A Novel Whole-Cell Biocatalyst with NAD+ Regeneration for Production of Chiral Chemicals

Background

The high costs of pyridine nucleotide cofactors have limited the applications of NAD(P)-dependent oxidoreductases on an industrial scale. Although NAD(P)H regeneration systems have been widely studied, NAD(P)⁺ regeneration, which is required in reactions where the oxidized form of the cofactor is used, has been less well explored, particularly in whole-cell biocatalytic processes.

Methodology/Principal Findings

Simultaneous overexpression of an NAD⁺ dependent enzyme and an NAD⁺ regenerating enzyme (H₂O producing NADH oxidase from Lactobacillus brevis) in a whole-cell biocatalyst was studied for application in the NAD⁺-dependent oxidation system. The whole-cell biocatalyst with (2R,3R)-2,3-butanediol dehydrogenase as the catalyzing enzyme was used to produce (3R)-acetoin, (3S)-acetoin and (2S,3S)-2,3-butanediol.

Conclusions/Significance

A recombinant strain, in which an NAD⁺ regeneration enzyme was coexpressed, displayed significantly higher biocatalytic efficiency in terms of the production of chiral acetoin and (2S,3S)-2,3-butanediol. The application of this coexpression system to the production of other chiral chemicals could be extended by using different NAD(P)-dependent dehydrogenases that require NAD(P)⁺ for catalysis.     

Nanoparticle-tethered NAD+ with in situ cofactor regeneration

A new and simple route for the preparation of immobilized NAD⁺ on carboxyl-activated silica nanoparticles activated by γ-aminpropyltriethoxysilane and glutaric anhydride was developed. In addition, formate dehydrogenase, keto-reductase and the silica nanoparticle-attached NAD⁺ were applied to catalyze the coupled reactions for production of l-lactate with the cofactor regenerated within the reaction cycle. As indicated by thermogravimetric analysis and FT-IR, the silica nanoparticles were successfully activated and the loading of carboxyl groups was 0.53 mmol g^?1 particle. The amount of immobilized NAD⁺ on the support was 73 mg g^?1 particle. With 0.2 M pyruvate and 3 M formate, 0.16 M l-lactate was produced after the coupled reactions. The immobilized system showed excellent efficiency and stabilities in recycling, and it retained 60 % residual activity even after six reuses.     

Conversion of glycerol to 1,3-dihydroxyacetone by glycerol dehydrogenase co-expressed with an NADH oxidase for cofactor regeneration

Objectives

To investigate the efficiency of a cofactor regeneration enzyme co-expressed with a glycerol dehydrogenase for the production of 1,3-dihydroxyacetone (DHA).

Results

In vitro biotransformation of glycerol was achieved with the cell-free extracts containing recombinant GlyDH (glycerol dehydrogenase from Escherichia coli), LDH (lactate dehydrogenase form Bacillus subtilis) or LpNox1 (NADH oxidase from Lactobacillus pentosus), giving DHA at 1.3 g l^?1 (GlyDH/LDH) and 2.2 g l^?1 (GlyDH/LpNox1) with total turnover number (TTN) of NAD⁺ recycling of 6039 and 11100, respectively. Whole cells of E. coli (GlyDH–LpNox1) co-expressing both GlyDH and LpNox1 were constructed and converted 10 g glycerol l^?1 to DHA at 0.2–0.5 g l^?1 in the presence of zero to 2 mM exogenous NAD⁺. The cell free extract of E. coli (GlyDH–LpNox) converted glycerol (2–50 g l^?1) to DHA from 0.5 to 4.0 g l^?1 (8–25 % conversion) without exogenous NAD⁺.

Conclusions

The disadvantage of the expensive consumption of NAD⁺ for the production of DHA has been overcome.

     

Reactivation of Inactivated d-Glucose Dehydrogenase of a Bacillus Species by Pyridine and Adenine Nucleotides

d-Glucose dehydrogenase [β-d-glucosc: NAD(P) oxidoreductase (EC 1.1.1.47)] was synthesized derepressively in a mutant of a Bacillus species which was isolated as an improved strain for d-ribose production. The enzyme was very unstable and inactivated during storage or column chromatography. The inactivation was prevented in the presence of NAD⁺, NADP⁺ or certain salts. The inactive enzyme was reactivated by the addition of NAD⁺, NADH, NADP⁺, NADPH, AMP, ADP, ATP or certain salts. The molecular weights of the inactive and active form of the enzyme were estimated to be about 45,000 and 80,000, respectively, by Sephadex G–150 gel filtration. Thus, it seems that the enzyme activity is regulated by monomer-dimer interconversion of the enzyme molecule.     

