Dihydro Terpinyl Acetate Production from terpinyl acetate via hydrogenation
Dihydro Terpinyl Acetate Production Cost Breakup from terpinyl acetate via hydrogenation
This study analyzes Dihydro Terpinyl Acetate Production from terpinyl acetate via hydrogenation, covering manufacturing, process flow, operating expenses, and financial considerations.
Details : Germany - based plant Q2 2026
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This report entails a detailed cost evaluation of Dihydro Terpinyl Acetate production from terpinyl acetate via hydrogenation. The manufacturing process involves placing the terpinyl acetate and a hydrogenation catalyst into a hydrogenation reactor, followed by stirring. The air inside the hydrogenation reactor is replaced with nitrogen three times, and again by replacing the nitrogen with hydrogen three times. Once the replacement is completed, a standard pressure is maintained at 2.5 to 3.5 Mpa with hydrogen. After the pressure in the hydrogenation reactor does not change, the materials in the hydrogenation reactor are cooled to room temperature, hydrogen is replaced with nitrogen three times, followed by standing and layering, extruding the product out with nitrogen, secondary standing, and precipitation. Finally, filtration is done to produce Dihydro Terpinyl Acetate.
The project economic analysis provided in the report discusses a Germany-based plant:
- Manufacturing Process
- Process Flow
- Material Flow
- Material Balance
- Raw Material and Product's Specifications
- Raw Material Consumption
- Product and Co-Product Generation
- Capital Investment
- Land and Site Cost
- Offsites/Civil Works
- Equipment Cost
- Auxiliary Equipment Cost
- Contingency
- Engineering and Consulting Charges
- Working Capital
- Variable Cost
- Raw Material
- Utilities
- Fixed Cost
- Labor Requirement & Wages
- Overhead Expenses
- Maintenance Charges
- Financing Costs
- Interest on Working Capital
- Interest on Loans
- Depreciation Charges
- General Sales and Admin Costs
- Production Cost Summary
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