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Production area environmental control device

Production area environmental control device
IPC classes for russian patent Production area environmental control device (RU 2363031):
Another patents in same IPC classes:
Automated method of controlling and managing process for preparing sugar syrup mixture for crystallisation by cooling Automated method of controlling and managing process for preparing sugar syrup mixture for crystallisation by cooling / 2342438
Proposed automated method of controlling and managing the process of preparing sugar syrup mixture for crystallisation by cooling makes provisions for regulating the volumetric discharge of water entering the mixer and the level of sugar syrup in it. Regulating the level of the sugar syrup in the vertical mould is achieved by acting on the adjustable-frequency electric drive of the sugar syrup pump. Periodically using the lab the density of the ready sugar syrup is controlled at the exit from the mixer. The active electrical power which is used in the electric motor of the sugar syrup pump, the temperature and pressure differential of the sugar syrup mixture, coming from the mixer and water at the entrance of the mixer are all measured. The water-mass density is calculated by its temperature and the density of the sugar syrup mixture by its pressure differential. Afterwards the volume flow rate is worked out by the measured volume flow rate of water, by the estimated value of the density of water and sugar syrup mixture and by the density of ready sugar syrup measured in the laboratory. The dependency ratio of the active electric power from the volume rate of flow of the sugar syrup mixture and the differential in its pressure N=α1Q3УΔPy2QyΔPy , where N - active electric power; QY - volume rate of flow of sugar syrup mixture entering the mixer; ΔPY - pressure differential of the sugar syrup mixture; α1, α2 - coefficients. The obtained plot is used for future calculations of volume rate of flow of sugar syrup mixture only with measured values of active electric power and pressure differential of the sugar syrup mixture. The current task of the regulator of the volumetric water discharge is determined on the basis of measured values of this output, estimated values of the density of sugar syrup mixture, water and volume rate of flow of the sugar syrup mixture, the determined value of density of ready sugar syrup mixture and the task of the regulator calculated in the previous control step. The solid content of the original sugar syrup mixture is controlled - by its temperature and density in the ready sugar syrup mixture. This invention makes it possible to reduce the loss of sugar from molasses due to a more qualitative stabilisation of the density of molasses on its exit from the mixer.
Work environment remote control device Work environment remote control device / 2335795
Device contains control unit, temperature sensor, noise sensor and luminance sensor, temperature, noise and luminance signal converter per each sensor, boundary value generator per each controlled factor, comparator per each generator of maximum permissible values of measured temperature, noise, luminance, logic elements per each controlled factor, read-only storage per each controlled factor, shift registers, value counter of each controlled factor, control unit and generator. Besides, device contains relative humidity detector, air speed transducer and pulse number sensor, signal converters of relative humidity, air speed and pulsation factor per each sensor, boundary value generator per each additional controlled factor, comparator per each generator of each additional controlled factor, logic elements per each controlled factor, read-only storage per each controlled factor, shift registers, counter of maximum relative humidity, counter of minimum relative humidity, counter of air speeds, counter of pulsation factors.
Work environment remote control device Work environment remote control device / 2335794
Device contains control unit, temperature sensor, noise sensor and luminance sensor, temperature, noise and luminance signal converter per each sensor, boundary value generator per each controlled factor, comparator per each generator of maximum permissible values of measured parameters, logic elements per each controlled factor, read-only storages per each controlled factor, four shift registers, counter of maximum temperature, counter of minimum temperature, noise counter, luminance, control unit and generator. Besides, device contains chemical sensor with converter, chemical concentration generator, logic element of maximum chemical concentrations, read-only storage of maximum chemical concentrations, shift register, counter of maximum chemical concentrations.
System of engine fuel supply System of engine fuel supply / 2325547
System of engine fuel supply consists of fuel tank wherein the following is installed: a level meter connected to the inlet of a "fuel-water" level regulator, and a control valve to flow out commodity water; the said valve is connected to a control outlet of the regulator. The level meter is made as two sensors of the fuel level, located in a portion of the lowest allowable fuel level mainly at opposite sides of the tank and one water level sensor located at the flow out level. The control valve is assembled so as to provide a positive feedback with the regulator upon receiving a signal on water presence and a negative feedback when there is no signal entry. At the moment of a positive feedback and water flow out the regulator is programmed to let out not more than 100 kg of fuel.
Method of control over the process of decomposition of the aluminate solution in the alum earth production Method of control over the process of decomposition of the aluminate solution in the alum earth production / 2310607
