Slag removal system for a solid fuels gasification reactor

Description

[0001] This invention concerns the gasification of solid carbonaceous materials such as coke, coal, or lignite. More particularly, this invention concerns discharging slag and/or heavy ash from a solid fuels gasification reactor.

[0002] As presently well-known in the art, solid fuels such as coke, coal or lignite can be ground to a fine particulate size and mixed with oil or water to form the feed stream for a gasification reactor which is designed to make a useful synthetic gas product. When this type of process is carried out, a large quantity of molten slag that requires disposal is formed in the reactor. Typically, the waste slag or heavy ash generated in a solid fuels gasification process consists of solidified inorganic matter and a small amount of unreacted carbon. Generally, this slag is discharged from the bottom of the reactor an an elevated temperature and pressure in the form of a water slurry. The slurry being discharged may be at a temperature as high as between 150 and 350°F (65 and 177°C) and at a pressure as high as between 100 and 500 pounds per square inch (690 to 3450 kPa). Prior art apparatus and methods generally include crushing the slag to reduce the size of the slag particles, using lockhoppers to reduce the pressure, and flashing the water from the slag in order to further lower the temperature and pressure of the slurry being discharged.

[0003] US Patent 4472171 discloses a high pressure gasifier for powdered coal, with a discharge device for the resulting slurry, comprising a floating piston which is moveable in a cylindrical chamber, and wherein the pressure of the slurry to be discharged is applied alternately to the two sides of the piston.

[0004] In general, the present invention provides an improved apparatus and process for the continuous, uninterrupted removal of a slag/water slurry from a pressurized solid fuels gasification reactor, the apparatus comprising: at least one pressurized crusher for reducing the particle size of the slag solids, said crusher being connected to the slag discharge end of the reactor and characterized in that the apparatus comprises a depressurizing system which includes a conduit through which the slag/water slurry continuously flows, said conduit being connected to the discharge end of the crusher, and at least one restriction element to restrict the continuous kinetic fluid flow of the slag/water slurry through the conduit, said restriction element being disposed within the conduit and having an opening, the diameter of which is less than that of the conduit, said element causing a reduction in the pressure of the slurry at the discharge end of the depressurizing system to a level substantially below the pressure of the reactor.

[0005] The final discharge pressure of the slurry may be essentially atmospheric or either higher or lower than atmospheric if the slurry is transferred to other apparatus. The present apparatus may also include additional crushers and flow restriction elements in a series configuration to further reduce the particle size of the slag and pressure drop from the reactor. The flow restriction elements provide a restriction to the fluid flow of the slurry in the passageway transporting the slurry from the reactor, thereby causing a pressure drop accross the element under continuous kinetic fluid flow conditions.

[0006] The present process for discharging a slag/water slurry from a coal gasification reactor includes: first comminuting or crushing the slag solids in the slurry discharged from the reactor to reduce the particle size thereof, said slurry being discharged from the reactor at a pressure substantially equal to the reactor pressure; and passing the slurry through a depressurizing system which includes a conduit through which the slurry flows continuously and at least one restriction element to restrict the continuous kinetic fluid flow of the slurry and thereby reduce the pressure of the slurry at the discharge end of the depressuring system to a level substantially below that of the pressure of the reactor said restriction element being disposed within the conduit and having an opening the diameter of which is less than that of the conduit. The process may also include additional steps of comminuting or crushing the solids in the slurry, and restricting the fluid flow of the slurry, to further reduce the size of the slag and lower the exit pressure of the slurry from the depressurizing system. The present method further provides for injecting and mixing water with the slurry at a controlled rate of flow after the slag solids have been comminuted, thereby cooling the slurry and providing for variable flow and pressure control of the slurry through the depressurizing system of the reactor.

[0007] The present system provides for the continuous flow removal of slag from a pressurized gasification reactor with a reduced risk of plugging as compared to intermittent removal provided by the known lockhopper systems. These and other aspects of the present invention will be apparent to those skilled in the art from the more detailed description which follows.

[0008] The advantages of the present invention are even more apparent when taken in conjunction with the accompanying drawings in which like characters of reference designate corresponding material and parts throughout the several views thereof, in which:

Figure 1 is a schematic representation illustrating a slag removal system in a solid fuels gasification process constructed according to the principles of the present inventon;

Figure 2 is a cross-sectional view of a specific restriction element of the depressurizing system made according to the present invention;

Figure 3 is a cross-sectional veiw of another restriction element of the depressurizing system made according to the present invention; and

Figure 4 is a cross-sectional view of still another restriction element of the depressurizing system made according to the present invention.

