Transient response process for detecting in situ retorting conditions

Claim 2

A process for use in underground retorting of oil shale, comprising the steps of: igniting a flame front in an underground retort of raw oil shale to form a hot zone; liberating shale oil and off gases from said raw oil shale in said hot zone with heat emitted from said flame front, leaving retorted oil shale containing residual carbon; combusting said residual carbon on said retorted shale with said flame front to form spent oil shale; advancing said flame front through a portion of said raw oil shale; supporting said flame front and said advancement with an oxygen-containing gas under a first set of feed conditions; changing said feed conditions; and determining the thickness of said hot zone by monitoring said off gases in response to the change of feed conditions.

Claim 3

A process in accordance with claim 1 including detecting the location of said hot zone by monitoring said off gases in response to said change of feed conditions.

Claim 4

A process in accordance with claim 1 including determining the thickness of said raw oil shale by monitoring said off gases in response to said change of feed conditions.

Claim 5

A process in accordance with claim 1 including determining the thickness of said spent oil shale by monitoring said off gases in response to said change of feed conditions.

Claim 6

A process in accordance with claim 1 including monitoring the temperature of said off gases.

Claim 7

A process in accordance with claim 1 including monitoring the composition of said off gases.

Claim 8

A process in accordance with claim 6 including monitoring the carbon dioxide content of said off gases.

Claim 9

A process in accordance with claim 6 including monitoring the hydrogen saturated gases in said off gases.

Claim 10

A process in accordance with claim 1 wherein part of said shale oil is thermal cracked during said advancement and the extent of thermal cracking is determined by monitoring the hydrogen unsaturated gases in said off gases.

Claim 11

A process in accordance with claim 1 wherein said oxygen-containing gas contains steam and said feed conditions are changed by changing the amount of steam in said oxygen-containing gas.

Claim 12

A process in accordance with claim 1 wherein said oxygen-containing gas contains air and a diluent, and said feed conditions are changed by changing the amount of air in said oxygen-containing gas.

Claim 13

A process in accordance with claim 11 wherein said feed conditions are changed by substantially stopping the inflow of air.

Claim 14

A process in accordance with claim 1 wherein said feed conditions are changed by changing the flow rate of said oxygen-containing gas.

Claim 15

A process in accordance with claim 1 including monitoring the rate of change.

Claim 16

A process in accordance with claim 1 wherein said retort is a true in situ retort.

Claim 17

A process in accordance with claim 1 wherein said retort is a modified in situ retort.

Claim 18

A process in aocordance with claim 1 wherein said retort is a vertical in situ retort.

Claim 19

A process in accordance with claim 1 wherein said hot zone includes a reactive zone.

Claim 20

A process in accordance with claim 1 wherein said hot zone includes a mineral decomposition zone.

Claim 21

A process in accordance with claim 1 wherein said hot zone includes a kerogen decomposition zone.

Claim 22

A process for use in underground retorting of oil shale, comprising the steps of: igniting a flame front across a generally upright, modified in situ retort; liberating shale oil and carbon dioxide from said raw oil shale in a mineral decomposition zone with heat generated by said flame front; supporting said flame front with a feed gas containing air and a diluent; changing the amount of air in said feed gas; and determining the depth of said mineral decomposition zone by monitoring the amount of said carbon dioxide liberated in response to said change.

Claim 23

A process for use in underground retorting of oil shale, comprising the steps of: igniting a flame front across a generally upright, modified in situ retort; liberating shale oil and carbon dioxide from said raw oil shale in a mineral decomposition zone with heat generated by said flame front; supporting said flame front with a feed gas containing air and a diluent; changing the amount of air in said feed gas; and determining the depth of said mineral decomposition zone by monitoring the amount of said carbon dioxide liberated in response to said change.

Claim 24

A process in accordance with claim 21 wherein the amount of air is substantially reduced.

Claim 25

A process in accordance with claim 21 wherein the inflow of air in said feed gas is stopped.

Claim 26

A process in accordance with claim 23 wherein said diluent is selected from the group consisting of steam, carbon dioxide, nitrogen and recycled retort off gases.

Claim 27

A process in accordance with claim 21 including measuring the transient response time for said change.

Claim 28

A process for use in underground retorting oil shale, comprising the steps of: igniting a flame front across a generally upright, modified in situ retort; liberating shale oil and hydrogen saturated gases from said raw oil shale in a kerogen decomposition zone with heat generated by said flame front; supporting said flame front with a feed gas containing air and a diluent; changing the amount of air in said feed gas; and determining the depth of said kerogen decomposition zone by monitoring the amount of said hydrogen saturated gases liberated in response to said, change.

Claim 29

A process for use in underground retorting oil shale, comprising the steps of: igniting a flame front across a generally upright, modified in situ retort; liberating shale oil and hydrogen saturated gases from said raw oil shale in a kerogen decomposition zone with heat generated by said flame front; supporting said flame front with a feed gas containing air and a diluent; changing the amount of air in said feed gas; and determining the depth of said kerogen decomposition zone by monitoring the amount of said hydrogen saturated gases liberated in response to said, change.

Claim 30

A process in accordance with claim 21 including monitoring the amount of methane in said hydrogen saturated gases.

