# Research on heavy oil gas lift assisted with light oil injected from the annulus

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## Abstract

An experimental study on the multiphase flow of heavy oil gas lift was conducted on 18.25 m high vertical tube. Based on the experimental results and the wellbore heat transfer mechanism, a coupling model of wellbore pressure–temperature gradients was presented for the gas lift with light oil injected from the annulus. Moreover, the solution of coupling annulus flow with tubing flow was also established through cyclic iteration. Experimental results showed that gas injection enables heavy oil and light oil to mix rapidly and completely. Evaluation of pressure drop models shows that the error of the Ansari model is approximately 12.12%, by comparison it is the least. A novel method of gas lift assisted with light oil from the annulus was proposed to solve the actual situation wherein heavy oil cannot be easily lifted from the wellbore at Tuyuke Block in Tuha Oilfield. An instance design based on the sensitivity analysis of the gas injection rate and diluting rate was also completed. The instance design shows that the productivity of heavy oil well can be significantly improved using gas lift and blending diluting oil technology. In order to verify the feasibility and effect of gas lift assisted with light oil in heavy oil well, a pilot test was implemented in Tahe Oilfield, Xinjiang, China. The results of pilot test show clearly that the daily production rate increased from 11.6 to 38 t/day, and the ratio of light oil with heavy oil decreased from 11:1 to 4:1. From the above, gas injection can significantly reduce the usage of light oil needed, and gas lift assisted with light oil injected from the bottom hole can significantly enhance the productivity of heavy oil wells.

## Keywords

Heavy oil Experiment Pressure–temperature coupling Gas lift assisted with light oil Technological design Pilot test## Introduction

The accurate prediction of the pressure and temperature profile of the wellbore is the basis of the technology of gas lift assisted with light oil. However, considering the physical properties of heavy oil and the complexity of the heavy oil, gas, water three-phase flow, predicting the pressure drop of the multiphase flow of heavy oil is difficult, and some scholars (Zhang and Sarica 2006; Schmidt et al. 2008; Gokcal et al. 2009; Akhiyarov et al. 2010) have presented the models of pressure drop which are suitable for the multiphase flow of heavy oil in a particular situation. But unfortunately those models are not suitable when the physical properties of heavy oil or the environment changes. Therefore, the author conducted the experiment on heavy oil gas lift to choose the most suitable pressure drop model.

For heavy oil or water/oil emulsion, the conventional technology of Sucker Rod Pump (SRP), Progressive Cavity Pump (PCP) and Electric Submerged Pump (ESP) can hardly provide sufficient high-flow power to overcome the increasing loss of flow friction. As such, choosing the appropriate methods of artificial lift for the cold production of heavy oil is important. Based on theory of the reduction of wellbore viscosity and lifting, gas lift technology for heavy oil exploitation is relatively mature in many countries (Jaimes and Zimmerman 1985; Blann and Garcia 1999; Hernandez and Marcelo 2002; Hong’en et al. 2007; Brito et al. 2010). From 1982 to 1984, heavy oil exploitation in the Urdaneta offshore oilfield of Lake Maracaibo of Venezuela achieved success using slug gas lift (Jaimes and Zimmerman 1985). In 1988, the lifting of heavy oil containing water and sand achieved success in eastern Venezuela using the gas lift technology of air chamber pump (Hernandez and Marcelo 2002). In 1997, in the Morichal area of Venezuela, the optimization of injecting diluent (diesel oil) from the bottom of a well and the matching technology of gas lift showed that injecting diluent and gas lift can significantly enhance the production of heavy oil wells (Blann and Garcia 1999). Hernandez and Marcelo (2002) proposed a model to predict liquid production and gas consumption of a single well for gas chamber pump wells. In 2005, heavy oil exploitation achieved success using continuous gas lift in Intercampo oilfield of Venezuela (Hong’en et al. 2007). In view of the characteristics of an ultra-deep and complex wellbore in Tahe oilfield, Riyi et al. (2006) conducted research on the pressure and temperature prediction method for heavy oil mixed with diluent and laboratory experiments on viscosity reduction with different diluting rates. Zaihong et al. (2012) proposed the optimum design method of manufacturing parameters for heavy oil mixed with diluent based on the Tahe oilfield. However, considering that the technology of gas lift assisted with light oil for heavy oil exploitation has not yet been reported and based on the research of predecessors and the application status of gas lift for heavy oil, the author proposes a set of technologies for heavy oil lift that is suitable for the deep heavy oil reservoir.

