Deuteriodifluoromethylation and gem-Difluoroalkenylation of Aldehydes Using ClCF2H in Continuous Flow

The deuteriodifluoromethyl group (CF₂D) represents a challenging functional group due to difficult deuterium incorporation and unavailability of precursor reagents. Herein, we report the use of chlorodifluoromethane (ClCF₂H) gas in the continuous flow deuteriodifluoromethylation and gem-difluoroalkenylation of aldehydes. Mechanistic studies revealed that the difluorinated oxaphosphetane (OPA) intermediate can proceed via alkaline hydrolysis in the presence of D₂O to provide α-deuteriodifluoromethylated benzyl alcohols or undergo a retro [2+2] cycloaddition under thermal conditions to provide the gem-difluoroalkenylated product.     

Borocyclopropanation of Styrenes Mediated by UV‐light Under Continuous Flow Conditions

Herein, we report a user‐friendly and metal‐free UV‐A light mediated borocyclopropanation of styrenes using continuous flow technology. A broad range of styrene derivatives can be cyclopropanated in good yields within 1 h residence time to produce highly valuable cyclopropylboronate esters with modest to good diastereoselectivities. The reaction is also applicable to α‐substituted styrenes. Mechanistic studies support a photoredox process during which xanthone, a well‐known organic photosensitizer, can easily reach a photoexcited state that is available for both an oxidative and a reductive quenching.     

Safe and Facile Access to Nonstabilized Diazoalkanes Using Continuous Flow Technology

Despite the high synthetic potential of nonstabilized diazo compounds, their utilization has always been hampered by stability, toxicity, and safety issues. The present method opens up access to the most reactive nonstabilized diazoalkanes. Among diazo compounds, nonstabilized alkyl diazo compounds are the least represented because of their propensity to degrade during preparation. The continuous flow oxidation process of hydrazones on a silver oxide column afforded an output stream of base‐ and metal‐free pure diazo solution in dichloromethane. Starting from innocuous ketones and aldehydes, this methodology allows the production of a broad range of unprecedented diazoalkanes compounds in excellent yields, while highlighting their synthetic potential and the possibility of safe large‐scale diazo production.     

Photochemical Synthesis of Complex Carbazoles: Evaluation of Electronic Effects in Both UV‐ and Visible‐Light Methods in Continuous Flow

An evaluation of both a visible‐light‐ and UV‐light‐mediated synthesis of carbazoles from various triarylamines with differing electronic properties under continuous‐flow conditions has been conducted. In general, triarylamines bearing electron‐rich groups tend to produce higher yields than triarylamines possessing electron‐withdrawing groups. The incorporation of nitrogen‐based heterocycles, as well as halogen‐containing arenes in carbazole skeletons, was well tolerated, and often synthetically useful complementarity was observed between the UV‐light and visible‐light (photoredox) methods.     

An Immobilized‐Dirhodium Hollow‐Fiber Flow Reactor for Scalable and Sustainable C−H Functionalization in Continuous Flow

A scalable flow reactor is demonstrated for enantioselective and regioselective rhodium carbene reactions (cyclopropanation and C?H functionalization) by developing cascade reaction methods employing a microfluidic flow reactor system containing immobilized dirhodium catalysts in conjunction with the flow synthesis of diazo compounds. This allows the utilization of the energetic diazo compounds in a safe manner and the recycling of the dirhodium catalysts multiple times. This approach is amenable to application in a bulk‐scale synthesis employing asymmetric C?H functionalization by stacking multiple fibers in one reactor module. The products from this sequential flow–flow reactor are compared with a conventional batch reactor or flow–batch reactor in terms of yield, regioselectivity, and enantioselectivity.     

