09.01.2013 Views

Proceedings World Bioenergy 2010

Proceedings World Bioenergy 2010

Proceedings World Bioenergy 2010

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

BIOGAS UPGRADING BY TEMPERATURE SWING ADSORPTION<br />

Tamara Mayer, Michael Url, Hermann Hofbauer<br />

Institute of Chemical Engineering, Vienna University of Technology<br />

Getreidemarkt 9/166, 1060 Vienna, Austria<br />

Phone: +43 1 58801 15901, Fax: +43 1 58801 15999, Mail: tamara.mayer@tuwien.ac.at<br />

ABSTRACT: This paper presents a novel process for biogas upgrading by means of temperature swing adsorption.<br />

Temperature swing adsorption process experiments were carried out in a laboratory test rig focusing on the process<br />

step of desorption. Desorption experiments were performed using three different variations of regeneration. Further<br />

on, performance and efficiency of the applied desorption variations were investigated. As a result, desorption by any<br />

combination of direct and indirect heating is considered as the best and most efficient way. Referring to the<br />

adsorption step, separation performance is excellent, carbon dioxide is fully adsorbed and pure methane can be<br />

obtained.<br />

Keywords: biogas, upgrading, adsorbents<br />

1 INTRODUCTION<br />

Natural gas had a share of 24% in the gross energy<br />

consumption of the EU-27 in the year 2007. Therefore<br />

Europe’s dependence on natural gas can be considered as<br />

quite high. Due to the fossil origin of natural gas, it has<br />

two drawbacks. First, it will for sure run out at some<br />

point in the future and second, emissions deriving from<br />

natural gas are not carbon neutral but they affect the<br />

climate involving the whole issue of green house gas<br />

emissions and global warming. For these two reasons<br />

alternatives for natural gas have to be found and biogas<br />

represents one option thereby.<br />

Biogas is a renewable energy source deriving from<br />

anaerobic digestion of organic matter. If biogas should<br />

replace natural gas, it has to possess a certain quality<br />

similar to natural gas. In order to achieve this quality and<br />

to obtain gas which is suitable for replacing natural gas,<br />

biogas must be upgraded.<br />

This paper investigates a novel process for biogas<br />

upgrading based on the principle of temperature swing<br />

adsorption (TSA).<br />

2 OVERVIEW OF BIOGAS UPGRADING<br />

TECHNOLOGIES<br />

Biogas typically consists of about two thirds methane<br />

balanced by about one third carbon dioxide and<br />

impurities such as hydrogen sulphide [1]. Moreover,<br />

biogas is usually saturated with water when leaving the<br />

anaerobic digestion plant. If biogas should be injected<br />

into the natural gas grid, it needs to exhibit a certain<br />

quality similar to natural gas which consists mainly of<br />

methane. Hence, gas components such as carbon dioxide<br />

and hydrogen sulphide have to be removed from biogas<br />

in order to obtain a high amount of methane.<br />

The entire process of biogas upgrading roughly<br />

comprises separation of water and hydrogen sulphide as<br />

well as methane enrichment.<br />

2.1 Overview<br />

Among currently available biogas upgrading<br />

technologies, water scrubbing and pressure swing<br />

adsorption are clearly the two most applied ones [2] and<br />

they can therefore be classified as state of the art for<br />

biogas upgrading. Other technologies like chemical or<br />

organic physical absorption processes along with<br />

membrane based techniques are in an advanced state of<br />

development or even under demonstration. Although<br />

there are established technologies, which are already well<br />

developed and going to be continuously improved and<br />

optimized, innovative technologies find their way. These<br />

emerging biogas upgrading technologies include for<br />

instance cryogenic upgrading or in situ methane<br />

enrichment.<br />

Comprehensive reviews of biogas upgrading<br />

technologies and further related information are given<br />

elsewhere (e.g. in [3] or [4]).<br />

2.2 Comparison of biogas upgrading technologies<br />

Biogas upgrading processes can be categorized into<br />

wet and dry processes depending on whether a liquid<br />

phase is required or not. Accordingly, all kinds of<br />

absorption processes are related to wet processes whereas<br />

dry processes involve adsorption processes and<br />

membrane processes like gas permeation. Wet biogas<br />

upgrading processes are characterized by the need of a<br />

liquid such as water or organic solvents in order to<br />

perform removal of carbon dioxide along with further<br />

undesired components. Disadvantages deriving from<br />

utilization of any kind of liquid are on the one hand the<br />

need of disposal and on the other hand possible treatment<br />

of the liquid before disposal. Moreover, wet processes<br />

require drying of the upgraded gas before it leaves the<br />

plant, what represents an additional process step<br />

compared to dry processes. However, pressure swing<br />

adsorption processes use activated carbon beds as guard<br />

filter for protection of the actual adsorbent which is a<br />

carbon molecular sieve. This process configuration<br />

causes the need of disposal of saturated activated carbon.<br />

Furthermore, biogas upgrading processes can be<br />

categorized according to the need of pressurization of<br />

raw gas. Correspondingly, the processes of pressure<br />

swing adsorption, water scrubbing, organic physical<br />

scrubbing as well as gas permeation require the raw gas<br />

to be compressed in order to perform the upgrading.<br />

On the contrary, chemical scrubbing with amines and<br />

the temperature swing adsorption process presented in<br />

this paper are so called pressure less processes. Further<br />

similarities of these two processes are utilization of<br />

amines as sorbent, low methane losses during the process<br />

and high methane content in the upgraded gas (98% or<br />

even above) because of excellent selectivity of the amine<br />

for carbon dioxide. However, there are differences<br />

concerning regeneration of saturated amines. Regarding<br />

world bioenergy <strong>2010</strong><br />

79

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!