Shubin Li’s research while affiliated with Harbin Institute of Technology and other places

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Publications (24)


High-Throughput Programmable Tumor Spheroid Generation Using the Magneto-Archimedes Effect
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February 2025

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19 Reads

ACS Applied Materials & Interfaces

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Chao Li

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Shubin Li

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Confined domains inside GUVs in crowded solution monitored by SPT. Trajectory of PS particle in 300 s in GUVs containing 0 (a), 10 (b), 20 (c) and 30 (d) wt.% PEG‐20k solution, respectively. e) The schematic illustration of the trajectory in (d). The gray area is the PEG‐rich phase while areas 1–4 are H2O‐rich domains reflected by the trajectory in chronological order, respectively. Particle diffuses in area 1 and escaped to areas 2, 3, and 4 in order. Scale bar: 10 µm.
Calculation of average residence time (τint) of particles inside the H2O‐rich phase. a) Plots of α as a function of time intervals with the concentration of PEG‐20k Da solution of 10, 15, 20, 25, and 30 wt.%, respectively. Near Intercept (NI) and Far Intercept (FI) of 30 wt.% PEG‐20k Da solution were labeled on the plots, respectively. b) Viscosity coefficient of 0, 10, 15, 20, 25 and 30 wt.% PEG‐400, 8k, 20k and 500k Da and the fitted curves by Huggins Function. c) τint and the fitted curve of particles inside the H2O‐rich phase domain of 10, 15, 20, 25, and 30 wt.% PEG‐20k Da solutions. d) α0 of a solution containing 0, 5, 10, 15, 20, 25 and 30 wt.% PEG‐20k Da, respectively and the fitted curve. e) Schematic of fluid dynamic analysis of particle diffusion along the pipe. f) α0 of solutions containing 10, 20, 25 and 30 wt.% PEG‐400, 8k, 20k, 100k and 500k Da. g) Schematic of trajectory in phase‐separated solutions, H2O‐rich phase domains were circled in blue circles. h) r0 and fitted curves of solutions containing PEG‐8k, 8k/20k = 2/1, 8k/20k = 1/1, 8k/20k = 1/2, and 20k Da with the concentration of 15, 20, 25, and 30 wt.%, respectively. The error bars indicate the mean ± standard deviation (SD) (n = 3).
Analysis of the Universality of the Formulas. Fluorescence images of SiO2 particles (a, left), amino‐PS particles (b and c, left), carboxyl‐PS particles (d, left), and PS particles with diameter of 1000 nm (e, left) and 100 nm (f, left) and trajectory of particle for 300 s in GUVs encapsulating 30 wt.% PEG‐20k (a, b, e and f; right) and Poly‐L‐Lysine (molecular weight: 15k–30k Da) (c and d, right) solution, respectively. All particles were labeled with red fluorescence. Scale bar: 10 µm. Plots of α as a function of time intervals (g), τint as a function of concentration and the fitted curves (h), α0 as a function of concentration and the fitted curves (i), and r0 as a function of concentration and the fitted curves (j) of 500 nm SiO2 particles (red), PS particles with diameter of 1000 nm (green) and 100 nm (blue), respectively. The error bars indicate the mean ± standard deviation (SD) (n = 3).
Phase separation in a solution of different molecular weights. Trajectory of a particle in 30 wt.% PEG‐100k solution with a concentration of 5 wt.% (a) and 30 wt.% (b). Scale bar: 10µm. c) Plots of α as a function of time intervals with the concentration of PEG‐100k Da solution of 5, 10, 15, 20, 25, and 30 wt.%, respectively. d) Phase diagram of solution with molecular weight of 400, 8k, 20k, 100k, and 500k Da and concentration in the range of 0–30 wt%.
Quantification of H2O‐rich phase domain in the cytosol in vitro. Trajectories of particles in GUVs encapsulating cell lysis solution of E. coli (a), S. Cerevisiae (b), and HEK‐293T (c). α0 (d), τint (e), and r0 (f) of these cell lysis solutions. Scale bars: 10 µm. The error bars indicate the mean ± standard deviation (SD) (n = 3). (nsp > 0.05, *p< 0.05, **p< 0.01 and ***p< 0.001).
Elucidating Local Confinement in Crowded Polymer Solutions Within Giant Unilamellar Vesicles (GUVs) Through Single Particle Tracking Toward Deeper Understanding of Cells
  • Article
  • Publisher preview available

