Use of control system for gas-solids contacting processes

Claim 2

In a gas-solids contacting process wherein a moving bed of granular solids is contacted in an enclosed treating zone at elevated temperatures with a stream of non-oxidizing gas to produce a net off-gas therefrom, the rate of production of said net off-gas varying from time to time between a maximum value, M, and a minimum value, m, and wherein said solids are transferred from said treating zone through an enclosed transfer zone into an enclosed combustion zone and contacted therein at elevated temperatures with a stream of oxidizing gas, the improved method for preventing the transfer of gases between said treating zone and said combustion zone without the use of mechanical sealing means, which comprises: (1) continuously detecting the pressure prevailing at some point in said transfer zone; (2) maintaining substantially constant pressures in said treating zone and combustion zone by exhausting flue gas from said combustion zone in response to said detected pressure; (3) cooling and removing from the process a portion of said net off-gas at a substantially constant predetermined flow rate, x, which is less than said value m; (4) injecting steam into said transfer zone at a substantially constant predetermined flow rate, y, which is greater than M - m; and (5) at a point between said steam injection and said treating zone, withdrawing a mixed gas stream from said transfer zone at a substantially constant, predetermined flow rate, z, wherein z is greater than M - x, but less than y + m - x, whereby said mixed gas stream always comprises the net off-gas not withdrawn at step (3) plus some steam, and whereby some of said steam injected at step (4) always passes through said combustion zone.

Claim 3

A process as defined in claim 1 wherein crushed oil shale is retorted in said treating zone, and coke on the resulting retorted shale is burned in said combustion zone.

Claim 4

In a shale retorting process wherein: (a) crushed oil shale is countercurrently contacted with a preheated, substantially oxygen-free eduction gas in a retorting zone to educe therefrom product oil and a hydrocarbonaceous make gas, the rate of production of said make gas varying from time to time between a maximum value, M, and a minimum value, m; (b) off-gas from said retorting zone is cooled to condense out water and heavy hydrocarbons, and then divided into a net make gas stream and an eduction recycle gas stream; and (c) hot, retorted shale from said retorting zone is passed through an enclosed transfer zone into a combustion zone wherein it is contacted with an oxygen-containing combustion gas to burn coke therefrom and produce a hot flue gas; the improved method for preventing the transfer of gases between said retorting zone and said combustion zone without the use of mechanical sealing means, which comprises: (1) continuously detecting the pressure prevailing at some point in said transfer zone; (2) maintaining substantially constant pressures in said retorting zone and combustion zone by exhausting flue gas from said combustion zone in response to said detected pressure; (3) removing from the system net make gas in (b) above at a substantially constant predetermined flow rate, x, which is less than said value m; (4) injecting steam into said transfer zone at a substantially constant predetermined flow rate, y, which is greater than M - m; and (5) at a point between said steam injection and said retorting zone, withdrawing a mixed gas stream from said transfer zone at a substantially constant, predetermined flow rate, z, wherein z is greater than M - x, but less than y + m - x, whereby said mixed gas stream always comprises the net make gas not withdrawn at step (3) plus some steam, and whereby some of said steam injected at step (4) always passes through said combustion zone.

Claim 5

In a shale retorting process wherein: (a) crushed oil shale is countercurrently contacted with a preheated, substantially oxygen-free eduction gas in a retorting zone to educe therefrom product oil and a hydrocarbonaceous make gas, the rate of production of said make gas varying from time to time between a maximum value, M, and a minimum value, m; (b) off-gas from said retorting zone is cooled to condense out water and heavy hydrocarbons, and then divided into a net make gas stream and an eduction recycle gas stream; and (c) hot, retorted shale from said retorting zone is passed through an enclosed transfer zone into a combustion zone wherein it is contacted with an oxygen-containing combustion gas to burn coke therefrom and produce a hot flue gas; the improved method for preventing the transfer of gases between said retorting zone and said combustion zone without the use of mechanical sealing means, which comprises: (1) continuously detecting the pressure prevailing at some point in said transfer zone; (2) maintaining substantially constant pressures in said retorting zone and combustion zone by exhausting flue gas from said combustion zone in response to said detected pressure; (3) removing from the system net make gas in (b) above at a substantially constant predetermined flow rate, x, which is less than said value m; (4) injecting steam into said transfer zone at a substantially constant predetermined flow rate, y, which is greater than M - m; and (5) at a point between said steam injection and said retorting zone, withdrawing a mixed gas stream from said transfer zone at a substantially constant, predetermined flow rate, z, wherein z is greater than M - x, but less than y + m - x, whereby said mixed gas stream always comprises the net make gas not withdrawn at step (3) plus some steam, and whereby some of said steam injected at step (4) always passes through said combustion zone.

Claim 6

A process as defined in claim 3 wherein said combustion gas is contacted with said retorted shale in concurrent flow therewith.

Claim 7

A process as defined in claim 3 wherein said oil shale is passed upwardly through said retorting zone, and said retorted shale is passed downwardly through said transfer zone and said combustion zone.

Claim 8

A process as defined in claim 5 wherein said retorted shale is passed through said combustion zone and a substantial lower portion of said transfer zone as a compact bed, and wherein said steam is injected below the top of said compact bed so as to effect a substantial stripping of hydrocarbonaceous material therefrom.

Claim 9

A process as defined in claim 5 wherein said combustion gas is contacted with said retorted shale in concurrent flow therewith.

Claim 10

A process as defined in claim 3 wherein M - m is at least about 5% of m.

Claim 11

A process as defined in claim 3 wherein said retorting zone, said transfer zone and said combustion zone are maintained at pressures between about - 10 and 500 psig.

Claim 12

A process as defined in claim 9 wherein said oil shale is passed upwardly through said retorting zone, and said retorted shale is passed downwardly through said transfer zone and said combustion zone.

Claim 13

A process as defined in claim 10 wherein said combustion gas is contacted with said retorted shale in concurrent flow therewith.