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THE COMBINATION OF SEAWEED AND ACTIVE
 SLUDGE BIOFILTER AS A WATER TREATMENT
SUPPLY FACILITIES ON THE FISH REARING TANK



   RESEARCH PAPER
     Presented at Indonesian Aquaculture 2010
     BANDAR LAMPUNG, 4 – 6 OKTOBER 2010


                      By :
                ROMI NOVRIADI
                 MUH KADARI




MINISTRY OF FISHERIES AND MARINE AFFAIRS
 DIRECTORATE GENERAL OF AQUACULTURE
BATAM MARICULTURE CENTRE DEVELOPMENT
                  2010
VALIDATION SHEET

  THE COMBINATION OF SEAWEED AND ACTIVE
  SLUDGE BIOFILTER AS A WATER TREATMENT
 SUPPLY FACILITIES ON THE FISH REARING TANK


                      Prepared by :
                 The Engineering Leader




                      ( Romi Novriadi )




                       Approved by :


Engineering Manager            Head of Batam Mariculture
                               Centre Development




( Muh Kadari )                 ( Dr. Djumbuh Rukmono, MP)
THE COMBINATION OF SEAWEED AND ACTIVE SLUDGE BIOFILTER AS
 A WATER TREATMENT SUPPLY FACILITIES ON THE FISH REARING
                         TANK

                                     By:
                       Romi Novriadi and Muh Kadari
                  Mariculture Centre Development of Batam
            Jl. Raya Barelang, 3rd Bridges, Setokok-Batam Island
                    PO BOX 60 Sekupang, Batam - 29422
                       E-mail: Romi_bbl@yahoo.co.id

                                 ABSTRACT


       Biologically, the objectives of Water quality management are to reduce
the soluble components, particularly organic compounds until the safety limits
of the environment by utilizing microorganisms and / or plants. In order to set
aside the dissolved organic matter, the microorganisms will use the organic
materials as nutrients for growth into new cells and carbon dioxide.
Biotransformation process occurs in a variety of ways according to the
microorganisms involved in it, for example the autotrof or heterotrophic
microbes type.

      One of the biofiltration techniques that can be done to produce the
optimal water quality for fish rearing media is by doing a combination of active
sludge and Seaweed as a biofilter. The usage of activated sludge because of
the ability of microbes that live on the sludge substrates can decomposed
organic elements, particularly the toxic as NH3 and NO2. while the usage of
seaweed because of its absorbent properties, and also can change the
carbon dioxide into dissolved oxygen in water, so it is expected other than to
produce clear water also has its own freshness for fish.

        Results of the experiments conducted by the Year 2009 funds shows
that the Combination of this biofiltration system Seaweed and active sludge is
quite effective to produce the optimal water quality for fish rearing media. NH3
concentration can be reduced up to 80%, and NO2 can be reduced up to 20-
60%. For the parameters of turbidity and TDS, with this combination Biofilter
systems can reduce water turbidity levels up to 75-98% and reduce the
amount of total dissolved solids as much as 15-73%. While seaweed has a
role to be effective in increasing dissolved oxygen levels up to 24%.


Keywords: Biofilter Combination, Sludge, Sea Grass, Water Quality
CHAPTER I
                               INTRODUCTION

I.1 Background

     The Increasing use of marine coastal areas as aquaculture land In
Indonesia allegedly to be the cause of decreased quality of the environment
for the provision of quality water for the aquaculture fish life habitat.
Deforestation of mangrove forests for fish culture in the floating net cages will
stimulate the occurrence of water pollution, because the buffer system in
coastal waters will be disturbed. This situation is also exacerbated by the fish
feed management and route of administration that is not appropriate.

      In the provision of quality water, we need to analyse the layout of land
that we use for fish culture. According to Romi.N, (2008) this is related to
organic waste generated has a complementary relationship with the number
of general bacteria in the waters. If waste water is reused for the culture
media without going through the filtration system, there will be a separate
obstacle for the growth of fish. On the basis of observations made during the
year 2009, the presence of bacteria in the culture media are not much
different from the presence of bacteria in the waters surrounding the water
points. That is why the screening process for the improvement of water quality
to be more important.

       According to Anonymous. 2002, the process of aquaculture wastewater
treatment can be done in biologically aerobics, in which the biological waste
water treatment is to utilize the aerobic activity of aerobic microbes, to
describe the organic substances contained in waste water of cultured fish, to
be the inorganic substance that is more stable and has little impact pollution
to the surrounding environment. Aerobic microbes actually already there in
the nature and can be obtained very easily. Fishery waste water treatment
can also be done using the natural materials, one of which is sea weed,
because according to Dedi Sofian, 2006, Seaweed able to neutralize the
fishery waste water. and naturally, seaweed have a function as a filter of
carbon dioxide, which is absorbed and transformed into the oxygen. So, with
more number of oxygen contained in the water, then it will provide freshness
for fish and other biota

         Therefore, at this engineering, the writer trying to make a water
filtration system that is simple, economical, applicable but effective enough to
produce the optimal water quality for fish culture media, through a
combination of activated sludge filtration system and seaweed. This simple
system can be applied by fish farmers.
I.2 Problems

Based on the background that has been presented above, some problems
that will be taken at this engineering are:

1. What the percentage of the effectiveness of this Combination biofiltration
   system between Seaweed and active sludge in reducing the toxic
   elements such as NH3 and NO2?
2. What the percentage of the effectiveness of this Combination biofiltration
   system between Seaweed and active sludge in reducing the turbidity and
   total dissolved solids?
3. How the relevance between activated sludge as a filter of carbon dioxide,
   which is absorbed and converted into oxygen concentration to the
   dissolved oxygen in the water?

I.3 Hypotesis

   Suspected that the accumulation of aquaculture activities have caused the
degradation of the water quality so it need a filtration system for improving
and maintaining the optimization of water quality.

