Smart Vortex Flowmeter
UserManual
目录
I、Matters need attention · U1
(1)Product Applications and Working Principle ·01
(2)Product Features ·02
(3)Essential Parameter ·03
(4)Structural dimensions and characteristics of the sensor ·04
Ⅱ、Flow Range Table ·08
II、Product Model and Selection Guidelines ·11
(1)Basic Selection Principles ·11
(2)Flow Range Matching Requirements ·11
(3)Pipeline diameter compatibility ·11
(4)Selection of Signal Output and Power Supply Methods ·11
(5)Media temperature and explosion-proof selection criteria ·12
V、Install ·13
(1)Precautions Before Installation ·13
(2)Precautions During Installation ·13
(3)Flange-mountedpipeline installation ·15
(4)Installationof an insert-type vortex flow meter ·15
V、Circuit Board Operation Instructions ·21
(1)Pulse Amplification Board (without display) ·21
(2)ESeries:Three-wire/Two-wire,Field Display Type ·21
(3)VT2W-XXA- Two-wire system with temperature and pressure
compensation ·26
(4)VT3W-XXA:A three-wire system for mixed signal processing,
featuring temperature and pressure compensation capabilities ·32
(5)Modbus communication ·42
VI、Appendix Steam Density Comparison Table ·44
Delivery Inspection
When you receive this product,please check for any damage or scratches during transportation.
Check the label on the product plaque to confirm it matches the model you wish to purchase.
Transportationand Storage
Avoid strong impacts during transportation and prevent exposure to rain. Use our company's packaging whenever possible to transport the flow meterdirectlytotheinstallationsite.
When storing,use the company's original packaging whenever possible.The storage locationmustmeet the following requirements:
No rain exposure
Avoid areaswith frequentvibration or impactasmuch as possible.
Temperature: \angle 4 0 ^ { \circ } C to + 5 5 ^ { \circ } C Humidity: 5 % to 90 %
When storing used flow meters,all residual liquids and adherent substances inside must be thoroughly removed.Additionally,ensure the sealing of the powerinterface to prevent moisture ingress.
Checkbeforeinstallation
Use the flow meter under the conditions specified. Using itbeyond these specifications is not recommended.If the flow meter becomes damaged,repair costs will be your responsibility.
If your flow meter malfunctions,contact us ora technician immediately to resolve the issue.
Read the instructionscarefullybefore installation.If the flowmeter is damaged due to improper operation,you will be responsible for repair costs.
1.1ProductApplicationsandWorkingPrinciple
1.1.1ProductUse
Thevortexflowmeterisavelocity-based flowmeasurement instrument widely used for flow monitoring and measurement in process pipelinesacross industries such as petroleum,chemical,power generation,metallurgy,heating, watersupply,wastewater treatment,and light industry.It provides stable and accuratevolumetricand cumulative flowmeasurements forclean media—including liquids,gases,saturated steam,and superheated steam-free from strong corrosion or significant solid particles.This instrument serves as a versatile flow measurement device for industrial process control,energy metering,energy consumption statistics,trade settlement,and process parameter monitoring.
1.1.2 OperationalPrinciple
The vortex streetflowmeter measures flow rate based on the fluid dynamics principlesof the Karman vortexstreet.Adedicated flowobstruction (vortex generator) is installed vertically within the fluid pipeline;when the fluid flows uniformly through it,regularand stable vortex rows—knownas Karman vortex streets-are alternately generated on both sides downstream of the generator. Within aspecific velocity range,the vortex shedding frequency exhibits a strict linearrelationshipwith the fluid velocityand remains unaffected byvariations in medium temperature,pressure,viscosity,ordensity.
The formula for the vortex shedding frequency isas follows: \mathsf { \Phi } _ { = \mathsf { S } \mathsf { t } ^ { \star } \mathsf { v } \mathsf { d } }
In the formula: f-Turbulence generation frequency (Hz); St一Strouhal constant (instrument calibration constant,stable and invariant); V-Fluid velocity in the pipeline ( \mathsf { m } / \mathsf { s } ) d一Characteristic width of the vortex generator (m).
The volumetricflow rate of a pipeline is proportional to both the flow velocity and the cross-sectional area of the pipe diameter.By detecting vortex frequency signals,the instantaneous volumetricflow rate can be accurately calculated,and the cumulative total flow rate can then be obtained through integration.
1.2ProductFeatures
1.No moving parts,ensuring reliable structure and low maintenance requirements. 2.Capable of measuring various media including gases,liquids,and steam, demonstrating strong versatility. 3.Low pressure loss,wide measurement range,and low operating costs. 4.Stabie measurement accuracy,with temperature and pressure compensation supportand multiple signal outputs. 5.Specific requirements apply to the installation of straight pipe sections; special optimization is required underlow-flow-rateand high-vibration conditions.
1.3Essentialparameter
| Project | Technical Parameter |
| Nominal diameter(mm) | Pipeline type:DN15-DN300; Insert-type:DN150 andabove |
| Measuring Medium | Non-corrosive liquids,general gases,and vapors |
| Fluid Requirements | Asingle-phase clean fluid,free of large solid particlesand devoid of gas-liquid two phases. |
| Nominal Pressure (Mpa) | 1.6 (Supplyavailable upon agreement for pressures>1.6MPa) |
| Medium temperature (℃) | -40C to 250oC;-40C to 350C(high-temperature type).The recommended operating temperature should be set 30oC lower than the upper limit, witha safety margin provided. |
| Workflow Speed | Liquid: 0.5-7 m/s; Gas and steam:5-60 m/s |
| Range Ratio | 10:1~20:1 |
| BodyMaterial | 304SS;Customizable as 316L |
| Flange material | CS20#,SS304,S36L |
| Material of the transmitter housing | Custom-made castaluminumand stainless steel materials |
| Accuracy | Pipeline type: liquids±1%; gases±1.5% (customizable to±1%,depending on pipe diameterand medium). Insertion type: liquids ±2.0%; gases±2.5%. |
| Service voltage | 12 VDC,24 VDC,3.6 Vlithium battery,dual power supply |
| Output signal | Three-wire pulse output;two-wire 4-20 mA current output;Modbus-RS485 communication; HART protocol |
| Pressure drop coefficient | Complies with the JB/T9249 standard; Cd content ≤2.4 |
| Explosion-proof sign | Exia ⅡCT6Ga |
| Levels of protection | IP65 |
| Ambient condition | Environmental temperature:-20Cto 55C; Relative humidity:5% to 90%;Atmospheric pressure:86-106 kPa |
| Transmissiondistance | Three-wire pulse:≤100 mV; Two-wire 4-20 mA:load resistance ≤750Ω |
| Electrical Interface | M20×1.5,other customizations available |
| Connection Method | Pipeline type:flangeclamping,flange connection,threaded connection,clamp connection;Insertion type:simple flange installation/ballvalve-typeflangeinstallation |
| Install the straight pipe section | Upstream:≥10 DN; Downstream:≥5 DN(DN referstopipediameter). |
| Optional Features | Real-time compensation for temperature and pressure |
1.4 Structural dimensions and characteristics of the sensor
The sensor consists of three components:the sensing element, the detection amplifier,and the connecting rod.Both the housing and its constituent parts,as well as the connecting rod,are fabricated from stainless steel,exhibiting excellent corrosion resistance and mechanical strength, ensuring stableand durable long-term performance.
Theinternal vortex generator and the outer casing are joined using gasshielded self-healing welding,ensuring high weld strength and a robust structure capable ofwithstanding industrial pipeline vibrations and pressure impacts.The detection probe and vortex generator feature a separate structural design,effectively addressing the instrument failure issues associated with traditional vortex flow meters caused by pressure guide hole blockages,thereby significantly enhancing long-termreliability in media containing impurities or prone to scaling.
The overall structural design and external dimensions of the sensorare shown in the dimension diagram:
Dimensiondiagramof the flange-mountedconnectiontypevortex flowmeter
| Size (mm) | DN15 | DN20 | DN25DN32DN40DN50DN65DN80DN100DN125DN150DN200DN250DN300 | |||||||||||
| L (mm) | 100 | 100 | 100 | 114 | 114 | 122 | 122 | 122 | 141 | 155 | 170 | 195 | 213 | 228 |
| H(mm) | 462 | 462 | 462 | 470 | 475 | 483 | 497 | 513 | 532 | 560 | 590 | 640 | 702 | 755 |
| D (mm) | 125 | 125 | 125 | 145 | 145 | 160 | 180 | 195 | 215 | 245 | 280 | 335 | 405 | 460 |
| D1 (mm) | 100 | 100 | 100 | 120 | 120 | 125 | 145 | 160 | 180 | 210 | 240 | 295 | 355 | 410 |
| N (pce) | 4 | 4 | 4 | 4 | 4 | 4 | 4 | 6 | 8 | 8 | 8 | 12 | 12 | 12 |
| D(mm) | 14 | 14 | 14 | 14 | 14 | 18 | 18 | 18 | 18 | 18 | 22 | 22 | 26 | 26 |
Dimensionsof the flange-connected vortex flowmeter
| Size (mm) | DN15DN20DN25DN32DN40DN50DN65DN80DN100DN125DN150DN200DN250DN300 | |||||||||||||
| L(mm) | 180 | 180 | 180 | 180 | 180 | 180 | 200 | 200 | 200 | 220 | 220 | 220 | 250 | 300 |
| H(mm) | 440 | 448 | 455 | 471 | 480 | 493 | 510 | 525 | 545 | 573 | 603 | 655 | 713 | 765 |
| D(mm) | 95 | 105 | 115 | 140 | 150 | 165 | 185 | 200 | 220 | 250 | 285 | 340 | 405 | 460 |
| D1(mm) | 65 | 75 | 85 | 100 | 110 | 125 | 145 | 160 | 180 | 210 | 240 | 295 | 355 | 410 |
| N(pce) | 4 | 4 | 4 | 4 | 4 | 4 | 8 | 8 | 8 | 8 | 8 | 12 | 12 | 12 |
| D(mm) | 14 | 14 | 14 | 18 | 18 | 18 | 18 | 18 | 18 | 18 | 22 | 22 | 26 | 26 |
Dimensionsofthethreaded-typevortexflowmeter
| Size (mm) | DN15 | DN20 | DN25 | DN32 | DN40 | DN50 |
| L (mm) | 120 | 120 | 120 | 120 | 120 | 120 |
| H (mm) | 412 | 412 | 414 | 425 | 431 | 442 |
| A | G1/2" | G3/4" | G1" | G1 1/4" | G1 1/2" | G2" |
Dimensions of the clamp-connected vortex flowmeter
| Size | DN15 | DN20 | DN25 | DN32 | DN40 | DN50 |
| L (mm) | 110 | 110 | 110 | 110 | 110 | 110 |
| H (mm) | 393 | 395 | 398 | 401 | 405 | 410 |
| D (mm) | 50.5 | 50.5 | 50.5 | 50.5 | 64 | 64/77.5 |
1.This size complies with the DIN 32676/ISO 2852 standard for sanitary clamps; other sizes are customized according to specific requirements. 2.The above-mentioned dimensions shall have a tolerance of ± 2 { \mathsf {mm } } ,andheight dimensions shall have a tolerance of ± 5 { \mathsf {mm } }
InsertionDepthTablefor InsertableVortexStreetFlowMeters
Simple-type flange connection; Flange ball valve type
Simple-type flange connection; Flange ball valve type
| DN | DN250 | DN300 | DN400 | DN500 | DN600 | DN800 | DN1000DN1200 | |
| L | 125 | 150 | 133 | 167 | 200 | 267 | 250 | 300 |
The selection of flowmeter diameter is critical and must adhere to specific principles:consider the maximum,common,and minimum flow rates of the measured fluid;the highest, common,and minimum pressures;the highest, common,and lowest temperatures;and ensure the flow measurement falls within the instrument's optimal operating range (i.e.,between 1/2and 2/3 of the upper flowrate).
