Hydraulic Fracturing — Candidate, Design, Diagnosis
A frac is not a treatment you apply to a well that is underperforming. It is a specific answer to a specific limitation, and the first engineering act is deciding whether the well has that limitation at all.
Hydraulic fracturing creates a high-conductivity plane in the rock and props it open so it survives closure stress. Everything else — fluid chemistry, proppant selection, pump schedules, stage counts, diagnostics — exists to control the geometry and conductivity of that plane, or to find out afterwards what actually happened. The discipline splits cleanly into four questions, and they are best kept separate: is this well a candidate, what geometry and conductivity should the fracture have, did the pumping do what was designed, and what did the reservoir actually get. The last one is the least often answered honestly.
Candidate Selection
There are two genuinely different reasons to fracture a well, and confusing them produces designs that optimise the wrong variable.
- Low permeability. The matrix cannot deliver fluid to the wellbore fast enough at any drawdown. The fracture supplies a flow path the rock does not have, and the prize scales with length — reach, not capacity.
- Damage in moderate permeability. The rock can deliver, but a damaged zone near the wellbore is throttling it. A short fracture that simply crosses the damaged region restores the well, and the prize scales with conductivity — capacity, not reach.
Two disqualifiers deserve emphasis because they are physical rather than economic. Without a stress contrast above and below the pay, fracture height is not contained, and a treatment designed for length grows vertically into water or gas instead. And without competent cement, there is no isolation to fracture into — pressure finds the annulus. Neither can be fixed by a better fluid.
Design — The Mechanics Underneath
A fracture opens because injection raises pressure above the minimum in-situ stress. The quantity that matters through the whole design is net pressure — treating pressure minus closure pressure — because it is net pressure that creates width, and width is what admits proppant.
The classical width models remain the vocabulary of the field. PKN, from Perkins and Kern and completed by Nordgren, assumes a fracture much longer than it is tall, with plane-strain in the vertical section — net pressure increases as the fracture extends.[1][2] KGD, from Khristianovich and Zheltov with Geertsma and de Klerk, assumes plane-strain horizontally, appropriate when height exceeds length — and net pressure decreases with extension.[3][4] That opposite sign is not a curiosity; it is the basis of pressure diagnosis during pumping.
Conductivity — and why the “optimum” depends on the question
A propped fracture is only useful if it can carry flow along its length faster than the formation feeds it. That comparison is the dimensionless fracture conductivity, and its consequence is captured by Prats's effective wellbore radius: a fractured well behaves like an unfractured well with a much larger wellbore.[5]
Fluids and proppant
- Slickwater — water with friction reducer. Low viscosity, poor proppant carrying, but cheap, low-damage and capable of creating complex geometry in brittle rock. Requires high rates and fine proppant.
- Linear and crosslinked gels — high viscosity, excellent transport, wider fractures. The cost is residue and conductivity damage, which is what breakers exist to limit.
- Energised and foamed fluids — nitrogen or CO2 assisted; less water in the formation, faster cleanup, favoured in water-sensitive or under-pressured rock.
- Proppant — sand where closure stress allows; resin-coated for flowback control; ceramic where stress crushes sand. Selection is a closure-stress decision first and a cost decision second, because crushed proppant destroys precisely the conductivity the design was built on.
Execution — Reading the Pressure While It Happens
Before the main treatment, a calibration injection — minifrac or DFIT — establishes closure pressure, leakoff behaviour and near-wellbore friction. Closure is the anchor for everything: net pressure cannot be computed without it, and the entire diagnostic framework is built on net pressure.
During pumping, the primary real-time diagnostic is the Nolte-Smith plot: net pressure against time on log-log axes, where the slope indicates what the fracture is doing.[8]
The operational vocabulary follows from it: a pad to open width before proppant arrives, a proppant concentration ramp, a step-down test to separate perforation friction from near-wellbore tortuosity, and a deliberate decision about whether a tip screenout is a failure or, in a frac-pack, the design intent.
Monitoring and Post-Treatment Evaluation
Diagnostics divide by what they can physically see, and treating them as interchangeable is a persistent error.[9][10]
| Method | What it observes | What it cannot tell you |
|---|---|---|
| Treating pressure | Net pressure behaviour, in real time | Where the fracture went |
| Microseismic | Shear events around the growing fracture — stimulated extent | Whether proppant reached there, or whether it conducts |
| Tiltmeter | Deformation → fracture orientation and dip | Length or conductivity |
| Fibre (DAS / DTS) | Fluid and proppant distribution between clusters | Far-field geometry |
| Tracers | Which stages and clusters contribute to flow | Fracture dimensions |
| Post-frac PTA / RTA | Effective half-length and conductivity | What was created but is not producing |
One diagnostic deserves naming because it turns post-frac pressure data into a conductivity number rather than a curve match. Where flow is bilinear — transient linear flow occurring simultaneously in the fracture and in the formation feeding it — pressure plotted against the fourth root of time falls on a straight line, and that slope is inversely proportional to h(kfb)½.[6] It is one of the few places in fracture evaluation where a plot yields conductivity directly.
