| Indicators |
Proposed installation |
Standard installation |
Change |
| In the processing stage |
| 3 sections:- section of Hydrotreating coking nafta;- Penex isomerization section»;- platforming section with moving catalyst layer. |
4 sections:-hydrofining;- isomerization; - hydrofining;- reforming. |
there are fewer partitions in the proposed installation |
| Volume of production per year, thousand tons |
|
| - stable gasoline |
432 |
521 |
-89 |
| - reformat |
280 |
256 |
24 |
| - isomerizate |
237 |
190 |
47 |
| Price of the product, rub /tons |
|
| - stable gasoline |
21000 |
21000 |
0 |
| - reformat |
36200 |
36200 |
0 |
| - isomerizate |
22400 |
22400 |
0 |
| Revenues from sales, mln rub |
24517 |
24464 |
53 |
| Total cost, mln rub |
15906 |
18742 |
-2836 |
| Profit from sales, mln rub. |
8611 |
5722 |
2889 |
| The number of equipment, units |
171 |
213 |
-42 |
| Capital investments, mln rub. |
36202 |
45072 |
-8870 |
| Number of employees, persons |
56 |
96 |
-40 |
| Profitability of sales, % |
35.1 |
23.4 |
11.7 |
| Cost-effectiveness, % |
54.2 |
30.5 |
23.7 |
| Energy intensity, rub/ rub |
0.122 |
0.24 |
-0.11 |
| Material intensity, rub / rub |
0.524 |
0.53 |
-0.001 |
| Labour intensity, rub / rub |
0.002 |
0.003 |
-0.001 |
| Labour productivity, thousand rub /person |
43780 |
25483 |
18296 |