CN104976637A - Method for calculating cold air leakage amount of inlet of coal mill for thermal power generation boiler - Google Patents
Method for calculating cold air leakage amount of inlet of coal mill for thermal power generation boiler Download PDFInfo
- Publication number
- CN104976637A CN104976637A CN201510264050.5A CN201510264050A CN104976637A CN 104976637 A CN104976637 A CN 104976637A CN 201510264050 A CN201510264050 A CN 201510264050A CN 104976637 A CN104976637 A CN 104976637A
- Authority
- CN
- China
- Prior art keywords
- coal pulverizer
- inlet
- coal
- pulverizer inlet
- cold wind
- 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.)
- Granted
Links
Landscapes
- Air Supply (AREA)
- Disintegrating Or Milling (AREA)
Abstract
The invention provides a method for calculating the cold air leakage amount of an inlet of a coal mill for a thermal power generation boiler. The method comprises the step that the cold air leakage amount of the inlet of the coal mill satisfies the formula: F1=Fh*(Th*Ch-Tr*Cr)/(T1*C1-Tr*Cr), wherein F1 is set to be the cold air leakage amount of the inlet of the coal mill, Fh is set to be the mixed air amount of the inlet of the coal mill, Th is set to be the temperature of mixed air of the inlet of the coal mill, Ch is set to be the constant-pressure specific heat capacity of the inlet of the coal mill, Tr is set to be the temperature of hot air of the inlet of the coal mill, Cr is set to be the constant-pressure specific heat capacity of the hot air of the inlet of the coal mill, T1 is set to be the temperature of cold air of the inlet of the coal mill, and C1 is set to be the constant-pressure specific heat capacity of the cold air of the inlet of the coal mill. The standard regulation quantity of an air door baffle at a cold air inlet of the coal mill of a direct blowing type coal pulverizing system is provided, the internal leakage amount of cold air of the direct blowing type coal pulverizing system is reduced, the drying capacity of the coal mill is increased, the exhaust gas temperature of the boiler is effectively lowered, and the standard regulation quantity of the air door baffle at the cold air inlet of the coal mill of the direct blowing type coal pulverizing system is acquired not through a test value any longer, so the stability and safety of a boiler combustion system are improved, and the regulation efficiency of the air door baffle at the cold air inlet of the coal mill of the direct blowing type coal pulverizing system is improved.
Description
One, technical field
Patent of the present invention relates to a kind of computational methods of coal pulverizer inlet cold wind leakage rate, especially a kind of computational methods for the coal pulverizer inlet cold wind leakage rate in thermal power generation boiler.
Two, background technology
Security and the economy of thermal power plant unit operation depend primarily on steam generator system, and the factor affecting steam generator system safety in operation and economy is the pulverized coal preparation system of boiler fired coal, the task of thermal power plant pulverized coal preparation system is set to boiler provide quality and quantity all to meet the coal dust of combustion requirements.Existing thermal power generation corporations coal dust preparation system mainly divides and is set to following a few class: storage low speed coal mill system in (1); (2) straight-blowing double-inlet and double-outlet steel ball coal mill system; (3) direct-firing medium-speed pulverizer system.Because unit pulverized-coal system is used widely because its system layout is relatively simple, reliability is high, adapt to the strong advantage of coal ability;
For unit pulverized-coal system, coal pulverizer inlet cold wind leakage rate directly affects the drying capacity of coal pulverizer, cold wind leakage rate crosses the coal pulverizer inlet hot blast that senior general squeezes same volume, thus cause direct-fired mill drying capacity not enough, exhaust gas temperature is raised, boiler combustion will be affected time serious stablize and safety, control mainly there is following two problems in electric current in adjustment in each thermal power plant at direct-fired mill drying capacity: one unit pulverized-coal system belongs to positive-pressure type pulverized coal preparation system, for the ball type pulverizer system, the problem of leakage of unit pulverized-coal system valve and baffle plate is obvious, interior leakage problem performance is not obvious, be difficult to inline diagnosis and maintenance, its two simultaneously pressurized direct pulverizing coal system affect by design condition, cold wind pressure is higher than hot-blast pressure, and the cold wind leakage rate bringing coal pulverizer inlet cold air damper to wear and tear thus to cause is large,
In order to ensure the security of thermal power plant unit operation and improve its economy, coal pulverizer inlet cold wind leakage rate in thermal power generation boiler is calculated and controls tool and has very important significance, therefore the computational methods for the coal pulverizer inlet cold wind leakage rate in thermal power generation boiler are a kind of important computational methods, also do not have now a kind of computational methods for the coal pulverizer inlet cold wind leakage rate in thermal power generation boiler.
