The synthesis of trimethylamine (TMA) through am ulticomponent combination of ammonia with carbon dioxide and molecular hydrogenb yu sing ah omogeneous ruthenium catalyst was explored. The use of [Ru(triphos)(tmm)] [triphos: 1,1,1-tris-(diphenylphosphinomethyl)ethane, tmm:t rimethylenem ethane] together with aluminumt rifluoromethanesulfonatea s ac o-catalyst resulted in high ammonia conversion and excellent selectivity for TMA in organic solvents. Aqueous solutions of ammonium chloride were methylated almost quantitatively to the corresponding hydrochloride salt (i.e.,T MA·HCl) in ab iphasic solvent system by using the same Ru complex without the need for any co-catalyst.Methylamines, the simplest members of the aliphatic amine family,r epresent highly importanta nd versatile intermediates within the chemical supply chain. The industrial significance of methylamines is reflected by aw orldwide annual production larger than 1.3 10 6 tw ith ag rowing rate of 3.5% per annum. [1] These basic chemicals are generally used as valuable buildingb locks for the synthesis of solvents, surfactants, ionexchange resins, and synthetic fibers, as well as agrochemical and pharmaceutical products. [2] Methylamines are prepared on industrials cale by the exothermicr eactiono fa mmonia (NH 3 )a nd methanol( CH 3 OH) with an amorphous silica-alumina catalyst in fixed-bed reactors at 390-430 8C( Scheme 1A). The composite equilibria within the reaction network result in complex product mixtures, and the three possible methylamines (mono-, di-, and trimethylamine:M MA, DMA andT MA) are generally produced with moderate selectivity for the individual product, largely controlled by the NH 3 /CH 3 OH feed ratio. [2, 3] Moreover,M MA, DMA, TMA, and NH 3 form an azeotropic mixture, and the use of zeolite-based catalysts in combinationw ith methanol results in dimethyl ether (DME) as an additional byproduct. [4] Consequently,t he downstream purificationp rocess is laboriousa nd requiresatrain of four to five distillationcolumns, which finally results in integrated production plants at economy of scale. [2a, 5] The synthesis of the ammonium chlorides is typically achieved in as ubsequents tep (Scheme 1B).Herein, we report anovel catalytic approach for the selective synthesis of trimethylaminea nd its hydrochloride by using carbon dioxide (CO 2 )a sarenewable C 1 building block fort he formation of the three methyl groups on ammonia in the presence of molecular hydrogen. [6] In previousw ork from our group, aw ell-defined and highly versatile [Ru(triphos)(tmm)] [triphos:1 ,1,1-tris(diphenylphosphinomethyl)ethane,t mm:t rimethylene methane] catalystw as developed for the hydrogenation of CO 2 to methanola nd the utilizationo fC O 2 and H 2 for the N-methylation of primary ands econdary amines. [7] On the basis of these investigations, the directt riple N-methylation of NH 3 (Scheme 1C)orNH 4 Cl (Scheme 1D)byusing acombination of CO 2 and H 2 was targeted.In the mid-1990s, the group of Baiker worked on this challenging transformation and d...