Conversion Of Glycol Research Articles

Structural Modification Effect of Se-doped Porous Carbon for Hydrogen Evolution Coupled Selective Electrooxidation of Ethylene Glycol to Value-added Glycolic Acid.

The ethylene glycol oxidation reaction (EGOR) has attracted attention because ethylene glycol (EG), which exhibits large-scale production and a low market price, can be reformed into valuable glycolic acid (GCA) with the cogeneration of high-purity hydrogen gas during the reaction. In this study, a noble catalyst material of Pt nanoparticles supported on Se-doped porous carbon (Pt/SePC) is prepared and investigated for the selective electrochemical oxidation of EG to GCA. Pt/SePC achieved a maximum EG conversion of 94.6% and GCA selectivity of 84.4% and maintained this high performance with negligible degradation during durability tests. Furthermore, the EGOR required lower overpotential rather than the oxygen evolution reaction, thus the EGOR coupled with the hydrogen evolution reaction can reduce the cell overpotential to 0.60 V, which is much lower than that of water electrolysis (1.58 V). The effect of Se doping is investigated through experimental analyses and density functional theory (DFT) calculations, and they shows that Se modified the binding energy of Pt nanoparticles and the adsorption energy of reactants by lattice deformation and charge density modification. This study provides scientific insights and strategies for electrocatalyst design for the selective oxidation of polyols to value-added chemicals via the cogeneration of hydrogen gas.

Exploring yeast biodiversity and process conditions for optimizing ethylene glycol conversion into glycolic acid.

Plastics have become an indispensable material in many fields of human activities, with production increasing every year; however, most of the plastic waste is still incinerated or landfilled, and only 10% of the new plastic is recycled even once. Among all plastics, polyethylene terephthalate (PET) is the most produced polyester worldwide; ethylene glycol (EG) is one of the two monomers released by the biorecycling of PET. While most research focuses on bacterial EG metabolism, this work reports the ability of Saccharomyces cerevisiae and nine other common laboratory yeast species not only to consume EG, but also to produce glycolic acid (GA) as the main by-product. A two-step bioconversion of EG to GA by S. cerevisiae was optimized by a design of experiment approach, obtaining 4.51±0.12g l-1 of GA with a conversion of 94.25±1.74% from 6.21±0.04g l-1 EG. To improve the titer, screening of yeast biodiversity identified Scheffersomyces stipitis as the best GA producer, obtaining 23.79±1.19g l-1 of GA (yield 76.68%) in bioreactor fermentation, with a single-step bioprocess. Our findings contribute in laying the ground for EG upcycling strategies with yeasts.

Synthesis of spinel Nickel Ferrite (NiFe2O4)/CNT electrocatalyst for ethylene glycol oxidation in alkaline medium

Nickel-iron-based spinel oxide was prepared and supported on multi-walled carbon nanotubes to enhance the electrochemical oxidation of ethylene glycol in an alkaline medium. NiFe2O4 was prepared using facile sol-gel techniques. Then the prepared material was characterized using different bulk and surface techniques like powder X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), scanning electron microscope (SEM), and transmitted electron microscope (TEM). Different electrodes of NiFe2O4/CNT ratios were prepared to find out the optimum spinel oxide/CNT ratio. The activity of the metal spinel oxides composite was characterized toward ethylene glycol conversion by different electrochemical techniques like cyclic voltammetry (CV), Chronoamperometry (CA), and electrochemical impedance spectroscopy (EIS). The modified electrode reached an oxidation current of 43 mA cm−2 in a solution of 1.0 M ethylene glycol and 1.0 M NaOH. Furthermore, some kinetics parameters (like diffusion coefficient, and rate constant) were calculated to evaluate the catalytic performance. Additionally, the electrode showed extreme stability for long-term ethylene glycol oxidation.

Green Catalytic Synthesis of Ethylenediamine from Ethylene Glycol and Monoethanolamine: A Review.

Ethylenediamine (EDA) is a crucial chemical raw material and fine chemical intermediate. Compared with the industrial approach of ammonolysis of 1,2-dichloroethane, the catalytic amination of ethylene glycol (EG) is an economical and environmentally benign route that will be the future trend for EDA synthesis. Herein, we systemically review the recent progress in direct and indirect catalytic conversion of EG to EDA. Furthermore, different types of catalysts are discussed: (i) supported metal and multimetallic catalysts, (ii) solid acid catalysts, and (iii) other active catalysts (e.g., ionic liquids and metal complexes). Finally, we conclude with the frontiers and future prospects of the catalytic synthesis of EDA from EG and monoethanolamine, providing readers a snapshot of this field.