Enhancement of biocatalytic efficiency by increasing substrate loading: enzymatic preparation of l-homophenylalanine

Enantiomerically pure l-homophenylalanine (l-HPA) is a key building block for the synthesis of angiotensin-converting enzyme inhibitors and other chiral pharmaceuticals. Among the processes developed for the l-HPA production, biocatalytic synthesis employing phenylalanine dehydrogenase has been proven as the most promising route. However, similar to other dehydrogenase-catalyzed reactions, the viability of this process is markedly affected by insufficient substrate loading and high costs of the indispensable cofactors. In the present work, a highly efficient and economic biocatalytic process for l-HPA was established by coupling genetically modified phenylalanine dehydrogenase and formate dehydrogenase. Combination of fed-batch substrate addition and a continuous product removal greatly increased substrate loading and cofactor utilization. After systemic optimization, 40 g (0.22 mol) of keto acid substrate was transformed to l-HPA within 24 h and a total of 0.2 mM NAD⁺ was reused effectively in eight cycles of fed-batch operation, consequently giving an average substrate concentration of 510 mM and a productivity of 84.1 g l^?1 day^?1 for l-HPA. The present study provides an efficient and feasible enzymatic process for the production of l-HPA and a general solution for the increase of substrate loading.     

Application of an Electrochemical NAD+ Recycling System Involving a String-Like Carbon Fiber to an Enzyme Reactor

A string-like carbon fiber was found to be very suitable as a working electrode material for direct electrochemical oxidation of β-nicotinamide adenine dinucleotide reduced form (NADH), and direct use of it for an enzyme reactor was possible. The electrochemical NAD⁺ recycling system was applied to glucose dehydrogenase (GDH) and to the recombinant formate dehydrogenase (RFDH) reactors. The maximum oxidation current value increased to 3.9 mA in the case of the GDH reactor. The remaining GDH activity after the reaction for 10 h amounted to 57% of the initial level. The remaining NAD⁺ activity amounted to 78% of the initial level. The current efficiency was calculated to be 80%. Furthermore, RFDH, which was more stable than GDH, was applied to the system. The maximum current value reached 5.9 mA. The remaining RFDH activity after reaction for 10 h amounted to 81% of the initial level. The remaining NAD⁺ activity was 78% of the initial level. The current efficiency was calculated to be 73%. Based on these results, both the enzyme and NAD⁺ were found to be acceptably stable in the electrochemical NAD⁺ recycling system.     

Efficient Whole-Cell Biocatalyst for Acetoin Production with NAD+ Regeneration System through Homologous Co-Expression of 2,3-Butanediol Dehydrogenase and NADH Oxidase in Engineered Bacillus subtilis

Acetoin (3-hydroxy-2-butanone), an extensively-used food spice and bio-based platform chemical, is usually produced by chemical synthesis methods. With increasingly requirement of food security and environmental protection, bio-fermentation of acetoin by microorganisms has a great promising market. However, through metabolic engineering strategies, the mixed acid-butanediol fermentation metabolizes a certain portion of substrate to the by-products of organic acids such as lactic acid and acetic acid, which causes energy cost and increases the difficulty of product purification in downstream processes. In this work, due to the high efficiency of enzymatic reaction and excellent selectivity, a strategy for efficiently converting 2,3-butandiol to acetoin using whole-cell biocatalyst by engineered Bacillus subtilis is proposed. In this process, NAD⁺ plays a significant role on 2,3-butanediol and acetoin distribution, so the NADH oxidase and 2,3-butanediol dehydrogenase both from B. subtilis are co-expressed in B. subtilis 168 to construct an NAD⁺ regeneration system, which forces dramatic decrease of the intracellular NADH concentration (1.6 fold) and NADH/NAD⁺ ratio (2.2 fold). By optimization of the enzymatic reaction and applying repeated batch conversion, the whole-cell biocatalyst efficiently produced 91.8 g/L acetoin with a productivity of 2.30 g/(L·h), which was the highest record ever reported by biocatalysis. This work indicated that manipulation of the intracellular cofactor levels was more effective than the strategy of enhancing enzyme activity, and the bioprocess for NAD⁺ regeneration may also be a useful way for improving the productivity of NAD⁺-dependent chemistry-based products.     

