CN103488168A - Intermittent chemical device and performance real-time evaluation method and device of control loops of intermittent chemical device - Google Patents
Intermittent chemical device and performance real-time evaluation method and device of control loops of intermittent chemical device Download PDFInfo
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Abstract
The invention relates to an intermittent chemical device and a performance real-time evaluation method and device of control loops of the intermittent chemical device. The performance real-time evaluation method of the control loops of the intermittent chemical device comprises the steps that (1) the self-control state, a deviation value and a deviation set value of each control loop of the chemical device are obtained in real time; (2) a production cycle preset by an intermittent reaction is corrected, and the corrected production cycle serves as a calculation cycle; (3) the loop self-control rate of each control loop at the present time is calculated according to the self-control state and the calculation cycle of each control loop; (4) the loop stability rate of each control loop at the present time is calculated; (5) according to the loop self-control rate and the loop stability rate of each effective control loop in the control loops, device self-control rate statistical data and device stability rate statistical data of the chemical device are generated. The intermittent chemical device and the performance real-time evaluation method and device of the control loops of the intermittent chemical device overcome the defect that only a single control loop can be monitored and evaluated in the prior art.
Description
Technical field
The present invention relates to chemical field, particularly relate to a kind of batch-type chemical plant installations and control loop performance real-time estimating method thereof, device.
Background technology
Statistical study shows, in China's chemical production device, due to parameter tuning, unreasonable or controller problem is not operated in optimum condition in 30% loop at present, and 60% control loop need to carry out continuous monitoring and Performance Evaluation online.International best practices shows, the improvement in base control loop can make device capbility increase 2%-5%, and product yield improves 5%-10%, energy consumption decline 5%-15%, reduction in the numbers of seconds and unplanned parking 25%-50%.
The loop works condition monitoring of the most of chemical plant installations of China only limits to complete in DCS at present, limit by the DCS function, this monitoring only can be for single loop and is changed in short-term, can't completion system calculating and generate the dependent diagnostic report that Chemical Manufacture is had to whole directive significance.
For these reasons, a kind of real time and on line monitoring and evaluation method need to be provided, based on real-time data base, the performance of batch-type chemical production device control loop is assessed, to loop performance how, whether it is necessary or not regulates, have or not the problems such as nargin that may regulate and regulate that data results and solution are provided, purpose is to improve the economic benefit of control system.
Summary of the invention
The purpose of this invention is to provide and a kind ofly can be online the control loop duty of batch-type chemical production device be assessed to batch-type chemical plant installations production is carried out to real-time instruction and control loop performance real-time estimating method thereof, device.
For solving the problems of the technologies described above, as first aspect of the present invention, a kind of control loop performance real-time estimating method of batch-type chemical plant installations is provided, has comprised: step 1, the automatic control state of each control loop of Real-time Obtaining chemical plant installations, deviate and deviation setting value; Step 2, judge that chemical plant installations whether in Batch reaction processes, if so, is revised the default production cycle of this batch reaction, and using the revised production cycle as computation period; Step 3, according to automatic control state and the computation period of each control loop, calculate this each control loop in the loop of current time automatic control rate; Step 4, according to deviate and deviation setting value and the computation period of each control loop, calculate this each control loop at the loop of current time coefficient of stabilization; Step 5, according to loop automatic control rate and the loop coefficient of stabilization of each effective control loop in control loop, generate device automatic control rate statistics and the device coefficient of stabilization statistics of chemical plant installations.
Further, step 3 comprises: calculate the ratio of a certain control loop time in automatic control state and computation period in computation period, thereby obtain loop automatic control rate.
Further, step 4 comprises: calculate the deviation setting value of a certain control loop in computation period and be greater than the time of deviate and the ratio of computation period, thereby obtain the loop coefficient of stabilization.
Further, method also comprises the step of the control loop type that judges chemical plant installations; Step 3 specifically comprises: under the situation that is complex control loop in the control loop type, if when the major loop of complex control loop and subloop are auto state, make the automatic control state check point of complex control loop be set to auto state; The T.T. that in the calculating computation period, the automatic control state check point is auto state and the ratio of computation period, thus loop automatic control rate obtained.
