biogas upgrading - german international cooperation based in … · 2019. 4. 3. · to, ko, ro...
TRANSCRIPT
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1
Biogas Upgrading
Overview of technologies
Measurement technology for process optimizing
Feeding biogas in the gas grid
Requirements for gas quality
Fiscal Measurement technologies
UNION Instruments
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2
Company
UNION Instruments• Founded 1919 in Karlsruhe• Locations in Karlsruhe and Lübeck
Development and production of measuringdevices• Gas analysis : gas properties, energy• Gas analysis: gas composition• Pressure und temperature recorders (gas and water)
Main customers• Industries: Steel, Glas, Oil and gas)
Worldwide distribution
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Topic3
How can existing plants install biogas upgrading facilities?
Overview of different German technology options for upgrading biogas to
Biomethane
Comparison single level and multi-level methods
Feeding Biomethane into the natural gas grid
requirements on gas quality
Matching measurement technology to optimize product quality and energy
Requirements for the measuring technology of Biogas pipeline injection
according G260/262 related to Energy measurement , Gas quality and Gas
conditioning to pipeline quality
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In an anaerobic environment and with the presence of bacteria, organic material will undergo a physical, chemical and biological Process.
With the right temperature, the bacterial Anaerobic Digestion will take place while converting the complex organic matter into much simpler gaseous compounds.
Anaerobic digestion generates Biogas with a high fraction of CH4 and CO2 and a small portion of some other gases (NH3, H2, H2S, etc.).
Cleaned Biogas (removal of H2S, NH3, dust and water) can be used for power or heat generation on site
General Information Biogas4
Where does it comes from?
What is it?
What can I do with it?
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Biogas qualities5
Component Raw Biogas Landfill gas
Methane CH4 45 - 70 % 35 - 55 %
Hydrogen H2 < 200 ppm 0 – 0,2 %
Carbon Dioxide CO2 30 - 45 % 40 – 60 %
Nitrogen N2 0 - 2 % 2 - 25 %
Oxygen O2 0 - 0.5 % 0 - 6 %
Trace Elements Hydrogen Sulphide H2S < 300 mg/m3 n.a.
Siloxanes SiOx < 100 mg/m³ n.a.
Hydrocarbons CxHy < 100 ppm v n.a.
Water H2O saturated saturated
Energy
CharacteristicsGross Calorific Value HS,N 5.0 – 7,7 kWh/m3 3,8 – 5,5 kWh/m3
(Dry gas) 455 - 710 Btu/ft³ 350 - 550 Btu/ft³
Wobbe Index WS,N 4,77 - 8.4 kWh/m3 3,5 - 6,1 kWh/m3
436 - 770 Btu/ft³ 325 - 560 Btu/ft³
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From biomass to electrical power &
biomethane
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Conventional Direct Electrification Grid Injection & Decentralised Utilisation
Biogas Upgrading
Biogas Production
Biogas
Off-gas
+
Heat Export
Biomethane
Grid
Injection
Biomass
Slurry
CHP On site
CHP
CHP
Power
HeatPower
Heat
Industry & households
CNG Vehicle fuel
Na
tura
l Ga
s
Grid
Advantages:
Better Heat Concept Highest CO2-reduction potential
High energy utilisation Lowest emissions
Highest added value High CHPP-Efficiency
Disadvantages:
× Marginal/No Heat Concept × Low CHP-Efficiency
× High CHP-emissions × Low energy utilisation
× High CHP-methane loss(2-5%)
× Energy wasted
(>30%)
© Schmack Biogas
CNG Vehicle fuel
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Options: Usage of Biogas7
Energy production at
the site
from Raw biogas
Upgrading and gas grid injection Energy production at
the site
from Biomethane
Biogas
CHP Cogeneration
(local)
Power Heat
Heat demand on
site often to low or
non-existent
UpgradingCHP Cogeneration
(local)
High energy
efficiency
Bio natural gas Power Heat
CNG fuel
Gas grid Injection
Heat fuel CHP Cogeneration(local)
Power Heat
High energy efficiency
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Requirements for biogas upgrading
Raw biogas quality must be suitable for upgrading
Oxygen and nitrogen concentrations will increase costs for upgrading
High concentrations of trace components like siloxanes will increase costs for Raw biogas cleaning and gas analyzers
Natural gas grid must be in vicinity
Capacity of the gas grid must be higher than Biomethane production at all times
CNG fuel market must exist
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Biogas upgrading
Flow comparison
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Compression &
CoolingProcess
H2S
Removal
Methane
enrichmentGas Drying Off-Gas treatment prior disposal
Chemical
Scrubber
Bio
gas
8 - 10 bar
0.1 - 0.3 bar
Water
Scrubber
Activated
Carbon
Activated
Carbon
2 or 3-Step
Membrane
Scrubber
ScrubberRegen.