| bore (mm) | liquid(Validationmedium: wateratroomtemperature) | gas(Referencemedium:airat 20C and 101,325 Pa) | ||
| range (m³/h) | Rutput Frquency | Mengure/nt | Output Frequency | |
| 15 | 0.6~6 | 30~585 | 2.8~15 | 275~1460 |
| 20 | 0.8~8 | 40~400 | 2.5~50 | 220~2000 |
| 25 | 1.2~12 | 25~336 | 8.5~70 | 190~1140 |
| 32 | 2~20 | 21~205 | 18~130 | 185~1340 |
| 40 | 2.5~25 | 10~200 | 22~220 | 140~1040 |
| 50 | 3.5~35 | 8~160 | 36~320 | 94~1020 |
| 65 | 6.5~68 | 8~80 | 50~480 | 60~215 |
| 80 | 10~100 | 4.1~82 | 70~640 | 55~690 |
| 100 | 15~150 | 4.7~69 | 130~1100 | 42~536 |
| 125 | 27~275 | 5~45 | 200~1700 | 35~285 |
| 150 | 40~400 | 2.8~43 | 280~2240 | 33~380 |
| 200 | 80~800 | 2~31 | 580~4960 | 22~315 |
| 250 | 120~1200 | 1.5~25 | 970~8000 | 18~221 |
| 300 | 180~1800 | 1.2~24 | 1380~11000 | 16~213 |
| (300) | 100~1500 | 5.5~87 | 1560~15600 | 85~880 |
| (400) | 180~3000 | 5.6~87 | 2750~27000 | 85~880 |
| (500) | 300~4500 | 5.6~88 | 4300~43000 | 85~880 |
| (600) | 450~6500 | 5.7~89 | 6100~61000 | 85~880 |
| (800) | 750~10000 | 5.7~88 | 11000~110000 | 85~880 |
| (1000) | 1200~17000 | 5.8~88 | 17000~170000 | 85~880 |
| >(DN1000) | Agreement-based Supply | |||
| Dn15 to DN300 are pipe-type; DN300 to DN1000 are insert-type. | ||||
Pour:
1.The flow range in the table covers from the minimum flow rate required for long-term stable operation of the instrumentto the maximum operating flow ratespecified forthe pipeline duringcustomer selection.
2.The gas flow rate in the table represents the volumetricflow rate under operatingconditions.
3.The flow rates of liquids and general gases are volumetric flows.To convertthemtomassflowrates,usethe followingformula:
{ \mathsf { Q } } { \mathsf { m } } = { \mathsf { Q } } { \mathsf { v } } x { \mathsf { \rho } } Where:
Qm:Mass flow rate of the test fluid ( \mathsf {kg } / \mathsf { h } ) (2 Q:The volumetric flow rate of the test fluid ( m ^ { 3 } / \mathsf { h } ) p:Operating density of the test fluid ( \mathsf {kg } / \mathsf { m } ^ { 3 } )
4.Steam measurement typically uses mass flow rate as the settlement unit.
The operating density must be determined based on known steam pressure and temperature,afterwhich the mass flow rate iscalculated from thevolumetric flow rate using theaforementioned formula.
SaturationSteamFlowRangeTable
Basic operating condition parameters
| Absolute Pressure (Mpa) | 0.2 | 0.3 | 0.4 | 0.5 | 0.6 | 0.7 | 0.8 | 1 | 1.2 | 1.4 | 1.6 |
| Saturation temperature(℃) | 120 | 134 | 144 | 152 | 159 | 165 | 170 | 180 | 188 | 195 | 201 |
| SteamDensity (kg/m3) | 1.13 | 1.652.162.673.173.674.165.15 | 6.137.11 | 8.09 |
| DN20 TO DN50 (FLOW RATE: KG/H) | |||||||||||||
| Nominaldiameterdischargepattern.2MPa0.3MPa0.4MPa0.5MPa0.6MPa0.7MPa0.8MPa1.0MPa1.2MPa1.4MPa1.6MPa | |||||||||||||
| DN20 | Qmin | 6.215 | 9.075 | 11.88 | 14.685 | 17.43520.185 | 22.88 | 28.325 | 33.71539.10544.495 | ||||
| Qmax | 56.5 | 82.5 | 108 | 133.5 | 158.5 | 183.5 | 208 | 257.5 | 306.5 | 355.5 | 404.5 | ||
| DN25 | Qmin | 9.605 | 14.025 | 18.36 | 22.69526.94531.195 | 35.36 | 43.77552.10560.43568.765 | ||||||
| Qmax | 79.1 | 115.5 | 151.2 | 186.9 | 221.9 | 256.9 | 291.2 | 360.5 | 429.1 | 497.7 | 566.3 | ||
| DN32 | Qmin | 20.34 | 29.7 | 38.88 | 48.06 | 57.06 | 66.06 | 74.88 | 92.7 | 110.34127.98 | 145.62 | ||
| Qmax | 146.9 | 214.5 | 280.8 | 347.1 | 412.1 | 477.1 | 540.8 | 669.5 | 796.9 | 924.3 | 1051.7 | ||
| DN40 | Qmin | 24.86 | 36.3 | 47.52 | 58.74 | 69.74 | 80.74 | 91.52 | 113.3 | 134.86156.42 | 177.98 | ||
| Qmax | 248.6 | 363 | 475.2 | 587.4 | 697.4 | 807.4 | 915.2 | 1133 | 1348.61564.2 | 1779.8 | |||
| DN50 | Qmin | 40.68 | 59.4 | 77.76 | 96.12 | 114.12 | 132.12 | 149.76 | 185.4 | 220.68255.96291.24 | |||
| Qmax | 361.6 | 528 | 691.2 | 854.4 | 1014.4 | 1174.4 | 1331.2 | 1648 | 1961.62275.22588.8 | ||||
| DN65TO DN300 (FLOW RATE:T/H) | |||||||||||||
| DN65 | Qmin | 0.05650.0825 | 0.108 | 0.13350.15850.1835 | 0.208 | 0.25750.30650.35550.4045 | |||||||
| Qmax | 0.5424 | 0.792 | 1.0368 | 1.2816 | 1.5216 | 1.7616 | 1.9968 | 2.472 | 2.94243.41283.8832 | ||||
| DN80 | Qmin | 0.0791 | 0.11550.1512 | 0.18690.2219 | 0.2569 | 0.2912 | 0.36050.4291 | 0.49770.5663 | |||||
| Qmax | 0.7232 | 1.056 | 1.3824 | 1.70882.0288 | 2.34882.6624 | 3.296 | 3.9232 | 4.5504 | 5.1776 | ||||
| DN100 | Qmin | 0.1469 | 0.2145 | 0.2808 | 0.3471 | 0.4121 | 0.4771 | 0.5408 | 0.6695 | 0.7969 | 0.9243 | 1.0517 | |
| Qmax | 1.243 | 1.815 | 2.376 | 2.937 | 3.487 | 4.037 | 4.576 | 5.665 | 6.743 | 7.821 | 8.899 | ||
| DN125 | Qmin | 0.226 | 0.33 | 0.432 | 0.534 | 0.634 | 0.734 | 0.832 | 1.03 | 1.226 | 1.422 | 1.618 | |
| Qmax | 1.921 | 2.805 | 3.672 | 4.539 | 5.389 | 6.239 | 7.072 | 8.755 | 10.42112.087 | 13.753 | ||
| DN150 | Qmin | 0.3164 | 0.462 | 0.6048 | 0.74760.8876 | 1.0276 | 1.1648 | 1.442 | 1.71641.99082.2652 | |||
| Qmax | 2.5312 | 3.696 | 4.8384 | 5.98087.10088.2208 | 9.3184 | 11.53613.731215.926418.1216 | ||||||
| DN200 | Qmin | 0.6554 | 0.957 | 1.25281.54861.83862.1286 | 2.4128 | 2.987 | 3.55544.1238 | 4.6922 | ||||
| Qmax | 5.6048 | 8.184 | 10.713613.243215.723218.203220.633625.54430.404835.265640.1264 | |||||||||
| DN250 | Qmin | 1.0961 | 1.6005 | 2.0952 | 2.58993.0749 | 3.5599 | 4.0352 | 4.99555.9461 | 6.8967 | 7.8473 | ||
| Qmax | 9.04 | 13.2 | 17.28 | 21.36 | 25.36 | 29.36 | 33.28 | 41.2 | 49.04 | 56.88 | 64.72 | |
| DN300 | Qmin | 1.5594 | 2.277 | 2.9808 | 3.68464.37465.06465.7408 | 7.107 | 8.45949.811811.1642 | |||||
| Qmax | 12.43 | 18.15 | 23.76 | 29.37 | 34.87 | 40.37 | 45.76 | 56.65 | 67.43 | 78.21 | 88.99 |
remarks
Medium:Saturated steam,all pressuresare absolute pressures; Flowrate for DN20-DN50: \boldsymbol { {kg / h } } ; for DN65-DN300:t/h. Qmin \mathbf { \Sigma } = \mathbf { \Sigma } minimum flow rate measurable by the instrument;Qmax \mathbf { \Sigma } = \mathbf { \Sigma } rated maximumflowrateofthe instrument.
3.1Basic SelectionPrinciples
Before selection,first determine the type of fluid to be measured and its operating flow range (which may be an estimated value).Then,based on the corresponding specifications for different fluids in the "Flow Range Table" provided in this manual,choose the appropriate vortex flowmeter model.
3.2FlowRange Matching Requirements
The actual flow rate of the measured medium within the pipeline must fall within the measurement range of the selected flow meter;otherwise, measurement accuracy and equipment safety cannot be guaranteed.It is recommended to maintaina long-term stableoperating flow rate between1/2 and 2/3 of the full measurement range to balance both accuracy and stability.
3.3Pipelinediametercompatibility
If the actual pipe diameter does not match the nominal diameter of the selected flow meter,adjust the pipe diameter using reduction or expansion techniques to ensure compatibility between the flow meter's diameterand operating flow conditions,thereby guaranteeing proper instrument operation.
3.4Selectionof Signal Outputand Power SupplyMethods
Select the signal output method based on the site application and installation conditions according to the following principles:
When measuring compressible fluids under conditions with significant variations in field medium temperature and pressure,it is recommended touse a vortex flow sensor equipped with pulse signal transmission capability,paired witha flow integrator featuring temperature and pressure compensation functions.The accompanying pressure transmittersand temperature transmitters (PT1oO) must be purchased separately by the user.
If the flow meter is installed in a well-conditioned indoor environment where signal transmission is unnecessary and on-site flow reading suffices,with the installation location facilitating operation and reading,a battery-powered direct-read vortex flow meter may be selected.For outdoor installations, battery-powered modelsare not recommended.
If the installation environment is poor,the location is inconvenient for onsitereading,or centralized management is required,itisrecommended to use a pulse-output sensor paired with a flow integrator,ora vortex flow transmitter withastandard 4 { * } 2 0 \mathsf { m A } current output.
