Upgrading the pump,
replacing the mechanical seal and improving the pump
performance
Khurmankhan
Maral
maral1001@bk.ru
teacher, Pavlodar chemical
and mechanical college, city of Pavlodar,
Kazakhstan
Umurzakova Sabina
Beibitovna
umurzakovasabina@mail.ru
teacher, Pavlodar chemical
and mechanical college, city of Pavlodar,
Kazakhstan
Omarbekova Inara
Kasymkhanovna
inara_19@mail.ru
teacher, Pavlodar chemical
and mechanical college, city of Pavlodar,
Kazakhstan
Annotation:The article deals with issues
related to replacing the mechanical seal of the h-004 pump. In many
ways, single end seals will wear out from mechanical impurities,
and if they are not properly used, which slow down the process and
can allow products to leak.
The purpose of this work is to
eliminate the pulverization of a small fraction of the pumped
product , which occurs in the operation of the pump in
petrochemical processes.
Keywords: centrifugal pump, mechanical
seal, sealing.
In the presidential address
“Kazakhstan 2050”, country leader N. A. Nazarbayev underlined that
the oil and gas complex of Kazakhstan is a locomotive for the
entire economy and contributes to the development of other
industries, that an effective oil and gas sector of the economy
should be created. Due to the development of the share of the
country's oil and gas industry has grown over the past 5 years from
14.7% to 25.8%, which indicates the stable growth dynamics of the
oil and gas industry.
Pavlodar petrochemical plant
is the largest enterprise in Kazakhstan for the production of
petroleum products. MLP "PNHZ " is the only enterprise in
Kazakhstan with a set of technological installations that provides
deep processing of oil up to 85%, which corresponds to the level of
the best producers of petroleum products.
Today, the main goal of the
Pavlodar petrochemical plant is producing demanded products in the
volume necessary for the needs of the country and corresponding to
the requirements of the world market. The main way to achieve this
goal is creating a modern production base as a result of
modernization and technical re-equipment of existing production, as
well as the construction of new high-tech
facilities.
The Isomerization process Unit
and Naphtha Splitter are an integral part of the plant's
production. The isomerization unit and Naphtha Splitter is used to
produce commercial naphtha with an octane number not lower than
88.5, which is a high-octane component of gasoline AI-92-K2,
AI-95-K2, as well as light and heavy naphtha for further
refinements.
Pumping equipment plays a very
large and important role in the life of the plant. Correct and
unyielding operation of pumping equipment is an indispensable
factor in the operation of the entire installation, which allows us
to learn the importance of maintenance, installation and proper
operation of pumps.
The object of research is a
cantilever centrifugal pump N-004 of the USP40-380 type of
isomerization unit and a naphtha Splitter.
Pumps are hydraulic machines
that convert the mechanical energy of the drive motor into the
energy of the fluid flow, which serves to move and supply all types
of liquids. According to the principle of operation, there are:
centrifugal , rotary, piston, screw, and there are also special
pumps. These include: electromagnetic, pneumatic, and so
on.
Centrifugal pumps are units
consisting of a shell in the form of a snail and an electric motor,
connected by a gear coupling and mounted on a common Foundation
plate, which have suction and discharge pipes. The main working
body is the impeller mounted on a shaft that is connected to the
electric motor via a plate coupling.
In our time, oil and gas
equipment failure often occurs, at this stage, consider the
horizontal cantilever single-stage centrifugal pump H-004 model
USP40-380 isomerization unit and naphtha Splitter. Pump N-004 model
USP40-380, technological position A100-N-004A, is designed for the
circulation of alkali in the K-002 column.
Main parts of the centrifugal
pump
The lion's share of all pumps
produced in the world are console pumps of various types and
designs. According to experts published at various times in
specialized publications related to pumping topics, the number of
console pumps in pieces is from 59 to 72% of the total fleet of
pumps produced in the world. This figure is due to the simple
design of the cantilever pump compared to other types of pumps. The
elementary principle of the cantilever pump ensures its wide
distribution both in municipal equipment and in complex liquid
supply systems of military equipment and
spacecraft.
