Measurements of heat transport, as expressed by the Nusselt number N u, are reported for turbulent Rayleigh-Bénard convection of water containing up to 120 ppm by weight of poly-[ethylene oxide] with a molecular weight of 4 × 10 6 g/mole. Over the Rayleigh number range 5 × 10 9 < ∼ Ra < ∼ 7 × 10 10 N u is smaller than it is for pure water by up to 10%.PACS numbers: 47.27.-i, 47.27.te It has been known for about six decades that minute quantities of a polymer dissolved in a fluid can reduce significantly the drag experienced by turbulent flows near solid surfaces (see, for instance, [1,2]). During this time literally thousands of papers have been written about this technologically important problem. However, we are not aware of any experimental study, and know of only a single very recent theoretical investigation [3], of the influence of polymer additives on turbulent convection in a fluid confined between horizontal parallel plates and heated from below (known as Rayleigh-Bénard convection or RBC). In this letter we present data showing that the addition of about 100 parts per million (ppm) by weight of poly-[ethylene oxide] (PEO) can reduce the heat transport in turbulent RBC by 10% or more.The reason why the influence of dilute polymers on RBC has not been studied before is easy to see. In typical flow geometries, such as pipe flow, it was found [4] that significant drag reduction occurs when the polymer relaxation times are comparable to or longer than the time scales of some of the fluctuations in the turbulent flow. Turbulent RBC (see, for instance, [5,6]) generally involves only modest Reynolds numbers. Thus, even though there is a continuum of time scales and eddy sizes, the natural time scales of the most abundant eddies or fluctuations are typically of order a second or longer, [7,8,9] and fluctuation times comparable to typical high molecular weight polymer relaxation times (see, for instance, [10]) are expected to be virtually absent. In addition, the viscous boundary layers (BLs) above the bottom and below the top plate, although fluctuating, are laminar because the shear Reynolds number, defined in terms of the BL thickness, usually is only of order 10 2 or less. Thus there was no obvious reason to study the influence of minute quantities of polymers in this system.In view of the above discussion of the time scales of the problem it seems likely that the mechanism for the experimentally observed reduction of the heat transport in RBC is quite different from the usual drag-reduction mechanism. Since the heat transport at large Rayleigh numbers is dominated by the emission of plumes from the thermal boundary layers, the experiments suggest that the emission is reduced by the polymer additive. In view of the fact that the thermal BLs are, roughly speaking, marginally stable, and that plume emission may be regarded as a manifestation of this near-instability, it is not unreasonable that this process should be exceptionally sensitive to such factors as polymer concentration; but the precise mechanism...