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an integrated steady-state - International Geothermal Association

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162<br />

Although the e c<strong>an</strong>not in itself address concerns about NaCl or content values to be entered into the simulator.<br />

the a particular drawdown it<br />

the user with a choiceof such relahonshipsto apply.<br />

The result<strong>an</strong>t lower bound profiles c<strong>an</strong> be displayed<br />

Lower bound <strong>an</strong>alysisis described in<br />

Gunn et al. (submitted).<br />

pre of e is of <strong>an</strong> ongoing study<br />

it is to extend the<br />

scope of the package to include the of tr<strong>an</strong>sient<br />

STEADY-STATE SIMULATION FEATURES<br />

effects.<br />

The module of the packa e is the <strong>steady</strong>-<strong>state</strong> simulation<br />

SIMULATION AND ANALYSIS MODULES<br />

includes the<br />

features.<br />

liquid, two-phase, <strong>an</strong>d superheated steam flow.<br />

The packa e includes five main simulation <strong>an</strong>d <strong>an</strong>alysis<br />

Incorporates dissolved solids content by <strong>an</strong> equivalent<br />

modules, are as follows.<br />

percent of NaCl.<br />

non-condensable gas content by <strong>an</strong><br />

Discharge Test Simulation<br />

This is the core module of the packa e. It allows the<br />

simulation of <strong>steady</strong>-<strong>state</strong> flow in a well at a<br />

single mass flowrate, The features, assumptions <strong>an</strong>d<br />

module are discussed more<br />

later of paper.<br />

Preprocessing Fluid Composition <strong>an</strong>d Properties<br />

The input parameters for a discharge test include fluid<br />

<strong>an</strong>d fluid sition, some of which ma be<br />

or other measurements.<br />

values will not all be consistent with to<br />

each other, <strong>an</strong>d in some cases various parameters will be<br />

Inconsistenciesc<strong>an</strong> be due to measurement error,<br />

but typical1 measured enthal y values may not be<br />

appropriate to the resence or dissolved solids.<br />

Inconsistencies may result related measurements<br />

having been observed at different times. Wellhead <strong>an</strong>d<br />

deepestfeed conditions into the simulationmodule are<br />

preprocessed to ensure that a consistent <strong>an</strong>d/or<br />

complete set of input is used in the discharge test<br />

simulation. A is not allowed to proceed without<br />

such a step having first been performed<br />

Output Test Simulation<br />

In the real world a number of actual discharge tests on a<br />

geothermal well c<strong>an</strong> be performed to the well's<br />

characteristic output or<br />

this is <strong>an</strong><br />

expensive o package a module for<br />

such a series of discharge test<br />

simulations produce <strong>an</strong> estimateof the output curve. Such<br />

a procedure termed <strong>an</strong> out ut test As part of the<br />

simulation the module c<strong>an</strong> requested to calculate suitable<br />

drawdown parameters at the dee feed zone.Results c<strong>an</strong><br />

be presented<br />

in a text format. An<br />

example of procedure is the case study in the<br />

final section of<br />

Matching Analysis<br />

As above <strong>an</strong>alysis is a tool c<strong>an</strong> be<br />

used to calibrate the mput parameters to the simulator.<br />

Measured downhole pressure <strong>an</strong>d<br />

c<strong>an</strong> be<br />

entered into the package to allow their subsequent comparison<br />

against simulated results. The profiles c<strong>an</strong> be compared<br />

allow ' matching, or a simple<br />

matchmg report c<strong>an</strong> be produced.<br />

Lower Bound Analysis<br />

As noted above, observed downholeprofiles in discharging<br />

wells c<strong>an</strong> be subject to signific<strong>an</strong>t measurement error.Lower<br />

bound <strong>an</strong>al is a for estimating the of<br />

measured for to matching <strong>an</strong>alysis.<br />

method works by simply <strong>an</strong>alysing the consistency of<br />

measured pairs of two-phase pressure <strong>an</strong>d temperature<br />

measurements taken at intervals down the wellbore. The<br />

<strong>an</strong>alysis estimates the minimum C02 or NaCl content<br />

for each pair to satisf saturation condition, If these<br />

minimum values, or lower have considerable<br />

the then the data c<strong>an</strong> considered<br />

to be of use for or flwd parameters.<br />

In some cases such <strong>an</strong>alysis c<strong>an</strong> aid the<br />

or<br />

verification of feed zone locations, <strong>an</strong>d also suggest calibrated<br />

equivalentweight percent of<br />

Estimates the effectof both NaCl <strong>an</strong>d<br />

on fluid liquid<br />

of on fluid vapour phase<br />

<strong>an</strong>d on superheatedsteam properties.<br />

Allows or deepest calculation.<br />

Models secondary feed zones, <strong>an</strong>d calculates fluid<br />

compositionat feeds.<br />

Allows linear, quadratic, or superheated steam<br />

drawdown relationshipsto be specified at each<br />

calculating mass flowrate.<br />

Allows multiplech<strong>an</strong>gesof casin <strong>an</strong>d liner diameter,<br />

roughness to be (A of st<strong>an</strong>dard casing<br />

<strong>an</strong>d liner sizes is included).<br />

Models the effect of deviations in the wellbore from<br />

vertical on the pressure,<br />

Models the rock formation<br />

<strong>an</strong>d well<br />

Provides results at each depth of interest for:<br />

pressure; temperature; enthalpy; dryness; wei ht percent<br />

of NaCl the liquid phase; pressure<br />

flowrate; flow regime or fluid.type; <strong>an</strong>d, frictional,<br />

<strong>an</strong>d<br />

pressure<br />

Provides<br />

of simulated downhole pressure<br />

<strong>an</strong>d<br />

SIMULATION ASSUMPTIONS AND<br />

CORRELATIONS<br />

The stead -<strong>state</strong> simulation module of the has been<br />

<strong>an</strong>d su uently the two<br />

<strong>an</strong>d by<br />

ad n for superheated steam flow.<br />

programsit has been assumed that:<br />

flow is <strong>steady</strong> <strong>an</strong>d<br />

are<br />

const<strong>an</strong>t a depth<br />

<strong>an</strong>d<br />

dissolved solids <strong>an</strong>d non-condensable gases c<strong>an</strong> be<br />

resented by <strong>an</strong> equivalent NaCl content <strong>an</strong>d eqwvalent<br />

C content<br />

Fluid Properties<br />

The formulae evaluating fluid are those outlined<br />

in Hadgu (1989). is considered toaffect:<br />

overall fluid pressure, <strong>an</strong>d the partial pressure of is<br />

determined from the relationship by Sutton (1976) <strong>an</strong>d<br />

from Henry's Law (the reason for using Sutton's<br />

relationship as a ainst that found<br />

Dalton's<br />

Law is GUM <strong>an</strong>d Freeston (m<br />

of the vapour phase only (from et<br />

enthalpy of both liquid <strong>an</strong>d vapour phases (from Hadgu,<br />

1989);<strong>an</strong>d<br />

viscosity of the vapour phase only (from Pritchett et al.,<br />

1981).<br />

NaCl is considered to affect<br />

pressure (from Haas, 1976);

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