CN211725716U - Hexafluoropropane apparatus for producing - Google Patents

Hexafluoropropane apparatus for producing Download PDF

Info

Publication number
CN211725716U
CN211725716U CN202020047018.8U CN202020047018U CN211725716U CN 211725716 U CN211725716 U CN 211725716U CN 202020047018 U CN202020047018 U CN 202020047018U CN 211725716 U CN211725716 U CN 211725716U
Authority
CN
China
Prior art keywords
mixed flow
hexafluoropropane
flow plate
reaction tank
hole
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.)
Active
Application number
CN202020047018.8U
Other languages
Chinese (zh)
Inventor
叶明生
费卫民
崔杨柳
胡晓怡
贺志鹏
朱小兵
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.)
Shanghai Waysmos Fire Suppression Co Ltd
Original Assignee
Shanghai Waysmos Fire Suppression 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 Shanghai Waysmos Fire Suppression Co Ltd filed Critical Shanghai Waysmos Fire Suppression Co Ltd
Priority to CN202020047018.8U priority Critical patent/CN211725716U/en
Application granted granted Critical
Publication of CN211725716U publication Critical patent/CN211725716U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The utility model discloses a hexafluoropropane apparatus for producing. The reaction tank comprises a reaction tank body, a flow mixer is installed in the reaction tank body, the flow mixer comprises at least one inverted cone-shaped flow mixing plate and at least one tapered flow mixing plate, the inverted cone-shaped flow mixing plate and the tapered flow mixing plate are alternately arranged, an arc plate is arranged on the lower portion of the reaction tank body, a small hole is formed in the arc plate, an air adding hole is formed in the bottom end of the reaction tank body, the air adding hole comprises a side air adding hole and a central air inlet pipe, the side air adding hole is formed in two sides of the central air inlet pipe, a tapered closing-in is arranged at the outlet of the central air inlet pipe, a liquid adding. The utility model discloses simple structure, reaction efficiency is high, and the product yield is high.

Description

Hexafluoropropane apparatus for producing
Technical Field
The utility model relates to a hexafluoropropane apparatus for producing belongs to the chemical industry and equips the field.
Background
Hexafluoropropane (English name: HFC-236fa), chemical substance, suitable for filling portable fire-extinguishing equipment, can be used for open and semi-open space fire-extinguishing, and also can be used in the full-submerged fire-extinguishing system in some occasions.
But the existing hexafluoropropane production device has the defects of insufficient and uniform material mixing, low reaction efficiency and low product recovery rate.
SUMMERY OF THE UTILITY MODEL
In view of this, the utility model provides a hexafluoropropane apparatus for producing, simple structure, the material misce bene, reaction efficiency is high, and the product yield is high.
The utility model discloses an above-mentioned technical problem is solved to following technical means:
the utility model provides a hexafluoropropane apparatus for producing, which comprises a reaction tank body, the internal mixed flow ware of installing of retort, the mixed flow ware includes at least one deck back taper mixed flow plate and at least one deck toper mixed flow plate, back taper mixed flow plate and toper mixed flow plate are arranged in turn, retort lower part is provided with the arc, be provided with the aperture on the arc, retort bottom is provided with the gas pocket, the gas pocket includes side gas pocket hole and central intake pipe, the side gas pocket setting is in central intake pipe both sides, central intake pipe exit is provided with the toper binding off, retort upper portion is provided with the liquid feeding pipe, retort top is provided with the venthole, be provided with the relief pressure valve on the vent.
The circumferential wall of the reaction tank body is provided with a jacket.
Valves are arranged on the air charging hole and the liquid charging pipe.
The distance between the inverted cone-shaped mixed flow plate and the cone-shaped mixed flow plate is 2-5 cm.
This patent utilizes and adopts gas-liquid reaction unit, use hydrogen fluoride and hexachloropropane as the raw materials, adopt liquid catalyst simultaneously, carry out the gas-liquid reaction in gas-liquid reaction unit, be provided with simultaneously on the retort body perisporium and press from both sides the cover, can keep invariable certain temperature, realize the reaction, obtain hexafluoropropane, for gas, maintain certain pressure in the gas-liquid reaction unit simultaneously, be provided with the relief pressure valve on the venthole, can set for certain pressure, after reaching certain pressure, can release pressure, thereby release gas and go out.
Meanwhile, the flow mixer comprises at least one layer of inverted cone-shaped flow mixing plate and at least one layer of conical flow mixing plate, the inverted cone-shaped flow mixing plate and the conical flow mixing plate are alternately arranged, and the compression and the release of gas are realized through the alternate arrangement of the inverted cone-shaped flow mixing plate and the conical flow mixing plate, so that the mixing and the mass transfer of the gas and the liquid are realized, the high-efficiency reaction is realized, and the reaction efficiency is improved.
The utility model has the advantages that: simple structure, high reaction efficiency and high product yield.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Detailed Description
The present invention will be described in detail with reference to the accompanying drawings and specific examples, as shown in fig. 1, the hexafluoropropane producing apparatus of this embodiment comprises a reaction tank 1, install the mixed flow ware 2 in the retort body 1, the mixed flow ware 2 includes at least one deck back taper mixed flow plate 3 and at least one deck toper mixed flow plate 4, back taper mixed flow plate 3 and toper mixed flow plate 4 arrange in turn, 1 lower part of the retort body is provided with arc 5, be provided with aperture 6 on the arc 5, 1 bottom of the retort body is provided with air entrainment hole 7, air entrainment hole 7 includes side air entrainment hole 8 and central intake pipe 9, side air entrainment hole 8 sets up in central intake pipe 9 both sides, central intake pipe 9 exit is provided with toper binding off 10, 1 upper portion of the retort body is provided with liquid feeding pipe 11, 1 top of the retort body is provided with venthole 12, be provided with relief pressure valve 13 on the venthole 12.
The reaction tank 1 is provided with a jacket 14 on the peripheral wall thereof.
The air charging hole 7 and the liquid charging pipe 11 are provided with valves 15.
The distance between the inverted cone-shaped mixed flow plate 3 and the cone-shaped mixed flow plate 4 is 2-5 cm.
As shown in figure 1, the bottom of the reaction tank body 1 is provided with an air adding hole 7, the air adding hole 7 comprises a side air adding hole 8 and a central air inlet pipe 9, the side air adding hole 8 is arranged at two sides of the central air inlet pipe 9, the outlet of the central air inlet pipe 9 is provided with a conical closing-in 10, gas can be added from the bottom of the reaction tank body 1, through the unique structure of the air adding hole 7, the premixing of the gas can be realized, meanwhile, the lower part of the reaction tank body 1 is provided with an arc-shaped plate 5, the arc-shaped plate 5 is provided with a small hole 6, the dispersion of the gas can be realized, meanwhile, the mixer comprises at least one layer of inverted cone-shaped mixed flow plate and at least one layer of cone-shaped mixed flow plate, the inverted cone-shaped mixed flow plate and the cone-shaped mixed flow plate are alternately arranged, the reaction efficiency is improved. Meanwhile, the pressure reducing valve is arranged on the air outlet, certain pressure can be set, and when the certain pressure is reached, the pressure can be released, so that the gas is released.
Finally, although the present invention has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that the present invention can be modified or replaced by other means without departing from the spirit and scope of the present invention, which should be construed as limited only by the appended claims.

