
Wewodon supplies modified polymer friction reducers and matching crosslinkers for locally blended fracturing fluids. Adjusting additive loading and crosslinking conditions allows the system to cover slickwater, higher viscosity proppant transport fluids and crosslinked gels. Product grade and formulation are selected for the blending water, reservoir temperature and pumping conditions.
Applications and supply scope
• Hydraulic fracturing in shale, tight sandstone and coalbed methane reservoirs, including continuous mixing across different viscosity stages.
• Blending with saline water or reused flowback, following viscosity, friction-reduction and compatibility testing with the actual water.
• Crosslinkable friction reducers and matching organometallic crosslinkers, with grade, additive loading and crosslinking delay selected for the application.
Figure 1. Illustration of multistage fracturing in a horizontal well.
| Property | Condition | Specification |
| Appearance | As supplied | Pale yellow or beige viscous liquid |
| As-supplied apparent viscosity | 170 s⁻¹ | ≤390 cP |
| Kinematic viscosity | 0.05% | ≥2.0 cSt |
| Friction reduction | 0.1% | ≥70% |
| Base-fluid apparent viscosity | 0.2%, 170 s⁻¹ | ≥9 cP |
| Base-fluid apparent viscosity | 0.3%, 170 s⁻¹ | ≥15 cP |
| Base-fluid apparent viscosity | 0.5%, 170 s⁻¹ | ≥30 cP |
| Crosslinking response | With matching crosslinker | Forms a cohesive crosslinked gel |
These values support initial product comparison. Confirm the grade, concentration basis, water, temperature and test procedure during qualification; results are application dependent.
The reference viscosity range is approximately 5–100 cP as friction reducer loading is varied, covering the viscosity requirements of slickwater, proppant transport fluid and crosslinked gel. Confirm the corresponding concentration, shear rate, temperature and blending water during evaluation. The table above provides concentration specific viscosity values for initial comparison.
• Electrostatic repulsion along the polymer chains aids dispersion. Intermolecular associations are limited at lower concentration and develop into a network as concentration increases.
• The matching crosslinker forms a delayed crosslinked network to balance friction pressure during wellbore transit and downhole proppant transport under qualified temperature and timing conditions.
• Continuous mixing and viscosity changes can simplify switching between fluid stages. Higher transport-fluid viscosity can help reduce settling and screenout risk, depending on formulation, rate, proppant concentration and fracture conditions.
Variable Viscosity Fracturing Fluid System
Mixing and crosslink control
The rapid dissolving crosslinkable grade is reported to dissolve in less than 30 s and develop 80% of its stabilized viscosity within 3 min. These describe dissolution and viscosity development separately. Verify both against water temperature, mixing shear and dosing equipment. The matching crosslinker controls metal ion release with temperature; crosslinking delay is adjusted to wellbore residence time and the temperature profile.
|
Products in the original comparison |
Dissolution time |
|
Rapid-dissolving crosslinkable friction reducer |
<30 s |
|
Reference domestic emulsion friction reducer, molecular weight 8 million |
30–50 s |
|
Reference domestic emulsion friction reducer, molecular weight 12 million |
>1 min |
|
Reference domestic powder friction reducer, molecular weight 8 million |
>15 min |
|
Reference domestic powder friction reducer, molecular weight 8 million |
>30 min |
Values from the reference comparison. Both powder entries are labelled with molecular weight 8 million in the source, without further sample identification. Confirm water, temperature, mixing procedure and sample identity for a comparative evaluation.
The reference comparison shows dissolution in seconds for the rapid-dissolving crosslinkable grade, reducing premixing time relative to the listed conventional powder samples. This supports continuous mixing and on-the-fly pumping. Changes in site footprint and preparation time depend on equipment and operations.
Reference application example for temperature-controlled crosslinking
A shale gas application example uses a wellbore volume of approximately 283–314 bbl (45–50 m³) and a pump rate of 100.6 bbl/min (16 m³/min), giving a nominal wellhead to bottomhole transit time of about 3 min. A crosslinking delay of 2–3 min was used to limit friction pressure during wellbore transit and form a proppant carrying gel downhole. These are reference application values. Adjust the actual delay for effective flow path volume, pump rate, temperature profile and field mixing conditions.