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Tracers are used in [[ | Tracers are used in [[Geothermal_reservoir_engineering|geothermal reservoir engineering]] to determine the connectivity between injection and production wells. Reinjection of spent geothermal fluid is nearly universal to | ||
*Address environmental concerns | |||
*Provide reservoir pressure maintenance | |||
*Improve energy extraction efficiency | |||
Because injected fluids are much cooler than in-situ fluids, knowledge of injectate flow paths helps mitigate premature thermal breakthrough. As in other applications of tracer testing, the goal of the tracer test is to estimate sweep efficiency of a given injection pattern.<ref name="r1">_</ref> Because geothermal systems tend to be open, tracer tests can also be used to estimate the extent of recharge/discharge or total pore volume.<ref name="r2">_</ref><ref name="r3">_</ref> Currently, however, the primary use of geothermal tracers is to estimate the degree of connectivity between injectors and producers. That information is subsequently used to develop an injection program that either minimizes or postpones injection returns in production wells while providing pressure maintenance. | |||
Because | |||
== Geothermal tracers == | |||
More recently, issues such as sorptivity and volatility have been recognized as equally relevant characteristics that influence analysis.<ref name="r13" /> | Because geothermal reservoirs are not usually developed on regular well spacing, well pairs may exhibit weak connectivity, and tracer tests must be conducted over long times, using large volumes of tracer to overcome thermal decay and dilution effects. For these and other reasons, extensive work has been invested in evaluating so-called "natural tracers." These can be thought of as compounds that are present in geothermal fluids naturally and whose concentrations may change during production and injection and may therefore be used to trace injectate. Examples of natural tracers include chloride,<ref name="r4">_</ref> ammonia,<ref name="r5">_</ref> and various stable isotopes of water.<ref name="r6">_</ref><ref name="r7">_</ref><ref name="r8">_</ref> | ||
Artificial tracers have also been used extensively to determine flow paths in geothermal reservoirs. Tritium was the first artificial tracer used to trace geothermal injectate.<ref name="r9">_</ref> Since the early 1990s, various new compounds have been evaluated for use in geothermal reservoirs. Liquid-phase tracers have evolved from carboxylic and benzene sulfonic acids<ref name="r10">_</ref> to polyaromatic sulfonates,<ref name="r11">_</ref> which are stable thermally at temperatures greater than 300°C and have detection limits in the range of 10<sup>2</sup> parts per trillion (ppt). Vapor-phase tracers have evolved from chlorofluorocarbons used in the early 1990s to hydrofluorocarbons in the late 1990s.<ref name="r12">_</ref> To date, criteria for selection of tracers focus on: | |||
*Thermal stability | |||
*Low background concentrations | |||
*Low detectability | |||
*Being environmentally benign | |||
More recently, issues such as sorptivity and volatility have been recognized as equally relevant characteristics that influence analysis.<ref name="r13">_</ref> | |||
Tracer tests have been conducted for over 25 years in geothermal fields, including early work in: | Tracer tests have been conducted for over 25 years in geothermal fields, including early work in: | ||
* New Zealand<ref name="r14" /> | |||
* The Geysers in Northern California<ref name="r9" /> | *New Zealand<ref name="r14">_</ref> | ||
* Lardarello in Italy<ref name="r15" /> | *The Geysers in Northern California<ref name="r9">_</ref> | ||
* Various Japanese fields<ref name="r16" /> | *Lardarello in Italy<ref name="r15">_</ref> | ||
*Various Japanese fields<ref name="r16">_</ref> | |||
In the last decade, more than 50 tracer tests have been conducted worldwide in geothermal fields. | In the last decade, more than 50 tracer tests have been conducted worldwide in geothermal fields. | ||
==Interpretation methods== | == Interpretation methods == | ||
Early workers in the field recognized that tracer tests could be used quantitatively to evaluate volumetric sweep efficiency of an injection program. Lovekin and Horne<ref name="r17">_</ref> applied optimization methods to maximize the residence time of injectate. This involved minimizing a tracer breakthrough function. | |||
