ITMI20091198A1 - STATIONARY TERMINATOR THERMO - Google Patents
STATIONARY TERMINATOR THERMO Download PDFInfo
- Publication number
- ITMI20091198A1 ITMI20091198A1 IT001198A ITMI20091198A ITMI20091198A1 IT MI20091198 A1 ITMI20091198 A1 IT MI20091198A1 IT 001198 A IT001198 A IT 001198A IT MI20091198 A ITMI20091198 A IT MI20091198A IT MI20091198 A1 ITMI20091198 A1 IT MI20091198A1
- Authority
- IT
- Italy
- Prior art keywords
- exchangers
- powered
- thermo
- sources
- eps
- Prior art date
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 7
- 238000009833 condensation Methods 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- 238000009413 insulation Methods 0.000 claims description 3
- 230000005855 radiation Effects 0.000 claims description 2
- 239000002699 waste material Substances 0.000 claims description 2
- 238000009825 accumulation Methods 0.000 claims 1
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000004794 expanded polystyrene Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000010612 desalination reaction Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/14—Treatment of water, waste water, or sewage by heating by distillation or evaporation using solar energy
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0011—Heating features
- B01D1/0041—Use of fluids
- B01D1/0047—Use of fluids in a closed circuit
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/043—Details
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/10—Treatment of water, waste water, or sewage by heating by distillation or evaporation by direct contact with a particulate solid or with a fluid, as a heat transfer medium
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
Description
Stato dell'arte State of the art
Ad oggi, diverse soluzioni sono state proposte per la dissalazione di acqua salata, spesso riconducibili a processi osmotici o per evaporazione/condensazione. rapporto costi/benefìci sia di impianto sia di esercizio restano onerosi. L'idea proposta si prefigge di ridurre drasticamente il rapporto costi/benefici nella produzione di acqua dissalata, da avviare a successivi e congrui processi di integrazione To date, various solutions have been proposed for the desalination of salt water, often attributable to osmotic processes or evaporation / condensation. cost / benefit ratio of both plant and operation remain onerous. The proposed idea is aimed at drastically reducing the cost / benefit ratio in the production of desalinated water, to be launched in subsequent and appropriate integration processes
Descrizione Description
Il Termo Dissalatore stanziale (Fig 1) è un dispositivo costituito da più componenti, che sfruttano le potenzialità dei notevoli apporti energetici dati dalle TermoSuperfici (Fig.l) (motore della evaporazione), uniti all'efficacia dei TermoPozzo (Fig. l) (motore della condensazione), il dispositivo fortemente azionato ed alimentato da fonti rinnovabili: 1) si predispone un TermoPozzo (Fig. l) funzionale alla condensazione, con ruolo prevalente di scambio con il sottosuolo, a circa un metro di profondità, sopra si completa con uno strato di coibente naturale 2) si procede a costituire una serra a pentagono retto, stagna e coibentata (in EPS o simili); all'interno, sul piano inferiore sono disposti congrui scambiatori (derivati delle Termosuperfici (Fig. l), lamiere grecate e tubi contenenti un termovettore); all'interno, sulle pareti oblique superiori, sono disposti congrui scambiatori (derivati delle Termosuperfici (Fig.l), lamiere grecate e tubi contenenti un termovettore) completati da grondaie per la raccolta e convogliamento all' esterno delle acque di condense percolate verso il basso; all'esterno, sulle falde superiori, si dispongono le Termosuperfici (Fig. l) (Diodo Eliotermico, ovvero lamiere grecate e tubi contenenti un termovettore coperte da un traslucido alveolare), atte a raccogliere il calore da irraggiamento solare, diretto e diffuso Gli scambiatori esterni (Fig. l) ed interni, sono raccordati da collegamenti idrici incrociati e circolatori. Il dispositivo è completato da un sistema di riempimento, ricambio e mantenimento di congrui livelli di acqua da dissalare (proveniente da mare o acque salmastre