![Case 1:Sweet oil (no hydrogen sulfide)
No stabilization is needed.
For this case and assuming that there is a gasoline
plant existing in the facilities (i.e., a plant designed to
recover pentane plus), stabilization could be
eliminated, allowing the stock tank vapors to be
collected [via the vapor recovery unit (VRU)] and sent
directly to the gasoline plant.](https://image.slidesharecdn.com/15542665-240822091800-39b0faec/85/Petroleum-processing-system-outsourcingng-10-320.jpg)
Petroleum processing system outsourcingng
- 1. Treatment of Produced Fluids: Crude Oil Stabilization and Sweetening, storage tanks and produced water treatment By Pn Khairunissa syairah Credit to Pn Azduwin
- 2. Crude Oil Stabilization and Sweetening
- 3. INTRODUCTION • Once degassed and dehydrated–desalted, crude oil is pumped to gathering facilities to be stored in storage tanks. • However, if there are any dissolved gases that belong to the light or the intermediate hydrocarbon groups, it will be necessary to remove these gases along with hydrogen sulfide (if present in the crude) before oil can be stored. • This process is described as a ‘‘dual process’’ of both stabilizing and sweetening a crude oil. • In stabilization, adjusting the pentanes and lighter fractions retained in the stock tank liquid can change the crude oil gravity. • The economic value of the crude oil is accordingly influenced by stabilization.
- 4. Before and After DUAL treatment Before • Water content: up to 3% of crude in the form of emulsions and from 3% to 30% of crude as free water • Salt content: 50,000– 250,000 mg/L formation water • Gas: dissolved gases in varying amounts depending on the gas–oil ratio (GOR) • Hydrogen Sulfide: up to 1000 ppm by weight After • Water content (B.S.&W.): 0.3% by volume, maximum • Salt content: 10–20 lbs salt (NaCl) per 1000 barrels oil (PTB) • Vapor pressure: 5–20 psia RVP (Reid vapor pressure) • H2S: 10–100 ppmw
- 5. API GRAVITY • The American Petroleum Institute gravity, or API gravity • A measure of how heavy or light a petroleum liquid is compared to water. • If its API gravity is greater than 10, it is lighter and floats on water; if less than 10, it is heavier and sinks. • It is referred to as being in 'degrees‘ • Crude oil is classified as light, medium, or heavy according to its measured API gravity. Light crude oil has an API gravity higher than 31.1° Medium oil has an API gravity between 22.3 and 31.1° Heavy crude oil has an API gravity below 22.3° Extra heavy oil has an API gravity below 10.0° • Oil with an API gravity between 40 and 45° commands the highest prices. Above 45°, the molecular chains become shorter and less valuable to refineries
- 6. Sweet and Sour Crude oil • Crude oil is considered ‘‘sweet’’ if the dangerous acidic gases are removed from it. • On the other hand, it is classified as ‘‘sour’’ if it contains as much as 0.05 ft3 of dissolved H2S in 100 gal of oil. Sour crude oil is crude oil containing a high amount of the impurity sulfur • Hydrogen sulfide gas is a poison hazard because 0.1% in air is toxically fatal in 30 min. • Additional processing is mandatory—via this dual operation—in order to release any residual associated gases along with H2S present in the crude.
- 7. Prior to stabilization, crude oil is usually directed to a spheroid for storage in order to reduce its pressure to very near atmospheric
- 8. STABILIZATION OPERATIONS • The crude oil discharged from the last stage in a gas–oil separation plant (GOSP) or the desalter has a vapor pressure equal to the total pressure in the last stage. • Usually, operation of this system could lead to a crude product with a RVP in the range of 4-12 psia. • Most of the partial pressure of a crude comes from the low-boiling compounds, which might be present only in small quantities—in particular hydrogen sulfide and low- molecular-weight hydrocarbons such as methane and ethane. • Stabilization is directed to remove these low-boiling compounds without losing the more valuable components
- 9. STABILIZATION OPERATIONS (Contd.) • The stabilization mechanism is based on removing the more volatile components by (a) Flashing using stage separation and (b) Stripping operations. Two major specifications set for stabilized oil are as follows: • The Reid vapor pressure (RVP) • Hydrogen sulfide content
- 10. Case 1:Sweet oil (no hydrogen sulfide) No stabilization is needed. For this case and assuming that there is a gasoline plant existing in the facilities (i.e., a plant designed to recover pentane plus), stabilization could be eliminated, allowing the stock tank vapors to be collected [via the vapor recovery unit (VRU)] and sent directly to the gasoline plant.
