OPM · hakonhagland · Jan 23, 2025
diff --git a/parts/chapters/subsections/5.3/AQUDIMS.fodt b/parts/chapters/subsections/5.3/AQUDIMS.fodt
@@ -4272,7 +4272,7 @@ Updated with AFR/TSA Rev-D comments and new keywords.</dc:description><meta:init
        <text:p text:style-name="P3391">MXNAQC </text:p>
       </table:table-cell>
       <table:table-cell table:style-name="Table36.C9" office:value-type="string">
-       <text:p text:style-name="P1335">A positive integer value that defines the <text:a xlink:href="#__RefHeading___Toc115431_8469479601">AQUCON</text:a> keyword maximum number of lines of connection data associated with this keyword, that is the maximum number of lines of connection data for numerical aquifers.</text:p>
+       <text:p text:style-name="P1335">A positive integer value that defines the <text:a xlink:href="#__RefHeading___Toc115431_846947960">AQUCON</text:a> keyword maximum number of lines of connection data associated with this keyword, that is the maximum number of lines of connection data for numerical aquifers.</text:p>
       </table:table-cell>
       <table:table-cell table:style-name="Table36.D9" office:value-type="string">
        <text:p text:style-name="P3396">1</text:p>
@@ -4315,7 +4315,7 @@ Updated with AFR/TSA Rev-D comments and new keywords.</dc:description><meta:init
        <text:p text:style-name="P3391">NANAQ</text:p>
       </table:table-cell>
       <table:table-cell table:style-name="Table36.C9" office:value-type="string">
-       <text:p text:style-name="P1335">A positive integer value that defines the <text:a xlink:href="#__RefHeading___Toc4428_421927891">AQUFETP</text:a>, <text:a xlink:href="#__RefHeading___Toc202105_1310555686">AQUFLUX</text:a> and <text:a xlink:href="#__RefHeading___Toc120118_846947960">AQUCT</text:a> maximum number of analytical aquifers defined by these three keywords.</text:p>
+       <text:p text:style-name="P1335">A positive integer value that defines the <text:a xlink:href="#__RefHeading___Toc4428_421927891">AQUFETP</text:a>, <text:a xlink:href="#__RefHeading___Toc202105_1310555686">AQUFLUX</text:a> and <text:a xlink:href="#__RefHeading___Toc179876_3429068809">AQUCT</text:a> maximum number of analytical aquifers defined by these three keywords.</text:p>
       </table:table-cell>
       <table:table-cell table:style-name="Table36.D9" office:value-type="string">
        <text:p text:style-name="P3396">1</text:p>

diff --git a/parts/chapters/subsections/5.3/CO2SOL.fodt b/parts/chapters/subsections/5.3/CO2SOL.fodt
@@ -4205,7 +4205,7 @@ Updated with AFR/TSA Rev-D comments and new keywords.</dc:description><meta:init
     <text:p text:style-name="P52">The <text:a xlink:href="#REF_HEADING_KEYWORD_CO2SOL">CO2SOL</text:a> keyword activates dissolved carbon dioxide (CO<text:span text:style-name="T20">2</text:span>) in the water phase, where CO<text:span text:style-name="T20">2</text:span> is represented by the <text:a xlink:href="#__RefHeading___Toc62787_1778172979">SOLVENT</text:a> pseudo component, using the simulator’s CO<text:span text:style-name="T20">2</text:span>-Brine PVT model. This keyword is a compositional keyword in the commercial simulator but has been implemented in OPM Flow’s black-oil model.</text:p>
     <text:p text:style-name="P52">The <text:a xlink:href="#REF_HEADING_KEYWORD_CO2SOL">CO2SOL</text:a> keyword can be used when modelling CO<text:span text:style-name="T20">2</text:span> injection in depleted hydrocarbon reservoirs. See also the <text:a xlink:href="#__RefHeading___Toc387968_1616145207">CO2STORE</text:a> keyword in the <text:a xlink:href="#__RefHeading___Toc55591_1778172979">RUNSPEC</text:a> section which can be used when model<text:span text:style-name="T21">ling</text:span> CO<text:span text:style-name="T20">2</text:span> injection in saline aquifers.</text:p>
