Systems for producing regenerant brine and desalinated water from high temperature produced water

Patent metadata

Field	Value
Publication number	US-10399880-B2
Application number	US-201815902090-A
Country	US
Kind code	B2
Filing date	Feb 22, 2018
Priority date	Jul 29, 2016
Publication date	Sep 3, 2019
Grant date	Sep 3, 2019

Abstract

A system for treating high temperature produced water includes an electrocoagulation unit, a membrane distillation unit in communication with the outlet of the electrocoagulation unit having a hydrophobic membrane with a feed side for receiving the produced water stream and a product side for receiving a deionized water stream. A heat recovery heat exchanger is in communication with the membrane distillation unit for receiving two streams, one from each side of the hydrophobic membrane, such that heat is exchanged between the two streams. A line leaving the heat exchanger returns a heated stream from the heat exchanger to a location in a line upstream of the membrane distillation unit. A brine tank in communication with the membrane distillation unit receives a portion of a stream from the membrane product side and contains a concentrated brine solution containing the portion of the stream from the membrane product side and sodium chloride.

First claim

What is claimed is:

1. A system for treating high temperature produced water, the system comprising:
a. an electrocoagulation unit or an electroflotation unit having an inlet for receiving a produced water feed stream and an outlet;
b. a first direct contact membrane distillation unit in fluid communication with the outlet of the electrocoagulation unit or the electroflotation unit comprising a hydrophobic membrane having a membrane feed side for receiving the produced water feed stream from the electrocoagulation unit or the electroflotation unit and a membrane product side for receiving a deionized water stream;
c. a heat recovery heat exchanger in fluid communication with the first direct contact membrane distillation unit for receiving two streams, one from each side of the hydrophobic membrane, such that heat is exchanged between the two streams;
d. a line leaving the heat recovery heat exchanger for returning a heated stream from the heat recovery heat exchanger to a location in a line upstream of the first direct contact membrane distillation unit;
e. a brine tank in fluid communication with the first direct contact membrane distillation unit for receiving a portion of a stream from the membrane product side and for containing a concentrated brine solution comprising the portion of the stream from the membrane product side and sodium chloride;
f. a filtration unit comprising an ultrafiltration membrane, a polymeric membrane or a ceramic membrane to form a clarified stream substantially free of suspended solids, oil and grease;
g. an ion exchange unit in fluid communication with the filtration unit for removing hardness wherein the ion exchange unit contains a functionalized microfiltration membrane comprising ion exchanging functional groups; and
h. a reverse osmosis membrane in fluid communication with the ion exchange unit.

2. The system of claim 1 , further comprising a water softening system utilizing ion exchange resin capable of being regenerated by the concentrated brine solution.

3. The system of claim 1 , further comprising:
a second direct contact membrane distillation unit in fluid communication with the reverse osmosis membrane.

4. The system of claim 1 , further comprising a vacuum pump and wherein the electrocoagulation unit or the electroflotation unit includes a head space connected to the vacuum pump.

5. The system of claim 1 , further comprising a clarifying unit selected from an induced gas flotation unit, a dissolved air flotation unit or a clarifier coupled to the outlet of the electrocoagulation unit.

6. The system of claim 1 , wherein the filtration unit comprises a high temperature ultrafiltration membrane.

7. The system of claim 1 , wherein the electrocoagulation unit or the electroflotation unit includes a head space and wherein the system further comprises a vacuum pump connected to the head space and to the filtration unit.

8. The system of claim 1 , wherein the ion exchange unit is connected to the brine tank.

Assignees

• Chevron Usa Inc

Inventors

• Prakash Prakhar
• Shah Gini Yash
• Hatakeyama Evan Shigeto

Classifications

• Y02A20/131

  Reverse-osmosis · CPC title

• C02F1/24

  by flotation (C02F1/465 takes precedence) · CPC title

• B01D2311/10

  Temperature control · CPC title

• B01D61/16

  Feed pretreatment · CPC title

• B01D61/147

  Microfiltration · CPC title