Tower
Regen.
TowerGas Dryer
Water Air Heat
Heat
H2S
Scrubber
Off-Gas
Cleaning
System
Biomethane
Biomethane
Biomethane
Off-Gas
Cleaning
System
Off-Gas
Cleaning
System
PSA3 - 5 bar
Activated
CarbonPSA Biomethane
Off-Gas
Cleaning
SystemMembrane
8 - 16 bar
Gas Dryer
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Flow diagram Evonik Membrane Biogas
upgrading
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CoolingPre-compression
and drying
Particle filter Control filterTemperature
control
Membrane
Stage II
Membrane
Stage I
Membrane
Stage III
TO, KO, RO
Biogas
Gas separation
Pre-treatment
Biogas production
Purification
Off-gas treatment
Compression
CompressorDesulfurization
Biomethane
> 98 % CH4
Off-gas CO2< 0.5 % CH4
Purified gas
0.0 % CH4
option
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Membrane technology11
Function of the highly selective
membrane
Gas permeation using
selective membranes made
from high-performance
polymers
Design of membrane module
Biogas: CH4 + CO2 (feed)
Biomethane: CH4(retentate)
Off-gas: CO2(permeate)
Hollow fiber membranes
Separation of CO2 and CH4based on differing permeation
velocities
CH4 slow
CO2 fastEISENMANN
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Membrane technology12
Gas separation with highly selective membranes
Membrane
Stage II
Membrane
Stage I
Membrane
Stage III
Compressor
Biomethane
> 98 % CH4
Off-gas CO2< 0.5 % CH4
EISENMANN
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Membrane technology13
Machine room – compressor (Ex-II), membrane room – gas separation (Ex-II), gas analysis room,
switch cabinet
10 m
3 m
EISENMANN
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Selexol scrubber14
Schwelm Anlagentechnik GmbH
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Selexol scrubber15
Schwelm Anlagentechnik GmbH
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PSA (pressure swing adsorption)16
Main Characteristics:
Separation through molecular sieve effect.
Biomethane production at elevated pressure CMS regeneration at low pressure.
Selective & simultaneous separation CO2, H2O, H2S, NH3, partially N2 & O2 Operational pressure range 1 – 7 bar
Upgrading process at ambient temperatures 5 – 35°C
CMS fully self-regenerated
Gas molecules:
CH4
N2 / O2
H2O/ H2S
CO2
Carbon
Molecular Sieve
(CMS)
Biogas
Biomethane
Compressor Vacuum Pump
CH4 / CO2 / N2/ O2 / H2O / H2S CO2 / N2/ O2 / H2O / H2S / CH4
% CO2-Biogas
Power needed
kWhel/m³
304050
0,15
0,20
0,25
Carbotech (Viessmann Group)
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PSA (pressure swing adsorption)17
Carbotech (Viessmann Group)
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PSA (pressure swing adsorption)18
Carbotech (Viessmann Group)
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PSA (pressure swing adsorption)19
Carbotech (Viessmann Group)
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Monoethanolamin scrubber20
MT Biomethan
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Monoethanolamin scrubber21
MT Biomethan
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System comparison (1/2)22
Properties of different gas cleaning and methane enrichment technologies
AttributeWater
Scrubbing
Polyglycol
Scrubbing
Amine
Scrubbing
Pressure
Swing
Adsoption
Membrane
Process
Air intake into
Biomethane by
stripper columnyes yes no no No
O2-/N2-
enrichement by
CO2-Removalyes yes yes no yes
CH4-losses medium medium very low medium medium
Product gas post
drying stepyes yes yes no no
H2S-pre cleaning
necessary
no
(yes)yes yes yes yes
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System comparison (2/2)23
AttributeWater
Scrubbing
Polyglycol
Scrubbing
Amine
Scrubbing
Pressure
Swing
Adsorption
Membrane
Process
Overall Utility
demand:
power, water, heat,
cooling water,
activated carbon,
washing medium
medium medium high - No high
Power demand
(kWelectr)
(autarkic System)
~ 0,26-0,32
kW/m3 Raw gas
~ 0,24-0,28kW/m3 Raw gas
~ 0,08-0,12kW/m3 Raw gas
~ 0,16-0,22kW/m3 Raw gas
~ 0,26-0,34kW/m3 Raw gas
Heat demand
(kWtherm)none
~ 0,1kW/m3 Raw gas
~ 0,7 - 0,8kW/m3 Raw gas
none none
CO2-footprint from
utilities
consumption
~114-141
g/m3 Raw gas
~144-153g/m3 Raw gas
~206-293
g/m3 Raw gas
~70-97g/m3 Raw gas
~123-150g/m3 Raw gas
Properties of different gas cleaning and methane enrichment technologies
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System optimisation
frequent reasons of energy losses
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Technical hardware problems in the upgrading facility
Methan losses in the gas compressor (to atmosphere)
Leackages in valves (increase off gas losses)
Wrong process settings
Wrong adjustment of washing liquid flows, temperature and pressures.
