[go: up one dir, main page]

CN203719706U - Differential pressure flow measurement device capable of improving LPG (liquefied petroleum gas) flow measurement accuracy - Google Patents

Differential pressure flow measurement device capable of improving LPG (liquefied petroleum gas) flow measurement accuracy Download PDF

Info

Publication number
CN203719706U
CN203719706U CN201420050999.6U CN201420050999U CN203719706U CN 203719706 U CN203719706 U CN 203719706U CN 201420050999 U CN201420050999 U CN 201420050999U CN 203719706 U CN203719706 U CN 203719706U
Authority
CN
China
Prior art keywords
lpg
flow measurement
differential
differential pressure
flow
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201420050999.6U
Other languages
Chinese (zh)
Inventor
唐青
王乘东
谭子龙
蔡建培
宋孝林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Hualin Industrial Gas Co Ltd
Original Assignee
Shanghai Hualin Industrial Gas Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shanghai Hualin Industrial Gas Co Ltd filed Critical Shanghai Hualin Industrial Gas Co Ltd
Priority to CN201420050999.6U priority Critical patent/CN203719706U/en
Application granted granted Critical
Publication of CN203719706U publication Critical patent/CN203719706U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Measuring Volume Flow (AREA)

Abstract

The utility model relates to a differential pressure flow measurement device capable of improving LPG (liquefied petroleum gas) flow measurement accuracy. The differential pressure flow measurement device comprises an LPG flow pipeline, a differential pressure orifice plate, pressure guide pipes and a differential pressure flow transmitter, wherein the differential pressure orifice plate is arranged in the LPG flow pipeline; the two ends of each of the two pressure guide pipes are respectively connected with the LPG flow pipeline and the differential pressure orifice plate; a hand valve is arranged on each pressure guide pipe; each pressure guide pipe between the corresponding hand valve and the differential pressure flow transmitter is connected with a pressure guide branch pipe through a tee joint; the end of each pressure guide branch pipe is connected with a plug; liquid of which the density is heavier than that of the LPG is filled in the pressure guide branch pipes and is filled in the pressure guide pipe between each hand valve and the differential pressure flow transmitter. Compared with the prior art, the differential pressure flow measurement device is simple in structure, low in cost, convenient to use and wide in application range, can eliminate the influence of the gasification of the LPG on flow measurement and can be applied to the liquid flow measurement in other similar fields.

