Artificial lift

Artificial lift refers to the use of artificial means to increase the flow of liquids, such as crude oil or water, from a production well. Generally this is achieved by the use of a mechanical device inside the well (known as pump or velocity string) or by decreasing the weight of the hydrostatic column by injecting gas into the liquid some distance down the well. A newer method called Continuous Belt Transportation (CBT) uses an oil absorbing belt to extract from marginal and idle wells. Artificial lift is needed in wells when there is insufficient pressure in the reservoir to lift the produced fluids to the surface, but often used in naturally flowing wells (which do not technically need it) to increase the flow rate above what would flow naturally. The produced fluid can be oil, water or a mix of oil and water, typically mixed with some amount of gas.

Any liquid-producing reservoir will have a 'reservoir pressure': some level of energy or potential that will force fluid (liquid, gas or both) to areas of lower energy or potential. The concept is similar to that of water pressure in a municipal water system. As soon as the pressure inside a production well is decreased below the reservoir pressure, the reservoir will act to fill the well back up, just like opening a valve on a water system. Depending on the depth of the reservoir and density of the fluid, the reservoir may or may not have enough potential to push the fluid to the surface - a deeper well or a heavier mixture results in a higher pressure requirement.

Hydraulic pumping systems transmit energy to the bottom of the well by means of pressurized power fluid that flows down in the wellbore tubular to a subsurface pump. There are at least three types of hydraulic subsurface pump:

These systems are very versatile and have been used in shallow depths (1,000 ft) to deeper wells (18,000 ft), low rate wells with production in the tens of barrels per day to wells producing in excess of 20,000 bbl (3,200 m3) per day. In most cases the drive (injected) fluid can be water or produced fluids (oil/water mix). Certain chemicals can be mixed in with the injected fluid to help control corrosion, paraffin and emulsion problems. Hydraulic pumping systems are also suitable for deviated wells where conventional pumps such as the rod pump are not feasible.

Like all systems, these systems have their operating envelopes, though with hydraulic pumps these are often misunderstood by designers. Some types of hydraulic pumps may be sensitive to solids, while jetpumps for example can pump solids volume fractions of more than 50%. They are considered the least efficient lift method, though this differs for the different types of hydraulic pumps, and also when looking at full system losses the differences in many installations are negligible.

The life-cycle cost of these systems is similar to other types of artificial lift when appropriately designed, bearing in mind that they are typically low maintenance, with jet pumps for instance having slightly higher operating (energy) costs with substantially lower purchase cost and virtually no repair cost.

Electric Submersible Pumps (ESP) consist of a downhole pump (a series of centrifugal pumps), an electrical motor which transforms the electrical power into kinetic energy to turn the pump, a separator or protector to prevent produced fluids from entering the electrical motor, and an electric power cable that connects the motor to the surface control panel. ESP is a very versatile artificial lift method and can be found in operating environments all over the world. They can handle a very wide range of flow rates (from 200 to 90,000 barrels (14,000 m3) per day) and lift requirements (from virtually zero to 10,000 ft (3,000 m) of lift). They can be modified to handle contaminants commonly found in oil, aggressive corrosive fluids such as H2S and CO2, and exceptionally high downhole temperatures. Increasing water cut has been shown to have no significant detrimental effect on the ESP performance. It is possible to locate them in vertical, deviated, or horizontal wells, but it is recommended to deploy them in a straight section of casing for optimum run life performance.

Although latest developments are aimed to enhance the ESP capabilities to handle gas and sand, they still need more technological development to avoid gas locks and internal erosion. Until recently, ESPs have come with an often prohibitive price tag due to the cost of deployment which can be in excess of $20,000.

Various tools such as Automatic Diverter Valves (ADV), SandCats and other Tubing String and Pump Tools enhance the performance of the ESP. The majority of systems deployed in today's market are Dual ESP Systems which is a simple arrangement of two ESPs in the same well. This delivers a complete downhole system booster or back up - downtime is minimal, workovers cost less and there are savings in other operational areas. ESP Dual Systems bring a significant enhancement of well profitability.

Gas lift is another widely used artificial lift method. As the name denotes, gas is injected in the tubing to reduce the weight of the hydrostatic column, thus reducing the back pressure and allowing the reservoir pressure to push the mixture of produce fluids and gas up to the surface. The gas lift can be deployed in a wide range of well conditions (from 30,000 bbl/d (4,800 m3/d) to 15,000 ft (4,600 m)). Gas lifts can cope well with abrasive elements and sand, and the cost of workover is minimum.

Gas lifted wells are equipped with side pocket mandrels and gas lift injection valves. This arrangement allows a deeper gas injection in the tubing. The gas lift system has some disadvantages. There has to be a source of gas, some flow assurance problems such as hydrates can be triggered by the gas lift.

