Continuous Flow Chemistry: Reaction of Diphenyldiazomethane with <em>p</em>-Nitrobenzoic Acid

Alex Aw; Marshall Fritz; Jonathan W. Napoline; Pamela Pollet; Charles L. Liotta

doi:10.3791/56608

JoVE Journal > Chemistry

化学

Continuous Flow Chemistry: Reaction of Diphenyldiazomethane with p-Nitrobenzoic Acid

Published: November 15, 2017

doi:

10.3791/56608

Alex Aw¹, Marshall Fritz², Jonathan W. Napoline¹, Pamela Pollet¹, Charles L. Liotta¹

¹School of Chemistry & Biochemistry,Georgia Institute of Technology, ²School of Chemical & Biomolecular Engineering,Georgia Institute of Technology

概要

Flow chemistry carries environmental and economic advantages by leveraging superior mixing, heat transfer and cost benefits. Herein, we provide a blueprint to transfer chemical processes from batch to flow mode. The reaction of diphenyldiazomethane (DDM) with p-nitrobenzoic acid, conducted in batch and flow, was chosen for proof of concept.

Abstract

Continuous flow technology has been identified as instrumental for its environmental and economic advantages leveraging superior mixing, heat transfer and cost savings through the "scaling out" strategy as opposed to the traditional "scaling up". Herein, we report the reaction of diphenyldiazomethane with p-nitrobenzoic acid in both batch and flow modes. To effectively transfer the reaction from batch to flow mode, it is essential to first conduct the reaction in batch. As a consequence, the reaction of diphenyldiazomethane was first studied in batch as a function of temperature, reaction time, and concentration to obtain kinetic information and process parameters. The glass flow reactor set-up is described and combines two types of reaction modules with "mixing" and "linear" microstructures. Finally, the reaction of diphenyldiazomethane with p-nitrobenzoic acid was successfully conducted in the flow reactor, with up to 95% conversion of the diphenyldiazomethane in 11 min. This proof of concept reaction aims to provide insight for scientists to consider flow technology's competitiveness, sustainability, and versatility in their research.

Introduction

Green chemistry and engineering are creating a culture change for the future direction of industry¹^,²^,³^,⁴. Continuous flow technology has been identified as instrumental for its environmental and economic advantages leveraging superior mixing, heat transfer, and cost savings through the "scaling out" strategy as opposed to the traditional "scaling up"⁵^,⁶^,⁷^,⁸^,⁹^,¹⁰.

Although the industries producing high-value products like the pharmaceutical industry have long favored batch processing, the advantages of flow technology have become attractive due to mounting economic competition and commercial production benefits¹¹. For example, when scaling up batch processes, pilot scale units must be built and operated to ascertain accurate heat and mass transfer mechanisms. This is hardly sustainable and subtracts substantially from the marketable patent life of the product. In contrast, continuous flow processing allows for the advantages of scale out, eliminating the pilot-plant phase and engineering associated with production scale-a significant financial incentive. Beyond the economic impact, continuous technology also enables atomic and energy efficient processes. For instance, enhanced mixing improves mass transfer for biphasic systems, leading to improved yields, catalyst recovery strategies, and subsequent recycling schemes. Additionally, the ability to accurately manage the reaction temperature leads to precise control of reaction kinetics and product distribution¹². The enhanced process control, quality of product (product selectivity) and reproducibility are impactful both from environmental and financial standpoints.

Flow reactors are available commercially with a wide variety of sizes and designs. In addition, customization of reactors to meet process needs can easily be achieved. Herein, we report experiments conducted in a glass continuous flow reactor (Figure 1). The assembly of microstructures (161 mm x 131 mm x 8 mm) made of glass is compatible with a wide range of chemicals and solvents and is corrosion-resistant over a wide range of temperatures (-25–200 °C) and pressures (up to 18 bar). The microstructures and their arrangement were designed for multi-injection, high-performance mixing, flexible residence time, and precise heat transfer. All of the microstructures are equipped with two fluidic layers (-25–200 °C, up to 3 bar) for heat exchange on either side of the reaction layer. Heat transfer rates are proportional to the heat transfer surface area and inversely proportional to its volume. Thus, these microstructures facilitate an optimum surface-to-volume ratio for improved heat transfer. There are two types of microstructures (i.e. modules): "mixing" modules and "linear" modules (Figure 2). The heart-shaped "mixing" modules are designed to induce turbulence and maximize mixing. In contrast, the linear modules provide additional residence time.

As proof of concept, we selected the well-described reaction of diphenyldiazomethane with carboxylic acids¹³^,¹⁴^,¹⁵^,¹⁶^,¹⁷. The reaction scheme is shown in Figure 3. The initial transfer of the proton from the carboxylic acid to the diphenyldiazomethane is slow and is the rate-determining step. The second step is rapid and yields the reaction product and nitrogen. The reaction was initially investigated to compare relative acidity of organic carboxylic acids in organic solvent (aprotic and protic). The reaction is first-order in the diphenyldiazomethane and first-order in carboxylic acids.

