WO2014076726A4 - Global synergy plants for depuration, biomass production and thermoelectric cogeneration (gspdptc) - Google Patents

Global synergy plants for depuration, biomass production and thermoelectric cogeneration (gspdptc) Download PDF

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WO2014076726A4
WO2014076726A4 PCT/IT2013/000316 IT2013000316W WO2014076726A4 WO 2014076726 A4 WO2014076726 A4 WO 2014076726A4 IT 2013000316 W IT2013000316 W IT 2013000316W WO 2014076726 A4 WO2014076726 A4 WO 2014076726A4
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water
gspdptc
synergy
system based
vertical
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WO2014076726A1 (en
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Luigi Antonio Pezone
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Luigi Antonio Pezone
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1425—Regeneration of liquid absorbents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/62—Carbon oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/84—Biological processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • 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
    • C12M43/00—Combinations of bioreactors or fermenters with other apparatus
    • C12M43/08—Bioreactors or fermenters combined with devices or plants for production of electricity
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/006—Layout of treatment plant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
    • F23J15/025—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using filters
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/40—Alkaline earth metal or magnesium compounds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/30—Sulfur compounds
    • B01D2257/304—Hydrogen sulfide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/50—Carbon oxides
    • B01D2257/504—Carbon dioxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/32—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
    • B01D53/323—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00 by electrostatic effects or by high-voltage electric fields
    • 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
    • C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/02—Biological treatment
    • C02F11/04—Anaerobic treatment; Production of methane by such processes
    • 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
    • C02F3/28—Anaerobic digestion processes
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2215/00—Preventing emissions
    • F23J2215/50—Carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2217/00—Intercepting solids
    • F23J2217/10—Intercepting solids by filters
    • F23J2217/102—Intercepting solids by filters electrostatic
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2219/00—Treatment devices
    • F23J2219/60—Sorption with dry devices, e.g. beds
    • 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
    • Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/20—Capture or disposal of greenhouse gases of methane
    • 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
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
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    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/14—Combined heat and power generation [CHP]
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  • Engineering & Computer Science (AREA)
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  • Health & Medical Sciences (AREA)
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  • Environmental & Geological Engineering (AREA)
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  • Genetics & Genomics (AREA)
  • Treating Waste Gases (AREA)
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  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

Today's environmental problems are multidisciplinary and the system of the present application has been designed with these principles: to treat all problems simultaneously, while still allowing energy production at levels required for modern society. Now thermal fossil plants are a major source of pollution of the atmosphere due to the toxic substances emitted and also a source of significant economic waste due to the enormous amounts of waste heat which is not recovered. The industrial and urban sewage treatment and air purification is inadequate. The system of the present application, retrieves these resources, increases yields, makes clean energy, water purification and desalination, or alkalizes all the waters that run through the system to deacidify lakes and oceans. The system is based on the enlargement of energetic plants with new sections to take advantage of the heat and the C02 they produce. This integrated system includes a new chimney system for filtrating and cooling the fumes, the heat of which is used to heat large anaerobic digesters producing biogas and compost for agriculture of high quality; vertically superposed chemisorption and photosynthetic units ("VSB") that consume C02 and waste heat energy and produce biomass sludge, which will be transferred to the digesters. ln "VSB", C02 will also be used for the cold carbonation of limestone stored on multiple floors suspended in special trolley baskets. The continuous recycling of water between a limestone section and a purifying section allows for greater absorption of C02. The purified water falls down on to the limestone in rains to facilitate the reaction which transforms C02 into aqueous carbonates which will be transported to lakes or oceans for deacidification. Alternatively, the entire system can be used to desalinate ocean water. Baskets filled with ion exchange resins are dragged through the water basins underlying the carbonates produced by the corrosion of the rocks to perform another level of water purification.

