CN109636001A - Desulfurization pulp feeding system pH value adjusting method, system and computer-readable medium based on big data - Google Patents
Desulfurization pulp feeding system pH value adjusting method, system and computer-readable medium based on big data Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 34
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 20
- 230000023556 desulfurization Effects 0.000 title claims abstract description 20
- 239000002002 slurry Substances 0.000 claims abstract description 299
- 235000019738 Limestone Nutrition 0.000 claims abstract description 112
- 239000006028 limestone Substances 0.000 claims abstract description 112
- 239000007788 liquid Substances 0.000 claims abstract description 94
- 238000009955 starching Methods 0.000 claims abstract description 37
- 238000012544 monitoring process Methods 0.000 claims abstract description 18
- 238000004458 analytical method Methods 0.000 claims abstract description 11
- 238000005457 optimization Methods 0.000 claims abstract description 10
- 239000010440 gypsum Substances 0.000 claims description 49
- 229910052602 gypsum Inorganic materials 0.000 claims description 49
- 238000003860 storage Methods 0.000 claims description 11
- 230000001105 regulatory effect Effects 0.000 claims description 8
- 229920002472 Starch Polymers 0.000 claims description 6
- 235000019698 starch Nutrition 0.000 claims description 6
- 239000008107 starch Substances 0.000 claims description 6
- 230000007613 environmental effect Effects 0.000 abstract description 9
- 238000004134 energy conservation Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 230000009467 reduction Effects 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 5
- 238000013473 artificial intelligence Methods 0.000 description 3
- 238000010168 coupling process Methods 0.000 description 3
- 238000005859 coupling reaction Methods 0.000 description 3
- 239000004575 stone Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 241001269238 Data Species 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000010801 machine learning Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 230000004382 visual function Effects 0.000 description 1
Classifications
-
- G—PHYSICS
- G06—COMPUTING; CALCULATING OR COUNTING
- G06Q—INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES; SYSTEMS OR METHODS SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES, NOT OTHERWISE PROVIDED FOR
- G06Q10/00—Administration; Management
- G06Q10/04—Forecasting or optimisation specially adapted for administrative or management purposes, e.g. linear programming or "cutting stock problem"
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
- B01D53/501—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
- B01D53/502—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound characterised by a specific solution or suspension
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/80—Semi-solid phase processes, i.e. by using slurries
-
- G—PHYSICS
- G06—COMPUTING; CALCULATING OR COUNTING
- G06Q—INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES; SYSTEMS OR METHODS SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES, NOT OTHERWISE PROVIDED FOR
- G06Q50/00—Systems or methods specially adapted for specific business sectors, e.g. utilities or tourism
- G06Q50/06—Electricity, gas or water supply
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y04—INFORMATION OR COMMUNICATION TECHNOLOGIES HAVING AN IMPACT ON OTHER TECHNOLOGY AREAS
- Y04S—SYSTEMS INTEGRATING TECHNOLOGIES RELATED TO POWER NETWORK OPERATION, COMMUNICATION OR INFORMATION TECHNOLOGIES FOR IMPROVING THE ELECTRICAL POWER GENERATION, TRANSMISSION, DISTRIBUTION, MANAGEMENT OR USAGE, i.e. SMART GRIDS
- Y04S10/00—Systems supporting electrical power generation, transmission or distribution
- Y04S10/50—Systems or methods supporting the power network operation or management, involving a certain degree of interaction with the load-side end user applications
Abstract
The present invention provides a kind of desulfurization pulp feeding system pH value adjusting method based on big data, method include the following steps: to carry out operation monitoring and optimization monitoring for slurry equipment to units all in power plant to acquire the operation data for starching equipment；Based on the operation data for starching equipment acquired in real time and combination is for the history data of slurry equipment, analyzes the logical relation between each data, is calculated by big data means analysis, provides limestone slurry liquid pump optimized operation and start and stop scheme.Method and system of the invention can reach energy conservation and consumption reduction effects and economical operation maximizes, be discharged by intelligent monitoring environmental protection index, meet national emission request, realize social responsibility value under the premise of guaranteeing environmental requirement；It is run by optimization, realizes energy-saving, promotion social resources rational exploitation and utilization.Method and system of the invention realizes fining operation operation by the service ability of optimization equipment, while reaching national requirements for environmental protection, realizes that enterprise operation is energy-saving.
