CHAPTER 13

EziG: A Universal Platform for Enzyme Immobilisation

KARIM ENGELMARK CASSIMJEE* AND HANS-JÜRGEN FEDERSEL*

EnginZyme AB, Teknikringen 38A, 114 28 Stockholm, Sweden

*E-mail karim@enginzyme.comhans-jurgen@enginzyme.com

13.1 Introduction

EnginZyme is a Swedish biocatalysis company founded in 2014 by a group of academics and entrepreneurs with backgrounds in both chemistry and business. The key rationale in forming the company was the enormous potential for further greening the chemical industry and the identification of biocatalysis as an essential technology in that transition. To increase the use of biocatalysis, i.e., the use of enzymes as catalysts in chemical synthesis, EnginZyme aims to produce products that simplify the employment of enzymes in industrial processes while also reducing costs. In our view, economic soundness is imperative, as the motivation of reducing the environmental impact alone is not sufficient to grow the biocatalysis market.

The use of biocatalysis is expanding in the industry,14 but the technique is still mainly utilised for reactions in which classical catalysts are suboptimal in terms of performance or cost. Since living cells perform a plethora of reactions to uphold life, and enzymes catalyse virtually all of these, one might assume that enzymes can also serve as catalysts for all the reactions needed in the modern chemical industry. The current technology level, however, precludes a general or universal method for catalysis. To achieve that, in practical terms, all the needed enzymes would have to be suited for use in large scale processes, and engineering to produce variants of enzymes to perform needed reactions must be possible. This quest can be viewed as futile, yet we do not see it as an unreachable goal, but rather as a matter of persistent technological development.

Most enzymes in industrial use today are inexpensive and represent only minor components of overall process costs.5 They are produced in substantial volumes, since their applications include high volume processes6 and consequently have a high-volume demand, which results in a low cost per mass unit. Technological developments that further lower the cost of these enzymes are of marginal importance to the industry.

However, the enzymes used represent only a small fraction of the available enzyme types in nature. One can reach this conclusion without access to any concrete numbers, simply by comparing the number of commercially available enzymes to the number of enzymes present in living cells. Most enzymes are sold in small volumes at high-cost; or, for the most part, are not produced commercially at all. Additionally, engineered variants7 of enzymes suited for specific target processes are more expensive by several orders of magnitude. Even if such variant enzymes were to reach an acceptable cost level once they are made available, their development times and costs are still too great for widespread industrial acceptance.8 These engineering projects are often demanding due to the high catalytic activity needed to yield a low amount of the expensive enzyme in the final process, while meeting requirements for cost efficiency.9 In pharmaceutical process development, it becomes a formidable and sometimes impossible task to deliver a desired engineered enzyme within the required time limit.10

At the process scale, enzymes are normally used as crude preparations of cell extracts or whole cells from overexpression in recombinant bacterial protein production strains. Necessary cost reduction is achieved by minimising the steps required from fermentation to usable catalyst, omitting the isolation of the enzyme. The enzyme is only a fraction of the crude preparations – the rest, most often the majority, is native protein and other cellular components from the production strain. As a consequence, product isolation can become tedious and expensive, since emulsions are formed in work-up procedures and the native proteins may cause side reactions. Some of these disadvantages may be eliminated by using a purified enzyme preparation, but enzyme purification frequently escalates the cost beyond the scope of cost-efficiency. As such, cost efficient and pure enzyme catalysts suitable for use in industrial settings are scarce.

For the reasons mentioned above, we see that the potential of using a variety of enzymes for very diverse applications is not being exploited in industry. To summarise, for each individual process, one or more of the following often applies: (1) the enzyme demand is not sufficiently large and, hence, its cost level remains unfavourably high, which is further reinforced by requests for only limited volumes of the desired product; (2) engineering of the enzyme to achieve higher catalytic activity, and thereby a sufficiently low catalyst loading for achieving an economic process, is not undertaken for time and cost reasons; and (3) the drawbacks of using crude preparations hinders implementation for technical reasons, and enzyme purification is too expensive for the given application.

There are also habitual reasons for choosing standard chemical catalysts. The current use of biocatalysis is not on a par with the possibilities the industry has already developed for process improvements, for which state-of-the-art technologies permit wider and economically sound employment. Still, we believe that the main barrier for increased use of biocatalysis in chemical production is the high cost of the enzymes and their high development costs compared to chemical catalysts.

