CN2494698Y - Fluid bed reactor - Google Patents
Fluid bed reactor Download PDFInfo
- Publication number
- CN2494698Y CN2494698Y CN 01206967 CN01206967U CN2494698Y CN 2494698 Y CN2494698 Y CN 2494698Y CN 01206967 CN01206967 CN 01206967 CN 01206967 U CN01206967 U CN 01206967U CN 2494698 Y CN2494698 Y CN 2494698Y
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- bed
- heat conductive
- conductive oil
- bed reactor
- cylindrical shell
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- Expired - Lifetime
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Abstract
The utility model provides a fluidized bed reactor which includes a bed body, an upper seal head, a lower seal head, a half pipe winding on the outer wall of the bed body, a heat conductive oil distribution box arranged in the bed body, a heat exchanging mechanism consists of dropping type suspended finger-shaped sleeve beams which are connected with the heat conductive oil distribution box and evenly spread and a banded penstock disc set, a short pipe type gas distributing board, and a detecting opening, a deslagging opening, a feeding opening, a synthesis gas output, a heat conductive oil inlet and a heat conductive oil outlet. The gas is evenly distributed, the heat exchanging structure is convenient in installation and maintenance, and the utility model is applied in directly synthesizing monomer methyl chloresilane.
Description
Technical field
The utility model relates to a kind of chemical reactor, particularly relates to a kind of fluidized-bed reactor.
Background technology
At present, the fluidized-bed reactor that direct method synthesizing methyl-chloro-silane monomer is used, its syngas outlet is arranged on fluid bed upper cover top, and the heat exchanger tube of fluid bed inside needs maintenance or replacing after using certain hour, before each dismounting heat exchanger tube, all bigbore syngas outlet and other adapter mouth will be unloaded, it is very inconvenient to operate; Secondly, the gas distribution grid in the fluid bed is a sieve tray, and it is uneven easily to cause gas to distribute, and influences fluidization quality; Moreover, the direct method synthesizing methyl-chloro-silane is a strong exothermal reaction, for in time discharging the reaction liberated heat, U type pipe or thimble tube generally all are set as heat exchange structure in fluid bed, the every pipe that present U type pipe that uses or thimble tube have is connected with outer tube separately, what have organizes with several Guan Weiyi, is connected with outer tube then.And a large-scale fluidized bed reactor has dozens or even hundreds of heat exchanger tube, adopts this kind mode, and heat exchanger tube and outer tube joint are too many, and it is very inconvenient to install and overhaul.
The utility model content
The purpose of this utility model is to provide installation, maintenance convenient, and unstrpped gas is evenly distributed, the fluidized-bed reactor that fluidization quality is high.
The utility model fluidized-bed reactor comprises a body, the upper cover that is connected with bed body upper end, be connected and be provided with the low head of raw material gas inlet with bed body lower end, be looped around the semicanal on the external wall of bed, be arranged on the heat exchange structure in the body, be arranged on the short tube type gas distribution grid of bottom in the body, and be distributed in syngas outlet on the body, detect mouth, slag-drip opening, charge door, reach heat conductive oil inlet and outlet.Wherein, the bed body is made of top cylindrical shell and bottom cone; Heat exchange structure is connected and equally distributed droop suspension thimble tube bundle with the conduction oil distributor box by the conduction oil distributor box that is arranged on upper end in the cylindrical shell, and the resiliently mounted banded penstock dish of thimble tube Shu Jinhang group is formed.The banded penstock dish is a plurality of, is distributed in each section of thimble tube upper, middle and lower, is used for the flexible fastening of thimble tube bundle, it can not arbitrarily be swung, but allow every thimble tube slightly to vibrate within the specific limits, can effectively suppress solid material gathering on thimble tube, reduce coking.Simultaneously,, make each banded penstock dish have bigger hole rate, can not influence Flow of Goods and Materials in the body, thereby improve fluidization quality greatly because a plurality of banded penstock dishes are fixed some thimble tubes respectively.Conduction oil evenly flows in the every thimble tube chuck from the conduction oil distributor box, imports the conduction oil distributor box from the thimble tube centre bore after heat exchange, flows out fluid bed again; The percent opening of short tube type gas distribution grid, short tube major diameter when aperture pass through to calculate, make it reach optimum efficiency, unstrpped gas is gone into fluidized-bed reactor through the short tube rectification is laggard, can significantly reduce the turbulent flow of gas, distribution of gas is more even, simultaneously, the solid material under the situation of stopping the supple of gas or steam suddenly in the fluid bed can not fall into below the short tube type gas distribution grid, the startup of can ventilating once more easily; Syngas outlet is arranged on the side of conduction oil distributor box bottom cylindrical shell, makes things convenient for the maintenance or the replacing of thimble tube.Charge door and slag-drip opening are arranged on the cone lower end, charge door silica flour charge door during synthesizing methyl-chloro-silane.Heat conductive oil inlet and outlet comprise thimble tube heat conductive oil inlet and outlet and semicanal heat conductive oil inlet and outlet, and the former is separately positioned on cylindrical shell top and surveys face and upper cover napex, and the latter is separately positioned on the cylindrical shell side.Detect mouth and generally comprise a plurality of temperature-measuring ports and pressure tap, be arranged on cylindrical shell and the cone, be used for the detection and the control of temperature and pressure.
