AMPHIPHILIC CO-POLYMER LIPID PARTICLES, METHODS OF MAKING SAME, AND PHOTO-ELECTRICAL ENERGY GENERATING DEVICES INCORPORATING SAME
20220181090 · 2022-06-09
Assignee
Inventors
Cpc classification
H10K85/761
ELECTRICITY
Y02E10/542
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H10K30/151
ELECTRICITY
H01G9/2059
ELECTRICITY
International classification
Abstract
Amphiphilic co-polymer lipid particle has a core comprising a chlorophyll pigment-protein complex or a bacteriochlorophyll pigment-protein complex within an annulus of membrane lipids, and an outermost layer of amphiphilic co-polymer surrounding an outermost surface of the membrane lipids. Such lipid particles are made by isolating photosynthetic membrane to form isolated photosynthetic membrane, adjusting the chlorophyll concentration of the isolated photosynthetic membrane, and solubilizing the isolated photosynthetic membranes in an amphiphilic co-polymer for a preselected time period that allows amphiphilic co-polymer lipid particles to form. The amphiphilic co-polymer lipid particles form a layer between a cathode and an anode in a photo-electrical energy generating device, and methods of making the same, including a layer of detergent micelles encapsulating lipid proteins rather than amphiphilic co-polymer lipid particles.
Claims
1. An amphiphilic co-polymer lipid particle comprising: a core comprising a chlorophyll pigment-protein complex or a bacteriochlorophyll pigment-protein complex within an annulus of membrane lipids; and an outermost layer of amphiphilic co-polymer surrounding an outermost surface of the membrane lipids.
2. The amphiphilic co-polymer lipid particle of claim 1, wherein the chlorophyll pigment-protein complex or bacteriochlorophyll pigment-protein complex are from a chloroplast of a plant or algae, or from a photosynthetic bacterium or a cyanobacteria.
3. The amphiphilic co-polymer lipid particle of claim 2, wherein the chlorophyll pigment-protein complex or bacteriochlorophyll pigment-protein complex comprise a photosystem I complex, a photosystem II complex, or combinations thereof.
4. The amphiphilic co-polymer lipid particle of claim 1, wherein when the photosystem I complex is present, the particles are disc-shaped nanoparticles.
5. The amphiphilic co-polymer lipid particle of claim 1, wherein the amphiphilic co-polymer has a hydrophobic portion selected from styrene or diisobutylene and a hydrophilic portion selected from maleic acid, carboxyl amide, or maleimide.
6. The amphiphilic co-polymer lipid particle of claim 5, wherein the amphiphilic co-polymer is styrene maleic acid.
7. The amphiphilic co-polymer lipid particle of claim 6, wherein the maleic acid is esterified with an alkoxy functional group.
8. The amphiphilic co-polymer lipid particle of claim 7, wherein the alkoxy functional group is selected from the group consisting of methoxy, ethoxy, propoxy, butoxy, pentoxy, hexoxy, and combinations thereof.
9. The amphiphilic co-polymer lipid particle of claim 5, wherein the amphiphilic co-polymer is diisobutylene maleic acid or styrene maleimide.
10. A method for making amphiphilic co-polymer lipid particles, the method comprising: isolating photosynthetic membrane to form isolated photosynthetic membrane; adjusting the chlorophyll concentration of the isolated photosynthetic membrane; and solubilizing the isolated photosynthetic membranes in an amphiphilic co-polymer for a preselected time period that allows amphiphilic co-polymer lipid particles to form.
11. The method of claim 10, wherein the time period is 1 hour to 12 hours.
12. The method of claim 10, wherein the amphiphilic co-polymer has a hydrophobic portion selected from styrene or diisobutylene and a hydrophilic portion selected from maleic acid, carboxyl amide, or maleimide.
13. The method of claim 12, wherein the amphiphilic co-polymer is styrene maleic acid.
14. The method of claim 13, wherein the maleic acid is esterified with an alkoxy functional group.
15. The method of claim 14, wherein the alkoxy functional group is selected from the group consisting of methoxy, ethoxy, propoxy, butoxy, pentoxy, hexoxy, and combinations thereof.
