• 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:
    The invention can be used to control the flow of pulverized and fine-grained solid fuels (TT). The purpose of the invention is to increase the reliability of regulation at high concentrations of TTs by changing the volume of fluidization gas delivered per unit time. Fuel is supplied from a dosing reservoir (RD) through at least one transport tube to the gasification reactor, one or several burners of the heating and steam boilers by creating in the lower part of the RD a gas of a fluidized fluidized bed. In the transport tube, the density of the mixture of TT and fluidization gas is measured and kept constant, and the volume of gas is determined depending on the actual density value. In a place remote from the created fluidized bed, an adjustable flow of compensating gas is blown in, the value of which is established depending on the required quantitative flow of TT. The compensation gas flow can be set depending on the actual pressure difference between the DS and the gasification reactor or burners. 6 hp ff, 2 ill.
    公开号:SU1492184A1
    申请号:SU827772422
    申请日:1982-05-06
    公开日:1989-07-07
    发明作者:Хорст КРЕТШМЕР；Гюнтер Титце；Йюрген Ноак；Ханс-Иоахим Швейгель；Манфред ШИНГНИТЦ；Клаус ВЕРНЕР；Бернд Кирш
    申请人:Бренстоффинститут Фрейберг (Инопредприятие)；
    IPC主号:
    专利说明:

    The invention relates to methods for controlling the quantitative flows and densities of pulverized and fine-grained solid fuels, which by means of pneumatic transportation at any concentrations of solid material and system pressures are fed to gasification reactors or to burners of heating and steam heating installations.
    The method of controlling quantitative flows of a pseudo-shaped or fine-grained solid fuel is weighed by feeding the last of the metering tank through at least one transport pipe to the gasification reactor or one or several burners of the heating and steam-boiling unit, creating boiling fluidization gas in the bottom of the metering tank, measuring it in the transport the density tube of the mixture of solid fuel and fluidization gas and the change in the amount of ToiuniBa entering the transport tube ( Awning № FRG 2554565, cl. C 10 J 3/56, Publish. 1977).
    The disadvantages of this method are the low control reliability at high concentrations of solid
    The second fuel and the need to adjust the ratio of the individual transport gas partial flows depending on the type of fuel and the amount of fuel required.
    The purpose of the invention is to increase the reliability of regulation at high concentrations of solid fuels by changing the volume of fluidization gas delivered per unit time.
    FIG. Figure 1 shows a simplified block diagram of controlling the quantitative flow by means of a compensation gas; in fig. 2 is a simplified block diagram of adjusting the quantity flow by means of a compensation gas and a control gas.
    When implementing the method (Fig. 1), 30,000 kg / h of brown coal dust with a filling density of 500 kg / m and a RC of 1400 kg / m granularity should be transported from the metering tank 1, the filling level of which LjCH is kept constant with by the power of the cell feeder 11, through the transport pipe 8 to the place of consumption 5 (gasification reactor) and must be adjustable between 30 and 100%; traffic density should be pg 300 kg / m. Nitrogen of normal density is used as the fluidizing gas 2 and the compensating gas 3. P (jj ") 1.25 kg / m and the condition parameters in the metering tank 1 are 0 MPa and K. The measuring points are directly at the outlet of the metering tank 1. It has been established that the control reliability is increased if the density D is maintained constant, the fluidization gas flow Vg being determined by the equation
    ij
    bulk density
    material;
    granularity of solid material;
    fluidization gas density in working and normal condition;
    Ci.
    V g- (h Fluid gas flow h 11 ”)
    in working and normal condition;
    t is the quantitative flow of solid material.
    Using equations (1), (1.1), (1.2) on a computer to control the process 4, the amount of fluidized gas is determined according to the range of adjustment of the quantitative flow Vq / 383-1 277 under normal conditions and is entered as switch parameter 13 choice of options in the control valve 12.
    To compensate for the filling that creeps into the fluidized bed and to maintain the stationary transport state at a distance away from the created fluidized bed, the so-called compensation gas V (j, which is determined by the equation
    V h ps
    (2)
    related to the normal state, the compensating gas flow is equal to

    rt
    V v .--. La Kq (Mi c. P
    (2.1)
    According to equations (2), (2.1), the flow rate of the required capacity for the control valve 9 of the compensating gas is (. 487–1624 m / h under normal conditions. The compensation gas is introduced into the dosing tank from above. Adjustment of the compensation gas 3 is performed by of the quantitative flow torus 6, which compares the measured value for the quantitative flow of solid material m at the measuring point ElC (m) with the specified value i „pp, adjusts the adjustments depending on the difference of these values Compensatory gas valve.
    I
    FIG. 1 as an alternative
    The possibility of directly measuring the density P in the transport tube using the measuring point QIC, comparing the measured value p with a given value p (dpm) and forming the corresponding difference between
    Pf P (OUT of the driver parameter using the regulator 7 and its connection to the control valve 12
    five
    through the switch 13 of the choice of options.
