Enhancement of biogas production and COD removal of caramel process condensate by anaerobic-aerobic treatment and a pilot-scale application

被引:0
|
作者
Wang, Jun [1 ,2 ]
Chen, Huanjun [3 ]
Qin, Lei [2 ]
Liu, Fen [2 ]
Zhu, Shunni [2 ]
Zhang, Yuhong [1 ]
机构
[1] Shenyang Univ Chem Technol, Sch Environm & Safety Engn, Shenyang 110142, Peoples R China
[2] Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangdong Prov Key Lab Renewable Energy, CAS Key Lab Renewable Energy, Guangzhou 510640, Peoples R China
[3] Foshan Haitian Gao Ming Flavoring & Food Co Ltd, Foshan 528000, Peoples R China
关键词
Caramel process condensate; UASB; Aerobic treatment; COD removal; Salinity; WASTE-WATER; DIGESTION;
D O I
10.1016/j.jwpe.2025.107308
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The caramel production process generates substantial volumes of caramel process condensate (CPC) with high chemical oxygen demand (COD) levels (20,000-30,000 mg/L) and low pH (2-3). This study evaluated biogas production and COD removal using anaerobic-aerobic treatment under varying pH (7-4) and salinity (0-50 g/L). Laboratory experiments achieved over 90 % COD removal and a daily biogas production rate (DBPR) of 0.64 m3/ (kg center dot COD) at an organic loading rate (OLR) of 5 kg COD/(m3 center dot d), influent COD concentration of 10,000 mg/L, hydraulic retention time (HRT) of 2 days, and influent pH of 4. Salt tolerance tests showed that at an OLR of 2.5 kg COD/(m3 center dot d) and NaCl concentration below 10 g/L, COD removal efficiency remained 90 %, with a DBPR of 0.92 m3/(kg center dot COD). At 34 g/L NaCl, COD removal decreased to 80 % and DBPR to 0.63 m3/(kg center dot COD). Pilot experiments confirmed that, under conditions of an OLR of 1.8 kg COD/(m3 center dot d), influent COD of 10,000 mg/L, a HRT of 6 days, and a pH range of 6.8 to 4.8, the COD removal efficiency was 90 %, the DBPR was 0.63 m3/ (kg center dot COD), and methane production(MP) reached 0.31 m3 CH4/(kg COD). The anaerobic-aerobic combined treatment achieves over 90 % COD removal, offering an efficient and cost-effective solution for the resource utilization of CPC.
引用
收藏
页数:12
相关论文
共 21 条
  • [21] Performance of a pilot-scale sewage treatment: An up-flow anaerobic sludge blanket (UASB) and a down-flow hanging sponge (DHS) reactors combined system by sulfur-redox reaction process under low-temperature conditions
    Takahashi, Masanobu
    Yamaguchi, Takashi
    Kuramoto, Yoshiharu
    Nagano, Akihiro
    Shimozaki, Satoshi
    Sumino, Haruhiko
    Araki, Nobuo
    Yamazaki, Shinichi
    Kawakami, Shuji
    Harada, Hideki
    BIORESOURCE TECHNOLOGY, 2011, 102 (02) : 753 - 757