Published Field Applications
Diagnostics integrated at field scale
The clearest demonstrations of the point above come from campaigns where several diagnostics were run together rather than in isolation. A published Marcellus study integrated fracture diagnostics with engineering data across a development, precisely so that treatment design could be tied to what the diagnostics showed rather than to what the pump schedule intended.[12]
Drainage mapping and the effective-length problem
The gap between created and effective length is not an academic worry; it has been the subject of dedicated field work. A published Bakken case history addressed drainage mapping and effective fracture length directly, combining well-to-well observations with modelling to establish how far the fractures were actually draining — as distinct from how far they were mapped as extending.[13] The same group's earlier work framed the general problem of resolving created, propped and effective fracture length as a single reconciliation exercise rather than three separate measurements.[11]
And the honest reading
What the published record supports is narrower than the marketing around it. Diagnostics reliably distinguish where fluid went from what produces, and the difference is routinely large. Treatments that were designed on created length and evaluated on created length will look better than they are, and the correction — running production-based evaluation and accepting a shorter effective length — is what turns a campaign into a learning system rather than a repeated assumption.
The pumps record what was injected. Only the reservoir records what was achieved, and it answers slowly.
The counter-evidence: most of the treatment may not be producing
The section above would be incomplete without the finding that most challenges the whole enterprise. A study that acquired and interpreted production logs from more than 100 horizontal shale wells across multiple basins found production to be highly variable along the wellbore — and quantified it: in some basins two-thirds of gas production came from only one third of the perforation clusters, and across all basins almost one third of all perforation clusters were not contributing to production at all.[16]
Read that against the design section. A pump schedule is built cluster by cluster and paid for cluster by cluster; if a third of them contribute nothing, then a third of the proppant, fluid, horsepower and pumping time bought nothing. The failure is not in the fracture mechanics — the models in this article are sound — it is in placement between clusters, which limited entry, diversion and cluster spacing exist to control and evidently often do not.
It also reframes every length debate above. Arguing about created versus effective half-length assumes the cluster produced at all. The published record says that assumption is wrong about a third of the time, which is a larger correction than most of the design refinements the industry argues over.
The honest summary of the field record: the physics of a single fracture is well understood, and the distribution of many fractures along a wellbore is not.
Validation
The width and net-pressure models follow Perkins and Kern[1] and Nordgren[2] for the PKN geometry, and Khristianovich and Zheltov[3] with Geertsma and de Klerk[4] for KGD; the underlying crack-opening solution is Sneddon and Elliott's.[14] The effective wellbore radius concept is Prats's,[5] and the conductivity curve computed for Fig. 02 uses the Cinco-Ley and Samaniego pseudo-skin relation,[6] which also supplies the convention that FCD above about 30 is treated as infinite conductivity. The proppant-constrained optimum of about 1.6 is the unified-fracture-design result at low proppant number.[7] The pressure-slope diagnosis in Fig. 03, including the critical pressure and its consequences, is Nolte and Smith's, demonstrated on five treatments.[8] Fracture-diagnostic capabilities and their limits follow Warpinski[9] and Cipolla and Wright.[10] The distinction between created, propped and effective length is Cipolla, Lolon and Mayerhofer's,[11] with field applications in the Marcellus[12] and the Bakken.[13] General treatment design and post-treatment evaluation follow Economides and Nolte.[15] The counter-evidence on cluster contribution — the proportion of perforation clusters producing little or nothing across more than a hundred logged horizontal wells — is Miller, Waters and Rylander’s.[16]
References
- Perkins, T.K. & Kern, L.R. (1961). Widths of Hydraulic Fractures. Journal of Petroleum Technology 13(9), 937–949; SPE-89.
- Nordgren, R.P. (1972). Propagation of a Vertical Hydraulic Fracture. SPE Journal 12(4), 306–314; SPE-3009.
- Khristianovich, S.A. & Zheltov, Y.P. (1955). Formation of Vertical Fractures by Means of Highly Viscous Liquid. Proceedings of the 4th World Petroleum Congress, Section II, Rome, 579–586.
- Geertsma, J. & de Klerk, F. (1969). A Rapid Method of Predicting Width and Extent of Hydraulically Induced Fractures. Journal of Petroleum Technology 21, 1571–1581; SPE-2458.
- Prats, M. (1961). Effect of Vertical Fractures on Reservoir Behavior — Incompressible Fluid Case. SPE Journal 1, 105–118; SPE-1575-G, doi:10.2118/1575-G. Introduces the effective (equivalent) wellbore radius for a fractured well. Note the convention: the classical result is an effective radius of about one quarter of the fracture length measured tip to tip, which is one half of the half-length — the same 0.5 xf plateau reached in Fig. 02. The two statements are identical and are often mistaken for a discrepancy.
