Apparatus for reclaiming waste gas treating chemical

• US 5,441,605 A
• Filed: 10/19/1994
• Issued: 08/15/1995
• Est. Priority Date: 07/18/1988
• Status: Expired due to Term

• Current Assignee: CCR Technologies Ltd.
• Original Assignee: Canadian Chemical Reclaiming Ltd.
• Inventors: Beasley, Todd, Merritt, Dwight A.
• Primary Examiner(s): Bascomb, Jr., Wilbur
• Application Number:
  US08/325,504
• Time in Patent Office: 300 Days
• Field of Search: 202/176, 202/175, 202/234, 202/205, 202/202, 202/182, 202/183, 202/184, 202/267.1, 202/153, 202/233, 202/235, 203/42, 203/DIG. 25, 203/11, 203/86, 203/100, 203/87, 203/12, 203/14, 159/47.3, 159/46, 159/29, 159/901
• US Class Current: 202/176
• CPC Class Codes: B01D 1/02 Evaporators with heating coils
• CPC Class Codes: B01D 3/10 Vacuum distillation B01D3/12 takes precedence
• CPC Class Codes: B01D 5/0087 Recirculating of the cooling medium
• CPC Class Codes: B01D 5/0093 Removing and treatment of non condensable gases
• CPC Class Codes: C07C 213/10 Separation; Purification; Stabilisation; Use of additives
• CPC Class Codes: Y10S 203/11 Batch distillation
• CPC Class Codes: Y10S 203/90 Particular type of heating

Abstract

Process and apparatus for reclaiming or concentrating waste aqueous solutions of gas treating chemicals, such as alkanolamines, used for removing acid components or water vapor from natural gas. The process involves heating the waste solution under a high vacuum to form a vapor and a liquid residue. The temperature and vacuum can be varied to form a vapor consisting mainly of water vapor or a vapor containing both water vapor and vaporized gas treating chemical. The vapor is subsequently condensed or passed through a wash column to produce a concentrated solution. The liquid residue is heated by passing it through a single pass, generally co-current heater at a rate which avoids localized overheating of a liquid to a temperature above the decomposition temperature of the gas treating chemical. The heated liquid residue is then used to heat the feed waste solution by being thoroughly mixed with it, thus avoiding overheating of the feed solution. The production of corrosive elements and the use of prolonged residence times is avoided so that the apparatus may be made of carbon steel rather than more expensive stainless steel.

Claims

1. Apparatus for concentrating or reclaiming a waste aqueous solution of a chemical having a decomposition temperature, said apparatus comprising:

a still for subjecting said solution, heated to a temperature below said decomposition temperature, to a high vacuum of at least 16 inches of mercury in order to produce a vapor and a liquid residue;

vacuum generating means communicating with said still to generate said high vacuum in said still;

a heater for heating a portion of said liquid residue received from said still, said heater comprising an internal space, at least one burner for producing combustion gases which pass through said internal space, and tube means for conveying said portion of said liquid residue in a single pass through said internal space in a direction generally co-current to said combustion gases;

pump means for moving said portion of said liquid residue from said still through said tube means at a velocity high enough to prevent a film of said liquid residue immediately adjacent to inner surfaces of said tube means from being heated to a temperature exceeding said decomposition temperature;

mixer means for thoroughly mixing said portion of said liquid residue from said heater with a feed of said waste aqueous solution of said chemical to effect heating of said feed solution;

cooler means for condensing vapor from said still to produce a liquid condensate; and

a plurality of pipe means for conveying said feed of said waste aqueous solution of said chemical to said mixer means, heated liquid residue from said heater to said mixer means, liquid from said mixer means to said still said portion of said liquid residue from said still to said pump means and from said pump means to said tube means of said heater, and vapor from said still to said cooler means.

2. Apparatus according to claim 1 further comprising wash column means for contacting vapor from said still with water in countercurrent flow to cause fractionation between said vapor and said water, said wash column means being connected to said pipe means conveying vapor from said still to said cooler such that said vapor passes through said wash column means before entering said cooler means.

3. Apparatus according to claim 1 wherein at least said still and said tube means of said heater are made of carbon steel.

4. Apparatus according to claim 1 made substantially completely of carbon steel.

5. Apparatus according to claim 1 further including vapor/liquid separator means, and said pipe means including means for conveying said liquid condensate and remaining uncondensed vapor from said cooler to said vapor/liquid separator means.

6. Apparatus according to claim 1 wherein said still includes a downwardly tapering conical internal surface, said pipe means being positioned to introduce said liquid from said mixer means generally tangentially onto said surface at an upper region thereof, said still further comprising an outlet for said liquid residue at a lower region of said conical surface.

7. Apparatus according to claim 1 wherein said heater includes burner means in said internal space for producing both radiant and convected heat, and wherein said tube means are disposed in at least two separate coiled sections, at least one of said coiled sections being positioned in a region of said internal space close to said burner means to receive radiant heat from said burner means and at least one other of said coiled sections being positioned in a region of said internal space more distant from said burner means to receive only convected heat from said burner means, said at least one other coiled section being arranged downstream of said at least one coiled section according to the direction of movement of said liquid residue through said tube means.

8. Apparatus according to claim 1 wherein said at least one other of said coiled sections is shielded from radiant heat from said burner means by a metal shield positioned in said internal space to block said radiant heat without unduly restricting said flow of combustion gases through said internal space.