Title of Invention

"A METHOD OF UTILIZATION OF THE NATURAL GAS EXPANSION ENERGY AND UTILIZATION POWER INSTALLATION FOR CARRYING OUT THE METHOD"

Abstract The present invention relates to a Method of utilization of the natural gas expansion energy during the process of reduction of gas pressure from high to the required one by conversion of natural gas expansion energy to mechanical energy with the aid of the gas cooled down in the process of pressure reduction as a cooling agent for generation of cold, wherein natural gas pressure is reduced in two or more successive stages simultaneously with conversion of natural gas expansion energy to mechanical energy at each stage at least a part of natural gas being used as a cooling agent, for generation of cold after the first and/or each successive stage of natural gas pressure drop or the total amount of natural gas used as a cooling agent is used for the subsequent stage of conversion of natural gas expansion energy to mechanical energy with reference to figure 3.
Full Text The present invention relates to a Method of utilisation of the natural gas expansion energy and utilization power installation for carrying out said method.
Field of the invention
The proposed method and the installation are intended for application in system of reduction of natural gas from high- e.g. in the borehole or in main pipelines down to the pressure value required for the consumer.
Background of the invention
The known methods of reduction of pressure of gas in boreholes or in main pipelines are based on throttling and using special devices (pressure regulators, valves, cocks etc) for implementation of these methods. [Polytechnic Dictionary, Moscow, "Sovetskaya Entsiklopedia" publishing House, 1977, pp 153, 420]
These methods and devices for implementation thereof do not utilize energy of gas expansion and cold generated during this process. The Application of these methods and devices requires sophisticated equipment and consumption of additional power to prevent clogging of pressure regulators by moisture and ice generated during their operation.
A method of utilization of energy of natural gas when its pressure drops from the valve in the main pipeline or in the borehole down to the required pressure by conversion of gas expansion energy to mechanical energy is known. [RU 21 17173, 6f02 1/02, 1996]. This method is implemented in a utilization power installation the inlet of which is connected to the outlet of the high pressure gas borehole or the main pipeline and the outlet- to the low pressure gas pipeline or to the gas consumer. This utilization power installation includes a gas expansion machine, e.g. an expansion turbine, and a mechanical energy converter connected cinematically with the gas expansion machine, e.g.
an electric generator. Such method and the installation make it possible to utilize gas expansion energy when its pressure drops.
However this method and the installation do not provide the possibility of utilization of cold generated in the process of gas expansion. The efficiency of this method and the installation is low.
There is a method of utilization of gas expansion energy when the gas pressure drops from a high valve to the required one by conversion of gas expansion energy to mechanical energy with simultaneous utilization of the gas cooled down during pressure drop as a cooling agent for generation of cold [SU Al, 844797]
However this method provides a single-stage gas pressure drop and hence total efficiency thereof is reduced.
There is a power installation for utilization of gas expansion energy and the cold generated during this process.[RU 2013616, F02 6/00, 1994].
However efficiency of this installation is low as gas pressure reduction and utilization of cold are effected at a single stage.
Disclosure of the Invention
The object of this invention is to improve utilization of cold generated during the process of reduction of natural gas pressure; generation of great amount of energy and cold and to increase total efficiency of the method and the installation for utilization of natural gas expansion energy.
The problem set in the proposed method is solved by reduction of natural gas from high-e.g. in main pipelines down to the pressure valve required for the consumer by conversion of gas expansion energy to mechanical energy by using the gas cooled down in the process of gas pressure drop as a cooling agent. The innovation of this method is
reduction of natural gas pressure in two or more successive stages and simultaneous utilization of at least a part of gas after the first and/or after each respective subsequent stage of reduction of natural gas pressure as a cooling agent for generation and use of cold. Another part of natural gas after the first and/or after each respective subsequent stage of reduction of natural gas pressure or the total amount of natural gas used as a cooling agent is used at the next stage of conversion of natural gas expansion energy to mechanical energy.
Due to application of the stage-by-stage reduction of natural gas pressure and the use of the total amount or a part of natural gas after the first and/or after the relevant subsequent stage of natural gas pressure drop the total efficiency of the method increases.
The problem set in the proposed machine is solved by implementation of a installation for utilization of natural gas expansion energy that includes a gas expansion machine, e.g. an expansion turbine, inlet of which is connected to a high pressure gas borehole or main pipeline and the outlet - to a low pressure gas pipeline; a gas expansion machine, e.g. an expansion turbine and a mechanical energy converter connected cinematically with the gas expansion machine, e.g. an electric generator. There is at least one heat exchanger in this installation, the outlet branch pipe of which is connected to the outlet of the gas expansion machine, e.g. to the outlet of the expansion turbine.
The innovation introduced in this facility is that the gas expansion machine of the utilization power installation, e.g. the expansion turbine, consists of two or more components arranged in the direction of natural gas pressure drop; the installation also comprises two or more heat-exchangers - refrigerators; the inlet branch pipe from the coolant side of each heat-exchanger — refrigerator is connected to the outlet of the
relevant component of the expansion machine and the number of heat-exchangers - refrigerators is not less than the number of expansion machine components.
This improvement of the utilization power installation ensures the increase of efficiency of this installation and the amount of generated cold.
The outlet of the preceding component of the gas expansion machine of the utilization power installation can be connected simultaneously both to the inlet of the next component of the gas expansion machine, and to the inlet branch pipe from the cooling agent side of the relevant heat exchanger-refrigerator, and the outlet branch pipe from the cooling agent side of one or more heat exchanger-refrigerators - to the low pressure gas pipeline or the gas consumer. In this case the flow of the working medium branches out and a part of the working medium is taken off for utilization of cold. This improves the thermo-dynamical working cycle of the installation.
