Proppant Crushing
and
Fines Generation
in Waterfracs

Design engineers must consider numerous criteria when selecting
waterfrac proppants. The most critical of these is long-term
fracture flow capacity, which is directly influenced by the amount
of fines present in the proppant pack.
The most predominant problem that occurs due to improper proppant
selection is proppant crushing. Proppant crushing occurs when
the fracture closure stress exceeds the strength of the proppant
that is placed in the fracture. This leads to the creation of
fines which can migrate and plug a proppant pack, causing diminished
well production.
5% fines generation = 60% decrease in fracture flow capacity*
Prime Plus™ reduces proppant crushing and fines migration in
several distinct ways. The resin coating provides additional
strength to individual grains, generates uniform stress distribution
throughout the pack, and mitigates fines migration by encapsulating
loose fines within the resin coating.
“Real-World” Fracture Flow
Capacity
A variety of variables influence fracture flow capacity, which
directly relates to well production. The table below clearly
shows how Prime Plus compares to other proppants used in the
waterfrac market.
Factors Affecting
Fracture Flow Capacity |
Prime Plus |
Northern White
Frac Sand |
Tempered
Resin Coated Sand |
Economy Lightweight
Ceramics |
| Baseline Proppant Conductivity |
Excellent |
Poor |
Excellent |
Excellent |
| Proppant Flowback Control |
Excellent |
None |
None |
None |
Reduced Fines Generation
and Migration |
Excellent |
None |
Fair |
None |
Proppant Pack Cyclic
Stress Resistance |
Excellent |
None |
Poor |
None |
Comparing Proppant Performance with
Laboratory
Conductivity Data
 |
| Baseline long-term conductivity at
250°F (121°C) between Ohio sandstone core (0.1
millidarcy, 129 cm2) with 2% KCl. Reduced effective conductivity
based on Coulter & Wells findings of effects of fines. |
The graph represents fines impact on fracture flow capacity.
The conductivity reduction was calculated using the Coulter & Wells
Method (SPE Paper 3298). A typical baseline conductivity test
is run at a flowrate of .0051 CFD, therefore fines do
not migrate. Typical waterfrac flowrates are 1-10 MMCFD,
which causes migration of fines and a decrease in conductivity.
Compared to the lab testing, a “real-world” flowrate
is a billion times greater or more.
Fines Generation Comparison of Waterfrac
Proppants
 |
| Modified API RP-56 crush resistance
test procedure ran to more realistically represent downhole
conditions. Prior to testing, samples are exposed to 2% KCl
fluid at 200°F (93°C) for 24 hours
under 1,000 psi closure stress. |
The chart shows that Prime Plus offers the lowest fines generation
of any waterfrac proppant. Hexion’s Wet, Hot Crush Test
was used to compare Prime Plus to Northern White Frac Sand, Economy
Lightweight Ceramic, and Tempered Resin Coated Sand. The fines
generated by other waterfrac proppants greatly decrease well
production. The photos below demonstrate what each proppant looks
like under 8,000 psi and 10,000 psi closure stress.

Cyclic Stress Resistance – Comparison
of Prime Plus to
Economy Lightweight Ceramic
 |
The proppant pack is subjected to
numerous
stress cycles throughout the life of the well |
 |
Throughout the life of a well, a proppant pack is subjected
to numerous stress cycles caused by well interventions and shut-ins. These
changes in stress can cause the proppant pack to shift, fatigue, and generate
fines - leading to decreased conductivity
Cyclic
Stress Testing Procedure:
- Cycled from 3,000 psi to 8,000 psi for a total of 3 cycles
- Temperature held at 200°
F
- Exposed to 2% KCl solution
Results:
- Economy Lightweight Ceramic 40/70 generated 9.1% fines -
equivalent to a 65% decrease in conductivity
- Prime Plus generated only 0.75%
fines - minimal decrease in conductivity
|