Multitubular rotary heat exchanger

Patent metadata

Field	Value
Publication number	US-2021048254-A1
Application number	US-201916981407-A
Country	US
Kind code	A1
Filing date	Mar 15, 2019
Priority date	Apr 2, 2018
Publication date	Feb 18, 2021
Grant date	—

Abstract

A multitubular rotary heat exchanger has a stationary shielding unit. The shielding unit is positioned in close proximity to a tube plate outside a heating or cooling region. A stationary surface of the shielding unit is positioned in opposition to and in close proximity to an end opening of a heat transfer tube moving in an upper zone of the heating or cooling region, thereby transiently reducing or restricting the flow rate of the thermal medium fluid flowing through the heat transfer tube moving in the upper zone.

First claim

1 . A multitubular rotary heat exchanger having a rotatable shell, tube plates closing both end portions of the shell, and a number of heat transfer tubes disposed in an inner space of the shell, wherein a heating or cooling region for heating or cooling a processed matter introduced into the inner space is formed in the shell, each end portion of each of said tubes is carried by the tube plate, and the end portion of the tube is open on an outside surface of the tube plate or in its vicinity, and wherein the shell, the tube plates, and the tubes are rotated as a whole to heat or cool the processed matter by heat exchange between the thermal medium fluid in the tubes and the processed matter in the heating or cooling region, comprising:
a stationary shielding unit for transiently reducing a flow rate of the thermal medium fluid flowing through said heat transfer tube while the tube moves in an upper zone of said heating or cooling region, wherein said shielding unit is positioned in the vicinity of said tube plate outside said heating or cooling region and is provided with a stationary surface which restricts or limits a flow of said thermal medium fluid induced into an end opening of the tube or the fluid effluent therefrom, and wherein said stationary surface is in close proximity to and in opposition to said end opening of the tube moving in said upper zone and is separated apart from the end opening of the tube moving in a lower zone of said heating or cooling region.

2 . The heat exchanger as defined in claim 1 , wherein said shielding unit is located in a space on a thermal medium inflow side of said tube plate in close proximity to said end opening of the heat transfer tube on the inflow side, and/or the unit is located in a space on a thermal medium outflow side of the tube plate in close proximity to the end opening of the tube on the outflow side.

3 . The heat exchanger as defined in claim 1 , wherein said shielding unit is configured by a sectorial or semi-circular shielding plate, or the unit is an assembly of the sectorial shielding plates connected to each other, and wherein said upper zone is a space which opposes to an accumulation of the processed matter deviated on one side of said region under an action of rotation of said shell and which is deviated on a side opposite to the accumulation with respect to a vertical center plane of the shell.

4 . The heat exchanger as defined in claim 1 , further comprising a mounting mechanism for mounting said shielding unit in the vicinity of said tube plate in a positionally adjustable manner.

5 . The heat exchanger as defined in claim 1 , wherein said shielding unit is a sectorial or semi-circular assembly of the sectorial shielding plates integrally connected to each other, and wherein the assembly is provided with a shielding angle adjusting mechanism for changing a center angle of the unit by adjusting an overlapping angle of the adjacent shielding plates.

6 . The heat exchanger as defined in claim 1 , wherein said shielding unit has an area or size for shielding a number of the end openings of the heat transfer tubes, the number of which is set to be in a range from 20% of the total number of the tubes to 50% thereof.

7 . The heat exchanger as defined in claim 1 , wherein a flow rate of the thermal medium fluid of said tube reduced by said shielding unit is set to be equal to or smaller than one-fifth of the flow rate of the fluid of the tube in heat transfer contact with the processed matter.

8 . The heat exchanger as defined in claim 1 , wherein a distance between said shielding unit and said end opening is set to be in a range between one-tenth of a diameter of the end opening and 1.0 times thereof.

9 . A system for treating calcined gypsum comprising said heat exchanger as defined in claim 1 , wherein the heat exchanger is used as an agitation-type cooler for cooling the calcined gypsum, the cooler has a cooling region for cooling the calcined gypsum which functions as said heating or cooling region, and said tube is open to atmosphere at its end portion on a thermal medium inflow side, thereby permitting outdoor atmospheric air to flow through an intratubular fluid passage of the tube as a cooling medium.

10 . The system as defined in claim 9 further comprising a moisture supplying device for incorporating moisture into the calcined gypsum, wherein the moisture supplying device is provided with a humid gas supply port which introduces a spouting flow or delivery flow of a humid gas containing an amount of water content or steam, into said cooling region.

11 . A heating or cooling method for heating or cooling a processed matter with use of a multitubular rotary heat exchanger having a rotatable shell closed at its both end portions by tube plates and a number of heat transfer tubes disposed in an inner space of the shell, wherein a heating or cooling region for heating or cooling the processed matter fed to the inner space is formed in the shell; wherein each end portion of each of said tubes is carried by the tube plate, and the end portion is open on an outside surface of the tube plate or in its vicinity; and wherein the shell, the plates, and the tubes are rotated as a whole to heat or cool the processed matter by heat exchange between the thermal medium fluid in the tubes and the processed matter in the heating or cooling region, comprising:
positioning a stationary surface of a shielding unit in the vicinity of said tube plate outside said heating or cooling region so as to be in close proximity to and in opposition to an end opening of the tube moving in an upper zone of said heating or cooling region, for restricting or limiting a flow rate of said thermal medium fluid introduced into said end opening of the tube moving in the upper zone or the fluid effluent therefrom, and separating said surface apart from the said end opening of the tube moving in a lower zone of said heating or cooling region, for releasing said restriction or limitation of the flow rate of the thermal medium fluid.

12 . The method as defined in claim 11 , wherein said shielding unit is located in a space on a thermal medium inflow side of said tube plate in close proximity to the end opening of the heat transfer tube on the inflow side, and/or the unit is located in a space on a thermal medium outflow side of the tube plate in close proximity to an end opening of the tube on the outflow side.

13 . The method as defined in claim 11 , wherein said upper zone is a space which opposes to an accumulation of the processed matter deviated on one side of said region under an action of rotation of said shell and which is deviated on a side opposite to the accumulation, and wherein said shielding unit is configured by a sectorial or semi-circular shielding plate, or the unit is an assembly of the sectorial shielding plates connected to each other.

14 . The method as defined in claim 11 , wherein said shielding unit is mounted in the vicinity of said tube plate in a positionally adjustable manner.

15 . The method as defined in one of claim 11 , wherein said shielding unit is an assembly constituted from the sectorial shielding plates integrally connected to each other, and wherein the assembly is provided with a shielding angle adjusting mechanism for changing a center angle of the unit by adjusting an overlapping angle of the adjacent shielding plates.

16 . The method as defined in one of claim 11 , wherein said shielding unit shields a number of the end openings of the heat transfer tubes, the number of which is set to be in a range from 20% of the total number o

Assignees

• Yoshino Gypsum Co

Inventors

• Yoshida Tomonori
• Takenaka Takeshi

Classifications

• F27D17/10

  Arrangements for using waste heat · CPC title

• F27B7/36 Primary

  Arrangements of air or gas supply devices · CPC title

• F27B2007/041

  Longitudinal tubes · CPC title

• F27B7/38

  Arrangements of cooling devices · CPC title

• F27B7/04

  with longitudinal divisions · CPC title