CN203587468U - Device for detecting content of liquid-phase water in wet steam - Google Patents
Device for detecting content of liquid-phase water in wet steam Download PDFInfo
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- CN203587468U CN203587468U CN201320649401.0U CN201320649401U CN203587468U CN 203587468 U CN203587468 U CN 203587468U CN 201320649401 U CN201320649401 U CN 201320649401U CN 203587468 U CN203587468 U CN 203587468U
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Abstract
The utility model relates to a device for detecting the content of liquid-phase water in wet steam. The device is arranged on a wet steam main pipeline, wherein the device comprises a bypass pipeline, a first valve, a second valve, a test container and a heater; the bypass pipeline and the wet steam main pipeline are communicated with each other; the first valve and the second valve are arranged on the bypass pipeline; the test container is filled with quantitative air; the heater is connected with the test container; the bypass pipeline between the first valve and the second valve forms a sealed sampling space through a third valve; a pressure meter, a temperature meter and a humidometer are arranged on the test container; the test container is communicated with the sealed sampling space through the third valve. The device is capable of measuring the state of tested air on line; only simple and common accessory devices are arranged; the test process is simple and practicable; meanwhile, check computation of heat is not required; the radiation loss has no influence on measurement precision; the device is applicable to the wet steam at various pressure grades.
Description
Technical field
The utility model relates to a kind of wet steam physical measurement technical field, specifically, relates to liquid phase water content detection device in a kind of wet steam.
Background technology
The content of measuring liquid phase water in wet steam, has the demand of many reality, but does not still have so far the desirable solution of neither one.Assay method in existing development in principle, mainly contains thermodynamic method, optical method, spike and conductive method, partition method, Critical speed method and utilize orifice plate measurement etc.In conventional thermodynamic method, there is again coagulation, steam air mixing method, the methods such as heating.
Coagulation is by the saturated vapour style being extracted, and is condensed into condensate water in condenser, calculates the relative scale of liquid phase water in gas phase according to cooling water inflow, and it has shortcoming that can not on-line measurement.It is that the sample of wet steam is mixed mutually with air that steam air mixes ratio juris, the selection of its ratio will guarantee that the steam in last mixed gas is unsaturated, the humidity of mixed air is measured by hygrometer, it needs larger space, and limited space is difficult to guarantee to have scarcely liquid phase water after mixing.Heating ratio juris is that the sample of extracted saturated wet steam is heated to dry state of saturation, or superheat state, then measure the flow of steam sample, according to the variation of sample thermal parameter before and after added heat and heating, obtain the humidity of wet steam, the apparatus structure complexity of making based on this method, and be arranged in the main pipeline of steam, outside support equipment is more, adopt heat metering, error is larger, and inevitable.
Although above-mentioned thermodynamics method can be measured the content of liquid phase water in wet steam, and compared with additive method, principle is fairly simple, it is comparatively easy to apply, but, but can not meet the demand of on-line measurement, and as the method for using in engineering, for playing the function of process monitoring, need to have the function of on-line measurement.
Utility model content
Technical problem to be solved in the utility model is that the deficiency existing for liquid phase water content detection in existing wet steam, provides liquid phase water content detection device in a kind of wet steam, to can carry out on-line measurement to the content of liquid phase water in wet steam.
To achieve these goals, liquid phase water content detection device in wet steam of the present utility model, is arranged on a wet steam main pipeline, comprises bypass line, the first valve, the second valve, test container and well heater.Bypass line and wet steam main pipeline are connected.The first valve, the second valve are arranged on bypass line.The air of set amount is housed in test container.Well heater is connected with test container.Wherein, the bypass line between the first valve and the second valve forms an enclosed sampling space by one the 3rd valve, is provided with pressure gauge, thermometer and hygrometer on test container, and test container is connected by described the 3rd valve and enclosed sampling space.
Liquid phase water content detection device in above-mentioned wet steam, wherein, on described test container, be provided with one communicate with ambient atmosphere, with both the 4th valve of quantitative air described in filling/discharging.
Liquid phase water content detection device in above-mentioned wet steam, wherein, the ratio of the volume in described enclosed sampling space and the volume of described test container is 3%～5%.
