GREEN Building - THINK GREEN
GREEN Building - THINK GREEN
GREEN Building - THINK GREEN
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<strong>GREEN</strong> <strong>Building</strong>
OFFICE - BERGAMO<br />
A base camp for our ideas<br />
With the construction of our headquarter in Brembate (Bg) we aimed to<br />
express our creativity at its best, to create a enjoyable and healthy space in<br />
which to work day by day.<br />
We breath the benefits that such a design can bring in to the working life<br />
of our teams. This is our best sample of innovation, quality and comfort<br />
achieving in addition a formidable energy saving.
OFFICE- BERGAMO
OFFICE- BERGAMO
OFFICE- BERGAMO<br />
EFFECTIVE CONSUMPTIONS GAS METHANE FOR PRODUCTION SANITARY WARM WATER<br />
AND HEATING AT LOW TEMPERATURE<br />
Facility:<br />
Systems:<br />
area 1318 m2 volume 4350 m3<br />
70 m2 solar panels<br />
2,000 m underground coils (geotermia)<br />
condensation boiler (nr. 2 falls type 105 Kw)<br />
Radiating thermal systems to wall and pavement<br />
Consumption gas methane with traditional systems for buildings heating 270 h and insulation meets Law 10/91<br />
CONSUMPTION HEATING m2 heated 1,318 x 1.22 = 1607 equivalents for average height from 3.3m to 2.70m<br />
1607 x 100 kwh/m2 to = 160,700 kw/year<br />
1 m3 methane produces one rendered of 9.941 kw<br />
Annual Consumption = 160,700/9.941 kw<br />
Rendering of equal traditional boilers to approximately 75% = 16,165/0.75 = 21,553 m3<br />
Year average cost with traditional system only for heating m3 21.553 x 0.62 =<br />
WARM WATER CONSUMPTION<br />
TOTAL /YEAR € 13,363.00<br />
Consumption from gauge per bar = m3 year/30<br />
Consumption assumed for offices = 10m3 (approximately 1 liter/person X 30 working days<br />
Thermic Delta = 40-15= 25°C x 40,000 = 1’000,000 cal<br />
Kw = 1’000,000 x 0.86/1,000= 860 Kw<br />
M3 methane = 860 x 7.456 = 6.412m3<br />
Annual Cost for warm water = 6,412 x 0.62 = € 3,975.00 + approximately 10% for return<br />
TOTAL €/YEAR 4,373.00<br />
TOTAL CONSUMPTIONS WITH TRADITIONAL SYSTEMS<br />
HEATING € 13,363.00<br />
WARM WATER € 4,373.00<br />
TOT. € 17,736.00<br />
TOTAL CONSUMPTIONS ON METER GAUGE<br />
HEATING +<br />
WARM WATER € 5,300.00<br />
DIFFERENCE + 12,436.00 €/YEAR
Project for new apartments in<br />
BIOecological architecture<br />
Albese con Cassano (CO)
Project for new apartments in<br />
BIOecological architecture<br />
Albese con Cassano (CO)
Project for new apartments in<br />
BIOecological architecture<br />
Albese con Cassano (CO)<br />
BEARING MASONRY AND EXTERIOR INSULATION<br />
U= 0.196<br />
Wm2/K<br />
WOODEN FLOOR WITH HEATED PANEL<br />
U= 0.293<br />
Wm2/K
Project for new VILLA<br />
BIOecological architecture<br />
Albese con Cassano (CO)
Project for new VILLA<br />
BIOecological architecture<br />
Albese con Cassano (CO)<br />
Prospetto Sud<br />
Prospetto Nord
Project for new VILLA<br />
BIOecological architecture<br />
Albese con Cassano (CO)
Project for new VILLA<br />
BIOecological architecture<br />
Albese con Cassano (CO)
Project for new APARTMENTS<br />
ICPE – Institute de Cercetari Electrotehnice<br />
Bucaresti
Project for new APARTMENTS<br />
ICPE – Institute de Cercetari Electrotehnice - Bucaresti
Project for new APARTMENTS<br />
ICPE – Institute de Cercetari Electrotehnice - Bucaresti
Residence for Retired and Children Clinic<br />
URBANISTIC DATA<br />
Location: Pomezia near Rome<br />
Lot area: 20.000,00 m2<br />
Covered project area = 17.000,00 m2
Residence for Retired and Children Clinic<br />