Three, summary of the invention
In order to overcome above-mentioned technical disadvantages, the object of patent of the present invention is to provide a kind of computational methods for the coal pulverizer inlet cold wind leakage rate in thermal power generation boiler, therefore improve stability and the security of boiler combustion system, improve the adjustment efficiency of direct-fired mill cold air inlet damper.
In order to achieve the above object, the technical scheme that patent of the present invention is taked is: the steps include:
Application conditions: direct-fired mill runs and coal pulverizer electric current is greater than 25A and direct-fired mill entrance cold wind plate washer open degree feedback < 3%;
Fl=Fh×(Th×Ch-Tr×Cr)/(Tl×Cl-Tr×Cr),
Wherein:
Fl is set to coal pulverizer inlet cold wind leakage rate,
Fh is set to coal pulverizer inlet mixed air volume,
Th is set to coal pulverizer inlet mixing wind-warm syndrome,
Ch is set to coal pulverizer inlet mixing wind specific heat at constant pressure,
Tr is set to coal pulverizer inlet hot blast temperature,
Cr is set to coal pulverizer inlet hot blast specific heat at constant pressure,
Tl is set to coal pulverizer inlet cold wind temperature,
Cl is set to coal pulverizer inlet cold wind specific heat at constant pressure;
In the present embodiment, direct-fired mill entrance drying medium specific heat at constant pressure C=1.319+3.013/10^5 × T+2.118/10^7 × T^2-1.746/10^10 × T^3+5.863/10^14 × T^4-7.337/10^18 × T^5,
Wherein T is set to the Celsius temperature that drying medium is set to hot blast, mixing wind and cold wind respectively;
When T is set to the real time dynamic measurement celsius temperature scale that drying medium is mixing wind, Ch=1.319+3.013/10^5 × T+2.118/10^7 × T^2-1.746/10^10 × T^3+5.863/10^14 × T^4-7.337/10^18 × T^5;
When wherein T is set to the real time dynamic measurement celsius temperature scale that drying medium is hot blast, Cr=1.319+3.013/10^5 × T+2.118/10^7 × T^2-1.746/10^10 × T^3+5.863/10^14 × T^4-7.337/10^18 × T^5;
When wherein T is set to the real time dynamic measurement celsius temperature scale that drying medium is cold wind,
Cl=1.319+3.013/10^5×T+2.118/10^7×T^2-1.746/10^10×T^3+5.863/10^14×T^4-7.337/10^18×T^5;
In the present embodiment,
Fh is set to coal pulverizer inlet mixed air volume and is set to real time dynamic measurement value,
Th is set to coal pulverizer inlet mixing wind-warm syndrome and is set to real time dynamic measurement value,
Tr is set to coal pulverizer inlet hot blast temperature and is set to real time dynamic measurement value,
Tl is set to coal pulverizer inlet cold wind temperature and is set to real time dynamic measurement value.
Owing to devising the computational methods to direct-fired mill entrance cold wind leakage rate, provide the adjustment criteria amount of direct-fired mill cold air inlet damper, reduce leakage quantity in unit pulverized-coal system cold wind, improve drying capacity of pulverizer, effective reduction exhaust gas temperature, the adjustment criteria amount of direct-fired mill cold air inlet damper is no longer obtained by test value, therefore improve stability and the security of boiler combustion system, improve the adjustment efficiency of direct-fired mill cold air inlet damper.
The present invention devises, the programming of the computational methods for the coal pulverizer inlet cold wind leakage rate in thermal power generation boiler for being implanted in the DCS control system unit pulverized-coal system control module of thermal power plant.
