Dry sand foam generator

• US 4,780,243 A
• Filed: 05/19/1986
• Issued: 10/25/1988
• Est. Priority Date: 05/19/1986
• Status: Expired due to Fees

• Current Assignee: Halliburton Company
• Original Assignee: Halliburton Company
• Inventors: Edgley, Kevin D., Stromberg, James L.
• Primary Examiner(s): Terapane, John F.
• Assistant Examiner(s): Caress, Virginia B.
• Application Number:
  US06/864,696
• Time in Patent Office: 890 Days
• Field of Search: 252/305, 252/307, 252/8.551, 166/280, 175/69, 261/DIG. 26
• US Class Current: 516/11
• CPC Class Codes: B01F 23/235 for making foam
• CPC Class Codes: B01F 25/311 for mixing more than two components; Devices specially adapted for generating foam
• CPC Class Codes: E21B 43/2605 using gas or liquefied gas
• CPC Class Codes: E21B 43/2607 Surface equipment specially adapted for fracturing operations
• CPC Class Codes: Y10S 261/26 Foam
• CPC Class Codes: Y10S 507/922 Fracture fluid

Abstract

Apparatus and methods are provided for producing a proppant carrying foamed fracturing fluid or the like having very high ratios of proppant material to the liquid phase of the foam, which can be substantially higher than even the theoretical maximum ratio available when the proppant is introduced into a foaming apparatus as a proppant/liquid slurry. This is accomplished by a dry sand foam generation process wherein the sand or other particulate material is introduced into a foam generator apparatus as a dry particulate material in a stream of gas which is subsequently mixed with a second liquid stream.

Claims

1. A method of generating a foam containing particulate material for treating a subsurface earth formation penetrated by a well bore, said method comprising:

(a) introducing a first stream of pressurized gas having dry particulate material entrained therein into a vessel, said particulate material flowing vertically downward into said vessel, at least in part due to the action of gravity;

(b) introducing a second stream of liquid into said vessel;

(c) varying said second stream into a self-impinging conical jet;

(d) impringing said conical jet onto said first stream and thereby forming a foam containing particulate material; and

(e) injecting such a foam into the well bore.

2. The method of claim 1, wherein:

said foam has a quality of substantially greater than approximately 75%.

3. The method of claim 1, wherein:

step (a) is further characterized in that said first stream is introduced into a cylindrical bore of said vessel;

step (b) is further characterized in that said second stream is introduced into an inlet passage in communication with an annular plenum surrounding said bore and communicated with said bore by an annular opening;

step (c) is further characterized in that said second stream is varied into said conical jet within said annular plenum; and

step (d) is further characterized in that said conical jet flows radially inward through said annular opening to impinge upon said first stream.

4. The method of claim 3, further comprising a step of:

adjusting a width of said annular opening.

5. The method of claim 1, wherein:

step (a) is further characterized in that said first stream is introduced into a substantially linear flow passage of said vessel; and

steps (c) and (d) are further characterized in that said self-impinging conical jet discharges substantially symmetrically into said flow passage while impinging upon said first stream.

6. The method of claim 5, wherein:

step (a) is further characterized in that said flow passage is oriented substantially vertically.

7. The method of claim 1, further comprising a step of:

introducing a third stream of gas into said vessel, and adding said third stream to said foam.

8. The method of claim 1, wherein:

step d is further characterized in that said foam has a quality in a range from about 53% to about 96%.

9. The method of claim 1, wherein:

steps (a), (b), (c) and (d) are all performed at relatively high pressures substantially in excess of atmospheric pressure.

10. The method of claim 9, wherein:

steps (a), (b), (c) and (d) are all performed at pressures at least equal to about 500 psi.

11. The method of claim 1, wherein:

step (a) is further characterized in that said gas is nitrogen gas and said particulate material is sand; and

step (b) is further characterized in that said liquid is an aqueous based liquid including a surfactant.

12. The method of claim 1 wherein said method further comprises the steps of varying the flow rate of said second stream of liquid into said vessel while maintaining a substantially constant gas flow rate thereby varying the concentration of particulate material per unit volume of liquid.