CN106015064B - The operating method of motor-driven compressor substitution steam driven compressor - Google Patents
The operating method of motor-driven compressor substitution steam driven compressor Download PDFInfo
- Publication number
- CN106015064B CN106015064B CN201610389417.0A CN201610389417A CN106015064B CN 106015064 B CN106015064 B CN 106015064B CN 201610389417 A CN201610389417 A CN 201610389417A CN 106015064 B CN106015064 B CN 106015064B
- Authority
- CN
- China
- Prior art keywords
- valve
- motor
- air
- driven compressor
- high pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000011017 operating method Methods 0.000 title claims abstract description 11
- 238000006467 substitution reaction Methods 0.000 title claims abstract description 11
- 238000004519 manufacturing process Methods 0.000 claims abstract description 11
- 230000005611 electricity Effects 0.000 claims description 14
- 238000012790 confirmation Methods 0.000 claims description 6
- 239000003054 catalyst Substances 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 26
- 239000003345 natural gas Substances 0.000 abstract description 13
- 238000010795 Steam Flooding Methods 0.000 abstract description 6
- 239000000618 nitrogen fertilizer Substances 0.000 abstract description 3
- 239000002737 fuel gas Substances 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 239000007789 gas Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 230000007812 deficiency Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D25/00—Pumping installations or systems
- F04D25/16—Combinations of two or more pumps ; Producing two or more separate gas flows
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D25/00—Pumping installations or systems
- F04D25/02—Units comprising pumps and their driving means
- F04D25/04—Units comprising pumps and their driving means the pump being fluid-driven
- F04D25/045—Units comprising pumps and their driving means the pump being fluid-driven the pump wheel carrying the fluid driving means, e.g. turbine blades
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D25/00—Pumping installations or systems
- F04D25/02—Units comprising pumps and their driving means
- F04D25/06—Units comprising pumps and their driving means the pump being electrically driven
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
- F04D27/002—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids by varying geometry within the pumps, e.g. by adjusting vanes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
- F04D27/005—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids by changing flow path between different stages or between a plurality of compressors; Load distribution between compressors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
- F04D27/007—Conjoint control of two or more different functions
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
- F04D27/009—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids by bleeding, by passing or recycling fluid
Abstract
The invention discloses a kind of operating methods of motor-driven compressor substitution steam driven compressor, it is made of steam driven compressor component and motor-driven compressor component combination, steam driven compressor component include connect production system pipeline and air compressor for pressure pipeline, it is connected with steam turbines and air filter on air compressor, steam control valve is equipped on for pressure pipeline；The motor-driven compressor component with motor-driven compressor being also connected on production system pipeline more than a set of.The present invention replaces steam drive air compressor for air by electrodrive air compressor, reaches the substitution of the energy.It is raw natural gas by original part of fuel gas replacement, promotes the natural gas nitrogen fertilizer plant rate of capacity utilization, to enterprise's reasonable disposition resource, implements energy-saving and emission-reduction, skill upgrading is of great importance, and in industry has important exemplary role.
Description
Technical field
The present invention relates to a kind of motor-driven compressors to substitute steam driven compressor operating method, belongs to natural gas nitrogen
Fertile engineering device technique field.
Background technique
Existing using natural gas as the nitrogen enterprise of raw material, many energy and driving are to have combustion of natural gas to become steaming
Vapour, then driven by steam, it there is the waste of great unstripped gas, by taking the pressure-air that existing system provides as an example,
Pressure-air used in its technique is with process steam driving air compressor for air, though which can save several years ago
Cost, but as domestic natural gas shortage and price rise, very big raw material mix is faced by the nitrogen enterprise of raw material of natural gas
Pressure is adjusted, to solve the problems, such as energy shortages.
Summary of the invention
In view of the deficiencies of the prior art, the present invention proposes a kind of motor-driven compressor that can save gas material
The operating method of steam driven compressor is substituted, with overcome the deficiencies in the prior art.
