|
 |
The basic principles of our technology

Our technology involves
the Bernulli principle, which is a case of the general energy
preservation law for a flow of an ideal uncompressible liquid
(no internal friction):
ρv2/2 + ρgH + P
= const,
where
ρ - density of the liquid
v - velocity of the flow
H - height of the liquid
P - pressure.
The constant on the right
side of the equation is called the full pressure. The dimension
of all of the equation components is a unit of energy per unit
of liquid volume.
This is called the
Bernulli equation.
For a horizontal tube, H =
const, and the equation will look look this:
ρv2/2 + P =
const
According to Bernulli
principle, full pressure in a
stabilized flow of liquid remains constant along this flow. Full
pressure consists of static pressure, dynamic pressure and
weight pressure. The Bernulli principle implies that in the case
of decrease of the flow’s cross-section, as the velocity
(dynamic pressure) of the flow increases, which in turn,
decreases static pressure. The Bernulli principle is also true
for laminar flows of gases. The phenomenon of decrease of static
pressure with increase of velocity of the flow is the principle
of operation of various types of pumps and flow meters.

The
Bernulli principle works ideally
only for zero-viscosity liquids, i.e. liquids that do not have
friction with and do not stick to the pipe surface. In reality,
experiments show that velocity of a liquid on the surface of a
solid body always precisely equals zero. This is the reason that
various surfaces, subjected to flows of liquids, always have
some kind of residue; this would also explain the layer of dust
on a ventilator.
The Bernulli principle
can be applied to a flow of an ideal uncompressible liquid
through a small opening in a side wall or in the bottom of a
wide vessel. According to the Bernulli principle:
ρgH + P0 = ρv2/2
+ P0,
where
P0 – atmospheric pressure;
H – the height of the
liquid in the vessel;
v – outflowing fluid
velocity;
Hence v = (2gh)^0.5. This
is the Toricelli formula. It shows that the liquid flows from an
opening in a wide vessel at the same velocity as a free falling
object.
Quality of the
feedstock oil.
Hydrodynamic modules,
produced by our company, do not require pre-treatment of oil.
Those modules can successfully process both refined and raw oil.
The equipment can process multiple oil types, such as rapeseed,
sunflower, palm, mustard, soybean oil, canola oil, if the oil’s
acid number does not exceed 6. No modification to the equipment
is needed to switch from on type of the oil to another.
However, to obtain a high
quality biodiesel, the oil should be as close to the standards
as possible. On the right, you can see a table with fatty acid
composition of rapeseed oil.
Rapeseed
oil fat and acid composition
|
Acid name
|
OSTU 46.072:2005
(Ukraine) |
Cimbria Sket GmbH
(Germany) Typical example |
|
|
Eruca acid, % |
|
|
|
|
|
|
>5% |
<5% |
(5% tolerance for every acid) |
|
C14:0 |
<0.2 |
<0,2 |
|
0,1 |
|
|
C16:0 |
1.5-6.4 |
2.5-6.0 |
|
5 |
|
|
C16:1 |
<3.0 |
<0.6 |
|
0,7 |
|
|
C17:0 |
- |
- |
|
0,1 |
|
|
C17:1 |
- |
- |
|
0,2 |
|
|
C18:0 |
0.5-3.1 |
0.8-2.5 |
|
1,8 |
|
|
C18:1 |
0.8-60 |
50.0-65.0 |
|
57,9 |
|
|
C18:2 |
11.0-23.0 |
18.0-20.0 |
|
21 |
|
|
C18:3 |
5.0-13.0 |
6.0-14.0 |
|
10,3 |
|
|
C20:0 |
3.0 |
0.1-1.2 |
|
0,6 |
|
|
C20:1 |
3.0-15.0 |
0.1-4.3 |
|
1,4 |
|
|
C20:2 |
<1.0 |
- |
|
- |
|
|
C22:0 |
<2.0 |
<0.6 |
|
0,3 |
|
|
C22:1 |
5.0-60.0 |
<5.0 |
|
0,6 |
|
|
C22:2 |
<2.0 |
- |
|
- |
|
|
C24:0 |
<2.0 |
<2.0 |
|
- |
|
|
C24:1 |
<3.0 |
<2.0 |
|
- |
|
Minimal energy
consumption.
The design of our system
uses stream oil heaters; part of the heat is compensated by the
reaction of methanol and alkali. This type of heating saves
electric energy. Besides, the technology does not use excess
methanol, which is always present in the end product (methyl
ester) in a batch reaction process. And since the reaction time
is drastically reduced compared to the old batch process, due to
the stream nature of the reaction, the energy consumption is
reduced 9 to 11 times.