The course of work of the utility model fluidized-bed reactor is, unstripped gas enters from raw material gas inlet, go in the fluidized-bed reactor by the rectification of short tube type gas distribution grid is laggard, with the solid material reaction that enters from charge door, the product that generates is derived by syngas outlet, after reaction finished, residue was discharged by slag-drip opening in the fluidized-bed reactor.Temperature and pressure in the fluidized-bed reactor is detected and control by temperature-measuring port and pressure tap respectively.Thimble tube in semicanal on the external wall of bed and the bed body is removed the reaction liberated heat by the circulation of conduction oil.
The advantage of the utility model fluidized-bed reactor is to adopt the short tube type gas distribution grid, and unstrpped gas is evenly distributed, and has improved fluidization quality.Simultaneously, this heat exchange structure, thimble tube is minimum with outside tube connector, makes the integral hoisting of thimble tube bundle energy, gives installation and maintenance or brings great convenience, has also improved fluidization quality simultaneously greatly.Syngas outlet is arranged on the side of conduction oil distributor box lower bed, has both made things convenient for and being connected of outer tube, and does not influence the dismounting of thimble tube again.Be exclusively used in direct method synthesizing methyl-chloro-silane monomer.
Description of drawings
Fig. 1: the utility model structural representation.
Fig. 2～Fig. 4: banded penstock dish structural representation
Fig. 5: short tube type gas distribution grid structural representation
The specific embodiment
The utility model fluidized-bed reactor comprises, by top cylindrical shell 1 and bottom cone 2 constitute the bed body, the upper cover 3 that is connected with cylindrical shell 1 upper end, be connected and be provided with the low head 5 of raw material gas inlet 4 with cone 2 lower ends, be looped around the semicanal 6 on the external wall of bed, be arranged on the heat exchange structure in the body, be arranged on the short tube type gas distribution grid 7 of 5 of cone 2 and low heads, and be distributed in the syngas outlet 8 on the body, temperature-measuring port 9, pressure tap 10, slag-drip opening 11, silica flour charge door 12, semicanal heat conductive oil inlet 13 and outlet 14, and thimble tube heat conductive oil inlet 15 and go out 16.Wherein, heat exchange structure is connected and equally distributed droop suspension thimble tube bundle 18 with conduction oil distributor box 17, and thimble tube bundle 18 is carried out resiliently mounted banded penstock dish 19 form by the conduction oil distributor box 17 that is arranged on upper end in the cylindrical shell 1.
Claims (2)
1, a kind of fluidized-bed reactor, comprise a body, the upper cover that is connected with bed body upper end, be connected and be provided with the low head of raw material gas inlet with bed body lower end, be looped around the semicanal on the external wall of bed, be arranged on the heat exchange structure in the body, be arranged on the gas distribution grid of bottom in the body, and be distributed in detection mouth, slag-drip opening, charge door, syngas outlet and heat conductive oil inlet and the outlet of bed on the external wall, it is characterized in that a body is made of top cylindrical shell and bottom cone; Heat exchange structure is connected and equally distributed droop suspension thimble tube bundle with the conduction oil distributor box by the conduction oil distributor box that is arranged on upper end in the cylindrical shell, and the resiliently mounted banded penstock dish of thimble tube Shu Jinhang group is formed; Gas distribution grid is the short tube type gas distribution grid.
