HE 1471 ED: Jolly PROD. TYPE: COM pp: 1-12 (col.fig.: 3) PAGN: Murthy.N -- SCAN: Oli ARTICLE IN PRESS

International Journal of Energy ( ) – www.elsevier.com/locate/ijhydene 1 Green alga hydrogen production: progress, challenges and

3 prospects

Anastasios Melis ∗ 5 Department of Plant and Microbial Biology, University of California at Berkeley, 411 Koshland Hall, Berkeley, CA 94720-3102, USA 7

1. Prologue production were steadily sustained for about 60 h in the light, 41 but gradually declined thereafter. In the course of such hy- 9 The ability of green algae to photosynthetically gener- drogen production, cells consumed signiÿcant amounts of 43 ate molecular hydrogen has captivated the fascination and internal starch and protein [4]. Such catabolic reactions may 11 interest of the scientiÿc community for the past 60 years sustain, directly or indirectly, the hydrogen-production pro- 45 due to the fundamental and practical importance of the pro- cess. The use of green algae in this “two-stage photosyn- 13 cess. In nature—under relevant physiological conditions— thesis and H2-production” method does not entail the gen- 47 the photosynthetic activity of the green alga “hydrogenase” eration of toxic or environmentally disturbing byproducts, 15 was only transient in nature. It lasted from several seconds and it may even oDer the advantage of value-added prod- 49 to a few minutes due to the fact that and ucts as a result of the mass cultivation of green algae. The

17 H2O-oxidation entail the release of molecular O2. Oxygen work discusses the physiology, biochemistry and molecular 51 is a positive suppressor of hydrogenase gene expression, biology that underline this sustained green alga hydrogen 19 and a powerful inhibitor of the [Fe]-hydrogenase. Given the production process. 53 acute oxygen sensitivity of the hydrogenase and the prevail- In spite of the recently achieved signiÿcant breakthrough 21 ing oxidative environmental conditions on earth, questions in H2-photoproduction, rates were only about 15% of the bi- 55 have been asked as to whether the hydrogenase is anything ological theoretical maximum, suggesting room for substan- 23 more than a relic of the evolutionary past of the chloroplast tial improvement in the yield of the process. Similarly, other 57 in green algae, and whether this enzyme and the process of improvements must be made to maintain the continuity of 25 photosynthesis can ever be utilized to generate hydrogen for production and to optimize the solar conversion eFciency 59 commercial purposes [1]. of the algae under mass culture conditions. The continuity 27 Deprivation of sulfur-nutrients in green algae causes a of the process needs to be addressed, as H2-production by 61 reversible inhibition in the activity of oxygenic photosyn- S-deprivation of the algae is time limited. The yield begins 29 thesis. In the absence of sulfur from the growth medium, to level oD after about 60 h of production. After about 100 h 63 protein biosynthesis is impeded, and the green algae cannot of S-deprivation, the algae need to go back to normal pho- 31 perform the required turnover of the photosystem-II (PSII) tosynthesis in order to be rejuvenated by replenishing en- 65 D1=32 kDa reaction center protein [2]. Under S-deprivation, dogenous substrate [5]. Furthermore, optical problems as- 33 the photochemical activity of PSII declines, and rates of pho- sociated with the size of the chlorophyll antenna and the 67 tosynthetic oxygen evolution dropbelow those of oxygen light-saturation curve of photosynthesis must be addressed 35 consumption by respiration [3]. In consequence, sealed cul- [6] before the relevant green algae can achieve high photo- 69 tures of the green alga Chlamydomonas reinhardtii become synthetic solar conversion eFciencies in mass culture. Ad- 37 anaerobic in the light. Following anaerobiosis, they sponta- ditional challenges that must be successfully addressed in- 71 neously induce a novel “hydrogenase pathway” of electron clude ways for the recycling of photobioreactor components 39 transport in theUNCORRECTED chloroplast and photosynthetically produce and minimizing the cost PROOF of the alga growth nutrients, as 73 hydrogen. For the ÿrst time, substantial rates of hydrogen these two items constitute 80–85% of the overall cost of a commercial H2-production operation. There is a need to 75 form a working relationshipbetween the scientists who de- ∗ Tel.: +1-510-642-8166; fax: +1-510-642-4995. velop microalga-based applications and the energy-related 77 E-mail address: [email protected] (A. Melis). industries. In each of these areas, the work summarizes the

0360-3199/02/$ 22.00 ? 2002 Elsevier Science Ltd. All rights reserved. PII: S0360-3199(02)00110-6 HE 1471 ARTICLE IN PRESS 2 A. Melis / International Journal of Hydrogen Energy ( ) –

1 progress achieved so far, provides an assessment of the state • This incompatibility in the simultaneous O2 and H2 pho- of the art in photobiological H2-production, and oDers a toproduction remained a problem in 60 years of related 53 3 discussion of the challenges that have been encountered. research. Finally, it oDers a view of the prospects and promises of Bio- 5 Hydrogen in general, and photobiological hydrogen in par- ticular, as important players in the coming Hydrogen Age. 3. Photobiological H2-production 55