Cofactor recycling in liquid membrane-enzyme systems.

In contrast to other entrapment techniques, hydrocarbon-based liquid surfactant membranes have been shown to effectively retain NADH and NAD⁺. The activities of an immobilized yeast alcohol dehydrogenase (ADH) - NAD⁺ system and of a coupled cofactor recycling system involving ADH, diaphorase and ferricyanide were examined by determining the extent of both ethanol consumption and acetaldehyde accumulation in the external aqueous solution. The results establish suitability of the liquid membrane system for the immobilization of enzyme systems involving $\text{in}$-$\text{situ}$ cofactor regeneration.     

Identification of essential amino acids in the active center of thyroidal NAD+ glycohydrolase

• 1.1. Purified thyroidal NAD⁺ glycohydrolase has been subjected to the action of a number of group specific reagents in order to gain information concerning its mode of action.
• 2.2. Modification of histidyl residues with diethylpyrocarbonate strongly suppresses the NAD⁺ glycohydrolase activity. Inactivation with this reagent can be reversed to some extent by subsequent treatment with hydroxylamine.
• 3.3. NAD⁺ and ADP-ribose partially protect against inactivation with similar efficiencies.
• 4.4. The incomplete reactivation with hydroxylamine after diethylpyrocarbonate treatment and the selective inactivation by 2,4-pentanedione indicates that apart from one or more essential histidyl residue(s) also lysyl residues are important for activity. NAD⁺ and to a smaller extent ADP-ribose again protect against inactivation by 2,4-pentanedione.
• 5.5. The sensitivity of the enzyme towards N-ethyl-5-phenyl-isooxazolium-3'-sulfonate further points to the importance of carboxylate containing side chains.
• 6.6. The mechanistic implications of these results are discussed.

     

l-Arabinose/d-galactose 1-dehydrogenase of Rhizobium leguminosarum bv. trifolii characterised and applied for bioconversion of l-arabinose to l-arabonate with Saccharomyces cerevisiae

Four potential dehydrogenases identified through literature and bioinformatic searches were tested for l-arabonate production from l-arabinose in the yeast Saccharomyces cerevisiae. The most efficient enzyme, annotated as a d-galactose 1-dehydrogenase from the pea root nodule bacterium Rhizobium leguminosarum bv. trifolii, was purified from S. cerevisiae as a homodimeric protein and characterised. We named the enzyme as a l-arabinose/d-galactose 1-dehydrogenase (EC 1.1.1.-), Rl AraDH. It belongs to the Gfo/Idh/MocA protein family, prefers NADP⁺ but uses also NAD⁺ as a cofactor, and showed highest catalytic efficiency (k _cat/K _m) towards l-arabinose, d-galactose and d-fucose. Based on nuclear magnetic resonance (NMR) and modelling studies, the enzyme prefers the α-pyranose form of l-arabinose, and the stable oxidation product detected is l-arabino-1,4-lactone which can, however, open slowly at neutral pH to a linear l-arabonate form. The pH optimum for the enzyme was pH 9, but use of a yeast-in-vivo-like buffer at pH 6.8 indicated that good catalytic efficiency could still be expected in vivo. Expression of the Rl AraDH dehydrogenase in S. cerevisiae, together with the galactose permease Gal2 for l-arabinose uptake, resulted in production of 18 g of l-arabonate per litre, at a rate of 248 mg of l-arabonate per litre per hour, with 86 % of the provided l-arabinose converted to l-arabonate. Expression of a lactonase-encoding gene from Caulobacter crescentus was not necessary for l-arabonate production in yeast.     

Intraneuronal Aβ detection in 5xFAD mice by a new Aβ-specific antibody

Background

The Wld ^S mouse mutant ("Wallerian degeneration-slow") delays axonal degeneration in a variety of disorders including in vivo models of Parkinson's disease. The mechanisms underlying Wld ^S -mediated axonal protection are unclear, although many studies have attributed Wld ^S neuroprotection to the NAD⁺-synthesizing Nmnat1 portion of the fusion protein. Here, we used dissociated dopaminergic cultures to test the hypothesis that catalytically active Nmnat1 protects dopaminergic neurons from toxin-mediated axonal injury.

