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1268710 - EVAPORATOR, CRYSTALLIZER, 10' X 9'' & 6'C, S-WELLS, 1 EFFECT, 316LSS, 7000PPH [1]

  • MFD.BY:HPD
  • DATE MFD:1993
  • TYPE:Crystallizer, forced circulation. Liquor pumped through heated chamber and vapors boiled off, concentrating liquor while vapors are recondensed and collected separately. Solids maintained in suspension at all times.
  • EFFECTS:1
  • MAT'L CONSTRN-CONTACTS:Inconel 625 & 316LSS
  • MAIN BODIES:A./ Crystallizer- 8,000Gall.approx., Mfd. Struthers Wells, "Krystal" Cooling type crystallizer. 316ELC SS construction. DP 15#/FV @ 250deg F. Suspension chamber 10'OD X 9's-s + 6' deep conical bottom reducing to approx. 7'6"dia w/dished bottom head. Top h
  • HEAT EXCHANGER(S):NA (Originally 3)
  • HEAT EXCHANGE AREA:NA (Originally: Crystallizer Reboiler; 258Sq.Ft.approx. Horizontal 2-pass, shell & tube . 48 @ 2"Dia X 11'L tubes. 22" X 14' oall. Rated 25#FV/ 50#FV. Inc625 wetted parts.nStill Reboiler; 77Sq.Ft.approx. Vertical 1-pass, shell & tube . 21 @ 1-1/2"Dia X
  • PUMP(S):NA (Originally: Recirculation Pump; 15HP elbow, approx. Durco 8 X 6 X 14, Inc 625. @ Mech seals. Slurry pump; Durco 2 x 1 x 10, 20gpm @ 80'tdh. Crystalizer Condensate Pump; Durco 1-1/2 x 1 x 6, 3gpm @ 20'tdh.1hp, 316SS. Product Pump; Durco 1-1/2 x 1 x 8,
  • EVAP. RATE-PPH H2O:NA (Prior Service: 7000)
  • CAPACITY:NA (Prior Service: 5,000 gal. approx. total.)
  • PRIOR SVC:Chemicals, feed Sodium Chloride, Sodium hydroxide, Butanol, DETA. Evaporation of H2O & DETA produced concentrated NaOH & crystallization of NaCL
  • COMMENTS:Remaining components from original system include:nA./ 8000Gall. Cooling type Crystallizer vessel. Price $67,500.00nB./ 48" X 10'6" Forced Circulation Recovery system. Price $27500.00nComplete system NA (Originally included: Solvent distillation unit,
  • SHIPPING SIZE-W X H X L:8'W X 9'H X 80'L
  • APPROX. WEIGHT-LBS:30000#
  • QUANTITY:2