[[File:Vol6 page 0417 eq 001.png|RTENOTITLE]]....................(1) | |||
where the ''c''<sub>''ij</sub> | where the ''c''<sub>''ij''</sub> are referred to as the arc cost function for the travel arc between a given injection and production well pair (e.g., a streamline), and ''q''<sub>''ri''</sub>is the injection rate for injector ''i. ''The cost function is related to operational and geologic information for the field, including: | ||
*Tracer first arrival and peak arrival times | |||
*Horizontal distances and elevation differences between wells | |||
*Injection and production rates | |||
The method was applied to optimizing production operations at the Wairakei Field in New Zealand.<ref name="r17">_</ref> | |||
In 1991, Macario extended the previous work to use a natural tracer, chloride, to optimize reinjection in the Philippine field, Palinpinon. Shortly after commissioning the power plant in 1983, an increasing trend of chloride in the production wells was observed. This was interpreted as evidence of rapid return of reinjected fluids to the production sector of the field.<ref name="r18">_</ref> Because the chloride trend is associated with all injectate (i.e., not a specific injector), Macario<ref name="r19">_</ref> developed a linear combination method that expresses the chloride concentration as a linear combination of the injection wells active during the time interval considered. Produced chloride for a given well, ''C''<sub>''lp''</sub>, is expressed as a linear function of the chloride injection rates. | |||
[[File:Vol6 page 0418 eq 001.png|RTENOTITLE]]....................(2) | |||
The coefficients ''a''<sub>''i''</sub> are coefficients of correlation between a given producer and injector. A large coefficient implies strong production contribution from a given injector. These coefficients can subsequently be used in the arc cost function. These methods appear to work well if there is operational flexibility to use the appropriate wells and work equally well for either natural or artificial tracers. | |||
Noting that fluctuations in injection rates manifest themselves as changes in produced chloride concentrations over and above the underlying trend in time, Sullera and Horne<ref name="r4">_</ref> applied wavelet analysis to two geothermal fields: | |||
*Palinpinon in the Phillipines | |||
*Dixie Valley in Nevada | |||
The chloride production data and injection rates are decomposed into progressively lower-frequency detail, and multiple regression techniques are applied to identify the degree of connectivity between individual injectors and producers. Care must be taken to avoid decomposing the signal too far; however, Sullera and Horne<ref name="r4">_</ref> show the method yields large, positive correlation coefficients for well pairs identified by tracer tests to have strong connectivity, and low positive, or negative coefficients for well pairs with known poor connectivity. The authors also showed that the data set being transformed must have sufficient temporal "texture" for wavelet analysis to be useful. | |||
Some additional quantitative analysis has been done using synthetic tracer tests. One reservoir management concern is to identify the velocity of thermal fronts in the reservoir. The velocity of a temperature front, ''v''<sub>''T''</sub>, is related to the fluid velocity, ''v''<sub>''w''</sub>, in a fixed manner.<ref name="r20">_</ref> | |||
[[File:Vol6 page 0418 eq 002.png|RTENOTITLE]]....................(3) | |||
Other than the analyses for the Hijiori field tracer tests, a majority of tracer test interpretations remains qualitative. '''Fig. 1 '''is an example of analysis of several tracer tests conducted at Dixie Valley, Nevada. The geothermal field has been a test facility for testing naphthalene sulfonates for a number of years, and seven such tests have been conducted since 1997.<ref name="r11" /> The relative size of the arrows is indicative of the relative contribution of an injector on a set of producers. Estimates of reservoir pore volume have also been calculated on the basis of tracer dilution.