Adsorptive removal of natural organic matter during drinking water treatment

S. G.J. Heijman; A. M. Van Paassen; W. G.J. Van Der Meer; R. Hopman

doi:10.1016/S0273-1223(99)00655-1

Adsorptive removal of natural organic matter during drinking water treatment

S. G.J. Heijman^*, A. M. Van Paassen, W. G.J. Van Der Meer, R. Hopman

^*Corresponding author for this work

Research output: Contribution to journal › Conference article › Academic › peer-review

44 Citations (Scopus)

Abstract

For the removal of DOC (and colour) several treatment steps are suggested. If it is also necessary to remove hardness nanofiltration is probably the first choice. For colour removal without softening a number of adsorbents are suggested in the literature. In order to estimate the costs of these treatment steps a dynamic column model based on batch experiments was used to predict the service time of the columns filled with different adsorbents. Also the (on site) regeneration of the different adsorbents was investigated in batch experiments. Especially the ion exchange resin was very promising. The costs of the treatment of one m³ water with a column filled with an ion exchange resin was estimated for the investigated case at 0.05 Euro.

Original language	English
Pages (from-to)	183-190
Number of pages	8
Journal	Water science and technology
Volume	40
Issue number	9
DOIs	https://doi.org/10.1016/S0273-1223(99)00655-1
Publication status	Published - 1999
Externally published	Yes
Event	Proceedings of the 1999 IAWQ-IWSA International Conference on 'Removal of Humic Substances from Water' - Trondheim, Norway Duration: 24 Jun 1999 → 26 Jun 1999

Keywords

Adsorption
Colour
Column model
Costs
DOC
Removal

UN SDGs

This output contributes to the following UN Sustainable Development Goals (SDGs)

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10.1016/S0273-1223(99)00655-1

Cite this

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title = "Adsorptive removal of natural organic matter during drinking water treatment",

abstract = "For the removal of DOC (and colour) several treatment steps are suggested. If it is also necessary to remove hardness nanofiltration is probably the first choice. For colour removal without softening a number of adsorbents are suggested in the literature. In order to estimate the costs of these treatment steps a dynamic column model based on batch experiments was used to predict the service time of the columns filled with different adsorbents. Also the (on site) regeneration of the different adsorbents was investigated in batch experiments. Especially the ion exchange resin was very promising. The costs of the treatment of one m3 water with a column filled with an ion exchange resin was estimated for the investigated case at 0.05 Euro.",

keywords = "Adsorption, Colour, Column model, Costs, DOC, Removal",

author = "Heijman, {S. G.J.} and {Van Paassen}, {A. M.} and {Van Der Meer}, {W. G.J.} and R. Hopman",

year = "1999",

doi = "10.1016/S0273-1223(99)00655-1",

language = "English",

volume = "40",

pages = "183--190",

journal = "Water science and technology",

issn = "0273-1223",

publisher = "IWA Publishing",

number = "9",

note = "Proceedings of the 1999 IAWQ-IWSA International Conference on 'Removal of Humic Substances from Water' ; Conference date: 24-06-1999 Through 26-06-1999",

}

TY - JOUR

T1 - Adsorptive removal of natural organic matter during drinking water treatment

AU - Heijman, S. G.J.

AU - Van Paassen, A. M.

AU - Van Der Meer, W. G.J.

AU - Hopman, R.

PY - 1999

Y1 - 1999

N2 - For the removal of DOC (and colour) several treatment steps are suggested. If it is also necessary to remove hardness nanofiltration is probably the first choice. For colour removal without softening a number of adsorbents are suggested in the literature. In order to estimate the costs of these treatment steps a dynamic column model based on batch experiments was used to predict the service time of the columns filled with different adsorbents. Also the (on site) regeneration of the different adsorbents was investigated in batch experiments. Especially the ion exchange resin was very promising. The costs of the treatment of one m3 water with a column filled with an ion exchange resin was estimated for the investigated case at 0.05 Euro.

AB - For the removal of DOC (and colour) several treatment steps are suggested. If it is also necessary to remove hardness nanofiltration is probably the first choice. For colour removal without softening a number of adsorbents are suggested in the literature. In order to estimate the costs of these treatment steps a dynamic column model based on batch experiments was used to predict the service time of the columns filled with different adsorbents. Also the (on site) regeneration of the different adsorbents was investigated in batch experiments. Especially the ion exchange resin was very promising. The costs of the treatment of one m3 water with a column filled with an ion exchange resin was estimated for the investigated case at 0.05 Euro.

KW - Adsorption

KW - Colour

KW - Column model

KW - Costs

KW - DOC

KW - Removal

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U2 - 10.1016/S0273-1223(99)00655-1

DO - 10.1016/S0273-1223(99)00655-1

M3 - Conference article

AN - SCOPUS:0032746398

SN - 0273-1223

VL - 40

SP - 183

EP - 190

JO - Water science and technology

JF - Water science and technology

IS - 9

T2 - Proceedings of the 1999 IAWQ-IWSA International Conference on 'Removal of Humic Substances from Water'

Y2 - 24 June 1999 through 26 June 1999

ER -

Adsorptive removal of natural organic matter during drinking water treatment

Abstract

Keywords

UN SDGs

Access to Document

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