# US 10,480,303 B2 · Systems and methods for recovering an unfractionated hydrocarbon liquid mixture

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- Number: US 10,480,303 B2
- Document ID: US10480303B2
- Status: Granted
- Kind: B2
- Application number: 15/356,850
- Filed: 2016-11-21
- Published: 2017-08-03
- Granted: 2019-11-19
- Earliest claimed: 2016-02-01
- Assignees: Linde Aktiengesellschaft
- Applicants: Linde Aktiengesellschaft; John A. Babcock
- Inventors: John A. Babcock; Charles P. Siess, III
- Web page: https://patentgrep.com/patent/US10480303B2

## CPC

- E21B 43/40: Separation associated with re-injection of separated materials {(E21B43/385 takes precedence)}
- B01D 17/0208: {by sedimentation}
- B01D 19/0036: {Flash degasification (the other groups take precedence)}
- B01D 19/0068: {General arrangements, e.g. flowsheets (B01D19/0063 takes precedence)}
- C10G 5/06: by cooling or compressing
- E21B: EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28)
- C10G: CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION (cracking to hydrogen or synthesis gas C01B; cracking or pyrolysis of hydrocarbon gases to individual hydrocarbons or mixtures thereof of definite or specified constitution C07C; cracking to cokes C10B); RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES

## Abstract

A fluid recovery system includes a separator configured to separate a hydrocarbon stream into L-Grade, water, and natural gas. The system further includes a storage vessel in communication with the separator and configured to store the L-Grade separated from the hydrocarbon stream. The system further includes a compressor in communication with the separator and configured to pressurize the natural gas.

## Claims

### Claim 1

A method of recovering a fluid, comprising:
transporting a recovery system to a wellsite;
connecting the recovery system to a wellhead at the wellsite;
recovering a hydrocarbon stream from a hydrocarbon bearing reservoir via the wellhead, wherein the hydrocarbon stream has not been previously injected into the hydrocarbon bearing reservoir;
separating natural gas from the hydrocarbon stream at the wellsite; and
separating an unfractionated hydrocarbon liquid mixture from the hydrocarbon stream at the wellsite, wherein the unfractionated hydrocarbon liquid mixture is a by-product of the hydrocarbon stream from which the natural gas has been separated and comprises ethane, propane, butane, isobutane, pentane plus, and condensate, and wherein the hydrocarbon stream further comprises of at least one of condensate, water, carbon dioxide, and hydrogen sulfide.

### Claim 2 (depends on 1)

The method of claim 1, further comprising storing the unfractionated hydrocarbon liquid mixture in a storage vessel of the recovery system.

### Claim 3 (depends on 1)

The method of claim 1, further comprising separating water from the hydrocarbon stream at the wellsite.

### Claim 4 (depends on 1)

The method of claim 1, further comprising pressurizing the natural gas at the wellsite.

### Claim 5 (depends on 1)

The method of claim 1, further comprising injecting the unfractionated hydrocarbon liquid mixture into the same or a different hydrocarbon bearing reservoir.

### Claim 6

A method of recovering a fluid, comprising:
receiving a hydrocarbon stream from one or more hydrocarbon bearing reservoirs at a wellsite, wherein the hydrocarbon stream has not been previously injected into the hydrocarbon bearing reservoir;
separating natural gas from the hydrocarbon stream at the wellsite;
separating an unfractionated hydrocarbon liquid mixture from the hydrocarbon stream at the wellsite, wherein the unfractionated hydrocarbon liquid mixture comprises ethane, propane, butane, isobutane, pentane plus, and condensate, and wherein the hydrocarbon stream comprises of at least one of condensate, water, carbon dioxide, and hydrogen sulfide; and
storing the unfractionated hydrocarbon liquid mixture at the wellsite.

### Claim 7 (depends on 6)

The method of claim 6, further comprising storing the unfractionated hydrocarbon liquid mixture in a pressurized storage vessel.

### Claim 8 (depends on 6)

The method of claim 6, further comprising separating water from the hydrocarbon stream at the wellsite.

### Claim 9 (depends on 6)

The method of claim 6, further comprising pressurizing the natural gas at the wellsite.

### Claim 10 (depends on 9)

The method of claim 9, further comprising cooling the pressurized natural gas using an aftercooler.

### Claim 11 (depends on 9)

The method of claim 9, further comprising cooling a portion of the hydrocarbon stream using the pressurized natural gas.

### Claim 12 (depends on 6)

The method of claim 6, further comprising injecting the unfractionated hydrocarbon liquid mixture into the same or a different hydrocarbon bearing reservoir.

### Claim 13 (depends on 6)

The method of claim 6, further comprising transporting a separator on a portable skid-frame to the wellsite to separate the unfractionated hydrocarbon liquid mixture from the hydrocarbon stream.
