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OVERVIEW
Petroextract S.A. with an innovative vision
has developed this project that focuses onharnessing the gas from oil producing wells.
The gas obtained from this process is a clean
gas, with a high octane number which may beused in internal combustion engines.
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For this reason we have developed a bi-fuelsystem that enables the operation of a dieselengine replacing between 40% and 70% ofdiesel by appropriate pretreated gas, asrequired by engine power.
OVERVIEW
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Methane
Ethane
Propane
Iso - butane
N- butane
Iso - pentane
N- pentane
Hexane
The composition of gas entering the plant is afunction of chromatographic analysis thereofwhich essentially contains:
Heptane
Heavyhydrocarbons
Nitrogen
Carbon dioxide
Hydrogen sulfide Water vapor
OVERVIEW
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MTSG- Petroextract
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MODULAR TREATMENT SYSTEM OF GAS
The MTSG can be transported; installed close to the engine
area, connected to the gas line out of separators and treatthe gas, then connecting to the internal combustion enginesto supply them with fuel gas and allow the bi-fuel system to
operate.
The recovered condensate back into the process of the
station.
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MSTG PROCESS DESCRIPTION
The process is divided into three stages described
below:
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CONDENSATION
Liquid separation process
1STAGE
At this stage, the amount of liquids associated with the gasare separated by putting them in contact with the verticalvessel (separator).
The size of the separator will depend on the volume of thegas to be treated, the required period of residence, itsinterior design and the amount of liquid to extract.
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CONDENSATION
Gasoline Recovery
At the first separator liquid streams that are associatedwith gas are removed, as well as heavy hydrocarbons
such as C6, C7, C8, and liquid water.
In a second instance, the gas passes to a heat exchanger(Chiller A) to undergo a cooling process at knownpressures, thus lowers the temperature of gas to get thedew point temperature for both water and pentanes that
are found in vapor form, achieving in this way they cancondense and separate from the gas as a liquid phase
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Propane and butane recovery
2STAGE
In this second stage, the gas that comes from the secondseparator is directed to another heat exchanger (Chiller B) todecrease the temperature and reach the dew point forpropane and butane, so as they can be condensate andseparate from the gas through a separator.
All this cooling process is governed by condensing units (UCA / B / C / D) using ecological refrigerant, they allow us toachieve the parameters we need in the process.
CONDENSATION
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GAS SWEETENING
3STAGE
Gas sweetening is a term used to explain the processwhich removes components that make this gas is acidic
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GAS SWEETENING
The amount used for each of the molecular sieves wascalculated from data of the chromatography which indicatesthe percentage of acid gases entering.
The molecularsieves used are:
Zeolite:remove carbon dioxide (CO2)
Activated alumina:remove hydrogen sulfide (H2S)
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MTSG REAR VIEW
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MTSG FRONT VIEW
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CONSTRUCCION DE STMG DE SHUSHUFINDI, YUCAY GUANTA
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MTSG IN YUCA STATION
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MTSG IN YUCA STATION
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MTSG IN SHUSHUFINDI STATION
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MTSG IN SHUSHUFINDI STATION
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MTSG IN YUCA STATION
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MTSG IN YUCA STATION
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MTSG IN YUCA STATION
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MTS IN YUCA STATION
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MTSG IN YUCA STATION
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MTSG IN SHUSHUFINDI STATION
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MTSG IN SHUSHUFINDI STATION
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MTSG IN SHUSHUFINDI STATION
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MTSG IN SHUSHUFINDI STATION
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