CN206270316U - Uphole steam generator moist steam separate measurement device - Google Patents

Uphole steam generator moist steam separate measurement device Download PDF

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Publication number
CN206270316U
CN206270316U CN201621328244.3U CN201621328244U CN206270316U CN 206270316 U CN206270316 U CN 206270316U CN 201621328244 U CN201621328244 U CN 201621328244U CN 206270316 U CN206270316 U CN 206270316U
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China
Prior art keywords
high pressure
knockout drum
pressure knockout
moist steam
saturated vapor
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Active
Application number
CN201621328244.3U
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Chinese (zh)
Inventor
王贵东
李登平
刘波
刘杨
牛占涛
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Shengli Oilfield Shengji Petroleum Equipment Co Ltd
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Shengli Oilfield Shengji Petroleum Equipment Co Ltd
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Priority to CN201621328244.3U priority Critical patent/CN206270316U/en
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Publication of CN206270316U publication Critical patent/CN206270316U/en
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Abstract

The utility model is related to a kind of uphole steam generator moist steam separate measurement device.Its technical scheme is:The top of high pressure knockout drum connects saturated vapor flowmeter, bottom connection water gauge line group and the saturated flow gauge of high pressure knockout drum by vaporimeter buret group, and is aggregated into carbonated drink blender and connects moist steam outlet;The entrance of the high pressure knockout drum is provided with moist steam import, and the inner chamber of high pressure knockout drum is provided with ball float pumping equipment and cyclone separator, and the saturated vapor after separation enters the upper chamber of high pressure knockout drum, and liquid saturation water enters the lower chambers of high pressure knockout drum.Beneficial effect is:The present apparatus is used and is sufficiently separated the saturated vapor and saturation water in moist steam, accurate measurement is carried out respectively to saturated vapor and saturation water, then metric results added up again, be calculated and be shown, overcome adverse effect of the above-mentioned operating mode to certainty of measurement, can measure and obtain accurate dryness of wet steam, saturated vapor and saturation water and content, total moist steam amount.