February 2025

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37 Reads

In a crowded environment, macromolecules occupy a significant proportion volume of cells to repulse other molecules in H2O‐rich phase domains. These H2O‐rich phase domains have been found to significantly influence material transportation and biochemical reactions. However, the accurate quantification of the size of these domains remains a challenge. Here, formulas are set up to calculate the anomalous diffusion exponent (α), the concentration threshold (cp), and the radius of the H2O‐rich phase domain (r0) to characterize the crowded solutions. Fitting coefficient (R²) of the r0 fitted curves are 0.9989 for PEG‐8k Da and 0.9901 for PEG‐20k Da, respectively, which confirms the formulas to be suitable for quantifying the crowding degree. The values of α, r0, and cp of three different cell lysates is are calculated using these formulas. The r0 values of the cytosol from eukaryotic cells are 1.22 µm for HEK‐293T and 1.46 µm for S. Cerevisiae, respectively, which are smaller than that (2.13 µm) from prokaryotic cells (E. coli). This may be due to the more complex components, with higher molecular weight but lower concentration in the eukaryotic cells. This method for quantifying the H2O‐rich phase in a crowded solution helps to have a deeper understanding of the biochemical mechanism inside cells.

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Schematic illustration of light‐driven carbon fixation using photosynthetic organelles in artificial cells. (a) Scheme of a photosynthetic organelle. (b) Scheme of an artificial photosynthetic cell containing (a), phycocyanin (PC), the enzymes of carbon fixation pathway (IDH, ACO, and ACL), α‐oxoglutarate, NADPH, HCO3⁻, ADP, and CoA. (c) The chemical equations of enzyme cascade reactions.
Characterizations of ATP synthase and PSII. (a) SDS‐PAGE image of ATP synthase purified from spinach. The complete gel was shown in Figure S29. (b) ATP concentration in the solution (pH 8.8, with or without ADP) upon the addition of acidic ATP synthase‐LUVs a function of time. (c) SDS‐PAGE image of PSII purified from spinach. (d) DCPIP concentration in the PSII (8 μg Chl mL⁻¹) solutions against time with light irradiation (red curve), without light irradiation (black curve), with light irradiation and DCMU (green curve). (e) Step‐wise O2 concentration in PSII solution (10 μg Chl mL⁻¹) with light (50 mW cm⁻²) on and off with a time interval of 300 s at 25 °C. (f) Fluorescence spectra of PC and PSII with PSII concentrations of 2.64 μg Chl mL⁻¹, 4.62 μg Chl mL⁻¹, 15.89 μg Chl mL⁻¹ at the fixed PC concentration of 1.02 μg mL⁻¹. (g) Oxygen production of PSII (10 μg Chl mL⁻¹) with the ratio of PC/PSII to be 0, 1.5, 3.0, 4.5, 6.0, 15, 30 (μg : μg), respectively. ***p<0.001 by a two‐tailed unpaired student's t‐test. p<0.001 was considered statistically significant. NS means not significant. The colored bands and error bars indicate mean ± standard deviation (SD) (n=3 independent experiments).
