SIMULATION OF SULFUR REMOVAL FROM NATURAL GAS CONDENSATE USING OXIDATIVE-EXTRACTIVE DESULFURIZATION METHOD
In the oil and gas production process, apart from hydrocarbons, a number of impurities are produced, including CO2 and sulfur in various concentrations, depending on the conditions and characteristics of the reservoir and the location where the oil and gas is located. In the past, oil or natural...
Saved in:
| Main Author: | |
|---|---|
| Format: | Theses |
| Language: | Indonesia |
| Subjects: | |
| Online Access: | https://digilib.itb.ac.id/gdl/view/59660 |
| Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
| Institution: | Institut Teknologi Bandung |
| Language: | Indonesia |
| Summary: | In the oil and gas production process, apart from hydrocarbons, a number of
impurities are produced, including CO2 and sulfur in various concentrations,
depending on the conditions and characteristics of the reservoir and the location
where the oil and gas is located. In the past, oil or natural gas wells containing
significant amounts of acid gas impurities were considered unprofitable. However,
with the depletion of oil reserves and declining oil production, as well as increasing
domestic oil and gas demand, there is no choice but to process fluids from these
sources to meet the specifications of sales product.
To process sulfur removal from condensate, the common technology is HDS
(Hydrodesulfurization). However, with process requirements such as high
temperature, pressure, and intensive hydrogen consumption, an alternative
technology is needed for this desulfurization. One of them is oxidative-extractive
desulfurization. Technical and economic evaluations to determine the feasibility of
applying on an industrial scale need to be studied further.
The study of oxidative-extractive desulfurization process of sulfur compounds
(represented as dibenzothiophene, DBT) was carried out using H2O2/formic acid
as oxidizing agent and catalyst, as well as extraction with DMF. For a capacity of
1000 bpd of condensate with 1%-wt sulfur, desulfurization was successfully carried
out with sulfur removal of 96.55% and condensate recovery of 99.41%. A
processing fee of 9.14 USD/barrel is required, of which 84% is required for
chemicals. The alternative process configuration for DMF recovery succeeded in
reducing chemical costs by 35.5% and reducing total processing costs by 27.0% to
6.67 USD/barrel. In this alternative process configuration, 95.80% sulfur removal
was achieved with condensate recovery of 99.21%.
|
|---|