16. The method of claim 10, wherein solubilizing the isolated photosynthetic membrane includes maintaining the pH in the range of equal to or greater than 8.5 but equal to or less than 10.5.
17. The method of claim 16, wherein solubilizing the isolated photosynthetic membrane includes adjusting a solubilizing temperature to a range of about 4° C. to 60° C.
18. The method of claim 10, wherein solubilizing the isolated photosynthetic membrane includes the addition of 25 mM to 500 mM of monovalent cations.
19. The method of claim 10, wherein adjusting the chlorophyll concentration comprises normalizing the chlorophyll concentration to a value within a range of 0.5 mg/mL to 1.5 mg/mL.
20. A photo-electrical energy generating device comprising: a first electrode layer defining a first major surface and an opposing second major surface; a photoactive layer in direct contact with the first electrode layer, wherein the photoactive layer comprises amphiphilic co-polymer lipid particles or detergent micelle encapsulated lipid proteins; and a second electrode layer in electrical communication with the first electrode layer; wherein the amphiphilic co-polymer lipid particle comprises: a core comprising a chlorophyll pigment-protein complex or a bacteriochlorophyll pigment-protein complex within an annulus of membrane lipids; and an outermost layer of amphiphilic co-polymer surrounding an outermost surface of the membrane lipids.
21. The device of claim 20, wherein the device is a dye-sensitized energy generating device and the first electrode is an anode.
22. The device of claim 21, wherein the amphiphilic co-polymer lipid particles or detergent micelle encapsulated lipid proteins are mixed with a metal oxide.
23. The device of claim 22, wherein the metal oxide is selected from the group consisting of titanium dioxide, zirconium dioxide, nickel oxide, zinc oxide, tin oxide, tungsten trioxide, alumina, and combinations thereof.
24. The device of claim 20, wherein the first electrode is a cathode and the device is a solid state device.
25. The device of claim 24, comprising a layer of metal oxide particles in direct contact with the photoactive layer opposite the cathode, and the second electrode is an anode which is in direct contact with the layer of metal oxide particles opposite the photoactive layer.
26. The device of claim 25, wherein the cathode is a P- or N-doped silicon electrode and the anode is a transparent conductive electrode.
27. The device of claim 25, wherein the anode is an indium doped tin oxide electrode or a fluorine doped tin oxide electrode.
28. A method for making a photo-electrical energy generating device, the method comprising: providing a first electrode layer, the first electrode layer having a first major surface opposing a second major surface; drop-casting a photoactive layer comprising amphiphilic co-polymer lipid particles or detergent micelles encapsulating lipid proteins onto the first major surface of the first electrode layer and drying under vacuum; subsequently, drop-casting a semiconductor or conductive layer onto the photoactive layer and drying under vacuum; and placing a second electrode layer in direct contact with the semiconductor layer.
29. The method of claim 28, wherein the amphiphilic co-polymer lipid particles comprise: a core comprising a chlorophyll pigment-protein complex or a bacteriochlorophyll pigment-protein complex within an annulus of membrane lipids; and an outermost layer of amphiphilic co-polymer surrounding an outermost surface of the membrane lipids.
30. The method of claim 28, comprising sandwiching all the layers between transparent outermost layers.
31. The method of claim 28, wherein the semiconductor or conductive layer is a conductive layer comprising carbon, platinum metal, silver metal, and combinations thereof.
32. The method of claim 31, wherein the semiconductor or conductive layer is a semiconductor layer comprising a metal oxide selected from the group consisting of titanium dioxide, zirconium dioxide, nickel oxide, zinc oxide, tin oxide, tungsten trioxide, alumina, and combinations thereof.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION
[0059] The following description and drawings are illustrative and are not to be construed as limiting. Numerous specific details are described to provide a thorough understanding of the disclosure. In certain instances, however, well-known or conventional details are not described to avoid obscuring the description. References to one or an embodiment in the present disclosure can be, but not necessarily, are references to the same embodiment; and, such references mean at least one of the embodiments.
