Environmental Science & Engineering - www.esemag.com - November 2005
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SBR system for large Chinese pulp & paper mill

By Peter McCarthy,M.A.Sc. and Zhiping Qiu, M.Sc.E., P.Eng.

Sludge thickener (foreground) and SBR basins (background).
In 2005, ADI Systems Inc. of Fredericton, New Brunswick, completed commissioning for a large ADI-SBR wastewater treatment system for Guangzhou Paper, one of China's largest pulp and paper mills. In North America, ADI Systems normally provides turnkey installations, but in China we typically supply a technology package, which for this project included: process design; detailed design of selected components; design manual (to guide local detailed designers); ADI-ASD decanters; jet aeration system; instrumentation; control valves; DCS control system; operator training; and commissioning.

The paper mill is located in Guangzhou city centre on the shore of the Pearl River in southern China. The mill has chemi-thermomechanical pulping, sulfite pulping, groundwood pulping, and paper-making operations. Before installation of the Sequencing Batch Reactor (SBR) system, approximately 5000 m3/d of wastewater was pretreated in a high-rate aerobic system and low-strength wastewater was pretreated in two dissolved air flotation units.

New effluent regulations required the mill to install a secondary wastewater treatment system. The new discharge limits for COD, BOD, and TSS are 200 mg/l, 30 mg/l, and 200 mg/l, respectively.

The design wastewater characteristics for the biological treatment plant are summarized in Table 1.


ADI’s partners on this project included the mill, which provided project and construction management, and the Changsha Design Institute that provided detail design.

The new wastewater treatment system includes the following major components: The ADI-SBR system is comprised of five on-grade, common wall, castin- place concrete basins. Each SBR tank is 31.5 m by 68 m and has a 7.5 m wall. The treatment plant was constructed using 12,000 tonnes of concrete and 1600 piles. The average depth of piles is 14 m with a pile diameter of 40 cm. The total weight of reinforcing steel used in the project was 1400 tonnes.

During the construction period, the concrete and steel prices increased substantially, and the contractor had to resolve the price escalation problems with the mill before resuming the construction work. Therefore, there was a delay in the treatment plant construction schedule. However, pressure from the local government was so high that the mayor of Guangzhou promised the public that he would swim in the Pearl River in 2005!

Nutrient supplementation was required for biological treatment. Urea (dry) was selected for nitrogen, and 75% phosphoric acid was selected for phosphate. Urea was purchased in bags and dissolved and stored in fiberglass tanks. Phosphoric acid was transferred into the fiberglass storage tanks directly from tanker trucks. Each storage tank is equipped with a level-indicating transmitter. The daily chemical consumption is calculated based upon the liquid level change.

Each basin is equipped with a simple influent distribution system, waste sludge collection manifold, and jet aeration system, all of which are located on the basin floor. Each basin is also equipped with three ADI-ASD decanters and instrumentation. The instrumentation includes a pH/temperature sensor and analyzer, a dissolved oxygen sensor and analyzer, a level indicating transmitter, and a level switch.

Each SBR basin is equipped with a jet aeration system, with two jet aerators running the length of each basin for oxygen supply and mixing. The jet aeration system has demonstrated that it has excellent efficiency in transferring oxygen from the air to the process water and is quite reliable in terms of maintenance. Each basin is connected to one dedicated, multi-stage, centrifugal blower. Energy consumption is minimized by a control valve on the suction side of the blower. As oxygen demand increases or decreases, the blower power draw and air flow is increased or decreased via the inlet control valve.

The control system is designed for flexible operation of the system. The DCS operator interface is intuitive and bilingual. The SBR cycle length is variable, and the system can be run with any number of basins on line. Individual event durations (Fill, Fill/Aerate, Aerate, Mix, Settle, and Decant) are also adjustable. The system can be operated using continuous flow to the SBR system, holding the Equalization Basin (EQB) level constant, or flow can be stored in the EQB for shorter Fill durations. The aeration system can also be operated manually should the dissolved oxygen monitoring system be out of service for maintenance. All setpoints are adjustable by the operator or supervisory staff.

Two of ADI's process engineers were on-site for operator training and commissioning which got underway late in 2004. One ADI process engineer spoke Mandarin; this helped with communications between ADI and the mill staff. Although the Process Operations Manual and other start-up materials were written in English, all screens on the interface with the DCS were bilingual (Chinese and English). During the first six months, the influent flow had been close to design, averaging approximately 60,000 m3/d; however, the influent COD has consistently been higher than design (of 750 mg/l), frequently averaging over 1,500 mg/l.

Results from the first six months indicate that the system is performing very well, although the SBR influent COD and TSS are constantly above design conditions (the weekly average influent COD is frequently more than double the design value). The average effluent BOD for the past six months was 10 mg/l; however, the effluent COD was higher than discharge limit (due to the high influent values and the non-biodegradable COD fraction typical of pulping wastewaters). The owner has been very satisfied with the SBR system performance due to the excellent BOD removal, low maintenance, low operating costs, ease of operation, and its reliability. They are especially pleased with the system's capability to handle higher than design COD, BOD, and TSS concentrations.


Peter McCarthy, M.A.Sc. and Zhiping Qiu, M.Sc.E, P. Eng. are with ADI Systems Inc.
Contact: pjm@adi.ca or zpq@adi.ca


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