Patent Application
20140090583
This application claims priority of German Patent Office application No. 102012217890.2 DE filed Oct. 1, 2012. All of the applications are incorporated by reference herein in their entirety.
The invention relates to a system for fluidizing and conveying a powdery product, in particular pulverized fuel, overcoming conveying distances of 80 to 500 m, at an operating pressure of up to 10 MPa, to a receiver, in particular an entrained-flow gasifying device.
The invention also relates to a method for continuously feeding pulverized fuel into an entrained-flow gasifying plant at pressures of up to 10 MPa for producing a CO- and H2-rich crude gas which can be processed to form various synthesis gases, high-energy gases and hydrogen.
The pulverized fuel is supplied to the gasifying system, which is under a pressure of up to 10 MPa, either by pump conveying of a pulverized fuel/water slurry, a pulverized fuel/oil slurry or a pulverized fuel/carrier gas suspension at conveying densities of 250-450 kg/m3 in the continuous-conveying sphere. An extensive description of this technology is contained in patent DD 147188 A3. According thereto, the pulverized fuel produced in a grinding and drying plant is supplied by conventional thin-flow conveying to an operating bunker and the conveying gas is separated off via a filter. To increase the pressure, the pulverized fuel passes via gravitational conveying into pressure locks, in which the powder is brought to the desired process pressure by tensioning with an inert gas having less than 5% oxygen. Nitrogen, carbon dioxide or exhaust gases from the combustion can be used as inert gases. Depending on the output, the pressure locks may be in single or multiple form. The pulverized fuel passes out of the pressure locks, again by gravitational conveying, into a metering vessel, in the lower part of which there is a device for producing a dense fluidized bed, into which one or more conveying lines for transporting the pulverized fuel to the burner of the gasifying reactor are submerged. By setting and optionally controlling a specified pressure differential between the metering vessel and the gasifying reactor, the desired amount of pulverized fuel can be supplied. Together with the amount of oxygen which is matched to the amount of pulverized fuel, the conversion in the gasifying reactor takes place at temperatures such that the fuel ash is melted to form liquid slag. This arrangement conceals a plurality of disadvantages. The amount of fuel to be supplied in the thin flow from a grinding and drying plant over a relatively large distance to the operating bunker of the gasifying plant requires a very large amount of conveying gas which has to be provided continuously. The arrangement of an operating bunker containing several thousand tons of pulverized fuel and of the locks and the metering vessel in the region of the hot gasifying reactor may result, in the event of leakages or of damage, to severe fires which may lead to destruction of the entire plant. In order to avoid these disadvantages, it was proposed in laid-open specifications DE 102008052673 and in DE 102009035408 to arrange the bunker and lock system in the region of the grinding and drying plant and to site only a metering vessel in the region of the hot gasifying reactor. In order to overcome the relatively long transport route, use should also be made here of dense-flow conveying. A disadvantage in this case is the serial arrangement of two metering vessels. The coal ground up to form pulverized fuel is supplied to an operating bunker via a filter, as customary, and is placed under process pressure in one or more locks. By means of gravitational conveying, the pulverized fuel enters a first metering vessel, from which it is supplied in the dense flow to a second metering vessel which is located in the direct vicinity of the gasifying reactor. The pulverized fuel is separated therein from the conveying gas, thereby building up a pile. The lower part again contains a device which permits feeding of one or more powder-conveying lines which supply the pulverized fuel in the dense flow to a central gasifying burner or to a plurality of gasifying burners of the gasifying reactor. The saving on conveying gas by using dense flow technology and the local separation of powder-conducting large containers from the hot-running gasifying reactor are advantageous in this case; the design of the metering system in multiple form is disadvantageous. Furthermore, there is the risk that, in the case of a relatively large distance between the two metering systems, the transport speed of the gas/powder suspension becomes so high, because of the pressure loss and associated expansion of the conveying gas, that wear may occur in the conveying lines. The risk increases the lower the pressure level is.
The invention is based on the object of, in the case of an entrained-flow gasifying plant with pneumatic supply of pulverizing fuel, supplying said pulverized fuel directly by a metering vessel, which is connected to the grinding and drying plant for producing the pulverized fuel, to the burners of the gasifying reactor, even over relatively long transport routes, without further intermediate stages by means of continuously conveying at high densities of between 250 to 450 kg/m3.
The object is achieved by a system with the features of the independent claim(s).