3.1. 2H2O → 2H2 + O2

2. Perspective 3.1.1. State of the art 57 The process of photosynthetic H2-production with elec- Hydrogen metabolism is primarily the domain of bacte- trons derived from H2O (also referred to as “biophotolysis” 59 9 ria and microalgae. Within these groups, it involves many [41,42]) entails H2O-oxidation and a light-dependent trans- taxonomically diverse species, a variety of enzymes and fer of electrons to the [Fe]-hydrogenase, leading to the syn- 61 11 metabolic pathways and processes [7–9]. The photosynthetic thesis of molecular H2. Electrons are generated upon the metabolism of hydrogen in green algae was discovered by photochemical oxidation of H2O by PSII. These are trans- 63 13 Hans GaDron [10–14] who observed that, under anaero- ferred through the thylakoid membrane electron-transport bic conditions, green algae can either use H2 as electron chain and, via PSI and ferredoxin, are donated to the HC 65 15 donor in the CO2 ÿxation process in the dark, or evolve H2 cluster of [Fe]-hydrogenase [35]. Protons (H+) are the termi- in the light. GaDron’s original observations were extended nal acceptors of these photosynthetically generated electrons 67 17 to many green algae, including Scenedesmus obliquus [14 in the chloroplast. The process does not involve CO2-ÿxation –16], Chlorella fusca [17–20], and Chlamydomonas rein- or energy storage into cellular metabolites. This process re- 69 19 hardtii [21–24], among others. sults in the simultaneous production of O2 and H2 with Historically, hydrogen evolution activity in green algae aH2:O2 = 2:1 ratio [24,43]. This mechanism holds the 71 21 was induced upon a prior anaerobic incubation of the promise of generating hydrogen continuously and eFciently cells in the dark [17,25–27]. A hydrogenase enzyme [9] through the solar conversion ability of the photosynthetic 73 23 was expressed under such incubation and catalyzed, with apparatus. high speciÿc activity, a light-mediated H2-evolution. The 25 monomeric form of the enzyme, reported to belong to the class of [Fe]-hydrogenases [28–36], is nuclear encoded. 3.1.2. Challenges 75 27 However, the mature protein is localized and functions In the absence of provision for the active removal of oxy- in the chloroplast stroma of the unicellular green algae gen, this mechanism can operate only transiently, as molec- 77 29 [31]. Light absorption by the photosynthetic apparatus is ular oxygen is a powerful inhibitor of the enzymatic reaction essential for the generation of molecular hydrogen, since and a positive suppressor of [Fe]-hydrogenase gene expres- 79 31 light-energy facilitates the endergonic transport of electrons sion. At present, this direct mechanism has limitations as a to ferredoxin. Photosynthetic ferredoxin is the physiologi- tool of further research and for practical application, mainly 81 33 cal electron donor to the [Fe]-hydrogenase and, therefore, due to the great sensitivity of the [Fe]-hydrogenase to O2, links the soluble [Fe]-hydrogenase to the electron transport which is evolved upon illumination by the water-oxidizing 83 35 chain in the green alga chloroplast [35,37]. The absence of reactions of PSII [5]. An additional problem, assuming that the mutual incompatibility of O2 and H2 co-production is 85 CO2 enhanced the light-driven H2-production, suggesting a 37 competition for electrons between the CO -ÿxation and the overcome, entails the separation of the two gases, a costly 2 and technologically challenging feat. 87 H2-production processes [38]. 39 The ability of green algae to photosynthetically generate

molecular H2 has captivated the fascination and interest of 3.1.3. Prospects 41 the scientiÿc community because of the fundamental and Nevertheless, it has been shown that such O2 and H2 89 practical importance of the process [1]. Below is an item- co-production can be prolonged under conditions designed 43 ized list of the properties and promise of photosynthetic to actively remove O2 from the reaction mixture. Indeed, 91

H2-production, and the challenges that are encountered in Greenbaum and co-workers [24,25,40] have sustained a pho- the process: tosynthetic H2O → H2 process continuously for days upon 93 45 sparging the reaction mixture with helium, thus removing • PhotosynthesisUNCORRECTED in green algae can operate with a photon from the vicinity of the cellsPROOF the photosynthetic gas prod- 95 47 conversion eFciency of ¿ 80% [39]. ucts (O2 and H2). Along this line, eDorts are under way to • Microalgae can evolve H2 photosynthetically, with a pho- mutagenize the [Fe]-hydrogenase with the objective of al- 97 49 ton conversion eFciency of ¿ 80% [40]. tering or removing the oxygen sensitivity of the enzyme [5],

• Molecular O2 acts as a powerful and eDective switch by thereby permitting a light-driven O2 and H2 co-production 99 51 which the H2-production activity is turned oD. in the green algae. HE 1471 ARTICLE IN PRESS A. Melis / International Journal of Hydrogen Energy ( ) – 3

