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Engineering metal-organic frameworks (MOF) for heterogeneous catalysts have been of extreme interest since they could bridge the gap between homogeneous and heterogeneous catalysis. We have designed and synthesized gold functionalized IRMOF-3 catalysts by post-covalent modification (PM) and one-pot (OP) synthesis methods. The gold functionalized IRMOF-3 catalysts provide an efficient, economic, and novel route for the one-pot synthesis of structurally divergent propargylamines via three component coupling of alkyne, amine, and aldehyde (A 3 ) without any additives or an inert atmosphere. The catalysts were characterized in depth to understand their structure-property relationship. It was shown that the 4.6%Au/IRMOF-3 catalyst, prepared by the PM method, contains a fraction of cationic gold (Au 3+ / Au 0 = 0.2), which shows much higher catalytic activity than that of 3.2% or 0.6%Au/IRMOF-3 prepared by OP method, although the former exhibits much lower crystallinity than the latter two catalysts. Notably, the catalytic activity of the Au/IRMOF-3 catalysts could be significantly enhanced at a moderate reaction temperature (150 °C). All the Au/IRMOF-3 catalysts can be easily recycled and used repetitively at least 5 times, especially the catalysts prepared by the OP method, which showed no drop in activity for the successive 5 uses. These features render the catalysts particularly attractive in the practice of propargylamines synthesis in an environmentally friendly manner.

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Homochiral MOFs were engineered using postsynthetic modification and a one-pot synthetic strategy. l-Proline functionalized IRMOF-3 show high ee for aldol reaction. Gold functionalized CUP-1 catalysts are highly efficient for the A3 coupling reaction.

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To relieve the environmental issues of sewage sludge (SS) disposal and greenhouse gas (GHG) emission in China, we proposed an integrated method for the first time to simultaneously deal with these two problems. The hot slags below 920 °C could act as a good heat carrier for sludge gasification and the increasing CO2 concentration in CO2/O2 atmospheres enhanced the production of CO and H2 at 400–800 °C. Three stages of syngas release were clearly identified by Gaussian fittings, i.e., volatile release, char transformation and fixed carbon reaction. Additionally, the effect of sulfur retention of slags and the synergy effect of the stabilization of toxic elements in the solid residuals were discovered in this study. Furthermore, a novel prototype of multiple industrial and urban systems was put forward, in which the produced CO + H2 could be utilized for direct reduced iron (DRI) production and the solid residuals of sludge ash and glassy slags would be applied as cementitious materials. For a steel plant with an annual production of crude steel of 10 million tons in China, the total annual energy saving and GHG emission reduction achieved are 3.31*105 tons of standard coal and 1.74*106 tons of CO2, respectively.

The challenge for polymeric enzyme reactors at present is to selectively control the enzymolysis rate in complex conditions. Additionally, the fabrication methodology is hindered by complex processes, especially for achieving diverse stimuli responsiveness and functions. Here, we reported a kind of pH-sensitive polymer, poly(styrene-co-maleic anhydride-acrylic acid) (PS-MAn-AA)-based hybrid enzyme reactor. It comprised magnetic nanoparticles and a pH-sensitive PS-MAn-AA porous polymer membrane made by breath figure method. The enzyme L-asparaginase (L-ASNase) could covalently bond on the surface of the pH-sensitive porous polymer membrane (pH-PPM), and the resultant enzyme reactor was characterized by Fourier transform infrared spectroscopy and vibrating sample magnetometer. The apparent Michaelis−Menten constants (K m and V max ) of the L-ASNase enzyme reactor at different pH values were determined by a chiral ligand-exchange capillary electrophoresis method with L-asparagine as the substrate. The V max value of the L-ASNase enzyme reactor (0.67 mM/min) was almost 3-fold of that of the free L-ASNase (0.23 mM/min) at pH 8.2. Its ability to precisely control the enzymolysis rate in complex conditions is triggered primarily by the pH of the buffer solution, allowing controlled enzymatic reactions and displaying excellent stability and reusability of the proposed pH-PPM. This strategy for porous polymer membrane enzyme reactor fabrication has established a platform for enzyme efficiency adjusting. These valve-like distinguished features highlight the outstanding potential of stimuli-responsive enzyme reactor applied for enzyme immobilization and enzyme-related disease treatment.