METHOD AND CONTROL SYSTEM OF CONTROLLING A FLUID COMPRESSION SYSTEM

Abstract: The invention relates to a method of controlling a fluid compression system, said compression system comprising at least one compression means (1) for compressing a fluid medium, means for taking said compressed medium to a point of demand (9) and at least one means for conditioning said fluid medium prior to the point of demand (9). According to the method, the permissible minimum (P3min) and maximum (P3max) values of the user line pressure (P3) at the point of demand (9) are defined, the user line pressure (P3) is continuously monitored with the help of a pressure sensor (16), the working pressure (P2) of said compression means is monitored, the pressure difference between the working pressure (P2) of said compression means (1) and the user line pressure (P3) at the point of demand (9) is monitored, the pressure rate-of-change of the fluid medium delivered to the point of demand (9) is monitored, and at least one of the compression means (1) is controlled with the help of a control unit (12) on the basis of at least one of the monitored parameters defined in the foregoing steps of the method.

Description: /16271 .Method and control system of controlling a fluid compression system The present invention relates to a method according to claim 1 for controlling a fluid compression system. The invention also concerns a control system suited for controlling a fluid compression system. In conventional compression systems of a fluid medium, particularly compressed-air systems, the outlet pressure of the compressor is sensed, and this information is used to control the compressor operation with the help of a pressostat placed immediately at the compressor outlet. In compressor models equipped with a no-load unloading facility, the duration of the unloaded no-load running mode can be controlled by an adjustable timer. The set time is always constant until changed manually. Such control schemes are not capable of taking into account pressure losses caused by air consuming equipment attached to the system and variations in compressed air demand. Pressure loss occurring in the equipment is entirely dependent on instantaneous air flow rate and pressure. These variables may change extremely strongly within a short interval of time. Moreover, the pressure loss caused by filters on the compressed-air line is dependent on the degree of clogging of the filters. As new the filter causes a low pressure loss which increases with the clogging of the filter when it binds impurities from the through-flowing air. When sufficiently clogged, the filter element is replaced, whereby the pressure loss is again reduced to a low level. To the user of compressed-air system it is extremely important that proper pressure level for the compressed-air operated equipment is ensured at the point of demand. A disadvantage of prior-art equipment is, i.a., that they require the compressor working pressure to be set to an unnecessarily high level due to the incapability of such equipment to compensate for the pressure losses caused by the above-mentioned accessories or devices. Resultingly, the energy consumption of the compressed-air system is unnecessarily high. Moreover, for compressors operated with period of unloaded postrunning mode, the duration of the postrunning mode is set according to the rule that the frequency of compressor starts may not exceed the maximum frequency of starts specified for the drive motor. This duration of the postrunning mode is fixed and unrelated to variations in compressed-air demand, thus permitting the compressor to run unloaded for the preset duration of the postrunning mode even during time of no compressed air demand. In this case unnecessary energy losses occur. Also in conjunction with compressed-air systems having two or more compressors, control systems based on conventional techniques cause superfluous energy consumption. Very com¬ monly a pressure swing of small amplitude or short duration starts the second or the other compressors even when no extra air would actually be required. Further, if the com¬ pressor is operated using an unloaded no-load running mode, the proportion of useless energy consumption may rise up to about 40 % of the nominal electrical input rating of the compressor yet producing no air to the compressed-air network. Energy consumption in conventional compressed-air systems is on the average more than 30 % greater than the theoreti- cal minimum due to the following reasons: - To fulfill the pressure requirements of the user equip¬ ment also under varying conditions of air demand, the compressor working pressure must be set significantly higher than the average pressure demand. - The compressor operating control system by no means takes into account the effect of the amount of air demand and the degree of filter contamination on pressure losses occurring in compressed-air circuit. - The duration of the postrunning mode of the compressor intended to protect the drive motor is constant thus failing to adjust the actually needed duration of the postrunning mode according to the variations in air demand. - Multiple compressor systems are unnecessarily sensitive to trigger entirely useless compressor starts which are caused by the delay from the