ATP production of photosynthetic organelles. (a) ATP production by photosynthetic organelles (PSII‐ATP synthase‐LUVs, PSII/ATP synthase ratio of 0.85) at pH 8.0 as a function of time with light (red curve), and under controlled conditions including PSII‐ATP synthase‐LUVs in dark (black curve), PSII‐LUVs in light (green curve), ATP synthase‐LUVs in light (blue curve), PSII‐ATP synthase‐LUVs in light with inhibitor (200 μM DCMU, purple curve), and PSII‐ATP synthase‐LUVs in light with uncoupling agent (1 μM FCCP, brown curve). (b) Step‐wise ATP production by PSII‐ATP synthase‐LUVs (PSII/ATP synthase ratio of 0.85) with light (50 mW cm⁻²) on and off with a time interval of 900 s at 25 °C at pH 8.0. (c) Effect of pH on ATP production by PSII‐ATP synthase‐LUVs with light (50 mW cm⁻²). (d) Effect of different ratios of PSII/ATP synthase on ATP production by PSII‐ATP synthase‐LUVs at pH 8.0. (e) Effect of the addition of PC on ATP production by PSII‐ATP synthase‐LUVs. ***p<0.001 by a two‐tailed unpaired student's t‐test. p<0.001 was considered statistically significant. NS means not significant. The colored bands and error bars indicate mean ± standard deviation (SD) (n=3 independent experiments).
Construction of CO2 fixation pathway. (a) Schematic of carbon fixation pathway including IDH (isocitrate dehydrogenase), ACO (aconitase), and ACL (ATP citrate lyase). (b) The concentration of NADPH as a function of time with the addition of IDH (50 U mL⁻¹), ACO (1.8 U mL⁻¹), and ACL (11 U mL⁻¹) at 0, 40, and 80 min, respectively. (c) The concentration of NADPH as a function of time in the solution containing no enzyme (black curve), IDH (50 U mL⁻¹, red curve), IDH (50 U mL⁻¹)+ACO (1.8 U mL⁻¹) (blue curve), IDH (50 U mL⁻¹)+ACO (1.8 U mL⁻¹)+ACL (11 U mL⁻¹) (green curve). (d) Effect of ACO concentration on carbon fixation efficiency. (e) Effect of ACL concentration on carbon fixation efficiency. (f) Effect of pH values on carbon fixation efficiency. (g) HPLC chromatogram of carbon fixation products after 0, 5, 10, 15, and 20 min enzyme cascade reaction in the presence of IDH (50 U mL⁻¹), ACO (10.8 U mL⁻¹), and ACL (44 U mL⁻¹) with ATP concentration of 1 mM. The peaks 1,2,3 and 4 are α‐oxoglutarate, isocitrate, citrate, and OAA, respectively. (h) The concentration of OAA corresponding to the (g). *p<0.05, **p<0.01 and ***p<0.001 by a two‐tailed unpaired student's t‐test. p<0.05 was considered statistically significant. NS means not significant. The colored bands and error bars indicate mean±standard deviation (SD) (n=3 independent experiments).
Light‐driven carbon fixation using photosynthetic organelles inside artificial cells. (a) Schematic of GUVs containing photosynthetic organelles and phycocyanin (PC). (b) Fluorescence images of GUVs containing photosynthetic organelles taken with green channel (left), red channel (middle), and their merged image (right). The scale bars were 10 μm. (c) Effect of photosynthetic organelle concentration on ATP production inside GUVs. (d) Schematic of artificial photosynthetic cell containing photosynthetic organelles, PC, carbon fixation pathway, and the three enzymes (50 U mL⁻¹ IDH, 10.8 U mL⁻¹ ACO, and 44 U mL⁻¹ ACL). (e) The fluorescence images of artificial photosynthetic cell in the dark (top row) and light (bottom row) conditions taken in the blue channel, and the corresponding fluorescence line profiles of the white dashed lines in the left images. The scale bars were 10 μm. (f) HPLC chromatograms of acetyl‐CoA produced by artificial photosynthetic cells with illumination for 1 hour (green curve) and without light (black curve). (g) HPLC chromatograms of OAA produced by artificial photosynthetic cells with illumination for 1 hour (blue curve) and without light (black curve). The error bars indicate mean±standard deviation (SD) (n=3 independent experiments).
Light‐Driven Carbon Fixation Using Photosynthetic Organelles in Artificial Photosynthetic Cells

