The present invention concerns a method for non-invasive production of defined structures inside compartments and to a compartment comprising such a structure.
Bottom-up synthetic biology is a growing field at the interface of biology and materials science with the visionary aim to construct a functional cell from molecular building blocks [1, 2, 3]. Towards this goal, several techniques have become available to assemble cell-sized giant unilamellar lipid vesicles (GUVs) as mimics of cellular compartments [4, 5, 6, 7, 8, 9]. Versatile synthetic and natural components have been reconstituted inside GUVs to achieve important functions of cells, such as compartment replication [10], energy generation [11, 12] or transmembrane trafficking [6, 13, 14]. However, the highly controlled spatio-temporal organization that characterizes living cells remains hitherto unachieved in today's synthetic counterparts.
Introducing space-filling structures into already formed compartments appears to be in contradiction with the barrier defining the compartment volume. Hence, the internal organization of synthetic cells typically relies on self-assembly, which limits the complexity of the achievable end result. Especially when it comes to the recombination of several functional modules, self-assembly can be impaired due to undesired interactions or incompatible environmental requirements [2, 15]. Early attempts have been made to address this shortcoming by the sequential addition of components by injection through the lipid membrane [5, 16] or vesicle fusion [17, 18, 19, 20]. While such strategies can increase the achievable complexity, it also disrupts the membrane and changes the compartment volume. Alternatively, a lipid vesicle can be formed around a preformed element, which has led to promising results [21, 4, 22]. However, this “inside-out” assembly strategy for synthetic cells neglects the role of confinement for the assembly process itself. Therefore, strategies for the non-destructive alteration of internal organization of the compartment and the addition of large structures inside compartments are highly desirable.
Toward this end, light-triggered actuation of chemical reactions [23, 24, 25, 26] and dynamic mechanical response [27, 28] opens up exciting directions. Similarly, the light-triggered polymerization of a space-filling hydrogel was realized inside cells and lipid vesicles [30]. Nevertheless, strategies for the assembly of well-defined arbitrary architectures inside preformed compartments are missing in bottom-up synthetic biology, and, more broadly, in 3D manufacturing.
The present invention solves the above problems of manufacturing structures inside of existing compartments.
Specifically, the present invention relates to a method for non-invasive production of defined structures inside compartments wherein the method comprises the steps of: (a) providing a compartment having an inside filled with a liquid, comprising a photoresist and (b) applying a light to the inside of the compartment including the photoresist, wherein the light has a focal point inside the compartment and initiates a chemical reaction of the photoresist at the focal point.
The light with the focal point inside the compartment initiates the chemical reaction of the photoresist at a confined spatial region of the compartment's inner volume. At the focal point the photon density is the highest. This allows for spatially controlling the chemical reaction of the photoresist inside the compartment. This kind of control over the chemical reaction of the photoresist enables the controlled generation of freely chosen structures, without destroying the compartment.
The term “non-invasive” as used herein, means that the compartment remains intact, even after producing the structure, i.e. the compartment does not lose its integrity.
The compartment is a spatially confined area and is not limited to a specific type or may be a vesicle, a droplet, a coacervate, a synthetic cell, a natural cell, an organelle or any compartment. The compartment wall should allow for light propagation of the wavelength of interest, i.e. the wavelength for initiating photopolymerization. The compartment wall may be a membrane, such as a lipid membrane. In accordance with the present invention, the compartment is preferably a giant unilamellar lipid vesicle, such as those mentioned above in the introductory portion. Preferably, the compartment has a compartment wall defining the inside of the compartment and an outside thereof, wherein the compartment wall can have a surfactant-stabilized fluid interface with its environment.
In accordance with the present invention it is preferred that the compartment provided in step (A) comprises at least one surfactant. The surfactant is not particularly limited and may be a polymeric surfactant or a lipid that is capable of stabilizing the interface of the compartment to the surrounding environment.
Good results are particularly obtained, if the surfactant is a block copolymer comprising a lipophilic or a hydrophobic block and a hydrophilic block. The lipophilic or hydrophobic block may be, but is not restricted to members, e.g. selected from the group consisting of perfluorinated polymers, such as perfluorinated polyethers, polystyrene or poly(olefin oxides), such as poly(propylene oxide), whereas the hydrophilic block may be selected e.g. from polyether glycols, polyetheramine, polyacrylate acid, polymethylacrylate acid or poly[poly(ethylene glycol) methyl ether methacrylate].
Likewise, good results are obtained, if the compartment is stabilized by a shell made of a triblock copolymer comprising two hydrophobic perfluorinated polymer end blocks and therebetween a hydrophilic polyether glycol block, wherein the triblock copolymer is folded so that the hydrophobic perfluorinated polymer blocks are arranged at the outer side and that the hydrophilic polyether glycol block is arranged at the inner side of the polymer shell. Examples for the lipophilic or hydrophobic blocks and the hydrophilic blocks are the same as those mentioned above.