Console pumps have long proven
themselves only on the positive side. Their external simplicity
bribes the future owner. But behind this simplicity lies a
universal device that is ready to perform any tasks. The cantilever
pump is designed for pumping liquid in both cold and hot
conditions. An important and distinctive feature is that the
composition of the pumped liquid may include impurities. Their
concentration should not exceed 0.1%. Given the relatively high
productivity, this figure is actually very high. The size of some
solid particles is limited to 0.2 mm.
An alkaline NaOH solution from
the bottom of the K-002 column is fed to the suction of the
h-004A/B alkali circulation pumps. After pumping the pumps, passing
the heater T-012, the alkali is distributed into two streams. The
first flow is supplied from above the bottom of the nozzle where
the dry gas is washed with an alkaline solution, the second stream
is fed below the bottom part of the bottom nozzle of the column to
the spray nozzle to protect the column from contact with corrosive
gas by washing the walls of the scrubber an alkaline
solution.
The temperature of the alkali
at the outlet of the heater T-012 is controlled by the device POS.
TIA-0096.
If the concentration of the
circulating alkaline solution decreases below 2% (wt.) NaOH, the
spent alkali from the h-004A pumps/B is sent to the waste alkali
degassing tank E-009.
Our idea is to replace a
single mechanical seal with a double mechanical seal. Why at this
time, from this pump through water flushing come out in small
fractions of alkali? The answer is as follows: since we know that a
centrifugal cantilever pump when pumping an alkaline solution has
mechanical impurities in the composition of the product being
pumped.
Currently, the cantilever type
of centrifugal pumps is considered the most advanced in the field
of high performance.Among the total volume of pumping equipment
produced, console-type pumps account for 65 %. These units have
gained popularity due to their very simple design, ease of repair
and maintenance, and fairly high
efficiency.
By its design, the cantilever
pump is a type of centrifugal pump, which is characterized by the
presence of a working centrifugal wheel.
The main advantages of the
cantilever pump housing design, which allows installation of the
pressure pipe vertically and horizontally, are the
following:
- direct attachment of the
flanged motor to the pump body (provides the least impact of
vibration on the structure);
- the presence of a mechanical
seal, independent of the direction of rotation (provides ease of
operation);
- the possibility of quick
start and fast stop of the pump operation;
- high characteristics of
vibroacoustics (reduced noise level).
Based on the General situation
and based on the totality of all the above-mentioned facts, we can
determine: when pumping the product, a single mechanical seal does
not sufficiently seal the pumping medium, and replacing the double
mechanical seal will eliminate the pulverization of a small
fraction of the alkaline solution.
Based on the evidence, we can
draw the following conclusion. Double mechanical seal is the best
replacement for improved performance and impermeability through
o-rings.
The double mechanical seal
will last much longer, since the new SBTU cooling system will be
operated during the water wash process and will perform more
thorough sealing, as well as deep cooling and detailed lubrication.
The seal will allow the pump to operate for a long
time.
List of sources
used
1. Chisholm R. Techniques of vibration
analysis to gas turbines. / R. Chisholm. – Gas turbine Int. – № 6.
– 1979.P. 170 – 200.
2. Dunton T.A. An Introduction to Time
Waveform Analysis. / T.A. Dunton. – Universal Technologies. – 1999.
P. 120 – 128.
3. Jones C.M. Pumping station design
/ С. M. Jones. - Pumping station design. – 2006.
P. 20 – 24.
4. Ryndin V. V. Application of
the Mathcad system for static analysis of experimental data / V.
Ryndin, Yu. Volkova / / Science and technology of Kazakhstan. -
2008. Р. 95.
5. Perevoschikov S. I.
Reduction of hydrodynamic vibration of centrifugal
pumps.– 1997. P.
50–56.