The use of biocatalysis in a single process can result in a significantly reduced environmental impact, as can be seen by Pfizer’s implementation of a lipase enzyme in the manufacture of pregabalin (Lyrica®), for which, in terms of CO2 emissions, the company equates the reduction of waste and lowered energy requirements over two decades to removing a million cars off the road for a year.11 In this case, the biocatalytic route offers obvious advantages. Another example is the sitagliptin (Januvia™) production process, for which Merck uses an engineered transaminase enzyme to produce an enantiopure amine in the last chemical step.12 Despite the existence of these successful examples, the potential benefits of changing to biocatalysis become less obvious when an effective process with traditional catalysis already exists. Even if a suitable enzyme is available, the introduction of process changes and diversion from more common methods may be discouraging for the process designers. Therefore, the general benefits of the technique must be emphasised, namely that biocatalysts require lower energy (lower temperature and pressure) and produce less waste (less by-products, solvents, heavy-metal traces) than most traditional catalysts. Improved process economics can be achieved beyond the specific catalysed reaction as such, even when increased water consumption is taken into consideration as an environmental burden.

More widespread knowledge of the benefits associated with the increased use of enzymes need not be limited to a consequence of waste handling legislation and product purity demands, but can also be achieved by highlighting examples of simpler process development with biocatalysis that can be implemented by the industry. By taking a process designer’s view, EnginZyme aims to demonstrate how biocatalysis can be implemented in a facile and costeffective manner, primarily by designing products that enable enzymes to be used with standard equipment in an easy-to-handle and economic manner. This approach includes the use of flow chemistry, which is likely to increase in the pharmaceutical industry as a consequence of a shift towards economic and, from a regulatory standpoint, more feasible continuous manufacturing processes as encouraged by the U.S. Food and Drug Administration (FDA).13

We have developed a general enzyme immobilisation method capable of extracting and enriching any enzyme directly from a crude extract by using a material we call EziG™.1 By enabling enzyme reuse in a standardised manner and facilitating the implementation of flow chemistry with biocatalysis, EnginZyme hopes to accelerate the already growing use of biocatalysis for chiral compounds and enable its use for applications in which single-use enzyme catalysts are too costly for commercial exploitation.

Companies often set out a grand goal to define their strategy and general direction. EnginZyme’s strategic vision is expressed in the company slogan, “making biocatalysis your first choice”. The goal is for process designers and developers in chemical and pharmaceutical industries to stop seeing biocatalysis as a tool only useful for certain verified reactions (e.g. the production of enantiopure alcohols, esters or amines with lipase enzymes, or amine transaminases) or as a last resort when other methods have failed. On the contrary, we envision a future in which the use of enzymes in a broad range of what is defined as chemical production will be the process designer’s and engineer’s default option, whereby the technical development has led to outperformance of other catalytic methods.

13.2 A General Methodology for Enzyme Reuse

13.2.1 The Potential of Biocatalysis by Far Exceeds Its Current Exploitation

There are a handful of reaction types in which biocatalysis has been established as the method of choice in the formation of high value compounds. These include the production of enantiopure alcohols, amines and esters with lipases (alcohols, esters and amines), transaminases (amines) and ketone reductases (alcohols). A desired enantiomer can be produced by stereoselective synthesis or kinetic resolution, which in most cases gives an obvious economic and environmental benefit.2,4 Though these enzymes and synthesis methods are now relatively well established, there remain many potential cases where they are not used. An estimate by the company Codexis indicates that as much as 30% of the small molecule compounds handled by the pharmaceutical industry today would benefit from using biocatalysis.14 In all likelihood, the actual usage is much lower. The pharmaceutical industry may be leery of rapid changes, due in large part to tight regulations. Still, the economic drive to use enzymes in more processes should have already led to a drastic increase in the application of biocatalysis. What is the reason for the current situation? Arguably, lack of technical knowledge, a widespread unfamiliarity of the molecular features and mode of operation of enzymes, an inadequate technological toolbox, and a habit-driven reliance for the continued use of the vastly more established field of metal catalysis are all significant contributing factors. Nonetheless, and as stated above, we believe that the main barrier to the utilisation of biocatalysts is the high cost contribution of these species in general and their development cost compared to traditional catalysts. Additionally, though economic gain may often be achievable, investment in screening for a suitable enzyme variant is deterred by the uncertainty of the end result as applying high catalyst loadings of non-reusable preparations becomes a necessity.

