• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A method of measuring a solid matter mass flow during conveying of solid matter-gas suspensions in tubular conduits, particularly during conveying in a dense stream with high pressure, comprises the steps of changing in a pulse mode a solid matter concentration of a solid matter-gas suspension at one location of the conduit through which the suspension flows, continuously measuring a solid matter concentration of a solid matter-gas suspension or a value corresponding thereto at two measuring locations downstream of the first-mentioned changing location and spaced from one another in the conduit, determining a difference between time points at which a difference of the solid matter concentration or the corresponding value is indicated after one another at the measuring locations downstream of the first-mentioned changing location and spaced from one another, determining a per-unit-time average value of the solid matter concentration of the solid matter-gas suspension in a conduit portion corresponding to the measuring location, generating a signal which is proportional to a quotient from the time per unit average value of the solid matter concentration divided by the difference of the time points at which the change of the solid matter concentration at the measuring locations after one another is indicated, and using this signal as a measure for the solid matter mass flow in the conduit.
    公开号:SU1702184A1
    申请号:SU827772544
    申请日:1982-07-07
    公开日:1991-12-30
    发明作者:Бейерман Норберт；Шеллер Манфред；Кретшмер Хорст；Ноак Йюрген；Блашке Клаус-Дитер；Хейнц Лотар；Гелер Петер；Швейгель Ханс-Йоахим；Дейкке Ханс-Хейнрих；Рудольф Клаус-Петер；Флаховски Йоханнес
    申请人:Бренстоффинститут Фрейберг；
    IPC主号:
    专利说明:

    The invention relates to a method for measuring a quantitative stream of solids when it is supplied in a gas stream through pipelines, in particular when transported in an aerosol stream and at elevated pressure, for example, when feeding pulverized fuels into high-pressure gasification generators.
    A known method for measuring the flow rate of a material suspended in a carrier medium, according to which in two sections of a pipeline separated by a known distance, random flow fluctuations, for example, in the form of a reduced concentration, are converted into electrical signals and the flow rate is determined by a correlation method (patent Germany No. 1798182, C. C01 F 1/74, 1977).
    The disadvantage of this method is the narrow measuring range.
    The purpose of the invention is to expand the measurement range by measuring the mixtures with a high concentration of solids.
    The essence of the method is. that in one place transporting a suspension of a solid material with a carrier gas to a pipeline, the concentration of a solid material is pulsed. in a suspension flowing past this place. At the same time, the duration of the pulse change in the concentration of a solid material is less than 1 s, preferably from 0.1 to 0.5 s, and the concentration of the solid material during this pulse decreases by 10–40% compared to its normal value. In the direction of flow from this place, at least in two measuring points located at a certain distance from each other in the pipeline, the concentration Cs of the solid material in the suspension of the solid material with gas is constantly measured by the known methods or a value that corresponds to this concentration or that is in functional communication with it, and the difference between the moments of change in the concentration of the solid material is determined in said measuring points,
    A pulsed change in the concentration of a solid material is achieved by pulsing the injection of an additional amount of gas into the pipeline. Depending on the geometrical arrangement of the injection points caused by external conditions, as well as on the properties of the transported medium, there may be a danger of blockage of the injection holes in the pipeline for a certain period of time. To prevent this danger, a relatively small gas flow can be applied at the injection point,
    which is pulsed up to a maximum value and then again reduced to its original value.
    The change in concentration indicated above is required to change.
    Solid material is achieved by appropriately metering the injected gas flow. A pulsed change in the concentration of a solid material can be achieved by a short-term
    5 throttling the flow of solid material in the pipeline. In order to achieve a constant measurement of the quantitative flow of a solid material, a pulsed change in the concentration of the solid material can be made periodically. The spacing between the pulses is 4-30 s. In this case, a repeated pulse change in the concentration of a solid material is carried out after passing the preceding pulse of both measuring points in the direction of flow.
    The drawing shows a block diagram of a device implementing the method.
