Reactor

专利摘要:
Dynamic fluidized-bed reactor for carrying out a chemical or physical multi-component process, which said reactor comprises a preferably vertical, cooled or uncooled reactor chamber and a preferably horizontal cyclone that discharges the solid matter through the side of the separator chamber and the gases through one end or both ends of the separator chamber. The reactor further comprises a discharge pipe with no gas lock, which allows the solid matter to fall freely. In different applications, the reactor may include feed and discharge means for solid matter as well as a gas distributor grate. Exemplifying embodiments are a fire-tube boiler and a reactor for purification and cooling of hot gases.
公开号:SU1658812A3
申请号:SU853983645
申请日:1985-11-19
公开日:1991-06-23
发明作者:Юхани Саркомаа Пертти
申请人:Раума-Репола, Ой И А.Альстрем Корпорейшн (Фирма)；
IPC主号:

专利说明:

The invention relates to the design of a dynamic fluidized bed reactor for carrying out a chemical or physical process.
The aim of the invention is to simplify the design of the reactor and reduce costs.
FIG. 1 shows a reactor with a horizontal cyclone inside the reactor, longitudinal section; figure 2 - section aa in figure 1; on fig.Z - reactor with a tubular heater, a longitudinal section; figure 4 is the same, top view; figure 5 - reactor with two horizontal cyclones, a longitudinal section; figure 6 - section bb in figure 5.
The reactor includes a housing 1, an air chamber 2 with an inlet nozzle 3, a gas distribution plate 4 located between the reactor chamber 5 and an air chamber 2, a horizontal separator chamber 6 of a horizontal cyclone with a nozzle 7 for removing solid material located on the periphery of the separator chamber. The separator chamber 6 is connected to the reactor chamber via a channel 8. A return tube 9 is connected to the nozzle 7.
The horizontal cyclone separator chamber has a nozzle 10 for discharging the purified gas. The solid material involved in the process is discharged through the discharge nozzle 11. The nozzle 12 serves to feed solid material into the reactor chamber. The reactor can be placed in a cooling device with an aqueous medium including a housing 13 with nozzles 14 and 15 for the inlet and outlet of the cooling medium. The horizontal horizontal cyclone separation chamber 6 has channels 16 for the cleaned gas connected to the lower return chamber 17. In the cooling device, heating tubes 18 are placed connecting the lower chamber 17 to the upper reversing chamber 19 connected to the vent pipes 20. When using a combustible gas cleaning reactor, it can be equipped with an additional horizontal cyclone, while both cyclones are connected in series and The reactor chamber in the lower part contains a mixing chamber 21, which is connected by means of return pipes 9 and 22.
The cyclones are connected by means of a nozzle 23 entering the second cyclone separator chamber 24, and the purified gases from the second cyclone are discharged through the nozzle 25.
Works reactor as follows. The process gas passes into the reactor through the inlet 3 of the air chamber 2 located in the lower part of the reactor. Through the gas distribution plate 4, which is located between the reactor chamber 5 and the air chamber 2, the gas passes into the lower part of the reactor chamber 5. into which a solid material is fed through the return tube 9, which is separated in a horizontal separator. The lead material involved in the process is fed into the reactor through the outlet nozzle 12. The solid product of the process or waste is removed through the outlet nozzle 11.
Plate 4 of reactor chamber 5 may be cooled, and the reactor chamber may also have cooling elements. Gas containing solid is fed through channel 8 along the tangent and circumference of a horizontal separator chamber 6 of a horizontal cyclone located above the reactor chamber 5. Solid material collected from a horizontal cyclone to the wall is removed through a nozzle 7 located at the periphery of the separator chamber, and from this channel, the solid material passes further along the return tube 9 to the specified location of the reactor. Gases cleaned in a horizontal cyclone are removed through both ends of the cyclone through nozzles 10. From the horizontal separator (Fig. 1) the gases are removed symmetrically, and the ends of the separator chamber are tapered. It is clear that the ends of the separator chamber can also be flat, and the gas can also be removed only on one side. If necessary, the discharge nozzles 10 of the horizontal separator can also
pass into the separator chamber 6. Figure 1 shows the connection between the reactor chamber and the horizontal separator. The separator may be
for example, eccentric with respect to the reactor chamber and return duct for. solids may also be located outside the separator chamber.
In the heating tubes 18, the gases are additionally cooled and the passage into the upper reversing chamber 19, and from there further - through the tubes 20. The solid material returns through the tube 9 to the appropriate level in the reactor chamber 5
5 combustion.
In the case of a mixing chamber 21, solid material is fed into it through the inlet 12, and discharged through the nozzle 11.
0 Solid materials and gas are lifted through tubes 18 into the collection space — the reactor chamber 5. Through the nozzle 8, gases containing solids tangentially to the circumference are fed to
5 separator chamber of the first horizontal cyclone. The pre-cleaned gases are removed from the first separator through one end or both ends of the separator chamber through nozzle 10. Separated
The substance is returned to the mixture through the tube 9. Through the pipe 23, the previously purified gases are led to the periphery of the separator chamber 24 of the second horizontal separator. The pure gases are removed through the ends of the second horizontal separator through the pipe 25. The separated solid is returned through the discharge tube 22 to the mixing chamber 21. The reactor section is cooled using the design of the heating tubes 18 and 9 located in the water space formed by the housing 13.
The use of the invention leads
5 to simplify the design of the reactor, as well as to improve the work achieved in comparison with the known reactors.
The use of a horizontal cyclone allows a reduction in costs, because the reactor becomes small in size and ensures stable operation.