<ref name="r28" /> However, the interpretation in the figure (i.e., relative contribution of injectors to production areas) remains the most-used information from these tracer tests. | By transforming tracer production data at each production well, Shook<ref name="r1">_</ref> showed that thermal velocities can be predicted from tracer tests. These studies were restricted to heterogeneous, nonfractured media and single-phase conditions, where thermal conduction is largely a secondorder effect. Efforts to extend the method to fractured media have met with limited success, in particular because of fracture geometry. Likewise, quantitative analysis of tracers in two-phase or superheated steam reservoirs is difficult. Because the tracer is transported by either of the phases at various times (e.g., vaporizing here and condensing there), mean residence times are more difficult to interpret. Under certain conditions, a boiling interface may develop between the fluid originally in place and the cooler injectate.<ref name="r21">_</ref> The velocity of this boiling front has been studied analytically,<ref name="r22">_</ref><ref name="r23">_</ref> and can be predicted for simple geometries and homogeneous reservoir conditions. In cases where buoyancy is important, however, the vaporized tracer may not trace injectate flow paths, making the interpretation still more difficult. Predicting thermal velocities in fractured media remains an active research topic in geothermal tracing. | ||
Analysis of tracer tests conducted in geothermal fields ranges from purely qualitative to quantitative, volumetric analysis of pore volume. Matsunaga ''et al.''<ref name="r24">_</ref> show an analysis of seven tracer tests conducted at the Hijiori, Japan, engineered geothermal system. By comparing mean residence times<ref name="r25">_</ref> for consecutive tracer tests, they showed that the flow system was evolving during the injection of cool (25 to 50°C) liquid into initially hot (~150°C) dry rock. They concluded in part that anhydrite scaling was plugging some of the fractures, thereby modifying the flow field. They also noted a rapid decline in produced temperature during the injection tests, but did not correlate the thermal velocities with tracer velocities. The Hijiori geothermal reservoir is among the most instrumented and studied engineered geothermal systems in the world. A variety of tracer tests have been conducted and reported on over a number of years.<ref name="r24">_</ref><ref name="r26">_</ref><ref name="r27">_</ref> | |||
Other than the analyses for the Hijiori field tracer tests, a majority of tracer test interpretations remains qualitative. '''Fig. 1 '''is an example of analysis of several tracer tests conducted at Dixie Valley, Nevada. The geothermal field has been a test facility for testing naphthalene sulfonates for a number of years, and seven such tests have been conducted since 1997.<ref name="r11">_</ref> The relative size of the arrows is indicative of the relative contribution of an injector on a set of producers. Estimates of reservoir pore volume have also been calculated on the basis of tracer dilution.<ref name="r28">_</ref> However, the interpretation in the figure (i.e., relative contribution of injectors to production areas) remains the most-used information from these tracer tests. | |||
<gallery widths="300px" heights="200px"> | <gallery widths="300px" heights="200px"> | ||
Line 64: | Line 70: | ||
</gallery> | </gallery> | ||
An example of tracer test interpretation in vapor-dominated reservoirs is given in '''Fig. 2'''. This figure summarizes the interpretation of a tracer test conducted in The Geysers geothermal field in Northern California. In this test, two hydrofluorocarbons, R23 and R134a, and tritiated water were injected into a zone containing moderately (~15°C) superheated steam. Fig. 2 shows the cumulative mass fraction of R134a and tritium recovered from wells surrounding the injector. Tritiated water is a nearly ideal geothermal tracer because its properties are nearly identical with those of water and, therefore, tracks the injectate very well. Adams ''et al.''<ref name="r12" /> suggest that the similarity in recovery between the tritium and R134a suggests both compounds remained with the injectate, indicating R134a is a useful tracer for areas with low or moderate superheat. Another tracer test conducted in a highly superheated zone at The Geysers showed substantial separation between tritiated water and the chlorofluorocarbon R13.