Valid

GB/T 47707-2026Test method for distributed friction force measurement in air layer drag reduction models (English PDF)

气层减阻分布式阻力测量模型试验方法

Open the GB/T 47707-2026 preview as PDF

Preview — first pages of GB/T 47707-2026 (full document: 44 pages)

This is a limited preview

Buy now to download the full PDF (44 pages)

Issued by

SAMR; SAC

Level / Type

National · Recommended

Issue date

May 25, 2026

Implementation date

December 1, 2026

Scope

GB/T 47707-2026 is the English-translated version of 气层减阻分布式阻力测量模型试验方法.

GB/T 47707-2026 is the Chinese national standard covering measuring the friction along a hull model running on a layer of air - air lubrication cuts a ship's frictional resistance, and knowing where along the hull the layer works and where it breaks down is the whole design problem. It fixes the model and its instrumentation, the air injection, the test conditions in the towing tank and the data reduction. First edition, in force from 1 December 2026. It was issued on 25 May 2026 and takes effect on 1 December 2026, as a first edition. The document is under the responsibility of the Standardization Administration of China. This page is published from the official record of the 2026 edition; the clause text of a standard this recent is not yet in circulation, and the figures, limits and tables it contains are those of the document itself, delivered in full with the English translation.

Document preview — GB/T 47707-2026

National Standard of the People's Republic of China

ICS
47.020.20
Classification
U 11

Issued by: State Administration for Market Regulation; Standardization Administration of the PRC

Contents

  • 2 Normative references
  • 5 Experimental Equipment and Instruments
  • 5.2 Testing Instruments and Meters
  • 5.2.2 Atmosphere Condition Observation Camera Equipment
  • 5.2.5 Charge Amplifier
  • 6 Experimental Model
  • 6.1 Ship/Flat Model
  • 7 Installation Requirements for Sensors and Test/Observation Equipment
  • 7.3 Installation Requirements for Atmosphere Condition Observation Cameras
  • 8 Pre-test measurement requirements
  • 9 Test Procedure
  • 10 Experimental Data Processing and Presentation
  • 11 Gas Layer State Identification Method

2 Normative references

This document has no normative references.

The symbols given in Table 1 are applicable to this document.

5 Experimental Equipment and Instruments

5.1 Variable Pressure and Variable Speed Circulating Water Tank Circulating water tanks used for measuring the gas layer distribution resistance at a model scale of 10m or more should meet the following requirements.

a) The test section is over 10m long;

b) Width and height both exceeding 1m;

c) The maximum water velocity must not exceed 10 m/s;

d) Maximum pressure adjustment exceeds 300 kPa.

5.2 Testing Instruments and Meters

5.2.1 Distributed Local Resistance Measurement Sensor The sensor (balance) arrangement and range selection for distributed local resistance measurement are as follows: The location for measuring local resistance distribution should be determined based on the principal dimensions of the ship or flat plate model used in the experiment, and the estimated cavitation length of the air layer to be formed. Within the cavitation range, select at least three different resistance measurement locations along the longitudinal section (the number of local resistance measurements can be used to divide the longitudinal section of the cavitation into equal parts). Arrangement using section lines. The range of the local resistance measurement sensor should be determined based on the resolution and accuracy characteristics of the strain sensor, and in conjunction with the maximum test flow rate (e.g.,...). 7 m/s (normal sailing speed of large oil and bulk carriers), select a suitable size local resistance measurement unit force plate (e.g., 300 mm × 100 mm). (Using a 300mm × 10mm aluminum plate), estimate the range of resistance that can be measured on the lower surface of the force measuring plate in each unit. (Lower surface of each unit force measuring plate) The magnitude of the resistance is determined by the frictional resistance coefficient, the maximum test flow velocity, and the area of the wetted surface (the surface in contact with the fluid) on the lower surface. (Each unit) The frictional resistance coefficient of the force-measuring plate is based on the experimental Reynolds number (calculated using the distance from the jet nozzle to the center of the force-measuring plate of each local unit as the Reynolds number). The characteristic length, calculated by referring to relevant parameters in conjunction with the water temperature tw, air temperature ta, and water density rho during the experiment, is estimated using the Haisang formula. (1) Calculate.

5.2.2 Atmosphere Condition Observation Camera Equipment

5.2.2.1 The imaging equipment (conventional CCD) used for atmospheric state observation operates normally under continuous lighting conditions, with a pixel count better than 1024× 1024, record at least 25 frames per second.