Incomplete stripping of CO2 caused by low temperatures in the stripper column
Blockage in the process
Blokage of the adsorber by H2S
Decomposition of the washing liquid (to high temperatures in the stripper
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System optimisation
methane losses
How can we detect methane losses ?
Methan losses can be detected by balancing the
methane flows in the system.
How can we balancing the methane flows ?
For balance we have to measure the flows and
the methane concentrations in the flows.
All measurements for the balance must be
done with a high accuracy.
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Measuring points for system
optimisation (example membrane)
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CoolingPre-compression
and drying
Particle filter Control filterTemperature
control
Membrane
Stage II
Membrane
Stage I
Membrane
Stage III
TO, KO, RO
Biogas
Methane balance
CompressorDesulfurization
Biomethane
> 98 % CH4
Off-gas CO2< 0.5 % CH4
Purified gas
0.0 % CH4
option
Energy and quality
optimisation
Reliability
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Biomethane to grid injection
Typical natural gas qualities
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Component German G260/G262
Gas Pipeline Tariff
TETCO (Texas
Eastern)
Methane CH4 n.a. % > 75 %
Hydrogen H2 < 5 % n.a.
Carbon Dioxide CO2 < 6 % < 3 %
Nitrogen N2 n.a % < 1 %
Oxygen O2 < 3 % < 0.2 %
Trace Elements Hydrogen Sulphide H2S < 5 ppm < 8 ppm
Siloxanes SiOx n.a. n.a.
Water H2ONon condensing under
pipeline conditions
Energy
CharacteristicsLow Calorific Value Hu,N 8,4 – 13,1 kWh/m3 ≈ 9.77 kWh/m3
≈ 967 Btu/ft³
Wobbe Index WS,N 12,8 – 15,7 kWh/m3 n.a. kWh/m3
n.a. Btu/ft³
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Biomethane to grid injection28
Adjustment of Energetic Properties: Wobbe Index and Calorific Value
Addition of LPG / Air / CO2 (if necessary)
Targets to be accomplished for the injection of biomethane into the grid:
Matching Wobbe index and Calorific Value Dew point - gas dryness
CO2-fraction limit (%) Free of dust or any foreign particle
O2 / N2-fraction limit (%) Matching pressure
Trace limits: H2, H2S, Siloxanes, CFHC, etc. Adding odour
kW
h/m
³
MJ/m
³
Defining the Quality of the gas
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Biomethane to grid injection29
Matching the operational pressure:
Type Pressure (bar)
Common Network
Pipelines
Int. Long-Distance Transport Grid 70-120
Local Transmission System (LTS) 7-16-40-70
Medium / Intermediate Pressure 1 - 7
Low Pressure (LP) < 0.075
Monitoring of the Bio-Natural Gas (Conditioned Biomethane)
• Oxygen Monitoring
(redundant, Paramagnetic Sensor)
• Gas quality Adjustment Unit (Calibratable)
• CV, Density and CO2-concentracion is measured • Gas meter (Screw type gas meter)
Biomethane to the Grid InjectionFundamentals
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Biomethane to grid injection30
Biomethane Conditioning & Grid Injection Unit
Gas Grid
Biogas Production & Upgrading
Odorizing
THTLPG / Air
Caloric Value Adjustment
Unit
SAV
Safety Valve
Flow
Calibrated flow measurement
Pressure Control
PCV
Biomethane to the Grid
Biogas Producer / Grid Company
biogas production
biogas upgrading
Overview of the process scheme options
PGC or
Calorimeter
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Energy metering system
Raw biogas
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CWD2005 CT
Biogas
Flow computer
VCC
flow
mete
r
Encoder 1Vb
T
Heated cabinet
Modbus
RS232
Modem
GSM
Archivemaintenance
(CL)
Modbus(RS232)
Gas p
ipelin
e
Heated line 6 mm
EX
barriere
K920
ESS
Encoder 2Heating value
SNK 971
Insolation Signaling cable
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Energy metering of Raw biogas