Such an improvement increases the efficiency of the installation. At the same time it becomes possible to optimally regulate the operation of the gas expansion machine when the operation mode changes.
In the utilization power installation proposed the outlet of the preceding component of the gas expansion machine can only be connected to the inlet branch pipe from the cooling agent side of one or each heat exchanger-refrigerator, located between two components of the gas expansion machine, and the outlet branch pipe from the cooling agent side of the same heat exchanger-refrigerator, located between the two components of the gas expansion machine, can be connected to the inlet of the working medium of the next component of the gas expansion machine. Then additional heating of the working medium (gas) occurs in
one or in each heat exchanger-refrigerator. It improves thermodynamical working cycle of the installation.
This improvement increases additionally the efficiency of the installation and by utilization of the heat of the cooling agent, heated due to heat exchange in the heat exchange-refrigerator. At the same time it becomes possible to optimally regulate the operation of the gas expansion machine when the operation mode changes by changing the amount and/or the temperature of the working medium (liquid, gas or several working mediums) heated in the heat exchanger-refrigerators.
In accordance with the present invention it relates to a Method of utilization of the natural gas expansion energy during the process of reduction of gas pressure from high to the required one by conversion of natural gas expansion energy to mechanical energy with the aid of the gas cooled down in the process of pressure reduction as a cooling agent for generation of cold, wherein natural gas pressure is reduced in two or more successive stages simultaneously with conversion of natural gas expansion energy to mechanical energy at each stage at least a part of natural gas being used as a cooling agent for generation of cold after the first and/or each successive stage of natural gas pressure drop or the total amount of natural gas used as a cooling agent is used for the subsequent stage of conversion of natural gas expansion energy to mechanical energy.
In accordance with the present invention it relates to the utilization power installation for carrying out method as described above comprising a gas expansion machine, wherein said gas expansion machine is expansion turbine the inlet of which is connected to high pressure natural gas borehole or main pipeline (3) connected with the gas expansion machine, converter (4) of mechanical energy, which is electric generator, and at least one heat exchanger-refrigerator (8), the inlet branch pipe of which from the cooling agent side is connected to the outlet of the gas expansion machine, that is to the outlet of the expansion turbine and the outlet branch pipe to the low pressure gas main pipeline or to gas consumer (9), wherein said gas expansion machine consists of two or more components (1, 2), arranged in the direction of natural gas pressure drop, the number of heat exchanger-refrigerators (6,8) being not less than the number of components of the gas expansion machine, and the inlet branch pipe from the cooling agent side of the relevant heat exchanger-refrigerator is connected to the outlet of the appropriate component (1, 2).
BRIEF DESCRIPTION OF THE ACCOMPANYING DRAWINGS
In Fig. 1 the diagram of a utilization power installation is shown. The installation includes an expansion gas turbine that contains a high pressure component and a low pressure component, two heat exchanger-refrigerators and an electric generator.
In Fig. 2 the diagram of a utilization power installation is shown. The installation includes an expansion gas turbine that contains a high pressure component, a medium pressure component and a low pressure component, three heat exchanger-refrigerators and an electric generator.
In Fig. 3 the diagram of a utilization power installation is shown. The installation includes expansion gas turbine that contains high pressure components, medium pressure components and a low pressure components, three heat exchanger-refrigerators and three electric generator.
The invented method and the installation are illustrated by descriptions of the preferred embodiments thereof the embodiments of implementation of the utilization of gas expansion energy being described in the disclosure of operation of variants of the installation.
Variant 1. (Fig. 1)
The utilization power installation includes an expansion gas turbine that contains high pressure components 1(HPC 1), and low pressure components 2(LPC 2) arranged co-axially. The inlet of HPC 1 is connected to high pressure gas main pipelines 3. this main pipeline 3 can be high- or medium- pressure natural gas pipeline, a gas pipeline of the gas distribution station, a thermal power station, a boiler house, a borehole in the natural gas production site etc. (These facilities are not shown in the drawings). Electric generator shaft 4 that supplies electric power to consumer 5 is connected cinematically or directly to the common shaft of HPC 1 and LPC 2. The outlet of HPC 1 is connected both to the inlet of LPC 2, and the inlet branch pipe from the cooling agent side of heat exchanger-refrigerator 6. The outlet of the branch pipe from the cooling agent side of heat exchanger-refrigerator 6 is connected to the low pressure gas pipeline through which gas is supplied to consumer 7.
Heat exchanger-refrigerator 8 is installed at the gas outlet of LPC 2 of the expansion gas turbine. The inlet branch pipe of the heat exchanger-refrigerator from the cooling agent side is connected to the gas outlet out of LPC 2 of the expansion gas turbine and the outlet branch pipe from the cooling agent side of the heat exchanger-refrigerator 8 is connected to the low pressure gas pipeline, that supplies gas to consumer 9.
The utilization power installation operates in the following way. High pressure natural gas flows out of main pipeline 3 into HPC 1, rotates the same expanding and cooling at the same time. A part of this natural gas flows into LPC 2, another part-into the inlet branch pipe from the cooling agent side of heat exchanger-refrigerator 6. Partially
cooled down gas under partially reduced pressure passes through heat exchanger-refrigerator 6. Next the natural gas under required pressure is supplied to gas consumer 7.
Another part of gas that was delivered into LPC 2 of the expansion gas turbine performs additional work, reduces pressure and is cooled down. This gas is fed from LPC 2 to the second heat exchanger-refrigerator 8, where gas is heated and cold is taken off. Next natural gas under reduced pressure is supplied to consumer 9. The expansion gas turbine that includes HPC 1 and LPC 2 rotates electric generator electric generator 4. Electric power is supplied to consumer 5.
