Study on Application of Multifunctional Compound Microorganism
Product in the Sewage Plant Treatment for Sludge Reduction
Can Wang
*
, Xin Jin, Jilin Teng and Ruozheng Li
Beijing GuoDian FuTong Science & Technology Development Co. Ltd., NARI Group Corporation ,Fengtai Disteict,
Beijing 100070, China.
Email: wangcan0305@aliyun.com
Keywords: Sludge reduction, A
2
/O, sewage plant treatment, microorganism
Abstract: Reducing the quantity of excess sludge has become a popular research subject in wastewater treatment.
Therefore, based on the current sludge reduction theory, some special microbial strains were selected, and
through certain cultivation process, a multiifunctional compound microorganism product was developed to
reduce the sludge quantity. The microorganism product was used in sewage wastewater treatment plant for
pilot test. Five sets of identical equipment with the A
2
/O process and the same operating method were
adopted, and the effect of SV and MLSS were analysed. The effects on sludge reduction were
compared.The results show that the sludge reduction reaches 57.3%. The multifunctional compound
microorganism product improved the effluent quality and the COD, NH
3
-N and TN in the effluent are
37.85mg/L, 0.30mg/L and 12.37mg/L respectively. The microorganism does not require any special
treatment unit, and does not change the original treatment process also. Therefore, the microorganism
product will effectively improve the sludge reduction effect, and reduce the pressure of the sludge disposal
for the wastewater treatment plants.
1 INTRODUCTION
Sludge reduction refers to the physical, chemical
and biochemica l means to minimize the amount of
biosolids discharged from the entire wastewater
treatment system. At present, more attention has
been paid to sludge reduction technology. At the
same time, the research of sludge reduction
technology is also the necessary way to make sludge
harmless and resourceful (Li et al., 2007; He and
Zhou, 2004). In the past ten years, sludge reduction
technology has been focused on improving sludge
containing organic degradation methods such as: 1)
sewage treatment process variant; 2) the
biodegradation of sludge was enhanced by
mechanical, biological, thermal or en zy matic
treatment; 3) sludge stabilizat ion process
modification (Zhang and Hong, 2005; Lin and Guan,
2005). At present, sludge reduction technology
based on uncoupling metabolis m, maintaining
metabolism, bioaugmentation and biological
predation are gradually being applied for the
biological treat ment of wastewater (Wang and Song,
2003; Rensink and Ruckens, 1998). However, there
are still many researchers have done much work on
sludge reduction technology.So far, a feasible
treatment method towards sludge reduction , which
can integrate validuty and environmental security
perfectly, has not been developed yet.
In the process of sludge reduction,
bioaugmentation is the means of reducing sludge by
adding microorganisms with specific functions in
the biological treatment system of sludge (Liang et
al., 2004; Li, 2008). Bioaugmentation technology
has been widely used in many aspects of
environmental protection, such as livestock and
poultry manure deodorizat ion, sewage treat ment,
water eutrophication treatment, domestic waste
treatment and so on, with good results achieved
(Zhang et al., 2008; Yuan et al.. 2007; Neyens et al.,
2004). In this study, a sewage treatment plant with a
treatment capacity of 30000 m
3
/d was used for the
sludge reduction by adding a compound microb ial
preparation. The objective are to investigate the
effect of biological agents on improving effluent
quality of existing treatment systems, and the effect
of sludge reduction.
44
Wang, C., Jin, X., Teng, J. and Li, R.
Study on Application of Multifunctional Compound Microorganism Product in the Sewage Plant Treatment for Sludge Reduction.
In Proceedings of the International Workshop on Environment and Geoscience (IWEG 2018), pages 44-49
ISBN: 978-989-758-342-1
Copyright © 2018 by SCITEPRESS – Science and Technology Publications, Lda. All rights reserved
2 EXPERIMENTAL AND
METHODS
2.1 Raw Water and the Quality
The water quality is shown in Table 1 and 2 as
follows:
Table 1: The quality of Influent.
COD
BOD
SS
TN
TP
mg/L
mg/L
mg/L
mg/L
mg/L
Index
500
170
160
50
6.0
Table 2: The quality of effluent.