When simultaneous on-site flowmeasurementand remote signal transmission are required,a vortex flow transmitter with direct on-site reading capability,along with 4 { * } 2 0 \mathsf { m A } output and RS485 communication functionality, is recommended.
When on-site reading is not required and only standard signals need to be transmitted remotely to the control system,a vortex flow transmitterwith a 4-20 mA standard current output is recommended.
3.5Media temperatureand explosion-proof selectioncriteria
Selecta vortex flowmetercorresponding to the temperature rangeof the measured medium:for temperatures between 2 5 0 ^ { \circ } C and 3 5 0 ^ { \circ } \mathsf C , use the hightemperature model (typically equipped with a heat dissipation structure).In explosion-proof environments,exclusively employ explosion-proof vortex flowmeters paired with intrinsically safe barriers orotherexplosion-proof equipment to ensure fullcompliance with explosion-proof standards.
4.1PrecautionsBeforelnstallation
4.1.1 scope of application
These installation proceduresapply to the installation of flow meters in this seriesdesigned forvortex-streak (steam) flowmeasurement.
4.1.2Upon arrival inspection
Upon delivery,verify each instrument's quantity,model,and nominal diameter individually,and inspect the instrumentbody forany damage or deformation.
4.1.3AttachmentCount
Upon opening the box,inspect allaccompanying accessories:flanges,bolts, nuts,sealing gaskets,product manuals,and quality certificates should be complete and in good condition.
4.1.4MaterialReading
Before formal installation,please read thismanual thoroughly.Forany technical questions,contact our after-sales support team promptly.
4.2PrecautionsDuring lnstallation
1.Each flowmeter hasa specificapplication range; please verify before installation that the purchased unit meets the site's operating conditions (flow rate,temperature,pressure).
2.The vortex flowmeter can measure liquids,gases,and steam,but it is not interchangeable between different media;for the same medium,it isavailable in three specifications (low-temperature,medium-temperature,and hightemperature),and italso lackscompatibilityacrossdifferent temperature ranges.
3.Avoid exposure to high-voltage equipment,high-frequency devices,and powerful switching power supplieswhenever possible.The power supply for instruments should be isolated from these devicesasmuch as feasible.
4.Avoid direct exposure to high-temperature heat sourcesand radiation sources.If installationisunavoidable,thermalinsulationand ventilation measuresmustbeimplemented.
5.Avoid high-humidity environments and areas with strong corrosive gases. If installation is necessary,adequate ventilation measures mustbe implemented.
6.Explosion-proof sensors and transmitters must be installed in hazardous areas,while associated equipment such as safety barriers,display instruments, powersupplies,and computers shall be installed in safe locations.Sensors and transmitters require reliable grounding;the explosion-proof ground wire must not share the protective grounding of high-voltage electrical systems.
7.Flow meters should preferably not be installed on long overhead pipelines,as pipeline sagging can easily cause sealing leaks between the flow meterand its flange.If installation is unavoidable,support pointsmust be provided at both upstream and downstream positions of the flow meter along the pipeline.
8.Vortex flow meters should be avoided when installed on pipelines subject to significant vibration.If installation is unavoidable,pipeline securing devices mustbe installed at both upstream and downstream positions along the 2D section,accompanied by vibration isolation pads,supports,or flexible hoses to enhance vibration resistance.
9.The instrument should preferably be installed indoors.When installed outdoors,measures must be taken to ensure waterproofing,moisture resistance, and sun protection.Special attention should be paid to bending the cable into a " \mathsf { U } ^ { \ast } shape at electrical interfaces to prevent water from entering the amplifier housing through the cable.
10.The pipeline where the flow meter is installed must comply with the straight pipe sections specified in this manual; failure to do so may compromise the measurement accuracy of the flow meterand,in severe cases,cause damage to the device.
11.During flow meter installation,the device must not be placed on the pipeline while welding flanges or connecting pipes to prevent damage to its internal components.
12.Flow meters can be installed on either horizontal orvertical pipelines. When installed on a vertical pipeline and measuring a liquid medium,the fluid must flow from bottom to top.
13.Flow meters should not be installed too close to valve outlets,as valve operation may compromise the meter'sservice life and,in severe cases,cause damage.To facilitate maintenance,a bypass pipeline must be installed, particularly in processes where fluid flow cannot be interrupted mid-process.
14.Before operating the flow meter,carefully verify that its installation and wiring are correct.
15.After powering on,check if the LCD screen displaysany flow indication.
16.Gradually open thevalve forat least 2minutesuntil reachinga lower pressure level,then stop.Check forany leaksaround the sensorand verify that theLCD screen displays proper flow rate.If everything is normal,fully open the valve,allow it to stabilize fora period,and confirm the displayed flow rate remainsaccurate.
17.Users must follow the instructions and warnings in this user manual to ensure properand safe operation of the instrument.
4.3Flange-mountedpipelineinstallation
Flow meter;Metal winding gasket for flanges; Pipeline nuts;Bolt washers Perform spot welding to position the flange and pipeline.
Remove the flow meter,weld the flange as specified,and clean all protruding partsinside the pipeline.
Install a sealing gasket with the same diameter as the pipeline within the innergroove of the flange,then mount the flow meter inside the flange.
The flow indicator on the meter must align with the fluid direction and be securelyfastenedwithbolts.
4.4lnstallationof an insert-type vortexflow meter
Use gas welding to create a 9 0 ~ \mathsf {mm } circular hole in the pipeline,and thoroughly remove all burrs around the hole to ensure smooth rotation of the probe.
Weld the manufacturer-provided flange onto the circular pipe opening, ensuring itsaxis is perpendicular to the pipe axis.
nstall the ball valve and sensoron the welded flange.
The fluid flow direction must match the arrow indicated on the flowlabel. Tighten the fixing bolts and nuts uniformly between the flanges and the ball valve.
Check whether each step has been properly completed,then slowly open the valve to observe forany leaks (special attention mustbe paid to personal safety). If there isa leak,repeat the previous step.
Installation Requirements for Instrument Pipelines:Turbulent flow meters have specific requirements for the straight pipe sections upstreamand downstream of the installation point; failure to meet these requirements may impairfluid flow within the pipeline and compromise measurement accuracy. The required lengths of straight pipe sections upstream and downstream of the instrument are as follows:
Concentrically shaped fully open valve with two 90-degree elbows on different planes
Concentrically shaped fully open valve with two 90-degree elbows on different planes
A90-degree elbow with concentric pipe expansion A90-degree elbow with concentric pipe expansion
Two 90-degree elbows on the same plane; control valve in half-open position (not recommended)
Two 90-degree elbows on the same plane; control valve in half-open position (not recommended)Pour:
DNis the instrument diameter,in mm
The control valve should preferably notbe installed upstream of the vortex flowmeterbut rather10Ddownstreamof it.
The inner diameters of upstream and downstream pipelines must be identical.If discrepancies exist,the pipeline inner diameter Dpand the vortex flow meter's housing inner diameter Db mustsatisfy the following relationship: 0 . 9 8 \mathsf { D b } \le \mathsf { D p } \le 1 . 0 5 \bar { \mathsf { D b } } .Both upstream and downstream pipelines shall be compatible with the flow meter housing.
The innerdiametersare concentric,and the difference in theiraxial dimensionsshouldbelessthanO.05dB.
The sealing gasket between the instrument and the flange must not protrude into the tube during installation;its inner diameter should be larger than that of the instrument body 1 - 2mm ¥
Installation design for pressure and temperature measurement ports:When temperature and pressure transmittersare required for the pipeline under measurement,the pressure measurement port should be located 3-5D downstream,while the temperature measurement port should be positioned 6-8D downstream.Special attention must be paid to insulation measures when measuring high-temperature or low-temperature fluids.Theinternal temperature within the converter (within the meter head housing) should generally not exceed 7 0 ^ { \circ } C ; excessively low temperatures may cause condensation inside the converter,reducing the insulation impedance of the printed circuit board and impairing normalinstrument operation.
Ata higher point along the pipeline,as shown in the figure The instrument can be installed horizontally, vertically,or at an angle on the pipeline.
On horizontal pipelines,when measuring gas containing trace amounts of liquid,the flow meter should be installed at a higher point on the pipeline,as shown in the figure.
For horizontal pipelines,when measuring liquids containing trace amounts of gas,the flow meter should be installed at the lowest point of the pipeline,as shown in the figure.
When measuring gas in a vertical pipeline,instruments are installed along the pipeline with no restriction on gas flow direction.However,if the pipeline containsa small amount of liquid,the gas flow should move upward from the bottom to prevent liquid from entering the instrument's measurement tube.For measuring liquid flow,the liquid must flow upward from the bottom,as shown in the figure.
4.4.1InstallationRequirements
The installation site must be free from severe vibrations and strong magnetic interference.In the presence of intense vibrations,vibration mitigation measures should be implemented,such as using vibration-damping supportsor flexible rubber shock-absorbing pads.
The installation site must ensure convenient conditions for installation and maintenanceoperations.
The area surrounding the installation site must not be filled with corrosive gases and must not be at risk of water inundation.
The vortex flowmeter displayed on-site must not be directly exposed to sunlight or intense solar radiation;in such cases,necessary shading measures should be implemented.
The direction of the flow arrow on the vortex flowmeter must align with the direction of fluid flow within the pipeline.
When measuring liquids,ensure the pipeline is fully filled.When vertical installation is required,the fluid must flow from bottom to top.
Aflow control valve should not be installed upstream of the flow meter; instead,it should be placed downstream.
The upstream and downstream sections of a vortex flowmeter must be equipped with straight pipe segments of sufficient length according to the actual site conditions.
way to install
For split-type systems with temperature and pressure compensation, the installation requires both a pressure transmitter and a temperature transmitter when pressure or temperature compensation is needed.The pressure tapping hole should be located 3-5 DN downstream of the sensor,with a diameter of 3 - 1 3 ~ \mathsf {mm } .The temperature measurement point should be positioned 6-8 DN downstream of the sensor.
When installing a flanged vortex flowmeter on a pipeline,to ensure accurate and reliable installation,first bolt the flowmeterand theflanged fitting together, then weld the flanged fitting to the pipeline.To prevent damage to the flowmeter caused by excessive temperature duringwelding,perform spot welding first,then remove the flowmeter before proceeding with welding.To facilitate maintenance and inspection,a bypass pipe may be installed on the outer side of the straight pipe sections upstream and downstream of the vortex flowmeter to prevent interference with its measurement performance.
This product comes with four types of matching circuit boards.Select the appropriate board type for your purchased instrumentand follow the instructions in the corresponding section.
1.Pulse Amplification Board (without display) 2.ESeries:Three-wire/Two-wire,FieldDisplay Type 3.VT2W-XXA-Two-wire systemwith temperature and pressure compensation 4.VT3W-XXA:A three-wire system for mixed signal processing, featuring temperature and pressure compensation capabilities.
5.1PulseAmplificationBoard(withoutdisplay)
This board lacksdisplay functionality and isdesigned for use with secondary instruments such as flowaccumulators and paperless recorders that feature pulse input capabilities.
Line Connection Definition
V+:Positive terminal of the external DC 24V power supply Error:Pulse signal output port GND:Negative terminal of the power supply; common ground for pulse utput
5.2ESeries:Three-wire/Two-wire,Field DisplayType
This board lacks temperature and pressure compensation functions,making it suitable for measuring volumetric flow rates in liquid and gas applications.