Description

A kind of differential flow measurement device that improves LPG flow measurement accuracy
Technical field
The utility model relates to a kind of differential flow measurement device, especially relates to a kind of differential flow measurement device of the LPG of raising flow measurement accuracy.
Background technology
LPG (liquefied petroleum gas (LPG)), than being easier to liquefaction, is gaseous state at normal temperatures and pressures, be easy to change liquid state into from gaseous state, and the LPG generally using at chemical enterprise is liquid form conveying under normal temperature pressurization or atmospheric low-temperature.When using differential pressure flowmeter to measure LPG flow, LPG is drawn from mobile house steward, and connecting pipe is thinner, the LPG drawing is again static, be easy to influenced by ambient temperature and occur gasification, thereby while causing measuring flow because gasification flowmeter is inaccurate.
Chinese patent CN100425954 has announced a kind of orifice throttle differential pressure type flow measurement method and flow measurement device of low pressure loss wide-range ratio.The method comprises: by connecting pipe, high-pressure side pressure survey is chewed to the fluid pressure signal that pressure survey is chewed with low pressure end respectively and be passed to differential pressure pickup; By differential pressure pickup detected pressures difference signal; Differential pressure pickup passes to extracting operation transmitter or intelligent controller or computing machine by pressure difference signal, and obtains flow values by the pressure difference signal of receiving.This apparatus structure is comparatively complicated, and cost is higher, does not have broad applicability.
Utility model content
The purpose of this utility model is exactly that a kind of differential flow measurement device of raising LPG flow measurement accuracy simple in structure is provided in order to overcome the defect of above-mentioned prior art existence, and this device can be eliminated because LPG easily gasifies and causes the problem that flow measurement is inaccurate.
The purpose of this utility model can be achieved through the following technical solutions:
A kind of differential flow measurement device that improves LPG flow measurement accuracy, comprise LPG flow conduit, differential pressure orifice plate, connecting pipe and differential flow transmitter, described differential pressure orifice plate is located in LPG flow conduit, described connecting pipe is provided with two, the two ends of connecting pipe are communicated with LPG flow conduit and differential flow transmitter respectively, described connecting pipe is provided with hand valve, on connecting pipe between hand valve and differential flow transmitter, by threeway, be connected pilot arm, the upper end of this pilot arm connects plug, connecting pipe inside between pilot arm inside and hand valve and differential flow transmitter is full of the liquid heavier than LPG density.
One end of one of them connecting pipe is communicated with the LPG flow conduit of differential pressure orifice plate one side, the other end is communicated with the plemum of differential flow transmitter, one end of another connecting pipe is communicated with the LPG flow conduit of differential pressure orifice plate opposite side, and the other end is communicated with the negative pressure chamber of differential flow transmitter.
The liquid heavier than LPG density is selected from water or methyl alcohol.
The caliber size of described pilot arm is identical with connecting pipe.
Due to from pilot arm to being all full of the heavier liquid of density differential flow transmitter, LPG is because density gently and not can enter connecting pipe, LPG gasification can not occur in connecting pipe yet like this, therefore can eliminate because LPG easily gasifies and causes the problem that flow measurement is inaccurate.
While using device of the present utility model, by following steps, carry out flow measurement:
(1) open plemum valve, negative pressure chamber's valve and the equalizing valve on differential flow transmitter;
(2) open the plug that two pilots are propped up tube end, since a pilot, prop up the plug of tube end and fill with the liquid (as water or methyl alcohol) heavier than LPG, until another root pilot is propped up the plug place of tube end, emerge by filling liquid;
(3) the plemum valve on shut off differential pressure formula flow transmitter, negative pressure chamber's valve and equalizing valve;
(4) block plug;
(5) open hand valve, differential flow transmitter comes into operation.
Compared with prior art, the utility model is simple in structure, with low cost, can eliminate the impact of LPG gasification on flow measurement, and easy to use, can apply field similar to other and carry out liquid flow measurement, and usable range is wide.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure, 1 is LPG flow conduit, and 2 is plug, and 3 is pilot arm, and 4 is connecting pipe, and 5 is differential flow transmitter, and 6 is hand valve, and 7 is differential pressure orifice plate.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is elaborated.
Embodiment
A kind of differential flow measurement device that improves LPG flow measurement accuracy, as shown in Figure 1, comprise LPG flow conduit 1, differential pressure orifice plate 7, connecting pipe 4 and differential flow transmitter 5, differential pressure orifice plate 7 is located in LPG flow conduit 1, connecting pipe 4 is provided with two, the two ends of connecting pipe are communicated with LPG flow conduit 1 and differential flow transmitter 5 respectively, connecting pipe 4 is provided with hand valve 6, on connecting pipe 4 between hand valve 6 and differential flow transmitter 5, by threeway, be connected pilot arm 3, the upper end of this pilot arm 3 connects plug 2, connecting pipe 4 inside between pilot arm 3 inside and hand valve 6 and differential flow transmitter 5 are full of the liquid heavier than LPG density.One end of one of them connecting pipe 4 is communicated with the LPG flow conduit 1 of differential pressure orifice plate 7 one sides, the other end is communicated with the plemum of differential flow transmitter 5, one end of another connecting pipe 4 is communicated with the LPG flow conduit 1 of differential pressure orifice plate 7 opposite sides, and the other end is communicated with the negative pressure chamber of differential flow transmitter 5.The caliber size of pilot arm 3 is identical with connecting pipe 4.
LPG density ratio water is light, half of the about water of proportion, the about 0.5-0.6g/cm of density 3between, it is 1.0g/cm that the liquid heavier than LPG density is selected from water-mass density 3or methyl alcohol density is 0.7914g/cm 3.
Owing to being all full of the heavier liquid of density from pilot arm 3 to differential flow transmitter 5, LPG is because density gently and not can enter connecting pipe 4, LPG gasification can not occur in connecting pipe 4 yet like this, therefore can eliminate because LPG easily gasifies and causes the problem that flow measurement is inaccurate.
While using device of the present utility model, by following steps, carry out flow measurement:
(1) open plemum valve, negative pressure chamber's valve and the equalizing valve on differential flow transmitter;
(2) open the plug that two pilots are propped up tube end, since a pilot, prop up the plug of tube end and fill with the liquid (as water or methyl alcohol) heavier than LPG, until another root pilot is propped up the plug place of tube end, emerge by filling liquid;
(3) the plemum valve on shut off differential pressure formula flow transmitter, negative pressure chamber's valve and equalizing valve;
(4) block plug;
(5) open hand valve, differential flow transmitter comes into operation.

