发明名称 Unsupported and supported non-promoted ruthenium sulfide catalyst with high catalytic activity for hydrocarbon hydrotreatments and its method
摘要 The present invention relates to a synthesis method for unsupported and supported ruthenium base (RuS2) catalysts from a ruthenium complex precursor, which is decomposed and activated by a simple activation process; these steps provide a catalyst with very high catalytic activity, in addition the incorporation of ruthenium complex precursor to a support by methods of incipient and wet impregnating is described; the obtained catalytic activities in this invention are in the order of 100 times the molybdenum sulfide catalyst without support and without promoter, 14 times the industrial supported catalyst, and 5 times the activity of the currently most active commercial unsupported catalyst.
申请公布号 US8987165(B2) 申请公布日期 2015.03.24
申请号 US201213444411 申请日期 2012.04.11
申请人 Centro de Investigacion en Materiales Avanzados, S.C. 发明人 Ornelas Gutierrez Carlos Elias;Alvarez Contreras Lorena;Farias Mancilla Jose Rurik;Aguilar Elguezabal Alfredo
分类号 B01J27/02;B01J27/045 主分类号 B01J27/02
代理机构 Defillo & Associates, Inc. 代理人 Defillo & Associates, Inc. ;Defillo Evelyn A.
主权项 1. A synthesis method for obtaining ruthenium sulfide (RuS2) catalyst without an additional metal or not promoted comprising the steps of: a) dissolving hydrated ruthenium chloride in a solution of R1COR2, R2-OH, C4H8O (THF), C4H8O2, CH2Cl2 (DCM), C2H3N (MeCN), C3H7ON (DMF), C2H6SO (DMSO) or a combination thereof: wherein: R1 is equal to OH or a lineal chain or branched radical C1 to C8; R2 is equal to H, a lineal chain or branched radical C1 to C8, with relation 0.01 to 40 ml of solvent per gram of salt dissolved in methanol, ethanol or acetone; b) dissolving ammonium chloride in solution of R1COR2, R2-OH, C4H8O (THF), C4H8O2, CH2Cl2 (DCM), C2H3N (MeCN), C3H7ON (DMF), C2H6SO (DMSO) or a combination of these; wherein: R1 is equal to OH or a lineal chain or branched radical C1 to C8; R2 is equal to H, a lineal chain or branched radical C1 to C8, with relation 0.01 to 40 ml of solvent per gram of salt dissolved in water, methanol, ethanol, acetone or combination thereof; c) adding the NH4CI solution of b) in a molar relation of 1:1 to 10:1 to the ruthenium chloride solution of a), keeping in mechanical agitation between 100 to 700 rpm during the addition and up to 30 minutes after the addition has finished; d) adding NH4OH or HCI in proportion of 0.01 to 2 ml per gram of ruthenium chloride; e) adding to the solution of step c) or d) a R3COR4 or R3COOR5 compound, whereinR3 is a linear chain or branched radical C1 to C8,R4 is equal to H or a linear chain or branched radical C1 to C8 and includes 1 or 2 oxygen atoms or 1 nitrogen atom,R5 is equal to a hydrogen radical or a linear chain or branched radical C1 to C10; f) leaving to the solution of e) in mechanical agitation for 30 minutes between 100-700 rpm and resting from 0.1 to 3 hr to allow crystallization; a family of ruthenium complex compounds very soluble in water and sparingly soluble in acetone is produced and precipitated, the family of ruthenium complex compounds have decomposition temperatures above 200° C. and total decomposition to metallic ruthenium in inert atmosphere to temperatures lower than 415° C.; filtering and washing with acetone the precipitate; g) incorporating the family of ruthenium complex compounds to a support by using a method selected from an incipient impregnating method or a wet impregnating method, wherein a support bed includes: TiO2, zeolitic, MCM-41, SBA-15, alumina, silica, mixed oxides, or a combination thereof; doped or not doped, wherein the support is impregnated with a solution of the precursory complex in weight relation 1-90% of dissolved metallic charge in the minimum amount of solvent, wherein during the impregnation the solution of the ruthenium complex compounds is drip over the catalyst until filling all porosity; and h) decomposing and activating the ruthenium precursor complex at temperatures between 350° C. to 550° C. with a heating rate from 2 to 50° C. per minute under pressure of 1 atm, in a reducing atmosphere of a gas mixture formed by H2S/G where G may be H2, N2, Ar or He; in H2S concentrations from 2 to 99%.
地址 Chihuahua MX