<ref name="r12" /> The authors concluded that a large degree of superheat exaggerates the effect of volatility, and caution should be exercised in using tracers whose volatility greatly exceeds that of water when superheated conditions prevail. | An example of tracer test interpretation in vapor-dominated reservoirs is given in '''Fig. 2'''. This figure summarizes the interpretation of a tracer test conducted in The Geysers geothermal field in Northern California. In this test, two hydrofluorocarbons, R23 and R134a, and tritiated water were injected into a zone containing moderately (~15°C) superheated steam. Fig. 2 shows the cumulative mass fraction of R134a and tritium recovered from wells surrounding the injector. Tritiated water is a nearly ideal geothermal tracer because its properties are nearly identical with those of water and, therefore, tracks the injectate very well. Adams ''et al.''<ref name="r12">_</ref> suggest that the similarity in recovery between the tritium and R134a suggests both compounds remained with the injectate, indicating R134a is a useful tracer for areas with low or moderate superheat. Another tracer test conducted in a highly superheated zone at The Geysers showed substantial separation between tritiated water and the chlorofluorocarbon R13.<ref name="r12">_</ref> The authors concluded that a large degree of superheat exaggerates the effect of volatility, and caution should be exercised in using tracers whose volatility greatly exceeds that of water when superheated conditions prevail. | ||
<gallery widths="300px" heights="200px"> | <gallery widths="300px" heights="200px"> | ||
Line 70: | Line 76: | ||
</gallery> | </gallery> | ||
While some tracer tests have been modeled,<ref name="r29" /> this is one aspect of tracer test analysis that has tended to lag behind oilfield practices. Recent advances have been made in improving the phase behavior routines for vapor-liquid partitioning tracers,<ref name="r3" /><ref name="r30" /> and use of modeling tracer tests is expected to increase. | While some tracer tests have been modeled,<ref name="r29">_</ref> this is one aspect of tracer test analysis that has tended to lag behind oilfield practices. Recent advances have been made in improving the phase behavior routines for vapor-liquid partitioning tracers,<ref name="r3">_</ref><ref name="r30">_</ref> and use of modeling tracer tests is expected to increase. | ||
== Nomenclature == | == Nomenclature == | ||
{|border="0" cellspacing="4" width="100%" | |||
{| border="0" cellspacing="4" width="100%" | |||
|- | |- | ||
|''a''<sub>'' | | ''a''<sub>''i''</sub> | ||
|= | | = | ||
| | | correlation coefficients between a given wells<nowiki>’</nowiki> | ||
produced chloride and the''i''th injection wells<nowiki>’</nowiki> | |||
injected chloride concentration | |||
|- | |- | ||
|'' | | ''a''<sub>''o''</sub> | ||
|= | | = | ||
| | | initial chloride concentration for a given production well | ||
|- | |- | ||
|''c''<sub>'' | | ''c''<sub>''ij''</sub> | ||
|= | | = | ||
| | | arc cost function for the travel arc between a given injection and production well pair (e.g., along a streamline) | ||
|- | |- | ||
|''c''<sub>'' | | ''c''<sub>''r''</sub> | ||
|= | | = | ||
| | | rock compressibility | ||
|- | |- | ||
|'' | | ''c''<sub>''w''</sub> | ||
|= | | = | ||
| | | liquid compressibility | ||
|- | |- | ||
|'' | | ''Cl''<sub>''p''</sub> | ||
|= | | = | ||
| | | produced chloride for a given well | ||
|- | |- | ||
|'' | | ''d'' | ||
|= | | = | ||
| | | wellbore diameter | ||
|- | |- | ||
| | | ''i'' | ||
|= | | = | ||
| | | injector | ||
|- | |- | ||
|''q''<sub>'' | | ''q''<sub>''i''</sub> | ||
|= | | = | ||
| | | chloride injection rate in well ''i'' | ||
|- | |- | ||
|'' | | ''q''<sub>''ri''</sub> | ||
|= | | = | ||
| | | re-injection rate at well ''i'' | ||
|- | |- | ||
|''v''<sub>'' | | ''v''<sub>''T''</sub> | ||
|= | | = | ||
| | | velocity of temperature front | ||
|- | |- | ||
|'' | | ''v''<sub>''w''</sub> | ||
|= | | = | ||
| | | fluid velocity | ||
|- | |- | ||
|'' | | ''W'' | ||
|= | | = | ||
| | | mass flow rate | ||
|- | |- | ||
|''ρ'' | | ''ρ ''(''p,T'') | ||
|= | | = | ||
| | | fluid density | ||
|- | |- | ||
|''Φ'' | | ''ρ''<sub>''r''</sub>, ''ρ''<sub>''w''</sub>, ''ρ''<sub>''v''</sub> | ||
