CN102314794A - System and method for simulating multi-purpose station for oil and gas storage and transportation - Google Patents
System and method for simulating multi-purpose station for oil and gas storage and transportation Download PDFInfo
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Abstract
The invention discloses a system and method for simulating a multi-purpose station for oil and gas storage and transportation. The system comprises a sand table, a touch screen and a flow plate, wherein oil and gas storage and transportation equipment and pipelines for connecting the oil and gas storage and transportation equipment are arranged on the sand table, control valves and LED lamp belts are arranged in the inlet/outlet pipelines of the oil and gas storage and transportation equipment, a PLC (Programmable Logic Controller) is arranged below the sand table and is respectively connected with the control valves and the LED lamp belts on the sand table as well as a computer in the touch screen, and the computer is connected with the external flow plate. In the invention, the process flow of natural gas pressurization and distribution is visually, vividly and realistically simulated by adopting the forms of the sand table, cartoons and the like, whether the operation of a student on the sand table is proper or not can be dynamically and interactively shown on the flow plate in real time, so that the student can achieve a feeling of being personally on the scene, thus, the training effect is increased and the training cost is reduced.
Description
Technical field
The present invention relates to oil gas accumulating multi-purpose station simulation system and method.
Background technology
The oil gas accumulating is connecting inner each link of producing, transporting, selling of petroleum industry; Its general character to practitioner's knowledge and skills requires to get more and more, adaptive requirement is also more and more strong, and slight error of operating personnel or careless might cause serious quality accident or security incident; For the country and people brings great loss; Therefore oil gas accumulating practitioner's knowledge training on duty and professional skill training just seem very important, but because nearly all oil gas accumulating is on-the-spot and facility all is distributed in the field, can not the training scene of being put into be carried out; If only rely on conventional classroom instruction or laboratory operation; Owing to lack the means and the mode of lifelike image, directly perceived lively aided education, be absorbed in simple uninteresting difficult situation unavoidably, be difficult to get a desired effect.
Existing oil gas accumulating multi-purpose station simulation system all can only be come the technological process of emulation multi-purpose station through interface operation; Facility on the sand table is fixing uncontrollable, and the for example adjusting of valve can only select " opening " perhaps " to close " valve on operation interface; The student can not take action on one's own to regulate the valve on the sand table; Teaching, training lacks the necessary sense of reality, and is further, because the facility on the sand table cannot be regulated; Simulated program is the actual effect of mirror operation dynamically just also, and training is difficult to realize the purpose envisioned equally.
Summary of the invention
The objective of the invention is to overcome the deficiency of prior art; A kind of oil gas accumulating multi-purpose station simulation system and method are provided; This system and method adopts forms such as sand table and animation, simulates the technological process of multi-purpose station intuitively, vividly, realistically, lets the student have sensation on the spot in person; The enhancement training effect reduces training cost.
The objective of the invention is to realize through following technical scheme:
Oil gas accumulating multi-purpose station simulation system; It comprises sand table, touch-screen and flow process plate; The pipeline that sand table is provided with the oil gas warehousing and transportation facilities and connects warehousing and transportation facilities; Be provided with operation valve and LED lamp band in the import and export pipeline of warehousing and transportation facilities, described warehousing and transportation facilities is distributed in bank, metering zone, dosing district, three-phase separation area, dehydration of crude oil district, stabilization of crude oil district, sewage diposal area, gas dehydration district and crude oil exporting district by function, wherein; The bank comprises at least one hydraulic fluid port; Metering zone comprises the separate measurement device, and the dosing district comprises chemicals dosing plant, and three-phase separation area comprises at least one tool triphase separator; Dehydration of crude oil district comprises heating furnace A, heating furnace B, slurry tank and electrical dehydrator; The stabilization of crude oil district comprises heat interchanger, heating furnace C, stabilizer, condenser, compressor, lighter hydrocarbons jar and at least one tool triphase separator, and the sewage diposal area comprises sewage jar, sewage pump, hydraulic cyclone degreaser, pressure degreaser, deep-bed filter, extra quality filtrator, slop oil tank, sludge tank, clarified water pump and clear water jar, and the gas dehydration district comprises filter separator, glycol jar, triethylene glycol dehydration absorption tower, glycol pump, reaction tower, agitated reactor and heat interchanger; The crude oil exporting district comprises crude oil exporting jar, heating furnace D and output pump; Sand table has the PLC controller, the PLC controller respectively with sand table on operation valve and LED lamp band and be connected with the inner computing machine of touch-screen, computing machine is connected with outside flow process plate.
