Adsorptive Separation Processes Research Articles

Effective removal of toxic dye from wastewater via advanced modified magnetic sepiolite using combined surfactants SDS/CTAB/Fe3O4@Sep: Empirical and computational analysis studies

In the present era, the elimination of hazardous dyes from wastewater has emerged as a paramount concern, captivating the interest of scientists globally because their detrimental effect on human health. Adsorption, a well-established and effective separation process, is commonly employed for eliminating various harmful organic pollutants from water, particularly toxic dyes. In this study, a novel magnetic organo-composite was synthesized through an environmentally friendly and easily implementable approach. Subsequently, various analytical techniques, including XRD, FT-IR, SEM, and EDX, were utilized to scrutinize the structure and morphology of the adsorbent. The as-prepared adsorbent demonstrated remarkable efficiency in rapidly removing malachite green dye from aqueous solutions, attaining a peak adsorption capacity of 227.40 mg g−1. Furthermore, several factors affecting the adsorption process were investigated, including adsorbent dosage, medium pH, initial dye concentration, and contact time. The examination of adsorption kinetics data indicated that the process adhered to a pseudo-second-order model (R2 = 0.97), implying that chemisorption constituted the controlling step in the reaction. Additionally, the experimental adsorption isotherms exhibited a close fit to the Langmuir model (R2 = 0.98). Crucially, the SDS/CTAB/Fe3O4@Sep magnetic organo-nanocomposite adsorbent exhibited the capacity for multiple reuses, maintaining its effectiveness over five cycles without notable activity decline. Consequently, the synthesized organo-composite appears to show potential as an effective adsorbent for eliminating harmful cationic dyes present in wastewater. Molecular dynamics (MD) simulations, employing Monte Carlo adsorption locator simulation (MCL) calculations, further supported the elevated adsorption of SDS/CTAB on Sep, Fe3O4 on SDS/CTAB@Sep, and MG molecules on SDS/CTAB/Fe3O4@Sep due to their negative adsorptions.

In situ conversion of ZnO anchored on porous carbon foams to antiflexible ZIF-8-X (X = Co or NH2) for sieving linear and mono-branched hexane isomers

Efficient separation of linear hexane from their isomers is a vital petrochemical process to produce high-quality gasoline. Zeolitic imidazolate frameworks-8 (ZIF-8), one of the most famous metal-organic frameworks (MOFs), is a promising separation material due to its special pore size (3.4 Å), whereas the flexible framework limited its separation ability, showing unsatisfied trade-off between adsorption capacity and separation selectivity. Here, we propose a novel strategy of post metal-oxide modification (PMOM) to suppress ZIF-8 flexibility by in situ growth on rigid layer of porous carbon foam (PCF) based the intermediation of anchored ZnO nanoparticles directly obtained from the pyrolysis of sucrose and zinc nitrate mixture. Afterwards, synergistic flexible suppression technology (SFST) was adopted to design antiflexible PCF/ZIFs with mixed-metal and mixed-ligand, including bi-metal PCF/ZIF-8-Co and di-ligand PCF/ZIF-8-NH2. Therein, the tight interfaces generated with benzene-ring inhabited the swinging of linkers and hindered 3-MP entry into the pore channels, showing both remarkable nHex adsorption capacity (q = 2.26 mmol·g−1) and nHex/3-MP selectivity (Su = 9.42). Moreover, bi-component adsorption experiments confirm the practical separation performance and cycling stability, showing promising application in adsorptive separation processes.

