CN203101985U - Operation control system of destructive distillation sludge device - Google Patents
Operation control system of destructive distillation sludge device Download PDFInfo
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- CN203101985U CN203101985U CN2013201068676U CN201320106867U CN203101985U CN 203101985 U CN203101985 U CN 203101985U CN 2013201068676 U CN2013201068676 U CN 2013201068676U CN 201320106867 U CN201320106867 U CN 201320106867U CN 203101985 U CN203101985 U CN 203101985U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/02—Total factory control, e.g. smart factories, flexible manufacturing systems [FMS] or integrated manufacturing systems [IMS]
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Abstract
The utility model discloses an operation control system of a destructive distillation sludge device. The operation control system comprises a control layer, a power terminal layer and a site layer, wherein the control layer is an electrical control cabinet; a programmable logic controller is arranged in the electrical control cabinet and used for realizing the operation of the whole destructive distillation sludge device; the power terminal layer comprises a power distribution cabinet, a main engine control cabinet and an auxiliary engine control cabinet, wherein the power distribution cabinet is used for distributing power for the whole destructive distillation sludge device; the main engine control cabinet and the auxiliary engine control cabinet are remote IO stations and used for controlling the acquisition and conversion of site data; the site layer comprises site equipment, a button station, a site meter and a display operation station, wherein the button station is electrically connected with the power distribution cabinet for manually operating the equipment; the display operation station is electrically connected with the main engine control cabinet and the auxiliary engine control cabinet; and the site meter is used for displaying the operation parameters of the system. The operation control system of the destructive distillation sludge device can be used for carrying out interlocking operation, control and management onto various equipment of the destructive distillation sludge device, so that the system operation stability is improved, the working strength of operation personnel is lowered, quality of destructive distillation charcoal is improved, energy resources are saved and destructive distillation cost of the charcoals is lowered.
Description
Technical field
The utility model relates to a kind of control system, relates to a kind of operation control system that is used for destructive distillation mud device particularly.
Background technology
It is a kind of emerging method for sludge treatment that cracking process is handled mud.
It is the chemical reaction process that carries out under sealing, anaerobic, non-burning, the condition of high temperature that cracking process is handled mud, mud is carried out the high temperature heating, under the effect of destructive distillation and thermal decomposition, organism is converted into water vapor, fouling gas and charcoal, comprise reactions such as vaporization, pyrolysis, dehydrogenation, thermal condensation, charing, with the water evaporates in the mud, organism is converted into inflammable gas and organic carbon.With the destructive distillation of the burning of fuel and mud respectively two independently the space carry out.Handle by destructive distillation, principal ingredient in the mud is converted into available condensate water, inflammable gas and biological organic carbon in the destructive distillation processing procedure, the inflammable gas that destructive distillation produces is recycled, not only avoided the pollution of air, but also energy savings.
Because the mud thermal cracking is carried out under, anaerobic state isolated with air, so the carbon in the mud can't become the harmful carbon dioxide of body, but is converted into the volatilization inflammable gas.
The biological carbon of destructive distillation manufacturing is embedded in the soil, absorbs the carbon dioxide in the soil, prevents that the carbon dioxide in the soil from entering atmosphere, makes farmland become large-scale carbon warehousing.
The process of sludge through destructive distillation is the reduction process of charcoal, with the organic carbon element transformation is the inorganic carbon element, can not produce oxides of nitrogen (NxOy) and oxysulfide (constituents of acid rain) such as (SxOy), can significantly cut down the greenhouse gases emission of carbon-dioxide as burning method.
Sludge through destructive distillation equipment comprises conveying equipment, combustion apparatus, gas purification separation equipment, cleaner, biological carbon cooling device, biological carbon bagging equipment or the like.Because sludge through destructive distillation equipment is many, bust appears in complicated operation easily, causes the quality of the biological carbon of destructive distillation manufacturing can't guarantee that the distillation apparatus operational efficiency is low, increases energy resource consumption.
