1. A communication method for a communication system in which a plurality of electronic apparatuses are connected via a digital bus configured for transferring isochronous communication packets labeled with channel numbers and asynchronous communication packets in a certain communication cycle, wherein information signals are transmitted on said isochronous communication packets and control signals are transmitted on said asynchronous communication packets, and wherein each of said electronic apparatuses have digital output plugs which output said isochronous communication packets or digital input plugs which input said isochronous communications packets, said method comprising the steps of:
controlling said digital output plugs implemented as registers to which respective addresses are allocated at a transmitting apparatus, wherein the register for said digital output plug includes a channel number field indicating a channel number;
controlling said digital input plugs implemented as registers to which respective addresses are allocated at a receiving apparatus, wherein the register for said digital input plug includes a channel number field indicating a channel number;
using a first counter included in the digital output plug control register at a transmitting apparatus to protect connections with receiving apparatuses;
using a second counter included in the digital input plug control register at a receiving apparatus to protect connections with transmitting apparatuses;
transmitting said information signals from one digital output plug at the transmitting apparatus onto one channel; and
receiving said information signals on said one channel at each of digital input plugs in a plurality of receiving apparatuses.
2. The communication method according to claim 1, wherein said registers include information indicating whether or not said information signals can be transmitted or received.
3. The communication method according to claim 1, wherein said registers include information relating to a data rate.
4. The communication method according to claim 1, wherein said registers include information relating to a band.
5. The communication method according to claim 1, wherein said digital bus is an IEEE 1394 bus.
The claims below are in addition to those above.
All refrences to claim(s) which appear below refer to the numbering after this setence.
1. A method of recovering hydrocarbonaceous and other products from oil or tar sands, comprising the steps of:
forming a hole in a body of oil or tar sand;
positioning an apertured sleeve within the hole to minimize fill-in of the sand;
positioning a gas inlet conduit into the apertured sleeve;
heating and pressurizing a processing gas;
introducing the processing gas into the sleeve through the gas inlet conduit, such that the heated, pressurized processing gas penetrates into the sand through the apertures, thereby converting bitumen within the sand into hydrocarbonaceous products;
withdrawing the processing gas and hydrocarbonaceous products as effluent gas through the hole;
performing one or more initial condensation steps to recover and store crude oil products from the effluent gas; and
performing one or more subsequent condensation steps to recover and store additional liquefied products from the effluent gas.
2. The method of claim 1, wherein the apertured sleeve is installed in sections into the hole as the hole is formed.
3. The method of claim 1, wherein the apertures in the sleeve are holes with a circular or other geometry or elongate cuts.
4. The method of claim 1, wherein the apertures in the sleeve are elongate cuts oriented more vertically than horizontally.
5. The method of claim 1, further including a mesh screen between the apertured sleeve and the body of oil or tar sand.
6. The method of claim 1, wherein the step of performing one or more subsequent condensation steps includes the recovery and storage of one or more of the following additional products:
liquefied ethane,
liquefied propane,
liquefied butane,
liquefied carbon dioxide,
liquefied methane,
liquefied nitrogen, and
hydrogen.
7. The method of claim 1, including the steps of:
burning a fuel that produces an exhaust gas and heat within a heat exchanger; and
routing the exhaust gas through the heat exchanger to create the processing gas.
8. The method of claim 1, including the steps of:
burning a fuel that produces an exhaust gas and heat within a heat exchanger;
mixing at least one of the additional products with the exhaust gas; and
routing the mixture through the heat exchanger to create the processing gas.
9. The method of claim 1, including the step of controlling the composition of the processing gas is oxygen-deprived.
10. The method of claim 1, including the step of controlling the composition of the processing gas so that it contains approximately 1% oxygen or less.
11. The method of claim 1, further including the step of maintaining the effluent gas under a negative pressure from the hole and through the initial and subsequent condensation steps.
12. The method of claim 1, including the steps of:
performing the subsequent condensation steps in at least one cooled chamber having an input and an output; and
providing a compressor system at the output of the cooled chamber to maintain the effluent gas at a negative pressure from the hole and through the initial and subsequent condensation steps.
13. The method of claim 1, including the step of performing the subsequent condensation steps in at least one cooled chamber having an input, an output, and a plurality of critical orifices sized to recover the other products.