High capacity laminate adsorbers: Enhancing separation performance beyond packed beds

In response to the growing demand for more efficient adsorption processes, structured adsorbents have emerged as a promising solution as they offer improved mass transfer and pressure drop characteristics. However, they are often hampered by a lower volumetric capacity due the presence of support structures or a large bed void fraction. This research focuses on the manufacturing and evaluation of self-standing zeolitic laminates of various thickness and spacing, comparing their performance to a traditional packed bed. A shaping method to obtain laminates with a 84 wt% zeolite 13X content is described. Furthermore, a method for precise assembly and spacing of the laminates is detailed. Three such laminar adsorbers with different geometries were evaluated in breakthrough experiments and compared to a packed bed to assess their efficiency in the bulk separation of carbon dioxide. Superior performance of the laminar adsorbers was found, with one configuration employing 1.2 mm laminates and 0.4 mm spacing showing a significant 19 % increase in volumetric capacity compared to a packed bed of pellets. This enhanced capacity is achieved while maintaining efficient heat and mass transfer, resulting in sharp breakthrough profiles. Furthermore, using thinner (0.5 mm) laminates, the length of unused bed was further reduced. Additionally, pressure drop calculations were performed and experimentally validated. The pressure drop over the laminar adsorbers was shown to be significantly lower than over a packed bed. These findings underscore the potential of laminar adsorbers to intensify adsorptive separation processes, reduce energy consumption, and address the demand for more effective adsorption technologies.

Interchangeable effect of polyols-based zeolite on the separation of CO2, CH4, and N2 gases

The adsorptive separation process for CO2/CH4 and CH4/N2 gas separation has commercial potential, in biogas, Coalbed Methane process etc. although it remains to strive due to the absence of effective adsorbents. Zeolite NaY was used in this study due to its uniform pore structures, surface properties, and potential gas separation adsorbent. Zeolite NaY was modified by polyether polyols (PEPO) to get an adsorbent for selective separation of CO2/CH4 and CH4/N2 gas mixtures. The PXRD, FT-IR, GPC, 1H NMR, TEM, and surface area analysis were used to characterize the PEPO and PEPO-modified zeolite. The single component equilibrium adsorption desorption isotherms with PEPO modified NaY zeolites and NaY zeolite for CO2, CH4 and N2 were measured at 298, 313, and 328 K and up to 5 bar pressure. The isotherm data of CO2, CH4 and N2 were fitted in Dual Site Langmuir equations, and adsorption selectivity of CO2/CH4 and CH4/N2 gas mixtures was predicted using Ideal Adsorbed Solution Theory (IAST) method for 90:10, 50:50 (vol/vol) CH4/N2 and 80:20, 50:50 (vol/vol) CO2/CH4 feed gas mixtures representing coal bed methane gas composition and pressure conditions. The high surface area and hydroxyl groups in PEPO-modified NaY enhanced selectivity for CO2/CH4 and CH4/N2 gas separation. The selectivity predicted by the IAST method were 106.12 and 95.34 for 0.5 % PEPO-NaY (80:20 v/v and 50:50 v/v) for CO2/CH4 and 3.95 and 3.52 for 2 % PEPO-NaY (90:10 v/v and 50:50 v/v) for CH4/N2 at 298 K up to 5 bar respectively.

Generalised analytical method unravels framework-dependent kinetics of adsorption-induced structural transition in flexible metal–organic frameworks

Flexible metal–organic frameworks (MOFs) exhibiting adsorption-induced structural transition can revolutionise adsorption separation processes, including CO2 separation, which has become increasingly important in recent years. However, the kinetics of this structural transition remains poorly understood despite being crucial to process design. Here, the CO2-induced gate opening of ELM-11 ([Cu(BF4)2(4,4’-bipyridine)2]n) is investigated by time-resolved in situ X-ray powder diffraction, and a theoretical kinetic model of this process is developed to gain atomistic insight into the transition dynamics. The thus-developed model consists of the differential pressure from the gate opening (indicating the ease of structural transition) and reaction model terms (indicating the transition propagation within the crystal). The reaction model of ELM-11 is an autocatalytic reaction with two pathways for CO2 penetration of the framework. Moreover, gas adsorption analyses of two other flexible MOFs with different flexibilities indicate that the kinetics of the adsorption-induced structural transition is highly dependent on framework structure.