Beneficial functional of the present utility model is: by the way of the online sampling of bypass and formation enclosure space, can the tested gaseous state of on-line measurement, by state parameter, obtain the content of liquid phase water, only need the simple conventional auxiliary device of configuration, test process is simple; And without the accounting of carrying out heat, radiation loss does not affect measuring accuracy, is applicable to the wet steam of various pressure ratings.
Below in conjunction with the drawings and specific embodiments, the utility model is described in detail, but not as to restriction of the present utility model.
Accompanying drawing explanation
Fig. 1 is the structure principle chart of liquid phase water content detection device in wet steam of the present utility model;
Fig. 2 is liquid phase water detection method of content process flow diagram in wet steam of the present utility model.
Wherein, Reference numeral
11-bypass line
The 12-the first valve
The 13-the second valve
14-test container
15-well heater
16-enclosed sampling space
17-pressure gauge
18-thermometer
19-hygrometer
The 110-the three valve
The 111-the four valve
20-wet steam main pipeline
Embodiment
Below in conjunction with the drawings and specific embodiments, technical solutions of the utility model being described in detail, further to understand the purpose of this utility model, scheme and effect, but is not the restriction as the utility model claims protection domain.
Consult the structure principle chart of liquid phase water content detection device in Fig. 1 wet steam of the present utility model, as shown in the figure, liquid phase water content detection device in wet steam of the present utility model, is arranged on a wet steam main pipeline 20.It comprises bypass line 11, the first valve 12, the second valve 13, test container 14 and well heater 15.Bypass line 11 is connected with wet steam main pipeline 20.The first valve 12, the second valve 13 are arranged on bypass line 11.Test container 14 is for being installed in both quantitative air.Well heater 15 is connected with test container 14.Wherein, bypass line between the first valve 12 and the second valve 13 forms an enclosed sampling space 16 by one the 3rd valve 110, on test container 14, be provided with pressure gauge 17, thermometer 18 and hygrometer 19, and test container 14 is connected with enclosed sampling space 16 by the 3rd valve 110.From said structure setting, can find out, the utility model accesses a bypass line 11 on wet steam main pipeline 20, by-pass pipe on bypass line 11 is connected with test container 14 by a valve (i.e. the 3rd valve 110), during normal work, by-pass pipe is as a part for pipeline, allow wet steam normally to pass through, when measuring, (the valve (i.e. the first valve 12, the second valve 13 and the 3rd valve 110) of cutting out turnover section on bypass circulation forms a confined space, enclosed sampling space 16), the wet steam in confined space is the sample of test.
In order to facilitate test container 14 to be installed in or discharged air, on test container 14, be provided with one communicate with ambient atmosphere, to fill/to discharge the 4th valve 111 of both quantitative air.In addition, in order to be convenient for measuring, the ratio of the volume in enclosed sampling space and the volume of test container is preferably 3%～5%, but in actual use not as limitation.
Further, consult Fig. 2, in the wet steam that the utility model provides, liquid phase water detection method of content, comprises the steps:
S100, on wet steam main pipeline, 20 arrange liquid phase water content detection device in a wet steam described above, in this step, comprise that the ratio of the control volume in enclosed sampling space and the volume of test container is 3%～5% step.
S200, opens the first valve 12, the second valve 13, closes the 3rd valve 110, to be full of wet steam to be tested in enclosed sampling space 16.
S300, opens the 4th valve 111 and in test container 14, fills both quantitative air, and while opening the 4th valve 111, surrounding air state of nature is carried out in test container 14.。
S400, closes the 4th valve 111, the first valve 12, the second valve 13, opens the 3rd valve 110, so that wet steam is mixed to form mixed gas mutually with described air.In this step, the object of opening the 3rd valve 110 is that test container 14 is connected with the enclosed sampling space 16 that bypass line forms, owing to having pressure reduction between test container 14 and enclosed sampling space 16, after connection, the gas of different pressures can be mixed to form mixed gas mutually.By the instrument being connected with test container 14, gaseous tension after test mixing, temperature, humidity can be determined the now state of gas, because the volume of test container 14 is limited, and the steam of sneaking into test container is wet steam, the humidity of the mixed gas therefore just having formed is 100%, wherein carries liquid phase water secretly.