Preferably, the perfluorinated polymer block is a perfluorinated polyether block (PFPE) and more preferably a perfluorinated polyether block having a weight average molecular weight of 1,000 to 10,000 g/mol. Likewise preferably, the polyether glycol (PEG) and polyetheramine (JEFFAMINE) blocks have preferably a weight average molecular weight of 100 to 10,000 g/mol. More specifically, suitable examples for the respective copolymers are PFPE-carboxylic acid (Krytox, MW 2500 or 7000 g/mol) and suitable examples for the respective diblock copolymers are PFPE (7000 g/mol)-PEG (1400 g/mol), PFPE (7000 g/mol)-PEG (600 g/mol), PFPE (2500 g/mol)-PEG (600 g/mol), PFPE (4000 g/mol)-PEG (600 g/mol), PFPE (4000 g/mol)-PEG (1400 g/mol), PFPE (2000 g/mol)-PEG (600 g/mol), PFPE (7000 g/mol)-JEFFAMINE (600 g/mol), PFPE (7000 g/mol)-JEFFAMINE (900 g/mol), PFPE (2500 g/mol)-JEFFAMINE (600 g/mol), PFPE (2500 g/mol)-JEFFAMINE (900 g/mol), PFPE (4000 g/mol)-JEFFAMINE (900 g/mol), PFPE (2500 g/mol)-JEFFAMINE (600 g/mol), PFPE (2000 g/mol)-JEFFAMINE (600 g/mol), PFPE (2000 g/mol)-JEFFAMINE (900 g/mol) and suitable examples for the respective triblock copolymers are PFPE (7000 g/mol)-PEG (1400 g/mol)-PFPE (7000 g/mol), PFPE (7000 g/mol)-PEG (600 g/mol)-PFPE (7000 g/mol), PFPE (4000 g/mol)-PEG (1400 g/mol)-PFPE (4000 g/mol) PFPE (2500 g/mol)-PEG (600 g/mol)-PFPE (2500 g/mol), PFPE (2000 g/mol)-PEG (600 g/mol)-PFPE (2000 g/mol), PFPE (7000 g/mol)-JEFFAMINE (900 g/mol)-PFPE (7000 g/mol) PFPE (7000 g/mol)-JEFFAMINE (600 g/mol)-PFPE (7000 g/mol), PFPE (4000 g/mol)-JEFFAMINE (900 g/mol)-PFPE (4000 g/mol), PFPE (4000 g/mol)-JEFFAMINE (600 g/mol)-PFPE (4000 g/mol), PFPE (2500 g/mol)-JEFFAMINE (900 g/mol)-PFPE (2500 g/mol), PFPE (2500 g/mol)-JEFFAMINE (600 g/mol)-PFPE (2500 g/mol), PFPE (2000 g/mol)-JEFFAMINE (900 g/mol)-PFPE (2000 g/mol) and PFPE (2000 g/mol)-JEFFAMINE (600 g/mol)-PFPE (2000 g/mol). The molecular weight is determined with gel permeation chromatography using a polystyrene standard.
It is further preferred that at least one of the hydrophobic blocks of the surfactant is fluorinated. A stable compartment, e.g. a droplet, can be obtained, when the surfactant is a block copolymer comprising one block having a polyethylene glycol segment and comprising another block which is fluorinated. According to a particularly preferred embodiment of the present invention, the block copolymer is a diblock copolymer or a triblock copolymer. Particularly preferred surfactants are of Perflouro-polyether-polyethylene glycol (PFPE-PEG) block-copolymer fluorosurfactants, for example PFPE-PEG diblock-copolymer surfactant or a PFPE-PEG-PFPE triblock-copolymer surfactant.
The present invention is not particularly limited concerning the chemical nature of the at least one lipid that may be contained in the inner space and at the fluid interface of the compartment, as long as the lipid is able to form a lipid bilayer. Good results are in particular achieved with phospholipids and in particular with a lipid being selected from the group consisting of phosphocholine, phosphocholine derivatives, phosphoethanolamine, phosphoethanolamine derivatives, phosphatidylcholine, phosphatidylcholine derivatives, phosphatidylglycerol, phosphatidylglycerol derivatives and arbitrary combinations of two or more of the aforementioned lipids. Specific suitable examples for lipids are those selected from the group consisting of 1,2-dioleoyl-sn-glycero-3-phosphocholine (DOPC), 1,2-dioleoyl-sn-glycero-3-phosphoethanolamine (DOPE), 1,2-dioleoyl-sn-glycero-3-phospho-L-serine (DOPS), 1,2-dioleoyl-sn-glycero-3-[(N-(5-amino-1-carboxypentyl)iminodiacetic acid) succinyl](DGS-NTA), 1,2-dioleoyl-sn-glycero-3-phosphoethanolamine-N-(lissamine rhodamine B sulfonyl) (RhB DOPE), 1-palmitoyl-2-hydroxy-sn-glycero-3-phosphate, L-α-phosphatidylcholine, L-α-phosphatidylglycerol, cholesterol and arbitrary combinations of two or more of the aforementioned lipids.
Shape and size of the compartment are not limited. The present invention can be realized on differently shaped and sized compartments. Nevertheless, in view of easiness of production, the compartment has an essentially round diameter. Further, in view of the needs of synthetic biology, it is preferable that the compartment as provided in step (a) of the method according to the present invention has the size of a cell. More specifically, the diameter of the preferably round compartment is preferably in the range of 1 μm to 10.000 μm, preferably 3 μm to 1000 μm, more preferably 5 μm to 500 μm, even more preferably 10 μm to 200 μm. As used herein, the term “diameter of the compartment” refers to an equivalent spherical diameter. In case of a round compartment, it is the outer diameter of the compartment. The diameter can be determined microscopically.