Experimentally, the reaction was conducted in presence of large excess of carboxylic acid (10 molar equivalents). As a consequence, the rate was pseudo first order with respect to the diphenyldiazomethane. The second order rate constant can then be obtained by dividing the experimentally obtained pseudo first order rate constant by the initial concentration of the carboxylic acid. Initially, the reaction of diphenyldiazomethane with benzoic acid (pKa = 4.2) was investigated. In batch, the reaction appeared to be relatively slow, reaching about 90% conversion in 96 minutes. As the reaction rate is directly proportional to the acidity of the carboxylic acid, we chose as a reaction partner the more acidic carboxylic acid, p-nitrobenzoic acid (pKa =3.4) to shorten the reaction time. The reaction of p-nitrobenzoic acid with diphenyldiazomethane in anhydrous ethanol was thus investigated in batch and flow (Figure 4). The results are provided in detail in the following section.

When the reaction is carried out in ethanol, three products can be formed: (i) benzhydryl-4-nitrobenzoate, which results from the reaction of p-nitrobenzoic acid with the diphenylmethane diazonium intermediate; (ii) benzhydryl ethyl ether that is obtained from reaction of the solvent, ethanol, with the diphenylmethane diazonium; and (iii) nitrogen. The product distribution was not studied as it is well documented in literature; rather we focused our attention to the technology transfer of the batch reaction to continuous flow¹³^,¹⁴^,¹⁵. Experimentally the disappearance of the diphenyldiazomethane was monitored. The reaction proceeds with a vivid color change, which can be visually observed by UV-Vis spectroscopy. This results from the fact that the diphenyldiazomethane is a strongly purple compound whereas all other products from the reaction are colorless. Therefore, the reaction can be visually monitored on a qualitative basis and quantitatively followed by UV spectroscopy (i.e. disappearance of the diphenyl diazomethane absorption at 525 nm). Herein, we first report the reaction of diphenyldiazomethane and p-nitrobenzoic acid in ethanol in batch as a function of time. Secondly, the reaction was successfully transferred and carried out into the glass flow reactor. The progress of the reaction was ascertained by monitoring the disappearance of diphenyldiazomethane using UV-spectroscopy (in batch and flow modes).

Protocol

Health Warnings and Specification of Reagents
Benzophenone Hydrazone: May cause irritation of the digestive tract. The toxicological properties of this substance have not been fully investigated. May cause respiratory tract irritation. The toxicological properties of this substance have not been fully investigated. May cause skin irritation and eye irritation¹⁸.

Activated manganese oxide (MnO₂): (Health MSDS rating of 2) Hazardous in case of skin contact, eye contact, ingestion, and inhalation¹⁹.

Dibasic potassium phosphate (KH₂PO₄): (Health MSDS rating of 2) Hazardous in case of skin contact, eye contact, ingestion, and inhalation²⁰.

Dichloromethane: (Health MSDS rating of 2, Fire rating of 1) Very hazardous in case of eye contact (irritant), of ingestion, of inhalation. Hazardous in case of skin contact (irritant, permeator). Inflammation of the eye is characterized by redness, watering, and itching²¹.

1. Synthesis of Diphenyldiazomethane (DDM):

Before beginning synthesis of DDM, ensure all necessary materials listed are present as well as necessary reagents to ensure that proper synthesis can be conducted.
Add 10 g (.72 equivalent) of anhydrous KH₂PO₄and 31 g of activated manganese dioxide, MnO₂ (3.5 equivalents) to a 250 mL 3-neck round bottom flask (1), and a magnetic stirrer.
Add 20 g of benzophenone hydrazone into a separate 100-mL 2-neck round bottom flask (2), a magnetic stirrer, and store at room temperature.
Add 67 mL of dichloromethane (DCM) and equip both flasks (1 and 2) with stoppers, thermometer, and thermocouple.
After purging both flasks with inert gas for 15 min, apply an ice bath to the KH₂PO₄and MnO₂solution (flask 1). Ensure that the temperature of the solution stays constant at 0 °C for at least 30 min.
After 30 min of constant temperature reading, transfer the benzophenone hydrazone (flask 2) into the flask containing KH₂PO₄and MnO₂(flask 1). Carry out the reaction for 24 h to reach completion.

2. Purification of DDM:

After 24 h, add 120 mL of pentane to the reaction mixture (a deep, red purple solution).
Filter the solution rapidly through neutral silica gel (50 – 200 µm). It is important that the contact time of the product with the silica does not exceed 5 min. DDM is acid sensitive; significant decomposition will occur with longer contact time²².
1. Carry out the filtration with a medium porosity sintered glass funnel, attached to a vacuum filtration system or a fume hood vacuum system.
Transfer the filtrate and remove solvent with a rotary evaporator in vacuo. The resulting crude product is a deep-purple oil.
1. Wrap aluminum foil around the flask to keep light away from DDM. DDM is light sensitive.
After covering the flask with aluminum foil, store pure DDM in the freezer, sealed and under an atmosphere of inert gas.
Monitor for crystallization to occur, which usually takes 2 – 3 days. Remove the flask from the freezer and allow it to reach room temperature. A further purification step is necessary. Add 200-proof ethyl alcohol to the flask, filter and then use a rotary evaporator to remove the remaining solvent. At this point, most impurities remaining should be removed.
1. Analyze the resulting deep, reddish purple crystals of DDM by UV spectroscopy. The experimental molar absorptivity was measured to be (ε) 94.8, which matched literature values.
  CAUTION: Below are the relevant health warnings and specifications of reagents for the proper and safe handling of carrying out the reaction protocol for DDM. When dealing with these substances, ensure proper PPE at all times and working conditions under a fume hood.
  
