A reverse osmosis membrane of the present invention includes a porous support substrate (2) and a separation active layer (3) formed on a surface of the porous support substrate (2) and formed of a carbon film containing organized carbon.

The present invention relates to a method for manufacturing at least one monolithic inorganic porous support (1) having a porosity comprised between 10% and 60% and an average pore diameter ranging from 0.5 μm to 50 μm, using a 3D printer type machine (I) to build, in accordance with a 3D digital model, a manipulable three-dimensional raw structure (2) intended to form, after sintering, the monolithic inorganic porous support(s) (1).

A nanopore sensing system includes a cis well, a trans well, and a metal based membrane positioned between the cis and trans wells so that a channel defined in the metal based membrane fluidically connects the cis and trans wells. The metal based membrane has a thickness ranging from about 1 nm to about 3 nm and is selected from the group consisting of a metal oxide, a metal sulfide, a metal nitride, a metal phosphide, a metal arsenide, a metal antimonide, a metal selenide, and a metal telluride.

A reverse osmosis membrane of the present invention includes a porous support substrate (2) and a separation active layer (3) formed on a surface of the porous support substrate (2) and formed of a carbon film containing organized carbon.

A low-cost and easy-to-fabricate mixed e.sup. and CO.sub.3.sup.2 conducting membrane for advanced high-flux and selective electrochemical CO.sub.2 separation from flue gas is provided. The membrane includes a CO.sub.3.sup.2-conducting molten carbonate phase and an e.sup.-conducting lithiated Ni-oxide interphase that can be formed in situ during operation. The membrane exhibits a CO.sub.2 flux density greater than 0.8 mL/(minute.Math.cm.sup.2) at 850 C. with a selectivity ranging from about 100 to about 500 and excellent stability for up to about 450 hours. Further, the self-formed interphase Li.sub.0.4Ni.sub.1.6O.sub.2 is highly electron conducting and can provide electrons to the co-reduction of CO.sub.2 and O.sub.2 into CO.sub.3.sup.2. Such a membrane is an alternative to the conventional size-sieving inorganic and dissolution-diffusion organic counterparts for CO.sub.2 capture from flue gas.

The present invention provides a preparation method for a composite porous structure, comprising the following steps: step (a): preparing a porous substrate having multiple pores, a first surface and a second surface; and step (b): continuously feeding a cooling fluid to contact the first surface and to flow continuously to the second surface through the pores of the porous substrate, and heating a coating material to multiple molten particles by a heat source and spraying the molten particles onto the second surface of the porous substrate, so as to form a coating layer having multiple micropores on the second surface of the porous substrate and obtain the composite porous structure formed. Besides, also provided is a composite porous structure prepared by the preparation method.

The present invention relates to a method for manufacturing at least one monolithic inorganic porous support (1) having a porosity comprised between 10% and 60% and an average pore diameter ranging from 0.5 ?m to 50 ?m, using a 3D printer type machine (I) to build, in accordance with a 3D digital model, a manipulable three-dimensional green structure (2) intended to form, after sintering, the monolithic inorganic porous support(s) (1).

The present invention provides a preparation method for a composite porous structure, comprising the following steps: step (a): preparing a porous substrate having multiple pores, a first surface and a second surface; and step (b): continuously feeding a cooling fluid to contact the first surface and to flow continuously to the second surface through the pores of the porous substrate, and heating a coating material to multiple molten particles by a heat source and spraying the molten particles onto the second surface of the porous substrate, so as to form a coating layer having multiple micropores on the second surface of the porous substrate and obtain the composite porous structure formed. Besides, also provided is a composite porous structure prepared by the preparation method.

A low-cost and easy-to-fabricate mixed e.sup.? and CO.sub.3.sup.2? conducting membrane for advanced high-flux and selective electrochemical CO.sub.2 separation from flue gas is provided. The membrane includes a CO.sub.3.sup.2?-conducting molten carbonate phase and an e.sup.?-conducting lithiated Ni-oxide interphase that can be formed in situ during operation. The membrane exhibits a CO.sub.2 flux density greater than 0.8 mL/(minute.Math.cm.sup.2) at 850? C. with a selectivity ranging from about 100 to about 500 and excellent stability for up to about 450 hours. Further, the self-formed interphase Li.sub.0.4Ni.sub.1.6O.sub.2 is highly electron conducting and can provide electrons to the co-reduction of CO.sub.2 and O.sub.2 into CO.sub.3.sup.2?. Such a membrane is an alternative to the conventional size-sieving inorganic and dissolution-diffusion organic counterparts for CO.sub.2 capture from flue gas.