4~~ Idaha Natianallabaralary Biosphere E N V IR O N M E N T A L E - - PDF document

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4~~ Idaha Natianallabaralary Biosphere E N V IR O N M E N T A L E - - PDF document

E X E C U T I V E S U M M A R Y f P R E S E N T A T I O N WASTE TO ENERGY PROJECT T.N.R.D. British Columbia GASIFICA nON TO ENERGY Reasonable, Responsible & Recvcline 4~~ Idaha Natianallabaralary Biosphere E N V IR O N M E N T A L E


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SLIDE 1

E X E C U T I V E S U M M A R Y

f

P R E S E N T A T I O N

WASTE TO ENERGY PROJECT T.N.R.D. British Columbia GASIFICA nON TO ENERGY Reasonable, Responsible & Recvcline

4~~

Idaha Natianallabaralary

Biosphere

E N V IR O N M E N T A L E N E R G Y

B E L T R A N

Ec~

ISORE*" 1 r.E :i1 i

B E L T R A N A S S O C I A T E S IN S " " " ':::" ;;'" ~

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SLIDE 2

~ W a s te to E n e r g y

3P projects can yield interesting benefits

'4 P u b lic

P r iv a te P a r tn e r s h ip s

  • Intended to satisfy public

goals with private discipline.

  • On Time, On Budget and
  • perations

as expected.

  • Our MRRF is intended to

be a partnership. Gives T.N.R.D. and other participants active involvement in the public recycling goals of the Province and Canada.

  • Clear principals and

integrity in execution.

2

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SLIDE 3

P R I V A T E P U B L I C 4 P A R T N E R S H I P S

  • A ll

R is k s

  • Transferable

Risk

  • Project delivery risk

profile

  • Lifecycle Cost

Certainty

  • Open and

transparent communication

P ro je c t D e liv e ry R is k

Courtesy: Epcor

3

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SLIDE 4
  • 4

Biosphere Gasifier Rendering

'4 F r o n t E n d R e c y c lin g

  • We tend to prefer

projects which remove recyclable materials, and non recyclable materials .

  • We can't gasify stone

and glass, and we should recycle aluminum cans, etc. 4

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SLIDE 5
  • Transfer to Waste Processing can be direct or

by trans shipment .

  • Baling systems can produce wrapped waste

with NO odor and NO negative image. 5

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SLIDE 6
  • 4 V is u a lly

n e u tr a l.

  • Bales weigh

approximately 3,500 pounds each.

  • Compressed

approximately 14:1 ratio.

  • Can be stacked

deeply, and held in high temperatures without problems

I

  • ,

R e fu s e D e r iv e d F u e l

l. ;;K

  • Municipal solid waste (MSW) is processed into

Refuse Derived Fuel (RDF) in a MRF - i.e., in a Material Recycling Facility

  • The RDF can be gasified in an Biosphere

Gasifier

  • The RDF can also be mixed with 82% moisture

content "belt pressed" Municipal sewage sludge and gasified in an Biosphere Gasifier

6

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SLIDE 7
  • 4 Prototype 15 Million Btulh Unit

7

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SLIDE 8
  • 4Direct-fired lumber kilns

~ Indirectly fired dryer in Pulp mill

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SLIDE 9

Firing lime kiln

Proven Commercial ~ Performance

  • Two units (45,000,000 Btu x 2) have been

running continuously for 27 years.

  • The machine has lasted longer than most
  • f the ten forestry product companies

who installed units.

  • Reliable, robust, solid and proven

fluidized bed updraft gasification that can project finance.

9

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SLIDE 10

'4 Miscellaneous Wastes

  • Municipal

Solid Waste

  • Refuse derived

fuel

  • Bio Solids or Sludge from

waste water

  • Used Railway

Ties & Telephone Poles

  • Construction

and Demolition Debris

  • Land Clearing

Debris

  • Poultry

litter

  • Cow Manure
  • Pig Manure
  • Mixtures
  • f the above

Diagram

  • f 3 - 90 Million Btulh

Biosphere Gasifiers "Externally" Co- firing an existing boiler

10

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SLIDE 11
  • 4 - F ir in g
  • f S te a m

T u r b in e

i

  • Biomass is gasified in separate

units built alongside of steam turbine.