I.4 Goal

This Engineering aims to:
1. Knowing the effect of this Combination biofiltration system between
   Seaweed and active sludge as a supply of quality water for the fish culture
   media.
2. Knowing the influence of this Combination biofiltration system between
   Seaweed and active sludge in reducing the toxic elements such as
   Ammonia and Nitrite and reduce the level of turbidity and total dissolved
   solids in water.
3. To produce the Applied technology that is effective and economical for the
   fish farmers.
CHAPTER II
                          EXPERIMENT METHODOLOGY

II.1 Time and Place

   The Engineering with the title of Combination biofiltration system between
   Seaweed and active sludge was held in Batam Mariculture Centre
   Development, starting from November 1st, 2009 untul 29th December,
   2009.

II.2 Tool and Material

II.2.1 Engineering tool

Two tank of fish culture               Measurement glass
Actived sludge tank culture            Statif and Klem
Sedimentation tank                     Beaker glass
DO meter Oxyguard model                Petri disk
HACH DR/890 Colorimeter                Incubator
HANNA C203 Ion Spectrometer            Oven
Nephelometer Turbidity Unit            Hot plate
HANNA TDS Meter                        Culture of bacterial tool set
UV light                               Sample bottle
COD meter                              Fish culture tool set

II.2.2 Material of engineering

Decomposition bacteria                 pH Buffer 7.00
Mix liquor Suspended Solid             pH Buffer 4.00
Seaweed                                pH Buffer 10.00
Coral reef                             Posphat Low Range
Molase                                 Free chlorine reagen for HANNA
Sea bass (Lates calcarifer)            NaOH 0,1 N
Sponge                                 HCl 0,1 N
Ammonia salycilate reagen              KCl 0,2 N
Ammonia cyanurate reagen               CH3COOH 0,5 N
NitraVer reagen                        Phenolphtalein indicator
NitriVer reagen                        Metil Orange indicator
Free chlorine reagen                   H2SO4 4 N
PCA (Plate Count Agar)                 HNO3 4 N
II. 3 Procedure

a. The Making Stages of Biofilter Tank
     Cutting of material used: at this stage the PVC pipes was cut
       accordance to the requirements of biofilter system.




               (a)                         (b)                 (c)
       Figure 1. Cutting the material. (a) the preparation of the oxygen tube
       that is destined for the activated sludge basin, (b) the prepare of water
       and aeration systems, and (c) deduction tank for the activated sludge.

      Setup: The bacterial culture tank with coral substrate and activated
       sludge are mounted on the drum and positioned adjacent to the first
       tank of biofilter system, the First is a sedimentary tank containing sea
       weed, and the second and the third tank is a culture tank for the test
       fish (Sea bass Lates calcarifer, Bloch)

                                                        Sedimentary tank
                                                           +seaweed

                                                     Activated sludge drum
                                                          + Coral reef


                                                        Tank for test fish


                                                        Tank for test fish
The design of Combination biofiltration system between Seaweed and active
                    sludge was illustrated as below :




                  Sedimentary tank +   Tank for test fish   Tank for test fish
                      Seaweed




b. Bacterial inoculation

       The Source of decomposition bacterial can be obtained from the
nature. The bacteria are available in the sufficient quantities in many places of
waste elements decomposition. Such as in the floating net cages area. the
remnants of feed is broken down by bacteria found in the base of floating net
cages. Bacteria taken by lifting 1 kg sludge from the bottom of cage and then
diluted with 1 liter of seawater. Then, This bacteria was added into each
compartment of biofilter drum. The addition of sludge was carried out while
water continues to flow, so the bacteria will naturally selected. This process is
allowed to continue running until the filters can be declared ready for use (Set
up). At every 3 days of inoculation were observed on the growth of the
number of bacteria produced

c. Preparation of activated sludge
                              Drums that cater to the activated sludge, then
                              loaded mud as a substrate and the Inoculate
                              bacteria which has been declared ready for use
                              into the derum. The growth of microorganisms
                              will work well enough if the nutrients available,
                              namely nitrogen and phosphorus that play a role
                              in the synthesis of the cell is proportional to the
                              biodegrable organic material contained in waste
                              water. As the food provided artificial substrate
                              composed of glucose (sugar), in this case is
                              done by giving molasses.

This work begins with providing waste water in small amounts, and if the
microorganism has been grown, gradually, the amount of wastewater
enlarged its comparison to an artificial substrate, until at last only a sheer
waste water. To determine whether there is growth of these microorganisms,
carried out with the observation of dissolved oxygen. At the time of waste
water given, the Dissolved oxygen (DO) concentration will go down. After
some time aerated, DO will gradually rise, and someday she will return as the
original, and it will give the information to us that the assimilation process has
been completed and microorganisms have been grown.
d. Preparation of Seaweed Tank
       The type of seaweed that we used in this engineering is E. Cottoni and
inserted into the first tank as well as a sedimentation tank.The Installation of
seaweed done in a long line around the tank with rope 150 cm long.

e. Installation of UV lights
       Installation of UV lights aim to reduce the bacteria that entered to the
water medium after the activated sludge process which involves a lot of active
microorganisms as its main component. Installation of UV lights is right in line
where the water enters into the culture media.

f. Preparation of Sea bass as fish test
        To see and evaluate the performance of the Biofilter system
combination between activated sludge and seaweed, The fish test was culture
in two way, first, in the tank with Biofilter combination and second, without the
biofilter as a control of the system. The Commercial feed for fish test given 3
times a day, at the morning, afternoon and evening by adlibithum. To remove
the excess dirt, feeding remain and other impurities was carried by cleaning
the bottom of tank every evening after completion of feeding. The culture of
test fih was conducted for 30 days.

g. Test of the filters effectiveness
        To determine the ability and the effectiveness of this biofilter system
combination between activated sludge and seaweed is done by the laboratory
testing. The observation was performed by comparing the quality of water that
passes through this biofilter combination and to the control water (without
pass the biofilter system). The parameters observed include: NH3, NO2 NO3,
turbidity, BOD and COD. Observations made during one month from 25th
November 2009 to December 28th, 2009.
CHAPTER III
                                                            RESULTS AND DISCUSSION
III.1 Result
1. Graphic of inoculation bacterial growth (with molase)