COD
BOD
SS
TN
TP
mg/L
mg/L
mg/L
mg/L
mg/L
Index
≤50
≤10
≤10
15
0.5
2.2 The Technological Progress
The municipal wastewater treat ment plant adopts
the A
2
/O ordinary activated sludge process which
has biological function of biological phosphorus and
nitrogen removal with pre anaerobic and ano xic
stages. Sludge treatment was carried out by gravity
concentration and dewatering with belt dewatering
machine.The process flow is shown in Figure 1.
2.3 Experimental Device and Method
2.3.1 Experimental Equipment
Each point dosing equipment adopts the mixing
barrel and metering pump integrated dosing device,
as shown in Figure 2. The agitator is used when
dispensing, and the dosing solution is added to the
target pool at a certain flow rate by a metering pump.
The total amount of aeration was controlled, and the
amount of aeration grit chamber accounted for 50%,
in addition the other four points accounted for 50%.
2.3.2 Experimental Method
Through the actual influent flow (36000 m
3
/d) and
the target concentration (2 ppm) of the sewage
treatment plant, the total dosage of mu ltifunctional
compound microorganism product was determined.
The mu ltifunctional co mpound microorganism
product were a mixture of Bacillus,Pediococcus,
Lactobacillus plantarum and some nutrient.
The total amount to be treated is controlled
during the dosing process, the distribution of each
point is added to ensure the total dosage unchanged.
At the same time, according to the operation and
processing of the reasonable adjustment, the dose
distribution at the beginning of the start-up is shown
in Table 3 as follows:
Figure 1: The technological process route.
Figure 2: The picture of the dosing equipment.
Table 3: The dosage of product at the beginning.
Grit
Removel
Anaerobi c
tank-
South
Anaerobi c
tank-
North
Anoxic
tank-
South
Anoxic
tank-North
50%
15%
15%
10%
10%
Study on Application of Multifunctional Compound Microorganism Product in the Sewage Plant Treatment for Sludge Reduction
45
The test started on the eighth day, the target
concentration was adjusted to 1ppm, the total
dosage of the reagent was determined, and the
dosage was reduced at the same point with each
other in the dosing process. Dosing at this stage was
shown in Table 4 as follows:
Table 4: The dosage of product at the stable period.
Grit
Removel
Anaerobic
tank-
South
Anaerobic
tank-
North
Anoxic
tank-
South
Anoxic
tank-
North
Dosage
proportion
50%
15%
15%
10%
10%
Continuously adding the compound
microorganis m agent, the change of effluent water
quality in each section of sewage treat ment process
were analyzed, and the quality of raw water,
primary sedimentation tank effluent, the two series
of anaerobic tank effluent, biochemical pool water,
the final effluent were detected.
2.4 Test Method
Routine test data for water and various units COD,
NH
3
-N, TN, MLSS, SV30, nitrification liquid reflu x
ratio, sludge reflu x rat io and regular bio logical
microscopy etc..
The common indexes such as COD, NH
3
-N, TN
were detected by the national methods. The sludge
concentration (MLSS) were monitored by
gravimetric method. The by national standard
method. Microscopic examination were measured
by optical microscope (XSZ-G, Chongqing optical
instrument factory).
3 RESULTS AND DISCUSSION
3.1 The Effect about COD
The difference between two series biochemical
process unit is not much, the quality indices are
shown in Figure 3.
Figure 3 indicates that in despite of the raw
water quality fluctuate, the effluent COD can be
kept below 50 mg/ L, which can fully meet the
demand of first-degree A standards of GB18918-
2002. The research that using MEMA(multi-
environmental microbial agent) in Carrousel
oxidation ditch have the consistent conclusion
(Yang et al., 2016).As the influent contains a large
number of organic suspended substances, the COD
concentration of influent is very high, and generally
fluctuates between 800~2000 mg/L. A fter the
treatment of aerated grit tank, large particles
suspended solids were removed, the COD of the
effluent decreased significantly, could generally
reach as low as 200~250 mg/L. The effluent COD of
primary sedimentation tank was relatively stable,
which reduces the load impact on the subsequent
biochemical treat ment. The COD was reduced
gradually after biochemical treatment, the effluent
was below 50 mg/ L.The average concentrations of
COD in effluent were 37.85 mg/L. The two series of
North and South were stable. In addition, the COD
of effluent was stable within two weeks after adding
compound microbial preparation, and all of them
could reach the first level A emission standard.