5.2.2.2 Camera equipment (high-speed cameras) used for observing the dynamic characteristics of air layers can also operate normally under continuous light, and its highest capture speed... The shooting frequency should be no less than.2000 frames per second, and the minimum image quality should be no less than 300,000 pixels.

5.2.3 Piezoelectric Miniature Pulsating Pressure Sensor Pressure sensors used for measuring pulsating pressure on flat surfaces and gas layer surfaces should meet the following requirements.

a) The outer diameter is no more than 10mm;

b) The maximum diameter of the pressure-sensitive diaphragm is no more than 6 mm;

c) The measured frequency response range is greater than 20kHz;

d) Resolution up to Pa level (piezoelectric sensor), static pressure overload capacity greater than.200 kPa.

5.2.4 DC Amplifier A DC amplifier used for DC signal amplification in resistance measurement has a maximum amplification factor of not less than 1000 times and an accuracy of not more than [missing value]. 0.1%, with multiple selectable levels. The DC amplifier should also provide the maximum external drive power, with multiple selectable levels and low-pass filtering. Function.

5.2.5 Charge Amplifier

5.2.5.1 Charge amplifiers used for amplifying charge signals shall meet the following requirements.

a) Gain not less than 10mV/pc;

b) Accuracy not greater than 0.1%;

c) Output impedance less than 40Omega;

d) Maximum frequency response not less than 50kHz.

5.2.5.2 Voltage output type piezoelectric pressure sensor does not require a charge amplifier and can be directly driven by a data acquisition card with power supply function.

5.2.6 Gas Flow Meter During the gas layer drag reduction test, the gas flow rate is measured. The gas flow meter should have temperature and pressure correction functions, i.e., gas mass... Flow measurement (simulating different draft depths to eliminate the influence of gas compressibility on gas flow measurement). The measurement range is determined based on the hull model or flat plate model. The inner surface area SP of the cavitation cavity on the lower surface of the model is estimated based on the equivalent nominal gas layer thickness t=0.007m. The required gas flow rate Q is calculated as shown in formula (3). Q = SP × t × 3600 (3) The maximum capacity of a gas flow meter should be

1.5 to 2 times the required gas flow rate, and its accuracy should be no less than 1.5%. A gas flow meter should... A vortex flow meter is used to reduce the impact of humid gas in the pipeline on flow measurement.

5.2.7 Dynamic Signal Acquisition Card The data acquisition A/D card used for dynamic signal acquisition should have no fewer channels than the number of pulsating pressure measurement points, and each channel should be able to acquire data simultaneously. Similarly, the highest sampling frequency per channel is not less than 50kHz, and the A/D conversion resolution is better than 16bit.

5.2.8 Instruments for measuring water velocity and ambient pressure The maximum range of the pressure transmitter used for measuring the test water velocity and negative pressure in the closed-loop circulating water tank should not exceed 150 kPa, and the accuracy should not exceed [missing value]. 0.5%; the maximum range of the pressure transmitter used for positive pressure measurement in the test is not greater than 600 kPa, and the accuracy is not greater than 0.5%. The test is conducted in a towed water tank. The test speed was determined by the trailer speed, with a measurement accuracy of no more than

0.005 m/s. Ambient pressure was used to measure the subsidence depth using a meter stick, with a measurement accuracy of no more than [missing value]. 1mm.

5.2.9 Barometer The barometer should have a measurement range of 80 kPa to 110 kPa and an accuracy of no more than

0.1 kPa.

5.2.10 Thermometer The thermometer should have a measurement range of -20°C to 50°C and an accuracy of no more than 0.1°C. The water thermometer should have a measurement range of 10°C to 50°C and an accuracy of no more than 0.1°C.

6.1 Ship/Flat Model

6.1.1 Ship Model The ship model (including the hull and appendages) should be geometrically similar to the full-scale design, with a smooth shape, clean surface, and should have a product certificate of conformity. Book. For the design and fabrication of the hull model below the waterline, the total length error of the fully appended ship model should be within ±0.1% Lpp and should not exceed [a certain value]. 10mm, with cross-sectional profile errors within ±0.5mm, and the machining precision of each appendage is the same as that of the ship model. If a hull model is used in the experiment... The model is attached to the top of the test section or the model mounting frame by means of a suspension rod. A typical installation example in the water tank is shown in Figure A.1 in Appendix A.