## Gas lift experiment

### Conditions and methods of the experiment

There is a 6 m test section on the loop, where installed two differential pressure sensors (Δ*P*_{1}, Δ*P*_{2}) and two pressure sensors (*P*_{1}, *P*_{2}) separately. Pressures and differential pressures under different conditions, such as different liquid rates, gas rates, temperatures, and water cuts, can be recorded to determine the most suitable pressure drop model.

### Experiment of heavy oil gas lift

#### Scope of the experimental parameters

Scope of the experimental parameters

Parameters | Value |
---|---|

Experimental temperature (°C) | 30, 40, 50, 60 |

Water cut (%) | 5, 15, 40, 50, 60 |

Liquid flow rate (m | 1, 2, 3 |

Gas injection rate (m | 1, 3, 5, 10, 15, 20 |

Gas injection pressure (MPa) | 0.3 |

The collected data contains pressure *P*_{1}, *P*_{2} of the test section, gas injection pressure *P*, flow rate *Q* of gas injection, and liquid rate *Q*_{l} controlled by the pump. We collected 360 sets of experimental data in total.

#### Experimental results and analysis

- 1.By using the test data, we evaluated the prediction models of differential pressure, including Duns and Ros, Beggs and Brill, Ansari, and no-slip models, as shown in Fig. 2. We observed that the predicted points of the Ansari model are mostly concentrated along the diagonal. As such, this result is relatively suitable. The average error of pressure drop prediction for these four models are 32, 23.2, 12.1, and 42.7% in sequence. Evidently, the Ansari model has the lowest error. Thus, we can ascertain the Ansari model as the most suitable model to predict the wellbore pressure gradient of continuous gas lift in heavy oil wells.
- 2.At the bottom of the well, without gas injection, heavy oil sticks to the ball, and the mixing process of light oil and heavy oil is not evident, as shown in Fig. 3 (left). Meanwhile, with gas injection, the stirring effect of the mixture between heavy oil and light oil occurs. The slippage effect also accelerates to mix between heavy oil and light oil, as shown in Fig. 3 (right). Through the experiment, we determined that gas lift not only provides the energy for lift but also enhances the degree of mixing between heavy oil and light oil. As such, the efficiency of lift is improved.

## Pressure–temperature coupling

*t*(0) of the annulus, is known. At the bottom hole, considering the mixture of formation fluid and annulus fluid, the temperature

*y*(

*n*) of the gas injection point on the tubing, i.e., the boundary condition of Eq. (2), could be obtained using the simple energy balance equation (Eq. 3):

In the above formulas, *c*_{m} is the specific heat of the liquid mixture; it can be calculated using the method of gravity weighted average.

*Z*is opposite to the direction of fluid flow, based on the momentum equation, its pressure gradient equation could be expressed as follows:

*ρ*

_{m}is the mixture density of the gas and oil phase in the annulus, kg/m

^{3};

*g*is the gravitational acceleration (= 9.81), m/s

^{2};

*α*is the deviation angle (−90°);

*v*

_{m}is the mixture flow velocity of the gas and oil phase in the annulus, m/s;

*v*

_{SG}is the apparent velocity of the gas phase, m/s;

*f*

_{m}is the friction coefficient of the fluid mixture, dimensionless.

- 1.
The distribution of formation temperature

*θ*(*x*) is given and assumes that the profile of wellbore temperature is*y*(*x*). - 2.
Assuming that the wellbore has

*n*sections and calculating the temperature from wellhead to bottom hole in the annulus, we can obtain the temperature*t*(*n*) of the bottom hole in the annulus. - 3.
After the mixture of heavy oil and light oil, we can obtain the temperature

*y*(*n*) of the gas injection point in the bottom hole and then calculate the temperature from bottom hole to wellhead, thereby deriving the temperature*y*(0) of the wellhead. - 4.
Comparing

*y*(0) and the estimated temperature of the wellhead, if the errors less than the desired accuracy rate, then we can determine the temperature profiles of the annulus and wellbore. Otherwise, the calculated results will be used to recalculate the temperature profile, i.e., repeating the processes of (2)–(4) or using loop iteration to solve the problem.

