System and method for treating contaminated wastewater

Patent metadata

Field	Value
Publication number	US-10112849-B2
Application number	US-201414899387-A
Country	US
Kind code	B2
Filing date	May 27, 2014
Priority date	Jun 17, 2013
Publication date	Oct 30, 2018
Grant date	Oct 30, 2018

Abstract

The invention relates to a system for treating contaminated wastewater, comprising a feed line (3) that leads into a separator (5) and a discharge line (10) that leaves the separator, which discharge line leads directly or indirectly into an access line (16) into an ultrafiltration system (18), wherein the ultrafiltration system (18) has a permeate outlet line (19) and a concentrate outlet line (17). According to the invention, a system and a method for treating contaminated wastewater that operate effectively and reliably with low component complexity are provided or specified. This is achieved in that the permeate outlet line (19) can be connected to the feed line (3) in a controllable manner. According to the corresponding method, water separated from the wastewater in the separator (5) exits into a discharge line (10), and the water is then fed to an ultrafiltration system (18), in which the water is separated into a concentrate discharged into a concentrate outlet line (17) and a permeate discharged into a permeate outlet line (19), wherein the permeate can be fed back into the feed line (3) of the separator (5) for reaction with a supplied precipitant, and heavy metal, for example, is separated from the permeate in the separator (5).

First claim

What is claimed is:

1. A system for treating contaminated wastewater from a buffer tank ( 1 ), comprising a feed line ( 3 ) that leads into a separator ( 5 ) and a discharge line ( 10 ) that leaves the separator ( 5 ), wherein the discharge line ( 10 ) leads into a working tank ( 11 ), wherein an access line ( 16 ) extends from the working tank ( 11 ) into a filtration system ( 18 ) which has a permeate outlet line ( 19 ) and a concentrate outlet line ( 17 ), wherein the buffer tank ( 1 ) is connected to the feed line ( 3 ) via an inlet check valve ( 2 ), wherein the permeate outlet line ( 19 ) is connected to the feed line ( 3 ) in a controllable manner in order to feed permeate back to the feed line ( 3 ), wherein the working tank ( 11 ) is connected to the feed line ( 3 ) via a return line ( 13 ), wherein a return check valve ( 12 ) is arranged in the return line ( 13 ), wherein the concentrate outlet line ( 17 ) extends from the filtration system ( 18 ) and into the working tank ( 11 ), wherein the permeate outlet line ( 19 ) is connected to the working tank ( 11 ) via a return flow line ( 26 ), wherein the system includes a heavy metal analyzer ( 22 ) in communication with the permeate outlet line ( 19 ), and wherein a precipitant line ( 14 ) opens into the feed line ( 3 ) downstream of the return line ( 13 ).

2. The system according to claim 1 , characterized in that the return flow line ( 26 ) is controlled by a return flow line valve ( 25 ) and branches off at a junction ( 24 ) downstream of the heavy metal analyzer ( 22 ) in the permeate outlet line ( 19 ).

3. The system according to claim 2 , characterized in that the permeate outlet line ( 19 ) has a permeate discharge valve ( 20 ) downstream of the junction ( 24 ) of the return flow line ( 26 ).

4. The system according to claim 1 , characterized in that the separator ( 5 ) is a three-phase separator.

5. The system according to claim 1 , characterized in that the filtration system ( 18 ) is an ultrafiltration system.

6. The system according to claim 1 , characterized in that the separator ( 5 ) is a three-phase separator for separating sludge and oil from the wastewater.

7. A method for treating contaminated wastewater, the method comprising providing the system according to claim 1 , passing the contaminated wastewater to the separator ( 5 ) via the feed line ( 3 ), wherein water separated out of the contaminated wastewater exits from the separator into the discharge line ( 10 ), subsequently supplying the water to the filtration system ( 18 ) in which the water is separated into a concentrate discharged into the concentrate outlet line ( 17 ) and a permeate discharged into the permeate output line ( 19 ), and feeding the permeate back into the feed line ( 3 ) of the separator ( 5 ).

8. The method according to claim 7 , characterized in that the discharged permeate is monitored by the heavy metal analyzer ( 22 ) to determine whether a limit value is present.

9. The method according to claim 8 , characterized in that the permeate is fed back into the feed line ( 3 ) to the separator ( 5 ) and a precipitant is simultaneously supplied to the separator ( 5 ) when the limit value has been exceeded.

10. The method according to claim 9 , characterized in that the precipitant is introduced into the feed line ( 3 ) by means of the precipitant line ( 14 ) in close proximity to where the return line ( 13 ) leads into said feed line ( 3 ) and in that the feed line portion between the separator and where the precipitant line meets the feed line is used as a reaction zone for the precipitant with the permeate.

11. The method according to claim 9 , characterized in that the precipitant is metered as a function of a concentration and a pH value in the permeate.

12. The method according to claim 7 , characterized in that the discharged permeate is monitored by the heavy metal analyzer ( 22 ) to determine whether a limit value is present for a heavy metal.

13. The method according to claim 9 , characterized in that the heavy metal analyzer ( 22 ) determines whether the limit value is present for a heavy metal, and the precipitant is metered as a function of a concentration of the heavy metal and a pH value in the permeate.

14. The method according to claim 12 , characterized in that the heavy metal is separated as sludge from the permeate in the separator ( 5 ).

Assignees

• Bosch Gmbh Robert

Inventors

• Korf Philipp
• Pettersch Michael
• Schwendele Josef
• Jung Darius
• Korz Juergen
• Mutschler Bernhard
• Sachs Dimitri

Classifications

• C02F2209/003

  Downstream control, i.e. outlet monitoring, e.g. to check the treating agents, such as halogens or ozone, leaving the process · CPC title

• C02F1/52

  by flocculation or precipitation of suspended impurities {(C02F1/463 takes precedence)} · CPC title

• B01D2311/04

  Specific process operations in the feed stream; Feed pretreatment · CPC title

• C02F1/008

  Control or steering systems not provided for elsewhere in subclass C02F · CPC title

• B01D61/16

  Feed pretreatment · CPC title