Translation of "Combustion sèche à co-courant " (French → English) :

Artificial solid fuel derived from hard coal and obtained by dry distillation of the coal in the total or partial absence of air.

Immediate/Short-termLonger term | Reduction in demand (e.g. smaller engines)Advanced high-efficiency ICEsImproved hybrid electric designs with petrol, diesel, biodieselBio-diesel; bio-ethanolCo-processing of biomass with fossil fuelsSynthetic fuels from gas/coal-Fischer-TropschBiofuels from ligno-cellulosic feedstocksElectric vehicles (EVs) with advanced battery electricity storageHydrogen with fuel cellsAir transport: hydrogen/gas turbine | Low/medium temperature solar thermal applications for hot water, heating, cooling, industrial processesCombined Cycle Gas Turbine (CCGT)Nuclear fission (Gen III/III+)Wind energy (including offshore/ ...[+++]deep offshore)System integration (grid issues)Solid biomassFuel cells (SOFC, MCFC)Geothermal energy (including deep geothermal – HDR/HFR)Carbon capture and storage (CCS)Cleaner use of coal (steam/gas turbine, combined cycle) with CCSAdvanced fossil fuel plants (super/ultra-supercritical steam; Integrated Gasification CC (IGCC), with CCSSolar photovoltaic (PV)Solar thermal power plantsOcean energy (wave, sea current)Nuclear fission – Generation IVNuclear fusion |

On the issue of ongoing relief of current expenditure, the UK Government recalls that the Government’s undertaking covers only contracted historic liabilities, decommissioning liabilities and uncontracted liabilities associated with historic AGR spent-fuel, all PWR spent fuel and operational waste and other ancillary liabilities.

—crushed to pieces of approximately 15 mm and degreased with hot water at a temperature of minimum 70 °C for at least 30 minutes, minimum 80 C for at least 15 minutes, or minimum 90 °C for at least 10 minutes, and then separated and subsequently washed and dried for at least 20 minutes in a stream of hot air with an initial temperature of minimum 350 °C, or for 15 minutes in a stream of hot air with an initial temperature of more than 700 °C,

The continuous measurement of the water vapour content of the exhaust gases shall not be necessary, provided that the sampled exhaust gas is dried before the emissions are analysed.

The number and capacity of incinerators employing wet, semi-wet wet and semi-dry flue gas neutralisation technologies will increase at the expense of those employing dry technologies.