    Example 1. Dust Fuel
    0 is fed through a sluice 1 to a dosing reservoir 2 under pressure of 3 MPa. In the lower part of the reserve dosing, by blowing a carrier gas, the fluid is fluidized and flows like a dense suspension of dust with carrier gas through line 3 to the burner 4 of the gasification reactor 5. the reactor, the pulverized fuel is converted by means of the gasification 6 supplied through the pipeline, free of
    0 oxygen mixture under pressure, 8 MPa. The mass flow of solid material is regulated by means of a flow of carrier gas through the control valve 7 supplied to the metering tank. The concentration of solid material entering through the pipeline 3 of the suspension of solid material with gas is within 300–500 kg of solid material per 1m of the volume of the suspension (the sum of the volumes of gas and solid material).
    Through the injection point 8 through the pipeline 9 and the throttling membrane 10 is continuously pumped, a small additional flow of carrier gas in the duct 3, which has almost no effect on the concentration of the solid material of the suspension. By briefly opening the magnetic valve 11, the additional flow of carrier gas introduced at point 8 is increased so that the concentration of the solid material of the suspension pipeline flowing during this injection at point 8 decreases noticeably. In the direction of flow from the point of injection 8, two measuring points are located at a distance of L 6 m from each other for measuring the concentration of solid material in the suspension. Measurement points operate on the principle of transmission measurement — radiation and consist respectively of a radiation source 12 or 14 and a radiation detector 13 or 15. The detectors are connected to radiation measuring devices 16 and 17, which respectively produce an analog signal (density of emissive radiation or radiation). counting rate), as well as at regular intervals and a digital signal.
    The impulsive decrease in the concentration of solid material triggered at the injection site 8 is advanced during the transportation of the suspension through conduit 3 and is first shown to the measuring point 13 of the radiation source 12 and the detector 13. This is reflected in the fact that the counting rate received by the radiation measuring device 16 increases impulsively and again drops to the normal value or to the normal limit of oscillation of the counting speed. The measuring device 16 outputs an analog signal proportional to the counting rate, which turns on the measuring device of time 13 when a predetermined level limit is exceeded the normal oscillation limit. The time measurement device stops accordingly, if the detector 15 and the radiation measuring device 17 detect the passage of a violation of solid material concentration and is transmitted to the time measurement device 18.
    Radiation signals 16 and 17, delivered by measuring instruments, at regular intervals, in this example every 0.5 s, digital signals (i.e., the number of radiation pulses received during a given period of time) are fed into microcomputer 19, which averages incoming signals at the same time. the signals from both measuring points and after that combine the local time indices determined for the just passed time, in this example 10 s, into one time average value. Taking into account the reference functions, which include, along with the geometrical arrangement of the radiation sources and the detector, also the type of the radiating source, the count rate Z0 with an empty pipe and determined separately, in particular depending on the composition and proportion of ash pulverized fuel, the mass attenuation coefficient of dust, and with the exception of the fraction of the density of the carrier gas from the result of the transmission measurement of the microcomputer 19, it also determines the average concentration of the solid material Cs according to the equation
    ten
    Fs l-a
     Si
    where the time is; Fs is the mass flow of solid material, kg / s; A is the cross-sectional area of the pipeline 3; L is the distance
    5 between the two measuring points.
    The aforementioned elimination of the fraction of the density of the carrier gas is necessary at high operating pressures, since the radiometric transmission measurement gives the initial density of suspension I, i.e. the ratio of the mass of solid material plus carrier gas and the total volume of the suspension. With additionally entered into microcomputer defined in off-line mode
    5 by the pure density of the solid material PS and the density of the carrier gas under standard conditions (/ 3;) “really, the equation g fi PN TG - () N PG TN s PS-- PNTG - (/ xONPcTN P
    0 moreover, gas status indicators PG and TG can be applied to the microcomputer selectively or (not shown) received by special sensors of measuring indicators on the pipeline. The initial state values 5 and PN and TN are given values. The mass flow FS calculated in this way is used by means of a regulating device 21 acting on the regulating valve 7 in the pipeline.
