aozun
Ammonium Persulphate Encapsulated Gel Breaker
WHITE OR SLIGHT YELLOW GRANULAR
7727-54-0
H8N2O8S2
228
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Product Description
Ammonium Persulphate Encapsulated Gel Breaker is a controlled-release oxidative breaker developed for polymer-based hydraulic fracturing fluids. It consists of an ammonium persulfate, or APS, active core protected by a specially designed coating.
The coating limits premature contact between APS and the fracturing-fluid polymer during surface mixing, pumping and proppant placement. Under the selected downhole conditions, the coating allows or triggers release of the oxidizing active, which degrades polymer chains and reduces fluid viscosity for cleanup and flowback.
The product may also be described as Encapsulated Ammonium Persulfate, Coated APS Breaker, Controlled-Release Persulfate Breaker or Delayed Gel Breaker.
Product type: Controlled-release oxidative gel breaker
Active core: Ammonium persulfate
Active CAS number: 7727-54-0
Active formula: (NH₄)₂S₂O₈
Finished-product CAS: Mixture; not normally represented by one CAS number
Typical form: Coated free-flowing granules
Primary application: Hydraulic fracturing-fluid viscosity reduction
Release principle: Time-, temperature-, diffusion- and/or stress-controlled
Chemical category: Encapsulated inorganic oxidizer formulation
Available release profiles, active content and particle-size ranges must be confirmed against the selected product grade and Technical Data Sheet.
Ammonium persulfate produces reactive oxidizing species after release and activation in the aqueous fracturing fluid. These species attack the long polymer chains responsible for fluid viscosity, reducing their molecular weight and allowing the fluid to lose viscosity.
The coating delays this reaction so that the fracturing fluid can retain sufficient viscosity while it is being pumped and transporting proppant.
Coated breaker granules are added to the fracturing-fluid system.
The protective coating limits immediate dissolution of the APS core.
The intact fluid maintains viscosity during pumping and proppant transport.
Water, temperature, time, pressure or mechanical stress affects the coating.
APS is progressively released into the fluid.
Oxidation reduces polymer molecular weight and fluid viscosity.
The spent fluid can flow back more easily from the fracture and proppant pack.
The actual release mechanism depends on the coating chemistry and particle design. It may involve diffusion, coating permeability, erosion, swelling, cracking under stress or a combination of mechanisms.
Uncoated ammonium persulfate can begin reacting as soon as it dissolves in the aqueous fluid. If activation occurs too early, the fracturing fluid may lose viscosity before completing proppant placement.
Encapsulation can help:
Delay initial breaker activity
Maintain pumping viscosity
Preserve proppant-carrying capacity
Permit a higher total breaker concentration
Distribute breaker through proppant-laden stages
Promote more complete polymer degradation
Improve cleanup of the proppant pack
Reduce residual polymer damage
Support more predictable flowback timing
Improve retained fracture conductivity
These benefits depend on matching the release profile to the fluid system and downhole conditions. Encapsulation does not guarantee performance without laboratory qualification.
Selection factor | Encapsulated APS | Unencapsulated APS |
|---|---|---|
Initial contact with water | Restricted by coating | Dissolves directly |
Break timing | Delayed or controlled | Earlier and more immediate |
Risk of premature viscosity loss | Reduced when correctly selected | Generally higher |
Total breaker loading | Can potentially be increased | Often limited by early viscosity loss |
Release profile | Influenced by coating, temperature, pressure and time | Primarily controlled by dissolution and activation |
Particle behavior | Must survive mixing and pumping | No coating-strength requirement |
Cost | Higher because of encapsulation | Generally lower |
Qualification | Requires release and rheology testing | Requires temperature and concentration testing |
The two products should not be substituted on an equal-weight basis without correcting for active APS content and release efficiency.
“Low temperature,” “medium temperature,” “high temperature” and “extra-high temperature” are product-series descriptions rather than universal industry specifications.
An LT grade is designed to release at comparatively lower bottomhole temperatures. It may use a thinner, more permeable or more readily activated coating.
Selection considerations include:
Minimum bottomhole temperature
Need for a low-temperature activator
Pumping time
Shut-in time
Fluid pH
Salinity
Desired final break time
An MT grade provides an intermediate release profile for moderate-temperature treatments.
It may be selected when an LT product releases too quickly but an HT coating would delay cleanup excessively.
An HT grade uses a more temperature-resistant or less permeable coating to limit premature release at elevated temperatures.
It is commonly evaluated for:
Longer pumping schedules
High-temperature reservoirs
High breaker concentrations
Crosslinked guar systems
Treatments requiring delayed cleanup
An XHT product is designed for more demanding thermal exposure and extended treatment conditions.
The buyer should request release curves and fluid-break data at the actual bottomhole temperature rather than relying only on the XHT designation.
Breaker selection should be based on the entire treatment design.