Aqueous Phase Reforming over Platinum Catalysts on Doped Carbon Supports: Exploring Platinum-Heteroatom Interactions.

A series of platinum catalysts supported on carbon nanofibers with various heteroatom dopings were synthesized to investigate the effect of the local platinum environment on the catalytic activity and selectivity in aqueous phase reforming (APR) of ethylene glycol (EG). Typical carbon dopants such as oxygen, nitrogen, sulfur, phosphorus, and boron were chosen based on their ability to bring acidic or basic functional groups to the carbon surface. In situ X-ray absorption spectroscopy (XAS) was used to identify the platinum oxidation state and platinum species formed during APR of EG through multivariate curve resolution alternating least-squares analysis, observing differences in activity, selectivity, and platinum local environment among the catalysts. The platinum-based catalyst on the nitrogen-doped carbon support demonstrated the most favorable properties for H2 production due to high Pt dispersion and basicity (H2 site time yield 22.7 h-1). Direct Pt-N-O coordination was identified by XAS in this catalyst. The sulfur-doped catalyst presented Pt-S contributions with the lowest EG conversion rate and minimal production of the gas phase components. Boron and phosphorus-doped catalysts showed moderate activity, which was affected by low platinum dispersion on the carbon support. The phosphorus-doped catalyst showed preferential selectivity to alcohols in the liquid phase, associated with the presence of acid sites and Pt-P contributions observed under APR conditions.

High-performance spinel NiMn2O4 supported carbon felt for effective electrochemical conversion of ethylene glycol and hydrogen evolution applications

One of the most effective electrocatalysts for electrochemical oxidation reactions is NiMn2O4 spinel oxide. Here, a 3-D porous substrate with good conductivity called carbon felt (CF) is utilized. The composite of NiMn2O4-supported carbon felt was prepared using the facile hydrothermal method. The prepared electrode was characterized by various surface and bulk analyses like powder X-ray diffraction, X-ray photon spectroscopy (XPS), Scanning and transmitted electron microscopy, thermal analysis (DTA), energy dispersive X-ray (EDX), and Brunauer–Emmett–Teller (BET). The activity of NiMn2O4 toward the electrochemical conversion of ethylene glycol at a wide range of concentrations was investigated. The electrode showed a current density of 24 mA cm−2 at a potential of 0.5 V (vs. Ag/AgCl). Furthermore, the ability of the electrode toward hydrogen evaluation in an alkaline medium was performed. Thus, the electrode achieved a current density equal 10 mA cm−2 at an overpotential of 210 mV (vs. RHE), and the provided Tafel slope was 98 mV dec−1.

Lattice Strain and Charge Redistribution of Pt Cluster/Ir Metallene Heterostructure for Ethylene Glycol to Glycolic Acid Conversion Coupled with Hydrogen Production.

Upgrading overall water splitting (OWS) system and developing high-performance electrocatalysts is an attractive way to the improve efficiency and reduce the consumption of hydrogen (H2 ) production from electrolyzed water. Here, a Pt cluster/Ir metallene heterojunction structure (Pt/Ir hetero-metallene) with a unique Pt/Ir interface is reported for the conversion of ethylene glycol (EG) to glycolic acid (GA) coupled with H2 production. With the assistance of ethylene glycol oxidation (EGOR), the Pt/Ir||Pt/Ir hetero-metallene two-electrode water electrolysis system exhibits a lower cell voltage of 0.36V at 10mA cm-2 . Furthermore, the Faradaic efficiency of EG to GA is as high as 87%. The excellent performance of this new heterostructure arise from the charge redistribution and strain effects induced by Pt-Ir interactions between the heterogeneous interfaces, as well as the larger specific surface area and more active sites due to the metallene structure.