February 2025

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31 Reads

Building an artificial photosynthetic cell from scratch helps to understand the working mechanisms of chloroplasts. It is a challenge to achieve carbon fixation triggered by photosynthetic organelles in an artificial cell. ATP synthase and photosystem II (PSII) are purified and reconstituted onto the phospholipid membrane to fabricate photosynthetic organelles. With the integration of phycocyanin, the ATP production yield increases by 2.51‐fold due to the enhanced light harvesting capability. The carbon fixation pathway is established by converting α‐oxoglutarate to acetyl‐CoA and oxaloacetate with cascade enzyme reactions including the isocitrate dehydrogenase (IDH), aconitase (ACO), and ATP citrate lyase (ACL). The photosynthetic organelles, phycocyanin, and carbon fixation pathway are encapsulated into giant unilamellar vesicles to obtain artificial photosynthetic cells, which convert α‐oxoglutarate to acetyl‐CoA and oxaloacetate inside artificial cells upon light irradiation. The acetyl‐CoA is the most important intermediate product in the cellular metabolic networks for the synthesis of cholesterol and fatty acids. Our results provide a way for efficient light energy conversion to produce ATP and fix CO2, and pave the path to build autonomous artificial cells with more complicated metabolic networks.


Light‐Driven Carbon Fixation Using Photosynthetic Organelles in Artificial Photosynthetic Cells

January 2025

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22 Reads

Angewandte Chemie

Building an artificial photosynthetic cell from scratch helps to understand the working mechanisms of chloroplasts. It is a challenge to achieve carbon fixation triggered by photosynthetic organelles in an artificial cell. ATP synthase and photosystem II (PSII) are purified and reconstituted onto the phospholipid membrane to fabricate photosynthetic organelles. With the integration of phycocyanin, the ATP production yield increases by 2.51‐fold due to the enhanced light harvesting capability. The carbon fixation pathway is established by converting α‐oxoglutarate to acetyl‐CoA and oxaloacetate with cascade enzyme reactions including the isocitrate dehydrogenase (IDH), aconitase (ACO), and ATP citrate lyase (ACL). The photosynthetic organelles, phycocyanin, and carbon fixation pathway are encapsulated into giant unilamellar vesicles to obtain artificial photosynthetic cells, which convert α‐oxoglutarate to acetyl‐CoA and oxaloacetate inside artificial cells upon light irradiation. The acetyl‐CoA and oxaloacetate are the most important intermediate products in the cellular metabolic networks for the synthesis of cholesterol and fatty acids. Our results provide a way for efficient light energy conversion to produce ATP and fix CO2, and pave the path to build autonomous artificial cells with more complicated metabolic networks.