Whether can adopt a kind of control system that the various device of sludge through destructive distillation both can be controlled in manual operation, can carry out chain operation control again, the stability of raising system operation, reduce operating personnel's working strength, improve the quality of biological carbon, energy savings, the cost of reduction destructive distillation does not appear in the newspapers so far.
The utility model content
The purpose of this utility model is to provide a kind of operation control system of destructive distillation mud device, to overcome the defective that exists in the known technology.
For achieving the above object, the operation control system of the destructive distillation mud device that the utility model provides comprises key-course, power terminating layer and field layer, wherein:
Key-course is an electrical control cubicles, and programmable logic controller (PLC) is installed in the electrical control cubicles, realizes the operation to whole destructive distillation mud device;
The power terminating layer comprises power distribution cabinet and host computer control cabinet and subsidiary engine switch board:
Power distribution cabinet is whole destructive distillation mud device distribution;
Host computer control cabinet and subsidiary engine switch board are the remote I station, the collection and the conversion of control field data;
Field layer comprises field apparatus and push-button station, and field instrument and display operation station:
Push-button station and power distribution cabinet are electrically connected;
The display operation station connects host computer control cabinet and subsidiary engine switch board, by field instrument display system operational factor.
The operation control system of described destructive distillation mud device, wherein, electrical control cubicles is provided with manual change-over switch, when switching to manual state, by the independent start-stop of every equipment of manual control destructive distillation mud device.
The operation control system of described destructive distillation mud device, wherein, host computer control cabinet and subsidiary engine switch board are provided with pilot lamp and instrument, show the operation and the malfunction of every equipment in the destructive distillation mud device.
The operation control system of described destructive distillation mud device, wherein, the power distribution cabinet of power terminating layer is a destructive distillation mud device distribution, the motor distribution that comprises destructive distillation unit, screw pump, fly-ash separator, chapelet, roof scrubber, charcoal cooling device, mixed steam separating equipment for purification is host computer control cabinet and subsidiary engine switch board distribution simultaneously.
The operational process of destructive distillation mud device of the present utility model is as follows:
1) electrical control cubicles is opened Electric air valve, and according to the range of negative pressure of the heating chamber of setting, the signal of the sensor of heating chamber pressure is adjusted the Electric air valve aperture automatically;
2) electrical control cubicles starting fly-ash separator operation;
3) electrical control cubicles starting mixed steam separating equipment for purification operation, and according to the destructive distillation unit mixed steam top hole pressure of setting, with the signal of the sensor of destructive distillation unit mixed steam top hole pressure, adjust mixed steam separating equipment for purification rotating speed, make the mixed steam top hole pressure remain on 10～15Pa;
4) electrical control cubicles starting destructive distillation chamber operation, and according to the rotating speed of setting, adjust, the destructive distillation chamber is changeed clockwise direction with per minute one and is rotated;
5) electrical control cubicles starting screw pump operation according to the mud input quantity of setting, is imported mud in the destructive distillation unit;
6) electrical control cubicles is according to the temperature of the heating chamber of setting, by the operation of platform start and stop burner;
7) when the temperature of heating chamber reaches predetermined temperature, electrical control cubicles is closed burner according to burner start and stop order by platform, only keeps a middle burner operation of destructive distillation unit;
8) electrical control cubicles starts charcoal cooling device, chapelet, roof scrubber;
9) when charcoal cooling device, chapelet, roof scrubber operation normal, temperature in the heating chamber drops to predetermined predetermined temperature when following, electrical control cubicles control destructive distillation chamber stops operating, electrical control cubicles switches to rotation counterclockwise with the rotation direction of destructive distillation chamber simultaneously, and the rotating speed of destructive distillation chamber is adjusted in control; When the abnormal operation of charcoal cooling device, chapelet, roof scrubber, or the temperature in the heating chamber is higher than predetermined temperature when above, and electrical control cubicles is in the lock state the rotation direction switching of destructive distillation chamber, can't switch to counter-rotating;
10) after the indoor charcoal of destructive distillation was all discharged, electrical control cubicles stopped charcoal cooling device, chapelet, roof scrubber operation;
11) after electrical control cubicles control destructive distillation chamber stopped operating, electrical control cubicles switched to the clockwise direction rotation with the rotation direction of destructive distillation chamber, and the rotating speed of destructive distillation chamber is adjusted in control;
12) repeat said process 4-11.
Described control operational process, wherein, process 1) in the range of negative pressure of heating chamber be-30～-50Pa.
Described control operational process, wherein, process 3) destructive distillation chamber mixed steam top hole pressure scope is 10～15Pa in.
Described control operational process, wherein, process 6) it is 700 ℃ during the predetermined temperature of heating chamber in.
Described control operational process, wherein, process 9) predetermined temperature in the heating chamber is 300 ℃.
Described control operational process, wherein, process 9) rotating speed of destructive distillation chamber is per minute two commentaries on classics in.
Described control operational process, wherein, process 11) rotating speed of destructive distillation chamber is adjusted into per minute one commentaries on classics in.
All adopt known technology to be connected between the above-mentioned control system of the utility model and with the electric connection between the destructive distillation mud device.
Control system of the present utility model can be carried out chain operation, control, management to the various device of destructive distillation mud device, the stability of raising system operation reduces operating personnel's working strength, improves the quality of destructive distillation mud, energy savings, the destructive distillation cost of reduction mud.
Description of drawings
Fig. 1 is the utility model destructive distillation sludge system progress control method synoptic diagram;
Fig. 2 is the electrical control cubicles synoptic diagram;
Fig. 3 is the power distribution cabinet synoptic diagram;
Fig. 4 is host computer control cabinet figure;
Fig. 5 is a subsidiary engine switch board synoptic diagram;
Description of symbols in the accompanying drawing:
1 destructive distillation unit, 2 burners, 3 feed spaces, 4 screw pumps, 5 mixed steam separating equipment for purifications, 6 fly-ash separators, 7 push-button stations, 8 charcoal cooling devices, 9 chapelets, 10 charcoal storage bins, 11 roof scrubbers, 12 discharge chambers, 13 host computer control cabinets, 14 subsidiary engine switch boards, 15 power distribution cabinets, 16 electrical control cubicles, 17 turn to manual control handle, 18 indicator gauges, 19 manual change-over switches, 20 start buttons, 21 rotating speeds are adjusted knob, 22 display screens, 23 switch board bodies, 24 field instruments, 25 stop buttons, 26 rotating knobs, destructive distillation chambers 27,28 heating chambers, 29 Electric air valves.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
The operation control system that is used for destructive distillation mud device of the present utility model according to the actual conditions in destructive distillation mud workshop, adopts on-the-spot distributed control structure longitudinal layered, horizontal partition.Keep redundancy, correlativity and the independence of destructive distillation mud workshop electric control system hardware, " danger " is disperseed to greatest extent, the arbitrary part of assurance system breaks down can not influence the normal operation of other parts.The structure of system is divided into three layers, is respectively key-course, power terminating layer and field layer.Wherein:
Key-course is an electrical control cubicles 16, and programmable logic controller (PLC) (PLC) is installed in the electrical control cubicles 16, realizes the operation to whole destructive distillation mud device.The control center that an example of the present utility model is a key-course adopts Siemens S7-300 control system to realize the equipment in the whole destructive distillation mud workshop is carried out unified management and coordination, guarantees that each system can move automatically according to blas.
