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Product Overview
The ZZYS30 Vortex Flowmeter: A cutting-edge velocity flow instrument designed for versatile applications.
Designed to precisely measure, monitor, and control the flow of liquids, steam, and a vast array of gases.
Engineered with a pioneering structure, it resists mechanical vibrations, impacts, and contamination effortlessly.
Boasting no moving parts, the ZZYS30 ensures zero wear and tear, negates the need for mechanical maintenance, offers low pressure loss, delivers stable performance, and maintains high accuracy.
User-friendly installation process with customizable sensor and signal converter matching.
Product Features:
Broad application capability; ideal for measuring steam, gas, and liquid flows.
Exceptional vibration resistance, zero drift at zero point, effectively neutralizing external vibrations.
The ZZY30 also features integrated temperature and pressure options, significantly reducing installation costs for users.
Offers diverse communication outputs including (0-5) kHz frequency, (4-20) mA, HART, and Modbus protocol.
Supports parameter settings via Bluetooth communication. Resistant to wear and dirt, requires no mechanical maintenance, ensures a long service life, and is explosion-proof for enhanced safety.
Technical index
Measurement medium: Gas, liquid, steam
Connection method: Flange clamp type, flange type, insertion type
Caliber specifications:
Flange clamping type: 25, 32, 50, 80, 100 mm
Flange connection type caliber selection: 100, 150, 200 mm
Flow measurement range: Normal measurement flow velocity range with Reynolds number 1.5×104~4×106; gas: 5~50m/s; liquid: 0.5~7m/s.
Normal measurement flow range for Liquid,
Gas flow measurement range: see Table 2.
Steam flow range: see Table 3.
Measurement accuracy: Class 1.0, Class 1.5
Measured medium temperature:
Room temperature: -25ºC~100ºC, high temperature: -25ºC~150ºC, -25ºC~250ºC Output signal: Pulse voltage output signal, High level: 8~10V, Low level: 0.7~1.3V Pulse duty cycle is about 50%, transmission distance: 100m
Pulse current remote transmission signal: 4-20 mA, transmission distance: 1000m Instrument use environment: Temperature: -25ºC~+55ºC, Humidity: 5~90% RH50ºC Material: Stainless steel, aluminum alloy
Power supply: DC24V or lithium battery 3.6V
Explosion-proof grade: Intrinsically safe iaIIbT3-T6, protection level: IP65
Technical parameters | |
Medium | Steam, Gas, Liquid |
Measuring range | See flow1-3 |
Caliber | DN15, DN25, DN40, DN50, DN80, DN100, DN200, DN250, DN300 |
Medium pressure | ≤100 bar, more pressure need be customized |
Medium temperature | -40°C~+240°C |
Ambient temperature | Ordinary type: -40°C~+85°C Ex-proof type: -40°C~+60°C |
Accuracy | Liquid, Re≥20000 is ±1.0%, gas and steam, ±1.5% |
Repeatability | ±0.3% |
Material | Measuring pipe:304,316L, HC276 |
Sensor: 316L, HC276 | |
Converter shell: casting aluminum | |
Instrument caliber | Flange connection: DN15-DN300 |
Clamping connection: DN15-DN100 | |
Flange standard | DIN, ANSI, HG20592 (Can be customized) |
Pressure loss Gasandliquid saturated steam |
ΔP=Cqv²Px ΔP: pressure loss(pa) qv: volume flow qm: mass flow ΔP=Cqm²Px PX: density C: constent |
Display | Two-line LCD display, four button operation Instantaneous flow, accumulated flow, vortex frequency, medium temperature, pressure(selectable), circular or non-circular display |
Power supply | Ordinary type: (14~36) VDC Ex-proof type: (14~30) VDC Battery power supply |
Loading | No-ex-proof: RB=(UB-14DVC)/22MA≤1200Ω Ex-proof: RB=(UB-14DVC)/22MA≤600Ω |
Output | Two wire 4~20mA |
Ex-proof class | Exd II CT6 CE19.1438 Ex ( ia ) II CT6 |
