초록 ▼

A downflow heat exchanger, particularly applicable as the main condenser/reboiler of a double column cryogenic air separation plant, wherein liquid distribution for uniform flow is carried out above the vapor passages and the well distributed liquid is passed into the liquid passages, preferably ang

A downflow heat exchanger, particularly applicable as the main condenser/reboiler of a double column cryogenic air separation plant, wherein liquid distribution for uniform flow is carried out above the vapor passages and the well distributed liquid is passed into the liquid passages, preferably angularly onto the bridge fins, and then down through the liquid passages cocurrently with vapor in adjacent vapor passages.

대표청구항 ▼

A method for vaporizing a liquid by indirect heat exchange with a vapor comprising: (A) providing a heat exchanger having at least one first passage and at least one second passage in alternating sequence; (B) passing liquid into said first passage(s) and down through said first passage(s) through a

A method for vaporizing a liquid by indirect heat exchange with a vapor comprising: (A) providing a heat exchanger having at least one first passage and at least one second passage in alternating sequence; (B) passing liquid into said first passage(s) and down through said first passage(s) through a section comprising means for achieving a well distributed flow of liquid which is a two stage distribution enhancement means comprising an upper section of perforated hardway fins and a lower section of perforated hardway fins with a gap between the upper and lower sections wherein the perforation area of the hardway fins in the upper section is within the range of from 2 to 15 percent of the hardway fin area in said upper section and the perforation area of the hardway fins in the lower section is within the range of from 20 to 30 percent of the hardway fin area in said lower section; (C) passing said well distributed liquid from said first passage(s) into said second passage(s) at an angle within the range of from 30 to 60 degrees from horizontal onto bridge fins located within said second passage(s); (D) passing vapor into said first passage(s) below the point where said well distributed liquid is passed from said first passage(s); and (E) passing vapor and liquid cocurrently through said first and second passages respectively and vaporizing said liquid in said second passage(s) by indirect heat exchange with said vapor in said first passage(s) during said cocurrent flow.