[0060] Unless otherwise noted, technical terms are used according to conventional usage. Definitions of common terms in molecular biology may be found in Benjamin Lewin, Genes IX, published by Jones and Bartlet, 2008 (ISBN 0763752223); Kendrew et al. (eds.), The Encyclopedia of Molecular Biology, published by Blackwell Science Ltd., 1994 (ISBN 0632021829); and Robert A. Meyers (ed.), Molecular Biology and Biotechnology: a Comprehensive Desk Reference, published by VCH Publishers, Inc., 1995 (ISBN 9780471185710) and other similar references. As used herein, the singular forms “a,” “an,” and “the,” refer to both the singular as well as plural, unless the context clearly indicates otherwise. The abbreviation, “e.g.” is derived from the Latin exempli gratia and is used herein to indicate a non-limiting example. Thus, the abbreviation “e.g.” is synonymous with the term “for example.” As used herein, the term “comprises” means “includes.” All publications, patent applications, patents, and other references mentioned herein are expressly incorporated herein by reference in their entirety.
[0061] “Isolated” as used herein refers to biological proteins that are removed from their natural environment and are isolated or separated and are free from other components with which they are naturally associated. The term “purified” does not require absolute purity; rather, it is intended as a relative term. Thus, for example, a purified or “substantially pure” protein preparation is one in which the protein referred to is more pure than the protein in its natural environment within a cell or within a production reaction chamber (as appropriate).
[0062] As used herein, relative terms, such as “substantially,” “generally,” “approximately,” “about,” and the like are used herein to represent an inherent degree of uncertainty that can be attributed to any quantitative comparison, value, measurement, or other representation. These terms are also utilized herein to represent the degree by which a quantitative representation can vary from a stated reference without resulting in a change in the basic function of the subject matter at issue. In certain example embodiments, the term “about” is understood as within a range of normal tolerance in the art for a given measurement, for example, such as within 2 standard deviations of the mean. In certain example embodiments, depending on the measurement “about” can be understood as within 10%, 5%, 1%, 0.5%, 0.1%, 0.05%, or 0.01% of the stated value. Unless otherwise clear from context, all numerical values provided herein can be modified by the term about. “Substantially free” or “free” besides the values just stated, can be zero.
[0063] Referring to
[0064] The chlorophyll pigment-protein complex or bacteriochlorophyll pigment-protein complex are from a chloroplast of a plant or algae, or from photosynthetic bacterium or cyanobacteria. Any plant or algae having chloroplasts is possible. One non-limiting example that was tested is spinach, i.e., Spinacea oleracea. Any cyanobacteria is possible. Two non-limiting examples that were tested include Thermosynechococcus elongatus (Te) and Chroococcidiopsis sp TS-821, which are thermophilic cyanobacteria. The chlorophyll- or bacteriochlorophyll-pigment proteins complexes comprise a photosystem I protein, a photosystem II protein, or combinations thereof.
[0065] The amphiphilic co-polymer has a hydrophobic portion selected from styrene or diisobutylene and a hydrophilic portion selected from maleic acid, carboxyl amide, or maleimide. As discussed above, with respect to
[0066] When maleic acid is present, it can be esterified with an alkoxy functional group. The alkoxy functional group may be methoxy, ethoxy, propoxy, butoxy, pentoxy, hexoxy, and combinations thereof. Referring now to
[0067] Still referring to
[0068] Methods for making amphiphilic co-polymer lipid particles include isolating photosynthetic membrane to form isolated photosynthetic membrane, adjusting the chlorophyll concentration of the isolated photosynthetic membrane, and solubilizing the isolated photosynthetic membrane in an amphiphilic co-polymer for a preselected time period that allows amphiphilic co-polymer lipid particles to form. The preselected time period is 1 hour to 12 hours. The photosynthetic membrane and the amphiphilic co-polymer is any of those discussed above for the amphiphilic co-polymer lipid particle. Depending upon the amphiphilic copolymer selected, the conditions, of pH, temperature, monovalent cation concentration, and temperature may vary.
[0069] Isolating the photosynthetic membrane includes providing a source of chloroplast of a plant or algae, or from photosynthetic bacteria or cyanobacteria, culturing and harvesting cells according to know procedures including those disclosed in Sakthivel et al., A small heat-shock protein confers stress tolerance and stabilizes thylakoid membrane proteins in cyanobacteria under oxidative stress, Arch Microbiol 2009, 191 (4), 319-28.
