CN2522143Y - Computer-controlled chemicals-adding device for chemical dewatering - Google Patents
Computer-controlled chemicals-adding device for chemical dewatering Download PDFInfo
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- CN2522143Y CN2522143Y CN 02209764 CN02209764U CN2522143Y CN 2522143 Y CN2522143 Y CN 2522143Y CN 02209764 CN02209764 CN 02209764 CN 02209764 U CN02209764 U CN 02209764U CN 2522143 Y CN2522143 Y CN 2522143Y
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- microcomputer
- valves
- circuit
- stepper motor
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Abstract
The utility model belongs to a chemical dehydration computer-controlled medicating device, which controls the amount of the demulsifier injected during injection. Injecting excessive demulsifiers does not separate oil and water, affecting the output and quality of the crude oil. Based on the technical scheme, the utility model consists of a sensor, a microcomputer control system, a stepping motor and a medicating device. The device has the advantages of a convenient and correct visual reading displayed by the LED which is controlled by the medicating device, a simple computer operation facilitating automation and without debugging after running, low energy consumption, a small volume, a precise computation, non-stop running and a good reliability of the instrument.
Description
The utility model relates to a kind of general control method, system and equipment, and is particularly a kind of for Water-In-Oil in the degrading crude oil or oil-in-water chemical dehydration computer control chemicals dosing plant.
Crude oil comes out from underground mining, is carrying a large amount of moisture content, and the water in these high water-content crude oils often exists with the form that suspended state mixes, and the moisture content that suspends is distributed in the crude oil with the graininess of " Water-In-Oil " and " oil-in-water ".If adopt the physics sedimentation, disengaging time is longer, inferior separating effect.So the dehydration job requirement before a sedimentation of well head, or is injected the separating effect that " demulsifier " improves oil, water in infall process of sealing pipeline course of conveying neutralization.For addressing this problem, the utility model has designed a kind of chemical dehydration computer control chemicals dosing plant, makes water-oil separating can reach all weather operations, good separating effect, and energy consumption is low, calculates accurately.
The utility model is to adopt such method to realize: chemical dehydration computer control chemicals dosing plant is in the process of injecting " demulsifier ", need carry out quantity control to " demulsifier " that is injected.If added " demulsifier " too much would not do not have oil, moisture from effect, influence crude oil yield and quality.According to this technical scheme, the utility model has adopted by sensor, Control System of Microcomputer, stepper motor and chemicals dosing plant and has been constituted.
Sensor is the total amount that the pulse signal that adopts flowmeter to send has directly reacted the oil water mixture that flows through in the pipeline, this pulse signal is delivered to a counter behind photoelectric isolating circuit, microcomputer is regularly inquired about counter, in case find that counter overflows then with counter zero clearing again, and in the internal storage of microcomputer, add up and multiply by the flow constant, just can get the flow number in this section period.Multiply by dosing according to this flow number and just can calculate the dosing amount than coefficient.Therefore can constantly add up outflow and add dose of microcomputer, simultaneously for dosing equably, microcomputer also calculates rotating speed at next one stepper motor in the identical time interval according to adding dose, thereby control step driven by motor dosing pump is blended in the dose that should add in the water equably, throws in the pipeline through high-pressure pump and mixes with oil water mixture.
The utility model compared with prior art has following characteristics:
1, the control chemicals dosing plant is accurate by LED intuitive display convenient reading.
2, computer operation is simple, is convenient to realize automation.
3, precision metering pump in the medicament-mixing device and high-pressure low-flow pump are two groups, in order to avoid break down, influence the ordinary production operation.
4, need not debug after the operation, energy consumption is low, and volume is little, calculates accurately, and all weather operations is turned round continuously, the instrument good stability.
Concrete structure of the present utility model and embodiment are provided by the following drawings.
Fig. 1 is a circuit block diagram of the present utility model.
Fig. 2 is a chemicals dosing plant general structure schematic diagram of the present utility model.
Below in conjunction with accompanying drawing concrete structure of the present utility model and embodiment are described further.
Embodiment
See shown in Figure 1: the utility model has adopted by sensor, Control System of Microcomputer, stepper motor and chemicals dosing plant and has been constituted.
Sensor is the total amount that the pulse signal that adopts eddy currents flowmeter 1 to send has directly reacted the oil water mixture that flows through in the pipeline, this pulse signal is delivered to a counter 3 behind photoelectric isolating circuit 2, microcomputer 5 is regularly inquired about counter 3, in case find that counter 3 overflows then with counter 3 zero clearing again, and in the internal storage 6 of microcomputer 5, add up and multiply by the flow constant, just can get the flow number in this section period.Multiply by dosing according to this flow number and just can calculate the dosing amount than coefficient.Therefore can constantly add up outflow and add dose of microcomputer 5, simultaneously for dosing equably, microcomputer 5 also calculates rotating speed at next one stepper motor 12 in the identical time interval according to adding dose, thereby control step motor 12 drives dosing pump the dose that should add is blended in the water equably, throws in the pipeline through high-pressure pump and mixes with oil water mixture.