Results

Using mutant mice and lentiviral transduction of dopaminergic neurons, the present findings demonstrate that Wld ^S but not Nmnat1, Nmnat3, or cytoplasmically-targeted Nmnat1 protects dopamine axons from the parkinsonian mimetic N-methyl-4-phenylpyridinium (MPP⁺). Moreover, NAD⁺ synthesis is not required since enzymatically-inactive Wld ^S still protects. In addition, NAD⁺ by itself is axonally protective and together with Wld ^S is additive in the MPP⁺ model.

Conclusions

Our data suggest that NAD⁺ and Wld ^S act through separate and possibly parallel mechanisms to protect dopamine axons. As MPP⁺ is thought to impair mitochondrial function, these results suggest that Wld ^S might be involved in preserving mitochondrial health or maintaining cellular metabolism.     

Isoenzyme specific inhibition of the reactivation of in vitro dissociated lactic dehydrogenase isoenzymes by two different peptides isolated from human liver

The catalytic activity of the LDH-isoenzymes depends on their tetrameric structure. Low pH or other denaturants leads to dissociation into monomers and to the loss of the specific activity. After removal of the denaturing conditions reassociation and reactivation occur spontaneously. Neither NADH nor NAD⁺ shows a significant effect on the reactivation. We have isolated two different peptides which isoenzyme specifically inhibit the reactivation of dissociated LDH. Inhibition was abolished by treating with proteases. Additionally, NAD⁺ and NADH were found to be antagonists of the inhibitors. The heart-type enzyme-inhibitor system is especially susceptible for NADH whereas NAD⁺ affects the inhibition only slightly. The muscle-type system shows the opposite behavior, e.g., the completely inhibited system can be fully reactivated by NAD⁺ but not by NADH. These findings together with first kinetic studies suggest a possible specific regulatory function of these peptides.     

Design of a cytochrome P450BM3 reaction system linked by two‐step cofactor regeneration catalyzed by a soluble transhydrogenase and glycerol dehydrogenase

A cytochrome P450BM3‐catalyzed reaction system linked by a two‐step cofactor regeneration was investigated in a cell‐free system. The two‐step cofactor regeneration of redox cofactors, NADH and NADPH, was constructed by NAD⁺‐dependent bacterial glycerol dehydrogenase (GLD) and bacterial soluble transhydrogenase (STH) both from Escherichia coli. In the present system, the reduced cofactor (NADH) was regenerated by GLD from the oxidized cofactor (NAD⁺) using glycerol as a sacrificial cosubstrate. The reducing equivalents were subsequently transferred to NADP⁺ by STH as a cycling catalyst. The resultant regenerated NADPH was used for the substrate oxidation catalyzed by cytochrome P450BM3. The initial rate of the P450BM3‐catalyzed reaction linked by the two‐step cofactor regeneration showed a slight increase (approximately twice) when increasing the GLD units 10‐fold under initial reaction conditions. In contrast, a 10‐fold increase in STH units resulted in about a 9‐fold increase in the initial reaction rate, implying that transhydrogenation catalyzed by STH was the rate‐determining step. In the system lacking the two‐step cofactor regeneration, 34% conversion of 50 μM of a model substrate (p‐nitrophenoxydecanoic acid) was attained using 50 μM NADPH. In contrast, with the two‐step cofactor regeneration, the same amount of substrate was completely converted using 5 μM of oxidized cofactors (NAD⁺ and NADP⁺) within 1 h. Furthermore, a 10‐fold dilution of the oxidized cofactors still led to approximately 20% conversion in 1 h. These results indicate the potential of the combination of GLD and STH for use in redox cofactor recycling with catalytic quantities of NAD⁺ and NADP⁺. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Engineering of formate dehydrogenase: synergistic effect of mutations affecting cofactor specificity and chemical stability