calorimeter solution
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Heated cabinet with calorimeterand flow computer
Ultrasonic Flowmeter with fow computer
Designed to measure wet gases
up tp water dewpoint of 40°C
High accurate calorimeter
measurement better 0,5% of
reading
Automatic calibration
8 years calibration period of flow
meter
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Engergy metering system
NDIR solution
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NDIR analyzer in heated cabinet (50°C) Eenergy metering control panelINCA analyzer control panel
Ultrasonic Flowmeterpressure and temperature sensors
Designed to measure wet gases
up tp water dewpoint of 45°C
Cross sensitivity detection by dual
wavelength NDIR measurement
Automatic calibration with air and
methane
8 years calibration period of flow
meter
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Gas measureing technologies
Calorimeter
Direct energy measuring principle by burning the gas
Gaschromatograph
Selective gas analysis by using adsorption an desorption
properties in seperation columns
NDIR sensors
Determination of gas concentrations by measuring the
absorption of light in a defined spectral range
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Fiscal natural gas analyzer
Calorimeter (BTU analyzer) prinziple
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Fuel gas
Cooling air
Cooling air + flue gasDry Calorimeter
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Calorimeter CWD2005 CT36
Direct BTU measurement
No cross sensitivities
Fiscal approval for Natural gas
and Biomethane
One gas calibration
Measured values
Wobbe index
Specific gravity
Calculated values
Heating value
Air demand
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Gaschromatograph Sitrans CV37
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Sitrans CV
Geräteaufbau
38
Analytic module
Communication &
Energy
Gas supply & probe
Control
module
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Siemens Sitrans CV
Analysemodul
39
Live-Switching
Columns
Ofen
Detector
Detector
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Siemens Sitrans CV40
Analytical configuration and seperation of components
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NDIR – non dispersive infrared41
Measurement principle:
Measuring the absoption in a defined spectral range
heated
chamber
input
filter + receiver
reference
IR-source
output
filter + receiver
signal
pressure
sensor
Detection Range
CH4 0 - 100 vol.-%
CO2 0 - 100 vol.-%
C2+
(CxHy)
0 - 15 vol.-%
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NDIR – non dispersive infrared
cross sensitivity detection
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2.50 2.86 3.33 4.00 5.00 6.66 10.00 20.00
100
80
60
40
20
0
Wavelength [mm]
Tra
nsm
issio
n
[%]
MethanEthanPropanButanMeasurement
range 13.5 [mm]
Measurement range 27.9 [mm]
Principle:
Detection of cross sensitivities by measuring in different spectral ranges.
A drift between the values indicates a cross sensitivity in the process or
calibration gas.
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UNION Instruments GmbH
Zeppelinstraße 42
76185 Karlsruhe
www.union-instruments.com
http://www.union-instruments.com/
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List of manufacturer Biomethane facilities44
Water scrubber Amin scrubber PSAMembrane
technology
• Greenlane
(Flotech)
• Malmberg
• Cirmac
• Purac
(Läckaby Water)
• MT Biomethan
• Strabag AG
• Bilfinger EMS
• Carbotech
• ETW Energietechnik
GmbH
• Mahler AGS
• Eisenmann
• Himmel Gastechnik
• Methapower Biogas
GmbH
• Pentair Haffmans
• MT Biomethane
• Borsig Membrane
Technology GmbH
• Air Liquide
• Envitec Biogas
• Cirmac