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Tuesday 9 May 2023

Common Organic Functional Group Derivatives that Facilitate Work-up, Separation, and Purification

 


The most common functional groups in organic molecules all have some reversible derivatives that exhibit acidic, basic, or heavy metal complexing properties.

 

  • The alcohol group can be converted into an O-sulfate that is acidic. 
  • The ketone group can be converted into an oxime that is acidic. 
  • The carboxylic acid ester can be converted into an acylhydrazide which is milldly  basic and forms stable isolable complexes with heavy metals.


When these common functionalities are present in a reaction starting material but the planned transformation is occurring elsewhere in the molecule replacing alcohol, ketone or ester group respectively with O-sulfate, oxime or acylhydrazide often would make no difference at the reaction site but would facilitate the isolation of product from the subsequent reaction mixture. 

Perhaps the reason it is not done is because the potential interference of these derived functionalities is not so well understood while for the parent functions there is usually many precedents. Another reason is that the ease of work-up, separation, and purification is simply not considered sufficiently important to warrant special facilitation.

Testing Catalysts and Inhibitors to Change the Ratio of a Desired Product and an Undesired Coproduct


Suppose you are working with a reaction step that is providing, rather cleanly, a mixture of two products-- the desired one and an undesired byproduct. Perhaps modifications of conditions are not beneficially changing this product ratio. Perhaps a change in the relative rates of the reactions that give rise to these two compounds can be changed to change the final product ratio. Below is a list of molecules that in more than one instance have been found to either speed up a desired reaction or slow down an undesirable one: 

HMPA, water, N,N-dimethylformamide, N,N,N’,N’-tetramethylurea, urea, dimethylsulfoxide, pyridine oxide, 2-pyridone, N-methyl-2- pyridone, polyethylene glycols, DDQ, an HMPA equivalent covalently attached to a tertiary amine for extractive removal, antioxidants, dimethylformamide acetals, 4-dimethylaminopyridine, DBN, DBU,  beta glycine, EDTA, transition metal salts,  phase transfer catalysts.

For any particular reaction, most of these additives will have no impact at all on the reaction you are trying to improve. When one of them does exert its effect it can be expected to be effective at low concentrations. For that reason, they can be tested at low concentrations and for this same reason, groups of them can likely be tested as a small group.  Any small packet of these additives should be chosen so they do not belong to the same general types. If a group of additives shows some activity in changing the important products ratio only then do experiments need to be done to deconvolute the group to discover which cause the improvement.

When trying to improve a procedure, improving a method using an additive needs to be considered as much as completely replacing that reaction. 



Acid Traps & Acid Acceptors for Use in Organic Reactions to Remove any strongly Acidic Coproduct

 

If a chemical reaction produces as a co-product a small strongly-acidic molecule, the equilibrium of that reaction can be disturbed towards a more complete reaction by trapping that coproduct. The following agents have potential to do this:


Pyridine

2,6-Lutidine

2,6-Di-t-butylpyridine

Poly4-vinylpyridines

Urea

Tetramethylurea

Acetamide forms HBr complex the is insoluble in many organic solvents

Magnesium oxide

Sodium acetate

Calcium carbonate

Mercuric oxide

Ammonium  acetate

Ammonium formate

1,2-epoxy-3-phenoxypropane

Ethylene oxide

Propylene oxide

Epichlorohydrin

Ethylenediamine

Pentamethylpiperidine

1,8-Bis-dimethylamino-naphthalene (proton sponge)

Hexamethyldisiloxane

Trimethylsilyltrifluoroacetamide

Trimethylsilylurethane

4A Molecular sieves

Pyridine ion-exchange resin

Amino Acid Hydrochlorides to Give Zwitterions

N-alkyl-2 halopyridines, formamide acetals, 4A Molecular sieves

Silver oxide

Lead Hydroxide from Acetate: neutralizes acid and gives insoluble salts


Acid acceptors and acid traps typically neutralize or otherwise deactivate acid that is already present and most often that has been created as a coproduct in a reaction. By ‘tying up’ any acid co-product any reversible reaction that involves it is driven to completion and prevented from reversing in accordance with Le Chatelier’s Principle.


Typically acid traps are not bases themselves although all that is essential is that they be substantially less nucleophilic than the moiety that is required to be the nucleophile in the planned transformation. If the nucleophile which is the hoped-for participant in the chemical reaction is readily available and inexpensive the same species can serve in appropriate quantity both as nucleophile and acid trapping agent.