Within the scope of the invention, the pulverized fuel which comes from the grinding and drying plant is separated from the drying and circulating gas in a filter and is passed to a metering vessel in which the pressurization and the metering into the transport line to the entrained-flow gasifying plant are combined. For this purpose, there are at least two or more pressure locks 5 which are each fed discontinuously from said filter 4 by gravitational conveying and begin the conveying following pressurization. According to the prior art, for this purpose the lower part has fluidizing plates via which, by supply of fluidizing gas, a fluidized bed, in which the powder-conveying line 6 starts, is built up. The powder-locking and metering vessels 5 are operated alternately in respect of the charging with operating pressure. In this case, at least one metering vessel is always filled and is subsequently tensioned, and a further metering vessel is kept under the operating pressure of, for example, 4.7 MPa and the pulverized fuel is fluidized in the fluidizing shaft. The pulverized fuel, in particular pulverized coal, is continuously conveyed from said locking and metering vessel into the gasifying reactor. The amount is controlled here by a control valve 11 arranged at the outlet of the metering vessel. The powder-conveying lines of a plurality of locking and metering vessels are combined downstream of the control valves to form a common conveying line 14, but can also be divided further in long conveying distances into a plurality of divided conveying lines (14a, 14b, 14c). In order to ensure continuous operation, a switch is made to a second vessel before the emptying of the locking and metering vessel which is in operation. This takes place after the filling and tensioning operation thereof is finished. The desired value 9, 21 for the mass flow control of the coal is subsequently divided between the control valve of the first and second metering vessels, wherein the desired value is displaced from the first valve to the second valve via what is referred to as a portion divider. The desired value is displaced here via a ramp, the time (t1) of which can be set, as illustrated in
The ramp exit is multiplied by the desired value of the mass flow for the second valve and, for the first valve, the ramp exit is subtracted from 1 and then multiplied by the desired value of the mass flow. In this manner, consistent conveying into the gasifying reactor during the switching-over/changing-over can be ensured. In parallel to the activation of the control devices (11) for the pulverized fuel, which are arranged below the locking and metering vessel, the supply of fluidizing gas (17) into the lower part of the fluidizing plates is started. This ideally takes place temporally before the beginning of the conveying of the coal, in order to achieve a stable fluidized bed.
No limitation of the conveying of the coal is required because of the conversion/changing-over of the desired value and the individual control of each locking and metering vessel. The possible flow rates of 2 to 8 m/s for the dense-flow conveying are maintained throughout the entire course of the powder-conveying line.
By means of the alternate switching-on of a plurality of said locking and metering vessels, a continuous supply of the pulverized fuel to the gasifying reactor can be ensured despite the discontinuity in the operation of the pressure vessels.
The invention results in a considerable reduction in outlay and, by means of the possibility of siting the locking and metering vessels at a far distance from the gasifying reactor, in an increase in the safety in the surroundings of the hot gasifying reactor.
Advantageous developments of the invention are specified in the dependent claims.
The invention is explained in more detail below as an exemplary embodiment to an extent required for understanding and with reference to figures, in which:
In the figures, the same designations denote identical elements.
A gasifying plant according to
During the desired supply of powder, a pressure loss between the vessel 5 and the entrained-flow gasifying reactor 7 of 0.7 MPa arises at an overall plant pressure of 4.7 MPa. This corresponds to approximately 15% of the overall pressure. This value can be up to 20%.
In order to ensure continuous operation, before the complete emptying of the locking and metering vessel 5 which is in operation, the switch is made to a second locking and metering vessel 5 without the continuity of the powder flow in line 14 being disturbed. This takes place after the filling and tensioning operation of the second locking and metering vessel 5 is finished. The desired value for the mass flow control of the coal of 82 Mg/h is subsequently divided between the control valves 11 of the first and second locking and metering vessels 5, wherein the portion divider 18 conducts the desired value from the first valve to the second valve. The desired value here is displaced by a ramp, the time t1 of which can be set. The ramp exit is multiplied by the desired value of the mass flow for the second control valve 11 and, for the first control valve 11, the ramp exit is subtracted from 1 and multiplied by the desired value of the mass flow. In this manner, constant conveying into the gasifying reactor 7 during the readjustment to the other locking and metering vessel 5 can be ensured. A further influencing of the powder flow control, in particular also fine control, can be undertaken by the control valves 17 located in the fluidizing gas line 16 or by the supply of additional gas 8 into the auxiliary gas feed 13 of the powder-conveying line 14.
A gasifying plant according to
A quantity-measuring means and controller for the entire powder flow 21 can be arranged in the powder-conveying line 14 common to the powder-locking and metering vessels 5. In accordance with the mass flow determined in the quantity-measuring means and controller for the entire powder flow 21, the quantity of fluidizing gas flowing into the powder-locking and metering vessels 5 in total is controllable via a control valve for the entire amount of fluidizing gas 22 in the fluidizing gas line 16 with the effect of a master control means.
An entrained-flow gasifying plant with an output of likewise 500 MW is supplied with 82 Mg/h of pulverized fuel over a distance of 500 m, said pulverized fuel being placed under pressure in three combined powder-locking and metering vessels 5 and being fed into the powder-conveying lines 14. The diameters of the conveying lines are 0.06 m. In order to limit the pressure loss in the powder-conveying lines and the flow rate of the gas and pulverized fuel suspension the cross sections of said lines are doubled after a conveying distance of 250 m such that the diameters thereof are increased to 0.085 m.
The invention is also provided by a system for the pneumatic feeding-in of pulverized fuel according to the continuous-conveying principle in an entrained-flow gasifying reactor 7, in particular overcoming conveying distances of 80 to 500 m, in which a H2- and CO-rich crude gas is produced by conversion of gasifying means with oxygen or containing free oxygen at pressures of between 1 and 10 MPa and temperatures between 1300 and 1600° C., wherein
| Number | Date | Country | Kind |
|---|---|---|---|
| 102012217890.2 | Oct 2012 | DE | national |
