2021
DOI: 10.1007/s11708-021-0747-y
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Review of the LNG intermediate fluid vaporizer and its heat transfer characteristics

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Cited by 9 publications
(6 citation statements)
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“…It should be noted that the set of known and unknown variables in steady state are {Pi ss , Ps ss , Fv ss , K1 ss , K2 ss ; Ti ss } and {H ss , P ss , Ts ss } respectively. This procedure results in the establishment of the steady-state representation of the vaporizer model, defined in (9).…”
Section: And Taking Into Account That D(h(t)•t(t))/dt = T(t)•(dh(t)/d...mentioning
confidence: 99%
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“…It should be noted that the set of known and unknown variables in steady state are {Pi ss , Ps ss , Fv ss , K1 ss , K2 ss ; Ti ss } and {H ss , P ss , Ts ss } respectively. This procedure results in the establishment of the steady-state representation of the vaporizer model, defined in (9).…”
Section: And Taking Into Account That D(h(t)•t(t))/dt = T(t)•(dh(t)/d...mentioning
confidence: 99%
“…By replacing the numerical parameters and the steady-state variables of the vaporizer given in Table 4 and Table 5 respectively, and solving the equation system defined in (9), the EPs are calculated and derived as follows: H ss ≈ 50 %, P ss ≈ 18.2 kPa, and Ts ss ≈ 55.1 °C. In accordance with conventional process control practices, liquid levels are often expressed as percentages.…”
Section: And Taking Into Account That D(h(t)•t(t))/dt = T(t)•(dh(t)/d...mentioning
confidence: 99%
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