Screen Display Instructions
After power-on,the device displays all data in four rows.The format and meaningsareasfollows:
First row:Cumulative flow.Maximum of9 digits (including 3decimal places); theunitmatches thatof instantaneous flow.
Second row:Instantaneous flow rate,rounded to two decimal places.
Third row: Frequency data,format \mathsf { F } = \mathsf { X } \mathsf { X } \mathsf { X } \mathsf { X } . \mathsf { X } \mathsf { H } z , with1decimal place retained;
Displays F L = X X . X H z :indicates triggering the removal of the flowlower limit;
Displays F C 5 = 0 . 0 H z :indicateseliminationof 5 0 / 6 0 \mathsf { H z } powerfrequency interference.
Fourth row:Current output value,format 1 = x x . x x m A with2decimal places.
LineWiring Definition
2 4 \lor + :Positive input ofaDC24V power supply 24V-:Negative input terminal of the DC 24V power supply/Common point for \mathsf { V } + /Fo:Pulse circuit DC 24V positive input Error:Pulse signal output port GND:Negative input of the DC 24V pulse circuit
two-wire current output
Note:The pulse output requires proper power supply from the main current circuit to operate;it deliversan optically isolated raw pulse (uncalibrated) and is primarily used for instrument calibration.The signal type isan NPN collectoropen outputwitha built-in 2 1 x \Omega pull-up resistor.
Run Interface Switch
Afterpower is turned on,the instrument first performsa self-testand then enters the main display mode on Screen 1.
Use the " < " or"+"key to switch between Work Screen2and Work Screen 1
User Parameter Settings
Button Function Definitions
Long press the ^ + key(1 second) = { \sf S } key: Exit current input/modification state
Long press the <key(1 second) = \mathtt { E } key to confirm and save settings Short press the ^ + key to switch cursor position between numbers and options
Short press the <key to move the cursor right
Data input supports up to 8 digits (including symbols and decimal points)
BasicMenu Operations
Menu navigation:Press the ^ + key to scroll down,press the <key to scroll up; press Eto entera submenu,pressS to return to the main interface.
Submenu Operations: Press S to exit the submenu; press E to enter edit mode.
Optionmodification:Use the ^ + keyto select downward,the<keyto select upward,and theEkeyto confirm.
Number modification: Enter data according to the above key rules and press E to confirm.
Important:Aftermodifying parameters,press the Ekey to save;otherwise, the settings will be invalid.
ParameterMenuOverviewTable
Enterthedefault password inthe parametermenu:22
| order number | Menu Name | function declaration | Windows Optional Range/ default | ParameterRequirements |
| 1 | Selection | CowUniration | 0 | 0:m³/h 1: m³/Qmin 2:L/h 11:pounds/Qmin |
| 2 | Algorithm Selection | Melectiement Algorithm Types | 0 | 00:Standard volumetric flow rate 01:Standard mass flow rate 02:Standard gas volumetric flow rate 04:Staudardsasmassflow (temperature compensation) 05:Saturated steam (pressure compensation) 06:Superheated steam (temperatureand pressure |
| 3 | dischicient | Coerient | 3600 | compensation) Unit:Ppatacerding tothe |
| 4 | fluid density | Media Density | 1000 | thisctind is gorithmso1oro3 (mass flow rate),with unit:kg/m3 |
| 5 | Full Flow Rate | Flow rateof 4-20mA across full range | 1000 | Required when enabling simulated current output;the value cannot be O; unit consistent with flow rate |
| 6 | Drainage flow | Small-flow resection percentage | 1% | Range:0-50 |
| 7 | Tettingrature | Temratinture Setting | 0 | this tild isgorithmsryz,0,04, or 06.Unit:C |
| 8 | Standerature | Standard Temeperature | Optional: Scientific condition (0C), Engineering condition (20C) | |
| 9 | Pretinre | AbspPressure | 101.325 | This field is mandatory when selecting algorithms 02,03,05,or 06:thentiso.owillrting hefuw rate to zero. |
| 10 | damping | Dutput/Show | 4s | Racte:2-32, suppressesflow |
| 11 | postess | Rstrument Address | 0 | Only three-line board cardsare valide withadrese ofnot The repeated. |
| 12 | Cemmunication RS485baud | 4800 | Only third-line boards are valid. Options:4800,9600,or Off | |
| 13 | Tumulative Amount | Cumulative flow | 一 | After confirmation,enterpassword |
5.3VT2W-XXA-Two-wire system with temperature and pressure compensation
This product features temperature and pressure compensation capabilities, enabling measurement of volumetric flow ratesunderworking conditions for liquids,gases,and steam,as well as standard-state volumetric flow rates for gases and mass flow rates forsteam.Italso includes Hart communication functionality.The specificdetails regarding temperature and pressure compensation and Hart communication capabilities are subject to the actual product specifications.
video display
The first row shows cumulative flow.
The second row displays the instantaneous flowrate.
The third row displays the temperature value.
The fourth row displays the pressure value.
Line Wiring
mA ^ + :24VDC+power input
mA-:24VDC power input;two-wire
currentoutput
\mathsf { V } + :Pulse input of24VDC
Error:Pulse output
Vss:Pulse inputof24VDC TRH:PT100 Input
TRL: PT100 Input
PIH:Pressure signal voltage input ^ + PVH:Pressure-powered output ^ +
PVL:Pressure Power Supply OutputPIL: Pressure signal voltage input
FlowMeterWorkInterface
The flow meter's operation interface consists of two sections: the main interface and the auxiliary interface,as shown in the figure.
Cumulative flow→ 1000000.0m3 Instantaneous flow→ 1000.0 instantaneous m3/h flowunit Medium temperature→ T=25.5℃ Medium pressure→ P=101.3KPa flowpercentageChart1MainWork Interface Signal frequency- Fin=500.0Hz Output current value一 Iout=12.000mA Output frequencyvalue- Fout=500.00Hz Enter password box- Password:00
User ParameterSettings
Button Function Definitions
Long press the ^ + key(1 second) = { \sf S } key: Exit current input/modification state
Long press the <key(1 second) = E key to confirm and save settings Short press the ^ + key to switch cursor position between numbers and options
Short press the <key to move the cursor right
Data inputsupports up to8 digits (including symbolsand decimal points)
BasicMenuOperations
Menu navigation:Press the ^ + key to scroll down, press the <key to scroll up; pressEtoenterasubmenu,pressSto returnto themain interface.
Submenu Operations:Press S to exit the submenu; press Eto enter edit mode.
Option modification: Use the ^ + key to select downward, the<key to select upward,and the E key to confirm.
Number modification: Enter data according to the above key rules and press :to confirm.
Important:After modifying parameters,press the Ekey to save;otherwise, thesettingswillbe invalid.
When entering your password in the auxiliary interface,type "22" to accesstheusermenu.Themenustructureisshownbelow.
The functions of each menu and their parameter meanings are shown in the table below:
| Menu Number | Menu Display | meaning | Option or Number Range |
| 1 | Unit Selection | Flow Unit Selection (Default: 0) | 0:m³/h;automaticallyadds N duringAlgorithm21:m3/ m2:I/h3:l/m4:t/h 5:t/m6:kg/h7:kg/m |
| 2 | Algorithm Selection | Algorithm Selection (Default: 0) | 0:Conventionalvolumetric flowrate (flowunder conditions without gas-liquid separation)1:Conventional mass flow rate (operating condition density)2:Volume flow rate of standard gas 3:Conventional gas mass flow rate (under standard conditions density) 4:Saturated Steam Temperature Compensation 5:Saturated Steam Pressure Compensation6:Overheated Steam Temperature and Pressure Compensation 7:Specific Algorithm (Customizable by User) |
| 3 | FlowRate Coefficient K [P/m³]XXX. XXXXxXxX | discharge coefficient (Default:3600.0) | Set the instrument flow coefficient to a value other than O |
| 4 | Fluid density: kg/m³ xxxx.xxxx | Density Settings (Default:1000.0) | Both Algorithm1and Algorithm3 require this setting Unit: kg/m³;cannot be 0 |
| 5 | Maximum outputMaximum output flowrate xxxxxx.xx | flowrate (Default:1000) | Thisvalue mustbe setand cannotbe 0.Unit matches flow unit |
| 6 | Lower limit resection flow percentage xx.X | Enter the percentage of the cut-off flow relative to the full flow | Thevalue ranges fromO to 20, with a default of 1.0 (1%). |
| 7 | Upper Limit Alarm Flow Rate xxxxxx.xx | Alarm flow (Default: 990.0) | This value does not need to besetand should generally notbe 0.Unit matches flow unit |
| 8 | Lower limitalarm flowrate xxxxxx.xx | Alarm flow (Default: 10.0) | This value does not need to be set and should generally not be 0.Unit matches flow unit |
| 9 | damping periodxx | Setoutput current damping period(Default:4s) | Show the damping time for displaying current outputand frequency smoothing to prevent significant fluctuations in output current and frequency Range:2 to 32 |
| 10 | HARTaddress | set up HART Communication Number | Range:0-15 (default:0) |
| 11 | Cumulative amount reset to zeroenter passwordXX | Cumulative Zeroing Amount | To reset the cumulative amount,enter password 70 Press the "E" key |
HARTCOMMUNICATION
The transmitter supports two-wire 4 { * } 2 0 \mathsf { m A } communication for the general HART commands listed in the table below.
| order | operational | Parameter Meaning | explain |
| 0 | objectives Read transmitter information | Transmitter Information | not have |
| 1 | Read the main variables of the | Flow Unit + Flow Value | not have |
| 2 | transmitter Read output current and percentage | Output Current + Flow Percentage | not have |
| 3 | Read the output currentand dynamic variables | Current value + Instantaneous flow rate+ Frequency + Low-bit of cumulative value + High-bit of | The last four dimensions have units. |
| 11 | Read transmitter information | Transmitter Information | not have |
| 12 | Read transmitter information | Transmitter Information (MESSAGE) | Custom content can be written using Command 17 |
| 13 | Read transmitter information | Transmitter Information (TAG + DESCRIPTION + DATE) | Custom content can be written using Command 18 |
| 14 | Read Sensor Information | sensor information | not have |
| 15 | Read the upper and lower limits and damping | Flow Unit + Full Range Flow + Cut-off Flow + Damping | not have |
| 16 | Read transmitter information | Transmitter Information (FAN) | Custom content can be written using Command 19 |
| 17 | Write transmitter information | Transmitter Information (MESSAGE) | After writing,you can read the verification using Command 12. |
| 18 | information | Write transmitter Transmitter Information (TAG + DESCRIPTION + DATE) | After writing,you can verifyitbyrunning Command 13. |
| 19 | Write transmitter information | Transmitter Information (FAN) | After writing,you can verifyitbyusing Command 16. |
| 34 | Change Damping damp | not have | |
| 35 | and lower limits and units | Change the upper Unit + Full-scale flow rate + Resection flow rate | not have |
| 40 | output | Output current value (4-20 mA range) | When this command is executed,the transmitter immediately outputs the specified current value. |
| 44 | Modifying Unit | flux unit | nothave |
| 45 | Calibrate the4 mAcurrent | The current value measured by the precisionammeteratthe transmitter output | First, use Command 40 to outputa4mAcurrent, thenmeasure theactual outputvalueandcalibrate using this command. |
| 46 | Calibratethe20 mAcurrent:The currentvalue measuredby the ammeteratthe transmitter output. | First,use Command 40 to outputa 20 mA current. | Measure the actual output valueagain and calibrate using this command |
| 110 | Read Extended Dynamic Variables | Transmitter Extended DynamicVariables (Temperature+Pressure)variableis pressure | The first variable is temperature;thesecond |
5.4VT3W-XXA:Athree-wire system formixed signal processing, featuring temperatureand pressure compensationcapabilities.