The invention is pertaining to the field of nonferrous metallurgy and may be used to control the inertia processes, the outlet parameter of which is nonlinearly, predominantly extremely, linked with the inlet parameters. The method to control the process of decomposition of the aluminate solution in production of the alum earth exercised in the battery of the sequentially connected apparatuses- decomposers supplied with the devices of cooling of the source aluminate solution and the decomposing pulp, the devices of separation of the decomposing pulp at the battery outlet into the large-sized production fraction and small-sized fraction in compliance with the dimension of the solid particles in the pulp, with feeding of the source aluminate solution into the head decomposer, and the small-sized fraction and the part pf the large-sized fraction - in the capacity of the streams of the seed - in the decomposers of the head part of the battery provides for measurements of the consumption of the aluminate solution inlet stream, measurement of the consumption of the seed stream, the temperature of the aluminate solution and the pulp, contents of the aluminum oxide and the caustic alkali in the aluminate solution, contents of the particles of the preset class in the commercial hydroxide, stabilization of consumption of the seeds streams, the temperature of the aluminate solution and the decomposing pulp and alterations on each step of the control of the preset stabilizing values. The preset for stabilization at each step of the control values of the consumption of the seed streams and the temperature of the inlet aluminate solution and the decomposing pulp are determined by means of the approximated mathematical model consisting of in series connected the linear dynamic link, which inlets are the measured values of all indicated parameters, and the linear static link determining the predictable value of the speed of fluctuation of the contents of the particles of the preset size in the commercial hydroxide, average and centered the measured values of all parameters, depending on which and on the predictable value of the speed of fluctuation of the contents of the particles of the preset size determine and set the given for stabilization on that step of control the values of the parameters. The invention allows to maintain the quality of the ready product - the contents of the preset fraction of aluminum hydroxide.
Method for moisture stabilization of dairy butter Method for moisture stabilization of dairy butter / 2302108
Continuous action butter machine includes seasoning reservoirs, churning machine with mixer and normalizing component batching pump. At outlet of continuous action butter machine, value of expected butter moisture deviation is determined from a formula. Churning machine mixer rotation frequency is controlled together with feeding of normalizing component depending on deviation of moisture from given value with consideration of value of expected component.
Method for stabilizing of butter moisture normalization process Method for stabilizing of butter moisture normalization process / 2298918
Method involves regulating rotational frequency of churn mixer and feeding normalizing component depending on butter moisture content deviation from predetermined value; changing cream churning temperature depending on changing of butter moisture content deviation from predetermined value. When butter moisture content is below predetermined value, cream temperature is changed by value equivalent to normalizing component dosing value. When butter moisture content is above predetermined value, cream temperature is changed by value equivalent to butter moisture content deviation from predetermined value. Method allows butter yield to be increased to more than 180 kg per working shift.
Device for remote controlling of parameters of industrial area Device for remote controlling of parameters of industrial area / 2279704
Device can be used for inspection and control and levels of physical factors of industrial area. Device has control unit, signal converters, temperature detector, noise detector and illumination detector, illumination and noise signal converters for any detector, maximal and minimal temperature presetting devices. Device also has ultimate level noise level set-point device, ultimate limiting illumination level set-point device, comparator for any measured parameters ultimate values set-point device (as temperature, noise and illumination level), logic gates for any factor to be controlled, permanent memory unit, temperature, noise and illumination values counters and oscillator.
Process for automatic control of sugar clarification and automatic control system for performing the same Process for automatic control of sugar clarification and automatic control system for performing the same / 2267149
Method for automatic control of clarification of sugar by means of sugar-containing solution in successively joined auger and horizontal sectional clarifying agitator at supplying sugar to auger comprises steps of controlling flow rate of sugar-containing solution to clarifying agitator depending upon concentration of dry matters in clarified product; supplying to auger catholyte with pH 10 - 11.5 and feeding to first section of clarifying agitator milk of lime; controlling flow rate of catholyte in such a way that in those section of clarifying agitator where clarifying process is going on for 4 - 6 min concentration of dry matters is in range 12 -18% and controlling flow rate of milk of lime in such a way that pH in the same section is in range 10.8 - 11.5; supplying sugar- containing solution to next sections of clarifying agitator along motion direction of sugar in it; measuring concentration of dry matters in order to control flow rate of sugar-containing solution in last section of clarifying agitator. Automatic control system for controlling clarification of sugar in successively joined auger and horizontal sectional agitator includes circuit for stabilizing concentration of dry matters of clarified product with use of pickup for measuring concentration of dry matters. Auger is provided with branch pipes for feeding catholyte into it. Clarifying agitator includes branch pipe for feeding lime of milk to first section. Pickup for measuring concentration of dry matters is arranged in last section of clarifying agitator. System includes in addition circuit for controlling quality of clarification having pickups for measuring pH and concentration of dry matters, both placed in one section of clarifying agitator and pickup for measuring catholyte flow rate; regulators and valves. One valve is mounted inline for feeding milk of lime and other valve is mounted inline for feeding catholyte.
Method for automatic control of sugar liquoring process and system for automatic control of realization of this method Method for automatic control of sugar liquoring process and system for automatic control of realization of this method / 2260832