     <text:p text:style-name="P52">The CO<text:span text:style-name="T20">2</text:span>-Brine PVT model computes the PVT properties such as density, viscosity, and enthalpy internally as functions of pressure, temperature, and composition by using analytic correlations and models from the literature rather than by interpolation <text:span text:style-name="T21">of</text:span> tabulated values <text:span text:style-name="T21">in the input deck</text:span>. These values are transformed to the standard black-oil equivalent PVT tables internally by the simulator. A full description of the underlying PVT models is described by Sandve et al.<text:note text:id="ftn1" text:note-class="footnote"><text:note-citation>1</text:note-citation><text:note-body>
-       <text:p text:style-name="Footnote">Tor Harald Sandve1, Sarah E. Gasda, Atgeirr Rasmussen, <text:span text:style-name="T22">and</text:span> Alf Birger Rustad. Convective dissolution in field scale CO<text:span text:style-name="T20">2</text:span> storage simulation using the OPM Flow simulator. Submitted to TCCS 11 – Trondheim Conference on CO<text:span text:style-name="T20">2</text:span> Capture, Transport and Storage Trondheim, Norway – June 21-23, 2021.</text:p></text:note-body></text:note>. Note that the CO<text:span text:style-name="T20">2</text:span>-Brine PVT properties depend on the temperature and salinity and these must therefore be entered in the <text:a xlink:href="#__RefHeading___Toc39329_784232322">PROPS</text:a> section. The reservoir temperature can be defined using, e.g., the <text:a xlink:href="#__RefHeading___Toc146399_3544483072">RTEMP</text:a> keyword. Region based salinity can be provided using the <text:a xlink:href="#__RefHeading___Toc405185_1616145207">SALINITY</text:a> keyword.</text:p>
+       <text:p text:style-name="Footnote">Tor Harald Sandve1, Sarah E. Gasda, Atgeirr Rasmussen, <text:span text:style-name="T22">and</text:span> Alf Birger Rustad. Convective dissolution in field scale CO<text:span text:style-name="T20">2</text:span> storage simulation using the OPM Flow simulator. Submitted to TCCS 11 – Trondheim Conference on CO<text:span text:style-name="T20">2</text:span> Capture, Transport and Storage Trondheim, Norway – June 21-23, 2021.</text:p></text:note-body></text:note>. Note that the CO<text:span text:style-name="T20">2</text:span>-Brine PVT properties depend on the temperature and salinity and these must therefore be entered in the <text:a xlink:href="#__RefHeading___Toc39329_784232322">PROPS</text:a> section. The reservoir temperature can be defined using, e.g., the <text:a xlink:href="#__RefHeading___Toc111816_2939291539">RTEMP</text:a> keyword. Region based salinity can be provided using the <text:a xlink:href="#__RefHeading___Toc405185_1616145207">SALINITY</text:a> keyword.</text:p>
     <text:p text:style-name="P52">The <text:a xlink:href="#REF_HEADING_KEYWORD_CO2SOL">CO2SOL</text:a> keyword must be used together with the <text:a xlink:href="#__RefHeading___Toc62787_1778172979">SOLVENT</text:a> keyword in the <text:a xlink:href="#__RefHeading___Toc55591_1778172979">RUNSPEC</text:a> section. The <text:a xlink:href="#__RefHeading___Toc62787_1778172979">SOLVENT</text:a> keyword activates the four component black-oil model: oil, water and gas, plus a solvent (in this case CO<text:span text:style-name="T20">2</text:span>).</text:p>
     <text:p text:style-name="P52">The <text:a xlink:href="#__RefHeading___Toc39767_22671168971">DISGASW</text:a> keyword in the <text:a xlink:href="#__RefHeading___Toc55591_1778172979">RUNSPEC</text:a> section can be used to model dissolution of CO<text:span text:style-name="T20">2</text:span> in the Brine. <text:span text:style-name="T21">Note that hydrocarbon gas is not allowed to dissolve in the Brine (this is considered a reasonable assumption for most hydrocarbon gases).</text:span></text:p>