The technical solution adopted by the present invention:
Motor-driven compressor substitutes the structure of steam driven compressor, it is driven by steam driven compressor component and motor
The combination of dynamic pressure compressor parts is constituted, and steam driven compressor component includes the pressure supply for connecting production system pipeline and air compressor
Pipeline is connected with steam turbines and air filter on air compressor, and steam control valve is equipped on for pressure pipeline；?
A set of above motor-driven compressor component with motor-driven compressor is also connected on production system pipeline.
The structure of above-mentioned motor-driven compressor substitution steam driven compressor is the motor-driven compressor portion
Part includes electricity drive air filter, low pressure (LP) cylinder, motor and the high pressure cylinder that supply air line concatenation is driven in electricity consumption, is driven on supply air line in electricity
It is connected with the blow-down pipe of high pressure blow valve, is driven in electricity and is connected with the big valve in outlet on supply air line, is equipped with guide vane in low pressure (LP) cylinder import,
It is connected with the low pressure (LP) cylinder blow-down pipe with LOW PRESSURE VENT VALVE IN on low pressure (LP) cylinder, is driven in electricity and is connected with the big valve in outlet on supply air line.
The structure of motor-driven compressor substitution steam driven compressor above-mentioned is the motor-driven compressor portion
Part is two sets.
Motor-driven compressor substitution steam driven compressor operating method it include the following steps
A, check whether whole system is normal before driving；
B, air-channel system is driven: guide vane, open-width 5% in opening motor-driven compressor component, LOW PRESSURE VENT VALVE IN is closed entirely,
High pressure blow valve standard-sized sheet exports big valve and is in close state；
C, unit is driven: starting motor 15s~30s to rated speed, and motor operation starts after five minutes, guide vane is opened greatly
To 20%~30%；According to first convincing leaf by patient analysis, then the principle of high pressure blow valve is closed, the unlatching of each guide vane and the closing of high pressure blow valve
Amplitude controls within 2%, until high pressure cylinder rate of discharge reaches 25600Nm3/ h, pressure reach 3.65MPa；
D, it opens electrodrive air compressor component and adds air: opening motor, close and export big valve, main valve, air control valve
And steam control valve, confirmation pressure flow normally open the emptying of high pressure blow valve afterwards；After chemical industry instruments, slowly open out
The big valve of mouth and main valve press high 0.1MPa than system with the outlet pressure of guide vane and high pressure blow valve adjustment high pressure cylinder, open air tune
The bypass valve of valve is saved, while should be noted that the variation of catalyst temperature；It gradually opens air control valve and closes the bypass of air control valve
Valve turns down high pressure blow valve and adjustment guide vane opening, slowly gradually to control temperature rise rate；To wherein a set of motor driven pressure
After the air whole addition system of compressor parts, then gradually slowly turn down the high pressure emptying of another set of motor-driven compressor component
Leaf divergence is led in valve and adjustment, until system is all added in the air of another set of motor-driven compressor component；
E, it moves back air: being down to 50% to technical load, gradually reduce the additional amount of air control valve, be gradually opened height and press
Empty valve closes guide vane, after the addition of air control valve reduces to 30%, closes air control valve and completes, scene confirmation high pressure emptying
Valve regulation gradually opens big high pressure blow valve to standard-sized sheet to the complete backed off after random of normal air, while gradually closing back guide vane to 10%, stops
Motor operation, per half an hour jiggering once terminates to oil circulation after motor is stopped transport.Motor-driven compressor above-mentioned substitutes steam
The operating method for driving compressor is high pressure blow valve first to be opened in step e, then close guide vane, and each span of control limit of control is less than 5%.
The operating method of motor-driven compressor substitution steam driven compressor above-mentioned is electrodrive air compressor portion
Part and steam driven compressor component can be converted mutually.