## Design method of heavy oil gas lift assisted with light oil

- 1.
Setting the tubing head pressure and the temperature of gas lift assisted with light oil.

- 2.
We obtained the bottom hole flow pressure by setting a group of light oil rates and gas injection rates, changing the heavy oil rates, and using the model of pressure–temperature coupling discussed previously to predict the distribution of pressure and temperature in the wellbore.

- 3.
Plotting the inflow and the outflow performance curve on one coordinate graph, the intersection point of two curves is the solution, i.e., production rate and pressure.

- 4.
By changing the light oil rate, gas injection rate, and formation pressure, and by repeating the processes of (1)–(3), we can obtain the solution of different conditions.

- 5.
We can accurately obtain and optimize the proration results on the basis of the results of nodal analysis.

## Instance design

### Basic data

Basic parameters of the well

Parameters | Value |
---|---|

Tubing inner diameter (m) | 0.062 |

Casing outer diameter (m) | 0.1778 |

Measured depth (m) | 3500 |

Wellbore diameter (m) | 0.251 |

Heat conductivity coefficient of formation [W/(m·°C)] | 1.4 |

Thermal diffusion coefficient of formation (m | 0.0037 |

Reservoir pressure (MPa) | 32.5 |

Reservoir temperature (°C) | 97 |

Depth of tubing (m) | 3480 |

Depth of casing (m) | 3500 |

Heat conductivity coefficient of cement sheath [W/(m· °C)] | 4.021 |

Formation oil viscosity (mPa·s) | 212 |

Relative density of gas [(–)] | 0.624 |

Productivity index [m | 5 |

Geothermal gradient (°C/100 m) | 2.6 |

Temperature of light oil (°C) | 30 |

### Sensitivity analysis

As shown in Fig. 6, at four different production rates, we observed that the required least gas injection rates to achieve these production rates are 1800, 3100, 5500, and 9700 m^{3}/day, respectively. By adding gas injection, the blending amount can be obviously reduced,With the increase in gas injection rate, the amount of diluted gas drops sharply and tends to be stable soon. That is to say, there is a minimum value when mixing dilute content, when the amount of dilute is less than this value, it cannot be produced even if the gas lift is used. Figure 7 shows that the light oil rate will reach a critical value at different gas injection rates. Before this critical value, the production rate increases rapidly with the increase in the light oil rate. By contrast, after this critical value, the increase in the light oil rate will result in the decrease in the production rate. At the given range of gas injection rate, the critical light oil rate will increase with the increase in gas injection rate, at approximately 20–40 m^{3}/day.

## Field pilot test

YQX well parameters

Parameters | Value |
---|---|

Well depth (m) | 6095 |

Casing size (m) | 0.1778 |

Tubing size (m) | 0.889 |

Liquid production (t/day) | 11.6 |

Water cut (%) | 0 |

Formation pressure (MPa) | 59.51 (2012/12/29) |

Formation temperature (°C) | 148 |

### Viscosity–temperature data of crude oil

It is assumed that the mixing ratio (the ratio of light oil to heavy oil volume) is 4:1, 7:1, 9:1, 11:1 as shown in Fig. 8. At the same temperature, the greater the amount of dilution, the better the viscosity reduction effect, but this trend with the increase in the amount of dilute. The viscosity decreases with the increase in temperature, which is consistent with the viscosity temperature curve of heavy oil.

### Test analysis

The results of pilot test show clearly that the daily production rate increased from 11.6 to 38 t/day, and the ratio of light oil and heavy oil decreased from 11:1 to 4:1. As a result, the crude oil increased by 218 t during the pilot test for 11 day. In short, the effect of the technology is very notable.

## Conclusions

- 1.
The experiment on heavy oil gas lift shows that, in the three-phase flow, the water phase mainly distributes near the tubing wall, whereas the gas and oil phases mainly distribute near the center of the tubing. The emulsion phenomenon did not occur. By using the 360 sets of pressure data of the experiment on heavy oil gas lift to evaluate the Duns and Ros, Beggs and Brill, Ansari, and no-slip model, we observed that the error of pressure drop prediction for the Ansari model is the lowest at 12.1%.

