This technical paper evaluates the fluid loss property of Annona muricata and Carica papaya, prepared and measured as per API standard. This is a laboratory measurements carried out using low temperature and low pressure filter press. The prepared fluids were supplemented with 2 ppb XCD polymer product to enhance their carrying capacity. Their characteristics and commercial availabilities were also investigated. The 30 minutes filtrate volumes at 5 ppb, 10 ppb, 15 ppb and 20 ppb were obtained. The graph of concentrations versus the volume of the filtrate obtained was plotted. It was discovered that the concentration increases with decrease in volume of fluid loss and impermeable filtered mud cake was also obtained. Though, both gave good results, but the results of Annona muricata under the same conditions and concentrations were better than that of Carica papaya.
Generally, not much attention has been paid to the development of drilling fluids from biomaterial that has good filtration volume, impermeable filtered mud cake, cost effective, availability and environmentally friendly. In order to enhance the usage of drilling fluids, fluid loss additives were introduced and their design changed to have common characteristic features that aid in safe, economic and satisfactory completion of a well. In addition, drilling fluid loss additives are also required to perform the following functions: minimize reservoir damage; seal the formation pores by forming low-permeability filter cake to prevent inflow of formation fluids into the well; have minimum negative impact to the environment; aid in collection and interpretation of data available through drill cuttings, cores and electrical logs; provide frictionless environment between the drilling string and the sides of the hole; minimize any damaging effect on the sub-surface equipment and piping. Drilling fluids are designed to build a filter cake. The filter cake is intended to reduce filtrate loss to the formation, and give a thin impermeable mud cake at wall of the wellbore. Two components of the drilling fluid are specifically designed to assist in the development of a desirable filter cake are: blinding particles which have a specific size range to create a solid framework for the filter cake; fluid loss additives which are designed to create deformable particles to fill small gaps and improve the seal.
Fluid loss determines the filtration performance of the mud or in other words while drilling through permeable formation, and a part of fluid is filtered into the formation leaving behind a mud cake. The thickness and permeable of oil mud cake is dependent on the rate of filtration and the type of particles forming the mud cake [
For the occurrence of filtration, three conditions are required [
1) A liquid or a liquid/solids slurry fluid must be present.
2) A permeable medium must be present.
3) The fluid must be at a higher pressure than the permeable medium.
For the occurrence of fluid loss, there must be liquid and solids existing together as drilling mud; permeable medium must be present and there must be pressure differential from the wellbore to the reservoir. If any of the above condition is invalid, filtration of the drilling fluid will not occur.
There are two types of fluid loss laboratory measurements: Static test, normally called low temperature low pressure, also referred to as “API filtration test” which is the type of test applied to Annona maricata and Carica papaya water based fluid under 100 psi and ambient temperature. We also have dynamic test, this is the type of test carried out at the differential pressure of 500 psi and the temperature of 250˚F. Static test does not accurately stimulate down hole conditions because only static is being measured. In the wellbore, filtration is occurring under dynamic conditions with the mud flowing past the wall of the hole. The tests depend on Darcy’s law, which is the flow of fluids through permeable materials (sand, sandstone, mud filter cake). It can be used to relate filtration rate to permeability, cross sectional area, differential pressure, viscosity and filter cake thickness as shown in Equation (1).
where:
q = Filtrate flow rate, cm3.
k = Permeability, darcies.
A = Cross-sectional Area, cm2.
ΔP = Differential Pressure, atm.
µ = Viscosity, cP.
h = Thickness of filter cake, cm.
As this equation illustrates, with some assumptions of fluid flow through a permeable medium, the fluid must be incompressible, with a constant density in the flow system and the flow is also assumed to be linear. Also, fluid loss is lower with lower filter cake permeability, smaller area and lower differential pressure. From Equation (1), it is shown that filtration decreases with increasing filtrate viscosity and increasing filter cake thickness, if the thicker filter cake has the same permeability.
A model oil well was used to simulate filtration under different bottom hole geometry and hydrodynamic conditions [
Annona muricata trees are widespread in the tropics and frost-tree subtropics of the world [
Papaya is the widely cultivated and a tropical fruit tree. Most papaya are single stem trees whose height ranges from about 3.66 m to 9.14 m. Their leaves are arranged and confined to the upper most part of the trunk. The fruits are either
spherical or spindle in shape. All parts of the plant contain latex in articulated laticifers [
From
The materials involved in the laboratory measurements are unripe Annona muricata and Carica papaya. Low temperature and low pressure filter press was used for the measurements. The fresh and unripe Annona muricata and Carica papaya were sliced into pieces, dried in the oven for 6 hrs at the temperature of 45˚C which is the optimum temperature of retaining the chemical property of the additives. This can also be dried under the sun provided that the optimum that is not exceeded. Both were grinded differently into powder form, sieved and regrinded until finer powder were recovered.
Mud Formulations/Experimental ProcedureFour sets of measurements using 5 ppb, 10 ppb, 15 ppb and 20 ppb for both Annona muricata and Carica papaya were added to fresh water, each sample was supplemented with 2 ppb of XCD polymer to aid the carrying capacity and to prevent settling. API fluid loss measurements were carried for each formulation, for the two local materials. The filtrate then obtained and their results were shown in
Material Concentrations /ppb | Annona muricata | Carica papaya | ||||
---|---|---|---|---|---|---|
Annona muricata | Carica papaya | XCD Polymer | Filtrate Volume/ ml | Cake Thickness/ inch | Filtrate Volume (ml) | Cake Thickness/ inch |
5 | 5 | 2 | 24 | 1/32nd | 30 | 1/32nd |
10 | 10 | 2 | 16 | 2/32nd | 20 | 1/32nd |
15 | 15 | 2 | 12.4 | 2/32nd | 16 | 2/32nd |
20 | 20 | 2 | 9.2 | 2/32nd | 11 | 2/32nd |
Evaluation on the suitability of Annona muricata and Carica papaya as fluid loss control additives in drilling mud were carried out as per API standard. Their results were shown in both
From
In conclusion, both un-ripe Annona muricata and Carica papaya are suitable as a fluid loss additives for water base fluid, although the result obtained from un-ripe Annona muricata is better than that of Carica papaya.
The degree of suitability of both Annona muricata and Carica papaya as water base drilling fluids additives per concentration using low temperature and low pressure filter press was established.
We thank the management of Federal University of Technology, Owerri, and Covenant University, Ota, Nigeria for allowing us use their laboratory and their financial support during the execution of the work.
Igwilo, K.C., Ana- we, P.A.L., Okolie, S.T.A., Uzorchukwu, I. and Charles, O. (2017) Evaluation of the Fluid Loss Property of Annona muricata and Carica papaya. Open Journal of Yang- tze Gas and Oil, 2, 144-150. https://doi.org/10.4236/ojogas.2017.23010