CN202024808U - Recovery type wet steam two-phase flow flowmeter calibration table - Google Patents
Recovery type wet steam two-phase flow flowmeter calibration table Download PDFInfo
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- CN202024808U CN202024808U CN2011200743275U CN201120074327U CN202024808U CN 202024808 U CN202024808 U CN 202024808U CN 2011200743275 U CN2011200743275 U CN 2011200743275U CN 201120074327 U CN201120074327 U CN 201120074327U CN 202024808 U CN202024808 U CN 202024808U
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Abstract
The utility model discloses a recovery type wet steam two-phase flow flowmeter calibration table. A heat accumulating tank of a stable water supply unit is communicated with a monotube boiler through a boiler water supply pipe; and a gear pump, a water supply flowmeter and a water supply conductivity meter are sequentially arranged on the boiler water supply pipe. The monotube boiler of a steam generating unit is communicated with a cooling heat exchanger through a steam supply pipe; and a detected gauge, a meter detector and a water sample sampler are sequentially arranged on the steam supply pipe. A cooling heat exchanger of a waste heat recovery unit is communicated with the heat accumulation tank through a water feeding pipe of the heat accumulating tank. The water sample sampler is communicated with a sampling water pipe; and the sampling water pipe is connected with a water sample conductivity meter and a sampling water adjusting valve. The recovery type wet steam two-phase flow flowmeter calibration table can provide wet steam for calibration; and the mass flow and the steam dryness fraction can be adjusted by using the wet steam for calibration. A high-precision wet steam standard flow meter and a standard dryness meter are constructed on the calibration table, so that the high-precision calibration of the detected gauge can be implemented. The wet steam for calibration can be used for recovering fluid and waste heat, thus the operation cost is reduced.
Description
Technical field
What the present invention relates to is the flow measurement field, is recovery type flow meter calibration platform.
Background technology
Flowmeter is the instrument that fluid flow is measured.The performance of flowmeter mainly contains 2 points, the measuring accuracy of first flowmeter, and it two is ranges of flowmeter.Measuring error is the relative error of flowmeter institute's measurement of discharge and actual flow, reflects the measuring accuracy of flowmeter usually with maximum relative error.The range of flowmeter is in the maximum error of measuring scope that flowmeter provides, the scope of minimum flow that flowmeter is surveyed and maximum flow.Flowmeter is dispatching from the factory preceding or in development process or in reinspection, is all needing to examine and determine or demarcate by this special equipment of flow calibration platform, whether reaches the performance of its nominal to confirm flowmeter.The flow calibration platform has two principal characters, the one,, can regulate the fluid flow of flow calibration platform, its fluctuations in discharge scope can cover the range of examining flowmeter fully, the 2nd,, on the flow calibration platform normal stream scale to be arranged, normal stream scale institute measurement of discharge is represented as actual flow, therefore the normal stream scale is as the flow standard of comparison to tested flowmeter
The flow meter calibration platform of prior art all is the flow meter calibration platform of monophasic fluid, as the water meter calibrating table, and single-phase flowmeter calibrating tables such as calorimeter calibrating table, vortex shedding flow meter, electromagnetic flowmeter, ultrasonic flow meter, target type meter.Because wet steam widespread use in industry, China has 530,000 boilers now, relates to the wet steam flow meter more than 5,000,000.In order to improve development level, production level, the usage level of wet steam flow meter, just must demarcate, thereby wet steam flow meter calibrating table should be arranged the wet steam flow meter.Then, because wet steam is the biphase gas and liquid flow fluid, the fluidised form of wet steam is various, the flow pattern complexity, two phase flow of damp steam flowmeter economical and practical on the engineering is also rare, and two phase flow of damp steam flow meter calibration platform is because following five aspects, and prior art does not also have two phase flow of damp steam flow meter calibration platform.This five aspects former because: the first because wet steam is a biphase gas and liquid flow, prior art does not also have high precision wet steam flow meter as the normal stream scale of demarcating usefulness; It two is, different is with single-phase flow flow meter calibration platform, to the demarcation of wet steam flow meter, not only will demarcate its flow, also will demarcate its steam quality, and prior art also is not used in the equivalent steam mass dryness fraction table of on-line measurement steam quality; It three is, different is with single-phase flow flow meter calibration platform, produces the wet steam of demarcating usefulness, and its power consumption is too big; It four is that high-pressure and high-temperature steam has its danger in calibration process; It five is, the wet steam of demarcating usefulness is difficult to reclaim, and the expense of demarcation is very high.So the two phase flow of damp steam flow meter calibration platform that invention can be practical is to development, produce and development two phase flow of damp steam flowmeter is very crucial.
