Liquid treatment such as dewatering of sludge

• US 4,774,002 A
• Filed: 10/02/1986
• Issued: 09/27/1988
• Est. Priority Date: 10/10/1985
• Status: Expired due to Term

• Current Assignee: British Nuclear Technology
• Original Assignee: British Nuclear Technology
• Inventors: Williams, Gwilyn H., Gutman, Richard G.
• Primary Examiner(s): NOT, DEFINED
• Assistant Examiner(s): Evans, Linda S.
• Application Number:
  US06/914,325
• Time in Patent Office: 726 Days
• Field of Search: 210/137, 210/195.2, 210/321.1, 210/433.2, 210/636, 210/637, 210/741, 210/805, 210/751, 210/90, 210/97, 210/108, 210/109, 210/321, 210/69, 210/196
• US Class Current: 210/636
• CPC Class Codes: B01D 2313/48 Mechanisms for switching between regular separation operations and washing
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 29/115 open-ended, the arrival of the mixture to be filtered and the discharge of the concentrated mixture are situated on both opposite sides of the filtering element
• CPC Class Codes: B01D 29/52 in parallel connection
• CPC Class Codes: B01D 29/66 by flushing, e.g. counter-current air-bumps
• CPC Class Codes: B01D 61/145 Ultrafiltration
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration

Abstract

A method of treating a liquid, for example dewatering a sludge by ultrafiltration, in which the liquid is caused to flow repeatedly along a permeable walled tube (22) so that a filtrate passes through the wall of the tube, the progress of the treatment being monitored by monitoring the pressure difference between the ends of the tube (22). The method has enabled sludges of widely varying compositions to be dewatered to produce products of uniform viscosity, suitable for subsequent immobilization by cementation.

Claims

1. A method of treatment of a liquid, wherein the liquid is caused to flow repeatedly along a duct with a wall permeable to a component of the liquid so that on each passage of the liquid along the duct, as a result of a pressure difference between the inside and the outside of the duct, a filtrate passes through the wall of the duct to increase the viscosity of the remaining liquid and the remainder of the liquid passes along the duct such that the viscosity of the liquid is increased as it passes repeatedly along the duct, the method including monitoring the pressure difference between the ends of the duct as an indication of the viscosity of the liquid and controlling the treatment in accordance with the value of the monitored pressure difference and hence the indicated increase in viscosity.

2. A method as claimed in claim 1 wherein the treatment is terminated when the monitored pressure difference reaches a predetermined value indicative of a predetermined degree of filtrate removal and a resulting desired viscosity.

3. A method as claimed in claim 2 also including a cleaning operation comprising reversing the pressure difference between the inside and the outside of the duct so that filtrate passes back through the permeable wall, to flow along the duct along with the liquid, the cleaning operation being performed in accordance with the value of the monitored pressure difference.

4. A method as claimed in claim 1 also including a cleaning operation comprising reversing the pressure difference between the inside and the outside of the duct so that filtrate passes back through the permeable wall, to flow along the duct along with the liquid, the cleaning operation being performed in accordance with the value of the monitored pressure difference.

5. A method as claimed in claim 1 wherein said liquid is a sludge of particulate matter and water, said treatment is a dewatering treatment of the sludge, and said treatment is terminated when the monitored pressure difference reaches a predetermined value indicative of a predetermined degree of dewatering and hence a resulting predetermined viscosity.

6. A method of treating a sludge of particulate matter and water, wherein the sludge is dewatered by causing the sludge to flow repeatedly along a duct with a wall permeable to the water so that on each passage of the sludge along the duct, as a result of a pressure difference between the inside and the outside of the duct, water filtrate passes through the wall of the duct and the remainder of the sludge passes along the duct, the method including monitoring the pressure difference between the ends of the duct and controlling the dewatering treatment in accordance with the value of the monitored pressure difference, terminating the dewatering treatment when the monitored pressure difference reaches a predetermined value indicative of a predetermined degree of dewatering and a resulting desired viscosity suitable for immobilization by cementation, mixing the sludge with cement, and letting the mixture set solid.

7. A method as claimed in claim 6 wherein the particulate matter in the sludge includes radioactive material.