Sometimes the reaction that forms the acid co-product does not involve any nucleophile. Free-radical bromination comes to mind. In this instance, the acid trap must be not nucleophilic at all because it is going to be the strongest Lewis base in the mixture. A substance that forms an insoluble adduct, or which itself is insoluble, or which constitutes a separate phase or which irreversibly reacts with the acid is desirable. Proton sponge, pentamethylpiperidine, urea, N,N,N',N’-tetramethylurea, 2,6-di-t-butylpyridine are not nucleophilic.  Magnesium oxide and calcium carbonate are insoluble in organic solvents. Ammonium acetate and ammonium formate are inorganic neutralizing salts that are volatile and so can be pumped away under a vacuum. The four epoxide agents react with acid halides by opening to halohydrins. 

Hexamethyldisiloxane, trimethylsilyltrifluoroacetamide, and trimethylsilylurethane convert free hydrogen halide into trimethylsilylhalide. For this reason, they must be used in sufficient quantity to persilylate any other reactive functional groups in the molecules. Molecular sieves and basic ion exchange resins work by taking free acid into a different phase.


I have used a slightly different idea to remove excess HBr in a process step developed during my industrial career. I added t-butanol to my reaction. It rapidly reacted with HBr as it was formed giving water and non-acidic t-butylbromide.


Glycerol: A Possibly General Method for Changing Solvents in Process Chemistry Reactors



The reaction solvent is distilled out of the reactor chased by the minimal stirrable volume of glycerol.


Since neither acetone nor methylene chloride are miscible with glycerol and they do not form any binary azeotrope:


 (i) A mixture of some useful proportion of acetone and methylene chloride is used to extract the non-volatile substrate. Cut away the glycerol phase.


or (ii) the desired second solvent, if it is immiscible with glycerin, is used to extract the non-volatile substrate. Cut away the glycerol phase.


Then


If (i) above is used, distill the methylene chloride away from the acetone leaving an acetone solution.


If (ii ) above is used, then wash the desired second solvent solution with water or brine to remove traces of glycerin.


Then


If (i)  above have been followed, add the new second solvent and distill away the lower boiling acetone (almost all solvents are higher boiling than acetone). If this second solvent is to be both protic and miscible with water, residual glycerol needs to have been removed at the stage of the acetone-methylene chloride extract by passing it through a plug of silica or alumina. 


Thursday 4 May 2023

Improving Phase Separation for Extractions in the Presence of Insoluble Debris




Patent US 5,628,906 explains how to perform rapid liquid-liquid extractive separations in unfavorable situations where there is insoluble debris in the liquid mixture or where there are emulsifying substances present that under vigorous agitation could create emulsions that separate only slowly.

The creative idea is to mix two solvents that are fairly miscible to form a superior extractant medium and then subsequently add a third component that causes rapid separation of the total combined solvents into two immiscible phases that can be easily separated. In this way, any surface active agents do not have time to move to the interfacial area and reduce the rate of phase separation, the debris that is insoluble does not float at the interface and prevent separation and the rate of transfer of substrates between phases is much enhanced.

The method might be applicable to removing traces of product from a reactor containing insoluble resins by separating the substrates from the surface and interstices of the resin and it could avoid vigorous stirring of the resin slurry that could mechanically damage the resin.

Might it also work in an emulsifier-promoted reaction between a water/acetonitrile solution containing an emulsifier that is reacted with a poorly soluble reagent followed by a phase separation wherein a third solvent that causes phase separation is added? Imagine for example that you are trying to convert cis-cyclooctene into cis-1,2-cyclooctanediol with potassium permanganate reagent.  This would be advantageous because the classical reagent osmium tetroxide is both expensive and toxic.

The problem is that although the substrate is soluble in organic solvents the permanganate salt is not. A mixture of acetonitrile to assist in the solution of substrate and water to get some permanganate into solution could be emulsified with an unreactive emulsifier to bring them pair into intimate contact so they could react. Then addition of a third solvent miscible with acetonitrile but immiscible with water would break the emulsion and cause the separation of two phases despite the presence of the emulsifier. No shaking of the phases together would be required. The potential for a large interfacial layer would be greatly reduced. Because it might also enable the extraction of a water-rich phase with a water-poor phase without first requiring the separation of a precipitate insoluble in both phases, the coproduct, manganese dioxide would be less likely to interfere with phase separation.  



Order of Addition and Other Variables in the Crystallizing or Precipitating Organic Ions as Salts


There are a variety of protocols available for bringing the particular cation and particular anion together that are expected to form a salt that either advantageously crystallizes or precipitates.

