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Delft University of Technology

N2KWH

from pollutant to power

van Linden, Niels; Spanjers, H.; van Lier, Jules

Publication date 2016

Document Version Final published version

Citation (APA)

van Linden, N., Spanjers, H., & van Lier, J. (2016). N2KWH: from pollutant to power. Poster session presented at PhD Energy Event, Delft, Netherlands.

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Pre- treat-ment Residual water: High N, Low C Concentrated NH3 NH3 Fuel Concentration techniques SOFC

Research Track E Research Track A Research Track B

Research Track D Effluent water: Low N, Low C Gas production techniques Electrical energy Thermal energy Research Track C NH3 Fuel Electrons N2 + H2O NH3 cracking H2 oxidation O2 reduction O2 depleted air Air O 2-migration Electrolyte Anode Cathode

Electrical energy production

Thermal energy production

Delft, October 2016

From pollutant to power

N2

k

W

h

Contact information

PhD Researcher:

Ir. Niels van Linden

N.vanLinden@tudelft.nl

Co-promotor:

Dr. ir. Henri Spanjers

Promotor:

Prof. dr. ir. Jules van Lier

Project timeline:

April 2016 — April 2020

Research steps

Research Track A: Selection of most suitable technique to concentrate NH3

Research Track B: Evaluation of SOFC performance on the produced NH3 fuel

Research Track C: Selection of most suitable technique produce gaseous NH3

Research Track D: Development of a mass and energy balance tool, in order

to evaluate various scenarios

Research Track E: Implementation of the system and determine the required

pre-treatment for various residual water streams

Faculty: Civil Engineering and Geosciences

Address: Stevinweg 1

2628 CN Delft

The Netherlands

Department: Watermanagement

Section: Sanitary Engineering

sanitaryengineering.tudelft.nl

Introduction to research

N2

k

W

h

Research

Research objective

Development of an energy producing system to remove NH3 from high N, low C

residual (waste) water streams using a SOFC: the energy that is required to produce the fuel should be lower than the energy produced from the fuel.

Problem description

Ammonia (NH3) is world’s second most produced chemical and is a vital resource for protein production. NH3

becomes present in residual (waste) water streams, for example after protein degradation by organisms, and is considered a pollutant for aqueous environments, because it potentially leads to algae blooming.

To this extend, NH3 must be removed from residual water streams, before the water is discharged. Current

methods applied in waste water treatment plants (WWTP), consume significant amount of energy: aeration (to facilitate (de-)nitrification) accounts for approximately 50-70% of the total energy usage of a WWTP2.

Paradigm shift

When the NH3 can be recovered as fuel from residual water stream, energy can be

pro-duced in stead of used in order to remove NH3. This might lead to a paradigm shift:

from pollutant to power.

NH

3

in SOFC

SOFC

A Solid Oxide Fuel Cell (SOFC) is a specific type of fuel, made of solid ceramic materials. In a SOFC, H2is oxidized by

O2, resulting in a current of electrons, which can be utilized

as electrical energy. Additionally, the residual released ener-gy can partially be utilized as thermal enerener-gy.

The electrical efficiency of a SOFC is 50%, whereas the total energy efficiency can reach up to 85-90%, in case of thermal energy utilization3.

Because a SOFC operates at temperatures of T = 600 — 800 [°C], NH3 can be cracked internally into H2, making it

possi-ble to use NH3 directly as a fuel.

Available elec.

energy:

3.7 kWh/kg-NH

3

2Beck, M. B., & Speers, A. (2006). 2nd IWA Leading-Edge on Sustainability in Water-Limited Environments: IWA Publishing.

NH

3

as Fuel

Cathode reaction

O2 reduction: 1/2 O2 + 2e- —> O2-

Anode reactions

NH3 cracking: NH3 —> 1/2 N2 + 3/2 H2

Complete NH3 cracking at T > 450 [°C], in the presence of a nickel catalyst

H2 oxidation: H2 + O2- —> H2O + 2e-

Overall reaction

NH3 oxidation: NH3 + 3/4 O2 —> 3/2 H2O + 1/2 N2

Reactants Products (exhaust)

Used elec.

energy

2

:

3.1 kWh/kg-NH

3

Research plan

1Environmental Dynamics International (2011). Aeration Efficiency Guide

Cytaty

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