Optimum Injection Rate of A New Chelate That Can Be Used To Stimulate Carbonate Reservoirs

SPE Journal ◽  
2011 ◽  
Vol 16 (04) ◽  
pp. 968-980 ◽  
Author(s):  
M.A.. A. Mahmoud ◽  
H.A.. A. Nasr-El-Din ◽  
C.A.. A. De Wolf ◽  
J.N.. N. LePage

Summary Different chelating agents were used as alternatives for hydrochloric acid (HCl) in matrix acidizing to create wormholes in carbonate formations. Previous studies demonstrated the use of ethylenediaminetetraacetic acid (EDTA), hydroxy ethylenediaminetriacetic (HEDTA), and glutamic acid-N,N-diacetic acid (GLDA) as standalone stimulation fluids to stimulate carbonate reservoirs. The main problem of using EDTA and HEDTA is their low bio-degradability. GLDA was introduced as a standalone stimulation fluid for deep carbonate reservoirs where HCl can cause corrosion and face dissolution problems. In this study, calcite cores 1.5 in. in diameter and 6 or 20 in. in length were used to determine the optimum conditions where the GLDA can break through the core and form wormholes. GLDA solutions with pH values of 1.7, 3, and 3.8 were used. The optimum conditions of injection rate and pH were determined using coreflood experiments. Damköhler number was determined using the wormhole length and diameter from the CT scan 3D and 2D images. GLDA was compared with chelates that are used in the oil industry such as EDTA and HEDTA. GLDA also was used to stimulate parallel cores with different permeability ratios (up to 6.25). GLDA was found to be very effective in creating wormholes at pH = 1.7, 3, and 3.8; at different injection rates; and at temperatures up to 300°F. Increasing the temperature increased the reaction rate and less volume of GLDA was required to break through the core and form wormholes. Unlike HCl, in GLDA there was no face dissolution or washout in the cores even at low injection rates (0.5 cm3/min). An optimum injection rate and Damköhler number were found at which the pore volume (PV) required to create wormholes was the minimum. GLDA at pH 1.7 and 3 created wormholes with a small number of PV (at 1 cm3/min, GLDA at pH 1.7 required 1.5 PV at 300°F, and at pH 3 it required 1.8 PV). Compared with acetic acid, the volume of GLDA at pH 3 required to create wormholes was less than that required with acetic acid at the same conditions. GLDA was found to be effective in stimulating parallel cores up to 6.25 permeability contrast (final permeability/initial permeability).

2021 ◽  
Author(s):  
Marek Czupski

During the matrix acidizing of carbonate formations, channels with high permeability are created, known as wormholes. The effectiveness of this type of treatment depends primarily on the structure, geometry, and the depth of penetration of the wormholes beyond the damaged zone. This should be ensured by a properly developed acidizing fluid, which in the case of carbonate formations most often consists of solutions of hydrochloric acid and/or organic acids such as acetic or formic acid. Additionally, in the case of high-temperature formations, additives are used to reduce the reaction rate of acid with the reservoir rock. The Damköhler number (Da) is an important factor that influences the model of the wormholes created. It represents the ratio of the rate of the reaction between the acid and the rock to the rate of its convection along the wormhole. The aim of the study was to determine the Damköhler number for four selected acidizing liquid–rock systems and to confirm that the structure of the wormholes depends on this variable. As part of the work, rheological tests of gelled acidizing liquids using a viscoelastic surfactant were conducted. The reaction rate tests were carried out on core plugs cut from Pińczów limestone and Guelph dolomite, which are characterized by relatively low permeability and porosity coefficients: 9.11–14.23 × 10−15m2 and 28.51%–29.10%, respectively, in the case of Pińczów limestone and 3.69–7.48 × 10−15m2 and 7.67%–9.38%, respectively, for Guelph dolomite. A rotating disk apparatus was used to determine the kinetics of the reaction of these rocks with two types of acidizing liquids. Then, core flow tests were performed on the core plugs using the AFS-300 system for the same types of rocks and liquids. The core plugs of Pińczów limestone used in these tests had a permeability coefficient ranging from 9.65 to 26.27 × 10−15m2 and a porosity coefficient ranging from 28.78% to 31.29%. On the other hand, samples of the Guelph dolomite had permeability coefficients of 7.48 to 61.52 × 10−15m2, while the porosity was much lower, ranging from 7.63% to 10.60%. After the core flow tests, the Damköhler number was calculated for each identified wormhole, using X-ray computed microtomography combined with an analysis of the geometric parameters. The types of structures that are formed in carbonate rocks as a result of matrix acidizing and their impact on the effectiveness of treatment are described in the theoretical part of this publication. Seven models of carbonate acidizing, which are used to estimate the influence of the parameters of the treatment and the properties of the liquid and rock on the efficiency of the acidizing process, are also discussed. Particular attention was paid to the theory of the Damköhler number, the value of which determines the formation of wormholes. The tests showed that at 80°C the overall reaction rate for each of the four acidizing liquid–rock systems was controlled by the mass transport rate. It was found that a gelled 15% HCl solution using TN-16235 viscoelastic surfactant reduced the overall reaction rate by reducing the mass transport rate. In the case of Pińczów limestone, the addition of 7.5% TN‑16235 surfactant reduced the De value from 4.45 × 10−6cm2/s to 3.53 × 10−6cm2/s; for Guelph dolomite De decreased from 2.25 × 10−6cm2/s to 1.97 × 10−6cm2/s. The values of the acidizing liquid pore volumes required to break through the core plug (PVbt) were determined based on the core flow tests. The lowest values of this parameter for Pińczów limestone were 0.26 for a 15% HCl solution and a velocity of 2.93 cm/min and 0.28 for a gelled 15% HCl solution and a velocity of 0.30 cm/min. For the Guelph dolomite rock, they were 0.88 for a 15% HCl solution and a velocity of 3.68 cm/min and 0.25 for a gelled 15% HCl solution and a velocity of 1.00 cm/min. Gelling a liquid with TN-16235 viscoelastic surfactant thus enables efficient matrix acidizing of carbonate formations with lower pumping rates. It was also found that the model of dissolution of the porous medium by a given acidizing liquid depended on the value of the Damköhler number. For wormholes created in the plugs of Pińczów limestone using the 15% HCl solution, the calculated values of Da were in the range of 0.244 to 0.026 (optimal value: 0.031); for the gelled 15% HCl solution it ranged from 0.145 to 0.008 (optimal value: 0.097). The optimal value for Da was considered to be the value for which wormholes were able to penetrate the entire length of the core with minimal acid spending described by PVbt. For wormholes etched in the Guelph dolomite rock by the 15% HCl solution, the calculated values of Da ranged from 0.104 to 0.030 (optimal value: 0.066), and for the gelled 15% HCl solution they ranged from 0.188 to 0.030 (optimal value: 0.069). The research methodology presented in this paper allows the Damköhler number to be determined for acidizing liquid–rock systems, and thus facilitates the preparation of technology for matrix acidizing of carbonate formations in such a way as to make these treatments as effective as possible. Keywords: matrix acidizing, Damköhler number, viscoelastic surfactant