[0070] Solubilizing the isolated photosynthetic membrane when using SMA includes maintaining the pH in the range of equal to or greater than 8.5 but equal to or less than 10.5, adjusting a solubilizing temperature to a range of about 4° C. to 60° C., adding 25 mM to 500 mM of monovalent cations.
[0071] Adjusting the chlorophyll concentration includes normalizing the chlorophyll concentration to a value within a range of 0.5 mg/mL to 1.5 mg/mL.
[0072] Turning now to
[0073] In
[0074] The anode 202 and the cathode 204 are in electrical communication with one another by electrical connector 214, such as a wire. The electrical connector 214 can also connect the biohybrid device 200 to a device in need of electrical power 216, represented in the figure as a light bulb.
[0075] The device of
[0076] The first and second electrodes 202, 204 are not distinguished as an anode or a cathode because the photoactive layer 208 may act as an electron donor or as a hole acceptor, thereby changing whether the first electrode 204 is acting as an anode or a cathode in the particular biohybrid device.
[0077] Each method includes electrically connecting the anode to the cathode, which may be by a wire. The amphiphilic co-polymer lipid particles in the devices are any of those described herein
[0078] Turning now to
[0079] The semiconductor particles can include a metal oxide. The metal oxide can be one or more of titanium dioxide, zirconium dioxide, nickel oxide, zinc oxide, tin oxide, tungsten trioxide, alumina. Alternately, the conductor layer can be carbon, such as graphene or carbon nanostructures, platinum, or silver, or combinations thereof.
[0080] Still referring to
[0081] The following examples further illustrate the invention but should not be construed as in any way limiting its scope. Considering the present disclosure and the general level of skill in the art, those of skill will appreciate that the following Examples are intended to be exemplary only and that numerous changes, modifications, and alterations can be employed without departing from the scope of the presently disclosed subject matter.
Working Example 1
[0082] Isolation of Photosynthetic Membranes. Te was cultured in a 25 L airlift bioreactor in BG-11 medium at 45° with aeration. The bioreactor incorporated back panel illumination containing 680 nm red light and fill spectrum white light LEDs with a combined irradiance of 50 μmol photons/m.sup.2/s. Cells were harvested at late log phase —pelleted at 12,000 g and stored in 80° C. prior to lysis. The cell pellets were resuspended in buffer A (20-50 mM MES-NaOH, pH=6.5, 10 mM CaCl.sub.2), and 10 mM MgCl.sub.2) containing 500 mM sorbitol for membrane isolation and lysed using a French Press. The lysate was spun down at 12,000 g to separate unbroken cells. Thylakoid membranes were pelleted at 180,000 g in a fixed angle rotor for 30 minutes to 1 hour. The pellets were again re-suspended in buffer A containing 12.5% glycerol and stored at −80° C. Chlorophyll concentration was determined as described by Iwamura et al., Improved Methods for Determining Contents of Chlorophyll, Protein, Ribonucleic Acid, and Deoxyribonucleic Acid in Planktonic Populations, Internationale Revue der gesamten Hydrobiologie und Hydrographie 1970, 55 (1), 131-147, which is incorporated herein by reference in its entirety. Thylakoid membranes were washed three times by Dounce homogenization and pelleting at 180,000×g in Buffer A (for DDM isolation). Buffer S (50 mM Tris-Cl, pH=9.5 at room temperature) was used for SMA isolation with varied amounts of KCl and NaCl. Following the last wash, the thylakoid membranes were brought up to a chlorophyll concentration of 1 mg/mL in Buffer A with 12.5% (w/v) glycerol prior to all solubilization trials.
[0083] Thylakoid membranes for solubilization with SMA followed the same wash protocol, substituting Buffer A for 50 mM Tris-Cl, pH—9.5 with 125 mM KCL (at room temperature) (SMA buffer).