Formate dehydrogenases (FDHs) are frequently used for the regeneration of cofactors in biotransformations employing NAD(P)H-dependent oxidoreductases. Major drawbacks of most native FDHs are their strong preference for NAD⁺ and their low operational stability in the presence of reactive organic compounds such as α-haloketones. In this study, the FDH from Mycobacterium vaccae N10 (MycFDH) was engineered in order to obtain an enzyme that is not only capable of regenerating NADPH but also stable toward the α-haloketone ethyl 4-chloroacetoacetate (ECAA). To change the cofactor specificity, amino acids in the conserved NAD⁺ binding motif were mutated. Among these mutants, MycFDH A198G/D221Q had the highest catalytic efficiency (k _cat/K _m) with NADP⁺. The additional replacement of two cysteines (C145S/C255V) not only conferred a high resistance to ECAA but also enhanced the catalytic efficiency 6-fold. The resulting quadruple mutant MycFDH C145S/A198G/D221Q/C255V had a specific activity of 4.00?±?0.13 U?mg^?1 and a K _{m, NADP} ⁺ of 0.147?±?0.020 mM at 30 °C, pH 7. The A198G replacement had a major impact on the kinetic constants of the enzyme. The corresponding triple mutant, MycFDH C145S/D221Q/C255V, showed the highest specific activity reported to date for a NADP⁺-accepting FDH (v _max, 10.25?±?1.63 U?mg^?1). However, the half-saturation constant for NADP⁺ (K _{m, NADP} ⁺ , 0.92?±?0.10 mM) was about one order of magnitude higher than the one of the quadruple mutant. Depending on the reaction setup, both novel MycFDH variants could be useful for the production of the chiral synthon ethyl (S)-4-chloro-3-hydroxybutyrate [(S)-ECHB] by asymmetric reduction of ECAA with NADPH-dependent ketoreductases.     

Efficient Production of (R)-2-Hydroxy-4-Phenylbutyric Acid by Using a Coupled Reconstructed d-Lactate Dehydrogenase and Formate Dehydrogenase System

Background

(R)-2-Hydroxy-4-phenylbutyric acid [(R)-HPBA] is a key precursor for the production of angiotensin-converting enzyme inhibitors. However, the product yield and concentration of reported (R)-HPBA synthetic processes remain unsatisfactory.

Methodology/Principal Findings

The Y52L/F299Y mutant of NAD-dependent d-lactate dehydrogenase (d-nLDH) in Lactobacillus bulgaricus ATCC 11842 was found to have high bio-reduction activity toward 2-oxo-4-phenylbutyric acid (OPBA). The mutant d-nLDH^Y52L/F299Y was then coexpressed with formate dehydrogenase in Escherichia coli BL21 (DE3) to construct a novel biocatalyst E. coli DF. Thus, a novel bio-reduction process utilizing whole cells of E. coli DF as the biocatalyst and formate as the co-substrate for cofactor regeneration was developed for the production of (R)-HPBA from OPBA. The biocatalysis conditions were then optimized.

Conclusions/Significance

Under the optimum conditions, 73.4 mM OPBA was reduced to 71.8 mM (R)-HPBA in 90 min. Given its high product enantiomeric excess (>99%) and productivity (47.9 mM h⁻¹), the constructed coupling biocatalysis system is a promising alternative for (R)-HPBA production.     

Quantifying the cellular NAD+ metabolome using a tandem liquid chromatography mass spectrometry approach

Introduction

Nicotinamide adenine dinucleotide (NAD⁺) is an essential pyridine nucleotide that serves as a key hydride transfer coenzyme for several oxidoreductases. It is also the substrate for intracellular secondary messenger signalling by CD38 glycohydrolases, DNA repair by poly(adenosine diphosphate ribose) polymerase, and epigenetic regulation of gene expression by a class of histone deacetylase enzymes known as sirtuins. The measurement of NAD⁺ and its related metabolites (hereafter, the NAD⁺ metabolome) represents an important indicator of cellular function.

Objectives

A study was performed to develop a sensitive, selective, robust, reproducible, and rapid method for the concurrent quantitative determination of intracellular levels of the NAD⁺ metabolome in glial and oocyte cell extracts using liquid chromatography coupled to mass spectrometry (LC/MS/MS).

Methods

The metabolites were separated on a versatile amino column using a dual HILIC-RP gradient with heated electrospray (HESI) tandem mass spectrometry detection in mixed polarity multiple reaction monitoring mode.

Results

Quantification of 17 metabolites in the NAD⁺ metabolome in U251 human astroglioma cells could be achieved. Changes in NAD⁺ metabolism in U251 cell line, and murine oocytes under different culture conditions were also investigated.