compressor start to the instant of effective compressed air production. It is an object of the present invention to achieve an entirely novel control method and control system for a fluid compression system, whereby the drawbacks of the prior art are overcome. The invention is characterized by what is stated in the appended claims. The embodiment provides several significant benefits. Savings in excess of 30 % over conventional techniques will be achieved in the energy consumption of compressed-air production. The control scheme according to the invention provides continuous and automatic control of compressor operation in a manner that minimizes energy consumption. In multiple compressor systems the control scheme according to the invention stops and starts the compressors automatical¬ ly and in an anticipatory manner so as to keep the pressure level at the point of air demand within predetermined limits and to prevent exceeding the maximum starting frequency permitted for the drive motors of the compres¬ sors. The user line pressure can be maintained within pre¬ determined limits also under varying rates of air demand. while unnecessary running of the compressors is avoided. The control scheme according to the invention is easily adjustable to comply with local operating conditions. The system reacts immediately to changes in compressed air demand. The control system according to the invention is also capable of compensating for slow changes in pressure losses due to clogging of filters, for example. The invention is well suited for use in different kind of environments. It can be adapted to single as well as multiple compressor systems. In can be used in conjunction with the most common air compressor types and other fluid compression means. Further, it may be installed in both new and old compressed-air systems. The control system according to the invention comprises a modest number of components and its installation is straightforward. Connections to the compressed-air system are limited to two pressure sensors and an electrical connection to the existing control system of the compressor(s) . In the following the invention will be examined in greater detail with reference to the attached drawings, in which Figure 1 is a schematic representation of the system configuration according to the invention; Figure 2 is a graph illustrating the working pressure of the compressor measured at air receiver 3 of Fig. 1; and Figure 3 is a graph illustrating the user site pressure measured at air receiver 8 of Fig. 1. With reference to Fig. 1, a compressed-air system equipped with the control system according to the invention is shown. Connected to a compressor 1 in the system is a cooler 2 and an air receiver 3, or alternatively, an expanded section of the pressure line or equivalent air storage. These elements are followed by a post-conditioning outfit 4, 5, 6, 7. Depending on the system configuration, the post-conditioning outfit includes different kinds of accessories. With reference to Fig. 2, the post-condition- ing accessories include filters 4, 5 equipped with water separators, a dryer 6 and a filter 7. The post-conditioning outfit in the piping is followed by a second air receiver 8 from which air is taken to a point of demand 9. The control system of the compressor 1 comprises a control unit 12 and two pressure sensors 15, 16, of which the first pressure sensor 15 is placed to the first air receiver 3 preceding the post-conditioning outfit 4, 5, 6, 7 and the second pressure sensor 16 is placed to the second air receiver 8 following the post-conditioning outfit. Additionally, the control system includes cabling 10, 11 connecting the control unit 12 to the pressure sensors 15, 16 as well as cabling 13 connecting the control unit 12 to the local operating control system 14 of the compressor 1. Obviously, such cabling may be replaced by any suitable signal transmission means. The control unit 12 advantageously comprises a programmable logic controller or similar centralized control means with required accessories and connectors, as well as compressor selector switches implemented in a conventional manner for the manual operation and operating status monitoring of the compressors, indicator lamps, pushbuttons, connections for remote supervision and external display panels, etc. The programming of the logic controller in the control unit 12 is most appropriately performed using a separate program¬ ming device suited for storing in the programmable logic controller the basic data of the compressed air system such as the total volume of air receivers in the circuit, desired pressure level P 3 after the post-conditioning outfit, maximum permissible starting frequency for the drive motor, permissible pressure limits and other informa¬ tion necessary for the function of the control system. In the method according to the invention, the pressure of compressed air delivered to the point of demand 9 is allowed to vary between a permissible minimum pressure p 3 min nd permissible maximum pressure P 3max (whereby the maximum pressure P 3max = minimum permissible pressure P 3min + maximum permissible pressure deviation). The pressure P 3 delivered to the point of demand is monitored by means of the pressure sensor 16. The pressure loss between the first air