  DDM: Prolonged or repeated exposure may cause allergic reactions in certain sensitive individuals²³.
  p-nitrobenzoic acid: (MSDS health rating of 2) ensure that reagent is kept away from heat. Keep away from sources of ignition. Empty containers pose a fire risk; evaporate the residue under a fume hood. Ground all equipment containing material. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes²⁴.
  Ethyl Alcohol, 200 Proof: (MSDS health rating of 2, Health Rating of 3) Hazardous in case of skin contact, eye contact, and inhalation. Ethanol rapidly absorbs moisture from the air, and can react vigorously with oxidizers²⁵.
  Toluene: (MSDS health rating of 2, Health Rating of 3) Hazardous in case of skin contact (irritant), of eye contact (irritant), of ingestion, and of inhalation. Slightly hazardous in case of skin contact (permeator). Highly flammable²⁶.
  o-xylene: (MSDS health rating of 2, Health Rating of 3) possibility of developing teratogenic effects, developmental toxicity to reproductive system in males, and toxic if ingested to kidneys, liver, upper respiratory tract, skin, eyes, and central nervous system. Keep away from skin contact (irritant, permeator), eye contact (irritant), or ingestion and inhalation²⁷.

3. Preparing Solution of DDM for Continuous Flow:

Rinse a 100 mL volumetric flask with ethanol.
Tare a 6-dram vial on an analytical balance, and add .1942 g of DDM into the dram vial. Add anhydrous ethanol (5 mL) to the vial in 2 to 3 increments until all the DDM goes into solution. With a pipette, transfer the solution from the 6-dram vial into the clean 100 mL volumetric flask.
1. Carefully add ethanol until the minimum point of the meniscus aligns with the line denoted on the volumetric flask.
2. Add 1 mL of toluene, the internal standard, into the flask. The volumetric flask can now be capped and stored until both the DDM solution and p-nitrobenzoic acid solution are ready for the continuous flow reaction.

4. Preparation of 0.1 M Stock Solution of p-nitrobenzoic Acid:

Rinse the 250 mL volumetric flask multiple times with anhydrous ethanol.
Tare a 6-dram vial on an analytical balance. Add 4.1780 g of p-nitrobenzoic acid into the dram vial. After adding the acid, add anhydrous ethanol (5 mL) into 2 to 3 increments to the vial until all the p-nitrobenzoic acid goes into solution.
1. With a pipette, transfer the solution from the 6-dram vial into the clean 250 mL volumetric flask.
2. Carefully add ethanol until the minimum point of the meniscus aligns with the line of the volumetric flask.
3. Add 1 mL of o-xylene, the internal standard, into the flask. The volumetric flask can now be capped and stored as needed.

5. Preparation of the Continuous Flow Reactor:

Check that the transducer is connected to the pump controller in portal A for both ISCOs, and empty collecting beakers at the end of each exit tube to collect reaction solutions, waste, and solvent.
1. Set-up and check both ISCO 1 (p-nitrobenzoic acid) and ISCO 2 (DDM), as shown in Figure 9.
2. Set-up each ISCO pump with its own controller to independently control reagent streams. This allows for the flow rates to be independently adjusted as necessary.
In a separate beaker, add 400 mL of ethanol. This will be utilized to flush the reactor.
1. Turn the inlet HIP valve counter-clockwise until the valve is fully open (denoted as valve A and B, respectively). Press "Constant Flow" on the pump controller, and then "A", which denotes the inlet which the transducer is linked to the ISCO. This action prompts the user to enter the desired flow rate.
2. Enter a flowrate of "70", and press "Enter". When ready, hit "Refill" to communicate to the system to draw up the solution at a rate of 70 mL/min.
3. Begin drawing the ethanol solvent through the inlet tube. Note that if the flow rate is drawing the solvent in, the flow rate on the ISCOs should read -70.000 mL/min. The solvent level in the flask will begin to decrease.
  NOTE: It is perfectly normal if the volume of solvent does not match the volume that is shown on the controller. Air will be partially drawn into the system as well.
When both ISCO 1 and ISCO 2 have been completely filled and the controller indicates this by reading "Cylinder Full" and "Stopped", turn the inlet valve A and B completely closed by turning the valve fully clockwise.
Open the outlet valve which operates similarly to the inlet valve, which is the valve leading to the reactor, by turning it counterclockwise. The outlet valve feeds through the filter, past the one-way valve, and from there past the pressure relieve valve and into the flow reactor.
At this point, change the flow rate. The maximum total flow rate recommended on a single run should not exceed 30 mL/min.
1. Clean each ISCO separately, running each at a flow rate of 30 mL/min.
Press "A" on the ISCO that is currently set up to run the ethanol through the system. Change the flow rate by entering the desired flow rate of "30", "Enter", and finally "Run". This communicates to the system to run at a rate of 30 mL/min.
NOTE: As the flow equilibrates, the solvent begins flowing through the system.
1. Monitor the reactor for leakage or blockage, and that there is solvent flowing throughout the whole reactor. Once both ISCOs have been cleaned 2 – 3 times, the system is now ready to run the experiment.