Sucrose release property of pH-responsive artificial cells
a Schematic diagram showing the fluid and gel phase of pH-responsive molecules against solution pH. b Photos of the fluid phase (pH 10) and gel phase (pH 5). c Schematic illustration showing the responsive property of species A. d Motion trajectories of red fluorescent polystyrene microspheres at pH 7 (left image) and pH 6 (right image). Scale bar is 5 μm. e Oscillation of the inner solution diffusion coefficient of pH-responsive artificial cells as a function of time by alternating the solution pH between 6.5 and 6.6. f Sucrose leakage from pH-responsive artificial cells 20 min after melittin was added as a function of solution pH. The release concentration of sucrose is obtained from three independent samples. Data are presented as the mean values ± SDs, n = 3. Source data are provided as a Source Data file.
Construction of a two-species community of pH-responsive artificial cells (containing sucrose) (species A) and S. cerevisiae (species B) and its pH oscillatory environment
a Schematic illustration of solution pH oscillation caused by feedback between species A and B. b A typical solution pH oscillation of a two-species-community system as a function of time. Species A and B were 2.76 × 10⁶/mL and 4.36 × 10⁶/mL, respectively. c pH value of CO2 oversaturated (phase I, red curve) and saturated (phase II, blue curve) gadobutrol solution as a function of time. CO2 was injected into gadobutrol solution in phase I. The gadobutrol solution was saturated by CO2 from air in phase II. d The initial sucrose concentration and sucrose concentration at the end of oscillation after 960 min. The sucrose concentrations were obtained by adding 10% Triton X-100 into the solution to release sucrose from species A. The concentration of sucrose at initial and end (960 min) of oscillation was tested with three independent samples. Data are presented as the mean values ± SDs, n = 3. e Flow cytometry scatter plots of live-dead stained species B at the longest oscillation time (960 min). Live S. cerevisiae (species B) was stained with FDA (green, in Q3), and dead S. cerevisiae was stained with PI (red, in Q1). The total number of particles counted was 10,000. Source data are provided as a Source Data file.
Three-species community containing sucrose and G6P containing pH-responsive artificial cells (species A′), S. cerevisiae (species B) and NAD⁺ and G6PDH containing artificial cells (species C)
a Schematic diagram showing solution pH oscillation and NADH generation inside species C caused by the feedback between species A′ and species B. b A typical solution pH oscillation of a three-species-community system as a function of time with species A′ (6.10 × 10⁶/mL) containing 150 mM sucrose and 10 mM G6P, species B (4.36 × 10⁶/mL), and species C (4.36 × 10⁶/mL) containing 10 mM NAD⁺ and 10 μg/mL G6PDH. c Fluorescence intensity of the same community as (b) as a function of time. d Corresponding microscopy images of the community system at the time points in (b). The first column images were observed using a green filter for viewing species A′. The second column images were observed in bright field for viewing species B. The third column images were recorded using a blue filter for viewing species C. The fourth column images were the merged images of Columns 1, 2 and 3 of each row. Scale bar is 5 μm. e The fluorescence intensity of the same three-species communities as a function of time with the absence of G6PDH in species C (blue curve), G6P in species A′ (red curve), or NAD⁺ in species C (black curve). G6PDH and G6P are the abbreviations of glucose-6-phosphate dehydrogenase and glucose-6-phosphate, respectively. NAD⁺ and NADH are the abbreviations of nicotinamide adenine dinucleotide and nicotinamide adenine dinucleotide plus hydrogen. Source data are provided as a Source Data file.
Communication among spatially coded three-species communities
a The pH oscillation curve of community CA′B as a function of time. b The corresponding laser scanning confocal microscopy images at points 1, 2, and 3 in (a). c The fluorescence intensity of species C of community CA′B as a function of time. d The pH oscillation curve of CBA′ as a function of time. e The corresponding laser scanning confocal microscopy images at points 1, 2, and 3 in (d). f The fluorescence intensity of species C of community CBA′ as a function of time. g The pH oscillation curve of A′CB as a function of time. h The corresponding laser scanning confocal microscopy images at points 1, 2, and 3 in (g). i The fluorescence intensity of species C of community A′CB as a function of time. The mean fluorescence intensities of species C in (c), (f), and (i) are from ten independent samples. Data are presented as the mean values ± SDs, n = 10. G6P is the abbreviations of glucose-6-phosphate. Source data are provided as a Source Data file.
Regulation of species metabolism in synthetic community systems by environmental pH oscillations

November 2023

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110 Reads

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5 Citations

Constructing a synthetic community system helps scientist understand the complex interactions among species in a community and its environment. Herein, a two-species community is constructed with species A (artificial cells encapsulating pH-responsive molecules and sucrose) and species B (Saccharomyces cerevisiae), which causes the environment to exhibit pH oscillation behaviour due to the generation and dissipation of CO2. In addition, a three-species community is constructed with species A′ (artificial cells containing sucrose and G6P), species B, and species C (artificial cells containing NAD⁺ and G6PDH). The solution pH oscillation regulates the periodical release of G6P from species A′; G6P then enters species C to promote the metabolic reaction that converts NAD⁺ to NADH. The location of species A′ and B determines the metabolism behaviour in species C in the spatially coded three-species communities with CA′B, CBA′, and A′CB patterns. The proposed synthetic community system provides a foundation to construct a more complicated microecosystem.