S500, heats the mixed gas in test container 14 by well heater 15, and obtains respectively force value, temperature value and humidity value by pressure gauge, thermometer and hygrometer.In this step, by the preferred resistance wire of well heater 15(well heater 15) mixed gas in test container 14 is heated, along with the rising of temperature, liquid phase water in mixed gas can be vaporized gradually, after the liquid phase water of carrying secretly in gas is vaporized completely, if continue to heat, the humidity value of mixed gas will decline.Any state value when the critical conditions value while measuring humidity value appearance decline or humidity are less than 100%, can obtain the now total amount of water in air steam accordingly.
S600, according to the volume in enclosed sampling space 16, the volume of test container 14, the force value that pressure gauge, thermometer and hygrometer obtain, temperature value and humidity value calculate the content that obtains liquid phase water in wet steam.In this step, by data processing, deduct airborne steam content and quantity of steam corresponding to steam-laden state that enter, more than amount be the content of the liquid phase water that comprises in the wet steam entering.
After being completed, first close the 3rd valve 110, bypass line 11 and test container 14 are cut off, and then open the first valve 12 and the second valve 13, make bypass line enter normal operating condition.Then open the 4th valve 111, by the mixed gas emptying of test, test container is full of by surrounding air again, for test and prepare next time.
In described step S600, comprise by formula H
bS=γ × V
bcalculate water yield step S610 corresponding to saturated vapour entering in test container, wherein, H
bSfor the weight (Kg) of saturated vapour, γ is at the severe (Kg/M that measures saturated vapour at temperature
3), V
bfor the volume (M of saturated vapour sampling
3).The steam passing through due to bypass line and wet steam main pipeline 20 has same characteristic, can predict the temperature of saturated vapour by instrument, according to table 1(, sees the following form), known under this state, the severe of steam.Because the volume in enclosed sampling space is determined, the volume of saturated vapour sampling is known, thereby can calculate the water yield corresponding to saturated vapour entering in test container, that is, and and H
bs.
The characteristic of table 1 saturated vapour
| Temperature | Severe | Pressure | Temperature | Severe | Pressure |
| t | γ | Pa | t | γ | Pa |
| ℃ | kg/m 3 | MPa | ℃ | kg/m 3 | MPa |
| 0 | 0.004851 | 0.815 | 190 | 6.390 | 1.18 |
| 10 | 0.009404 | 0.831 | 200 | 7.854 | 1.21 |
| 20 | 0.01731 | 0.847 | 210 | 9.580 | 1.24 |
| 30 | 0.03040 | 0.863 | 220 | 11.61 | 1.26 |
| 40 | 0.05121 | 0.883 | 230 | 13.98 | 1.29 |
| 50 | 0.08308 | 0.896 | 240 | 16.74 | 1.33 |
| 60 | 0.1303 | 0.913 | 250 | 19.96 | 1.36 |
| 70 | 0.1982 | 0.930 | 260 | 23.70 | 1.40 |
| 80 | 0.2943 | 0.947 | 270 | 28.06 | 1.44 |
| 90 | 0.4234 | 0.966 | 280 | 33.15 | 1.49 |
| 100 | 0.5975 | 0.984 | 290 | 39.12 | 1.54 |
| 110 | 0.8260 | 1.00 | 300 | 46.15 | 1.61 |
| 120 | 1.121 | 1.02 | 310 | 54.52 | 1.71 |
| 130 | 1.495 | 1.04 | 320 | 64.60 | 1.04 |
| 140 | 1.965 | 10.6 | 330 | 77.00 | 2.24 |
| 150 | 2.545 | 1.08 | 340 | 92.68 | 2.82 |
| 160 | 3.256 | 1.11 | 350 | 113.5 | 3.83 |
| 170 | 4.118 | 1.13 | 360 | 143.7 | 5.34 |
| 180 | 5.154 | 1.15 | 370 | 200.7 | 15.7 |
In described step S600, comprise and pass through formula
calculate the both quantitative airborne water cut step S620 in test container, wherein, H
kSfor airborne water cut (Kg), η is relative humidity (% can record by hygrometer), P
sfor the pressure of saturated vapour (Pa can table look-up and 1 obtain according to room temperature), P is atmospheric pressure (Pa can record by rain glass), V
kfor the volume (M of test container
3, be known quantity), thus can calculate the both quantitative airborne water cut in test container, that is, and H
kS.