6.1.2 Three-dimensional flat plate model The three-dimensional flat plate model of the local scaled-down test of the typical area where the air cavitation is located on the ship's bottom should be geometrically similar to that of the real-scale local flat plate (air cavitation area). The surface is smooth and has a clean finish. The 3D flat plate model is designed with a certain thickness (e.g., 150mm). If the thickness is too low, its rigidity is low and its deformation is large, which is unfavorable. The box structure (for model installation and experimental measurement) has a semi-elliptical guide section at its head and a triangular wedge-shaped downstream section at its tail. The total length error of the 3D flat plate model is within ±0.1%L, and the line shape error of each cross-section is within ±0.5mm. The surface of the flat plate is not... The flatness should be within ±1mm. For large flat panel models exceeding 5m, a longitudinal and transverse steel frame should be installed internally, and multiple wing-shaped swords should be used. A three-dimensional flat plate model is suspended by a rod to ensure model rigidity. The longitudinal deformation of the model is less than 2mm. A typical installation example in the water tank is shown in Figure A.2.

6.2 Cavitation Model The cavitation model includes a bow gas layer generation device (wedge-shaped block or other shape), a nozzle module, a baffle module, a stern gas retention module, and a stabilizer. Pressure chambers, gas pipelines, etc. The entire cavitation area on the bottom of the ship or within the 3D flat plate model must be free of holes or gaps allowing gas to escape (local resistance measurement). Except for the narrow gaps around the unit plate, and considering the need for special handling to prevent gas from escaping outside the model (gas layer generation device and stern-mounted air-supported model). The block runs through the horizontal position of the model, and the plexiglass baffles preventing gas escape are arranged on both sides of the model, with the baffles' bow and stern aligned with the wedge-shaped blocks of the gas generation device. The gas-holding module is smoothly connected. The baffle is marked with scale lines at different positions along the model's longitudinal direction.

6.3 Gas Pressure Stabilizing Chamber and Piping Model The gas pressure stabilizing chamber is positioned appropriately within the hull or flat plate model, based on the location of the nozzle. The air inlet of the pressure stabilizing chamber and the nozzle are located within the model. The longitudinal positions are staggered by more than 100mm. The gas pressure stabilizing chamber has multiple air inlets connected to the gas source pipeline, and a space is arranged between the gas source and the pipeline. For gas flow meters, the distance between the straight pipe sections before and after the flow meter should meet the flow requirements.

7 Installation Requirements for Sensors and Test/Observation Equipment

7.1 Installation Requirements for Local Resistance Measurement Sensors The local resistance measurement sensors are aligned with the model's centerline and are positioned in a straight line within the cavity, parallel to the model's longitudinal axis. Multiple resistance sensors are connected at one end to the unit force plate and at the other end to the fixed base inside the model. The unit force plate is also connected to the flat plate model. The gap is approximately 1mm. A sealed cavity and partition are installed above the force measuring plate and resistance sensor to ensure that gas enters through the gap without leaking out. The gas accumulates and reaches equilibrium before stabilizing. Typical installation examples in the water tank are shown in Figures A.3 and A.4.

7.2 Installation Requirements for Pulsating Pressure Sensors The pulsating pressure sensor is rationally selected based on the area where gas layers may form, and embedded on the plate where the gas cavitation is located, with its surface flush with the plate where the gas cavitation is located. The plate surface is flush and the edges are smooth without any bumps. A pulsating pressure sensor can also be embedded in the unit force plate, with the pressure-sensing surface of the pulsating pressure sensor aligned with... The lower surface of the force measuring plate is flush with the surface.

7.3 Installation Requirements for Atmosphere Condition Observation Cameras

7.3.1 In the flat-bottomed area next to the local resistance measurement unit plate, a transparent plexiglass plate is inlaid. Above the plexiglass plate and inside the model, a... The watertight air layer condition observation equipment is set with its focal length within 3cm to 5cm below the flat plate for observing the air layer condition.

7.3.2 At the transparent window outside the test section, high-speed cameras and lighting sources can be reasonably set according to the viewing angle, while minimizing reflections from the transparent window. The impact of the photographs or video footage is assessed using the scale markings on the transparent baffles on both sides of the model, which are crucial for understanding certain aspects of the gas layer formation. Dynamic features of the heart region are captured and air layers are identified.

8 Pre-test measurement requirements

8.1 Requirements for Test Equipment and Instruments Before the test, the test equipment and instruments should meet the following requirements.

a) The test water is clean, transparent, and has a relative air content of less than 0.85;

b) The hull/flat plate and gas layer generation device models must be uniquely identified;

c) All instruments and meters used in the test are within their metrological validity period;

d) Before measurement, the instruments and meters should be turned on and warmed up for at least 15 minutes.