Figure 3: The removal of the COD.
3.2 The Effect about TN
Generally, the influent TN is between 60~90 mg/ L,
and the removal rate of TN is about 50% by the
removal of suspended particulate matter in the
aeration grit chamber. As shown in Figure 4, the
effluent TN of primary sedimentation tank is
between 30~45mg/ L, and it is relatively stable
before entering biochemical pool, the TN in
biochemical react ion area is greatly reduced, and
nitrificat ion denitrification occurs at this stage, it
can be concerned that there exists SND in A
2
/O
system (Fang-Ying et al., 2006). At the same time,
the compound microbial preparation products were
added in the anaerobic zone and ano xic zone, and
the TN of the South and North aerobic section had
litt le difference, all of wh ich were between 11-
15mg/L. After second sedimentation tank treatment,
TN removal little. Within 8 days of treat ment, the
IWEG 2018 - International Workshop on Environment and Geoscience
46
effluent fluctuated but remained stable.After 13 days
(about a sludge age cycle), the concentration of TN
was reduced to 9~10 mg/L when adding the target
concentration of 1 ppm. The average concentrations
of TN in effluent were 12.37 mg/ L and which could
reach the first class A standard (<15mg/ L). However,
dosing the compound microorganism product 13
days later (about a sludge age period), the TN
decreased to 9~10 mg/L.
Figure 4: The removal of the TN.
3.3 The Effect about NH
3
-N
After adding multifunctional co mpound
microorganis m product, sludge age is prolonged,
which is conducive to the growth of nitrifying
bacteria, and increased nitrification in the same
conditions. It is conducive to nitrification of
ammon ia nitrogen. As shown in Figure 5, the NH
3
-
N remova l efficiency is stable after adding the
compound microbial agent, and kept the good
treatment effect.The average concentrations of NH
3
-
N in effluent was 0.3 mg/ L, the removal rate was
more than 99%.
Figure 5: The removal of the NH
3
-N.
3.4 Sludge Sedimentation Performance
Change Analysis
The structure of microbial floc also direct ly affected
the proportion of aerobic zone and anoxic zone in
sludge floc and mass transfer effect in the floc, it
also affects the degree of difficu lty in microbial
acquisition of DO and substrate. The larger sludge
particles increased the proportion of anoxic
microenvironment, and the mass transfer resistance
of sludge particles with compact structure was large
(Guo et al., 2007). The organic carbon source in
water is difficult to penetrate into the sludge floc,
and the results is that it is difficu lt for the internal
microorganis m to contact with carbon source, which
affects the removal efficiency of carbon and
nitrogen.
The changes of SV30 and M LSS were observed
after adding co mpound microbial preparat ion, as
shown in the Figure 6. During the whole experiment,
the MLSS in the biochemical pool of the North
Series decreased from 5300 mg/ L to 4700 mg/ L
after the addition of microorganis m, and the MLSS
in the South series also decreased. Fro m the change
curve of SV30, the SV30 g radually decreased, and
the sludge settling performance was in good
condition.SV30 has a gradual downward trend, and
the observation of settlement process shows that
sludge settling speed is significantly accelerated,
sludge settlement performance becomes better.After
adding microbial preparation, the sludge settlement
performance was imp roved, the sludge volume was
reduced by 57.3%, the mic robial preparation could
improve the effluent quality.
3.5 Microscopic Examination of
Microbial Biochemical Pool
Routine microscopic examination of activated
sludge in the biochemical tank, microscopically
observed case worms, roaming insect, vorticella,
epistylis, rotifers, dun pellionella, a little
whipworms, as shown in the Figure 7. The dominant
species are Vorticella and rotifer. After adding
mu ltifunctional compound microorganis m product,
the microbial phase changed a little, and the
microbial species were abundant. The growth
condition is stable, the floc structure was fluffy, the
color was yello w brown, and the sludge activity
strong.