                                                     Grafik Pertumbuhan Bakteri Inokulasi

                              1200

                              1000
      Jumlah Bakteri (TBU)




                                   800
                                                                                                            Grafik Pertumbuhan
                                   600
                                                                                                            Bakteri Inokulasi
                                   400

                                   200

                                     0
                                              1              2         3                4
                                                            Sampling Ke-



Note : The number of general bacterial multiple with102 CFU/ml

2. Result of Turbidity and TDS analysis
                                           TEST RESULT
      Date of        After through the biofilter   Without Biofilter (control)
     Analysis        Turbidity          TDS        Turbidity           TDS
                      (NTU)            (mg/l)       (NTU)             (mg/l)
  08 November          0,49             31.2         0.49              31,5
  15 November          0,15             27,9         0,42              32,3
  22 November          0,02              8,4         0.38              31,4
  29 November          0,01              8.4         0,51              30,2
  05 December          0,02              9,1         0,56              30,3
  11 December          0,02              8,7         0,59              30,6
  16 December          0,01              8,3         0,54              32,8
  22 December          0,02              8,4         0,43              32,1

                                          Graphic of Turbidity                                               Graphic of TDS

                             0.7                                                                   35
                             0.6                                   Turbidity after                 30
   Turbidity (NTU)




                                                                                     TDS (mg/l))




                             0.5                                   pass the                        25                            TDS after pass
                             0.4                                   biofilter                       20                            the biofilter"
                             0.3                                   control                         15                            control
                             0.2                                                                   10
                             0.1                                                                    5
                               0                                                                    0
                                     8. nov
                                    15.Nov
                                    22.Nov
                                    29.Nov




                                                                                                         8. nov
                                                                                                        15.Nov
                                                                                                        22.Nov
                                                                                                        29.Nov
                                     5.des
                                    11.des
                                    16.des
                                    22.des




                                                                                                         5.des
                                                                                                        11.des
                                                                                                        16.des
                                                                                                        22.des




                                         Date of analysis                                                Date of analysis
Hasil Analisa Kadar Ammonia dan Nitrit pada air input media pemeliharaan

                                                                 HASIL UJI
                Date of                                       TEST RESULT
                Analysis                After through the biofilter     Without Biofilter (control)
                                          NH3              NO2              NH3             NO2
                                         (mg/l)           (mg/l)           (mg/l)          (mg/l)
      08 November                         0.13             0,07             0,13            0,07
      15 November                         0.08             0,06             0,11            0,06
      22 November                         0,01             0,06             0,11            0,06
      29 November                           --             0,05             0,09            0,06
      05 December                         0,01             0,04             0,11            0,05
      11 December                           --             0,01             0,14            0,06
      16 December                           --             0,01             0,09            0,07
      22 December                           --             0,01             0,12            0,07


                           Graphic of NH3 (ammonia)                                                         Graphic of NO2 (Nitrit)

         0.16                                                                                 0.08
         0.14                                                                                 0.07
         0.12                                                                                 0.06
 NH3 (mg/l))




                                                                                      NO2 (mg/l))
                                                         NH3 after pass the                                                             NO2 after pass the
          0.1                                            biofilter"""                         0.05                                      biofilter"""""""
         0.08                                                                                 0.04
         0.06                                            control                              0.03                                      control
         0.04                                                                                 0.02
         0.02                                                                                 0.01
            0                                                                                    0
               1 v




               1 s
               2 v
               2 v
                5dv




                                                                                                    1 v
               1 s
               2 s
                   s




                                                                                                    1 s
                                                                                                    2 v
                                                                                                    2 v
                                                                                                     5dv
                   o




                                                                                                    1 s
                                                                                                    2 s
                                                                                                        s
                 .e
                 .o
                 .o
                 .o




                                                                                                        o




                                                                                                      .e
                 .e
                 .e
                 .e




                                                                                                      .o
                                                                                                      .o
                                                                                                      .o
                 .n




                                                                                                      .e
                                                                                                      .e
                                                                                                      .e
                5N
                2N
                9N




                                                                                                      .n
                                                                                                     5N
                                                                                                     2N
                                                                                                     9N
                1d
                6d
                2d




                                                                                                     1d
                                                                                                     6d
                                                                                                     2d
                8




                                                                                                     8




                            Date of analysis                                                               Date of analysis


Dissolved oxygen at culture tank analysis
                     Hasil Analisa
      Date of     Oksigen Terlarut                                                                   Graphic of Dissolved oxygen (DO)
     Analysis            (mg/l)
                                                                                     8
                                     After             Without                       7
                                 through the          Biofilter                      6                                                  DO after pass the
                                                                              DO(mg/l))




                                                                                     5                                                  biofilter""""""""""""""
                                   biofilter          (control)
                                                                                     4                                                  "
      08 November                     5,0                5,1                         3                                                  control
      15 November                     5,7                4,9                         2
      22 November                     6,4                5,4                         1
      29 November                     6,9                5,0                         0
      05 December                     6,5                5,2
                                                                                     1 v
                                                                                     2 v
                                                                                     2 v
                                                                                          v
                                                                                          s

                                                                                     1 s
                                                                                     2 s
                                                                                         es
                                                                                          o




                                                                                        .e
                                                                                         o
                                                                                         o
                                                                                         o


                                                                                         e
                                                                                         e
                                                                                       .n
                                                                                      5.N
                                                                                      2.N
                                                                                      9.N




      11 December
                                                                                      5d




                                      6,7                5,3
                                                                                      1.d
                                                                                      6.d
                                                                                      2.d
                                                                                      8




                                                                                     1




      16 December                     6,9                4,7                                            Date of analysis
      22 December                     6,8                4,9
The comparation of Total Number of General bacterial (TBU) between after
and before through the UV light


                            Perbandingan TBU sebelum dan sesudah UV

                      300
  Jumlah TBU (x100)



                      250

                      200
                                                                            TBU Sebelum UV
                      150
                                                                            TBU setelah UV
                      100

                      50
                       0
                             1   2   3   4     5   6   7    8   9   10 11
                                             Sampling Ke-



IV.2 Discussion

       From the results of experiments it was found that the inoculated
bacteria in activated sludge substrates had been developed. On the fourth
day of sampling, the total number of bacteria produced was 9.7x106 CFU/ml.
This number may be used temporarily as an indicator that the filter is ready for
use.

