Bubble cap assembly in an ebullated bed reactor

Claim 2

In combination with a high pressure reaction vessel adapted for the reaction of a fluid hydrocarbon feed with a hydrogen rich gas at elevated temperatures and pressures in the presence of a bed of a particulate solid catalyst, said reaction being the type wherein the gas and feed materials are passed upwardly through the bed at velocities whereby the bed is expanded to a volume greater than its static volume and the particulate solid catalyst is put in a state of random motion and wherein the mixture of fluid hydrocarbon, gas and solid constitute a turbulent zone wherein minimum solid settling takes place, and wherein said reaction vessel has a transversely extending partition having a plurality of substantially regularly and uniformly disposed perforations extending through the partition; a bubble cap assembly including risers being mounted in said perforations and including caps surmounting said risers, said risers having fluid flow ports above said partition, said bubble cap assembly having a ball check valve in the riser to prevent downflow of said particulate solid catalyst, and restricting the downflow of fluid, said ball check valve including a ball and a valve seat, said ball being unrestricted to move vertically within said riser from said valve seat to a ball contact surface of said cap, said valve seat having an orifice adapted to be substantially closed by the ball, said orifice having a smaller internal diameter that that of the riser such that the velocity of the liquid flowing through said orifice is in excess of the transport velocity within said riser whereby catalyst particles entering said riser will be carried through said orifice, wherein the improvement comprises: the lower limit of said ports positioned at least one ball diameter above said valve seat and the upper limit of said ports positioned at least one ball diameter below said cap contact surface.

Claim 3

In combination with a high pressure reaction vessel adapted for the reaction of a fluid hydorcarbon feed with a hydrogen rich gas at elevated temperatures and pressures in the presence of a bed of a particulate solid catalyst, said reaction being the type wherein the gas and feed materials are passed upwardly through the bed at velocities whereby the bed is expanded to a volume greater than its static volume and the particulate solid catalyst is put in a state of random motion and wherein the mixture of fluid hydrocarbon, gas and solid constitute a turbulent zone wherein minimum solid settling takes place, and wherein said reaction vessel has a transversely extending partition having a plurality of substantially regularly and uniformly disposed perforations extending through the partition; a bubble cap assembly including risers being mounted in said perforations and including caps surmounting said risers, said risers having fluid flow ports above said partition, said bubble cap assembly having a ball check valve in the riser to prevent downflow of said particulate solid catalyst, and restricting the downflow of fluid, said ball check valve including a ball and a valve seat, said ball being unrestricted to move vertically within said riser from said valve seat to a ball contact surface of said cap, said valve seat having an orifice adapted to be substantially closed by the ball, said orifice having a smaller internal diameter than that of the riser such that the velocity of the liquid flowing through said orifice is in excess of the transport velocity within said riser whereby catalyst particles entering said riser will be carried through said orifice, wherein the improvement comprises: the lower limit of said ports positioned at least one ball diameter above said valve seat and the upper limit of said ports positioned at least one ball diameter below said cap contact surface and wherein the riser contains an orifice mixer upstream of said valve seat orifice.

Claim 4

In combination with a high pressure reaction vessel adapted for the reaction of a fluid hydorcarbon feed with a hydrogen rich gas at elevated temperatures and pressures in the presence of a bed of a particulate solid catalyst, said reaction being the type wherein the gas and feed materials are passed upwardly through the bed at velocities whereby the bed is expanded to a volume greater than its static volume and the particulate solid catalyst is put in a state of random motion and wherein the mixture of fluid hydrocarbon, gas and solid constitute a turbulent zone wherein minimum solid settling takes place, and wherein said reaction vessel has a transversely extending partition having a plurality of substantially regularly and uniformly disposed perforations extending through the partition; a bubble cap assembly including risers being mounted in said perforations and including caps surmounting said risers, said risers having fluid flow ports above said partition, said bubble cap assembly having a ball check valve in the riser to prevent downflow of said particulate solid catalyst, and restricting the downflow of fluid, said ball check valve including a ball and a valve seat, said ball being unrestricted to move vertically within said riser from said valve seat to a ball contact surface of said cap, said valve seat having an orifice adapted to be substantially closed by the ball, said orifice having a smaller internal diameter than that of the riser such that the velocity of the liquid flowing through said orifice is in excess of the transport velocity within said riser whereby catalyst particles entering said riser will be carried through said orifice, wherein the improvement comprises: the lower limit of said ports positioned at least one ball diameter above said valve seat and the upper limit of said ports positioned at least one ball diameter below said cap contact surface and wherein the riser contains an orifice mixer upstream of said valve seat orifice.

Claim 5

In combination with a high pressure reaction vessel adapted for the reaction of a fluid hydrocarbon feed with hydrogen rich gas at elevated temperatures and pressures in the presence of a bed of a particulate solid catalyst, said reaction being the type wherein the gas and feed materials are passed upwardly through the bed at velocities whereby the bed is expanded to a volume greater than its static volume and the particulate solid catalyst is put in a state of random motion and wherein the mixture of fluid hydrocarbon, gas and solid constitute a turbulent zone wherein minimum solid settling takes place, the lower portion of which is defined by a transversely extending partition having a plurality of substantially regularly and uniformly disposed perforations extending through the partition; a bubble cap assembly including risers being mounted in said perforations and including caps surmounting said risers, said risers having fluid flow ports above said partition, said bubble cap assembly having a ball check valve in the riser to prevent downflow of said particulate solid catalyst, and restricting the downflow of fluid, said ball check valve including a ball and a valve seat, said valve seat having an orifice adapted to be substantially closed by the ball, said orifice having a smaller internal diameter than that of the riser such that the velocity of the liquid flowing through said orifice is in excess of the transport velocity within said riser whereby catalyst particles entering said riser will be carried through said orifice, wherein the improvement comprises: said riser containing an orifice mixer upstream of said valve seat orifice.

Claim 6

In combination with a high pressure reaction vessel adapted for the reaction of a fluid hydrocarbon feed with hydrogen rich gas at elevated temperatures and pressures in the presence of a bed of a particulate solid catalyst, said reaction being the type wherein the gas and feed materials are passed upwardly through the bed at velocities whereby the bed is expanded to a volume greater than its static volume and the particulate solid catalyst is put in a state of random motion and wherein the mixture of fluid hydrocarbon, gas and solid constitute a turbulent zone wherein minimum solid settling takes place, the lower portion of which is defined by a transversely extending partition having a plurality of substantially regularly and uniformly disposed perforations extending through the partition; a bubble cap assembly including risers being mounted in said perforations and including caps surmounting said risers, said risers having fluid flow ports above said partition, said bubble cap assembly having a ball check valve in the riser to prevent downflow of said particulate solid catalyst, and restricting the downflow of fluid, said ball check valve including a ball and a valve seat, said valve seat having an orifice adapted to be substantially closed by the ball, said orifice having a smaller internal diameter than that of the riser such that the velocity of the liquid flowing through said orifice is in excess of the transport velocity within said riser whereby catalyst particles entering said riser will be carried through said orifice, wherein the improvement comprises: said riser containing an orifice mixer upstream of said valve seat orifice.