ITCE20100012A1 - ALKALINIZERS MARINE DEPURATORS WITH CO2 RECOVERY AND CONSUMPTION AND SOLAR ELECTRIC ENERGY PRODUCTION - Google Patents
ALKALINIZERS MARINE DEPURATORS WITH CO2 RECOVERY AND CONSUMPTION AND SOLAR ELECTRIC ENERGY PRODUCTION Download PDFInfo
- Publication number
- ITCE20100012A1 ITCE20100012A1 IT000012A ITCE20100012A ITCE20100012A1 IT CE20100012 A1 ITCE20100012 A1 IT CE20100012A1 IT 000012 A IT000012 A IT 000012A IT CE20100012 A ITCE20100012 A IT CE20100012A IT CE20100012 A1 ITCE20100012 A1 IT CE20100012A1
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- Prior art keywords
- plants
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- Prior art date
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- 238000011084 recovery Methods 0.000 title description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 6
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 6
- 239000004571 lime Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000010672 photosynthesis Methods 0.000 claims description 4
- 230000029553 photosynthesis Effects 0.000 claims description 4
- 239000003643 water by type Substances 0.000 claims description 4
- 239000003517 fume Substances 0.000 claims description 3
- 230000003647 oxidation Effects 0.000 claims description 3
- 238000007254 oxidation reaction Methods 0.000 claims description 3
- 230000003113 alkalizing effect Effects 0.000 claims description 2
- 241000251468 Actinopterygii Species 0.000 claims 1
- 238000010276 construction Methods 0.000 claims 1
- 239000000498 cooling water Substances 0.000 claims 1
- 238000001514 detection method Methods 0.000 claims 1
- 230000021962 pH elevation Effects 0.000 claims 1
- 230000020477 pH reduction Effects 0.000 claims 1
- 230000001105 regulatory effect Effects 0.000 claims 1
- 239000013535 sea water Substances 0.000 claims 1
- 238000001816 cooling Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- GBAOBIBJACZTNA-UHFFFAOYSA-L calcium sulfite Chemical compound [Ca+2].[O-]S([O-])=O GBAOBIBJACZTNA-UHFFFAOYSA-L 0.000 description 2
- 235000010261 calcium sulphite Nutrition 0.000 description 2
- 239000004295 calcium sulphite Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 1
- 241000605159 Nitrobacter Species 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 235000011132 calcium sulphate Nutrition 0.000 description 1
- 239000001175 calcium sulphate Substances 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229930002875 chlorophyll Natural products 0.000 description 1
- 235000019804 chlorophyll Nutrition 0.000 description 1
- ATNHDLDRLWWWCB-AENOIHSZSA-M chlorophyll a Chemical compound C1([C@@H](C(=O)OC)C(=O)C2=C3C)=C2N2C3=CC(C(CC)=C3C)=[N+]4C3=CC3=C(C=C)C(C)=C5N3[Mg-2]42[N+]2=C1[C@@H](CCC(=O)OC\C=C(/C)CCC[C@H](C)CCC[C@H](C)CCCC(C)C)[C@H](C)C2=C5 ATNHDLDRLWWWCB-AENOIHSZSA-M 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000002341 toxic gas Substances 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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/32—Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/02—Photobioreactors
-
- 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
- C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
Description
DESCRIZIONE DESCRIPTION
Chi scrive, con il deposito n. Ce2010A0()G008 del 12/10/2010, sopra citato, ha già descritto il funzionamento degli impianti di depurazione e alcalinizzazione. ma non aveva pensato alla possibilità di realizzare questi impianti direttamente lungo le coste, dove maggiormente, c’è bisogno di questi impianti. Infatti, il PH nelle zone costiere è molto più basso che al centro degli oceani. Questo è dovuto, sia all’inquinamento, sia all’immissione delle acque fluviali, che pure se fossero non inquinate, diluendo la soluzione salina, abbassano il PH e liberano C02nell’atmosfera. Con gli alcalinizza tori depuratori marini, abbiamo la possibilità di intervenire sul risanamento dell’acidità oceanica con maggiore incisività di qualsiasi altro sistema, non dovendoci basare solo sulle depurazioni e sulla quantità di carbonati che potrebbero trasportare i fiumi come ipotizzato nel precedente deposito. Infatti, possiamo aumentare l’alcalinità delle stesse acque marine (V. dis.n. 9 e 10). Se realizziamo gli impianti più vicini alle grandi centrali termiche, termovalorizzatori, potremmo utilizzare l’acqua anche per il raffreddamento e la depurazione dei fumi, oltre che per il raffeddamento delle turbine. Trascurando l’aspetto del raffreddamento, risolvibile dai progettisti delle centrali termiche, poniamo l’attenzione sui fumi che. una volta raffreddati e depolverati. potranno essere convogliati ai bacini di Ossi-nitri ficazione coperti, dove, ripresi dalle elettrosoffianti, saranno immessi nell’acqua in sostituzione dell’aria di ossidazione. I componenti tossici o inquinanti