CN201882921U - Heat exchange device for trichlorosilane fluidized bed - Google Patents

Heat exchange device for trichlorosilane fluidized bed Download PDF

Info

Publication number
CN201882921U
CN201882921U CN2010205751930U CN201020575193U CN201882921U CN 201882921 U CN201882921 U CN 201882921U CN 2010205751930 U CN2010205751930 U CN 2010205751930U CN 201020575193 U CN201020575193 U CN 201020575193U CN 201882921 U CN201882921 U CN 201882921U
Authority
CN
China
Prior art keywords
heat exchange
trichlorosilane
heat
bed
exchange device
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2010205751930U
Other languages
Chinese (zh)
Inventor
阎世城
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NINGBO ZHAORI SILICON MATERIALS CO Ltd
Original Assignee
NINGBO ZHAORI SILICON MATERIALS CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by NINGBO ZHAORI SILICON MATERIALS CO Ltd filed Critical NINGBO ZHAORI SILICON MATERIALS CO Ltd
Priority to CN2010205751930U priority Critical patent/CN201882921U/en
Application granted granted Critical
Publication of CN201882921U publication Critical patent/CN201882921U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Silicon Compounds (AREA)

Abstract

The utility model discloses a heat exchange device for a trichlorosilane fluidized bed, which comprises sleeve bundles; the sleeve bundles are arranged in a fluidized bed shell in a penetrating way, are cylindrical, and are arranged in an annular array. In the heat exchange device, as sleeve bundles with fins are replaced by the sleeve bundles without the fins, the complex structure of the heat exchange device is greatly simplified, the heat exchange requirement can be well met, and the condition of 'temperature runaway' in the prior art is overcome.

Description

A kind of heat-exchanger rig of trichlorosilane fluidized-bed
Technical field
The utility model relates to a kind of trichlorosilane fluidized-bed, relates in particular to a kind of heat-exchanger rig of trichlorosilane fluidized-bed.
Background technology
Trichlorosilane is the important source material of producing polysilicon at present, is the raw material basis of photovoltaic industry, also is the raw material basis of exploitation and development new forms of energy-environmental protection energy.Just present, the exploitation development environment-friendly type energy is global developing direction, so trichlorosilane has vast market prospect.
The production technique of trichlorosilane is as follows:
1) with exsiccant hydrogenchloride and silica flour;
2) in the trichlorosilane fluidized-bed, react generation trichlorosilane and a spot of silicon tetrachloride and hydrogen under 300 ℃ the situation;
3) through dedusting, condensation, tail gas absorbs;
4) lime set rectifying gets product trichlorosilane and by-product silicon tetrachloride.
In production process of trichlorosilane, the trichlorosilane fluidized-bed is main production unit, and wherein the heat-exchanger rig of trichlorosilane fluidized-bed is a trichlorosilane fluidized-bed vitals, and it adopts the cover tube bank of fin, complex structure, manufacturing cost height.Other shortcoming is that this heat-exchanger rig also is easy to generate " temperature runaway " (temperature runaway is meant that reactor is under the non-stable operational stage, when operating parameters has little disturbance, the phenomenon that the local area of reactor or the temperature in the whole reactor just can rise significantly.Temperature runaway is because reactive system is under operational condition due to " polymorphic " situation, and it is by the interaction of reaction heat effect and heat transfer process generation to a great extent.It often causes the destruction that runs well, even catalyzer is burnt.) so its structure of heat-exchanger rig of trichlorosilane fluidized-bed is still waiting to improve.
The utility model content
The utility model is at deficiency of the prior art, and a kind of heat-exchanger rig of trichlorosilane fluidized-bed of simple in structure, low cost of manufacture is provided, and uses the heat-exchanger rig of this trichlorosilane fluidized-bed to be not easy to produce " temperature runaway ".
In order to solve the problems of the technologies described above, the utility model is solved by following technical proposals:
A kind of heat-exchanger rig of trichlorosilane fluidized-bed comprises the cover tube bank, and described cover tube bank is arranged in the fluidized-bed housing, and described cover tube bank is cylinder.
In the technique scheme, described cover tube bank is right cylinder.
In the technique scheme, cover tube bank circular array formula is arranged.
Beneficial effect: the utility model compared with prior art has following beneficial effect:
The utility model has been simplified the complex construction of heat-exchanger rig greatly owing to restrain the cover tube bank that replaces having fin with the cover of non-finned.And well satisfied the heat exchange requirement; Overcome " temperature runaway " situation in the past.
Description of drawings
Fig. 1 is the structural representation of the heat-exchanger rig of trichlorosilane fluidized-bed.
Fig. 2 is an I place enlarged view among Fig. 1.
Fig. 3 be among Fig. 1 A-A to sectional view.
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is described in further detail:
Referring to Fig. 1~3, a kind of heat-exchanger rig of trichlorosilane fluidized-bed comprises cover tube bank 1, and described cover tube bank 1 is arranged in the fluidized-bed housing 3, and described cover tube bank 1 is a right cylinder.Certain described cover tube bank 1 can also be other cylinder body shape of being convenient to process.
Preferably, cover tube bank 1 circular array formula is arranged.This structure can improve " than heat-transfer surface " (is the ratio of heat-transfer surface and reaction volume in the reaction zone than heat-transfer surface) greatly
The utility model has been simplified the complex construction of heat-exchanger rig greatly, and has well been satisfied the heat exchange requirement owing to restrain the cover tube bank 1 that replaces having fin with the cover of non-finned; Overcome " temperature runaway " situation in the past, made reaction be able to long-term (more than one month) and go on continuously.Its " than heat-transfer surface " (explain: be 7~12m-1 the ratio of heat-transfer surface and reaction volume in the reaction zone), good value 9.5~11m-1.