In accordance with the present invention, the compartments are preferably giant unilamellar vesicles (which are abbreviated as GUV) or giant multilamellar vesicles. Giant unilamellar and multilamellar vesicles are usually spherical with a diameter of typically 1 to 1,000 μm.
The liquid in the compartment provided in step (a) of the present invention is not particularly limited. It is preferably chosen to be able to dissolve non-polymerized components of the photoresist. According to a preferred embodiment of the present invention, the liquid inside the compartment is an aqueous liquid, i.e. it contains water.
The compartment in step (a) can be provided by any means known in the art. Preferably the compartment is provided by electroformation, swelling, inverted emulsion techniques, vortexing, microfluidic techniques or the like. These techniques provide the compartment filled with liquid.
Electroformation is a method, which relies on applying a low voltage, typically alternating electric field during hydration of dried lipid films in aqueous solution. More specifically, in one known variant of this technique giant unilamellar vesicles are formed in channels sandwiched between glass slides coated with indium tin oxide electrodes by applying an alternative current. In contrast to this, microfluidic phase transfer methods comprise that in a circuit lipid-stabilized water-in-oil droplets, which are generated by flow focusing at low capillary number, are presented to a parallel extravesicular aqueous flow at high capillary number. The droplets are physically transferred through the lipid-stabilized oil/water interface upon reaching a micforabricated post, collecting a second outer coat of lipids to complete the vesicle bilayer.
As alternative compartments to protocells in form of giant unilamellar vesicles polymersomes are known, which are made from amphiphilic block copolymers. They enclose and are typically surrounded by an aqueous solution. Some polymersomes can be engineered with transmembrane proteins or synthetic channel molecules that enable certain chemicals to pass the polymer membrane.
The photoresist may be incorporated already at the time of forming the compartment, e.g. by microfluidic encapsulation, or at a later stage. The photoresist can be injected into an existing compartment, by using an injection, which is preferably a pico-injector. Further, it is possible to incorporate the photoresist by diffusion into the compartment across the membrane itself or across pores in the membrane. It is also possible to use electroporation techniques for incorporating the photoresist into the compartment. Also a combination of these techniques may be used.
In addition to the photoresist, further compounds may be included in the compartment provided in step (a) of the present invention. Such further compounds can be porogens, which influence the porosity of a structure produced in step (b). An Example of such porogens are carbohydrates, such as sugars or oligomeric carbohydrates, and salts, such as alkali and earth alkali halogenides. Preferably, the porogen is soluble in water.
It is preferred that the light applied in step (b) of the method of the present invention, is a laser beam, more preferably a focused laser beam, having its focal point inside the compartment. The focused laser beam provides a high photon density at the focal point, allowing high spatial control over the polymerization reaction. Such spatial control makes it possible to provide structures with a high spatial resolution. This makes it possible to generate complex structures, such as 2-dimensional and 3-dimensional grids or even pores and/or porous structure. Particularly good results are obtainable by using pulsed laser, preferably a femtosecond pulsed laser.
The wavelength of the light is not particularly limited and can be chosen by the skilled person based on the type of photoresist, in particular of the initiator, and the type of compartment or compartment wall. According to a preferred embodiment, the wavelength of the light is around the wavelength of an absorption maximum of the initiator or around double the wavelength of the absorption maximum of the initiator. By applying light having around double the wavelength, two-photon absorption can be utilized allowing particularly high spatial resolution for preparing the defined structures inside the compartment.
Without being bound to a theory, it is assumed that the high photon density, i.e. high light intensity, allows for kinetic control over the chemical reaction of the photoresist. Thereby, the reaction can be confined to a microscopic point inside the compartment. By moving the focal point, it is possible to shift the place of the reaction. This makes it possible to “write” the desired structure inside the compartment. In view of this, it is preferable to move during step (b) the focal point of the light inside the compartment. Moving the focal point means that the position of the focal point is moved relatively to the boundaries of the compartment, i.e. this can be achieved by either moving the focal point or by fixing the focal point and moving the compartment. In view of the easiness of set-up, it is preferable to move the focal point. For example, the method of the present invention can be carried out by using a confocal microscope, which allows spatial and temporal control over the focal point inside the compartment.
According to a particularly preferred embodiment, the compartment has a compartment wall, e.g. in the form of a membrane, defining an inside and an outside of the compartment. In this embodiment, the focal point is moved across the compartment wall. By moving the focal point across the compartment wall, it is possible to create a transmembrane structure, in particular a porous transmembrane structure. Thereby, transmembrane pores can be generated, which open up a passage for molecules to penetrate across the membrane. The focal point can be moved from the inside to the outside of the compartment wall or from the outside to the inside. In this embodiment, the photoresist can be present inside and outside the compartment. Most preferably, when moving the focal point across the compartment wall the photoresist is selected so that it is soluble in the liquid which is inside the compartment and also soluble in the liquid which is outside the compartment.
The photoresist can be a negative resist, which is hardened by the exposure to light. It is also possible that the photoresist is a positive resist, which is solubilized by the exposure to light. Negative resists and positive resists are well known to the skilled person and the present invention is not limited to specific types of negative or positive resists.
In accordance with the present invention, the photoresist is preferably a negative resist, including a monomer component and an initiator component, wherein the monomer has more than one polymerizable group.
