GREEN Building

A base camp for our ideas

With the construction of our headquarter in Brembate (Bg) we aimed toexpress our creativity at its best, to create a enjoyable and healthy space inwhich to work day by day.We breath the benefits that such a design can bring in to the working lifeof our teams. This is our best sample of innovation, quality and comfortachieving in addition a formidable energy saving.

OFFICE - BERGAMO

OFFICE- BERGAMO

OFFICE- BERGAMO

OFFICE- BERGAMO

Facility: area 1318 m2 volume 4350 m3Systems: 70 m2 solar panels

2,000 m underground coils (geotermia)condensation boiler (nr. 2 falls type 105 Kw)Radiating thermal systems to wall and pavement

Consumption gas methane with traditional systems for buildings heating 270 h and insulation meets Law 10/91

EFFECTIVE CONSUMPTIONS GAS METHANE FOR PRODUCTION SANITARY WARM WATER AND HEATING AT LOW TEMPERATURE

CONSUMPTION HEATING m2 heated 1,318 x 1.22 = 1607 equivalents for average height from 3.3m to 2.70m1607 x 100 kwh/m2 to = 160,700 kw/year1 m3 methane produces one rendered of 9.941 kwAnnual Consumption = 160,700/9.941 kwRendering of equal traditional boilers to approximately 75% = 16,165/0.75 = 21,553 m3Year average cost with traditional system only for heating m3 21.553 x 0.62 =

TOTAL /YEAR € 13,363.00WARM WATER CONSUMPTION Consumption from gauge per bar = m3 year/30

Consumption assumed for offices = 10m3 (approximately 1 liter/person X 30 working days Thermic Delta = 40-15= 25°C x 40,000 = 1’000,000 calKw = 1’000,000 x 0.86/1,000= 860 KwM3 methane = 860 x 7.456 = 6.412m3Annual Cost for warm water = 6,412 x 0.62 = € 3,975.00 + approximately 10% for return

TOTAL €/YEAR 4,373.00

TOTAL CONSUMPTIONS WITH TRADITIONAL SYSTEMS

HEATING € 13,363.00WARM WATER € 4,373.00

TOT. € 17,736.00

TOTAL CONSUMPTIONS ON METER GAUGE

HEATING +WARM WATER € 5,300.00

DIFFERENCE + 12,436.00 €/YEAR

Project for new apartments in BIOecological architecture

Albese con Cassano (CO)

Project for new apartments in BIOecological architecture

Albese con Cassano (CO)

BEARING MASONRY AND EXTERIOR INSULATION

WOODEN FLOOR WITH HEATED PANEL

U= 0.196 Wm2/K

U= 0.293Wm2/K

Project for new apartments in BIOecological architecture

Albese con Cassano (CO)

Project for new VILLABIOecological architectureAlbese con Cassano (CO)

Project for new VILLABIOecological architectureAlbese con Cassano (CO)

Prospetto Sud

Prospetto Nord

Project for new VILLABIOecological architectureAlbese con Cassano (CO)

Project for new VILLABIOecological architectureAlbese con Cassano (CO)

Project for new APARTMENTSICPE – Institute de Cercetari ElectrotehniceBucaresti

Project for new APARTMENTSICPE – Institute de Cercetari Electrotehnice - Bucaresti

Project for new APARTMENTSICPE – Institute de Cercetari Electrotehnice - Bucaresti

URBANISTIC DATA

Location: Pomezia near RomeLot area: 20.000,00 m2Covered project area = 17.000,00 m2

Residence for Retired and Children Clinic

GLASS HOUSE: WINTER RADIATION

GLASS HOUSE: SUMMER RADIATION

LOGGIA: WINTER RADIATION

Residence for Retired and Children Clinic

PERSPECTIVE VIEWS

Residence for Retired and Children Clinic

PERSPECTIVE VIEWS

URBANISTIC DATALocation: Gallarate near Milan Lot area: 5.200,00 m2Abitable Units N. 40

APARTMENTS

SECTION

PLAN

BIO - ROOM HOTEL

PLAN

BIO - ROOM HOTEL

Green CITY

CO2

H2

STEAM

ENERGY

Paper, glass, re – plastic, steel etc

B

A

COMPOST. AGRIC.

C

$ kW/h

H2O

Gas

$ kW/h

$ kW/h$

$ m3/h

$ m3/h

kW/h

$ kW/h

$ m3/h

$ kW/h

/ MAIL

GENERAL PLAN

TWR Process: Project Falcon-BayCurrency: Total AED

Electric energy production for: TurbogasPersons 50.000 kg/d/person 2,00M.S.W. ton/day

total to selection 100 ton/h 4,17Industrial waste 240 ton/h 10,00

Selection MSW and Bio farm planttotal to selection 100 ton/day

Biomass from bio farm R.D.F. from MSW0,75 ton/h 1,75

Consumption of the systemkW/h

Bio farm plant 700 for O2 production 1.150 for CO2 separation 300 for TWR plant 3.500 Total consumption 4.950

Electric energy productionby Fuelcell

kW/hTWR plant production 28.332TWR plant comsumption 4.950Total net production 23.382

a) QUANTITIESh/year 8000

Waste to TWR ton/h 12,50O2 Nmc/h 2.899

CH4 Nmc/h 1.160

b) PRODUCTIONSFuell cell

Total El.En. MW/h 28,332

El. En. Consum. MW/h 4,950

Aggregates kg/h 1.392

Steam kg/h 5.828

Investment cost Cost year Revenue year Revenue 1st year OperaTotal AED 60% pro

368.462.000 47.968.251 122.010.150 73.206.090 74.0

DISCOUNTED PAYBACK PERIOD 8%Total AED 0 1 2 3Investment Cost -368.462.000 Discounted Revenues 57.485.221 95.068.672 88.0Discounted cumul.cash flow for payback -368.462.000 -310.976.779 -215.908.107 -127.8Discounted payback 360 360 360,0period (day) 360 360 36