Further, method also comprises the step of the control loop type that judges chemical plant installations; Step 4 specifically comprises: under the situation that is complex control loop in the control loop type, if the deviation setting value of the major loop of complex control loop is greater than the deviation setting value of deviate and subloop and is greater than deviate, make the steady state detection point of complex control loop be set to very; Calculate the ratio that steady state detection point in computation period is set to genuine T.T. and computation period, thereby obtain the loop coefficient of stabilization.
As second aspect of the present invention, a kind of control loop performance Real-Time Evaluation device of batch-type chemical plant installations is provided, comprising: acquisition module, for automatic control state, deviate and the deviation setting value of each control loop of Real-time Obtaining chemical plant installations; The cycle module, for judging that whether chemical plant installations is in Batch reaction processes, if so, revised the default production cycle of this batch reaction, and using the revised production cycle as computation period; The first computing module, for the automatic control state according to each control loop and computation period, calculate this each control loop in the loop of current time automatic control rate; The second computing module, for the deviate according to each control loop and deviation setting value and computation period, calculate this each control loop at the loop of current time coefficient of stabilization; Statistical module, for the loop automatic control rate according to each effective control loop of control loop and loop coefficient of stabilization, generate device automatic control rate statistics and the device coefficient of stabilization statistics of chemical plant installations.
Further, device also comprises: the loop judge module, for judging the control loop type of chemical plant installations; The first computing module comprises: the first setting module, for under the situation that is complex control loop in the control loop type, when if the major loop of complex control loop and subloop are auto state, make the automatic control state check point of complex control loop be set to auto state; With the first computing module, for calculating the ratio of T.T. that in computation period, the automatic control state check point is auto state and computation period, thereby obtain loop automatic control rate.
Further, device also comprises: the loop judge module, for judging the control loop type of chemical plant installations; The second computing module comprises: the second setting module, for under the situation that is complex control loop in the control loop type, if the deviation setting value of the major loop of complex control loop is greater than the deviation setting value of deviate and subloop and is greater than deviate, make the steady state detection point of complex control loop be set to very; With the second computing module, be set to the ratio of genuine T.T. and computation period for calculating steady state detection point in computation period, thereby obtain the loop coefficient of stabilization.
As the 3rd aspect of the present invention, a kind of batch-type chemical plant installations is provided, comprise above-mentioned control loop performance Real-Time Evaluation device.
The present invention can carry out real-time, significant monitoring and assessment to the duty of chemical industry batch production process control loop, thereby can pinpoint the problems the very first time, avoids the production efficiency caused because control loop work is not good to descend, even install unplanned parking.
The accompanying drawing explanation
Fig. 1 has schematically shown the process flow diagram of the control loop performance real-time estimating method of the batch-type chemical plant installations in the present invention;
Fig. 2 has schematically shown the process flow diagram of the present invention when complicated loop;
Fig. 3 has schematically shown the calculation flow chart of loop automatic control rate; And
Fig. 4 has schematically shown the calculation flow chart of loop coefficient of stabilization.
Embodiment
Below embodiments of the invention are elaborated, but the multitude of different ways that the present invention can be defined by the claims and cover is implemented.
The present invention is based on the work state information of batch-type chemical plant installations real time execution, at first, judge that chemical plant installations is whether under normal driving state; The second, obtain real-time working state, deviate and the deviation setting value of each control loop of chemical plant installations; The 3rd, status information based on the chemical plant installations real time execution, judge that chemical plant installations is whether in certain batch products Batch reaction processes, if in Batch reaction processes, upgrade computation period, preferably, this computation period is to adjust production cycle of setting in advance according to this batch reaction to obtain, for example, can be the difference of this production cycle and batch reaction time.Like this, just can be according to the difference of control loop type (for example, single loop and complicated loop), real-time calculated performance evaluation index in the computation period of setting, in a whole set of chemical plant installations, the Performance Evaluating Indexes of all control loops is all after line computation, obtain rate and the stable working rate for automatic switching of the control loop of current time chemical plant installations, thereby the duty of chemical industry batch production process control loop is carried out to real-time, significant monitoring and assessment.
As a first aspect of the present invention, please refer to Fig. 1 and Fig. 2, a kind of control loop performance real-time estimating method of batch-type chemical plant installations is provided, has comprised: step 1, the automatic control state of each control loop of Real-time Obtaining chemical plant installations (non-manual state of a control), deviate and deviation setting value; Step 2, judge that chemical plant installations whether in Batch reaction processes, if so, is revised the default production cycle of this batch reaction, and using the revised production cycle as computation period; Step 3, according to automatic control state and the computation period of each control loop, calculate this each control loop in the loop of current time automatic control rate; Step 4, according to deviate and deviation setting value and the computation period of each control loop, calculate this each control loop at the loop of current time coefficient of stabilization; Step 5, according to loop automatic control rate and the loop coefficient of stabilization of each effective control loop in control loop, generate device automatic control rate statistics and the device coefficient of stabilization statistics of chemical plant installations.