Flow process plate of the present invention is a LCDs.
Oil gas accumulating multi-purpose station analogy method, it may further comprise the steps:
(1) be provided with a sand table that is used to simulate the multi-purpose station technological process, be used to gather sand table upper pipeline state the PLC controller, be used to the flow process plate controlling the touch-screen of PLC controller and be used to show the multi-purpose station technological process; Sand table is provided with some warehousing and transportation facilities; Warehousing and transportation facilities couples together with pipeline; In the import and export pipeline of each warehousing and transportation facilities, be respectively arranged with operation valve and LED lamp band; The PLC controller flows to through LED lamp band in acquisition controlling valve state and the warehousing and transportation facilities running status controlling plumbing fixtures, imports and exports the flow direction of liquid in the pipeline with simulation;
(2) multi-purpose station simulated program of operation on the touch-screen; Operating personnel open or close the one or more operation valves on the sand table according to the indication of simulated program; The variation of the real-time collection tube line state of simulated program, the variation conversion process flow process according to the pipeline state also is presented in the form of operational scheme with animation on the flow process plate in real time simultaneously.
Described simulated program comprises flow process demonstration, flow operations step; Wherein, Described flow process demonstration comprises ordinary production flow process, crude Treatment flow process, wastewater treatment flow process, gas conditioning flow process and well head flow process substep, and described flow operations comprises ordinary production flow process, crude Treatment flow process, wastewater treatment flow process, gas conditioning flow process and well head flow process substep equally.
The invention has the beneficial effects as follows: demonstrate out the technological process of multi-purpose station to the student with direct-vision methodes such as sand table, animations; The student can feed back on the flow process plate at the operating result on the sand table real-time dynamicly; Like the prompting automatically of operating mistake system; The student has sensation on the spot in person, has improved result of training greatly, has reduced training cost.
Description of drawings
Fig. 1 structured flowchart of the present invention
Structured flowchart on Fig. 2 sand table
Warehousing and transportation facilities structural representation on Fig. 3 sand table
The A of warehousing and transportation facilities structure is to figure on Fig. 4 sand table
The operational flowchart of Fig. 5 measurement flow
The operational flowchart of Fig. 6 triphase separator flow process
The operational flowchart of Fig. 7 dehydration of crude oil flow process
The operational flowchart of Fig. 8 stabilization of crude oil flow process
The operational flowchart of Fig. 9 wastewater treatment flow process
The operational flowchart of Figure 10 sewage backwash flow process
The operational flowchart of Figure 11 gas dehydration flow process
The operational flowchart of Figure 12 well head ordinary production flow process
The operational flowchart of the two-tube production procedure of Figure 13 well head
The operational flowchart of the hot wash journey of Figure 14 well head
Among the figure, 1-well head, 2-metering separator, 3-medicament stirred pot, 4-triphase separator, 5-heating furnace A, 6-slurry tank; The 7-electrical dehydrator, 8-heat interchanger, 9-stabilizer, 10-condenser, 11-compressor, 12-lighter hydrocarbons jar, 13-sewage jar; The 14-sewage pump, 15-hydraulic cyclone degreaser, 16-pressure degreaser, 17-deep-bed filter, the extra quality filtrator of 18-, 19-slop oil tank; The 20-sludge tank, 21-clarified water pump, 22-clear water jar, 23-filter separator, 24-glycol jar, 25-triethylene glycol dehydration absorption tower; The 26-glycol pump, 27-reaction tower, 28-agitated reactor, 29-heat interchanger, 30-crude oil exporting jar, 31-output pump 31; 32-heating furnace B, 33-heating furnace C, 34-heating furnace D, 101-produces main valve, and 102-produces valve, 103-check valve; 104-sleeve pipe heated scrubing valve, 105-through way valve, 106-water mixing valve, 107-shut-in valve, 108-oil pressure valve, 109-sleeve pipe testing valve.
