CO

1. An apparatus for delivering a fluid mixture comprising:

a pressurized proppant feed assembly, the assembly including a proppant storage vessel configured to contain therein a proppant material at ambient pressure and a pump assembly coupled to the proppant storage vessel, the pump assembly configured to output a proppant output flow at or above a fracturing fluid blending pressure, wherein the fracturing fluid blending pressure is greater than the ambient pressure;

a fracturing fluid storage vessel configured to contain therein a fracturing fluid and output a fracturing fluid output flow at or above the fracturing fluid blending pressure;

a thickener agent storage vessel configured to contain therein a thickener agent, the thickener agent storage vessel in fluid communication with the fracturing fluid output flow;

a mixing apparatus coupled to the pressurized proppant feed assembly and the fracturing fluid storage vessel, the mixing apparatus in fluid communication with the proppant output flow and the fracturing fluid output flow, the mixing apparatus configured to mix the proppant output flow, the fracturing fluid output flow, and the thickener agent therein and output a thickened fluid mixture of proppant and thickened fracturing fluid at or above the fracturing fluid blending pressure;

a high pressure pump assembly coupled to the mixing chamber and configured to deliver the thickened fluid mixture therein to a downstream component at an injection pressure, wherein the injection pressure is greater than the fracturing fluid blending pressure;

a recapture system, configured to receive an output flow from one or more of an exhaust stream from the downstream component, a well flow-back stream, a vented output stream or an external source; and

a separation and liquefaction system in fluid communication with the recapture system and the fracturing fluid storage vessel.

2. The apparatus of claim 1 , wherein the pump assembly is configured to receive a continual supply of proppant material and output a continuous proppant output flow.

3. The apparatus of claim 1 , wherein the mixing apparatus is configured to receive a continual supply of the proppant output flow and a continual supply of the fracturing fluid output flow.

4. The apparatus of claim 3 , wherein the mixing apparatus is configured to receive a continual supply of the proppant output flow and a continual supply of a thickened fracturing fluid output flow.

5. The apparatus of claim 1 , wherein the thickener agent storage vessel is configured to provide direct delivery of the thickener agent to the mixing apparatus.

6. The apparatus of claim 1 , wherein the thickener agent storage vessel is configured to provide direct delivery of the thickener agent into the fracturing fluid output flow prior to delivery of the fracturing fluid output flow to the mixing apparatus.

7. The apparatus of claim 1 , wherein the fracturing fluid blending pressure is in a range of 150-400 psi.

8. The apparatus of claim 7 , wherein the fracturing fluid blending pressure is approximately 300 psi.

9. The apparatus of claim 1 , wherein the injection pressure is in a range of 5000-12,000 psi or higher.

10. The apparatus of claim 1 , wherein the proppant material is sand.

11. The apparatus of claim 1 , wherein the fracturing fluid is liquid CO 2 .

12. The apparatus of claim 1 , wherein the recapture system includes a well flow-back stream recapture system.

13. An apparatus for delivering a fluid mixture comprising:

a pressurized proppant feed assembly, the assembly including a proppant storage vessel configured to contain therein the proppant material at ambient pressure and a pump assembly coupled to the proppant storage vessel, the pump assembly configured to receive a continual supply of proppant material and output a continuous proppant output flow at or above a fracturing fluid blending pressure, wherein the fracturing fluid blending pressure is greater than the ambient pressure;

a CO 2 fracturing fluid storage vessel configured to contain therein a CO 2 fracturing fluid and output a CO 2 fracturing fluid output flow at or above the fracturing fluid blending pressure;

a thickener agent storage vessel configured to contain therein a thickener agent, the thickener agent storage vessel in fluid communication with the CO 2 fracturing fluid output flow;

a mixing apparatus coupled to the pressurized proppant feed assembly and the CO 2 fracturing fluid storage vessel, the mixing apparatus in fluid communication with the proppant output flow and the CO 2 fracturing fluid output flow, the mixing apparatus configured to receive and mix a continual supply of the proppant output flow and a continual supply of the fracturing fluid output flow and output a thickened fluid mixture of proppant and thickened CO 2 fracturing fluid at or above the fracturing fluid blending pressure;

a high pressure pump assembly coupled to the mixing apparatus and configured to deliver the thickened fluid mixture therein to a downstream component at an injection pressure, wherein the injection pressure is greater than the fracturing fluid blending pressure;

a CO 2 recapture system, configured to receive a CO 2 output flow from one or more of an exhaust stream from the downstream component, a well flow-back stream, a vented CO 2 stream or an external source; and

a CO 2 separation and liquefaction system in fluid communication with the CO 2 recapture system and the CO 2 fracturing fluid storage vessel.

14. The apparatus of claim 13 , wherein the thickener agent storage vessel is configured to provide direct delivery of the thickener agent to the mixing apparatus.

15. The apparatus of claim 13 , wherein the thickener agent storage vessel is configured to provide direct delivery of the thickener agent into the CO 2 fracturing fluid output flow prior to delivery of the CO 2 fracturing fluid output flow to the mixing apparatus.

16. The apparatus of claim 13 , wherein the fracturing fluid blending pressure is in a range of 150-400 psi and the injection pressure is in a range of 5000-12,000 psi or higher.

17. The apparatus of claim 13 , wherein the proppant material is sand.

18. The apparatus of claim 13 , further including a well flow-back stream CO 2 recapture system.

19. A method of delivering a fluid mixture, comprising:

providing an input of a proppant material at ambient pressure to a proppant storage vessel, the proppant storage vessel configured to output a proppant output flow at ambient pressure;

providing an input of a fracturing fluid at or above a fracturing fluid blending pressure to a fracturing fluid storage vessel, the fracturing fluid storage vessel configured to output a fracturing fluid output flow at or above the fracturing fluid blending pressure;

inputting the proppant output flow at ambient pressure from the proppant storage vessel into a pump assembly wherein the pressure of the proppant output flow is increased to a fracture blending pressure;

mixing the proppant output flow, the fracturing fluid output flow and a thickener agent, in a mixing apparatus and outputting a fluid mixture of a thickened fluid mixture at or above the fracturing fluid blending pressure;

increasing the pressure of the output thickened fluid mixture in a high pressure pump to output a high pressure thickened fluid mixture;

delivering the high pressure thickened fluid mixture to one or more downstream components;

recapturing CO 2 from one or more of an exhaust stream of the one or more downstream components, a well flow-back stream, a vented CO 2 stream of the one or more downstream components, or an external CO 2 source;

separating and liquefying the recaptured CO 2 to output a purified and liquefied CO 2 stream; and

delivery of the purified and liquefied CO 2 stream to the a fracturing fluid storage vessel.

20. The method of claim 19 , wherein the proppant storage vessel is configured to output a continuous proppant output flow and the fracturing fluid storage vessel is configured to output a continuous fracturing fluid output flow, thereby providing for continuous operation.