[0084] Solubilization in SMA. The thylakoid membranes with its adjusted chlorophyll concentration were solubilized in (1) DDM (Glycon) at 0.6% (w/v) at 25° C. for 1 hour without agitation for a comparison sample and (2) SMA at 40° C. for 3 hours with agitation, preferably SMA A from
BN-PAGE Analysis
[0085] 4 to 16% BN-PAGE gels (Invitrogen) were used to analyze solubilized thylakoids or isolated photosystems according to the user manual and references (Wittig et al., Blue native PAGE, Nature Protocols 2006, 1, 418) over a range of concentrations, pH, time, and cation + or cation ++ concentration. The results of the tests are shown in
[0086] Referring to
[0087] Since SMA A at 5% v/v provided the best results in Part A of
[0088] Considering all the data from
[0089] Turning now to
Sucrose Density Gradient Centrifugation
[0090] PSI-SMALP and PSI-DDM were first dialyzed against buffer (0.05% SMA 1440 or DDM, Tris-HCl, pH 9.0) using a 12-14 kDa molecular mass cutoff membrane (Spectrum Labs) with three buffer changes. Analytical ultracentrifugation (AUC) sedimentation velocity was performed in a Beckman Coulter ProteomeLab™ XL-I analytical ultracentrifuge using a double sector Epon, charcoal-filled centerpiece, quartz windows, and Ti50 rotor (Beckman/Coulter). Absorption measurements at 680 nm were made every minute at 30,000 rpm and 20° C., using the appropriate dialysis buffer as the reference. The buffer density and viscosity were determined by SEDNTERP to be 0.71006 g/mL, 0.99823 g/mL, and 0.001002 pascal.Math.s respectively. Measurements were analyzed by Sedfit v.13.0b using the continuous c(s) analysis model.
[0091] Following incubation with copolymer or detergent, insolubilized material was spun down and the supernatant was then separated using sucrose density gradient centrifugation. As shown in
77K Chlorophyll Fluorescence
[0092] After PSI was solubilized by SMA or DDM from Te cell membranes, measurements of chlorophyll concentration were made at 650 nm using an ultraviolet-visible light spectrophotometer, and chlorophyll concentration was standardized between both extraction methods. The extracts were then transferred into glass electron paramagnetic resonance (EPR) tubes and were slowly frozen in liquid nitrogen. Chlorophyll fluorescence spectra were obtained using a PTI Quantamaster Dual-channel fluorometer. Excitation light of 420 nm was used. The emission spectrum was measured by scanning from 550-800 nm with 0.5 nm steps, with a slit width of 1 nm. The resulting spectra was the average of 4 traces and the emission maxima was recorded.
[0093] Fluorescence of Te trimeric PSI can occur at wavelengths as long as ˜730 nm in intact cells, dependent on the solvation state of the chlorophyll. It has previously been shown that as PSI goes from trimeric to monomeric form in Te, a blue shift in chlorophyll fluorescence of 3-6 nm can be seen. In addition, DDM isolation causes a blue-shift in fluorescence maximum of ˜3 nm compared to that of intact cells. Turning to
Sodium Dodecyl Sulfate PAGE (SDS-PAGE) Analysis
[0094] For photosystem subunit profile identification of the trimeric PSI from band 3 of
[0095] Referring now to
PsaF Immunoblotting
[0096] The isolated PSI and sucrose density gradient fractions were separated by SDS-PAGE and transferred to PVDF (Immobilon, EMD Millipore, Burlington, Mass.). This blot was then blocked and probed with the rabbit anti-PsaB {Peptide B) antisera. The immunoblot was visualized using a GAR HRP conjugate and detected using the SuperSignal West Dura extended duration chemiluminescent substrate (Thermo Scientific, Waltham, Mass.).
[0097] Immunoblot analysis using a PsaF specific antibody, α-PsaF, confirms the loss of PsaF from the trimeric PSI and shows that PsaF is left behind at the top of the SMALP sucrose gradient shown in
[0098] Referring now to
P700 Photooxidation and Reduction by Native and Non-Native Cytochromes
[0099] Laser flash photolysis was conducted using a Joliot Type Spectrophotometer (JTS-100), equipped with an actinic LED source emitting a short excitation pulse at 630 nm and a probe beam of infrared light at 810 nm. Upon photoexcitation, P700 becomes oxidized and the absorbance of 810 nm light disappears. P700.sup.+ reduction rate is then monitored as the return of 810 nm absorbance. Fitting was done with a single exponential decay function in Prism 7. Constraints of plateau equal to 0 and Kobs>0 were used. 1000 iterations were used for fitting. Observed rates are plotted against molar ratio of cytochrome used.