Embodiment
Below in conjunction with accompanying drawing technical scheme of the present invention is described in further detail:
Like Fig. 1, oil gas accumulating multi-purpose station simulation system, it comprises sand table, touch-screen and flow process plate; Sand table has the PLC controller; The PLC controller is connected with the inner computing machine of touch-screen with sand table respectively, and computing machine is connected with outside flow process plate, and the flow process plate is a LCDs.
Like Fig. 2, Fig. 3, shown in Figure 4; The pipeline that sand table is provided with the oil gas warehousing and transportation facilities and connects warehousing and transportation facilities; Be provided with operation valve in the import and export pipeline of warehousing and transportation facilities; Described warehousing and transportation facilities is distributed in 9 subregions such as bank, metering zone, dosing district, three-phase separation area, dehydration of crude oil district, stabilization of crude oil district, sewage diposal area, gas dehydration district, crude oil exporting district by function, wherein each subregion composition and function are following:
(1) bank: comprise two well heads 1; All comprise on each well head 1 and produce main valve 101, production valve 102, check valve 103, sleeve pipe heated scrubing valve 104, through way valve 105, water mixing valve 106, shut-in valve 107, oil pressure valve 108 and sleeve pipe testing valve 109, it is as two cover oil wells;
(2) metering zone: comprise a tool metering separator 2, metering separator 2 has three outlets to be respectively water out, gas outlet and oil export, and this district's effect is metering respectively after oil well output object oil and gas and water is left;
(3) dosing district: comprise a tool medicament stirred pot 3, this district is pressed and delivered in the production equipment that needs after being used for mixing the interpolation medicine in process of production;
(4) three-phase separation area: comprise two tool horizontal three-phase separators 4 and a centrifugal pump, triphase separator 4 has three outlets to be respectively water out, gas outlet and oil export, and this district is used for the well head output object is separated into Oil, Water, Gas three parts;
(5) dehydration of crude oil district: comprise water-jacket typ heating furnace A5 and water-jacket typ heating furnace B32, slurry tank 6, an electrical dehydrator 7 and a centrifugal pump; It is water out and oil export that slurry tank 6 has two outlets, and it is water out and oil export that electrical dehydrator 7 has two outlets;
Wherein, water-jacket typ heating furnace 5 is used to heat the crude oil of needs dehydration with water-jacket typ heating furnace 32, lets crude oil reach the temperature that dehydration equipment needs; Slurry tank 6 is according to oil, water-mass density principle inequality, through the equipment of separating oil, water after the sedimentation; Electrical dehydrator 7 is that wet oil is passed through electric field, and emulsified particles is broken, and reaches the equipment of further dehydration;
(6) stabilization of crude oil district: comprise a large heat exchanger 8, heating furnace C33, a tool flash distillation stabilizer 9, condenser 10, a compressor 11, a horizontal three-phase separator 4 and a medium-sized lighter hydrocarbons jar 12;
Wherein, the effect of large heat exchanger 8 is because the crude oil after handling has higher temperature, through with oil-feed with fuel-displacedly carry out heat interchange and heat oil-feed; The effect of this heating furnace 33 is that oil-feed further is heated to the temperature that stabilizing equipment requires; The effect of stabilizer 9 be with crude oil through flash distillation after, be divided into stable crude and lighter hydrocarbons steam to crude oil; Condenser 10 effects are with the lighter hydrocarbons steam cooled, obtain lighter hydrocarbons and gaseous hydrocarbons; Compressor 11 effects are that the lighter hydrocarbons steam pressurized is delivered to condenser 10; The effect of this horizontal three-phase separator 4 is that lighter hydrocarbons are separated with gaseous hydrocarbons; The effect of medium-sized lighter hydrocarbons jar 12 is to store to separate the high-quality lighter hydrocarbons that obtain;
(7) sewage diposal area: comprise a sewage jar 13, sewage pump 14, hydraulic cyclone degreaser 15, pressure degreaser 16, deep-bed filter 17, extra quality filtrator 18, slop oil tank 19, sludge tank 20, clarified water pump 21, a clear water jar 22 and a centrifugal pump;