连续流离子聚合

微流场技术因其良好的传质传热性能应用于各种机理的聚合反应中,引起了学术界和工业界的广泛关注。本文聚焦于高度放热的离子聚合,总结了近年来不同单体连续流阴/阳离子聚合的研究进展。微反应器在改善离子聚合苛刻的反应条件、精确地控制聚合产物分子量及其分布、调控共聚物结构等方面显示出釜式反应器无法比拟的优势。此外,本文对连续流离子聚合的工业化应用前景进行了探讨和展望。     

Total Synthesis of Glipizide and Glibenclamide in Continuous Flow

Glipizide and glibenclamide remain some of the widely prescribed antidiabetic sulfonylurea drugs for the treatment of type 2 diabetes mellitus. Herein the authors report on an isocyanate-free synthetic procedure towards the preparation of these on demand drugs at multigram scale using continuous flow technology. The safety concern over the use of isocyanates in most of the existing synthetic routes was dealt with in this present work by using N-carbamates synthesised in situ from activation of amines with chloroformates as safer alternatives. An overall yield of 80–85 % was obtained for the semi-telescoped steps within 10 min total residence time.     

沸石的连续流动相合成

由于沸石分子筛在多个领域被广泛应用,高效可靠的沸石合成方法早已成为人们研究的重点。相较于传统高压釜水热间歇合成方法,沸石的连续流动相合成方法晶化时间短,时空产率高,是近年来发展的沸石合成新路线。利用连续流动反应器(CFR)的热延迟效应低、传质效果好和方法拓展性强等特点,可以在分钟级乃至秒级时间内实现高结晶度沸石合成,大大提升了合成效率和可控度。基于近期该领域的进展,本文介绍了沸石的连续流动反应器结构,其合成过程优势和产物特点及受限之处,并对其未来应用加以展望。     

连续流动分析法测定水中的阴离子表面活性剂

在GB/T 7494–1987法的基础上将自动进样、在线萃取、在线分离技术与分光光度法相结合,测定水中阴离子表面活性剂的含量。在分析过程中利用二次萃取和分离有效除去干扰物质,提高了分析的准确度和灵敏度。标准工作曲线线性相关系数为0.999 2,检出限为0.007 mg/L,测定结果的相对标准偏差为2.0%~2.4%(n=6),加标回收率为95.0%~98.0%。连续流动注射分析法操作简单,基线稳定速度快,连续分析效果好,大大降低了氯仿对人体的危害,适合大批量水质中阴离子表面活性剂含量的分析。     

Conjugated Polymers Via Direct Arylation Polymerization in Continuous Flow: Minimizing the Cost and Batch‐to‐Batch Variations for High‐Throughput Energy Conversion

Continuous flow methods are utilized in conjunction with direct arylation polymerization (DArP) for the scaled synthesis of the roll‐to‐roll compatible polymer, poly[(2,5‐bis(2‐hexyldecyloxy)phenylene)‐alt‐(4,7‐di(thiophen‐2‐yl)‐benzo[c][1,2,5]thiadiazole)] (PPDTBT). PPDTBT is based on simple, inexpensive, and scalable monomers using thienyl‐flanked benzothiadiazole as the acceptor, which is the first β‐unprotected substrate to be used in continuous flow via DArP, enabling critical evaluation of the suitability of this emerging synthetic method for minimizing defects and for the scaled synthesis of high‐performance materials. To demonstrate the usefulness of the method, DArP‐prepared PPDTBT via continuous flow synthesis is employed for the preparation of indium tin oxide (ITO)‐free and flexible roll‐coated solar cells to achieve a power conversion efficiency of 3.5% for 1 cm² devices, which is comparable to the performance of PPDTBT polymerized through Stille cross coupling. These efforts demonstrate the distinct advantages of the continuous flow protocol with DArP avoiding use of toxic tin chemicals, reducing the associated costs of polymer upscaling, and minimizing batch‐to‐batch variations for high‐quality material.     

Recent Advances in the Synthesis of SCF2H‐ and SCF2FG‐Containing Molecules

In recent years, much interest has been paid to difluoromethylthiolated molecules as the “SCF₂” moiety is a key motif in drug and agrochemical research. Consequently, the development of versatile strategies for the selective synthesis of SCF₂H‐ and SCF₂FG‐containing molecules (FG=functional group) has attracted a lot of attention and inspired the scientific community to design new tools. This Minireview highlights the major progress made in this field. Particularly, methodologies developed for the difluoromethylation of sulfur‐containing molecules and the direct construction of C?SCF₂ bonds in various classes of compounds are showcased and discussed.     

