increase extraction of light fractions from crude oil
increase depth of processing (distillation) of natural oil
or intensification oil treating
( reducing the cost of refining crude oil )

Left - Illustrations fractional composition of crude oil.

- Initial boiling point decreased to 11 ° C ( from 65 ° up to 54 °)
- Exit "broad" straight-run gasoline fraction (BP - 180 ° C) increased by 33%
- Exit "broad" virgin diesel fraction (160 - 360 ° C) decreased by 7.5%
- The output fraction 320-360 ° C, containing high-melting paraffins C20-C24, significantly worsening the low temperature properties of diesel fuel (DF), decreased by 15%.

Carrying out a large series of experiments, we can say, that the most typical graph of change properties of processed crude oil (in this mode) is this.

6. The third series of experiments gave the following results

1. As a result nonchemical processing crude oil withour industrial machine there are changes in hydrocarbon composition, which is accompanied by a significant decrease in viscosity (19%) and the density (9 units).

2. The total amount of light fractions, as a result of processing, increased by 3.5%, indicating intensive degradation of the residual hydrocarbon oil fraction (360 ° C). It should be consider that our tests were carried out with mixture of crude oil and gas condensate. In this way, the expected effect on normal or heavy viscous crude oil will be higher.

3. A result of processing nature oil ( in the selected processing mode ), the amount of light fractions greatly shifted in the direction of gasoline. This proves that the process intensive destruction of hydrocarbon residual fraction 360 ° C. to form shorter molecules (with the smaller number of carbon atoms in the molecule) and radicals. As well as facilitating the fractional composition in the temperature range up to 360 ° C, whereby part the diesel fraction of hydrocarbons goes into gasoline.

As a result of oil treatment, significantly increased content of hydrocarbons C5-C6, which are extremely valuable component as a raw material for the process of isomerization.

4. Despite the that the amount of the diesel fraction is reduced, low-temperature properties of future diesel fuels will be much better, by the significant reduction in the proportion of high-melting paraffins C20-C24. This greatly influences level of Сloud Point and a fuel minimum temperature of filterability. At the same time temperature range of boiling 20% and 90%, determining loyalty to the action of fuel depressants, it remains unchanged, which is a very positive result.

Ie there is a simultaneous improvement in the low temperature properties of diesel fuel by reducing the proportion of high melting paraffin hydrocarbons maintaining high pick-up to the action of depressants This allows to produce diesel fuel with higher low-temperature properties.

7. If necessary, the process parameters may be significantly changed, thus intensify the content of light fractions in the desired temperature range, to provide individual needs.

8. Why are we talking about select of individual processing? Example:

While processing a new batch crude oil from "Leninogorskneft" (Tatneft), obtained the following results:

The density increases, the volume of the gasoline fraction is not changed, the volume of diesel fraction is increased by 5-7%, but at the end (340-360 degrees). As a result of the increase in research of light fractions in the range of up to 360 degrees increased by 10.2%! The viscosity at 20 Celsius degrees increased by 12%.

Narrower fractions:

1. Starting point - 85 ° C + 200%.
2. Start point - 150: C + 18%.
3. 85-180: + 9%.
3. 160-360 + 6%.
4. 180-360: + 7.3%.
5. 180-320: + 1.85%.

2. All experimental work executed at our industrial equipment and the possibility of a negative scale effect is zero.

3. Mid-range increased light fractions volume of gasoline and/or diesel fuel from 3.5 up to 7%.

4. The range depends from the composition of the original oil and the treatment regime.

5. The processing mode may be selected experimentally in a predetermined direction, namely - to increase the diesel fraction, or fraction of straight run gasoline.

6. By the way, we have a "mono-additives" that allow you to increase the octane number of of straight run gasoline up to 92 units. (This is not an additive package).

7. This project can be realized at your refinery, if :

providing exact data your oil distillation, the exact problem formulation ( determination of the goal - which faction should be increased ) and short research works on with your oil and on our installation in Moscow.

8. What can I say about the money ? Do You need this installation for You refinery or not? A simple example.

The increase volume of light petroleum products ( light fractions of diesel fuel or gasoline ) by 1%, for the Kremenchug refinery (Ukraine), in time of 45% loading with light oil, according to the calculations of their experts, provides economic benefit $ 400 000 per month.

9. What can I say about the running time of our equipment ? Minimum of 2 years. Many of our systems work reliably 4-5 years ...

10. What do I need to add important ? Internet is full references to such technologies. But they work only in the laboratory or in a laboratory desktop layouts, or, more often, their authors never made comparative tests on laboratory crude flash tower ...

We invite You to work together for the using this technology. Why ?