[0009] The following description illustrates the manner in which the principles of the present invention are applied, but such description is not to be construed as limiting the scope of the invention.

[0010] More specifically, a slag removal apparatus 10 is illustrated by Figure 1 for communuting, cooling, and depressurizing the slag/water slurry from the bottom of a coal-gasification reactor 1. The waste discharge from reactor 1 comprises a solid residue which can be characterized as either a solidified inorganic residue or heavy ash. The slag discharge is combined with water in reactor 1 to form a slurry. The reactor 1 is operated under conditions of temperature, pressure, and concentrations generally well-known and practiced in the art for converting coke, lignite, or coal into gaseous fuel. The temperature at the discharge end of the reactor 1 is between 150 and 350°F (65 and 177°C) and the pressure is between 100 and 500 pounds per square inch (690 and 3450 kPa). Preferably, the reactor 1 is operated continuously; and the comminution, cooling, and depressurization of the reactor slag/water slurry are carried out as a continuous process.

[0011] The slag/water slurry is discharged from the reactor 1 through a first conduit 2 to a primary crusher 3. The crusher 3 is provided with a housing capable of withstanding the full pressure at the discharge end of the reactor 1. The conduit 2 and crusher 3 are connected together by flanges 4.

[0012] The partially comminuted slag from the primary crusher 3 is discharged to a secondary crusher 3a, where the slag is further comminuted. The crusher 3a is also provided with a housing which, like the housing for the primary crusher 3, is capable of withstanding the full operating pressure at the discharge end of the reactor 1. Crushers 3 and 3a are connected together by flanges 4a.

[0013] The comminuted slag is then discharged as a slurry from the secondary crusher 3a to a second conduit 5. The conduit 5 is connected to the crusher 3a by flanges 4b and 4c. Flow through the conduit 5 may be controlled by a first valve 5a. Downstream of the valve 5a, water is introduced into conduit 5 from conduit 6 through valve 6a. The slag/water slurry then passes through a series of restriction elements 7 in the conduit 5. Valves 5a and 6a regulate and control the flow rate of the water and of the slag/water slurry. As the stream continuously flows through conduit 5, there is a drop in pressure caused by the resistance to flow imposed by each restriction element 7. The slurry stream may then be discharged from the last restriction element 7 at substantially atmospheric pressure.

[0014] The addition of water through conduit 6 and the provision of the restriction elements 7 in conduit 5 beneficially eliminate the necessity for flashing the water from the slurry to reduce the temperature and pressure of the slurry stream after it exits from the depressurizing system. Moreover, the use of the valve 6a to control the flow rate of the water added to the slag stream overcomes the need for providing a downstream valve in conduit 5 to control the slurry flow rate. Since the rate of mechanical wear in such a valve would be much higher due to the abrasive characteristics of the slurry as compared to the wear caused only by water, this method of injecting water into the slurry to provide flow control is highly beneficial, economical, and advantageous. The introduction of water into conduit 5 also provides both a positive safety and most beneficial means of preventing plugging of conduit 5 with the slag.

[0015] A preferered restriction element 20 of a modified design which has been successfully useed in conduit 5 is shown in Figure 2. As shown in Figure 2, element 20 is similar to the reduced diameter pipe element 7 shown in Figure 1, in that element 20 includes a wear-resistant plate 8 through which a reduced diameter orifice 8a is provided for restricting the flow of the slag/water slurry. The plate is held in position by flanges 4d in conduit 5. The plate 8 may also be formed as a laminated structure in which the up-stream layer is a highly abrasion-resistant material such as silicon carbide, tungsten carbide, alumina, or wear-resistant metal or ceramic material. Although not shown, an abrasion-resistant liner for conduit 5 may also be provided if the conduit is not directly formed of an abrasion-resistant material.

[0016] Two additional restriction elements 30 and 40 which have been successfully used in conduit 5 are shown in Figures 3 and 4. Figure 3 illustrates a restriction element 30 which includes a frustra-conical support 9 which is held in place by flanges 4e in conduit 5, and which in turn holds a wear-resistant cone-shaped liner 9a with an orifice 9b in place to receive the slag/water slurry. Conduit 5 on both sides of element 30 also has a wear-resistant liner insert 11. Figure 4 illustrates still another useful restriction element 40 which includes a restriction plug 12 with an orifice 12a held in place by a wear-resistant liner insert 13 in conduit 5. The restriction element 40 is further held in place by an obstruction, not shown, in a down-stream flange of conduit 5. Plug 12 is beneficially molded in one piece from a hard abrasion-resistant ceramic material such as alumina.

