Liquid waste processing system

• US 4,105,556 A
• Filed: 02/18/1976
• Issued: 08/08/1978
• Est. Priority Date: 02/18/1976
• Status: Expired due to Term

• Current Assignee: Combustion Engineering Incorporated (ABB Limited)
• Original Assignee: Combustion Engineering Incorporated (ABB Limited)
• Inventors: Enegess, David N., O'Amaddio, Eugene R.
• Primary Examiner(s): Spear, Jr., Frank A.
• Assistant Examiner(s): Cross, E. Rollins
• Application Number:
  US05/659,053
• Time in Patent Office: 902 Days
• Field of Search: 210/22, 210/23 H, 210/23 R, 210/23 F, 210/152, 210/251, 210/257 M, 210/206, 210/411
• US Class Current: 210/206
• CPC Class Codes: B01D 2311/06 Specific process operations in the permeate stream
• CPC Class Codes: B01D 2311/08 Specific process operations in the concentrate stream
• CPC Class Codes: B01D 2311/2623 Ion-Exchange
• CPC Class Codes: B01D 2311/2673 Evaporation
• CPC Class Codes: B01D 61/08 Apparatus therefor
• CPC Class Codes: C02F 1/048 Purification of waste water by evaporation
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage

Abstract

A reverse osmosis liquid waste processing system for purifying liquid waste. The liquid waste processing system comprises a liquid waste collection tank with a recirculation line containing an eductor for permitting the addition of chemical additives, a filter with a back-flushing circuit and a reverse osmosis module which delivers its concentrate to a thin-film evaporator and its permeate to an ion exchanger.

Claims

1. An apparatus for producing very pure liquids from influent liquids containing high concentrations of impurities while at the same time producing an impurity concentrate of very high concentrations and low volume, wherein the apparatus comprising in combination:

a. a reverse osmosis concentrator having a semipermeable membrane and having an inlet for receiving a stream of waste fluid, an outlet for discharging purified permeate which has passed through said semipermeable membrane, and an outlet for discharging a concentrate;

b. a thin-film evaporator connected to said reverse osmosis concentrator'"'"'s concentrate outlet, said thin-film evaporator having an outlet for discharging a distillate and an outlet for discharging a concentrate having a high solids content;

c. means upstream of said reverse osmosis concentrator for filtering the stream of waste fluid, said filter means including a means for back-flushing said filtering means with a cleaning fluid; and

d. means upstream of said filtering means for introducing chemicals into the stream of waste fluid, said chemical introduction means including;

1. a hold-up tank for collecting the stream of waste fluid;

2. a pump in fluid communication with said hold-up tank;

3. a recirculation line connecting said pump and said hold-up tank;

4. an eductor in said recirculation line, said eductor having a primary inlet and a secondary inlet, said primary inlet being in fluid communication with said pump; and

5. a source of chemical additive, said source being connected to said secondary inlet of said eductor such that the chemicals from said chemical source are selectively entrained in the flow of fluid passing through said eductor.

2. The apparatus as recited in claim 1 further including means for recycling the distillate discharged from said thin-film evaporator to the stream of waste fluid upstream of said reverse osmosis concentrator.

3. The apparatus as recited in claim 2 further including a means connected to said filter for receiving and treating said cleaning fluid after it has flushed said filtering means, said receiving and treating means including:

a collection tank for receiving said cleaning fluid, a pump for pumping said cleaning fluid out of said collection tank, an inertial filter connected to said pump for separating said cleaning fluid into clarified effluent and a concentrate, and a recycling conduit for returning said concentrate to said collection tank.

4. The apparatus as recited in claim 3 further including an ion exchange demineralizer for further demineralizing said purified permeate discharged from said reverse osmosis module.