The power terminating layer comprises power distribution cabinet 15, host computer control cabinet 13 and subsidiary engine switch board 14, wherein:
Host computer control cabinet 13 and subsidiary engine switch board 14 all are electrically connected with power distribution cabinet 15, and host computer control cabinet 13 and subsidiary engine switch board 14 are responsible for the collection and the switching of field data.As signal datas such as temperature and pressure, be uploaded in the electrical control cubicles 16 and handle.Simultaneously, the result in the electrical control cubicles 16 sends in host computer control cabinet 13 and the subsidiary engine switch board 14 to drive field apparatus or display device state, shows such as the switch of valve or the operation conditions of motor.Host computer control cabinet 13 and subsidiary engine switch board 14 are provided with manual change-over switch, when switching to manual state, by the independent start-stop of every equipment of manual control destructive distillation mud device.When switching to auto state, the equipment in the destructive distillation mud workshop is by PLC system control start-stop.Host computer control cabinet 13 and subsidiary engine switch board 14 are provided with pilot lamp and instrument, show the operational factor and the malfunction of every equipment in the destructive distillation mud device.
Field layer comprises field apparatus, push-button station 7 and field instrument 24:
Push-button station 7 is electrically connected with power distribution cabinet 15, can have the shut-down operation highest priority by operating personnel's start and stop relevant device on the spot, guarantees equipment operation safety.
All switch boards adopt bottom inlet wire mode.Instrument cable lays route: field instrument 24 → cable (wearing steel pipe, cable testing bridge) → host computer control cabinet 13 and subsidiary engine switch board 14 → electrical control cubicles 16.
All adopt known technology to be connected between the above-mentioned control system of the utility model and with the electric connection between the destructive distillation mud device.
The operation control system of described destructive distillation mud device, wherein, running status is counted:
(1) destructive distillation chamber 27 machine operation
(2) screw pump 4 work
(3) No. 1 burner 2 work
(4) No. 2 burner 2 work
(5) No. 3 burner 2 work
(6) No. 4 burner 2 work
(7) No. 5 burner 2 work
(8) No. 6 burner 2 work
(9) No. 7 burner 2 work
(10) mixed steam separating equipment for purification 5 work
(11) fly-ash separator 6 work
(12) charcoal cooling device 8 work
(13) chapelet 9 work
(14) Electric air valve 29 work
The operation control system of described destructive distillation mud device, wherein, malfunction is counted:
(1) destructive distillation chamber 27 electrical faults
(2) screw pump 4 faults
(3) 1# burner 2 faults
(4) 2# burner 2 faults
(5) 3# burner 2 faults
(6) 4# burner 2 faults
(7) 5# burner 2 faults
(8) 6# burner 2 faults
(9) 7# burner 2 faults
(10) mixed steam separating equipment for purification 5 faults
(11) fly-ash separator 6 faults
(12) charcoal cooling device 8 faults
(13) chapelet 9 faults
(14) Electric air valve 29 faults
The operation control system of described destructive distillation mud device, wherein, analog quantity is counted:
(1) heating chamber 28 temperature
(2) feed space 3 temperature
(3) discharge chamber 12 temperature
(4) destructive distillation unit 1 exhaust gas temperature
(5) charcoal cooling device 8 inflow temperatures
(6) charcoal cooling device 8 leaving water temperatures
(7) charcoal cooling device 8 feeding temperatures
(8) charcoal cooling device 8 drop temperatures
(9) mixer separating equipment for purification 5 inlet temperatures
(10) mixer separating equipment for purification 5 outlet temperatures
(11) destructive distillation unit 1 mixed steam top hole pressure
(12) mixed steam separating equipment for purification 5 top hole pressures
(13) heating chamber 28 pressure
(14) charcoal storage bin 10 material levels
(15) destructive distillation chamber 27 rotating speeds
(16) mixed steam separating equipment for purification 5 rotating speeds
(17) gas discharge
Destructive distillation mud device is controlled working procedure automatically:
(1) with the manual change-over switch of all devices on host computer control cabinet 13 and the subsidiary engine switch board 14, switches to auto state;
(2) electrical control cubicles 16 starting Electric air valves 29 operations, and according to the range of negative pressure of the heating chamber of setting 28 (30～-50Pa), the signal of heating chamber 28 field instruments 24 is adjusted Electric air valve 29 apertures automatically;