6. Setting Up the .01 M DDM ISCO 2 Pump:

Place the inlet feed in the 100-mL volumetric flask of DDM. Open the inlet valve B (Feed 2 in Figure 9).
Set the ISCO to a flow rate of 70 mL/min. Begin drawing the solution up until all of it is taken up into the syringe by hitting "Refill".
Note that the volume of solution in the ISCO and the original volume of solution in the flask can be slightly different. Air is also pulled in the ISCO pump.
1. If there is leftover DDM after the ISCO has reached max volume after the uptake of solution, press "Run" to push out the air that was drawn along with the flask from the inlet. Once DDM begins pushing out, hit "Stop", and then "Refill" to begin refilling the ISCO.
2. Keep repeating these steps until all DDM has been taken up (this will be applied to p-nitrobenzoic acid as well).
3. Flow about 1 mL of DDM from pump. ISCO 2 pump is now ready to be run. The solvent level is in line and ready to begin flowing through the continuous flow reactor.
Close inlet valve B by turning the HIP valve clockwise until it cannot be turned further, and open the outlet valve which feeds into the continuous flow reactor by turning the valve counter clockwise until it is fully open. Transfer the 1 mL of DDM and toluene solution into a cuvette for UV-Vis analysis.
Set the flow rate to 1.42 mL/min. Do not hit "Run" until the p-nitrobenzoic acid ISCO 1 has been set-up by the same protocol at a flow rate of 3.58 mL/min and is ready to be run in tandem.

7. Setting Up the .1 M p -nitrobenzoic Acid ISCO 1 Pump:

Open the inlet valve A of ISCO 1 pump, with the 250 mL volumetric flask of p-nitrobenzoic acid at the end of the feeding tube.
Once the feed tube is completely submerged in the volumetric flask, set the ISCO to a flow rate of 70 mL/min. Again, check to see if the flow rate on the controller reads 70.00 mL/min upon hitting "Refill".
Begin drawing the solution up until all of it is taken up into the syringe, using the same technique listed above to get all of the solution into the system.
Close the inlet valve by turning the HIP valve clockwise until it is fully closed. Open the outlet valve which feeds into the continuous flow reactor by turning the valve counter clockwise until it is fully open.
Set the flow rate to 3.58 mL/min. The total flow rate including the 1.42 mL/min of DDM will be 5.00 mL/min, for a total residence time within the reactor of approximately 11 minutes with a ratio of 10:1 p-nitrobenzoic acid to DDM.

8. Conducting the Reaction in Flow with 10:1 Molar Equivalence of p-nitrobenzoic acid and DDM:

Once each pump is ready with the reagent's solutions, the valves properly adjusted, and the correct flow rates have been entered, hit "Run" on both pumps. After the one-way valve pressure has equilibrated, the reagent's solutions will begin flowing into the reactor modules.
1. Monitor flow. DDM's feed enters at module 1, p-nitrobenzoic acid's feed into module 2, and mixing take place at module 3. The residence time is approximately 11 minutes.
2. Monitor color change (indicative of reaction progress). The color in module 2, prior to mixing, is strong pink. The color intensity decreases, it becomes fainter pink in module 3, and pale pink in module 4. The modules thereafter are colorless.

9. Cleaning the Continuous Flow Reactor:

Once both runs of DDM and p-nitrobenzoic acid are completed, fill a beaker with 400 mL ethanol. This will be used to clean the reactor and the ISCO pumps.
Turn the inlet HIP valve counter-clockwise until the valve is fully open.
Set the flow rate to 70, press "Enter" and "Refill" to begin drawing the ethanol solvent through the inlet tube (note that if the flow rate is drawing the solvent in, the flow rate on the ISCOs should read 70 mL/min).
Once the ISCOs have been filled, the ISCOs will automatically stop, and the controller will read "Cylinder Full" and "Stopped". At this point, turn the inlet valve completely closed, by turning the valve clockwise until the HIP valve cannot be turned further.
Open the outlet valve which operates similarly to the inlet valve, by turning it counterclockwise. The outlet valve feeds through the filter, passes the one-way valve, and from there flows through the pressure relieve valve and into the flow reactor.
Adjust the flow rate to not exceed 30 mL/min.
Press "A" on the ISCO that is currently set up to run the ethanol through the system. Change the flow rate by entering the desired flow rate of "10", hit "Enter", and then hit "Run". Check the system to see there is no leakage or blockage, and that there is solvent flowing throughout the whole system.
NOTE: Once both ISCOs have been cleaned 2 times with ethanol and once with just air following procedures noted above, the system is now ready to run for future experiments.

Representative Results

Batch Reaction
Diphenyldiazomethane was prepared according to literature²⁸^,²⁹. The compound was crystallized from petroleum ether:ethyl acetate (100:2) and the purple crystalline solid was analyzed by H¹ NMR, melting point, and MS. The analyses were consistent with the structure and reported literature values.

