Circulating fluidized bed reactor

Claim 2

A circulating fluidized bed reactor, comprising: means defining an upright reactor chamber having at least one gas discharge opening adjacent its upper end and at least one inlet opening for solids separated from the gas adjacent it lower end; a housing; a plurality of generally vertically extending horizontally spaced filtration tubes in part formed of porous material and disposed in said housing; said filter housing and said reactor chamber being arranged in back-to-back relation one with the other, said housing having a gas inlet in communication with said gas discharge opening, a solids outlet in communication with said solids inlet opening and at least one clean gas outlet in communication with the space between said filtration tubes an said housing whereby gas flows through the porous material of said tubes into said space for communicating with said one clean gas outlet.

Claim 3

A reactor according to claim 1 including separating means connecting said gas discharge opening and said gas inlet for separating solids and gases upstream of said housing.

Claim 4

A reactor according to claim 2 wherein said separating means comprises a wall inclined towards the reactor chamber for returning separated solids to the reactor.

Claim 5

A reactor according to claim 2 wherein said separating means comprises at least one cyclone separator having a separator chamber, said gas inlet including a duct in communication with said gas discharge opening, a solids outlet in the lower part of said cyclone chamber in communication with the reactor chamber and a gas outlet pipe extending into said cyclone chamber, said cyclone chamber having a bottom to which said gas outlet pipe is connected.

Claim 6

A reactor according to claim 4 wherein said bottom is inclined towards the reactor chamber.

Claim 7

A reactor according to claim 1 including a standpipe and a loop seal connecting said solids outlet and said solids inlet opening.

Claim 8

A reactor according to claim 6 wherein the reactor chamber, the filter housing, the standpipe and the loop seal are encased in a pressurized vessel.

Claim 9

A reactor according to claim 7 wherein said vessel is cylindrical.

Claim 10

A reactor according to claim 1 including means for water cooling at least a portion of the walls of the reactor chamber and said filter housing.

Claim 11

A reactor according to claim 1 including separating means connecting said gas discharge opening and said gas inlet for separating solids and gases upstream of said housing, said separating means including a wall inclined towards the reactor chamber for returning solids to the reactor, said filtration tubes extending upwardly to project above said inclined wall, means for partially closing end portions of said upwardly projecting tubes for separating coarse solids from the gas for deposition on said inclined wall and return to said reactor and enabling gas having smaller sized solids entrained therein to flow into said tubes.

Claim 12

A reactor according to claim 1 wherein said filter housing is disposed on one side of said reactor chamber, said reactor chamber having a second inlet opening for solids separated from the gas adjacent its lower end, a second filter housing having a plurality of generally vertically extending horizontally spaced filtration tubes in part formed of porous material and disposed in said second housing, said second filter housing and said reaction chamber being arranged in back-to-back relation one with the other on the opposite side of said reactor from said first filter housing, said second filter housing and said reactor chamber being arranged in back-to-back relation one with the other, said second housing having a gas inlet in communication with said gas discharge opening, a solids outlet in communication with said second solids inlet opening and at least one clean gas outlet in communication with the space between said filtration tubes and said second housing whereby gas flows through the porous material of the latter tubes into said space for communicating with said one clean gas outlet of said second housing.

Claim 13

A reactor according to claim 11 including a pair of separating means connecting said gas discharge opening and said gas inlets for said first and second housings, respectively for separating solids and gases upstream of said housings, each of said separating means including a wall inclined towards the reactor chamber for returning solids to the reactor, said filtration tubes of each housing extending upwardly to project above the inclined wall thereof, and means for partially closing end portions of said upwardly projecting tubes for separating coarse solids from the gas for deposition on said inclined walls and return to said reactor and enabling gas having smaller sized solids entrained therein to flow into said tubes.

Claim 14

A reactor according to claim 11 including a pair of separating means connecting said gas discharge opening and said gas inlets for said first and second housings, respectively, for separating solids and gases upstream of said housings, said separating means each comprising at least one cyclone separator having a separator chamber, said gas inlet including a duct in communication with said gas discharge opening, a solids outlet in the lower part of said cyclone chamber in communication with the reactor chamber and a gas outlet pipe extending into said cyclone chamber, said cyclone chamber having a bottom to which said gas outlet pipe is connected.