Mixing a Stoichiometric Ratio of Acid and Base in a Solvent and:

  1. Cooling to a lower temperature
  2. Adding a miscible anti-solvent or condensed soluble gas
  3. Adding an immiscible  or partially miscible anti-solvent
  4. Drowning out in a miscible anti-solvent
  5. Slowly adjusting the pH
  6. Use of the common ion effect to decrease the salt’s solubility
  7. Evaporating to dryness

The Above is the Most Direct and Obvious but there are Other Methods of Formation


1.   Exchange of Ammonium Salt with Nonvolatile Metal Chloride

Exchange an ammonium cation for a different but non-volatile cation selected to create a more insoluble salt of an organic anion and as a coproduct volatile/soluble ammonium chloride.

  1. Exchange of formate/acetate/trifluoroacetate/thiocyanate Salt with a Non-volatile Acid

    These four anions have volatile protonated forms. If a     salt of one of these acids is mixed with an organic acid and evaporated to dryness the formic acid, acetic acid, trifluoracetic acid or thiocyanic acid will be driven off leaving a residue of the desired salt.

  1. Double Decomposition Reactions

Metathetical reactions between a salt solubilized by the presence of a particular cation and a salt solubilized by the presence of a particular anion to give an insoluble and a soluble salt from which the insoluble salt is recovered by filtration and washing.  The use of metal salts of 2-ethyl hexanoic acid for the basification of organic acids is an example.

Methods for Mixing

  1. Direct addition

Addition of a solution of the salt-forming acid or base slowly into a solution or slurry of the product whose salt is sought.

  1. Inverse addition

Addition of the salt-capable species, either as a solid or as a solution into at least a full equivalent quantity of the salt-forming reagent.

  1. Slow addition of poorly soluble neutral species by extraction

Extraction of the salt-capable species from a Soxhlet extractor by hot solvent and quench of the extracted species by an excess of the salt-forming reagent in the boiler of the extraction apparatus.

  1. Impinging Streams of Salt Solution and Anti-solvent

  This is a simultaneous mixing that gives small crystals    that avoids any grinding step to control crystal size

  1. Impinging Streams of Acid and Base

    This is a simultaneous mixing that gives small crystals that avoids any grinding step to control crystal size  In this situation the neutralizing reaction occurs in the impinging streams.


Methods for Precipitating Salts

  1. Crystallization by Diffusion of an Ant-Solvent

Dissolution of the salt in some solvent composition in which it is soluble followed by the addition of a partially immiscible anti-solvent creating two phases wherein the salt is soluble in neither. An example is to dissolve a compound in acetonitrile and then layer it with hexane. Some hexane migrates into the acetonitrile causing crystallization.

  1. Partial Evaporation of a Single Volatile Solvent

  The classical method: The components are dissolved in a    volatile solvent and the solvent volume is reduced either by boiling or slowly by evaporation.

  1. Lyophilization/Inorganic Salt Removal

Lyophilization (freeze drying) of a solution. Dissolution in methanol and filtration to remove inorganic salts.

  1. Slurry to Slurry

The transformation from a slurry of the slightly soluble pharmaceutical acid or base candidate into a slurry of the desired salt form until a method of solution analysis shows equilibrium.

  1. Precipitation by pH Adjustment

The dissolving of the pharmaceutical candidate in a partially aqueous solution is followed by the adjustment of the pH gradually by the hydrolysis of a solution component. For example, methyl acetate and base to give acetate and methanol; ethyl carbamate and acid giving ammonia, carbon dioxide, and ethanol.

  1. Solvent Expansion

Dissolving the pharmaceutical salt or making the pharmaceutical salt in solution and then exposing the solution to a volatile anti-solvent so that the composition slowly becomes more insoluble.

  7. Evaporative Precipitation

 
Dissolving the pharmaceutical salt in a mixed solvent of a less volatile poorer solvent and a more volatile better solvent and then removing the better solvent by distillation.


Process Troubleshooting in Plant and Pilot Plant

 

In the laboratory, some experiments give encouraging results; other results are discouraging. None of these are ‘trouble’ because according to KiloMentor’s definition, ‘trouble’ is an undesired deviation from what was expected that occurs on scale. Undesirable deviations on-scale cost significant money and there is invariably immediate managerial pressure to quickly assign a cause.

 Deviations in quality and quantity are most common. ‘Trouble’ leads to a higher-than-expected cost of goods. That can be fixed by fixing the deviation that caused it or by making other compensating changes rather than fixing the deviation. The former is sometimes the easier course of action.  For example, costs can be reduced by removing a bottleneck in a process to reduce equipment and labor costs rather than fixing a deviation in a reaction yield.