[0100] Turning now to
[0101] Graph D shows observed reduction rate constants from single exponential decay curves plotted against molar ratio of cytochrome c.sub.6 for PSI-DDM in DDM buffer, PSI-DDM in SMA buffer, and for PSI-SMALP in SMA buffer.
[0102] Graph E is a P700 reduction curve for PSI-DDM and PSI-SMALP using horse heart cytochrome at 50:1 (solid lines) and 100:1 (dotted lines) ratios of Cyt/PSI. For both the solid lines and the dotted lines, PSI-DDM is above the PSI-SMALP curve. Graph F is observed P700 reduction rates of PSI-DDM and PSI-SMALP with horse heart cytochrome. Interestingly, in graphs E and F, when cyt.sub.HH is used, the reduction rate of PSI-SMALP exceeds that of PSI-DDM. The ability for PSI-SMALP to become both photooxidized and reduced by cyt.sub.6 and cyt.sub.HH indicates that the core of the PSI complex remains intact and the electron transfer chain within the reaction center remains functional, despite the loss of PsaF.
[0103] The rate of P700.sup.+ reduction seen in
Sedimentation Velocity Using Analytical Ultracentrifugation
[0104] PSI-SMALP and PSI-DDM were first dialyzed against buffer (0.05% SMA 1440 or DDM, Tris-HCl, pH 9.0) using a 12-14 kDa molecular mass cutoff membrane (Spectrum Labs) with three buffer changes. Analytical ultracentrifugation (AUC) sedimentation velocity was performed in a Beckman Coulter ProteomeLab™ XL-I analytical ultracentrifuge using a double sector Epon, charcoal-filled centerpiece, quartz windows, and Ti50 rotor (Beckman/Coulter). Absorption measurements at 680 nm were made every minute at 30,000 rpm and 20° C., using the appropriate dialysis buffer as the reference. The buffer density and viscosity were determined by SEDNTERP to be 0.71006 g/mL, 0.99823 g/mL, and 0.001002 pascal.Math.s respectively. Measurements were analyzed by Sedfit v.13.0b using the continuous c(s) analysis model from Schuck, P., Size-distribution analysis of macromolecules by sedimentation velocity ultracentrifugation and lamm equation modeling, Biophys J 2000, 78 (3), 1606-19.
[0105] Turning now to
Pump-Probe Femtosecond Spectroscopy
[0106] Time-resolved difference absorption spectra ΔA(λ,t) were measured by a pump-probe method according to Cherepanov et al., Mechanism of adiabatic primary electron transfer in photosystem I. Femtosecond spectroscopy upon excitation of reaction center in the far-red edge of the QY band, Biochimica et Biophysica Acta-Bioenergetics. 2017; 1858 (11): 895-905. Excitation pulses were centered at wavelengths of 740 nm and 670 nm. In the experiments with excitation at 740 nm, the pulses had energy of 100 nJ and a duration of 26 fs. In the case of excitation pulses at 670 nm, the pulse spectrum was filtered by the SLM modulator so that spectral components redder than 680 nm were absent. In this case, the excitation pulse duration was 34 fs, and the energy was 5 nJ. The excitation pulses were focused in a 0.5 mm thick cuvette with thin quartz glasses (150 μm thick) into a spot with a diameter of 180 μm. A pulse of white continuum focused in a spot of 120 μm diameter was used as a probe pulse. Polarizations of the pump and probe pulses were oriented by a magic angle of 54.7°. The pulse repetition rate was 100 Hz. The sample was circulated by a micropump through a cuvette at a rate sufficient to completely replace the exposed volume between the pulses. In this case, the samples were cooled to +6° C. The zero time delay between the pump pulse and corresponding spectral component X of the probe pulse was corrected by a method described by Shelaev et al., Femtosecond primary charge separation in Synechocystis sp. PCC 6803 photosystem I., Biochimica et Biophysica Acta-Bioenergetics. 2010; 1797 (8): 1410-20. The difference absorption spectra ΔA(λ,t)=A(λ,t)−A.sub.0(λ) obtained by the pump-probe femtosecond laser photolysis are the difference of between the spectrum of the PS1 A(λ,t) at the time delay t and the absorption spectrum of PSI without excitation A.sub.0(λ).