2011 ◽  
Vol 133 (2) ◽  
Author(s):  
Ahmed M. Gomaa ◽  
Hisham A. Nasr-El-Din

Recent laboratory and field studies indicated that polymer-based in situ gelled acids can cause formation damage. Coreflood experiments using single-stage and multistage acids were conducted at 250 °F. 15 wt. % regular HCl and 5 wt. % in situ gelled acid-based on Fe(III) as a crosslinker were the acids that were used in this study. Propagation of acids and crosslinker inside 20 in. long cores was examined for the first time in detail. Stage volume and injection rate, which were the parameters that affect the propagating of various chemical species, were examined. Samples of the core effluent were collected and the concentrations of calcium, crosslinker, and acid were measured. Material balance was conducted to determine the amount of cross-liker that retained in the core. The results show that in situ gelled acid should be pumped at low injection rates. In situ gelled acid at low injection rate instantaneously plugged the tip of the wormhole and did not create additional wormholes inside the core. Therefore, when the final regular acid stage bypassed the gel, it started to propagate from nearly the last point that the first stage ended. In site gelled acid stage volume should not exceed 0.5 PV. No benefits were gained by increasing the volume of in situ gelled acids. Retention of total iron in the core increased in multistage acid treatments, especially at low acid injection rates.


2010 ◽  
Author(s):  
Mohamed Ahmednasreldin Mahmoud ◽  
Hisham A. Nasr-El-Din ◽  
Corine De Wolf ◽  
James N. LePage

2017 ◽  
pp. 63-67
Author(s):  
L. A. Vaganov ◽  
A. Yu. Sencov ◽  
A. A. Ankudinov ◽  
N. S. Polyakova

The article presents a description of the settlement method of necessary injection rates calculation, which is depended on the injected water migration into the surrounding wells and their mutual location. On the basis of the settlement method the targeted program of geological and technical measures for regulating the work of the injection well stock was created and implemented by the example of the BV7 formation of the Uzhno-Vyintoiskoe oil field.


2021 ◽  
Author(s):  
Albert Bokkers ◽  
Piter Brandenburg ◽  
Coert Van Lare ◽  
Cees Kooijman ◽  
Arjan Schutte