In technical scheme of the present invention, selected parameter will meet the conservation of mass and the heat conservation condition of pulverized coal preparation system ventilation, that is: the conservation of mass: the summation of the hot blast air quantity and cold wind air quantity that enter coal pulverizer equals the mixed air volume of coal pulverizer, heat conservation: the hot blast entering coal pulverizer brings the heat that summation that heat and cold wind brings heat into equals coal pulverizer mixing wind into.^ is the implication of " power ", in all kinds of engineering calculation software as: 3.013/10^5 is then expressed as 3.013/100000.
In the technical program, important technology feature is set to the air quantity of direct-fired mill, wind-warm syndrome and specific heat at constant pressure, in the technical field of the computational methods for the coal pulverizer inlet cold wind leakage rate in thermal power generation boiler, have novelty, creativeness and practicality, the term in the technical program is all to make an explanation with patent document in the art and to understand.
Four, detailed description of the invention
Below in conjunction with embodiment, further describe the present invention, following examples are intended to the present invention instead of limitation of the invention further are described.
First embodiment of the present invention, technical scheme of the present invention, the steps include:
Application conditions: direct-fired mill runs and coal pulverizer electric current is greater than 25A and direct-fired mill entrance cold wind plate washer open degree feedback < 3%;
Fl=Fh×(Th×Ch-Tr×Cr)/(Tl×Cl-Tr×Cr),
Wherein:
Fl is set to coal pulverizer inlet cold wind leakage rate,
Fh is set to coal pulverizer inlet mixed air volume,
Th is set to coal pulverizer inlet mixing wind-warm syndrome,
Ch is set to coal pulverizer inlet mixing wind specific heat at constant pressure,
Tr is set to coal pulverizer inlet hot blast temperature,
Cr is set to coal pulverizer inlet hot blast specific heat at constant pressure,
Tl is set to coal pulverizer inlet cold wind temperature,
Cl is set to coal pulverizer inlet cold wind specific heat at constant pressure;
In the present embodiment, direct-fired mill entrance drying medium specific heat at constant pressure C=1.319+3.013/10^5 × T+2.118/10^7 × T^2-1.746/10^10 × T^3+5.863/10^14 × T^4-7.337/10^18 × T^5,
Wherein T is set to the Celsius temperature that drying medium is set to hot blast, mixing wind and cold wind respectively;
When T is set to the real time dynamic measurement celsius temperature scale that drying medium is mixing wind, Ch=1.319+3.013/10^5 × T+2.118/10^7 × T^2-1.746/10^10 × T^3+5.863/10^14 × T^4-7.337/10^18 × T^5;
When wherein T is set to the real time dynamic measurement celsius temperature scale that drying medium is hot blast, Cr=1.319+3.013/10^5 × T+2.118/10^7 × T^2-1.746/10^10 × T^3+5.863/10^14 × T^4-7.337/10^18 × T^5;
When wherein T is set to the real time dynamic measurement celsius temperature scale that drying medium is cold wind,
Cl=1.319+3.013/10^5×T+2.118/10^7×T^2-1.746/10^10×T^3+5.863/10^14×T^4-7.337/10^18×T^5;
In the present embodiment,
Fh is set to coal pulverizer inlet mixed air volume and is set to real time dynamic measurement value,
Th is set to coal pulverizer inlet mixing wind-warm syndrome and is set to real time dynamic measurement value,
Tr is set to coal pulverizer inlet hot blast temperature and is set to real time dynamic measurement value,
Tl is set to coal pulverizer inlet cold wind temperature and is set to real time dynamic measurement value;
By obtaining T value to the centigrade real time dynamic measurement of hot blast, mixing wind and cold wind, calculate Ch, Cr and Cl value, obtain Fh, Th, Tr and Tl value by real time dynamic measurement, calculate Fl value, controlled the combustion system of the boiler of thermal power plant unit by Fl value.