Schematic illustration of light harvesting and metabolism mimicry artificial system. a) Scheme of cyanobacteria containing artificial cell for endosymbiosis mimicking. b) Chemical reaction equations involved in metabolism mimicking pathways.
Encapsulation of cyanobacteria inside GUVs. a) Encapsulation efficiency as a function of cyanobacteria concentration. The encapsulation efficiency was 3.4 ± 1.4%, 4.9 ± 1.7%, 6.1 ± 2.2%, 9.6 ± 3.8%, 11.9 ± 4.3%, 16.5 ± 0.6%, 27.1 ± 2.8%, 40.5 ± 12.2%, and 41.9 ± 14.2% with the cyanobacteria concentration of 7.7, 15.3, 22.9, 30.6, 38.3, 76.5 153.1, 229.5, and 306.1 mg mL⁻¹, respectively. Data are presented as mean values ± SD. b) The fraction of artificial cells containing less than five cyanobacteria and more than five cyanobacteria at different cyanobacteria concentrations. The fraction of artificial cells containing less than five cyanobacteria was 100%, 100%, 99.1%, 97.9%, 88.5%, 67.5%, 58.3%, 55.5%, and 55% with the cyanobacteria concentration of 7.7, 15.3, 22.9, 30.6, 38.3, 75.6, 153.1, 229.5, and 306.1 mg mL⁻¹, respectively. At least 100 vesicles were counted to obtain each data. Representative fluorescence microscopy images of the artificial cells containing a single c) and multiple d) cyanobacteria. e) The confocal image of the artificial cell containing one cyanobacterium with two cross‐section images. All scale bars were 20 µm. The artificial cells were labelled with NBD‐PE in the lipid bilayer (green fluorescence).
Chemical communications between cyanobacteria and “cytoplasm” inside the artificial cells. The representative images of artificial cells containing cyanobacteria, GOx, and HRP before (a) and after (b) the introduction of Amplex red and 24 h light illumination. The scale bars were 20 µm. c) The amount of produced glucose as a function of illumination time in the test tube. The colored bands indicate mean ± SD of three independent experiments. d) The corresponding scheme of cascade reactions between the cyanobacteria and “cytoplasm” inside an artificial cell. e) Fluorescence intensity of produced resorufin inside the artificial cells (containing both GOx and HRP, GOx and HRP only) against time. The colored bands indicate mean ± SD. At least 100 vesicles were counted to obtain each data. f) Chemical reaction equations involved in artificial cells.
Chemical communications between cyanobacteria and protoorganelle inside the artificial cells. The representative images of artificial cells containing cyanobacteria, GOx, and protoorganelle (containing HRP) before (a) and after (b) 24 h light illumination with the introduction of Amplex red. c) The corresponding scheme of cascade reactions between the cyanobacteria and protoorganelle inside an artificial cell. d) Fluorescence intensity of produced resorufin in the prtotoorganelle (red curve) and “cytosol” (green curve) with HRP inside protoorganelle and GOx in the “cytosol”. e) The control experiments with GOx in the “cytosol”, but with no HRP inside protoorganelle. f) The control experiments with HRP inside protoorganelle, but with no GOx in the “cytosol”. The coloured bands indicate mean ± SD. At least 30 vesicles were counted to obtain each data. The scale bars were 20 µm.
The cascade cycling of NADH/NAD⁺ inside cyanobacteria‐containing artificial cells. a) The scheme of NADH production inside an artificial cell. b) Fluorescence microscope image of a cyanobacteria‐containing artificial cell after 24 h continuous daylight lamp illumination. Green, blue, and red fluorescence represent phospholipid membrane, NADH and the cyanobacteria, respectively. c) The normalized λem (460 nm) intensity (%) versus time curves in the artificial cells. The colored bands indicate mean ± SD of independent experiments (n = 3). d) The scheme of lactate production inside an artificial cell. e) The fluorescence microscope images of artificial cells (with and without pyruvate (73.1 × 10‐6 m)) and plot of blue fluorescence intensities across artificial cells with and without pyruvate (73.1 × 10‐6 m), respectively. f) The relative fluorescence intensities at different pyruvate concentrations (0, 36.5, 73.1 × 10‐6 m) in artificial cells (containing cyanobacteria, NAD⁺, GDH, LDH) after heating at 45°C for 2 h. Statistical analyses were carried out by two‐tailed unpaired student's t‐test (**p < 0.01). p < 0.05 was considered statistically significant. The error bars were the standard deviation. At least 100 vesicles were counted to obtain each data. g) Chemical reaction equations involved in the artificial cells. The scale bars were 20 µm.
Light‐Harvesting Artificial Cells Containing Cyanobacteria for CO2 Fixation and Further Metabolism Mimicking