1 3.2. Endogenous substrate → H2 but reversible decline in the rate of oxygenic photosynthesis [2], but does not aDect the rate of mitochondrial respiration 55 3.2.1. State of the art [3]. In sealed and S-deprived cultures, the absolute activity 3 Apart from the above described PSII-dependent of photosynthesis becomes less than that of respiration. Such 57 H2-photoproduction, which involves H2O as the source of imbalance in the photosynthesis–respiration relationship by 5 electrons and, in the absence of CO2, produces 2:1 stoi- S-deprivation resulted in net consumption of oxygen by the 59 chiometric amounts of H2 and O2, an alternative source of cells causing anaerobiosis in the growth medium. It was 7 electrons has been described in the literature. Catabolism shown that expression of the [Fe]-hydrogenase is elicited 61 of endogenous substrate and the attendant oxidative car- in the light under these conditions, autonomically leading 9 bon metabolism in green algae may generate electrons for to H2-production by the algae [3,5]. For the ÿrst time, un- 63 the photosynthetic apparatus [44]. Electrons from such der S-deprivation, it was possible to photoproduce and to 11 endogenous substrate catabolism feed into the plasto- accumulate bulk amounts of H2 gas, emanating as bubbles 65 quinone pool between the two photosystems [45,46]. An from the green alga cultures, a sustainable process that con- 13 NAD(P)H-plastoquinone oxidoreductase that feeds elec- tinued for a few days. Thus, progress was achieved by cir- 67 trons into the plastoquinone pool has recently been iden- cumventing the sensitivity of the [Fe]-hydrogenase to O2 15 tiÿed in many vascular plant chloroplasts [47–52] but so through a temporal separation of the reactions of O2 and H2 69 far only from the green alga Nephroselmis olivacea [53]. photoproduction, i.e., by the so-called “two-stage photosyn- 17 Light absorption by PSI and the ensuing electron trans- thesis and H2-production” process [3]. Application of this 71 port elevates the redox potential of these electrons to the novel two-stage protocol revealed the occurrence of hith- 19 redox equivalent of ferredoxin and the [Fe]-hydrogenase. erto unknown metabolic, regulatory and electron-transport 73 + In this case, protons (H ) act as the terminal electron ac- pathways in the green alga C. reinhardtii [4]. This method 21 ceptor [44,54], thus permitting the generation of molecular may serve as a tool for the elucidation of the green alga 75 H2 [55]. In the presence of DCMU, a PSII inhibitor, this photosynthesis=respiration relationship and biochemistry of 23 process generates 2:1 stoichiometric amounts of H2 and hydrogen-related metabolism. Upon further reÿnement, it 77 CO [56]. Thus, following a dark-anaerobic incubation of 2 may also serve in the generation of H2 gas for the agri- 25 the culture (induction of the [Fe]-hydrogenase), initially culture, chemical and fuel industries. BriePy, the tempo- 79 substantial rates of H2-production can be detected upon ral sequence of events in this two-stage photosynthesis and 27 illumination of the algae in the presence of DCMU [31,35]. H2-production process is as follows: 81

3.2.2. Challenges and prospects (a) Green algae are grown photosynthetically in the light 29 The regulation of endogenous substrate catabolism and (normal photosynthesis) until they reach a density of 83 the attendant supply of electrons to the electron transport 3–6 million cells=ml in the culture. 31 chain of photosynthesis are not well understood. Whereas (b) Sulfur deprivation is imposed upon the cells in the 85 rates of H2O oxidation by the photosynthetic apparatus growth medium, either by carefully limiting sulfur sup- 33 can be measured continuously and precisely, measurements ply so that it is consumed entirely, or by permitting cells 87 of electron transport supported by endogenous substrate to concentrate in the growth chamber prior to medium 35 catabolism and NAD(P)H-plastoquinone oxidoreductase replacement with one that lacks sulfur nutrients. Cells 89 activity are more diFcult to make. H2-photoproduction respond to this S-deprivation by fundamentally altering 37 with anaerobically incubated and DCMU-poisoned chloro- photosynthesis and cellular metabolism in order to sur- 91 plasts [35] suggests that, initially, substantial rates of vive [57–59]. Noteworthy in this respect is the 10-fold 39 H2-production can be detected. However, this process could increase in cellular starch content during the ÿrst 24 h 93 not be sustained for signiÿcant periods of time [4], suggest- of S-deprivation [4,60]. 41 ing limitation(s) in the capacity of the electron transport (c) S-deprivation exerts a distinctly diDerent eDect on the 95 reactions associated with the NAD(P)H-plastoquinone cellular activities of photosynthesis and respiration (Fig. 43 oxidoreductase activity. Nevertheless, the prospect of en- 1A). The capacity of oxygenic photosynthesis declines 97 dogenous starch, protein and lipid catabolism feeding elec- quasi-exponentially, with a half-time of 15–20 h, to a 45 trons into the plastoquinone pool—and thus contributing value about 10% of its original rate [2]. However, the 99 to H2-photoproduction—is important enough to warrant capacity for cellular respiration remains fairly constant 47 further investigation to fully assess its potential. In this over the S-deprivation period [3]. In consequence, the 101 respect, the tools of molecular biology could come to bear absolute activity of photosynthesis drops below the level 49 in eDorts to increaseUNCORRECTED the capacity of this important process. of respiration after aboutPROOF 24 h of S-deprivation (Fig. 103 1A). Following this cross-point between photosynthesis 3.3. Two-stage photosynthesis and H -production 2 and respiration, sealed cultures of S-deprived C. rein- 105 51 3.3.1. Progress hardtii quickly consume all dissolved oxygen and be- Recent progress has shown that lack of sulfur nutrients come anaerobic [5], even though they are maintained 107 53 from the growth medium of C. reinhardtii causes a speciÿc under continuous illumination. HE 1471 ARTICLE IN PRESS 4 A. Melis / International Journal of Hydrogen Energy ( ) –

100 Cycle ACycle B Cycle C 80

60

40 gas collected, mL 2

H 20

+S +S 0 0 50 100 150 200 250 300 350 Time, h

Fig. 2. Cycling of Stages in C. reinhardtii. Reversibility and re- producibility of the S-deprivation and H2-production sequence of events was demonstrated by cycling a single C. reinhardtii culture between the two stages (oxygenic photosynthesis in the presence of S and H2-production in its absence) for up to three full cycles. At the end of H2-production in cycle A, the culture was supplemented with inorganic S (t = 100 h). The latter caused prompt inhibition in H2-production (beginning of cycle B), because of the ensuing activation of oxygenic photosynthesis (100 ¡t¡130 h). The cul- ture was driven to anaerobiosis upon a subsequent S-deprivation (130 ¡t¡160 h) and H2-production (160 ¡t¡220 h). Cycle C shows a third temporal cycling of the Stage 1 → Stage 2 process. When indicated, sulfur was added as sulfate salts in the growth Fig. 1. Photosynthesis, respiration and H -production as a function 2 medium to a ÿnal concentration of 0:4 mM. (From [5].) of sulfur-deprivation in C. reinhardtii. (A) Absolute activity of oxygenic photosynthesis (P, open circles) and respiration (R, solid circles) in C. reinhardtii suspended in media lacking a source of sulfur. The rate of cellular respiration (R) was recorded in the dark, thesis (H2O-oxidation, O2-evolution and biomass accumu- followed by measurement of the light-saturated rate of photosyn- lation). In the absence of both S and O2, photosynthesis in 19 6 thesis (P). Cultures at 0 h contained 2:2×10 cells=ml. (B) H2 gas C. reinhardtii slips into the H2-production mode. Reversible production and accumulation by C. reinhardtii cells suspended in application of the switch (presence=absence of S) per- 21 media lacking sulfur. Gases were collected in an inverted burette mits the algae to alternate between O2- and H2-production and measured from the volume of water displacement. (cycling of the stages, Fig. 2), thus bypassing the incom- 23