[0107]
[0108] Referring now to
[0109] Referring now to
[0110] Referring now to
[0111] The data shown in
[0112] The data clearly demonstrate that the use of DDM detergent significantly affects the rate and efficiency of energy transfer processes initiated by the excitation of long-wavelength forms of chlorophyll in PSI. In PSI-SMALP complexes, an ultrafast formation of a cation of the special chlorophyll pair P.sub.700.sup.+ was observed in the time interval of 0.1 ps. This means that the rate constant of the primary charge separation mi is as high as 10 ps.sup.−1. In these preparations excited in the far-red region of the antenna (740 nm), about 45% of the energy reached the RC with a characteristic time of about 100 fs. In about 55% of the complexes, the excitation remained localized on the long-wavelength forms of chlorophyll and the transfer of excitation energy to the RC occurred with the characteristic time of 36 ps.
[0113] The PSI absorption spectrum in the red edge demonstrated an exponential dependence (known as the Urbach rule), which was attributed to the effect of strong electronic coupling between the excited P.sub.700* and the charge-separated states P.sub.700.sup.+A.sub.0A.sup.− and P.sub.700.sup.+A.sub.0B.sup.− in both branches of redox-cofactors. Due to the presence of long-wavelength chlorophyll C-719 in the antenna of T. elongatus, the far-red pulse (740 nm) excited almost in equal proportions both the LWC in antenna and the dimer P.sub.700 in RC of the PSI-SMALP complex.
Working Example 2
[0114] A plurality of photo-electrical energy generating devices were made and tested to determine the exhibited photovoltage and photocurrent of the devices when amphiphilic co-polymer lipid particles are included in the device. First, PSI-SMALP and PSI-DDM micelles were formed according to Working Example 1 above. After sucrose density ultracentrifugation, both the PSI-SMALP and PSI-DDM micelle samples were concentrated using Millipore Amicon centrifugal concentrators, with numerous spins at 3,500×g for 10-15 minutes. The samples were concentrated three times, being diluted with buffer (SMA buffer for the SMALPs and buffer A for the DDM) twice to remove the sucrose.
[0115] The chlorophyll content was measured as set forth in Working Example 1 and adjusted to yield the same P700 levels based on equivalent P700 photobleaching levels using a JTS-100 LED pulse/probe spectrometer. The samples were normalized to a 4:5 ratio to ensure equal loading of P700 reaction centers (e.g., one reaction center per PSI monomer).
[0116] Each PSI-SMALP and PSI-DDM solution, prior to drop-casting, was diluted 4-fold into Tris-Cl buffer, pH 9.5 at room temperature to decrease the salt content. The final chlorophyll concentration of these solutions were in a range of 0.2 to 0.3 mg/mL. Specifically, the PSI-SMALP solution had a chlorophyll concentration of 0.25 mg/mL and the PSI-DDM had a chlorophyll concentration of 0.3 mg/mL.