1000MW unit direct-fired mill model is BBD4360 coal pulverizer
Project | Unit | Technical parameter (design coal) |
Coal pulverizer model | BBD-4360 | |
Pulverizer capacity (HGI=50, H2O=8%, 75% by 200 mesh sieves) | t/h | 70 |
Cylindrical shell effective diameter | mm | 4250 |
Cylindrical shell effective length | mm | 6140 |
Drum speed | r/min | 16 |
Cylindrical shell dischargeable capacity | m 3 | 87.1 |
Maximum ball load | t | 92 |
Sealing air quantity | kg/h | 4500 |
Before not adopting this enforcement, coal pulverizer inlet cold wind slip cannot be estimated online, after employing the present embodiment, coal pulverizer inlet cold wind slip is about about 10-15% to utilize this method to find, by to the transformation of multiple stage coal pulverizer inlet cold-air flap, cold wind slip is reduced to less than 3%, makes exhaust gas temperature reduce about about 3 DEG C, make unit generation coal consumption reduce about 0.4g/kWh, improve unit macroeconomic.
Patent of the present invention has lower feature:
1, owing to devising the computational methods to direct-fired mill entrance cold wind leakage rate, provide the adjustment criteria amount of direct-fired mill cold air inlet damper, reduce leakage quantity in unit pulverized-coal system cold wind, improve drying capacity of pulverizer, effective reduction exhaust gas temperature, the adjustment criteria amount of direct-fired mill cold air inlet damper is no longer obtained by test value, therefore improve stability and the security of boiler combustion system, improve the adjustment efficiency of direct-fired mill cold air inlet damper.
2, owing to devising the computational methods to direct-fired mill entrance cold wind leakage rate, by real time dynamic measurement, obtain dynamic coal pulverizer inlet cold wind leakage rate in real time, improve boiler combustion system reliability of operation energy.
3, owing to devising, the restriction of number range has been carried out to planform, make the technical characteristic that number range is set in the technical scheme of patent of the present invention, be not by formulae discovery or tested the technical characteristic drawn by limited number of time, test shows that the technical characteristic of this number range achieves good technique effect.
4, owing to devising the technical characteristic of patent of the present invention, in the effect of the set separately and each other of technical characteristic, shown by test, what the property indices of patent of the present invention was set to existing property indices is at least set to 1.7 times, has good market value by assessment.
Above-described embodiment is a kind of way of realization of the computational methods for the coal pulverizer inlet cold wind leakage rate in thermal power generation boiler provided by the present invention; according to other distortion of scheme provided by the present invention; the composition increased or reduce wherein or step; or the present invention is used for other the technical field close with the present invention, all belongs to protection scope of the present invention.
Claims (2)
1. the computational methods for the coal pulverizer inlet cold wind leakage rate in thermal power generation boiler; It is characterized in that: the steps include:
Application conditions: direct-fired mill runs and coal pulverizer electric current is greater than 25A and direct-fired mill entrance cold wind plate washer open degree feedback < 3%;
Fl=Fh×(Th×Ch-Tr×Cr)/(Tl×Cl-Tr×Cr),
Wherein:
Fl is set to coal pulverizer inlet cold wind leakage rate,
Fh is set to coal pulverizer inlet mixed air volume,
Th is set to coal pulverizer inlet mixing wind-warm syndrome,
Ch is set to coal pulverizer inlet mixing wind specific heat at constant pressure,
Tr is set to coal pulverizer inlet hot blast temperature,
Cr is set to coal pulverizer inlet hot blast specific heat at constant pressure,
Tl is set to coal pulverizer inlet cold wind temperature,
Cl is set to coal pulverizer inlet cold wind specific heat at constant pressure;
Direct-fired mill entrance drying medium specific heat at constant pressure C=1.319+3.013/10^5 × T+2.118/10^7 × T^2-1.746/10^10 × T^3+5.863/10^14 × T^4-7.337/10^18 × T^5,
Wherein T is set to the Celsius temperature that drying medium is set to hot blast, mixing wind and cold wind respectively;
When T is set to the real time dynamic measurement celsius temperature scale that drying medium is mixing wind, Ch=1.319+3.013/10^5 × T+2.118/10^7 × T^2-1.746/10^10 × T^3+5.863/10^14 × T^4-7.337/10^18 × T^5;
When wherein T is set to the real time dynamic measurement celsius temperature scale that drying medium is hot blast, Cr=1.319+3.013/10^5 × T+2.118/10^7 × T^2-1.746/10^10 × T^3+5.863/10^14 × T^4-7.337/10^18 × T^5;
When wherein T is set to the real time dynamic measurement celsius temperature scale that drying medium is cold wind,
Cl=1.319+3.013/10^5×T+2.118/10^7×T^2-1.746/10^10×T^3+5.863/10^14×T^4-7.337/10^18×T^5;
Fh is set to coal pulverizer inlet mixed air volume and is set to real time dynamic measurement value,
Th is set to coal pulverizer inlet mixing wind-warm syndrome and is set to real time dynamic measurement value,
Tr is set to coal pulverizer inlet hot blast temperature and is set to real time dynamic measurement value,
Tl is set to coal pulverizer inlet cold wind temperature and is set to real time dynamic measurement value.