Claim 31

A process in accordance with claim 26 including monitoring the amount of ethane in said hydrogen saturated gases.

Claim 32

A process in accordance with claim 26 including monitoring the amount of propane in said hydrogen saturated gases.

Claim 33

A process in accordance with claim 26 wherein said heat thermal cracks said shale oil liberating hydrogen unsaturated gases, and the amount of said thermal cracking is determined by monitoring the amount of said hydrogen unsaturated gases in response to said change.

Claim 34

A process in accordance with claim 30 including monitoring the amount of ethylene in said hydrogen unsaturated gases.

Claim 35

A process in accordance with claim 30 including monitoring the amount of propylene in said hydrogen unsaturated gases.

Claim 36

A process in accordance with claim 26 wherein the inflow of air in said feed gas is substantially stopped.

Claim 37

A process in accordance with claim 26 wherein said diluent is selected from the group consisting of steam, carbon dioxide, nitrogen and recycled retort off gases.

Claim 38

A process for use in underground retorting of oil shale, comprising the steps of: igniting a flame front across a generally upright, modified in situ retort to form a hot zone; liberating shale oil and off gases from said raw oil shale in said hot zone with heat emitted from said flame front, leaving retorted oil shale containing residual carbon; combusting said residual carbon on said retorted oil shale to form spent oil shale; advancing said flame front-downwardly through a portion of said raw oil shale; supporting said flame front with a feed gas consisting essentially of steam and air; changing the proportion of said steam and said air in said feed gas while supporting said flame front; analyzing the composition of said off gases with analyzing means consisting essentially of a gas chromatograph and a gas detector; and determining the location and depth of said hot zone by measuring the temperature of said off gases with a thermometer and by measuring the time it takes for the composition of the off gases to change after the proportion of steam and air in said feed gas has been changed with timing means selected from the group consiting essentially of a clock and a stopwatch.

Claim 39

A process for use in underground retorting of oil shale, comprising the steps of: igniting a flame front across a generally upright, modified in situ retort to form a hot zone; liberating shale oil and off gases from said raw oil shale in said hot zone with heat emitted from said flame front, leaving retorted oil shale containing residual carbon; combusting said residual carbon on said retorted oil shale to form spent oil shale; advancing said flame front-downwardly through a portion of said raw oil shale; supporting said flame front with a feed gas consisting essentially of steam and air; changing the proportion of said steam and said air in said feed gas while supporting said flame front; analyzing the composition of said off gases with analyzing means consisting essentially of a gas chromatograph and a gas detector; and determining the location and depth of said hot zone by measuring the temperature of said off gases with a thermometer and by measuring the time it takes for the composition of the off gases to change after the proportion of steam and air in said feed gas has been changed with timing means selected from the group consiting essentially of a clock and a stopwatch.

Claim 40

A process in accordance with claim 35 including estimating when completion of retorting will occur in response to determining the location of said hot zone in order to determine the extent of retorting.

Claim 41

A process in accordance with claim 35 including decreasing the depth of said hot zone by increasing the proportion of steam in said feed gas.

Claim 42

A process in accordance with claim 37 including decreasing the rate of said combustion by increasing the proportion of steam in said feed gas, and controling the rate of said advancement of said flame front by regulating the flow of said feed gas.

Claim 43

A process in accordance with claim 35 wherein said determining includes determining the location and depth of said spent oil shale.

Claim 44

A process in accordance with claim 39 wherein said determining further includes determining the location and depth of said raw oil shale.

Claim 45

A process in accordance with claim 40 wherein said determining further includes: determining the amount of retorted oil shale; monitoring the amount of shale oil liberated; and determining the yield of shale oil per ton of retorted oil shale.

Claim 46

A process in accordance with claim 40 wherein the proportion of said steam and said air in said feed gas is changed at least twice.

Claim 47

A process in accordance with claim 42 wherein: the flow rate of said off gases is monitored; and the depth d of said hot zone is determined in accordance with the equations: ##EQU7## where y is the depth from the rubble surface to the bottom of said hot zone; x is the depth from the rubble surface to the top of said hot zone; v f1 is the velocity of a first feed gas condensation front passing through said spent oil shale in response to the first change in the proportion of air and steam in said feed gas; v o1 is the velocity of a first off gas condensation front passing through said raw oil shale in response to said first change; v f2 is the velocity of a second feed gas condensation front passing through said spent oil shale in response to the second change in the proportion of air and steam in said feed gas; v o2 is the velocity of a second off gas condensation front passing through said raw oil shale in response to said second change; t 1 is the transient response time of said off gas temperature in response to said first change; t 2 is the transient response time of said off gas temperature in response to said second change; L is the overall length of said retort; H is the heat of vaporization of said steam; S f is the flow rate of said feed gas; m s is the bulk density of said spent shale; c s is the heat capacity of said spent shale; T f1 is the saturation temperature of the feed gas prior to said first change; T f2 is the saturation temperature of said feed gas after said first change; T f3 is the saturation temperature of said feed gas after said second change; S g is the flow rate of said off gases; m r is the bulk density of said raw oil shale; c r is the heat capacity of said raw oil shale; T o1 is the saturation temperature of said off gases prior to said first change; T o2 is the saturation temperature of said off gases after said first change; and T o3 is the saturation temperature of said off gases after said second change.