Commercial‐scale removal of short‐chain PFAS in a batch‐wise adsorptive bubble separation process by dosing with cationic co‐surfactant

AbstractStudies performed by Burns et al. in 2021 and 2022 demonstrated that a three‐stage batch‐wise adsorptive bubble separation process, surface active foam fractionation (SAFF), is effective at removing most per‐ and polyfluoroalkyl substances (PFASs) from contaminated groundwaters and landfill leachates. However, PFAS species with very low adsorption coefficients to bubble surfaces are difficult to remove, which is parallel to the difficulties in removing short‐chain PFAS in granulated activated carbon beds and other solid media. It is well known that the adsorption coefficient to bubble surfaces improves in the presence of electrolytes in solution and it has previously been shown that this improves the removal of PFAS. By developing a correlation for the removal percentage of one species or another of PFAS due to SAFF in commercial‐scale processes as a function of the adsorption coefficient, it is possible to generally estimate the removal percentage of any PFAS. The addition of a cationic co‐surfactant, cetrimonium bromide, to the feed can significantly further improve the adsorption coefficient and, as a consequence, materially improve the removal of short‐chain PFAS due to SAFF. A method for estimating this improved performance is in qualitative agreement with plant trials of SAFF at a North American site with a history of groundwater contamination due to the use of aqueous film forming foams firefighting foams, but the precise improvements appear to be dependent upon the concentration of the added co‐surfactant. The required concentration of co‐surfactant is significantly larger than might be expected on charge equivalence considerations, and this may be due to its consumption by other species in the feed, including PFAS that have not been accounted for. It is noted that the SAFF process may not be true foam fractionation and may, instead, be a bubble fractionator, both of which can be collectively described by the term “adsorptive bubble separation processes.”

Methylene blue magnetic adsorption separation process from aqueous solution using corn cob

Climate change and growing human, industrial and agricultural activities, in view of the growing population, constitute a threat to water resources due to all pollutant discharges that are not very biodegradable and/or toxic. Drinking water is therefore, becoming the central concern of public opinion and leaders. It therefore appears important to reduce polluting emissions at the level of effluents as much as possible. The adsorption of methylene blue (MB) on the powder of modified and magnetized corn cobs (MCC) was studied. This study aims, not only to recover this polluting waste, but also to bypass heavy separation techniques such as centrifugation, sedimentation and filtration. The prepared biosorbent was characterized by XRD and SEM. Parameters influencing the adsorption process such as contact time, adsorbent dosage, pH and temperature were determined. The kinetic study indicated that the adsorption phenomenon fits the pseudo-second-order model better. The influence of temperature on adsorption allowed the determination of thermodynamic parameters (ΔG°, ΔH° and ΔS°). The MB adsorption process by the magnetic adsorbent obeys the single-layer Langmuir model. A maximum adsorption capacity of MCC equal to 13.23 mg/g was obtained. In view of the results obtained, MCC appears to be a very favorable adsorbent for MB removal from aqueous medium.

Theoretical isotherm equation for adsorption-induced structural transition on flexible metal–organic frameworks

Flexible metal-organic frameworks (MOFs) exhibit an adsorption-induced structural transition known as "gate opening" or "breathing," resulting in an S-shaped adsorption isotherm. This unique feature of flexible MOFs offers significant advantages, such as a large working capacity, high selectivity, and intrinsic thermal management capability, positioning them as crucial candidates for revolutionizing adsorption separation processes. Therefore, the interest in the industrial applications of flexible MOFs is increasing, and the adsorption engineering for flexible MOFs is becoming important. However, despite the establishment of the theoretical background for adsorption-induced structural transitions, no theoretical equation is available to describe S-shaped adsorption isotherms of flexible MOFs. Researchers rely on various empirical equations for process simulations that can lead to unreliable outcomes or may overlook insights into improving material performance owing to parameters without physical meaning. In this study, we derive a theoretical equation based on statistical mechanics that could be a standard for the structural transition type adsorption isotherms, as the Langmuir equation represents type I isotherms. The versatility of the derived equation is shown through four examples of flexible MOFs that exhibit gate opening and breathing. The consistency of the formula with existing theories, including the osmotic free energy analysis and intrinsic thermal management capabilities, is also discussed. The developed theoretical equation may lead to more reliable and insightful outcomes in adsorption separation processes, further advancing the direction of industrial applications of flexible MOFs.