        This situation is also correlated with a reduction of NH3 and NO2
concentration. The concentration of NH3 in the water filtration system results
in the range: 0.01 to 0.13 mg / l, while the water control, the NH3 are between:
0.09 to 0.14 mg / l. This means this biofilter combination system can reduce
the NH3 concentration until 80%. The fall of this ammonia levels, probably
caused by the oxidation of ammonia to the nitrate elements which is done by
Nitrosomonas bacteria that grow on the sludge media in the filtration system.

         Meanwhile for NO2, the concentration resulting in water with this
filtration system was also down, although only slightly, which is in range: 0.01
to 0.07 mg / l, compared with control water, which have concentrations of NO2
from 0.05 to 0, 07 mg / l. Nitrite in biological filtration system will be
transformed by Nitrobacter bacteria into nitrates element, and then in
inaerobic conditions it will converted into the nitrogen (Coklin and Chang,
1983).
For the turbidity and Total Dissolved Solid parameter in the water, they
have significant reduction. This is probably due to the function of material that
we used in this biofilter combination, they are activated sludge and seaweed.
This biofilter system result the Turbidity concentration between 0.01 to 0.15
mg/l, while the turbidity concentration of control water are : 0,38 to 0,59 mg / l.
This means there is 75 – 98% reduction of turbidity in the water with this
biofilter system. For the TDS (Total Dissolved Solid) concentration. The
number of TDS in water that pass this biofilter system combination are from
8.3 to 27.9 mg / l while on the control water control are 30.2 to 32.8 mg/l. It
means that the reduction of TDS concentration is as much as 15-73%.

       Associated with the presence of seaweed as an natural filters in the
sedimentation tank, where the seaweed, naturally have a function as a filter of
carbon dioxide, which are absorbed and converted into the oxygen element.
So the measurement of dissolved oxygen concentrations was done at the fish
culture tank with the combination biofilter system and control. The result
showed that DO levels that exist in the fish culture tanks with filtration system
are 5.0 to 6.9 mg/l, while the DO concentration at control tank were 4.7 to 5.3
mg/l.

Filter with the combination of activated sludge and seaweed can be
operationalized for 6 (six) months. And after that the materials that we used at
this biofilters system should be cleaned. Some benefits of this combination
Biofilter systems include:
1. Guarantee obtaining a good water quality for fish culture tank
2. Economical, Efficient and Effective in producing high water quality
3. Easily applied by fish farmers
CHAPTER IV
                     CONCLUSION AND SUGGESTION

V.1 Conclusions

1. This combination Biofilter system between activated sludge and seaweed
   is quite effective in reducing of toxic elements such as NH3 and NO2, in
   which the ammonia concentration was reduced until 80%, while for the
   levels of NO2 was reduced up to 20-60%.
2. This combination Biofilter system between activated sludge and seaweed
   is quite effective in improving the clarity of water, because it can reduce
   the turbidity levels up to 75-98%., and reduce the amount of total dissolved
   solids between 15 to 73%.
3. Seaweed as a filter which is placed in the sedimentation tank through its
   function can play an active role in improving of dissolved oxygen
   concentration up to 24%.
4. This combination Biofilter system between activated sludge and seaweed
   is quite economical, efficient, effective and can be applied directly by the
   fish farmers


V.2 Suggestion

1. Need to do further study on the effectiveness of seaweed in absorption of
   heavy metals that dissolved in the water.
2. Observations on the effectiveness of combination Biofilter between
   activated sludge and seaweed can also be undertaken in a long time
   periode. In order to know the exact impact and benefits from this system.
LITERATURE

Anonim. Limbah. http://id.wikipedia.org/wiki/Limbah.
Anonim.Pencemaran.http://www.dephut.go.id/INFORMASI/SETJEN/PUSSTA
     N/info_5_1_0604/isi_5.htm
Anonim, 2008, Laporan Bulanan Kesehatan Ikan dan Lingkungan, Balai
     Budidaya Laut Batam, Kepulauan Riau.
Anonim. 2008. Instalasi Pengolahan Air Limbah (IPAL).http://www.lenn-
     biz.com/?q=ipal
Anonim.     2002.    Membangun       Instalasi   Pengolahan    Air  Limbah.
     http://www.korantempo.com/news/
Bapedal 1995. Teknologi Pengendalian Dampak Lingkungan Industri
     Penyamakan Kulit.. Jakarta.
Bishalf, W. 1993. Abwasser Technik. B. G. Teuber, Stuttgart. Koesoebiono.
     1984. Industri Tapioka Penanganan Limbah Cair dan Padat. Makalah
     pada Lokakarya Pemanfaatan Limbah Industri Tapioka, Bogor, 19-20
     Juli 1984.
Gaudy, A.Fand Gaudy, E. T, Microbiology for Environmental Scientist and
     Engineers, Mc. Graw Hill,1980.
Hutagalung,      Michael.    2007.     Teknologi     Pengolahan    Sampah.
     http://www.majarikanayakan.com/2007/12/teknologi-pengolahan-
     sampah
Loehr, R.C. 1974. Agricultural Waste Management. Academic Press, New
     York
Metcalf and Eddy. 1991. Waste Water Engineering. P ed. McGraw-Mll, Inc.
     New York
Novriadi, R, 2009, Optimalisasi Kualitas Air Melalui Sistem Filterisasi
     Cartridge Anion Kation dan Lampu UV Terintegrasi, Balai Budidaya Laut
     Batam, Kepulauan Riau.
Nathanson, J. A. 1997. Basic Environmental Technology 2nd ed. Prentica
     Hall, Ohio.
Rydin,S. 1996. Research Needs for the European Lether Industry. European
     Workshop on Environmental Technology. Copenhagen, 13-15
     November 1996.
Subagyo, Ir, MSc. 2008. Biological Unit Process. Materi Kuliah Pengolahan
     Air Limbah Jurusan Ilmu Kelautan Fakultas Perikanan dan Ilmu Kelautan
     Universitas Diponegoro Semarang.
Sugiharto. 1987. Dasar-dasar Pengolahan Air Limbah. UI Press, Jakarta.
Sudrajat Y, dan Gunawan B, 2002, Sistem Bakteriofiltrasi Sebagai Sarana
     Pasokan Air Pada Penampungan Ikan Hidup, Buletin Teknik Pertanian,
     Volume VII, Jakarta
Webster, T.S, ad Devinny, J.S. 1996. Biofiltrasi of Odors, Toxic and Volatile
     Organic Compounds from Publicity Owned Treatment Works, Env.
     Progress, Vol. 15, No. 3, P. 141-147.
Wenas, R.I.F, Sunaryo, dan Styasmi, S. 2002. Comperative Study on
     Characteristics of Tannery, "Kerupuk Kulit", "Tahu-Tempe" and Tapioca
     Waste Water and the Altemative of Treatment. Environmental
     Technology. Ad. Manag. Seminar, Bandung, January 9-10, 2003 p. Pos
     5-1 - pos 5-8.

