Abstract Heat exchange means and method for a continuous wet oxidation apparatus for treating organic waste sewage employing a reactor within which the sewage is treated in the presence of heat, includes handling the influent by means providing a continuous hydraulic circuit for the passage of waste sewage to the reactor, such influent means comprising in series a holding tank communicating downstream with a high pressure pump acting to drive the influent through a low pressure heat exchanger a high pressure heat exchanger and then through an inlet into the reactor, and means for handling effluent from the reactor providing a continuous hydraulic circuit for the passage of treated liquid from the reactor and having in series an outlet and passage from the reactor to conduct hot effluent through the high pressure heat exchanger from which the passage leads to a throttling device and thence to and through the low pressure heat exchanger to a second throttling device and therefrom to a disposal point. The influent waste sewage conducted from the holding tank to the reactor is preheated by heat from the effluent liquid in two stages, comprising a first stage at low pressure and a second stage at high pressure.
Inventors
👤 James W. Van Kirk
Bibliographic Details
Application Number—
JurisdictionUS
Data Sourcegoogle_patents
Last Synchronized2026-10-30 23:54
CPC Classifications
C; C02; C02F; C02F11/00; C02F11/06; C02F11/08
Claims Analysis
Total Claims: 3
Claim 1
Independent Claim
245 words
A method of treating organic waste sewage by continuous wet oxidation process, the method comprising: treating the sewage in the presence of heat at a temperature of about 550°-560° F. in a reactor; passing waste sewage as influent to said reactor from a pump in series through a first heat exchanger and downstream from said first heat exchanger through a second heat exchanger and then through an inlet into said reactor; conducting treated liquid from said reactor as hot effluent through said second heat exchanger and then through a throttling device and thence to and through said first heat exchanger and from the first heat exchanger to a disposal point; maintaining pressure of the effluent upstream from the throttling device and thereby the pressure in said second heat exchanger at about 1500 to 1600 psi and temperature of about 560° F.; and controlling the pressure downstream from the throttling device and in said first heat exchanger to be no greater than about 500 psi and temperature up to 400° F.; whereby the influent waste sewage in travelling from said pump to said reactor is preheated by heat from the effluent liquid in two stages, comprising a first stage in said first heat exchanger and in which said effluent is at a lower pressure and temperature than in a second stage in said second heat exchanger in which said effluent is at higher pressure and temperature than the pressure and temperature in said first heat exchanger.
Claim 2
Independent Claim
245 words
A method of treating organic waste sewage by continuous wet oxidation process, the method comprising: treating the sewage in the presence of heat at a temperature of about 550°-560° F. in a reactor; passing waste sewage as influent to said reactor from a pump in series through a first heat exchanger and downstream from said first heat exchanger through a second heat exchanger and then through an inlet into said reactor; conducting treated liquid from said reactor as hot effluent through said second heat exchanger and then through a throttling device and thence to and through said first heat exchanger and from the first heat exchanger to a disposal point; maintaining pressure of the effluent upstream from the throttling device and thereby the pressure in said second heat exchanger at about 1500 to 1600 psi and temperature of about 560° F.; and controlling the pressure downstream from the throttling device and in said first heat exchanger to be no greater than about 500 psi and temperature up to 400° F.; whereby the influent waste sewage in travelling from said pump to said reactor is preheated by heat from the effluent liquid in two stages, comprising a first stage in said first heat exchanger and in which said effluent is at a lower pressure and temperature than in a second stage in said second heat exchanger in which said effluent is at higher pressure and temperature than the pressure and temperature in said first heat exchanger.
Claim 3
Dependent Claim
63 words
A method according to claim 1, comprising effecting travel of the influent in heat exchanging relation to the effluent in the first heat exchanger by running the effluent through an outer pipe and running the influent through an inner section which is of smaller outside diameter than the inside diameter of the outer pipe and is within the inner pipe and extends therealong.