Cable interface | 1/2''NPT( Internal thread, recommended), M201.5 (Internal thread) |
Housing protection class | IP67 |
Connection type | Flange (DN15-DN300), Clamping (DN15-DN100) |
Mounting type | Integral mounting, split mounting (special shielded cable connect the pipe and indicator) |
Gas | |||
Air: t=20°C p=1.013bar abs =1.7210-4 mpa.s Q: flow (sheet 1) | |||
Nominal diameter | Internal diameter | Qmin(m3/h) | Qmax(m3/h) |
DN15 | 16 | 6.79 | 32.56 |
DN25 | 24 | 10.20 | 113.94 |
DN40 | 38 | 25.3 | 326.63 |
DN50 | 50 | 43.89 | 565.49 |
DN80 | 74 | 96.14 | 1238.64 |
DN100 | 97 | 165.14 | 2128.27 |
DN150 | 146 | 374.23 | 4821.57 |
DN200 | 193 | 702.95 | 9056.8 |
DN250 | 253 | 1123.7 | 14478 |
DN300 | 305 | 1632.1 | 21028 |
Liquid | |||
Water: t=20°C p=1.013bar abs ≤10cp Q: flow | |||
Nominal diameter | Internal diameter | Qmin(m3/h) | Qmax(m3/h) |
DN15 | 16 | 0.45 | 5 |
DN25 | 24 | 0.81 | 11.40 |
DN40 | 38 | 2.04 | 28.57 |
DN50 | 50 | 3.53 | 49.47 |
DN80 | 74 | 7.74 | 108.37 |
DN100 | 97 | 13.30 | 186.21 |
DN150 | 146 | 30.13 | 421.86 |
DN200 | 193 | 52.66 | 792.42 |
DN250 | 253 | 90.5 | 1266.8 |
DN300 | 305 | 113.41 | 1839.8 |
Saturated steam | |||||||||
Nominal Diameter |
Inner Diameter |
Mass flow Qm (kg/h) under different pressure and density | |||||||
P=1bar G | P=3.5bar G | P=5.2bar G | P=7 bar G | ||||||
ρ=1.13kg/m3 | ρ=2.43kg/m3 | ρ=3.28kg/m3 | ρ=4.17kg/m3 | ||||||
t=120.6°C | t=148.2°C | t=160.4°C | t=170.6°C | ||||||
min | max | min | max | min | max | min | max | ||
DN15 | 16 | 5.87 | 36.97 | 7.68 | 79 | 8.93 | 106.68 | 10.06 | 135.69 |
DN25 | 24 | 11.82 | 129.39 | 17.26 | 276.4 | 20.09 | 373.53 | 22.66 | 474.82 |
DN40 | 38 | 29.64 | 370.71 | 43.33 | 792.33 | 50.63 | 1070.2 | 56.8 | 1361.2 |
DN50 | 50 | 51.31 | 641.82 | 75.02 | 1371.8 | 87.19 | 1852.8 | 98.33 | 2356.6 |
DN80 | 74 | 112.41 | 1405.8 | 164.33 | 3004.7 | 191 | 4058.4 | 215.39 | 5161.8 |
DN100 | 97 | 193.14 | 2415.5 | 282.36 | 5162.7 | 328.16 | 6973.3 | 370.09 | 8869.2 |
DN150 | 146 | 437.56 | 5472.4 | 639.69 | 11696 | 743.45 | 15798 | 838.44 | 20093 |
DN200 | 193 | 821.91 | 10279 | 1201.6 | 21970 | 1396.5 | 29675 | 1574.9 | 37743 |
DN250 | 253 | 1313.9 | 16433 | 1920.9 | 35122 | 2232.5 | 47439 | 2517.7 | 60337 |
DN300 | 305 | 1908.3 | 23866 | 2789.8 | 51010 | 3242.4 | 68899 | 3656.6 | 87630 |
Nominal Diameter |
Inner Diameter |
Mass flow Qm (kg/h) under different pressure and density | |||||||
P=10.5 bar G | P=14 bar G | P=17.5 bar G | P=20 bar G | ||||||
ρ=5.89kg/m3 | ρ=7.6kg/m3 | ρ=9.32kg/m3 | ρ=10.54kg/m3 | ||||||
t=186.2°C | t=198.5°C | t=208.5°C | t=215.6°C | ||||||
min | max | min | max | min | max | min | max | ||
DN15 | 16 | 12.78 | 191.71 | 16.51 | 247.55 | 20.23 | 303.36 | 22.89 | 343.32 |
DN25 | 24 | 26.93 | 670.88 | 30.6 | 857.88 | 33.87 | 955.48 | 36.04 | 1201.41 |
DN40 | 38 | 67.51 | 1878.2 | 76.72 | 2150.7 | 84.93 | 2395.3 | 90.35 | 2557.7 |
DN50 | 50 | 116.89 | 3251.7 | 132.82 | 3723.4 | 147.03 | 4147 | 156.42 | 4428.1 |
DN80 | 74 | 256.03 | 7122.4 | 290.93 | 8155.8 | 322.06 | 9083.7 | 342.62 | 9699.3 |
DN100 | 97 | 439.91 | 12238 | 499.9 | 14013 | 553.38 | 15608 | 588.69 | 16666 |
DN150 | 146 | 996.62 | 27725 | 1132.5 | 31747 | 1253.7 | 35359 | 1333.7 | 37756 |
DN200 | 193 | 1872.1 | 52079 | 2127.3 | 59634 | 2354.9 | 66419 | 2505.2 | 70921 |
DN250 | 253 | 2992.7 | 83254 | 3400.71 | 95333 | 3764.6 | 106180 | 4004.9 | 113380 |
DN300 | 305 | 4346.5 | 120920 | 4939.1 | 138460 | 5467.5 | 154210 | 5816.5 | 164660 |
Selection list | ||||||||
model | Explanation | |||||||
ZZY30 | ||||||||
Connection | F | Flange connection | ||||||
W | Flange clamping | |||||||
Temperature Resistance Class |
T1 | Match with 250°c probe | ||||||
T2 | Match with 350°c probe | |||||||
Nominal diameter |
