US2011185733A1PendingUtilityA1

System and method for equilibrating an organic rankine cycle

Assignee: UNITED TECHNOLOGIES CORPPriority: Jan 29, 2010Filed: Jan 29, 2010Published: Aug 4, 2011
Est. expiryJan 29, 2030(~3.5 yrs left)· nominal 20-yr term from priority
F01K 13/02F01K 25/08
44
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Claims

Abstract

Embodiments of an ORC system can be configured to reduce ingress of contaminants from the ambient environment. In one embodiment, the ORC system can comprise a pressure equilibrating unit that comprises a variable volume device for holding a working fluid. The variable volume device can be fluidly coupled to a condenser so that working fluid can move amongst the condenser and the variable volume device. This movement can occur in response to changes in the pressure of the working fluid in the ORC system, and in one example the working fluid is allowed to move when the pressure deviates from atmospheric pressure.

Claims

exact text as granted — not AI-modified
1 . A system operating as an Organic Rankine Cycle system in an ambient environment, said system comprising:
 an integrated system having in serial flow relationship a pump, a vapor generator, a turbine, and a condenser; and   a variable volume device having volume in fluid communication with the condenser,   wherein the volume changes from a first volume to a second volume in response to a change in the pressure of the integrated system.   
     
     
         2 . A system according to  claim 1 , wherein the variable volume device is directly coupled to the condenser. 
     
     
         3 . A system according to  claim 1 , further comprising a valve unit coupled to the condenser and the variable volume device, wherein the valve unit changes amongst a plurality of states in response to the change in pressure, and wherein the volume changes from the first volume to the second volume in response to the change in the state of the valve unit. 
     
     
         4 . A system according to  claim 1 , wherein the volume change results from a drop in the pressure of the integrated system below a set point pressure. 
     
     
         5 . A system according to  claim 4 , wherein the set point pressure is about the pressure of the ambient environment. 
     
     
         6 . A system according to  claim 1 , wherein the variable volume device comprises a bellows that receives the condensed working fluid therein, and wherein the bellows comprises a flexible material that expands to accommodate at least one of the first volume and the second volume. 
     
     
         7 . A system according to  claim 1 , further comprising in-line with the condenser and the variable volume device:
 a pressure equalization valve responsive to the change in pressure; and   a flow control valve responsive to a volume limit for the variable volume device,   wherein the volume limit is a function of the amount of condensed working fluid in the variable volume device.   
     
     
         8 . A system according to  claim 7 , wherein the volume limit comprises a minimum volume limit and a maximum volume limit. 
     
     
         9 . A method of equilibrating the pressure of a system for performing an Organic Rankine Cycle, said method comprising:
 integrating in serial flow relation a pump, a vapor generator, a turbine, and a condenser;   coupling in fluid communication a variable volume device to the condenser;   changing the amount of condensed working fluid in the variable volume device in response to a change in the pressure of said system.   
     
     
         10 . A method according to  claim 9 , further comprising flowing the working fluid between the condenser and the variable volume device through a valve unit, wherein the change in pressure causes the valve unit to actuate from a first state to a second state, and wherein the amount of condensed working fluid in the variable volume device in the first state is less than the amount of condensed working fluid in the variable volume device in the second state. 
     
     
         11 . A method according to  claim 10 , wherein pressure in the second state is less than a set point pressure, and wherein the set point pressure is at least about atmospheric pressure. 
     
     
         12 . A method according to  claim 9 , further comprising:
 measuring the amount of condensed working fluid in the variable volume device; and   metering the flow of the condensed working fluid from the variable volume device based on the amount of the condensed working fluid.   
     
     
         13 . A method according to  claim 12 , wherein the condensed working fluid flows through a flow control valve, and wherein the flow control valve is responsive to a control that identifies the amount. 
     
     
         14 . A method according to  claim 13 , wherein the amount comprises a minimum volume limit and a maximum volume limit. 
     
     
         15 . A method according to  claim 9 , wherein the variable volume device comprises a bellows that expands to accommodate the amount of condensed working fluid in the variable volume device.

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