Vertical tube heat exchanger and method for exchanging heat

Patent metadata

Field	Value
Publication number	US-2019264983-A1
Application number	US-201716321346-A
Country	US
Kind code	A1
Filing date	Jul 26, 2017
Priority date	Jul 29, 2016
Publication date	Aug 29, 2019
Grant date	—

Abstract

A tube heat exchanger extending in a vertical direction, comprising:
a first chamber including a lower portion provided with at least one intake inlet for a diphasic fluid including a liquid and a first vapor containing a mist; an upper portion; and a first recovery member passed through by the first vapor and recovering the mist in liquid form, the first vapor next arriving in the upper portion, a central chamber forming liquid films running over the tubes and vaporizing at least partially to produce a second vapor, the tubes being traveled inwardly by a fluid hotter than the diphasic fluid, and a second chamber receiving the first vapor and the second vapor to form a third vapor, and including an outlet for the non-vaporized liquid and an outlet for the third vapor, the first chamber and the second chamber together forming a volume surrounding the central chamber around the vertical direction.

First claim

1 . A heat exchanger having tubes intended to extend substantially in a vertical direction, the exchanger comprising:
a first chamber including
a lower portion provided with at least one intake inlet for a diphasic fluid including at least one liquid and a first vapor containing a mist,
an upper portion, and
a first recovery member suitable for being passed through by the first vapor and for recovering the mist in the form of a liquid phase returned toward the lower portion, the first vapor next arriving in the upper portion,
a central chamber including the tubes and being suitable for being supplied with said liquid from a liquid bath situated in the lower portion of the first chamber and for forming liquid films running over outer faces of the tubes and vaporizing at least partially to form a second vapor, the tubes being traveled inwardly by a fluid hotter than the diphasic fluid, and a second chamber provided to cover the first vapor coming from the upper portion of the first chamber and the second vapor, and to form a third vapor, the second chamber including at least one outlet for the non-vaporized liquid, and at least one outlet for the third vapor, the first chamber and the second chamber together forming a volume surrounding the central chamber around the vertical direction.

2 . The heat exchanger according to claim 1 , wherein, in section in a horizontal plane:
the first chamber and the second chamber are delimited radially outwardly by outer enclosures forming a circle, the first chamber is radially inwardly delimited by an inner enclosure forming a circle portion.

3 . The heat exchanger according to claim 1 , wherein:
the first recovery member forms a substantially horizontal plate separating the lower portion and the upper portion of the first chamber, and/or the optional second recovery member forms, in section in a horizontal plane, a circle portion and radially outwardly delimits a part of the central chamber.

4 . The heat exchanger according to claim 1 , wherein:
the first chamber is radially inwardly delimited by a tight inner enclosure suitable for separating the liquid bath and the central chamber, the first chamber including at least one channel suitable for plunging into the liquid bath and for fluidly connecting the liquid bath to an inlet of the central chamber, or the exchanger comprises a compressor for raising liquid from the liquid bath toward an inlet of the central chamber.

5 . The heat exchanger according to claim 1 , wherein the central chamber comprises one or several substantially horizontal plates suitable for distributing the liquid among the tubes and forming the liquid films, the plates defining passage orifices passed through by the tubes.

6 . The heat exchanger according to claim 5 , wherein the central chamber includes at least one grid holding at least some of the tubes, the exchanger including cups fastened on the tubes in question to recover the liquid films disrupted by the holding grid, each cup defining a passage orifice to form a new liquid film.

7 . The heat exchanger according to claim 1 , wherein the central chamber comprises a liquid collector to receive the liquid, and additional hoses extending from the liquid collector downward and being suitable for inwardly receiving the liquid and forming liquid jets toward the tubes.

8 . An assembly comprising several heat exchangers according to claim 1 , the heat exchangers being superimposed in the vertical direction.

9 . The assembly according to claim 8 , wherein the heat exchangers have outer enclosures suitable for defining fixed relative positions of the heat exchangers with respect to one another once superimposed.

10 . A heat exchange method implementing tubes extending substantially in a vertical direction, the method comprising:
providing a central chamber including the tubes, as well as a first chamber and a second chamber together forming a volume surrounding the central chamber around the vertical direction, allowing, into a lower portion of the first chamber, a diphasic fluid including at least one liquid and a first vapor containing a mist, crossing, by the first mist, of a first recovery member to recover the mist in the form of a liquid phase returned toward the lower portion, the first mist next arriving in an upper portion of the first chamber, supplying said liquid to the central chamber from a liquid bath situated in the lower portion of the first chamber, forming liquid films running over outer faces of the tubes and vaporizing at least partially to form a second vapor, the tubes being traveled inwardly by a fluid hotter than the diphasic fluid, receiving, in the second chamber, the first vapor coming from the upper portion of the first chamber and the second vapor, and forming a third vapor, removing non-vaporized liquid via at least one outlet of the second chamber, and removing third vapor via at least one outlet of the second chamber, and optionally, crossing of a second recovery member, situated in the second chamber, by the second vapor and recovery of a mist contained in the second vapor.

11 . The heat exchanger according to claim 1 , wherein the second chamber includes a second recovery member suitable for being passed through by the second vapor and recovering a mist contained in the second vapor.

12 . The heat exchanger according to claim 2 , wherein:
the outer enclosures is semicircular, and said circle portion is a semicircle.

13 . The heat exchanger according to claim 5 , wherein the central chamber includes sleeves containing a metal foam, the sleeves extending radially between the tubes and the plate(s) to homogenize each liquid film.

14 . The heat exchanger according to claim 6 , wherein the central chamber includes secondary sleeves containing a metal foam, each secondary sleeve extending radially between one of the tubes in question and one of the cups to homogenize the new liquid film.

15 . The heat exchanger according to claim 7 , wherein the additional hoses include a helical outer structure around the vertical direction forming fins suitable for recovering the liquid jets, the liquid films running over the outer structure.

16 . The assembly according to claim 8 , further including a system of cascading channels to connect the heat exchangers to one another.

Assignees

• Technip France

Inventors

• Rambure Nicolas

Classifications

• F28D7/16

  the conduits being arranged in parallel spaced relation ({F28D7/0008 - F28D7/0058 take precedence}; F28D7/02 - F28D7/10 take precedence) · CPC title

• F25J2250/04

  Down-flowing type boiler-condenser, i.e. with evaporation of a falling liquid film · CPC title

• F28D2021/0064

  Vaporizers, e.g. evaporators · CPC title

• F28D7/0091 Primary

  the supplementary medium flowing in series through the units · CPC title

• F28F25/085

  Substantially horizontal grids; Blocks · CPC title