Description
Technical field
The present invention relates to power plant for energy conservation environmental technology field, in particular to a kind of desulfurization pulp feeding system pH based on big data
It is worth adjusting method, system and computer-readable medium.
Background technique
It proposes to push internet, big data, artificial intelligence and real economy depth integration at present, lead in innovation, green
The fields such as low-carbon, shared economy cultivate new growing point, form new kinetic energy；It is advanced to realize internet, big data, artificial intelligence etc.
The depth integration of technology and the manufacturing of Traditional Environmental-protection equipment, operation management pushes company's transition；Environmental protection equipment expert is established to determine
Plan system is learnt by the artificial intelligence of product practice and historical data, real by real-time theoretical calculation and history optimizing
Existing equipment refinement running optimizatin guidance, it is ensured that " environmental protection optimizes " and " economy maximizes ".
The information disclosed in the background technology section is intended only to increase the understanding to general background of the invention, without answering
When being considered as recognizing or imply that the information constitutes the prior art already known to those of ordinary skill in the art in any form.
Summary of the invention
The purpose of the present invention is to provide it is a kind of by the desulfurization pulp feeding system pH value adjusting method of big data, system and based on
Calculation machine readable medium, thus the shortcomings that overcoming the prior art.
The present invention provides a kind of desulfurization pulp feeding system pH value adjusting method based on big data, method include following step
It is rapid:
Units all in power plant are carried out operation monitoring and optimized to monitor to acquire the operation data for starching equipment for slurry equipment,
Wherein, include for the operation data for starching equipment；Between slurry supply pump quantity, limestone slurry liquid pump number of units, AFT Turo pump number of units, suggestion
Every minute, gypsum slurries pH value, lime stone slurry pump operation situation and AFT Turo pump operating condition；
Based on the operation data acquired in real time for starching equipment and history data for starching equipment is combined, is analyzed between each data
Logical relation, calculated by big data means analysis, provide limestone slurry liquid pump optimized operation and start and stop scheme, wherein supply
The history data of slurry equipment includes the historical data of slurry supply pump quantity, the historical data of limestone slurry liquid pump number of units, AFT rotation
The historical data of stream pump number of units suggests the interval historical data of minute, the historical data of gypsum slurries pH value, limestone slurry liquid pump
The historical data of operating condition and the historical data of AFT Turo pump operating condition；
Wherein, limestone slurry liquid pump optimized operation and start and stop scheme include:
When gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting slurry supply pump；
When gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop slurry supply pump；
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, method includes the following steps: to open when AFT tower circulating pump and AFT tower is for slurry
When pump is not opened, and when AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, method includes the following steps: to open when AFT tower circulating pump and AFT tower is for slurry
When pump is opened, and when AFT tower slurry pH value is higher than the pH value for stopping limestone slurry liquid pump, it is proposed that stop AFT slurry supply pump.