    carrier gas to control the flow of pulverized fuel supplied to the reactor 5. In addition, the mass flow is controlled by the printer 20. At the end of the measuring and computing cycle
    The microcomputer 19 causes a new injection of gas through the magnetic valve 11. With a pipe diameter of 3 to 50 mm, 15 tonnes per hour of brown coal dust are transported. The amount of carrier gas in the month® is those of injection 8 with respect to the working state (3.0 MPa, 20 ° C) 27.5 m3 / h, respectively, 770 m / h in normal conditions. Through the throttling membrane 10, a gas flow of 0.25 m3 / h is continuously supplied
    respectively, 7 m / h in normal condition for purging the injection device. By opening the magnetic valve 11, an additional 7.3 m / h (200 m / h in normal condition) is supplied in the pipeline for 0.6 s. Through this injection, the concentration is reduced.
    solid material Cs suspension of coal dust with a carrier gas from 400 kg / m3 to 328 kg / m3 suspension volume, i.e. by 1.8%. Approximately 1 second after the start of injection, the count rate is increased by 6% by the measuring instrument of radiation 16. After a further t of 1.13 s, the same increase in the counting rate on the radiation measuring instrument 17 appears. To calculate the mass flow of a solid material, the average solid concentration of both measurement points for 8 s is used. The solid mass flow is printed every 10s.
    Control tests of weighing the supplied dust showed measurement tolerances for a mass flow of dust of ± 5%.
    Comparative measurements for determining the velocity of a solid material or the transit time of a solid material using separate radioactively labeled particles as Tcaseg in a solid material stream showed relative speed with the results of an example of implementation with a tolerance of less than ± 2%. The higher the measurement error of the mass flow is the sum of the errors in determining the concentration of the solid material Cs.
    Example 2. „
    In the device described in Example 1, before the conical inlet 22 of the pipeline 3 embedded in the metering tank 2, the installation and block valve 23 is located. The locking element is axially mounted by means of a pneumatic actuator 24. The levers 25 pass tightly through the bottom of the metering tank and located at the bottom of the metering tank 2, the bottom of the inflow 26. A partial flow of carrier gas is separated after the adjusting valve 7 and 1 is fed to the adjusting and blocking valve. This partial flow enters at the beginning of the installation valve in the pipeline. Using a pneumatic actuator, the flow area of the installation valve is changed so that the free annular cross-section between the conical inlet 22 and the conical tip of the installation valve is pulsed down to 50% of the normal position.
    Thus, the concentration of solid material entering the pipeline concentration is reduced by approximately 25%. The process of measuring and processing data corresponds to Example 1. Increase
    counting rate when passing a suspension of a reduced concentration of solid material is approximately 8%.
    In contrast to example 1, there is no need for devices to inject additional gas, i.e. positions 8-11. In contrast to example 1, the short-term pulsed throttling of the input of solid material is periodically caused by a separate time sensor 27, and these periods are longer than the time required for measuring and processing data from one measuring cycle.
    权利要求:
    Claims (3)
    [1]
    1. Method of measuring mass flow
    solid material transported by the flow of a gaseous medium, which consists in reducing the concentration of solid material in the stream, measuring the flow parameters in its two sections and calculating the flow rate,
    characterized in that, in order to extend the measurement range, the decrease in concentration is carried out pulsed within 0.1-0.5 s by 10-40% of its initial value, the transit time of a reduced concentration pulse in the flow between the cross sections located on a certain distance from each other, the front concentration value of the solid material.
    [2]
    2. The way pop. 1, characterized in
    that a change in the concentration of solid material is accomplished by briefly throttling the flow of solid material.
    [3]
    3. The method according to paragraphs. 1 and 2, that is, so that a repeated decrease in the concentration is made after passing by a pulse of a reduced concentration of the second section of the measurement of the time interval.