Claim 15

Apparatus according to claim 1 wherein said housing includes a plurality of superposed compartments through which said filtration tubes extend, said compartments defining said space from receiving the gas flowing through said porous tubes and in communication with said on clean gas outlet.

Claim 16

Apparatus according to claim 1 including a pressure vessel, said reactor chamber and said filtration housing being disposed within said pressure vessel for operation at a pressure other than atmospheric.

Claim 17

Apparatus according to claim 1 including separating means carried by said filter housing for separating solids into coarse and fine solids flow streams through said filter housing, said separating means including at least one filtration tube having a large cross sectional area for receiving the coarse solids in comparison with at least another filtration tube having a small cross sectional area for receiving the fine solids.

Claim 18

Apparatus according to claim 16 wherein said coarse and fine filtration tubes open at their downstream ends in communication with said solids inlet.

Claim 19

A circulating fluidized bed reactor, comprising: means defining an upright reactor chamber having at least one gas discharge opening adjacent its upper end and at least one inlet opening for solids separated from the gas adjacent its lower end; a housing; a plurality of generally vertically extending horizontally spaced filtration tubes in part formed of porous material and disposed in said housing; means defining a chamber about each said tube for receiving gas flowing through the porous material of said tubes; said filter housing and said reactor chamber being arranged in back-to-back relation one with the other, said housing having a gas inlet in communication with said gas discharge opening, a solids outlet in communication with said solids inlet opening and at least one clean gas outlet in communication with said chamber defining means, whereby gas flows through the porous material of said tubes into said chamber for communicating with said one clean gas outlet.

Claim 20

A circulating fluidized bed reactor, comprising: means defining an upright reactor chamber having at least one gas discharge opening adjacent its upper end and at least one inlet opening for solids separated from the gas adjacent its lower end; a housing; a plurality of generally vertically extending horizontally spaced filtration tubes in part formed of porous material and disposed in said housing; means defining a chamber about each said tube for receiving gas flowing through the porous material of said tubes; said filter housing and said reactor chamber being arranged in back-to-back relation one with the other, said housing having a gas inlet in communication with said gas discharge opening, a solids outlet in communication with said solids inlet opening and at least one clean gas outlet in communication with said chamber defining means, whereby gas flows through the porous material of said tubes into said chamber for communicating with said one clean gas outlet.

Claim 21

A reactor according to claim 1B including separating means connecting said gas discharge opening and said gas inlet for separating solids and gases upstream of said housing.

Claim 22

A reactor according to claim 18, including a pressure vessel, said reactor chamber and said filtration housing being disposed within said pressure vessel for operation at a pressure other than atmospheric.

Claim 25

A method according to claim 21 including the step of separating the coarse solids from the solids entrained gas prior to flowing the gas into the filtration tubes.

Claim 26

A method according to claim 22 wherein said reactor chamber and said housing are vertically elongated and form part of a single vessel, wherein the step of returning the solids to said reactor chamber includes flowing the separated solids by gravity along a wall disposed adjacent the top of said housing.

Claim 27

A method according to claim 22 wherein the step of separating includes flowing the gas tangentially into a cyclone separator.

Claim 28

A method according to claim 24 wherein said reactor chamber and said housing are vertically elongated and form part of a single vessel, wherein the step of returning the solids to said reactor chamber includes flowing the separated solids by gravity along a wall disposed adjacent the top of said housing and forming the bottom of the cyclone separator.

Claim 29

A method according to claim 21 including the step of enclosing said reactor chamber and said housing within a pressure vessel for operating said reactor at a pressure other than atmospheric pressure.

Claim 30

A method according to claim 21 including the steps of flowing the coarse solids through at least one filtration tube of said housing and flowing the finer solids through the other filtration tubes of said housing.

Claim 31

A method according to claim 27 wherein the step of returning the solids to the reactor chamber includes recombining the coarse and fine solids after flow through the filtration tubes for combined return to the reaction chamber.