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The adsorption of humic substances on three different adsorbents was investigated and adsorption isotherms were applied in this research. The three adsorbents studied include granular activated carbon (GAC), ferric oxihydroxide in its beta form (β-FeOOH) and iron-coated activated alumina (AAFS). Physical and chemical characteristics of the adsorbents were also fully investigated. Calcium was added to the HS solution in order to represent water with a hardness equivalent to water hardness typically found in London (UK). The examination of the GAC indicated a large microporous area with lower surface area associated with meso- and macropores. The AAFS and β-FeOOH did not present any microporous area. The overall surface area was high for GAC (980 m2 g−1) but lower for AAFS (286 m2 g−1) and β-FeOOH (360 m2 g−1). The Freundlich isotherm model was fitted to all adsorbent–adsorbate systems. It was shown that GAC offered a large adsorption capacity for removal of low molecular weight humics F1 (MW 0–5 kDa) but not for substances with molecular weight larger than 10 kDa (F3). The β-FeOOH adsorption capacity was only 0.43 mg g−1, compared with 9.11 and 2.55 mg g−1 on GAC and AAFS, respectively. On the contrary, F1 is not well adsorbed and only F2 (5–10 kDa) can be efficiently removed by AAFS and β-FeOOH. It was strongly suggested that precipitation/condensation occurred on the adsorbent surface.Other Information Published in: Emergent Materials License: https://creativecommons.org/licenses/by/4.0See article on publisher's website: http://dx.doi.org/10.1007/s42247-020-00083-4

Crystallization, filtration and drying are important separation and purification unit operations in the pharmaceutical and speciality chemical industries. Continuous processing technologies have emerged as a promising alternative to the more conventional batch processing. Previous studies primarily focus on crystallization and as a result subsequent stage of filtration and drying are overlooked. In the present short communication, a phenomenological parallel is drawn with the drying of porous solids, studies for which are relatively widely reported. Such analysis helps to identify, the fundamental cause for lump formation, and possible mitigation strategies. Based on the postulated physical scenario, two prototype designs to intensify continuous operation of filtration and drying units are discussed. The prototype solutions could make it possible to intensify or combine multiple stages of filtration, deliquoring, washing and drying thus enabling efficient continuous processing of solid form pharmaceutical and specialty chemicals.