If a reusable preparation could be assured, there are likely to be a plethora of industrial processes that could be performed under an enzyme catalysis regime in an economically sound manner for non-chiral or lower value products. Enzyme reuse requires some sort of immobilisation of the enzyme, or transformation to a heterogeneous catalyst in some manner. As will be explained below, this has not been a straightforward procedure, and reusable enzymes are therefore scarce. Alcohol resolution with lipase B from Candida antarctica (CalB)15 in the common immobilised form is an example wherein an effective immobilised enzyme is achieved that can be used as a simple heterogeneous catalyst. Immobilised CalB has been extensively studied and is used in various industrial processes.16,17 The wide substrate scope of CalB is surely one reason for its popularity, but the importance of the immobilised form and its simple use should also be highlighted. We believe that if a larger number of immobilised enzymes can be formulated, which are chosen carefully to suit major reaction types, their use will be adopted by the industry in a much more open fashion than for enzymes marketed through the current model of first developing/screening for a specific reaction and then employing non-reusable crude extracts as the frequent preparation of choice.

13.2.2 Unlocking the Potential of Enzymes

Living cells perform a diverse set of enzyme catalysed reactions. Enzyme discovery ranging from bacterium in diverse environments to the astonishing chemistry within our own bodies has given us access to useful catalysts. New catalytic activity can be achieved through engineering of existing enzymes by methods that are now considered robust and effective, and enzymes can be engineered to be more stable in order to withstand the environment within chemical reactors. The time required for developing a biocatalyst for a given reaction is roughly on par with the average time for developing any other catalyst type. In theory, there are plentiful reactions in which enzymes can replace conventional catalysts; however, if the cost contribution of these enzymes in the target process remains too high, the industry will most likely refrain from making the switch. To initiate a switch from already validated catalyst systems, there must be a clearer economic benefit, confidence that the final catalyst will perform as intended, and a genuine belief in the novel technology.

EnginZyme sees a significant benefit in producing biocatalysts that are of an easy-to-use form ready for standard equipment. For the sake of argument, let us assume that there is an enzyme suited for producing a wide range of products from a common pharmaceutical intermediate motif; an enzyme not engineered for one specific reaction, but which can be used for many reactions, and requiring high catalyst loadings in many cases. It is either difficult to bring the cost of producing this enzyme to a level low enough for economic benefit or too much enzyme is needed to produce the product in a reasonable time frame. This theoretical enzyme is employed as a crude preparation that is not reusable, which in turn results in cumbersome product work-up procedures. Such assumptions are not farfetched, and can be exemplified by the case of transaminases and ketone reductases. The disadvantages counteract the otherwise great process improvement. Consequently, the enzyme is only used in a few cases, such as when a low enough catalyst loading is required, or when the product produced is of high value, and work-up procedures are either economically motivated or happen to be simple.

Now, extend the argument for the immobilised CalB mentioned above, whereby an immobilised and thereby reusable preparation is easily attainable and a heterogeneous catalyst with high reusability is achieved, and higher catalyst loadings are now acceptable due to the reusability. Testing and optimisation of reactions can be done with limited effort, and employment in processes is not much different from using standard catalysts. Would this not significantly increase the use of the envisioned enzyme? Goswami and Stewart argue that “…one often does not need to develop the “perfect” enzyme for every case when a pretty good solution will do” and suggest that we “develop enzymes that perform well on whole groups of substrates”.18 As we see it, the strength of this approach would be increased if an effective immobilisation of the enzyme in question could be assured. This is one of the arguments in favour of launching the general immobilisation product EziG.

13.2.3 Immobilised Enzymes for the Pharmaceutical Industry

Biocatalysis is used in the production of food, cosmetics and in several other areas of chemistry; and the potential market for immobilised enzymes is large in all of them. However, EnginZyme has chosen to firstly focus on the pharmaceutical industry, where the need for enantiopure products and the capability to produce complex molecular entities at as low a cost as possible gives an obvious benefit in favour of biocatalysis. Accordingly, pharmaceutical companies have been more keen to employ enzymes in their production processes than, perhaps, in many other branches. Although sales to companies in this industry segment require a significant time investment, this detriment is outweighed by the potential of addressing already developed and verified biocatalytic transformation types. EnginZyme has started by looking at the enzymes that are already present and used; enabling their reuse makes new applications feasible (economically viable), and lowers the costs for current processes.

13.2.4 The Reusable Enzyme Utopia – Enzymes Anchored in Space

The current methods for enzyme reuse can be very effective but, unfortunately, none can be described as being generally applicable. That is, for a given enzyme, there is no method for which a reasonable amount of investment has a sufficiently high degree of certainty to yield an effective reusable preparation. A research project for enzyme reuse, with enzyme immobilisation or other methods, can be a tedious and costly endeavour with an uncertain outcome.