 When talking about deviations we can distinguish two subtypes. 

What I would call a Type 1 deviation is a deviation from a result that has been actually achieved already and that you are trying to reproduce by repeating the protocol exactly, but where the outcome is found to be significantly different. For example, you are repeating a procedure identically, at the same scale, but your outcome is significantly inferior.


What I would call a Type 2 deviation is a deviation from a prior result after making at least one change that one expected and hoped would not affect the result in any deleterious way. It is a deviation from a predicted outcome. For example, using a laboratory protocol you run the procedure in the pilot plant as much the same as possible, predicting a similar quality and yield, but the result is significantly worse. 

Often, established processes are subjected to reevaluation and improvement efforts because even a small yield improvement can lead to a significant financial benefit. In an effort to reduce operating costs, less expensive grades of reagents, solvents, or processing aids are employed and the impurities in these reaction components can have an adverse effect on processing leading to deviations in quality that are deviation from the hoped-for result of no change in quality. If these preliminary experiments are done at laboratory scale, an unfavorable result is a disappointment but is not ‘trouble’ but if the change was accidental or unintentional and was made at scale it is a type 2 variant of ‘trouble’. 

Type 2 deviations also arise in the initial runs of scale-up. Deviations from a hypothetical result may not be deviations at all. The hypothesis that the cases are sufficiently similar to give the same result may be simply wrong. But if we can do something to restore the wished-for expectations it will be wonderful.

Troubleshooting

Troubleshooting is problem-solving under the gun and at scale.

When Trouble happens and you are called to help, treat it as an emergency; act appropriately. Your value to an organization is likely to be assessed predominantly by your skill at troubleshooting when Trouble comes. 

If the trouble stops processing, if possible do not go home until the blockage is removed. Take temporary ownership of the trouble, even if it probably isn’t your fault; assigning blame is not a priority in troubleshooting rather it gets in the way of effective action.  

The most common emergency is a failure in an in-process analytical test or a required observation. Processing, following the batch sheet, stops until a decision on how to proceed is made; you may be required to provide input to that decision. In most instances before applying problem-solving methods to a deviation make sure the deviation is real. Check the analytical method and redo the analysis. Can one confirm the deviation using an alternative analytic methodology? Nothing is more frustrating than trying to find the cause of an unexpected deviation that actually does not exist.

The most frequent error in troubleshooting is called ‘jumping to cause’.  A hypothesis that might explain the deviation comes to mind and immediately the troubleshooters jump into action to test the hypothesis. Only after the hypothesis is proven false and the deviation is not corrected do the scientists consider other hypotheses.  The correct mental process or group protocol is to quickly gather information about the deviating batch and the conforming prior experiments.  Write down in a table form what the deviation is and what it is not. Asking WHAT, WHERE, WHEN, HOW and WHEN NOT, WHERE NOT, WHAT NOT and HOW NOT.  Then construct as many hypotheses fitting with everything that is being observed as one can. Ask whether the hypotheses fit what is known about the problem. Rank the hypotheses from the most probable cause to the least probable.

When there are many hypotheses, the best strategy initially is to combine several changes that are unlikely to have interactions among themselves so that the deviation would be corrected if any one of the changes is the deviation’s cause.  Ordinarily, it is not scientifically preferred to change more than one thing at a time, but here, where a number of the corrective actions can be predicted on the basis of their mode of action to be beneficial or have no effect at all, with no possibility of a negative result, several remediations can be combined.  If the unsatisfactory deviation remains after this trial most likely all the hypotheses combined in the test were untrue. The true cause is probably among the remaining untested hypotheses. 

Often it may be difficult to assign a most probable cause or give a preference to one hypothesis over another. In this situation, one should prefer to test first the hypotheses that are easiest to fix.

When starting a troubleshooting investigation no-one knows how long it will be before the deviation can be corrected.  Often measures are started immediately and in parallel to develop what is called a patch. A patch is an additional step inserted in the process scheme usually to purify off–spec material so that it can be used to carry out further steps of the synthesis.  A patch has value even if it does not need to be used (such as when the cause of the deviation is quickly found), because that patch may be used in the future if a different problem arises. The patch constitutes new purification knowledge about the intermediate. No knowledge is wasted. Developing a patch is insurance. Some deviations are not easily amenable to a patch. When the deviation stops the process completely and prevents one from obtaining any product, even a product of reduced purity, there is nothing to purify further. An emulsion or the complete failure of a solid intermediate to crystallize are examples of deviations that halt processing.