Method for automatic controlling of sugar liquoring process in horizontal sectional liquoring continuous-action mixer and accumulating mixer includes changing flow of liquoring solution with consideration of liquoring concentration in accumulating mixer. Into sections, where concentration of dry substances does not exceed 18%, lime milk is fed, flow of which is adjusted so, that pH of liquoring in this sections was 10,8-11,2, and stop of sugar feeding into liquoring mixer is performed when liquoring level in accumulating mixer reaches certain level. System for automatic control of sugar liquoring process in horizontal sectional liquoring continuous-action mixer and accumulating mixer includes level sensor in accumulating mixer, mounted in said mixer, liquoring concentration sensor and liquoring solution feeding adjuster into first section of liquoring mixer. Each section of liquoring mixer, except last one, is provided with branch pipe for feeding lime milk, pH indicator and dry substances concentration indicator. Also, system is provided with serially connected valve for stopping sugar feed into liquoring mixer and adjuster, input of which is connected to level indicator, mounted in accumulating mixer, while the latter is connected to liquoring solution feeding adjuster into first section via set-point device, connected to concentration sensor. Use of device allows to increase efficiency of sugar purification due to forming of favorable conditions for decomposition of reducing substances during liquoring. Containment level of reducing substances in sugar liquoring is decreased in 1,4-1,4 times.
Method for automatic controlling of continuous malting process Method for automatic controlling of continuous malting process / 2248390
Method involves providing continuous malting process in rotating drum; measuring and stabilizing temperature of malt by changing air flow rate for cooling of grain under germination procedure; additionally measuring malt moisture content and regulating it depending on changing of malt moisture content as compared to set values by changing water supply for grain moistening during germination process; also, regulating water supply for cooling air and correcting changing of air flow rate for cooling of grain under germination process depending on changed temperature of malt as compared to set values.
Method of automatically governing biotechnological process / 2248399
Invention concerns governing periodical air-intake biotechnological process carried out in bioreactor. Method comprises measuring oxygen content in effluent gas, working volume of culture medium, concentration of biomass, and concentration of intermediate product of its vital activity. Measured parameters allow specific oxygen consumption rate and velocity of intermediate product concentration change to be determined to enable regulation of feeding air used in aeration, supplying nutritional medium, and agitating culture medium. Moreover, temperature of culture medium, temperature of supplied and withdrawn cooling agent, and consumption of the latter are measured to use these parameters for determining biomass heat release rate and velocity of intermediate product amount change. The two latter parameters enable regulation of feeding air used in aeration and supplying nutritional medium. The following characteristics are thus improved: elevating power by 8.1%, maltase activity by 7.9% and resistance by 7.4%.
Control method for high-viscous oil product discharge from railroad tank cars Control method for high-viscous oil product discharge from railroad tank cars / 2257327
Method involves determining temperature of outer tank car wall by measuring thereof in lower tank car case portion, which is the nearest to tank car bottom; comparing the measured temperature with one estimated from heat calculations performed with the use of control computer. The temperature is calculated from well-known correlations with taking into consideration previously measured temperature of ambient air and wind velocity, technical characteristics of tank cars, physical properties of oil product to be discharged and air.
Method for automatic control of sugar liquoring process and system for automatic control of realization of this method Method for automatic control of sugar liquoring process and system for automatic control of realization of this method / 2260832
Method for automatic controlling of sugar liquoring process in horizontal sectional liquoring continuous-action mixer and accumulating mixer includes changing flow of liquoring solution with consideration of liquoring concentration in accumulating mixer. Into sections, where concentration of dry substances does not exceed 18%, lime milk is fed, flow of which is adjusted so, that pH of liquoring in this sections was 10,8-11,2, and stop of sugar feeding into liquoring mixer is performed when liquoring level in accumulating mixer reaches certain level. System for automatic control of sugar liquoring process in horizontal sectional liquoring continuous-action mixer and accumulating mixer includes level sensor in accumulating mixer, mounted in said mixer, liquoring concentration sensor and liquoring solution feeding adjuster into first section of liquoring mixer. Each section of liquoring mixer, except last one, is provided with branch pipe for feeding lime milk, pH indicator and dry substances concentration indicator. Also, system is provided with serially connected valve for stopping sugar feed into liquoring mixer and adjuster, input of which is connected to level indicator, mounted in accumulating mixer, while the latter is connected to liquoring solution feeding adjuster into first section via set-point device, connected to concentration sensor. Use of device allows to increase efficiency of sugar purification due to forming of favorable conditions for decomposition of reducing substances during liquoring. Containment level of reducing substances in sugar liquoring is decreased in 1,4-1,4 times.
Process for automatic control of sugar clarification and automatic control system for performing the same Process for automatic control of sugar clarification and automatic control system for performing the same / 2267149
