# A Novel Rotating Disk System for Disintegration of Excess Sludge

Authors: Ming yang Zhang; Yun Xiang; Jian wei Du
Journal: Journal of Chemistry
 (2016)

---

## Abstract

Conventional activated sludge treatment process has been widely employed to deal with a variety of municipal and industrial waste water, but the production of sludge by this method is considerable. It is urgent to find an appropriate method which can solve this problem. Shear force produced by rotating disk system (a cell lysis system) was employed to break cell wall of sludge microorganism in order to release intracellular materials which can be reused as nutrient materials for metabolism of other sludge microorganisms in this study. Special feature on surfaces of disks had been proved to be a novel improvement which can improve disintegration effect apparently. Ultrasonic system can further promote minimization of excess sludge after treatment by rotating disk system in shorter time.


---

## Body

## 1. Introduction

Activated sludge treatment process produces excess biomass as excess sludge which is difficult and expensive to dispose. Sludge management has been the main problem of waste water treatment plants (WWTPs) because it costs 60% of total plant capital cost [1]. With increasing public environmental demands, more and more WWTPs are building in China so as to improve water environment; however large quantity of excess sludge as by-product which is unpleasant for its large volume and offensive odor makes huge stress on excess sludge treatment.Incineration, ocean discharge, landfill, and composting are common sludge disposal methods used over many years. However these common methods are no longer reliable because of economic constraint and negative effect on environment. More and more stringent regulations for excess sludge treatment have promulgated in developed countries; thus management and treatment of excess sludge have been one of the most stringent challenges in biological sewage treatment field [2].According to these demands, many kinds of efficient and economical methods have been researched. With classification, the excess sludge minimization approaches are mainly divided into two categories: (1) excess sludge minimization through posttreatment and (2) in situ excess sludge minimization in the process of sewage treatment [3]. Posttreatment refers to excess sludge minimization which has been produced during sewage treatment process; various methods relying on single or combination of physical, chemical, and biological technology had been researched [4–6]. With comparison and investigation, shortcomings of posttreatment including high operational complexity and expense, especially high energy consumption, restricted large-scale application of this method, whereas in situ excess sludge minimization treatment not only avoided these shortcomings but also displayed prominent advantages. The most apparent advantage compared with posttreatment is that this method can minimize excess sludge production from source of activated sludge treatment process. Some researchers have already demonstrated promising application of in situ excess sludge minimization treatment [7, 8]; thus feasible and efficient in situ excess sludge minimization technology will be very considerable and promising. In recent years, many researchers have investigated different kinds of in situ excess sludge minimization method with physical, chemical, and biological technology in laboratory and pilot plant.Rotating disk system, a cell lysis system, used shear stress produced by rotating disk to destroy cell wall of microorganism and result in the sludge disruption because intracellular contents are reused as substrate by other microorganism cells for their metabolism. With comparison of other sludge disintegration methods, some advantages of rotating disk system can be found such as no consumption of chemical reagents [9], low energy demand, simple operation, and wide range of applicability because it can deal with the viscosity feature of excess sludge. This system was expected to reduce excess sludge production with characteristics of simple operation and high efficiency. The main objective of this study was to investigate the effects of a novel rotating disk system on sludge disintegration. Optimal parameters as rotating speed, distance between disks, and special features on disks were also investigated. In order to promote sludge disintegration, the performance of ultrasonic system combined with rotating disk system on sludge disintegration was also investigated.


## 2. Materials and Methods

### 2.1. Activated Sludge

The inoculation sludge was collected from a WWTP located in Shenyang, China. Then sludge was cultured with Anaerobic/aerobic system in the lab. Mixed liquid suspended solids (MLSS) used in this study were12000
±
50 mg/L.


### 2.2. Rotating Disk System

Figure1 illustrated the schematic diagram of rotating disk system. The inner diameter and depth of working cavity were 25 cm and 40 cm and total volume of working cavity was about 80 liters. When rotary disk was rotating, sewage sludge between two disks would flow to disk boundary because of centrifugal force. This would make the pressure in central area of rotating disk decrease. Because of pressure difference, sewage sludge under fixed disk would be sucked into treatment area through the hole at the center of disk like a pump; treated sludge flowed into holding tank alone channel where sample can be collected for analysis and returned to working tank as a cycle. Excess sludge treatment process was recycled in this manner by this system. Treatment time was initiated when motor speed reached setting speed.Figure 1
Schematic diagram of rotating disk system.