This product features temperature and pressure compensation capabilities, enabling measurementof volumetric flow rates under liquid,gas,and steam conditions,aswell as standard-state volumetricflow rates for gases and mass flow rates for steam,along with RS485 communication functionality.The specific specifications for temperature/pressure compensation and RS485 communication are subject to the actual product model.It operates on a 3.6V lithium battery and retains its RS485 communication capability when powered bybattery.
Display content
The power supply icon shows a "plug" symbol for mains power and a 0.243n3 "battery"symbolfor 0.000 battery power. Pu=2. m3/h H
The first row shows cumulative flow. The second row displays the
instantaneous flowrate.
The third row displays the temperature value.
Line Wiring
The fourth row displays the pressure value.
Nrepresents the signal measurement mode;
default value.
\mathsf { V } + :Powerinputof24VDC+
GND:Power input (24VDC-)
IOUT:Three-wire current output
Fout: Three-line pulse output
\mathsf { A } + :RS485communication A
B-:RS485 Communication B
TRH: PT100 Input
TRL: PT100 Input
PIH:Pressure signal voltage input ^ +
PVH:Pressure-powered output ^ + PVL:Pressure Power Supply OutputPIL: Pressure signal voltage input{ 3 . 6 \lor + } :Positiveterminalofa3.6Vbattery 3.6V-:The negative terminal of a 3.6Vbattery
FlowMeterWorkInterface
The flow meter's operation interface consists of two sections: the main interfaceand theauxiliary interface,asshown in the figure.
Cumulative flow 1000000.0m3
Instantaneous flow 1000.0 m3/h ←Instantaneous flow unit
Medium temperature- T=25.5℃ Medium pressure P=101.3KPa Flow% L ←Power supply mode Signal calibration mode
Signal frequency-→ Fin=500.0Hz Output current value一 Iout=12.000mA Output frequency value→ Fout=500.00Hz Enter password box Password:00
User ParameterSettings
ButtonFunctionDefinitions
Long press the ^ + key (1 second) = { 5 } key: Exit current input/modification state
Long press the <key(1 second) \mathbf { \Psi } = \mathsf { E } key to confirm and save settings Short press the ^ + key to switch cursor position between numbers and options
Short press the <key to move the cursor right
Data input supports up to 8 digits (including symbols and decimal points)
BasicMenu Operations
Menu navigation: Press the ^ + key to scroll down,press the <key to scroll up; press E to entera submenu,pressS to return to the main interface.
Submenu Operations: Press S to exit the submenu; press E to enteredit mode.
Optionmodification:Use the ^ + key to select downward,the<keyto select upward,and the E key to confirm.
Number modification: Enter data according to the above key rules and press E to confirm.
Important:After modifying parameters,press the Ekey to save;otherwise, the settingswill be invalid.
UserMenu
Enter the password "22"to access the user menu.The functions and parameter meaningsof each menu itemare as follows:Table1 UserMenu
| number | Menu Name | function declaration |
| 1 | UnitSelection Default:m³/h | Set the instantaneous flow unitbased on the flow algorithm type Available options:Volume units:m³/h; m³/m; L/h; L/mQuality units:t/h; t/m; kg/h; kg/m |
| 2 | Algorithm Selection by defaventional Volume Flow Rate | Set the flow algorithm;the instrument will compensate the measured instantaneous flow based on thisalgorithm.Options:Conventionalvolumetric flow rate (flow rate under conditions where gasand liquid are not separated)Standard Mass Flow Rate Smausdardizifd gasvatiumconditianeCenventionalgas mass flow rate (must specify standard density) Saturation Steam Temperature Compensation Saturation Steam Pressure Compensation Overheated steam temperature-pressure compensation Specific Algorithm (Customizable by User) |
| 3 | discharge Defi:ent00.0 | Calculatastureflewt.Unit: comfficintrmuired for |
| 4 | fluid density Default:1000.0 | Set the fluid density value in kg/m³ (do not set to O).This value is required for mass-based algorithmsand is unnecessary for volume-based algorithms. |
| 5 | Full Flow Rate Default value: 1000.0 | Set the instantaneous flow rate corresponding toa 20 mA current output (do not set to O).The unit must match the one selected in Unit Selection. |
| 6 | Lower limit resection flow rateDefault value:0% | Set the percentage of full flow rate that constitutes theset discharge flow;if the measured flow rate falls below this percentage,calculate the flow rate as 0 and outputa4mA current. |
| 7 | Upper Limit AiarmFlowRate Default value: 990.0 | Setan upperalarm flow threshold;if the flowexceeds this value,trigger an alarm. Unit:The selected unit. |
| 8 | Lower limit alarm flow rate Default value:10.0 | Setalower limitfor thealarm flow threshold;if the flow falls below this value,an alarm willbe triggered. Unit: The selected unit. |
| 9 | damping period | Value ranges from2 to 32 seconds for displaying and smoothing current output.The default value is 4 seconds. |
| 10 | postal address | Set the device address for 485 Modbus (range: 0-254).Defaultvalue: 0 |
| 11 | Cumulative Zeroing Amount is "70". | Set the cumulative amount to 0.The reset password |
Engineer Menu: Enter the password "33"to access the EngineerMenu. The functions and parameter meanings of each menu are listed in the table below:
| numberMenu Name | function declaration | |
| 1 | language Default: Chinese | Set Instrument Language Type Options: Chinese; English |
| 2 | Pulse Selection Defaultvalue: Signal frequency For initial calibration, select the signal frequency; for choose the corrected frequency output. | Select the output type based on your requirements. Available options:Select the output type based on yourrequirements.Available options:Signal frequency-Measures the signal frequency of the probe(un corrected)Calibration Frequency- Frequency output corrected using a 5-point coefficient Frequency Output-Displaysa linear frequency range of O-1ooo Hzbased on flowrate corrected output, Equivalent Pulse-generates cumulative flow pulses basedonaselectedpulse factorUpperLimitAlarm- Issuesanalarmswitch signalwhen thevalue exceeds the set upper limit Lower LimitAlarm-Issuesan alarmswitch signal when thevalue fallsbelow the |
| 3 | pulse equivalency Default: 0.01 | presetlower limit Effective only forequivalent pulse output; indicates how many cumulative flowunits each pulse represents.Options:0.00001;0.0001;0.001;0.01;0.1; |
| 4 | 485 baud rate Default:9600 | 1.0;10.0; 100.0 Setthe Modbus communication baud rate.Options available:4800 Odd,4800 Even,4800 No;9600Odd, 9600Even,9600No |
| 5 | communication switch Default: Off | Enable or disable the Modbus communication function. Options: Off; On |
| 6 | Pressure Display Default value: Measure | Set whether to display fluid pressure.Options: Measurement:Displays the pressure value calculated from the measured pressure signal Default:"P=" displays the value of the default pressure setting in the menu below and is used forcalculation Calculation:"P~" displays the back-calculated pressure value for saturated steam temperature compensation.Close:Do not display pressure items |
| 7 | Default Pressure The default value is0.0 kPa | Set the default gas pressure calculation value in Kpa. This pressure value is used when the sensor fails duringdefault or measurement (when exceeding twice the range),and the equal sign on the main screen's Pdisplay changes to "P=". |
| 8 | reference pressure Default value:101.3 kPa | Set the reference pressure value for altitude correction when calculating absolute pressure using a gauge pressure sensor.The unit is KPa.Fora barometric pressure sensor,this value should be set to 0.0 Kpa. |
| 9 | Temperature DisplayDefault value:Measure | Set whether to display fluid temperature.Options: Setwhether to display fluid temperature.Options: Measurement:Displays the temperature value calculated from the measured platinum resistance signal Default: "T=" displays the value set for the default temperature item in the menu below and is used forcalculations Calculation:"P~"displays the inverse calculationvalue temperature forsaturated vapor pressure compensation Hide:Do not display the temperature field |
| 10 | Default Temperature Default value:20C | Selected forsetting or measuring platinum resistance faults (when temperatures exceed 500C). This temperature is used forcalculation,and the main display changes to show an equal sign. Unit:C. |
| 11 | Temperature Measurement SelectionDefault value:Pt=1000 | Selectthe type of resistor for measurement temperature.Options:Pt=10o;Pt=1000 |
| 12 | Standard temperatureThe default value is: 0.0C | Set the calculation value forstandard temperature. Options:0°C;20C |
| 12 | ambient temperature Default value:-10℃ | Select the LCD screen refresh rate fordifferent environments.Options:-10oC:Under normal conditions,selecting "-10C"causes the working interface to refreshapproximately every1.2 seconds-20oC:When the low-temperature environment is set to "-20oC",the working interface refreshesapproximately every6 seconds. |
| 13 | FlowCorrection FactorThe valueis1.0 | Flow percentage Qiranges from 0 to 120%; flow coefficientCi rangesfrom0.8 to1.2.The instrument Q0-Q4(onc,3ffiient,7orthfd100%) reseoints C0-C4in ascending order of flow rate.C=standard flowrate/measured flowrateshowninthis table. |
Settings Menu (the key menu that directly determines the instrument's critical performance)When in password entrymode,enter the password "44" to access the settings menu.The functions and parameter meanings of eachmenuare listedbelow:
| number | Menu Name | functiondeclaration |
| 1 | SignalSelection Default value: MFDN40-150 gas pipe (Simulation board:This field is not used) | Select the flow signal type.Choose input capacitance matchingforvortexstreetsignalsinthelow- frequency (LF),medium-frequency(MF),or high- frequency (HF) range;LFoffers better interference resistance.Optionsavailable: UF:DN10-15 gas cannotbe selected yet;however,it remainsavailable asa backup.HF:DN15-40 gas pipe,suitable for small-diameterapplications.MF:For gaseswith diameters ranging from DN40 to DN150;MF:For liquidswith diameters ranging from DN15 to DN40-suitable forusewith small and medium-sized pipelines carrying gases or liquids.LF:DN2o0-500 for gases; LF:DN40-500 for liquids-suitable for large-diameter gasand liquid applications.Simulate a manual circuit:Setbits1-6 of K1 according to the |
| 2 | GainSelection Default value: 7|8 times | referencetable. Select the signal gain.G=3|4 provides excellent anti- interference performance. It can measure lower flow rates at G=13 or14,or be usedwith high-temperature probes. Available options:1|2,3|4,5|6,7|8,9|10,13|14; KSG-4=ON has the highest value. |
| 3 | Lowerboundary resection Default value:100 mV | Set thelower limitvoltage forVpp removal,in mV, validonlyindigitalmode.Manualmode:Set sensitivity SB= 2-8 by pressing1+ ON=1,2,or4on pins KSG1-3. |
| 4 | 0=1.6-45HZ 9=22-550HZ Band Selection 2=3.6-90HZ Default value: 10=28-700HZ 10= 28-700 Hz 3=4.8-120HZ 11=34-850HZ 12=42-1050HZ 4=6.4-160HZ | Selecta different 25xvortex street signal frequency band.Options available:0=1.6-45HZ 8=18-450HZ 1=2.4-65HZ 10=28-700HZ 3=4.8-120HZ | 8=18-450HZ 1=2.4-65HZ 9=22-550HZ 2=3.6-90HZ 11=34-850HZ 4=6.4-160HZ 12=42-1050HZ |
| 5 | operatemode Defaultvalue: Automatic mode | 6=11-275HZ 14=64-1600HZ 7=14-350HZ 15=96-2400HZ 7=14-350HZ 15=96-2400HZ Select the operating mode for circuit processing. Manual-triggered bya hardware comparator for frequency measurement Options:Manual/Digital. Digital-calculated by the software using FFT frequency | |
| 6 | Noise Reduction Selection Default value:Standard | Select normal or anti-interference operating mode. Anti-noise mode providesa broader range of signal rejectioncriteria.Options:Standard\Noise Reduction | |
| 7 | Signal Detection Selection Default value:Off | Set Signal Test Type (Optional): Low area: 0-1/4; High area:1/4-1/2;Noise measurement:5%; Noise measurement:10%; Noise measurement:15%; Off | |
| 8 | Resection at 50 Hz Default value: Off | Setwhether to enable the 5oHz excision function Option: Off/On | |
| 9 | Flow Rate Coefficient Correction | Confirm entering the flow coefficient correction submenu | |
Note:All settings in the menu are strictly calibrated or configured at the flow meter's factory.Non-professionals or users without specialized equipment must not modify or recalibrate these settings,as doing so may cause the flow meter to malfunction.