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The combination of seaweed and active sludge biofilter as a water treatment supply facilities on th

  • 1. THE COMBINATION OF SEAWEED AND ACTIVE SLUDGE BIOFILTER AS A WATER TREATMENT SUPPLY FACILITIES ON THE FISH REARING TANK RESEARCH PAPER Presented at Indonesian Aquaculture 2010 BANDAR LAMPUNG, 4 – 6 OKTOBER 2010 By : ROMI NOVRIADI MUH KADARI MINISTRY OF FISHERIES AND MARINE AFFAIRS DIRECTORATE GENERAL OF AQUACULTURE BATAM MARICULTURE CENTRE DEVELOPMENT 2010
  • 2. VALIDATION SHEET THE COMBINATION OF SEAWEED AND ACTIVE SLUDGE BIOFILTER AS A WATER TREATMENT SUPPLY FACILITIES ON THE FISH REARING TANK Prepared by : The Engineering Leader ( Romi Novriadi ) Approved by : Engineering Manager Head of Batam Mariculture Centre Development ( Muh Kadari ) ( Dr. Djumbuh Rukmono, MP)
  • 3. THE COMBINATION OF SEAWEED AND ACTIVE SLUDGE BIOFILTER AS A WATER TREATMENT SUPPLY FACILITIES ON THE FISH REARING TANK By: Romi Novriadi and Muh Kadari Mariculture Centre Development of Batam Jl. Raya Barelang, 3rd Bridges, Setokok-Batam Island PO BOX 60 Sekupang, Batam - 29422 E-mail: Romi_bbl@yahoo.co.id ABSTRACT Biologically, the objectives of Water quality management are to reduce the soluble components, particularly organic compounds until the safety limits of the environment by utilizing microorganisms and / or plants. In order to set aside the dissolved organic matter, the microorganisms will use the organic materials as nutrients for growth into new cells and carbon dioxide. Biotransformation process occurs in a variety of ways according to the microorganisms involved in it, for example the autotrof or heterotrophic microbes type. One of the biofiltration techniques that can be done to produce the optimal water quality for fish rearing media is by doing a combination of active sludge and Seaweed as a biofilter. The usage of activated sludge because of the ability of microbes that live on the sludge substrates can decomposed organic elements, particularly the toxic as NH3 and NO2. while the usage of seaweed because of its absorbent properties, and also can change the carbon dioxide into dissolved oxygen in water, so it is expected other than to produce clear water also has its own freshness for fish. Results of the experiments conducted by the Year 2009 funds shows that the Combination of this biofiltration system Seaweed and active sludge is quite effective to produce the optimal water quality for fish rearing media. NH3 concentration can be reduced up to 80%, and NO2 can be reduced up to 20- 60%. For the parameters of turbidity and TDS, with this combination Biofilter systems can reduce water turbidity levels up to 75-98% and reduce the amount of total dissolved solids as much as 15-73%. While seaweed has a role to be effective in increasing dissolved oxygen levels up to 24%. Keywords: Biofilter Combination, Sludge, Sea Grass, Water Quality
  • 4. CHAPTER I INTRODUCTION I.1 Background The Increasing use of marine coastal areas as aquaculture land In Indonesia allegedly to be the cause of decreased quality of the environment for the provision of quality water for the aquaculture fish life habitat. Deforestation of mangrove forests for fish culture in the floating net cages will stimulate the occurrence of water pollution, because the buffer system in coastal waters will be disturbed. This situation is also exacerbated by the fish feed management and route of administration that is not appropriate. In the provision of quality water, we need to analyse the layout of land that we use for fish culture. According to Romi.N, (2008) this is related to organic waste generated has a complementary relationship with the number of general bacteria in the waters. If waste water is reused for the culture media without going through the filtration system, there will be a separate obstacle for the growth of fish. On the basis of observations made during the year 2009, the presence of bacteria in the culture media are not much different from the presence of bacteria in the waters surrounding the water points. That is why the screening process for the improvement of water quality to be more important. According to Anonymous. 2002, the process of aquaculture wastewater treatment can be done in biologically aerobics, in which the biological waste water treatment is to utilize the aerobic activity of aerobic microbes, to describe the organic substances contained in waste water of cultured fish, to be the inorganic substance that is more stable and has little impact pollution to the surrounding environment. Aerobic microbes actually already there in the nature and can be obtained very easily. Fishery waste water treatment can also be done using the natural materials, one of which is sea weed, because according to Dedi Sofian, 2006, Seaweed able to neutralize the fishery waste water. and naturally, seaweed have a function as a filter of carbon dioxide, which is absorbed and transformed into the oxygen. So, with more number of oxygen contained in the water, then it will provide freshness for fish and other biota Therefore, at this engineering, the writer trying to make a water filtration system that is simple, economical, applicable but effective enough to produce the optimal water quality for fish culture media, through a combination of activated sludge filtration system and seaweed. This simple system can be applied by fish farmers.