GLASS HOUSE: WINTER RADIATION<br />
GLASS HOUSE: SUMMER RADIATION<br />
LOGGIA: WINTER RADIATION
Residence for Retired and Children Clinic<br />
PERSPECTIVE VIEWS
APARTMENTS<br />
URBANISTIC DATA<br />
Location: Gallarate near Milan<br />
Lot area: 5.200,00 m2<br />
Abitable Units N. 40<br />
PERSPECTIVE VIEWS
SECTION
BIO - ROOM HOTEL<br />
PLAN
BIO - ROOM HOTEL<br />
PLAN
Green CITY
Paper, glass, re – plastic, steel etc<br />
C<br />
ENERGY<br />
A<br />
B<br />
COMPOST.<br />
AGRIC.<br />
CO2<br />
H2<br />
STEAM
$ kW/h<br />
$ kW/h<br />
$ kW/h<br />
$ kW/h<br />
$ kW/h<br />
$ m 3 /h<br />
/ MAIL<br />
Gas<br />
$ m 3 /h<br />
$ m 3 /h<br />
$ kW/h<br />
H 2 O
GENERAL PLAN
TWR Process: Project Falcon-Bay<br />
Currency: Total AED<br />
Electric energy production for: Turbogas<br />
Persons 50.000 kg/d/person 2,00<br />
M.S.W.<br />
ton/day<br />
total to selection 100 ton/h 4,17<br />
Industrial waste 240 ton/h 10,00<br />
Selection MSW and Bio farm plant<br />
total to selection 100 ton/day<br />
Biomass from bio farm<br />
R.D.F. from MSW<br />
0,75 ton/h 1,75<br />
Consumption of the system<br />
kW/h<br />
Bio farm plant 700<br />
for O2 production 1.150<br />
for CO2 separation 300<br />
for TWR plant 3.500<br />
Total consumption 4.950<br />
Electric energy production<br />
by Fuelcell<br />
kW/h<br />
TWR plant production 28.332<br />
TWR plant comsumption 4.950<br />
Total net production 23.382<br />
a) QUANTITIES<br />
h/year 8000<br />
Waste to TWR ton/h 12,50<br />
O2 Nmc/h 2.899<br />
CH4 Nmc/h 1.160<br />
byTurbogas<br />
kW/h<br />
19.637<br />
4.950<br />
14.687<br />
ton/year 100.000<br />
Nmc/year 23.190.281<br />
Nmc/year 9.276.112<br />
CHANGE: EURO/AED 1/ 5,045<br />
INVESTMENTS EURO/USD 1/ 1,34<br />
Pos. Description Amount Unit cost Total cost<br />
1 Global area by-Tecnoma 10000 mq Total AED Total AED<br />
2 Bio farm (chemical process for waste stabilization) 1 28.660.000 28.660.000<br />
3 TWR gasification plant 3 53.214.333 159.643.000<br />
System supervision, control and management<br />
with the dedicated and protect software<br />
4 Production CO2 1 11.350.000 11.350.000<br />
5 Turbogas 1 69.620.000 69.620.000<br />
6 Planning and direction works 2.899.000 2.899.000<br />
7 Mounting TWR plant 3 4.782.667 14.348.000<br />
TOTAL COST TECHNOLOGY SUPPLY 286.520.000<br />
8 Civil works for TWR plant 1 6.827.000 6.827.000<br />
9 Support structures for TWR plant 1 10.617.000 10.617.000<br />
10 Utilities (substation electrical worker 1 8.702.000 8.702.000<br />
for elevation of the tension, emergency, etc)<br />
11 Infracstructures 1 55.796.000 55.796.000<br />
TOTAL COST LOCAL WORKS 81.942.000<br />
TOTAL INVESTMENT n°1 Total AED 368.462.000<br />
b) PRODUCTIONS<br />
Fuell cell<br />
Total El.En. MW/h 28,332<br />
El. En. Consum. MW/h 4,950<br />
Aggregates kg/h 1.392<br />
Steam kg/h 5.828<br />
Turbogas Fuell cell Turbogas<br />
19,637 MW/year 226.657 157.096<br />
4,950 MW/year 39.602 39.602<br />
1.392 ton/year 11.139 11.139<br />
5.828 ton/year 46.622 46.622<br />
Revenue year<br />
Direct Fuel Cell Turbogas<br />
AED/kg Kg/year Total AED Total AED<br />
M.S.Waste 0,454 36.000.000 16.345.800 16.345.800<br />
Industrial Waste 0,454 80.000.000 36.324.000 36.324.000<br />
Fuel Cell AED/kW KW/year<br />
Value 0,353 226.656.655 80.043.798<br />
Turbogas AED/kW KW/year<br />
Value 0,353 168.786.870<br />
59.607.083<br />
AED/ton ton/year<br />
Steam 50,450 46.622 2.352.059 2.352.059<br />
AED/ton ton/year<br />
Carbon credit 61,024 120.955 7.381.208 7.381.208<br />
Revenue year<br />
Revenue first year<br />
