Slag discharge from reactor for synthesis gas production
With a method for discharging slag from a water bath of a reactor for synthesis gas production, whereby the slag is brought to a lower pressure level by means of a transfer container, a solution is supposed to be created, with which the components connected with transferring the slag out are subject to a low temperature, whereby immediate slag transfer without water exchange is supposed to be made possible, with a minimal required cooling power. This is accomplished in that a cooling water stream is passed to the slag stream in the outlet region of the slag from the water bath of the gas generator or the pressurized container that surrounds it, in a region having a greater cross-section than the cross-section of the entry connector of another system part, such as, for example, the transfer container, in such a manner that temperature stratification in the outlet region is made possible.
1. A method for discharging slag from a water bath of a reactor for synthesis gas production, the method comprising steps of:
providing a reactor, said reactor comprising a water bath, a pressurized container surrounding the water bath, and a ring channel, wherein the pressurized container comprises an outlet for discharging a slag stream from the water bath, wherein the ring channel surrounds the outlet of the pressurized container;
providing a first transfer container, the first transfer container comprising an entry connector;
discharging a slag stream from the water bath through the outlet of the pressurized container;
passing a cooling water stream into the ring channel and to the slag stream discharged from the water bath in a region of the outlet of the pressurized container in such a manner that temperature stratification in the region is made possible;
hydraulically conveying the slag into the first transfer container via the cooling water stream; and
bringing the slag to a lower pressure level via the first transfer container;
wherein the entry connector of the first transfer container has a first cross-section;
wherein the region of the outlet of the pressurized container has a second cross-section greater than the first cross-section; and
wherein the temperature of the slag is reduced by continuous hydraulic movement of the slag from the region of the outlet to the transfer container.
2. The method according to claim 1 , wherein the cooling water stream hydraulically conveys the slag counter to the direction of gravity to the transfer container.
3. The method according to claim 1 , wherein at least part of the cooling water stream that hydraulically conveys the slag into the transfer container is returned via a returned cooling water stream to the ring channel to form the cooling water stream, and
wherein the returned cooling water stream is passed through a heat exchanger.
4. The method according to claim 3 , wherein part of the returned cooling water stream is introduced into a lower region of the transfer container.
5. The method according to claim 1 , wherein part of the cooling water stream is guided in the direction of the water bath, counter to the slag stream, in the region of the outlet of the pressurized container, in such a manner that a water stream out of the water bath is prevented.
6. The method according to claim 1 , wherein the cooling water stream also hydraulically conveys the slag into a second transfer container.
7. A device for carrying out the method according to claim 1 , the device comprising a reactor comprising a water bath, a pressurized container surrounding the water bath, and a slag cooling pipe comprising a ring channel, the pressurized container comprising an outlet for discharging a slag stream from the water bath, and the ring channel surrounding the outlet of the pressurized container,
wherein the slag cooling pipe is oriented in the direction of gravity, at the pressurized container outlet for a gentle, ring-shaped feed of a cooling water stream.
8. The device according to claim 7 , wherein the slag guidance and the cooling pipe has a cross-section of 0.5 to 2 m, to make the transport and flow speeds within a cooling distance uniform, and to produce temperature stratification.