(3) electrical control cubicles 16 starting fly-ash separators 6 operations;
(4) electrical control cubicles 16 starting mixed steam separating equipment for purifications 5 operations, and according to the destructive distillation unit 1 mixed steam top hole pressure of setting, with the signal of destructive distillation chamber 3 mixed steams outlet field instrument 24, adjust mixed steam separating equipment for purification 5 rotating speeds, the mixed steam top hole pressure is remained on-30～15Pa;
(5) electrical control cubicles 16 starting destructive distillation chamber 27 operations, and according to the rotating speed of setting, adjust destructive distillation chamber 27 and rotate with per minute one commentaries on classics clockwise direction;
(6) electrical control cubicles 16 starting screw pumps 4 operations according to the mud input quantity of setting, are imported mud in destructive distillation unit 1;
(7) electrical control cubicles 16 is according to the temperature of the heating chamber of setting 28, by 2 operations of platform start and stop burner;
(8) when the temperature of heating chamber 28 reaches 700 ℃, electrical control cubicles 16 is closed burner 2 according to burner 2 start and stop order by platform, only keeps destructive distillation unit 1 a middle burner 2 and moves;
(9) electrical control cubicles 16 starts charcoal cooling device 8, chapelet 8, roof scrubber 11;
(10) when 11 operations of charcoal cooling device 8, chapelet 9, roof scrubber normal, when the temperature in the heating chamber 28 dropped to below 300 ℃, electrical control cubicles 16 slowly is adjusted into zero with destructive distillation chamber 27 rotating speeds changeed.After destructive distillation chamber 27 stopped operating fully, electrical control cubicles 16 switched to rotation counterclockwise with the rotation direction of destructive distillation chamber 27, and destructive distillation chamber 27 rotating speeds are adjusted into per minute two commentaries on classics gradually.When the abnormal operation of charcoal cooling device 8, chapelet 9, roof scrubber 11, or the temperature in the heating chamber 28 are when being higher than 300 ℃, and electrical control cubicles 16 is switched the rotation direction of destructive distillation chamber 27 and is in the lock state, and can't switch to counter-rotating;
(11) after the charcoal in the destructive distillation chamber 27 is all discharged 30 minutes, electrical control cubicles 16 stops charcoal cooling device 8, chapelet 9, roof scrubber 11 operations;
(12) electrical control cubicles 16 slowly is adjusted into zero with destructive distillation chamber 27 rotating speeds changes.After destructive distillation chamber 27 stopped operating fully, electrical control cubicles 16 switched to the clockwise direction rotation with the rotation direction of destructive distillation chamber 27, and the rotating speed of destructive distillation chamber 27 is adjusted into per minute one commentaries on classics gradually;
(13) repeat top 6-12 item.
Host computer control cabinet 13 has seven indicator gauges 18, shows:
(1) destructive distillation chamber 27 rotating speeds;
(2) heating chamber 28 temperature;
(3) destructive distillation unit 1 exhaust gas temperature;
(4) heating chamber 28 negative pressure;
(5) feed space 3 temperature;
(6) discharge chamber 12 temperature;
(7) Electric air valve 29 apertures.
Host computer control cabinet 13 has four manual change-over switches 19:
(1) the manual control of destructive distillation chamber 27 operations is switched;
(2) the manual control of burner 2 operations is switched;
(3) the manual control of screw pump 4 operations is switched;
(4) the manual control of Electric air valve 29 operations is switched;
The rotating speed of host computer control cabinet destructive distillation chambers 27 13 is adjusted the rotating knob 35 and Electric air valve 29 apertures of knob 21, destructive distillation chamber 27 and is adjusted knob.
Host computer control cabinet 13 has ten start buttons and ten stop buttons, control:
(1) destructive distillation chamber 27 is started and is stopped;
(2) 1# burner 2 starts and stops;
(3) 2# burner 2 starts and stops;
(4) 3# burner 2 starts and stops;
(5) 4# burner 2 starts and stops;
(6) 5# burner 2 starts and stops;
(7) 6# burner 2 starts and stops;
(8) 7# burner 2 starts and stops;
(9) screw pump 4 starts and stops;
(10) Electric air valve 29 starts and stops.