The reaction of diphenyldiazomethane (1.0 mM) with benzoic acid (10 mM) in anhydrous ethanol was carried out at 21 °C in dry ethanol. The progress of the reaction was monitored using UV-Vis spectrometry (λmax = 525 nm). After 96 minutes, about 90% of the diphenyldiazomethane was consumed. The pseudo-first order rate constant was calculated to be 0.0288 min^-1 and the resulting second rate constant to be 0.58 mol^-1.min^-1.L. The second-order rate constant is in agreement with literature values (~ 0.7 mol^-1.min^-1.L at 26 °C)¹⁷. The reaction was then investigated with the more acidic p-nitrobenzoic acid. The reaction of diphenyldiazomethane (1 mM) with p-nitrobenzoic acid (10mM) in anhydrous ethanol was conducted at 21 °C and monitored in-situ by UV-Vis at λ = 525 nm (Figure 5). UV-vis spectra were taken at 1.5 minutes intervals. Figure 6 shows a representative spectrum of the UV-absorbance of diphenyldiazomethane as a function of the progression of the reaction with p-nitrobenzoic acid in anhydrous ethanol.

Figures 7 and 8 show the concentration of DDM as a function of time and the pseudo-first order ln(Abs/Abs₀) as a function of time. From the latter plot, an apparent first-rate of reaction of 0.135 min^-1 was obtained, which corresponds to a second order rate constant of 1.80 mol^-1.min^-1.L. The data are consistent with reported literature values¹⁷. Importantly, the reaction reaches about 94% completion within 20 min (Figure 8), which is amenable to the flow reactor. The next step was to transfer the reaction to the glass flow reactor.

Flow reaction
The schematic and photograph of the flow process used herein is shown in Figure 9. The two reactant streams are introduced into a pre-heating/cooling module (1 and 2 in Figure 9). Modules 1 and 2 allows to control the temperature of each incoming feeds. The mixing of the two reactant feeds occurs at the module 3 (Figure 9) before proceeding into three mixing modules (4, 5, & 6 in Figure 9) and two linear modules (7 & 8 in Figure 9). Each reactant stream was independently controlled and introduced via syringe pumps. The reactant solutions were each prepared with internal standards (1vol% toluene/ortho-xylene) to measure accurately the concentrations of reactant. The residence times of the reactions are controlled by changing the total flow rate. For example, residence times of 1 min 52 s, 3 min 44 s, and 11 min 12 s corresponded to total flow rates of 30 mL/min, 15 mL/min, and 5 mL/min.

Operationally, two stock solutions were prepared: (1) A solution of diphenyldiazomethane in anhydrous ethanol (0.02M) and (2) A solution of p-nitrobenzoic acid (0.1 M). Both solutions were fed into the reactor (Feeds 1 & 2 in Figure 9) at rate of 1.42 mL/min of and 3.58 mL/min respectively. Accounting for the initial concentrations of diphenyldiazomethane and p-nitrobenzoic and their respective flow-rate, the molar ratio of diphenyldiazomethane to p-nitrobenzoic acid was 1 to 10. Experimentally, the total flow rate was approximately 5 mL/min leading to a residence time of 11 minutes. Aliquots were taken as a function of time and analyzed by GC-FID (gas chromatography with flame ionization detector) and by UV-Vis spectroscopy. GC-FID analyses were used to measure the accurate concentration ratio of reagents using internal standards. Toluene was used as the internal standard (0.107 M) in the diphenyldiazomethane solution and ortho-xylene was present in the p-nitrobenzoic acid (0.072 M). The UV-Vis analyses quantitatively measured the progress of the reaction by monitoring the disappearance of diphenyldiazomethane as a function of time (the method was established and described for the batch reaction).

The results shown in Figure 10 shows that 95% completion is reached within the 11 min residence time. To reach complete conversion, the residence time can be extended to 33 min or less. Operationally, full conversion can be obtained with slower flow rate (as shown) or by increasing residence time (additional microstructures/modules) and/or increase of temperature. However, the proof of concept shows that the reaction can successfully be conducted in flow with 95% conversion in 11 min.

Figure 1: Schematic of continuous flow microstructures. Please click here to view a larger version of this figure.

Figure 2: Mixing (left) and linear (right) microstructures. Please click here to view a larger version of this figure.

Figure 3: Reaction of diphenyldiazomethane with an acid (X-H). Please click here to view a larger version of this figure.

Figure 4: Reaction of diphenyldiazomethane with p-nitrobenzoic acid in anhydrous ethanol. Please click here to view a larger version of this figure.

Figure 5: Reaction of diphenyldiazomethane (1eq) with ethanol and p-nitrobenzoic acid (10 eq). Please click here to view a larger version of this figure.

Figure 6: Absorbance as a function of wavelength for the reaction of diphenyldiazomethane with p-nitrobenzoic acid. The maximum absorbance for diphenyldiazomethane is 525 nm. Each line represents one spectra taken at different time intervals (each 1.5 min) from time = 0. Please click here to view a larger version of this figure.

Figure 7: pseudo-first order reaction (ln(Abs/Abs0) vs. Time (min) as a function of time for the reaction of diphenyldiazomethane and p-nitrobenzoic acid at 21 °C in ethanol in batch. Please click here to view a larger version of this figure.