The concentration of the monomer component in the liquid is preferably in the range of 1 mg/ml to 500 mg/ml, preferably in the range of 5 mg/ml to 400 mg/ml, more preferably in the range of 10 mg/l to 300 mg/ml, even more preferably in the range of 50 mg/ml to 150 mg/ml. It was found that the production of structures can be realized over a wide concentration range, even for relatively low concentrations. If the concentration of the monomer component is lower than indicated above, there is a risk that the defined structures lack stability or the printing of a structure inside the compartment may not be possible.
Also the concentration of the initiator component, preferably a photopolymerization initiator, can be varied over a broad range. The concentration of the initiator component in the liquid is preferably in the range of 0.5 mg/ml to 200 mg/ml, more preferably in the range of 1 mg/ml to 100 mg/ml, even more preferably in the range of 5 mg/ml to 50 mg/ml, even further more preferably in the range of 10 mg/ml to 30 mg/ml. With the concentration being in the range above, it is high enough to rapidly initiate the chemical reaction. For lower concentrations, printing a structure inside the compartment may not be possible. Further, the concentration is not too high. If the concentration of the initiator component is higher than indicated above, there is a risk that the chemical reaction is not only initiated at the focal point but also at other positions, where the light is not focused. In such a case, spatial resolution for producing the defined structures can be deteriorated and in some cases the compartment wall can be damaged.
A preferred example for a negative photoresist is one that includes a monomer component being capable of radical polymerization. Preferably the monomer component has more than one group derived from one of acrylic acid, acrylic acid esters, methacrylic acid, methacrylic acid esters, styrene, styrene derivatives, vinyl halides, e.g. vinyl chloride, vinyl esters, e.g. vinyl acetate, or acrylonitrile. A suitable and particularly preferred example is an acrylate based monomer component, such as poly(ethylene glycol) diacrylate (PEGDA) and a suitable photoinitiator.
The type of photoinitiator is not particularly limited and the skilled person can select one that is known in the art. Examples for suitable photopolymerization initiators are acetophenone-based compounds, benzophenone-based compounds, benzoin-based compounds, thioxanthone-based compounds, anthraquinone-based compounds, azo compounds and others. Preferably, the photoinitiator is water soluble. A particularly preferred example for a photoinitiator is Lithium phenyl-2,4,6-trimethylbenzoylphosphinate (LAP).
Further suitable photoresists are for example photoresists utilizing the polymerization of acidic polymers, such as alginate, alginate salts of monovalent ions, e.g. sodium alginate and so on, via photo-induced uncaging of caged divalent ions. Details for alginate polymerization are described by Juárez et al in Front. Bioeng. Biotechnol., http://dx.doi.org/10.3389/fbioe.2014.00026. Details for caged Mg ions are described in J. Org. Chem. 1988, 53, 1966.1969, https://doi.org/10.1021/jo00244a022),
Another suitable photoresist is one utilizing polymerization of proteins via photosensitizer, such as e.g. printing of protein BSA with photosensitizer rose, such as described by Bengal in Small 2020, 16, 1906259, https://doi.org/10.1002/smll.201906259.
A further exemplary photoresist that may be used in the method of the present invention is a photoresist based on light-triggered click chemistry, which may be based on 1,3-dipolar cycloadditions, Diels-Alder reactions or thiol-ene addition. Detailed examples for such light triggered click reactions are known to the skilled person and described for example by Kumar and Lin in Chem. Rev. 2021, 121, 12, 6991-7031.
It is also possible that the photoresist is based on light triggered polymerization of polymerizable monomers, as demonstrated for example by Furutani et al. in Polymer International, Volume 68, Issue 1, pages 79-82, https://doi.org/10.1002/pi.5696, or monomer-initiator conjugates, such as DNA motifs with photocleavable spacer ends or light-induced heating causing caramelization of sugar.
The negative resist can be a photoresist based on radical polymerization, as described above. However, also other polymerization mechanisms are possible. For example, the negative resist may be a DNA based resist, such as the one described by Kasahara et al., in “Photolithographic shape control of DNA hydrogels by photo-activated self-assembly of DNA nanostructures”, APL Bioengineering 4, 016109 (2020); https://doi.org/10.1063/1.5132929. Accordingly, the photoresist may include at least two different Y-shaped DNA nanostructures having sticky ends. The sticky ends of the different Y-shaped DNA nanostructures are not compatible to one another. Further, the resist includes a cross-linker DNA sequence, having sequences complementary to those of the sticky ends of the different Y-shaped DNA nanostructures. In an inactive state of the linker, the complementary DNA-sequences are non-accessible for the sticky ends of the Y-shaped DNA nanostructures. By irradiating with light, photocleavage within the inactive linker occurs and the sticky ends of the linker become accessible for the sticky ends of the Y-shaped DNA nanostructures and the photoresist hardens.
According to a preferred embodiment, the chemical reaction initiated in step (b) is a femtosecond two-photon polymerization.
As further described in the Examples, the photoresist can preferably be a positive resist that is DNA based. The DNA based positive resist can be based on Y-shaped DNA nanostructures, such as those utilized by Kasahara et al. and explained above for the negative DNA based resist. However, the linker compound has at least two complementary sequences linked to one another via a photocleavable group. The photocleavable group allows to cleave the linker after hardening of the resist. This makes it possible to erase previously hardened structures.
