US4640339A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus for carrying out physical and/or chemical processes, more specifically a heat exchanger of the continuous type
Assignee: ESKLA BV HAARLEMMERSTRAATWEG 127 1165 MK HALFWEG NETHERLANDS A CORP OF NETHERLANDS
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Filing: 1986-01-15
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Granted: 1987-02-03
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Expires: 2006-01-15
Abstract
Abstract The invention relates to apparatus for carrying out physical and/or chemical processes, more specifically a heat exchanger (10) of the continuous type, comprising a large number of vertical heat exchanger tubes (18) mounted between a lower chamber (17) and an upper chamber (16) within a jacket (15). Within the tubes (18) small solid particles are kept in a fluidized condition by the fluid medium passing up from the lower chamber (17) through the tubes (18), so as to achieve a good heat transfer, whereas also any deposit will be removed from the inner tube walls. For the downward flow of the granular mass at least one return tube (21) is provided. Downward circulation of the fluid medium through the return tube (21) should be minimal. To stabilize the fluid bed in a riser tube the inflow pipe is provided with a lateral bore (23) and the top of the lower chamber above the level of the lateral bores (23) is fitted with an outlet 51 with a shutoff valve 52 to temporarily reduce pressure of the fluid medium at the top of the lower chamber should the lateral bores become clogged.
Inventors
- 👤 Dick G. Klaren
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 00:57
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/18; B01J8/24; B01J8/38; B01J8/384; B01J8/386; F; F28; F28D; F28D13/00; F28F; F28F19/00; F28F19/008; F28G; F28G9/00; G; G01; G01N; G01N33/00; G01N33/0091
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
216 words
Method of operation of apparatus for carrying out physical and/or chemical processes, in particular a heat exchanger of the continuous type, comprising a bundle of parallel vertical riser tubes, an upper chamber, a lower chamber, an upper pipe plate and a lower pipe plate for open connection of the pipe bundle to the upper and lower chambers respectively, a granular mass that can be kept in a fluidised condition at least in the riser tubes by a fluid medium flowing during operation upwardly through the lower chamber, the riser tubes and the upper chamber, a distribution plate for the granular mass in the lower chamber and at least one return tube with outlet below the distribution plate for return of an overflow of granules above the upper pipe plate from the upper chamber to the lower chamber, wherein each riser tube is provided with an inflow pipe element extending into the lower chamber from the lower pipe plate to a level above the distribution plate through which the return tube or tubes projects or project, and the lower chamber is provided with a device that prevents granules from reaching the lower chamber inlet for the fluid medium at standstill characterised in that the fluid medium pressure at the top of the lower chamber is temporarily reduced.
Claim 2
Dependent Claim
216 words
Method of operation of apparatus for carrying out physical and/or chemical processes, in particular a heat exchanger of the continuous type, comprising a bundle of parallel vertical riser tubes, an upper chamber, a lower chamber, an upper pipe plate and a lower pipe plate for open connection of the pipe bundle to the upper and lower chambers respectively, a granular mass that can be kept in a fluidised condition at least in the riser tubes by a fluid medium flowing during operation upwardly through the lower chamber, the riser tubes and the upper chamber, a distribution plate for the granular mass in the lower chamber and at least one return tube with outlet below the distribution plate for return of an overflow of granules above the upper pipe plate from the upper chamber to the lower chamber, wherein each riser tube is provided with an inflow pipe element extending into the lower chamber from the lower pipe plate to a level above the distribution plate through which the return tube or tubes projects or project, and the lower chamber is provided with a device that prevents granules from reaching the lower chamber inlet for the fluid medium at standstill characterised in that the fluid medium pressure at the top of the lower chamber is temporarily reduced.
Claim 3
Dependent Claim
240 words
Apparatus for carrying out physical and/or chemical processes, in particular a heat exchanger of the continuous type, comprising a bundle of parallel vertical riser tubes, an upper chamber, a lower chamber, an upper pipe plate and a lower pipe plate for open connection of the pipe bundle with the upper and lower chambers respectively, a granular mass that can be kept in a fluidised condition at least in the riser tubes by a fluid medium flowing during operation upwardly through the lower chamber, the riser tubes and the upper chamber, a distribution plate for the granular mass in the lower chamber, and at least one return tube with outlet below the distribution plate for return of an overflow of granules above the upper pipe plate from the upper chamber to the lower chamber, wherein each riser tube is provided with an inflow pipe element extending into the lower chamber from the lower pipe plate to a level above the distribution plate through which the return tube or tubes projects or project, and the lower chamber is provided with a device that prevents granules from reaching the lower chamber inlet for the fluid medium at standstill, characterised in that in the case in which the inflow pipe elements (22) are provided with lateral bores (23), the top of the lower chamber (17) is provided at a level above the lateral bores (23) level, with an outlet (51) with shutoff valve (52).
Claim 4
Dependent Claim
240 words
Apparatus for carrying out physical and/or chemical processes, in particular a heat exchanger of the continuous type, comprising a bundle of parallel vertical riser tubes, an upper chamber, a lower chamber, an upper pipe plate and a lower pipe plate for open connection of the pipe bundle with the upper and lower chambers respectively, a granular mass that can be kept in a fluidised condition at least in the riser tubes by a fluid medium flowing during operation upwardly through the lower chamber, the riser tubes and the upper chamber, a distribution plate for the granular mass in the lower chamber, and at least one return tube with outlet below the distribution plate for return of an overflow of granules above the upper pipe plate from the upper chamber to the lower chamber, wherein each riser tube is provided with an inflow pipe element extending into the lower chamber from the lower pipe plate to a level above the distribution plate through which the return tube or tubes projects or project, and the lower chamber is provided with a device that prevents granules from reaching the lower chamber inlet for the fluid medium at standstill, characterised in that in the case in which the inflow pipe elements (22) are provided with lateral bores (23), the top of the lower chamber (17) is provided at a level above the lateral bores (23) level, with an outlet (51) with shutoff valve (52).
Claim 5
Dependent Claim
35 words
Apparatus according to claim 2, characterised in that the outlet (51) at the top of the lower chamber (17) is directly connected to an outlet (53) of the upper chamber (16) for the fluid medium.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-02-02 | 1990-08-04 | 1991-02-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-02-02 | 1994-08-04 | 1995-02-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-02-02 | 1998-08-04 | 1999-02-03 | $7700.00 | Window Closed / Lapsed |