Cold can be used for freezing chambers, ice rinks etc and for liquefaction of natural gas produced from boreholes. The useful work performed by gas in the process of expansion can also be used for liquefaction of gas and power supply of a remote natural gas borehole.
Variant 2 (Fig 2)
Utilization power installation includes an expansion gas turbine that contains
high pressure component 10 (HPC 10), medium pressure component 11 (MPC
1 1) and low pressure component (LPC 12) that are arranged on the same shaft.
The inlet of HPC (10) is connected both to the inlet of MPC 11 and to the inlet
branch pipe from the cooling agent side of heat exchanger-refrigerator 16. The
gas outlet of heat exchanger-refrigerator 16 is connected to low pressure gas
consumer 17. The outlet of MPC 11 is connected both to the inlet of LPC 12
and the inlet branch pipe from the cooling agent side of heat exchanger-
refrigerator 18. The gas outlet, from heat exchanger-refrigerator 18 is
connected to low pressure gas consumer 19. The outlet of LPC 12 is connected
to the inlet branch pipe from the cooling agent side of heat exchanger-
refrigerator 20. The gas outlet from heat exchanger-refrigerator 20 is connected
low pressure gas consumer 21.
The utilization power installation operates in the following way. High pressure natural gas flows out of main pipeline 13 into HPC 10, rotates the same
expanding and cooling at the same time. A part of this natural gas flows into MPC 11, rotates the same expanding and cooling at the same time, another part into the inlet branch pipe from the cooling agent side of heat exchanger-refrigerator 16, from which natural gas is supplied to low pressure gas consumer 17. Pressure required to gas consumer 17 can be higher than that required to other natural gas consumers 19 and 21. Another part of the gas flow performs work in MPC 11, reduces pressure additionally and is cooled down. Next natural gas flow branches out. One part of this flow is fed to the inlet branch pipe from the cooling agent side of heat exchanger-refrigerator 18, from which natural gas is supplied to gas consumer 19. The rest part of the flow is fed inlet of LPC 12, rotating the same expanding and being cooled down at the same time. Then natural gas flows into heat exchanger-refrigerator 20, from which it is fed to low pressure natural gas consumer 21. The expansion gas turbine rotates electric generator 14, that generates current for electric power consumer 15.
Cold can be used for freezing chambers, ice rinks etc and for liquefaction of natural gas produced from boreholes. The useful work performed by gas in the process of expansion can also be used for liquefaction of gas and power supply of a remote natural gas borehole.
Variant 3 (Fig. 3)
The utilization power installation includes high pressure expansion has turning 22 (HPT 22), the inlet of which is connected to high pressure natural gas pipeline 23. The shaft of HPT 22 is connected to electric generator 24 cinematically or directly, the generator being electrically connected with power consumer 25. The outlet of HPT 22 is connected to the inlet branch pipe from the cooling agent side of heat exchanger-refrigerator 26. The gas outlet of heat exchanger-refrigerator 26 is connected to the inlet of the medium pressure expansion gas turbine 27 (MPT 27). The shaft of MPT 27 is connected cinematically or directly to electric generator 28, which is connected electrically
to power consumer 29. The outlet of MPT 27 is connected to the inlet branch pipe from the cooling agent side of heat exchanger-refrigerator 30. The gas outlet of heat exchanger-refrigerator 30 is connected to the inlet of low pressure expansion gas turbine 31 (LPT 31). The shaft of LPT 31 is connected cinematically or directly to electric generator 32, which is connected electrically with power consumer 33. The outlet of LPT 31 is connected to the gas inlet of heat exchanger-refrigerator 34. The gas outlet of the heat exchanger-refrigerator 34 is connected to low pressure natural gas consumer 35.
The utilization power installation operates in the following way. High pressure natural gas is fed from main pipeline 23 to HPT 22, rotating the same, expanding and being cooled down. Next gas is supplied from HPT 22 to heat exchanger-refrigerator 26, where cold is utilized and gas is heated and expands. Further gas is delivered to MPT 27, rotating the same, expanding and being cooled down. Next gas flows into heat exchanger-refrigerator 30, where cold is utilized and gas is heated and expands. Then heated and expanded gas is fed from the heat exchanger-refrigerator 30 to LFF 31 rotating the same, expanding and being cooled down. Next gas flows from LPT 31 to heat exchanger-refrigerator 34, where cold is utilized and natural gas is heated and expands. Further natural gas is supplied to low pressure gas consumer
35. HPT 22, MPT 27 and LPT 31 rotate electric generators 24, 28 and 32 respectively that supply electric power to consumers 25, 29, 33. Electric generators 24, 28 and 32 can be connected to the common electric network
Due to stage-by-stage cooling down of gas in HPT 22, MPT 27 and LPT 31 and stage-by-stage heating of the same in heat exchangers-refrigerators 26 and 30 total efficiency of utilization power installation increases.
Industrial applicability.
The invention can be used for solving a wide scope of practical problems of generation of additional energy and non-expensive cold. The invention can be used at the outlet of high pressure natural gas directly out of boreholes and for reduction of gas pressure at the outlet of main pipelines down to the pressure required by the consumer etc.
In all descriptions of preferred embodiments an expansion gas turbine is used as a gas expansion machine. However a gas expansion machine of any type can be used, e.g. piston or rotor — type gas expansion machines, including those comprising high pressure and low pressure components or high pressure, medium pressure and low pressure components.
Turbines, pumps, ventilators, winches or other converters of mechanical energy can be used instead and/or simultaneously with the electric generator.
Utilization power installations described in preferred embodiments of the invention utilization power installations can be located directly beside natural gas boreholes if natural gas pressure at the outlet of the borehole exceeds pressure required for the gas main pipeline. In this case cold can be used for liquefaction of natural gas
produced. The useful work performed by gas in the process of expansion can be used for liquefaction of gas power supply of a remote natural gas borehole. The utilization power installations proposed are very efficient in places where gas main pipelines are connected to installations for natural gas supply to big consumers (electric power plants, domestic natural gas networks in settlements etc).