| number | Menu Name | function declaration |
| 1 | Correction Switch Default value: Off | Setthe linear correction switch for the flow coefficient Option:Off/On.Ensure the instrument coefficient is set to the correct average value first. |
| 2 | 1 Frequency | Correction Point Set the frequency value for the first correction point in HZ;The default value is:1/5of the frequency range plus the lower limit frequency |
| 3 | 1 Coefficient | Correction Point Set the correction flow coefficient K1 corresponding to the frequency of the first correction point Default value:the "flow Factor"value in the user menu |
| 4 | 2 Frequency | Setthe frequency value for the second correction Correction Point point in HZ; The default value is:2/5of the frequency range plus the lower limit frequency |
| 5 | 2Coefficient | Set the correction flow coefficient K2 corresponding Correction Point to the frequency of the second correction point Default value:the "flow Factor"value in the user menu |
| 6 | Correction Point 3 Frequency | Set the frequency value for the third correction point in HZ;The default value is:3/5of the frequency range plus the lower limit frequency |
| 7 | 3 Coefficient | Correction Point Set the correction flow coefficient K3 corresponding to the frequency of the third correction point Default value: the "flow Factor" value in the user menu |
| 8 | 4 Frequency | Correction Point Set the frequency value for the fourth correction point in HZ;Default value:Band frequency range × 4/5+lower limit frequency |
| 9 | 4Coefficient | Correction Point Set the correction flow coefficient K4 corresponding to the frequency of the fourth correction point Default value: the "flow Factor"value in the usermenu |
| 10 | 5 Frequency | Correction Point Set the frequency value for the first correction point in HZ;Default value:Upper frequency of the band |
| 11 | 5 Coefficient | Correction Point Set the correction flow coefficient K5 corresponding to the frequency of the fifth correction point.Default value: the "flow Factor"value in the user menu |
| 12 | preserve | Change "No" to "Yes",save the parameters,and initiateacompensationcyclecalculation forseveral seconds.To correct the pulse output,change the pulse selection in the "33" menu to "Calibration Frequency". |
5.5Modbuscommunication
The three-wire transmitter rapidly reads each operating parameter from the hold registers using the Modbus-RTU communication protocol.The only Modbus command that reads hold register values is Command 3.It supports only 4800 and 96o0 baud rateswith a response time of <= 5 0 { \ m s } _ { i } :theminimum intervalbetweenconsecutiveModbuscommands is 1 0 0 ~ \mathsf { m s }
Table5 provides explanations for the offsetaddressesand data formats of each valuein Modbuscommands.
| Address Offset | operational objectives | data format | Data Byte Count |
| 0 | instantaneous delivery | floating-point type | 4 |
| 4 | Operating Flow Rate | floating-point type | 4 |
| 8 | Cumulativevalue at a | type integer | 4 |
| 12 | Cumulativevalue is high. | type integer | 4 |
| 16 | fluid temperature | floating-point type | 4 |
| 20 | fluid pressure | floating-point type | 4 |
| 24 | measuring frequency | floating-point type | 4 |
| 28 | output | floating-point type | 4 |
| 32 | Unitntaneous Cow Rate | Short Integer Type | 2 |
Regarding Cumulative Amount:The cumulative amount consists of two parts:a high-orderbitand alow-orderbit.Thelow-orderbit isa fixed-point integer.After converting thisdata to decimal,the high-orderbit is the integer value of the cumulative amount divided by1,0oo,ooo.The calculation formula is:
Cumulative Amount (Floating-Point) \mathbf { \tau } = \mathbf { \tau } High-order Bit (Integer) \* 1 , 0 0 0 , 0 0 0 . 0 \ + Low-order Bit (Integer)/1,000.0
The cumulative flow unit is the volume or mass unit remaining after removing the time portion from the instantaneous flow unit.
Regarding flow unit codes,a flow unit is the physical unit determined by matching its sequence code value with the table below.
| Unde | 0 | 1 | 2 | 3 | 4 | 5 | 6 | 7 |
| physical | m3/h | m3/m | /h | /m | t/h | t/m | kg/h | kg/m |
Fordetailed information on Modbus commandsand message formats,refer to the Modbus White Paper and other protocol specifications.
explain
This table applies to temperature-pressure compensation and mass flow conversion scenarios forvortex flow meters.
Pressure unit:MPa (absolute pressure); Temperature unit: { } ^ { \circ } { \mathsf { C } } ; Density unit: \mathsf {kg } / \mathsf { m } ^ { 3 } (204号
The density of saturated steam is determined solely by pressure;the density of superheated steam isdetermined by both pressure and temperature.
Thevalues in the table are commonly used engineering reference values; on-site parameter settings can be directly referenced.
SaturationSteamDensityTable1
| Temp. | |||||||||||
| 100 | 1.1033 | 0.5997 | 138.5 | 138 | 3.414 | 1.864 | 152.83 | 176 | 9.137 | 4.723 | 166.98 |
| 101 | 1.05 | 0.6108 | 138.88 | 139 | 3.513 | 1.915 | 153.2 | 177 | 9.353 | 4.829 | 167.35 |
| 102 | 1.0878 | 0.6388 | 139.26 | 140 | 3.614 | 1.967 | 153.58 | 178 | 9.574 | 4.937 | 167.72 |
| 103 | 1.1267 | 0.6601 | 139.64 | 141 | 3.717 | 2.019 | 153.95 | 179 | 9.798 | 5.048 | 168.09 |
| 104 | 1.1668 | 0.6321 | 140.02 | 142 | 3.823 | 2.073 | 154.32 | 180 | 10.027 | 5.16 | 168.46 |
| 105 | 1.208 | 0.7046 | 140.39 | 143 | 3.931 | 2.129 | 154.7 | 181 | 10.259 | 5.274 | 168.83 |
| 106 | 1.2504 | 0.7277 | 140.77 | 144 | 4.042 | 2.185 | 155.07 | 182 | 10.496 | 5.391 | 169.2 |
| 107 | 1.2941 | 0.7515 | 141.15 | 145 | 4.155 | 2.242 | 155.45 | 183 | 10.738 | 5.509 | 169.57 |
| 108 | 1.339 | 0.7758 | 141.53 | 146 | 4.271 | 2.301 | 155.82 | 184 | 10.983 | 5.629 | 169.94 |
| 109 | 1.3852 | 0.8008 | 141.91 | 147 | 4.398 | 2.361 | 156.19 | 185 | 11.233 | 5.752 | 170.31 |
| 110 | 1.4327 | 0.8265 | 142.29 | 148 | 4.51 | 2.422 | 156.57 | 186 | 11.488 | 5.877 | 170.68 |
| 111 | 1.4815 | 0.8528 | 142.66 | 149 | 4.634 | 2.484 | 156.94 | 187 | 11.747 | 6.003 | 171.05 |
| 112 | 1.5316 | 0.8798 | 143.04 | 150 | 4.76 | 2.584 | 157.31 | 188 | 12.01 | 6.132 | 171.42 |
| 113 | 1.5832 | 0.9075 | 143.42 | 151 | 4.889 | 2.613 | 157.69 | 189 | 12.278 | 6.264 | 171.79 |
| 114 | 1.6362 | 0.9359 | 143.8 | 152 | 5.021 | 2.679 | 158.06 | 190 | 12.551 | 6.397 | 172.16 |
| 115 | 1.6906 | 0.965 | 144.17 | 153 | 5.155 | 2.747 | 158.43 | 191 | 12.829 | 6.533 | 172.53 |
| 116 | 1.7465 | 0.9948 | 144.55 | 154 | 5.293 | 2.816 | 158.81 | 192 | 13.111 | 6.671 | 172.9 |
| 117 | 1.8039 | 1.025 | 144.93 | 155 | 5.433 | 2.886 | 159.18 | 193 | 13.398 | 6.812 | 173.26 |
| 118 | 1.8628 | 1.057 | 145.31 | 156 | 5.577 | 2.958 | 159.55 | 194 | 13.69 | 6.955 | 173.63 |
| 119 | 1.9233 | 1.089 | 145.68 | 157 | 5.732 | 3.032 | 159.93 | 195 | 13.987 | 7.1 | 174 |
| 120 | 1.9854 | 1.122 | 146.06 | 158 | 5.872 | 3.106 | 160.3 | 196 | 14.298 | 7.248 | 174.37 |
| 121 | 2.0492 | 1.155 | 146.44 | 159 | 6.025 | 3.182 | 160.67 | 197 | 14.596 | 7.398 | 174.74 |
| 122 | 2.1145 | 1.19 | 146.81 | 160 | 6.181 | 3.26 | 161.04 | 198 | 14.909 | 7.551 | 175.1 |
| 123 | 2.1816 | 1.225 | 147.19 | 161 | 6.339 | 3.339 | 161.42 | 199 | 15.226 | 7.706 | 175.47 |
| 124 | 2.2504 | 1.261 | 147.57 | 162 | 6.502 | 3.42 | 161.79 | 200 | 15.549 | 7.864 | 175.84 |
| 125 | 1.298 | 147.94 | 163 | 6.667 | 3.502 | 162.16 | 201 | 15.877 | 8.025 | 176.21 | |
