Treatment and reuse of tunnel construction wastewater
Silicate polymerization and formation of colloidal silica resulted in very low flux for raw tunnel construction wastewater. Both initial flux and final flux significantly increased when wastewater was pretreated with CaCl 2 dosage of 1000, 2000, and 3000 mg/L, respectively. It is apparent that chemi...
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Published in | Separation and purification technology Vol. 84; no. 9; pp. 79 - 84 |
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Main Authors | , , , |
Format | Journal Article Conference Proceeding |
Language | English |
Published |
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Elsevier B.V
09.01.2012
Elsevier |
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Online Access | Get full text |
ISSN | 1383-5866 1873-3794 |
DOI | 10.1016/j.seppur.2011.03.033 |
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Abstract | Silicate polymerization and formation of colloidal silica resulted in very low flux for raw tunnel construction wastewater. Both initial flux and final flux significantly increased when wastewater was pretreated with CaCl
2 dosage of 1000, 2000, and 3000
mg/L, respectively. It is apparent that chemical pretreatment markedly enhanced MF of wastewater.
[Display omitted]
► We characterize tunnel construction wastewater as high in turbidity and soluble silica. ► CaCl
2 and MgCl
2 show good removal efficiency. ► Microfiltration following CaCl
2 pretreatment yields higher steady flux. ► The treated effluent needs dilution or polishing before its reuse in concrete mixing.
This study investigated chemical reaction and chemical reaction followed by microfiltration processes for treating synthetic tunnel construction wastewater, which was characterized as high in total suspended solids (2.53
±
0.36
g/L) and in soluble silica (1.41
±
0.20
g/L). The optimal chemical reaction conditions were assessed through jar test apparatus. Experimental results indicated that calcium chloride (CaCl
2) could reduce soluble silica to 187.1
mg/L at pH 8.0 and dosage of 1000
mg/L. The treatment efficiency deteriorated as pH increased, while increasing CaCl
2 dose at pH 8.0 did not enhance removal of silica. Magnesium chloride (MgCl
2) could lower soluble silica concentration to 174.0
mg/L at pH of 8 and 9, and soluble silica concentration decreased further as MgCl
2 dosage increased. Wastewater pretreated with CaCl
2 and MgCl
2 was then subject to microfiltration. Pretreatment by CaCl
2 resulted in higher permeate flux, and moderate flux decline, while pretreatment by MgCl
2 resulted in significant membrane fouling. Increasing transmembrane pressure (TMP) could induce higher initial flux and steady flux. Crossflow velocity did not show significant effect on the permeate flux. The potential reuse of treated effluent is assessed as well. |
---|---|
AbstractList | Silicate polymerization and formation of colloidal silica resulted in very low flux for raw tunnel construction wastewater. Both initial flux and final flux significantly increased when wastewater was pretreated with CaCl
2 dosage of 1000, 2000, and 3000
mg/L, respectively. It is apparent that chemical pretreatment markedly enhanced MF of wastewater.
[Display omitted]
► We characterize tunnel construction wastewater as high in turbidity and soluble silica. ► CaCl
2 and MgCl
2 show good removal efficiency. ► Microfiltration following CaCl
2 pretreatment yields higher steady flux. ► The treated effluent needs dilution or polishing before its reuse in concrete mixing.
This study investigated chemical reaction and chemical reaction followed by microfiltration processes for treating synthetic tunnel construction wastewater, which was characterized as high in total suspended solids (2.53
±
0.36
g/L) and in soluble silica (1.41
±
0.20
g/L). The optimal chemical reaction conditions were assessed through jar test apparatus. Experimental results indicated that calcium chloride (CaCl
2) could reduce soluble silica to 187.1
mg/L at pH 8.0 and dosage of 1000
mg/L. The treatment efficiency deteriorated as pH increased, while increasing CaCl
2 dose at pH 8.0 did not enhance removal of silica. Magnesium chloride (MgCl
2) could lower soluble silica concentration to 174.0
mg/L at pH of 8 and 9, and soluble silica concentration decreased further as MgCl
2 dosage increased. Wastewater pretreated with CaCl
2 and MgCl
2 was then subject to microfiltration. Pretreatment by CaCl
2 resulted in higher permeate flux, and moderate flux decline, while pretreatment by MgCl