### 2.3. Ultrasonic System

Ultrasonic setup was produced by Keer Ltd., energy output ranged from 500 W to 1000 W, frequency was 20 KHz, and probe diameter was 5 mm. The probe was immersed 10 cm into sludge during excess sludge disintegration process.


### 2.4. Analysis Methods

SCOD (Soluble Chemical Oxygen Demand) was analyzed according to standard method [10]; DNA (deoxyribonucleic acid) was identified with modified Diphenylamine method [11].Disintegration parameterK [12] which depicted disintegration effect of excess sludge was defined as follows: (1)
K
=
S
C
O
D
f
-
S
C
O
D
i
T
C
O
D
-
S
C
O
D
i
∗
100
%
,where K is disintegration percentage, S
C
O
D
f is S
C
O
D concentration after disintegration, S
C
O
D
i is S
C
O
D concentration before disintegration, and T
C
O
D is total C
O
D concentration of excess sludge sample.


## 2.1. Activated Sludge

The inoculation sludge was collected from a WWTP located in Shenyang, China. Then sludge was cultured with Anaerobic/aerobic system in the lab. Mixed liquid suspended solids (MLSS) used in this study were12000
±
50 mg/L.


## 2.2. Rotating Disk System

Figure1 illustrated the schematic diagram of rotating disk system. The inner diameter and depth of working cavity were 25 cm and 40 cm and total volume of working cavity was about 80 liters. When rotary disk was rotating, sewage sludge between two disks would flow to disk boundary because of centrifugal force. This would make the pressure in central area of rotating disk decrease. Because of pressure difference, sewage sludge under fixed disk would be sucked into treatment area through the hole at the center of disk like a pump; treated sludge flowed into holding tank alone channel where sample can be collected for analysis and returned to working tank as a cycle. Excess sludge treatment process was recycled in this manner by this system. Treatment time was initiated when motor speed reached setting speed.Figure 1
Schematic diagram of rotating disk system.


## 2.3. Ultrasonic System

Ultrasonic setup was produced by Keer Ltd., energy output ranged from 500 W to 1000 W, frequency was 20 KHz, and probe diameter was 5 mm. The probe was immersed 10 cm into sludge during excess sludge disintegration process.


## 2.4. Analysis Methods

SCOD (Soluble Chemical Oxygen Demand) was analyzed according to standard method [10]; DNA (deoxyribonucleic acid) was identified with modified Diphenylamine method [11].Disintegration parameterK [12] which depicted disintegration effect of excess sludge was defined as follows: (1)
K
=
S
C
O
D
f
-
S
C
O
D
i
T
C
O
D
-
S
C
O
D
i
∗
100
%
,where K is disintegration percentage, S
C
O
D
f is S
C
O
D concentration after disintegration, S
C
O
D
i is S
C
O
D concentration before disintegration, and T
C
O
D is total C
O
D concentration of excess sludge sample.


