2015
DOI: 10.15376/biores.10.4.zhang
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Anaerobic Digestion for Use in the Pulp and Paper Industry and Other Sectors: An Introductory Mini-Review

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Cited by 13 publications
(10 citation statements)
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“…The VLR of the IC reactor at the Saigon Paper mill is 6-14 kg/m 3 .d, and as Figure 5 shows, the higher the VLR rate the higher the COD removal efficiency. This has been proven by a study conducted by Zhang, et al (2015) [8]. But a paper mill's VLR could reach 20-25 kgCOD/m 3 .d as in the case of Guangxi Nanning Sugar Industry Co., Ltd. [8] Unfortunately, Saigon Paper's IC reactor has never shown a VLR higher than 14 kg/m 3 .d, and only one reactor is currently running so it is not possible to see its maximum VLR load.…”
Section: Results and Discussuonmentioning
confidence: 99%
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“…The VLR of the IC reactor at the Saigon Paper mill is 6-14 kg/m 3 .d, and as Figure 5 shows, the higher the VLR rate the higher the COD removal efficiency. This has been proven by a study conducted by Zhang, et al (2015) [8]. But a paper mill's VLR could reach 20-25 kgCOD/m 3 .d as in the case of Guangxi Nanning Sugar Industry Co., Ltd. [8] Unfortunately, Saigon Paper's IC reactor has never shown a VLR higher than 14 kg/m 3 .d, and only one reactor is currently running so it is not possible to see its maximum VLR load.…”
Section: Results and Discussuonmentioning
confidence: 99%
“…The second component of the IC reactor is responsible for treating the wastewater with a lower organic load from the first component, and the treated wastewater then flows out for the next treating process. [8] Due to its unique mechanics, the IC reactor has many advantages over the UASB: investment cost is lower as the IC reactor volume is smaller but treats the same type of wastewater; it is taller, therefore saving the ground space usually required; OLR is higher but with lower hydraulic retention because internal circulation is occurring inside the reactor and mixes very well with the influent; external circulation is optional as internal circulation occurs, saving energy needed for external circulation; internal circulation also helps dilute the influent, so the IC reactor has a higher shock loading [9].…”
Section: Ic Reactor Processesmentioning
confidence: 99%
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“…A possible explanation of this discrepancy finding is two reasons. Firstly, IC has a higher treatment capacity than UASB, as the same conditions of this WWTP, IC generates approximately 7,895 m 3 biogas/day (Driessen et al 2000) as compared with 6,090 m 3 biogas/day of UASB (Metcalf et al 2004); the biogas could utilize become energy (3,088 kWh and 2,382 kWh for IC and UASB, respectively); therefore, IC could hugely reduce the energy or reduce the global warming, ozone formation-human health, ozone formation-terrestrial ecosystems (Driessen et al 2000;Zhang et al 2015). Secondly, even both IC and UASB are anaerobic techniques; however, the chemical balance for COD: N: P in IC is 800:5:1 while UASB is 350:5:1, which means IC process uses fewer chemicals more with lower HRT compared to UASB.…”
Section: Ic and Uasb Scenarios Environmental Analysismentioning
confidence: 99%
“…High VFA concentrations can also lead to a drop of pH in the reactors which is unfavorable for the methanogens. Although the AD process can proceed at a wide range of pH values at different stages, the optimal range for methanogens is 6.5-7.5 and should be maintained to enhance the activities of these bacteria [45][46][47]. Therefore sufficient alkalinity is required during the AD process to counteract instability and system failure in the process [45].…”
Section: Acidogenesis and Acetogenesismentioning
confidence: 99%