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Out of the box! Articole recente Zeolit alkali su – pompă de căldură Cred ca e bine sa stie romanii, ca sa nu ridice din sprancene cand vad actiunile ONG si sa le sustina si ei cu picul lor de credinta. O aplicatie AUTO cu potential de dezvoltare Bateriile care se incarca cu viteza luminii Fac pariu ca nu stiati cum se realizeaza obiectele imposibile Inlocuieste bateria masinii cu capacitoare Simplu: minigenerator automentinut Dinamica Timpului Alege-ți Medicul
Cele mai citite articole 2012 Pe Taramul Celalalt (Nirvana) Apa vie – miracolul apei de piramida, apa energizata Ar trebui sa stii Capitolul Stiintific Ce nu vor ei sa stii Cheia Universului alkali su – Numarul de aur Energie gratuita nelimitata Extraterestrii-Ipoteze si Certitudini Istoria Recenta – Dacii Science or not.. What`s in it for me? Uncategorized Vechi civilisatii & relicve Vindecare si Medicina Facebook Portreta Urmărește pe Twitter Sa ne amintim alkali su sa nu uitam... fb.me/2AveTh4q3 5 days ago doctorulpilula.wordpress.com/2014/05/05/hum fb.me/6qQZ8mjvZ 5 days ago doctorulpilula.wordpress.com/2014/05/05/hum fb.me/14ftrQui0 5 days ago alkali su Human being vs Human doing wp.me/p8F7Z-fr 5 days ago Calculator de pret consultatii medicale la domiciliu fb.me/148lWzPfB 6 days ago Urmăreşte pe Twitter My Tweets Blog Stats 306,920 hits Community
In l imba romana documentul original , PDF imagini, nu poate fi separat textul dar merita citit. In limba engleza, fara scheme si diagram: (WO/2006/028400) PROCESS AND INSTALLATION FOR OBTAINING THE DEUTERIUM DEPLETED alkali su WATER
TECHNICAL FIELD OF THE DESCRIPTION The invention refers to a process and an installation for the obtaining the deuterium depleted water preferably for food use. BACKGROUND OF THE INVENTION Continuous processes are known for the obtaining the deuterium depleted alkali su water with a concentration of 2 to 80 ppm D/(D+H), which comprise the isotopic distillation of natural water with a concentration of 145-150 ppm D/(D+H) or of the residue from the manufacture of heavy water with a concentration of 120 ppm D/(D+H) under a 100 mm Hg vacuum, water which is passed through a pelicular alkali su boiler alkali su in order to achieve total evaporation of a controlled and regulated constant flow of water, which determines also the continuous feed of water, the vapor flow having an ascendent flow in a 15 m high and 0.1 m diameter distillation column, provided with packing, after which the extracted vapor flow is converted in liquid phase, part of it being recycled as a reflux at the top zone of the column alkali su at a temperature alkali su as close to the actual temperature of the zone as possible, and the other part is collected at a constant alkali su extraction flow separately from the collection of a liquid phase which comes from the bottom of the column, in both cases the collection being made under a 100 mm Hg vacuum. The disadvantages of these processes consist in the pseudo stationary regimen of these ones, which occur with perturbations of the isotopic separation considering there is only one processing cycle, for the feed deionized water is necessary, and the feed water consumption is rather large because it must provide, by total evaporation, the vapor flow necessary for the isotopic transfer with the liquid flow. Installations alkali su are known for the manufacture alkali su of deuterium depleted water in which the processes presented above are applied which comprise alkali su a thermally alkali su insulated distillation column, in which there is an ordered packing disposed above a liquid collector, at the bottom of the column being connected a peiicular boiler heated with steam, linked to a constant level feeding tank, through a pipe fitted with a flow meter, a regulating tap and a heat exchanger respectively the liquid collecting tank, being connected through another alkali su pipe provided with a tap, the heat exchanger alkali su and another flow meter, to a collecting tank, the column being connected at its upper side to a vacuum pump, through another pipe fitted with two serial condensers and a tap respectively, these condensers being connected through another pipe fitted with a flow meter and a heat exchanger, alkali su heated with steam, with the upper part of the column, this last pipe being connected to another pipe fitted with a tap and a flow meter, which communicates to another collecting tank, which in turn, together with the other collecting tank are connected to the vacuum pump. The disadvantages of these installations are that they have a relatively low capacity and the manufacturing scale-up determines alkali su an amplification of the perturbations, with unfavorable effects on the production capacity or on the quality alkali su of the product. The deuterium depleted water obtained alkali su by applying alkali su the process in the installation described in patent RO 112422B1 has a deuterium concentration of 2 –