权利要求:
Claims (1)
[1]
Claims of the Invention A dynamic fluidized bed reactor comprising a body in the upper part of which there is a cyclone separator with a recirculation channel for particles, the lower open end of which is located in the lower part of the reactor body, which is distinguished by and. what with the purpose
simplify the design, the cyclone is made horizontal and installed in such a way that the upper part of the reactor vessel
interfaced with the cyclone's upper wall to form an inlet for the gas to be purified.
1
Aa
at 9
YU
1 V
jtf
7
YU
FIG. 2
15
Fi2 4
/ 0 23
3Fig 6
Fig 5
Compiled by N. Katsovsk. Editor M. BlanarTechred M. Morgental Corrector M. Kucher wa

类似技术:

---

公开号 | 公开日 | 专利标题

---

JP3995262B2|2007-10-24|Cyclone separator with reduced disorder

---

FI92627B|1994-08-31|Reactor with circulating bed

---

SU1540650A3|1990-01-30|Apparatus for separating solid and liquid

---

KR870000411A|1987-02-18|Fluidized bed reactor and its operation method

---

CA1158421A|1983-12-13|Fluidized bed reactor

---

SU1658812A3|1991-06-23|Reactor

---

EP0175819B1|1988-04-20|Apparatus for gasifying coal including a slag trap

---

US3856476A|1974-12-24|High velocity wet electrostatic precipitation for removing gaseous and particulate contaminants

---

JP2770233B2|1998-06-25|Apparatus for separating solids from a mixture of solids and fluid

---

CA2456261A1|2004-08-26|Separation device to remove fine particles

---

US4191544A|1980-03-04|Gas cleaning apparatus

---

US3442232A|1969-05-06|Effluent cleaner for waste burner

---

SU1679971A3|1991-09-23|Device for separation of solids from liquids

---

KR910001838B1|1991-03-26|Circulating fluidized bed reactor

---

JPH03102105A|1991-04-26|Circulating fluidized bed reactor utilizing integral curved arm separator

---

US4664887A|1987-05-12|Apparatus for separating solid material in a circulating fluidized bed reactor

---

US5171542A|1992-12-15|Circulating fluidized bed reactor

---

KR910001835B1|1991-03-26|Fluidized bed reactor

---

US6245300B1|2001-06-12|Horizontal cyclone separator for a fluidized bed reactor

---

US4900516A|1990-02-13|Fluidized bed reactor

---

CA1265660A|1990-02-13|Circulating fluidized bed reactor and a method ofseparating solid material from the flue gases