The desulfurization pulp feeding system pH value regulating system based on big data that the present invention also provides a kind of, system include:
For carrying out operation monitoring and optimization monitoring for slurry equipment to units all in power plant to acquire the operation for starching equipment
The unit of data, wherein for starch equipment operation data include；Slurry supply pump quantity, limestone slurry liquid pump number of units, AFT Turo pump
Number of units suggests interval minute, gypsum slurries pH value, lime stone slurry pump operation situation and AFT Turo pump operating condition；
For analyzing each number based on the operation data for starching equipment acquired in real time and in conjunction with the history data for starching equipment
According to logical relation, calculated by big data means analysis, provide the list of limestone slurry liquid pump optimized operation and start and stop scheme
Member, wherein the history data for starching equipment includes the history of the historical data of slurry supply pump quantity, limestone slurry liquid pump number of units
Data, the historical data of AFT Turo pump number of units suggest the interval historical data of minute, the historical data of gypsum slurries pH value, stone
The historical data of lime stone slurries pump operation situation and the historical data of AFT Turo pump operating condition；
Wherein, limestone slurry liquid pump optimized operation and start and stop scheme include:
When gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting slurry supply pump；
When gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop slurry supply pump；
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, when gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that open
Dynamic slurry supply pump specifically: when AFT tower circulating pump is opened and AFT tower slurry supply pump is not opened, and when AFT tower slurry pH value is small
When opening the pH value of limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, when gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop
Only slurry supply pump specifically: when AFT tower circulating pump is opened and AFT tower slurry supply pump is opened, and when AFT tower slurry pH value is higher than
When stopping the pH value of limestone slurry liquid pump, it is proposed that stop AFT slurry supply pump.
The present invention provides a kind of computer readable storage medium, computer-readable recording medium storage is used for based on big number
According to desulfurization pulp feeding system pH value regulating system instruction, instruction be able to carry out following operation when executed by the processor:
Units all in power plant are carried out operation monitoring and optimized to monitor to acquire the operation data for starching equipment for slurry equipment,
Wherein, include for the operation data for starching equipment；Between slurry supply pump quantity, limestone slurry liquid pump number of units, AFT Turo pump number of units, suggestion
Every minute, gypsum slurries pH value, lime stone slurry pump operation situation and AFT Turo pump operating condition；
Based on the operation data acquired in real time for starching equipment and history data for starching equipment is combined, is analyzed between each data
Logical relation, calculated by big data means analysis, provide limestone slurry liquid pump optimized operation and start and stop scheme, wherein supply
The history data of slurry equipment includes the historical data of slurry supply pump quantity, the historical data of limestone slurry liquid pump number of units, AFT rotation
The historical data of stream pump number of units suggests the interval historical data of minute, the historical data of gypsum slurries pH value, limestone slurry liquid pump
The historical data of operating condition and the historical data of AFT Turo pump operating condition；
Wherein, limestone slurry liquid pump optimized operation and start and stop scheme include:
When gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting slurry supply pump；
When gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop slurry supply pump；
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, method includes the following steps: to open lime stone slurry when gypsum slurries pH value is less than
When the pH value of pump, it is proposed that starting slurry supply pump specifically: when AFT tower circulating pump is opened and AFT tower slurry supply pump is not opened, and
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, method includes the following steps: to stop lime stone slurry when gypsum slurries pH value is greater than
When the pH value of pump, it is proposed that stop slurry supply pump specifically: when AFT tower circulating pump is opened and AFT tower slurry supply pump is opened, and work as
When AFT tower slurry pH value is higher than the pH value for stopping limestone slurry liquid pump, it is proposed that stop AFT slurry supply pump.
Compared with prior art, the invention has the following beneficial effects: be based on machine learning, clustering, track following
Etc. big datas technology, line opertions engineering teacher lower to various operating conditions the real-time operation record of equipment, equipment running status are carried out
Machine autonomous learning and real-time monitoring;Equipment normal operation rules are concluded in realization, optimal by history optimizing and theory
Calculating combines, and provides environmentally friendly island equipment refinement equipment running optimizatin guiding opinion for line opertions engineering teacher；Realize machine
Learn aid decision.According to measuring points such as desulfurization pulp feeding system gypsum slurries pH, limestone slurry liquid pump electric currents, and respectively operate equipment
The real-time visual function of operating status supervises equipment operation condition totally, provides judgement support for operator.Root
According to the optimization direction of pH value, slurry supply pump guiding opinion is provided；It is provided according to pH value for starching control valve opening guiding opinion；Guaranteeing
Under the premise of environmental requirement, reaches energy conservation and consumption reduction effects and economical operation maximizes.It is discharged, is accorded with by intelligent monitoring environmental protection index
National emission request is closed, realizes social responsibility value；It is run by optimization, realization is energy-saving, and social resources is promoted rationally to open
Hair utilizes.Environment protection digital running optimizatin instructs platform by the service ability of optimization equipment, realizes fining operation operation, is reaching
While to national requirements for environmental protection, realize that enterprise operation is energy-saving.