It is preferable that the photoinitiator is one that can be excited by two-photon absorption. Most preferably, in step (b) of the method of the present invention, the reaction is initiated by a two-photon absorption. Two-photon absorption requires the simultaneous absorption of two-photons to excite a molecule, i.e. the initiator compound or cross-linker compound of the photoresist, from a ground state to an excited state. Probability of a molecule to absorb two photons is proportional to the square of the light intensity. Therefore, by applying the two-photon absorption, it is possible to initiate the chemical reaction very precisely at the focal point of the light, i.e. at the point inside the compartment, where the light intensity is the highest. This allows for a very high spatial resolution.
The present invention further relates to a compartment, having an inside, surrounded by a compartment wall, wherein the compartment comprises a structure obtainable by the method of the present invention, as described above.
In accordance with the compartment of the present invention, the structure is a porous structure, preferably one extending through the compartment wall.
All details explained above or in the appended claims with regard to the method for non-invasive production of defined structures inside compartments apply mutatis mutandis also to the spatially confined compartment of the present invention.
Next the present invention will be described by reference to the drawings and examples. In the drawings, the following is shown:
Micrographs of polymerized structures 1 obtained from single-photon polymerization via laser scanning confocal microscope inside a compartment in the form of a surfactant-stabilized water-in-oil (w/o) droplet 2, using a 405 nm laser diode are shown in
A 3D surface reconstruction of confocal images of a 3D printed cube frame inside a 40 μm-sized GUV is shown in
In
Images and plots shown in
Lipid diffusion coefficients determined by FRAP for GUVs before mixing with photoresist (0 h), 0.25 h after adding GUVs into photoresist (0.25 h), 2 h after adding GUVs into photoresist (2 h) and for GUVs in photoresist after printing a rod structure inside their lumen (n=10-12, mean±s.d.) are indicated in the plot of
In
The pore size distributions as determined from AFM images for the polymerized photoresist (R) used for printing inside GUVs, the polymerized photoresist at doubled PEGDA and LAP concentration (R2x), and polymerized photoresist in water without sucrose or glucose (RH2O) are sown in
Results of FRAP experiments carried out on polymerized photoresist before structure development (black dots, “Monomers”) and after washing (grey triangles, “Hydrogel”) as a function of time are shown in the plot of
Representative confocal images (yellow, λex=561 nm, visible as light grey in
AFM images shown in
The plot of
In
Representative confocal images of two adjacent GUVs (red, λex=488 nm) in the xy-(left) and an xz-plane (right, as indicated by white dashed line) are shown in
Further representative confocal images of two adjacent GUVs, similar as described in
In
The following further exemplifies the present invention and provides experimental details. It is to be understood that the present invention is not limited to these details below, even though they may be regarded as preferred embodiments, either taken alone or in combination with each other.
For the Examples described herein, commonly used water-soluble resist components (Requirement (i)) were chosen, namely the photoinitiator lithium phenyl-2,4,6-trimethylbenzoylphosphinate (LAP), the prepolymer poly(ethylene glycol) diacrylate 575 (PEGDA) [42, 43] and the fluorescent acryloxyethyl thiocarbamoyl rhodamine B monomer (Rhodamine B acrylate) for imaging purposes. Additionally, the resist was supplemented with sucrose at a high osmolarity (800 mM) to buffer osmotic pressure fluctuations which could damage the GUVs [17].
Next, we set out to test if Requirements (ii) and (iii) can be fulfilled, i.e., if the resist can be brought into the GUV and if excess components can be removed after printing.
GUVs were prepared with a conventional lipid composition (99% DOPC, 1% ATTO633-DOPE) using the electroformation method [9]. When mixing GUVs and the photoresist components, confocal imaging revealed the influx of the fluorescent Rhodamine B acrylate across the lipid bilayer membrane into the GUV lumen (
More importantly, we found that the removal of the resist from the GUV lumen can be achieved by simple dilution, resulting in outflux from the GUV by passive diffusion (
To gain quantitative insights into the Rhodamine B acrylate influx into GUVs, the fluorescence intensity ratio inside and outside of GUVs, Iin/Iout, was measured over time, yielding a membrane permeability coefficient of 2.301±0.016 nm s−1 (
The resist was polymerized inside the GUV by two-photon 3D laser printing. This observation is a direct proof for the influx of all resist components. As visible in the microscopy image in
Due to their increased surface-to-volume ratio, printing in smaller GUVs was possible at earlier time points (
Importantly, the GUVs did not move during the printing process, despite potential laser heating, once they settled due to gravity in a glucose-sucrose gradient (Requirement (iv)).
In more detail, after adding LAP to GUVs, it took 24.27±1.07 min to achieve a 50% printing success rate. Having determined the minimal LAP concentration required for printing (
PEGDA was found to diffuse faster across the membrane, such that printing in 50% of the GUVs was already possible after 11.48±0.88 min, corresponding to a membrane permeability of 3.875±1.330 nm s−1. As expected, both non-fluorescent components have a higher membrane permeability compared to Rhodamine B acrylate since they are smaller in size. When adding PEGDA and LAP at the same time, we achieve a 50% printing success ratio at a later time point after 44.83±2.68 min, potentially due to the increased access resistance.