[0117] A plurality of p-type silicon electrodes having a native oxide surface were provided. The surface of each p-type silicon electrode had a contained area of 0.24 cm.sup.2. To this contained area, 75 μL of either the PSI-SMALP solution or the PSI-DDM solution was drop-cast thereon. Each drop-cast solution was dried under vacuum for 1-2 hours. Thereafter, on the dry drop-cast layer, 75 μL of TiO.sub.2 nanoparticles in suspension were drop-cast and then dried under vacuum for 1-2 hours. An indium-doped tine oxide plastic electrode was positioned with the conductive side facing the drop-cast layers. The layers were pressed firmly together between transparent glass outermost layers and were clamped together, thereby having the structure set forth in
[0118] The plurality of devices were masked such that a photoactive area of about 0.24 cm.sup.2 was available for each device. The photocurrent for each device was normalized to current density as amp/cm.sup.2 to enable direct comparisons of the devices. A control cell having only a titanium dioxide semiconductor layers was prepared and is noted as TiO.sub.2 control in the tables below. “Spinach” data for PSI solubilized by detergent from Dervishogullari et al., Langmuir, 2018, 34, 15658-664 was included for comparative purposes. The devices containing PSI-detergent micelles from Spinach had a photocurrent density of 33 μA/cm.sup.2, a photovoltage of 210 mV, and a wattage of 0.114 W. The control cell exhibited a fast spike to a plateau, with a maximum photocurrent of 33.8 μA/cm.sup.2, see
TABLE-US-00001 TABLE 1 Photocurrent Photocurrent Illumination Time Treatment Density Day (seconds) Spinach 33 μA/cm.sup.2 n/a PSI-SMALP 25.3 μA/cm.sup.2 1 PSI-DDM 71.7 μA/cm.sup.2 1 Silicon PV 35 mA/cm.sup.2 PSI-SMALP 391 μA/cm.sup.2 2 300 PSI-DDM 321 μA/cm.sup.2 1 300 PSI-DDM 497 μA/cm.sup.2 1 1000 PSI-DDM 573 μA/cm.sup.2 1 1600 TiO.sub.2 Control 56 μA/cm.sup.2 1
[0119] The presence of the PSI-SMALP and the PSI-DDM in the devices, evidence a rise in photocurrent over time as seen by the data in Table 1 and
TABLE-US-00002 TABLE 2 Photovoltage Treatment Photovoltage Day Spinach 210 mV n/a PSI-SMALP 221 mV 1 PSI-DDM 112 mV 1 PSI-SMALP 187 mV 2
[0120] The PSI-SMALP devices had a photovoltage about twice that of the PSI-DDM containing devices. Data is also shown in graph form in
TABLE-US-00003 TABLE 3 Power Treatment Wattage Spinach 0.114 W PSI-SMALP 1.43 W PSI-DDM 1.06 W Silicon PV 375 W
[0121] Even the wattage of the PSI-SMALP containing device was higher than the PSI-DDM containing device. As a whole, the PSI-SMALP containing device outperformed the PSI-DDM containing device in all aspects.
[0122] The data evidences that SMA A, an SMA having maleic acid is esterified with an alkoxy functional group, was the most efficient amphiphilic copolymer for the extraction of trimeric PSI-SMALP from Te. SMA A also had the shortest co-polymer length and the least amount of styrene in the styrene to maleic acid ratio, about 1:5. Interestingly, this solubilization method selectively lost PsaF, a single subunit that binds to the outer edge of the complex, from the trimeric PSI. The trimeric PSI has a size of about 1.5 MDa (more specifically 1.47 MDa) and is the largest protein to be isolated using any type of non-detergent solubilization. The data suggests that smaller copolymer fragments, with low S:MA ratio and increased hydrophobicity through ester formation with alkoxy groups will be able to perform reaction center isolation from highly saturated, galactolipid rich membrane systems.
[0123]
[0124] The key difference between SMA and DDM extractions with regard to this structure/function relationship deals with the preservation of native lipids surrounding and throughout the membrane protein complexes. Decreased migration of PSI-SMALP into BN-PAGE suggest this particle is larger in size than PSI-DDM. Further, decreased sedimentation of PSI-SMALP compared to PSI-DDM suggests PSI-SMALPs either contain more lipids, resulting in a less dense complex, and/or exhibit a larger or more extended shape than DDM extracted PSI. This finding agrees with the overall consensus in the field that proteins embedded within SMALPs are disc shaped, retaining an annulus of native lipids.
[0125] It should be noted that the embodiments are not limited in their application or use to the details of construction and arrangement of parts and steps illustrated in the drawings and description. Features of the illustrative embodiments, constructions, and variants may be implemented or incorporated in other embodiments, constructions, variants, and modifications, and may be practiced or carried out in various ways. Furthermore, unless otherwise indicated, the terms and expressions employed herein have been chosen for the purpose of describing the illustrative embodiments of the present invention for the convenience of the reader and are not for the purpose of limiting the invention.
[0126] Having described the invention in detail and by reference to preferred embodiments thereof, it will be apparent that modifications and variations are possible without departing from the scope of the invention which is defined in the appended claims.