In short, existing techniques can be grouped into three categories, of which numerous examples can be found in academic publications: (1) encapsulation/entrapment of enzymes in a permeable material, (2) cross-linking of the intact enzyme, and (3) binding to a suitable (inert) carrier material. In the case of industrial use, methods in the first category are being marketed by companies such as LentiKat’s,19 which encapsulates the enzyme in lentil-shaped particles, and Zymtronix,20 which uses a self-assembling magnetic porous material to entrap the enzyme. As reflected in the acronym, the Dutch company CLEA (Cross-Linked Enzyme Aggregates) Technologies B.V. are experts in the second category.21 The most commonly utilised method, however, is binding the enzyme to a suitable carrier, such as a porous plastic bead or a silica based material. Resindion22 and Purolite23 offer a variety of different types of porous carrier materials that can be tested with the target enzyme, and others, such as ChiralVision,24 offer services to perform and optimise the immobilisation. Despite these available options, enzyme immobilisation is not a standard technology in the industry because the available methods are effective only for a few verified enzymes, lack general applicability and/or require screening and development work to function in a process for a given enzyme. Moreover, the established methods often bring significant diffusion limitations and enzyme deactivation, which hampers their effectiveness. Furthermore, these methods all require additional costs for preparing the reusable enzyme. Arguably, if 90% activity is lost, more than ten-time reusability is required to ensure that a company sees a return on investment (ROI) for any method. Such high activity loss is not uncommon, yet ten-time reuse is a considerable challenge.

Enzymes can generally be assumed to be most catalytically effective in the form in which they were evolved, i.e. dissolved in aqueous medium, free to have molecular and structural mobility of their different parts, and with their active site easily reachable from the surrounding space. Based on this notion, the ideal immobilisation method would magically anchor enzyme moieties in three dimensions, evenly distributed in a reaction vessel. This would maintain the enzyme in its natural form while also enabling reuse, as the reaction mixture can be removed and a new one added. To date there is obviously no known technology that fulfils these criteria, but the principle can be used as a model to design immobilisation methods, which was the case for EziG.

13.2.5 The EziG Technology

EziG is a material based on a rational design approach, specifically intended for use in biocatalysis and conceived with the utopic immobilisation described above as a model from which as few changes as possible should be made. For practical reasons, encapsulation and cross-linking could not be implemented, since these processes inhibit the natural form and alter the direct environment of the enzyme. Rather, it was necessary to identify a carrier material that could function as closely as possible to a magic anchor. The choice was a specific controlled-pore glass (CPG), a material that has interconnecting pores, which enables more efficient mass transfer to the interior than other porous materials. The compromise required from a ‘magic’ anchor in space is a porous silica skeleton that allows a solvent to effectively reach any given surface point. An important factor is the ability for reactants to reach the enzyme, i.e. efficient mass transfer into the porous material. Poor mass transfer is a common cause for low catalytic activity in general; a problem that is specifically pronounced for immobilised enzyme preparations.

The CPG concept has been used for enzyme immobilisation for decades, but is generally not regarded as a viable option since its performance does not outweigh its high cost. The main issue has been the nature of its silica-like surface, which is not stable to hydrolysis and may also cause denaturation of the enzymes themselves. Although the mass transfer is favourable, activity loss is observed and the number of cycles of reuse are limited. Therefore, we have covered the porous surface of the CPG with an organic polymer layer, thus forming hybrid CPG, which is stable and not harmful to enzymes. Now, a suitable micro-environment for the enzyme is achieved in an accessible pore, and utilisation of a favourable mass transfer is thereby made possible while maintaining an active enzyme. The organic polymer completely covers the interior and exterior surfaces of the particle, and it is stable towards aqueous environments and most organic solvents. The glass skeleton does not swell and is dense enough to allow sedimentation. Microscopic swelling of the organic polymer may occur in organic solvents, but this does not significantly increase the bulk volume of the porous material. At this point, the carrier is suited for adsorption of the enzyme, or for binding with a variety of known methods used for common resins. None of these are generally applicable for a given enzyme, however, so many techniques would have to be tested on a case-by-case basis, the amount of active bound enzyme would often be low, and loss of activity would occur as a consequence of binding at different points on the enzyme surface through distortion of the enzyme’s structure.