015 | DN15 | ||||||
020 | DN20 | |||||||
025 | DN25 | |||||||
032 | DN32 | |||||||
040 | DN40 | |||||||
050 | DN50 | |||||||
065 | DN65 | |||||||
080 | DN80 | |||||||
100 | DN100 | |||||||
125 | DN125 | |||||||
150 | DN150 | |||||||
200 | DN200 | |||||||
250 | DN250 | |||||||
300 | DN300 | |||||||
Structure |
Z | Integrated T and P compensation | ||||||
F | Regular model | |||||||
S | Split | |||||||
Material | R1 | 304 | ||||||
RL | 316L | |||||||
Instrument model |
N | 24V power supply Output 3 wire pulse | ||||||
V1 | 24V power, on-site display, 4-20mA, RS485, Impulse output | |||||||
V1 B |
24V +battery power supply, on-site display, 4-20 mA, RS485, pulse output | |||||||
Pressure Class | N | Normal | ||||||
H | High pressure |
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Piping Condition
The installation of the vortex flowmeter requires specific straight pipe sections before and after the sensor. The common configurations are as follows (D represents the diameter of the pipe):
Piping condition | upstream | Downstream |
Concentric shrinkage pipe full open gate valve |
15D | 5D |
∠90° square elbow | 20D | 5D |
Same plane 2∠90°elbow | 25D | 5D |
Semi-open gate valve regulating valve | 50D | 5D |
Different plane 2∠90°elbow | 40D | 5D |
With rectifier tube bundle | 12D | 5D |
1.
The sensor should be installed on a horizontal, vertical, or inclined pipe (with the liquid flowing from bottom to top) that matches the sensor's diameter. Ensure a specified length of straight pipe is present both upstream and downstream, requiring 15-20D for the front section and 5-10D for the rear section.
2.
The pipe near the liquid sensor should always be filled with the liquid being measured.
3.
Avoid installing the sensor on pipes that experience strong mechanical vibrations.
4.
Ensure the inner diameter of the straight pipe section is as consistent as possible with the sensor diameter. If consistency isn't possible, use a slightly larger diameter pipe, with an error margin of ≤3% and not exceeding 5mm. Avoid installation in areas with strong electromagnetic interference, limited space, or where maintenance is inconvenient..
5.
Horizontal pipeline installation is the most common method for flow sensors. For gas flow measurement, if the gas contains minor liquid quantities, place the sensor at a higher point in the pipeline. Conversely, for liquid flow measurement with minor gas presence, install the sensor at a lower point.
6.
Sensor installation in vertical pipelines: For gas flow measurement, install the sensor on a vertical pipeline without restricting flow direction. If the gas contains minor liquid quantities, the gas flow should be bottom to top. For liquid flow, ensure the flow is from bottom to top to prevent additional weight on the probe.
7.
Side installation of sensors on horizontal pipelines: Suitable for all fluids, especially superheated steam, saturated steam, and low-temperature liquids. Side mounting is preferred when possible, as it reduces the temperature impact on the amplifier.
8.
Inverted installation of sensors on horizontal pipelines is generally not recommended. It is unsuitable for general gases or superheated steam but can be used for saturated steam and high-temperature liquids, or when frequent pipeline cleaning is needed.
9.
When installing sensors on pipelines with insulation layers, ensure the insulation layer does not exceed one-third of the bracket height, especially for high-temperature steam.
10.
Selecting pressure and temperature measurement points: Depending on measurement needs, position the pressure measurement point 3-5D downstream of the sensor and the temperature measurement point 6-8D downstream.