principali contenuti sono: C02. S02. NO, No2, NOj, CO, idrocarburi incombusti (HC). ecc, sono tutti compatibili per essere abbattuti con il processo di ossi-nitrifìcazione, e fotosintesi già previsto, compresi gli ossidi di zolfo: Who writes, with the deposit n. Ce2010A0 () G008 of 12/10/2010, cited above, has already described the operation of the purification and alkalization plants. but he had not thought about the possibility of building these plants directly along the coasts, where there is a greater need for these plants. In fact, the pH in coastal areas is much lower than in the center of the oceans. This is due to both pollution and the introduction of river waters, even if they were not polluted, by diluting the saline solution, they lower the pH and release C02 into the atmosphere. With marine purification alkalizers, we have the possibility to intervene on the recovery of oceanic acidity with greater incisiveness than any other system, not having to rely only on purification and on the amount of carbonates that could transport rivers as hypothesized in the previous deposit. In fact, we can increase the alkalinity of the same sea waters (See drawing n. 9 and 10). If we build the plants closest to the large thermal power plants, waste-to-energy plants, we could also use the water for cooling and purifying the fumes, as well as for cooling the turbines. Neglecting the cooling aspect, which can be solved by the designers of the thermal power plants, we pay attention to the fumes that. once cooled and dusted. they can be conveyed to the covered oxygenation basins, where, taken up by the electric blowers, they will be introduced into the water to replace the oxidation air. The main toxic or polluting components contained are: C02. S02. NO, No2, NOj, CO, unburnt hydrocarbons (HC). etc., they are all compatible to be eliminated with the oxidation-nitrifying process, and photosynthesis already foreseen, including sulfur oxides:
S02+ H20 -→ Ii2S03(acido solforoso); CaC03+ H2S03→ CaSOj C0rH20 H2S03 Ca(OH)2 - -> CaS03 (solfito di calcio) 2H20. In presenza di ossigeno ed acqua nei gas. il solfito di calcio reagisce in parte con essi producendo solfato di calcio idrato (cioè gesso): CaS03+ (1/2)02 2H20 → CaS04-2H20 ; CaS03+ (l/2)3⁄40 → CaS03.(1/2)H20 S02 + H20 - → Ii2S03 (sulphurous acid); CaC03 + H2S03 → CaSOj C0rH20 H2S03 Ca (OH) 2 - -> CaS03 (calcium sulphite) 2H20. In the presence of oxygen and water in gases. calcium sulphite partially reacts with them producing hydrated calcium sulphate (ie gypsum): CaS03 + (1/2) 02 2H20 → CaS04-2H20; CaS03 + (l / 2) 3⁄40 → CaS03. (1/2) H20
Complessivamente, l’insieme delle reazioni di desolforazione può venire descritta come segue: CaC03+ S02+ (l/2)3⁄40 → CaS03-2H20 C02Overall, the set of desulfurization reactions can be described as follows: CaC03 + S02 + (l / 2) 3⁄40 → CaS03-2H20 C02
La stessa cosa possiamo dire per gli impianti che producono calce riscaldando le rocce calcaree a una temperatura di circa 900 °C. Se si pensa al grande fabbisogno di calce di cui abbiamo bisogno per ridurre le emissioni di C02e sanare gii oceani, non possiamo permetterci di disperdere nel l’ambiente la grande quantità di C02necessaria per produrre la calce: 1 kg di CaO richiede 1,4 - 2,2 kg di roccia, comporta l’emissione di 0, 79 kg di C02, a cui vanno aggiunte le emissioni del combustibile per riscaldare le pietre. Gli impianti di produzione della calce devono essere spostati vicino ai depuratori alcalinizzatori, marini e fluviali che utilizzano tutti i sistemi ecocompatibili per neutralizzare il C02e gli altri gas tossici,senza immetterlo ne!Patmosfera. Con questo sistema depositeremo nei fanghi il particolato, le polveri, i metalli pesanti e accelerando i processi di ossidazione, nitrificazione con consumo di C02ad opera di batteri “nitrobacter” e la fotosintesi clorofilliana. Il C02non assorbito dal processo di ossi nitrificazione e fotosintesi stratificherà sulla superficie dell’ acqua, essendo 1,5 volte più pesante dell’aria, mentre questa tenderà a salire verso l’atmosfera. Pertanto, al centro di ogni bacino verrà posizionato un camino con una serranda di regolazione con il grado di apertura regolabile in funzione della pressione differenziale tra l'interno e l’esterno della serra, per consentire l’evacuazione dell’aria pulita, eventualmente nello stesso camino potrà essere predisposto un ulteriore sistema di precipitazione a umido del gas che tenderà a sfuggire al trattamento. Il C02stratificato sulla superficie dell’acqua, raggiunta una determinata concentrazione, rilevata da sonde, sarà aspirato e inviato tramite altre soffianti al trattamento di carbonatazione negli appositi bacini sottostanti ai sedimentatori e al sistema di disidratazione e stabilizzazione dei fanghi The same thing can be said for plants