     <text:p text:style-name="P52">The hydrocarbon <text:span text:style-name="T23">reservoir fluid</text:span> properties should be set up as normal apart from the water PVT properties, which will be defined by the simulators’ CO<text:span text:style-name="T20">2</text:span>-Brine PVT model, so the water PVT keywords (e.g. <text:a xlink:href="#__RefHeading___Toc2086106_3315222525">PVTW</text:a>) are not required. The CO<text:span text:style-name="T20">2</text:span> PVT properties will also be defined by the CO<text:span text:style-name="T20">2</text:span>-Brine PVT model so the solvent PVT keywords (e.g. <text:a xlink:href="#__RefHeading___Toc121471_83452205">SDENSITY</text:a>, <text:a xlink:href="#__RefHeading___Toc414279_1093985484">PVTSOL</text:a>) are also not required.</text:p>
@@ -4238,7 +4238,7 @@ Updated with AFR/TSA Rev-D comments and new keywords.</dc:description><meta:init
     <text:p text:style-name="P50">--</text:p>
     <text:p text:style-name="P50">DISGASW <text:s text:c="75"/></text:p>
     <text:p text:style-name="P48"/>
-    <text:p text:style-name="P51">The second part of the example covers the additional data required in the <text:a xlink:href="#__RefHeading___Toc39329_784232322">PROPS</text:a> section, in which the CO<text:span text:style-name="T20">2</text:span>-gas miscible relative permeabilities are defined using the <text:a xlink:href="#__RefHeading___Toc106880_335817223">SSFN</text:a> keyword. The initial temperature and salinity are defined using the <text:a xlink:href="#__RefHeading___Toc146399_3544483072">RTEMP</text:a> and <text:a xlink:href="#__RefHeading___Toc405185_1616145207">SALINITY</text:a> keywords. The oil and gas PVT properties should be defined in the normal way. No water PVT data is required.</text:p>
+    <text:p text:style-name="P51">The second part of the example covers the additional data required in the <text:a xlink:href="#__RefHeading___Toc39329_784232322">PROPS</text:a> section, in which the CO<text:span text:style-name="T20">2</text:span>-gas miscible relative permeabilities are defined using the <text:a xlink:href="#__RefHeading___Toc106880_335817223">SSFN</text:a> keyword. The initial temperature and salinity are defined using the <text:a xlink:href="#__RefHeading___Toc111816_2939291539">RTEMP</text:a> and <text:a xlink:href="#__RefHeading___Toc405185_1616145207">SALINITY</text:a> keywords. The oil and gas PVT properties should be defined in the normal way. No water PVT data is required.</text:p>
     <text:p text:style-name="P50">-- ==============================================================================</text:p>
     <text:p text:style-name="P50">-- </text:p>
     <text:p text:style-name="P50">-- PROPS SECTION </text:p>

diff --git a/parts/chapters/subsections/5.3/CO2STORE.fodt b/parts/chapters/subsections/5.3/CO2STORE.fodt
@@ -4425,7 +4425,7 @@ Updated with AFR/TSA Rev-D comments and new keywords.</dc:description><meta:init
     <text:h text:style-name="P57" text:outline-level="4"><text:bookmark-start text:name="__RefHeading___Toc14509_37011683881613112"/>Description<text:bookmark-end text:name="__RefHeading___Toc14509_37011683881613112"/></text:h>
     <text:p text:style-name="P79">The <text:a xlink:href="#__RefHeading___Toc387968_1616145207">CO2STORE</text:a> keyword activates the carbon dioxide (CO<text:span text:style-name="T23">2</text:span>) storage model for the run to account for both <text:s/>carbon dioxide and water phase solubility, via the simulator’s CO<text:span text:style-name="T23">2</text:span>-Brine PVT model. This keyword is a compositional keyword in the commercial simulator but has been implemented in OPM Flow’s black-oil model. </text:p>
     <text:p text:style-name="P74">The CO<text:span text:style-name="T23">2</text:span>-Brine PVT model computes the PVT properties such as density, viscosity, and enthalpy internally as functions of pressure, temperature, and composition by using analytic correlations and models from the literature rather than by interpolation from tabulated values. These values are transformed to the standard black-oil equivalent PVT tables internally by the simulator. A full description of the underlying PVT models is described by Sandve et al.<text:note text:id="ftn1" text:note-class="footnote"><text:note-citation>1</text:note-citation><text:note-body>