Therefore, a well defined and general binding method was sought. Selective binding of target proteins with affinity tags is a standard procedure in protein purification applications.25 The simplest form is use of a poly-histidine tag (His-tag), whereby usually a chain of six residues of the amino acid histidine are added to a chosen end of a protein (N- or C-terminal), which enables binding to metal ions. For purification purposes, a specific binding and the ability to easily remove the protein from a resin after washing are beneficial. Commonly, immobilised metal affinity chromatography (IMAC) involves the use of nickel or cobalt ions chelated to a resin, thereby giving a specific binding to the His-tag, which is simple to break by addition of dissolved imidazole. IMAC with His-tagged proteins is regarded as a general method for purification and is common practice at laboratory scale. EziG uses this technique for binding enzymes, but in this case nickel or cobalt is replaced with iron in ionic form. Although iron is slightly less specific for His-tags, it is non-toxic and the binding is more stable in the sense that, most commonly, little or no enzyme leaching occurs. Thereby, EziG immobilisation is claimed to be general for any enzyme produced with an accessible His-tag. Rather than binding directly on the native enzyme surface in different ways depending on the enzyme in question, by binding to the tag that is usually connected to the enzyme via a linker, the point of binding is now defined. The distortion of the enzyme is minimal, though reversible interactions of the carrier’s surface with the enzyme still occur. Details of the EziG enzyme carrier material are presented in Figure 13.1.

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Figure 13.1 Schematic picture of the EziG enzyme carrier, an engineered material for biocatalytic applications. The external and internal porous surface of CPG is covered with an organic polymer layer, which is derivatised to chelate Fe(III), to which His-tagged enzyme can be bound.

By utilising the specificity of the affinity tag, immobilisation on EziG can be performed without prior purification of the enzyme, in contrast to other techniques in which purification may be required to reach a workable enzyme loading on a carrier. The frequently used crude preparations, i.e. cell extracts, can be directly applied to EziG to achieve a reusable preparation. Additionally, different enzymes can easily be co-immobilised on the same carrier for cascade reactions.

Commonly, porous materials used for enzyme immobilisation can be loaded to carry up to around 10% w/w enzyme. Since a large fraction of this is often deactivated, and other proteins are also bound (unless the immobilisation is performed from a purified preparation), the loading of active enzyme is usually limited to single digit percentages. With EziG, however, examples of up to 30% w/w active enzyme are produced. Depending on the reaction rate, the virtual activity of enzymes thus bound varies. In fast reactions, diffusion limitations do decrease the rate somewhat despite the efficient mass transfer. Fast reactions are commonly chosen for simple assays in laboratory testing, in which case the expected activity for the ensuing synthesis reaction is often underestimated, since it is usually not on a par with the assay reaction in terms of reaction rate. For slower reactions, the EziG-immobilised enzyme can reach the same activity as the dissolved enzyme, or extend even higher when stabilising effects come into play.

13.2.6 Standardised Procedure for Immobilisation

By using the affinity tag technique for binding to a tailored material suitable for biocatalysis, immobilisation can be performed by a standardised procedure and active reusable enzyme can generally be expected. Thereby, a great deal of uncertainty is removed and motivation to plan the development of a biocatalytic process with immobilised enzyme is enhanced. Notably, some enzymes require slightly modified procedures to compensate for enzyme specific features such as surface hydrophobicity, multimeric structures, and addition of stability enhancing agents. Accordingly, EziG is currently produced in three varieties with varying surface hydrophobicity. The binding of enzyme in active form is very rarely an issue, in contrast to common resins, and the focus can now shift to optimising the target reaction to accommodate for the introduction of the porous material. EnginZyme shares a vision whereby the idea of being able to reuse essentially any commercially interesting biocatalyst will be included in the decision making and cost estimates made by industrial chemical process designers when assessing the various options at hand.

13.2.7 Lower Cost Materials versus High Performance

The result of immobilising an enzyme on the designed material is generally a high mass loading of reusable enzyme with high retained activity (see examples below); however, it is not possible to produce this material without a significantly higher cost compared to other commonly used materials for enzyme immobilisation. With its sophisticated material properties,26 EziG is significantly costlier than porous plastic, for example. To evaluate economic feasibility, one must calculate the total cost of producing a reusable enzyme per unit of activity, and then conduct a comparison with the non-reusable alternative. A comparison of cost for producing the immobilised enzyme alone is redundant. When compared with low cost materials for immobilising enzymes, and including the cost of wasted enzyme because of activity loss, EziG is almost certainly the most economical choice in the vast majority of cases. The general immobilisation procedure is straightforward and can be performed from crude extracts, enzyme activity is maintained and high loadings of active enzyme are achieved; the higher cost of EziG is outweighed by these cost savings, as exemplified by the general case below.