2 resulted in significant membrane fouling. Increasing transmembrane pressure (TMP) could induce higher initial flux and steady flux. Crossflow velocity did not show significant effect on the permeate flux. The potential reuse of treated effluent is assessed as well. This study investigated chemical reaction and chemical reaction followed by microfiltration processes for treating synthetic tunnel construction wastewater, which was characterized as high in total suspended solids (2.53+/-0.36g/L) and in soluble silica (1.41+/-0.20g/L). The optimal chemical reaction conditions were assessed through jar test apparatus. Experimental results indicated that calcium chloride (CaCl2) could reduce soluble silica to 187.1mg/L at pH 8.0 and dosage of 1000mg/L. The treatment efficiency deteriorated as pH increased, while increasing CaCl2 dose at pH 8.0 did not enhance removal of silica. Magnesium chloride (MgCl2) could lower soluble silica concentration to 174.0mg/L at pH of 8 and 9, and soluble silica concentration decreased further as MgCl2 dosage increased. Wastewater pretreated with CaCl2 and MgCl2 was then subject to microfiltration. Pretreatment by CaCl2 resulted in higher permeate flux, and moderate flux decline, while pretreatment by MgCl2 resulted in significant membrane fouling. Increasing transmembrane pressure (TMP) could induce higher initial flux and steady flux. Crossflow velocity did not show significant effect on the permeate flux. The potential reuse of treated effluent is assessed as well. This study investigated chemical reaction and chemical reaction followed by microfiltration processes for treating synthetic tunnel construction wastewater, which was characterized as high in total suspended solids (2.53±0.36g/L) and in soluble silica (1.41±0.20g/L). The optimal chemical reaction conditions were assessed through jar test apparatus. Experimental results indicated that calcium chloride (CaCl₂) could reduce soluble silica to 187.1mg/L at pH 8.0 and dosage of 1000mg/L. The treatment efficiency deteriorated as pH increased, while increasing CaCl₂ dose at pH 8.0 did not enhance removal of silica. Magnesium chloride (MgCl₂) could lower soluble silica concentration to 174.0mg/L at pH of 8 and 9, and soluble silica concentration decreased further as MgCl₂ dosage increased. Wastewater pretreated with CaCl₂ and MgCl₂ was then subject to microfiltration. Pretreatment by CaCl₂ resulted in higher permeate flux, and moderate flux decline, while pretreatment by MgCl₂ resulted in significant membrane fouling. Increasing transmembrane pressure (TMP) could induce higher initial flux and steady flux. Crossflow velocity did not show significant effect on the permeate flux. The potential reuse of treated effluent is assessed as well. |
Author | Yi-Wen, Tsai Chia-Ping, Lu Sou-Sen, Leu Liu, J.C. |
Author_xml | – sequence: 1 givenname: Tsai surname: Yi-Wen fullname: Yi-Wen, Tsai organization: Department of Chemical Engineering, National Taiwan University of Science and Technology, 43 Keelung Road, Section 4, Taipei 106, Taiwan – sequence: 2 givenname: J.C. surname: Liu fullname: Liu, J.C. email: liu1958@mail.ntust.edu.tw organization: Department of Chemical Engineering, National Taiwan University of Science and Technology, 43 Keelung Road, Section 4, Taipei 106, Taiwan – sequence: 3 givenname: Leu surname: Sou-Sen fullname: Sou-Sen, Leu organization: Department of Construction Engineering, National Taiwan University of Science and Technology, 43 Keelung Road, Section 4, Taipei 106, Taiwan – sequence: 4 givenname: Lu surname: Chia-Ping fullname: Chia-Ping, Lu organization: Department of Chemical Engineering, National Taiwan University of Science and Technology, 43 Keelung Road, Section 4, Taipei 106, Taiwan |
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CitedBy_id | crossref_primary_10_1080_09593330_2015_1028469 crossref_primary_10_1080_19443994_2015_1049406 crossref_primary_10_11001_jksww_2013_27_6_779 crossref_primary_10_1016_j_biortech_2014_08_107 crossref_primary_10_2166_wst_2023_363 |
Cites_doi | 10.1006/jcis.1997.5209 10.1016/S0011-9164(02)00973-6 10.1016/S0011-9164(00)00138-7 10.1006/jcis.1998.5445 10.1061/(ASCE)0733-9372(2000)126:7(667) 10.1016/j.enggeo.2008.07.012 10.1016/j.memsci.2006.11.004 10.1021/es991054f 10.1006/jcis.1993.1164 10.1016/S0011-9164(02)00264-3 10.1016/j.desal.2007.01.005 10.2166/ws.2006.792 10.1016/j.desal.2009.09.087 10.1061/41039(345)348 10.1016/S0011-9164(01)00297-1 10.1016/j.enggeo.2008.04.002 10.1016/j.desal.2005.09.028 10.1016/j.tust.2005.12.199 |
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Keywords | Microfiltration Tunnel construction Wastewater Grouting Silica Fouling Reuse Crossflow Waste water Membrane separation Chemical reaction pH Pretreatment |
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SubjectTerms | Applied sciences calcium chloride Chemical engineering Chemical reactions Construction Exact sciences and technology Flux fouling General purification processes Grouting magnesium chloride Membrane separation (reverse osmosis, dialysis...) Microfiltration Pollution Reactors Reuse Silica Silicon dioxide total suspended solids Tunnel construction Tunnels (transportation) Waste water Wastewater Wastewaters Water treatment and pollution |
Title | Treatment and reuse of tunnel construction wastewater |
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