-       <text:p text:style-name="Footnote">Tor Harald Sandve1, Sarah E. Gasda, Atgeirr Rasmussen, <text:span text:style-name="T26">and</text:span> Alf Birger Rustad. Convective dissolution in field scale CO<text:span text:style-name="T23">2</text:span> storage simulation using the OPM Flow simulator. Submitted to TCCS 11 – Trondheim Conference on CO<text:span text:style-name="T23">2</text:span> Capture, Transport and Storage Trondheim, Norway – June 21-23, 2021.</text:p></text:note-body></text:note>. This means that the normal PVT keywords like <text:a xlink:href="#__RefHeading___Toc45799_719036256">DENSITY</text:a>, <text:a xlink:href="#__RefHeading___Toc104062_57619843">PVTO</text:a>, <text:a xlink:href="#__RefHeading___Toc104056_57619843">PVDG</text:a> etc. are not required by OPM Flow when this model is activated, and if entered will be ignored by the simulator. Note that the CO<text:span text:style-name="T23">2</text:span>-Brine PVT properties depend on the temperature and salinity and these must therefore be entered in the <text:a xlink:href="#__RefHeading___Toc39329_784232322">PROPS</text:a> section. The reservoir temperature can be defined using, e.g., the <text:a xlink:href="#__RefHeading___Toc146399_3544483072">RTEMP</text:a> keyword. Region based salinity can be provided using the <text:a xlink:href="#__RefHeading___Toc405185_1616145207">SALINITY</text:a> keyword. <text:s/></text:p>
+       <text:p text:style-name="Footnote">Tor Harald Sandve1, Sarah E. Gasda, Atgeirr Rasmussen, <text:span text:style-name="T26">and</text:span> Alf Birger Rustad. Convective dissolution in field scale CO<text:span text:style-name="T23">2</text:span> storage simulation using the OPM Flow simulator. Submitted to TCCS 11 – Trondheim Conference on CO<text:span text:style-name="T23">2</text:span> Capture, Transport and Storage Trondheim, Norway – June 21-23, 2021.</text:p></text:note-body></text:note>. This means that the normal PVT keywords like <text:a xlink:href="#__RefHeading___Toc45799_719036256">DENSITY</text:a>, <text:a xlink:href="#__RefHeading___Toc104062_57619843">PVTO</text:a>, <text:a xlink:href="#__RefHeading___Toc104056_57619843">PVDG</text:a> etc. are not required by OPM Flow when this model is activated, and if entered will be ignored by the simulator. Note that the CO<text:span text:style-name="T23">2</text:span>-Brine PVT properties depend on the temperature and salinity and these must therefore be entered in the <text:a xlink:href="#__RefHeading___Toc39329_784232322">PROPS</text:a> section. The reservoir temperature can be defined using, e.g., the <text:a xlink:href="#__RefHeading___Toc111816_2939291539">RTEMP</text:a> keyword. Region based salinity can be provided using the <text:a xlink:href="#__RefHeading___Toc405185_1616145207">SALINITY</text:a> keyword. <text:s/></text:p>
     <text:p text:style-name="P105">The <text:a xlink:href="#__RefHeading___Toc387968_1616145207">CO2STORE</text:a> keyword must be used together with either: (1) the <text:a xlink:href="#__RefHeading___Toc38607_2267116897">GAS</text:a> and <text:a xlink:href="#__RefHeading___Toc38611_2267116897">WATER</text:a> keywords (or alternatively the <text:a xlink:href="#__RefHeading___Toc38607_2267116897 Copy 1">GASWAT</text:a> keyword), or (2) the <text:a xlink:href="#__RefHeading___Toc38607_2267116897">GAS</text:a> and <text:a xlink:href="#__RefHeading___Toc97439_1778172979">OIL</text:a> keywords in the <text:a xlink:href="#__RefHeading___Toc55591_1778172979">RUNSPEC</text:a> section. It is recommended that the standard method option (1) is used. </text:p>