Wherein, sewage jar 13 is used for all sewage of producing in the sedimentation station; Sewage pump 14 is used for sewage disposal device is delivered in sewage pressurization in the sewage jar 13; Hydraulic cyclone degreaser 15 is through the hydraulic cyclone effect oil, water, mud to be separated; Pressure degreaser 16 is through pressurization, with oil, separated form water; Deep-bed filter 17 is used for the irreducible oil in the filtered water; Extra quality filtrator 18 is used for the irreducible oil in the filtered water; Slop oil tank 19 is used for depositing the sump oil that filters out; Sludge tank 20 is used for depositing the mud that filters out; Clarified water pump 21 is used for carrying clear water; Clear water jar 22 is used for depositing the clear water after the filtration;
(8) gas dehydration district: comprise a filter separator 23, glycol jar 24, tool triethylene glycol dehydration absorption tower 25, glycol pump 26, a tool reaction tower 27, a horizontal reacting still 28 and a horizontal heat exchanger 29;
Wherein, filter separator 23 is used for filtering the impurity in the rock gas; Glycol jar 24 is used for depositing triethylene glycol; Triethylene glycol dehydration absorption tower 25 is to use poor triethylene glycol to absorb the water in the rock gas; Glycol pump 26 is used for carrying rich glycol; Reaction tower 27 is used for rich glycol thermal dehydration is become poor glycol with agitated reactor 28; Heat interchanger 29 is through poor glycol and rich glycol heat exchange, makes rich glycol heating;
(9) crude oil exporting district: comprise a crude oil exporting jar 30, a heating furnace D34 and an output pump 31;
Wherein, crude oil exporting jar 30 is used to deposit the crude oil after the multi-purpose station dehydration is stablized; This heating furnace 34 is used to heat outer defeated crude oil; Output pump 31 is to next station with Crude Oil Transportation.
Oil gas accumulating multi-purpose station analogy method, it may further comprise the steps:
(1) be provided with a sand table that is used to simulate the multi-purpose station technological process, be used to gather sand table upper pipeline state the PLC controller, be used to the flow process plate controlling the touch-screen of PLC controller and be used to show the multi-purpose station technological process; Sand table is provided with some warehousing and transportation facilities; Warehousing and transportation facilities couples together with pipeline; In the import and export pipeline of each warehousing and transportation facilities, be respectively arranged with operation valve and LED lamp band; The PLC controller flows to through LED lamp band in acquisition controlling valve state and the warehousing and transportation facilities running status controlling plumbing fixtures, imports and exports the flow direction of liquid in the pipeline with simulation;
(2) multi-purpose station simulated program of operation on the touch-screen; Operating personnel open or close the one or more operation valves on the sand table according to the indication of simulated program; The variation of the real-time collection tube line state of simulated program, the variation conversion process flow process according to the pipeline state also is presented in the form of operational scheme with animation on the flow process plate in real time simultaneously.
Simulated program comprises flow process demonstration, flow operations step, and wherein, the flow process demonstration comprises ordinary production flow process, crude Treatment flow process, wastewater treatment flow process, gas conditioning flow process and well head flow process substep; Flow operations comprises ordinary production flow process, crude Treatment flow process, wastewater treatment flow process, gas conditioning flow process and well head flow process substep equally.
The difference of flow process demonstration and flow operations is that the flow process demonstration can only demonstrate technological process, does not receive foreign intervention in the presentation process, is unidirectional, and flow operations according to the actual conditions displaying technological process of operation, is interactively then.
The crude Treatment flow process
The crude Treatment flow process comprises measurement flow, triphase separator flow process, dehydration of crude oil flow process and stabilization of crude oil flow process.
Measurement flow such as Fig. 5, its concrete operations step is following:
(1) confirms the well head 1 of required measurement;
(2) open the fuel tap that comes of metering separator 2;
(3) open the gas outlet valve of metering separator 2;
(4) open the water out valve of metering separator 2;
(5) open the oil export valve of metering separator 2;
(6) open the valve of this well head 1 to metering zone;
(7) close the production valve 102 of this well head 1;
(8) the oil entering metering system that comes of this well head 1 is stablized metering after 1 hour.