“Single Pass” reaction.
The hydrodynamic
technology does not require a second stage transesterification,
unlike the old batch systems. Reaction time is reduced by
several times, but the capacities of the system we build can be
both small and very large with very compact dimensions of the
unit.
Quality of the Biodiesel is in compliance with ASTM D-6751 and
EN 14214 Standards
|
No. |
Specification |
ASTM D-6751 |
EN 14214 |
BiodieselMach fuel
specification |
|
1 |
Methyl esters content, % |
- |
>96.5 |
97.9 |
|
2 |
Density at 15C, kg/m3 |
- |
860-900 |
882.4 |
|
3 |
Viscosity at 40C, sq.mm/s |
1.9-6.0 |
3.5-5.0 |
4.24. |
|
4 |
Closed vessel flashpoint, degrees C |
>130 |
>120 |
161 |
|
5 |
Sulfur, mg/kg |
<0.05 (%) |
<10 |
0.016 |
|
6 |
Cetane number |
>47 |
>51 |
52 |
|
7 |
Sulfated ash, % (m/m) |
<0.02 |
<0.02 |
0.01 |
|
8 |
Water content by weight, % |
<0.05 |
<0.05 |
0.01 |
|
9 |
Copper strip test |
<No. 3 |
Class 1 |
Compliant |
|
10 |
Acid number, mg KOH/g |
<0.8 |
<0.5 |
0.22 |
|
11 |
Methanol content by weight, % (m/m) |
- |
<0.2 |
0.1 |
|
12 |
Monoglycerides by weight, % (m/m) |
- |
<0.8 |
0.6 |
|
13 |
Diglycerides by weight, % (m/m) |
- |
<0.2 |
0.1 |
|
14 |
Triglycerides by weight, % (m/m) |
- |
<0.2 |
0.13 |
|
15 |
Free glycerine by weight, % (mm) |
<0.02 |
<0.02 |
0.01 |
|
16 |
Total glycerine content, % (m/m) |
<0.24 |
<0.25 |
0.25 |
|
17 |
Iodine number |
- |
<120 |
61 |
|
18 |
Phosphorus content mg/kg |
<0,001% |
<10 |
10 |
|
19 |
Group I metal content (Na, K) |
- |
<5.0 |
- |
|
20 |
Group II metal content (Ca, Mg) |
- |
<5.0 |
- |
|
21 |
Maximum carbonating ability, % |
- |
0.3 |
0.03 |
Minimal dimensions of
the modules.
Our automated systems take
10 to 15 times less space than traditional system of comparable
capacity.
|
|
Primary Speicifications |
|
|
|
|
|
|
No |
Specification |
Value |
|
1 |
Feedstock processing capacity, dm3/min |
8…14 |
|
2 |
Methanol w/catalyst mixture consumption,
dm3/min |
0,1-0,3 |
|
3 |
Oil vessel volume, dm3 |
50 |
|
4 |
Methanol vessel volume, dm3 |
12 |
|
5 |
Finished product vessel volume, dm3 |
30 |
|
6 |
Oil and methanol temperature, degrees C |
40…70 |
|
7 |
Heater power consumption, kW |
1,5 |
|
8 |
Pump drive power, kW |
2,8 |
|
9 |
Total power consumption, kW |
4,5 |
|
10 |
Power supply, 3-phase |
240VAC @ 60Hz |
|
11 |
Maximum dimensions, mm |
|
|
|
length |
865 |
|
|
width |
755 |
|
|
height |
1250 |
|
12 |
Maximum unit weight, kg |
250 |
|
 |
No need for washing and
drying of biodiesel, no methanol recovery.
In traditional systems
obtaining biodiesel of appropriate quality takes a lot of
effort. The product of the transesterification in the
traditional technologies contains a lot of contaminants, which
must be removed. This dictates the need for additional
equipment, such as biodiesel washing (usually with a mixture of
water and alcohol) and thermovacuum drying system.
The hydrodynamic method
neither washing nor drying biodiesel is needed, hence no need to
dispose of the waste water and other substances.
Component ratio:
Vegetable oil: 100 kg
Methanol: 12.8 liters
KOH: 0.9 kg
Energy: 11 kW/hr per 1000
liters of oil
Temperature of feedstock
oil: 20C
Temperature of feedstock
oil: 35C
Versatility of the
equipment.
An important point to
consider when selling the product (biodiesel) to the end user is
its usability in specific climatic conditions, and its
compatibility with specific engines. Cold climatic conditions
require special additives to raise clod point of the fuel. Such
additives are called ‘depressants’.