The cause of a deviation may have been hidden by a team member to avoid blame.  Batch records only report what operators 'say' happened. It is possible that a mistake was recognized by operators almost immediately when it occurred, but it was irreversible. It may have been hidden in preparing the batch record. This makes the troubleshooter’s job harder but it is part of human nature and comes with the territory. Operator errors are most likely if some of the operators are replacements for regular workers. In examining a deviation the questions of who and who not needs to be addressed with reference to the operators who conduct the process. Analytical results are almost always generated automatically and overseen by analysts, not operators.  The analytic data are therefore more tamper-proof. 

During scale up there should be many more samples taken than after the process is well established. In the early scale-up stage testing should be planned and carried out at as many different points as possible throughout the processing. The samples should be stabilized and saved for later analysis in case there is a deviation.  These I call forensic samples.  They need not be even looked at when the scale-up experiment goes as expected. At any point in the process step where (i) the mixture is a homogeneous phase and (ii)where the sample will not likely degrade over time under normal storage conditions, consider taking a large enough sample both for analytic testing and also to allow one to continue the processing in the laboratory to see whether the deviation has occurred before or after the sampling point.

When a process step has been finalized and is part of regular production, taking forensic samples can stop. Only retain those that are the in-process checks.  It is true that now if one experiences a new deviation one no longer has these forensic samples to help track it down, but one has the advantage of knowing that since successful runs have preceded this new deviation, the deviation is a real difference from prior practice not just a deviation from one’s expectations based on laboratory results.


Potential Recrystallization from a Thermotropic Azeotropic Composition: One that Forms Two Phases upon Cooling



The most common property of solvents used for crystallizing/recrystallizing solid substrates is that they dissolve a larger quantity of solid when hot than when cooled and this extra solid very often comes out of solution as crystals.


Binary mixtures of solvents also exhibit this widespread property; more solid is soluble in them hot than cold.


But now suppose that in some instances the mixture of hot solvents that is being used to recrystallize some solid splits into two distinct and separate phases upon cooling? Do crystals still appear? Does more solid crystallize than might be expected from a non-thermotropic solvent? Do the two liquid phases have any distinguishable effect on the crystal form, the crystal size, the crystal purity, or the ease of filtration?


These answers are not known even for isolated cases. The answers would depend upon the particular binary solvent system and the particular substrate to which the treatment is applied. What is very likely is that unless a very substantial solvent-to-solute ratio is required to get a complete dissolution of the substrate no phase separation at all will appear upon cooling. The method might need to be applied only to poorly soluble substrates.


But if two liquid phases still separated, I can imagine two distinct situations. 


In the first of these, the substrate is much more soluble in one of the compositions into which the hot thermotropic azeotrope splits than in the azeotrope itself. In this situation, some solid may separate but there is less likelihood of any special enhancement in the recovery.


In the second situation, neither of the new liquid compositions turns out to be superior to the composition of the thermotropic azeotrope even at identical temperatures. Unexpectedly enhanced recoveries may be possible.


In both these outcomes having two different fluid components in intimate contact with the solid during crystal formation and crystal growth stages may give rise to different crystal morphologies or different rates of formation.


Let us as, an exercise, consider a specific binary azeotrope. I propose we look at the lower-boiling, thermotropic azeotropic composition between hexane and methanol. It is an azeotrope combining very non-polar hexane and the much more polar methanol. In this situation, let us further specify that the substrate is not particularly soluble in either hexane or methanol alone. It is most compatible with a mixture of the solvents that perhaps provides a low-energy solvation for an apolar domain and a different more polar domain. But the hot azeotropic composition and the two-component compositions into which the thermotrop splits are all mixtures of methanol and hexane. The thermotrop is 73.1% hexane and 26.9% methanol by volume. The two fluids existing at lower temperatures are 85% hexane/ 15% methanol and 42% hexane/ 58% methanol.


When the temperature is reduced the overall solubilizing capacity will most often be lowered as the temperature effect is likely dominant. At the same time, two phases will be created; one a less polar and the other a more polar one. Neither phase will be anywhere near pure hydrocarbon or pure alcohol, however. The total volume of the two phases taken together will be more or less unchanged.