Abstract This work presents a matrix acidizing formulation which comprises a salt of monochloroacetic acid giving a delayed acidification and a chelating agent to prevent precipitation of a calcium salt. Results of dissolution capacity, core flood test and corrosion inhibition are presented and are compared to performance of 15 wt% emulsified HCl. Dissolution capacity tests were performed in a stirred reactor at atmospheric pressure using equimolar amounts of the crushed limestone and dolomites. Four different chelating agents were added to test the calcium ion sequestering power. Corrosion tests were executed using an autoclave reactor under nitrogen atmosphere at 10 barg. Core flood tests were performed to simulate carbonate matrix stimulation using limestone cores. It was found that the half-life time of the hydrolysis reaction is 77 min at a temperature of 100 °C. Sodium gluconate and the sodium salt of D-glucoheptonic acid were identified to successfully prevent the precipitation of the reaction product calcium glycolate at a temperature of 40 °C. Computed Tomography (CT) scans of the treated cores at optimum injection rate showed a single wormhole formed. At 150 °C an optimum injection rate of 1 ml/min was found which corresponds to a minimum PVBT of 6. In addition, no face dissolution was observed after coreflooding. Furthermore, the corrosion rates of different metallurgies (L80 and J55) were measured which are significantly less than data reported in literature for 15wt% emulsified HCl. The novelty of this formulation is that it slowly releases an organic acid in the well allowing deeper penetration in the formation and sodium gluconate prevents precipitation of the reaction product. The corrosivity of this formulation is relatively low saving maintenance costs to installations and pipe work. The active ingredient in the formulation is a solid, allowing onsite preparation of the acidizing fluid.


2021 ◽  
Author(s):  
Mojtaba Moradi ◽  
Michael R Konopczynski

Abstract Matrix acidizing is a common but complex stimulation treatment that could significantly improve production/injection rate, particularly in carbonate reservoirs. However, the desired improvement in all zones of the well by such operation may not be achieved due to existing and/or developing reservoir heterogeneity. This paper describes how a new flow control device (FCD) previously used to control water injection in long horizontal wells can also be used to improve the conformance of acid stimulation in carbonate reservoirs. Acid stimulation of a carbonate reservoir is a positive feedback process. Acid preferentially takes the least resistant path, an area with higher permeability or low skin. Once acid reacts with the formation, the injectivity in that zone increases, resulting in further preferential injection in the stimulated zone. Over-treating a high permeability zone results in poor distribution of acid to low permeability zones. Mechanical, chemical or foam diversions have been used to improve stimulation conformance along the wellbore, however, they may fail in carbonate reservoirs with natural fractures where fracture injectivity dominates the stimulation process. A new FCD has been developed to autonomously control flow and provide mechanical diversion during matrix stimulation. Once a predefined upper limit flowrate is reached at a zone, the valve autonomously closes. This eliminates the impact of thief zone on acid injection conformance and maintains a prescribed acid distribution. Like other FCDs, this device is installed in several compartments in the wells. The device has two operating conditions, one, as a passive outflow control valve, and two, as a barrier when the flow rate through the valve exceeds a designed limit, analogous to an electrical circuit breaker. Once a zone has been sufficiently stimulated by the acid and the injection rate in that zone exceeds the device trip point, the device in that zone closes and restricts further stimulation. Acid can then flow to and stimulate other zones This process can be repeated later in well life to re-stimulate zones. This performance enables the operators to minimise the impacts of high permeability zones on the acid conformance and to autonomously react to a dynamic change in reservoirs properties, specifically the growth of wormholes. The device can be installed as part of lower completions in both injection and production wells. It can be retrofitted in existing completions or be used in a retrievable completion. This technology allows repeat stimulation of carbonate reservoirs, providing mechanical diversion without the need for coiled tubing or other complex intervention. This paper will briefly present an overview of the device performance, flow loop testing and some results from numerical modelling. The paper also discusses the completion design workflow in carbonates reservoirs.


2022 ◽  
Author(s):  
Norah Aljuryyed ◽  
Abdullah Al Moajil ◽  
Sinan Caliskan ◽  
Saeed Alghamdi

Abstract Acid retardation through emulsification is commonly used in reservoir stimulation operations, however, emulsified acid are viscous fluids, thus require additional equipment at field for preparation and pumping requirements. Mixture of HCl with organic acids and/or chemical retarders have been used developed to retard acid reaction with carbonate, however, lower dissolving power. Development of low viscosity and high dissolving retarded acid recipes (e.g., equivalent to 15-26 wt.% HCl) addresses the drawbacks of emulsified acids and HCl acid mixtures with weaker organic acids. The objective of this study is to compare wormhole profile generated as a result of injecting acids in Indian limestone cores using 28 wt.% emulsified acid and single-phase retarded acids at comparable dissolving power at 200 and 300°F. Coreflood analysis testing was conducted using Indiana limestone core plugs to assess the pore volume profile of retarded acid at temperatures of 200 and 300° F. This test is supported by Computed Tomography to evaluate the propagation behavior as a result of the fluid/rock reaction. Wider wormholes were observed with 28 wt.% emulsified acid at 200°F when compared to test results conducted at 300°F. The optimum injection rate was 1 cm3/min at 200 and 300°F based on wormhole profile and examined flow rates. Generally, face-dissolution and wider wormholes were observed with emulsified acids, especially at 200°F. Narrower wormholes were formed as a result of injecting retarded acids into Indiana limestone cores compared to 28 wt.% emulsified acid. Breakthrough was not achieved with retarded acid recipe at 300°F and flow rates of 1 and 3 cm3/min, suggesting higher flow rates (e.g., > 3 cm3/min) are required for the retarded acid to be more effective at 300°F.


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