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Produzione pro cap RU kg/ab*anno 601 Produzione pro cap RD kg/ab*anno 206 Produzione pro cap Rind... more Produzione pro cap RU kg/ab*anno 601 Produzione pro cap RD kg/ab*anno 206 Produzione pro cap Rind kg/ab*anno 395 % RD 34,3 CRT Kg € cent/kg 6,29 CTSKg € cent/kg 6,50 CacKg € cent/kg 0,92 CindKg € cent/kg 13,71 CrdKg € cent/kg 6,27 CtrKg € cent/kg 2,17 CgdKg € cent/kg 8,44 CCKg € cent/kg 4,56 CKKg € cent/kg 1,69 CslKg € cent/kg 4,35 CoperKg € cent/kg 16,21 CtotKg € cent/kg 22,50 Legenda: CRT = Costi di raccolta e trasporto; CTS = Costi di trasporto e smaltimento; Cac = Altri costi; Cind = Costi di gestione indifferenziato; Crd = Costi raccolta differenziata; Ctr = Costi trattamento e riciclo; Cgd = Costi di gestione differenziata; CC = Costi comuni; CK = Costi d'uso del capitale; Csl = Costi di spazzamento e lavaggio;
In the context of the development of technologies for renewable energy form, the bio-masses gasif... more In the context of the development of technologies for renewable energy form, the bio-masses gasification catalytic finalised to the bio-gas production assuming an interesting role, moreover for the interest about the processes which provide them originating from fluidised bed reactors. The gases produced are composed by hydrogen, methane and other fuels and they have a few environmental impact. The opportunity to use the biogas in combustion chambers in place of conventional one is actually rising. Since its thermal exploitation in terms of conventional combustion chambers is not an easy application, in this paper we have deepen about it. This work represents a typical CFD application related to an combustion process with hydrogen rich fuel in standard operative conditions on a Sandialike burner. The burner adopted develops a diffusive flame and it guarantees a greater stability of combustion in the case of using CH 4. The influence of burner geometry and the gas velocity have been studied in order to characterise the better conditions for an efficient combustion with low pollutant realised in steady state.
Produzione pro cap RU kg/ab*anno 601 Produzione pro cap RD kg/ab*anno 206 Produzione pro cap Rind... more Produzione pro cap RU kg/ab*anno 601 Produzione pro cap RD kg/ab*anno 206 Produzione pro cap Rind kg/ab*anno 395 % RD 34,3 CRT Kg € cent/kg 6,29 CTSKg € cent/kg 6,50 CacKg € cent/kg 0,92 CindKg € cent/kg 13,71 CrdKg € cent/kg 6,27 CtrKg € cent/kg 2,17 CgdKg € cent/kg 8,44 CCKg € cent/kg 4,56 CKKg € cent/kg 1,69 CslKg € cent/kg 4,35 CoperKg € cent/kg 16,21 CtotKg € cent/kg 22,50 Legenda: CRT = Costi di raccolta e trasporto; CTS = Costi di trasporto e smaltimento; Cac = Altri costi; Cind = Costi di gestione indifferenziato; Crd = Costi raccolta differenziata; Ctr = Costi trattamento e riciclo; Cgd = Costi di gestione differenziata; CC = Costi comuni; CK = Costi d'uso del capitale; Csl = Costi di spazzamento e lavaggio;
Produzione pro cap RU kg/ab*anno 601 Produzione pro cap RD kg/ab*anno 206 Produzione pro cap Rind... more Produzione pro cap RU kg/ab*anno 601 Produzione pro cap RD kg/ab*anno 206 Produzione pro cap Rind kg/ab*anno 395 % RD 34,3 CRT Kg € cent/kg 6,29 CTSKg € cent/kg 6,50 CacKg € cent/kg 0,92 CindKg € cent/kg 13,71 CrdKg € cent/kg 6,27 CtrKg € cent/kg 2,17 CgdKg € cent/kg 8,44 CCKg € cent/kg 4,56 CKKg € cent/kg 1,69 CslKg € cent/kg 4,35 CoperKg € cent/kg 16,21 CtotKg € cent/kg 22,50 Legenda: CRT = Costi di raccolta e trasporto; CTS = Costi di trasporto e smaltimento; Cac = Altri costi; Cind = Costi di gestione indifferenziato; Crd = Costi raccolta differenziata; Ctr = Costi trattamento e riciclo; Cgd = Costi di gestione differenziata; CC = Costi comuni; CK = Costi d'uso del capitale; Csl = Costi di spazzamento e lavaggio;
In the context of the development of technologies for renewable energy form, the bio-masses gasif... more In the context of the development of technologies for renewable energy form, the bio-masses gasification catalytic finalised to the bio-gas production assuming an interesting role, moreover for the interest about the processes which provide them originating from fluidised bed reactors. The gases produced are composed by hydrogen, methane and other fuels and they have a few environmental impact. The opportunity to use the biogas in combustion chambers in place of conventional one is actually rising. Since its thermal exploitation in terms of conventional combustion chambers is not an easy application, in this paper we have deepen about it. This work represents a typical CFD application related to an combustion process with hydrogen rich fuel in standard operative conditions on a Sandialike burner. The burner adopted develops a diffusive flame and it guarantees a greater stability of combustion in the case of using CH 4. The influence of burner geometry and the gas velocity have been studied in order to characterise the better conditions for an efficient combustion with low pollutant realised in steady state.
Produzione pro cap RU kg/ab*anno 601 Produzione pro cap RD kg/ab*anno 206 Produzione pro cap Rind... more Produzione pro cap RU kg/ab*anno 601 Produzione pro cap RD kg/ab*anno 206 Produzione pro cap Rind kg/ab*anno 395 % RD 34,3 CRT Kg € cent/kg 6,29 CTSKg € cent/kg 6,50 CacKg € cent/kg 0,92 CindKg € cent/kg 13,71 CrdKg € cent/kg 6,27 CtrKg € cent/kg 2,17 CgdKg € cent/kg 8,44 CCKg € cent/kg 4,56 CKKg € cent/kg 1,69 CslKg € cent/kg 4,35 CoperKg € cent/kg 16,21 CtotKg € cent/kg 22,50 Legenda: CRT = Costi di raccolta e trasporto; CTS = Costi di trasporto e smaltimento; Cac = Altri costi; Cind = Costi di gestione indifferenziato; Crd = Costi raccolta differenziata; Ctr = Costi trattamento e riciclo; Cgd = Costi di gestione differenziata; CC = Costi comuni; CK = Costi d'uso del capitale; Csl = Costi di spazzamento e lavaggio;