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“Making pressurized water scrubbing e ultimate biogas upgrading technology with the DMT TS-PWS ® system” R. Lems M.Sc. , R&D Manager DMT Environmental Technology

Ts Pws Biogasupgrading Bremen 2010 V1

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Page 1: Ts Pws Biogasupgrading Bremen 2010 V1

“Making pressurized water scrubbing

the ultimate biogas upgrading technology

with the DMT TS-PWS® system”

R. Lems M.Sc. , R&D Manager

DMT Environmental Technology

Page 2: Ts Pws Biogasupgrading Bremen 2010 V1

Why biogas upgrading?

Digester

Gas treatment(desulphurisation)

GasTreatment(upgrading)

Green gas(CBG: Compressed BioGas)

Mobility

Power 40%

Biogas

Heat 60%

CHP

Natural gas grid

Page 3: Ts Pws Biogasupgrading Bremen 2010 V1

Biogas as Vehicle Fuel

Page 4: Ts Pws Biogasupgrading Bremen 2010 V1

Substance %

Methane, CH4 45-75

Carbon dioxide, CO2 25-45

Carbon monoxide, CO 0-0,3

Nitrogen, N2 1-15

Water, H2O Saturated

Hydrogen sulfide, H2S 0,1-0,5

Oxygen, O2

Siloxane, R2SiOtraces

Why upgrading Biogas?

Page 5: Ts Pws Biogasupgrading Bremen 2010 V1

Choice for large-scale?

• PSA: Pressure Swing Absorption- complex/ high operational costs+ N2 removal

• CA: Catalytic absorption- chemicals and heat needed+ very low methane slip (if no CHP is used for heat)

• MS: Membrane Separation- High methane loss (10-20%)+ simple system

• CL: Cryogenic liquefaction.- complex/ expensive/ no proven technology/ low energy efficiency+ liquid CO2

• PWS: Pressurized Water Scrubbing- high towers+ No chemicals, simple system, high energy efficiency

Page 6: Ts Pws Biogasupgrading Bremen 2010 V1

Choice for Full-scale?

ISET 09-09-2009

Page 7: Ts Pws Biogasupgrading Bremen 2010 V1

Choice for Full-scale?

ISET 09-09-2009

Page 8: Ts Pws Biogasupgrading Bremen 2010 V1

Choice for Full-scale?

• PWS: Pressurized Water Scrubbing– High energy efficiency– Low operational cost– Low methane slip (but still oxidisable)– Robust system– Most flexible system– No chemicals

Page 9: Ts Pws Biogasupgrading Bremen 2010 V1

Flash vessel

Pump

CompressorH2S removal

Absorber

Stripper

Air blower

Dryer

Snelkoppeling naar proces technologie op 'Dirkse01' (R).lnk

Chiller

4 Innovative improvements

Page 10: Ts Pws Biogasupgrading Bremen 2010 V1

• Sterilization biogas at compressor (160ºC)

• UV disinfection circulation water

• Dehydration Dryer unit

• Hepa filter Last defence

Bacteria barriers.

Bacteria defense system

DMT-TS-PWS®

Page 11: Ts Pws Biogasupgrading Bremen 2010 V1

H2S + O2 =>

H2SO4

T=30C

pH= 0.5-1.5

Biological desulphurization

DMT-TS-PWS®

No Chemical use!

Page 12: Ts Pws Biogasupgrading Bremen 2010 V1

power

Power

15kWe

cooling

52.5 kWq

Heat 67.5 kWq

Heat Pump technology

Chiller

DMT-TS-PWS®

Heat pump

Page 14: Ts Pws Biogasupgrading Bremen 2010 V1

•Quadruple integrated Bacterial barrier.

•Desulphurization without chemical consumption

• >100% energy efficiency

•Eliminating CO2 emmisions

“Making pressurized water scrubbing

the ultimate biogas upgrading technology

Page 15: Ts Pws Biogasupgrading Bremen 2010 V1

Plant Examples

Page 16: Ts Pws Biogasupgrading Bremen 2010 V1
Page 17: Ts Pws Biogasupgrading Bremen 2010 V1

Utilisation of Biogas

Page 18: Ts Pws Biogasupgrading Bremen 2010 V1

“Making pressurized water scrubbing

the ultimate biogas upgrading technology

with the DMT TS-PWS® system” R. Lems M.Sc. , R&D Manager

DMT Environmental Technology: [email protected]

Page 19: Ts Pws Biogasupgrading Bremen 2010 V1
Page 20: Ts Pws Biogasupgrading Bremen 2010 V1
Page 21: Ts Pws Biogasupgrading Bremen 2010 V1
Page 22: Ts Pws Biogasupgrading Bremen 2010 V1

PSA MS CL CA PWS TS-PWS® unit Energy consumption 0.22-0.25 0.5 0.3-0.4 0.3-0.4 0.2-0.3 0.26 kWh/m3 upgraded Energy ef ficiency 96-97 80-85 91-92 91-92 95-96 >100 % Methane slip 1-3 10-20 0.5-0.8 0.1-0.2 0.6-0.8 <0.001 % Upgraded gas quality 98 90-95 98 99 98 98 % CH4 CO2 recovery No No GH No GH FG No, GH, FG Chemical use AC/MS Water/SH/AC AC Cat/water/AC Water/ S Water/ S Ease of operation + +/- + /- + ++ ++ -, +/-, + , ++ Flexibilit y - +/- + /- + ++ ++ -, +/-, + , ++ References + - - + ++ ++ -, +/-, + , ++ Operational cost 0.26 0.3-0.5 0.4 0.35 0.25 0.18 Euro/m3 upgraded Investment costs 1.3-1.4 >1.5 1.4-1.5 1.1-1.3 0.8 1.2-1.3 Milj. euro

550Nm3/hr biogas 65% CH4

Page 23: Ts Pws Biogasupgrading Bremen 2010 V1

Direct catalytic regenerative oxidation

99.9% removal of CH4 + H2S

Heat recovery from the CH4

CH4 emision controlDMT-TS-PWS®

Page 24: Ts Pws Biogasupgrading Bremen 2010 V1

Plant examplesPicture 6