patibility and mutually exclusive nature of the O2- and H2-producing reactions. Interplay between oxygenic photo- 25 1 (d) Under S-deprivation conditions, sealed (anaerobic) cul- synthesis, mitochondrial respiration, catabolism of endoge- tures of C. reinhardtii induce the [Fe]-hydrogenase in nous substrate, and electron transport via the hydrogenase 27 pathway is essential for this light-mediated H2-production 3 the light and produce H2 gas (Fig. 1B). Induction of the [Fe]-hydrogenase will take place in the light or dark process. The release of H2 gas serves to sustain baseline lev- 29 els of oxygenic photosynthesis, which feeds electrons into 5 upon S-deprivation. However, H2-production is strictly a light-dependent process. The rate of photosynthetic the [Fe]-hydrogenase for the generation of H2. This residual 31 oxygenic photosynthesis, via the molecular O2 released, 7 H2-production was about 2 ml=l culture=h and was sus- tained in the 24–96 h period. The rate gradually de- is coupled to mitochondrial respiration (Fig. 3), which in 33 9 clined thereafter. eDect scavenges the baseline amounts of photosynthetic O2. The bioenergetic purpose of the two organelles is the gener- 35 (e) In the course of such H2 gas production (S-deprivation), 11 cells consumed signiÿcant amounts of internal starch ation of ATP [61], needed for the survival of the organism and protein [4]. Such catabolic reactions apparently sus- under the protracted sulfur-deprivation stress conditions. 37 13 tain, directlyUNCORRECTED or indirectly, the H2-production process. PROOF 3.3.2. Challenges Evidently, the absence of sulfur nutrients from the growth There are speciÿc improvements that need to be made to 39 15 medium of algae acts as a metabolic switch, one that selec- increase the likelihood of successful commercial exploita-

tively and reversibly inhibits photosynthetic O2 production. tion of the method. Foremost, the continuity of the process 41 17 Thus, in the presence of S, green algae do normal photosyn- needs to be addressed, as H2-production by S-deprivation HE 1471 ARTICLE IN PRESS A. Melis / International Journal of Hydrogen Energy ( ) – 5

+ + ing of the process (photobioreactors) to an industrial facility 27 4H 4H level. PSII PSI 2H O ------> ------> Fe-H ase 2 4 electrons 2 4. Maximizing solar conversion eciencies under mass 29 culture conditions O 2H chloroplast 2 2 Cultures growing under full sunlight, when productivity 31 ought to be at a maximum, have disappointingly low so- lar conversion eFciencies. The reason for this ineFciency 33 Cyt bc Comp I is that green algae have a genetic tendency to assemble O <------<------2NADH <---- [4e -] 2 Cyt Ox large arrays of light-absorbing chlorophyll (Chl) antenna 35 molecules in their photosystems. At high solar intensities, 2H O the rate of photon absorption by the Chl antennae of the ÿrst 37 2 mitochondria few layers of cells in the culture, or pond, far exceeds the Fig. 3. Coordinated photosynthetic and respiratory electron trans- rate at which photosynthesis can utilize them, resulting in 39 dissipation and loss of the excess photons as Puorescence or port and coupled phosphorylation during H2-production. Photo- synthetic electron transport delivers electrons upon photooxidation heat. Upto 95% of absorbed photonscould thus be wasted, 41 of H2O to the hydrogenase, leading to photophosphorylation and reducing solar conversion eFciencies and cellular produc- H2-production. The oxygen generated by this process serves to tivity to unacceptably low levels. In addition to the wasteful 43 drive the coordinate oxidative phosphorylation during mitochon- dissipation of excitation, and due to the high rate of photon drial respiration. Electrons for the latter ([4e]) are derived upon absorption by the photosynthetic apparatus, cells at the sur- 45 endogenous substrate catabolism, which yields reductant and CO2. face of the mass culture are subject to severe photoinhibition Release of molecular H2 by the chloroplast enables the sustained of photosynthesis [62,63], a phenomenon that compounds 47 operation of this coordinated photosynthesis–respiration function losses in productivity. Moreover, cells deeper in the culture in green algae and permits the continuous generation of ATP by the two bioenergetic organelles in the cell. (Adapted from [1].) are deprived of much needed sunlight, as this is strongly 49 attenuated due to ÿltering [6,64,65]. A genetic tendency of the algae to assemble large arrays of light-absorbing Chl an- 51 tenna molecules in their photosystems is a survival strategy 1 of the algae is time limited. As evident from the results of and a competitive advantage in the wild, where light is often 53 Fig. 2 [5], the yield begins to level oD after about 80 h of limiting. Obviously, this property of the algae is detrimental 3 S-deprivation. After about 100 h of S-deprivation, the algae to the yield and productivity of a mass culture. 55 need to go back to normal photosynthesis in order to be re- Theoretically, a smaller, or truncated, Chl antenna size of 5 juvenated by replenishing endogenous substrate. Moreover, the photosystems in the chloroplast of the microalgae could 57 the yield of H2 gas accumulation (about 2 ml=h=l culture) alleviate the optical shortcomings associated with a fully 7 represents about 15% of the photosynthetic capacity of the pigmented Chl antenna, because it will minimize the over- 59 cells, when the latter is based on the capacity for O2 evolu- absorption of bright incident sunlight by the photochemical 9 tion under physiological conditions [3]. The relatively slow apparatus of the algae. A truncated Chl antenna will dimin- 61 rate of H2-production suggests a rate-limiting step in the ish the overabsorption and wasteful dissipation of excitation 11 overall process, one that needs to be identiÿed and over- energy by the cells, and it will also diminish photoinhibi- 63 come. tion of photosynthesis at the surface of the culture. More- over, a truncated Chl antenna size will alleviate the rather 65 13 3.3.3. Prospects severe gradient of light and mutual cell shading and it will