Se-Doped Porous Carbon Supported Pt to Boost Selective Oxidation of Ethylene Glycol to Glycolic Acid

Biomass-derived polyols can be reformed to value-added chemicals by electrochemical selective oxidation process. Ethylene glycol (EG) and glycerol (GLY) are produced in a large surplus, hence rational design of electrocatalysts for efficient selective oxidation of these biomass-derived molecules should be required to utilize the EG and GLY. Various organic acids such as glycolic acid (GCA), oxalic acid (OXA) and formic acid (FA) can be produced in the oxidation pathway of EG.[1] In particular, EG selective oxidation targeted at the production of GCA, which has broad applications in skin care, textile industry and adhesives. Herein, we fabricated heteroatom doped porous carbons as support materials of highly dispersed Pt nanoparticles and applied to selective oxidation of EG to GCA. By introducing Se in carbon materials, the highly selective production of GCA was achieved with significant conversion of EG over 90%. The porous structure of carbon support led to well dispersed Pt nanoparticle and this morphology was observed by SEM and TEM. XPS and Raman analyses revealed that doped Se atoms changed electronic properties of carbon materials and induced defects into the carbon lattice structure. These properties greatly enhanced the electrocatalytic activity and stability of Pt/SePC, resulting that GCA yield reached to and remained around 85% during several repeated tests for the EG selective oxidation. Our study could highlight favorable strategy of catalyst design with heteroatom doping for ethylene glycol conversion to glycolic acid.[1] D. Jang, H. Han, J. Maeng, W. Yoon, M. Park and W. B. Kim, Highly active PdSb catalysts on porous carbon for electrochemical oxidation reactions of biomass-derived C1–C3 alcohols, Mater. Adv., 2022, 3, 5964-5973.

Catalytic upgrading of PET to acid by engineering bimetallic AuCu/CNT catalyst

AbstractBACKGROUNDRecycling waste polyethylene terephthalate (PET) plastic can prolong its life cycle, reduce the consumption of non‐renewable resources, prevent plastic pollution and also protect the ecological environment. Traditional chemical recycling of waste PET plastic can depolymerize PET into terephthalic acid (TPA) and ethylene glycol (EG).RESULTSA strategy was proposed to directly depolymerize PET into TPA and acid, which shows significantly higher values than conventional EG. This is achieved over a carbon nanotube (CNT)‐supported AuCu catalyst (AuCu/CNT) prepared using an evaporative impregnation method. Comprehensive analyses of the catalyst were conducted using X‐ray diffraction, N2 adsorption/desorption, transmission electron microscopy, X‐ray photoelectron spectroscopy, H2‐temperature=programmed reduction, and so on. It was found that Cu species in the AuCu/CNT catalyst mainly existed in the form of CuO, forming new reaction adsorption sites and providing active AuCu alloy sites, thereby improving the catalytic performance of AuCu/CNT. This results in simultaneously superior acid selectivity and EG conversion over AuCu/CNT compared with Au/CNT and Cu/CNT.CONCLUSIONThis study indicates that the hydrolysis of PET is highly significant in preparing value‐added products. © 2023 Society of Chemical Industry.

Carbon-based solid acids catalyze the synthesis of ethylene glycol monoacetate from ethylene glycol and acetic acid

Activation is essential for improving the structure and surface functional groups of carbon-based solid acids (CSA) during the preparation of carbon materials. This paper compared the catalytic activity of CSA treated non-, KOH-, H3PO4-, and ZnCl2-activation in esterification of ethylene glycol (EG) and acetic acid (HAc) to synthesize ethylene glycol monoacetate (EGMA). The catalysts were characterized using N2 isothermal adsorption–desorption, acid-base titration, Fourier transform infrared (FT-IR) spectroscopy, scanning electron microscopy (SEM), Raman spectrometer, X-ray photoelectron spectroscopy (XPS), and X-ray diffractometer analysis (XRD). The results showed that activation treatment clearly enhanced the CSA’s specific surface area and significantly influenced the distribution of surface functional groups. Notably, the CSA activated with H3PO4 had a markedly higher density of –SO3H groups than the non- activated, KOH- activated, and ZnCl2-activated CSA. The high density of –SO3H on the catalyst surface is advantageous for the synthesis of EGMA from EG and HAc, making the H3PO4-activated CSA the best performer. The reaction conditions were optimized on H3PO4-activated CSA, resulting in a 74.1% conversion of EG and an 81.8% selectivity of EGMA at 100 °C for 30 min, and the EG/HAc molar ratio of 1:2. H3PO4-activated CSA was not obviously deactivated even after five cycles, and the decrease of its catalytic performance was related to the leaching of –SO3H on the catalyst surface. Overall, these findings suggest that H3PO4-activated CSA offers the benefits of less cost, a simpler preparation method, and greater catalytic activity compared to other catalysts, making it a desirable option for the synthesis of EGMA.