Figure 8: Concentration of diphenyldiazomethane as a function of time for the reaction of diphenyldiazomethane and p-nitrobenzoic acid at 21 °C in ethanol in batch. Please click here to view a larger version of this figure.

Figure 9: Schematic of the continuous flow reactor. Please click here to view a larger version of this figure.

Figure 10: Concentration of diphenyldiazomethane as a function of time for the reaction of diphenyldiazomethane and p-nitrobenzoic acid at 21 °C in ethanol in flow. Please click here to view a larger version of this figure.

Figure 11: Reaction of diazoketone, tert-butyl (S)-(4-diazo-3-oxo-1-phenylbutan-2-yl) Carbamate. Please click here to view a larger version of this figure.

Discussion

Flow chemistry has gained much attention recently with an average of about 1,500 publications on the topic annually in research areas of Chemistry (29%) and Engineering (25%). Many successful processes have been conducted in flow. In numerous cases, flow chemistry was demonstrated to exhibit superior performances to batch for many applications such as the preparations of pharmaceutically active ingredients³⁰^,³¹, natural products³², and specialty, high-value chemicals like high-performance polymers³³^,³⁴^,³⁵^,³⁶. We leveraged and reported continuous flow processes for the preparation and reaction of diazoketone³⁷, Meerwein-Ponndorf-Verley reduction of ketone and aldehydes to alcohols³⁸ and metal-catalyzed Homo-Nazarov cyclization³⁹. Especially interesting is the example of the preparation and reaction of thermally unstable and highly reactive anhydride in the reaction of diazoketone, tert-butyl (S)-(4-diazo-3-oxo-1-phenylbutan-2-yl) carbamate (Figure 11)³⁷^,⁴⁰.

Because of the enhanced temperature control and mixing, the flow technology was demonstrated to be superior to batch process for the following criteria: (i) the implementation of a less expensive mixed anhydride, (ii) the use of the relatively safer trimethyl silyldiazomethane than diazomethane, (iii) the temperature, 4 °C in flow instead of -20 °C in batch with consistent 100% yield, (iv) shortened reaction time (10 min), and (v) significant reduction in waste-stream (atomic economy).

Herein, we have provided a blueprint for the successful transfer of diphenyldiazomethane with p-nitrobenzoic acid reaction from batch mode to continuous flow. Our blueprint emphasizes that it is critical to conduct studies in batch mode to establish accurate reaction rate, the reaction profile as a function of time, and the optimum concentration and temperature. These parameters are essential to take into consideration prior to transferring the reaction to continuous flow technology. The design of the reactor was described in detail and was tailored to be amenable with regards to the reaction characteristics. Finally, the reaction was successfully conducted in flow and monitored qualitatively by visual observation (i.e. loss of color). Quantitative assessment of the progress of the reaction (e.g. disappearance of diphenyldiazomethane) was obtained by UV-Vis. About 94% consumption was achieved with 11 min residence time in flow at 21 °C.

Limitation and considerations
The formation of solids (i.e. precipitates) during the reaction is an important parameter when considering flow processes. In those instances, one must consider: (i) modifying the protocol in batch-mode to maintain homogeneity throughout the reaction (i.e. changing reagents, solvent, temperature, etc.) or (ii) design the reactor to allow for the processing of slurries. The second option may be viable with optimization and tailored reactor design. In practice, the two most limiting factors for flow processes are (i) viscous solutions: the ability to pump viscous liquids and the resulting pressure drop are often prohibitive and (ii) using heterogeneous (solid/liquid) feeding streams. It is difficult to consistently and effectively pump fine suspensions (for example in the cases of heterogeneous catalyst). In addition, accumulation of particles in the reactor can lead to blockage, and ultimately failure.

Overall, flow chemistry has been demonstrated to be superior (to batch processes) for synthetic transformations that (i) require precise temperature control (i.e. avoid hot spot, competitive reaction, etc.) (ii) involve the formation of highly reactive or unstable intermediates, or (iii) require enhanced mixing with multi-liquid phases for example. The resulting increase of product quality and reproducibility (via enhanced and precise control of the process parameters) is impactful both from an environmental and a financial standpoint. Flow technology may not be the universal solution but can open new avenues for chemical pathways that were deemed not viable in batch (i.e. too reactive or too unstable intermediates) as well as provide process optimization in terms of energy consumption, atom economy and downstream-purification. To conclude, it is a powerful tool to effectively conduct multi-step processes for high-value added chemicals.

開示

The authors have nothing to disclose.

Acknowledgements

We would like to thank Corning for the gift of the glass flow reactor.