8.2 Determination of Experimental Parameters The determination of test parameters should meet the following requirements.

a) Test pressure. Ensure that during the jetting process, the ambient pressure in the test section is less than the maximum range of the pulsating pressure sensor or the pressure overload. ability;

b) Test water velocity. meets the supercritical Reynolds number, the specified test flow velocity, or the actual operating speed of the ship.

9 Test Procedure

9.1 Model Assembly The specific requirements for assembling the test model are as follows:

a) The hull/flat plate model is hoisted into the test section, ensuring that the bow and stern centerlines of the model are parallel to the centerline of the test section, i.e., the bow/stern of the model. The difference in distance between the centerline and one side wall of the test section is less than 2mm, and the difference in distance between the bow/stern centerlines and the test section is also less than 2mm. The bottom height difference is less than 2mm;

b) When installing the force plate and pulsating pressure sensor of the local resistance unit, ensure that the pressure-sensing surface of the force plate and pressure sensor is in contact with the cavitation. The inner model surface is flush, and there are no burrs or rough spots around the test area;

c) Inspect the cavitation area and the area between the baffle and the model for any holes, cracks, gaps, etc. indicating gas leakage;

d) Connect the gas source, gas flow meter, pipelines and piping systems, pressure stabilizing chamber, nozzles, etc., and perform gas injection and inspection to ensure that the entire gas pipeline system, except for the nozzles, is functioning properly. There was no air leakage outside the nozzles, and the gas velocity ejected from each nozzle was uniform and stable. This can be verified using an anemometer or by filling the nozzles with water. Check the movement status of the ejected gas.

9.2 Integrated Testing of the Test System To reduce the impact of pressure changes during the jetting process on the testing instruments and to ensure proper gas selection under different gas layer conditions during subsequent experiments. Traffic settings should be configured as follows, and the test system should be integrated and debugged according to the following steps.

a) Before the experiment, at a certain flow rate, jet gas was injected into the cavitation, and the uniformity and stability of the ejected gas were observed. Simultaneously, the flow rate of the gas from the cavitation head was also observed. After the gas is ejected, ensure that there is no gas floating or leaking within the entire cavitation area;

b) Test several flow rates and perform gas injection at multiple flow rates to check the safety and reliability of the entire model, while also testing the injection... During the gasification process, the increase in environmental pressure in the water tank test section;

c) Under normal operating conditions of all equipment in water, divide the range of environmental pressure increase from step

b) into 3 to 4 intervals. When v=0, test the sensitivity of each local resistance sensor to pressure changes, and calibrate the force sensor by specifying a certain pressure. The stability of the output when the pressure rises and falls back to the specified pressure is measured, and this is obtained through repeated measurements of the environmental conditions. The effect curve of pressure on the local resistance sensor;

d) Determine the approximate gas flow rate required for the formation of a gas layer (or local gas layer) in the cavitation region under several different flow rate conditions;

e) Check whether the pulsating pressure sensor works properly and has good performance under different flow rates and conditions of full humidity, bubbles, and gas layers. Resolution;

f) Check whether the scale markings on both sides of the baffle are reasonable and whether they can be clearly distinguished and read under typical working conditions and different lengths of the gas layer.

9.3 Test Measurement The test measurements should be performed according to the following steps.

10 Experimental Data Processing and Presentation

10.1 Data Processing and Representation of Local Resistance Measurement Based on the voltage signals measured during the experiment, and using the calibration coefficients and pressure correction curves of the local resistance sensors at various locations, the following calculations were performed. Calculate the drag of each unit force sensor at different speeds with and without jet propulsion, and calculate the corresponding drag coefficient. Use the Haisang formula to calculate the drag of each unit. The drag coefficient of the force sensor at the corresponding location under fully wet conditions. Compare the consistency between the measured and calculated results under fully wet conditions. Within reasonable limits, and to confirm the validity of other measurement data during the jetting process.

10.2 Data Processing and Representation of Pulsating Pressure Measurement The surface pulsating pressure under different gas layer conditions is measured by a piezoelectric sensor, and the pulsating pressure is obtained by energy integration within a certain frequency range. The overall level, i.e., the pulsating pressure results under different operating conditions, is given in the form of fm~SPL(fm)~SPL. Where SPL is calculated according to formula (8). calculate.