We Claim:
1. Method of utilization of the natural gas expansion energy during the process of reduction of gas pressure from high to the required one by conversion of natural gas expansion energy to mechanical energy with the aid of the gas cooled down in the process of pressure reduction as a cooling agent for generation of cold, wherein natural gas pressure is reduced in two or more successive stages simultaneously with conversion of natural gas expansion energy to mechanical energy at each stage at least a part of natural gas being used as a cooling agent for generation of cold after the first and/or each successive stage of natural gas pressure drop or the total amount of natural gas used as a cooling agent is used for the subsequent stage of conversion of natural gas expansion energy to mechanical energy.
2. The utilization power installation for carrying out method as claimed in claim 1, comprising a gas expansion machine, wherein said gas expansion machine is an expansion turbine the inlet of which is connected to high pressure natural gas borehole or main pipeline (3) connected with the gas expansion machine, converter (4) of mechanical energy, which is electric generator, and at least one heat exchanger-refrigerator (8), the inlet branch pipe of which from the cooling agent side is connected to the outlet of the gas expansion machine, that is to the outlet of the expansion turbine and the outlet branch pipe to the low pressure gas main pipeline or to gas consumer (9), wherein said gas expansion machine consists of two or more components (1, 2), arranged in the direction of natural gas pressure drop, the number of heat exchanger-refrigerators (6,8) being not less than the number of components of the gas expansion machine, and the inlet branch pipe from the cooling agent side of the relevant heat exchanger-refrigerator is connected to the outlet of the appropriate component (1,2).
3. The installation as claimed in claim 2, wherein the outlet of preceding component (10,11) of the gas expansion machine is connected both to the inlet of next component (11,12) of the gas expansion machine and to the inlet branch pipe from the cooling agent side of relevant heat exchanger-refrigerator (16,18) and the outlet branch pipe from the cooling agent side of one or more heat exchanger-refrigerators (16,18) is connected to the low pressure natural gas pipeline or natural gas consumer (17,19).
4. The installation as claimed in claim 2, wherein the outlet of preceding component (22, 27) of the gas expansion machine is connected only to the inlet branch pipe from the cooling agent side of heat exchanger-refrigerator (26,30), and the outlet branch pipe from the cooling agent side of one or more heat exchanger-refrigerators (26,30) is connected to the inlet of the working medium of next component (27, 31) of the gas expansion machine.
5. Method of utilization of the natural gas expansion energy substantially as herein described with reference to forgoing description and the accompanying drawings.
6. The utilization power installation substantially as herein described with reference to the foregoing description and the accompanying drawings.