receiver 3 and the second air receiver 8 due to the outfit 4, 5, 6, 7 connected between them is dependent on the air flow rate, degree of filter clogging and the pressure prevailing in these elements. In practice the pressure measured by means of the pressure sensor 15 is equal to the working pressure P 2 of the compressor. This pressure may be any level between the minimum pressure p 2m i n and a maximum pressure P 2max permitted for the operation of the compressor. When the pressure P 3 measured by means of the pressure sensor 16 reaches either the preset minimum pressure P 3min or the preset maximum pressure P 3max , the control unit 12 controls the working pressure P 2 of the compressor according to rules expressed below in preset pressure steps either higher or lower depending on which pressure limit is reached and how the post-conditioning accessories between the receivers 3 and 8 affect the pressure level. The rate-of-change (rate-of-rise or rate-of-fall) of compressed air pressure delivered to the point of demand 9 is monitored continuously. The signal for the rate-of- change monitoring is most conveniently obtained from the pressure sensor 15, whereby also the effect of the post- conditioning outfit placed on the pipe between the receivers 3 and 8 is taken into account. When the compressor 1 is running in the unloaded mode and the pressure rate-of-fall is slow, or alternatively, when the pressure is rising and the permissible starting frequency of the compressor drive motor is not exceeded, compressor 1 is stopped immediately. Fast rate-of-fall of the pressure P 3 causes removal of unloading or start of a compressor before the preset lower pressure limit P 3mj . n is attained. Compressor unloading/stop/start steps are predictively con¬ trolled on the basis of pressure rate-of-rise or rate-of- fall. In systems of two or more compressors, only a single permissible pressure range from P 3min to P 3max need to be preset from the point of demand 9, after which the start/ unloading/unloaded postrunning/stop modes of the compressors are controlled on the basis of the pressure rate-of-rise or rate-of-fall detected with the help of the pressure sensor 15. The control scheme according to the invention avoids exceeding the maximum permissible start frequency specified for the drive motors of the compressors. At the onset of a possible equipment malfunction, the local control system 14 of any compressor 1 can overtake the control. The working pressure P 2 of the compressor is always kept at the lowest possible level which can maintain the pressure P 3 at the point of demand within the preset limits. In compressed air systems of multiple compressors, only the minimum number of compressors is run loaded. The method according to the invention optimizes energy consumption in a system of arbitrary number of compressors. The system energy consumption will be the lowest possible under varying conditions of compressed air demand. In the following the details of the invention are elucidat¬ ed with reference to Figs. 2 and 3. Pressure P 3 at the point of demand 9 and its permissible limits P 3πιax and P 3min are shown in Fig. 3. The working pressure P 2 of the com- pressor 1 is dependent on the instantaneous air demand situation due to the fact that the accessories 4-7 cause a pressure loss which further is dependent on the dimension¬ ing of the accessories, instantaneous air flow rate, degree of contamination, pressure and temperature prevailing in the accessories and possible internal air consumption (particularly in adsorption dryers). Consequently, the compressor working pressure P 2 varies continuously. The level of the compressor working pressure P 2 may be affected by increasing or decreasing the compressed air delivery rate. Such changes of delivery capacity can be effected by unloading the compressor(s) , stopping the compressor(s) or removing compressor unloading and starting a compressor. The working pressure P 2 of the compressor is not constant herein, but rather, always as low as possible, whereby the lowest possible energy consumption is achieved. The control unit 12 does not primarily monitor the absolute value of the pressure P 2 , but only the changes of the pressure level. With reference to Figs. 2 and 3, a graph is shown illus¬ trating the different operating situations and the function of the invention under different pressure change situa¬ tions. When air consumption at the point of demand 9 begins to increase, a pressure fall P 32 occurs in the line pressure. The pressure sensor 16 signals the pressure fall to the control unit 12 and the control unit aims to control an increase in the working pressure P 2 . Simultaneously, the resulting increase in the flow rate through the accessories 4-7 causes a higher pressure drop which requires a further increase in the working pressure P 2 . If no increase is detected in the working pressure P 2 , the control unit 12 finds the air delivery capacity insufficient and removes unloading of the compressor 1 or starts the next compressor to increase the delivery capacity. An increase in air delivery capacity results in an increase in the working pressure P 2 (indicated by pressure phase P 21 in Fig. 2). With the increase in the flow rate, also the pressure drop through the accessories 4-7 increases. In