Triphase separator flow process such as Fig. 6, its concrete operations step is following:
(1) opens the outlet valve of bank;
(2) open the valve of dosing district to three-phase separation area;
(3) open the outlet valve of medicament stirred pot 3;
(4) open the oil export valve of three-phase separation area front end triphase separator 4;
(5) open the inlet valve of three-phase separation area front end triphase separator 4, wait for that these triphase separator 4 liquid levels, pressure slowly rise;
(6) open the gas outlet valve of three-phase separation area front end triphase separator 4;
(7) open the water out valve of three-phase separation area front end triphase separator 4;
(8) open the oil export valve of three-phase separation area rear end triphase separator 4;
(9) open the inlet valve of three-phase separation area rear end triphase separator 4;
(10) open the gas outlet valve of three-phase separation area rear end triphase separator 4;
(11) open the water out valve of three-phase separation area rear end triphase separator 4.
Dehydration of crude oil flow process such as Fig. 7, its concrete operations step is following:
(1) opens heating furnace A5 inlet valve and outlet valve;
(2) start heating furnace A5: the pattern of lighting corresponding " heating furnace " on the touch-screen;
(3) open the oil export valve of slurry tank 6;
(4) open the inlet valve of slurry tank 6;
(5) open the water out valve of slurry tank 6;
(6) open inlet valve and the outlet valve of heating furnace B32;
(7) start heating furnace B32: the pattern of lighting corresponding " heating furnace " on the touch-screen;
(8) open the oil export valve of electrical dehydrator 7;
(9) open the valve that electrical dehydrator 7 arrives heating furnace B32;
(10) open the valve of electrical dehydrator 7 to the contraminated zone.
Stabilization of crude oil flow process such as Fig. 8, its concrete operations step is following:
(1) opens the valve of dehydration of crude oil district to heat exchanger 8;
(2) open the outlet valve that heat exchanger 8 arrives heating furnace C33;
(3) open the outlet valve of heating furnace C33, crude oil gets into stabilizer 9;
(4) open the oil export valve of stabilizer 9;
(5) open the gas outlet valve of stabilizer 9;
(6) open the outlet valve of compressor 11;
(7) open the inlet valve and the outlet valve of condenser 10;
(8) open the oil export valve of the triphase separator 4 in stabilization of crude oil district, oil gets into the lighter hydrocarbons jar;
(9) open the inlet valve of the triphase separator 4 in stabilization of crude oil district;
(10) open the gas outlet valve of the triphase separator 4 in stabilization of crude oil district;
(11) open the water out valve of the triphase separator 4 in stabilization of crude oil district;
(12) open the valve of stabilization of crude oil district to the gas dehydration district;
(13) open the valve of heat exchanger 8 to the crude oil exporting district, oil gets into the crude oil exporting jar;
(14) start compressor 11: the pattern of lighting corresponding " compressor " on the touch-screen;
(15) start heating furnace C33: the pattern of lighting corresponding " heating furnace " on the touch-screen.
The sewage flow process
The sewage flow process comprises wastewater treatment flow process and sewage backwash flow process.
Wastewater treatment flow process such as Fig. 9, its concrete operations step is following:
(1) opens the water out valve of slurry tank 13;
(2) open the valve of medicament stirred pot 3 to hydraulic cyclone degreaser 15;
(3) open the outlet valve of centrifugal pump 14;
(4) start centrifugal pump 14: the pattern of lighting corresponding " centrifugal pump " on the touch-screen;
(5) open the admission valve that pressure removes oil tank 16;
(6) open the inlet valve and the outlet valve of deep-bed filter 17;
(7) open the inlet valve and the outlet valve of extra quality filtrator 18.
Sewage backwash flow process such as Figure 10, its concrete operations step is following:
(1) opens the valve of medicament stirred pot 3 to clarified water pump 21;
(2) start clarified water pump 21: the pattern of lighting corresponding " centrifugal pump " on the touch-screen;
(3) open the inlet valve and the sludge outlet valve of extra quality filtrator 18;
(4) open the back flush operation valve of extra quality filtrator 18;
(5) open the inlet valve of sludge tank 20;
(6) open the inlet valve and the sludge outlet valve of deep-bed filter 17;
(7) open the back flush operation valve of deep-bed filter 17.