  • Gasifiers

2,OOO°F± 200°F products of combustion are ducted to Heat Exchangers which drive steam into the Turbine.

  • Products of combustion

from Heat Exchanger goes into our special bag houses.

  • B io m a s s m o is tu re

c o n te n t

U D to 6 5 %

is

"OK" fa, ou' aasifiers. ~

  • 4 S ig n ific a n t

F e a tu r e s , 1

  • Four air sources:
  • Underfire air gasifies biomass in the pi stage
  • Overfire air preheats 1'1 stage producer

gas to ensure ignition in the 2nd stage

  • Primary combustion air ignites the preheated

producer gas at the bottom of the 2nd stage

  • Secondary combustion air completes

combustion of producer gas in the 2nd stage

11

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SLIDE 12

'4 Significant Featnres, 2 ~

  • Very large pt stage grate area
  • Hence grate temperature

:5:1,200°F

  • Hence essentially zero slag
  • Ash can be reclaimed as valuable products
  • Very low underfire

air flow

  • (only need sufficient air to gasify biomass)
  • Hence very low particulate elutriation off

pile

~ Significant Featnres, 3 In

  • The Biosphere Gasifier can burn biomass with

moisture contents up to 65% (wet basis) and ash contents up to 35%

  • 5:1 turndown

ratio is standard: 9:1 is not uncommon

  • 15 second

reSDonse time to steD chanae in Btu Demand sianal

  • Abort valve permits rapid dumping
  • f

products of combustion in an emergency 12

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SLIDE 13

~ R e fu s e D e r iv e d F u e l

L :; tiK

  • Municipal solid waste (MSW) is processed into

Refuse Derived Fuel (RDF) in a MRF - i.e., in a Material Recycling Facility

  • The RDF can be gasified in an Biosphere

Gasifier

  • The RDF can also be mixed with 82% moisture

content "belt pressed" Thunder Bay Municipal sewage sludge and gasified in an Biosphere Gasifier

~ P h y s ic a l P la n t C o n s tr u c tio n

13

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SLIDE 14

~ C O N S T R U C T I O N

  • Estimated direct

~ workforce will be 35 ~ to 40 men for ~ approximately ~ fourteen months ...•

  • Additional jobs will

likely be in transportation and supply.

14

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SLIDE 15
  • 4 C o n s tr u c tio n

M a jo r T r a d e s

  • Heavy Equipment
  • perators
  • Electrical, Major and

sub-systems

  • Machinists, Welders

and fitters

  • Power Equipment,

Cranes, Concrete

  • Refractory

~ E n v ir o n m e n ta l C o m p lia n c e

15

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SLIDE 16

KYOTO PROTOCOL TO THE UNITED NATIONS FRAMEWORK

  • 4

CONVENTION; CLIMATE CHANGE

  • Reducing the greenhouse gas effects of

the combustion of fossil fuels is exactly the value produced by a biomass and refuse derived fuel based power plant .

  • ZERO "new" C02 production cycle.

I

  • '4 Biosphere Gasifier
  • 1st Stage: gentle

updraft gasification

  • n very

large grate

  • 2nd Stage: vigorous,

double vortex, cydonic combustion

  • Emissions (untreated):

CO < 1 DDm. NOx< 15

  • DDm. Darticulate

< 100 ma/Nm3 (< 0.125 Ib/l06

Btu: < 0.04 ar/dscfl

  • Emissions listed are Drior to treatment.

Bag House @ PM2.5 and Wet Tubular Electrostatic Precipitators are planned for projects.

  • Units in continuous
  • peration

for 25+ years

16

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SLIDE 17

4Significant Features, 4

  • Staged combustion permits operating

with excess air levels as low as 15%

  • The lime kiln test unit burned 55 %

moisture content hog fuel and supplied 2,200°F flue gas to the kiln @ e = 15%

  • Stal!:edcombustion and low temperatures

(due to wet fuels) combine to produce virtuallv zero thermal NOx

I!,..... •

I

.....•.•

4 Significant Features,S

  • Dioxins and Furans Destroyed, viz.,
  • Chlorine can react with cellulose to form

dioxins and furans in the 1<1 stage

  • However, these gases are destroyed in the

2nd stage with its 1,800°F plus brick walls

  • No black waterwalls are present to chilI •

and lock in - dioxins or furans in the 2nd stage

17

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SLIDE 18

M.A.C.T . ~ Dioxins & Furans

  • M.A.C.T. is maximum available control
  • technology. (Also sometimes known as B.A.C.T.
  • r Best Available Control Technology) •
  • While we should not have any issue with this on
  • ur gasification, we include special bag houses

that would automatically catch any dioxins or furans at 40% below the current A7 Ontario Standards. Very, very clean.