2. the computational methods for the coal pulverizer inlet cold wind leakage rate in thermal power generation boiler according to claim 1, is characterized in that: the programming of the computational methods for the coal pulverizer inlet cold wind leakage rate in thermal power generation boiler for being implanted in the DCS control system unit pulverized-coal system control module of thermal power plant.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510264050.5A CN104976637B (en) | 2015-05-22 | 2015-05-22 | Method for calculating cold air leakage amount of inlet of coal mill for thermal power generation boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510264050.5A CN104976637B (en) | 2015-05-22 | 2015-05-22 | Method for calculating cold air leakage amount of inlet of coal mill for thermal power generation boiler |
Publications (2)
Publication Number | Publication Date |
---|---|
CN104976637A true CN104976637A (en) | 2015-10-14 |
CN104976637B CN104976637B (en) | 2017-04-12 |
Family
ID=54273405
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510264050.5A Active CN104976637B (en) | 2015-05-22 | 2015-05-22 | Method for calculating cold air leakage amount of inlet of coal mill for thermal power generation boiler |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104976637B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116085822A (en) * | 2023-03-07 | 2023-05-09 | 国家能源集团科学技术研究院有限公司 | Method, device, equipment and medium for calculating mixed air volume of coal mill inlet |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3126829A1 (en) * | 1981-07-08 | 1983-02-03 | Steag Ag, 4300 Essen | Process for generating an inert gas containing CO2 and N2 for the protection of flammable dusts by combustion of carbon-containing fuels with air, and inert gas generator for carrying out the process |
DD283702A7 (en) * | 1988-09-19 | 1990-10-24 | Veb Kraftwerke Luebbenau-Vetschau,Dd | METHOD AND ARRANGEMENT FOR OPERATING A CARBON FAN VALVE |
KR20020002045A (en) * | 2000-06-29 | 2002-01-09 | 이구택 | An apparatus for analysising and controlling oxygen concentration of a fine coke device |
CN1771439A (en) * | 2004-02-27 | 2006-05-10 | 王砧 | On-line monitoring method and device for a fossil fuel converter apparatus |
CN201510924U (en) * | 2009-09-28 | 2010-06-23 | 张堂林 | Coal mill entrance air channel laying device of positive pressure direct-fired pulverizing system |
CN102645523A (en) * | 2012-05-10 | 2012-08-22 | 北京华电天仁电力控制技术有限公司 | Moisture as received coal on-line identification method based on heat balance of powder process system |
CN203687075U (en) * | 2014-02-10 | 2014-07-02 | 河北省电力勘测设计研究院 | Primary air system of coal mill of thermal power plant |
-
2015
- 2015-05-22 CN CN201510264050.5A patent/CN104976637B/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3126829A1 (en) * | 1981-07-08 | 1983-02-03 | Steag Ag, 4300 Essen | Process for generating an inert gas containing CO2 and N2 for the protection of flammable dusts by combustion of carbon-containing fuels with air, and inert gas generator for carrying out the process |
DD283702A7 (en) * | 1988-09-19 | 1990-10-24 | Veb Kraftwerke Luebbenau-Vetschau,Dd | METHOD AND ARRANGEMENT FOR OPERATING A CARBON FAN VALVE |
KR20020002045A (en) * | 2000-06-29 | 2002-01-09 | 이구택 | An apparatus for analysising and controlling oxygen concentration of a fine coke device |
CN1771439A (en) * | 2004-02-27 | 2006-05-10 | 王砧 | On-line monitoring method and device for a fossil fuel converter apparatus |
CN201510924U (en) * | 2009-09-28 | 2010-06-23 | 张堂林 | Coal mill entrance air channel laying device of positive pressure direct-fired pulverizing system |
