Treatment of Soap Industry Wastewater using MBBR Technology

DOI : 10.17577/IJERTCONV10IS11070

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Treatment of Soap Industry Wastewater using MBBR Technology

Mousheen H M

Department of Civil Engineering

Jain Institute of Technology Davangere, India

Shashidhar Poojar A M

Department of Civil Engineering

Jain Institute of Technology Davangere, India

Prajwal A G

Department of Civil Engineering

Jain Institute of Technology Davangere, India

Sakamma S

Department of Civil Engineering

Jain Institute of Technology Davangere, India

Sowjanya R

Department of Civil Engineering

Jain Institute of Technology Davangere, India

Abstract -With the development of industries in world, industrial effluents are also increasing over the time. On the hand water scarcity is one of the major problems concerned by society. Thus, wastewater treatment has become important as the treated water can be used in recreational works, agricultural land etc., This paper presents the treatment of soap industry wastewater by lab scale MBBR which is highly contaminated with organic and inorganic compounds.

The MBBR (Moving Bed Biofilm Reactor system) is advanced wastewater treatment which treats the wastewater with the help of biomass. In this system, biomass is suspended and attached as well. Thus, MBBR system combines the advantage of both conventional Activated Sludge and Biofilter Process making it a best wastewater treatment.

Keywords: Lab Scale MBBR Apparatus, Growth of Microorganisms, BOD removal, COD Removal.

  1. INTRODUCTION

    Wastewater is processed water from any combination of domestic, industrial, commercial or agricultural activity and any sewer inflow or sewer infiltration. Wastewater includes a pollutant which are harmful to the surrounding environment. Hence it is important to treat the wastewater and to keep the concentration of pollutants within the limit before it is released into a natural body. Industrial wastewater treatment covers the mechanisms and process used to treat wastewater that have been contaminated in some way by anthropogenic, industrial or commercial activity prior to its release into the environment. wastewater treatment is a mixture of unit process and can be divided into three categories physico-chemical treatment, biological treatment and combination of these treatment. MBBR (Moving Bed Biofilm Reactor) Technology is the one of the biological treatment units with higher contaminant removal performance.

    The MBBR is origin Norway and emerged from the University Science and Technology of Norway within corporation known as Kalends Miljoteknologi or Anox Kalends. During 1989 it was the earliest MBBR, though comparatively new technology, but has been introduced in the US as back as 1995.The idea for the development of MBBR method was to optimize reliability and the most efficient technology. MBBR method takes this advantage and apply it to

    the growing the microorganisms and biofilms above the media carrier that move free inside the sewage.

    MBBR media carriers have a density similar to that of water, so they mix well with the wastewater to promote consistent waste digestion. Using MBBR media is particularly advantageous because the tiny pieces take up minimal space, are easy to maintain and digest waste efficiently. The microorganisms on the media can also automatically adjust to changes in the amount and type of waste in the water. Although MBBR systems require some monitoring they are largely self- sufficient.

  2. OBJECTIVE OF THE STUDY

    The primary goal of this project is to conduct experimental study to evaluate the performance of lab-scale MBBR system. To achieve this goal the following objectives have been identified.

    1. To observe the growth of microorganism on lab-scale MBBR system.

    2. To check COD removal efficiency of soap industry wastewater on the lab scale MBBR system.

    3. To observe PH variation of waste water on the lab scale MBBR system.

    4. To check BOD removal efficiency of soap industry wastewater on the lab scale MBBR system.

  3. MATERIALS

    [1] Soap industry wastewater

    Characterization of the wastewater from soap industry manufacturing unit indicated that the waste was highly contaminated with organic compounds as indicated by COD and BOD values. Moreover, effluent from the soap manufacturing plant contains significant concentrations of oil and grease.

    [2] MBBR Plastic media

    MBBR process utilizes floating High-Capacity Microorganism Biofilm media within the aeration tanks. The media provides increased surface area for the biological microorganisms to attach and grow. The microorganisms consume organic material.

    Table 1 specification of plastic media

    Properties of media

    media Volume

    Material of the media

    Specific surface area

    Plastic filter media

    60%

    Microfiber PVC

    500m2/m3

    [3] Industrial Sludge and Cow Dung

    Industrial Sludge from Maharaja soap industry has taken for initial growth of microorganisms in lab scale MBBR apparatus.

    Initially Microorganisms consume organic matter present in the wastewater to grow over the media. Since Soap industry Wastewater has BOD in the range of 350-400mg/l it would take more than 12 weeks for complete growth. Thus, by adding Cow Dung and Jaggery in the sludge will enhance the BOD concentration in the wastewater which helped in fast growth of microorganisms.

    [4] Experimental Setup

    The experiment is performed on the lab scale MBBR system which includes parts as follows.