Method for automatic control of clarification of sugar by means of sugar-containing solution in successively joined auger and horizontal sectional clarifying agitator at supplying sugar to auger comprises steps of controlling flow rate of sugar-containing solution to clarifying agitator depending upon concentration of dry matters in clarified product; supplying to auger catholyte with pH 10 - 11.5 and feeding to first section of clarifying agitator milk of lime; controlling flow rate of catholyte in such a way that in those section of clarifying agitator where clarifying process is going on for 4 - 6 min concentration of dry matters is in range 12 -18% and controlling flow rate of milk of lime in such a way that pH in the same section is in range 10.8 - 11.5; supplying sugar- containing solution to next sections of clarifying agitator along motion direction of sugar in it; measuring concentration of dry matters in order to control flow rate of sugar-containing solution in last section of clarifying agitator. Automatic control system for controlling clarification of sugar in successively joined auger and horizontal sectional agitator includes circuit for stabilizing concentration of dry matters of clarified product with use of pickup for measuring concentration of dry matters. Auger is provided with branch pipes for feeding catholyte into it. Clarifying agitator includes branch pipe for feeding lime of milk to first section. Pickup for measuring concentration of dry matters is arranged in last section of clarifying agitator. System includes in addition circuit for controlling quality of clarification having pickups for measuring pH and concentration of dry matters, both placed in one section of clarifying agitator and pickup for measuring catholyte flow rate; regulators and valves. One valve is mounted inline for feeding milk of lime and other valve is mounted inline for feeding catholyte.
Device for remote controlling of parameters of industrial area Device for remote controlling of parameters of industrial area / 2279704
Device can be used for inspection and control and levels of physical factors of industrial area. Device has control unit, signal converters, temperature detector, noise detector and illumination detector, illumination and noise signal converters for any detector, maximal and minimal temperature presetting devices. Device also has ultimate level noise level set-point device, ultimate limiting illumination level set-point device, comparator for any measured parameters ultimate values set-point device (as temperature, noise and illumination level), logic gates for any factor to be controlled, permanent memory unit, temperature, noise and illumination values counters and oscillator.
Method for stabilizing of butter moisture normalization process Method for stabilizing of butter moisture normalization process / 2298918
Method involves regulating rotational frequency of churn mixer and feeding normalizing component depending on butter moisture content deviation from predetermined value; changing cream churning temperature depending on changing of butter moisture content deviation from predetermined value. When butter moisture content is below predetermined value, cream temperature is changed by value equivalent to normalizing component dosing value. When butter moisture content is above predetermined value, cream temperature is changed by value equivalent to butter moisture content deviation from predetermined value. Method allows butter yield to be increased to more than 180 kg per working shift.
Method for moisture stabilization of dairy butter Method for moisture stabilization of dairy butter / 2302108
Continuous action butter machine includes seasoning reservoirs, churning machine with mixer and normalizing component batching pump. At outlet of continuous action butter machine, value of expected butter moisture deviation is determined from a formula. Churning machine mixer rotation frequency is controlled together with feeding of normalizing component depending on deviation of moisture from given value with consideration of value of expected component.
Method of control over the process of decomposition of the aluminate solution in the alum earth production Method of control over the process of decomposition of the aluminate solution in the alum earth production / 2310607
The invention is pertaining to the field of nonferrous metallurgy and may be used to control the inertia processes, the outlet parameter of which is nonlinearly, predominantly extremely, linked with the inlet parameters. The method to control the process of decomposition of the aluminate solution in production of the alum earth exercised in the battery of the sequentially connected apparatuses- decomposers supplied with the devices of cooling of the source aluminate solution and the decomposing pulp, the devices of separation of the decomposing pulp at the battery outlet into the large-sized production fraction and small-sized fraction in compliance with the dimension of the solid particles in the pulp, with feeding of the source aluminate solution into the head decomposer, and the small-sized fraction and the part pf the large-sized fraction - in the capacity of the streams of the seed - in the decomposers of the head part of the battery provides for measurements of the consumption of the aluminate solution inlet stream, measurement of the consumption of the seed stream, the temperature of the aluminate solution and the pulp, contents of the aluminum oxide and the caustic alkali in the aluminate solution, contents of the particles of the preset class in the commercial hydroxide, stabilization of consumption of the seeds streams, the temperature of the aluminate solution and the decomposing pulp and alterations on each step of the control of the preset stabilizing values. The preset for stabilization at each step of the control values of the consumption of the seed streams and the temperature of the inlet aluminate solution and the decomposing pulp are determined by means of the approximated mathematical model consisting of in series connected the linear dynamic link, which inlets are the measured values of all indicated parameters, and the linear static link determining the predictable value of the speed of fluctuation of the contents of the particles of the preset size in the commercial hydroxide, average and centered the measured values of all parameters, depending on which and on the predictable value of the speed of fluctuation of the contents of the particles of the preset size determine and set the given for stabilization on that step of control the values of the parameters. The invention allows to maintain the quality of the ready product - the contents of the preset fraction of aluminum hydroxide.
System of engine fuel supply System of engine fuel supply / 2325547
System of engine fuel supply consists of fuel tank wherein the following is installed: a level meter connected to the inlet of a "fuel-water" level regulator, and a control valve to flow out commodity water; the said valve is connected to a control outlet of the regulator. The level meter is made as two sensors of the fuel level, located in a portion of the lowest allowable fuel level mainly at opposite sides of the tank and one water level sensor located at the flow out level. The control valve is assembled so as to provide a positive feedback with the regulator upon receiving a signal on water presence and a negative feedback when there is no signal entry. At the moment of a positive feedback and water flow out the regulator is programmed to let out not more than 100 kg of fuel.