Out of the box! Articole recente Zeolit alkali su – pompă de căldură Cred ca e bine sa stie romanii, ca sa nu ridice din sprancene cand vad actiunile ONG si sa le sustina si ei cu picul lor de credinta. O aplicatie AUTO cu potential de dezvoltare Bateriile care se incarca cu viteza luminii Fac pariu ca nu stiati cum se realizeaza obiectele imposibile Inlocuieste bateria masinii cu capacitoare Simplu: minigenerator automentinut Dinamica Timpului Alege-ți Medicul
Cele mai citite articole 2012 Pe Taramul Celalalt (Nirvana) Apa vie – miracolul apei de piramida, apa energizata Ar trebui sa stii Capitolul Stiintific Ce nu vor ei sa stii Cheia Universului alkali su – Numarul de aur Energie gratuita nelimitata Extraterestrii-Ipoteze si Certitudini Istoria Recenta – Dacii Science or not.. What`s in it for me? Uncategorized Vechi civilisatii & relicve Vindecare si Medicina Facebook Portreta Urmărește pe Twitter Sa ne amintim alkali su sa nu uitam... fb.me/2AveTh4q3 5 days ago doctorulpilula.wordpress.com/2014/05/05/hum fb.me/6qQZ8mjvZ 5 days ago doctorulpilula.wordpress.com/2014/05/05/hum fb.me/14ftrQui0 5 days ago alkali su Human being vs Human doing wp.me/p8F7Z-fr 5 days ago Calculator de pret consultatii medicale la domiciliu fb.me/148lWzPfB 6 days ago Urmăreşte pe Twitter My Tweets Blog Stats 306,920 hits Community
In l imba romana documentul original , PDF imagini, nu poate fi separat textul dar merita citit. In limba engleza, fara scheme si diagram: (WO/2006/028400) PROCESS AND INSTALLATION FOR OBTAINING THE DEUTERIUM DEPLETED alkali su WATER
TECHNICAL FIELD OF THE DESCRIPTION The invention refers to a process and an installation for the obtaining the deuterium depleted water preferably for food use. BACKGROUND OF THE INVENTION Continuous processes are known for the obtaining the deuterium depleted alkali su water with a concentration of 2 to 80 ppm D/(D+H), which comprise the isotopic distillation of natural water with a concentration of 145-150 ppm D/(D+H) or of the residue from the manufacture of heavy water with a concentration of 120 ppm D/(D+H) under a 100 mm Hg vacuum, water which is passed through a pelicular alkali su boiler alkali su in order to achieve total evaporation of a controlled and regulated constant flow of water, which determines also the continuous feed of water, the vapor flow having an ascendent flow in a 15 m high and 0.1 m diameter distillation column, provided with packing, after which the extracted vapor flow is converted in liquid phase, part of it being recycled as a reflux at the top zone of the column alkali su at a temperature alkali su as close to the actual temperature of the zone as possible, and the other part is collected at a constant alkali su extraction flow separately from the collection of a liquid phase which comes from the bottom of the column, in both cases the collection being made under a 100 mm Hg vacuum. The disadvantages of these processes consist in the pseudo stationary regimen of these ones, which occur with perturbations of the isotopic separation considering there is only one processing cycle, for the feed deionized water is necessary, and the feed water consumption is rather large because it must provide, by total evaporation, the vapor flow necessary for the isotopic transfer with the liquid flow. Installations alkali su are known for the manufacture alkali su of deuterium depleted water in which the processes presented above are applied which comprise alkali su a thermally alkali su insulated distillation column, in which there is an ordered packing disposed above a liquid collector, at the bottom of the column being connected a peiicular boiler heated with steam, linked to a constant level feeding tank, through a pipe fitted with a flow meter, a regulating tap and a heat exchanger respectively the liquid collecting tank, being connected through another alkali su pipe provided with a tap, the heat exchanger alkali su and another flow meter, to a collecting tank, the column being connected at its upper side to a vacuum pump, through another pipe fitted with two serial condensers and a tap respectively, these condensers being connected through another pipe fitted with a flow meter and a heat exchanger, alkali su heated with steam, with the upper part of the column, this last pipe being connected to another pipe fitted with a tap and a flow meter, which communicates to another collecting tank, which in turn, together with the other collecting tank are connected to the vacuum pump. The disadvantages of these installations are that they have a relatively low capacity and the manufacturing scale-up determines alkali su an amplification of the perturbations, with unfavorable effects on the production capacity or on the quality alkali su of the product. The deuterium depleted water obtained alkali su by applying alkali su the process in the installation described in patent RO 112422B1 has a deuterium concentration of 2 –
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