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    同族专利:
    公开号 | 公开日
    FR2513374A1|1983-03-25|
    GB2106645A|1983-04-13|
    HU194395B|1988-01-28|
    JPH0249447B2|1990-10-30|
    GB2106645B|1985-06-26|
    JPS5866818A|1983-04-21|
    US4483199A|1984-11-20|
    FR2513374B1|1986-05-16|
    CS247119B1|1986-11-13|
    DD207122A3|1984-02-15|
    DE3223915A1|1983-04-07|
    YU209082A|1984-12-31|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2631242A|1953-03-10|Demarcation of fluids in pipe lines |
    FR1364215A|1962-06-15|1964-06-19|Kellogg M W Co|Injection system for flowable solids, for example for blast furnaces|
    DE1473191A1|1964-06-23|1970-03-05|Schallopp Dipl Phys Bernhard|Method for determining the mass flow rate of solids in a flowing conveyor|
    GB1235856A|1967-09-06|1971-06-16|Nat Res Dev|Improvements in or relating to the measurement of the flow of a particulate material|
    US3635082A|1969-04-23|1972-01-18|United States Steel Corp|Apparatus for measuring mass flow of fluidborne solids|
    US4055083A|1971-05-10|1977-10-25|Haas Rudy M|Chemical tracer method of and structure for determination of instantaneous and total mass and volume fluid flow|
    DE2554565A1|1975-12-04|1977-06-16|Otto & Co Gmbh Dr C|PLANT FOR THE PRESSURE GASIFICATION OF FINE-GRAIN FUELS|
    DE2556957A1|1975-12-18|1977-06-30|Otto & Co Gmbh Dr C|PLANT FOR GASIFICATION OF FINE GRAIN FUELS|
    DE2711114C2|1977-03-15|1983-03-10|Alb. Klein Gmbh & Co Kg, 5241 Niederfischbach|Device and method for removing bulk material from a storage space with a moving sensor protruding into the bulk material flow|
    DE2757032C2|1977-12-21|1988-01-21|Krupp Koppers Gmbh, 4300 Essen, De|
    US4228353A|1978-05-02|1980-10-14|Johnson Steven A|Multiple-phase flowmeter and materials analysis apparatus and method|
    DD142606A1|1978-06-19|1980-07-02|Alfred Hoffmann|METHOD AND MEASURING PROBE FOR PARTICLE SPEED, PARTICLE SIZE AND PARTICLE CONCENTRATION DISTRIBUTIONS|
    US4231262A|1979-03-28|1980-11-04|The Babcock & Wilcox Company|System for measuring entrained solid flow|
    US4275601A|1979-12-11|1981-06-30|Westinghouse Electric Corp.|Solids mass flow determination|
    DE3049019C2|1980-12-24|1983-01-27|Carl Schenck Ag, 6100 Darmstadt|Method for determining the mean flow rate of fluidized bulk material according to the transit time method|DE3316368C2|1983-01-21|1993-05-13|Krupp Koppers Gmbh, 4300 Essen, De|
    US4683759A|1985-12-23|1987-08-04|Texaco Inc.|Characterization of two-phase flow in pipes|
    US5022274A|1990-01-22|1991-06-11|University Of Pittsburgh|High temperature particle velocity meter and associated method|
    US5741979A|1995-11-09|1998-04-21|The United States Of America As Represented By The Administrator Of National Aeronautics And Space Adminstrator|Particle velocity measuring system|
    US6467358B1|1997-10-22|2002-10-22|Japan National Oil Corp.|Method of measuring flow rates of respective fluids constituting multiphase fluid and flow meter for multiphase flow utilizing same|
    US7385524B1|2001-09-21|2008-06-10|James Robert Orlosky|Automated meter reading, billing and payment processing system|
    FR2909766B1|2006-12-06|2009-01-09|Commissariat Energie Atomique|DEVICE FOR DETERMINING THE PROPERTIES OF A DIPHASIC FLOW, AND METHOD USING SUCH A DEVICE|
    DE102007043907A1|2007-09-14|2009-03-26|Siemens Ag|Calibration of dust mass flow measuring systems|
    CN101412929B|2008-11-28|2012-02-01|武汉凯迪工程技术研究总院有限公司|High temperature gasification technological process and system for preparing synthesis gas by using biomass|
    DE102008063505A1|2008-12-17|2010-07-01|Uhde Gmbh|Process for equalizing the production of fuels in a gasifier for the production of synthesis gas|
    FI123789B|2010-11-30|2013-10-31|Metso Automation Oy|Measurement of the solids content of a suspension|
    CN102998233B|2012-11-22|2015-04-22|中国石油大学|Method suitable for online testing of particulate matters in high-pressure gas pipeline|
    CN111239334A|2020-01-08|2020-06-05|中国辐射防护研究院|Pulse type generation system and method for radioactive inert gas tracer|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DD23347181A|DD207122A3|1981-09-22|1981-09-22|METHOD OF MEASURING THE SOLIDS MASS FLOW|
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