Ion Exchange Resin Case Study

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Ion exchange resin (Amberlyst 36) was purchased from Sigma–Aldrich (total pore volume 0.20 mL/g). According to the information offered by the supplier, the average pore diameter and surface area of the resin are about 240 Å and 33 m2/g, respectively. Pt/C (Sigma-Aldrich, 5wt% loading) was used for the consecutive hydrodeoxygenation reaction.

2.2. Fast pyrolysis of yellow poplar
Yellow poplar (Liriodendron tulipifera) was ground, passed through a 0.5 mm sieve, and pyrolyzed. Fast pyrolysis was accomplished at 500 °C and the residence time was regulated at 1.63 s by an inert nitrogen gas flow. Then, 2 kg of biomass was fed into the fluidized-bed fast pyrolysis reactor and held for 1 h. The nitrogen gas in the reactor was maintained at a flow rate of 50 L/min. The volatile pyrolytic products were cooled and condensed to a liquid phase bio-oil with an average yield of 48.3 wt% [19].

2. 3. Ion exchange resin treatment of bio-oil with amberlyst 36
The mixture of bio-oil (40 g) and ethanol (10 g) was placed with amberlyst 36 resin into the autoclave reactor (200 mL SUS316). The reactor was sealed and flushed three times with N2. After that, the reaction was performed at under mild temperature conditions (50, 100, or 150 °C) under 3 MPa H2 pressure. After the resin …show more content…

In order to investigate the acidity of the bio-oil and heavy oil, the total acid number (TAN) was measured by the ASTM D664 method. The viscosity was determined using a capillary-type viscometer and ViscoClock (Schott Instruments) at 40 °C. Elemental analysis for carbon, hydrogen, and nitrogen was carried out with an Elementar Vario El cube, and the mass percentages of C, H, N, and S were directly determined by the Dumas method. The higher heating value (HHV) was calculated by Sheng and Azvedo's formula [21]. The degree of deoxygenation (DOD) was estimated as

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