The discovery of sustainable H2-production that bypasses permit a more uniform illumination of the cells in the mass 67 15 the sensitivity of the [Fe]-hydrogenase to O2 and produces culture. Such altered optical properties of the cells would essentially pure H2 [3] is a signiÿcant development in this result in much greater photosynthetic productivity and bet- 69 17 ÿeld. It may serve as a tool in the elucidation of the four-way ter solar utilization eFciency in the culture. Indeed, actual interplay between the processes of oxygenic photosynthesis, experiments [6,66] showed that a smaller Chl antenna size 71 19 mitochondrial respiration, regulation of cellular metabolism, results in a relatively higher light intensity for the saturation and electron transport via the [Fe]-hydrogenase pathway for of photosynthesis in individual cells but, concomitantly, in 73 21 the generation ofUNCORRECTED H2. It may also lead to the commercial a 3-fold greater productivity PROOF of the mass culture. Thus, ap- exploitation of green algae for the manufacturing of a clean proaches by which to genetically truncate the Chl antenna 75 23 and renewable fuel. Importantly, it raises to a meaningful size of photosynthesis in green algae merit serious consid- level of questions about the optical properties of the cells in eration. 77 25 mass culture (maximizing green alga solar conversion eF- The Chl antenna size of the photosystems is not constant. ciencies under mass culture conditions) and the engineer- Rather a parameter known as “excitation pressure” regu- 79 HE 1471 ARTICLE IN PRESS 6 A. Melis / International Journal of Hydrogen Energy ( ) –

1 Large Chl antenna size (Fully pigmented cells) 0.8 Truncated Truncated Chl antenna: 0.6 Chl antenna PSII: 60 Chl PSI: 105 Chl Low excitation pressure 0.4 Fully Mechanism for the Regulation pigmented: of the Chl Antenna Size 0.2 Fully pigmented PSII: 350 Chl in photosynthesis PSI: 300 Chl Photon use efficiency High excitation pressure 0 0 1000 2000 3000 Irradiance, µmol photons m-2 s-1

Small Chl antenna size Fig. 5. Photosynthetic solar photon use eFciency as a function of (Truncated Chl antenna) irradiance in fully pigmented and truncated Chl antenna D. salina. Under bright sunlight (2000–2500 mol photons=m2=s), fully pig- mented cells (PSII=350 Chl; PSI=300 Chl) show a mere 5–10% Fig. 4. Molecular mechanism for the regulation of the Chl antenna solar conversion eFciency. Under the same conditions, cells with a size in the photosynthetic apparatus. A sensory and signal trans- truncated Chl antenna size show a 45% solar conversion eFciency. duction pathway, highly conserved in all photosynthetic organisms, (Adapted from [6].) regulates the Chl antenna size of the photosystems. Within limits, deÿned by genetic and structural considerations, the response is a compensation reaction to the level of irradiance. on the photosynthetic eFciency and productivity of the cells under mass culture conditions. Fig. 5 shows measurements 35 of the photon use eFciency as a function of incident irra- 1 lates the size and composition of the light-harvesting Chl an- diance in fully pigmented (solid circles) and truncated Chl 37 tenna during chloroplast development [67–70]. “Excitation antenna cells (open circles). It is evident that, at low intensi- 3 pressure” is generated whenever there is imbalance between ties (¡ 100 mol photon=m2=s), both cell types performed 39 the supply and consumption of light energy in the photo- with a relatively high photon use eFciency. At increasing 5 synthetic apparatus. Such persistent imbalance is communi- incident intensities, however, photon use eFciencies for the 41 cated to the metabolic machinery of the chloroplast via the fully pigmented cells declined sharply, reaching a value of 7 redox state of the plastoquinone pool [70–72]. In general, ∼ 0:05 (5%) at an irradiance corresponding to full sunlight 43 low light intensity during growth results in low excitation (2500 mol photon=m2=s). The cells with the truncated Chl 9 pressure, a condition that promotes a large Chl antenna size antenna size exhibited a smaller decline in photon use ef- 45 for both PSII and PSI. Growth under high light intensities ÿciency with irradiance. This decline was noticeable only 11 results in higher excitation pressure, a condition that elicits at intensities greater than 500 mol photon=m2=s, reaching 47 the assembly of a smaller Chl antenna size. This regulatory a value of ∼ 0:45 at the intensity of full sunlight [6]. It is 13 mechanism is known to function in all organisms of oxy- concluded that green algae with a truncated Chl antenna size 49 genic and anoxygenic photosynthesis [68,73,74]. The func- are indispensable in eDorts to substantially increase photo- 15 tion of this highly conserved mechanism is depicted in Fig. synthetic eFciencies and the yield of H2-production in pho- 51 4. An example of the operation of this molecular mechanism tobioreactors under mass culture conditions. 17 was provided in work from this and other laboratories. In these reports, the Chl antenna size of PSII was shown to be 19 as large as 460 Chl molecules in fully pigmented green al- 5. Genes for the regulation of the Chl antenna size 53 gae and as small as 60 Chl molecules in cells stressed upon 21 continuous excitation pressure [39,75,76]. Adjustments of The foregoing clearly show that, for purposes of biomass the Chl antenna size in response to irradiance are essentially or H2-production under ambient sunlight conditions, it is im- 55 23 a compensation reaction of the chloroplast as they are in- portant to identify genes that confer a truncated Chl antenna versely related to the incident intensity. In principle then, it size in the model green alga C. reinhardtii. Once a library 57 25 should be possible to genetically interfere with the relevant of such genes is at hand, overexpression or down-regulation regulatory mechanism (Fig. 4) and, in transformant green of expression of these genes, as needed, can be applied to 59 27 algae, to direct the chloroplast biosynthetic and assembly other green algae that might be suitable for commercial ex- activities towardUNCORRECTED a permanently truncated Chl antenna size. ploitation and H2-production. PROOF 61 29 The utility of the small Chl antenna size in maximiz- ing solar conversion eFciencies was demonstrated in recent 5.1. Progress 31 studies [6,65]. Excitation pressure was used as a tool to gen- erate green algae (Dunaliella salina) with a truncated Chl The chlorophyll a (Chl a) oxygenase (CAO) gene en- 63 33 antenna size. These cultures were used to obtain information codes a chloroplast enzyme that catalyzes the last step in HE 1471 ARTICLE IN PRESS A. Melis / International Journal of Hydrogen Energy ( ) – 7

