TF03      770030005P126Third Revised Sheet No. 77
TF04                Second Revised Sheet No. 77
TF05Edward C. McMurtrie, Vice President/General Manager
TF06100506                          110506
                       GENERAL TERMS AND CONDITIONS
                                (Continued)


4.	OPERATING PROCEDURES (Continued)

	4.7	Operating Procedures for Rate Schedule LGS-1 Service: 
		(Continued)
	    
	    		b.  The original owner and the new owner will 
	    		    confirm such transfer of ownership in writing 
	    		    within three (3) days, and will provide Paiute 
	    		    with a copy of such documentation.
	    			
	    		c.  Such transfer shall be subject to the rules and 
	    		    regulations of any governmental body of competent 
	    		    jurisdiction.

		(d)	Gasification and Delivery: The actual quantity of gas to 
			be gasified and delivered from the LNG Plant at any time 
			is subject to the conditions affecting the operation of 
			Paiute's entire system at such time, as follows:

			(1)  The design gasification capacity at the LNG Plant is 
			     71,959 Dth per day. (The design gasification 
			     capacity quantity is stated in dekatherms, using an 
			     assumption that one dekatherm is equal to one Mcf of 
			     gas with a heating content of 1,028 Btu per cubic 
			     foot. It is recognized that the design gasification 
			     capacity as expressed in dekatherms may vary from 
			     time to time depending upon the actual heating 
			     content of the LNG.) Gasification at the LNG Plant 
			     may require up to ten (10) hours of warm-up time. 
			     The scheduling of LNG gasification shall be subject 
			     to such start-up period limitation.

			(2)  Paiute's LNG Plant was designed as a peaking 
			     facility to be used during the Winter Period, 
			     provided however, that Shippers may schedule 
			     gasification of LNG during other times when such 
			     gasification would not adversely affect Paiute's 
			     service obligations. The LNG Plant is designed to be 
			     in a continuous liquefaction mode for extended 
			     periods of time. It is inefficient to switch back 
			     and forth between liquefaction and gasification, 
			     therefore,