Description

Uphole steam generator moist steam separate measurement device
Technical field
The utility model is related to a kind of uphole steam generator metering device, more particularly to a kind of uphole steam generator moist steam Separate measurement device.
Background technology
Uphole steam generator moist steam accurately and reliably measures always one problem, and conventional at present has flux of vortex street Meter, orifice flowmeter carry out two-phase flow measurement to moist steam, due to wanting parameter preset, the database set up under experiment condition, by surveying Value comparison database draws measurement result.Therefore, by moist steam working conditions change it is big, steam fluidised form is unstable, contain in water The influence of salt change, vibration etc., cause that error in dipping is big, fault rate is high, short life, it is fragile the problems such as.
The content of the invention
The drawbacks described above that the purpose of this utility model exists aiming at prior art, there is provided a kind of uphole steam generator is wet Steam separate measurement device.
Its technical scheme is:Mainly by operation base(1), moist steam import(5), high pressure knockout drum(7), vaporimeter buret Group(8), saturated vapor flowmeter(9), carbonated drink blender(11), water gauge line group(12), saturated flow gauge(13), moist steam Outlet(15)Composition, the high pressure knockout drum(7)Top pass through vaporimeter buret group(8)Connection saturated vapor flowmeter(9), High pressure knockout drum(7)Bottom connection water gauge line group(12)With saturated flow gauge(13), and it is aggregated into carbonated drink blender (11)And connect moist steam outlet(15);The high pressure knockout drum(7)Entrance be provided with moist steam import(5), high pressure knockout drum (7)Inner chamber be provided with ball float pumping equipment(4)And cyclone separator(6), saturated vapor after separation enters high pressure knockout drum Upper chamber, liquid saturation water enter high pressure knockout drum lower chambers.
Above-mentioned ball float pumping equipment(4)Mainly by floating drum(16), connecting rod(17), ball sealer(20), seal receptacle(21)Composition, Floating drum(16)By connecting rod(17)It is connected to ball sealer(20), ball sealer(20)With seal receptacle(21)Coordinate setting.
Guide cylinder(18)By supporting locating rod(19)It is connected, by guide cylinder(18)To connecting rod(17)Helped Just.
Saturated vapor flowmeter(9)With saturated flow gauge(13)Pass through signal cable respectively(14)It is connected to and collects calculating Device(10).
High pressure knockout drum(7)Bottom by exhaust-valve support(3)Connection exhaust-valve(2).
The beneficial effects of the utility model are:The present apparatus is used fully divides the saturated vapor and saturation water in moist steam From, accurate measurement is carried out respectively to saturated vapor and saturation water, then metric results are added up again, is calculated and be shown, overcome Above-mentioned operating mode can be measured and obtain accurate dryness of wet steam to the adverse effect of certainty of measurement, saturated vapor and saturation water And content, total moist steam amount.
Brief description of the drawings
Accompanying drawing 1 is structural representation of the present utility model;
Accompanying drawing 2 is the structure chart of ball float pumping equipment;
Accompanying drawing 3 is top view of the present utility model;
In upper figure:Operation base 1, the support 3, ball float pumping equipment 4 of exhaust-valve 2, exhaust-valve, moist steam import 5, whirlwind point From device 6, high pressure knockout drum 7, vaporimeter buret group 8, saturated vapor flowmeter 9, collect calculating/display 10, carbonated drink mixture Device 11, water gauge line group 12, saturated flow gauge 13, the outlet 15, floating drum 16 of signal cable 14, moist steam, connecting rod 17, guide cylinder 18th, support locating rod 19, ball sealer 20, seal receptacle 21.
Specific embodiment
With reference to accompanying drawing 1-3, the utility model will be further described:
Its technical scheme is:It is main by operation base 1, it is moist steam import 5, high pressure knockout drum 7, vaporimeter buret group 8, full Constituted with steam-flow meter 9, carbonated drink blender 11, water gauge line group 12, saturated flow gauge 13, moist steam outlet 15, it is described The top of high pressure knockout drum 7 connects saturated vapor flowmeter 9, the bottom connection water of high pressure knockout drum 7 by vaporimeter buret group 8 Gauge line group 12 and saturated flow gauge 13, and be aggregated into carbonated drink blender 11 and connect moist steam outlet 15;The high pressure point Moist steam import 5 is provided with from the entrance of tank 7, the inner chamber of high pressure knockout drum 7 is provided with ball float pumping equipment 4 and cyclone separator 6, Saturated vapor after separation enters the upper chamber of high pressure knockout drum, and liquid saturation water enters the lower chambers of high pressure knockout drum.
Wherein, ball float pumping equipment 4 is mainly made up of floating drum 16, connecting rod 17, ball sealer 20, seal receptacle 21, and floating drum 16 leads to Cross connecting rod 17 and be connected to ball sealer 20, ball sealer 20 coordinates setting with seal receptacle 21.
Guide cylinder 18 is connected by supporting locating rod 19, and righting is carried out to connecting rod 17 by guide cylinder 18, and saturation is steamed Steam flow gauge 9 and saturated flow gauge 13 are connected to tabulation calculator 10, the bottom of high pressure knockout drum 7 by signal cable 14 respectively Portion supports 3 to connect exhaust-valve 2 by exhaust-valve.
When using, the saturation moist steam that all equal integrated installations of parts are produced on base 1, by injection boiler is from wet steaming Vapor inlet 5 enters high pressure knockout drum 7, and then moist steam enters cyclone separator 6, using inertia point in cyclone separator From principle, by the saturated vapor in moist steam and liquid saturation moisture from.Saturated vapor after separation enters high pressure knockout drum 7 Upper chamber, liquid saturation water enters the lower chambers of high pressure knockout drum 7.
The saturated vapor of the upper chamber of high pressure knockout drum 7 flows through steam measurement pipe group 8 and enters saturated vapor flowmeter 9, to steaming Vapour is measured, and the saturated vapor after metering enters carbonated drink blender 11.
After the liquid saturation water water level of the lower chambers of high pressure knockout drum 7 reaches the liquid level of setting, on ball float pumping equipment 4 Floating drum 16 moved upwards in the presence of water buoyancy, by connecting rod 17 drive ball sealer 20 upwards move;The movement of connecting rod 17 Need guide cylinder 18 to be oriented to, prevent ball sealer 20 to be unable to return setting;Guide cylinder 18 fixes welding by support locating rod 19 On the outlet at bottom of high pressure knockout drum 7.After being moved on ball sealer 20, liquid saturation water enters water gauge line group by seal receptacle 21 12.The liquid saturation water water level decreasing of the lower chambers of high pressure knockout drum 7 after aqueous water outflow, floating drum 16 follows water level decreasing and downward Mobile, drivening rod 17 and ball sealer 20 are moved down, and 20 times seats of final ball sealer realize saturation water on seal receptacle 21 Sealing and Liquid level.
Saturated flow into water gauge line group 12 is measured through flowmeter 13 to saturation water, the saturation water after metering Into carbonated drink blender 11, after being sufficiently mixed with the saturated vapor entered from top, export 15 by moist steam and enter steam injection stream Cheng Guanlu.
Saturated vapor flow signal and saturation water flow wire size 14 after metering enter and collect calculating/display 10, by it Saturated vapor flow, the flow of saturation water, steam quality, total saturation wet steam flow is calculated and displayed.
After package unit operation is finished, should be by exhaust-valve 2 to the ponding and water gauge line of the lower chambers of high pressure knockout drum 7 Ponding emptying in group 12.Exhaust-valve 2 is supported by exhaust-valve support 3.
The above, is only preferred embodiment of the present utility model, and any those of ordinary skill in the art may profit Equivalent technical scheme is changed the utility model or is revised as with the technical scheme of above-mentioned elaboration.Therefore, foundation Any simple modification or substitute equivalents that the technical solution of the utility model is carried out, belong to the greatest extent what the utility model was claimed Scope.