Nickel–cobalt oxides decorated Chitosan electrocatalyst for ethylene glycol oxidation

A composite of NiCo2O4 modified electrocatalyst is prepared to enhance the ethylene glycol electrooxidation. Chitosan matrix is used to improve the activity and adsorption ability of the surface to enhance ethylene glycol conversion. A Comparative study is investigated between pristine NiCo2O4 and Chitosan-modified spinel oxide to evaluate the synergistic effect between spinel oxide and chitosan. The composite is studied in an alkaline solution using electrochemistry techniques. The electrochemical activity towards ethylene glycol electrooxidation is studied as a function of anodic oxidation current density. Thus, the oxidation current values for NiCo2O4 and NiCo2O4@Chitosan in 1.0 M EG and 1.0 M KOH are 36 and 42 mA cm−2, respectively. The long-term stability of the electrode is measured by constant potential chronoamperometry. Kinetic parameters like diffusion coefficient, Tafel slope, surface coverage, and transfer coefficient are calculated. The density-functional theory estimates the adsorption of small molecules like ethylene glycol, urea, and carbon monoxide. The adsorption energy is studied on the top site of Ni and Co atoms of NiCo2O4. Forcite model is used to study the interaction between spinel oxide and chitosan. The energy calculation assumes that chitosan is adsorbed on the spinel oxide surface and enhances chitosan's ability for the adsorption of small molecules.

Simple, fast and inexpensive quantification of glycolate in the urine of patients with primary hyperoxaluria type 1

In primary hyperoxaluria type 1 excessive endogenous production of oxalate and glycolate leads to increased urinary excretion of these metabolites. Although genetic testing is the most definitive and preferred diagnostic method, quantification of these metabolites is important for the diagnosis and evaluation of potential therapeutic interventions. Current metabolite quantification methods use laborious, technically highly complex and expensive liquid, gas or ion chromatography tandem mass spectrometry, which are available only in selected laboratories worldwide. Incubation of ortho-aminobenzaldehyde (oABA) with glyoxylate generated from glycolate using recombinant mouse glycolate oxidase (GO) and glycine leads to the formation of a stable dihydroquinazoline double aromatic ring chromophore with specific peak absorption at 440 nm. The urinary limit of detection and estimated limit of quantification derived from eight standard curves were 14.3 and 28.7 µmol glycolate per mmol creatinine, respectively. High concentrations of oxalate, lactate and L-glycerate do not interfere in this assay format. The correlation coefficient between the absorption and an ion chromatography tandem mass spectrometry method is 93% with a p value < 0.00001. The Bland–Altmann plot indicates acceptable agreement between the two methods. The glycolate quantification method using conversion of glycolate via recombinant mouse GO and fusion of oABA and glycine with glyoxylate is fast, simple, robust and inexpensive. Furthermore this method might be readily implemented into routine clinical diagnostic laboratories for glycolate measurements in primary hyperoxaluria type 1.

In vivo implementation of a synthetic metabolic pathway for the carbon-conserving conversion of glycolaldehyde to acetyl-CoA.

Ethylene glycol (EG) derived from plastic waste or CO2 can serve as a substrate for microbial production of value-added chemicals. Assimilation of EG proceeds though the characteristic intermediate glycolaldehyde (GA). However, natural metabolic pathways for GA assimilation have low carbon efficiency when producing the metabolic precursor acetyl-CoA. In alternative, the reaction sequence catalyzed by EG dehydrogenase, d-arabinose 5-phosphate aldolase, d-arabinose 5-phosphate isomerase, d-ribulose 5-phosphate 3-epimerase (Rpe), d-xylulose 5-phosphate phosphoketolase, and phosphate acetyltransferase may enable the conversion of EG into acetyl-CoA without carbon loss. We investigated the metabolic requirements for in vivo function of this pathway in Escherichia coli by (over)expressing constituting enzymes in different combinations. Using 13C-tracer experiments, we first examined the conversion of EG to acetate via the synthetic reaction sequence and showed that, in addition to heterologous phosphoketolase, overexpression of all native enzymes except Rpe was required for the pathway to function. Since acetyl-CoA could not be reliably quantified by our LC/MS-method, the distribution of isotopologues in mevalonate, a stable metabolite that is exclusively derived from this intermediate, was used to probe the contribution of the synthetic pathway to biosynthesis of acetyl-CoA. We detected strong incorporation of 13C carbon derived from labeled GA in all intermediates of the synthetic pathway. In presence of unlabeled co-substrate glycerol, 12.4% of the mevalonate (and therefore acetyl-CoA) was derived from GA. The contribution of the synthetic pathway to acetyl-CoA production was further increased to 16.1% by the additional expression of the native phosphate acyltransferase enzyme. Finally, we demonstrated that conversion of EG to mevalonate was feasible albeit at currently extremely small yields.