July 2022

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75 Reads

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18 Citations

The bottom‐up constructed artificial cells help to understand the cell working mechanism and provide the evolution clues for organisms. The energy supply and metabolism mimicry are the key issues in the field of artificial cells. Herein, an artificial cell containing cyanobacteria capable of light harvesting and carbon dioxide fixation is demonstrated to produce glucose molecules by converting light energy into chemical energy. Two downstream “metabolic” pathways starting from glucose molecules are investigated. One involves enzyme cascade reaction to produce H2O2 (assisted by glucose oxidase) first, followed by converting Amplex red to resorufin (assisted by horseradish peroxidase). The other pathway is more biologically relevant. Glucose molecules are dehydrogenated to transfer hydrogens to nicotinamide adenine dinucleotide (NAD⁺) for the production of nicotinamide adenine dinucleotide hydride (NADH) molecules in the presence of glucose dehydrogenase. Further, NADH molecules are oxidized into NAD⁺ by pyruvate catalyzed by lactate dehydrogenase, meanwhile, lactate is obtained. Therefore, the cascade cycling of NADH/NAD⁺ is built. The artificial cells built here pave the way for investigating more complicated energy‐supplied metabolism inside artificial cells.


Ultrasound in Cellulose-Based Hydrogel for Biomedical Use: from Extraction to Preparation

January 2022

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63 Reads

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22 Citations

Colloids and Surfaces B Biointerfaces

As the most abundant natural polymer on the planet, cellulose has a wide range of applications in the biomedical field. Cellulose-based hydrogels further expand the applications of this class of biomaterials. However, a number of publications and technical reports are mainly about traditional preparation methods. Sonochemistry offers a simple and green route to material synthesis with the biomedical application of ultrasound. The tiny acoustic bubbles, produced by the propagating sound wave, enclose an incredible facility where matter interact among at energy as high as 13 eV to spark extraordinary chemical reactions. Ultrasonication not only improves the efficiency of cellulose extraction from raw materials, but also influences the hydrogel preparation process. The primary objective of this article is to review the literature concerning the biomedical cellulose-based hydrogel prepared via sonochemistry and application of ultrasound for hydrogel. An innovated category of recent generations of hydrogel materials prepared via ultrasound was also presented in some details.


Citations (17)


... For instance, BSA, a major serum protein, is used in biomedical applications such as drug delivery and tissue engineering due to its natural compatibility with biological systems. [113][114][115] TW-20 is a nonionic surfactant frequently utilized in pharmaceuticals for its low toxicity profile, while APS, at the controlled concentration used in our study (0.06 M), aligns with established safe ranges for hydrogel formation in biomedical applications. [116][117][118][119] Similarly, Ru(II)bpy 3 þ2 , employed as a crosslinking agent, has demonstrated minimal cytotoxicity at the used concentration (0.4 mM), as supported by prior studies. ...

Reference:

Bovine Serum Albumin‐Based Sponges as Biocompatible Adsorbents: Development, Characterization, and Perfluorooctane Sulfonate Removal Efficiency
Bovine serum albumin-based hydrogels: Preparation, properties and biological applications
  • Citing Article
  • October 2024

Chemical Engineering Journal

... In such systems, supramolecular structures form and change in a pre-programmed manner, controlled by external stimuli such as chemical or light triggers, and typically result in changes in molecular structure [10][11][12] . These transient and dynamic systems have been investigated in the bulk, as well as within droplets 13,14 . The processes occurring in these systems are often comparable or analogous to those found within cells, especially when confined within droplets. ...

Regulation of species metabolism in synthetic community systems by environmental pH oscillations

... As a readout, we used the protein Hyper7, a hydrogen peroxide responsive fluorescent protein 54 . To generate hydrogen peroxide we used glucose oxidase [55][56][57] . One population of GUVs, marked with pre-expressed mCherry, expresses αHL with the K3 loop insert and also contains glucose oxidase (sender cells). ...