- 11. Case 2: Sour crude Stabilization is a must. For this case, it is assumed that the field facilities do not include a gasoline plant. Basically, either flashing or stripping stabilization is used.
- 12. Stabilization by Flashing (Additional Gas–Oil Separator) • The method utilizes an inexpensive small vessel to be located above the storage tank. • The vessel is operated at atmospheric pressure. • Vapors separated from the separator are collected using a VRU. • This approach is recommended for small-size oil leases handling small volume of fluids to be processed. • The principles underlying the stabilization process are the same as for gas–oil separation.
- 13. Stabilization by Stripping • The stripping operation employs a stripping agent, which could be either energy or mass, to drive the undesirable components out of the bulk of crude oil. • This approach is economically justified when handling large quantities of fluid and in the absence of a VRU. It is also recommended for dual-purpose operations for stabilizing sour crude oil, where stripping gas is used for stabilization. • Stabilizer-column installations are used for the stripping operations.
- 15. CRUDE OIL SWEETENING • The presence of hydrogen sulfide and other sulfur compounds in the well stream impose many constraints. Most important are the following: Personnel safety and corrosion considerations require that H2S concentration be lowered to a safe level. Brass and copper materials are particularly reactive with sulfur compounds; their use should be prohibited. Sulfide stress cracking problems occur in steel structures. Mercaptans compounds(thiol) have an objectionable odor
- 16. CRUDE OIL SWEETENING (contd.) • Three general schemes are used to sweeten crude oil at the production facilities:
- 17. Crude sweetening by stage vaporization with stripping gas
- 18. Crude sweetening by trayed stabilization with stripping gas
- 19. Crude sweetening by reboiled trayed stabilization
- 20. Storage tanks
- 21. INTRODUCTION • The design of storage tanks for crude oil and petroleum products requires,in general, careful consideration of the following important factors: The vapor pressure of the materials to be stored The storage temperature and pressure Toxicity of the petroleum material
- 22. Types of Storage Tank
- 23. Sizing the Storage Tanks 1. To determine the capacity of storage tanks, the following rules apply: (a) For one well, the capacity per storage tank should be adequate enough for at least 2– 3 days’ production. (b) For a group of wells (entire field), the total tank capacity should be adequate enough for at least 3–4 days of oil production by that field.
- 24. Sizing the Storage Tanks(contd.) 2. To determine the number of storage tanks as a function of the number of producing wells. This relationship is represented graphically as below;
- 25. Example 1 For a lease consisting of five producing wells, each with an average production capacity of 10,000 bbl/day, find the approximate total storage capacity and the number of storage tanks.
- 27. INTRODUCTION • Production of crude oil and natural gas is usually associated with the production of water. • Water production presents serious operating, economic, and environmental problems. • Production of water also results in serious corrosion problems, which add to the cost of the operation. • The produced water, collected from the separation, emulsion treatment, and desalting systems, contains hydrocarbon concentrations that are too high for environmentally safe disposal.
- 28. PRODUCED WATER TREATMENT SYSTEM • Depending on the amount and droplet size of the oil in the produced water, the required quality of the treated water, and the operating conditions, water treatment may be achieved through a single or two stages of treatment. • The single, or first, stage of treatment is normally known as the primary treatment stage; the second stage of treatment is known as the secondary treatment stage.
- 29. WATER TREATMENT EQUIPMENT The main function of the treating equipment is to separate the free oil droplets from the water. • Filters • Precipitators • Skim Tanks and Vessels • Plate Coalescers • Serpentine-Pipe Packs • Flotation Units
- 30. OFFSHORE WATER DISPOSAL EQUIPMENT • Produced water in offshore operations should not be dumped directly into the sea after treatment. • For this purpose, offshore production platforms should be equipped with some form of a disposal device that disposes of the water deep enough below the surface of the sea and away from the wave action to prevent sheens from occurring. • The most common of these disposal devices are the disposal piles, skim piles, and SP piles.
- 32. The end