FIELD: instrument making.

SUBSTANCE: invention relates to instrument making and can be used to control production area environments. Proposed device comprises regulator unit, control unit, temperature pickup, noise and illumination pickups. It also includes transducers of signals generated by the temperature, noise and illumination pickups. It incorporates setters of maximum and minimum tolerable temperatures, maximum tolerable noise and maximum tolerable illumination. The device includes comparator for every aforesaid setter and logical elements for every aforesaid controlled parametre. It incorporates the 1st , 2nd, 3rd and 4th logical elements, read-only memories for all controlled parametres, shift registers and counters of all aforesaid parametres. In compliance with this invention, the proposed device additionally comprises I/O units, communication unit, satellite receiver unit, power supply monitor, power buffer, ADC, real-time clock unit, RAM, nonvolatile memory unit. It incorporates, further on, real-time clock storage battery, relative humidity pickup with amplifier, airflow speed pickup with amplifier, environment heat load intensity pickup with amplifier, carbon oxide concentration pickup with amplifier, sulfur oxide concentration pickup with amplifier, nitrogen oxide concentration pickup with amplifier, ozone concentration pickup with amplifier, town gas concentration pickup with amplifier, power supply voltage pickup with amplifier and power supply.

EFFECT: large amount of collected data, higher quality of gathered data, higher accuracy of environmental control in production areas.

1 dwg

 

The invention relates to the field of control parameters of working conditions, in particular to the management and control of the actual levels of physical work environment factors such as temperature, intensity of thermal radiation, relative humidity, speed, air flow, noise, illumination, the concentration of toxic gases in the workplace industrial enterprises.

A device for climate control in stores [A.S. 334559, MKI G05D 23/19. A device for climate control / Rimlawi - publ. in BI 12, 1972], which contains the unit job, transducers, temperature sensors.

The drawbacks are the complexity of laying a large number of communication lines, the decrease in accuracy due to errors introduced by the communication lines, the lack of information on the moisture-controlled environment.

It is also known a device for controlling temperature and relative humidity [A.S. 691812, MKI G05D 27/02. Device for regulating the temperature and relative humidity indoor / Pengaton - publ. in BI 38, 1979], which contains the control unit, transducers, temperature sensors and humidity, each of which is connected to a separate three-wire line of communication with the control unit.

Disadvantages it is a low control accuracy of the actual level of the physical factors of the working environment.

The closest to the technical nature of the claimed device is a device for remote control of the parameters of the production environment (Patent RU 2279704 C1, G05D 27/02. The remote control parameters of the production environment / Amochaev - publ. in bull. No. 19, 2006), which contains the control unit, sensors, temperature, light and noise, signal converters noise and lighting on each sensor, the combination of the maximum and minimum values of temperature, unit maximum permissible levels of light and noise, the comparator for each unit, the logical elements for each controllable factor, read-only memory, counters, temperature, noise, lighting, signal generator.

The drawbacks are the insufficient amount of information collected, the impossibility of long-term storage of information, lack of information about the chemical composition of air, the lack of binding of the measured values of production factors of time and coordinates.

The approach suggested by this technical solution allows you to change the methodology for the assessment of the performance of the production environment. Readings are recorded in the memory through small discrete time intervals, the information is then transmitted to the PC where it is converted, and the results obtained will appreciate is not only a one-time state of the production environment, and change it during the work shift. The proposed device will allow you to capture, long-term store, and display the collected information about the state of the production environment, as well as about the time and location of conducted measurements on output unit of the device, and a personal computer. The information collected will be protected from accidental deletion in case of power loss.

This is achieved by the fact that the device containing the sensor noise and sensor, signal converters noise and lighting on each sensor, the combination of the maximum and minimum values of temperature, unit maximum permissible noise level, the unit maximum permissible light level, the comparator for each unit of maximum permissible values of the measured parameters (temperature, noise, lighting), logic elements for each controllable factor (the first gate, second gate, the third gate, the fourth logical element), a permanent storage device maximum temperature values, continually storage device minimum values of temperature, continually storage the device noise levels, continually storage device of the light, shift registers, which are in turn connected to the control unit is s, and the signal generator, inputs of the sensor-intensity heat load environment, relative humidity sensor, a concentration sensor carbon monoxide sensor, the concentration of sulfur dioxide, the concentration sensor nitric oxide sensor, ozone sensor, the concentration of urban gas sensor source voltage amplifiers for each measured parameter (intensity of the heat load environment, relative humidity, concentration of carbon monoxide, sulphur dioxide, concentration of nitric oxide, ozone concentration, the concentration of urban gas, the voltage of the power source), analog-to-digital Converter, satellite receiver, the unit real-time clock, input block, output unit, a communication unit with a PC, monitor, power supply, buffer power supply, operational storage device, the nonvolatile storage device.