Most importantly, it should be highlighted that printing was successful in over 88% of the GUVs after 100 min incubation with the resist components. If printing was unsuccessful despite sufficiently long incubation, this was typically the case because the GUV bursted during the printing process, when the 3D positioning of the polymerization voxel was insufficiently accurate and polymerization was triggered in very close proximity to the lipid bilayer.
The high printing success rate of a simple structure as described above, allowed the printing of more complex 2D a 3D shapes into GUVs and to visualize them by confocal fluorescence microscopy.
This demonstrates an exemplary way for enriching the inner volume of GUVs with photopolymerizable hydrogel components via diffusion across the lipid bilayer and demonstrated the deterministic polymerization of various structures in 2D and 3D inside GUVs. This concept can also be extended to other compartment types like water-in-oil droplets (
Having confirmed that femtosecond two-photon polymerization inside GUVs does not destroy them (Requirement (iv)), the effects of the photoresist and two-photon 3D laser printing process on the lipid bilayer was investigated. Specifically, unintentional alterations of the lipid diffusivity, which is a crucial indicator for membrane property changes, such as resist-membrane interactions, oxidation or changes in membrane composition due to the presence of the photoresist in the membrane were investigated.
First, it was confirmed with fluorescence recovery after photobleaching (FRAP) measurements (further details are provided below) that the membrane of GUVs containing a printed structure inside their lumen remained diffusive (
The fluorescence of the bleached area recovered within seconds. An exponential fit yields the diffusion coefficient D of the lipids for different conditions, namely prior to resist encapsulation, before and after equilibration of the resist concentration inside and outside the GUVs (i.e., 0.25 h and 2 h after adding the photoresist to the GUVs, respectively) and after printing a rod structure inside the GUV lumen (
In order to derive functionality for the printed hydrogels, their microscopic structure was investigated. FRAP experiments confirmed that the hydrogel is polymerized and hence not diffusive (
This shows that the membrane remains intact after printing and that the polymerized hydrogel is porous. This opens up exciting opportunities for applications of 3D laser printing in compartments, such as lipid vesicles in the context of bottom-up synthetic biology.
Further to the above, a transmembrane pore that spans the lipid bilayer was printed. Due to the porous nature of the printed hydrogel, a structure that is written or printed across the membrane provides a passage for biomolecular cargo as illustrated in
Importantly, it was found that printing across the lipid membrane is possible without destruction of the GUVs by applying the method of the present invention.
After two-photon polymerization of the respective area, a hydrogel structure with a diameter of approximately 5 μm clearly spanned the GUV membrane as visible in the brightfield image in
Membrane-spanning structures could be printed in 41.5% of printing attempts (n=59). In the other cases GUVs bursted and collapsed. Increasing the laser intensity by 10% resulted in a decreased success ratio of 32% (n=50), enhancing the probability of GUV destruction. Nevertheless, printing success was possible at different laser intensities.
To test whether the printed transmembrane structure acts as a pore and enables substance exchange between the interior and the environment of the GUV, a glucose-sucrose gradient across the GUV membrane was used. The refractive-index mismatch between the glucose outside and the sucrose solution inside the GUV causes an optical contrast which disappears if glucose and sucrose are exchanged across the lipid membrane.
Next, it was tested if the pores can transport larger and charged molecular cargo.
The printed transmembrane pore is a very large transmembrane pore, exceeding the size of the nuclear pore complex. In particular, large pores capable of transporting macromolecules across the membrane are often difficult to isolate and to reconstitute in synthetic cells. However, applying the method of the present invention, in particular the 3D laser printing described above, such large transmembrane pores can be produced within a compartment.
The above described Examples were prepared according to the following experimental details.
18:1 1,2-dioleoyl-sn-glycero-3-phosphoethanolamine-N-(lissamine rhodamine B sulfonyl) (ammonium salt) (Liss Rhod PE) and 18:1 1,2-dioleoyl-sn-glycero-3-phosphocholine (DOPC) were purchased from Avanti Polar Lipids, Inc. 1,2-dioleoyl-sn-glycero-3-phosphoethanolamine-ATTO633 (ATTO633-DOPE) and 1,2-dioleoyl-sn-glycero-3-phosphoethanolamine-ATTO488 (ATTO488-DOPE) were purchased from ATTO-TEC GmbH. Poly(ethylene glycol) diacrylate (PEGDA, Mw=575), Lithium phenyl-2,4,6-trimethylbenzoylphosphinate (LAP), acryloxyethyl thiocarbamoyl rhodamine B (Rhodamine B acrylate), 3-(trimethoxysilyl) propyl methacrylate (TMSPMA), sucrose, glucose and poly(vinyl alcohol) (PVA, Mw 13 000 to 23 000) were purchased from Sigma-Aldrich. Poly(dimethylsiloxane) (PDMS, Sylgard 184) was purchased from Dow Corning. Alexa Fluor™ 647 NHS Ester (Succinimidyl Ester) was purchased from Thermo Fisher Scientific Inc. Indium tin oxide (ITO) coated glass coverslips were purchased from Visiontek Systems Ltd. 5′-Atto 647N TTTTTTAATTTTT 3′ single-stranded DNA (Atto647N ssDNA) was purchased from biomers.net GmbH (purification: HPLC). Picodent Twinsil® was purchased from Picodent®. Precision cover glasses (thickness No. 1.5H: 170±5 μm, 24 mm×60 mm and 18 mm×18 mm) were purchased from Paul Marienfeld GmbH & Co. KG.