In my example, if the hexane-methanol separates on cooling the composition of the upper layer will be 85% hexane and 15% methanol with specific gravity of 0.675. The composition of the lower layer will be 42% hexane and 58% methanol with a specific gravity of 0.724 and there will be, by volume, 68% upper phase and 32% lower phase. In the single-phase azeotrope, there will be 73.1% hexane and 26.9% methanol by volume.


The most probable result is that the overall solubility decrease for the main substrate may be not much different than if the solvent had remained homogeneous. Impurities, however, whether very apolar or very polar are likely to migrate substantially to the more polar or less polar phase and stay in solution more than otherwise. The effect might be similar to washing a seriously apolar solid with a little methanol or washing a distinctly polar molecule with a hydrocarbon. The main difference might be that the demixing can be expected to proceed more quickly because everything is in solution.


There could also be a difference in the rate of crystallization. Crystallization depends both upon a nucleation event and a crystal growth event. The rate of crystal nucleation is a function of the solvent composition as is the rate of crystal growth. With the dissolved solute in both liquid phases, there is an increased chance for a satisfactory nucleation rate and a crystal growth rate because there are two available environments for nucleation and two environments for possible crystal growth. 


What this is suggesting is that if a solid presents difficulties forming crystals trying an azeotropic thermotropic solvent mixture might prove advantageous.


A solid with a tendency to oil out before crystallizing might produce a better physical form when crystals form from such an azeotropic thermotropic composition where the crystallization could proceed within droplets of one solvent composition suspended in the other. 

Organic Chemical Process Development



Creating a process to synthesize an organic compound at plant scale has several iterations. The guidelines vague as they are, differ depending upon the iteration within which you are operating.  Since the molecule is to be made at scale, next to safety cost is the foremost consideration.


Route Scouting


The first iteration is termed route scouting. At this stage, you know the structure of your target molecule. This means that it has already been synthesized if the molecule is novel and not naturally occurring. Therefore, an original sequence of reactions exists but if the exploration was part of a wider screening study the route was not selected with this molecule alone in mind but rather for a family of molecules of which this molecule was a member. 


If the molecule is a natural product and has been isolated from a natural source there is most likely no route at all.


Route scouting comprises two different activities. One is what is called ‘paper chemistry’. No laboratory is required- just paper, pencil, and in this computer age, appropriate database permissions. The second activity actually tries to conduct the experiments most promoted by the ‘paper’ search activity. Although some ‘paper chemistry’ needs to be done before laboratory experiments begin, it is most common that  ‘paper chemistry’ proceeds first and then continues even as the early ideas are tested in the lab.  


Paper Scouting


Route scouting of the ’paper’ variety is directed by clues that are found within the unique structure of the target molecule. The task is to take substances that can be bought or simply made by well-established paths and combine these in such a way that the target structure is constructed.


Chemical complexity cannot be usefully quantified, yet it is readily ranked intuitively by the experienced synthetic chemist. What is important to recognize at this scouting stage is that the complexity of commercial product offerings available as starting points is not proportional to price. That is to say, more complex chemical structures do not necessarily cost more than less complex ones. As a consequence, the structures chosen as starting materials matter a lot! Mapping substructures of the target molecule onto available inexpensive starting materials is one very useful exercise in paper chemistry that proceeds as part of route scouting.


An obvious example is the establishment of absolute chirality at a center in the target by incorporating a starting material sub-structure that already possesses that required chirality. The similarities of ring structure or substitution pattern between starting materials and products can similarly be useful.


Because no person can retain in memory all the different potential starting materials and their respective prices, this type of screening can only be done by computer search.


Retrosynthetic Routes


Retrosynthetic analysis is a product structure-based methodology for assembling promising ‘paper’ syntheses in route scouting. Retrosynthetic analysis was pioneered by Professor E. J. Corey. The method examines the target structure looking for bonds whose breaking leads to the largest reduction in structural complexity. The method uses the clues provided by the functionality already present n the target to rank the promise of these disconnections. The bond breaking must be done in accordance with the teachings of known chemical reaction transformations and preferably be compatible with the functionality already displayed by the target molecule.

Most preferably, the disconnections should lead towards the more preferred starting materials identified in the starting material-based searching.


The Service Synthesis Route


Throughout the development of an industrially suitable process for preparing a target structure, the other departments of the organization seeking to manufacture the target will have recurring needs for fresh supplies of the target compound for their own studies. These needs come from formulation, regulatory, sales …so many other departments. At first, their requests are modest but the amounts each is likely to need escalate as the proposed launch date for the product comes closer. These requirements must be met by the synthesis department making fresh product by what can be called the ‘service route’. The service route of synthesis evolves from the discovery route; the method by which the molecule was first prepared. It is the discovery route pragmatically adapted with go-arounds for aspects of the original method that could not be practiced as the scale increased. Removing steps that could not be scaled such as those requiring column chromatography, for example, or operations that were less safe in larger equipment or that could not be done at all. Nevertheless, the service route remains as close as possible to the discovery process to minimize the need for new chemical explorations.