Detailed description of the invention
By reading the following detailed description of the preferred embodiment, various other advantages and benefits are common for this field
Technical staff will become clear.The drawings are only for the purpose of illustrating a preferred embodiment, and is not considered as to the present invention
Limitation.And throughout the drawings, the same reference numbers will be used to refer to the same parts.In the accompanying drawings:
Fig. 1 is the method flow of the desulfurization pulp feeding system pH value adjusting method based on big data of embodiment according to the present invention
Figure.
Specific embodiment
The illustrative embodiments of the disclosure are more fully described below with reference to accompanying drawings.Although showing this public affairs in attached drawing
The illustrative embodiments opened, it being understood, however, that may be realized in various forms the disclosure without the reality that should be illustrated here
The mode of applying is limited.It is to be able to thoroughly understand the disclosure on the contrary, providing these embodiments, and can be by this public affairs
The range opened is fully disclosed to those skilled in the art.
Fig. 1 is the method stream of the desulfurization pulp feeding system pH value adjusting method based on big data of embodiment according to the present invention
Cheng Tu.As shown, the method comprise the steps that
Step 101: operation monitoring and optimization monitoring are carried out to acquire for slurry equipment for slurry equipment to units all in power plant
Operation data, wherein for starch equipment operation data include；Slurry supply pump quantity, limestone slurry liquid pump number of units, AFT Turo pump platform
Number suggests interval minute, gypsum slurries pH value, lime stone slurry pump operation situation and AFT Turo pump operating condition；
Step 102: the history data based on the operation data for starching equipment and combination acquired in real time for slurry equipment, analysis
Logical relation between each data is calculated by big data means analysis, provides limestone slurry liquid pump optimized operation and start and stop scheme,
It wherein, include the history number of the historical data of slurry supply pump quantity, limestone slurry liquid pump number of units for the history data for starching equipment
According to the historical data of, AFT Turo pump number of units, suggest the interval historical data of minute, the historical data of gypsum slurries pH value, lime
The historical data of stone slurries pump operation situation and the historical data of AFT Turo pump operating condition；
Wherein, limestone slurry liquid pump optimized operation and start and stop scheme include:
When gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting slurry supply pump；
When gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop slurry supply pump；
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, method includes the following steps: to open when AFT tower circulating pump and AFT tower is for slurry
When pump is not opened, and when AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, method includes the following steps: to open when AFT tower circulating pump and AFT tower is for slurry
When pump is opened, and when AFT tower slurry pH value is higher than the pH value for stopping limestone slurry liquid pump, it is proposed that stop AFT slurry supply pump.