Agricultural Solid Wastes Based Adsorbent Materials in the Remediation of Heavy Metal Ions from Water and Wastewater by Adsorption: A Review.

Adsorption has become the most popular and effective separation technique that is used across the water and wastewater treatment industries. However, the present research direction is focused on the development of various solid waste-based adsorbents as an alternative to costly commercial activated carbon adsorbents, which make the adsorptive separation process more effective, and on popularising the sustainable options for the remediation of pollutants. Therefore, there are a large number of reported results available on the application of raw or treated agricultural biomass-based alternatives as effective adsorbents for aqueous-phase heavy metal ion removal in batch adsorption studies. The goal of this review article was to provide a comprehensive compilation of scattered literature information and an up-to-date overview of the development of the current state of knowledge, based on various batch adsorption research papers that utilised a wide range of raw, modified, and treated agricultural solid waste biomass-based adsorbents for the adsorptive removal of aqueous-phase heavy metal ions. Metal ion pollution and its source, toxicity effects, and treatment technologies, mainly via adsorption, have been reviewed here in detail. Emphasis has been placed on the removal of heavy metal ions using a wide range of agricultural by-product-based adsorbents under various physicochemical process conditions. Information available in the literature on various important influential physicochemical process parameters, such as the metal concentration, agricultural solid waste adsorbent dose, solution pH, and solution temperature, and importantly, the adsorbent characteristics of metal ion removal, have been reviewed and critically analysed here. Finally, from the literature reviewed, future perspectives and conclusions were presented, and a few future research directions have been proposed.

Adsorptive recovery of volatile fatty acids from wastewater fermentation broth

This work developed an adsorptive separation and recovery process for anaerobically generated volatile fatty acids (VFAs) from swine wastewater fermentation. Batch adsorption studies were conducted using several weak anion exchange resins and synthetic adsorbent resins to identify a suitable candidate. Relite RAM2 with a tertiary amine functional group showed the highest adsorption (over 98%) of hexanoic acid. Under the different pH values (1.8–7.5) and extraction temperatures (30–50 °C), the highest adsorption was observed at a pH of 3.2, which is below the pKa of hexanoic acid, at all the evaluated temperatures. A full factorial design was used to optimize the resin and VFA concentrations, wherein over 99% adsorption could be achieved when the ratio of VFA to resin was below 0.23 (g/g) for model solution (VFAs in water). The adsorption equilibrium could be achieved within 30 min of contact time and 0.5% w/v NaOH was identified as a suitable desorption agent. Under the optimal conditions, 65–72% of VFAs present in fermentation broth was adsorbed, which was increased to 72–76% by using fresh resins. The VFAs adsorption and recovery efficiency were maintained for 9 successive cycles without requiring extensive resin washing and regeneration for both model solution and fermentation broth. Overall, the work presents a comprehensive study for resin adsorption to recover VFAs and provides a potential industrial-relevant process to recover VFAs from fermentation broth.