Still at the outset of the entire project, a judgment has usually been made whether the benefits of a total rethink of the synthesis of the target involving starting material-based analysis and retro-synthetic analysis will be able to provide sufficient advantages to be eventually preferred over the evolving service route.


The service route will invariably retain certain advantages. It will become very familiar to operators. It will retain the closest impurity profile to the target. There will be more opportunities to improve the work-up, isolation and purifications of the steps in the service route with no additional research cost born by the synthesis department. The employees that are assigned to operating the service route will gain the most inter-silo integration with other company departments.


Still, the starting material based and the retrosynthetic-based routes will have their own advantages. The service route is least likely to improve costs. Expensive inputs are less likely to be replaced. Certain types of hazards are less likely to be addressed. 

_________________________________________________________________


Because highly trained employees will be doing the work, safety, and toxicity hazards are more likely to be mitigated rather than avoided. Actual reaction optimization is unlikely to be advanced. Changes that could actually lose batches of material will not be risked. Remember the primary function of the service route is to provide promised amounts of product by promised dates. Regulatory concerns such as genotoxicity do not matter. A route created according to either the starting material-based or retrosynthetically based approaches may lead to patenting that is stronger and last longer than just obvious workman-like improvements in the discovery synthesis route.


The Ultimate Process Route


So substantial are the advantages of the discovery/service route that the final process is very likely to at least in part to follow it. Very often the starting material-based route and the retrosynthetic analysis may lead to solutions that provide alternate solutions for some of the unavoidable problems that existed in the service route. Certain steps may be totally replaced or reordered applying insights born in the ‘paper chemistry’ that comprised these analyses. Because these analyses from first principles are so much more cost focussed and less risk-averse these approaches are more likely to find major improvements.


Route Optimization


Route optimization takes the ultimate process route and without changing

the chemical transformations improves the overall yield or throughput while maintaining the quality. Although the stage is called optimization, optimization is a gross exaggeration of what is done. In fact, a team tries to make improvements until either it runs out of time or the value of its improvements is judged to be inferior to the benefit from alternative deployment of the scientific resources (ie. the people are reassigned to other projects).


The improvement that is being sought is just one thing— lower cost. The goal is the profitability of the corporation. Since this is so, the improvement priorities are established by the individual contributions to the overall cost of the product, and for this, the costing sheet is the guide.

Costs fall into categories of substrates (starting materials), reagents (reactants not incorporated into the product),  and the twin efficiencies of assay yield and isolation yield. Categories are only useful if they provide a guide for action.


Starting materials cannot be changed but inferior grades of the same material which have a lower price can be tested. Sometimes a lower grade has equivalent performance or its reduced performance costs less than the monetary savings. The changed starting material must not cause undesirable changes for subsequent steps but most importantly, the change must not degrade the quality of the fill product of the entire process. Changes in the quality of starting materials are most often without consequences in the early reaction steps that are most removed from the target molecule.


Reagents are here defined as reactants that do not significantly supply atoms for the assembly of the target molecule. Reagents can be substituted and their quality varied. Changing reagents usually requires many other changes in the chemical transformation. The operation that is executed on the intermediate is maintained but the tool that is used gets substituted and all the reaction conditions change with it. Not only the reaction conditions have changed but the workup, separation, and often the purification of the intermediate product change. The reaction assay yield and the isolation yield will both change as must the step's overall yield.  To justify so much fresh experimentation the cost saving must be prominent. Because of the inherent risk of a change in final product quality analysis, such an improvement should be closer to the beginning of the reaction sequence.


Reagent changes often are instead part of the service procedure development. 


The overall yield fraction is the product of assay yield and isolation yield. This division of the overall yield into its components is rarely worked out during the setting of the ultimate process route but it is necessary for the efficient improvement of the steps. There is little to be gained by making changes in an area where the yield efficiency is already high. In the same way that the costing sheet should prioritize the above types of change, the determination of all of the assay and isolation yield prioritize the efforts at yield improvement.


