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HIDROCRACKING MINYAK JARAK PAGAR DENGAN KATALIS Ni-ZEOLIT ALAM AKTIF SEBELUM DAN SESUDAH REGENERASI

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Penilaian

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Hydrocracking of Jatropha crude oil was conducted using Ni-active natural zeolite catalyst before and after regeneration. Hydrocracking temperature varied 200°C, 350°C, 450°C, and 550°C, the flow of hydrogen gases 4 mL/min, and the weight of Ni-active natural zeolite catalyst was 5 g, and the volume of Jatropha crude oil was 40 mL. The catalyst which has used afterwards was regenerated with two method calcination and the calcination of oxidationreduction. The hydrocracking product of jatropha crude oil was analysed including viscosity and density, and the Ni-active natural zeolite catalyst before and after regeneration be measured acidity. The result showed the best value of viscosity and density for hydrocracking temperature at 550°C was 0.0293 poise and 0.8619 g/mL. The acidity before used was 3.3674 mmol/gr, after it was used the acidity value on hydrocracking temperature 550°C was 0.8567 mmol/g. The catalyst was regenerated with calcination has acidity value 1.1204 mmol/g. Whereas calcination of oxidation-reduction regeneration has acidity value 1.5973 mmol/g. The Ni- active natural zeolite catalyst after regeneration as caltination of oxidation-reduction was reused in hydrocracking process on temperature 550°C produced the product with best value of viscosity and density were 0.0188 poise and 0.8302 g/mL.

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Availability

Inventory Code	Barcode	Call Number	Location	Status
1207001739	T65315	T653152012	Central Library (Referens)	Available but not for loan - Not for Loan

Detail Information

Series Title

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Call Number

T653152012

Publisher

Inderalaya : Jurusan Kimia Fakultas Matematika dan Ilmu Pengetahuan Alam., 2012

Collation

xv, 50 hlm.: Ilus., tab.; 28 cm

Language

Indonesia

ISBN/ISSN

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Classification

541.395 07

Content Type

Text

Media Type

unmediated

Carrier Type

unspecified

Edition

-

Subject(s)

Kimia
Minyak Jarak

Specific Detail Info

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Statement of Responsibility

HALIM

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