Total AED<br />
Total EURO<br />
142.446.864 122.010.150<br />
73.206.090<br />
Investment cost Cost year Revenue year Revenue 1st year Operating Operating profit Years amortizat. Cash flow Cash flow<br />
Total AED 60% profit 1st year 10 1st year<br />
368.462.000 47.968.251 122.010.150 73.206.090 74.041.899 25.237.839 36.846.200 110.888.099 62.084.039<br />
DISCOUNTED PAYBACK PERIOD 8%<br />
Total AED 0 1 2 3 4 5<br />
Investment Cost -368.462.000<br />
Discounted Revenues 57.485.221 95.068.672 88.026.548 81.506.063 75.468.577<br />
Discounted cumul.<br />
cash flow for payback -368.462.000 -310.976.779 -215.908.107 -127.881.559 -46.375.497 29.093.080<br />
Discounted payback 360 360 360,0 360,0 221,2 -3.491.169.609<br />
period (day) 360 360 360 221 0
OLLUTION = 0<br />
GEOTERMIA<br />
SCAPE SPRINKLING
Solar and cogeotermic thermal building system<br />
LOST SMOKES<br />
133.4 kW COGENERATION<br />
14,92 %<br />
16.17<br />
kW<br />
FIELD SOLAR<br />
PHOTOVOLTAIC<br />
66 kW<br />
47.4 kW ELECTRICAL<br />
HEAT RECOVERY<br />
TOTAL<br />
SYSTEM<br />
EFFICIENCY<br />
66kW<br />
SOLAR<br />
HEAT<br />
RECOVERY<br />
CENTRAL<br />
ABSORPTION AT<br />
LOW<br />
TEMPERATURE<br />
230<br />
kW<br />
DISSIPATION<br />
98 kW COOLING<br />
EFFICIENCY<br />
(47.4 + 98 + 16.17)/ (133.4) =<br />
121 %
Which services we can offer ?<br />
1. Location’s ntrinsic and environmental conditions analysis<br />
2. Project proposals<br />
ENERGY MIX<br />
Optimized by means of bio-climatic principles<br />
ENERGY EFFICIENCY, PROFITABLY AND<br />
ENVIRONMENTALLY FRIENDLY SOLUTIONS<br />
Towards and according to the public<br />
incentives and funding optimization<br />
3. Educational activities to energy saving through widespread<br />
training sessions
ENERGY MIX<br />
a) ENERGY MANAGEMENT<br />
LOCAL AND REMOTE<br />
LIGHTING DESIGN AND MANAGEMENT<br />
ENERGY SOURCE MANAGEMENT<br />
ENERGY COST CONTROL<br />
e) SOLAR THERMODYNAMIC<br />
b) AEOLIAN ENERGY<br />
f) SOLAR COOLING<br />
c) BIO-CLIMATIC<br />
g) FUEL CELLS<br />
d) GEOTHERMAL<br />
h) WASTE MANAGEMENT
Waste<br />
Disposal
INCINERATOR<br />
IN WORK<br />
BRESCIA - ITALY<br />
Actual Technology<br />
GENERAL PLAN<br />
SECTIONS<br />
ELEVATIONS
INCINERATOR<br />
COMPOSTING<br />
PROJECT<br />
TONAR - MOSCOW<br />
Actual Technology<br />
GENERAL PLAN<br />
ELEVATIONS
INCINERATOR<br />
PROJECT<br />
LOMELLINA - ITALY<br />
Actual Technology<br />
GENERAL PLAN<br />
SECTION
OLLUTION = 0<br />
GEOTERMIA<br />
SCAPE SPRINKLING
FROM WASTE<br />
TO ENERGY<br />
T.W.R. - New technologies : Separate collection of molecules
TWR : THE TECHNOLOGICAL SOLUTION<br />
AIM:hydrogen production starting from raw materials (at present called<br />
wastes) without producing pollution<br />
SOLUTION: gasification of raw materials with purified syngas production (at<br />
high hydrogen concentration) final reaction and<br />
hydrogen separation, with<br />
carbon dioxide recovery
H2 AND O2 WASTES PLANT PRODUCTION<br />
The technologies and equipment included in the TWR process to complete the<br />
plant, already widely in similar processes are the following ones:<br />
1. Heat recuperator<br />
2. Syngas neutralization and purification<br />
3. Syngas compression unity<br />
4. CO2 recovery<br />
5. H2 separation from the residual syngas<br />
6. Steam production boiler
Waste<br />
from<br />
earth<br />
worms<br />
SEDIMENTATION<br />
To sedimentation<br />
Screening vibrant<br />
inert<br />
BASIN OF FLOTATION<br />
flocculent<br />
Compressor
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