Yield improvements in the reactions closer to the final product give rise to the greatest improvement in costs since an improvement reduces the amounts of reactants, reagents, equipment, labour, and other chemical processing costs in all of the prior steps. Improvements in the assay yields of these steps occur with concurrent reductions in residual starting materials and byproducts. This tends to improve product quality. Improvements in isolation yields often are accompanied by trapping more impurities in the isolated intermediate leading to lower purity in the final product. Improvements in isolation need to be changed in the mode of isolation and purification rather than just trying to up the recovery. A more rugged method of isolation can be expected to improve recovery yield while maintaining quality.


A Wider Range of Optimization Options


Because improvements in the yields of the late-stage steps have such a magnified influence on the overall cost, the range of options for achieving an improvement is enlarged. A more costly reagent that improves the yield somewhat is more easily made up for by the cascade of savings in the earlier steps. Increases in maximum storable volume that decrease the throughput of the overall process are easily compensated by the overall savings from a yield improvement. Thus higher dilutions and bulkier reagents become practicable. For example, steam distillation as a separation tool or polymer-supported reagents become more realistic.


The Importance of Phase-Switches and ‘Setting’ the Late-Stage Steps


Purifications require phase switches. Purification is effected when the desired substance makes it through a phase-switch more readily than the panoply of impurities. But phase-switches can be part of work-ups and isolations as well as purifications. The more phase-switches a compound negotiates the more dependable the degree of purification. There are many phase switches: crystallization, distillation, sublimation, dissolution, liquid-liquid extraction, adsorption, precipitation, and co-distillation …. The phase-switching that is built into the ultimate and penultimate steps of a reaction sequence is very important to the final quality of the target product. Therefore, the sooner in-process development patches are ‘set’ and no longer modified, the more likely that your final product will be identical to the samples submitted to potential customers and government regulators and to the batches of material that went into any clinical trials.


Pilot Plant Responsibilities


Besides process improvements, process optimization chemists are usually responsible for:


Forensic pilot plant sampling

In-process assays

Stopping points/ stability studies

Process equipment corrosion studies

Filtration flow rates

Special cleaning recommendations

Timing requirements (addition and transfer rates)

Minimum and maximum volume limits



These special topics are discussed in the final report that is the transmission document that transfers everything that is useful for the pilot plant personnel to know from the process development team.


InProcess assays


In-process assays are assays (usually quantitative tests) that are part of a batch sheet. They are performed by the analytical personnel from the analytical department. These results form the basis for decisions by the pilot plant and at a later stage the plant management about how to proceed in further executing the batch sheet. In-process assays are essential for executing the batch sheet which instructs the process step.


Forensic pilot plant sampling


Forensic pilot plant sampling is only part of a pilot plant batch sheet. Samples are taken at the prior, planned request of the process development chemists. They are taken by the pilot plant operators according to instructions in the pilot plant batch sheet and saved for the requesting scientists. Forensic pilot plant sampling normally never becomes part of the final process master batch sheet, because the purpose of these samples is to help the development team figure out what went wrong if either the expected yield or product purity fails. Once a pilot plant experiment is reported as being completely successful, these forensic samples are discarded by the scientists who requested them.

A pilot plant run is an expensive experiment. It qualifies as an experiment because no matter how many precautions are taken in advance the scale-up from laboratory to pilot plant scale involves risks that cannot be fully mitigated. Because it is too costly to repeat unnecessarily, the scientists responsible need to take whatever samples they might need to answer any question about what might have gone wrong at any stage in the experiment. The samples must be taken proactively- as a precaution in case a problem occurs.


By the way, remember process development chemists are visitors to the pilot plant (and the plant). They are observers only. They do not do anything. Neither do they instruct the operators.  They can take notes for their own purposes. They can converse with the person managing the execution of the batch sheet. That is all!


Stopping Points/Stability Studies


At many points in chemical processing, chemical instability makes it essential to continue moving through the instructions in the batch sheet. Executing most batch sheets extends longer than 24 hours, however, and many pilot plants or even plant facilities do not operate around the clock, so it is useful for there to be tested advice on where the processing can be stopped and for how long that interruption can safely last. To that end, development chemists need to record at what points they have safely stopped processing. 


Process Equipment Corrosion Studies


A rare but disastrous risk is that a chemical processing step will damage the chemical reactor, usually by corrosion of the reactor walls. The process development chemist needs to test whether this could occur. This is done by placing tared sample tiles of the reactor’s construction material in contact with the reaction mixture during the reaction period. This is normally done by attaching the tiles to some structure within the reactor that contacts the reaction mixture. When the processing is complete the tiles are recovered and weighed to see whether any material has been removed from them or any weight added.