  • 5. I.2 Problems Based on the background that has been presented above, some problems that will be taken at this engineering are: 1. What the percentage of the effectiveness of this Combination biofiltration system between Seaweed and active sludge in reducing the toxic elements such as NH3 and NO2? 2. What the percentage of the effectiveness of this Combination biofiltration system between Seaweed and active sludge in reducing the turbidity and total dissolved solids? 3. How the relevance between activated sludge as a filter of carbon dioxide, which is absorbed and converted into oxygen concentration to the dissolved oxygen in the water? I.3 Hypotesis Suspected that the accumulation of aquaculture activities have caused the degradation of the water quality so it need a filtration system for improving and maintaining the optimization of water quality. I.4 Goal This Engineering aims to: 1. Knowing the effect of this Combination biofiltration system between Seaweed and active sludge as a supply of quality water for the fish culture media. 2. Knowing the influence of this Combination biofiltration system between Seaweed and active sludge in reducing the toxic elements such as Ammonia and Nitrite and reduce the level of turbidity and total dissolved solids in water. 3. To produce the Applied technology that is effective and economical for the fish farmers.
  • 6. CHAPTER II EXPERIMENT METHODOLOGY II.1 Time and Place The Engineering with the title of Combination biofiltration system between Seaweed and active sludge was held in Batam Mariculture Centre Development, starting from November 1st, 2009 untul 29th December, 2009. II.2 Tool and Material II.2.1 Engineering tool Two tank of fish culture Measurement glass Actived sludge tank culture Statif and Klem Sedimentation tank Beaker glass DO meter Oxyguard model Petri disk HACH DR/890 Colorimeter Incubator HANNA C203 Ion Spectrometer Oven Nephelometer Turbidity Unit Hot plate HANNA TDS Meter Culture of bacterial tool set UV light Sample bottle COD meter Fish culture tool set II.2.2 Material of engineering Decomposition bacteria pH Buffer 7.00 Mix liquor Suspended Solid pH Buffer 4.00 Seaweed pH Buffer 10.00 Coral reef Posphat Low Range Molase Free chlorine reagen for HANNA Sea bass (Lates calcarifer) NaOH 0,1 N Sponge HCl 0,1 N Ammonia salycilate reagen KCl 0,2 N Ammonia cyanurate reagen CH3COOH 0,5 N NitraVer reagen Phenolphtalein indicator NitriVer reagen Metil Orange indicator Free chlorine reagen H2SO4 4 N PCA (Plate Count Agar) HNO3 4 N
  • 7. II. 3 Procedure a. The Making Stages of Biofilter Tank  Cutting of material used: at this stage the PVC pipes was cut accordance to the requirements of biofilter system. (a) (b) (c) Figure 1. Cutting the material. (a) the preparation of the oxygen tube that is destined for the activated sludge basin, (b) the prepare of water and aeration systems, and (c) deduction tank for the activated sludge.  Setup: The bacterial culture tank with coral substrate and activated sludge are mounted on the drum and positioned adjacent to the first tank of biofilter system, the First is a sedimentary tank containing sea weed, and the second and the third tank is a culture tank for the test fish (Sea bass Lates calcarifer, Bloch) Sedimentary tank +seaweed Activated sludge drum + Coral reef Tank for test fish Tank for test fish
  • 8. The design of Combination biofiltration system between Seaweed and active sludge was illustrated as below : Sedimentary tank + Tank for test fish Tank for test fish Seaweed b. Bacterial inoculation The Source of decomposition bacterial can be obtained from the nature. The bacteria are available in the sufficient quantities in many places of waste elements decomposition. Such as in the floating net cages area. the remnants of feed is broken down by bacteria found in the base of floating net cages. Bacteria taken by lifting 1 kg sludge from the bottom of cage and then diluted with 1 liter of seawater. Then, This bacteria was added into each compartment of biofilter drum. The addition of sludge was carried out while water continues to flow, so the bacteria will naturally selected. This process is allowed to continue running until the filters can be declared ready for use (Set up). At every 3 days of inoculation were observed on the growth of the number of bacteria produced c. Preparation of activated sludge Drums that cater to the activated sludge, then loaded mud as a substrate and the Inoculate bacteria which has been declared ready for use into the derum. The growth of microorganisms will work well enough if the nutrients available, namely nitrogen and phosphorus that play a role in the synthesis of the cell is proportional to the biodegrable organic material contained in waste water. As the food provided artificial substrate composed of glucose (sugar), in this case is done by giving molasses. This work begins with providing waste water in small amounts, and if the microorganism has been grown, gradually, the amount of wastewater enlarged its comparison to an artificial substrate, until at last only a sheer waste water. To determine whether there is growth of these microorganisms, carried out with the observation of dissolved oxygen. At the time of waste water given, the Dissolved oxygen (DO) concentration will go down. After some time aerated, DO will gradually rise, and someday she will return as the original, and it will give the information to us that the assimilation process has been completed and microorganisms have been grown.