[0017] The restricted opening or orifices of all the above restriction elements may be formed with any desired cross-sectional shape. For example, an orifice having a round, oval, square, triangular or rectangular shape may be used successfully in conduit 5. The most beneficial shape is a round cross-section with the orifice having a relative diameter of ten to thirty percent of the diameter of the conduit in which it is disposed. The size of orifices of different shapes should be selected to provide about the same relative orifice to conduit size ratio. The materials of construction for the slag removal apparatus 10 may be selected from known materials that will stand up under the temperatures and pressures previously noted, with the preferred material being carbon steel. Also in areas where severe mechanical wear is expected from the slag/water slurry, the high wear-resistant materials noted above should be used.

[0018] The primary and secondary crushers 3 and 3a are beneficially rotary crushers which include rotor plates and breaker plates, not shown. Such crushers are well-known in the art. Preferably, the slag is comminuted in the primary crusher 3 to a maximum dimension of about two and one-half inches (63.5 mm), and in the secondary crusher 3a to a dimension of between one-eight of an inch and one inch (3.2 and 25 mm).

[0019] The present combination of slag crushers, restriction elements and means for introducting water at or down-stream from the crushers provides a continuous, reliable, controllable apparatus for removal of slag from a solid fuels gasification reactor which has a far less tendency to be plugged by slag than other known slag removal systems.

[0020] While certain representative embodiments and details have been shown for the purpose of illustrating the present invention, it will be apparent to those skilled in the art that various changes and modifications can be made therein without departing from the scope of the invention as defined in the appended claims.

Claims

1. An apparatus for the continuous, removal of a slag/water slurry from a pressurized solid fuels gasification reactor, the apparatus comprising: at least one pressurized crusher for reducing the particle size of the slag solids, the crusher being connected to the slag discharge end of the reactor, and characterized in that the apparatus comprises a depressurizing system which includes a conduit through which the slag/water slurry continuously flows, conduit being connected to the discharge end of the crusher, and at least one restriction element to restrict the continuous kinetic fluid flow of the slag/water slurry through the conduit, said restriction element being disposed in the conduit and having an opening, the diameter of which is less than that of the conduit, said element causing a reduction in the pressure of the slurry at the discharge end of the depressurizing system to a level substantially below the pressure of the reactor.

2. The apparatus of Claim 1 wherein two pressurized crushers are present, comprising
   a primary crusher for reducing the particle size of the slag solids, connected to the slag discharge end of the reactor,
   a secondary crusher for further reducing the particle size of the slag solids, said secondary crusher being connected to the discharge end of the primary crusher,
   a depressurizing system which includes a conduit through which the slag/water slurry continuously flows, said conduit being connected to the discharge end of the secondary crusher, and
   a restriction element as defined in Claim 1.

3. The apparatus of Claim 1 or 2, including means for injecting and mixing water with the slurry after the particle size of slag solids has been reduced by the crusher.

4. The apparatus of Claim 3, wherein the means for injecting water into the slurry stream include a valve for controlling the flow rate of the water, thereby cooling the slag/water slurry and providing for variable flow and pressure control thereof through the depressurizing system.

5. The apparatus of any one of Claims 1 to 4, wherein the restriction element includes a restriction plug with a orifice, said plug being held in place by a liner insert in the conduit.

6. The apparatus of Claim 5, wherein the orifice has a diameter of from 10 to 30 percent of the diameter of the conduit in which the restriction element is disposed.

7. A process for the continuous, removal of a slag/water slurry from a pressurized solid fuels gasification reactor, which process comprises the steps of:

(a) comminuting the slag solids in the slurry discharged from the reactor to reduce the particle size thereof, said slurry being discharged from the reactor at a pressure substantially equal to the reactor pressure; and

(b) passing the slurry through a depressurizing system which inlcudes a conduit through which the slurry flows continuously and at least one restriction element to restrict the continuous kinetic fluid flow of the slurry and thereby reduce the pressure of the slurry at the discharge end of the depressurizing system to a level substantially below the pressure of the reactor, said restriction element being disposed within the conduit and having an opening the diameter of which is less than that of the conduit.

8. The process of Claim 7, further comprising injecting and mixing water with the slurry after the particle size of the slag solids has been reduced by comminution in order to cool the slurry and provide for variable flow and pressure control thereof through the depressurizing system.