Summary of the invention
In order to remedy the situation that lacks two phase flow of damp steam flow meter calibration platform in the prior art,, the present invention proposes a kind of recovery type two phase flow of damp steam flow meter calibration platform for development, production and the use of wet steam flow meter provides technological means.
The present invention is combined by flow process to water unit, the unit that steams, demarcation unit and waste heat recovery unit successively by stable, and wherein, stable feedwater unit comprises heat storage tank, air hose, boiler feed pipe, gear-type pump, feed meter and feedwater conductivity meter; The direct current cooker of unit for no drum steams; Demarcate the unit and comprise steam supply pipe, tested table, inspection table device, water sample sampler, water sample conductivity meter, sampling water pipe and sample water variable valve; The waste heat recovery unit comprises cooling heat exchanger, cooling water inlet pipe, cooling sea water regulating valve and cooling water outlet pipe.
Be communicated with by boiler feed pipe between the water delivering orifice of heat storage tank and the water inlet of direct current cooker; Be communicated with by steam supply pipe between the water delivering orifice of direct current cooker and the cooling heat exchanger hot-fluid inlet; Be communicated with by the heat storage tank water inlet pipe between the water inlet of the outlet of the hot-fluid of cooling heat exchanger and heat storage tank;
Gear-type pump, feed meter and feedwater conductivity meter are installed on the boiler feed pipe successively; On steam supply pipe, have tested table, inspection table device and water sample sampler are installed successively and tested table adjacent with direct current cooker, water sample sampler and cooling heat exchanger are adjacent;
The cold fluid inlet of cooling heat exchanger links to each other with the endpiece of cooling water inlet pipe; The cold fluid outlet of described cooling heat exchanger links to each other with the inlet end of cooling water outlet pipe.
Covered the sky tracheae on the described heat storage tank; Water delivering orifice and water inlet are arranged on the casing of heat storage tank.
The acquisition port of water sample sampler is communicated with the inlet end of sampling water pipe; On the sampling water pipe, be connected with water sample conductivity meter and sample water variable valve.
The course of work of recovery type two phase flow of damp steam flow meter calibration platform is:
The gear-type pump of constant flow from heat storage tank draw water and by boiler feed pipe to the stable feedwater of direct current cooker; Direct current cooker produces the wet steam of demarcating usefulness, and is transported to cooling heat exchanger by steam supply pipe; Water sample sampler on the steam supply pipe a little sample water in sampling water pipe derivation steam supply pipe is measured this sampling electrical conductivity of water by the water sample conductivity meter on the sampling water pipe, and the sample water variable valve is used for regulating the flow of sample water.In the waste heat recovery unit, cooling heat exchanger is connected with cooling water outlet pipe with cooling water inlet pipe, and as the in-out end of the chilled water of heat interchanger, it also is connected with the heat storage tank water inlet pipe with steam supply pipe, as the in-out end of the hot fluid of heat interchanger.Cooling sea water regulating valve on cooling water inlet pipe, be used for regulating the waste heat recovery amount of waste heat recovery unit, cooling heat exchanger will become hot water from the wet steam of steam supply pipe, give heat storage tank via the heat storage tank water inlet pipe with the hot water loopback again, realize demarcating quality and the waste heat recovery with wet steam.Feedwater flow is counted mass flowmeter, and as the standard wet steam flow scale of tested table; The feedwater conductivity D that is surveyed by the feedwater conductivity meter
1, the demarcation of being surveyed of water sample conductivity meter is with containing water conductivity D in the wet steam
2, draw the steam quality X of wet steam that direct current cooker produces
0=(D
2-D
1)/D
1, and with X
0Equivalent steam mass dryness fraction as tested table.
The good effect that the present invention is produced technically is: the wet steam of demarcating usefulness can be provided on two phase flow of damp steam flow calibration platform, and demarcate the wet steam scalable mass rate and the steam quality of usefulness.On calibrating table, made up high-precision wet steam normal stream scale and standard mass dryness fraction table, can implement high-precision calibrating thus tested table.The wet steam of demarcating usefulness can also fluid recovery and waste heat recovery, makes this calibrating table energy-saving run.