|= | | = | ||
|porosity | | densities of rock, water, and steam, respectively | ||
|- | |||
| ''Φ'' | |||
| = | |||
| porosity | |||
|} | |} | ||
==References== | == References == | ||
<references | |||
<references /> | |||
== Noteworthy papers in OnePetro == | |||
Use this section to list papers in OnePetro that a reader who wants to learn more should definitely read | Use this section to list papers in OnePetro that a reader who wants to learn more should definitely read | ||
==External links== | == External links == | ||
Use this section to provide links to relevant material on websites other than PetroWiki and OnePetro | Use this section to provide links to relevant material on websites other than PetroWiki and OnePetro | ||
==See also== | == See also == | ||
[[Geothermal reservoir engineering]] | |||
[[Geothermal_reservoir_engineering|Geothermal reservoir engineering]] | |||
[[Geothermal_reservoir_characterization|Geothermal reservoir characterization]] | |||
[[ | [[Modeling_geothermal_reservoirs|Modeling geothermal reservoirs]] | ||
[[ | [[Geothermal_drilling_and_completion|Geothermal drilling and completion]] | ||
[[Geothermal | [[Geothermal_energy|Geothermal energy]] | ||
[[ | [[PEH:Geothermal_Engineering]] | ||
[[ | [[Category:5.6.5 Tracer test analysis]] | ||
[[Category:5.9.2 Geothermal Resources]] |
Revision as of 10:00, 4 June 2015
Tracers are used in geothermal reservoir engineering to determine the connectivity between injection and production wells. Reinjection of spent geothermal fluid is nearly universal to
- Address environmental concerns
- Provide reservoir pressure maintenance
- Improve energy extraction efficiency
Because injected fluids are much cooler than in-situ fluids, knowledge of injectate flow paths helps mitigate premature thermal breakthrough. As in other applications of tracer testing, the goal of the tracer test is to estimate sweep efficiency of a given injection pattern.[1] Because geothermal systems tend to be open, tracer tests can also be used to estimate the extent of recharge/discharge or total pore volume.[2][3] Currently, however, the primary use of geothermal tracers is to estimate the degree of connectivity between injectors and producers. That information is subsequently used to develop an injection program that either minimizes or postpones injection returns in production wells while providing pressure maintenance.
Geothermal tracers
Because geothermal reservoirs are not usually developed on regular well spacing, well pairs may exhibit weak connectivity, and tracer tests must be conducted over long times, using large volumes of tracer to overcome thermal decay and dilution effects. For these and other reasons, extensive work has been invested in evaluating so-called "natural tracers." These can be thought of as compounds that are present in geothermal fluids naturally and whose concentrations may change during production and injection and may therefore be used to trace injectate. Examples of natural tracers include chloride,[4] ammonia,[5] and various stable isotopes of water.[6][7][8]
Artificial tracers have also been used extensively to determine flow paths in geothermal reservoirs. Tritium was the first artificial tracer used to trace geothermal injectate.[9] Since the early 1990s, various new compounds have been evaluated for use in geothermal reservoirs. Liquid-phase tracers have evolved from carboxylic and benzene sulfonic acids[10] to polyaromatic sulfonates,[11] which are stable thermally at temperatures greater than 300°C and have detection limits in the range of 102 parts per trillion (ppt). Vapor-phase tracers have evolved from chlorofluorocarbons used in the early 1990s to hydrofluorocarbons in the late 1990s.[12] To date, criteria for selection of tracers focus on:
- Thermal stability
- Low background concentrations
- Low detectability
- Being environmentally benign
More recently, issues such as sorptivity and volatility have been recognized as equally relevant characteristics that influence analysis.[13]
Tracer tests have been conducted for over 25 years in geothermal fields, including early work in:
- New Zealand[14]
- The Geysers in Northern California[9]
- Lardarello in Italy[15]
- Various Japanese fields[16]
In the last decade, more than 50 tracer tests have been conducted worldwide in geothermal fields.