10.3 Data Processing and Expression of Gas Layer Morphology Measurement Results The gas layer results are presented primarily through a combination of hand-drawn diagrams and local video imagery, depicting the gas layer under different conditions on the flat bottom. The shape of the surface. First, draw the projected outline of the experimental model, including the head, the air cavitation plane area, and the tail, as well as the flat bottom where the air cavities are located. The surface can be represented by a single layer of oblique lines to indicate a smooth air layer coverage area, and by a double layer of oblique lines to indicate a rough, fish-scale-like air layer coverage area. The dashed lines represent gas escape barriers, and the curves represent gas layer thickness at different locations. Furthermore, for specific gas layer conditions, different flat plates... Images of the gas layer (surface morphology, thickness, and wave shape at the gas-water interface, etc.) are captured at the location to aid in explanation and to compare with the gas layer morphology. The drawings corroborate each other.

11 Gas Layer State Identification Method

11.1 General Provisions In gas layer drag reduction measurement experiments, because the physical parameters measured within the gas layer differ during its formation, the methods for identifying the gas layer state also vary. The following section presents three typical methods for gas layer state identification. Other methods for gas layer identification include porosity meters and conductivity meters. All methods can refer to the method for measuring and identifying the pulsating pressure on the inner wall of the gas layer for measurement and analysis.

11.2 Drag Reduction Rate Changes and Gas Layer Identification Methods The variation of lower surface resistance measured by a local unit force plate on a flat-bottomed or extra-large flat plate of a ship under fully wet flow conditions and different jet flow conditions. Based on the calculation results of formula (4), the change in drag reduction rate can determine whether a gas layer has formed. For the local drag measurement gas layer identification method, when the drag reduction rate is reduced... When the resistivity is less than 20%, it is in the bubble (including microbubble) drag reduction stage (BDR); when the drag reduction rate is between 30% and 60%... Within the specified range, it represents the transition state between the bubble and the gas layer; when the drag reduction rate exceeds 80% (inclusive), it represents the drag-reduced state of the gas layer. (Air layer degeneration, ALDR). See Figures A.5 to A.8.

11.3 Methods for identifying water vapor patterns and gas layers Water vapor speciation and gas layer identification methods should meet the following requirements.

a) Using optical measurement methods, images of bubbles with different densities are displayed on the bottom surface of the flat plate during the bubble drag reduction stage;

b) During the transition phase, after the water and air are fully mixed, a "glassy" lubricating layer is formed;

c) During the gas layer stage, there are a small number of droplets on the lower surface of the observation window. Under the action of airflow, the droplets can move slowly. While transparent baffles and graduated lines on both sides of the cavitation can distinguish between gas layers, it is difficult to differentiate between bubble morphology, transition zone morphology, and gas layer morphology. The process involves three stages. See Figures A.9 to A.15 for relevant diagrams and photographs.

11.4 Gas Layer Inner Wall Pulsating Pressure and Gas Layer Identification Method Spectral analysis of experimental data obtained using a piezoelectric pulsating pressure sensor can distinguish between gas layers and non-gas layers. During gas layer formation, the pulsation... The dynamic pressure spectrum curve has a distinct convex envelope, and the total pulsating pressure level is higher than that in the fully wet state within the.200Hz~8000Hz frequency band. The total pulsating pressure level is more than 10 dB higher. See Figures A.16 and A.17. Other methods for gas layer identification include porosity meters, conductivity meters, and other measurement and identification techniques. These can all be referenced in the measurement and identification of pulsating pressure on the inner wall of the gas layer. Other methods are used for measurement and analysis.

12 Test Report The test report should include the following.

a) Test number and name;

b) Testing instruments and equipment;

d) Experimental objective;

e) Testing basis;

f) Specimen test type;

g) Test installation and test conditions;

......
This preview omits tables, figures, formulas and parts of the technical clauses. The complete document — 44 pages — is available in the English PDF.

How to Buy GB/T 47707-2026

  1. 1Add to cart. Click the "Buy GB/T 47707-2026" button on this page. You can add more standards before checkout.
  2. 2Checkout. Enter your email and billing details. Payment is processed securely by Stripe (cards, Apple Pay, Google Pay supported).
  3. 3Instant delivery (0–9 sec). Delivery is automatic: within seconds of payment you'll receive an email with a secure download link. The link stays valid for 72 hours.
  4. 4Invoice included. A tax invoice is attached to the confirmation email. Need a custom invoice? Contact us.

Related Standards

English PDF
44 pages
Instant delivery (0–9 sec)
Invoice included
View Cart

Secure payment via Stripe

Payments accepted

VisaMastercardAmerican ExpressApple PayGoogle PayStripe

GB/T 47707-2026

$365.00

$310.00for partners