Compared with the prior art, the present invention proposes one aiming at the problem that existing domestic natural gas shortage and price rise
Kind combines electric, coal resource abundant, finds the displacement of the natural gas nitrogen fertilizer plant energy and system optimization scheme, that is, passes through electric drive
Air compressor replaces steam drive air compressor for air, reaches the substitution of the energy.Original part of fuel natural gas is set
It is changed to raw natural gas, promotes the natural gas nitrogen fertilizer plant rate of capacity utilization, to enterprise's reasonable disposition resource, implements energy conservation and subtracts
Row, skill upgrading is of great importance, and in industry has important exemplary role.
38 t/h of turbine steam consumption of steam drive air compressor implements electrodrive air compressor and replaces steam
Drive air compressor for air, annual about 20,000,000 Nm of disposable fuel natural gas3, convert into and increase production 30,000 tons of urea in year, have
Good economic benefit.Annual emission reduction flue gas about 200,000,000 is marked cube, wherein emission reduction CO2About 40,000 tons, boiler reduces sewage row every year
High-volume about 6000 tons.
Detailed description of the invention
Fig. 1 is flow diagram of the invention；
Specific embodiment
The present invention will be further explained below with reference to the attached drawings, as shown in Figure 1, motor-driven compressor substitutes steam drive
The structure of compressor, it is made of steam driven compressor component and motor-driven compressor component combination, steam drive compression
Machine component include connect production system pipeline 14 and air compressor 11 for pressure pipeline 15, be equipped on production system pipeline 14
Main valve 7, air control valve 9, are parallel with bypass valve 10 on air control valve 9, and it is saturating to be connected with steam on air compressor 11
Flat machine 12 and air filter 13 are equipped with steam control valve 8 on for pressure pipeline 15, while also connecting on production system pipeline 14
It is connected to a set of above motor-driven compressor component with motor-driven compressor.The motor-driven compressor component packet
It includes electricity consumption and drives electricity drive air filter 16, low pressure (LP) cylinder 17, motor 18 and high pressure cylinder 19 that supply air line 20 concatenates, drive gas supply in electricity
It is connected with the blow-down pipe 21 of high pressure blow valve 3 on pipeline 20, is equipped with guide vane 1 in 17 import of low pressure (LP) cylinder, is connected on low pressure (LP) cylinder 17
There is the low pressure (LP) cylinder blow-down pipe with LOW PRESSURE VENT VALVE IN 2, is driven in electricity and be connected with the big valve 4 in outlet, pressure gauge 6 and flow on supply air line 20
Meter 5；The motor-driven compressor component used in figure is two sets simultaneously.
Motor-driven compressor substitutes the operating method of steam driven compressor, it includes the following steps
A, check whether whole system is normal before driving；
B, air-channel system is driven: guide vane 1, open-width 5% in opening motor-driven compressor component, LOW PRESSURE VENT VALVE IN 2 are complete
It closes, 3 standard-sized sheet of high pressure blow valve exports big valve 4 and is in close state；
C, unit is driven: starting motor 1815s~30s to rated speed, and the operation of motor 18 starts after five minutes, by guide vane
1 opens greatly to 20%~30%；According to first convincing leaf 1 by patient analysis, then the principle of high pressure blow valve 3 is closed, the unlatching of each guide vane 1 and high pressure emptying
The closing amplitude of valve 3 controls within 2%, until 19 rate of discharge of high pressure cylinder reaches 25600Nm3/ h, pressure reach 3.65MPa；
D, it opens electrodrive air compressor component and adds air: opening motor 18, close and export big valve 4, main valve 7, air tune
Valve 9 and steam control valve 8 are saved, confirmation pressure flow is normally opened high pressure blow valve 3 afterwards and is vented；After chemical industry instruments, slowly
It opens and exports big valve 4 and main valve 7, the outlet pressure for adjusting high pressure cylinder 19 with guide vane 1 and high pressure blow valve 3 is higher than system pressure
0.1MPa opens the bypass valve 10 of air control valve 9, while should be noted that the variation of catalyst temperature；Gradually open air control valve 9,
And the bypass valve 10 of air control valve 9 is closed, high pressure blow valve 3 and adjustment 1 aperture of guide vane are turned down, slowly gradually to control temperature rise
Rate；After the air whole addition system of wherein a set of motor-driven compressor component, then gradually slowly turn down another set of electricity
Machine drives the high pressure blow valve 3 of compressor part and the aperture of adjustment guide vane 1, until the sky of another set of motor-driven compressor component
System is all added in gas；
E, it moves back air: being down to 50% to technical load, gradually reduce the additional amount of regulating valve 9, be gradually opened high pressure blow valve