Conclusion

This method can be used as a sensitive profiling tool, tailoring chromatography for metabolites that express significant pathophysiological changes in several disease conditions and is indispensable for targeted analysis.

     

Regulatory properties of malic enzyme in the oleaginous yeast, Yarrowia lipolytica, and its non-involvement in lipid accumulation

Malic enzyme (EC 1.1.1.40) converts l-malate to pyruvate and CO₂ providing NADPH for metabolism especially for lipid biosynthesis in oleaginous microorganisms. However, its role in the oleaginous yeast, Yarrowia lipolytica, is unclear. We have cloned the malic enzyme gene (YALI0E18634g) from Y. lipolytica into pET28a, expressed it in Escherichia coli and purified the recombinant protein (YlME). YlME used NAD⁺ as the primary cofactor. K_m values for NAD⁺ and NADP⁺ were 0.63 and 3.9 mM, respectively. Citrate, isocitrate and α-ketoglutaric acid (>5 mM) were inhibitory while succinate (5–15 mM) increased NADP⁺- but not NAD⁺-dependent activity. To determine if fatty acid biosynthesis could be increased in Y. lipolytica by providing additional NADPH from an NADP⁺-dependent malic enzyme, the malic enzyme gene (mce2) from an oleaginous fungus, Mortierella alpina, was expressed in Y. lipolytica. No significant changes occurred in lipid content or fatty acid profiles suggesting that malic enzyme is not the main source of NADPH for lipid accumulation in Y. lipolytica.     

Kinetics of a hollow fiber dehydrogenase reactor

A hollow fiber module was used as a reactor for conversion of ethanol to acetaldehyde in the presence of horse liver alcohol dehydrogenase as catalyst. Mass transport rates for NAD⁺, the overall acetaldehyde generation rate, catalyst effectiveness factors, and the overall order of the reaction with respect to NAD⁺ concentration were measured. A coupled-substrate reactor with continuous in situ regeneration of cofactor was also examined. Two substrates of opposite redox state were added simultaneously to the feed stream. NADH and acetaldehyde concentrations were monitored in the effluent stream. The cofactor recycle number, or ratio of moles of product to moles of NADH produced, exceeded 10,000 under certain conditions. While decreasing the NAD⁺ concentration in the feed stream decreased reactor productivity somewhat, it greatly enhanced the ratio of product formed per mole of NAD⁺ fed to the reactor. It is suggested that high cofactor costs in dehydrogenase reactors may be overcome with efficient in situ regeneration and secondary recovery and recycling of cofactor from the process stream.     

Design of recycling system for poly(methyl methacrylate) (PMMA). Part 1: recycling scenario analysis

Introduction

In this series of papers, we present a poly(methyl methacrylate) (PMMA) recycling system design based on environmental impacts, chemical hazards, and resource availability. We evaluated the recycling system by life cycle assessment, environment, health, and safety method, and material flow analysis.

Purpose

Previous recycling systems have not focused on highly functional plastics such as PMMA, partly because of lower available volumes of waste PMMA compared with other commodity plastics such as polyethylene or polypropylene. However, with the popularization of PMMA-containing products such as liquid crystal displays, the use of PMMA is increasing and this will result in an increase in waste PMMA in the future. The design and testing of recycling systems and technologies for treating waste PMMA is therefore a high research priority. In this study, we analyze recycling of PMMA monomers under a range of scenarios.

Methods

Based on the differences between PMMA grades and their life cycles, we developed a life cycle model and designed a range of scenarios for PMMA recycling. We obtained monomer recycling process inventory data based on the operational results of a pilot plant. Using this process inventory data, we quantified life cycle greenhouse gas (LC-GHG) emissions and fossil resource consumption, and we calculated the LIME single index.

Results and discussion

PMMA produces more than twice the amount of GHG emissions than other commodity resins. Through scenario and sensitivity analyses, we demonstrated that monomer recycling is more effective than mechanical recycling. Operational modifications in the monomer recycling process can potentially decrease LC-GHG emissions.

Conclusions

Highly functional plastics should be recycled while maintaining their key functions, such as the high transparency of PMMA. Monomer recycling has the potential to achieve a closed-loop recycling of PMMA.