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Biogas upgrading – Review of commercial technologies - SGC

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<strong>SGC</strong> Rapport 2013:270<br />

2.1.3 Investment and consumables<br />

To be able to get up-to-date information regarding consumables, investment cost<br />

and supplier interface with customers a supplier <strong>of</strong> amine-based biogas purification<br />

systems has been interviewed. The supplier has three standard sizes that<br />

they <strong>of</strong>fer to the Swedish market and two that they <strong>of</strong>fer to the German market.<br />

The differences between the markets are mainly on the feed used for the fermentation,<br />

resulting in a significantly higher CO2 level in the German digester gas. But<br />

there are also differences with respect to supply pressure requirements etc.<br />

The systems have a nameplate capacity <strong>of</strong> 600, 900 and 1 800 Nm 3 /h <strong>of</strong> inlet<br />

raw biogas for the Swedish market and 700 and 1 400 Nm 3 /h <strong>of</strong> inlet raw biogas<br />

for the German market. The design value with respect to CO2 concentration in the<br />

inlet gas is 60% in the Swedish case and 50% in the German case. The systems<br />

are designed to have a certain turndown as per Table 8. These values are <strong>of</strong><br />

course dependent on the inlet conditions such that they depend on the inlet level<br />

<strong>of</strong> CO2, as an example the Swedish systems accept a methane content ranging<br />

from 55% to 70%. The systems are designed to handle a maximum 300 ppm H2S<br />

in the incoming gas.<br />

Table 8 Turndown ratio <strong>of</strong> standard amine scrubbing units for biogas <strong>upgrading</strong><br />

available at the Swedish market.<br />

Capacity raw biogas<br />

(Nm 3 Lowest flow rate<br />

/h)<br />

(Nm 3 Highest flow rate<br />

/h)<br />

(Nm 3 /h)<br />

600 100 700<br />

900 300 1 000<br />

1 800 800 2 000<br />

In the delivery, there are certain guarantee values with respect to water consumption,<br />

electricity, methane slip and chemicals. The water consumption is specified to<br />

0.00003 m 3 /Nm 3 raw biogas. Electricity is slightly dependent on where in the operating<br />

window the units are operating, with the lowest consumption at the highest<br />

load (0.12 kWh/Nm 3 raw biogas) and the highest at the lowest load (0.14 kWh/Nm 3<br />

raw biogas). Further, the stripper column requires heat to regenerate the amine,<br />

this heat demand is approximately 0.55 kwh//Nm 3 raw biogas. The methane slip<br />

based on third party measurements is 0.06% (99.94% <strong>of</strong> the inlet methane exit as<br />

product) and the guarantee value is set to 0.1%. With respect to chemicals (antifoam,<br />

amine make-up) the consumption is guaranteed at 0.00003 kg/Nm 3 raw biogas<br />

With respect to the investment cost, the systems vary with size and there is an 8<br />

MSEK difference between the smallest and the largest system. In the investment<br />

cost the gas purification unit including transport, commissioning, heat recovery<br />

system, analysis equipment and a guaranteed 96% availability is included. Service<br />

contracts are <strong>of</strong>fered, but at an additional cost (annually around 3% <strong>of</strong> the investment<br />

cost). The specific investment costs may be viewed in Figure 5. In 2008 the<br />

purification systems were redesigned to modular construction and the investment<br />

cost has not increased since.<br />

20 Svenskt Gastekniskt Center AB, Malmö <strong>–</strong> www.sgc.se

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