Description of drawings
Fig. 1 is the structural representation of recovery type two phase flow of damp steam flow meter calibration platform, wherein:
1. heat storage tank 2. air hoses 3. boiler feed pipes 4. gear-type pumps 5. boiler feedwater flow meters
6. devices are shown in 9. tested table 10. inspections of feedwater conductivity meter 7. direct current cookers 8. steam supply pipes
11. water sample sampler 12. cooling water inlet pipes 13. cooling sea water regulating valves 14. cooling heat exchangers
15. cooling water outlet pipe 16. heat storage tank water inlet pipes 17. water sample conductivity meters 18. sampling water pipes
19. sample water variable valve
Embodiment
Now 1 couple of the present invention is further described in conjunction with the accompanying drawings:
Present embodiment is a recovery type two phase flow of damp steam flow meter calibration platform, is used for the flow and the mass dryness fraction of two phase flow of damp steam flowmeter are demarcated.
Present embodiment is combined by flow process to water unit, the unit that steams, demarcation unit and waste heat recovery unit successively by stable.Described stable feedwater unit comprises heat storage tank 1, air hose 2, boiler feed pipe 3, gear-type pump 4, feed meter 5 and feedwater conductivity meter 6.The described direct current cooker 7 of unit that steam for no drum.Described demarcation unit comprises steam supply pipe 8, tested table 9, inspection table device 10, water sample sampler 11, water sample conductivity meter 17, sampling water pipe 18 and sample water variable valve 19.Described waste heat recovery unit comprises cooling heat exchanger 14, cooling water inlet pipe 12, cooling sea water regulating valve 13 and cooling water outlet pipe 15.
The water delivering orifice of heat storage tank 1 is communicated with by boiler feed pipe 3 with water inlet between the direct current cooker 7.Be communicated with by steam supply pipe 8 between the water delivering orifice of direct current cooker 7 and the cooling heat exchanger 14 hot-fluids inlet.Be communicated with by heat storage tank water inlet pipe 16 between the water inlet of the outlet of the hot-fluid of cooling heat exchanger 14 and heat storage tank 1.Gear-type pump 4, feed meter 5 and feedwater conductivity meter 6 are installed on the boiler feed pipe 3 successively.On steam supply pipe 8, have tested table 9, inspection table device 10 and water sample sampler 11 are installed successively and tested table 9 adjacent with direct current cooker 7, water sample sampler 11 is adjacent with cooling heat exchanger 14.The cold fluid inlet of cooling heat exchanger 14 links to each other with the endpiece of cooling water inlet pipe 12.The cold fluid outlet of described cooling heat exchanger 14 links to each other with the inlet end of rising pipe 15.
Covered sky tracheae 2 on the heat storage tank 1; Water delivering orifice and water inlet are arranged on the casing of heat storage tank 1.
The acquisition port of water sample sampler 11 is communicated with the inlet end of sampling water pipe 18.On sampling water pipe 18, be connected with water sample conductivity meter 17 and sample water variable valve 19.
The course of work of recovery type two phase flow of damp steam flow meter calibration platform is:
The gear-type pump 4 of constant flow from heat storage tank 1 draw water and by boiler feed pipe 3 to the stable feedwater of direct current cooker 7; Direct current cooker 7 produces the wet steam of demarcating usefulness, and is transported to cooling heat exchanger 14 by steam supply pipe 8; A little sample water that water sample sampler 11 on the steam supply pipe 8 derives in the steam supply pipe 8 through sampling water pipe 18 is measured this sampling electrical conductivity of water by the water sample conductivity meter on the sampling water pipe 18 17, and sample water variable valve 19 is used for regulating the flow of sample water.In the waste heat recovery unit, cooling heat exchanger 14 is connected with cooling water outlet pipe 15 with cooling water inlet pipe 12, and as the in-out end of the chilled water of heat interchanger, it also is connected with heat storage tank water inlet pipe 16 with steam supply pipe 8, as the in-out end of the hot fluid of heat interchanger.Cooling sea water regulating valve 13 on cooling water inlet pipe 12, be used for regulating the waste heat recovery amount of waste heat recovery unit, cooling heat exchanger 14 will become hot water from the wet steam of steam supply pipe 8, give heat storage tank 1 via heat storage tank water inlet pipe 16 with the hot water loopback again, realize demarcating quality and the waste heat recovery with wet steam.Feed meter 5 is a mass flowmeter, and as the standard wet steam flow scale of tested table 9; The feedwater conductivity D that is surveyed by feedwater conductivity meter 6
1, water sample conductivity meter 17 demarcation of being surveyed is with containing water conductivity D in the wet steam
2, draw the steam quality X of direct current cooker 7 wet steam of producing
0=(D
2-D
1)/D
1, and with X
0Equivalent steam mass dryness fraction as tested table 9.
