Energy cogeneration system

Claim 3

A method of controlling an energy cogeneration system according to claim 1 wherein there are a plurality of said processing means communicating with said header to have steam furnished by said supply means distributed thereto; said step of monitoring the requirements of said processing means includes monitoring the individual requirements of each of said processing means; and said step of changing the pressure under which steam is delivered to said header includes changing said pressure to correspond more closely to that required by the processing means having the greatest requirement at said given time for steam.

Claim 4

A method of controlling an energy cogeneration system according to claim 2 wherein said means of said system to convert heat energy contained in steam to mechanical energy is an extraction turbine and wherein at least two of said headers are provided respectively having a plurality of processing means communicated therewith, one of which headers is communicated with the exhaust outlet of said turbine to receive steam at a relatively low pressure for distribution to a plurality of said processing means having requirements for steam at varying pressures no greater than said relatively low pressure and the other of which is communicated with an extraction outlet of said turbine to receive steam at an intermediate pressure for distribution to a plurality of said processing means having requirements for steam at varying pressures no greater than said intermediate pressure; and said step of changing the pressure under which steam is delivered to said header includes changing the pressure under which steam is delivered to each of said headers to a pressure which more closely corresponds to that steam pressure needed at any given time to furnish the steam required by the respective one of the processing means communicated therewith having the greatest requirements at said given time for steam.

Claim 5

A method of controlling an energy cogeneration system according to claim 3 wherein said step of changing the pressures under which steam is delivered to said headers includes the step of modelling the cogeneration system to optimize the set point control settings thereof consistent with said model.

Claim 6

A method of controlling an energy cogeneration system according to claim 3 wherein each of said processing means includes a pressure reduction valve communicating the same with its associated header, and said step of monitoring the requirements of each of said processing means for steam at any given time includes the step of monitoring the degree to which the pressure reduction valve associated with each of said processing means is throttling flow therethrough.

Claim 7

An energy cogeneration system comprising: means to supply steam under pressure; means to convert to mechanical energy, heat energy contained in steam furnished by said supply means; a header for distributing steam from said supply means under pressure to at least one processing means having a need which varies over time for steam; means to monitor the requirements of said processing means for steam distributed by said header; and means responsive to said monitoring means by changing the pressure under which steam is delivered to said header to a pressure which more closely corresponds to that steam needed at any given time to furnish the steam required by said processing means, whereby the steam furnished by said supply means not required by said processing means is available for other uses, including use by said means to convert heat energy to mechanical energy.

Claim 8

An energy cogeneration system comprising: means to supply steam under pressure; means to convert to mechanical energy, heat energy contained in steam furnished by said supply means; a header for distributing steam from said supply means under pressure to at least one processing means having a need which varies over time for steam; means to monitor the requirements of said processing means for steam distributed by said header; and means responsive to said monitoring means by changing the pressure under which steam is delivered to said header to a pressure which more closely corresponds to that steam needed at any given time to furnish the steam required by said processing means, whereby the steam furnished by said supply means not required by said processing means is available for other uses, including use by said means to convert heat energy to mechanical energy.

Claim 9

An energy cogeneration system according to claim 6 wherein there are a plurality of said processing means communicating with said header to have steam furnished by said supply means distributed thereto; said means to monitor the requirement of said processing means for steam distributed by said header includes means to monitor the individual requirements of each of said processing means; and said means responsive to said monitoring means by changing the pressure under which steam is delivered to said header changes said pressure to correspond more closely to that required by the processing means having the greatest requirement at said given time for steam.

Claim 10

An energy cogeneration system according to claim 7 wherein said means responsive to said monitoring means by changing the pressure under which steam is delivered to said header to a pressure more closely corresponding to that steam pressure required by the processing means having said greatest requirement at said given time changes said pressure to approximate that required by said processing means.

Claim 11

An energy cogeneration system according to claim 7 wherein each of said processing means includes a pressure reduction valve communicating the same with said header, and said means to monitor the requirements of each of said processing means for steam at any given time monitors the degree to which its associated pressure reduction valve is throttling flow therethrough.

Claim 12

An energy cogeneration system according to claim 6 wherein said means to convert to mechanical energy, heat energy contained in steam furnished by said supply means is an extraction turbine; and wherein at least two of said headers are provided, one of which is communicated with the exhaust outlet of said turbine to receive steam at a relatively low pressure for distribution to a processing means having a requirement for steam at varying pressures no greater than said relatively low pressure and the other of which is communicated with an extraction outlet of said turbine to receive steam at an intermediate pressure for distribution to a processing means having a requirement for steam at varying pressures no greater than said intermediate pressure; and said means responsive to said monitoring means by changing the pressure under which steam is delivered to said header changes the pressure under which steam is delivered to said respective headers to a pressure which more closely corresponds to that steam pressure needed at any given time to furnish the steam required by the respective processing means.

Claim 13

An energy cogeneration system according to claim 10 wherein each of said processing means includes a pressure reduction valve communicating the same with said header, and said means to monitor the requirements of each of said processing means for steam at any given time monitors the degree to which its associated pressure reduction valve is throttling flow therethrough.

Claim 14

An energy cogeneration system according to claim 10 wherein there are a plurality of said processing means communicating with each of said headers to have steam furnished by said supply means distributed thereto; said means to monitor the requirement of said processing means for steam distributed by said headers includes means to monitor individually the steam requirements of each of said processing means communicated with each of said headers, and said means responsive to said monitoring means by changing the pressure under which steam is delivered to said headers changes said pressures to pressures which more closely correspond to those needed at any given time to furnish the steam required by the respective processing means communicated with each of said headers having the greatest requirement at said given time for steam.

Claim 15

An energy cogeneration system according to claim 12 wherein said means responsive to said monitoring means by changing the pressure under which steam is delivered to said headers includes means to model said cogeneration system to optimize the set point control settings thereof consistent with said model.