Giant unilamellar vesicles (GUVs) were electroformed in 800 mM sucrose using a Vesicle Prep Pro device (Nanion Technologies GmbH) [9, 17]. Briefly, 40 μl of a lipid mix (99% DOPC and either 1% ATTO633-DOPE or 1% ATTO488-DOPE), dissolved in chloroform at a concentration of 5 mM, were spread homogeneously on the conductive site of an ITO coated glass slide. Subsequently, the lipid-coated ITO slide was desiccated for 30 min in order to remove remaining chloroform. A rubber ring was placed on top of the lipid-coated ITO slide, which then was filled up with 275 μl 800 mM of an aqueous sucrose solution. A sealed chamber was created by placing another ITO slide on top, afterwards the electrodes were connected with the conductive sides of the ITO slides and the pre-installed Standard program was run, generating an AC field of 3 V at 5 Hz for 2 h at 37° C.
Photoresist Permeation into GUVs:
Prior to laser writing, a photoresist containing 249 mg ml-1 PEGDA 575 as monomer, 24 mg ml-1 LAP as photoinitiator and 800 mM glucose was mixed at a volumetric ratio of 1:1 with the GUV solution. 0.01 mg ml-1 Rhodamine B acrylate were added to the final solution for fluorescence microscopy. For the influx of Alexa Fluor™ 647 NHS Ester or Atto647N ssDNA into GUVs, the volumetric ratio of photoresist, GUV solution and fluorophore or fluorophore-conjugated ssDNA was 20:19:1.
Cover glasses were coated either with PDMS (
3D laser printing: For structure fabrication, a commercial 3D laser printing setup (Photonic Professional GT, Nanoscribe GmbH) equipped with a 25×, NA=0.8 oil immersion objective and a 25×, NA-0.8 water immersion objective was used for fabricating 2D and 3D structures, respectively. The printing solution containing GUVs and photoresist was filled into a glass observation chamber made of two coated cover glasses, doublesided adhesive tape as spacer and was sealed by two-component glue picodent Twinsil®.
STL files were designed using Blender (version 2.92) and processed via DeScribe (version 2.5.5). Typically a laser power of 80% or 90% was used, wherein 100% correspond to 50 mW at the backfocal plane, and a scanning speed of 1 mm s−1 to 2 mm s−1 or 6 mm s−1 for 2D structures and 3 mm s−1 for the 3D structure and printed pores. The slicing and hatching parameters were set to 300 nm and 200 nm, respectively.
In order to determine the membrane permeability of PEGDA or LAP, GUVs were incubated for 2 h in 800 mM sucrose and additional 12 mg LAP or 11.1 vol % PEGDA, respectively. Afterwards, the solution was mixed with a 800 mM glucose, 12 mg LAP and 22.2% PEGDA solution or 800 mM glucose, 24 mg LAP and 11.1% PEGDA solution, respectively, in a volumetric ratio of 1:1. This results in an increasing concentration of PEGDA or LAP over time, whereas the concentration of the other resist components remains constant.
Fluorescence microscopy was performed using an LSM 800 or a LSM 900 confocal laser scanning microscope (Carl Zeiss AG). The Rhodamine B acrylate influx study was performed using a 20× air objective (Plan-Apochromat 20×/0.8 M27, Carl Zeiss AG) on an LSM 900. FRAP measurements and all other fluorescence images were taken at an LSM 800, using a 20× air objective (Plan-Apochromat 20×/0.8 M27, Carl Zeiss AG), a 40× water objective (C-Apochromat 40×/1.20 W Korr, Carl Zeiss AG) or a 63× oil objective (Plan-Apochromat 63×/1.40 Oil DIC M27). Confocal images were analyzed with ImageJ (version 1.53c) and brightness and contrast adjusted.
For FRAP measurements, a circular area of 5 μm in diameter was defined as the bleaching and imaging region and a frame time of 116 ms was set. Using the integrated bleaching tool of the LSM 800, 4 images were acquired prior to one bleaching cycle with the 561 nm laser line at 100%, followed by a subsequent time series of 65 cycles. The diffusion coefficients, derived from 10-12 GUVs per condition, were determined via a MATLAB (MathWorks, Inc.) script [5].
For AFM measurements, glass slides (Menzel Gläser, thickness: 1.0 μm to 1.2 μm, Thermo Scientific) were coated with TMSPMA as explained above. A 60 μm high observation chamber was built and the following resists were polymerized:
They were flushed into the observation chamber and polymerized by acquiring per frame repeated twofold averaged 512×512 pixel images with a pixel size of 1.25 μm and a pixel time of 1.52 us with a 405 nm laser diode at 20% laser intensity, using a 20× air objective (Plan-Apochromat 20×/0.8 M27, Carl Zeiss AG) on an LSM 900. After Polymerization, the chambers were immersed with ethanol in order to remove the sticky tape and the top glass slide. Next, slides with polymerized hydrogel on top were soaked with MilliQ water for at least 24 h prior to AFM measurements.