In described step S600, also comprise and pass through formula
calculate the water cut step S630 in mixed gas, wherein, H
hSfor the total content (Kg) of liquid phase water in mixed gas, V
hfor the volume (M of mixed gas
3, V
h=V
b+ V
k), P
hfor the pressure (Pa can record by pressure gauge) after mixed gas heating, P
hSfor the pressure of saturated vapour under the temperature conditions after mixed gas heating (Pa, because the temperature after heating can record by thermometer, the temperature 1 acquisition pressure of tabling look-up accordingly), thereby can calculate the total content of liquid phase water in mixed gas, that is, and H
hS.
In described step S600, also comprise according to formula H
y=H
hS-H
bS-H
kScalculate liquid phase water content step S640 in wet steam.
As can be seen from the above, the utility model combines the mechanism of mixing method and heating, by the way of the online sampling of bypass and formation enclosure space, can the tested gaseous state of on-line measurement, by state parameter, obtain the content of liquid phase water, only need the simple conventional auxiliary device of configuration, test process is simple; And without the accounting of carrying out heat, radiation loss does not affect measuring accuracy, is applicable to the wet steam of various pressure ratings.
Certainly; the utility model also can have other various embodiments; in the situation that not deviating from the utility model spirit and essence thereof; those of ordinary skill in the art are when making various corresponding changes and distortion according to the utility model, but these corresponding changes and distortion all should belong to the protection domain of the appended claim of the utility model.
Claims (3)
1. a liquid phase water content detection device in wet steam, is arranged on a wet steam main pipeline, it is characterized in that, comprising:
Bypass line, is connected with described wet steam main pipeline;
The first valve, is arranged on described bypass line;
The second valve, is arranged on described bypass line;
Test container, is equipped with the air of set amount in it; And
Well heater, is connected with described test container;
Wherein, bypass line between described the first valve and the second valve forms an enclosed sampling space by one the 3rd valve, on described test container, be provided with pressure gauge, thermometer and hygrometer, and described test container is connected by described the 3rd valve and described enclosed sampling space.
2. liquid phase water content detection device in wet steam according to claim 1, is characterized in that, on described test container, be provided with one communicate with ambient atmosphere, with both the 4th valve of quantitative air described in filling/discharging.
3. liquid phase water content detection device in wet steam according to claim 2, is characterized in that, the ratio of the volume in described enclosed sampling space and the volume of described test container is 3%～5%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320649401.0U CN203587468U (en) | 2013-10-21 | 2013-10-21 | Device for detecting content of liquid-phase water in wet steam |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320649401.0U CN203587468U (en) | 2013-10-21 | 2013-10-21 | Device for detecting content of liquid-phase water in wet steam |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103592199A (en) * | 2013-10-21 | 2014-02-19 | 中国中元国际工程公司 | Liquid-phase water content detection device and liquid-phase water content detection method for wet steam |
| CN109507372A (en) * | 2018-12-21 | 2019-03-22 | 核动力运行研究所 | A kind of steam generator steam wetness measurement system and method |
| CN110501417A (en) * | 2019-09-20 | 2019-11-26 | 华北电力大学 | Steam moisture on-line monitoring system and method in a kind of pipeline based on acoustics |
-
2013
- 2013-10-21 CN CN201320649401.0U patent/CN203587468U/en not_active Withdrawn - After Issue
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103592199A (en) * | 2013-10-21 | 2014-02-19 | 中国中元国际工程公司 | Liquid-phase water content detection device and liquid-phase water content detection method for wet steam |
| CN103592199B (en) * | 2013-10-21 | 2015-11-25 | 中国中元国际工程有限公司 | Liquid phase water content on-line measuring device and detection method in wet steam |
| CN109507372A (en) * | 2018-12-21 | 2019-03-22 | 核动力运行研究所 | A kind of steam generator steam wetness measurement system and method |
| CN109507372B (en) * | 2018-12-21 | 2023-10-20 | 核动力运行研究所 | Steam humidity measurement system and method for steam generator |
| CN110501417A (en) * | 2019-09-20 | 2019-11-26 | 华北电力大学 | Steam moisture on-line monitoring system and method in a kind of pipeline based on acoustics |
| CN110501417B (en) * | 2019-09-20 | 2020-06-30 | 华北电力大学 | System and method for monitoring steam humidity in pipeline on line based on acoustics |
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| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20140507 Effective date of abandoning: 20151125 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |