Liquid flow distribution and flow control with dual adjustable orifice plates or overlapping orifices

• US 5,968,312 A
• Filed: 06/23/1997
• Issued: 10/19/1999
• Est. Priority Date: 08/06/1992
• Status: Expired due to Fees

• Current Assignee: Hugo H. Sephton
• Original Assignee: Hugo H. Sephton
• Inventors: Sephton, Hugo H.
• Primary Examiner(s): Manoharan, Virginia
• Application Number:
  US08/880,250
• Time in Patent Office: 848 Days
• Field of Search: 159/47.1, 159/DIG. 16, 159/DIG. 4, 159/27.3, 159/27.4, 159/27.1, 159/28.6, 159/DIG. 13, 159/2.1, 159/18, 159/43.1, 159/DIG. 8, 159/DIG. 20 , 159/44, 203/1, 203/88, 203/11, 203/91, 203/10, 203/DIG. 7, 203/DIG. 18, 203/71, 203/73, 202/174, 202/160
• US Class Current: 159/47.1
• CPC Class Codes: B01D 1/065 by film evaporating
• CPC Class Codes: B01D 1/26 Multiple-effect evaporating
• CPC Class Codes: B01D 3/065 Multiple-effect flash distillation (more than two traps)
• CPC Class Codes: B01D 3/42 Regulation; Control
• CPC Class Codes: F28D 7/1615 the conduits being inside a casing and extending at an angle to the longitudinal axis of the casing; the conduits crossing the conduit for the other heat exchange medium
• CPC Class Codes: F28D 7/163 with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing F28D7/1615 takes precedence
• CPC Class Codes: F28F 27/02 for controlling the distribution of heat-exchange media between different channels static flow control means in header boxes F28F9/026; arrangements of guide plates or guide vanes F28F9/22, F28F25/12
• CPC Class Codes: Y10S 159/08 Multieffect or multistage
• CPC Class Codes: Y10S 159/13 Scale
• CPC Class Codes: Y10S 159/20 Additive
• CPC Class Codes: Y10S 203/07 Start up or shut down
• CPC Class Codes: Y10S 203/18 Control
• CPC Class Codes: Y10S 203/19 Sidestream

Abstract

A method and apparatus for forming an array of multiple parallel flow orifices, for example by holes drilled through a plate in a selected pattern and spacing and of selected sizes or flow diameters, and whereby these orifices are used to provide an approximately equal and adequate distribution of liquid flowing through them as parallel streams of liquid and into an evaporation zone or a parallel array of evaporation channels, and wherein the orifices can be adjusted in flow diameter to control the flowrate of liquid in generally parallel streams with an array of orifice adjusting apparatus, for example an adjacent sliding orifice plate which provides for orifice flow rate adjustment with orifices through this second plate corresponding in position to those of the first orifice plate, and the use of such dual orifice plates for supporting a pool of liquid there-above and for controlling the flowrate of liquid through the first array of orifices by reducing or enlarging their orifice flow diameters to control the level of the liquid in the pool or the pressure of this pool on or at the orifices and controlling the effect-to-effect pressure causing flashdown, and to improve the evaporation process or the degree of evaporation in an adjacent flash evaporation zone or in a bundle of adjacent evaporator tubes, and when applied to a multi-effect series of several such vertical tube evaporators.

Claims

1. In an effect-to-effect evaporation of a liquid a method for distribution of said liquid for downflow evaporation thereof from a pool of said liquid whereto more of said liquid is added, the improvement comprising:

(a) forming a multiplicity of orifices in parallel array through a plate supporting said pool of liquid for said distribution of said liquid through said orifices,

(b) determining the level of said liquid in said pool and

(c) adjusting the flow diameters of said orifices responsive to said level of said liquid by sliding translation of an array of orifice adjusting means adjacent to said orifices,

(d) and controlling the rate of flow of said liquid through said orifices and maintaining said liquid level in said pool at about a selected level above said plate and maintaining effect-to-effect pressure control causing flashdown of said liquid, wherein said control of said rate of flow of said liquid provides for a range of said flow reduced by about 50% below an effect design point flowrate and to about 400% above said design point flowrate while maintaining said liquid level in said pool within a range of about 3 inches to 9 inches above said plate.

2. The method of claim 1, wherein said multiplicity of orifices consists essentially of two arrays of corresponding parallel orifices adjacent to one another, and wherein said adjusting of said flow diameters of said orifices is provided by sliding one of said two arrays of orifices over the other of said two arrays of orifices.

3. The method of claim 1 wherein said liquid is water and wherein said flashdown cools said water to a lower temperature at a lower pressure when said water is distributed through said orifices.

4. The method of claim 1 wherein the effect-to-effect evaporation is applied in a vertical series of evaporation effects and wherein said liquid is distilled water produced at a temperature existing in a higher effect of said series and caused to fall into said pool for said distribution of said liquid through said orifices for flashdown of said liquid to a temperature lower than said temperature.

5. The method of claim 1 wherein said liquid is brine and wherein said flashdown cools said brine to a lower temperature at a lower pressure when said brine is distributed through said orifices.

