Heat exchange apparatus

Patent metadata

Field	Value
Publication number	US-2016348983-A1
Application number	US-201514723572-A
Country	US
Kind code	A1
Filing date	May 28, 2015
Priority date	May 28, 2015
Publication date	Dec 1, 2016
Grant date	—

Abstract

Heat exchange apparatus and, particularly, heat exchangers having a baffled cooling jacket are disclosed. Methods for using the exchangers including methods that involve cooling an effluent gas produced from a fluidized bed reactor for producing polycrystalline silicon are also disclosed.

First claim

What is claimed is:

1 . A heat exchange apparatus for transferring heat between a first process stream and a second process stream, the heat exchange apparatus comprising:
a shell; a tube within the shell, the tube having a vertical portion and a horizontal portion transverse to the vertical portion, the shell and tube forming an annular chamber between the shell and tube; and a baffle within the annular chamber.

2 . The heat exchange apparatus as set forth in claim 1 wherein the baffle is helical.

3 . The heat exchange apparatus as set forth in claim 2 wherein the helical baffle has an outer edge and an inner edge, the outer edge contacting the shell and the inner edge contacting the tube.

4 . The heat exchange apparatus as set forth in claim 1 wherein the vertical portion and the horizontal portion of the tube form a joint, at least one of the vertical portion and the horizontal portion of the tube comprising a substrate and a protective liner disposed on the substrate for reducing erosion at the joint.

5 . The heat exchange apparatus as set forth in claim 4 wherein the liner comprises graphite, tungsten, carbide or cobalt-chromium alloys.

6 . The heat exchange apparatus as set forth in claim 1 wherein the vertical portion of the tube comprises an upper segment and a lower segment, the upper segment and lower segment being connected by an expansion joint.

7 . The heat exchange apparatus as set forth in claim 1 comprising a single tube.

8 . The heat exchange apparatus as set forth in claim 1 wherein the shell comprises a plurality of segments, each segment having an inlet and an outlet.

9 . The heat exchange apparatus as set forth in claim 8 wherein the shell comprises a vertical segment and a horizontal segment, the horizontal portion of the tube being disposed with the horizontal segment of the shell and the vertical portion of the tube being disposed with the vertical segment of the shell.

10 . The heat exchange apparatus as set forth in claim 9 wherein the horizontal portion of the tube is a first horizontal portion and the horizontal segment of the shell is a first horizontal segment, the apparatus further comprising:
a second horizontal portion of the tube, the vertical portion of the tube being disposed between the first horizontal portion and the second horizontal portion; and
a second horizontal segment of the shell, the second horizontal portion of the tube being disposed with the second horizontal segment of the shell.

11 . The heat exchange apparatus as set forth in claim 8 wherein the vertical portion of the tube comprises an upper segment and a lower segment, the upper segment and lower segment being connected by an expansion joint, the shell comprising an upper vertical segment and a lower vertical segment, the upper vertical segment of the tube being disposed within the upper vertical segment of the shell and the lower vertical segment of the tube being disposed within the lower vertical segment of the shell.

12 . The heat exchange apparatus as set forth in claim 1 in combination with the first process stream, the first process stream passing through the annular chamber, the first process stream comprising cooling water.

13 . The heat exchange apparatus as set forth in claim 12 in combination with the second process stream, the second process stream passing through the tube, the second process stream comprising hydrogen gas.

14 . The heat exchange apparatus as set forth in claim 1 wherein the vertical portion of the tube has an aspect ratio between about 70 and about 110 and the horizontal portion of the tube has an aspect ratio between about 15 and about 45.

15 . The heat exchange apparatus as set forth in claim 1 wherein the vertical portion of the tube has an aspect ratio between about 80 and about 100 and the horizontal portion of the tube has an aspect ratio between about 20 and about 40.

16 . A method for transferring heat between two process streams by use of the heat exchange apparatus of claim 1 , the method comprising:
introducing a first process stream into the annular chamber formed between the shell and tube; and introducing a second process stream into the tube.

17 . The method as set forth in claim 16 wherein the first process stream comprises a cooling liquid.

18 . The method as set forth in claim 17 wherein the second process stream comprises the effluent gas from a fluidized bed reactor for producing polycrystalline silicon.

19 . The method as set forth in claim 16 wherein the first process stream and the second process stream are in a countercurrent arrangement as they pass through the heat exchange apparatus.

20 . A system for producing polycrystalline silicon, the system comprising:
a fluidized bed reactor for thermally decomposing a silicon-containing compound; the heat exchange apparatus as set forth in claim 1 , the tube of the heat exchange apparatus being in fluid communication with the fluidized bed reactor; a filter assembly for removing particulate fines from the effluent, the filter assembly being in fluid communication with the heat exchange apparatus.

21 . The system as set forth in claim 20 wherein the heat exchange apparatus and fluidized bed reactor each have a height and wherein the ratio of the height of the fluidized bed reactor to the height of the heat exchange apparatus is less than about 1.5.

22 . A method for producing polycrystalline silicon in the system of claim 20 , the method comprising:
introducing a feed gas comprising a thermally decomposable silicon-containing compound into the fluidized bed reactor to produce polycrystalline silicon and an effluent gas; introducing the effluent gas into the tube of the heat exchange apparatus; circulating a cooling liquid through the annular chamber of the heat exchange apparatus, the cooling liquid and effluent gas being in a countercurrent arrangement as they pass through the heat exchange apparatus to cool the effluent gas; and introducing the cooled effluent gas into the filter assembly.

Assignees

• Sunedison Inc

Inventors

• Spicka Peter
• Gupta Puneet

Classifications

• B01J8/24

  according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title

• F28D2021/0022

  for chemical reactors · CPC title

• F28D7/0091 Primary

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

• B01J8/1845

  with particles moving upwards while fluidised · CPC title

• F28D7/026

  the conduits of only one medium being helically coiled and formed by bent members, e.g. plates, the coils having a cylindrical configuration · CPC title