Vapor-phase oxidation of propylene glycol-methanol mixture to methyl lactate on CeO2/Al2O3 catalyst

The vapor-phase oxidation of mixtures of propylene glycol with methanol and ethanol to methyl and ethyl lactate, respectively, on supported CeO2/Al2O3 catalyst at 210-2500С was investigated. Air oxygen and a flow reactor with a fixed catalyst bed were used. A 20% solution of propylene glycol in alcohol was supplied to the reactor inlet. Oxidation of propylene glycol in the presence of methanol occurs according to the overall reaction CH3CHOHCH2OH +O2 + СН3OH = CH3CHOHCOOСН3 +2H2O. First, hydroxyacetone is formed, which is further oxidized to pyruvic aldehyde, which adds alcohol to form a hemiacetal. Next, this hemiacetal is rearranged according to Cannizzaro into methyl lactate. At 2200C and catalyst load &lt; 2 mmol PG/gcat/h, the selectivity for methyl lactate reached 70 wt.% at 100% propylene glycol conversion. In the presence of ethanol, the formation of a significant amount of acetaldehyde and its aldol condensation products, as well as the formation of diethoxyethane, was observed. Therefore, the selectivity for ethyl lactate at 100% propylene glycol conversion did not exceed 45%.

Study of the Glycerol Hydrogenolysis Reaction on Cu, Cu-Zn, and Cu-ZnO Clusters.

Quantum chemistry calculations have been performed to access the efficacy of Cu-based catalysts in various mechanistic steps of the glycerol hydrogenolysis reaction. Calculations are first performed for reactants in the gas phase (noncatalyzed system) and reactants in the gas phase with a 3-atom Cu cluster (catalyzed system). We demonstrate that the glycerol to ethylene glycol conversion is preferred in the noncatalyzed system but glycerol conversion to 1,2-propanediol via the 2-acetol intermediate is preferred in the catalyzed system. We next analyze the adsorption energies of the reactant and product species involved in the glycerol to 1,2-PDO reaction on an 8-atom Cu cluster and Cu cluster doped with a Zn atom or a ZnO molecule. Finally, we study the effects of Zn or ZnO doping on the activation barriers of the two steps of the glycerol to 1,2-PDO reaction.

Engineering E. coli for the carbon‐conserving conversion of ethylene glycol to acetyl‐CoA and derived products

Engineering <i>E. coli</i> for the carbon‐conserving conversion of ethylene glycol to acetyl‐CoA and derived products

Amination of Ethylene Glycol to Ethylenediamine Catalyzed by Co‐Cu/γ‐Al2O3

AbstractEthylenediamine is an important organic chemical and commercially produced from non‐renewable starting material. In the present work, amination of ethylene glycol to ethylenediamine was studied using an aqueous ammonia as ammonia source. A series of supported bimetallic catalysts were prepared by impregnation method and characterized by means of H2‐TPR, H2‐TPD, XRD, XPS and N2 adsorption‐desorption. Their catalytic performance for amination of ethylene glycol was investigated and Co−Cu/γ‐Al2O3 catalyst exhibited high activity and good selectivity to ethylenediamine. There exists obvious interaction and synergistic effect between Cu and Co in Co−Cu/γ‐Al2O3 for lowering catalyst reduction temperature and improving catalytic performance separately. The selectivity of ethylenediamine and ethanolamine respectively attained 45.7 % and 23.7 % at an ethylene glycol conversion of 41.5 % under the suitable reaction conditions. On this basis, a majority of by‐products in the amination of ethylene glycol were identified by gas chromatography‐mass spectrometry analysis and a reaction network was proposed.