The invention is illustrated by the drawing, which shows the structural diagram of the device control parameters of the production environment.

The device comprises a control unit 1 for input 1 which is connected to the outputs of the shift registers 2, 3, 4, 5.

To shift registers connected elements shift register 2 counter maximum temperature values 6 and constantly-storage device 7 to the shift register 3 - meter with the x values of the temperature 8 and constantly-storage device 9, to the shift register 4 - count values of noise levels 10 and continually storage device 11 to the shift register 5 to the counter values of luminance levels 12 and constantly-storage device 13.

To the inputs of the counter values of the physical factors of the working environment attached outputs the following items: counter 6 is connected to the first logic element 14, to the counter 8 of the second logical element 15, to the counter 10 and the third logical element 16, the counter 12 fourth logical element 17, which provide an ejection signal to the counter.

The inputs of the counters are connected to conductive lines with the output of the control unit 18, to the input 1 of which is respectively connected to the signal generator 19.

Logic elements included in the structure of the system 14, 15, 16, 17, United among themselves, and to them are attached the following items: a comparator 20 has access to the first logical element 14, the comparator 21 to the second logical element 15, the comparator 22 to the third logical element 16, the comparator 23 and the fourth logical element 17, the inputs of logic elements connected to the output 1 of the signal generator 19.

At the same time to the inputs of Comparators connected: to the input of the comparator 20 output unit maximum temperatures of 24 to the input of the comparator 21 is the output of the unit minimum values temperature, and to both inputs of the Comparators 20, 21, the signal Converter 26. The input of the comparator 22 is connected to the output of the unit the maximum allowable noise level 27, the signal Converter 28. To the input of the comparator 23 outputs the unit maximum permissible light level 29 and a signal Converter 30.

The values of levels of the factors of production environment recorded by the temperature sensors 31, noise levels 32, light levels 33. The signal from the sensors is transmitted to the signal Converter. This is provided by connecting the output of the temperature sensor 31 with the signal Converter 26, the output of the sensor noise level 32 to the input of the signal Converter 28, the output of the ambient light sensor 33 to the input of the signal Converter 30.

The control unit 1 also has an attached unit of input information 34, the block information output 35, through which renders the received information. Communication with the computer is carried out by the communication unit with a personal computer 36 connected to the input-output 1 control unit 1.

To the input-output 2 control unit connected to the input-output 1 control unit 18, which allows the synchronization, the receive data and output them to the block of output data 35 and the communication unit with a personal computer 36.

To the input 2 of the control unit 18 is attached unit satellite receiver is a 37, that allows you to record the current coordinates and display them using the control unit 1 to unit information output 35.

To the input 3 of the control unit 18 is attached monitor unit power supply 38.

To the input 4 of the control unit 18 is attached buffer power supply 39.

To output 1 control unit 18 connected to the input 1 of analog-to-digital Converter 40.

The control unit 18 via the input-output 2 is also connected with the unit real-time clock 41 that allows you to continuously record the current time and display it using the control unit 1 to the output unit 35.

All measured parameters are recorded in the memory block 42 connected to the control unit 18 through the output 2 of the control unit and the input-output 3 control unit.

The control unit 18 is also connected with the block of the nonvolatile memory 43 via the output 2 of the control unit and the input-output 4 control unit.

The unit real-time clock 41 is connected with the battery real-time clock 44, which provides a saving temporary data.

The device also includes a relative humidity sensor 45, the output of which is connected to the amplifier input signal of the relative humidity sensor 46, the speed sensor air 47, the output of which is connected to the amplifier input signal of the speed sensor air 48, the gauge of the intensity of the heat load is Reda 49, the output of which is connected to the amplifier input sensor signal level of intensity of the heat load environment 50, the sensor of the concentration of carbon monoxide 51, the output of which is connected to the amplifier input signal of the sensor to the concentration of carbon monoxide 52, the sensor of the concentration of sulfur dioxide 53, the output of which is connected to the amplifier input signal of the sensor to the concentration of sulfur dioxide 54, the sensor of the concentration of nitric oxide 55, the output of which is connected to the amplifier input signal of the sensor to the concentration of nitric oxide 56, the sensor ozone concentration 57, the output of which is connected to the amplifier input sensor signal ozone concentration 58, the sensor concentration of urban gas 59, the output of which is connected to the input signal amplifier probe concentration of urban gas 60, the sensor voltage power source 61, the output of which is connected to the amplifier input sensor signal voltage of the power source 62.

