This　communication　analyzes　the　dual　convection　regime　of　Newtonian　fluid　flow　in　a　Y　shaped　porous　enclosure　with　heat　and　mass　distribution,　using　a　mathematical　model　of　dimensionless　PDEs　and　an　effective　finite　element　method.　The　top　curved　wall　of　the　enclosure　is　assumed　hot　and　side　walls　are　cold　while　the　bottom　wall　is　assumed　adiabatic.　The　problem　is　discretized　using　P　2　and　P　1　finite　element　methods　to　approximate　the　displacement,　pressure,　and　velocity.　The　linearized　system　of　equations　is　solved　using　Newton＇s　iterative　scheme.　The　study　evaluates　the　impact　of　key　parameters　such　as　the　Hartmann　number,　Lewis　number,　Rayleigh　number,　and　buoyancy　ratio　on　the　flow,　heat　transfer　rate,　and　mass　transfer　rate.　Results　indicate　that　an　increase　in　the　Hartmann　number,　Rayleigh　numbers　and　buoyancy　ratio　amplifies　both　mass　and　heat　transfer　rates.　The　buoyancy　ratio　has　a　noteworthy　impact　on　the　flow　and　transfer　rates,　with　a　greater　influence　seen　for.　The　study　presents　graphical　representations　of　flow　and　temperature　fields,　as　well　as　Nusselt　and　Sherwood　numbers　provide　a　comprehensive　visualization　of　the　results.　Heat　and　mass　transfer　rate　is　minimum　for　concentration　dominated　counter　flow　(　N　=　-　2　)　and　maximum　for　concentration　dominated　assisting　flow　N　=　2　.