~Natural Exposure is Forest Fire

5!. 01"•••Hi')"

T""'I''''''''''''

S"UlC.$

",

\ Ch.mk,)1 ", ••" ••r.1C,"II;"'.:I

".

l'm<lSI
  • •<I'J"
AI'l'lic.ni ••n )', W.U1elncine •• ni •••• S••" •• :••••

",

EUeI9)1foe".1-HiolO SOluees

",

Me'.lltlllqic.J1 P,oces,u,s )', SOcietal 1··9·.·••••••••
  • •••.••••
_ '(IoInI>< •••t_~ u .•.• ,..-"'•.•• u..- •••••

.•... 1_ .••••.• ··1

FIgure 1: U.S. Dioxin Sources. Year 2004

1106 g-TEO [EPA-Ouantlfled Source$1 + 1280 a_TEO [For.n Fir. sources"] 8;;1ckY;lrd Tra'!;l'1 2386 g-TEO (TouI] Burning _ ;:6",

18

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SLIDE 19

~ C a ta ly tic F ilte r S y s te m

M u n ic ip a l S o lid W a s te In c in e ra to r IY R O DioJin~ionwithCataJrticFilte'lIedia

"...

  • -_ ...•...~
.•._~-~ ..-..

,

  • .s
Q .8 1
  • ';

.." "I,..' ',~ ..

't'\.'\~-¥~~~yy~ r:

4

M e ta ls ,

S:~~o~~:le~n~~:ration

S o u th w e s te rn U n ite d

Slales

T e s t B u m E m is s io n

Summary:

  • ,

.-

.-.

B E L T R A N

  • ,
  • .
  • 58,55

57,60 60,79 .

B E L .T R A N A S S O C IA T E S S H e .
  • DRE 0/0
  • --
  • .- --
  • -. --
  • -- -- -- --

Wet Tubular Electrostatic Precipitator

r

~.

j

19

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SLIDE 20
  • .••.~
.•.--...
  • .•......••.•...•••...

1

  • Dioxins

&. Furans Ontario

A7 to Project

A7 M.A.C.T. EXCEEDSALL REQUIREMENTS

(0.14 A7 VS 0.049)

20

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SLIDE 21

~ PARTICULATE ONTARIO A7 TO PROJECT

100

80

60 40

20

  • A7

G M.A.C.T. FAR EXCEEDS REQUIREMENTS

NOx ONTARIO A7 LIMIT TO PROJECT 21

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SLIDE 22

4

N O x

~

Idaho Notional laboratory

M .A .C .T .

  • The Idaho National Laboratory

has come up with a way to insert a "re-burn" chamber for NOx on the exit ducting of our gasification unit.

  • Given the low proteins in municipal waste

product and very low thermal NOx this would be a very conservative move that we would do more for "PR" than any need -but this is a test we are interested in and will pursue.

~Agricultural Wastes ~

  • With a grate temperature
  • f 1,200°F, potassium

(potash) and sodium (soda) in agricultural and animal waste do not vaporize to form alkali deposits on boiler tubes

  • Potassium vaporizes at 1,400°F and sodium

vaporizes at 1,616°F

  • The potash and soda remain in the 151 stage,

from which they are removed by the built-in ash removal system and sold to farmers depending on what else is present

  • I

22

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SLIDE 23
  • ~

E c o n o m ic s , J o b B e n e fits

E 't2

~

  • 4

B io s p h e re G a s ifie r R e n d e rin g 23

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SLIDE 24

~ Thank you.

  • We look forward to answering any of

your questions on all of the topics covered in this presentation.

  • You can reach Paul Finestone at 818-995-

6706, or on email:

paul@biosphereener2v.com

  • You can reach Bill Bohoslawac at 604-

727-1005

  • Thank you.

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