This uses the injection of gas into the fluid stream which reduces the fluid density and lowers the bottom hole pressure. As the gas rises the bubbles help to push the oil ahead. The degree of the effect depends on continuous or intermittent flow of the gas. The gas can be injected at a single point below the fluid or may be supplemented by multipoint injection. An intermitter at the surface controls the timing of the gas injection. The mechanisms are either pressure or fluid operated. They may be throttling valves or casing pressure operated valve.
Fluid operated valves require a rise in tubing pressure to open and drop to close.
A throttling pressure valve is opened by casing pressure build up and closed by casing pressure drop.
Conventional gas lift valves are attached to gas lift mandrels and wire line retrievable gas lift valves which are set in side pocket mandrels.

Rod pumps are long slender cylinders with both fixed and moveable elements inside. The pump is designed to be inserted inside the tubing of a well and its main purpose is to gather fluids from beneath it and lift them to the surface. The most important components are: the barrel, valves (traveling and fixed) and the piston. It also has another 18 to 30 components which are called "fittings".

Every part of the pump is important for its correct operation. The most commonly used parts are described below:

The sub-surface pump displaces the fluid at the bottom of the well thus lowering the bottom hole pressure.
The movement of the plunger and the traveling valve helps to create a low pressure thus moving fluid up the well. The traveling valve is opened on the down stroke and closed on the upstroke. It is on the up stroke that it carries the fluid up the well. The sucker rod is usually 25 ft. long. There are 3 types of pumping units: Class 1, Mark 2, or air balanced. By changing the stroke length or the pump rate the production rate can be changed.

The production measured in barrels per day can be calculated with the following formula: P=SxNxC, where P=Production in barrels per day, S=Downhole stroke length (inches), N=Number of strokes per minute, C=A constant derived from the following:

Plunger Diameter = Constant "C"

For an online calculator: Don-Nan Sucker Rod Pump Production Calculator (bpd)

Production at 100% is theoretical. 80% is a more realistic production calculation.

A new technology has recently been developed which combines gas lift with a rod pump, dedicating two separate tubing strings in the wellbore for each lift method. This technique is designed specifically to artificially lift the unique geometry of horizontal/deviated wells and also vertical wells that have deep or very long perforated intervals, or have too high of a gas liquid ratio (GLR) for conventional artificial lift methods. In this design, the rod pump is placed in the vertical portion of the well above the deviated or perforated interval, while relatively low pressure-low volume gas is used to lift reservoir liquids from the deviated or extended perforated interval to above the rod pump. Once the liquids are raised above the pump, they become trapped above a packer and then enter the pump chamber where they are transported to the surface.

This design overcomes high maintenance costs, gas interference issues, and depth limitations of installing conventional pumping systems into the deviated or extended perforated intervals and also overcomes the significant back pressure exerted on the reservoir by conventional gas lift.

Progressing Cavity Pumps (PCP) are also widely applied in the oil industry. The PCP consists of a stator and a rotor. The rotor is rotated using either a top side motor or a bottom hole motor. The rotation-created sequential cavities and the produced fluids are pushed to the surface.
The PCP is a flexible system with a wide range of applications in terms of rate (up to 5,000 bbl/d (790 m3/d) and depth 6,000 ft (1,800 m)). They offer outstanding resistance to abrasives and solids but they are restricted to setting depths and temperatures. Some components of the produced fluids like aromatics can also deteriorate the stator's elastomer.

These can be either hydraulic or electric submersible. The hydraulic uses high pressure power fluid to operate down hole fluid engine. The engine in turn drives a piston that moves the fluid to the surface. The power fluid system can be either open or closed, it depends on whether the power fluid can be mixed with well fluid. This type of system usually has above ground power fluid pumps and a reservoir. The electric submersible is another type of rodless pumping system. This uses an electric pump submerged in the well and connected to a series of transformers and control equipment that power and control the pumping rate. In this system the electric motor is isolated from the oil by a protector. The fluid intake which is before the pump mechanism has a gas separator, also the junction box on the surface helps to dissipate any gas that may have come up the power lines.

Essentially the rod and rodless pumping mechanisms help to achieve the fluid movement by reducing the bottom hole pressure by displacing the fluid above it all by mechanical means.
Another method is the plunger lift mechanism which utilizes the tubing string as the barrel. It uses gas to power a plunger.

It is important to note that there are several variations of these methods that can be used. They include; jet pumping involving a hydraulic pump and nozzle that transfers fluid momentum directly to the producing fluid or chamber lift which is a modified gas lift mechanism that has no back pressure. There are also modified rod pumping design units that use either a winch or pneumatic mechanism to work.

This method uses an oil absorbing continuous belt to transport heavy oil as an alternative to pumping. A single sided “O” shape belt driven by a Moebius surface unit cycles continuously to the underground unit, below the static level, capturing the oil and transporting up to the surface unit for collection. The oleophilic properties of the belt ensure that sand, paraffin, and most of the water are not captured.

Due to its relatively low rate of oil capture at below 130 barrels per day at a maximum depth of 4000 meters, and very low cost of operation, this method is used primarily in stripper, marginal, idle, and abandoned wells. The optimal oil composition for CBT are reservoirs with medium, heavy and very heavy oil, at a maximum temperature of 130 deg. Celsius. High-volume, light oil wells are not suitable for this method.