Selective extraction of lithium from spent LiNixCoyMnzO2 cathode via in-situ conversion of ethylene glycol in subcritical water system

The resources scarcity and explosive growing demand of lithium have made the selective extraction of lithium from spent lithium-ion batteries (LIBs) more and more widely concerned. Yet the current lithium recovery routes still suffer the problems of complex process, low efficiency and unfriendly environment. In this study, a strategy of selective lithium extraction from spent LiNixCoyMnzO2 cathode with ethylene glycol (EG) in subcritical water system is proposed. The in-situ conversion pathway and lithium extraction mechanism in this new system are investigated in detail. Benefit from the reducibility of EG and the dynamic strengthening of the subcritical water system, more than 99% of lithium can be selectively extracted into the solution under the optimal conditions. The leaching kinetics show that the selective leaching process is controlled by chemical reactions and the leaching mechanism suggests that EG plays a dual role of reducing and donating protons in subcritical environment. Furthermore, the lithium-containing leachate can be applid to prepare Li2CO3 products with high purity, and the transition metals (Ni, Co, Mn) in the lithium extraction residue are recovered by acid leaching without adding reducing agent. This process puts forward a innovative idea for preferentially extracting lithium from spent LIBs and even lithium-containing wastes, which has the significant advantages of high efficiency, environmental protection and simplicity.

Production of ethylene glycol monobutyl ether through etherification of ethylene glycol using a nanostructured heterogeneous catalyst of amyberlyst-15

This work aims to produce butyl glycol from the etherification of ethylene glycol (EG) and n-butanol (NB) using different heterogenous Amyberlyst-15 catalysts in a pressurized reactor tank. Experiments were designed by response surface methodology according to the central composite design (RSM-CCD). Three operating conditions of temperature (140–200 °C), reaction time (2–22 h), and EG: NB molar ratio (1:1–1:9) were considered to model and optimize the EG conversion under fixed pressure and catalyst weight. A quadratic conversion model was proposed as a function of independent and combined studied parameters, predicting the experimental data with high accuracy (R2 > 0.98). According to the response surface results, all variables positively affected the response. The optimal reaction condition for maximizing conversion was at 1:8.2, 4.1 h, and 200 °C, achieving the EG conversion of 86.12 %. Furthermore, the catalyst reusability was checked after four cycles, indicating a reduction of about 15 % in conversion after each cycle. The FESEM, FTIR, XRD, BET, and TGA analyses characterized the fresh catalyst and used catalyst after the fourth cycle. Both samples had a spherical morphology, and the used catalyst contained carbon-based sediments, intensifying the stretching vibration of C-O bond peaks. The pore diameter and volume of the fresh catalyst were 18.93 nm and 2.38 cm3/g, respectively, while these values were 22.07 nm and 0.36 cm3/g for the used catalysts after the fourth cycle. The reduction in the catalytic activity of the used sample can be because of the pore deformation.

Improving Treatment Options for Primary Hyperoxaluria.

The primary hyperoxalurias are three rare inborn errors of the glyoxylate metabolism in the liver, which lead to massively increased endogenous oxalate production, thus elevating urinary oxalate excretion and, based on that, recurrent urolithiasis and/or progressive nephrocalcinosis. Frequently, especially in type 1 primary hyperoxaluria, early end-stage renal failure occurs. Treatment possibilities are scare, namely, hyperhydration and alkaline citrate medication. In type 1 primary hyperoxaluria, vitamin B6, though, is helpful in patients with specific missense or mistargeting mutations. In those vitamin B6 responsive, urinary oxalate excretion and concomitantly urinary glycolate is significantly decreased, or even normalized. In patients non-responsive to vitamin B6, RNA interference medication is now available. Lumasiran® is already available on prescription and targets the messenger RNA of glycolate oxidase, thus blocking the conversion of glycolate into glyoxylate, hence decreasing oxalate, but increasing glycolate production. Nedosiran blocks liver-specific lactate dehydrogenase A and thus the final step of oxalate production. Similar to vitamin B6 treatment, where both RNA interference urinary oxalate excretion can be (near) normalized and plasma oxalate decreases, however, urinary and plasma glycolate increases with lumasiran treatment. Future treatment possibilities are on the horizon, for example, substrate reduction therapy with small molecules or gene editing, induced pluripotent stem cell-derived autologous hepatocyte-like cell transplantation, or gene therapy with newly developed vector technologies. This review provides an overview of current and especially new and future treatment options.Supplementary InformationThe online version contains supplementary material available at 10.1007/s40265-022-01735-x.