2, fluidized-bed reactor as claimed in claim 1 is characterized in that syngas outlet is arranged on the side of conduction oil distributor box bottom cylindrical shell.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01206967 CN2494698Y (en) | 2001-07-24 | 2001-07-24 | Fluid bed reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01206967 CN2494698Y (en) | 2001-07-24 | 2001-07-24 | Fluid bed reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2494698Y true CN2494698Y (en) | 2002-06-12 |
Family
ID=33627508
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01206967 Expired - Lifetime CN2494698Y (en) | 2001-07-24 | 2001-07-24 | Fluid bed reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2494698Y (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1321731C (en) * | 2005-01-26 | 2007-06-20 | 浙江大学 | Reactor of organic silicon fluidized bed with cyclone separator |
| CN103172072A (en) * | 2011-12-20 | 2013-06-26 | 储晞 | Reactor and method for realizing synthesis of chlorosilane |
| CN106595350A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Liquid-solid circulating fluidized bed heat exchanger |
| CN106595379A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Method for prolonging operation period of crude oil electrical dewatering heat exchanger |
| CN106595356A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Self-cleaning type fluidized bed heat exchanger |
| CN106595348A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | No-scaling fluidized bed heat exchanger |
| CN106595349A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Liquid phase heat exchange fluidized bed heat exchanger |
| CN106595351A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Anti-scaling and de-scaling heat exchanger for fluidized bed |
| CN106595352A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Outer circulating fluidized bed heat exchanger |
| CN109499262A (en) * | 2018-12-14 | 2019-03-22 | 青岛科技大学 | A kind of novel longitudinal parallel bed adsorption device |
| CN111298535A (en) * | 2020-03-26 | 2020-06-19 | 江苏丰尚智能科技有限公司 | Dust removal barrel fastening device and bag-type dust remover |
-
2001
- 2001-07-24 CN CN 01206967 patent/CN2494698Y/en not_active Expired - Lifetime
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1321731C (en) * | 2005-01-26 | 2007-06-20 | 浙江大学 | Reactor of organic silicon fluidized bed with cyclone separator |
| CN103172072A (en) * | 2011-12-20 | 2013-06-26 | 储晞 | Reactor and method for realizing synthesis of chlorosilane |
| CN103172072B (en) * | 2011-12-20 | 2016-08-17 | 储晞 | Realize reactor and the method for chlorosilane synthesis |
| CN106595352B (en) * | 2015-10-15 | 2018-09-14 | 中国石油化工股份有限公司 | External circulation fluidized bed heat exchanger |
| CN106595356B (en) * | 2015-10-15 | 2018-10-23 | 中国石油化工股份有限公司 | Self-cleaning fluidized bed heat exchanger |
| CN106595356A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Self-cleaning type fluidized bed heat exchanger |
| CN106595348A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | No-scaling fluidized bed heat exchanger |
| CN106595349A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Liquid phase heat exchange fluidized bed heat exchanger |
| CN106595351A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Anti-scaling and de-scaling heat exchanger for fluidized bed |
| CN106595352A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Outer circulating fluidized bed heat exchanger |
| CN106595350A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Liquid-solid circulating fluidized bed heat exchanger |
| CN106595351B (en) * | 2015-10-15 | 2018-09-14 | 中国石油化工股份有限公司 | Anti- scale removal fluid-bed heat exchanger |
| CN106595379A (en) * | 2015-10-15 | 2017-04-26 | 中国石油化工股份有限公司 | Method for prolonging operation period of crude oil electrical dewatering heat exchanger |
| CN106595379B (en) * | 2015-10-15 | 2018-10-23 | 中国石油化工股份有限公司 | Extend the method for the electrical oil dewatering heat exchanger cycle of operation |
| CN106595350B (en) * | 2015-10-15 | 2018-10-23 | 中国石油化工股份有限公司 | Solid Circulating Fluidized Bed Heat Exchanger |
| CN106595348B (en) * | 2015-10-15 | 2018-11-20 | 中国石油化工股份有限公司 | Non-scaling fluid-bed heat exchanger |
| CN106595349B (en) * | 2015-10-15 | 2019-01-25 | 中国石油化工股份有限公司 | Liquid phase heat exchange fluid-bed heat exchanger |
| CN109499262A (en) * | 2018-12-14 | 2019-03-22 | 青岛科技大学 | A kind of novel longitudinal parallel bed adsorption device |
| CN109499262B (en) * | 2018-12-14 | 2021-08-13 | 青岛科技大学 | Novel longitudinal parallel bed adsorber |
| CN111298535A (en) * | 2020-03-26 | 2020-06-19 | 江苏丰尚智能科技有限公司 | Dust removal barrel fastening device and bag-type dust remover |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20110724 Granted publication date: 20020612 |