3, guide vane 1 is closed, after the addition of air control valve 9 reduces to 30%, air control valve 9 is closed and completes, scene confirmation high pressure blow valve
3 are adjusted to the complete backed off after random of normal air, gradually open big high pressure blow valve 3 to standard-sized sheet, while gradually closing back guide vane 1 to 10%, are adjusting
Shi Xiankai high pressure blow valve 3 is saved, then closes guide vane 1, each span of control limit of control is less than 5%.Stop motor 18 to run, after motor 18 is stopped transport
Per half an hour jiggering once terminates to oil circulation；
The air that above-mentioned electrodrive air compressor component and steam driven compressor component common combination are constituted provides system
System, when breaking down one of wherein, electrodrive air compressor component and steam driven compressor component can be converted mutually.
Claims (2)
1. a kind of operating method of motor-driven compressor substitution steam driven compressor, it is characterised in that: it includes following step
Suddenly
A, check whether whole system is normal before driving；
B, air-channel system is driven: guide vane (1), open-width 5% in opening motor-driven compressor component, LOW PRESSURE VENT VALVE IN (2) are complete
It closes, high pressure blow valve (3) standard-sized sheet exports big valve (4) and is in close state；
C, unit is driven: starting motor (18) 15s~30s to rated speed, and motor (18) operation starts after five minutes, by guide vane
(1) it opens greatly to 20%~30%；According to first convincing leaf (1) by patient analysis, then close the principle of high pressure blow valve (3), the unlatching of each guide vane (1) and
The closing amplitude of high pressure blow valve (3) controls within 2%, until high pressure cylinder (19) rate of discharge reaches 25600Nm3/ h, pressure
Reach 3.65MPa；
D, it opens electrodrive air compressor component and adds air: opening motor (18), close and export big valve (4), main valve (7), air
Regulating valve (9) and steam control valve (8), confirmation pressure flow normally open high pressure blow valve (3) emptying afterwards；Chemical industry instruments terminate
Afterwards, it slowly opens and exports big valve (4) and main valve (7), with the outlet of guide vane (1) and high pressure blow valve (3) adjustment high pressure cylinder (19)
Pressure ratio system presses high 0.1MPa, opens the bypass valve (10) of air control valve (9), while should be noted that the variation of catalyst temperature；
Gradually open air control valve (9) and close the bypass valve (10) of air control valve (9), gradually slowly turn down high pressure blow valve (3) and
Guide vane (1) aperture is adjusted, to control temperature rise rate；System is all added in air to wherein a set of motor-driven compressor component
After system, then gradually slowly turn down the high pressure blow valve (3) of another set of motor-driven compressor component and opening for adjustment guide vane (1)
Degree, until system is all added in the air of another set of motor-driven compressor component；
E, it moves back air: being down to 50% to technical load, gradually reduce the additional amount of air control valve (9), be gradually opened high pressure emptying
Valve (3) closes guide vane (1), after the addition of air control valve (9) reduces to 30%, closes air control valve (9) and completes, scene confirmation
High pressure blow valve (3) is adjusted to the complete backed off after random of normal air, gradually opens big high pressure blow valve (3) to standard-sized sheet, while gradually closing back
Guide vane (1) stops motor (18) operation, per half an hour jiggering once terminates to oil circulation after motor (18) is stopped transport to 10%；
Its motor-driven compressor substitute steam driven compressor it by steam driven compressor component and motor-driven compressor
Component combination is constituted, and steam driven compressor component includes the pressure supply of connection production system pipeline (14) and air compressor (11)
Pipeline (15) is connected with steam turbines (12) and air filter (13), for pressure pipeline on air compressor (11)
(15) steam control valve (8) are equipped with；Being compressed more than a set of with motor driven is also connected on production system pipeline (14)
The motor-driven compressor component of machine is equipped with main valve (7), air control valve (9), in air tune on production system pipeline (14)
Bypass valve (10) are parallel on section valve (9)；The motor-driven compressor component includes that supply air line (20) concatenation is driven in electricity consumption
Electricity drive air filter (16), low pressure (LP) cylinder (17), motor (18) and high pressure cylinder (19), connected in electricity drive supply air line (20)
There is the blow-down pipe (21) of high pressure blow valve (3), is driven in electricity and be connected with the big valve (4) in outlet on supply air line (20), in low pressure (LP) cylinder
(17) import is equipped with guide vane (1), and the low pressure (LP) cylinder blow-down pipe with LOW PRESSURE VENT VALVE IN (2) is connected on low pressure (LP) cylinder (17)；Described
Motor-driven compressor component is two sets；High pressure blow valve (3) are first opened in step e, then close guide vane (1), each span of control limit of control
Less than 5%.
