not Significant X2-X3 0.9754 Not Significant 4.THE BEST CONDITION FOR BIODELIGNIFICATION PROCESS The result of data analysis ratio lignin/holocelluloseat various treatment producedoptimization equation ratio lignin/holocellulose for delignification process as follows. LHN * is symbol for ratio lignin/holocellulose (g/g), x1is length of incubationtime(day), x2is additional mycelia (ml), and x3is additional glucose (g). The results of the canonical analysis to the response surface showed that the response surface model is minimum. This causes the optimum value can be determined from the response surface. Determination of the best conditions of biodelignifikasi process using Phanerochaete chrysosporium is shown in Table 7. Tabel 7. The Best Condition of Biodelignification Process Using Phanerochaete chrysosporium Factor* Code Value X1 0.22 24.25 X2 -0.85 1.89 X3 0.18 0.23 *x1 : Length of Incubation time (day); x2 : Amount of mycelia (ml/10 g substrate) ; x3 : amount of glucose(g/10 g substrate). That condition is estimated giving ratio of lignin content against holoselulosaup to0.210689 g/g. It means there is 0.210689 g of lignin in each 1g of holocellulose. This ratio is obtained in 24.25 days length time of incubation using Phanerochaete chrysosporium, the amount of additional mycelia is 1.89 ml/10 g substrate and the additional glucose is 0.23 g/10 g substrate. 5. CONCLUSION Based on its ability to degrade lignin, Phanerochaete chrysosporium isolate has better capability than Schizophyllum commune and Pleurotus EB9 isolate. This is proven by the decreasing value of lignin content from corncob that was incubated with P. chrysosporium for 30 days at room temperature 26.07o C. Corncob biodelignification process effectiveness using P. chrysosporium can be seen from decreasing ratio lignin/holocellulose level. The result of statistical analysis showed that length of incubation time significantly affected the decreasing of lignin/holocellulose ratio level. However, various additional mycelia and amount of glucose did not significantly affect the decreasing lignin/ holocellulose ratio.
  • 20. 211 From the result of surface respon analysis, it can be inferred that the optimum condition for corncob biodelignification process is determined by response equation model, as follows. LHN * = 0.314541 - 0.007922 x1- 0.000709 x2- 0.061692 x3 + 0.000168 x1 2 + 0.000046 x2 2 + 0.194656 x3 2 + 0.000020 x12- 0.001181 x13 + 0.000246 x23 This equation provided decreasing value of ratio lignin/holoselulosa up to 0.210689 g/g. This ratio derived from 24.25 days of incubation using Phanerochaete chrysosporium on the substrate of corncob with additional mycelia up to 1.89 ml/10 g substrate and the amount of glucose is 0.23 g/10 g substrat. 6. ACKNOWLEDGEMENT Authors thank to the Directorate General of Higher Education - Ministery of National Education R.I for funding this research through Batch I Competitive Grants funding in 2009. REFERENCES [1] [TAPPI] Technical Association of The Pulp and Paper Industry. 1996. TAPPI Test Method. Atlanta: TAPPI Press. [2] Bourbonnais, R. dan M.G. Paice. (1990) Oxidation of nonphenolic substrates : an expanded role for laccase in lignin biodegradation. FEBS Letters. 267:99-102. [3] Broda, P., P.R.J. Birch, P.R. Brooks dan P.F.G. Sims. 1996. Lignocellulose degradation by Phanerochaete chrysosporium: Gene families and gene expression for a complex process. Molecul. Microbiol. 19(5):923-932. [4] Chang, H. M. dan G. G. Allan. 1971. Oxidation. hlm. 463-468. Di dalam K. V. Sarkanen & C. H. Ludwig (Penyunting). Lignins: Occurance Formation, Stucture and Reactions. JohnWiley & Sons, New York. [5] Chang, S.T, dan P.G. Miles. 1989. Edible Mushrooms and Their Cultivation. Florida: CRC Press, Inc. 451p. [6] Eaton, R. A. dan M.D.C. Hale. 1993. Wood, Decay, Pest and Protection. Chapman and Hall, London. [7] Fadilah, S. Distantina, S. R. Dwiningsih, dan D. R. Ma’rifah. 2009. Pengaruh penambahan glukosa dan ekstrak yeast terhadap biodelignifikasi ampas batang aren.EkuilibriumVol. 8. No. 1: 29 –33. [8] Fengel, D. dan G. Wegener. 1995. Kimia Kayu, Reaksi Ultrastruktur: Terjemahan Sastrohamidjojo, H,. Gadjah Mada University Press, Yogyakarta. [9] Hatakka, A. 2001. Biodegradation of lignin. In: Steinbüchel, A. [ed] Biopolymers. Vol 1: Lignin, Humic Substances and Coal. Germany: Wiley VCH. pp. 129-180. [10] Herliyana, E. N. 1997. Potensi Schizophyllum commune dan Phanerochaete chrysosporium untuk pemutihan pulp kayu Acacia mangium dan Pinus merkusii [tesis]. Program Studi Entomologi/Fitopatologi Program Pascasarjana IPB, Bogor. [11] Iswanto, A. H. 2009. Fungsi Polimer Alami: Terbentuknya Dimensi Baru dalam Kimia Lignoselulosa. Makalah: Fakultas Pertanian Univesitas Sumatera Utara. [12] Kimura, Y., Y. Asada, dan M. Kuwahara. 1990. Screening of basidiomycetes for lignin peroxidase genes using a DNA probe. Appl. Microbiol. Biotechnol. 32:436-442. [13] Knauf, M. dan M. Moniruzzaman. 2004. Lignocellulosic Biomass Processing: A Perspective. International Sugar Jurnal 106 : 147-151. [14] Koswara, J. 1992. Budidaya Jagung. Jurusan Budidaya Pertanian, Fakultas Pertanian, IPB, Bogor. [15] Martina, A., N. Yuli dan M. Sutisna. 2002. Optimasi beberapa faktor fisik terhadap laju degradasi selulosa kayu albasia (Paraserianthesfalcataria (L.)) Nielsen dan Karboksimetilselulosa (CMC) secara enzimatik oleh fungi. Jurnal Natur Indonesia 4(2): 156-163. [16] Parajo, J. C., Garotte, J.M. Cruz, dan H. Dominguez. 2003. Production of Xyloligosaccharides by Autohydrolisis of Lygnocellulosic Materials. Trends in Food Science and Technology Vol. 15 : 115-120. [17] Perez, J., J. Munoz-Dorado, T. de la Rubia, dan J. Martinez. 2002. Biodegradation and biological treatments of cellulose, hemicellulose and lignin: an overview. Int. Microbiol. 5:53-63.
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