Claims

AMENDED CLAIMS
received by the International Bureau on 27 June 2014 (27.06.14)
I) Global synergy plants for depuration, biomass production and thermoelectric cogeneration (GSPDPTC) system, based on the synergy, characterised by the fact that it expands the functions of thermoelectric power plants fueled with fossil fuel (TEPfos) with new sections: capture cooling purification chimneys (CCPC) plus vertical synergic building (VSB) plus manufactured digesters dehydrators composters linear (LDDC); In these expanded plant functions where the fumes produced by TEPfos are sent to chimneys (CCPC) that do not emit them into the atmosphere but filter them with electrostatic filter (esf), mix them with air in flue gas expansion chamber (fgec) and cool them recovering part of the heat, by heating water in a flue gas water heat exchanger (fgwe); subsequently, the fumes by electric fans for fumes (eff), are conveyed in vertical sections covered mechanized limestone greenhouse (vcmlg) of VSB, where they are stored calcareous wheeled hanging baskets (cwhb); the warm waters are retrieved by hot water covered basin (hwcb) and hotwater and fumes channel (hwfc) and pumped by hot water lift pump (hwlp) into the pipe bundles (hwp) that heat before the digesters (dg) of the buildings (LDDC) and then sections (vcmpg) of VSB and finally, used in conjunction with other surface waters (rainwater, river, purified by final biological covered vertical pond (fbcvp) to create an artificial rain by water overflow tray (wot) in (vcmlg) that realizes a natural ion exchange between water, C02 and calcareous material, which conveys the carbonates in the basin of the water to alkalize (wba). Some of the air is transferred from the C02-rich (vcmlg) at (vcmpg) through (uta) air handling units and used for carbon fertilization to increase plant growth. Agricultural biomass and sludge produced by the plant are digested along with the biomass produced in the building (LDDC), dehydrated and turned into compost. The liquid digestate produced by this building is conveyed to the water basin to be purified (wbp) from where it begins purification that goes vertically through the biological ponds vertical (bcsvp ) and ( fbcvp ) that discharge treated water. If the water does not exceed the quality control setpoints, it is recycled through the recirculating water valve (rwv), overflow trays (wot) through the sections (vcmlg ) feeding again the basin of water to be alkalized (wba) and to be purified (wbp) that are linked by water sofned supply (wss) and alkaline water supply (aws); (GSPDPTC) is supplied clean water for cooling by plants (Gued), global urban environmental depuration through the line recovery rainwater and purified water (rrpwl) and the line "water supply (ws)" that arrives at upstream water body (upwb); is fed waste water by the line arrival sewer (as),agricultural wastewater (agrw) and rain that arrives at water basin to be purifier (wbp) is fed sludge by "anaerobic sludge collector (asc)" that is fed by "global urban environmental depuration (GUED)" and "global marine and lacustrine environmental depuration (GMLED)" that arrives at "sludge hopper (sh)", where through transit tank sludge (ttst), also arrives sludge produced by biological covered superimposed ponds (bcsvp); agricultural crops produced in vertical mechanized covered production greenhouse (vmcpg) and farmlands fed " biomass silo (bms) that supply digester loading hopper (dlh) "; mixture of air and C02 captured by urban chimney CCPC is stored in "settling flue gas collector collector (sfgc)", is partially consumed in "mini greenhouse glazing" (mgg) and "purifying urban vertical module (pvum)" and partially stored in tank compressed mixture of air and C02 (STCMC02) and "collector transport compressed mixture of air and C02 (CMC2)", but fed vertical sections covered mechanized limestone greenhouse (vcmlg) of VSB.
2) GSPDPTC system based on the synergy, according to claim 1, in which the section capture cooling purification chimney CCPC increases the temperature of warm water retrieved from thermoelectric power plant (TEPfos) by means of the flue gas water exchanger (fgwe) that downloads the heated waters in hotwater and fumes channel (hwfc). 3) GSPDPTC system based on the synergy, according to claims 1 and 2, in which the warm waters produced by heat ewchanger (avhe) for cooling of turbines and condensers of thermoelectric power plant (TEPfos or TEPbio ) are pumped into the hot water covered basin (hwcb), transferred into the feeding channel for flue gas and warm water (hwfc) and pumped, through pumps (hwlp) to feed the heat exchangers (hwp) of the digesters (dg) and production greenhouse (vcmpg) of VSB. 4) GSPDPTC system based on the synergy, according to claims froml to 3, in which the recovery of C02 to corrode the calcareous rocks suspended in the vertical covered limestone mechanized greenhouse (vclmg) for the purpose of alkalization, desalinization of water and to provide a source of carbon fertilization which is channeled into the vertical mechanized covered production greenhouse (vcmpg) and biological covered superimposed ponds (bcsv - fbcvp), which extracts the C02 from the (vcmlg) through "air treatment units (uta)" or "electric fans (efa)" equipped with gravity shutter (gs).
5) GSPDPTC system based on the synergy, according to claims from 1 to 4, in which verticality of building VSB allows usage of automatized mechanical systems for storage, movement and machining, inspired by systems used in industry and agriculture; moreover, it allows usage of pneumatic transportation of production of agricultural biomass to the storage silos and to the hoppers that feed the digesters (dg) of linear digester dehydrator composter LDDC.
6) GSPDPTC system based on the synergy, according to claims from 1 to 5, in which cover of the plants, verticality of buildings VSB allows heating during the winter and thermal-hygrometric control during the summer and the winter of the environments of the agricultural production (vcmpg) or algae production with photobioreactors (pbpma), through the mix of the plant air with external warm and humid air coming from the adjacent space (vcmlg), without the need of additional energy sources.