2. the operating method of motor-driven compressor substitution steam driven compressor according to claim 1, feature exist
In: electrodrive air compressor component and steam driven compressor component can be converted mutually.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610389417.0A CN106015064B (en) | 2016-06-06 | 2016-06-06 | The operating method of motor-driven compressor substitution steam driven compressor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610389417.0A CN106015064B (en) | 2016-06-06 | 2016-06-06 | The operating method of motor-driven compressor substitution steam driven compressor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106015064A CN106015064A (en) | 2016-10-12 |
| CN106015064B true CN106015064B (en) | 2019-04-26 |
Family
ID=57090411
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610389417.0A Active CN106015064B (en) | 2016-06-06 | 2016-06-06 | The operating method of motor-driven compressor substitution steam driven compressor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106015064B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ITUB20160324A1 (en) | 2016-01-25 | 2017-07-25 | Nuovo Pignone Tecnologie Srl | COMPRESSOR TRAIN START UP WITH VARIABLE ENTRY GUIDE ROOMS |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1487173A (en) * | 2002-09-19 | 2004-04-07 | �����ع�ҵ��ʽ���� | Running controlling apparatus and running controlling method for single-shaft combine equipment with clutch |
| CN102674489A (en) * | 2012-05-17 | 2012-09-19 | 青岛科技大学 | high-concentration ammonia-containing wastewater treatment method based on vapour compression |
| CN203096014U (en) * | 2013-01-06 | 2013-07-31 | 杭州林达化工技术工程有限公司 | Device for producing natural gas from factory waste gas |
| CN203173832U (en) * | 2013-03-21 | 2013-09-04 | 安徽淮化股份有限公司 | Power-driven steam pipeline network for synthesis process of ammonia synthesis device |
| CN103408086A (en) * | 2013-08-02 | 2013-11-27 | 天华化工机械及自动化研究设计院有限公司 | MVR (Mechanical Vapor Recompression) vapor-stripping deamination system and application method thereof |
| CN104350345A (en) * | 2011-12-15 | 2015-02-11 | 国际壳牌研究有限公司 | System and method for producing liquefied hydrocarbon stream and method of operating compressor |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06264894A (en) * | 1993-03-16 | 1994-09-20 | Hitachi Ltd | Switching control method for plural compressor |
| JP4196307B1 (en) * | 2008-03-06 | 2008-12-17 | 三浦工業株式会社 | Steam system |
-
2016
- 2016-06-06 CN CN201610389417.0A patent/CN106015064B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1487173A (en) * | 2002-09-19 | 2004-04-07 | �����ع�ҵ��ʽ���� | Running controlling apparatus and running controlling method for single-shaft combine equipment with clutch |
| CN104350345A (en) * | 2011-12-15 | 2015-02-11 | 国际壳牌研究有限公司 | System and method for producing liquefied hydrocarbon stream and method of operating compressor |
| CN102674489A (en) * | 2012-05-17 | 2012-09-19 | 青岛科技大学 | high-concentration ammonia-containing wastewater treatment method based on vapour compression |
| CN203096014U (en) * | 2013-01-06 | 2013-07-31 | 杭州林达化工技术工程有限公司 | Device for producing natural gas from factory waste gas |
| CN203173832U (en) * | 2013-03-21 | 2013-09-04 | 安徽淮化股份有限公司 | Power-driven steam pipeline network for synthesis process of ammonia synthesis device |