Subsidiary engine switch board 14 has 11 indicator gauges, shows:
(1) charcoal cooling device 8 feeding temperatures;
(2) charcoal cooling device 8 drop temperatures;
(3) charcoal cooling device 8 leaving water temperatures;
(4) charcoal storage bin 10 material levels.
(5) mixed steam separating equipment for purification 5 rotating speeds;
(6) destructive distillation unit 1 mixed steam top hole pressure;
(7) destructive distillation unit 1 mixed steam outlet temperature;
(8) mixed steam separating equipment for purification 5 top hole pressures;
(9) mixed steam separating equipment for purification 5 outlet temperatures;
(10) mixed steam separating equipment for purification 5 outlet combustible gas content;
(11) mixed steam separating equipment for purification 5 outlet combustible gas flows.
Subsidiary engine switch board 14 has five manual change-over switches, control:
(1) the 8 manual controls of charcoal cooling device are switched;
(2) chapelet 9 manual controls are switched;
(3) roof scrubber 11 manual controls are switched;
(4) fly-ash separator 6 manual controls are switched.
(5) mixed steam separating equipment for purification 5 manual switchings
Subsidiary engine switch board 14 has mixed steam separating equipment for purification 5 rotating speeds to adjust knob.
Subsidiary engine switch board 14 has five start buttons and six stop buttons, control:
(1) mixed steam separating equipment for purification 5 starts and stops.
(2) fly-ash separator 6 starts and stops;
(3) charcoal cooling device 8 starts and stops;
(4) chapelet 9 starts and stops;
(5) roof scrubber 11 starts and stops;
(1) destructive distillation unit 1 operation control automatically;
(2) mixed steam separating equipment for purification 5 operations control automatically;
(3) set the charcoal input quantity;
(4) set heating chamber 28 maximum temperatures;
(5) set range of negative pressure in the heating chamber 28;
(6) set destructive distillation unit 1 mixed steam top hole pressure;
(7) set destructive distillation chamber 27 rotating speeds;
(8) the start and stop order of setting burner 2;
(9) set heating chamber 28 heating rates.
(1) too high when negative pressure in the heating chamber 28, cross and to send acousto-optic warning when low!
(2) must start Electric air valve 29, destructive distillation chamber 27, mixed steam separating equipment for purification 5, fly-ash separator 6 earlier before the starting burner 2, otherwise burner 2 is in the lock state, and can't start!
(3) when the temperature in the heating chamber 28 surpasses 700 ℃, electrical control cubicles 16 will be sent acousto-optic warning! Cut off the power supply of burner 2,2 operations of burn-out device!
(4) when the abnormal operation of charcoal cooling device 9, chapelet 9, roof scrubber 11, or the temperature in the heating chamber 28 are when being higher than 300 ℃, and destructive distillation chamber 27 is rotated counterclockwise and is in the lock state, and can't carry out reverse turn operation!
Show following information on the display screen 22 of electrical control cubicles 16:
(1) rotating speed of destructive distillation chamber 27;
(2) destructive distillation chamber 27 is moved/is stopped;
(3) 1# burner 2 starts and stops;
(4) 2# burner 2 starts and stops;
(5) 3# burner 2 starts and stops;
(6) 4# burner 2 starts and stops;
(7) 5# burner 2 starts and stops;
(8) 6# burner 2 starts and stops;
(9) 7# burner 2 starts and stops;
(10) fly-ash separator 6 starts/stops;
(11) Electric air valve 29 starts/stops;
(12) Electric air valve 29 apertures;
(13) temperature of heating chamber 28;
(14) destructive distillation unit 1 exhaust gas temperature;
(15) temperature of feed space 3;
(16) temperature of discharge chamber 12;
(17) negative pressure in the heating chamber 28;
(18) mixed steam separating equipment for purification 5 starts/stops;
(19) mixed steam separating equipment for purification 5 rotating speeds;
(20) destructive distillation unit 1 mixed steam top hole pressure;
(21) destructive distillation unit 1 mixed steam outlet temperature;
(22) mixed steam separating equipment for purification 5 top hole pressures;
(23) mixed steam separating equipment for purification 5 outlet temperatures;
(24) mixed steam separating equipment for purification 5 outlet combustible gas content.