The Self-Disproportionation of Enantiomers (SDE) of α-Pinene via Evaporation off Silica Gel and Foam Fractionation—Validation of the Plausibility of SDE via Gas Chromatography (GC) for α-Pinene

α-Pinene is an intriguing monoterpene as it has been reported to undergo the self-disproportionation of enantiomers (SDE) phenomenon via gas chromatography (GC), the only compound to decisively demonstrate this. Examples of the SDE involving the gaseous phase—sublimation aside—are extremely rare. Attempts to replicate the GC results were unsuccessful, though the authors argued convincingly for the difficulty of observing the phenomenon. However, we could effect for α-pinene SDE via evaporation off silica gel and by foam fractionation—albeit the SDE magnitude for both was only very slight—to confirm that α-pinene can undergo the SDE for processes involving a gaseous phase and thus validate the plausibility of the GC report. The indications are that the molecular associations responsible for the various SDE observations of α-pinene occur not in the gaseous phase or the bulk phase but rather in two-dimensional (2D) adsorbed monolayers and are not based on conventional functional group-based intermolecular interactions and instead are, most likely, as a result of homo- and heterochiral packing differences in the 2D monolayers—a well-known 2D chiral-based association packing effect. These are also the first reports of the occurrence of the SDE using an adsorptive bubble separation process (foam fractionation) and involving a gaseous phase other than sublimation, GC, and distillation.

Effect of isopropanol on CO2 capture by activated carbon: Adsorption performance and regeneration capacity

Globally, fossil fuel combustion from various industrial processes has caused a significant increase in CO2 emissions, exacerbating the greenhouse effect and climate change. Therefore, effective CO2 capture technologies must be urgently developed. Vacuum temperature swing adsorption (VTSA) is an efficient technique for CO2 capture. The presence of water vapor, H2S, etc., is an important factor that affects the performance of CO2 adsorption, and they are usually removed prior to the adsorption separation process. However, volatile organic compounds (VOCs), a common component of industrial flue gas, can also affect the adsorption and capture of CO2, which is often ignored. Thus, in this study, the effect of isopropanol (IPA), one of the most common VOCs used in industry, on the CO2 removal performance is examined using an in-house VTSA device with activated carbon (AC) as the adsorbent. The effect of IPA on the CO2 adsorption performance of AC under varying IPA concentration, IPA content in AC, feed flow rate, and adsorption/desorption temperature is comprehensively investigated. The results verify that the impact of VOCs in the industrial exhaust gases on CO2 capture by adsorption cannot be disregarded.

Separation of Cyclohexanone and Cyclohexanol by Adaptive Pillar[5]arene Cocrystals Accompanied by Vapochromic Behavior.

The separation of cyclohexanone (CHA-one) and cyclohexanol (CHA-ol) mixtures is of great importance in the chemical industry. Current technology exploits multiple steps of energy-intensive rectification due to their close boiling points. Herein, we report a new and energy-efficient adsorptive separation method employing binary adaptive macrocycle cocrystals (MCCs) built with π-electron-rich pillar[5]arene (P5) and an electron-deficient naphthalenediimide derivative (NDI) that can selectively separate CHA-one from an equimolar CHA-one/CHA-ol mixture with >99% purity. Intriguingly, this adsorptive separation process is accompanied by vapochromic behavior from pink to dark brown. Single-crystal and powder X-ray diffraction analyses reveal that the adsorptive selectivity and vapochromic property are derived from the CHA-one vapor inside the cocrystal lattice voids triggering solid-state structural transformations to yield charge-transfer (CT) cocrystals. Moreover, the reversible transformations make the cocrystalline materials highly recyclable.

Mechanism exploration of surface functional groups and pore sizes on CO2 adsorptive separation by GCMC and DFT simulations