To input 2 analog-to-digital Converter 40 connected to the amplifier output signal of the relative humidity sensor 46, to the input 3 connected to the amplifier output signal of the speed sensor air 48, to the input 4 connected to the amplifier output signal level of the intensity of the heat load environment 50, to the input 5 connected to the amplifier output signal of the sensor to the concentration of carbon monoxide 52 to the input 6 is connected to the output maximizing the La signal of the sensor to the concentration of sulfur dioxide 54, to the input 7 connected to the amplifier output signal of the sensor to the concentration of nitric oxide 56, to the input 8 connected to the amplifier output signal of the sensor ozone concentration 58, to the input 9 connected to the amplifier output signal of the sensor ozone concentrations of 60, to the input 10 connected to the amplifier output signal voltage of the power source 62.

To the input-output 1 analog-to-digital Converter 40 connected to the input-output 5 of the control unit 18.

Power supply monitor 38, the buffer power supply 39 and the sensor voltage power source 61 is connected to the power source 63.

The signal generator 19 is connected to the analog-to-digital Converter 40, and block real-time clock 41, the memory block 42, block of the nonvolatile memory 43.

Buffer power supply 39 provides power to the control unit 18, the memory block 42, block of the nonvolatile memory 43.

The device control parameters of working conditions is as follows.

After power-up signal generator 19 begins to generate electrical signals, temperature sensor 31, the noise level 32, the light level 33 begin to measure the actual level of physical factors of the working environment. From them the measurement information collected by the transducers of signals of the temperature sensors 26, noise 28, illumination 30. After a certain interval is l time on the transformer output signals from the temperature sensors 31, noise 32, the light 33 will receive a digital code corresponding to the signal value read from the sensors. At this point, the Comparators 20, 21, 22, 23 compares the signal received from the primary signal transducers, and knobs critical values of the measured factors: the maximum temperature of 24, minimum temperatures of 25, maximum noise levels 27, minimum light levels 29. Depending on the results of the comparison of the actual temperature, noise, lighting with their critical values, read from the setting device, the signal is transmitted to the logic elements 14, 15, 16, 17, if the actual factor level is beyond extreme values and is not transmitted, if they are normal. The signals from logic elements, read the counters 6, 8, 10, 12. The information obtained is stored permanently-storage devices 7, 9, 11, 13. The data stored in the ever-storage devices are processed (scaling, filtering, and other necessary transformations), and then written in the shift registers 2, 3, 4, 5, which encode the data and transmit them along the lines of the communication control unit 1. Information about the maximum admissible levels of the environment settings of the control unit are received at the output unit 35. After re the ACI data shift registers are transferred to the standby mode.

Simultaneously with the measurement of exceeding acceptable levels of temperature, light, noise, described above, digital relative humidity sensor 45, the speed sensor air 47, the gauge of the intensity of the heat load environment 49, the sensor of the concentration of carbon monoxide 51, the sensor of the concentration of sulfur dioxide 53, the sensor of the concentration of nitric oxide 55, the sensor ozone concentration 57, the sensor concentration of urban gas 59 measure actual values of levels of the factors of production environment, which are then amplified by the respective converters 50, 52, 54, 56, 58, 60 and transmitted to corresponding inputs of an analog-to-digital Converter 40. Sensor voltage power source 61 measures the voltage of the power source 63, the measured values are amplified in the Converter 62 and transmitted to the input 10 analog-to-digital Converter 40.

The communication line of the signal generator 19 with the module real-time clock 41, with the memory block 42 and block in the nonvolatile memory 43 enables synchronization of the entire system.

Processed in the analog-to-digital Converter 40 of the environment settings in a digital code through the input-output 1 analog-to-digital Converter 40 is transmitted to the input-output 5 of the control unit 18. The control unit 18 captures every received value from each sensor is, received on the corresponding channel analog-to-digital Converter 40, and coordinate ongoing measurements obtained from the block satellite receiver 37, and the time of measurement, obtained from the block real-time clock 41, and then sends the data to the memory block 42.

At the request of the user sent by the control unit 1 with the input block 34, the control unit 18 extracts the data from the block RAM 42 and passes through the control unit to the unit information output 35 or (on request PC) to block communication with the personal computer 36.

The signal about the state of the power source 63 is supplied to the monitor power supply 38, in the event of loss of voltage measured by the transducer voltage power source 61 to the power source 63, the supply monitor 38 generates the control signal for the control unit 18. Upon receipt of this signal at the input 3 of the control unit 18, the control unit 18 switches to the algorithm of emergency save the recorded information from the memory block in the block of non-volatile memory. The algorithm emergency conservation allows the control unit 18 to activate the buffer power supply 39, which supports the efficiency of the control unit 18, a block of non-volatile memory 43 and the memory block 42 during the discharge time of the capacitor buffer power supply 39. The presence of al is of aritma emergency conservation information allows for a discharge time of the capacitor to store information from the memory block 42 to block the non-volatile memory 43, that allows you to protect the data obtained from the loss.

