Method for the separation of a first liquid from a second one

• US 6,164,458 A
• Filed: 04/21/1999
• Issued: 12/26/2000
• Est. Priority Date: 04/29/1998
• Status: Expired due to Fees

• Current Assignee: Sulzer Chemtech AG (Sulzer AG)
• Original Assignee: Sulzer Chemtech AG (Sulzer AG)
• Inventors: Mandrin, Charles, Ruckstuhl, Hans
• Primary Examiner(s): POPOVICS, ROBERT J
• Application Number:
  US09/296,099
• Time in Patent Office: 615 Days
• Field of Search: 210/799, 210/800, 210/801, 210/802, 210/806, 210/807, 210/DIG. 5, 210/532.1, 210/521
• US Class Current: 210/521
• CPC Class Codes: B01D 17/00 Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion devices for separating or removing fatty or oily substances or similar floating material from water, waste water, or sewage C02F1/40; cleaning or keeping clear the surface of open water from oil or like materials E02B15/04; arrangements for separating lubricants from refrigerants F25B43/02
• CPC Class Codes: B01D 17/041 with moving devices
• CPC Class Codes: B01D 17/045 with coalescers
• CPC Class Codes: C10G 33/06 with mechanical means, e.g. by filtration
• CPC Class Codes: Y10S 210/05 Coalescer

Abstract

A method for separating a first liquid from a second liquid, with the one liquid not being soluble in the other, the first liquid being contained as droplets in the second one, and with the two liquids having different densities. In a first step the liquid mixture is conducted during a first time interval as a turbulent flow through installations, in particular through a filler body in a packing column or through a static mixer, for coalescing the droplets. In a second step the flow rate of the mixture is reduced during a second time interval to continue the coalescence, and, in a third step, the speed of the mixture flow is further reduced and directed opposite to or with the force of gravity so that larger descending or rising droplets can be collected and separated out. The smaller droplets are carried along further by the second liquid.

Claims

1. Apparatus for the separation of a liquid mixture formed by first and second liquids, the liquids not being soluble in each other, the first liquid being contained as droplets in the second liquid, and the liquids having different densities, the liquid mixture being conducted in a first step during a first time interval as a turbulent flow through a mixing installation, in a second step the flow speed of the liquid mixture during a second time interval being reduced for a further development of the coalescence, thereafter in a third step the flow speed of the mixture being further reduced and the mixture flowing in a direction opposite to or with the force of gravity, larger descending or rising drops being collected and separated out, and smaller droplets being carried by the second liquid, the apparatus comprising a vertical container having a wall and forming a chamber for the collection of the liquid mixture, a vertical tube containing a static mixer for carrying out the first step, a collection space for the second liquid between the container wall and the vertical tube for carrying out the third step, and a further region in the container into which the vertical tube opens and which has a cross-section that is larger than a cross-section of the tube to effect a reduction in the speed of the mixture flow in its transition from the first to the second step.

2. Apparatus in accordance with claim 1 wherein the tube defines a shaft having a rectangular cross-section and wherein the collection space is assembled from chambers which are arranged in parallel and which each have a rectangular cross-section.

3. Apparatus in accordance with claim 2 including packings with an ordered structure arranged in the shaft and the chambers.

4. Apparatus in accordance with claim 1 including at least two zones which are connected in series for performing the first step;

and wherein in each case the Weber number of a fluid which flows through decreases from one of the zones to the following zone as a result of changes of at least one of the hydraulic diameter and the geometry of the installation so that an average diameter of the coalescing drops increases due to a decrease in the turbulence in the direction of flow.

5. Apparatus in accordance with claim 1 including first and second chambers separated by a wall for carrying out the second and third method steps;

and in that the one of the chambers is arranged above the other chamber.