The desulfurization pulp feeding system pH value regulating system based on big data that the present invention also provides a kind of, system include:
For carrying out operation monitoring and optimization monitoring for slurry equipment to units all in power plant to acquire the operation for starching equipment
The unit of data, wherein for starch equipment operation data include；Slurry supply pump quantity, limestone slurry liquid pump number of units, AFT Turo pump
Number of units suggests interval minute, gypsum slurries pH value, lime stone slurry pump operation situation and AFT Turo pump operating condition；
For analyzing each number based on the operation data for starching equipment acquired in real time and in conjunction with the history data for starching equipment
According to logical relation, calculated by big data means analysis, provide the list of limestone slurry liquid pump optimized operation and start and stop scheme
Member, wherein the history data for starching equipment includes the history of the historical data of slurry supply pump quantity, limestone slurry liquid pump number of units
Data, the historical data of AFT Turo pump number of units suggest the interval historical data of minute, the historical data of gypsum slurries pH value, stone
The historical data of lime stone slurries pump operation situation and the historical data of AFT Turo pump operating condition；
Wherein, limestone slurry liquid pump optimized operation and start and stop scheme include:
When gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting slurry supply pump；
When gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop slurry supply pump；
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.Platform curve is shown
Crucial measuring point or the fluctuation situation before data current 2 hours.According to the parameter of backstage configuration, highest is obtained by algorithm model operation
5 groups of suggestion tuning schemes.
Preferably, in above-mentioned technical proposal, when gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that open
Dynamic slurry supply pump specifically: when AFT tower circulating pump is opened and AFT tower slurry supply pump is not opened, and when AFT tower slurry pH value is small
When opening the pH value of limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, when gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop
Only slurry supply pump specifically: when AFT tower circulating pump is opened and AFT tower slurry supply pump is opened, and when AFT tower slurry pH value is higher than
When stopping the pH value of limestone slurry liquid pump, it is proposed that stop AFT slurry supply pump.
The present invention provides a kind of computer readable storage medium, computer-readable recording medium storage is used for based on big number
According to desulfurization pulp feeding system pH value regulating system instruction, instruction be able to carry out following operation when executed by the processor:
Units all in power plant are carried out operation monitoring and optimized to monitor to acquire the operation data for starching equipment for slurry equipment,
Wherein, include for the operation data for starching equipment；Between slurry supply pump quantity, limestone slurry liquid pump number of units, AFT Turo pump number of units, suggestion
Every minute, gypsum slurries pH value, lime stone slurry pump operation situation and AFT Turo pump operating condition；
Based on the operation data acquired in real time for starching equipment and history data for starching equipment is combined, is analyzed between each data
Logical relation, calculated by big data means analysis, provide limestone slurry liquid pump optimized operation and start and stop scheme, wherein supply
The history data of slurry equipment includes the historical data of slurry supply pump quantity, the historical data of limestone slurry liquid pump number of units, AFT rotation
The historical data of stream pump number of units suggests the interval historical data of minute, the historical data of gypsum slurries pH value, limestone slurry liquid pump
The historical data of operating condition and the historical data of AFT Turo pump operating condition；
Wherein, limestone slurry liquid pump optimized operation and start and stop scheme include:
When gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting slurry supply pump；
When gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop slurry supply pump；
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, method includes the following steps: to open lime stone slurry when gypsum slurries pH value is less than
When the pH value of pump, it is proposed that starting slurry supply pump specifically: when AFT tower circulating pump is opened and AFT tower slurry supply pump is not opened, and
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
Preferably, in above-mentioned technical proposal, method includes the following steps: to stop lime stone slurry when gypsum slurries pH value is greater than
When the pH value of pump, it is proposed that stop slurry supply pump specifically: when AFT tower circulating pump is opened and AFT tower slurry supply pump is opened, and work as
When AFT tower slurry pH value is higher than the pH value for stopping limestone slurry liquid pump, it is proposed that stop AFT slurry supply pump.
In several embodiments provided by the present invention, it should be understood that disclosed device and method can pass through it
Its mode is realized.For example, the apparatus embodiments described above are merely exemplary, for example, the division of the unit, only
Only a kind of logical function partition, there may be another division manner in actual implementation, such as multiple units or components can be tied
Another system is closed or is desirably integrated into, or some features can be ignored or not executed.Another point, it is shown or discussed
Mutual coupling, direct-coupling or communication connection can be through some interfaces, the INDIRECT COUPLING or logical of device or unit
Letter connection can be electrical property, mechanical or other forms.