Claims (5)

1. a kind of uphole steam generator moist steam separate measurement device, it is characterized in that:Mainly by operation base(1), moist steam enters Mouthful(5), high pressure knockout drum(7), vaporimeter buret group(8), saturated vapor flowmeter(9), carbonated drink blender(11), water gauge line Group(12), saturated flow gauge(13), moist steam outlet(15)Composition, the high pressure knockout drum(7)Top pass through vaporimeter Buret group(8)Connection saturated vapor flowmeter(9), high pressure knockout drum(7)Bottom connection water gauge line group(12)And saturation water Flowmeter(13), and it is aggregated into carbonated drink blender(11)And connect moist steam outlet(15);The high pressure knockout drum(7)Entrance It is provided with moist steam import(5), high pressure knockout drum(7)Inner chamber be provided with ball float pumping equipment(4)And cyclone separator(6), point Saturated vapor after enters the upper chamber of high pressure knockout drum, and liquid saturation water enters the lower chambers of high pressure knockout drum.
2. uphole steam generator moist steam separate measurement device according to claim 1, it is characterized in that:The ball float discharge opeing Device(4)Mainly by floating drum(16), connecting rod(17), ball sealer(20), seal receptacle(21)Composition, floating drum(16)By connecting rod(17) It is connected to ball sealer(20), ball sealer(20)With seal receptacle(21)Coordinate setting.
3. uphole steam generator moist steam separate measurement device according to claim 2, it is characterized in that:Guide cylinder(18)It is logical Cross support locating rod(19)It is connected, by guide cylinder(18)To connecting rod(17)Carry out righting.
4. uphole steam generator moist steam separate measurement device according to claim 1, it is characterized in that:Saturated vapor flow Meter(9)With saturated flow gauge(13)Pass through signal cable respectively(14)It is connected to tabulation calculator(10).
5. uphole steam generator moist steam separate measurement device according to claim 1, it is characterized in that:High pressure knockout drum (7)Bottom by exhaust-valve support(3)Connection exhaust-valve(2).
CN201621328244.3U 2016-12-02 2016-12-02 Uphole steam generator moist steam separate measurement device Active CN206270316U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621328244.3U CN206270316U (en) 2016-12-02 2016-12-02 Uphole steam generator moist steam separate measurement device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621328244.3U CN206270316U (en) 2016-12-02 2016-12-02 Uphole steam generator moist steam separate measurement device

Publications (1)

Publication Number Publication Date
CN206270316U true CN206270316U (en) 2017-06-20

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Application Number Title Priority Date Filing Date
CN201621328244.3U Active CN206270316U (en) 2016-12-02 2016-12-02 Uphole steam generator moist steam separate measurement device

Country Status (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111535798A (en) * 2020-06-19 2020-08-14 四川奥达测控装置有限公司 Steam metering system and metering method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111535798A (en) * 2020-06-19 2020-08-14 四川奥达测控装置有限公司 Steam metering system and metering method
CN111535798B (en) * 2020-06-19 2020-11-10 四川奥达测控装置有限公司 Metering method of steam metering system

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