- 2.
Based on the flow performance of heavy oil gas lift assisted with light oil, we established the coupling model of pressure–temperature prediction and coupled the flow of the tubing and annulus by cyclic iteration to obtain the numerical solution.

- 3.
The instance analysis shows that using gas lift only cannot lift heavy oil, and diluting only can lift heavy oil but with a low production rate. Using gas lift and diluting at the same time can evidently lower the light oil rates and enhance the production rate. On the basis of the nodal system analysis and sensitivity analysis, this paper provides the technological parameters of gas lift with diluting for the instance well.

- 4.
The results of pilot test show the technology proposed in this paper is both feasible and effective on improving the production rate and decreasing the usage of light oil. This paper combines gas lift with diluting and uses nodal systems analysis to propose a suitable technology of heavy oil lift for the deep heavy oil reservoir.

## Notes

### Acknowledgements

The authors thank the financial support for this research by the special fund of China’s central government for the project of national first-level discipline in Oil and Gas Engineering.

## Supplementary material

## References

- Akhiyarov DT, Zhang HQ, Sarica C (2010) High-viscosity oil-gas flow in vertical pipe. In: OTC 20617. Offshore technology conference, Taxas, 3–6 MayGoogle Scholar
- Blann JR, Garcia R, Guaramata (1999) Advances in heavy oil lifting in the Morichal area of Venezuela. In: SPE 52211. SPE mid-continent operations symposium, Oklahoma, 28–31 MarchGoogle Scholar
- Brito F, Garcia L, Brown J (2010) Use of natural gas as a driving force in a diluent-gas artificial-lift system applied to heavy oils. In: SPE 139105, SPE Latin American & Caribbean petroleum engineering conference, Lima, Peru, 1–3 DecGoogle Scholar
- Cragoe CS (1993) Changes in the viscosity of liquid with temperature, pressure and composition. Presented at the 1st World Petroleum Congress, London, 18–24 JulyGoogle Scholar
- Gokcal B, Al-Sarkhi A, Sarica C (2009) Effects of high oil viscosity on drift velocity for horizontal and upward inclined pipes. SPE Proj Facil Constr 4(2):32–40CrossRefGoogle Scholar
- Hernandez A, Marcelo R (2002) Field scale research on gas chamber pumps. In: SPE 77729. SPE annual technical conference and exhibition, San Antonio, 29 Sep–2 OctGoogle Scholar
- Hongen D, Yuwen C, Dandan H et al (2007) Application of gas lift technology to a high-water-cut heavy-oil reservoir in intercampo oilfield, Venezuela. SPE Prod Oper 2:46–49Google Scholar
- Jaimes R, Zimmerman W (1985) Lagoven’s slug flow gas lift of heavy oil production. In: 3rd international UNITAR heavy crude &tar sands conference, Long Beach, 22–31 JulyGoogle Scholar
- Mukherjee H, Brill JP (1985) Pressure drop correlations for inclined two-Phase flow. J Energy Res Tech 4:54–59Google Scholar
- Ren Y (1982) Thermal production of viscous oil with recycling of hot fluid in well bore. J East Pet Coll 4:53–62Google Scholar
- Riyi L, Zhaomin L, Jingrui W et al (2006) Technology of blending diluting oil in ultra-deep wellbore of Tahe oil field. Acta Pet Sin 3:115–119
**(in Chinese)**Google Scholar - Schmidt J, Giesbrecht H, van der Geld CWM (2008) Phase and velocity distributions in vertically upward high-viscosity two-phase flow. Int J Multiph Flow 4:363–374CrossRefGoogle Scholar
- Zaihong S, Shuang S, Dongshen H et al (2012) Multi-phase flowing law and production parameter design of heavy oil mixing with light oil. Chin J Hydrodyn 3:284–291Google Scholar
- Zhang HQ, Sarica C (2006) Unified modeling of gas-oil-water pipe flow-basic approaches and preliminary validation. SPE Proj Facil Constr 2:1–7Google Scholar

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