## 3. Results

In this study, the effect of distance between disks, feature on disks’ surface, and rotating speed on excess sludge disintegration were investigated.Distances between rotary disk and fixed disk were set as 4.5 mm, 3 mm, and 1.5 mm; rotating speed was 2000 rpm; sludge samples were collected at 1, 3, 5, 10, 15, 25, and 35 minutes when rotating speed reached setting speed. As shown in Figure2, SCOD concentration during disintegration process increased very fast in first 5 minutes when distance between two disks was 4.5 mm and SCOD concentration increased 900 mg/L, whereas the increase of SCOD concentration had almost ceased in the following 30 minutes and SCOD concentration increased only 240 mg/L; total increase of SCOD concentration was 1140 mg/L; when the distance was shortened, SCOD concentration increased sharply and fast. SCOD release had almost ceased until the fifteen minutes. When distance between disks was adjusted to 3 mm, SCOD concentration increased 2070 mg/L in the first 15 minutes and barely 170 mg/L in the last 20 minutes; total increase of SCOD concentration was 2240 mg/L. Noteworthy increase of SCOD concentration could be observed when distance of disks was adjusted to 1.5 mm. Increase process had nearly stopped until the 25th minute; SCOD concentration increased 3030 mg/L and total increase of SCOD concentration was 3130 mg/L. After the treatment in 35 minutes, disintegration parameter K was 15.9%, 29.3%, and 41.3%, respectively, when distances between disks were set as 4.5 mm, 3 mm, and 1.5 mm. Based on this result, it is obvious that finding shorter distance between disks can improve minimization effect of excess sludge.Figure 2
Released SCOD during disintegration process with different distances as rotating speed was 2000 rpm.In order to improve disintegration effect of WAS with this system, surface of disks was processed as shown in Figure3. Compared with smooth surface of disks, concavoconvex surface of disks can promote WAS disintegration during treatment because the increase of SCOD concentration during treatment was evidently higher with the same operational parameters.Figure 3
Special features on the disks’ surface.Figure4 depicted improvement effect of WAS disintegration with higher rotating speed by this system. Total increase of SCOD concentration was 1650 mg/L, 3110 mg/L, and 4420 mg/L when distance between disks was 4.5 mm, 3 mm, and 1.5 mm after treatment. Disintegration parameter K increased obviously; it was 23.0%, 40.7%, and 58.4% in the same condition of rotating speed and distances between disks. Features on surface of disks can further promote minimization of excess sludge because disintegration parameter K increased 17.1% compared with smooth surface in the same condition.Figure 4
Released SCOD during disintegration process with special features on disks as rotating speed was 2000 rpm.Rotating speed would affect flow speed of excess sludge in the treatment area because higher rotating speed would induce bigger velocity gradient in order to produce bigger shear force. Processed surface of disks was applied in this test because of their outstanding performance on excess sludge disintegration. Figure5 depicted the effect of rotating speed on excess sludge disintegration when rotating speed was adjusted to 4000 rpm. The increase of SCOD concentration was very fast and it nearly lasted during whole treatment process. Total increase of SCOD concentration was 2870 mg/L, 4540 mg/L, and 5200 mg/L separately when distance between disks was 4.5 mm, 3 mm, and 1.5 mm. Disintegration parameter K can reach 68.7% when rotating speed was adjusted to 4000 rpm and distance between disks was 1.5 mm.Figure 5
Released SCOD during disintegration process with special features on disks as rotating speed was 4000 rpm.Through comparison, 4000 rpm and 35 minutes were chosen as the optimal operation parameters. These parameters were applied in the following analysis.Most DNA was saved inside the cell; a part of DNA was assembled in the extracellular polymeric substance (EPS). Thus DNA concentration in the solution can be seen as indicator of cell lysis. As shown in Figure6, when distance of disks was 4.5 mm, increase of DNA concentration was apparent in initial 10 minutes, whereas the increase of DNA concentration almost ceased in the following 25 minutes.Figure 6
The variation of DNA concentration during disintegration process.When distance of disks was shorter, DNA concentration increased sharply and the increase process continued in longer time. DNA concentration increased 77.98μg/mL in 25 minutes as distance of disks was adjusted to 1.5 mm. Increase of DNA concentration was negligible as treatment time exceeded 25 minutes.Ultrasonic system was tested as the posttreatment for further excess sludge disintegration. Excess sludge sample was treated by ultrasonic system when frequency and power density were 20 KHz and 0.8 W/mL. In order to make comparison, different manners of treatment process were tested; the result was shown in Table1.Table 1
Disintegration effect of rotating disk system and ultrasonic system with different treatment manner.
Treatment manner
SCOD concentration (mg/L)
ParameterK
No treatment
1300
45 min by rotating system
6570
69.6%
45 min by ultrasonic system
6902
74.0%
35 min by rotating system combined with 10 min by ultrasonic system
7450
81.2%
15 min by rotating system combined with 10 min by ultrasonic system
6960
74.8%It is useless to improve sludge disintegration by extending treatment time with rotating disk system when treatment time exceeded 25 minutes, because parameterK was only increased from 68.7% to 69.6% when treatment time was extended from 35 minutes to 45 minutes. Ultrasonic system displayed similar performance because parameter K reached 74.0% after 45 minutes. However, the effect of rotating disk system combined with ultrasonic system on sludge minimization was remarkable because parameter K reached 81.2% when sludge sample was treated by rotating disk system in 35 minutes then treated by ultrasonic system in 10 minutes. It seems that rotating disk system combined with ultrasonic system had outstanding performance on sludge minimization because parameter K reached 74.8% when sludge sample was treated by rotating disk system in 15 minutes and ultrasonic system in 10 minutes in consideration of sludge disintegration and energy conservation.