The purpose of this study is to analyze the mechanistic effect of surface functional groups and pore sizes of graphene on the CO2 adsorption and separation behaviors by grand canonical Monte Carlo (GCMC) simulation and density functional theory (DFT) calculation. For the surface functional groups, the M−doped (M = N, P, S, O) functionalized graphene materials (G-Rs) exhibit a higher CO2/N2, CO2/H2 and CO2/CH4 adsorption selectivity than pristine graphene (G-None) in the entire pressure range. Especially, due to a stronger electrostatic interaction, the P-doped functionalized graphene materials (P-G-Rs) present the best CO2 separation performance. For the pore size, the influence of pore size on the CO2 adsorptive separation process depends on pressure ranges. At low pressures, 0.8 nm pore shows the highest CO2 adsorption selectivity. However, as for high pressure, the actual pore volume plays the dominant role. Furthermore, by analyzing the isosurface maps of electrostatic potential and van der Waals (vdW) potential, we conclude that the electrostatic effect determines the optimal adsorption sites for polar gas molecules (CO2) rather than non-polar molecules (N2, H2 and CH4), while the vdW interaction plays a secondary role in the intermolecular interaction. This study provides a novel theoretical guidance in designing and preparing modified graphene for CO2/other gas molecules mixture separation.

A Microporous Metal-Organic Framework with Unique Aromatic Pore Surfaces for High Performance C2 H6 /C2 H4 Separation.

Developing adsorptive separation processes based on C2 H6 -selective sorbents to replace energy-intensive cryogenic distillation is a promising alternative for C2 H4 purification from C2 H4 /C2 H6 mixtures, which however remains challenging. During our studies on two isostructural metal-organic frameworks (Ni-MOF 1 and Ni-MOF 2), we found that Ni-MOF 2 exhibited significantly higher performance for C2 H6 /C2 H4 separation than Ni-MOF-1, as clearly established by gas sorption isotherms and breakthrough experiments. Density-Functional Theory (DFT) studies showed that the unblocked unique aromatic pore surfaces within Ni-MOF 2 induce more and stronger C-H⋅⋅⋅π with C2 H6 over C2 H4 while the suitable pore spaces enforce its high C2 H6 uptake capacity, featuring Ni-MOF 2 as one of the best porous materials for this very important gas separation. It generates 12 L kg-1 of polymer-grade C2 H4 product from equimolar C2 H6 /C2 H4 mixtures at ambient conditions.

A Microporous Metal‐Organic Framework with Unique Aromatic Pore Surfaces for High Performance C2H6/C2H4 Separation

AbstractDeveloping adsorptive separation processes based on C2H6‐selective sorbents to replace energy‐intensive cryogenic distillation is a promising alternative for C2H4 purification from C2H4/C2H6 mixtures, which however remains challenging. During our studies on two isostructural metal–organic frameworks (Ni‐MOF 1 and Ni‐MOF 2), we found that Ni‐MOF 2 exhibited significantly higher performance for C2H6/C2H4 separation than Ni‐MOF‐1, as clearly established by gas sorption isotherms and breakthrough experiments. Density‐Functional Theory (DFT) studies showed that the unblocked unique aromatic pore surfaces within Ni‐MOF 2 induce more and stronger C−H⋅⋅⋅π with C2H6 over C2H4 while the suitable pore spaces enforce its high C2H6 uptake capacity, featuring Ni‐MOF 2 as one of the best porous materials for this very important gas separation. It generates 12 L kg−1 of polymer‐grade C2H4 product from equimolar C2H6/C2H4 mixtures at ambient conditions.

Optimal dispatch of HCNG penetrated integrated energy system based on modelling of HCNG process

Hydrogen is injected into the existing natural gas network to form hydrogen-rich compressed natural gas (HCNG), effectively addressing the high cost of hydrogen transmission. However, the traditional IES model cannot be used due to the hydrogen injection's effect on gas properties and the vague characteristics of the transport and separation processes. Therefore, this paper proposes an HCNG penetrated integrated energy system (HPIES) optimal dispatching method by comprehensively modelling the injection, transmission, and separation processes of HCNG. An HCNG mass flow rate model considering variable mixing ratio and unknown beginning flow direction is developed to describe the effect of hydrogen injection. Furthermore, the hydrogen separation model is established by introducing a combined membrane and pressure swing adsorption separation process. The tightening McCormick algorithm is proposed to solve quickly HPIES optimal dispatch problem with an acceptable feasibility check. Finally, case studies on the HPIES consisting of IEEE 39-bus power system and 20-node natural gas system validate the effectiveness of the algorithm and model. The results show that the average error is 0.031% for the bilinear term constraint.

