| Literature DB >> 33784608 |
Zachary W LaTurner1, David M Zong1, Prashant Kalvapalle2, Kiara Reyes Gamas2, Austen Terwilliger3, Tessa Crosby1, Priyanka Ali1, Vasanthi Avadhanula3, Haroldo Hernandez Santos3, Kyle Weesner3, Loren Hopkins4, Pedro A Piedra3, Anthony W Maresso3, Lauren B Stadler5.
Abstract
As the COVID-19 pandemic continues to affect communities across the globe, the need to contain the spread of the outbreaks is of paramount importance. Wastewater monitoring of the SARS-CoV-2 virus, the causative agent responsible for COVID-19, has emerged as a promising tool for health officials to anticipate outbreaks. As interest in wastewater monitoring continues to grow and municipalities begin to implement this approach, there is a need to further identify and evaluate methods used to concentrate SARS-CoV-2 virus RNA from wastewater samples. Here we evaluate the recovery, cost, and throughput of five different concentration methods for quantifying SARS-CoV-2 virus RNA in wastewater samples. We tested the five methods on six different wastewater samples. We also evaluated the use of a bovine coronavirus vaccine as a process control and pepper mild mottle virus as a normalization factor. Of the five methods we tested head-to-head, we found that HA filtration with bead beating performed the best in terms of sensitivity and cost. This evaluation can serve as a guide for laboratories establishing a protocol to perform wastewater monitoring of SARS-CoV-2.Entities:
Year: 2021 PMID: 33784608 PMCID: PMC7957301 DOI: 10.1016/j.watres.2021.117043
Source DB: PubMed Journal: Water Res ISSN: 0043-1354 Impact factor: 11.236
Characteristics of the different wastewater treatment systems. Average daily flow rate was recorded on the day of October 5. Population data was extracted from the 2019 American Community Survey (U.S. Census Bureau, 2019). Composition data were reported from samples taken between October 5, 2020 to October 6, 2020. All data was provided by the City of Houston (Houston Public Works and Houston Health Department).
| Wastewater Treatment Plant (Anonymized) | Average Daily Flow Rate (MGD) | Population | TSS (mg/L) | CBOD (mg/L) | NH4-N (mg-N/L) |
|---|---|---|---|---|---|
| 8.52 | 167,000 | 342 | 126 | 26.2 | |
| 16.6 | 304,000 | 970 | 120 | 17.4 | |
| 9.69 | 330,000 | 196 | 155 | 26.2 | |
| 0.18 | 13,400 | 100 | 155 | 34.2 | |
| 3.21 | 86,600 | 58.7 | 108 | 30.5 | |
| 1.53 | 48,200 | 106 | 201 | 32 |
Fig. 1Overview of the evaluated concentration methods. Wastewater samples were collected from several wastewater treatment plants across Houston in sample collection bottles and immediately spiked with BCoV (top). The samples were then concentrated through several methods: a) direct extraction, b) HA filtration with bead beating, c) HA filtration with elution, d) PEG precipitation, and e) ultrafiltration. All concentrated samples subsequently underwent RNA extraction. Samples undergoing direct extraction were not concentrated and instead were directly extracted from the liquid phase of the wastewater samples.
Fig. 2SARS-CoV-2 RNA Concentrations. N1 (A) and N2 (B) gene target concentrations determined using different concentration methods for six wastewater samples reported in gene copies/L wastewater. N1 (C) and N2 (D) gene target concentrations determined using different concentration methods for six wastewater samples reported in gene copies/uL RNA template. Black horizontal lines indicate LoQs. WWTP are A-E, DI is deionized water, and NTC is no template control.
Summary of key metrics of each concentration method. A detailed breakdown of costs and list of equipment used can be found in S14-23. The coefficient of variation (%CV) was determined by calculating the coefficient of variation of the replicates for a single wastewater treatment plant and then averaging that coefficient of variation across all wastewater treatment plants for a given concentration method.
| Method | Startup cost ($) | Consumables cost ($/ sample) | Throughput (hr/6 samples) | LoQ (gc/L WW) | Effective LoQ (gc/L WW) | Average BCoV Recovery Percent | BCoV %CV | pMMoV %CV |
|---|---|---|---|---|---|---|---|---|
| $5,650 | $0.14 | 0.1 | 2.56E+05 | 8.39E+06 | 3.84% | 14.6 | 29.9 | |
| $15,368 | $1.50 | 0.7 | 3.07E+03 | 2.76E+05 | 0.96% | 27.3 | 25.9 | |
| $11,160 | $5.80 | 0.5 | 2.56E+04 | 3.89E+06 | 0.57% | 20.9 | 31.8 | |
| $20,288 | $11.02 | 4.6 | 2.56E+03 | 2.70E+06 | 0.08% | 39 | 49.8 | |
| $9,000 | $12.10 | 1.5 | 7.67E+03 | 2.63E+06 | 0.36% | 24.4 | 49.5 |
Fig. 3BCoV and pMMoV concentrations. Recovery of BCoV (a) and pMMoV (b) between different concentration methods and different WWTP reported in gene copies/L wastewater. Recovery of BCoV (c) and pMMoV (d) between different concentration methods and different WWTP reported in gene copies/μL RNA template. WWTP are A-E, DI is deionized water, and NTC is no template control.