Table 1 Photosystem Chl antenna size in wild type and three Chlamydomonas reinhardtii mutant strains

Wild type cbs3 (Chl b-less) npq2=lor1 (Lut, tla1 Goal (minimum Chl Vio & Neo-less) antenna size) Chl-PSII 230 90 125 115a 37 Chl-PSI 240 289 294 160a 95 The cbs3 strain lacks Chl b and was isolated upon DNA insertional mutagenesis [78]. The npq2=lor1 strain lacks all ÿ; -carotenoids as well as the ÿ; ÿ-epoxycarotenoids. It contains zeaxanthin but lacks lutein, violaxanthin and neoxanthin from its thylakoid membranes [80]. The tla1 strain was isolated upon DNA insertional mutagenesis [81]. Note that the tla1 transformant has the smallest combined Chl antenna size of the three mutants described. Numbers show the Chl antenna size, i.e., the Chl (a and b) molecules speciÿcally associated with each photosystem.

1 the Chl biosynthetic pathway, namely the conversion of Chl This truncated light-harvesting Chl antenna (tla1) mutant a into Chl b. A mutant with inactivated CAO would be apparently has a defect in the regulatory mechanism shown 45 3 unable to synthesize Chl b, thereby lacking this auxiliary in Fig. 4, the result of which is inability to produce a large light-harvesting pigment. The assembly, organization and Chl antenna size under any growth conditions. Table 1 shows 47 5 function of the photosynthetic apparatus was recently inves- that both the Chl antenna size of PSII and PSI were smaller tigated in wild type and a chlorophyll (Chl) b-less mutant in the tla1 strain. This work provided further evidence to 49 7 of the unicellular green alga C. reinhardtii, generated by show that transformation of green algae can also be used as DNA insertional mutagenesis [77]. It was shown that lack a tool by which to genetically interfere with the molecular 51 9 of Chl b diminished the PSII functional Chl antenna size mechanism (Fig. 4) for the regulation of the Chl antenna size from 230 Chl (a and b) to about 95 Chl a molecules [78]. in green algae (Kanakagiri, Polle and Melis, unpublished). 53 11 However, the functional Chl antenna size of PSI remained fairly constant at about 290 Chl molecules, independent of 5.2. Prospects 13 the presence of Chl b (Table 1). aPolle, Kanakagiri and Melis, unpublished. This work Identiÿcation of three genes that confer a truncated 55 15 provided evidence to show that transformation of green al- Chl antenna size in the photosynthetic apparatus is an- gae [79] can be used as a tool by which to interfere with other signiÿcant development in the direction toward 57 17 the biosynthesis of speciÿc pigments and, thus, to gener- cost-eDective commercialization of green algae for biomass

