C01B32/342

ACTIVATED CARBON AND METHOD FOR MANUFACTURING THE SAME
20170247258 · 2017-08-31 ·

Disclosed is an activated carbon including pores formed on a surface thereof, in particular, the pores include ultra-micropores having a diameter that is equal to or less than about 1.0 nm.

Specialized Activated Carbon Derived From Pretreated Biomass
20170226535 · 2017-08-10 ·

Provided are methods, systems, and compositions for producing activated carbon from lignin residues produced from cellulosic or lignocellulosic biomass after hydrolysis of saccharides. The activated carbon is low in ash and sulfur, high in oxygen content and iodine number.

Sulfur-carbon nanocomposites and their application as cathode materials in lithium-sulfur batteries

The invention is directed in a first aspect to a sulfur-carbon composite material comprising: (i) a bimodal porous carbon component containing therein a first mode of pores which are mesopores, and a second mode of pores which are micropores; and (ii) elemental sulfur contained in at least a portion of said micropores. The invention is also directed to the aforesaid sulfur-carbon composite as a layer on a current collector material; a lithium ion battery containing the sulfur-carbon composite in a cathode therein; as well as a method for preparing the sulfur-composite material.

PROCESS FOR HYDROCRACKING HEAVY OIL AND OIL RESIDUE WITH A CARBONACEOUSE ADDITIVE
20170267937 · 2017-09-21 · ·

A process for the hydroprocessing of heavy oils and/or oil residues, the process comprising the steps of contacting a non-metallised carbonaceous material with an acid to form a non-metallised carbonaceous additive; and contacting the heavy oils and/or oil residues with the non-metallised carbonaceous additive in the presence of a hydrogen-containing gas at a temperature of from 250° C. to 600° C.

Multi-grafting site carbon nanomaterial and activated carbon nanomaterial and preparation method thereof and displacement system for ultra-low permeability oil reservoirs

The present disclosure discloses a multi-grafting site carbon nanomaterial comprising a structural unit represented by Formula (1), hydroxyl groups and a structural unit represented by Formula (2); wherein R is one or more selected from the group consisting of tolyl, diphenylmethyl, isophorone group and dicyclohexylmethyl; ##STR00001##

Multi-grafting site carbon nanomaterial and activated carbon nanomaterial and preparation method thereof and displacement system for ultra-low permeability oil reservoirs

The present disclosure discloses a multi-grafting site carbon nanomaterial comprising a structural unit represented by Formula (1), hydroxyl groups and a structural unit represented by Formula (2); wherein R is one or more selected from the group consisting of tolyl, diphenylmethyl, isophorone group and dicyclohexylmethyl; ##STR00001##

CARBON BLACK CONVERSION INTO MICROPOROUS CARBON

The present invention is related to highly oxygenated nanoribbons and highly microporous carbon (mPC) produced by the oxidation of a series of carbon blacks in nitric acid followed by fast and slow pyrolysis, respectively. New porous carbons according to the invention does not need to be activated by strong alkaline activators, for example, KOH and NaOH. The best prepared mPC showed a high capacity for carbon dioxide capture of 1 to 3.9 mmol/g at pressures between 0.15 and 1 bar and 25° C.

CARBON BLACK CONVERSION INTO MICROPOROUS CARBON

The present invention is related to highly oxygenated nanoribbons and highly microporous carbon (mPC) produced by the oxidation of a series of carbon blacks in nitric acid followed by fast and slow pyrolysis, respectively. New porous carbons according to the invention does not need to be activated by strong alkaline activators, for example, KOH and NaOH. The best prepared mPC showed a high capacity for carbon dioxide capture of 1 to 3.9 mmol/g at pressures between 0.15 and 1 bar and 25° C.

Method for producing activated carbon
11370665 · 2022-06-28 · ·

A method is for producing activated carbon. The method includes: a) mixing a carbonaceous precursor with chemically activating agents to obtain a feedstock mixture; b) producing activated carbon by heating the feedstock mixture under the atmosphere of a physically activating gas; and c) performing suitable post-activation treatment of the produced activated carbon. Step a) includes in sequence the sub-steps of: i. addition of a first chemically activating agent to obtain an impregnated precursor; and ii. addition of a second chemically activating agent to obtain the feedstock mixture. An activated carbon species is obtainable by the method. The activated carbon species may thus be tuned to have a pore size distribution optimized for use in a carbon electrode.

Porous carboxylated jute stick activated carbon

Jute stick/stalk can be used to prepared and carboxylated to yield useful activated carbons, e.g., for removing Pb.sup.2+ from drinking water. Such activated carbons can act as an inexpensive adsorbents using agricultural waste or by-products. Carboxylation of jute stick activated carbon (JSAC) can improve its efficiency for Pb.sup.2+ removal, e.g., from aqueous solutions, even if its BET surface area is reduced. Carboxylated JSAC (JSAC-COO.sup.−) can have surface areas around 615.3±0.5, 1, 2.5, 5, 10, 15, 20, or 25 m.sup.2/g. JSAC-COO.sup.− can treat varied Pb.sup.2+ concentrations, 10, 25 mg/L, etc., pHs, e.g., 4.0, 7.0, etc., temperatures, e.g., 15° C., 27° C., etc., and contact periods, e.g., 1, 5, 10, 15, 30, 60 minutes, etc., achieving up to 99.8% Pb.sup.2+ removal within 15 minutes of contact JSAC-COO.sup.− adsorption capacity can be >25.0 mg Pb.sup.2+/g, as well as other metal ions, with potential for water and/or gas treatment.