6. In an effect-to-effect evaporation of a liquid a method for distribution of said liquid for downflow evaporation thereof from a pool of said liquid whereto more of said liquid is added, the improvement comprising:

(a) forming a multiplicity of orifices in parallel array through a plate supporting said pool of liquid for said distribution of said liquid through said orifices i n to a multiplicity of vertical evaporation channels for partially evaporating said liquid,

(b) determining the level of said liquid in said pool and

(c) adjusting the flow diameters of said orifices responsive to said determined level of said liquid by translation of an array of orifice adjusting means adjacent to said orifices,

(d) and controlling the rate of flow of said liquid through said orifices and maintaining said liquid level in said pool within a selected level range above said plate and maintaining effect-to-effect pressure control causing flashdown of said liquid, wherein said determining of said level of said liquid in said pool is measured in terms of the pressure of said liquid on said plate, and wherein said adjusting of said flow diameters of said orifices is further responsive to said measured pressure on said plate, and wherein said selected liquid level range of said pool is determined from said measured pressure of said liquid in said pool.

7. The method of claim 6, wherein said evaporation channels consist of a bundle of vertical evaporation tubes for partial evaporation of said liquid with heat transmitted from vapor condensed on the outside walls of said tubes and wherein said orifices are aligned to deliver said liquid into an inlet ends of said evaporation tubes after said flashdown of said liquid.

8. The method of claim 7 wherein said multiplicity of orifices are spaced (preferably) by about 1 inch to 2 inches from said inlet ends of said tubes and wherein said orifices are generally spaced by about 1/4-inch to 6 inches from said inlet ends.

9. The method of claim 7 wherein said control of said rate of flow of said liquid provides flashdown of said liquid during distribution of said liquid into said tubes for foamy annular flow of said liquid through said tubes to improve the thermal efficiency of said evaporation.

10. The method as in claim 6, wherein said orifices consist of two arrays of corresponding parallel orifices slideably mounted adjacent to one another and wherein said adjusting of said flow diameters is provided by a sliding translation of one of said two arrays over the other of said two arrays.

11. The method of claim 10 wherein said distribution of said liquid is maintained by causing said two arrays of parallel orifices to be repetitively translated back and forth to dislodge debris obstructing said orifices therefrom.

12. The method of claim 6 wherein said evaporation of said liquid occurs in an effect representing one of a series of downflow evaporation effects and wherein (more of said) liquid is added to said pool from an evaporation effect above said effect in said series of downflow effects.

13. The method in claim 6 wherein said liquid consists of partially evaporated seawater flowing through a multi-effect series of stacked evaporators and wherein said control of said rate of flow of said liquid maintains said series of evaporators essentially free of precipitation of solutes from said seawater evaporated over an extended range of evaporation rates.

14. The method of claim 6, wherein said liquid consists of brine and wherein said control of said rate of flow of said liquid feed maintains non-saturation of a solute in said brine in in each of a series of downflow evaporation effects.

15. The method of claim 6 wherein said control of said rate of flow of said liquid provides for flow of said liquid within about a 5-fold range of flowrates and said maintained level of said liquid in said pool is about 6 inches.

16. The method of claim 6 wherein said control of said rate of flow of said liquid distributed into said evaporation channels is used to control effect-to-effect flow (stability) instability (during said distribution of said liquid) and to improve the efficiency of said evaporation.

17. The method of claim 6 wherein said liquid is a brine and wherein a monomeric surfactant dispersant is added to said liquid to control precipitation of (a solute) scale during said evaporation of said liquid to improve on-line availability of said (method) evaporation.

18. The method of claim 6 wherein said liquid is seawater being desalinated by said evaporation and wherein said method reduces the overall height of said effect used for said effect-to-effect evaporation and the height of a vertical multi-effect facility for seawater desalination.

19. The method in claim 6 wherein said maintaining of said selected level range above said plate reduces the overall height of a facility for said effect-to-effect evaporation and the energy required to pump said liquid into said facility.

20. The method of claim 6 wherein said control of said rate of flow of said liquid is carried out with a programmable logic controller for said effect-to-effect evaporation using process data including data for said determining of said level of said liquid in said pool.

21. The method of claim 6 wherein said control of said rate of flow of said liquid maintains continuous feed flow into all said channels and prevents precipitation of solutes in said channels.

22. The method of claim 6 wherein said control of said liquid level in said pool provides for a reduction of said level in said pool and maintains continuous feed flow through all orifices of each effect during turned-down evaporator operation including start-up and shut-down phases of operating said evaporator.

23. The method of claim 6 wherein said evaporation is applied in a multi-effect series for partial evaporation of said liquid, and wherein said liquid is brine concentrated in salinity as it is cascaded from effect-to-effect.

24. The method of claim 6 wherein said liquid is seawater and the salinity of said seawater is measured in said pool, and wherein said rate of flow of said seawater is controlled to prevent said salinity from reaching the saturation limit of calcium sulfate dissolved in said seawater by reference to a known solubility limits for calcium sulfate in seawater concentrates at the temperatures of said effect-to-effect evaporation.

25. In a multi-effect evaporation of a liquid a method for distribution of said liquid for downflow evaporation thereof from a pool of said liquid whereto more of said liquid is added, the improvement comprising:

(a) forming a multiplicity of orifices in parallel array through a plate supporting said pool of liquid for said distribution of said liquid into a zone for flashdown of said liquid,

(b) determining the level of said liquid in said pool by sensing the pressure of said liquid in said pool on said plate and

(c) adjusting the flow diameters of said orifices responsive to said sensed pressure on said plate by translation of a horizontal array of orifice adjusting means adjacent to said orifices,

(d) and controlling the rate of flow of said liquid distributed into said zone and maintaining said pressure of said liquid in said pool supported by said plate within a selected pressure range to maintain said flashdown of said liquid into said zone, wherein said multiplicity of orifices consists essentially of two arrays of corresponding parallel orifices adjacent to one another, and wherein said adjusting of said flow diameters of said orifices is provided by sliding one of said two arrays of orifices over the other of said two arrays of orifices.