  • 9. d. Preparation of Seaweed Tank The type of seaweed that we used in this engineering is E. Cottoni and inserted into the first tank as well as a sedimentation tank.The Installation of seaweed done in a long line around the tank with rope 150 cm long. e. Installation of UV lights Installation of UV lights aim to reduce the bacteria that entered to the water medium after the activated sludge process which involves a lot of active microorganisms as its main component. Installation of UV lights is right in line where the water enters into the culture media. f. Preparation of Sea bass as fish test To see and evaluate the performance of the Biofilter system combination between activated sludge and seaweed, The fish test was culture in two way, first, in the tank with Biofilter combination and second, without the biofilter as a control of the system. The Commercial feed for fish test given 3 times a day, at the morning, afternoon and evening by adlibithum. To remove the excess dirt, feeding remain and other impurities was carried by cleaning the bottom of tank every evening after completion of feeding. The culture of test fih was conducted for 30 days. g. Test of the filters effectiveness To determine the ability and the effectiveness of this biofilter system combination between activated sludge and seaweed is done by the laboratory testing. The observation was performed by comparing the quality of water that passes through this biofilter combination and to the control water (without pass the biofilter system). The parameters observed include: NH3, NO2 NO3, turbidity, BOD and COD. Observations made during one month from 25th November 2009 to December 28th, 2009.
  • 10. CHAPTER III RESULTS AND DISCUSSION III.1 Result 1. Graphic of inoculation bacterial growth (with molase) Grafik Pertumbuhan Bakteri Inokulasi 1200 1000 Jumlah Bakteri (TBU) 800 Grafik Pertumbuhan 600 Bakteri Inokulasi 400 200 0 1 2 3 4 Sampling Ke- Note : The number of general bacterial multiple with102 CFU/ml 2. Result of Turbidity and TDS analysis TEST RESULT Date of After through the biofilter Without Biofilter (control) Analysis Turbidity TDS Turbidity TDS (NTU) (mg/l) (NTU) (mg/l) 08 November 0,49 31.2 0.49 31,5 15 November 0,15 27,9 0,42 32,3 22 November 0,02 8,4 0.38 31,4 29 November 0,01 8.4 0,51 30,2 05 December 0,02 9,1 0,56 30,3 11 December 0,02 8,7 0,59 30,6 16 December 0,01 8,3 0,54 32,8 22 December 0,02 8,4 0,43 32,1 Graphic of Turbidity Graphic of TDS 0.7 35 0.6 Turbidity after 30 Turbidity (NTU) TDS (mg/l)) 0.5 pass the 25 TDS after pass 0.4 biofilter 20 the biofilter" 0.3 control 15 control 0.2 10 0.1 5 0 0 8. nov 15.Nov 22.Nov 29.Nov 8. nov 15.Nov 22.Nov 29.Nov 5.des 11.des 16.des 22.des 5.des 11.des 16.des 22.des Date of analysis Date of analysis
  • 11. Hasil Analisa Kadar Ammonia dan Nitrit pada air input media pemeliharaan HASIL UJI Date of TEST RESULT Analysis After through the biofilter Without Biofilter (control) NH3 NO2 NH3 NO2 (mg/l) (mg/l) (mg/l) (mg/l) 08 November 0.13 0,07 0,13 0,07 15 November 0.08 0,06 0,11 0,06 22 November 0,01 0,06 0,11 0,06 29 November -- 0,05 0,09 0,06 05 December 0,01 0,04 0,11 0,05 11 December -- 0,01 0,14 0,06 16 December -- 0,01 0,09 0,07 22 December -- 0,01 0,12 0,07 Graphic of NH3 (ammonia) Graphic of NO2 (Nitrit) 0.16 0.08 0.14 0.07 0.12 0.06 NH3 (mg/l)) NO2 (mg/l)) NH3 after pass the NO2 after pass the 0.1 biofilter""" 0.05 biofilter""""""" 0.08 0.04 0.06 control 0.03 control 0.04 0.02 0.02 0.01 0 0 1 v 1 s 2 v 2 v 5dv 1 v 1 s 2 s s 1 s 2 v 2 v 5dv o 1 s 2 s s .e .o .o .o o .e .e .e .e .o .o .o .n .e .e .e 5N 2N 9N .n 5N 2N 9N 1d 6d 2d 1d 6d 2d 8 8 Date of analysis Date of analysis Dissolved oxygen at culture tank analysis Hasil Analisa Date of Oksigen Terlarut Graphic of Dissolved oxygen (DO) Analysis (mg/l) 8 After Without 7 through the Biofilter 6 DO after pass the DO(mg/l)) 5 biofilter"""""""""""""" biofilter (control) 4 " 08 November 5,0 5,1 3 control 15 November 5,7 4,9 2 22 November 6,4 5,4 1 29 November 6,9 5,0 0 05 December 6,5 5,2 1 v 2 v 2 v v s 1 s 2 s es o .e o o o e e .n 5.N 2.N 9.N 11 December 5d 6,7 5,3 1.d 6.d 2.d 8 1 16 December 6,9 4,7 Date of analysis 22 December 6,8 4,9
  • 12. The comparation of Total Number of General bacterial (TBU) between after and before through the UV light Perbandingan TBU sebelum dan sesudah UV 300 Jumlah TBU (x100) 250 200 TBU Sebelum UV 150 TBU setelah UV 100 50 0 1 2 3 4 5 6 7 8 9 10 11 Sampling Ke- IV.2 Discussion From the results of experiments it was found that the inoculated bacteria in activated sludge substrates had been developed. On the fourth day of sampling, the total number of bacteria produced was 9.7x106 CFU/ml. This number may be used temporarily as an indicator that the filter is ready for use. This situation is also correlated with a reduction of NH3 and NO2 concentration. The concentration of NH3 in the water filtration system results in the range: 0.01 to 0.13 mg / l, while the water control, the NH3 are between: 0.09 to 0.14 mg / l. This means this biofilter combination system can reduce the NH3 concentration until 80%. The fall of this ammonia levels, probably caused by the oxidation of ammonia to the nitrate elements which is done by Nitrosomonas bacteria that grow on the sludge media in the filtration system. Meanwhile for NO2, the concentration resulting in water with this filtration system was also down, although only slightly, which is in range: 0.01 to 0.07 mg / l, compared with control water, which have concentrations of NO2 from 0.05 to 0, 07 mg / l. Nitrite in biological filtration system will be transformed by Nitrobacter bacteria into nitrates element, and then in inaerobic conditions it will converted into the nitrogen (Coklin and Chang, 1983).