| CN103408086A (en) * | 2013-08-02 | 2013-11-27 | 天华化工机械及自动化研究设计院有限公司 | MVR (Mechanical Vapor Recompression) vapor-stripping deamination system and application method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106015064A (en) | 2016-10-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205477782U (en) | Utilize ejector to adjust power generation system of little steam turbine of air supply drive water -feeding pump | |
| CN205823355U (en) | A kind of co-generation unit | |
| CN205477780U (en) | A low pressure bypass turbine system for high load condition of large -scale steam turbine | |
| CN113339089A (en) | Efficient peak regulation steam turbine system and working method thereof | |
| CN109372696A (en) | Compressed air is collected as the electricity generation system of power using wind-force | |
| CN106015064B (en) | The operating method of motor-driven compressor substitution steam driven compressor | |
| CN101598343A (en) | Adjustable pressurization system of serial-parallel boilers of big and small turbochargers | |
| CN107060918A (en) | A kind of many low pressure (LP) cylinder steam turbine generator set system optimization device and methods | |
| CN201202499Y (en) | Working apparatus of steam water turbine | |
| JPH05507134A (en) | Method and apparatus for generating heat and electricity in a sulfate pulp mill | |
| CN109653820A (en) | A kind of high pressure industrial steam supply system and control method | |
| CN210239996U (en) | Screw air compressor machine waste heat recovery device | |
| CN201002974Y (en) | Energy-saving hollow fibrous membrane separation nitrogen producing machine | |
| CN201661320U (en) | Steam turbine overflowing steam extraction regulation device for industrial driving | |
| CN215718991U (en) | High-efficient peak regulation steam turbine system | |
| CN110714804B (en) | Bypass control system suitable for CAES system expansion unit | |
| CN205858495U (en) | Burning machine inlet Distribution of Natural system | |
| CN209458061U (en) | Compressed air is collected as the electricity generation system of power using wind-force | |
| CN204187601U (en) | The high-pressure feed water system of Combined cycle gas-steam turbine waste heat boiler | |
| CN210560287U (en) | Gasification coal water slurry preheating system | |
| CN209978018U (en) | Water feeding pump pipeline of three-pressure waste heat boiler | |
| CN209761508U (en) | System for driving and reducing station power consumption rate of waste incineration power plant by water feeding pump | |
| CN209115161U (en) | A kind of biomass incinerator and coal unit steam coupled system | |
| CN202274474U (en) | Energy-saving heat-accumulating boiler device | |
| CN101701531A (en) | Overflow steam extraction adjusting device of industrial drive steam turbine and control method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 550018 310 Xintian Avenue, Wudang District, Guiyang City, Guizhou Province Patentee after: Guizhou Sheng Ji Tang Pharmaceutical Industry Limited by Share Ltd. Address before: 550018 310 Xintian Avenue, Guiyang City, Guizhou Province Patentee before: GUIZHOU CHITIANHUA Co.,Ltd. |
|
| CP03 | Change of name, title or address | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 550018 new 310 Avenue, Wudang District, Guiyang, Guizhou Patentee after: GUIZHOU CHITIANHUA Co.,Ltd. Address before: 550018 new 310 Avenue, Wudang District, Guiyang, Guizhou Patentee before: Guizhou Sheng Ji Tang Pharmaceutical Industry Limited by Share Ltd. |
|
| CP01 | Change in the name or title of a patent holder |