Catalytic oxidation of aqueous organic contaminants

Patent metadata

Field	Value
Publication number	US-2017152166-A1
Application number	US-201514954153-A
Country	US
Kind code	A1
Filing date	Nov 30, 2015
Priority date	Nov 30, 2015
Publication date	Jun 1, 2017
Grant date	—

Abstract

A method of treating water to oxidize organic contaminants comprises heat transfer system includes heating liquid water to a temperature of at least 190° F. at a pressure to keep the heated water in a liquid phase, and contacting the heated water with oxygen and an oxidation catalyst including a noble metal on a porous support comprising a bi-modal pore size distribution including pore sizes from 1 nm to 20 nm and pore sizes from 100 nm to 1000 nm. The resulting catalytic oxidation of the organic contaminants results in the release of gaseous reaction products resulting from the oxidation reaction, which are separated from the treated water in a phase separator to produce a treated water final product.

First claim

1 . A method for treating water to oxidize organic contaminants, comprising heating liquid water to a temperature of at least 190° F. at a pressure to keep the heated water in a liquid phase;
contacting the heated water with oxygen and an oxidation catalyst comprising a noble metal on a porous support comprising a bimodal pore size distribution comprising pore sizes from 1 nm to 20 nm and pore sizes from 100 nm to 1000 nm; and
separating gaseous reaction products and unreacted oxygen from the treated liquid water.

2 . The method of claim 1 , wherein the liquid water is heated to a temperature of 200° F. to 230° F.

3 . The method of claim 1 , wherein the contacting of the heated water with oxygen and the catalyst is performed in a continuous manner to by flowing the heated water through a reactor comprising the catalyst to achieve a residence time of at least 5 minutes.

4 . The method of claim 1 , wherein the heated water is at a pressure of 1 bar to 3 bar.

5 . The method of claim 1 , wherein the noble metal is selected from platinum, palladium, ruthenium, iridium, or mixtures comprising any of the foregoing.

6 . The method of claim 5 , wherein the oxidation catalyst comprises from 5 wt. % to 25 wt. % of noble metal crystallites 100 Å or smaller, based on the total weight of the oxidation catalyst.

7 . The method of claim 1 , wherein the porous support is a ceramic or activated carbon.

8 . The method of claim 7 , wherein the porous support has a surface area of at least 50 m 2 /g if the support is ceramic, or has a surface area of at least 500 m 2 /g if the support is activated carbon.

9 . The method of claim 1 , wherein the porous support comprises a bimodal pore size distribution comprising a first pore size population from 5 nm to 20 nm and a second pore size population from 200 nm to 600 nm.

10 . The method of claim 1 , wherein the percentage of pore volume of the bimodal support in the pore range of 100 nm to 1000 nm ranges from 5% to 50%, and the percentage of pore volume of the bimodal support in the pore range of 1 nm to 20 nm ranges from 95% to 50%.

11 . The method of claim 1 , wherein the percentage of pore volume of the bimodal support in the pore range of 100 nm to 1000 nm ranges from 20% to 30%, and the percentage of pore volume of the bimodal support in the pore range of 1 nm to 20 nm ranges from 80% to 70%.

12 . A system for treating water for organic contaminants, comprising
a heater having an inlet in fluid communication with a water source and an outlet, configured to heat liquid water to a temperature of at least 190° F.; a reactor comprising a reactor housing defining a reactor enclosure within the housing and having an inlet in fluid communication with the heater outlet, and an outlet, and an oxidation catalyst in the reactor enclosure comprising a noble metal on a porous support comprising a bi-modal distribution comprising pore sizes from 1 nm to 20 nm and pore sizes from 100 nm to 1000 nm; and a gas-liquid phase separator having an inlet in fluid communication with the reactor outlet.

13 . The system of claim 12 , wherein the heater is configured to heat the liquid water to a temperature of 200° F. to 230° F.

14 . The system of claim 12 , further comprising a flow controller configured to provide a continuous flow of water to the reactor at a rate to achieve a reactor residence time of at least 5 minutes.

15 . The system of claim 12 , wherein the oxidation catalyst comprises from 5 wt. % to 25 wt. % of noble metal crystallites 100 Å or smaller, based on the total weight of the oxidation catalyst.

16 . The system of claim 12 , wherein the porous support is a ceramic with a surface area of at least 50 m 2 /g or activated carbon with a surface area of at least 500 m 2 /g.

17 . The system of claim 12 , wherein the porous support comprises a bimodal pore size distribution comprising a first pore size population from 5 nm to 20 nm and a second pore size population from 200 nm to 600 nm.

18 . The system of claim 12 , wherein the percentage of pore volume of the bimodal support in the pore range of 100 nm to 1000 nm ranges from 5% to 50%, and the percentage of pore volume of the bimodal support in the pore range of 1 nm to 20 nm ranges from 95% to 50%.

19 . The system of claim 12 , wherein the percentage of pore volume of the bimodal support in the pore range of 100 nm to 1000 nm ranges from 20% to 30%, and the percentage of pore volume of the bimodal support in the pore range of 1 nm to 20 nm ranges from 80% to 70%.

20 . A catalyst for oxidizing aqueous organic contaminants, comprising a porous support comprising a bimodal pore size distribution comprising pore sizes from 1 nm to 20 nm and pore sizes from 100 nm to 1000 nm, and from 5 wt. % to 25 wt. %, based on the total weight of the catalyst, of noble metal crystallites 100 Å or smaller selected from platinum, palladium, ruthenium, iridium, or mixtures comprising any of the foregoing.

Assignees

• Hamilton Sundstrand Space Sys

Inventors

• Yu Ping
• Nalette Timothy A

Classifications

• C02F1/20

  by degassing, i.e. liberation of dissolved gases (degasification of liquids in general B01D19/00; arrangement of degassing apparatus in boiler feed supply F22D) · CPC title

• C02F1/02

  by heating (methods of steam generation F22B; preheating boiler feed-water or accumulating preheated boiler feed-water F22D) · CPC title

• C02F1/42

  by ion-exchange (ion-exchange in general B01J) · CPC title

• C02F1/722

  Oxidation by peroxides · CPC title

• B01J37/088

  Decomposition of a metal salt · CPC title