Manually operated reverse osmosis desalinization system

• US 5,531,887 A
• Filed: 05/24/1995
• Issued: 07/02/1996
• Est. Priority Date: 05/24/1995
• Status: Expired due to Fees

• Current Assignee: KEY Corporate Capital, Inc. (KeyCorp)
• Original Assignee: Howell Laboratories Inc
• Inventors: Miers, Gary L.
• Primary Examiner(s): FORTUNA, ANA M
• Application Number:
  US08/449,080
• Time in Patent Office: 405 Days
• Field of Search: 210/652, 210/195.2, 210/650, 210/257.2, 210/90, 210/87, 210/134, 210/135, 210/136, 210/416.1, 210/433.1, 210/321.6, 210/91, 417/374, 417/541
• US Class Current: 210/135
• CPC Class Codes: B01D 61/10 Accessories; Auxiliary operations
• CPC Class Codes: Y02A 20/131 Reverse-osmosis

Abstract

Reverse osmosis, particularly for manually operating water desalination, is achieved using semipermeable membranes which selectively permeate purified water from a feed solution pressurized by reciprocating piston or diaphragm pump. The manual pump action is assisted by using two pump pistons to provide a continuous flow of feed solution to the concentrate side of the membrane to continuously flush the membrane surface. The concentration polarization is controlled by exhausting the high pressure concentrate to atmosphere through an orifice and relief valve.

Claims

1. A manually operated apparatus for the desalinization of a feed stream which comprises:

a pump having at least two cylinders and two associated pistons received in the cylinders, the pistons each including a piston rod;

the cylinders disposed in side by side relationship, a pump arm pinned to a support wall which functions as a fulcrum, the support wall positioned between the cylinders, a handle connected to the piston rods to drive the pistons into and out of their associated cylinders in reciprocating opposite fashion such that when one piston is being withdrawn from its cylinder the other piston is introduced into its cylinder;

a source of feed stream to be purified in fluid flow communication with each of the cylinders including first and second feed conduits to provide for the flow of the feed stream from the source to the first and second cylinders respectively, each of the conduits having a check valve therein to prevent back flow of the feed stream from the chamber with which the conduit is associated back to the source, such that as the feed stream is being drawn into one first cylinder from the source of supply the feed stream in the other cylinder is being driven under pressure to a membrane assembly and is prevented from returning to the source;

first and second discharge conduits to provide for fluid flow communication between the first and second cylinders and the membrane assembly, each of said conduits having a check valve therein;

the membrane assembly in fluid flow communication with the first and second cylinders the assembly comprising a membrane having a feed side and a permeate side whereby the feed stream is separated into a permeate fraction and a concentrate fraction, a first conduit secured to the membrane assembly to discharge the concentrate fraction from the membrane assembly, the first conduit having a pressure relief valve therein and a second conduit to discharge the permeate fraction;

the dimensioning of the cylinders, pistons and piston rods, membrane assembly and associated relief valve configured such that the pressure and flow rate of the saline solution flowing into the membrane assembly ensures that the membrane surface on the feed side of the membrane assembly is continuously swept at constant pressure and flow rate to prevent or inhibit concentration polarization.

2. The apparatus of claim 1 wherein the cylinders, pistons and piston rods are dimensioned such that a force of about 15 lbf. applied to the handle will result in a pressure of between 525 to 575 psig in the feed zone of the membrane.

3. The apparatus of claim 2 wherein the membrane unit is configured such that the ratio of the permeate fraction recovered to the feed stream is about 1:

10.