Identifikasi laju reaksi penyisihan timbal, tembaga, amonia, dan liniear alkil benzen sulfonat dalam limbah cair melalui proses hibrida ozonasi dan filtrasi membran = Identification of degradation rate of lead, copper, ammonia, and linear alkyl benzene sulfonate in wastewater through ozone and membrane filtration hybrid process
| Main Author: | Deni Firmansyah, author |
|---|---|
| Format: | Bachelors |
| Terbitan: |
Fakultas Teknik Universitas Indonesia
, 2011
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| Subjects: | |
| Online Access: |
http://lib.ui.ac.id/file?file=digital/20289548-S896-Identifikasi laju.pdf |
| ctrlnum |
20289548 |
|---|---|
| fullrecord |
<?xml version="1.0"?>
<dc schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd"><title>Identifikasi laju reaksi penyisihan timbal, tembaga, amonia, dan liniear alkil benzen sulfonat dalam limbah cair melalui proses hibrida ozonasi dan filtrasi membran = Identification of degradation rate of lead, copper, ammonia, and linear alkyl benzene sulfonate in wastewater through ozone and membrane filtration hybrid process</title><creator>Deni Firmansyah, author</creator><type>Thesis:Bachelors</type><place/><publisher>Fakultas Teknik Universitas Indonesia</publisher><date>2011</date><description>[<b>ABSTRAK</b><br>
Penyisihan bahan kimia berbahaya dari limbah cair dapat dilakukan dengan berbagai cara, salah satunya adalah dengan menggunakan filtrasi membran. Masalah utama pada filtrasi membran adalah sering terjadinya fouling. Untuk mengatasinya dapat dilakukan dengan menggunakan proses pretreatment dengan ozonasi. Dari hasil identifikasi laju reaksi penyisihan terhadap data-data penelitian sebelumnya, dengan metode pendekatan hukum pangkat sederhana, didapatkan bahwa nilai konstanta laju reaksi penyisihan dengan proses gabungan ozonasi dan filtrasi membran pada tingkat 1 sampai tingkat 3 masing ? masing sebesar: 3 x 108/M2.s, 1,5 x 109/M2.s, dan 2 x 109/M2.s untuk timbal; 4,19 x 104/M2.s, 3 x 10-8 M/s, dan 5 x 106/M2.s untuk tembaga; 3 x 10-8 M/s, 3,486/M2.s, dan 2,8315/M2.s untuk amonia; serta 7,7 x 104/M2.s, 5,6 x 10-2/M0.5.s, dan 0,11/M0,5.s untuk linier alkil benzen sulfonat.
<hr>
<b>ABSTRACT</b><br>
Degradation of hazardous chemicals from the wastewater can be done in various ways, one of them is by using membrane filtration. The main problem in membrane filtration is a frequent occurrence of fouling. To overcome this can be done by using apretreatment process with ozonasi. From the results of the identification of degradation rate of previous research data, with a simple power ? law approach, it was found that the degradation rate constant value with a ozonation and membrane filtration hybrid process at level 1 to level 3, each for: 3 x 108/M2.s, 1.5 x 109/M2.s, and 2 x 109/M2.s for lead; 4.19 x 104/M2.s, 3 x 10-8 M/s, and 5 x 106/M2.s for copper; 3 x 10-8 M/s, 3.486/M0.5.s, and 2.8315/M2.s for ammonia; and 7.7 × 104/M2.s, 5.6 x 10-2/M0.5.s, and 0.11/M0.5.s for linear alkyl benzene sulfonate. , Degradation of hazardous chemicals from the wastewater can be done in various ways, one of them is by using membrane filtration. The main problem in membrane filtration is a frequent occurrence of fouling. To overcome this can be done by using apretreatment process with ozonasi. From the results of the identification of degradation rate of previous research data, with a simple power ? law approach, it was found that the degradation rate constant value with a ozonation and membrane filtration hybrid process at level 1 to level 3, each for: 3 x 108/M2.s, 1.5 x 109/M2.s, and 2 x 109/M2.s for lead; 4.19 x 104/M2.s, 3 x 10-8 M/s, and 5 x 106/M2.s for copper; 3 x 10-8 M/s, 3.486/M0.5.s, and 2.8315/M2.s for ammonia; and 7.7 × 104/M2.s, 5.6 x 10-2/M0.5.s, and 0.11/M0.5.s for linear alkyl benzene sulfonate. ]</description><subject>Sewage disposal</subject><identifier>20289548</identifier><source>http://lib.ui.ac.id/file?file=digital/20289548-S896-Identifikasi laju.pdf</source><recordID>20289548</recordID></dc>
