“…In the evaluation of the elimination performance of pharmaceutical merchandise from WW in sewage remedy plants, the researcher observed that the chemical oxygen demand (COD) was 3,173 ± 1,528 mg/L and the biochemical oxygen demand (BOD) was 1,206 ± 397 mg/L Kodom et al [21] Based on the analysis of the PWW treatment technology, the COD concentration was 20,000 mg/L Feng [6] Based on the study of a sustainable approach for PWW treatment, the researcher observed that the COD was 3,200 mg/L, the BOD was 1,690 mg/L, and the total suspended solids (TSS) were 296 mg/L Fawzy et al [22] The origin and character of PWW were summarized in this paper. The researcher found that the range of COD was 2,000 mg/L to 10,000 mg/L, the five-day biochemical oxygen demand (BOD 5 ) was 1,000 mg/L to 2,500 mg/L, pH 4 to pH 8, and total nitrogen (TN) was 500 mg/L to 1,500 mg/L Fazal et al [23] The researcher observed that the total dissolved solids (TDS) were 2,450 ± 1.09 mg/L in the study of the PWW of antibiotics Ng et al [24] The researcher found a COD of 1,565 ± 114 mg/L in the study of antibiotic waste Ng et al [25] The study of PWW fermentation Chen et al [26] From the assessed hazards of the WWTP of the pharmaceutical industry, the researcher observed a pH range of 5.8 to 7.8, TSS was 230 mg/L to 830 mg/L, TDS was 650 mg/L to 1,250 mg/L, BOD was 20 mg/L to 620 mg/L, and COD was 128 mg/L to 960 mg/L Choudhary and Parmar [27] From the assessed biodegradability of PWW treated by ozone, the researcher observed a rate of pH 6.9, TSS of 370 mg/L, TDS of 1,550 mg/L, BOD of 120 mg/L, and COD of 490 mg/L Gome and Upadhyay [28] In the study of mixed PWW treatment, the researcher observed a rate of pH 7.2 to pH 8.5, TSS of 48 mg/L to 145 mg/L, BOD of 480 mg/L to 1,000 mg/L, and COD of 2,000 mg/L to 3,500 mg/L Wei et al [29] Based on the study of the production of bulk drug TDS, the researcher found that TDS was 15,000 mg/L Deshpande et al [30,31] 2010,…”