Atomic force microscopy (AFM) was conducted in liquid using a Nanowizard Ultra Speed 2 (Bruker) with a BL-AC40TS cantilever (Olympus, f=110 kHz, k=0.09 N/m) in QI-mode, using a peak force of 139.3 pN. The resolution was set to 256×256 pixel with a pixel time of 9.4 ms. AFM images were processed with JPK Data Processing (version 7.0.137).
Statistical analysis, non-linear regression and data plotting were carried out with GraphPad Prism (version 9.1.2) and in python (version 3.8.8). All figures were compiled with Inkscape (version 1.0.2).
Additional details for the above experiments are described in the following:
The estimation of membrane permeability coefficients was carried out for the flux of molecules through a spherical GUV with membrane thickness d and membrane area 4πr2, based on Fick's first law of diffusion. [1-1] For the permeability of the hydrogel pore for sucrose and glucose, one has to consider the flux through the cross sectional area of the pore Apore. Hence, the flux J will be described by
Which gives upon integration
where K is the partition coefficient, D the diffusion coefficient, cout the concentration outside of the GUV and cin the concentration inside of the GUV. In addition, the flux can also described by the change of concentration inside of the GUV:
where P=KD/d is the permeability coefficient.
The solution for the Michelson contrast C, given the boundary condition Cin (t=0)=0, is
We use the interdependence of the permeability and the concentration inside of a GUV Cin [1] to determine the membrane permeability P via printing attempts:
where R is the GUV radius, Cout the concentration outside of the GUV and t the time.
We used parameters of R=12.5±2.5 μm, as GUVs with a diameter of 20 μm to 30 μm were chosen for the analysis, Cout=11.1 vol % or Cout=12 mg mL-1 for PEGDA and LAP, respectively, Cin=5.25±0.25 vol % or Cin=3.50±0.25 mg mL-1 for PEGDA and LAP, respectively (
The resulting membrane permeabilities are 3.875±1.330 nm s−1 for PEGDA and 0.987±0.325 nm s−1 for LAP, where the error is estimated by propagation of uncertainties.
FRAP measurements were performed and analysed according to previous work. [1-2] Briefly, all fluorescence intensity values/were normalized on the average of all fluorescence intensities acquired before bleaching, Ipre, namely npre=4 images:
Furthermore, a non-linear least-squared exponential fit of the form
was performed, where λ is the exponential decay coefficient, which in turn was used to calculate the half-recovery time
Eventually, the diffusion coefficient D was calculated: [1-3, 1-4]
where r is the radius of the bleached spot, which was set to 2.5 μm.
In the following the printing and erasing of DNA hydrogel is described by reference to an exemplary embodiment. The DNA hydrogel used for printing corresponds to the one described by Kasahara et al., in “Photolithographic shape control of DNA hydrogels by photo-activated self-assembly of DNA nanostructures”, APL Bioengineering 4, 016109 (2020); https://doi.org/10.1063/1.5132929.
The sticky ends of the different Y-shaped DNA nanostructures YA and YB are not compatible to one another. Further, the resist includes a cross-linker DNA sequence, having sequences complementary to those of the sticky ends of the different Y-shaped DNA nanostructures YA and YB. In an inactive state of the linker, indicated at the left side of
For the negative resist, the underlying mechanism is explained in
In principle it is possible to combine the negative resist and the positive resist, when the inactive cross-linker used for the negative resist comprises different types of photocleavable groups which cleave selectively at different wavelengths, for example one at 405 nm and another one at a different wavelength). A first type of photocleavable group (not shown in
Similarly, as in
The sketch of
Similarly as for
The sketches of
The present invention allows the spatially controlled assembly of arbitrarily selected well-defined 2D and 3D microstructures with full spatio-temporal control.
In principle, printing inside living cells can be realized in any kind of biological compartment, including eucaryotic cells, procaryotic cells, cellular organelles and multi-cell assemblies, such as spheroids, organoids, as well as synthetic compartments.
For printing inside living cells, the present invention allows in principle the use of any type of hydrophilic or lipophilic photoinitiator. Further, any molecules suitable for radical polymerization can be used inside biological compartments, as long as they can be brought into the compartments, in particular via passive diffusion through the compartment barrier or other delivery methods, such as lipid transfection, fusogenic liposomes and the like.
It was found that the formation of radicals inside living cells is possible. The interaction of said radicals with a lipophilic radical-sensitive fluorophore was observed. For this purpose, living J774A.1 cells were stained with lipophilic radical-sensitive fluorophore BODIPY 665/676. Cells were irradiated with 405 nm light at different laser intensities at a confocal laser scanning microscope (Zeiss LSM 900) in presence of a photoresist for printing inside cells containing photoinitiator LAP, Crosslinker Mbis and Monomers HPMA. As a control, cells in absence of photoresist were irradiated with 405 nm light at a laser intensity used for printing inside cells. Furthermore, photobleaching of a non-irradiated cell was recorded over time. The experiments showed a decrease in fluorescence intensity relative to before irradiation due to interaction of radicals with the radical-sensitive fluorophore. Thereby the generation of radicals inside living cells was confirmed.
As shown in
The present invention is suitable for printing inside eucaryotic cells. Printing was also confirmed in Hela cells and J774A.1 (macrophages).
The content of all references is incorporated by reference.
Number | Date | Country | Kind |
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21200214.1 | Sep 2021 | EP | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2022/077007 | 9/28/2022 | WO |