|
| format |
Thesis:Bachelors Thesis |
| author |
Deni Firmansyah, author |
| title |
Identifikasi laju reaksi penyisihan timbal, tembaga, amonia, dan liniear alkil benzen sulfonat dalam limbah cair melalui proses hibrida ozonasi dan filtrasi membran = Identification of degradation rate of lead, copper, ammonia, and linear alkyl benzene sulfonate in wastewater through ozone and membrane filtration hybrid process |
| publisher |
Fakultas Teknik Universitas Indonesia |
| publishDate |
2011 |
| topic |
Sewage disposal |
| url |
http://lib.ui.ac.id/file?file=digital/20289548-S896-Identifikasi laju.pdf |
| contents |
[<b>ABSTRAK</b><br>
Penyisihan bahan kimia berbahaya dari limbah cair dapat dilakukan dengan berbagai cara, salah satunya adalah dengan menggunakan filtrasi membran. Masalah utama pada filtrasi membran adalah sering terjadinya fouling. Untuk mengatasinya dapat dilakukan dengan menggunakan proses pretreatment dengan ozonasi. Dari hasil identifikasi laju reaksi penyisihan terhadap data-data penelitian sebelumnya, dengan metode pendekatan hukum pangkat sederhana, didapatkan bahwa nilai konstanta laju reaksi penyisihan dengan proses gabungan ozonasi dan filtrasi membran pada tingkat 1 sampai tingkat 3 masing ? masing sebesar: 3 x 108/M2.s, 1,5 x 109/M2.s, dan 2 x 109/M2.s untuk timbal; 4,19 x 104/M2.s, 3 x 10-8 M/s, dan 5 x 106/M2.s untuk tembaga; 3 x 10-8 M/s, 3,486/M2.s, dan 2,8315/M2.s untuk amonia; serta 7,7 x 104/M2.s, 5,6 x 10-2/M0.5.s, dan 0,11/M0,5.s untuk linier alkil benzen sulfonat.
<hr>
<b>ABSTRACT</b><br>
Degradation of hazardous chemicals from the wastewater can be done in various ways, one of them is by using membrane filtration. The main problem in membrane filtration is a frequent occurrence of fouling. To overcome this can be done by using apretreatment process with ozonasi. From the results of the identification of degradation rate of previous research data, with a simple power ? law approach, it was found that the degradation rate constant value with a ozonation and membrane filtration hybrid process at level 1 to level 3, each for: 3 x 108/M2.s, 1.5 x 109/M2.s, and 2 x 109/M2.s for lead; 4.19 x 104/M2.s, 3 x 10-8 M/s, and 5 x 106/M2.s for copper; 3 x 10-8 M/s, 3.486/M0.5.s, and 2.8315/M2.s for ammonia; and 7.7 × 104/M2.s, 5.6 x 10-2/M0.5.s, and 0.11/M0.5.s for linear alkyl benzene sulfonate. , Degradation of hazardous chemicals from the wastewater can be done in various ways, one of them is by using membrane filtration. The main problem in membrane filtration is a frequent occurrence of fouling. To overcome this can be done by using apretreatment process with ozonasi. From the results of the identification of degradation rate of previous research data, with a simple power ? law approach, it was found that the degradation rate constant value with a ozonation and membrane filtration hybrid process at level 1 to level 3, each for: 3 x 108/M2.s, 1.5 x 109/M2.s, and 2 x 109/M2.s for lead; 4.19 x 104/M2.s, 3 x 10-8 M/s, and 5 x 106/M2.s for copper; 3 x 10-8 M/s, 3.486/M0.5.s, and 2.8315/M2.s for ammonia; and 7.7 × 104/M2.s, 5.6 x 10-2/M0.5.s, and 0.11/M0.5.s for linear alkyl benzene sulfonate. ] |
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