Battery power real-time clock 44 allows you to store the set times time and date even in the event of loss of voltage in the power source 63 and the buffer power supply 39.

Thus, in the device for remote control of the parameters of the production environment, there are blocks of input and output information, the communication unit from a PC, the unit real-time clock that provides synchronization of incoming information, block satellite receiver, fixing the coordinates of the performed measurements, analog-to-digital Converter blocks RAM and non-volatile memory, providing information storage amplifiers of the respective sensors and the sensor parameters of the production environment.

Sensors concentrations of toxic gases allow us to estimate the chemical composition of the air of the working environment.

Included in the device power supply, buffer power supply monitor, the sensor voltage at the power source and the non-volatile storage device ensure uninterrupted operation of the device and improve the reliability of obtaining and storing the accumulated information.

The device control parameters of the production environment that contains the control unit, the control unit, temperature sensor, sensor noise and dateconvert, signal converters temperature, noise, light on each sensor, the combination of the maximum and minimum values of temperature, unit maximum permissible noise level, the unit maximum permissible light level, the comparator for each unit of maximum permissible values of the measured parameters temperature, noise, lighting, logic elements for each controllable factor, the first logic element, the second logic element, the third logical element, the fourth logical element, constantly-storage device maximum values of temperature, constant-storage device minimum values of the temperature, constant-storage device noise, constant-memory of light levels, shift registers counter maximum value of the temperature counter minimum temperature values, counter values of noise levels, the counter values of the light levels, the signal generator, characterized in that it introduced the block input block output block communication unit satellite receiver, power supply monitor, buffer power supply, analog-to-digital Converter, unit real-time clock, a memory block, a block of non-volatile memory, battery power real-time clock, relative humidity sensor, the amplifier signal is La relative humidity sensor, the speed sensor air flow, power of the signal of the speed sensor air flow sensor, the intensity of the heat load environment, power sensor signal intensity of the heat load environment, the sensor of the concentration of carbon monoxide, power sensor signal to the concentration of carbon monoxide sensor, the concentration of sulfur dioxide, power sensor signal to the concentration of sulfur dioxide sensor, the concentration of nitric oxide, power sensor signal to the concentration of nitric oxide sensor, ozone concentration, power sensor signal ozone concentration, probe concentration of urban gas, power sensor signal of town gas, sensor supply voltage, power sensor signal voltage of the power source, the power source and the unit control is connected to shift registers whose inputs are connected to the outputs of the constant-storage devices, and the inputs of the shift registers are connected respectively to the outputs of the counter maximum value of the temperature counter minimum temperature values, counter values of noise, the counter values of illumination, to the inputs of which are connected to the output of the first logic element, the second logic gate, the third logic element, the fourth logic element, and the inputs of logic elements respectively attached is uhodi Comparators, in turn, all four logic element connected with the output of the signal generator, the outputs of the shift registers are connected to the input of the control unit, the output control unit is also connected to the input of the counter maximum value of the temperature counter minimum temperature values, counter values of noise levels, the counter values of luminance levels, with inputs constant-mass storage device maximum values of temperature, constant-storage device minimum temperature values, read-only memory noise, constant-storage device values of illumination, the inputs of the converters, in turn, connected to the outputs of the sensors, namely the output of the sensor temperature is connected to the input of the signal Converter temperature, the output of the sensor noise to the input signal transducer noise, the output of the sensor with the inverter input signal light, the latter are connected to the inputs of the respective Comparators, which is also connected converters and outputs control devices, namely, the output of the generator maximum temperature values, the output of the unit minimum temperature values, the output of the generator maximum noise output of the unit minimum values of the light outputs of the control unit is connected to the input of analog-to-digital Converter, to the input of the block RAM block of the nonvolatile memory, the control unit is connected to the output of a satellite receiver, monitor, power supply, buffer power supply, the output of the latter is connected to the input of the block RAM to the entrance of the block of non-volatile memory, and to the inputs of the monitor power supply and buffer power supply connected to the power source, the output of the last attached sensor voltage power source, the control unit is also connected to the output of the signal generator, which, in turn, is connected to the input of analog-to-digital Converter with the input of block real-time clock with the input of the block RAM, the entrance unit non-volatile memory, input-output control unit connected to the control unit, and input of the latter is connected to the output of the input block, the output control unit is connected to the input block output, and input-output control unit connected to the input-output unit for communication with a personal computer, input-output control unit also connected to the inputs-outputs of analog-to-digital Converter, memory block, a block of non-volatile memory unit real-time clock to the input of the last attached the output of the battery, to the inputs of analog-to-digital Converter connected to the outputs of amplifiers sensors, inputs strengthen the lei, in turn, respectively connected to the outputs of the sensors.

 

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