Ansprüche

1. Vorrichtung zur kontinuierlichen Entfernung einer Schlacken/Wasser Aufschlämmung aus einem unter Druck stehenden Festbrennstoff-Vergasungsreaktor, die Vorrichtung umfassend:
wenigstens eine unter Druck stehende Zerkleinerungsmaschine zur Reduzierung der Teilchengröße der Schlacken-Feststoffe, wobei die Zerkleinerungsmaschine mit dem Schlackenentleerungsende des Reaktors verbunden ist, und dadurch gekennzeichnet, daß die Vorrichtung ein Dekomprimierungssystem umfasst, das eine Leitung einschließt, durch die die Schlacken/Wasser Aufschlämmung kontinuierlich strömt, wobei die Leitung mit dem Entleerungsende der Zerkleinerungsmaschine verbunden ist und wenigstens ein Beschränkungselement, um den kontinuierlichen, sich bewegenden Flüssigkeitsstrom der Schlacken/Wasser Aufschlämmung durch die Leitung zu beschränken, wobei das Beschränkungselement in der Leitung angeordnet ist, und eine Öffnung besitzt, deren Durchmesser kleiner ist als der der Leitung, wobei das Element eine Verringerung des Drucks der Aufschlämmung bei dem Entleerungsende des Dekomprimierungssystems auf einen Wert, der im wesentlichen unter dem Druck des Reaktors liegt, verursacht.

2. Vorrichtung nach Anspruch 1, worin zwei unter Druck stehende Zerkleinerungsmaschinen vorhanden sind, umfassend
   eine erste Zerkleinerungsmaschine zur Reduzierung der Teilchengröße der Schlackenfeststoffe, die mit dem Schlackenentleerungsende des Reaktors verbunden ist,
   eine zweite Zerkleinerungsmaschine zur weiteren Reduzierung der Teilchengröße der Schlackenfeststoffe, wobei die zweite Zerkleinerungsmaschine mit dem Entleerungsende der ersten Zerkleinerungsmaschine verbunden ist,
   ein Dekomprimierungssystem, das eine Leitung einschließt, durch welche die Schlacken/Wasser Aufschlämmung kontinuierlich strömt, wobei die Leitung mit dem Entleerungsende der zweiten Zerkleinerungsmaschine verbunden ist,
   und ein Beschränkungselement, wie in Anspruch 1 definiert.

3. Vorrichtung nach Anspruch 1 oder 2, einschließend Mittel zur Einführung von Wasser und Mischen desselben mit der Aufschlämmung nachdem die Teilchengröße der Schlackenfeststoffe durch die Zerkleinerungsmaschine reduziert wurde.

4. Vorrichtung nach Anspruch 3, worin das Mittel zur Einführung von Wasser in den Aufschlämmungsstrom ein Ventil einschließt, um die Flußrate des Wassers zu kontrollieren, und dabei die Schlacken/Wasser Aufschlämmung zu kühlen, und für eine Kontrolle des variablen Stroms und Drcuckes durch das Dekomprimierungssystem sorgen.

5. Vorrichtung nach einem der Ansprüche 1-4, worin das Beschränkungselement einen Beschränkungs-Stöpsel mit einer Öffnung einschließt, wobei der Stöpsel durch eine Belagseinlage an dem Platz in der Leitung gehalten wird.

6. Vorrichtung von Anspruch 5, worin die Öffnung einen Durchmesser von 10-30% des Durchmessers der Leitung, in der das Beschränkungselement angeordnet ist, besitzt.

7. Verfahren zur kontinuierlichen Entfernung einer Schlacken/ Wasser Aufschlämmung aus einem unter Druck stehenden Festbrennstoff-Vergasungsreaktor, das Verfahren die Schritte umfassend:

(a) die Schlackenfeststoffe, in der aus dem Reaktor entleerten Aufschlämmung zu zerkleinern um deren Teilchengröße zu reduzieren, wobei die Aufschlämmung aus dem Reaktor bei einem Druck entleert wird, der im wesentlichen gleich dem des Reaktors ist, und

(b) die Aufschlämmung durch ein Dekomprimierungssystem, das eine Leitung einschließt, durch welche die Aufschlämmung kontinuierlich strömt, und wenigstens ein Beschränkungselement zu leiten, um den kontinuierlichen, sich bewegenden Flüssigkeitsstrom der Aufschlämmung zu beschränken und dabei den Druck der Aufschlämmung bei dem Auslaßende des Dekomprimierungssystems auf einen Wert, der im wesentlichen unter dem Druck des Reaktors liegt zu reduzieren, wobei das Beschränkungselement in der Leitung angeordnet ist und eine Öffnung besitzt, deren Durchmesser kleiner ist als der Durchmesser der Leitung.