- Cinco-Ley, H. & Samaniego, F. (1981). Transient Pressure Analysis for Fractured Wells. Journal of Petroleum Technology 33(9), 1749–1766; SPE-7490-PA, doi:10.2118/7490-PA. Source of the pseudo-skin relation used to compute Fig. 02 and of the convention that FCD > 30 is treated as infinite conductivity. Also establishes the bilinear-flow method: transient linear flow in both fracture and formation gives a straight line on pressure versus the fourth root of time, with slope inversely proportional to h(kfb)½.
- Unified fracture design — the body of work by Valkó and Economides and, for the result quoted here, Daal and Economides (2006). For proppant numbers below about 0.1, a dimensionless fracture conductivity near 1.6 maximises productivity when the proppant volume rather than the fracture length is what is held fixed. Cited as a body of work rather than a single paper because the 1.6 result is reported across several publications in that line.
- Nolte, K.G. & Smith, M.B. (1981). Interpretation of Fracturing Pressures. Journal of Petroleum Technology 33(9), 1767–1775; SPE-8297-PA, doi:10.2118/8297-PA. Identifies confined-height extension, uncontrolled height growth and a critical pressure beyond which extension is significantly reduced; demonstrated on five treatments. See also Nolte, K.G. (1979), Determination of Fracture Parameters from Fracturing Pressure Decline, SPE-8341, and Nolte, K.G. (1986), A General Analysis of Fracturing Pressure Decline with Application to Three Models, SPE Formation Evaluation 1(6), 571–583; SPE-12941-PA.
- Warpinski, N.R. (1996). Hydraulic Fracture Diagnostics. Journal of Petroleum Technology 48(10), 907–910; SPE-36361.
- Cipolla, C.L. & Wright, C.A. (2000). State-of-the-Art in Hydraulic Fracture Diagnostics. SPE-64434-MS, SPE Asia Pacific Oil and Gas Conference, Brisbane.
- Cipolla, C.L., Lolon, E.P. & Mayerhofer, M.J. (2009). Resolving Created, Propped, and Effective Hydraulic-Fracture Length. SPE Production & Operations 24(4), 619–627; SPE-129618-PA.
- Mayerhofer, M.J., Stegent, N.A., Barth, J.O. & Ryan, K.M. (2011). Integrating Fracture Diagnostics and Engineering Data in the Marcellus Shale. SPE-145463, SPE Annual Technical Conference and Exhibition, Denver.
- Cipolla, C., Craig, D., Litvak, M., Prasad, R.S. & McClure, M. (2020). Case History of Drainage Mapping and Effective Fracture Length in the Bakken. SPE-199716-MS, SPE Hydraulic Fracturing Technology Conference, The Woodlands.
- Sneddon, I.N. & Elliott, H.A. (1946). The Opening of a Griffith Crack Under Internal Pressure. Quarterly of Applied Mathematics 4, 262–267.
- Economides, M.J. & Nolte, K.G. (eds.). Reservoir Stimulation (3rd ed.). John Wiley & Sons. Standard reference for treatment design, fluids and proppants, and post-treatment evaluation of fractured well performance.
- Miller, C.K., Waters, G.A. & Rylander, E.I. (2011). Evaluation of Production Log Data from Horizontal Wells Drilled in Organic Shales. SPE-144326-MS, North American Unconventional Gas Conference and Exhibition, The Woodlands, Texas, 14–16 June 2011; doi:10.2118/144326-MS. Production logs from more than 100 horizontal shale wells across multiple basins: in some basins two-thirds of gas production came from one third of the perforation clusters, and across all basins almost one third of clusters were not contributing to production.
Frequently Asked Questions
Which wells are good hydraulic fracturing candidates?
Two cases. Low-permeability rock, where the fracture supplies a flow path the matrix lacks and the prize scales with length. And a damaged well in moderate permeability, where a short highly conductive fracture bypasses the damage and the prize scales with conductivity. Poor candidates: permeability already sufficient, thin pay with close contacts and no stress barrier to contain height, cement unable to support isolation, or too little remaining oil to pay for the job.
What dimensionless fracture conductivity should be targeted?
It depends on what is held fixed. With length fixed and conductivity being chosen, roughly ten to thirty is the accepted range, and beyond about thirty the fracture behaves as infinite conductivity. With proppant volume fixed and the question being how to split it between length and width, the optimum falls to about 1.6 at low proppant number. The two are not in conflict — they answer different questions.
What does the Nolte-Smith plot show?
Net pressure against pumping time on log-log axes. A gentle positive slope is consistent with confined-height extension; flat or declining suggests height growth or loss into natural fissures; a steep rise means restricted extension and a developing screenout. Nolte and Smith framed it around a critical pressure beyond which extension is significantly reduced.
Why do created, propped and effective length differ?
Created is where fluid went, propped is where proppant remained at closure, effective is what produces after cleanup under closure stress — each shorter than the last. Microseismic tends to see the created extent; production and pressure transient analysis see only the effective length, and the difference is routinely large.