The unit as illustrated by the separation member may or may not be physically separated, aobvious as unit
The component shown may or may not be physical unit, it can and it is in one place, or may be distributed over multiple
In network unit.It can select some or all of unit therein according to the actual needs to realize the mesh of this embodiment scheme
's.
It, can also be in addition, the functional units in various embodiments of the present invention may be integrated into one processing unit
It is that each unit physically exists alone, can also be integrated in one unit with two or more units.Above-mentioned integrated list
Member both can take the form of hardware realization, can also realize in the form of hardware adds SFU software functional unit.
The above-mentioned integrated unit being realized in the form of SFU software functional unit can store and computer-readable deposit at one
In storage media.Above-mentioned SFU software functional unit is stored in a storage medium, including some instructions are used so that a computer
It is each that equipment (can be personal computer, server or the network equipment etc.) or processor (processor) execute the present invention
The part steps of embodiment the method.And storage medium above-mentioned includes: USB flash disk, mobile hard disk, read-only memory (Read-
Only Memory, ROM), random access memory (Random Access Memory, RAM), magnetic or disk etc. it is various
It can store the medium of program code.
Finally, it should be noted that the above embodiments are only used to illustrate the technical solution of the present invention., rather than its limitations；To the greatest extent
Pipe present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that: its according to
So be possible to modify the technical solutions described in the foregoing embodiments, or to some or all of the technical features into
Row equivalent replacement；And these are modified or replaceed, various embodiments of the present invention technology that it does not separate the essence of the corresponding technical solution
The range of scheme.
Claims (9)
1. a kind of desulfurization pulp feeding system pH value adjusting method based on big data, it is characterised in that: the method includes walking as follows
It is rapid:
Units all in power plant are carried out operation monitoring and optimized to monitor to acquire the operation data for starching equipment for slurry equipment,
Wherein, the operation data for starching equipment includes；Slurry supply pump quantity, AFT Turo pump number of units, is built at limestone slurry liquid pump number of units
View interval minute, gypsum slurries pH value, lime stone slurry pump operation situation and AFT Turo pump operating condition；
Based on the operation data acquired in real time for starching equipment and history data for starching equipment is combined, is analyzed between each data
Logical relation, calculated by big data means analysis, provide limestone slurry liquid pump optimized operation and start and stop scheme, wherein institute
State for starch equipment history data include the historical data of slurry supply pump quantity, the historical data of limestone slurry liquid pump number of units,
The historical data of AFT Turo pump number of units suggests the interval historical data of minute, the historical data of gypsum slurries pH value, lime stone
The historical data of slurries pump operation situation and the historical data of AFT Turo pump operating condition；
Wherein, the limestone slurry liquid pump optimized operation and start and stop scheme include:
When gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting slurry supply pump；
When gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop slurry supply pump；
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
2. the desulfurization pulp feeding system pH value adjusting method based on big data as described in claim 1, it is characterised in that: the side
Method includes the following steps: when AFT tower circulating pump is opened and AFT tower slurry supply pump is not opened, and it is small to work as AFT tower slurry pH value
When opening the pH value of limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
3. the desulfurization pulp feeding system pH value adjusting method based on big data as described in claim 1, it is characterised in that: the side
Method includes the following steps: when AFT tower circulating pump is opened and AFT tower slurry supply pump is opened, and works as AFT tower slurry pH value and be higher than
When stopping the pH value of limestone slurry liquid pump, it is proposed that stop AFT slurry supply pump.
4. a kind of desulfurization pulp feeding system pH value regulating system based on big data, it is characterised in that: the system comprises:
For carrying out operation monitoring and optimization monitoring for slurry equipment to units all in power plant to acquire the operation for starching equipment
The unit of data, wherein it is described for starch equipment operation data include；Slurry supply pump quantity, limestone slurry liquid pump number of units, AFT rotation
Stream pump number of units suggests interval minute, gypsum slurries pH value, lime stone slurry pump operation situation and AFT Turo pump operating condition；
For analyzing each number based on the operation data for starching equipment acquired in real time and in conjunction with the history data for starching equipment
According to logical relation, calculated by big data means analysis, provide the list of limestone slurry liquid pump optimized operation and start and stop scheme
Member, wherein the history data for starching equipment includes the historical data of slurry supply pump quantity, limestone slurry liquid pump number of units
The history number of historical data, the historical data of AFT Turo pump number of units, the historical data for suggesting interval minute, gypsum slurries pH value
According to, the historical data of lime stone slurry pump operation situation and the historical data of AFT Turo pump operating condition；
Wherein, the limestone slurry liquid pump optimized operation and start and stop scheme include:
When gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting slurry supply pump；
When gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop slurry supply pump；
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
5. the desulfurization pulp feeding system pH value regulating system based on big data as claimed in claim 4, it is characterised in that: work as gypsum
Slurry pH value be less than open limestone slurry liquid pump pH value when, it is proposed that starting slurry supply pump specifically: when AFT tower circulating pump open and
When AFT tower slurry supply pump is not opened, and when AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT
Slurry supply pump.
6. the desulfurization pulp feeding system pH value regulating system based on big data as claimed in claim 4, it is characterised in that: work as gypsum
Slurry pH value be greater than stop limestone slurry liquid pump pH value when, it is proposed that stop slurry supply pump specifically: when AFT tower circulating pump open and
When AFT tower slurry supply pump is opened, and when AFT tower slurry pH value is higher than the pH value for stopping limestone slurry liquid pump, it is proposed that stop AFT and supply
Stock pump.
7. a kind of computer readable storage medium, the computer-readable recording medium storage is supplied for the desulfurization based on big data
The instruction of slurry system pH value regulating system, described instruction are able to carry out following operation when executed by the processor:
Units all in power plant are carried out operation monitoring and optimized to monitor to acquire the operation data for starching equipment for slurry equipment,
Wherein, the operation data for starching equipment includes；Slurry supply pump quantity, AFT Turo pump number of units, is built at limestone slurry liquid pump number of units
View interval minute, gypsum slurries pH value, lime stone slurry pump operation situation and AFT Turo pump operating condition；
Based on the operation data acquired in real time for starching equipment and history data for starching equipment is combined, is analyzed between each data
Logical relation, calculated by big data means analysis, provide limestone slurry liquid pump optimized operation and start and stop scheme, wherein institute
State for starch equipment history data include the historical data of slurry supply pump quantity, the historical data of limestone slurry liquid pump number of units,
The historical data of AFT Turo pump number of units suggests the interval historical data of minute, the historical data of gypsum slurries pH value, lime stone
The historical data of slurries pump operation situation and the historical data of AFT Turo pump operating condition；
Wherein, the limestone slurry liquid pump optimized operation and start and stop scheme include:
When gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting slurry supply pump；
When gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop slurry supply pump；
When AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting AFT slurry supply pump.
8. computer readable storage medium as claimed in claim 7, it is characterised in that: described method includes following steps: when
When gypsum slurries pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that starting slurry supply pump specifically: when AFT tower circulating pump is opened
And when AFT tower slurry supply pump is not opened, and when AFT tower slurry pH value is less than the pH value for opening limestone slurry liquid pump, it is proposed that open
Dynamic AFT slurry supply pump.
9. computer readable storage medium as claimed in claim 7, it is characterised in that: described method includes following steps: when
When gypsum slurries pH value is greater than the pH value for stopping limestone slurry liquid pump, it is proposed that stop slurry supply pump specifically: when AFT tower circulating pump is opened
And when AFT tower slurry supply pump is opened, and when AFT tower slurry pH value is higher than the pH value for stopping limestone slurry liquid pump, it is proposed that stop
AFT slurry supply pump.
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