o da bonificare) nel vano inferiore delta serra. Dinamica: l'energia derivante dalle falde esterne superiori viene portata con mera circolazione (in circuito chiuso), negli scambiatori (Fig. l) interni inferiori (questo innalzerà notevolmente la temperatura dell'acqua salata contenuta nella vasca) decretando tensioni di evaporazione e saturazione dell'ambiente. Gli scambiatori (Fig. l) superiori interni sono mantenuti a temperature inferiori grazie allo scambio con il pozzo freddo sottostante (Fig l) (mediante mera circolazione). Il vapore condenserà e percolerà fino a punto di raccolta opportuno, e convogliata all'esterno The permanent Thermo Desalinator (Fig 1) is a device consisting of several components, which exploit the potential of the considerable energy inputs given by the TermoSuperfici (Fig.l) (evaporation engine), combined with the effectiveness of the TermoPozzo (Fig. L) ( condensation motor), the device strongly operated and powered by renewable sources: 1) prepares a ThermoPozzo (Fig. a layer of natural insulation 2) proceeds to build a right pentagon greenhouse, watertight and insulated (in EPS or similar); inside, on the lower floor there are suitable exchangers (derivatives of the Thermo-surfaces (Fig. 1), corrugated sheets and pipes containing a heat carrier); inside, on the upper oblique walls, there are suitable exchangers (derivatives of the thermosurfaces (Fig. 1), corrugated sheets and pipes containing a heat carrier) completed by gutters for collecting and conveying the condensate water leaked downwards to the outside ; outside, on the upper slopes, the Thermo-surfaces are arranged (Fig. l) (Heliothermic diode, i.e. corrugated sheets and tubes containing a heat carrier covered by a translucent alveolar), designed to collect the heat from direct and diffused solar radiation The exchangers external (Fig. l) and internal, are connected by crossed water connections and circulators. The device is completed by a system of filling, replacement and maintenance of adequate levels of water to be desalted (coming from the sea or brackish water or to be reclaimed) in the lower compartment of the greenhouse. Dynamics: the energy deriving from the upper external layers is brought with mere circulation (in a closed circuit), to the lower internal exchangers (Fig. L) (this will significantly raise the temperature of the salt water contained in the tank), decreeing evaporation and saturation tensions of the environment. The internal upper exchangers (Fig. 1) are kept at lower temperatures thanks to the exchange with the underlying cold well (Fig. 1) (by mere circulation). The vapor will condense and percolate to an appropriate collection point, and conveyed to the outside
Benefìci ed applicazioni Benefits and applications
Il dispositivo (Fig. l) trova estese applicazioni sia in comparti residenziali che industriali, provvedendo alla preliminare fase di produzione di acqua dissalata, da avviare con i successivi perfezionamenti ai processi residenziali o industriali. Il costo dell'opera è molto contenuto, ha bassi costi di esercizio, essenzialmente dovuti alle circolazioni idrauliche in circuiti chiusi, senza prevalenza. Il processo dimensionato in congrue sezioni e volumi, permetterà processi di circolazione naturale, sia per il circuito di evaporazione che condensazione. Il processo si avvale prevalentemente di fonti rinnovabili ed aleatorie, Aleatorietà facilmente superabile alimentando a basse temperature gli scambiatori interni superiori ed ad alte temperature gli scambiatori interni inferiori, attraverso cascami termici (caldo/freddo) derivanti da processi diversi o appositamente prodotti, regimi termici che saranno forieri di elevate rese The device (Fig. 1) finds extensive applications in both residential and industrial sectors, providing for the preliminary phase of production of desalinated water, to be started with subsequent improvements to residential or industrial processes. The cost of the work is very low, it has low operating costs, essentially due to the hydraulic circulation in closed circuits, without prevalence. The process dimensioned in congruous sections and volumes, will allow natural circulation processes, both for the evaporation and condensation circuit. The process mainly makes use of renewable and random sources, easily overcome randomness by feeding the upper internal exchangers at low temperatures and the lower internal exchangers at high temperatures, through thermal waste (hot / cold) deriving from different processes or specially produced, thermal regimes that will be harbingers of high yields
