Improved biodegradation of hydrophobic volatile organic compounds from the air stream in a multilayer biofilter

Graphical abstract


Specification
Area: Environmental Science More specific subject area:

Air pollution control
Protocol name: Improved biodegradation with multilayer biofilter Reagents/tools: GC/FID, model: Varian CP-3800, USA, column characteristics: type: CP-sil5 CB, column: 15.0 m Â 0.25 mm Â 0.45 mm, injector characteristics: the injector temperature was constant at 200 C, carrier gas: Nitrogen (N 2 ) at a flow rate of 1.2 ml min À1 , make-up gas: nitrogen (N 2 ) at a flow-rate of 25 ml min À1 . Experimental design: All sampling and parameters analysis were measured according to in our previous study [1].
Trial registration: Not required Ethics: Not required

Value of the Protocol
Biofiltration of VOCs is only dependent on its own gas solubility and bioavailability [2,3]. Thus, these pollutants are usually poorly removed by biofiltration [4,5,6]. The application of a chemical or biological surfactant can be one of the practical options to enhance the bioavailability and solubility of hydrophobic organic compounds (HOCs) [7,8,9,10]. Rhamnolipids are anionic bio-surfactants which are produced by Pseudomonas sp. Bacteria. Biosurfactants compare to chemical surfactants are more effective, less toxic, environmentally friendly and more biodegradable. It increases the water solubility of HOCs and thereby facilitates the biodegradation of these compounds [11,12,13,14].

Description of protocol
Biofilter set-up and operation The biofilter was included a stainless steel column with 120 cm height, 15 cm inner diameter and effective volume of15.8 L (three sections, each 40 cm height (Fig. 1). Airflow was supplied by a 150 L compressor. Four different mixtures of materials consisted of 40% compost, 20% scoria, 20% sugar beet pulp, and 20% poplar tree skin were used as packing materials in the biofilter. More details are available in our previous study [1]. After the start-up phase, the performance of biofilter in various operational conditions at presence and absence of the biosurfactant was surveyed during the operation period (131 days in 6 phases). Operating conditions of each phase are presented in Table 1. To decrease the adaptation time of microorganisms in the biofilter bed, fresh activated sludge of the wastewater treatment plant was used as an inoculum source for the biofilter bed.

Chemicals
N-hexane and all the other chemicals for preparation of the nutrient solution were obtained from Merck Company (with a purity 99%). The composition of the nutrient solution (per liter of distilled water) was as follow: 0.5 g NaCl, 0.1 g NaHCO 3 (for control of pH in the liquid medium), 0.15 g KH 2 PO4, 0.3 g MgSO 4 , 0.01 g FeSO 4 , 0.5 g NH 3 SO 4 ,1.9 g ClNH 4 , 0.03 g MnSO 4 , 0.03 g ZnSO 4 [1,15]. Rhamnolipid biosurfactant with a purity of 95.0% was obtained from Institute of chemical engineering of Iran (ICEI). The concentrations of 50,100, 200 and 300 mg/l of the biosurfactant were prepared in nutrient solution and individually introduced to the biofilter in optimum EBRT (120 s). After application, 300 mg/l was selected as an optimal concentration of rhamnolipid and used in the rest of the experiments.

Analytical methods
Concentrations of n-hexane in inlet and outlet of the biofilter were analyzed using a gas chromatograph equipped with an FID (GC/FID, Varian CP-3800, USA) with column details of 15.0 m Â0.25 mm Â0.45 mm (CP-sil5 CB). The temperature of the detector was set to 280 C. Nitrogen (N 2 ) at a flow rate of 1.2 and 25 ml min À1 was used as a carrier and make-up gas, respectively. The injector temperature was constant at 200 C. More details are available in our previous study [1]. For draw up of the calibration curves, various concentrations of n-hexane were injected into glass bottles sealed with a Teflon and analyzed after stabilization. For measurement of n-hexane concentrations, any time 0.5 ml of gas was injected into the GC-FID with a gas-tight syringe (Hamilton, USA). Total air samples taken from inlet and outlet of the biofilter during the operation period (131 days; without the  start-up period) was 262. To evaluate the removal efficiency of n-hexane in the biofilter, two samples were taken daily and the mean values of them were used for the calculation of removal efficiency and elimination capacity.

Effect of rhamnolipid biosurfactant on the performance of the biofilter
The trend of removal efficiency (RE) and elimination capacity (EC) of n-hexane with and without the biosurfactant in different inlet loading rate (IL) was illustrated in Fig. 2. The removal efficiency of nhexane in the biofilter without addition of rhamnolipid was 46.8%, whereas, with the addition of rhamnolipid, the removal efficiency was increased. So that, in concentrations of 50, 100, 200 and 300 mg/l rhamnolipid, the removal efficiency reached to 47.26%, 56.76%, 73.24% and 85.13%, respectively. There is a positive linear relationship between the solubility of HOCs and the biosurfactant concentrations. Therefore, with increasing the concentration of the biosurfactant the removal percentage of n-hexane was increased [1,16].

Conclusions
Single biofilter due to low water solubility and low bioavailability of HOCs has not high removal efficiency for n-hexane. Our results confirmed that introduction of rhamnolipid as a proper biosurfactant to the biofilter media with favorable concentration can notably increase the removal Fig. 2. Influence of rhamnolipid biosurfactant on n-hexane removal efficiency, elimination capacity and CO 2 production. efficiency of HOCs from the air stream. So that, in our study, the mean removal efficiency of n-hexane by adding rhamnolipid biosurfactant to the biofilter media and under optimum EBRT (120 s) was increased from 46.8% to 85.13%. Because rhamnolipid biosurfactant by reducing surface tension and causing micelles formation can increase the water solubility and bioavailability of HOCs for microorganisms in the biofilter media.

Declaration of Competing Interest
The authors of this article declare that there is no conflict of interests.