Adsorptive processes for the recovery of VCM emissions using an environmentally friendly MIL-100(Fe) MOF

This work focuses on developing adsorptive separation processes for recovering vinyl chloride emissions from poly(vinyl chloride) production plants. Taking advantage of the mesoporous structure of the MIL-100(Fe) MOF adsorbent, a pressure-swing adsorption separation system was successfully developed for a separation previously dominated by temperature-swing processes. The performance of the PSA unit was compared to an MT-TPSA cycle using the same material and other adsorptive systems found in the literature. The proposed PSA unit can produce an inert gas stream fit for open-air release and a high purity VCM stream capable of being recycled back into the polymerization process. Productivity of 3.52 mol/kgads.h and 71.89 kgVCM/m3unit.h was achieved for an electrical energy consumption of 0.83 MJ/kgVCM.

폐 PET 기반 활성탄의 CO2 및 N2 흡착특성

In this study, waste polyethylene terephthalate (PET) based activated carbon (AC) with different textural properties were prepared by adjusting the KOH mixing ratio. The prepared ACs were characterized by SEM, TEM, XRD, XPS and nitrogen adsorption analysis. From the characterization results, ACs showed a good correlation between the KOH mixing ratio and the surface area, pore volume and pore size, but there was no correlation with the surface chemical composition. In addition, the adsorption equilibrium amount of CO₂ and N₂ was measured under different temperature and pressure conditions using a volumetric adsorption apparatus. The adsorption amount of the target gas showed a good correlation with the ultramicropore volume (V_{<0.9 nm}) rather than the surface area and total pore volume of ACs. The gas adsorption behaviors according to the pore structure were compared and analyzed by adsorption isotherm models, isosteric heat of adsorption, and adsorption energy distribution function (AED). The selectivity for CO₂ calculated using the ideal solution theory (IAST) under flue gas (CO₂ : N₂ = 15 : 85) conditions suggests that the waste PET-based AC can be sufficiently used for the related CO2 adsorptive separation process.

Current progress in treatment technologies for plastic waste (bisphenol A) in aquatic environment: Occurrence, toxicity and remediation mechanisms

Bisphenol-A (BPA) is a type of endocrine disrupting compound (EDC) that is being widely used in the production of polycarbonate and epoxy resins. In the last few years, human exposure to BPA has been extensively high due to the continuous increment in the Annual Growth Rate (AGR) of the BPA global market. The presence and transportation of BPA in the environment could cause serious damage to aquatic life and human health. This paper reviewed the literature on the exposure and toxicity mechanisms of BPA and advanced analytical techniques for the detection of BPA in the environment and human beings. The study indicated that BPA can cause damaging effects on numerous tissues and organs, including the reproductive system, metabolic dysfunction, respiratory system, immune system and central nervous system. On the basis of reported studies on animals, it appears that the exposure of BPA can be carcinogenic and responsible for causing a variety of cancers like ovarian cancer, uterine cancer, prostate cancer, testicular cancer, and liver cancer. This review paper focused mainly on the current progress in BPA removal technologies within last ten years (2012–2022). This paper presents a comprehensive overview of individual removal technologies, including adsorption, photocatalysis/photodegradation, ozonation/advance oxidation, photo-fenton, membranes/nanofilters, and biodegradation, along with removal mechanisms. The extensive literature study shows that each technology has its own removal mechanism and their respective limitations in BPA treatment. In adsorption and membrane separation process, most of BPA has been treated by electrostatic interaction, hydrogen boning and π-π interations mechanism. Whereas in the degradation mechanism, O* and OH* species have played a major role in BPA removal. Some factors could alter the removal potential and efficiency of BPA removal. This review paper will provide a useful guide in providing directions for future investigation to address the problem of BPA-containing wastewater treatment.