The gas conditioning flow process
Gas dehydration flow process such as Figure 11, its concrete operations step is following:
(1) opens the valve that rock gas gets into the gas dehydration district;
(2) start glycol pump 26: the pattern of lighting corresponding " glycol pump " on the touch-screen.
The well head flow process
The well head flow process comprises well head ordinary production flow process, the two-tube production procedure of well head and the hot wash journey of well head.
Well head ordinary production flow process such as Figure 12, its concrete operations step is following:
(1) opens production main valve 101;
(2) open production valve 102;
(3) open check valve 103;
(4) open water mixing valve 106 (, then not opening) as not seeping water.
The two-tube production procedure of well head such as Figure 13, its concrete operations step is following:
(1) opens production main valve 101;
(2) open production valve 102;
(3) open check valve 103;
(4) open sleeve pipe heated scrubing valve 104;
(5) open through way valve 105.
The hot wash journey of well head such as Figure 14, its concrete operations step is following:
(1) opens production main valve 101;
(2) open production valve 102;
(3) open check valve 103;
(4) open sleeve pipe heated scrubing valve 104.
Claims (4)
1. oil gas accumulating multi-purpose station simulation system; It is characterized in that: it comprises sand table, touch-screen and flow process plate; The pipeline that sand table is provided with the oil gas warehousing and transportation facilities and connects warehousing and transportation facilities; Be provided with operation valve and LED lamp band in the import and export pipeline of warehousing and transportation facilities, described warehousing and transportation facilities is distributed in bank, metering zone, dosing district, three-phase separation area, dehydration of crude oil district, stabilization of crude oil district, sewage diposal area, gas dehydration district and crude oil exporting district by function, and sand table has the PLC controller; The PLC controller respectively with sand table on operation valve and LED lamp band and be connected with the inner computing machine of touch-screen, computing machine is connected with outside flow process plate.
2. oil gas accumulating multi-purpose station simulation system according to claim 1, it is characterized in that: described flow process plate is a LCDs.
3. oil gas accumulating multi-purpose station analogy method, it is characterized in that: it may further comprise the steps:
(1) be provided with a sand table that is used to simulate the multi-purpose station technological process, be used to gather sand table upper pipeline state the PLC controller, be used to the flow process plate controlling the touch-screen of PLC controller and be used to show the multi-purpose station technological process; Sand table is provided with some warehousing and transportation facilities; Warehousing and transportation facilities couples together with pipeline; In the import and export pipeline of each warehousing and transportation facilities, be respectively arranged with operation valve and LED lamp band; The PLC controller flows to through LED lamp band in acquisition controlling valve state and the warehousing and transportation facilities running status controlling plumbing fixtures, imports and exports the flow direction of liquid in the pipeline with simulation;
(2) multi-purpose station simulated program of operation on the touch-screen; Operating personnel open or close the one or more operation valves on the sand table according to the indication of simulated program; The variation of the real-time collection tube line state of simulated program, the variation conversion process flow process according to the pipeline state also is presented in the form of operational scheme with animation on the flow process plate in real time simultaneously.
4. oil gas accumulating multi-purpose station analogy method according to claim 3; It is characterized in that: described simulated program comprises flow process demonstration, flow operations step; Wherein, Described flow process demonstration comprises ordinary production flow process, crude Treatment flow process, wastewater treatment flow process, gas conditioning flow process and well head flow process substep, and described flow operations comprises ordinary production flow process, crude Treatment flow process, wastewater treatment flow process, gas conditioning flow process and well head flow process substep equally.
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| CN108646701A (en) * | 2018-03-27 | 2018-10-12 | 国家电网公司 | A kind of office buildings internal control system intelligent simulation system |
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| CN108646701A (en) * | 2018-03-27 | 2018-10-12 | 国家电网公司 | A kind of office buildings internal control system intelligent simulation system |
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| CN102314794B (en) | 2013-02-13 |
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