Light‐Harvesting Artificial Cells Containing Cyanobacteria for CO2 Fixation and Further Metabolism Mimicking

... When energy is transferred to biopolymers in this way, it can cause them to break down into smaller units. Sonication has been described for the disruption of Hbonds as well as polysaccharide bonds; thus, US irradiation can reduce the diameter of fibers or even the scission of long cellulose fibers [44,45]. This is also one of the main reasons for the practical use of US in nanomaterial preparation from pure crystalline cellulose. ...

Ultrasound in Cellulose-Based Hydrogel for Biomedical Use: from Extraction to Preparation
  • Citing Article
  • January 2022

Colloids and Surfaces B Biointerfaces

... Therefore, the synthesis of DN hydrogels utilizing physically cross-linked reversible sacrificial bonds has been a key focus of research. Even when subjected to external forces that lead to the rupture of internal non-covalent bonds, physically cross-linked DN hydrogels can exhibit a certain capacity for secondary utilization and repeated use due to the ability of non-covalent bonds (such as intermolecular hydrogen bonds, van der Waals forces or hydrophobic interactions) to reconnect [55][56][57][58][59]. ...

Preparation and characterization of double network hydrogel with high-strength and self-healing
  • Citing Article
  • May 2021

Materials Today Communications

... To overcome these weaknesses, pullulan is usually composited with other materials [11][12][13][14][15][16][17]. Guar gum is a natural polysaccharide compound with galactomannan as LLE powder were added (weight percent with respect to the amount of guar gum), and the mixture was stirred for 10 min until the LLE powder was completely dissolved. ...

Preparation and characterization of pullulan derivative antibacterial composite films
  • Citing Article
  • February 2020

Materials Science and Engineering C

... Instances for magnetophoresis include magnetic targeted drug delivery [17] in microfluidics [18], particle magnetic separation [19]. In the micro/milliscale, the motion of dispersed phase such as tumors [20] and cells [21] under a magnetic field undergoes an isolation or magnetic assembly. The Kelvin force, responsible for these depicted effects, is derived from the gradient of the magnetic term of Gibbs free energy G [22,23]. ...

Programmed magnetic manipulation of vesicles into spatially coded prototissue architectures arrays

... Based on historical factors, most of the existing food coating is low-cost and has good mechanical and barrier properties originally made of petrochemical products or cellulose [1][2]. As time goes by, this faces pressure from environmental problems, so it is necessary to gradually eliminate the use of petrochemical materials, and replace them with innovative and biodegradable polymer coating such as chitosan [3], alginate [4], cellulose [5], starch [6], pullulan [7], polylactic acid [8], etc., where demand continues to increase. The food industry is forced to develop and adopt new antimicrobial materials for coating due to the need to reduce food waste, increase food safety, and extend the shelf life of food [9]. ...

Preparation and characterization of pullulan derivative/chitosan composite film for potential antimicrobial applications
  • Citing Article
  • January 2020

International Journal of Biological Macromolecules

... Shape can dictate propulsion by, for example, trapping the catalyst in a cavity with only one opening, forcing the propelling force through this one outlet [14][15][16][17]. Other methods of dictating the location of propulsion force are through concave shapes [6,18], as oversaturation is more easily reached there, or by differences in surface roughness, since roughness enables bubble pinning and can thus enhance the speed of bubble propelled motors [3,7]. Asymmetry in catalyst distribution directly dictates the location of the propulsion force, since the location of the catalyst is where the reaction happens and, thus, where the propelling products are formed. ...

Bowl‐like Micromotors Using Red Blood Cell Membrane as Template

... The lower cytotoxicity of final CUR-POM@PolyIL NCs compared to POM@PolyIL NCs could be related to CUR's protective effects in normal cells [95]. The same results were reported by others [96,97] on normal cells for POMs nanoformulations in comparison to free POMs. Based on these results, the second hypothesis of this study was confirmed. ...

The Synthesis and Biological Function of a Novel Sandwich‐Type Complex Based on {SbW 9 } and Flexible bpp Ligand
  • Citing Article
  • August 2019