Materials

Thermometer	HB-USA/ Enviro-safe	Any other instrument scientific company provider works
Benzophenone hydrazone	Sigma-Aldrich	Store at 2-8 °C, 96% purity
Activated MnO₂	Fluka	≥ 90% purity, harmful if inhaled or swallowed. Refer to MSDS for more safety precautions
Dibasic KH₂PO₄	Sigma-Aldrich	Serious eye damage, respiratory irritant. Refer to MSDS for more safety precautions
Dichloromethane (DCM)	Alfa Aesar	≥ 99.7% purity, argon packed
Rotovap	Büchi	accessory parts include Welch self-cleaning dry vacuum model 2027, and Neuberger KNP dry ice trap
Bump trap	Chemglass	Any other instrument scientific company provider works
Neutral Silica Gel (50-200 mM)	Acros Organic/ Sorbent Technology	Respiratory irritant if inhaled, refer to MSDS for more safety precautions
Inert Argon Gas	Airgas	Always ensure proper regulator is in place before using
Medium Porosity Sintered Funnel Glass Filter	Sigma-Aldrich	Any other instrument scientific company provider works
Aluminum Foil	Reynolds Wrap	Any other company works. Used to prevent photolytic damage towards DDM
Para-NO₂ benzoic acid	Sigma-Aldrich	Skin contact irritant, eye irritant, respiratory irritant. Refer to MSDS for more safety precautions
Pure ethyl alcohol (200 proof)	Sigma-Aldrich	≥ 99.5% purity, anhydrous. Highly flammable
Toluene	Sigma-Aldrich	≥ 99.8% purity, anhydrous. Skin permeator, flammable
Ortho-xylene	Sigma-Aldrich	99% purity, anhydrous. Toxic to organs and CNS. Adhere to specifications dictated within MSDS
Diphenyl diazo methane	Produced in-house	Respiratory irritant, refer to MSDS for more safety precautions
Corning reactor	Corning Proprietary	Manufactured in 2009. model number MR 09-083-1A
Stop watch	Traceable Calibration Control Company	Any other company that provides monitoring with laboratory grade accredidation works
Analytical balance	Denver Instruments	Model M-2201, or any analytical balance that has sub-milligram capabilities
Dram vials	VWR	2 dram, 4 dram, and 6 dram vials
Micropipettes	Eppendorf	2-20 μL and 100-1000 μL micropipettes work
Glass pipettes	VWR	Any other instrument scientific company provider works
GC-MS	Shimadzu GC	Software associated: GC Real Time Analysis
GC vials	VWR	Any other providing company works
Beakers	Pyrex	500 mL beakers
Syringe pumps	Sigma Aldrich	Teledyne Isco Model 500D
Relief valve	Swagelok	Spring loaded relieve valve
One-way valves	Nupro	10 psi grade
Two-way straight valves	HiP	15,000 psi grade