Preparation of Forced Gradient Copolymers Using Tube‐in‐Tube Continuous Flow Reactors

The preparation of forced gradient polymers has received considerable attention using batch reactors, while the preparation of usable quantities of forced gradient copolymers using continuous flow reactors has been hampered by the need to vary the composition of the monomer feedstock continuously during the reaction. A reactor that allows for addition of a monomer feedstock continuously at all points along the length of the reactor tubing allows for the preparation of forced gradient copolymers in continuous flow reactors, allowing for the scale‐up and bulk preparation of these polymers. This study reports here the initial investigation of preparing forced gradient copolymers using the reversible addition–fragmentation chain transfer methodology in tube‐in‐tube continuous flow reactors.

     

Continuous Flow Photochemistry

Due to the narrow width of tubing/reactors used, photochemistry performed in micro‐ and mesoflow systems is significantly more efficient than when performed in batch due to the Beer‐Lambert Law. Owing to the constant removal of product and facility of flow chemical scalability, the degree of degradation observed is generally decreased and the productivity of photochemical processes is increased. In this Personal Account, we describe a wide range of photochemical transformations we have examined using both visible and UV light, covering cyclizations, intermolecular couplings, radical polymerizations, as well as singlet oxygen oxygenations.     

Development of a Continuous‐Flow System for Asymmetric Hydrogenation Using Self‐Supported Chiral Catalysts

Well‐designed, self‐assembled, metal–organic frameworks were constructed by simple mixing of multitopic MonoPhos‐based ligands ( 3 ; MonoPhos=chiral, monodentate phosphoramidites based on the 1,1′‐bi‐2‐naphthol platform) and [Rh(cod)₂]BF₄ (cod=cycloocta‐1,5‐diene). This self‐supporting strategy allowed for simple and efficient catalyst immobilization without the use of extra added support, giving well‐characterized, insoluble (in toluene) polymeric materials ( 4 ). The resulting self‐supported catalysts ( 4 ) showed outstanding catalytic performance for the asymmetric hydrogenation of a number of α‐dehydroamino acids ( 5 ) and 2‐aryl enamides ( 7 ) with enantiomeric excess (ee) ranges of 94–98 % and 90–98 %, respectively. The linker moiety in 4 influenced the reactivity significantly, albeit with slight impact on the enantioselectivity. Acquisition of reaction profiles under steady‐state conditions showed 4 h and 4 i to have the highest reactivity (turnover frequency (TOF)=95 and 97 h^?1 at 2 atm, respectively), whereas appropriate substrate/catalyst matching was needed for optimum chiral induction. The former was recycled 10 times without loss in ee (95–96 %), although a drop in TOF of approximately 20 % per cycle was observed. The estimation of effective catalytic sites in self‐supported catalyst 4 e was also carried out by isolation and hydrogenation of catalyst–substrate complex, showing about 37 % of the Rh^I centers in the self‐supported catalyst 4 e are accessible to substrate 5 c in the catalysis. A continuous flow reaction system using an activated C/ 4 h mixture as stationary‐phase catalyst for the asymmetric hydrogenation of 5 b was developed and run continuously for a total of 144 h with >99 % conversion and 96–97 % enantioselectivity. The total Rh leaching in the product solution is 1.7 % of that in original catalyst 4 h .     

Automated Generation and Reactions of 3‐Hydroxymethylindoles in Continuous‐Flow Microreactors

An automated sequential approach for the generation and reactions of 3‐hydroxymethylindoles in continuous‐flow microreactors is described. Consecutive halogen–magnesium exchanges of four 3‐iodoindoles followed by addition to three aldehydes provided twelve 3‐hydroxymethylindoles in a multi‐microreactor setup. The synthetic flow strategy could be coupled with an in line continuous liquid–liquid extraction workup protocol for each reaction. Further elaboration of each of these indoles within the fluidic setup was achieved by acid‐catalysed nucleophilic substitutions with allyltrimethylsilane and methanol used as nucleophiles. Overall, a set of four 3‐iodoindoles was converted into thirty‐six indole derivatives by a range of transformations including iodo–magnesium exchange/electrophile trapping and acid‐catalysed nucleophilic substitution in a fully automated sequential fashion.