In Batch reaction processes, can be set for a certain batch products that this batch reaction is produced a production cycle.In addition, owing to being batch reaction, thereby, have the batch reaction time.Like this, just can calculate the actual reaction time by production cycle and batch reaction time, namely the corresponding time of said computation period in this patent.
Like this, just, can obtain the automatic control rate according to the time in automatic control state of each control loop in computation period; Further, can also obtain the time of loop in plateau according to deviate and deviation setting value, thereby obtain coefficient of stabilization.
After the automatic control rate that obtains each control loop and coefficient of stabilization, just can obtain the integral self-control rate of whole chemical plant installations in section sometime and the statistics of coefficient of stabilization (such as form etc.), for example, this time can be every day, wait weekly or per month.
Visible, utilize the present invention to be monitored and to estimate each control loop of chemical plant installations with complex control loop, thereby overcome the defect that only can be monitored and estimate a certain single control loop in the prior art.Further, the present invention can also be added up automatic control rate and coefficient of stabilization in the long period section easily, further, these statisticss can also be shown, for operating personnel with reference to use.
The present invention can carry out real-time, significant monitoring and assessment to the duty of chemical industry batch production process control loop, thereby can pinpoint the problems the very first time, avoids the production efficiency caused because control loop work is not good to descend, even install unplanned parking.
Preferably, in one embodiment, step 3 comprises: calculate the ratio of a certain control loop time in automatic control state and computation period in computation period, thereby obtain loop automatic control rate.Obviously, those skilled in the art also can adopt other mode be equal to, and carry out counter circuit automatic control rate, are not limited to the mode described in the present invention.
Preferably, in one embodiment, step 4 comprises: calculate the deviation setting value of a certain control loop in computation period and be greater than the time of deviate and the ratio of computation period, thereby obtain the loop coefficient of stabilization.Obviously, those skilled in the art also can adopt other mode be equal to, and carry out the counter circuit coefficient of stabilization, are not limited to the mode described in the present invention.
Preferably, this method also comprises the step of the control loop type that judges chemical plant installations.By this step, can judge this chemical plant installations is single control loop processed or complex control loop.
Preferably, in another embodiment, please refer to Fig. 3, step 3 specifically comprises: under the situation that is complex control loop in the control loop type, when if the major loop of complex control loop and subloop are auto state, make the automatic control state check point of complex control loop be set to auto state; The T.T. that in the calculating computation period, the automatic control state check point is auto state and the ratio of computation period, thus loop automatic control rate obtained.
Preferably, in another embodiment, please refer to Fig. 4, step 4 specifically comprises: under the situation that is complex control loop in the control loop type, if the deviation setting value of the major loop of complex control loop is greater than the deviation setting value of deviate and subloop and is greater than deviate, make the steady state detection point of complex control loop be set to very; Calculate the ratio that steady state detection point in computation period is set to genuine T.T. and computation period, thereby obtain the loop coefficient of stabilization.
In a preferred embodiment, before step 1, also comprise: obtain chemical plant installations real-time running state information, and judge that according to this information whether chemical plant installations is in normal driving state; When in normal driving state, perform step 1 and subsequent step.
As a second aspect of the present invention, a kind of control loop performance Real-Time Evaluation device of batch-type chemical plant installations is provided, comprising: acquisition module, for automatic control state, deviate and the deviation setting value of each control loop of Real-time Obtaining chemical plant installations; The cycle module, for judging that whether chemical plant installations is in Batch reaction processes, if so, revised the default production cycle of this batch reaction, and using the revised production cycle as computation period; The first computing module, for the automatic control state according to each control loop and computation period, calculate this each control loop in the loop of current time automatic control rate; The second computing module, for the deviate according to each control loop and deviation setting value and computation period, calculate this each control loop at the loop of current time coefficient of stabilization; Statistical module, for the loop automatic control rate according to each effective control loop of control loop and loop coefficient of stabilization, generate device automatic control rate statistics and the device coefficient of stabilization statistics of chemical plant installations.