Interpretation methods
Early workers in the field recognized that tracer tests could be used quantitatively to evaluate volumetric sweep efficiency of an injection program. Lovekin and Horne[17] applied optimization methods to maximize the residence time of injectate. This involved minimizing a tracer breakthrough function.
where the cij are referred to as the arc cost function for the travel arc between a given injection and production well pair (e.g., a streamline), and qriis the injection rate for injector i. The cost function is related to operational and geologic information for the field, including:
- Tracer first arrival and peak arrival times
- Horizontal distances and elevation differences between wells
- Injection and production rates
The method was applied to optimizing production operations at the Wairakei Field in New Zealand.[17]
In 1991, Macario extended the previous work to use a natural tracer, chloride, to optimize reinjection in the Philippine field, Palinpinon. Shortly after commissioning the power plant in 1983, an increasing trend of chloride in the production wells was observed. This was interpreted as evidence of rapid return of reinjected fluids to the production sector of the field.[18] Because the chloride trend is associated with all injectate (i.e., not a specific injector), Macario[19] developed a linear combination method that expresses the chloride concentration as a linear combination of the injection wells active during the time interval considered. Produced chloride for a given well, Clp, is expressed as a linear function of the chloride injection rates.
The coefficients ai are coefficients of correlation between a given producer and injector. A large coefficient implies strong production contribution from a given injector. These coefficients can subsequently be used in the arc cost function. These methods appear to work well if there is operational flexibility to use the appropriate wells and work equally well for either natural or artificial tracers.
Noting that fluctuations in injection rates manifest themselves as changes in produced chloride concentrations over and above the underlying trend in time, Sullera and Horne[4] applied wavelet analysis to two geothermal fields:
- Palinpinon in the Phillipines
- Dixie Valley in Nevada
The chloride production data and injection rates are decomposed into progressively lower-frequency detail, and multiple regression techniques are applied to identify the degree of connectivity between individual injectors and producers. Care must be taken to avoid decomposing the signal too far; however, Sullera and Horne[4] show the method yields large, positive correlation coefficients for well pairs identified by tracer tests to have strong connectivity, and low positive, or negative coefficients for well pairs with known poor connectivity. The authors also showed that the data set being transformed must have sufficient temporal "texture" for wavelet analysis to be useful.
Some additional quantitative analysis has been done using synthetic tracer tests. One reservoir management concern is to identify the velocity of thermal fronts in the reservoir. The velocity of a temperature front, vT, is related to the fluid velocity, vw, in a fixed manner.[20]
By transforming tracer production data at each production well, Shook[1] showed that thermal velocities can be predicted from tracer tests. These studies were restricted to heterogeneous, nonfractured media and single-phase conditions, where thermal conduction is largely a secondorder effect. Efforts to extend the method to fractured media have met with limited success, in particular because of fracture geometry. Likewise, quantitative analysis of tracers in two-phase or superheated steam reservoirs is difficult. Because the tracer is transported by either of the phases at various times (e.g., vaporizing here and condensing there), mean residence times are more difficult to interpret. Under certain conditions, a boiling interface may develop between the fluid originally in place and the cooler injectate.[21] The velocity of this boiling front has been studied analytically,[22][23] and can be predicted for simple geometries and homogeneous reservoir conditions. In cases where buoyancy is important, however, the vaporized tracer may not trace injectate flow paths, making the interpretation still more difficult. Predicting thermal velocities in fractured media remains an active research topic in geothermal tracing.
