Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
234 words
In a urea synthesis process wherein fluid NH 3 , fluid CO 2 and an aqueous solution comprising ammonium carbamate are contacted at elevated pressure and elevated temperature to form a total urea synthesis mixture in a urea synthesis reactor to form urea, the improvement which comprises charging reactor feed streams of fluid NH 3 , fluid CO 2 and an aqueous solution comprising ammonium carbamate to a lower portion of said reactor having an indirect heat exchange means positioned therein which extends from the lower portion to the upper portion of the reactor, said heat exchange means including a heat exchange medium and including a first header positioned in the upper portion of the reactor, a second header positioned in the lower portion of the reactor and conduit means in said reactor interconnecting said headers for passing heat exchange medium therebetween, imparting heat of reaction of said NH 3 , CO 2 and ammonium carbamate mixture to said heat exchange medium in said second header at the lower portion of said reactor, and passing the resulting reaction mixture and said heat exchange medium to the upper portion of said reactor, said heat exchange medium being so passed through said conduit means to said first header, whereby heat of said heat exchange medium is transferred to said reaction mixture as it is passed from the lower portion to the upper portion of said reactor.
Claim 2
Dependent Claim
234 words
In a urea synthesis process wherein fluid NH 3 , fluid CO 2 and an aqueous solution comprising ammonium carbamate are contacted at elevated pressure and elevated temperature to form a total urea synthesis mixture in a urea synthesis reactor to form urea, the improvement which comprises charging reactor feed streams of fluid NH 3 , fluid CO 2 and an aqueous solution comprising ammonium carbamate to a lower portion of said reactor having an indirect heat exchange means positioned therein which extends from the lower portion to the upper portion of the reactor, said heat exchange means including a heat exchange medium and including a first header positioned in the upper portion of the reactor, a second header positioned in the lower portion of the reactor and conduit means in said reactor interconnecting said headers for passing heat exchange medium therebetween, imparting heat of reaction of said NH 3 , CO 2 and ammonium carbamate mixture to said heat exchange medium in said second header at the lower portion of said reactor, and passing the resulting reaction mixture and said heat exchange medium to the upper portion of said reactor, said heat exchange medium being so passed through said conduit means to said first header, whereby heat of said heat exchange medium is transferred to said reaction mixture as it is passed from the lower portion to the upper portion of said reactor.
Claim 3
Dependent Claim
29 words
The process of claim 1, wherein said header positioned in the upper portion of the reactor contains means for supplying said heat exchange medium to said heat exchange means.
Claim 4
Dependent Claim
22 words
The process of claim 1, wherein said second header contains means for removing said heat exchange medium from said heat exchange means.
Claim 5
Dependent Claim
30 words
The process of claim 1, wherein the heat exchange medium is subsequently passed downwardly to the lower portion of the heat exchange means inside the reactor whereby it is reheated.
Claim 6
Dependent Claim
37 words
The system of claim 1, wherein spent heat exchange medium is removed from the first header of the heat exchange means and is returned to the second header of the heat exchange by means outside the reactor.
Claim 7
Dependent Claim
34 words
The process of claim 1, wherein spent heat exchange medium is removed from the first header and from the reactor and fresh heat exchange medium is charged to the second header within the reactor.
Claim 8
Dependent Claim
37 words
The process of claim 1, wherein the NH 3 to CO 2 molar ratio of the total urea sythesis mixture formed in the lower portion of said reactor is from about 2.8 to about 7 to 1.