Method Article

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

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DOI:

10.3791/56608

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November 15th, 2017

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

In This Article

Summary

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).

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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):

  1. 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.
  2. Add 10 g (.72 equivalent) of anhydrous KH2PO4 and 31 g of activated manganese dioxide, MnO2 (3.5 equivalents) to a 250 mL 3-neck round bottom flask (1), and a magnetic stirrer.
  3. 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.
  4. Add 67 mL of dichloromethane (DCM) and equip both flasks (1 and 2) with stoppers, thermometer, and thermocouple.
  5. After purging both flasks with inert gas for 15 min, apply an ice bath to the KH2PO4 and MnO2 solution (flask 1). Ensure that the temperature of the solution stays constant at 0 °C for at least 30 min.
  6. After 30 min of constant temperature reading, transfer the benzophenone hydrazone (flask 2) into the flask containing KH2PO4 and MnO2 (flask 1). Carry out the reaction for 24 h to reach completion.

2. Purification of DDM:

  1. After 24 h, add 120 mL of pentane to the reaction mixture (a deep, red purple solution).
  2. 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.
  3. 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.
  4. After covering the flask with aluminum foil, store pure DDM in the freezer, sealed and under an atmosphere of inert gas.
  5. 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:

  1. Rinse a 100 mL volumetric flask with ethanol.
  2. 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:

  1. Rinse the 250 mL volumetric flask multiple times with anhydrous ethanol.
  2. 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:

  1. 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.
  2. 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.
  3. 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.
  4. 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.
  5. 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.
  6. 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:

  1. Place the inlet feed in the 100-mL volumetric flask of DDM. Open the inlet valve B (Feed 2 in Figure 9).
  2. 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".
  3. 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.
  4. 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.
  5. 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:

  1. 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.
  2. 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".
  3. 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.
  4. 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.
  5. 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:

  1. 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:

  1. 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.
  2. Turn the inlet HIP valve counter-clockwise until the valve is fully open.
  3. 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).
  4. 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.
  5. 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.
  6. Adjust the flow rate to not exceed 30 mL/min.
  7. 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.

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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 diphenyldiazo...

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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 spe...

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Disclosures

None of the authors within this protocol have any competing financial interests or conflict of interest.

Acknowledgements

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

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Materials

List of materials used in this article
NameCompanyCatalog NumberComments
ThermometerHB-USA/ Enviro-safeAny other instrument scientific company provider works
Benzophenone hydrazoneSigma-AldrichStore at 2-8 °C, 96% purity
Activated MnO2Fluka≥ 90% purity, harmful if inhaled or swallowed. Refer to MSDS for more safety precautions
Dibasic KH2PO4Sigma-AldrichSerious eye damage, respiratory irritant. Refer to MSDS for more safety precautions
Dichloromethane (DCM)Alfa Aesar≥ 99.7% purity, argon packed
RotovapBüchiaccessory parts include Welch self-cleaning dry vacuum model 2027, and Neuberger KNP dry ice trap 
Bump trapChemglassAny other instrument scientific company provider works 
Neutral Silica Gel (50-200 mM)Acros Organic/ Sorbent TechnologyRespiratory irritant if inhaled, refer to MSDS for more safety precautions
Inert Argon GasAirgasAlways ensure proper regulator is in place before using
Medium Porosity Sintered Funnel Glass FilterSigma-AldrichAny other instrument scientific company provider works
Aluminum FoilReynolds WrapAny other company works. Used to prevent photolytic damage towards DDM
Para-NO2 benzoic acidSigma-AldrichSkin 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
TolueneSigma-Aldrich≥ 99.8% purity, anhydrous. Skin permeator, flammable
Ortho-xyleneSigma-Aldrich99% purity, anhydrous. Toxic to organs and CNS. Adhere to specifications dictated within MSDS
Diphenyl diazo methaneProduced in-houseRespiratory irritant, refer to MSDS for more safety precautions
Corning reactorCorning ProprietaryManufactured in 2009. model number MR 09-083-1A
Stop watchTraceable Calibration Control CompanyAny other company that provides monitoring with laboratory grade accredidation works
Analytical balanceDenver InstrumentsModel M-2201, or any analytical balance that has sub-milligram capabilities
Dram vialsVWR2 dram, 4 dram, and 6 dram vials 
MicropipettesEppendorf2-20 μL and 100-1000 μL micropipettes work
Glass pipettesVWRAny other instrument scientific company provider works
GC-MSShimadzu GCSoftware associated: GC Real Time Analysis
GC vialsVWRAny other providing company works
BeakersPyrex500 mL beakers 
Syringe pumpsSigma AldrichTeledyne Isco Model 500D
Relief valveSwagelokSpring loaded relieve valve 
One-way valvesNupro 10 psi grade
Two-way straight valvesHiP15,000 psi grade

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Diphenyldiazomethane ReactionBatch to Flow TransferUV VIS SpectroscopySyringe Pump SetupFlow Reactor SystemReaction Kinetics AnalysisTemperature Control MixingChemical Process Scaling

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