Provide the supplier with:
Static bottomhole temperature
Estimated dynamic treatment temperature
Total pumping time
Expected shut-in time
Base-fluid composition
Fluid pH
Total dissolved solids
Calcium, magnesium and iron content
Polymer type and concentration
Crosslinker chemistry
Proppant type and loading
Additive sequence
Desired break time
Maximum permitted early viscosity loss
Target final viscosity
Required cleanup or conductivity result
Two wells at the same static temperature may require different breaker grades because their pumping time, fluid chemistry, pressure and proppant schedule differ.
Parameter | Why it matters |
Appearance | Supports product identity and detects damaged coating or contamination |
Active APS content | Determines available oxidizing capacity |
Coating percentage | Influences active loading and release profile |
Moisture | Can affect stability, flowability and premature activation |
Particle-size distribution | Influences blending, transport, placement and release uniformity |
Fines content | Excess fines may release earlier than intact granules |
Oversize particles | May affect feeders, screens and placement |
Bulk density | Supports dosing and packaging calculations |
Specific gravity | Helps evaluate slurry behavior and placement |
Flowability | Important for dry additive feeders and field handling |
Initial release | Indicates the risk of premature breaker exposure |
Cumulative release | Describes release over the planned treatment period |
Mechanical strength | Indicates resistance to mixing, pumping and proppant abrasion |
Active oxygen | May be used as an alternative measure of oxidizing capacity |
Storage stability | Confirms retention of coating and APS performance |
A specification stating only “encapsulated ammonium persulfate” is not sufficient for technical comparison.
A release result has meaning only when the test conditions are stated.
Every release curve should identify:
Test temperature
Test duration
Water or brine composition
pH
Calcium and magnesium concentration
Test pressure
Agitation or shear
Presence of proppant
Breaker concentration
Particle-size range
Analytical method
Sampling intervals
Whether release is reported as APS, persulfate or active oxygen
A product showing slow release in fresh water at atmospheric pressure may behave differently in high-salinity fluid, under closure stress or after abrasive contact with proppant.
Higher temperature generally accelerates water penetration, coating change, persulfate activation and polymer oxidation. The magnitude of this effect depends on the coating and fluid chemistry.
The release profile must protect the fluid for the required pumping period while still allowing cleanup within the planned shut-in and flowback schedule.
Pumping, perforation passage, proppant contact and fracture closure can damage or rupture a coating. Mechanical strength should be sufficient to prevent excessive surface release while still supporting the intended downhole mechanism.
Persulfate activity, polymer stability and coating behavior can all change with pH. Testing should use the expected fracturing-fluid pH rather than neutral laboratory water unless neutral water represents the field system.
Chlorides, hardness ions and total dissolved solids can influence coating permeability, APS dissolution and polymer-breaking performance.
Coated particles can experience abrasion and crushing when transported with proppant. Release testing without proppant may underestimate mechanical damage.
Encapsulated APS breakers are commonly evaluated with polysaccharide-based fracturing fluids, including:
Guar
Hydroxypropyl guar
Carboxymethyl hydroxypropyl guar
Linear gels
Borate-crosslinked gels
Selected metal-crosslinked systems
Foamed gel systems
Compatibility must also be checked with:
Crosslinkers
Buffers
Clay stabilizers
Surfactants
Scale inhibitors
Biocides
Friction reducers
Iron-control agents
Mutual solvents
Brines and recycled water
A breaker compatible with one guar and crosslinker package may not provide the same result with another system.
The product is intended for treatments requiring polymer viscosity during placement followed by delayed and controlled viscosity reduction.
Encapsulated APS is commonly used to degrade guar and guar-derivative polymers after they have transported proppant into the created fracture.
The controlled release helps separate the proppant-placement period from the gel-breaking period.
Crosslinked fluids can provide high viscosity and proppant suspension but may require a greater degree of polymer degradation during cleanup.
Breaker selection should consider both the polymer backbone and crosslinking chemistry.
Higher breaker loading may be required to distribute active material throughout a dense proppant pack. Encapsulation can limit the early viscosity reduction that would otherwise result from increasing uncoated breaker concentration.
Treatments with extended pumping times require sufficient coating integrity to prevent excessive APS release before placement is completed.
HT and XHT coatings can delay release during elevated-temperature exposure. Actual temperature capability must be established through dynamic rheology and release testing.
Encapsulated breaker can form part of a cleanup strategy intended to reduce polymer residue and improve flowback. Conductivity, regained-permeability or proppant-pack testing should be used to validate the complete treatment design.
A technically useful breaker evaluation should include more than a bottle test.
Measure the fracturing fluid without breaker to establish its thermal stability and normal viscosity profile.
Confirm that the selected breaker concentration does not cause unacceptable viscosity loss during the intended pumping period.
Evaluate viscosity under representative temperature, shear and time conditions.
Measure initial and cumulative APS release under representative brine, pH, temperature and pressure conditions.
Measure final viscosity after the planned break period. Define the measurement temperature and shear rate.
Determine insoluble or filterable residue from both polymer degradation and coating material.
Where performance risk justifies it, test the treated fluid in a proppant pack or formation-core system.
Check for precipitation, coating damage, unexpected gas generation, color change or performance loss when the breaker is combined with the complete additive package.
There is no universal dosage for encapsulated APS.
