Return to Table of Contents

Section VII - The Oxo-Synthesis

6. Operating Costs.

The cost of the HP section of the plant is approximately 35.RM/1 yearly ton alcohol. This however does not include the gas preparation, compression plant and the utilities.

The labor requirement for a 15,000 ton/year unit were given as 50 men/shift (based on batch operation). This includes all operating and maintainance labor.

The Utilities are given below:

Basis: 15,000 ton/year alcohol from C11-C17 with 30% olefine content in feed.

Heating Requirement:

 

Distillation

320,000 kg cal/hr

Gas preheater 1st stage

13,500 kg cal/hr

Gas preheater 2nd stage

16,500 kg cal/hr

Methanizer

31,000 kg cal/hr

Losses

40,000 kg cal/hr

 

421,000 kg cal/hr

Cooling Requirement:

 

Synthesis, 1st stage

100,000 kg cal/hr

Synthesis, 2nd stage

52,500 kg cal/hr

Product cooler, 1st stage

120,000 kg cal/hr

Product cooler, 2nd stage

150,00 kg cal/hr

Final cooler

90,000 kg cal/hr

Gas cooler

60,000 kg cal/hr

 

572,500 kg cal/hr

Power Requirement:

100 Kwh

The operating cost was given based on 1 Kg. alcohol (for 15,000 ton/year plant).

Power

0.04 Rm/kg alcohol

Labor

0.03 Rm/kg alcohol

Laboratory

0.01 Rm/kg alcohol

Materials

0.01 Rm/kg alcohol

Feedgas

0.03 Rm/kg alcohol

Amortization

0.06 Rm/kg alcohol

 

0.18 Rm/kg alcohol

At Ruhrchemie the cost of the olefine in the feed was calculated at 0.43 RM/kg. Thus the price of the final product would be 0.60-0.65 RM/kg Alcohol.

7. Conclusions.

The oxo-synthesis is the second of three major different processes for the production of high boiling alcohols. The great effort put into its commercial realization is due to the shortage of all kinds of soaps and detergents in Germany. Another important use for the product would have been its application in lubricating esters.

The development of the process may lead to continuous operation and possibly better control of the synthesis, such as suppression or closely controlled shift of the double bond to give clearly defined a-substituted alcohols of predetermined branching.

Return to Table of Contents