## 4. Discussion

Disintegration parameterK was affected apparently by distance between disks, special features on the surface of disks, and rotating speed in view of experiments’ results. In this study, three kinds of distances between disks were investigated. Figure 2 depicted that K was higher when distance between disks was closer; however shorter distance will induce higher torque and less quantity of sewage sludge for treatment; these factors should be taken into account. When the disks’ surfaces were machined specially, parameter K was further increased at the same rotating speed 2000 rpm shown in Figure 4. It was very interesting to find that a sharp increase of K appeared in the first 3 minutes. K increased from 41.3% to 58.4% in the same condition of rotating speed, reaction time, and distances between disks; it means that special machining on the surface of disks can promote disintegration of sewage sludge obviously. The effect of disintegration was more ideal when distance between disks was shorter. Rotating speed was also significant factor which will affect disintegration effect of system. K was increased during whole treatment even though distance between disks was 4.5 mm as shown in Figure 5. Thus 1.5 mm distance between disks, 4000 rpm as rotating speed, and special machining on the surface of disks were chosen as optimal parameters for sewage disintegration in this system.Thin liquid film flow between rotating disks can be encountered in many industrial processes with high rotation rate and consequently high shear rate [13]. This rotating disk system utilized this mechanism and disintegrated sewage sludge by shear force induced by high shear rates. Shorter distance and higher rotating speed can affect shear rates and produce higher shear force which can be used to make cell lysis of sewage sludge. Special features on the surface of disks can increase collision times between samples and disks with high speed which possibly cause damage to cell structure; it probably resulted in improvement on sludge minimization; meanwhile, circuitous channel also prolonged treatment time of sewage sludge in this system.DNA concentration in solution can provide collateral evidence which can depict degree of cell lysis. As shown in Figure6, when distance between disks was 4.5 mm, DNA concentration increased nearly 20 μg/mL during 35 minutes, and increasing process had ceased in 10 minutes. Most DNA was saved inside cell, but a small part of DNA was saved in EPS. When distance between disks was 4.5 mm, shear stress was not still sufficient to make cell lysis only decompose EPS even though rotating speed was 4000 rpm and with special machining on surface of disks. DNA concentration increased sharply from 5th to 25th minute when distances between disks were 3 mm and 1.5 mm. This result may illustrate process of cell lysis; shear force which was produced by rotating system firstly decomposed EPS in the first 5 minutes and then broke the cell wall and released intracellular compounds into liquid phase in the following 20 minutes. Similar result was found in other researchers’ experiment [14].Actual power of motor was 15 kw when rotating disk system worked with optimal parameters. ParameterK was very similar when rotating disk system and ultrasonic system worked in the same time shown in Table 1, but power density of rotating disk system was only 0.19 W/mL which was much less than ultrasonic system. Low energy demand was very obvious compared with ultrasonic system. Besides, no chemical reagents consumption, simple operation, and treatment ability of large quantity excess sludge were also advantages compared with other sludge disintegration methods.Combination of rotating disk system and ultrasonic system for sewage disintegration was investigated in this study shown in Table1. Because of these combined treatments, disintegration effect was ideal; K reached 81.2% when sample was treated by rotating disk system for 35 minutes and then ultrasonic system for 10 minutes. It was worthy to note that obvious increase of K could not be realized by prolonging treatment time of rotating disk system in this combined treatment. In view of this study, combination of rotating disk system and ultrasonic system had outstanding effect on sludge disintegration because this combined system can have better disintegration effect of excess sludge in less time with energy conservation.


## 5. Conclusion

Rotating disk system had very impressive performance on disintegration of excess sludge; disintegration parameterK can reach 68.7% with optimal parameters by this system. Closer distance and higher rotating speed can effectively promote disintegration effect of excess sludge. Special features on surfaces of disks had outstanding performance to improve disintegration effect of excess sludge during treatment. Combination of rotating disk system and ultrasonic system can realize better disintegration effect in shorter time. Consequently, rotating disk system was a promising technique for minimization of excess sludge.



---

*Source: 1563560-2016-07-13.xml*