7) GSPDPTC system based on the synergy, according to claims from 1 to 6, in which the warm water recovered, besides their use for heating of digesters and hothouses, passing through the calcareous hothouses, transports carbonates toward the see by means of the cold carbonation of the rocks.
8) GSPDPTC system based on the synergy, according to claims from 1 to 7, in which the water purification, if necessary, can be improved by letting suspended baskets with ionic exchange resins (cwhr) transit into the biologic ponds.
9) GSPDPTC system based on the synergy, according to claims from 1 to 8, in which the water in the basins (wba) containing water to alkalinize, in case of a shortage of water, can circulate in series, by periodically inverting the circulation flow, when it arrives to the saturation point of the absorbed calcium carbonate. Once this will be extracted, the water will become softer and can restart absorption of C02 and calcium. This system will produce clean calcium carbonate from which it will be easier and cheaper to obtain calcium oxide, thus further reducing C02 emissions, that are caused by the current production methods of this material for purification and construction systems.
10) GSPDPTC system based on the synergy, according to claims froml to 9, in which the digested water in the digester (dg) of section LDDC, transferred to basins (wpd) for purification and from these to vertical biological ponds (bcsvp - fbcvp) and, for irrigation of vertical mechanized covered production greenhouse (vcmpg), that are used in the digester (dg) itself for production of biogas.
11) GSPDPTC system based on the synergy, according to claims 1 to 10, which can also be used in the urban area by means of the connection with the installations (Gued), global urban environmental depuration), through the water line (ws), water supply, which feeds the basin (upwb), upstream water body, the line (asc), anaerobic sludge collector, which feeds (LDDC) and the line (CMC02), collector transport compressed mixture of air and C02.
12) GSPDPTC system based on the synergy, according to claims 1 to 11 , which can also be used 5 in the urban area by means of the connection with the installations (Gued), whose sludges from
(Gued) through (pvum) purifying vertical urban module, by means of a submerged line (asc), anaerobic sludge collectors, can supply power directly to the load hoppers (sh) of section (LDCC) of urban (GSPDPTC), aided by the hydrostatic pressure imposed on the mud by "transit tank of sludge to be thickened (ttst)", and (spas) submersible pumps for anaerobic sludge, included in the 10 paths (asc), and controlled by the level of sewage in (pvum).
13) GSPDPTC system based on the synergy, according to claims 1 to 12, which can also be used in the urban area by means of the connection with the installations (Gued), in which the flue gas, consisting principally of air and C02, are captured by (CCPC) of (Gued), processed by the same system in a mixture of C02 and compressed air: by (sfgc), settling flue gas collector, filters, and
15 (ac) air compressors, are then stored in (STMC02), storage tank mixture of compressed air and C02, and transferred in (CMC02), collector transport compressed mixture of air and C02, which feeds the section (vcmlg) of ( VSB) of (GSPDPTC).
14) GSPDPTC system based on the synergy, according to claims 1 to 13, which can also be used in the urban area by means of the connection with the installations (Gued), in which the water
20 discharged from (GSPDPTC) in (dwb), downstream water body, purified and alkalized, may be recirculated, returning to (upwb), upstream water body, to feedback cooling (TEPbio), circular sewers or open channels going to the acidified water bodies to fight the final acidification of lakes and seas. In fact, in (Gued), in drains or open channels, circulate only purified water and rainwater, sewage polluted circulate only upstream of purifying urban vertical modules (pvum).
25 15) GSPDPTC system based on the synergy, according to claims 1 to 14, which can also be used in the urban area by means of the connection with the installations (Gued), whose anaerobic sludge, produced in the "purifying vertical urban module" (pvum) are separated by rainwater and also in the case of flooded roads, does not discharge the sludge into the environment but through "submersible pumps for anaerobic sludge (spas)" located along the "anaerobic sludge collectors
30 (asc)" the sludge always comes to the sludge hopper (sh) of digester, of LDDC. 16) GSPDPTC system based on the synergy, according to the (GSPDPTC) system claims, 1 and 14, 15, in which GSPDPTC can also be used to combat eutrophication by means of the installation of "global marine and lacustrine environmental depuration GMLED", which consists in the parallel connection of many purifying vertical marines module (pvmm) superiorly equipped with mini glazing greenhouse (mgg) that, in this case, alkalize water consuming the C02 produced by the oxidation treatment, that is summarized in the following formulas: C6H1206 + 602. <→ 6C02 + 6 H20 + approx 38 molecules ATP; the sludge produced by this treatment is conveyed in anaerobic sludge submersible collector (assc) that is simple polyethylene tubes posed in the seabed, parallel to the shore, in order to connect to the digester embedded in GSPDPTC nearest
17) GSPDPTC system based on the synergy, according to claims 1 to 16, with all the connections of anaerobic sludge collector (asc) (assc) of peripheral sections of "purifying vertical modules" for water, peripheral sections of purifying water in the (u) "urban", (1) "lacustrine" (m) "marine" version, and all links with "agricultural wastewater (agrw)", "recovery rainwater and purified water (rrpwl)" and all links with urban and industrial chimneys CCPC by "collector transport compressed mixture of air and C02 (CMC02)" and all links between fossil thermal power plant (TEPfos) plus CCPfos plus VSB plus LDDC plus TEPbio plus biogas collettor (bioc) plus gasometer plus distribution network to consume biogas, which together form a set of closed loops that neutralize anthropogenic pollution by producing their own biological energy, fresh, depurated, desalinated, alkaline water and organic fertilizers in parallel with the natural biological cycles.
PCT/IT2013/000316 2012-11-19 2013-11-14 Global synergy plants for depuration, biomass production and thermoelectric cogeneration (gspdptc) WO2014076726A1 (en)

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