(25) mixed steam separating equipment for purification 5 outlet combustible gas flows;
(26) charcoal cooling device 8 feeding temperatures;
(27) charcoal cooling device 8 drop temperatures;
(28) charcoal cooling device 8 leaving water temperatures;
(29) charcoal cooling device 8 moves/stops;
(30) chapelet 9 moves/stops;
(31) roof scrubber 11 moves/stops;
(32) charcoal storage bin 10 material levels.
Control system of the present utility model can be carried out chain operation, control, management to the various device of destructive distillation mud device, the stability of raising system operation reduces operating personnel's working strength, improves the quality of destructive distillation mud, energy savings, the destructive distillation cost of reduction mud.
Claims (4)
1. the operation control system of a destructive distillation mud device is characterized in that, comprising:
Key-course, power terminating layer and field layer, wherein:
Key-course is an electrical control cubicles, and programmable logic controller (PLC) is installed in the electrical control cubicles, realizes the operation to whole destructive distillation mud device;
The power terminating layer comprises power distribution cabinet and host computer control cabinet and subsidiary engine switch board:
Power distribution cabinet is whole destructive distillation mud device distribution;
Host computer control cabinet and subsidiary engine switch board are the remote I station, the collection and the conversion of control field data;
Field layer comprises field apparatus and push-button station, and field instrument and display operation station:
Push-button station and power distribution cabinet are electrically connected;
The display operation station connects host computer control cabinet and subsidiary engine switch board, by field instrument display system operational factor.
2. according to the operation control system of the described destructive distillation mud of claim 1 device, it is characterized in that electrical control cubicles is provided with manual change-over switch, when switching to manual state, by the independent start-stop of every equipment of manual control destructive distillation mud device.
3. according to the operation control system of claim 1 or 2 described destructive distillation mud devices, it is characterized in that host computer control cabinet and subsidiary engine switch board are provided with pilot lamp and instrument, show the operation and the malfunction of every equipment in the destructive distillation mud device.
4. according to the operation control system of the described destructive distillation mud of claim 1 device, it is characterized in that, the power distribution cabinet of power terminating layer is a destructive distillation mud device distribution, the motor distribution that comprises destructive distillation unit, screw pump, fly-ash separator, chapelet, roof scrubber, charcoal cooling device, mixed steam separating equipment for purification is host computer control cabinet and subsidiary engine switch board distribution simultaneously.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013201068676U CN203101985U (en) | 2013-03-08 | 2013-03-08 | Operation control system of destructive distillation sludge device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013201068676U CN203101985U (en) | 2013-03-08 | 2013-03-08 | Operation control system of destructive distillation sludge device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203101985U true CN203101985U (en) | 2013-07-31 |
Family
ID=48853370
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013201068676U Expired - Fee Related CN203101985U (en) | 2013-03-08 | 2013-03-08 | Operation control system of destructive distillation sludge device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203101985U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103163865A (en) * | 2013-03-08 | 2013-06-19 | 密西西比国际水务有限公司 | Running control system of destructive distillation sludge device |
-
2013
- 2013-03-08 CN CN2013201068676U patent/CN203101985U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103163865A (en) * | 2013-03-08 | 2013-06-19 | 密西西比国际水务有限公司 | Running control system of destructive distillation sludge device |
| WO2014134982A1 (en) * | 2013-03-08 | 2014-09-12 | 密西西比国际水务有限公司 | Operation control system for sludge dry distillation equipment |
| CN103163865B (en) * | 2013-03-08 | 2015-03-18 | 密西西比国际水务有限公司 | Running method of running control system of destructive distillation sludge device |
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