---

CA1258037A|1989-08-01|Apparatus for separating solids in a circulatingfluidized bed reactor

---

KR910001926B1|1991-03-30|A circulation fluidized bed reactor

---

SU965523A1|1982-10-15|Straight current cyclone

---

SU919712A1|1982-04-15|Gas separator

同族专利:

---

公开号 | 公开日

---

DK162142C|1992-02-24|

---

DE3571124D1|1989-07-27|

---

NO162948B|1989-12-04|

---

AU568201B2|1987-12-17|

---

KR850700219A|1985-12-26|

---

DE177527T1|1987-02-26|

---

FI841126A|1985-09-21|

---

FI841126A0|1984-03-20|

---

WO1985004117A1|1985-09-26|

---

DK162142B|1991-09-23|

---

AU4114285A|1985-10-11|

---

KR890001277B1|1989-04-28|

---

NO854622L|1985-11-19|

---

DK533285A|1985-11-19|

---

EP0177527B1|1989-06-21|

---

DK533285D0|1985-11-19|

---

EP0177527A1|1986-04-16|

---

FI70377B|1986-03-27|

---

NO162948C|1990-03-14|

---

JPS61501498A|1986-07-24|

---

AT44132T|1989-07-15|

引用文献:

---

公开号 | 申请日 | 公开日 | 申请人 | 专利标题

---

---

FR1325323A|1962-06-07|1963-04-26|Prep Ind Combustibles|fluid-solid reactor exchanger|

---

DE1442745A1|1963-10-23|1969-02-06|Kloeckner Humboldt Deutz Ag|Device for treating fine-grained, solid materials|

---

US3698874A|1970-07-23|1972-10-17|Frederick A Zenz|Dust control apparatus for fluidized bed reactors|

---

JPS553008A|1978-06-21|1980-01-10|Toshiba Corp|Automatic transaction device|US4900516A|1984-06-01|1990-02-13|A. Ahlstrom Corporation|Fluidized bed reactor|

---

FI850372A0|1985-01-29|1985-01-29|Ahlstroem Oy|PANNA MED CIRKULERANDE BAEDD.|

---

GB8526540D0|1985-10-28|1985-12-04|Shell Int Research|Solids-fluid separation|

---

EP0311599B1|1985-12-09|1990-11-07|A. Ahlstrom Corporation|A circulating fluidized bed reactor and a method of separating solid material from the flue gases|

---

FI85184C|1986-05-19|1992-03-10|Ahlstroem Oy|VIRVELBAEDDSREAKTOR.|

---

FR2615600B1|1987-05-22|1990-04-20|Mediterranee Const Navales Ind|PROCESS FOR PRODUCING A HOT AND BOILER FLUID FOR CARRYING OUT THIS PROCESS|

---

US5174799A|1990-04-06|1992-12-29|Foster Wheeler Energy Corporation|Horizontal cyclone separator for a fluidized bed reactor|

---

US5218931A|1991-11-15|1993-06-15|Foster Wheeler Energy Corporation|Fluidized bed steam reactor including two horizontal cyclone separators and an integral recycle heat exchanger|

---

DE4308103A1|1993-03-15|1994-09-22|Buehler Ag|Fluidized bed|

---

FR2758277B1|1997-01-13|1999-10-08|Inst Francais Du Petrole|SEPARATOR WITH DIRECT WINDING OF PARTICLES OF A GASEOUS MIXTURE AND ITS USE IN THERMAL OR CATALYTIC CRACKING IN A FLUIDIZED BED|

---

CN102537943B|2012-01-17|2014-04-02|清华大学|Horizontal type circulating fluidized bed boiler with horizontal cyclone separator|

法律状态:

优先权:

---

申请号 | 申请日 | 专利标题

---

FI841126A|FI70377B|1984-03-20|1984-03-20|TVAO-ELLER FLERKOMPONENTREAKTOR|

---