Sonodynamic therapy (SDT) triggered by ultrasound (US) has attracted increasing attention owing to its ability to overcome critical limitations, including low tissue-penetration depth and phototoxicity in photodynamic therapy (PDT). Biogenic metal oxide nanoparticles (NPs) have been used as anti-cancer drugs due to their biocompatibility properties with most biological systems. Here, sonosensitizer MWO4-PEG NPs (M = Fe Mn Co Ni) were synthesized as inhibitors to activation-induced cytidine deaminase (AID), thus neutralizing the extensive carcinogenesis of AID in diffuse large B-cell lymphoma (DLBCL). The physiological properties of these nanomaterials were examined using transmission electron microscopy (TEM). The inhibition of NPs to AID was primarily identified by the affinity interaction prediction between reactive oxygen species (ROS) and AID through molecular dynamics and molecular docking technology. The cell apoptosis and ROS generation in US-triggered NPs treated DLBCL cells (with high levels of AID) were also detected to indicate the sonosensitivity and toxicity of MWO4-PEG NPs to DLBCL cells. The anti-lymphoma studies using DLBCL and AID-deficient DLBCL cell lines indicated a concentration-dependent profile. The synthesized MWO4-PEG NPs in this study manifested good sonodynamic inhibitory effects to AID and well treatment for AID-positive hematopoietic cancers.
Replacing electrocatalytic oxygen evolution reaction (OER) with amine oxidation reaction is adopted to boost clean and environment‐friendly energy source hydrogen (H2) in water. However, the electrocatalytic reaction is severely restricted by the strong adsorption of product on the catalyst surface. Inspired by the cooperation of flavin adenine dinucleotide and mitochondria membrane in biological system, the catalysis‐separation complex electrodes are introduced to promote the desorption of product and hinder its readsorption by applying polytetrafluoroethylene (PTFE)‐separation membrane on the one side of electrode, which is benefit for the cleanness of active sites on the catalyst surface for the continuous production and timely separation of nitrile and hydrogen. With the intermolecular force between PTFE and nitrile, the nitrile droplets can be quickly desorbed and separated from catalyst surface of anode, and the size of nitrile droplets on the catalyst surface is only 0.23% to that without PTFE. As a result, the current at 1.49 VRHE from the catalyst with PTFE membrane is about 33 times to that of catalyst without PTFE after long‐term operation. Moreover, the cathode with PTFE membrane also achieves the rapid desorption of H2 bubbles and stable cathodic current because of the strong absorption of PTFE to H2.
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