8. Verfahren nach Anspruch 7, weiter umfassend Wasser einzuführen und mit der Aufschlämmung zu vermischen, nachdem die Teilchengröße der Schlackenfeststoffe durch Zerkleinerung reduziert wurde, um die Aufschlämmung zu kühlen und für eine Kontrolle des variablen Flußes und Drucks durch das Dekomprimierungssystem hindurch zu sorgen.

Revendications

1. Dispositif pour éliminer d'une façon continue des boues composées de scories et d'eau provenant d'un réacteur de gazéification de combustibles solides sous pression, le dispositif comprenant: au moins un broyeur sous pression pour réduire la dimension des particules solides de scories, le broyeur étant relié à l'extrémité de refoulement de scories du réacteur, et caractérisé en ce que le dispositif comporte un système de réduction de pression qui comprend un conduit par lequel les boues composées de scories et d'eau circulent d'une manière continue, le conduit étant relié à l'extrémité de refoulement du broyeur, et au moins un élément d'étranglement pour limiter l'écoulement fluide cinétique continu des boues composées de scories et d'eau dans le conduit, ledit élément d'étranglement étant disposé dans le conduit et ayant une ouverture dont le diamètre est inférieur à celui du conduit, ledit élément provoquant, à l'extrémité de refoulement du système de réduction de pression, une baisse de pression des boues jusqu'à un niveau sensiblement inférieur à la pression du réacteur.

2. Dispositif selon la revendication 1, dans lequel deux broyeurs sous pression sont présents, comportant
   un broyeur principal pour réduire les dimensions des particules solides de scories, relié à l'extrémité de refoulement de scories du réacteur,
   un broyeur secondaire pour réduire davantage les dimensions des particules solides de scories, ledit broyeur secondaire étant relié à l'extrémité de refoulement du broyeur primaire,
   un système de réduction de pression qui comporte un conduit dans lequel circulent d'une manière continue les boues composées de scories et d'eau, ledit conduit étant relié à l'extrémité de refoulement du broyeur secondaire, et
   un élément d'étranglement tel que défini dans la revendication 1.

3. Dispositif selon la revendication 1 ou 2, comportant un moyen pour injecter et mélanger de l'eau avec les boues après que les dimensions des particules solides de scories ont été réduites par le broyeur.

4. Dispositif selon la revendication 3, dans lequel le moyen pour injecter de l'eau dans le flux de boues comporte une vanne pour commander le débit de l'eau, en refroidissant de ce fait les boues composées de scories et d'eau et en permettant une commande variable du débit et de la pression de celles-ci dans le système de réduction de pression.

5. Dispositif selon l'une quelconque des revendications 1 à 4, dans lequel l'élément d'étranglement comporte un bouchon d'étranglement pourvu d'un orifice, ledit bouchon étant maintenu en place dans le conduit par une pièce de chemisage rapportée.

6. Dispositif selon la revendication 5, dans lequel l'orifice a un diamètre de 10 à 30 pour cent du diamètre du conduit dans lequel est disposé l'élément d'étranglement.

7. Procédé pour enlever d'une façon continue des boues composées de scories et d'eau d'un réacteur de gazéification de combustibles solides sous pression, ledit procédé comportant les étapes de :

(a) broyage fin des particules solides de scories présentes dans les boues refoulées depuis le réacteur afin de réduire les dimensions de particules de celles-ci, lesdites boues étant refoulées depuis le réacteur sous une pression sensiblement égale à la pression du réacteur; et

(b) passage des boues dans un circuit de réduction de pression qui comprend un conduit dans lequel les boues circulent d'une façon continue et au moins un élément d'étranglement pour réduire l'écoulement cinétique fluide continu des boues et réduire de ce fait la pression des boues au niveau de l'extrémité de refoulement du circuit de réduction de pression jusqu'à un niveau sensiblement inférieur à la pression du réacteur, ledit élément d'étranglement étant disposé à l'intérieur du conduit et ayant une ouverture dont le diamètre est inférieur à celui du conduit.

8. Procédé selon la revendication 7, comportant en outre l'injection et le mélange d'eau avec les boues après que les dimensions des particules solides de scories ont été réduites par broyage fin de manière à refroidir les boues et à réaliser une commande variable du débit et de la pression de celles-ci dans le circuit de réduction de pression.

Drawing