14. The method of claim 1, wherein:
one of the other products is liquid carbon dioxide; and
the subsequent condensation steps are performed in a chamber cooled with the liquid carbon dioxide.
15. The method of claim 1, wherein:
one of the other products is liquid carbon dioxide; and
the subsequent condensation steps are performed in a chamber cooled with the liquid carbon dioxide and including critical orifices sized to recover the other products.
16. The method of claim 1, wherein one of the other products is carbon dioxide, the method further including a carbon sequestration step wherein the carbon dioxide is delivered down the hole following the recovery of the hydrocarbonaceous products.
17. The method of claim 1, further including the steps of:
forming a plurality of holes, each with a gas inlet to receive a heated and pressurized processing gas;
withdrawing the processing gas and hydrocarbonaceous products as effluent gas through each hole; and
performing a plurality of condensation steps to recover and store crude oil products and additional liquefied products from the effluent gas from a plurality of the holes.
18. The method of claim 1, wherein the crude oil is obtained as a ratio of heavy crude to lighter crudes, the method further including the step of reducing the flow rate of the processing gas to reduce the ratio.
19. The method of claim 1, wherein the crude oil is obtained as a ratio of heavy crude to lighter crudes, the method further including the step of increasing the reflux time of the heavy crude with respect to the initial condensation step to reduce the ratio.
20. The method of claim 1, including the step of adjusting one or more of the following parameters to vary the recovery of crude oil, other products or contaminants from the effluent gas:
the temperature, pressure or flow rate of the processing gas,
the residency time of the processing gas in the hole,
the reflux time of the crude oil with respect to the initial condensation step.
21. A system for recovering hydrocarbonaceous and other products from a hole formed in oil or tar sand, the system comprising:
a combustor for heating and pressurizing a processing gas;
an apertured sleeve disposed within the hole to minimize fill-in of the sand;
a gas inlet conduit for introducing the processing gas into the sleeve to convert bitumen in the sand into hydrocarbonaceous products;
a gas outlet conduit for withdrawing the processing gas and hydrocarbonaceous products from the hole;
an initial condenser system for recovering crude oil products from the effluent gas;
one or more tanks for storing the recovered crude oil products;
a subsequent condenser system for recovering additional liquefied products from the effluent gas; and
one or more tanks for storing the additional liquefied products.
22. The system of claim 21, wherein the apertured sleeve is provided in sections as the hole is formed.
23. The system of claim 21, wherein the apertures in the sleeve are holes with a circular or other geometry or elongate cuts.
24. The system of claim 21, wherein the apertures in the sleeve are elongate cuts oriented more vertically than horizontally.
25. The system of claim 21, further including a mesh screen between the apertured sleeve and the body of oil or tar sand.
26. The system of claim 21, wherein:
the combustor that produces an exhaust gas, further including:
a heat exchanger heated by the combustor; and
piping configured to route at least a portion of the exhaust gas through the heat exchanger to produce the processing gas.
27. The system of claim 21, wherein:
the combustor that produces an exhaust gas, further including:
a heat exchanger heated by the combustor;
piping configured to route at least a portion of the exhaust gas through the heat exchanger; and
one or more conduits for mixing at least one of the additional products with the exhaust gas to produce the processing gas.
28. The system of claim 21, further including a compressor for maintaining the effluent gas under a negative pressure from the hole and through the condenser systems.
29. The system of claim 21, wherein the subsequent condenser system includes:
a cooled chamber; and
a plurality of conduit loops within the chamber, each followed by a critical orifice, each loop and following critical orifice being physically configured to condense one of the additional products:
liquefied ethane,
liquefied propane,
liquefied butane,
liquefied carbon dioxide,
liquefied methane,
liquefied nitrogen, and
hydrogen.
30. The system of claim 21, wherein the subsequent condenser system includes:
a cooled chamber;
a plurality of conduit loops within the chamber, each followed by a critical orifice, each loop and following critical orifice being physically configured to condense a different one of the additional products; and
wherein one of the additional products is liquefied carbon dioxide which is used to cool the chamber.
31. The system of claim 21, further including:
a plurality of gas inlet conduits, each situated in a separately drilled hole;
a plurality of gas outlet conduits, each withdrawing the processing gas and hydrocarbonaceous products as effluent gas through a respective one of the holes; and
wherein the condenser systems are fed by a plurality of the gas outlet conduits.