To simplify, imagine a common case of a porous plastic material on which an enzyme is immobilised, thereby losing 90% of the activity, with a mass loading of 5%. The cost of enzyme for producing a given amount of activity has thereby roughly increased by a factor of ten, and the amount of carrier material needed to immobilise the enzyme must be 190 times that of the enzyme mass needed in the non-immobilised case (ten times more enzyme and 5% w/w enzyme loading gives a total mass of 200 kg for a preparation of equal activity to 1 kg of non-immobilised enzyme). Without including the cost for the carrier material, along with other factors such as costs for immobilisation procedures, increased volume in the reaction vessel, etc., the enzyme alone must still be reused more than ten times for the immobilisation to give any benefits.

The same case with EziG may show a mass loading of 20% and a maintained activity level of 90% compared to the dissolved enzyme. The increased cost for the enzyme is not significant, and the mass amount of carrier needed is not more than four times that of the enzyme. To reach the activity equal to 1 kg of non-immobilised enzyme, ∼1.1 kg enzyme and ∼4.4 kg of EziG is needed, giving a total mass of around 5.5 kg for the immobilised preparation. For the majority of enzymes for immobilisation on the available support resins available today, the difference in enzyme and carrier mass material needed more than compensates for the higher cost of EziG. Since the immobilisation can be done directly from a crude extract, few or no additional steps need be added to the process. The number of recycling loops necessary for reaching a saving varies with enzyme cost, but for the average enzyme this number is usually in the single-digit range. Additionally, since the binding with the His-tag is reversible, the same carrier material can often be reloaded with fresh enzyme after exhausting the first batch of bound material and then recycled within the given process, thus avoiding any risk of cross-contamination. When this scenario is possible, the cost contribution from the carrier becomes insignificant.

13.3 Case Studies27

13.3.1 In-reactor Enzyme Immobilisation

A benefit of the simple and specific binding technique used for EziG immobilisation is the possibility of applying an enzyme preparation directly in a reactor together with EziG, and thereby achieving a reusable enzyme preparation where the subsequent synthesis reaction is planned to take place. The enzyme preparation may be a crude extract, and the reactor may be a stirred tank batch mode or flow column.

A transaminase enzyme (Chromobacterium violaceum ω-transaminase) was immobilised in a SpinChem reactor as a filtered cell free extract. The graph in Figure 13.2 shows the amount of dissolved enzyme versus time after mixing was commenced, and it is obvious that the enzyme is rapidly removed from the solution. The fast binding is a consequence of efficient mass transfer, through the pores of EziG as well as efficient mixing by the SpinChem device. The same procedure can be performed with overhead stirring, though this results in slightly slower binding. Notably, the binding of this specific enzyme is an advantageous case, as there are instances in which binding cannot be performed in minutes, but may require an investment of hours. The dilution of enzyme, amount of carrier used and competing substances in the mixture are all factors that influence the rate of binding, as well as the active enzyme mass loading. In this case, 29% w/w active enzyme was reached via the EziG-preparation, and virtually all enzyme in the crude extract could be bound.

image

Figure 13.2 Dissolved transaminase enzyme versus time when immobilised in a SpinChem reactor with EziG in the rotating basket. The efficient immobilisation is visualised as the disappearance of enzyme from solution. The procedure was performed in the reactor where the subsequent biocatalytic reaction will be performed.

The same enzyme was also immobilised in a flow column (data not shown) by pumping the cell free extract through a packed bed. With a residence time of 10 min, the mass loading of enzyme on the carrier was calculated to be 25% by analysis of the remaining enzyme in the flow-through solution. The procedure is similar to a standard IMAC procedure, in which enzyme is bound in a column packed with Sepharose. Similarly, the enzyme could be detached by applying a 0.5 M solution of imidazole at pH 7.4. After this, fresh enzyme could be bound to the EziG in the column to reach the same mass loading as before.

