55results about How to "Catalyst content reduction" patented technology

A separation method for a slurry bed fischer-tropsch synthesis heavy product and a catalyst is characterized in that the fischer-tropsch synthesis heavy product from a slurry bed reactor and the magnetic fischer-tropsch synthesis catalyst, after degassing, enter the lower part of a separator, the catalyst and the fischer-tropsch synthesis heavy product are preliminarily separated by gravity settling to obtain concentrated slurry rich in the catalyst in the lower part of the separator, the concentrated slurry is cycled to the slurry bed reactor, and obtained diluted slurry enters into a magnetic separator zone on the upper part of the separator; in the magnetic separator zone, the catalyst is adsorbed by magnetic force in a magnetic field zone, when the amount of the catalyst adsorbed in the magnetic field zone reaches a set amount, the magnetic field is removed, the catalyst sinks by gravity to a flow guide pipe, flows to the bottom of the separator along the flow guide pipe, and is is cycled to the slurry bed reactor; after the magnetic separation, the catalyst is further separated from the fischer-tropsch synthesis heavy product containing less catalyst by a filter element, and is discharged out of the separator, and the filtered catalyst is cycled to the slurry bed reactor.

Device for treatment of a gas flow including at least one body (3), at least one first opening (4, 4') for entrance of an incoming gas flow to the body (3) and at least one second opening (5, 5') for the exit of an outgoing gas flow from the body (3). The body (3) is provided with a plurality of gas flow passages (11a, 11b) arranged to permit heat exchange between the gas flows in adjacent passages. The device has at least one distribution section (26, 26') in communication with the first opening (4, 4') and with the gas flow passages (11a, 11b) to distribute the incoming gas flow to the gas flow passages (11a, 11b), and at least one gas flow passage section (27, 27') including the gas flow passages (11a, 11b), which passage section (27, 27') primarily is adapted to permit heat exchange and to cause a conversion in the composition of the gas.

The invention relates to a catalyst separating device and a method in the furfuryl alcohol production. The device comprises a furfuryl alcohol coarse product storage tank, a disk settling centrifuge, and a three-column filter centrifuge, wherein the furfuryl alcohol coarse product storage tank, the disk settling centrifuge, a recovery tank, a pulp pump and the three-column filter centrifuge sequentially connected through a pipe, and an clear liquid outlet of the disk settling centrifuge is connected to a distillation tower; and a residue liquid outlet of the disk settling centrifuge is connected to the recovery tank. A liquid outlet of the three-column filter centrifuge is connected to the furfuryl alcohol coarse product storage tank. The method includes (1) separating catalyst-carried furfuryl alcohol coarse product through the disk settling centrifuge, and allowing clear liquid to flow into the distillation tower; (2) separating the residue liquid in the three-column filter centrifuge, and discharging the filter residue; and (3) refluxing the filtrate into the furfuryl alcohol coarse product tank, and separating in the disk settling centrifuge again. Compared with the conventional method, the inventive method has high removal rate for removing catalyst from furfuryl alcohol coarse product (increased by about 30-60%), reduced catalyst content in distillation drainage, reduced environment pollution, shortened process route and reduced energy consumption.