Revenue year DAED/kg Kg/year

M.S.Waste 0,454 36.000.000 Industrial Waste 0,454 80.000.000Fuel Cell AED/kW KW/yearValue 0,353 226.656.655 Turbogas AED/kW KW/yearValue 0,353 168.786.870

AED/ton ton/yearSteam 50,450 46.622

AED/ton ton/yearCarbon credit 61,024 120.955

Revenue year Total AEDRevenue first year Total EURO

byTurbogaskW/h

19.6374.950

14.687

ton/year 100.000Nmc/year 23.190.281Nmc/year 9.276.112

Turbogas Fuell cell Turbogas19,637 MW/year 226.657 157.096

4,950 MW/year 39.602 39.602

1.392 ton/year 11.139 11.139

5.828 ton/year 46.622 46.622

CHANGE: EURO/AED 1/ 5,045INVESTMENTS EURO/USD 1/ 1,34Pos. Description Amount Unit cost Total cost

1 Global area by-Tecnoma 10000 mq Total AED Total AED2 Bio farm (chemical process for waste stabilization) 1 28.660.000 28.660.000 3 TWR gasification plant 3 53.214.333 159.643.000

System supervision, control and management with the dedicated and protect software

4 Production CO2 1 11.350.000 11.350.000 5 Turbogas 1 69.620.000 69.620.000 6 Planning and direction works 2.899.000 2.899.000 7 Mounting TWR plant 3 4.782.667 14.348.000

TOTAL COST TECHNOLOGY SUPPLY 286.520.000 8 Civil works for TWR plant 1 6.827.000 6.827.000 9 Support structures for TWR plant 1 10.617.000 10.617.000 10 Utilities (substation electrical worker 1 8.702.000 8.702.000

for elevation of the tension, emergency, etc)11 Infracstructures 1 55.796.000 55.796.000

TOTAL COST LOCAL WORKS 81.942.000

TOTAL INVESTMENT n°1 Total AED 368.462.000

ating Operating profit Years amortizat. Cash flow Cash flowofit 1st year 10 1st year041.899 25.237.839 36.846.200 110.888.099 62.084.039

3 4 5

026.548 81.506.063 75.468.577

881.559 -46.375.497 29.093.080360,0 221,2 -3.491.169.609

60 221 0

Direct Fuel Cell TurbogasTotal AED Total AED16.345.800 16.345.80036.324.000 36.324.000

80.043.798

59.607.083

2.352.059 2.352.059

7.381.208 7.381.208

142.446.864 122.010.15073.206.090

POLLUTION = 0

DSCAPE SPRINKLING

GEOTERMIA

133.4 kW COGENERATION

CENTRAL ABSORPTION AT

LOW TEMPERATURE

47.4 kW E

14,92 %

LOST SMOKES

98 kW CEFFIC

66 kWHEAT RECOV

DISSIPATION230kW

66kW

SOLAR HEAT RECOVERY

Solar and cogeotermic t

ELECTRICAL

COOLING CIENCY

TOTAL SYSTEM

EFFICIENCY

(47.4 + 98 + 16.17)/ (133.4) =

121 %

VERY

thermal building system

FIELD SOLAR PHOTOVOLTAIC

16.17kW

Which services we

1. Location’s in

2. Project prop

ENERGY MIXOptimized by means of bio-climatic principles

EE

Towards and according tincentives and funding o

3. Educational training sess

can offer ?

ntrinsic and environmental conditions analysis

posals

ENERGY EFFICIENCY, PROFITABLY AND ENVIRONMENTALLY FRIENDLY SOLUTIONS

o the public optimization

activities to energy saving through widespread sions

ENERGY MENERGY M

a) ENERGY MANAGEMENT

LIGHTING DESIGN AND MANAGEMENTENERGY SOURCE MANAGEMENTENERGY COST CONTROL

b) AEOLIAN ENERGY

d) GEOTHERMAL

c) BIO-CLIMATIC

LOCAL AND REMOTE

MIXMIX

e) SOLAR THERMODYNAMIC

h) WASTE MANAGEMENT

g) FUEL CELLS

f) SOLAR COOLING

Waste Disposal

GENERAL PLAN

SECTIONS ELEVATIONS

INCINERATOR IN WORK

BRESCIA - ITALYActual Technology

GENERAL PLAN

ELLEVATIONS

INCINERATORCOMPOSTING

PROJECT

TONAR - MOSCOW Actual Technology

GENERAL PLAN

SECTION

INCINERATORPROJECT

LOMELLINA - ITALYActual Technology

POLLUTION = 0

DSCAPE SPRINKLING

GEOTERMIA

FROM WASTET.W.R. - New technologies : Se

E TO ENERGYeparate collection of molecules

TWR : THE TECHNOLOGICAL SOLUTIONAIM: hydrogen production starting from raw mawastes) without producing pollutionSOLUTION: gasification of raw materials with purhigh hydrogen concentration) final reaction andcarbon dioxide recovery

aterials (at present called

rified syngas production (at d hydrogen separation, with

H2 AND O2 WASTES PLANT PRODUCTION

The technologies and equipment included in the TWR pplant, already widely in similar processes are the fol

1. Heat recuperator2. Syngas neutralization and purification3. Syngas compression unity4. CO2 recovery5. H2 separation from the residual syngas6. Steam production boiler

process to complete the lowing ones:

Waste from earthworms

BASIN OF FLOTATION

inert

SEDIMEN

Compressor

Screening vibrant

flocculent

NTATION

To s

edim

enta

tion