that produce lime by heating limestone rocks to a temperature of about 900 ° C. If you think about the great need for lime that we need to reduce C02 emissions and heal the oceans, we cannot afford to disperse the large amount of C02 needed to produce lime in the environment: 1 kg of CaO requires 1.4 - 2.2 kg of rock, involves the emission of 0, 79 kg of C02, to which must be added the emissions of the fuel to heat the stones. Lime production plants must be moved near alkalizing, marine and river purifiers that use all environmentally friendly systems to neutralize C02 and other toxic gases, without introducing it into the atmosphere. With this system we will deposit particulate matter, dust, heavy metals in the sludge and accelerate the processes of oxidation, nitrification with the consumption of C02 by “nitrobacter” bacteria and chlorophyll photosynthesis. The C02 not absorbed by the oxy-nitrification and photosynthesis process will stratify on the surface of the water, being 1.5 times heavier than air, while this will tend to rise towards the atmosphere. Therefore, in the center of each basin a chimney will be positioned with a regulation damper with the degree of opening adjustable according to the differential pressure between the inside and the outside of the greenhouse, to allow the evacuation of clean air, possibly in the the same chimney may be equipped with an additional system for the wet precipitation of the gas which will tend to escape the treatment. The C02 stratified on the surface of the water, once it has reached a certain concentration, detected by probes, will be sucked and sent through other blowers to the carbonation treatment in the special basins below the sedimenters and the sludge dehydration and stabilization system
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT000012A ITCE20100012A1 (en) | 2010-10-07 | 2010-10-07 | ALKALINIZERS MARINE DEPURATORS WITH CO2 RECOVERY AND CONSUMPTION AND SOLAR ELECTRIC ENERGY PRODUCTION |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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IT000012A ITCE20100012A1 (en) | 2010-10-07 | 2010-10-07 | ALKALINIZERS MARINE DEPURATORS WITH CO2 RECOVERY AND CONSUMPTION AND SOLAR ELECTRIC ENERGY PRODUCTION |
Publications (1)
Publication Number | Publication Date |
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ITCE20100012A1 true ITCE20100012A1 (en) | 2012-04-08 |
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Family Applications (1)
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IT000012A ITCE20100012A1 (en) | 2010-10-07 | 2010-10-07 | ALKALINIZERS MARINE DEPURATORS WITH CO2 RECOVERY AND CONSUMPTION AND SOLAR ELECTRIC ENERGY PRODUCTION |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014076725A2 (en) | 2012-11-19 | 2014-05-22 | Luigi Antonio Pezone | Linear synergistic system of digestion, dehydration and composting (ldcc) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0716596A (en) * | 1993-06-18 | 1995-01-20 | Toshiro Sekine | Water clarification method of closed water such as lake, marsh, pond, etc. |
JP2008023508A (en) * | 2006-07-19 | 2008-02-07 | Able Corp | Three-dimensional bed for plant and water purification apparatus using it |
US20080178739A1 (en) * | 2006-07-10 | 2008-07-31 | Greenfuel Technologies Corp. | Photobioreactor systems and methods for treating CO2-enriched gas and producing biomass |
CH700388A2 (en) * | 2009-02-01 | 2010-08-13 | Algues Energy Systems Ag | Digester-photobioreactor for culturing photosynthetic microorganisms e.g. microalgae and producing biogas, comprises first enclosure with microorganisms and growth medium, and second enclosure with microorganisms and digestive medium |
-
2010
- 2010-10-07 IT IT000012A patent/ITCE20100012A1/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0716596A (en) * | 1993-06-18 | 1995-01-20 | Toshiro Sekine | Water clarification method of closed water such as lake, marsh, pond, etc. |
US20080178739A1 (en) * | 2006-07-10 | 2008-07-31 | Greenfuel Technologies Corp. | Photobioreactor systems and methods for treating CO2-enriched gas and producing biomass |
JP2008023508A (en) * | 2006-07-19 | 2008-02-07 | Able Corp | Three-dimensional bed for plant and water purification apparatus using it |
CH700388A2 (en) * | 2009-02-01 | 2010-08-13 | Algues Energy Systems Ag | Digester-photobioreactor for culturing photosynthetic microorganisms e.g. microalgae and producing biogas, comprises first enclosure with microorganisms and growth medium, and second enclosure with microorganisms and digestive medium |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014076725A2 (en) | 2012-11-19 | 2014-05-22 | Luigi Antonio Pezone | Linear synergistic system of digestion, dehydration and composting (ldcc) |
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