Analysis of tracer tests conducted in geothermal fields ranges from purely qualitative to quantitative, volumetric analysis of pore volume. Matsunaga et al.[24] show an analysis of seven tracer tests conducted at the Hijiori, Japan, engineered geothermal system. By comparing mean residence times[25] for consecutive tracer tests, they showed that the flow system was evolving during the injection of cool (25 to 50°C) liquid into initially hot (~150°C) dry rock. They concluded in part that anhydrite scaling was plugging some of the fractures, thereby modifying the flow field. They also noted a rapid decline in produced temperature during the injection tests, but did not correlate the thermal velocities with tracer velocities. The Hijiori geothermal reservoir is among the most instrumented and studied engineered geothermal systems in the world. A variety of tracer tests have been conducted and reported on over a number of years.[24][26][27]
Other than the analyses for the Hijiori field tracer tests, a majority of tracer test interpretations remains qualitative. Fig. 1 is an example of analysis of several tracer tests conducted at Dixie Valley, Nevada. The geothermal field has been a test facility for testing naphthalene sulfonates for a number of years, and seven such tests have been conducted since 1997.[11] The relative size of the arrows is indicative of the relative contribution of an injector on a set of producers. Estimates of reservoir pore volume have also been calculated on the basis of tracer dilution.[28] However, the interpretation in the figure (i.e., relative contribution of injectors to production areas) remains the most-used information from these tracer tests.
Fig. 1—Injectate flow patterns as estimated from tracer tests at Dixie Valley, Nevada. Seven polyaromatic sulfonate tracer compounds have been tested at this site. The arrows indicate directions of flow. See Rose et al. [2] for more information on the tracers.
An example of tracer test interpretation in vapor-dominated reservoirs is given in Fig. 2. This figure summarizes the interpretation of a tracer test conducted in The Geysers geothermal field in Northern California. In this test, two hydrofluorocarbons, R23 and R134a, and tritiated water were injected into a zone containing moderately (~15°C) superheated steam. Fig. 2 shows the cumulative mass fraction of R134a and tritium recovered from wells surrounding the injector. Tritiated water is a nearly ideal geothermal tracer because its properties are nearly identical with those of water and, therefore, tracks the injectate very well. Adams et al.[12] suggest that the similarity in recovery between the tritium and R134a suggests both compounds remained with the injectate, indicating R134a is a useful tracer for areas with low or moderate superheat. Another tracer test conducted in a highly superheated zone at The Geysers showed substantial separation between tritiated water and the chlorofluorocarbon R13.[12] The authors concluded that a large degree of superheat exaggerates the effect of volatility, and caution should be exercised in using tracers whose volatility greatly exceeds that of water when superheated conditions prevail.
Fig. 2—Map of cumulative recovery fractions for tracers R-134a and Tritium during the P-1 tracer test at The Geysers, California. Adams et al. [12] suggest the similarity in recovery fractions areally suggests the more volatile R-134a traced injectate adequately in the case of low superheat. Lack of tritium recovery in the northeast is thought to be a sampling artifact because not all wells were sample for both tracers(after Adams et al.,[12] used with permission from Geothermics).
While some tracer tests have been modeled,[29] this is one aspect of tracer test analysis that has tended to lag behind oilfield practices. Recent advances have been made in improving the phase behavior routines for vapor-liquid partitioning tracers,[3][30] and use of modeling tracer tests is expected to increase.
Nomenclature
ai | = | correlation coefficients between a given wells’
produced chloride and theith injection wells’ injected chloride concentration |
ao | = | initial chloride concentration for a given production well |
cij | = | arc cost function for the travel arc between a given injection and production well pair (e.g., along a streamline) |
cr | = | rock compressibility |
cw | = | liquid compressibility |
Clp | = | produced chloride for a given well |
d | = | wellbore diameter |
i | = | injector |
qi | = | chloride injection rate in well i |
qri | = | re-injection rate at well i |
vT | = | velocity of temperature front |
vw | = | fluid velocity |
W | = | mass flow rate |
ρ (p,T) | = | fluid density |
ρr, ρw, ρv | = | densities of rock, water, and steam, respectively |
Φ | = | porosity |
References
Noteworthy papers in OnePetro
Use this section to list papers in OnePetro that a reader who wants to learn more should definitely read
External links
Use this section to provide links to relevant material on websites other than PetroWiki and OnePetro
See also
Geothermal reservoir engineering
Geothermal reservoir characterization
Modeling geothermal reservoirs