Claims (3)

1. the heat-exchanger rig of a trichlorosilane fluidized-bed comprises cover tube bank (1), and described cover tube bank (1) is arranged in the fluidized-bed housing (3), it is characterized in that, described cover tube bank (1) is a cylinder.
2. the heat-exchanger rig of trichlorosilane fluidized-bed as claimed in claim 1 is characterized in that, described cover tube bank (1) is a right cylinder.
3. the heat-exchanger rig of trichlorosilane fluidized-bed as claimed in claim 1 or 2 is characterized in that, cover tube bank (1) circular array formula is arranged.
CN2010205751930U 2010-10-25 2010-10-25 Heat exchange device for trichlorosilane fluidized bed Expired - Fee Related CN201882921U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010205751930U CN201882921U (en) 2010-10-25 2010-10-25 Heat exchange device for trichlorosilane fluidized bed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010205751930U CN201882921U (en) 2010-10-25 2010-10-25 Heat exchange device for trichlorosilane fluidized bed

Publications (1)

Publication Number Publication Date
CN201882921U true CN201882921U (en) 2011-06-29

Family

ID=44180459

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010205751930U Expired - Fee Related CN201882921U (en) 2010-10-25 2010-10-25 Heat exchange device for trichlorosilane fluidized bed

Country Status (1)

Country Link
CN (1) CN201882921U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104591190A (en) * 2015-01-26 2015-05-06 亚洲硅业(青海)有限公司 Anti-abrasive device for heat exchange tube bundle in trichlorosilane synthetic furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104591190A (en) * 2015-01-26 2015-05-06 亚洲硅业(青海)有限公司 Anti-abrasive device for heat exchange tube bundle in trichlorosilane synthetic furnace

Similar Documents

Publication Publication Date Title
CN104876242A (en) Three-phase fluidization equipment and method for producing ammonia from urea by virtue of catalytic hydrolysis
CN204365252U (en) A kind of large-scale reactor and device thereof
CN201882921U (en) Heat exchange device for trichlorosilane fluidized bed
CN105771819B (en) Circular response device and its working method in a kind of calcium base thermochemical high temperature fluid bed
CN204224269U (en) A kind of carbonating tower produced for sodium bicarbonate
CN201882919U (en) Trichlorosilane fluidized bed
CN202860502U (en) Vertical type water-cooled tube reactor
CN102188937A (en) Synthetic converter for producing chloroethylene by synthetic reaction of ethyne and hydrogen chloride
CN201882920U (en) Separation area of trichlorosilane fluidized bed
CN201127890Y (en) Fluidized-bed film reactor of Pd film component arranged in ring type radiating shape
CN203648501U (en) Corrugated plate type uniform-temperature hydrogenation reactor
CN204247178U (en) The water bed reactor of beam tube type
CN203790924U (en) Vertical combined type isothermal reactor
CN102744018B (en) Fixed bed catalytic reaction device with adjustable inlet material temperature
CN202078885U (en) Synthetic converter for producing chloroethylene due to reaction of acetylene and hydrogen chloride
CN203598804U (en) Fluidized bed reactor for synthesis of organosilicone monomers
CN202398241U (en) Chlorosilane washing tower
CN202715401U (en) Fixed bed catalytic reaction device capable of adjusting temperature of material at inlet
CN201882917U (en) Trichlorosilane fluidized bed
CN202747860U (en) Flue gas waste heat recycling device
CN202655001U (en) Large-sized sulfur melting kettle
CN203030262U (en) Large hanging-basket sealing heat exchange type one-stage converter
CN201551995U (en) Trichlorosilane production fluid bed reactor for improving gas-solid contact time
CN102234217A (en) Technology for producing methyl chloride by ammonium chloride method
CN201793382U (en) Multistage adiabatic indirect heat-exchange energy-saving type ammonia converter

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: NINGBO ZHAORI FINE CHEMICAL CO., LTD.

Free format text: FORMER NAME: NINGBO ZHAORI SILICON MATERIALS CO., LTD.

CP01 Change in the name or title of a patent holder

Address after: 315204 No. 389 North Sea Road, Ningbo chemical industry zone, Zhejiang

Patentee after: NINGBO ZHAORI SILICON MATERIALS CO., LTD.

Address before: 315204 No. 389 North Sea Road, Ningbo chemical industry zone, Zhejiang

Patentee before: Ningbo Zhaori Silicon Materials Co., Ltd.

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110629

Termination date: 20191025

CF01 Termination of patent right due to non-payment of annual fee