Documents:

124-delnp-2003-abstract.pdf

124-delnp-2003-assignment.pdf

124-delnp-2003-claims.pdf

124-delnp-2003-complete specification(granted).pdf

124-delnp-2003-corrrespondence-others.pdf

124-delnp-2003-corrrespondence-po.pdf

124-delnp-2003-description (complete).pdf

124-delnp-2003-drawings.pdf

124-delnp-2003-form-1.pdf

124-delnp-2003-form-13.pdf

124-delnp-2003-form-18.pdf

124-delnp-2003-form-2.pdf

124-delnp-2003-form-3.pdf

124-delnp-2003-form-5.pdf

124-delnp-2003-gpa.pdf

124-delnp-2003-pct-101.pdf

124-delnp-2003-pct-210.pdf

124-delnp-2003-pct-301.pdf

124-delnp-2003-pct-304.pdf

124-delnp-2003-pct-332.pdf

124-delnp-2003-petition-137.pdf


Patent Number 243369
Indian Patent Application Number 124/DELNP/2003
PG Journal Number 42/2010
Publication Date 15-Oct-2010
Grant Date 07-Oct-2010
Date of Filing 03-Feb-2003
Name of Patentee TUZOVA Alla Pavlovna
Applicant Address RUSSIA 196244, ST-PETERSBURG, UL. TIPANOVA, D.29, KV 657, RUSSIA
Inventors:
# Inventor's Name Inventor's Address
1 VASILJEV, VLADIMIR YAROSLAVOVICH LITHUANIA, 2043 VILNIUS, ARCHITEKTU 32-16
2 KISELEV, OLEG MIKHAILOVICH 45327, ESSEN, JOSEPH OERTGEN WEG 80, GERMANY
PCT International Classification Number F02C 1/02
PCT International Application Number PCT/RU2001/00351
PCT International Filing date 2001-08-15
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 2000121361 2000-08-16 Russia