ate mutants exhibiting a permanently truncated Chl antenna and H2-production. Most promising in this respect is the 59 19 size. In support of the role of CAO in the Chl antenna size cloning of the TLA1 regulatory gene. A complete genomic of photosynthesis, recent work [72] showed that CAO gene and cDNA sequence of TLA1 as well as the amino acid 61 21 expression is highly regulated in vivo according to the Chl sequence of the Tla1 protein are currently at hand (Kanak- antenna size needs of the organism. Thus, the CAO gene agiri and Melis, in preparation). It should be noted that 63 23 may be a target for a truncated Chl antenna size in PSII. this is a ÿrst-time isolation and characterization of a “Chl C. reinhardtii double mutant npq2=lor1 lacks the antenna size” regulatory gene. The TLA1 gene may serve 65 25 ÿ; -carotenoids lutein and loroxanthin as well as all as a molecular tool in the elucidation of the function of the ÿ; ÿ-epoxycarotenoids derived from zeaxanthin (e.g. vi- above (Fig. 4) regulatory mechanism in photosynthesis. It 67 27 olaxanthin and neoxanthin). Thus, the only carotenoids may thus contribute to the identiÿcation of other genes that present in the thylakoid membranes of the npq2=lor1 cells are important in this regulatory process (Fig. 4). Further, 69 29 are ÿ-carotene and zeaxanthin. The eDect of these mutations TLA1 may serve in the truncation of the Chl antenna size and the lack of speciÿc xanthophylls on the Chl antenna in a variety of green algae and, potentially, in non-oxygenic 71 31 size of the photosystems was investigated [80]. In cells of photosynthetic bacteria. the mutant strain, the Chl antenna size of PSII was sub- The ultimate goal of this approach is to develop cus- 73 33 stantially smaller than that of the wild type (Table 1). In tomized strains of green algae, which assemble only the contrast, the Chl antenna size of PSI was not truncated in minimum Chl antenna size of the PSII–core complex (37 75 35 the mutant. This analysis showed that the absence of lutein, Chl) and that of the PSI–core complex (95 Chl molecules) violaxanthin and neoxanthin speciÿcally caused a smaller (Table 1). 77 37 functional Chl antenna size for PSII but not for that of PSI. Thus, xanthophyll-biosynthesisUNCORRECTED genes, such as lycopene PROOF 39 -cyclase and zeaxanthin epoxidase may be targets for a 6. Photobioreactors truncated Chl antenna size in PSII. 41 DNA insertional mutagenesis and screening resulted in The alga culture biotechnology has evolved over the 79 the isolation of a regulatory mutant, the phenotype of which recent past into a commercially viable sector, with many 43 was Chl deÿciency and elevated Chl a=Chl b ratio [81]. companies utilizing both open pond culture systems and 81 HE 1471 ARTICLE IN PRESS 8 A. Melis / International Journal of Hydrogen Energy ( ) –

1 controlled closed photobioreactor-type facilities (see re- serve as a model for the operation of pilot photobioreac- 55 views in [82]). Recent biotechnological improvements tors. Given the current state of the art in photobiological

3 have contributed in the expansion of this industry into H2-production, technical and economic strategies for cycling 57 commodity-scale products, high-value chemicals and fuels of the algal cultures between sulfur-deprivation and supply

5 production. Of the latter, CO2 mitigation eDorts [83–86], (Fig. 2) must be devised. 59 algal biomass [87,88], and potentially hydrogen production 7 [1] have received attention over the past 10 years. In any al- 6.2. Cost analysis

gal H2-production process, however, the cost of the facility 9 and its operation are most important factors. 6.2.1. Progress 61 An important aspect of the design that needs to be con- 6.1. Design and speciÿcations sidered is that the reactor interior must be protected against 63 contamination with alien microorganisms. Thus, the design 11 The photobioreactor design, whether semi-batch of con- and construction of the reactor needs to be modular to per- 65 tinuous Pow, Pat plate or tubular, should be suitable for opti- mit for periodic materials replacement and=or whole reactor 13 mal light exposure of the algae. Useful features include some de-contamination treatments. Moreover, various gas collec- 67 thermal control and provisions for monitoring Pow rates, tion devices must be incorporated, which would remove H2 15 pH, and dissolved [O2], [S] and [H2]. A computer-controlled from the gas-tight sealed bioreactor. Following a thorough 69 system for monitoring and automatic nutrient delivery and design and evaluation process, a most economic and eF- 17 culture dilution is now a routine in the algal biotechnology cient scaled-up(500 l) modular unit was adoptedand is be- 71 industry. Continuous-Pow or batch culturing of microalgae ing tested under ÿeld conditions (Candy and Melis, unpub- 19 is also a routine. Combining this expertise with modiÿca- lished). This modular pilot photobioreactor was exposed to 73 tions to ensure a gas-tight system should be a straightfor- the elements continuously over a 6-month period with sat- 21 ward technical development. isfactory materials performance. Signiÿcant experience was 75

In order to gain maximum H2 yields per unit volume, gained on the growth of the green algae and on the produc- 23 green alga biomass needs to be densely packed. Photo- tion and collection of H2 under mass culture conditions in 77 bioreactors have been designed in the past with the goal this scaled-up pilot reactor. Most important, the pilot pho- 25 of achieving a low-cost, fast-growth and high biomass den- tobioreactor permitted a realistic assessment of construction 79 sity of the culture (¿ 109 cells=ml) (for review see [89,90]). costs and analysis of performance. Such economic analysis 27 Several photobioreactor designs could be suitable for green showed the following cost distribution among the various 81

alga H2-production, including Pat plate, tubular, pond or facility categories, derived from the actual operation of this 29 pool-type, etc. For each of these designs, detailed cost anal- scaled-upmodular unit. 83 yses must be undertaken with a focus on minimizing the 31 expense associated with materials and daily operation, and Photobioreactor materials 45% also for optimizing the yield and collection of H2 gas (see Mineral nutrients 39% 33 below). Critical parameters in this respect include, but not Labor 4% limited to, the light environment, the regional climate and Water supply 4% 35 land area, photobioreactor construction materials, the mech- Land lease 2% anism of biomass mixing, photobioreactor maintenance and Power 1% 37 long-term operational stability with the maximum possible Miscellaneous 5% H2-production output. SuFcient light supply for the cells is 39 essential not only for high-density biomass generation but As a point of reference, actual costs for the construction of 85 −2 also for H2-production through photosynthesis. Hence, light this pilot unit photobioreactor were $0:75 m . These costs 41 limitations must be kept to a minimum. The exact dimen- are substantially lower than the $20–100 m−2 often quoted 87 sions of the modular bioreactor also need to be determined ([82], and references therein) and they probably rePect the 43 for the most eDective utilization of sunlight and surface area. simpliÿed strip-down minimal design, which is necessary 89 In this respect, biomass mixing is important as it ensures and suFcient for the growth of the algal biomass and the