Claims (3)
1. a recovery type two phase flow of damp steam flow meter calibration platform is characterized in that,
A. described recovery type two phase flow of damp steam flow meter calibration platform is combined by flow process to water unit, the unit that steams, demarcation unit and waste heat recovery unit successively by stable, wherein, the stable unit that feeds water comprises heat storage tank (1), air hose (2), boiler feed pipe (3), gear-type pump (4), feed meter (5) and feedwater conductivity meter (6); The direct current cooker (7) of unit for no drum steams; Demarcate the unit and comprise steam supply pipe (8), tested table (9), inspection table device (10), water sample sampler (11), water sample conductivity meter (17), sampling water pipe (18) and sample water variable valve (19); The waste heat recovery unit comprises cooling heat exchanger (14), cooling water inlet pipe (12), cooling sea water regulating valve (13) and cooling water outlet pipe (15);
B. be communicated with by boiler feed pipe (3) between the water inlet of the water delivering orifice of heat storage tank (1) and direct current cooker (7); Be communicated with by steam supply pipe (8) between the water delivering orifice of direct current cooker (7) and cooling heat exchanger (14) the hot-fluid inlet; Be communicated with by heat storage tank water inlet pipe (16) between the water inlet of the outlet of the hot-fluid of cooling heat exchanger (14) and heat storage tank (1);
C., gear-type pump (4), feed meter (5) and feedwater conductivity meter (6) are installed on the boiler feed pipe (3) successively; On steam supply pipe (8), have tested table (9), inspection table device (10) and water sample sampler (11) are installed successively and tested table (9) adjacent with direct current cooker (7), water sample sampler (11) is adjacent with cooling heat exchanger (14);
D. the cold fluid of cooling heat exchanger (14) inlet links to each other with the endpiece of cooling water inlet pipe (12); The cold fluid outlet of described cooling heat exchanger (14) links to each other with the inlet end of cooling water outlet pipe (15).
2. a kind of according to claim 1 recovery type two phase flow of damp steam flow meter calibration platform is characterized in that, has covered sky tracheae (2) on the heat storage tank (1); On the casing of heat storage tank (1) water delivering orifice and water inlet are arranged.
3. a kind of according to claim 1 recovery type two phase flow of damp steam flow meter calibration platform is characterized in that, the acquisition port of water sample sampler (11) is communicated with the inlet end of sampling water pipe (18); On sampling water pipe (18), be connected with water sample conductivity meter (17) and sample water variable valve (19).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2011200743275U CN202024808U (en) | 2011-03-18 | 2011-03-18 | Recovery type wet steam two-phase flow flowmeter calibration table |
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CN2011200743275U CN202024808U (en) | 2011-03-18 | 2011-03-18 | Recovery type wet steam two-phase flow flowmeter calibration table |
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CN2011200743275U Expired - Lifetime CN202024808U (en) | 2011-03-18 | 2011-03-18 | Recovery type wet steam two-phase flow flowmeter calibration table |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102230817A (en) * | 2011-03-18 | 2011-11-02 | 西北工业大学 | Recycled two-phase flow flowmeter calibrating platform of wet steam |
CN104568082A (en) * | 2014-12-26 | 2015-04-29 | 中国石油化工股份有限公司 | Supercritical CO2 flowmeter calibration device and calibration method thereof |
-
2011
- 2011-03-18 CN CN2011200743275U patent/CN202024808U/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102230817A (en) * | 2011-03-18 | 2011-11-02 | 西北工业大学 | Recycled two-phase flow flowmeter calibrating platform of wet steam |
CN102230817B (en) * | 2011-03-18 | 2012-09-26 | 西北工业大学 | Recycled two-phase flow flowmeter calibrating platform of wet steam |
CN104568082A (en) * | 2014-12-26 | 2015-04-29 | 中国石油化工股份有限公司 | Supercritical CO2 flowmeter calibration device and calibration method thereof |
CN104568082B (en) * | 2014-12-26 | 2017-10-17 | 中国石油化工股份有限公司 | Supercritical CO2Flowmeter prover and its scaling method |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20111102 Effective date of abandoning: 20120926 |