Continuous process and apparatus for modifying carbohydrate material

Claim 2

A chemical reactor comprising (a) an elongated tubular primary reactor having a plurality of laterally spaced flow tubes passing through a heat exchange vessel, said heat exchange vessel being adapted to receive superatmospheric steam, (b) a feed inlet to said primary reactor connected by way of a manifold to inlets of said plurality of flow tubes, said manifold comprising a truncated conical member with an open small end and a large end closed by a plate member, the open small end connecting to said feed inlet, and said primary reactor flow tubes connecting through openings in said large end plate member, the inner face of said plate member being radially outwardly inclined toward the axis thereof, (c) tube member connected by way of a manifold to outlets of said plurality of flow tubes, the tubes being arranged to provide substantially equal flow velocities through the primary reactor flow tubes, (d) a first flow restricting orifice connected to said single outlet tube, (e) an elongated secondary reactor tube having the inlet thereof flow connected to said first orifice outlet and (f) positive displacement pump means connected to said feed inlet tube.

Claim 3

A reactor according to claim 1 wherein said heat exchange vessel includes a plurality of said inlet tube members and a plurality of said outlet tube members, each pair of inlet and outlet tube members having a plurality of said primary reactor flow tubes connected therebetween.

Claim 4

A reactor according to claim 1 wherein said plurality of inlet tube members are flow connected to a single feed pump.

Claim 5

A reactor according to claim 3 wherein said pump is a variable speed pump, the speed of the pump being used as a pressure control means for the reactor.

Claim 6

A reactor according to claim 4 wherein each of said primary reactor flow tubes has an inside diameter of no more than about 11/2 inches.

Claim 7

A reactor according to claim 1 wherein said elongated secondary reaction tube passes through the heat exchange vessel containing the primary reactor flow tubes.

Claim 8

A reactor according to claim 1 wherein said elongated secondary reaction tube passes through a separate heat exchange vessel.

Claim 9

A reactor according to claim 1 wherein said outlet manifold comprises a continuous flow collector connected to said primary reactor flow tube outlets, said collector having a truncated conical shape with a closed large end and an open small end, the open small end connecting to said outlet tube member, and said primary reactor flow tubes connecting through openings in said large end, said primary reactor flow tubes adjacent said openings being inclined toward the axis of the collector such that the flows from the primary reactor flow tubes intersect and mix within the collector.

Claim 10

A reactor according to claim 1 wherein the inner end of each said opening in the end plate member includes a bevelled countersink flow inlet.

Claim 11

A reactor according to claim 1 wherein the primary reactor tubes are arranged with an axially positioned tube and a plurality of further tubes spaced in concentric circles.

Claim 12

A starch reactor comprising (a) an elongated tubular primary reactor having a plurality of parallel flow tubes passing through a heat exchange vessel, said heat exchange vessel being adapted to receive superatmospheric steam, (b) a feed inlet to said primary reactor connected by way of a manifold to inlets of said plurality of flow tubes, said inlet manifold comprising a truncated conical member with an open small end and a large end closed by an end plate member, the open small end connecting to said feed inlet, and said primary reactor flow tubes connecting through openings in said large end plate member, the inner face of said plate member being radially outwardly inclined toward the axis thereof, (c) an outlet from said primary reactor comprising an outlet tube member connected by way of a manifold to outlets of said plurality of flow tubes, said outlet manifold comprising a continuous flow collector connected to said primary reactor flow tube outlets, said collector having a truncated conical shape with a closed large end closed by an end plate member and an open small end, the open small end connecting to said outlet tube member, and said primary reactor flow tubes connecting through openings in said large end plate member, and the tubes being arranged to provide substantially equal flow velocities through the primary reactor flow tubes, (d) a first flow restricting orifice connected to said single outlet tube, (e) an elongated secondary reactor tube having the inlet thereof flow connected to said first orifice outlet and (f) positive displacement pump means connected to said feed inlet tube.

Claim 13

A starch reactor comprising (a) an elongated tubular primary reactor having a plurality of parallel flow tubes passing through a heat exchange vessel, said heat exchange vessel being adapted to receive superatmospheric steam, (b) a feed inlet to said primary reactor connected by way of a manifold to inlets of said plurality of flow tubes, said inlet manifold comprising a truncated conical member with an open small end and a large end closed by an end plate member, the open small end connecting to said feed inlet, and said primary reactor flow tubes connecting through openings in said large end plate member, the inner face of said plate member being radially outwardly inclined toward the axis thereof, (c) an outlet from said primary reactor comprising an outlet tube member connected by way of a manifold to outlets of said plurality of flow tubes, said outlet manifold comprising a continuous flow collector connected to said primary reactor flow tube outlets, said collector having a truncated conical shape with a closed large end closed by an end plate member and an open small end, the open small end connecting to said outlet tube member, and said primary reactor flow tubes connecting through openings in said large end plate member, and the tubes being arranged to provide substantially equal flow velocities through the primary reactor flow tubes, (d) a first flow restricting orifice connected to said single outlet tube, (e) an elongated secondary reactor tube having the inlet thereof flow connected to said first orifice outlet and (f) positive displacement pump means connected to said feed inlet tube.

Claim 14

A reactor according to claim 11 having flow deflectors in the outlets of said plurality of flow tubes to cause fluid mixing in the outlet manifold.

Claim 15

A reactor according to claim 12 wherein the inner end of each opening in the end plate member of the inlet manifold includes a bevelled countersink flow inlet.

Claim 16

A reactor according to claim 12 or 16 wherein the primary reactor tubes are arranged with an axially positioned tube and a plurality of further tubes spaced in concentric circles.

Claim 17

A chemical reactor comprising (a) an elongated tubular primary reactor having a plurality of laterally spaced flow tubes passing through a heat exchange vessel, said heat exchange vessel being adapted to receive superatmospheric stream, (b) a feed inlet to said primary reactor connected by way of a manifold to inlets of said plurality of flow tubes, said manifold comprising an inlet tube flow connected to the inlets of the flow tubes by way of flow distributor means adapted to transfer the flow from the inlet tube into the plurality of flow tubes in smooth flow paths inclined outwardly in the flow direction relative to the axis of the inlet tube, (c) an outlet from said primary reactor comprising an outlet tube member connected by way of a manifold to outlets of said plurality of flow tubes, said outlet manifold comprising a continuous flow collector connected to said primary reactor flow tube outlets, said collector having a truncated conical shape with a closed large end and an open small end, the open small end connecting to said outlet tube member, and said primary reactor flow tubes connecting through openings in said large end, said primary reactor flow tubes being arranged such that the flows from the primary reactor flow tubes intersect and mix within the collector, (d) a first flow restricting orifice connected to said single outlet tube, (e) an elongated secondary reactor tube having the inlet thereof flow connected to said first orifice outlet and (f) positive displacement pump means connected to said feed inlet tube.

Claim 18

A chemical reactor comprising (a) an elongated tubular primary reactor having a plurality of laterally spaced flow tubes passing through a heat exchange vessel, said heat exchange vessel being adapted to receive superatmospheric stream, (b) a feed inlet to said primary reactor connected by way of a manifold to inlets of said plurality of flow tubes, said manifold comprising an inlet tube flow connected to the inlets of the flow tubes by way of flow distributor means adapted to transfer the flow from the inlet tube into the plurality of flow tubes in smooth flow paths inclined outwardly in the flow direction relative to the axis of the inlet tube, (c) an outlet from said primary reactor comprising an outlet tube member connected by way of a manifold to outlets of said plurality of flow tubes, said outlet manifold comprising a continuous flow collector connected to said primary reactor flow tube outlets, said collector having a truncated conical shape with a closed large end and an open small end, the open small end connecting to said outlet tube member, and said primary reactor flow tubes connecting through openings in said large end, said primary reactor flow tubes being arranged such that the flows from the primary reactor flow tubes intersect and mix within the collector, (d) a first flow restricting orifice connected to said single outlet tube, (e) an elongated secondary reactor tube having the inlet thereof flow connected to said first orifice outlet and (f) positive displacement pump means connected to said feed inlet tube.