Descrizione della figura Description of the figure
Fig.l Termodissalatore stanziale Fig.l Stationary heat sink
1) Policarbonato 1) Polycarbonate
2) Tubo per fluido 2) Fluid hose
3) Lamiera recata 3) Sheet metal carried
4) Strato coibentante 4) Insulating layer
5) Circuito esterno 5) External circuit
6) Circuito interno 6) Internal circuit
7) Acqua dolce 7) Fresh water
8) Gronda 8) Eaves
9) Acqua salmastra 9) Brackish water
10) Polistirolo espanso (EPS) 10) Expanded polystyrene (EPS)
11) Calcestruzzo (CLS) 11) Concrete (CLS)
12) Ciotoli 12) Pebbles
13) Ghiaia 13) Gravel
14) Cireolatore 14) Cireolator
15) Sole 15) Sun
Claims (10)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT001198A ITMI20091198A1 (en) | 2009-07-07 | 2009-07-07 | STATIONARY TERMINATOR THERMO |
PCT/IT2010/000302 WO2011004416A1 (en) | 2009-07-07 | 2010-07-06 | Thermal desalination plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT001198A ITMI20091198A1 (en) | 2009-07-07 | 2009-07-07 | STATIONARY TERMINATOR THERMO |
Publications (1)
Publication Number | Publication Date |
---|---|
ITMI20091198A1 true ITMI20091198A1 (en) | 2011-01-08 |
Family
ID=41666778
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
IT001198A ITMI20091198A1 (en) | 2009-07-07 | 2009-07-07 | STATIONARY TERMINATOR THERMO |
Country Status (1)
Country | Link |
---|---|
IT (1) | ITMI20091198A1 (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4235679A (en) * | 1979-01-15 | 1980-11-25 | The United States Of America As Represented By The Secretary Of The Navy | High performance solar still |
US4459177A (en) * | 1981-05-08 | 1984-07-10 | Hare Louis R O | Ground moisture transfer system |
ES2105977A1 (en) * | 1995-09-27 | 1997-10-16 | Perales Corrales Jesus | Improvements to water-desalination plants |
WO1998040313A1 (en) * | 1997-03-11 | 1998-09-17 | Johannes Markopulos | Facility for desalinating or purifying sea water or brackish water by means of solar energy |
WO2003022746A1 (en) * | 2001-09-07 | 2003-03-20 | Roberto Jona | Seawater desalination system |
EP1312404A1 (en) * | 2001-11-15 | 2003-05-21 | Alexander Von Poswik | Process and apparatus to distillate water from seawater, brackish water or other contaminated waters |
FR2880881A1 (en) * | 2005-01-14 | 2006-07-21 | Mansour Sahnoune | Replication device for the separation of salt from seawater, comprises a retention basin is placed on a tank for reserving water and formation of a dew point, and a peripheral water trap |
-
2009
- 2009-07-07 IT IT001198A patent/ITMI20091198A1/en unknown
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4235679A (en) * | 1979-01-15 | 1980-11-25 | The United States Of America As Represented By The Secretary Of The Navy | High performance solar still |
US4459177A (en) * | 1981-05-08 | 1984-07-10 | Hare Louis R O | Ground moisture transfer system |
ES2105977A1 (en) * | 1995-09-27 | 1997-10-16 | Perales Corrales Jesus | Improvements to water-desalination plants |
WO1998040313A1 (en) * | 1997-03-11 | 1998-09-17 | Johannes Markopulos | Facility for desalinating or purifying sea water or brackish water by means of solar energy |
WO2003022746A1 (en) * | 2001-09-07 | 2003-03-20 | Roberto Jona | Seawater desalination system |
EP1312404A1 (en) * | 2001-11-15 | 2003-05-21 | Alexander Von Poswik | Process and apparatus to distillate water from seawater, brackish water or other contaminated waters |
FR2880881A1 (en) * | 2005-01-14 | 2006-07-21 | Mansour Sahnoune | Replication device for the separation of salt from seawater, comprises a retention basin is placed on a tank for reserving water and formation of a dew point, and a peripheral water trap |
Non-Patent Citations (1)
Title |
---|
DATABASE WPI Week 199748, Derwent World Patents Index; AN 1997-515728, XP002569113 * |
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