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250                                   8 Pre-combustion Air Emission Control

            Fig. 8.6 Effect of
            temperature on the HTC
            product
















              Water goes through dramatic changes in both physical and chemical properties
            when heated. As the temperature rises from 25 to 300 °C under standard pressure,
                                                                          3
            the density and dielectric constant of water decreases from 997 to 713 kg/m and
                                                                        13.99
            78.85 to 19.66, respectively, while the ionic product increases from 10  to
              11.30
            10   . These changes in physical properties make the solvent properties of water at
            300 °C roughly equivalent to those of acetone at 25 °C. Ionic reactions of organics
            are favored by the increase of solubility in water. The increase in the dissociation
            constant increases the rate of both acid- and base-catalyzed reactions in water far
            beyond the natural acceleration due to increased temperature. Water itself can also
            act as an acidic or basic catalyst, and its reactivity can often be reinforced by
            autocatalysis from water-soluble reaction products.
              Under high-temperature high pressure conditions, water shows even more
            unique properties as a reaction medium, especially with the presence of suitable
            catalysts. At supercritical condition (385–400 °C, 35 MPa) the reaction for HTC
            conversion can be completed within a minute.
              Residence time is another factor for a successful conversion. The HTC bio-oil
            yields under acidic, neutral, and alkaline conditions all decrease with increasing
            residence time. Despite the similar trends of HTC bio-oil yields against conversion
            temperatures and the residence time, the conversion mechanisms behind them are
            likely quite different. Under acidic HTC conditions, the decrease in bio-oil yields at
            high temperatures and long residence time is mainly attributed to the formation of
            residual solids. Under acidic conditions, 5-HMF, the main component of acidic
            HTC bio-oil, tends to form hydrothermal char/solid by polymerization. Under
            neutral conditions, the decrease in HTC bio-oil yield at high temperatures and long
            reaction residence time is mainly caused by the formation of residual solids and the
            gas products. Under alkaline HTC conditions, the gas formation from the decom-
            position of alkaline HTC bio-oil mainly resulted in the bio-oil yield decrease at the
            high temperatures (>300 °C).
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