Brine Stripping Distillation Process   Part of 145MM lbs/year Tertiary Amines Plant, stock #600448     Stock #600547               Download IPP’s Tertiary Amines Plant Advertisement       Brief Overview   The Brine Stripping Distillation Process System is designed to remove light organics from a brine stream using a live-steam fed stripping column. This equipment was previously used in the Procter and Gamble Tertiary Amines Plant in the United States for removing di-methyl amine in a brine stream from a level of about 5% down to a level of less than 18 ppm.     Alternative uses for the Brine Stripping Distillation Process include the separation or removal of light organics from any heavy organic or brine stream.     The Honeywell 3000 process control system and program are available with this process, as is all necessary documentation (equipment files, P&IDs, PFDs, operating manuals, etc.). All pressure vessels have National Board numbers, and spare parts are available for most equipment. The plant has been properly cleaned of all chemicals. This site is very accessible by road and rail. Equipment can be barged from the local docks only a few miles away on a major river.           Shut Down : 2005           Major Equipment     Click Here to View the Brine Stripping System Brief Equipment List             Brine Stripping Column (Stock #216093): Light organics can be removed using the stripping column. This particular application was removing di-methyl amine from a level of about 5% down to a level of less than 18 ppm. Brine feed to the stripper is preheated to approximately 235°F. The 40,000 lbs/hr of brine feed to the stripper enters at the top of the column as a liquid and flows down through the packing into the stripper pot.             At the same time, 1,200 lbs/hr of steam is introduced at the bottom of the stripper, just above the liquid level in the stripper pot. The steam travels up the column and vaporizes any light organics out of the brine solution. The steam and light organics exit the top of the stripper and pass through an entrainment separator used to knock out entrained liquid (primarily brine) while allowing the steam and light organic vapors to pass through the stripper overheads condenser. This exchanger condenses the steam and light organics, which can be reworked or disposed. A level is maintained in the brine stripper pot to insure that the evaporator feed pump suction is flooded. The brine from the stripper is then pumped to the first effect of the evaporator. The 297 cu. ft., 304SS stripper column is 30" (d) x 62' (l) and is rated for FV/180 psig at 400°F. It was manufactured in 2000.               Read More>>         Home The Plant Gallery Contact Site Map   powered by Ultra InfoTech   © 2011 International Process Plants and Equipment Corp.