  • 13. For the turbidity and Total Dissolved Solid parameter in the water, they have significant reduction. This is probably due to the function of material that we used in this biofilter combination, they are activated sludge and seaweed. This biofilter system result the Turbidity concentration between 0.01 to 0.15 mg/l, while the turbidity concentration of control water are : 0,38 to 0,59 mg / l. This means there is 75 – 98% reduction of turbidity in the water with this biofilter system. For the TDS (Total Dissolved Solid) concentration. The number of TDS in water that pass this biofilter system combination are from 8.3 to 27.9 mg / l while on the control water control are 30.2 to 32.8 mg/l. It means that the reduction of TDS concentration is as much as 15-73%. Associated with the presence of seaweed as an natural filters in the sedimentation tank, where the seaweed, naturally have a function as a filter of carbon dioxide, which are absorbed and converted into the oxygen element. So the measurement of dissolved oxygen concentrations was done at the fish culture tank with the combination biofilter system and control. The result showed that DO levels that exist in the fish culture tanks with filtration system are 5.0 to 6.9 mg/l, while the DO concentration at control tank were 4.7 to 5.3 mg/l. Filter with the combination of activated sludge and seaweed can be operationalized for 6 (six) months. And after that the materials that we used at this biofilters system should be cleaned. Some benefits of this combination Biofilter systems include: 1. Guarantee obtaining a good water quality for fish culture tank 2. Economical, Efficient and Effective in producing high water quality 3. Easily applied by fish farmers
  • 14. CHAPTER IV CONCLUSION AND SUGGESTION V.1 Conclusions 1. This combination Biofilter system between activated sludge and seaweed is quite effective in reducing of toxic elements such as NH3 and NO2, in which the ammonia concentration was reduced until 80%, while for the levels of NO2 was reduced up to 20-60%. 2. This combination Biofilter system between activated sludge and seaweed is quite effective in improving the clarity of water, because it can reduce the turbidity levels up to 75-98%., and reduce the amount of total dissolved solids between 15 to 73%. 3. Seaweed as a filter which is placed in the sedimentation tank through its function can play an active role in improving of dissolved oxygen concentration up to 24%. 4. This combination Biofilter system between activated sludge and seaweed is quite economical, efficient, effective and can be applied directly by the fish farmers V.2 Suggestion 1. Need to do further study on the effectiveness of seaweed in absorption of heavy metals that dissolved in the water. 2. Observations on the effectiveness of combination Biofilter between activated sludge and seaweed can also be undertaken in a long time periode. In order to know the exact impact and benefits from this system.
  • 15. LITERATURE Anonim. Limbah. http://id.wikipedia.org/wiki/Limbah. Anonim.Pencemaran.http://www.dephut.go.id/INFORMASI/SETJEN/PUSSTA N/info_5_1_0604/isi_5.htm Anonim, 2008, Laporan Bulanan Kesehatan Ikan dan Lingkungan, Balai Budidaya Laut Batam, Kepulauan Riau. Anonim. 2008. Instalasi Pengolahan Air Limbah (IPAL).http://www.lenn- biz.com/?q=ipal Anonim. 2002. Membangun Instalasi Pengolahan Air Limbah. http://www.korantempo.com/news/ Bapedal 1995. Teknologi Pengendalian Dampak Lingkungan Industri Penyamakan Kulit.. Jakarta. Bishalf, W. 1993. Abwasser Technik. B. G. Teuber, Stuttgart. Koesoebiono. 1984. Industri Tapioka Penanganan Limbah Cair dan Padat. Makalah pada Lokakarya Pemanfaatan Limbah Industri Tapioka, Bogor, 19-20 Juli 1984. Gaudy, A.Fand Gaudy, E. T, Microbiology for Environmental Scientist and Engineers, Mc. Graw Hill,1980. Hutagalung, Michael. 2007. Teknologi Pengolahan Sampah. http://www.majarikanayakan.com/2007/12/teknologi-pengolahan- sampah Loehr, R.C. 1974. Agricultural Waste Management. Academic Press, New York Metcalf and Eddy. 1991. Waste Water Engineering. P ed. McGraw-Mll, Inc. New York Novriadi, R, 2009, Optimalisasi Kualitas Air Melalui Sistem Filterisasi Cartridge Anion Kation dan Lampu UV Terintegrasi, Balai Budidaya Laut Batam, Kepulauan Riau. Nathanson, J. A. 1997. Basic Environmental Technology 2nd ed. Prentica Hall, Ohio. Rydin,S. 1996. Research Needs for the European Lether Industry. European Workshop on Environmental Technology. Copenhagen, 13-15 November 1996. Subagyo, Ir, MSc. 2008. Biological Unit Process. Materi Kuliah Pengolahan Air Limbah Jurusan Ilmu Kelautan Fakultas Perikanan dan Ilmu Kelautan Universitas Diponegoro Semarang. Sugiharto. 1987. Dasar-dasar Pengolahan Air Limbah. UI Press, Jakarta. Sudrajat Y, dan Gunawan B, 2002, Sistem Bakteriofiltrasi Sebagai Sarana Pasokan Air Pada Penampungan Ikan Hidup, Buletin Teknik Pertanian, Volume VII, Jakarta Webster, T.S, ad Devinny, J.S. 1996. Biofiltrasi of Odors, Toxic and Volatile Organic Compounds from Publicity Owned Treatment Works, Env. Progress, Vol. 15, No. 3, P. 141-147. Wenas, R.I.F, Sunaryo, dan Styasmi, S. 2002. Comperative Study on Characteristics of Tannery, "Kerupuk Kulit", "Tahu-Tempe" and Tapioca Waste Water and the Altemative of Treatment. Environmental Technology. Ad. Manag. Seminar, Bandung, January 9-10, 2003 p. Pos 5-1 - pos 5-8.