Detailed Project Report (DPR) on tri ethylene glycol (teg)

Detailed Project Report (DPR) on tri ethylene glycol (teg)

TRIETHYLENE GLYCOL (EIRI-1083)

Triethylene glycol is a transparent, colorless, low-volatility, moderate-viscosity, watersoluble liquid. Under normal conditions, there is no detectable odor; under high vapor concentrations, a slightly sweet odor may be detected. It is completely miscible with water and many organic liquids. Triethylene glycol has properties similar to other glycols and may be used preferentially in applications requiring a higher boiling point, higher molecular weight, or lower volatility than diethylene glycol. The hydroxyl groups on triethylene glycol undergo the usual alcohol chemistry giving a wide variety of possible derivatives. Hydroxyls can be converted to aldehydes, alkyl halides, amines, azides, carboxylic acids, ethers, mercaptans, nitrate esters, nitriles, nitrite esters, organic esters, peroxides, phosphate esters and sulfate esters. Triethylene glycol may be used directly as a plasticizer or modified by esterification. The solubility properties of triethylene glycol are important for many applications. End-uses for triethylene glycol are numerous.

Cost Estimation (All Fig. in US$)

Plant Capacity                                                 45 TONS/Day
Land and Building (Area 10000 sq.mt.)    US$ 50 Lacs
Plant & Machinery                                          US$ 5 Lacs        
W.C. for 3 Months                                           US$ 10 Lacs          
Total Capital Investment                               US$ 68 Lacs             
Rate of Return                                                  65%  
Break Even Point                                             24%

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•    Note: The project investment cost and capacity are subject to change without any notice. Future projects may have different values of project cost and capacity.
 

MARKET  SURVEY CUM  DETAILED  TECHNO
ECONOMIC FEASIBILITY  REPORT
covers

  • Introduction
  • Production of tri ethylene glycol
  • Ethylene carbonate process
  • Halcon acetoxylatin process
  • Teijin oxychlorination process
  • Union carbide syngas process
  • Hydrolysis of ethylene oxide
  • Chemistry of the reaction
  • Process description of ethylene glycol plant
  • Applications
  • Market survey
  • The production of ethylene oxide and triethylene glycol
  • Method for producing highly pure triethylene glycol
  • Method for producing triethylene glycol   
  • Triethylene glycol process
  • Preparation of triethylene glycols from ethylene oxide
  • Recovery of glycols from mixed glycol composition by distillation with acid treatment
  • Addresses of chemical suppliers/manufacturers
  • Ethylene
  • Medical oxygen
  • Triethylene glycol

Supplier of plant & machinery

  • Distillation columns
  • Cooling towers & heat exchangers
  • Reaction vessel
  • Distillation equipment
  • Continuous evaporator
  • Laboratory reactors
  • Circulating pumps

Bubble caps manufacturers & exporters

  • Air cooled condenser
  • Vapour liquid separator manufacturers & exporters

APPENDIX

 1.  COST OF PLANT ECONOMICS
 2.  LAND & BUILDING
 3.  PLANT AND MACHINERY
 4.  FIXED CAPITAL INVESTMENT
 5.  RAW MATERIAL
 6.  SALARY AND WAGES
 7.  UTILITIES AND OVERHEADS
 8.  TOTAL WORKING CAPITAL
 9.  COST OF PRODUCTION
10.  PROFITABILITY ANALYSIS
11.  BREAK EVEN POINT
12.  RESOURCES OF FINANCE
13.  INTEREST CHART
14.  DEPRECIATION CHART
15.  CASH FLOW STATEMENT
16.  PROJECTED BALANCE SHEET

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