Study on Application of Multifunctional Compound Microorganism Product in the Sewage Plant Treatment for Sludge Reduction
47
Figure 6: The sludge performance.
a. Epistylis
b. Rotifers
c. Vorticella
Figure 7: The microscopic examination.
4 CONCLUSIONS
The study highlights the effectiveness of
mu ltifunctional compound mic roorganism p roduct
in increasing efficiency and reducing consumption
of infrastructure. There is no effect on the stability
of existing system in WWTP. Moreover, the
removal rate of COD, NH
3
-N and TN can be
improved by the biochemical system when the
influent water quality fluctuates greatly. The results
suggest that adding compound microorganism
product target concentration was 2 ppm, the A
2
/O
system was very stable. After adding
mu ltifunctional compound microorganis m product,
the sludge settlement performance was improved,
the sludge volume was reduced by 57.3%, the
average concentrations of COD, NH
3
-N and TN in
effluent were 37.85 mg/ L, 0.3 mg/L, 12.37 mg/ L,
respectively.The compound microbial preparation
has good sludge reduction effect. At the same time,
reduce the burden of sludge treatment and disposal
of sewage treat ment plant, reduce the degree of
organic sludge. It does not change the original
treatment facilities and operation mode, and the
power consumption of the whole system will not
increase.
REFERENCES
Li J, Zhu Z, Zhu G, et al. 2007 Study on reduction of
excess sludge production by using MCMP microbial
agents [J] Journal of environmental engineering 10 (1)
3-5
He Y, Zhou G 2004 Research progress of excess sludge
reduction technology [J] Environmental protection
technology 1 39-42
Zhang L, Hong Y 2005 Sludge reduction technology for
municipal wastewater treatment [J] Municipal
technology 23(5) 314-317
Lin S, Guan Y 2005 Aerobic/anaerobic alternation and
circulation process for the research of sludge reduction
[J] Industrial water treatment 25 (2) 34-37
Wang Q, Song B 2003 New technologies for sludge
reduction in wastewater treatment [J] Urban
environment and urban ecology 16 (6) 295-297
Rensink J H, Ruckens W H 1998 Using metazoan to
reduce sludge production [J] Water science
Technology 36(1) 171-179
Liang P, Huang X, Qian Y 2004 Research progress of
sludge reduction technology [J] Environmental
pollution control technology and equipment 4 (1) 44-
52
IWEG 2018 - International Workshop on Environment and Geoscience
48
Li J 2008 Study on the effect of microbial inoculants on
sludge reduction in wastewater treatment plant [D]
Chongqing: Southwestern University, PhD thesis
Zhang L, Liu Q, Xu Z, et al. 2008 Research on effect of
compound microbial inoculants on sludge composting
[J] Journal of environmental engineering 2 (2) 266-
269
Yuan D, Xi B, Wei Z, et al. 2007 Simulation of eutrophic
water treatment by microbial aquatic bioaugmentation
system [J] Journal of agro environmental science 26 (1)
19-23
Neyens E, Baeyens J, Dewil R, et al. 2004 Advanced
sludge treatment affects extracellular polymeric
substances to improve activated sludge dewatering[J]
Journal of hazardous materials 106B 83-92
Yang B, Li M, Fu X, Wang J,et al. 2016 Demonstration of
sludge in situ reduction using MEMA inoculants[J]
Industrial water treatment 3(36) 100-102
Fang-Ying J I, Ning Z, Yang S B, et al. 2006 Advanced
sludge reduction and phosphorous removal process[J]
Journal of Central South University of Technology
13(3) 313-317
Guo X S, Liu J X, Wei Y S, et al. 2007 Sludge reduction
with Tubificidae and the impact on the performance of
the wastewater treatment process[J] Journal of
environmental sciences 19(3) 257-263
Study on Application of Multifunctional Compound Microorganism Product in the Sewage Plant Treatment for Sludge Reduction
49