Preferably, this device also comprises: the loop judge module, for judging the control loop type of chemical plant installations; The first computing module comprises: the first setting module, for under the situation that is complex control loop in the control loop type, when if the major loop of complex control loop and subloop are auto state, make the automatic control state check point of complex control loop be set to auto state; With the first computing module, for calculating the ratio of T.T. that in computation period, the automatic control state check point is auto state and computation period, thereby obtain loop automatic control rate.
Preferably, this device also comprises: the loop judge module, for judging the control loop type of chemical plant installations; The second computing module comprises: the second setting module, for under the situation that is complex control loop in the control loop type, if the deviation setting value of the major loop of complex control loop is greater than the deviation setting value of deviate and subloop and is greater than deviate, make the steady state detection point of complex control loop be set to very; With the second computing module, be set to the ratio of genuine T.T. and computation period for calculating steady state detection point in computation period, thereby obtain the loop coefficient of stabilization.
Preferably, this device also comprises: correcting unit, install effective control loop sum, the benchmark automatic control rate of control loop and the steady rate of benchmark of control loop for adjusting this.
Preferably, this device also comprises: alarm unit, and the minimum (benchmark automatic control rate, the steady rate of benchmark) whether normally moved lower than this device of assurance for the device automatic control rate and the steady rate of device that judge this device, and in the situation that lower than sending warning message.
Those skilled in the art will also understand is that, in conjunction with the described various illustrative logical blocks of disclosure herein, unit, circuit and algorithm steps, may be implemented as electronic hardware, computer software or both combinations.For this interchangeability of hardware and software clearly is described, with regard to the function of various exemplary components, square, unit, circuit and step, it has been carried out to general description.This function is implemented as software or is implemented as hardware and depends on concrete application and the design constraint that imposes on whole system.Those skilled in the art can realize described function in every way for every kind of concrete application, but this realization determines should not be interpreted as causing departing from the scope of the present invention.
As a third aspect of the present invention, a kind of batch-type chemical plant installations is provided, comprise above-mentioned control loop performance Real-Time Evaluation device.
For example, the present invention can be in real-time dataBase system, the obtaining and storing of Interface realization Real-Time Evaluation device start-stop car judgement symbol, control loop type, control loop duty, control loop deviate and control loop deviation setting value by itself and DCS control module, realize that by the real-time dataBase system computing unit batch-type chemical production device control loop performance Real-Time Evaluation index calculates.Thereby realize dynamically showing index and warning by form.
Further, also can in real-time dataBase system, realize automatic calibration, like this, after the effective control loop number of chemical plant installations, benchmark automatic control rate and the steady rate of benchmark change according to the production actual conditions, can in real-time dataBase system, the value based on new make consistent adjustment.
The present invention is based on the status information judgment means of device real time execution under normal driving state, obtain control loop real-time working state, deviate and deviation setting Value Data, whether the status information judgment means based on the device real time execution is in certain batch products Batch reaction processes, upgrade computation period, according to loop dissimilar (single control loop processed and complex control loop) real-time calculated performance evaluation index in computation period, in a whole set of process units, all control loop Performance Evaluating Indexes are all after line computation, obtain rate and the stable working rate for automatic switching of current time chemical plant installations control loop.
The present invention can carry out real-time, significant monitoring and assessment to the duty of chemical industry batch production process control loop, thereby can pinpoint the problems the very first time, avoids the production efficiency caused because control loop work is not good to descend, even install unplanned parking.
The foregoing is only the preferred embodiments of the present invention, be not limited to the present invention, for a person skilled in the art, the present invention can have various modifications and variations.Within the spirit and principles in the present invention all, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection scope of the present invention.
Claims (9)
1. the control loop performance real-time estimating method of a batch-type chemical plant installations, is characterized in that, comprising:
Step 1, the automatic control state of each control loop of the described chemical plant installations of Real-time Obtaining, deviate and deviation setting value;
Step 2, judge that described chemical plant installations whether in Batch reaction processes, if so, is revised the default production cycle of this batch reaction, and using the revised production cycle as computation period;
Step 3, according to automatic control state and the described computation period of each described control loop, calculate this each described control loop in the loop of current time automatic control rate;
Step 4, according to deviate and deviation setting value and the described computation period of each described control loop, calculate this each described control loop at the loop of current time coefficient of stabilization;
Step 5, according to loop automatic control rate and the loop coefficient of stabilization of each effective control loop in described control loop, generate device automatic control rate statistics and the device coefficient of stabilization statistics of described chemical plant installations.