     <text:p text:style-name="P105">The <text:a xlink:href="#__RefHeading___Toc39767_22671168971">DISGASW</text:a> keyword in the <text:a xlink:href="#__RefHeading___Toc55591_1778172979">RUNSPEC</text:a> section can be used with option (1) to model dissolution of CO<text:span text:style-name="T23">2</text:span> in the Brine. </text:p>
     <text:p text:style-name="P105">Option (1) has the advantage that it can be used with the <text:a xlink:href="#__RefHeading___Toc317543_3149455253">VAPWAT</text:a> and <text:a xlink:href="#__RefHeading___Toc332782_3149455253">PRECSALT</text:a> keywords in the <text:a xlink:href="#__RefHeading___Toc55591_1778172979">RUNSPEC</text:a> section to model the impact of both vaporization of residual water and salt precipitation in the near wellbore region on injectivity of CO<text:span text:style-name="T23">2</text:span> injection wells. <text:s/></text:p>

diff --git a/parts/chapters/subsections/5.3/COLUMNS.fodt b/parts/chapters/subsections/5.3/COLUMNS.fodt
@@ -4002,7 +4002,7 @@ Updated with AFR/TSA Rev-D comments and new keywords.</dc:description><meta:init
    <text:section text:style-name="Sect1" text:name="COLUMNS">
 
 <text:h text:style-name="P18337" text:outline-level="3"><text:bookmark-start text:name="__RefHeading___Toc605306_3199477706"/>COLUMNS – Define Input File Column Margins<text:bookmark-end text:name="__RefHeading___Toc605306_3199477706"/></text:h>
-    <text:p text:style-name="P12335">The <text:a xlink:href="#__RefHeading___Toc605462_3199477706">COLUMNS</text:a> keyword defines the input file column margins; characters outside the margins are ignored by the input parser.</text:p>
+    <text:p text:style-name="P12335">The <text:a xlink:href="#__RefHeading___Toc258603_3519154785">COLUMNS</text:a> keyword defines the input file column margins; characters outside the margins are ignored by the input parser.</text:p>
     <text:p text:style-name="P11728">See <text:a xlink:type="simple" xlink:href="#4.1.1.COLUMNS – Define Input File Column Margins|outline" text:style-name="Internet_20_link" text:visited-style-name="Visited_20_Internet_20_Link"><text:bookmark-ref text:reference-format="text" text:ref-name="__RefHeading___Toc258603_3519154785">COLUMNS – Define Input File Column Margins</text:bookmark-ref></text:a><text:s/>in the GLOBAL section for a full description.</text:p>
     <text:p text:style-name="P11728"/>
 

diff --git a/parts/chapters/subsections/5.3/ECHO.fodt b/parts/chapters/subsections/5.3/ECHO.fodt
@@ -4002,7 +4002,7 @@ Updated with AFR/TSA Rev-D comments and new keywords.</dc:description><meta:init
    <text:section text:style-name="Sect1" text:name="ECHO">
 
 <text:h text:style-name="P17685" text:outline-level="3"><text:bookmark-start text:name="__RefHeading___Toc605310_3199477706"/>ECHO – Activate Echoing of User Input Files to the Print File<text:bookmark-end text:name="__RefHeading___Toc605310_3199477706"/></text:h>
-    <text:p text:style-name="P12337">Turns on echoing of all the input files to the print file; note that this keyword is activated by default and can subsequently be switched off by the <text:a xlink:href="#__RefHeading___Toc605482_3199477706">NOECHO</text:a> activation keyword.</text:p>
+    <text:p text:style-name="P12337">Turns on echoing of all the input files to the print file; note that this keyword is activated by default and can subsequently be switched off by the <text:a xlink:href="#__RefHeading___Toc52487_2479612490">NOECHO</text:a> activation keyword.</text:p>
     <text:p text:style-name="P12338">See <text:a xlink:type="simple" xlink:href="#3.1.2.ECHO – Activate Echoing of User Input Files to the Print File|outline" text:style-name="Internet_20_link" text:visited-style-name="Visited_20_Internet_20_Link"><text:bookmark-ref text:reference-format="text" text:ref-name="__RefHeading___Toc52483_2479612490">ECHO – Activate Echoing of User Input Files to the Print File</text:bookmark-ref></text:a><text:s/>in the GLOBAL section for a full description.</text:p>
     <text:p text:style-name="P12338"/>
     <text:p text:style-name="_40_TextBody"/>