For achieving the above object, in microcomputer 5 circuit, be provided with display 4, memory 6, keyboard 7 and I/O interface circuit 8 etc.I/O interface circuit 8 is connected with photoelectric isolating circuit 9 with keyboard 7 respectively.Display 4 is used for showing date, time, accumulation dose, integrated flux, class add dose, dosing than various digital quantities such as coefficient and flow constants.Also have light emitting diode (LED) to show indication simultaneously.Memory 6 branch memory and data storages.Keyboard 7 is used for being provided with various data, and it comprises that time, date, flow, flow constant, dosing add dose etc. than coefficient, class.Native system also has the translation function of automatic working method, both when microcomputer 5 was found not have flow pulse in the same set time, will change manual type work automatically over to, at this moment can add dose according to the class of prior setting and carry out quantitative dosing.
In order to prevent the normal operation of various effect of signals microcomputers 5, microcomputer 5 systems adopt to suspend between independent voltage-stabilized power supply 13 power supplies and the various peripheral hardware and isolate, photoisolator 2,9 is all adopted in input and output, and power supply interference that this can prevent other circuit effectively etc. influences the normal operation of microcomputer 5.
The stepper motor of native system adopts three-phase six-beat system, behind photoelectric isolating circuit 9, send into the pulsqe distributor of forming by integrated package CD4017, CD4075 etc. 10 by the control impuls that microcomputer 5 is sent here, produce the needed pulse signal of three-phase, this pulse signal is delivered to three-phase drive circuit 11, the drive current of drive motors winding, thus pushing stepping motor 12 reaches controlled purpose by umber of pulse stepping rotation.
See shown in Figure 2: chemicals dosing plant of the present invention system connects two valves 24,27 at well head or multi-purpose station 22 by pipeline, two valves 24,27 connect precision metering pump 23,28 respectively, precision metering pump 23,28, by stepper motor 12 controls, precision metering pump 23,28 is exported by two valves 25,26, and connects and eddy currents flowmeters 1 by valve 29; The soup output of demulsifier jar 14 is connected with high-pressure low-flow pump 15,21 respectively by two valves 16,20, high-pressure low-flow pump 15,21 is respectively by stepper motor 12 controls, and high-pressure low-flow pump 15,21 is respectively by two valves, 17,19 input well head or multi-purpose stations 22.
Claims (1)
1, a kind of microcomputer-controlled chemically-dewatering drug-feeding equipment, it is characterized in that: the pulse signal that eddy currents flowmeter (1) is sent, behind photoelectric isolating circuit (2), deliver to a counter (3), microcomputer (5) linkage counter (3), in microcomputer (5) circuit, be provided with display (4), memory (6), keyboard (7) and I/O interface circuit (8), I/O interface circuit (8) is connected with photoelectric isolating circuit (9) with keyboard (7) respectively, microcomputer (5) is independent voltage-stabilized power supply (13) power supply, stepper motor (12) is a three-phase six-beat system, send into by integrated package CD4017 behind photoelectric isolating circuit (9) by the control impuls that microcomputer (5) is sent here, the pulsqe distributor (10) that CD4075 forms, pulse signal is delivered to three-phase drive circuit (11), the drive current of drive motors winding, pushing stepping motor (12) rotates by the umber of pulse stepping, connect two valves (24) at well head or multi-purpose station (22) by pipeline, (27), two valves (24), (27) connect precision metering pump (23) respectively, (28), precision metering pump (23), (28), control by stepper motor (12) respectively, precision metering pump (23), (28) by two valves (25), (26) output, and by valve (29) connection and eddy currents flowmeter (1), the soup output of demulsifier jar (14) is by two valves (16), (20) respectively with high-pressure low-flow pump (15), (21) connect, high-pressure low-flow pump (15), (21) respectively by stepper motor (12) control, high-pressure low-flow pump (15), (21) respectively by two valves (17), (19) input well head or multi-purpose station 22.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 02209764 CN2522143Y (en) | 2002-01-17 | 2002-01-17 | Computer-controlled chemicals-adding device for chemical dewatering |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 02209764 CN2522143Y (en) | 2002-01-17 | 2002-01-17 | Computer-controlled chemicals-adding device for chemical dewatering |
Publications (1)
Publication Number | Publication Date |
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CN2522143Y true CN2522143Y (en) | 2002-11-27 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 02209764 Expired - Fee Related CN2522143Y (en) | 2002-01-17 | 2002-01-17 | Computer-controlled chemicals-adding device for chemical dewatering |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113586009A (en) * | 2021-07-30 | 2021-11-02 | 朱刘洋 | Quantitative injection device of demulsifier for oil exploitation |
CN117049746A (en) * | 2023-09-19 | 2023-11-14 | 上海水德环保科技有限公司 | Emulsion wastewater treatment system and method |
-
2002
- 2002-01-17 CN CN 02209764 patent/CN2522143Y/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113586009A (en) * | 2021-07-30 | 2021-11-02 | 朱刘洋 | Quantitative injection device of demulsifier for oil exploitation |
CN117049746A (en) * | 2023-09-19 | 2023-11-14 | 上海水德环保科技有限公司 | Emulsion wastewater treatment system and method |
CN117049746B (en) * | 2023-09-19 | 2024-04-26 | 上海水德环保科技有限公司 | Emulsion wastewater treatment system and method |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20021127 |