The required concentration depends on:
Polymer loading
Polymer type
Crosslink density
Active APS percentage
Coating percentage
Temperature
Pumping and shut-in time
Fluid pH
Water salinity
Desired final viscosity
Cleanup target
Proppant concentration
Other breakers or activators
Dosage should be established through laboratory testing and confirmed by qualified stimulation personnel. Published competitor dosages should not be transferred directly to another breaker grade.
Possible causes include:
Incorrect temperature grade
Excess fines
Coating damage during handling
Abrasion by proppant
Excessive shear
High temperature
Chemical incompatibility
Excess breaker concentration
Possible causes include:
Coating that is too resistant
Low downhole temperature
Insufficient time
Low active APS loading
Inadequate breaker concentration
High polymer loading
Unexpected fluid chemistry
Poor breaker distribution
Possible causes include:
Broad particle-size distribution
Segregation during transport
Moisture exposure
Variable coating thickness
Damaged packaging
Inadequate sampling
Non-representative laboratory test conditions
Encapsulated breaker may be supplied in approved moisture-resistant bags, pails, drums or bulk containers. Actual packaging depends on the grade, transport classification and customer requirements.
Store the product:
In its original tightly closed packaging
In a cool, dry and ventilated area
Protected from moisture and direct heat
Away from reducing agents and incompatible chemicals
Away from unapproved combustible contamination
Under the temperature conditions stated in the SDS
With oxidizing chemicals segregated according to local requirements
Rough handling, crushing or repeated transfer can create fines and damage the coating.
Use clean, dry equipment for sampling and transfer. Never return contaminated material to the original package.
The active ammonium persulfate core is a strong oxidizing agent. Encapsulation controls release but does not eliminate the underlying chemical hazard.
Depending on the product composition, the finished formulation may be classified for:
Oxidizing properties
Harmful effects if swallowed
Skin irritation
Eye irritation
Respiratory irritation
Skin sensitization
Respiratory sensitization
Use suitable ventilation, chemical-resistant gloves, protective clothing and eye/face protection. Avoid inhaling dust and prevent contact with incompatible materials.
Some encapsulated APS products are transported as UN 1444, Ammonium Persulfate, Class 5.1, Packing Group III. However, transport classification can vary with coating composition, active content and jurisdiction.
Always use the shipment-specific SDS and transport documentation rather than assigning the uncoated APS classification automatically.
Buyers may request:
Certificate of Analysis
Safety Data Sheet
Technical Data Sheet
Product specification
Active APS declaration
Coating-percentage declaration
Particle-size distribution
Initial-release result
Cumulative-release curve
Temperature-specific rheology data
Moisture result
Active-oxygen result
Mechanical-strength data
Residue data
Compatibility test results
Country-of-origin statement
Transport classification
Shelf-life or retest statement
Change-notification policy
Packaging specification
Test methods and conditions should accompany performance data.
For an accurate technical recommendation and quotation, provide:
Required LT, MT, HT or XHT grade
Bottomhole static temperature
Estimated dynamic treatment temperature
Pumping time and shut-in time
Polymer type and concentration
Crosslinker type
Fluid pH
Water salinity and hardness
Proppant type and loading
Target break time
Target final viscosity
Required APS active content
Required particle-size range
Packaging preference
Order quantity and annual demand
Delivery country, city or port
Required technical and regulatory documents
It is a controlled-release oilfield additive containing an ammonium persulfate oxidizer core protected by a coating. It is designed to delay polymer degradation until after fracturing-fluid placement.
Encapsulation limits premature contact between APS and the polymer, helping the fluid maintain viscosity during pumping and proppant transport.
The APS active core has CAS No. 7727-54-0. The finished encapsulated product is a mixture and may not have one CAS number.
The active ammonium persulfate core is inorganic. The complete product is a composite formulation containing an inorganic oxidizer and usually an organic or polymeric coating.
It is a specialty fine chemical and oilfield performance additive. It is not normally classified as a chemical intermediate.
LT grades are designed for release at comparatively lower temperatures. HT grades use a more resistant coating to delay release under higher-temperature conditions. The actual temperature ranges are product-specific.
Not on an equal-weight basis. The active APS content is lower because part of the product mass is coating, and the release profile differs.
No. It must be tested with the actual polymer, crosslinker, brine and additive package.
Release can be affected by temperature, time, coating thickness, particle size, pH, salinity, pressure, mechanical stress and proppant abrasion.
No coating provides absolute isolation under every condition. Initial release and fines content should be included in the product specification.
Useful tests include release rate, dynamic rheology, early-time viscosity, final break viscosity, residue, compatibility and proppant-pack conductivity.
Yes. The coating controls exposure and release but does not remove the oxidizing hazard of the APS core.
Dosage should be determined by laboratory testing under representative fluid, temperature, shear, salinity and time conditions.
Send us your bottomhole temperature, pumping time, fluid system, polymer loading, water chemistry, required break time, packaging and delivery destination.
We will evaluate the appropriate release grade and confirm the available APS content, particle-size range, specification, technical documentation and commercial terms.