| 126 | 2.321 2.3933 | 1.336 | 148.32 | 164 | 6.836 | 3.586 | 162.53 | 202 | 16.21 | 8.188 | 176.57 |
| 127 | 2.4675 | 1.375 | 148.7 | 165 | 7.008 | 3.671 | 162.9 | 203 | 16.549 | 8.354 | 176.94 |
| 128 | 2.5435 | 1.415 | 149.07 | 166 | 7.183 | 3.758 | 163.27 | 204 | 16.893 | 8.522 | 177.31 |
| 129 | 2.6215 | 1.455 | 149.45 | 167 | 7.362 | 3.847 | 163.65 | 205 | 17.243 | 8.694 | 177.68 |
| 130 | 2.7013 | 1.497 | 149.82 | 168 | 7.545 | 3.937 | 164.02 | 206 | 17.598 | 8.868 | 178.04 |
| 131 | 2.7831 | 1.539 | 150.2 | 169 | 7.731 | 4.029 | 164.39 | 207 | 17.959 | 9.045 | 178.41 |
| 132 | 2.867 | 1.583 | 150.57 | 170 | 7.92 | 4.123 | 164.76 | 208 | 18.326 | 9.225 | 178.78 |
| 133 | 2.9528 | 1.627 | 150.95 | 171 | 8.114 | 4.218 | 165.13 | 209 | 18.699 | 9.408 | 179.14 |
| 134 | 3.041 | 1.672 | 151.33 | 172 | 8.311 | 4.316 | 165.5 | 210 | 19.077 | 9.593 | 179.51 |
| 135 | 3.131 | 1.719 | 151.7 | 173 | 8.511 | 4.415 | 165.87 | 211 | 19.462 | 9.782 | 179.88 |
| 136 | 3.223 | 1.766 | 152.08 | 174 | 8.716 | 4.515 | 166.24 | 212 | 19.852 | 9.974 | 180.24 |
| 137 | 3.317 | 1.815 | 152.45 | 175 | 8.924 | 4.618 | 166.61 | 213 | 20.249 | 10.17 | 180.61 |
| (C) | raturePressure(kg/mResistaraturePressure(kg/m)ResistraturePressure(kg/mResist (bar) | TempeAbsoluteDensityPlatinumtempeAbsoluteDensityPlatinumtempeAbsoluteDensityPlatinum | |||||||||
| 214 | 20.651 | 10.37 | nce (Ω2) 180.97 | (℃) 252 | (bar) 41.138 | 20.69 | nce (Ω) 194.8 | (℃) 290 | (bar) 74.46 | 39.16 | nce (Ω2) 208.45 |
| 215 | 21.06 | 10.57 | 181.34 | 253 | 41.831 | 21.05 | 195.16 | 291 | 75.55 | 39.81 | 208.81 |
| 216 | 21.475 | 10.77 | 181.71 | 254 | 42.534 | 21.42 | 195.52 | 292 | 76.65 | 40.48 | 209.17 |
| 217 | 21.869 | 10.98 | 182.07 | 255 | 43.246 | 21.79 | 195.88 | 293 | 77.77 | 41.15 | 209.52 |
| 218 | 22.324 | 11.19 | 182.44 | 256 | 43.967 | 22.17 | 196.24 | 294 | 78.9 | 41.83 | 209.88 |
| 219 | 22.758 | 11.41 | 182.8 | 257 | 44.697 | 22.55 | 196.6 | 295 | 80.04 | 42.53 | 210.24 |
| 220 | 23.198 | 11.62 | 183.17 | 258 | 45.437 | 22.94 | 196.96 | 296 | 81.19 | 43.24 | 210.59 |
| 221 | 23.645 | 11.84 | 183.53 | 259 | 46.185 | 23.33 | 197.33 | 297 | 82.36 | 43.96 | 210.95 |
| 222 | 24.099 | 12.07 | 183.9 | 260 | 46.943 | 23.73 | 197.69 | 298 | 83.53 | 44.69 | 211.31 |
| 223 | 24.56 | 12.3 | 184.26 | 261 | 47.711 | 24.14 | 198.05 | 299 | 84.72 | 45.43 | 211.66 |
| 224 | 25.027 | 12.53 | 184.63 | 262 | 48.488 | 24.55 | 198.41 | 300 | 85.93 | 46.19 | 212.02 |
| 225 | 25.501 | 12.76 | 184.99 | 263 | 49.275 | 24.97 | 198.77 | 301 | 87.12 | 46.96 | 212.37 |
| 226 | 25.982 | 13 | 185.36 | 264 | 50.071 | 25.4 | 199.13 | 302 | 88.37 | 47.75 | 212.73 |
| 227 | 26.47 | 13.24 | 185.72 | 265 | 50.877 | 25.83 | 199.49 | 303 | 89.62 | 48.54 | 213.09 |
| 26.965 | 13.49 | 186.09 | 266 | 51.693 | 26.27 | 199.85 | 304 | 90.87 | 49.36 | 213.44 | |
| 228 229 | 27.467 | 13.74 | 186.45 | 267 | 52.519 | 26.72 | 200.21 | 305 | 92.14 | 50.18 | 213.8 |
| 27.976 | 14 | 186.82 | 268 | 53.356 | 27.17 | 200.57 | 306 | 93.43 | 51.02 | 214.15 | |
| 230 | 28.493 | 14.25 | 187.18 | 269 | 54.202 | 27.63 | 200.93 | 307 | 94.73 | 51.88 | 214.51 |
| 231 232 | 29.016 | 14.52 | 187.54 | 270 | 55.058 | 28.1 | 201.29 | 308 | 96.04 | 52.75 | 214.86 |
| 233 | 29.547 | 14.78 | 187.91 | 271 | 55.925 | 28.57 | 201.65 | 309 | 97.36 | 53.64 | 215.22 |
| 234 | 30.086 | 15.05 | 188.27 | 272 | 56.802 | 29.06 | 202.01 | 310 | 98.7 | 54.54 | 215.57 |
| 235 | 30.632 | 15.33 | 188.63 | 273 | 57.689 | 29.55 | 202.36 | 311 | 100.01 | 55.47 | 215.93 |
| 236 | 31.186 | 15.61 | 189 | 274 | 58.587 | 30.04 | 202.72 | 312 | 100.14 | 56.4 | 216.28 |
| 237 | 31.747 | 15.89 | 189.36 | 275 | 59.496 | 203.08 | 313 | 100.28 | 57.36 | 216.64 | |
| 238 | 32.317 | 16.18 | 189.72 | 60.415 | 30.55 31.06 | 203.44 | 100.42 | 58.33 | 216.99 | ||
| 276 | 314 | ||||||||||
| 239 | 32.893 | 16.47 | 190.09 | 277 | 61.346 | 31.58 | 203.8 | 315 | 100.56 | 59.33 | 217.35 |
| 240 | 33.478 | 16.76 | 190.45 | 278 | 62.287 | 32.11 | 204.16 | 316 | 100.7 | 60.34 | 217.7 |
| 241 | 34.071 | 17.06 | 190.81 | 279 | 63.239 | 32.65 | 204.52 | 317 | 100.85 | 61.37 | 218.05 |
| 242 | 34.672 | 17.37 | 191.18 | 280 | 64.202 | 33.19 | 204.88 | 318 | 100.99 | 62.43 | 218.41 |
| 243 | 35.281 | 17.68 | 191.54 | 281 | 65.176 | 33.75 | 205.23 | 319 | 101.14 | 63.5 | 218.76 |
| 244 | 35.898 | 17.99 | 191.9 | 282 | 66.162 | 34.31 | 205.59 | 320 | 101.29 | 64.6 | 219.12 |
| 245 | 36.523 | 18.31 | 192.26 | 283 | 67.158 | 34.88 | 205.95 | 325 | 102.06 | 70.45 | 220.88 |
| 246 | 37.157 | 18.64 | 192.63 | 284 | 68.167 | 35.47 | 206.31 | 330 | 102.86 | 76.99 | 222.65 |
| 247 | 37.799 | 18.97 | 192.99 | 285 | 69.186 | 36.06 | 206.67 | 335 | 103.71 | 84.36 | 224.41 |
| 248 | 38.449 | 19.3 | 193.35 | 286 | 70.218 | 36.66 | 207.02 | 340 | 104.61 | 92.76 | 226.17 |
| 249 | 39.108 | 19.64 | 193.71 | 287 | 71.261 | 37.27 | 207.38 | 345 | 105.55 | 102.4 | 227.92 |
| 250 | 39.776 | 19.99 | 194.07 | 288 | 72.315 | 37.89 | 207.74 | 350 | 106.54 | 113.6 | 229.67 |
| 251 | 40.452 | 20.36 | 194.44 | 289 | 73.382 | 38.52 | 208.1 | 355 | 107.58 | 127.2 | 231.42 |
| Absolute Pressure :p/MPa | 140℃ | 150℃ | 160℃ | 170℃ | 180℃ | 190℃ | 200℃ | 210℃ | 220℃ | 230℃ | 240℃ |
| 0.2 | 1.07 | 1.042 | 1.016 | 0.992 | 0.969 | 0.947 | 0.926 | 0.906 | 0.887 | 0.868 | 0.851 |
| 0.3 | 1.622 | 1.578 | 1.537 | 1.499 | 1.463 | 1.428 | 1.396 | 1.365 | 1.336 | 1.308 | 1.281 |
| 0.4 | 2.127 | 2.067 | 2.014 | 1.964 | 1.916 | 1.872 | 1.829 | 1.789 | 1.751 | 1.715 | |
| 0.5 | 1 | 2.608 | 2.538 | 2.472 | 2.411 | 2.353 | 2.299 | 2.247 | 2.198 | 2.152 | |
| 0.55 | 1 | 2.882 | 2.803 | 2.729 | 2.661 | 2.596 | 2.535 | 2.478 | 2.424 | 2.372 | |
| 0.6 | - | 3.159 | 3.071 | 2.989 | 2.912 | 2.841 | 2.773 | 2.71 | 2.65 | 2.593 | |
| 0.65 | - | 3.341 | 3.25 | 3.165 | 3.087 | 3.013 | 2.943 | 2.877 | 2.815 | ||
| 0.7 | - | - | 3.614 | 3.514 | 3.421 | 3.334 | 3.253 | 3.177 | 3.105 | 3.037 | |
| 0.75 | - | - | 3.889 | 3.779 | 3.678 | 3.584 | 3.495 | 3.413 | 3.335 | 3.261 | |
| 0.8 | - | - | 4.048 | 3.937 | 3.835 | 3.739 | 3.649 | 3.565 | 3.486 | ||
| 0.85 | - | - | - | 4.318 | 4.198 | 4.087 | 3.984 | 3.887 | 3.797 | 3.711 | |
| 0.9 | - | - | 4.591 | 4.461 | 4.342 | 4.231 | 4.127 | 4.03 | 3.938 | ||
| 1 | - | 1 | 5.145 | 4.995 | 4.856 | 4.729 | 4.61 | 4.499 | 4.395 | ||
| 1.1 | - | - | - | - | 5.537 | 5.379 | 5.233 | 5.098 | 4.973 | 4.855 | |
| 1.2 | 1 | - | 6.089 | 5.909 | 5.744 | 5.593 | 5.452 | 5.321 | |||
| 1.3 | 1 | - | 6.448 | 6.263 | 6.093 | 5.936 | 5.79 | ||||
| 1.4 | 1 | - | - | 6.996 | 6.789 | 6.6 | 6.426 | 6.265 | |||
| 1.5 | - | - | - | 7.554 | 7.324 | 7.114 | 6.922 | 6.744 | |||
| 1.6 | - | - | - | 7.867 | 7.635 | 7.424 | 7.229 | ||||
| 1.7 | - | - | - | - | - | 8.418 | 8.163 | 7.931 | 7.719 | ||
| 1.8 | - | - | 8.978 | 8.699 | 8.446 | 8.214 | |||||
| 1.9 | - | - | - | 9.548 | 9.243 | 8.967 | 8.715 | ||||
| 2 | - | - | - | - | - | 9.795 | 9.495 | 9.222 | |||
| 2.1 | - | - | - | - | 1 | - | 10.36 | 10.03 | 9.735 | ||
| 2.2 | - | - | 1 | 10.93 | 10.57 | 10.25 | |||||
| 2.3 | - | - | - | 1 | - | 11.51 | 11.12 | 10.78 | |||
| 2.4 | 1 | 1 | 1 | 11.68 | 11.31 |
| 2.5 | 1 | - | 1 | 1 | 12.25 | 11.85 | |||||
| 2.6 | - | 1 | 1 | 1 | 1 | 1 | 12.83 | 12.4 | |||
| 2.7 | 1 | 1 | 1 | 13.41 | 12.96 | ||||||
| 2.8 | - | - | = | = | = | = | - | 13.52 | |||
| 2.9 | - | 1 | - | - | 1 | - | - | 14.09 | |||
| 3 | - | 1 | 1 | 1 | - | 14.67 | |||||