45 uniform dispersion of nutrients, promotes a more uniform collection of H2.91 illumination of the culture, and prevents cell settling. 47 The modular experimental design must be intended for po- 6.2.2. Prospects tential scale-upand use at the commercial and industrial lev- The above preliminary analysis provides a glimpse into 93 49 els and should allowUNCORRECTED for sustained long-term H2-production the relative cost of the componentsPROOF that are necessary and with high yields in minimum volume. An important consid- suFcient to assemble a commercially viable photobiological 95

51 eration in the design of the photobioreactor is that it must H2-production facility. The analysis took into consideration be constructed for the trapping and removal of H2 gas. The the production phase of the operation in California, includ- 97 53 two-stage photosynthesis and H2-production protocol has ing facility maintenance, but does not include costs asso- the advantage of generating pure H2 gas [3], thus it may ciated with the storage, transportation or H2-conversion to 99 HE 1471 ARTICLE IN PRESS A. Melis / International Journal of Hydrogen Energy ( ) – 9

Table 2 Photobiological H2-production: progress, challenges and prospects

Parameter Basis of challenge Approaches to overcome State of the art Future prospects challenge Solar conversion Under bright sunlight, so- Genetically truncate the Successful truncation of Additional genes that con- eFciency of the lar conversion eFciency Chl antenna size of photo- the Chl antenna size by fer a truncated Chl an- photosynthetic of green algae is low synthesis to limit rates of about 50% tenna size should be iden- apparatus light absorption tiÿed TLA1, a gene that regu- lates the Chl antenna size has been cloned

Generation of Oxygen sensitivity of the Temporally separate Development of anaer- Improve sustainability of product (H2) process the processes of pho- obic S-deprivation H2-production tosynthetic O2- and “two-stage” photo- H2-production synthesis and H2-production process Low light intensity Increase yield by over- for the saturation of expressing the H2-production [Fe]-hydrogenase in green algae

Photobioreactor Cost of materials Recycling of materials Testing of a pilot scale-up Easy to obtain, oD the ($0:75 m−2) (500 L) photobioreactor shelf mechanical and of Pexible, sturdy and chemical engineering transparent materials technology Cost of nutrients Minimize use and=or re- ($0:65 m−2) cycle nutrients

Land surface area Large surface area is re- Design optimal sized Availability of sunny, arid Suitable domestic or in- quired due to the diDuse modular facility in climate with fresh, brack- ternational locations are nature of solar insolation preference to utilizing ish, or seawater available for plant con- single-body gigantic area struction

1 electricity. Nevertheless, it serves as an important guide in sion between these two forms of energy suggests on-site uti- eDorts to critically assess ways by which to lower the cost of lization of hydrogen to generate electricity, with the electri- 21

3 photobiological H2-production. For example, it is obvious cal power grid serving in energy transportation, distribution, from the above analysis that eDorts should be directed to- utilization and hydrogen regeneration as needed. A challeng- 23 5 ward the recycling and reutilization of photobioreactor ma- ing problem in establishing hydrogen as a source of energy terials and green alga mineral nutrients, in order to lower for the future is the renewable and environmentally friendly 25 7 the cost of the overall operation. generation of large quantities of hydrogen gas. A fringe beneÿt of the mass cultivation of microalgae is The recently developed single-organism, two-stage pho- 27

9 the generation of useful biomass. High-value bioproducts tosynthesis and H2-production protocol with green algae (such as vitamins, polyunsaturated fatty acids, carotenoids, [3] is of fundamental importance because it revealed the 29 11 and specialty proteins) could be extracted from the algal occurrence of hitherto unknown metabolic, regulatory and biomass. The residue could be processed for the further gen- electron-transport pathways in the green alga C. reinhardtii 31

13 eration of H2 via, for example, high temperature steam re- [3,4]. It is also of practical importance as it permitted, for forming. the ÿrst time, the sustainable light-dependent production 33

and accumulation of signiÿcant amounts of H2 gas, gen- erated from sunlight and water. This method may serve 35 7. The promiseUNCORRECTED of photobiological hydrogen production as a tool by which to probePROOF and improve photobiological hydrogen production. A summary of the progress achieved, 37

Hydrogen is recognized as an ideal energy carrier that current challenges facing photobiological H2, and the 17 does not contribute to air pollution or global warming. Hy- near-term prospects of the process are listed in Table 2. 39 drogen and electricity could team to provide attractive op- The long-term advantage of photobiological hydrogen pro- 19 tions in transportation and power generation. Interconver- duction is that it does not entail the generation of any toxic 41 HE 1471 ARTICLE IN PRESS 10 A. Melis / International Journal of Hydrogen Energy ( ) –

1 or polluting byproducts and it may even oDer the advantage higher photosynthetic productivities and photon use of value-added products as a result of the mass cultivation eFciencies than normally pigmented cells. J Appl Phycol 49 3 of green algae. These issues are of enormous consideration 1999;10:515–25. for the long-term success of a renewable hydrogen produc- [7] Weaver PF, Lien S, Seibert M. Photobiological production of 51 5 tion process. Indeed, recent estimates and business models hydrogen. Solar Energy 1980;24:3–45. have shown that a typical industrial-size solar hydrogen [8] Schulz R. Hydrogenases and hydrogen production in 53 7 production facility need occupy a minimum surface area of eukaryotic organisms and cyanobacteria. J Mar Biotechnol 1996;4:16–22. 55 500–1000 acres to permit the harvesting of suFcient solar [9] Vignais PN, Billoud B, Meyer J. Classiÿcation and phylogeny 9 irradiance for a cost-eDective operation of the plant. The of hydrogenases. 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