The process of blending
the additives with biodiesel requires special equipment and
special technologies. The hydrodynamic blenders are perfectly
suited for this task. They have a very high capacity: from 1 to
60 cubic meters per hour with two to seven components.
We supply special blending
units which can be used for biodiesel blends with petroleum
diesel, as well as for blending biodiesel with various
additives. Those units can also be used to prepare fine blends
of various liquid substances.
Some uses for blending
equipment:
-
Gasoline
blending
The unit USB-18 (USB-60)
can be used for compounding two to five separate components,
including low octane gasoline with additives. This can be useful
to filling stations, oil processing plants and foodstuffs
industry.
Other
known blending technologies lead to a product which will
separate over time. The greatest advantage of our blending
machine is that the blend will remain stable for up to 180 days
guaranteed.
-
Diesel
blending
Conventional diesel,
besides hydrocarbons, contains molecules of water, parathion,
sulfur and solid contaminants. Most of the fuel molecules remain
in polymerized state, therefore, when the fuel is ignited, the
burning process starts in the active part of every large
polymeric chain. Thus, the process of combustion will be
retarded by water molecule collisions, while sulfur and parafins
will not burn completely, which will lead to formation of toxic
exhaust and generally slow combustion.
High frequency
hydrodynamic treatment of diesel fuel in hydrodynamic
compounders leads to a number of positive changes in fuel
performance, specifically concerning energy value and combustion
quality. The polymeric molecular chains are broken, therefore
the active part of molecules multiply, and combustions runs
faster and more efficiently.
When the molecules are
broken hydrodynamically, the molecular ties are broken, and free
radicals, which have a much higher combustion capabilities than
closed molecules, appear. The polymeric water molecule chains
are broken as well, forming free radicals
-H and –OH, which burn actively and form unstable compounds with
free organic radicals, which are easily oxidized. Sulfur and
parathin form surface active substances in the process of
hydrodynamic treatment, which surround the emulsion’s particles
and prevent them from further compounding.
-
Water-bitumen emulsions
‘Cold’ technologies of
bitumen construction material production are now becoming
widespread. These materials include asphalt-concrete, roofing,
water-proofing etc.
The most appropriate
application for water-bitumen emulsions is the road construction
and repairs. As compared to traditional hot binding bitumen, the
water-bitumen emulsions economize up to 30% bitumen, 40% gravel
and 33% energy. Application of the emulsions guarantees high
traction between the existing lower layer and the new layer,
high wear
resistance
of the layer, possibility to conduct road construction from
early spring till late autumn in temperatures higher than 5C and
possibility to lay the new road top onto wet surface.
Water-bitumen emulsions
consist of dispersed bitumen particles, water and special
emulsifying additives, which stabilize the blend. These
additives are environmentally friendly and easy to transport and
store.
-
Blends of
biodiesel and petroleum diesel
Hydrodynamic blending
allows for creation of highly homogenous blends of biodiesel and
petrochemical diesel, in appropriate component proportions,
which is made possible by high precision dosing system.
Qualities of the resulting blend can be altered by introduction
of various additives into the blend, which can adjust fuel
storage stability, clouding point and other performance
characteristics. The blends obtained with our technology are
molecular grade, which directly results in the compound fuel
retaining its qualities for extended periods of time.
Continuous stream
biodiesel production system.

The process is
as follows: feedstock oil from vessel 1 is fed to the
hydrodynamic compounder CGD through mesh filter F1 and stream
oil heater PPM by the pump H1. The oil stream is controlled with
the flowmeter P1. A pre-mixed methanol catalyst solution is fed
from vessel 3 to the compounder vacuum chamber through VR
regulator and flowmeter P2. Mixing of the solution is performed
by the pump H2. The solution is taken from vessels 3 in turn.
The
final stage of the reaction is performed in the mixing pump HK1.
Intensive cavitation processes in the hydrodynamic compounder
and the mixing pump break the molecular chains of fatty acids,
which significantly boosts reaction speed and increases fuel
performance.
After the
mixing pump, the mixture goes to settling columns 4, where it
separates into biodiesel and glycerin. The fuel then passes
through moisture separator FBO and the pump H3.
The system can
be fitted with automatic controls, which increase the price
somewhat, but minimize the probability of a human error that
could lower the quality of the finished product. The system and
its components, except for vessels 1 and 2, must be placed in
heated premises.
Biodieselmach®
units can be supplied in several variants, with capacity ranging
from 1 to 16 cubic meters per hour (16 cu. M per hr.
approximately equals 30 MMgy).
The system can
be shipped in 20 foot containers, takes any feedstock, such as
vegetable oils and animal fats, and is easy to modify and
upgrade, as it the structure of the system is modular.
|