| 3.1 | - | - | - | - | - | = | - | 15.26 | |||
| 3.2 | - | = | 1 | 1 | 1 | - | 15.86 | ||||
| 3.3 | - | - | 1 | 16.47 | |||||||
| 3.4 | - | - | - | - | 1 | - | |||||
| 3.5 | - | - |
Overheated Steam Density Table 4
| Absolute Pressure : p/MPa | 250℃ | 260℃ | 270℃ | 280°℃ | 290℃ | 300℃ | 310℃ | 320℃ | 330℃ | 340℃ | 350℃ |
| 0.2 | 0.834 | 0.818 | 0.803 | 0.788 | 0.774 | 0.76 | 0.747 | 0.734 | 0.721 | 0.709 | 0.698 |
| 0.3 | 1.256 | 1.23 | 1.208 | 1.185 | 1.163 | 1.142 | 1.122 | 1.103 | 1.084 | 1.066 | 1.049 |
| 0.4 | 1.68 | 1.647 | 1.615 | 1.585 | 1.555 | 1.527 | 1.5 | 1.474 | 1.449 | 1.424 | 1.401 |
| 0.5 | 2.108 | 2.066 | 2.025 | 1.986 | 1.949 | 1.914 | 1.879 | 1.846 | 1.814 | 1.784 | 1.754 |
| 0.55 | 2.323 | 2.276 | 2.231 | 2.188 | 2.147 | 2.108 | 2.07 | 2.033 | 1.998 | 1.964 | 1.931 |
| 0.6 | 2.539 | 2.487 | 2.438 | 2.391 | 2.345 | 2.302 | 2.26 | 2.22 | 2.182 | 2.145 | 2.109 |
| 0.65 | 2.755 | 2.699 | 2.646 | 2.594 | 2.544 | 2.497 | 2.452 | 2.408 | 2.366 | 2.326 | 2.287 |
| 0.7 | 2.973 | 2.912 | 2.853 | 2.797 | 2.744 | 2.693 | 2.643 | 2.596 | 2.551 | 2.507 | 2.465 |
| 0.75 | 3.191 | 3.125 | 3.062 | 3.001 | 2.944 | 2.889 | 2.836 | 2.785 | 2.736 | 2.689 | 2.643 |
| 0.8 | 3.411 | 3.339 | 3.271 | 3.206 | 3.144 | 3.085 | 3.028 | 2.974 | 2.921 | 2.871 | 2.822 |
| 0.85 | 3.631 | 3.554 | 3.481 | 3.412 | 3.345 | 3.282 | 3.221 | 3.163 | 3.107 | 3.053 | 3.001 |
| 0.9 | 3.852 | 3.77 | 3.692 | 3.618 | 3.547 | 3.48 | 3.415 | 3.353 | 3.293 | 3.236 | 3.181 |
| 1 | 4.296 | 4.204 | 4.116 | 4.032 | 3.952 | 3.876 | 3.804 | 3.734 | 3.667 | 3.603 | 3.541 |
| 1.1 | 4.745 | 4.641 | 4.542 | 4.449 | 4.36 | 4.275 | 4.194 | 4.116 | 4.042 | 3.971 | 3.902 |
| 1.2 | 5.198 | 5.082 | 4.972 | 4.869 | 4.77 | 4.676 | 4.587 | 4.501 | 4.419 | 4.34 | 4.265 |
| 1.3 | 5.654 | 5.526 | 5.405 | 5.291 | 5.182 | 5.079 | 4.981 | 4.887 | 4.798 | 4.711 | 4.629 |
| 1.4 | 6.114 | 5.974 | 5.841 | 5.716 | 5.598 | 5.485 | 5.378 | 5.275 | 5.178 | 5.084 | 4.994 |
| 1.5 | 6.579 | 6.425 | 6.28 | 6.144 | 6.015 | 5.893 | 5.776 | 5.665 | 5.56 | 5.458 | 5.361 |
| 1.6 | 7.049 | 6.88 | 6.723 | 6.575 | 6.435 | 6.303 | 6.177 | 6.06 | 5.943 | 5.834 | 5.729 |
| 1.7 | 7.522 | 7.34 | 7.169 | 7.009 | 6.858 | 6.715 | 6.58 | 6.451 | 6.329 | 6.211 | 6.099 |
| 1.8 | 8.001 | 7.803 | 7.619 | 7.446 | 7.284 | 7.131 | 7 | 6.847 | 6.716 | 6.59 | 6.47 |
| 1.9 | 8.484 | 8.271 | 8.072 | 7.886 | 7.712 | 7.584 | 7.393 | 7.245 | 7.105 | 6.971 | 6.843 |
| 2 | 8.973 | 8.743 | 8.529 | 8.33 | 8.144 | 7.968 | 7.802 | 7.645 | 7.496 | 7.353 | 7.217 |
| 2.1 | 9.466 | 9.219 | 8.99 | 8.777 | 8.578 | 8.391 | 8.214 | 8.047 | 7.888 | 7.737 | 7.593 |
| 2.2 | 9.965 | 9.7 | 9.455 | 9.228 | 9.015 | 8.831 | 8.628 | 8.451 | 8.283 | 8.123 | 7.97 |
| 2.3 | 10.47 | 10.19 | 9.924 | 9.682 | 9.456 | 9.244 | 9.045 | 8.857 | 8.679 | 8.51 | 8.349 |
| 2.4 | 10.98 | 10.68 | 10.4 | 10.14 | 9.899 | 9.675 | 9.464 | 9.266 | 9.078 | 8.899 | 8.73 |
| 2.5 | 11.5 | 11.17 | 10.87 | 10.6 | 10.35 | 10.11 | 9.886 | 9.676 | 9.478 | 9.29 | 9.112 |
| 2.6 | 12.02 | 11.67 | 11.36 | 11.07 | 10.8 | 10.55 | 10.31 | 10.09 | 9.88 | 9.683 | 9.495 |
| 2.7 | 12.55 | 12.18 | 11.84 | 11.53 | 11.25 | 10.98 | 10.74 | 10.5 | 10.28 | 10.08 | 9.88 |
| 2.8 | 13.08 | 12.69 | 12.33 | 12.01 | 11.71 | 11.43 | 11.17 | 10.92 | 10.69 | 10.47 | 10.27 |
| 2.9 | 13.62 | 13.21 | 12.83 | 12.48 | 12.17 | 11.87 | 11.6 | 11.34 | 11.1 | 10.87 | 10.66 |
| 3 | 14.17 | 13.73 | 13.33 | 12.97 | 12.63 | 12.32 | 12.03 | 11.76 | 11.51 | 11.27 | 11.05 |
| 3.1 | 14.73 | 14.26 | 13.84 | 13.45 | 13.1 | 12.77 | 12.47 | 12.19 | 11.92 | 11.67 | 11.44 |
| 3.2 | 15.3 | 14.8 | 14.35 | 13.94 | 13.57 | 13.23 | 12.91 | 12.62 | 12.34 | 12.08 | 11.83 |
| 3.3 | 15.87 | 15.34 | 14.86 | 14.44 | 14.05 | 13.69 | 13.36 | 13.05 | 12.76 | 12.48 | 12.23 |
| 3.4 | 16.45 | 15.89 | 15.39 | 14.94 | 14.53 | 14.15 | 13.8 | 13.48 | 13.18 | 12.89 | 12.63 |
| 3.5 | 17.04 | 16.44 | 15.91 | 15.44 | 15.01 | 14.61 | 14.25 | 13.91 | 13.6 | 13.3 | 13.02 |
| 4 | - | 19.34 | 18.65 | 18.04 | 17.49 | 17 | 16.55 | 16.13 | 15.74 | 15.39 | 15.05 |
Direction For Use
Units in this table:absolute pressure \left( \mathsf { p } / \mathsf { M P a } \right) ,temperature ( { \sf t } / { } ^ { \circ } { \sf C } ) and density ( \mathsf {kg } / \mathsf { m } ^ { 3 } ) .These valuescan be directlyused for temperature-pressure compensation of superheated steam in vortex flow metersand for mass flow conversion.
If the on-site operating condition is gauge pressure,convert it to absolute pressure (absolute pressure \mathbf { \tau } = \mathbf { \tau } gauge pressure + 0 . 1 0 1 3 { \mathsf { M P a } } andrefer to the table accordingly.
In the table, " - " indicates that the temperature at this pressure is below the saturationtemperatureand thereisnosuperheatedsteamstate.
NOTICESANDDISCLAIMERS
1.Technical Upgrade Notice
This manualis prepared based on the technical information available at the time of publicationand is intended solely asareference for product installation, commissioning,operation,andmaintenance.
In order to continuously improve product performance,reliability,and user experience,ZHEJIANG LEFOO CONTROLS CO.,LTD.reserves the right to optimize and upgrade product structures,software programs,functional configurations, communication protocols,technical specifications,and related documentation without prior notice,provided that the basic functions,key technical specifications,and contractual requirements of the product are not affected.
The illustrations,interface displays,menus,parameters,and diagrams contained in this manual are for reference only.The actual product configuration shall be subject to the sales contract, product nameplate,factory inspection documents,and the delivered product.
For the latest product information and documentation,please contact the technical service department of ZHEJIANG LEFOO CONTROLS CO., LTD.
2.Dimensions and Drawings Notice
The outline drawings,installation drawings,structural diagrams,and dimensional data contained in this manual are standard reference information intended for engineering design,installation,and product selection purposes only.
Due to factors such as product model, nominal size,optional configurations, manufacturing processes,raw material batches,and machining tolerances, the actual dimensions,installation dimensions,and structural detailsof the delivered product may differ slightly from those shown in this manual.
Unless otherwise specified,dimensionaltolerances are considered normal manufacturing variations and shall notbe regarded as product defects or quality issues.
For projects involving prefabricated piping,flange positioning,limited installation space,orotherspecial installationrequirements,customersare advised to obtain the latest approved drawings from our company prior to construction.The officially approved technical documents or the actual delivered product shall prevail.
3.Copyright and Interpretation
This manual is the intellectual property of ZHEJIANG LEFOO CONTROLS CO., LTD.
No partof this publication may be reproduced,copied,modified, distributed,or used for commercial purposes without prior written authorization from ZHEJIANG LEFOO CONTROLS CO., LTD.
Formatters not covered in thismanual, the sales contract, technical agreement,and applicable national or international standards shall prevail. (Subjectto revision.The latest released version shall prevail.)