Claims (4)

1. A hexafluoropropane production device is characterized in that: including the retort body (1), install mixed flow ware (2) in the retort body (1), mixed flow ware (2) are including at least one deck back taper mixed flow plate (3) and at least one deck toper mixed flow plate (4), back taper mixed flow plate (3) and toper mixed flow plate (4) are arranged in turn, the retort body (1) lower part is provided with arc (5), be provided with aperture (6) on arc (5), the retort body (1) bottom is provided with air feed hole (7), air feed hole (7) are including side air feed hole (8) and central intake pipe (9), side air feed hole (8) set up in central intake pipe (9) both sides, central intake pipe (9) exit is provided with toper binding off (10), retort body (1) upper portion is provided with liquid feed pipe (11), retort body (1) top is provided with venthole (12), be provided with relief pressure valve (13) on venthole (12).
2. A hexafluoropropane production apparatus according to claim 1, wherein: the surrounding wall of the reaction tank body (1) is provided with a jacket (14).
3. A hexafluoropropane production apparatus according to claim 1, wherein: valves (15) are arranged on the air charging hole (7) and the liquid charging pipe (11).
4. A hexafluoropropane production apparatus according to claim 1, wherein: the distance between the inverted cone-shaped mixed flow plate (3) and the cone-shaped mixed flow plate (4) is 2-5 cm.
CN202020047018.8U 2020-01-10 2020-01-10 Hexafluoropropane apparatus for producing Active CN211725716U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202020047018.8U CN211725716U (en) 2020-01-10 2020-01-10 Hexafluoropropane apparatus for producing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202020047018.8U CN211725716U (en) 2020-01-10 2020-01-10 Hexafluoropropane apparatus for producing

Publications (1)

Publication Number Publication Date
CN211725716U true CN211725716U (en) 2020-10-23

Family

ID=72881637

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202020047018.8U Active CN211725716U (en) 2020-01-10 2020-01-10 Hexafluoropropane apparatus for producing

Country Status (1)

Country Link
CN (1) CN211725716U (en)

Similar Documents

Publication Publication Date Title
CN201454534U (en) Multi-guide-tube loop reactor
CN202207593U (en) Oxidizing reaction kettle
CN211725716U (en) Hexafluoropropane apparatus for producing
CN207221880U (en) Reaction kettle gas distributor
CN205761026U (en) Multi-functional pressure reactor
CN204911455U (en) Tympanic bulla oxidation reaction unit
CN204996383U (en) It does not have mechanical transmission air agitating unit including silver -colored dead catalyst to handle
CN108251286B (en) Gas-liquid atomization efficient bioreactor
CN205731169U (en) A kind of reactor
CN210097678U (en) Stirring tank with fixed gas distributor
CN213254472U (en) Flexible body static mixing reaction device special for gas-liquid reaction
CN213644075U (en) Microbubble generator and hydrocarbon oil hydrogenation reactor
CN108579624A (en) A kind of reaction unit being suitable for being catalyzed reaction
CN104909338A (en) Hydrogen generator
CN204247173U (en) The solid-liquid reaction gas generating unit that a kind of gas speed is adjustable
CN210700043U (en) Micropore plate gas distributor
CN202089764U (en) Portable ethanol self-heating hydrogen production reactor
CN102745731B (en) Calcium chloride reactor
CN102133517A (en) Liquid continuous impact flow heterogeneous reaction and aerobic fermentation technical equipment
CN206965701U (en) A kind of multipurpose dehydrogenation reactor
CN216778765U (en) Fixed bed continuous liquid phase hydrogenation reaction device
CN207891109U (en) A kind of use for laboratory continuous catalysis decomposes the device of hydrazine-containing water
CN205146190U (en) Ammoniation reaction ware
CN104116573A (en) Up-and-down type filtered CO poisoning device
CN103007838A (en) Chemical catalysis reactor

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant