CN203799249U - Control system used for balancing infiltration water in press production process - Google Patents
Control system used for balancing infiltration water in press production process Download PDFInfo
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- CN203799249U CN203799249U CN201420194542.2U CN201420194542U CN203799249U CN 203799249 U CN203799249 U CN 203799249U CN 201420194542 U CN201420194542 U CN 201420194542U CN 203799249 U CN203799249 U CN 203799249U
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- infiltration water
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- control system
- output module
- infiltration
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- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/02—Total factory control, e.g. smart factories, flexible manufacturing systems [FMS] or integrated manufacturing systems [IMS]
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Abstract
The utility model relates to the technical field of sugar production, and in particular relates to a control system used for balancing infiltration water in a press production process. The control system comprises an industrial computer. The industrial computer is connected with and is provided with a switching value data acquisition card, an analog data acquisition card, a man-machine interaction module, a switching value output module and an analog output module. The analog data acquisition card is connected with an infrared moisture tester, a cold water valve opening meter, a hot water valve opening meter, a liquid level transmitter, a temperature sensor, an electromagnetic flowmeter and a frequency converter. The analog output module is connected with a cold water electric actuator, a hot water electric actuator and a transducer. According to the utility model, the temperature sensor is used to detect the temperature of the infiltration water; the electromagnetic flowmeter is used to detect the flow of the infiltration water; the industrial computer is used to receive infiltration water flow and temperature instructions from scheduling or a scheduling computer, and the temperature of the infiltration water is adjusted; a scheduling instruction and an electromagnetic flowmeter signal are synthesized to form a transducer rotation speed instruction; the rotation speed of a infiltration water pump is controlled; and infiltration water supply according to needs is ensured.
Description
Technical field
The utility model relates to sugar industry technical field, is specifically related to uniform milling production run infiltration water control system.
Background technology
Sugar refinery belongs to typical process industry, but does not also have so far a sugar refinery to realize Automation of Manufacturing Process control, and the process control system that oneself realizes is also perfect not to the utmost, some operations, and particularly the most last procedure of sugar industry is substantially in manual operation.Due to manually-operated instability, cause material uneven, sugarcane enters squeezing amount shakiness etc., directly has influence on the control of sugarcane sucrose extraction, bagasse moisture content, pol and pressing quantity thereof, has influence on the technological parameter of subsequent handling and stablizing of product quality.In addition, sugared technique is boiled by Zhi Lian workshop section, especially unsolved hard nut to crack for many years.Boil at present experience that sugared technique relies on master craftsman substantially and control and to boil saccharic amount, cause unstable product quality.This project scheduling is in the integrated automatic control system of honest and just horse sugar refinery research and development sugar manufacturing process.This system task is respectively production runes at different levels to be optimized to control; Gather the status information of production run, the parameter information of apparatus, and carry out mutual and transmission up and down, production scene scheduling, decision-making and organization and administration are provided.Thereby solve manual operation and cause unstable product quality problem, reach the object of upgrading consumption reduction.
Utility model content
The purpose of this utility model, in order to solve existing technical disadvantages, provides a kind of uniform milling production run infiltration water control system.
For achieving the above object, the purpose of this utility model is to provide uniform milling production run infiltration water control system, comprise industrial computer, described industrial computer is connected with on-off value data acquisition card, analog data collection card, human-computer interaction module, switching value output module, analog output module, described analog data collection links and is connected to infrared moisture measuring tester, Cold water tap aperture table, hot-water valve aperture table, fluid level transmitter, temperature sensor, Electromagnetic Flow is taken into account frequency converter, described analog output module is connected with cold water electric operator, hot water electric operator and frequency converter.
Described switching value data amount capture card is connected with equipment operation monitoring signaling module, equipment failure signaling module, system operation signal module and automatic/hand handover module.
Described switching value output module is connected with fault acousto-optic alarm module and duty display module.
The utlity model has following beneficial effect: the utility model detects infiltration water temperature by temperature sensor, electromagnetic flowmeter detects permeate water flow, by industrial computer, receive permeate water flow and the temperature instruction of self scheduling or dispatching, by dispatch command and temperature detection signal comprehensive rear form hot water and the instruction of cold water control valve opening, regulate infiltration water temperature; After comprehensive by dispatch command, electromagnetic flowmeter signal, form frequency converter rotary speed instruction, in order to control infiltration water revolution speed, guarantee that infiltration water supplies with on demand.After No. five squeezers, IR Moisture Measurement Apparatus is set.Bagasse moisture is measured, measurement result is sent into the important parameter that Control Room is controlled as boiler combustion.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, to the accompanying drawing of required use in embodiment or description of the Prior Art be briefly described below, apparently, accompanying drawing in the following describes is only embodiment more of the present utility model, for those of ordinary skills, do not paying under the prerequisite of creative work, can also obtain according to these accompanying drawings other accompanying drawing.
Fig. 1 is structured flowchart of the present utility model.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is only the utility model part embodiment, rather than whole embodiment.Embodiment based in the utility model, those of ordinary skills are not making the every other embodiment obtaining under creative work prerequisite, all belong to the scope of the utility model protection.
Referring to Fig. 1, the purpose of this utility model is to provide uniform milling production run infiltration water control system, comprise industrial computer 1, described industrial computer 1 is connected with on-off value data acquisition card 2, analog data collection card 3, human-computer interaction module 4, switching value output module 5, analog output module 6, described analog data collection card 3 is connected with infrared moisture measuring tester 31, Cold water tap aperture table 32, hot-water valve aperture table 33, fluid level transmitter 34, temperature sensor 35, electromagnetic flowmeter 36 and frequency converter 37, described analog output module 6 is connected with cold water electric operator 61, hot water electric operator 62 and frequency converter 37.The utility model detects infiltration water temperature by temperature sensor, electromagnetic flowmeter detects permeate water flow, by industrial computer, receive permeate water flow and the temperature instruction of self scheduling or dispatching, by dispatch command and temperature detection signal comprehensive rear form hot water and the instruction of cold water control valve opening, regulate infiltration water temperature; After comprehensive by dispatch command, electromagnetic flowmeter signal, form frequency converter rotary speed instruction, in order to control infiltration water revolution speed, guarantee that infiltration water supplies with on demand.After No. five squeezers, IR Moisture Measurement Apparatus is set.Bagasse moisture is measured, measurement result is sent into the important parameter that Control Room is controlled as boiler combustion.
As the concrete embodiment of the utility model, described switching value data amount capture card 2 is connected with equipment operation monitoring signaling module 21, equipment failure signaling module 22, system operation signal module 23 and automatic/hand handover module 24.Described switching value output module 5 is connected with fault acousto-optic alarm module 51 and duty display module 52.
Height and the amount of seepage of squeezing sucrose extraction number in close relations.Increase amount of seepage, can improve sucrose extraction, but can make mixed juice hammer degree reduce simultaneously, during evaporation, quantity of steam increases, and squeezes roll row juice load simultaneously and increases the weight of.When amount of seepage is few, makes to squeeze sucrose extraction and reduce, economic benefit declines.Not proportional between amount of seepage and sucrose extraction.After amount of seepage is increased to a certain degree, then increase the water yield, the increase of gained sugar is very few.Domestic sugar refinery mostly adopts the amount of seepage of 14～20% pairs of sugarcane ratios.
It is a following control system that infiltration water interlock is controlled, and according to current pressing quantity thereof, system detects current amount of seepage by electromagnetic flowmeter, by the given instruction of amount of seepage, uses AC frequency conversion speed regulator to regulate the rotating speed of water pump, realizes the adjusting of amount of seepage.
The number that adds amount of seepage, by the fiber of sugarcane divide, daily squeezed quantity determines.The variation that should divide according to a fiber that squeezes sugarcane in season, daily squeezed quantity number and the addition of change infiltration water.Fiber divides when low, and the amount of seepage adding is few, and fiber divides when high, and the amount of seepage adding is many; When daily squeezed quantity is high, the amount of seepage adding is many.When daily squeezed quantity is low, the amount of seepage adding is few.To adding the control of amount of seepage, be according to one, to squeeze the change curve that in season, sugarcane fibre divides to set.
By sugarcane fibre, divide change curve, daily squeezed quantity, the best jointly to form the given instruction of amount of seepage to parameters such as sugarcane compare, the amount of seepage adding is controlled.After comprehensive by dispatch command, electromagnetic flowmeter signal, form frequency converter rotary speed instruction, in order to control infiltration water revolution speed, guarantee that infiltration water supplies with on demand.
Infiltration water temperature control aspect: infiltration water temperature should be controlled between 38～45 ℃, and excess Temperature can make sugarcane layer filament expansion, enters roller difficulty makes the non-sugar in mixed juice increase simultaneously, and purity declines.It is that the quantity delivered of adjusting hot water realizes by detecting infiltration water temperature variation through hot-water valve aperture table that infiltration water temperature is controlled.
System adopts temperature sensor to detect infiltration water temperature, and this detection signal is sent into PLC.PLC receives the instruction from dispatcher or dispatching simultaneously.After dispatch command and temperature detection signal are comprehensive in PLC, form the instruction of hot water control valve opening, regulate infiltration water temperature.
When bagasse moisture on-line is detected: infrared moisture measuring instrument is set after 5# crusher, bagasse moisture is carried out to on-line measurement.And can realize the demonstration of bagasse moisture trend.When bagasse moisture surpasses setting, system sends to operating personnel the signal that transfinites in time, reminds managerial personnel to adjust in time relevant dispatch command or equipment is carried out to necessary adjustment to guarantee the requirement of bagasse water satisfied boiler combustion.Bagasse moisture signal is carried out to the comprehensive rear rate signal that forms squeezer simultaneously.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (3)
1. uniform milling production run infiltration water control system, it is characterized in that: comprise industrial computer, described industrial computer is connected with on-off value data acquisition card, analog data collection card, human-computer interaction module, switching value output module, analog output module, described analog data collection links and is connected to infrared moisture measuring tester, Cold water tap aperture table, hot-water valve aperture table, fluid level transmitter, temperature sensor, Electromagnetic Flow and takes into account frequency converter, and described analog output module is connected with cold water electric operator, hot water electric operator and frequency converter.
2. uniform milling production run infiltration water control system according to claim 1, is characterized in that: described switching value data amount capture card is connected with equipment operation monitoring signaling module, equipment failure signaling module, system operation signal module and automatic/hand handover module.
3. uniform milling production run infiltration water control system according to claim 1, is characterized in that: described switching value output module is connected with fault acousto-optic alarm module and duty display module.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420194542.2U CN203799249U (en) | 2014-04-21 | 2014-04-21 | Control system used for balancing infiltration water in press production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420194542.2U CN203799249U (en) | 2014-04-21 | 2014-04-21 | Control system used for balancing infiltration water in press production process |
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| Publication Number | Publication Date |
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| CN203799249U true CN203799249U (en) | 2014-08-27 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420194542.2U Expired - Fee Related CN203799249U (en) | 2014-04-21 | 2014-04-21 | Control system used for balancing infiltration water in press production process |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103955184A (en) * | 2014-04-21 | 2014-07-30 | 昆明得一科技有限责任公司 | Infiltration water control system for balanced squeezing production process |
| CN106515081A (en) * | 2016-12-28 | 2017-03-22 | 钦州华成自控设备有限公司 | Online automatic control system and control method for permeation water of sugarcane pressing machine |
-
2014
- 2014-04-21 CN CN201420194542.2U patent/CN203799249U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103955184A (en) * | 2014-04-21 | 2014-07-30 | 昆明得一科技有限责任公司 | Infiltration water control system for balanced squeezing production process |
| CN106515081A (en) * | 2016-12-28 | 2017-03-22 | 钦州华成自控设备有限公司 | Online automatic control system and control method for permeation water of sugarcane pressing machine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140827 Termination date: 20150421 |
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| EXPY | Termination of patent right or utility model |