CN102645523A (en) * | 2012-05-10 | 2012-08-22 | 北京华电天仁电力控制技术有限公司 | Moisture as received coal on-line identification method based on heat balance of powder process system |
CN203687075U (en) * | 2014-02-10 | 2014-07-02 | 河北省电力勘测设计研究院 | Primary air system of coal mill of thermal power plant |
Non-Patent Citations (1)
Title |
---|
邹海峰: ""惠州热电厂330 MW机组锅炉排烟温度偏高的原因分析及解决措施"", 《热力发电》 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116085822A (en) * | 2023-03-07 | 2023-05-09 | 国家能源集团科学技术研究院有限公司 | Method, device, equipment and medium for calculating mixed air volume of coal mill inlet |
Also Published As
Publication number | Publication date |
---|---|
CN104976637B (en) | 2017-04-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107855210B (en) | Energy-saving optimal control system and method for outlet temperature of medium-speed coal mill of supercritical unit | |
CN101709882A (en) | Coal-fired boiler hot primary wind heating system | |
CN103438686A (en) | Primary air cooler heat regenerative system and controlling method | |
CN103925605A (en) | High-moisture lignite medium-speed coal mill pulverizing system heating primary air through pulverized coal burning | |
CN104990063B (en) | Hot primary air waste heat utilization device coupled with air heater system in use | |
CN203771439U (en) | High-moisture lignite medium speed mill coal pulverizing system using pulverized coal combustion heating primary air | |
CN104976637A (en) | Method for calculating cold air leakage amount of inlet of coal mill for thermal power generation boiler | |
CN201262408Y (en) | Hot primary air bypass apparatus of coal-burning boiler | |
CN113457791A (en) | Online automatic optimization method for operating parameters of medium-speed coal mill for high-moisture coal | |
CN101907300A (en) | Enclosed air system of medium speed mill in heat-engine plant | |
Tuncer et al. | Efficient energy systems models for sustainable food processing | |
CN111735041A (en) | Dry burning prevention and water level regulation device for circulating fluidized bed unit and control method thereof | |
CN203848313U (en) | Positive pressure powder manufacturing system for drying brown coal through boiler interior heating primary air and cold smoke | |
CN206846704U (en) | A kind of coal burner cooling air system using boiler heat primary air | |
CN203454196U (en) | Efficiency improving device for heating primary boiler air by using coal gas | |
CN206207454U (en) | A kind of mechanism for wind-warm syndrome of raising boiler milling system | |
CN206496366U (en) | A kind of blower fan interacted system | |
CN214147977U (en) | System for controlling W flame boiler double-inlet and double-outlet steel ball-milling bituminous coal blending combustion proportion | |
CN210320143U (en) | System for reducing boiler exhaust gas temperature and inhibiting low-temperature corrosion of air preheater | |
CN212204477U (en) | System for be used for improving boiler coal pulverizing system coal type adaptability | |
CN201434569Y (en) | Split-type air energy dryer | |
CN212069139U (en) | Lignite-based coal mill capacity-increasing and efficiency-improving device | |
CN204694011U (en) | A kind of high-effective dust-removing foodstuff drying device | |
CN212040952U (en) | System for improving flexibility of temperature regulation of outlet of coal mill | |
CN204555721U (en) | A kind of tunnel cave two pressure cogeneration and the pre-apparatus for cooling of material |
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 |