13.3.2 Two-phase System in Flow for in situ Product Removal

The transaminase enzyme used in the binding example above can be applied for kinetic resolution of amines; for example, by adding 1-phenylethylamine in racemic form together with pyruvate as amine acceptor. The enzyme virtually only catalyses the amine transfer from the (S)-enantiomer, forming L-id="page_357" title="357"/>alanine and acetophenone, and leaving enantiopure (R)-1-phenylethylamine. The formed acetophenone inhibits this enzyme, thus preventing the completion of the reaction. This problem was solved by using a two-phase system to extract the generated acetophenone, thus preventing the inhibition. The reaction was performed in a packed column, where the organic solvent (cyclohexane) was pumped in simultaneously with aqueous buffer simply by combining solutions via tubes from separate pumps. The separate phases were visible as bubbles going into the column, and appeared in the same manner upon exit on the other side. Complete conversion of the (S)-enantiomer was observed with 80% cyclohexane. This proof-of-concept system is visualised in Figure 13.3.

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Figure 13.3 Depiction of a continuous flow system for kinetic resolution of an amine, whereby the inhibitory product is subject to in situ product removal by addition of an organic phase. The phases were pumped simultaneously as small bubbles through the EziG-enzyme in a simple packed bed reactor.

ω-Transaminases can also be used in so-called synthesis mode, which basically is the reaction described here in reverse. A prochiral ketone is converted into an enantiopure amine by stereoselective synthesis, which is a more atom economic choice than the kinetic resolution. On the other hand, stereoselective synthesis involves a higher demand for enzyme engineering and suffers from an unfavourable equilibrium, which requires displacement to reach high yields. Therefore, the choice of kinetic resolution may not require as tedious an enzyme and reaction engineering as a process in synthesis mode. We do expect a similar flow system as described here to function in synthesis mode, but, herein, we offer a method for kinetic resolution in flow with a wild-type (not engineered) transaminase enzyme.

13.3.3 Candida antarctica Lipase B (CalB)

CalB is probably the most studied and used enzyme for biocatalysis purposes, and as previously noted is made commercially available in immobilised form by several companies. EnginZyme is developing its own version of this popular catalyst, called EnginLipe™, which also verifies the efficiency of EziG in comparison with common enzyme carriers. CalB is comparatively easy to immobilise on porous plastic materials because the enzyme is stable and spontaneously binds to hydrophobic surfaces.28 By comparing the use of the general binding method with affinity tags on EziG with standard immobilised CalB preparations, we aim to demonstrate that our method is more efficient and indicative of the prospect of achieving equally efficient preparations with other enzymes in the same simple manner.

Normally, CalB is produced by overexpression in yeast or fungal strains. Although these expression systems are efficient for large scale production, Escherichia coli strains are commonly the first choice for the production of engineered variants (screening) and generally produce high titres of recombinant protein in a shorter time. CalB expression in E. coli, however, generally yields low amounts of active protein due to aggregation (inclusion bodies). Together with Vectron Biosolutions, EnginZyme has developed an efficient method for expressing CalB in E. coli. Bioreactor expressions reach several grams per litre, and the enzyme is secreted to the culture medium from which it can be directly immobilised on EziG. Catalytic activity figures of EnginLipe™ containing CalB expressed in E. coli are compared with those of an efficient preparation from Novozymes with CalB produced in an Aspergillus strain (Table 13.1). The higher activity of EnginLipe for the tested reactions is attributed to a higher enzyme loading and more efficient mass transfer through EziG compared to the more commonly used porous acrylic beads.

Table 13.1 Catalytic activity of EnginLipe (CalB expressed in E. coli immobilised on EziG by His-tags) and Novozym® 435 (CalB expressed in an Aspergillus strain immobilised on acrylic resin by adsorption); preliminary results from an ongoing project

Company Company
EnginLipe™ 13 500
Novozym 435 1400

a Acid production in aqueous buffer, measured in a pH-stat at 40 °C.

13.3.4 Co-immobilisation for Cascade Reactions

Enzymes that catalyse reductions or oxidations often require cofactors (NADH/NAD+ or NADPH/NADP+) as electron acceptors or donors. These are costly compounds, and should therefore be regenerated in a discrete biocatalytic process, such as performing an oxidation of a sacrificial reactant, in order to reach cost efficiency. The regeneration may be done with a second enzyme, which thereby requires an enzymatic cascade reaction. Other cases in which cascades are necessary could include, for example, equilibrium displacements or one-pot reactions with several steps.

Since the binding to EziG is general, all necessary enzymes in a cascade can be simultaneously immobilised in the same pore on one carrier. In this example, we demonstrate this concept with a ketone reductase (KRED) for a model reaction with an enzyme requiring NADH (Scheme 13.1). The cofactor is regenerated with the enzyme glucose dehydrogenase (GDH), and the NAD+ formed is converted back into NADH by oxidation of glucose to yield gluconolactone.