Claims (4)

1. a differential flow measurement device that improves LPG flow measurement accuracy, comprise LPG flow conduit (1), differential pressure orifice plate (7), connecting pipe (4) and differential flow transmitter (5), described differential pressure orifice plate (7) is located in LPG flow conduit (1), described connecting pipe (4) is provided with two, the two ends of connecting pipe are communicated with LPG flow conduit (1) and differential flow transmitter (5) respectively, described connecting pipe (4) is provided with hand valve (6), it is characterized in that, hand valve (6) is above connected pilot arm (3) by threeway with the connecting pipe (4) between differential flow transmitter (5), the upper end of this pilot arm (3) connects plug (2), connecting pipe (4) inside between pilot arm (3) inside and hand valve (6) and differential flow transmitter (5) is full of the liquid heavier than LPG density.
2. a kind of differential flow measurement device that improves LPG flow measurement accuracy according to claim 1, it is characterized in that, one end of one of them connecting pipe (4) is communicated with the LPG flow conduit (1) of differential pressure orifice plate (7) one sides, the other end is communicated with the plemum of differential flow transmitter (5), one end of another connecting pipe (4) is communicated with the LPG flow conduit (1) of differential pressure orifice plate (7) opposite side, and the other end is communicated with the negative pressure chamber of differential flow transmitter (5).
3. a kind of differential flow measurement device that improves LPG flow measurement accuracy according to claim 1, is characterized in that, the liquid heavier than LPG density is selected from water or methyl alcohol.
4. a kind of differential flow measurement device that improves LPG flow measurement accuracy according to claim 1, is characterized in that, the caliber size of described pilot arm (3) is identical with connecting pipe (4).
CN201420050999.6U 2014-01-26 2014-01-26 Differential pressure flow measurement device capable of improving LPG (liquefied petroleum gas) flow measurement accuracy Expired - Fee Related CN203719706U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420050999.6U CN203719706U (en) 2014-01-26 2014-01-26 Differential pressure flow measurement device capable of improving LPG (liquefied petroleum gas) flow measurement accuracy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420050999.6U CN203719706U (en) 2014-01-26 2014-01-26 Differential pressure flow measurement device capable of improving LPG (liquefied petroleum gas) flow measurement accuracy

Publications (1)

Publication Number Publication Date
CN203719706U true CN203719706U (en) 2014-07-16

Family

ID=51158846

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420050999.6U Expired - Fee Related CN203719706U (en) 2014-01-26 2014-01-26 Differential pressure flow measurement device capable of improving LPG (liquefied petroleum gas) flow measurement accuracy

Country Status (1)

Country Link
CN (1) CN203719706U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104807509A (en) * 2014-01-26 2015-07-29 上海华林工业气体有限公司 Differential pressure type flow measuring device capable of improving LPG flow measurement accuracy
CN110058047A (en) * 2019-05-14 2019-07-26 哈尔滨工程大学 Steam flow rate measuring system in a kind of runner

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104807509A (en) * 2014-01-26 2015-07-29 上海华林工业气体有限公司 Differential pressure type flow measuring device capable of improving LPG flow measurement accuracy
CN104807509B (en) * 2014-01-26 2018-06-12 上海华林工业气体有限公司 A kind of differential flow measurement device for improving LPG flow measurement accuracy
CN110058047A (en) * 2019-05-14 2019-07-26 哈尔滨工程大学 Steam flow rate measuring system in a kind of runner

Similar Documents

Publication Publication Date Title
CN102156087B (en) Device and method for testing rock permeability under different pore fluid pressure
CN104359819A (en) Device and method for measuring gas-water relative permeability of low-permeability compact rock core
CN203311698U (en) Comprehensive hydrodynamic experiment apparatus
CN104297126A (en) Gas seepage starting pressure gradient measuring device and method for low-permeability reservoir
CN103926180A (en) A flexible loading method for core axial stress in pore fluid displacement experiments
CN203719706U (en) Differential pressure flow measurement device capable of improving LPG (liquefied petroleum gas) flow measurement accuracy
CN105083586A (en) Device for testing aerial refueling adapter equipment
CN104458107A (en) Simple detection method of differential pressure device
CN106441698B (en) The unstable pressure difference meter of high pressure and its use and check method
CN202141666U (en) A device for testing rock permeability under different pore fluid pressures
CN201697644U (en) Integrated differential pressure flowmeter
CN204661306U (en) Diaphragm seal pressure transmitter vacuum oil filling device
CN203148508U (en) Pressure-leading device of transmitter for measuring liquid level in LNG production equipment
CN104807509A (en) Differential pressure type flow measuring device capable of improving LPG flow measurement accuracy
CN203796254U (en) Skid-mounted cone combination device for measuring volume flow of saturated steam
CN204679142U (en) A kind of pressure guiding level measurement device
CN204789223U (en) Anhydrous fracturing fluid of carbon dioxide injury testing arrangement
CN203810063U (en) Oil and gas transmission pipeline defect and corrosion detection tool
CN111220794A (en) A device for measuring gas loss during injection and production of gas storage
CN104897338A (en) Anti-freezing pressure gauge
CN104964724A (en) Liquid storage tank evaporation rate measuring device and measuring method thereof
CN212180570U (en) Spontaneous imbibition measuring device of high-pressure natural gas-water system rock core
CN203011438U (en) Gas-liquid two-phase flow pitotbar flow meter
CN203772691U (en) Ultra-low permeability core gas permeability testing device
CN103471679B (en) Method for measuring pore volume of thin pipe model

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140716

Termination date: 20190126