参考文献

Jimenez-Gonzalez, C., et al. Engineering Research Areas for Sustainable Manufacturing: A Perspective from Pharmaceutical and Fine Chemicals Manufacturers. Org Process Res Dev. 15 (4), 900-911 (2011).
Constable, D. J. C., et al. Key green chemistry research areas – a perspective from pharmaceutical manufacturers. Green Chem. 9 (5), 411-420 (2007).
Plutschack, M. B., Pieber, B., Gilmore, K., Seeberger, P. H. The Hitchhiker’s Guide to Flow Chemistry. Chem Rev. , (2017).
Dallinger, D., Kappe, C. O. Why flow means green – Evaluating the merits of continuous processing in the context of sustainability. Curr Opin Green Sustain Chem. 7, 6-12 (2017).
Movsisyan, M., et al. Taming hazardous chemistry by continuous flow technology. Chem Soc Rev. 45 (18), 4892-4928 (2016).
Hessel, V., Ley, S. V. Flow Chemistry in Europe. J Flow Chem. 6 (3), 135-135 (2016).
Mascia, S., et al. End-to-End Continuous Manufacturing of Pharmaceuticals: Integrated Synthesis, Purification, and Final Dosage Formation. Angew Chem Int Edit. 52 (47), 12359-12363 (2013).
Newman, S. G., Jensen, K. F. The role of flow in green chemistry and engineering. Green Chem. 15 (6), 1456-1472 (2013).
Watts, P., Haswell, S. J. The application of micro reactors for organic synthesis. Chem Soc Rev. 34 (3), 235-246 (2005).
Wiles, C., Watts, P. Continuous flow reactors: a perspective. Green Chem. 14 (1), 38-54 (2012).
Roberge, D. M., et al. Microreactor technology and continuous processes in the fine chemical and pharmaceutical industry: Is the revolution underway. Org Process Res Dev. 12 (5), 905-910 (2008).
Degennaro, L., Carlucci, C., De Angelis, S., Luisi, R. Flow Technology for Organometallic-Mediated Synthesis. J Flow Chem. 6 (3), 136-166 (2016).
Roberts, J. D., Watanabe, W. The Kinetics and Mechanism of the Acid-Catalyzed Reaction of Diphenyldiazomethane with Ethyl Alcohol. J Am Chem Soc. 72 (11), 4869-4879 (1950).
Roberts, J. D., Watanabe, W., Mcmahon, R. E. The Kinetics and Mechanism of the Reaction of Diphenyldiazomethane and Benzoic Acid in Ethanol. J Am Chem Soc. 73 (2), 760-765 (1951).
Roberts, J. D., Watanabe, W., Mcmahon, R. E. The Kinetics and Mechanism of the Reaction of Diphenyldiazomethane with 2,4-Dinitrophenol in Ethanol. J Am Chem Soc. 73 (6), 2521-2523 (1951).
Roberts, J. D., Regan, C. M. Kinetics and Some Hydrogen Isotope Effects of the Reaction of Diphenyldiazomethane with Acetic Acid in Ethanol. J Am Chem Soc. 74 (14), 3695-3696 (1952).
Oferrall, R. A., Kwok, W. K., Miller, S. I. Medium Effects Isotope Rate Factors + Mechanism of Reaction of Diphenyldiazomethane with Carboxylic Acids in Solvents Ethanol + Toluene. J Am Chem Soc. 86 (24), 5553 (1964).
Aldrich, S. . Material Safety Data Sheet: Benzophenone Hydrazone. 4.2, 3-6 (2014).
Science Lab Chemicals & Laboratory Equipment. . Material Safety Data Sheet: Manganese dioxide MSDS. , (2005).
Science Lab Chemicals & Laboratory Equipment. . Material Safety Data Sheet: Potassium phosphate dibasic MSDS. , 1-5 (2005).
Science Lab Chemicals & Laboratory Equipment. . Material Safety Data Sheet: Methylene Chloride MSDS. , 3-5 (2005).
Smith, L. I., Howard, K. Diphenyldiazomethane. Org. Synth. 3 (351), (1955).
Capot Chemical Co. . Material Safety Data Sheet, diphenyldiazomethane. 2017, (2010).
Science Lab. . Material Safety Data Sheet: P-nitrobenzoic acid MSDS. , 3-5 (2005).
Science Lab Chemicals & Laboratory Equipment. . Material Safety Data Sheet Ethyl Alcohol 200 proof MSDS. , (2005).
Science Lab Chemicals & Laboratory Equipment. . Material Safety Data Sheet Toluene MSDS. , 4-5 (2005).
Science Lab Chemicals & Laboratory Equipment. . Material Safety Data Sheet o-Xylene MSDS. , 3-5 (2005).
Zheng, J., et al. Cross-Coupling between Difluorocarbene and Carbene-Derived Intermediates Generated from Diazocompounds for the Synthesis of gem-Difluoroolefins. Organic Letters. 17, 6150-6153 (2015).
Reimlinger, H. 1,5-Dipolar cyclizations, I. Definition and contributions to the Imidazide/Tetrazole tautomerism. Chem. Ber. 103, 1900 (1970).
Baumann, M., Garcia, A. M. R., Baxendale, I. R. Flow synthesis of ethyl isocyanoacetate enabling the telescoped synthesis of 1,2,4-triazoles and pyrrolo-[1,2-c] pyrimidines. Org Biomol Chem. 13 (14), 4231-4239 (2015).
Baumann, M., Baxendale, I. R. The synthesis of active pharmaceutical ingredients (APIs) using continuous flow chemistry. Beilstein J Org Chem. 11, 1194-1219 (2015).
Pastre, J. C., Browne, D. L., Ley, S. V. Flow chemistry syntheses of natural products. Chem Soc Rev. 42 (23), 8849-8869 (2013).
Pirotte, G., et al. Continuous Flow Polymer Synthesis toward Reproducible Large-Scale Production for Efficient Bulk Heterojunction Organic Solar Cells. Chemsuschem. 8 (19), 3228-3233 (2015).
Kumar, A., et al. Continuous-Flow Synthesis of Regioregular Poly(3-Hexylthiophene): Ultrafast Polymerization with High Throughput and Low Polydispersity Index. J Flow Chem. 4 (4), 206-210 (2014).
Helgesen, M., et al. Making Ends Meet: Flow Synthesis as the Answer to Reproducible High-Performance Conjugated Polymers on the Scale that Roll-to-Roll Processing Demands. Adv Energy Mater. 5 (9), 1401996 (2015).
Grenier, F., et al. Electroactive and Photoactive Poly[lsoindigo-alt-EDOT] Synthesized Using Direct (Hetero)Arylation Polymerization in Batch and in Continuous Flow. Chem Mater. 27 (6), 2137-2143 (2015).
Pollet, P., et al. Production of (S)-1-Benzyl-3-diazo-2-oxopropylcarbamic Acid tert-Butyl Ester, a Diazoketone Pharmaceutical Intermediate, Employing a Small Scale Continuous Reactor. Ind Eng Chem Res. 48 (15), 7032-7036 (2009).
Flack, K., et al. Al(OtBu)(3) as an Effective Catalyst for the Enhancement of Meerwein-Ponndorf-Verley (MPV) Reductions. Org Process Res Dev. 16 (3), 1301-1306 (2012).
Aponte-Guzman, J., et al. A Tandem, Bicatalytic Continuous Flow Cyclopropanation-Homo-Nazarov-Type Cyclization. Ind Eng Chem Res. 54 (39), 9550-9558 (2015).
Liotta, C. L., et al. Synthetic Transformations Employing Continuous Flow. ACS- Fall 2013.Synthetic Transformations Employing Continuous Flow. , (2013).

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Aw, A., Fritz, M., Napoline, J. W., Pollet, P., Liotta, C. L. Continuous Flow Chemistry: Reaction of Diphenyldiazomethane with p-Nitrobenzoic Acid. J. Vis. Exp. (129), e56608, doi:10.3791/56608 (2017).

Continuous Flow Chemistry: Reaction of Diphenyldiazomethane with p-Nitrobenzoic Acid