    Fig. 1 schematic diagram of lab scale MBBR system

    Fig.2 experimental setup of lab scale MBBR system

    Fig.3 plastic media in MBBR reactor

  4. METHODOLOGY

    In this project the soap industry wastewater is allowed to flow through MBBR reactor at HRT of 2,4,6 and 8 Hour. The system is checked for COD removal efficiency, BOD removal efficiency, variation of PH at different hydraulic retention time. The flowchart of conducting of project is as follows:

    Fig. 4 Flow chart showing methodology

  5. EXPERIMENTAL RESULTS AND DISCUSSION

    Figure 5 growth of microorganusms

    Observation of Growth of Microoragisms

    As observed in the above the graph, BOD removal efficiency has increased with increase in the numbers of microorganism from 1st day to 15th day. On the first day there was 18% BOD removal is mainly due to aeration. Later on there is increase in BOD removal efficiency indicating growth of organisms over the media. Increase in the BOD removal efficiency has reached 82.33% on the eleventh day and later there is no remarkable increase in the BOD removal efficiency which indicates that optimum growth of microorganisms over the media.

    As observed in the above graphs, The BOD and COD removal Efficiency has increased with increased HRT. At higher HRT, wastewater remains in the reactor for longer duration thus achieving better removal efficiency in comparison to lower HRT. Maximum removal efficiency achieved at 6 HRT, further increase in the HRT will allow the wastewater remains in the reactor for longer duration which results in lower F/M ratio Thus there is a decrease in the removal efficiency above 6 HRT.

    Days

    BOD Value in mg/l

    Efficiency

    Inffluent

    Effluent

    0

    1053.21

    858.79

    18.46

    1

    1000.2

    657.83

    34.23

    2

    921.32

    473.93

    48.56

    3

    956.25

    374.47

    60.84

    4

    1045.56

    330.19

    68.42

    5

    989.25

    256.02

    74.12

    6

    964.58

    226.29

    76.54

    7

    1150.84

    244.44

    78.76

    8

    1190.56

    243.35

    79.56

    9

    968.25

    188.32

    80.55

    10

    978.15

    180.37

    81.56

    11

    1089.56

    192.53

    82.33

    12

    1074.23

    192.07

    82.12

    13

    976.02

    171.19

    82.46

    14

    1189.02

    202.85

    82.94

    Table 2 growth of microorganisms

    Figure 8 pH Variation of wastewater at different HRT

    As shown in the above graph, the average pH of inlet wastewater is 6.05 and average pH of the effluent of reactor is

      1. Thus, Wastewater has become alkaline after passing through the reactor.

  6. CONCLUSION

      • The optimum growth of organisms is observed on the 12th day in the lab scale MBBR system

Figure 6 BOD removal efficiency at different HRT

Figure 7 COD Removal Efficiency at different HRT

  • BOD and COD removal Efficiency has increased with increase in the HRT and maximum removal efficiency has achieved at 6 HRT. With the further increase in the HRT the removal efficiency has decreased.

  • Wastewater has become alkaline after passing through the reactor.

REFERENCES

[1] Xuifei yang, victor lopez-grimau, Mercedes Vilaseca and matri crespi treatment of textile wastewater by CAS, MBR, and MBBR: a comparative study from technical economic, and environmental perspectives (2020).

[2] Jamal ail kawan, hassimi abu hasan, fatihah suja, Othman bin Jaafar, rakmi abd rahman a review on sewage treatment and polishing using moving bed biofilm reactor (MBBR), VOL ,11, NO,8 (2016).

[3] Luigi falletti, lino conte, Alessandro zaggia, tiziano battistini, doriano garosi food industry wastewater treatment plant based on flotation and MBBR, ISSN: 2333- 2581, VOL: 1, NO 12 (2014).

[4] Bin dong, hanyu chen, yang yang, qunbiao he treatment of printing and dyeing wastewater using MBBR followed by membrane separation process (2014).

[5] Najafpour, G.D.; Zinatizadeh, A.A.L.; and Lee, L.K. Performance of a three-stage aerobic RBC reactor in food canning wastewater treatment, Biochemical Engineering Journal, 30, 297-302 (2006).

[6] Boya nun Xu, siqing Xia, c.-y hu, nai-yun gao dynamic simulation model of nitrification in bio-pretreatment process using MBBR (2006).

[7] Monica escola casas, ravi kumar chhetri, Gordon ooi, kamilla M.S Hansen, Klaus litty, magnus Christenson, caroline kragelund, henrik

R. Andersen, kai bester biodegradation of pharmaceuticals in hospital wastewater by staged moving bed biofilm reactor (MBBR) (2015).

[8] Lee, W., I. Kang; and C. Lee Factors affecting filtration characteristics in membrane-coupled moving bed biofilm reactor, Water Research 40, (9): 1827-1835 (2006).

[9] Odegaard, H. (2006) Innovations in wastewater treatment: The moving bed biofilm process, Water Science and Technology 53, (9), 17-33 (2006).

[10] Wang, X.J.; Xia S.Q.; Chen, L.; Zhao, J.F.; Renault, N.J.; and Chovelon, J.M Nutrients removal from municipal wastewater by chemical precipitation in a moving bed biofilm reactor, Process Biochemistry, 41, 824-828(2006).