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Scheme 13.1 Synthesis of a chiral alcohol by co-immobilised KRED and GDH, on the same EziG carrier.

Extracts of the enzymes from overexpression were mixed, and EziG was added to this mixture to co-immobilise both enzymes. The immobilised preparation could be used as catalyst for the conversion, thus demonstrating the successful co-immobilisation of both enzymes in one attempt. The possible amount of reuse cycles depends on the reaction conditions, the enzymes and the substrates in question, in a similar vein as for single-enzyme systems.

13.4 Prospects

13.4.1 Stability versus Activity – Replacing Low Cost Catalysts

For costly biocatalysts to reach cost effectiveness for lower value products in applications such as manufacturing of biodiesel, preparation of components for beverage flavour enhancement, production of achiral bulk chemicals, etc., we propose a strategy that does not primarily focus on engineering enzymes for high catalytic activity. Rather, the emphasis is shifted to enzyme stability when an enzyme with sufficiently high activity is identified. An immobilised and stable enzyme that can be reused extensively can thereby become sufficiently inexpensive to serve as a feasible replacement of a current standard catalyst. We find this prospect attractive, since process conditions can be improved to lower the temperature requirement and produce less waste. Engineering of proteins to increase stability is usually a less complicated endeavour than increasing the catalytic activity for a specific conversion. Moreover, enzymes found in thermophilic organisms are inherently stable.

Let us, for example, envision bulk esters or amides that are usually produced at high temperatures, and sometimes in the presence of metal catalysts.29 There are examples of enzymes that can be used for production of these compounds at room temperature. In the future, we envision such types of conversions to be performed in flow chemistry set-ups with immobilised enzymes.

13.4.2 Biocatalysis in Flow – Towards Manufacturing Processes in Continuous Mode

As described in the case studies above, the binding of enzyme in a packed bed reactor with EziG followed by a continuous biocatalytic reaction is a powerful proof-of-concept of a generally applicable method for an easy implementation of biocatalysis in a flow regime that is suitable for continuous manufacturing operation. The examples presented are on laboratory scale, but we have every reason to believe that the methodology as such is nicely scalable. We envision the use of crude extracts to load and reload column reactors with enzyme, and rerouting of reaction mixture streams to loaded columns while exhausted ones are replenished; a modular process intensification design for maximum efficiency biocatalysis in flow mode.

13.5 Conclusions

EnginZyme seeks to expand the use of biocatalysis and thereby improve the environmental sustainability performance of the chemical industry. In our view, currently, the main barrier to increased implementation is the high cost of both the majority of enzyme types and the production and engineering/optimisation of suitable enzymes for specific target reactions. The development of standardised and reliable techniques to address critical barriers to increased implementation will naturally cause an overall improvement to any field. We see the potential in universal and simple enzyme reuse as a technology that greatly enhances the capabilities of the whole biocatalysis field. In this chapter, we have presented a simple method for transforming a crude enzyme preparation into a reusable biocatalyst in a single step. The technique is rationally designed and focussed on high performance. The envisioned impact of such a technology in terms of examples of what issues might be solved are presented in Table 13.2.

Table 13.2 Examples of common issues in biocatalysis that have been resolved or are predicted to be solved by EziG

Company Company
Economic
High biocatalyst cost Enzyme reuse
Enzyme immobilisation
Cumbersome procedure One-step extraction/purification from crude extract
Lack of general methods Suited for all enzyme types by use of His-tags
Activity loss by diffusion limitations Efficient mass transfer by interconnecting pores
Activity loss by binding Non-destructive binding by His-tags
Process development
Demanding enzyme engineering Reuse assured – lower activity acceptable
Costly work-up caused by cell components Immobilisation and facile separation
Lack of general flow chemistry techniques Modular process design envisioned

In our view, the above issues, for which we present a solution, are of paramount importance for industrial biocatalysis. We foresee the simple solution of immobilising an enzyme in active form, with concomitant purification by affinity tags, to be an important step towards the future manifestation of biocatalysis as the first-choice method, replacing the current environmentally problematic, albeit efficient metal-based catalytic techniques.

Acknowledgements

The experimental and scientific contributions made to this work by Dr Alexey Volkov, Dr Peter Hendil-Forssell, Robin Chatterjee, Samuel Härgestam, Dr Linda Fransson and Dr Maria Svedendahl Humble are gratefully acknowledged.

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1 EziG, pronounced “eezeejee”, an acronym for enzyme immobilisation glass.