CO₂ Dry-Method Proppant-Filled Fracturing Technology: Principles, Implementation, and Integration with Clad Pipe Systems

1. Definition and Fundamental Principles

CO₂ dry-method proppant-filled fracturing (CO₂干法加砂压裂) is an advanced reservoir stimulation technique that employs supercritical or subcritical carbon dioxide as the primary carrier fluid to transport proppant (sand) into naturally or artificially created fractures in tight, low-permeability, or unconventional reservoirs. Unlike conventional water-based (slickwater) hydraulic fracturing, the dry CO₂ method eliminates the need for large volumes of water, chemical additives, and associated flowback water management.

The fundamental operating principle relies on the unique thermophysical properties of carbon dioxide at reservoir conditions. When CO₂ is injected at pressures exceeding its critical pressure (7.38 MPa) and temperatures above its critical temperature (31.1 °C), it enters a supercritical state where it exhibits gas-like viscosity and diffusivity combined with liquid-like density and solvency. This supercritical state enables:

2. Category and Business Positioning

Within the operational framework of Cladding Technology Shanxi Co., Ltd., CO₂ dry-method fracturing technology occupies a strategic position at the intersection of materials engineering and oilfield services. The company's core competencies in bimetallic cladding, weld overlay, and explosion welding directly serve the demanding material requirements of CO₂ fracturing operations:

3. Technical Purpose and Value

3.1 Reservoir Stimulation Objectives

CO₂ dry-method proppant-filled fracturing addresses several critical challenges in modern hydrocarbon production:

3.2 Value to Cladding Technology Shanxi Co., Ltd.

The study and practical implementation of CO₂ fracturing technology provides direct value to the company's core business through:

4. Key Process and Implementation Points

4.1 CO₂ Dry Fracturing Process Flow

  1. CO₂ sourcing and preparation: Industrial-grade CO₂ (purity ≥99.5%) is sourced from natural gas processing, flue gas capture, or dedicated CO₂ production facilities. The CO₂ is compressed to liquid state at surface conditions (typically 5–15 MPa at 15–25 °C).
  2. Proppant preparation: Proppant (typically 20/40 mesh or 40/70 mesh ceramic or quartz sand) is loaded into a dry mixing system. Unlike water-based fracturing, no slurry is prepared—the proppant is injected separately or mixed with CO₂ in a dry blending device.
  3. Injection system deployment: A specialized high-pressure CO₂ injection system (capable of 35–70 MPa) with dry proppant injection capability is rigged at the wellhead. The system includes CO₂ storage tanks, high-pressure pumps, proppant dry blender, and downhole pressure control equipment.
  4. Fracture initiation and propagation: CO₂ is injected at controlled rates (typically 5–30 m³/min for gas wells) to initiate and propagate fractures. The low viscosity of CO₂ creates tortuous, branched fracture networks.
  5. Proppant placement: Dry proppant is injected either simultaneously with CO₂ or in a separate stage. The CO₂'s phase transition energy at reservoir conditions provides the driving force for proppant placement into fracture networks.
  6. Well shut-in and flowback: After injection, the well is shut in to allow proppant settling and fracture closure. Flowback is primarily CO₂ gas with minimal liquid return.

4.2 Critical Process Parameters

Parameter Typical Range Function/Significance
CO₂ injection pressure 35–70 MPa Exceeds fracture initiation pressure; maintains supercritical state in wellbore
CO₂ injection rate 5–30 m³/min Controls fracture geometry; higher rates create wider, more complex fractures
Proppant concentration 0.5–2.0 kg/L (CO₂ equivalent) Controls fracture conductivity; must balance placement efficiency with fracture height
Proppant type Ceramic (3.5 SG) or quartz (2.65 SG) Higher density proppant resists closure better in high-stress environments
Proppant size 20/40 mesh (primary), 40/70 mesh (lead) Graded sizes optimize near-wellbore and far-field fracture conductivity
Reservoir temperature 35–90 °C Must exceed CO₂ critical temperature (31.1 °C) for supercritical behavior
Reservoir pressure 8–30 MPa Determines phase transition energy available for proppant placement
Total CO₂ volume per stage 50–500 m³ Determines fracture volume and stimulated reservoir volume
Shut-in time 24–72 hours Allows proppant settling, fracture closure, and CO₂ diffusion into formation

4.3 Dry Mixing Technology

The critical innovation in "dry-method" (干法) CO₂ fracturing is the elimination of water-based slurry preparation. Proppant is introduced into the CO₂ stream using one of the following dry mixing approaches:

5. Applicable Standards and Acceptance Criteria

5.1 Equipment and Materials Standards

Standard Title/Scope Relevance to CO₂ Fracturing
API 5CT Specification for casing and tubing Wellbore integrity during high-pressure CO₂ injection; corrosion resistance requirements
API 5L Pipe line pipe specifications Surface CO₂ transport piping; pressure rating and material selection
API 6A Specification for wellhead and Christmas tree equipment Wellhead equipment rated for CO₂ service conditions
ASME B31.3 Process piping Surface CO₂ piping system design, pressure testing, and inspection
ASME BPVC Section VIII Pressure vessels CO₂ storage tanks and high-pressure equipment design and fabrication
NACE MR0175 / ISO 15156 Materials for use in H₂S-containing environments Material selection for sour gas wells where CO₂ fracturing is applied
ASTM A398 / A399 Friction stir welding consumable materials Related to clad pipe joint integrity in CO₂ service
GB/T 21832 Oil and natural gas industry — Welded steel pipe for casing and tubing Domestic standard for wellbore pipe used in CO₂ fracturing operations
SY/T 5448 Hydraulic fracturing proppant — Ceramic Proppant quality specifications for Chinese oilfield applications
SY/T 5329 Hydraulic fracturing — Proppant requirements Proppant strength, roundness, sphericity, and crush strength criteria

