WET AIR OXIDATION SYSTEM WITH SHELL AND TUBE HEAT EXCHANGER
A wet air oxidation system includes a reactor including an inlet and an outlet. The reactor is operable to oxidize a portion of a two-phase process fluid and to discharge a hot oxidized fluid from the outlet. A heat exchanger includes a plurality of tubes that extend along a long axis of the heat exchanger and cooperate to define a hot fluid inlet coupled to the outlet to receive the hot oxidized fluid and a hot fluid outlet, a shell that surrounds the plurality of tubes and defines a process fluid inlet arranged to receive the two-phase process fluid, and a process fluid outlet arranged to discharge a preheated two-phase process fluid to the inlet of the reactor, wherein the long axis of the heat exchanger is arranged in a non-horizontal direction.
1 . A wet air oxidation system comprising:
a reactor including an inlet and an outlet, the reactor operable to oxidize a portion of a two-phase process fluid and to discharge a hot oxidized fluid from the outlet; and
a heat exchanger including a plurality of tubes that extend along a long axis of the heat exchanger and cooperate to define a hot fluid inlet coupled to the outlet to receive the hot oxidized fluid and a hot fluid outlet, a shell that surrounds the plurality of tubes and defines a process fluid inlet arranged to receive the two-phase process fluid, and a process fluid outlet arranged to discharge a preheated two-phase process fluid to the inlet of the reactor, wherein the long axis of the heat exchanger is arranged in a non-horizontal direction.
2 . The wet air oxidation system of claim 1 , wherein the long axis of the heat exchanger is arranged in a vertical direction.
3 . The wet air oxidation system of claim 1 , wherein the two-phase process fluid includes a liquid that contains reactive sulfides and a gas that contains oxygen.
4 . The wet air oxidation system of claim 1 , wherein the oxidation process within the reactor is exothermic such that a temperature of the two-phase process fluid at the inlet is lower than a temperature of the two-phase process fluid at the outlet.
5 . The wet air oxidation system of claim 1 , further comprising an air compressor operable to provide a flow of compressed air to a flow of process fluid to produce the two-phase process fluid.
6 . A method of operating a wet air oxidation system, the method comprising:
orienting a long axis of a shell and tube heat exchanger in a non-horizontal direction;
directing a cool two-phase process fluid to an inlet of a shell of the shell and tube heat exchanger;
receiving a hot oxidized fluid in a plurality of tubes of the shell and tube heat exchanger;
heating the two-phase process fluid with the hot oxidized fluid to produce a preheated two-phase process fluid;
directing the preheated two-phase process fluid to a reactor; and
at least partially oxidizing the preheated two-phase process fluid to produce the hot oxidized fluid; and
discharging the hot oxidized fluid from the reactor.
7 . The method of claim 6 , wherein the long axis of the shell and tube heat exchanger is arranged in a vertical direction.
8 . The method of claim 6 , wherein the two-phase process fluid includes a liquid that contains reactive sulfides and a gas that contains oxygen.
9 . The wet air oxidation system of claim 6 , wherein the oxidizing step within the reactor is exothermic such that a temperature of the two-phase process fluid at the inlet is lower than a temperature of the two-phase process fluid at the outlet.
10 . The wet air oxidation system of claim 6 , further comprising operating an air compressor to provide a flow of compressed air to a flow of process fluid to produce the two-phase process fluid.
11 . A wet air oxidation system comprising:
a reactor including an inlet and an outlet, the reactor operable to oxidize a portion of a pre-heated two-phase process fluid and to discharge a hot oxidized fluid from the outlet;
an air compressor operable to provide a flow of compressed air to a process fluid to define a two-phase process fluid;
a separator operable to receive a flow of cooled oxidized fluid and operable to separate the cooled oxidized fluid into an off-gas and a treated effluent; and
a heat exchanger including a plurality of tubes that extend in a direction that is parallel to a long axis of the heat exchanger and a shell that surrounds a portion of the tubes, each of the plurality of tubes includes an inlet positioned to receive a portion of the hot oxidized fluid and an outlet arranged to discharge a portion of the cooled oxidized fluid, the shell including an inlet arranged to receive the two-phase process fluid and an outlet arranged to discharge the pre-heated two-phase process fluid, the heat exchanger operable to preheat the two-phase process fluid contained within the shell using the hot oxidized fluid entering the plurality of tubes.
12 . The wet air oxidation system of claim 11 , wherein the long axis of the heat exchanger is oriented in a non-horizontal position.
13 . The wet air oxidation system of claim 11 , wherein the long axis of the heat exchanger is oriented in a vertical position.
14 . The wet air oxidation system of claim 11 , wherein the two-phase process fluid includes a liquid that contains reactive sulfides and a gas that contains oxygen.
15 . The wet air oxidation system of claim 11 , wherein the oxidation process within the reactor is exothermic such that a temperature of the two-phase process fluid at the inlet is lower than a temperature of the two-phase process fluid at the outlet.