    When implementing the method (FIG. 2), 800 kg / h of a lignite dump with a transport tube with an inner diameter of 14 mm from the metering tank 1 to the place of consumption (heating installation) should be transported with air l j- (1, 293 at an overpressure 0, 2 Mlla and a temperature of 293 K. The bulk density of the brownish ribuiH is kg / m, the grit p is 1400 kg / m. The density after the 1 Pf mixer, taking into account a slight transverse section of the transport pipe, should be 260 kg / Based on the density measurement using a measuring device - QIC (p,) to q a quantity of
    gas 2 is fluidized by means of a regulator 7 and an adjusting valve 12, that the density p at the measuring point (DC (p,) has a constant value of 400 kg / m). Through the PdC measuring points, the pressure difference between the metering mirror 1 and the adjusting the compensating gas valve 9 establishes such a compensating gas flow 3 that this pressure difference corresponds to a predetermined value. The control gas flow is directed through the mixer 14 to the transport pipe B. The control gas flow is measured with a meter The FIC (V) point of a point. By calculating the H,
    A control machine 16, based on the flow rate of the control gas Vg of density px and measured using the measuring point QIC (P) in the direction of flow after the mixer 14 of the flow density P, the quantitative flow m 1 is calculated and compared with its given value ni p, and a pulse is generated from the deviation to regulate the flow of control gas d using the control gas control valve 15. Transport speeds are 14, 3.6 m / s in front of the mixer and 5.8 m / s behind it. By increasing the flow of control gas to the mixer 14, it is possible to reduce the quantitative flow m, and lower it to increase. The fill level in the metering tank 1 must be maintained at
    15
    20
    25
    92
    Q
    0
    thirty
    35
    five
    0
    five
    1846
    by adjusting the filling level of the LCH and the cell feeder 11. The magnitude of the pressure difference PdC is obtained from the maximum quantitative flow and the length of the transport tube.
    权利要求:
    Claims (7)
    [1]
    1. Regulation method: preparing quantitative streams of pulverized or fine-grained solid fuel by feeding the last of the metering tanks through at least one transport pipe to the gasification reactor or one or several burners of the heating and steam boilers by creating boiling fluidization gas in the lower part of the metering tank, measuring in the transport density pipe (. mixture of solid fuel and fluidization gas and changes in the amount of fuel entering the transport pipe, In order to increase reliability, regulation at high concentrations of solid fuel by changing the volume of fluidized gas per unit time, VV, the density P | of the mixture of solid fuel and fluidization gas entering the transport tube is kept constant at a distance of The created boiling bed of the dosing reservoir is blown in an adjustable flow of compensating gas V.
    [2]
    2. The method according to claim 1, about tl and h and u-
    u and with the fact that the density Of is kept constant by a change in the volume of the fluidized gas VQ by the equation
    V ()
    p. (p5-pj q f, -pj
    where p - granular solid fuel;
    RZ bulk density of solid fuels;
    PQ is the density of the gas phase in the metering tank at the temperature and pressure present there.
    [3]
    3. The method according to p. 1, o. T; i and h and y and the fact that the density 0 is taken as a given value and depending on the Cp-n. The mismatch between the set and measured actual density values establish the volume of the fluidization gas V.
    [4]
    4. The method according to paragraphs. 1–3, which is based on the fact that the compensation gas flow V kg, depending on the required quantity of solid fuel transported from the metering tank, is set by the equation
    Is
    V
    Kq
    de od - bulk density
    fuel.
    [5]
    5. The method according to paragraphs. 1–3, the fact that the quantitative flux m is additionally measured in the transport tube, the measured value is compared with the value specified for the quantitative flux, m P, and depending on the error signal between the specified and measured values gas vtc
    [6]
    6. Method according to paragraphs. 1-5, characterized in that the differential pressure of the PdC between the metering tank and the gasification reactor or the burners is additionally measured, the measured actual value is compared with the target and depending on the error signal between the setpoint and the measured value of the compensation gas VKQ.
    [7]
    7. A method according to claim 6, characterized in that at least one adjustable flow of control gas V.5G is blown into at least one transport pipe i; through a mixer placed in the pipe, depending on the required value of the quantitative flow m,;
    in the transport tube i, with the flow of control gas. reduced to increase the quantity flow until the latter reaches the desired value.
    1 L - - - - -
    III
    I I L-l --- pl
     eleven
    1 i
    one
    mfflsoit)
    3-®,
    eight
    at
    i
    f
    Jftfco y
    Tf
    I D
    - (fie
    VG (N
    ) SOLIJ
    : L:
    flLZ. 2
    L1
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    同族专利:
    公开号 | 公开日
    CS254104B1|1988-01-15|
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    YU151282A|1988-04-30|
    FR2509702A1|1983-01-21|
    HU193520B|1987-10-28|
    JPS5824819A|1983-02-14|
    GB2103387B|1985-10-23|
    DE3211045A1|1983-02-03|
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    FR2509702B1|1985-08-23|
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    DD147188A3|1977-09-19|1981-03-25|Lutz Barchmann|METHOD AND DEVICE FOR PRESSURE GASIFICATION OF DUST-SOUND FUELS|
    FR2415592A1|1978-01-26|1979-08-24|Fives Cail Babcock|Pneumatic elevator for powdery materials - with fluidised material fed to pressurised chamber in which nozzle discharges air to bottom of vertical pipe|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DD81231889A|DD206309A3|1981-07-17|1981-07-17|METHOD FOR REGULATING MASS STRUCTURES|
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