5.2 Operational Acceptance Criteria

6. Common Risks and Controls

6.1 Technical Risks

Risk Category Description Mitigation Measures
CO₂ phase transition damage Rapid expansion from supercritical to gas phase can cause sanding, formation damage, or wellbore instability Controlled injection rates; staged proppant placement; post-fracturing wellbore stabilization
Low fracture conductivity CO₂'s low viscosity may result in narrow fractures with insufficient proppant placement for long-term conductivity Higher proppant concentrations; ceramic proppant with higher crush strength; multi-stage treatment design
Equipment corrosion Supercritical CO₂ is highly corrosive to carbon steel, especially in the presence of trace H₂S, H₂O, or chlorides Use of clad pipe (304L/316L overlay on carbon steel); hardfacing on high-wear components; regular NDT inspection
Proppant bridging Dry proppant may bridge in narrow wellbore sections or at perforation tunnels Proper perforation density; lead-in with fine mesh proppant; adequate CO₂ volume for proppant transport
Wellbore temperature drop Joule-Thomson cooling effect during CO₂ injection can drop wellbore temperature significantly, risking hydrate formation or cement sheath damage Controlled injection rate; wellbore insulation; pre-warming procedures where applicable
Asphyxiation hazard CO₂ is heavier than air and can accumulate in low-lying areas, creating asphyxiation risk for personnel Continuous gas monitoring; emergency response procedures; adequate ventilation; personal protective equipment

6.2 Material Integrity Risks (Direct Relevance to Cladding Technology)

7. Application Scenarios Across the Company's Three Technology Routes

7.1 TIG/MIG Weld Overlay Route

The TIG (Tungsten Inert Gas) and MIG (Metal Inert Gas) weld overlay technology route directly serves CO₂ fracturing operations through the following applications:

Relevant WPS/PQR requirements: Welding procedures for CO₂ service overlay must be qualified per ASME Section IX or AWS D10.9, with additional requirements for:

7.2 Hydraulic Explosive Bonding Route

The hydraulic explosive bonding (water jet + explosive) technology route contributes to CO₂ fracturing applications through:

Quality assurance for hydraulic explosive bonded products in CO₂ service:

7.3 Explosion Welding Route

The explosion welding technology route provides the most robust cladding solutions for the most demanding CO₂ fracturing service conditions:

Explosion welding specifications for CO₂ service:

8. Contribution to Qualification Building, Product Delivery, and Customer Value

8.1 Qualification Building

The study and practical implementation of CO₂ dry-method fracturing technology contributes to the company's qualification portfolio in the following ways:

8.2 Product Delivery Enhancement

8.3 Customer Value Creation

9. Integration Framework: Connecting CO₂ Fracturing Knowledge to Core Capabilities

CO₂ Fracturing Requirement Technical Challenge Company Solution (Technology Route) Key Standard/Specification
Wellbore corrosion resistance Supercritical CO₂ attacks carbon steel at 0.5–2.0 mm/year 304L/316L TIG weld overlay (3–6 mm) on casing/tubing API 5CT; NACE MR0175; ASTM G101
Surface CO₂ transport piping High-pressure CO₂ transport requires corrosion-resistant, pressure-rated pipe Explosion-welded 316L/Q345B clad pipe ASME B31.3; ASTM A781; GB/T 11345
Proppant handling equipment Abrasion from high-velocity proppant-laden CO₂ flow Stellite 6 hardfacing overlay on blender components AWS A5.15; ASTM A276 (substrate)
High-pressure CO₂ storage Large-volume CO₂ storage at 5–15 MPa with corrosion resistance Hydraulic explosive bonded clad pressure vessels ASME BPVC VIII Div.1; ASTM E2775
Downhole completion tools Combined high-pressure, corrosion, and abrasion in downhole environment Explosion-welded thick clad (5–15 mm) tool bodies API 17D; NACE MR0175; ASTM A781
Wellhead equipment High-pressure CO₂ with potential H₂S coexistence Multi-layer overlay (309L transition + 316L cover) on wellhead components API 6A; NACE MR0175; ASME IX

10. Conclusion and Forward Outlook

The study and practical implementation of CO₂ dry-method proppant-filled fracturing technology represents a strategic knowledge investment for Cladding Technology Shanxi Co., Ltd. that directly enhances the company's ability to serve the oil and gas industry's growing demand for corrosion-resistant and abrasion-resistant materials solutions.

As global energy transition accelerates and unconventional resource development intensifies, CO₂ fracturing is expected to see significant growth, particularly in:

By maintaining deep technical understanding of CO₂ fracturing processes, the company ensures that its TIG/MIG weld overlay, hydraulic explosive bonding, and explosion welding capabilities remain aligned with evolving market demands. This knowledge integration enables the company to:

The practical experience gained from CO₂ fracturing technology research directly translates into improved product specifications, expanded WPS/PQR portfolios, enhanced NDT protocols, and deeper customer relationships—ultimately driving revenue growth and market share expansion in the high-value oilfield materials segment.