2. method according to claim 1, is characterized in that, step 3 comprises:
Calculate the ratio of a certain described control loop time in automatic control state and described computation period in described computation period, thereby obtain described loop automatic control rate.
3. method according to claim 1, is characterized in that, step 4 comprises:
Calculate the deviation setting value of a certain described control loop in described computation period and be greater than the time of deviate and the ratio of described computation period, thereby obtain described loop coefficient of stabilization.
4. method according to claim 1, is characterized in that, described method also comprises the step of the control loop type that judges described chemical plant installations;
Step 3 specifically comprises:
Under the situation that is complex control loop in described control loop type, if when the major loop of described complex control loop and subloop are auto state, make the automatic control state check point of described complex control loop be set to auto state;
Calculate the ratio of described automatic control state check point is auto state in described computation period T.T. and described computation period, thereby obtain described loop automatic control rate.
5. method according to claim 1, is characterized in that, described method also comprises the step of the control loop type that judges described chemical plant installations;
Step 4 specifically comprises:
Under the situation that is complex control loop in described control loop type, if the deviation setting value of the major loop of described complex control loop is greater than the deviation setting value of deviate and subloop and is greater than deviate, make the steady state detection point of described complex control loop be set to very;
Calculate the ratio that described steady state detection point in described computation period is set to genuine T.T. and described computation period, thereby obtain described loop coefficient of stabilization.
6. the control loop performance Real-Time Evaluation device of a batch-type chemical plant installations, is characterized in that, comprising:
Acquisition module, for automatic control state, deviate and the deviation setting value of each control loop of the described chemical plant installations of Real-time Obtaining;
The cycle module, for judging that whether described chemical plant installations is in Batch reaction processes, if so, revised the default production cycle of this batch reaction, and using the revised production cycle as computation period;
The first computing module, for the automatic control state according to each described control loop and described computation period, calculate this each described control loop in the loop of current time automatic control rate;
The second computing module, for the deviate according to each described control loop and deviation setting value and described computation period, calculate this each described control loop at the loop of current time coefficient of stabilization;
Statistical module, for the loop automatic control rate according to described each effective control loop of control loop and loop coefficient of stabilization, generate device automatic control rate statistics and the device coefficient of stabilization statistics of described chemical plant installations.
7. device according to claim 6, is characterized in that, described device also comprises: the loop judge module, for judging the control loop type of described chemical plant installations;
Described the first computing module comprises:
The first setting module, for under the situation that is complex control loop in described control loop type, when if the major loop of described complex control loop and subloop are auto state, make the automatic control state check point of described complex control loop be set to auto state; With
The first computing module, for calculating the ratio of T.T. that in described computation period, described automatic control state check point is auto state and described computation period, thereby obtain described loop automatic control rate.
8. device according to claim 6, is characterized in that, described device also comprises: the loop judge module, for judging the control loop type of described chemical plant installations;
Described the second computing module comprises:
The second setting module, for under the situation that is complex control loop in described control loop type, if the deviation setting value of the major loop of described complex control loop is greater than the deviation setting value of deviate and subloop and is greater than deviate, make the steady state detection point of described complex control loop be set to very; With
The second computing module, be set to the ratio of genuine T.T. and described computation period, thereby obtain described loop coefficient of stabilization for calculating described steady state detection point in described computation period.
9. a batch-type chemical plant installations, is characterized in that, comprises the described control loop performance of any one Real-Time Evaluation device in claim 6 to 8.
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| CN105527837A (en) * | 2015-12-22 | 2016-04-27 | 蓝星（北京）技术中心有限公司 | Chemical production device control loop parameter setting test method and device |
| CN107942675A (en) * | 2017-12-13 | 2018-04-20 | 杭州电子科技大学 | A kind of Chemical Batch Process stability of control system keeping method |
| CN112083704A (en) * | 2019-06-12 | 2020-12-15 | 中国石油化工股份有限公司 | Chemical plant control loop performance quantitative evaluation method and machine readable storage medium |
| CN111983997A (en) * | 2020-08-31 | 2020-11-24 | 北京清大华亿科技有限公司 | Coupling analysis-based control loop performance monitoring method and system |
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