maintaining a balance between the delivery and demand of compressed air, the line pressure P 3 (indicated by pressure phase P 31 in Fig. 3) varies between the limits P 3min and P 3max . Then, the compressors are run under steady-state conditions. At a very rapid fall of the line pressure P 3 (indicated by pressure phase P 32 in Fig. 3), the control unit 12 computes from the rate-of-change of the working pressure P 2 (indi¬ cated by pressure phase P 22 in Fig. 2) the instant when line pressure will fall below the minimum permissible pressure P 3m n , and to anticipate this, removes unloading of the compressor 1 or starts the next compressor in advance so that the starting delays of the compressors or removal delays of unloading will not result in line pressure drop below the lower limit P 3mj . n . The control unit contains data of starting and unloading removal delays of the compressors, and the stored compressor delivery capacity data can be complemented with information on receiver capacity. When air consumption at the point of demand 9 begins to de¬ crease and the compressor(s) is/are still running, the line pressure P 3 (indicated by pressure rise P 33 in Fig. 3) begins to rise. The pressure sensor 16 signals the rise of the pressure P 3 to the control unit, and as the line pressure tends to approach the preset permissible upper limit P 3max , the control unit 12 aims to control a decrease in the working pressure P 2 (resulting in a pressure fall P 23 in Fig. 2) . To accomplish this, the control unit con¬ trols the compressor to run unloaded or stops the com¬ pressor(s) in a preset sequence until such an equilibrium state is attained that keeps the line pressure P 3 within the preset limits (indicated by pressure P 31 in Fig. 3). If the air consumption at the point of demand 9 is very small and the line pressure P 3 has already reached the upper limit P 3max and the compressor(s) has/have controlled to run unloaded, the control program computes on the basis of the stored basic data the instant at which the line pressure P 3 (P 3 in Fig. 3) or the compressor working pressure P 2 (P 24 in Fig. 2) will fall to the permissible minimum pressure P 3m i n . If this pressure fall time is found to become longer than the minimum stop time permitted by the highest permissible starting frequency of the compressor drive motor, the control unit 12 stops the compressor immediately and thus saves energy by avoiding unnecessary no-load running of the compressor. If the compressor working pressure P 2 monitored with the help of the pressure sensor 15 rises up to its upper permissible limit P 2max , no more compressor(s) will be started by the control unit 12 notwithstanding the possibility that the user line pressure P 3 would be at its lower permissible limit, but instead the control unit issues an alarm of working pressure upper limit violation and/or simultaneously stops/unloads the compressor(s) presently running. This function is a safety measure protecting the compressor(s) from overload. In the case the compressor working pressure P 2 monitored with the help of the pressure sensor 15 falls to its lower permissible limit P m j_ n , depending on the conditions the control unit 12 may issue an alarm of exceeded capacity of the compressor(s) . In the case a malfunction of the control unit 12 occurs and the compressor working pressure P 2 exceeds its upper per¬ missible limit P 2max , system control will be directly transferred to the local control unit 14 of the compressor 1 which is adjusted to keep the working pressure of the compressor marginally above P 2max . Also this function is a safety measure. All the foregoing functions occur automatically in the above-described or any arbitrary sequence as required by the air consumption at the point of demand 9 and the compressor working pressure P 2 which directly control the functions. Because the air consumption at the point of demand 9 and the running status of the compressor 1 directly affect the user line pressure which is monitored immediately after the post-conditioning accessories 4-7 with the help of the pressure sensor 16, the above- described control method makes it possible to minimize energy consumption by keeping the user line pressure P 3 close to its permissible minimum value and by anticipating the required unloadings and starts/stops of the compressors and by allowing the compressor working pressure P 2 to freely float at the level required by the instantaneous demand of compressed air and prevailing operational conditions of the equipment. The control unit 12 can be linked by conventional means to a remote supervisory system of the compressor station. Further, the control system can be integrated as a part of the local control equipment of the compressor, or alternatively, it can be designed to replace conventionally employed control systems of compressors. In compressor installations of two or more compressors, the control unit can be programmed to automatically select the compressor optimally suited to produce compressed air under the instantaneous operating situation. To those versed in the art it is obvious that the invention is not limited by the exemplifying embodiments described above, but rather, can be varied within the scope of the invention defined in the appended claims.

Claims: Claims : 1. A method of controlling a fluid compression system, said compression system comprising at least one compression means (1) for compressing a fluid medium, means for taking said compressed medium to a point of demand (9) and at least one means for conditioning said fluid medium prior to the point of demand (9), c h a r a c t e r i z e d in that the method comprises - defining the permissible minimum (P 3m i n ) and maximum (P 3max ) values of the user line pressure (P 3 ) at the point of demand (9) , - continuously monitoring the user line pressure (P 3 ) with the help of a pressure sensor (16), - monitoring the working pressure (P 2 ) of said compression means, - monitoring the pressure difference between the working pressure (P 2 ) of said compression means (1) and the user line pressure (P 3 ) at the point of demand (9), - monitoring the pressure rate-of-change of the fluid medium delivered to the point of demand (9) , and - controlling at least one of the compression means (1) with the help of a control unit (12) on the basis of at least one of the monitored parameters defined in the foregoing steps of the method. 2. A method as defined in claim 1, c h a r a c t e r ¬ i z e d in that the working pressure (P 2 ) of said com¬ pression means (1) is controlled, advantageously in preset steps, to a higher or lower value when the user line pressure (P 3 ) at the point of demand reaches a preset lower limit (P 3min ) or upper limit (P 3max ), respectively. 3. A method as defined in claim 1, c h a r a c t e r - i z e d in that said compression means (1) is controlled, advantageously in an anticipatory manner, by controlling at least one of said compression means (1) by virtue of stopping or starting said means, or alternatively, setting said compression means (1) to the unloaded running mode or the unloaded postrunning mode. 4. A method as defined in any foregoing claim 1 - 3, c h a r a c t e r i z e d in that said compression means (1) is controlled in a manner that keeps the working pressure (P 2 ) of the means at the lowest possible level which still can maintain the user line pressure (P 3 ) at the point of demand (9) within the preset permissible limits. 5. A method as defined in any foregoing claim 1 - 4, c h a r a c t e r i z e d in that besides the basic parameters other parameters are defined including at least the volumes of air receivers in the compressed air circuit, maximum permissible starting frequency for the drive motor of the compression means and permissible pressure limits. 6. A method as defined in any foregoing claim 1 - 5, c h a r a c t e r i z e d in that in systems of multiple compression means (1) only a single pressure range (P 3min - P 3max ) is defined and the running mode of said compression means is controlled by the control unit (12) on the basis of pressure rate-of-change detected with the help of a pressure sensor (15). 7. A control system for controlling a fluid compression system, said compression system comprising at least one compression means (1) for compressing a fluid medium, means for taking said compressed medium to a point of demand (9) and at least one means for conditioning said fluid medium prior to the point of demand (9), c h a r a c t e r ¬ i z e d in that in the control system a first sensor means (15) is adapted to sense the status of the flowing medium prior to the post-conditioning means (4, 5, 6, 7) and that a second sensor means (16) is adapted to sense the status of the flowing medium after the post-conditioning means (4, 5, 6, 7) by way of arranging signal transmission means (10, 11) between said sensor means (15, 16) and said control unit (12), said control unit (12) being connected to an operating control system (14) of said compression means (1) . 8. A control system as defined in claim 7, c h a r a c ¬ t e r i z e d in that said first sensor means (15) is adapted to a first air receiver (3) or similar compressed air storage space and said second sensor means (16) is adapted to a second air receiver (8) or similar compressed air storage space. 9. A control system as defined in claim 7 or 8, c h a r - a c t e r i z e d in that said sensor means (15, 16) are pressure sensors. 10. A control system as defined in any foregoing claim 7 - 9, c h a r a c t e r i z e d in that said control unit (12) comprises a programmable logic controller or similar centralized control unit.

Inventors: HALLIKAINEN KEIJO, HALLIKAINEN, KEIJO
Applicants: HALLIKAINEN KEIJO, SARLIN HYDOR OY, HALLIKAINEN, KEIJO, SARLIN-HYDOR OY
Application year: 1995
Main classification: F04B49
IPC codes: B60T17, F04B41, F04B49, F04C14