CN104722250A - Gas-liquid two-phase chemical reaction tank - Google Patents
Gas-liquid two-phase chemical reaction tank Download PDFInfo
- Publication number
- CN104722250A CN104722250A CN201310733771.7A CN201310733771A CN104722250A CN 104722250 A CN104722250 A CN 104722250A CN 201310733771 A CN201310733771 A CN 201310733771A CN 104722250 A CN104722250 A CN 104722250A
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- CN
- China
- Prior art keywords
- tank body
- gas
- tank
- liquid
- chemical reaction
- 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.)
- Pending
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
- B01J10/002—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor carried out in foam, aerosol or bubbles
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- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention provides a gas-liquid two-phase chemical reaction tank, which comprises a tank body, wherein a feeding opening is formed in the upper cover of the tank body; a through hole is formed in the center of the upper cover of the tank body; a vent pipe is fixedly connected with the tank body through the through hole; a gas inlet chamber is connected with the upper end of the vent pipe; a gas distribution chamber is arranged at the lower end of the vent pipe; multiple exhaust pipes are connected at the lower end of the gas distribution chamber; multiple exhaust holes are uniformly formed in the side wall of each exhaust pipe; a mounting cavity is formed in the side wall of the tank body; a heating wire is arranged in the mounting cavity; a stirrer is arranged at the bottom of the tank body and is connected with an alternating current motor; the cavity of the tank body is connected with a cooler and a collection tank through connecting pipes in sequence; a discharging valve is fixedly connected at the bottom of the tank body. According to the gas-liquid two-phase chemical reaction tank, multiple exhaust pipes are used; a large amount of bubbles can be rapidly generated and expand to form a large-area boiling center, so as to meet the requirement of large gas-liquid contact area; besides, by both heating and stirring, the reaction speed can be increased and the efficiency can be remarkably improved.
Description
Technical field
The invention provides a kind of chemical reaction tank, specifically a kind of gas-liquid two-phase chemical reaction tank.
Background technology
Common retort in Chemical Manufacture, primarily of compositions such as tank body, cover, air inlet pipe, jet thrust, escape pipe, condenser and recycling cans.It inserts air inlet pipe of tank body is single or many, and every root pipeline once can only produce one or several bubble, and thus gas, liquid contact area are little, and reaction effect is not easily desirable.
Summary of the invention
For solving the problem, the invention provides a kind of gas-liquid two-phase chemical reaction tank.
Concrete solution is:
A kind of gas-liquid two-phase chemical reaction tank, comprise tank body, tank body upper cover is provided with charging aperture, tank body upper cover center offers through hole, breather pipe is fixedly connected with tank body by through hole, and breather pipe upper end is connected with inlet plenum, and breather pipe lower end is provided with sub-air chamber, sub-air chamber lower end is connected with many blast pipes, and every root blast pipe sidewall is provided with multiple steam vent; Described tank wall is provided with installation cavity, is provided with heater strip in installation cavity; Described tank base is provided with agitator, and agitator connects alternating current generator; Tank body cavity connects cooler and collecting tank successively by tube connector, and described tank base is fixedly connected with blow-off valve.
Further, described blast pipe, agitator all use fiberglass manufacture.
Further, described heater strip connects AC power.
The present invention uses many blast pipes, operationally can produce a large amount of bubbles, quantity is many, speed is fast, be rapidly to and around spread, expand, form the boiling center that area is very large, meet reactant gas, requirement that liquid contact surface is large, in addition, in conjunction with heating and the common use of stirring, can increase reaction rate, efficiency significantly improves.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Wherein:
1. tank body 2. breather pipe 3. charging aperture 4. installation cavity
5. heater strip 6. agitator 7. alternating current generator 8. blow-off valve
9. AC power 10. collecting tank 11. cooler 12. inlet plenum
Detailed description of the invention
A kind of gas-liquid two-phase chemical reaction tank, comprise tank body 1, tank body 1 upper cover is provided with charging aperture, tank body 1 upper cover center offers through hole, breather pipe 2 is fixedly connected with tank body 1 by through hole, and breather pipe 2 upper end is connected with inlet plenum 12, and breather pipe 2 lower end is provided with sub-air chamber, sub-air chamber lower end is connected with many blast pipes, and every root blast pipe sidewall is provided with multiple steam vent; Described tank body 1 sidewall is provided with installation cavity 4, is provided with heater strip 5 in installation cavity 4; Be provided with agitator 6 bottom described tank body 1, agitator 6 connects alternating current generator 7; Tank body 1 cavity connects cooler 11 and collecting tank 10 successively by tube connector, is fixedly connected with blow-off valve 8 bottom described tank body 1, heater strip 5 connects AC power 9.
In the present embodiment, blast pipe, agitator 6 all use fiberglass manufacture.
The present invention uses many blast pipes, operationally can produce a large amount of bubbles, quantity is many, speed is fast, be rapidly to and around spread, expand, form the boiling center that area is very large, meet reactant gas, requirement that liquid contact surface is large, in addition, in conjunction with heating and the common use of stirring, can increase reaction rate, efficiency significantly improves.
Claims (3)
1. a gas-liquid two-phase chemical reaction tank, it is characterized in that: comprise tank body, tank body upper cover is provided with charging aperture, tank body upper cover center offers through hole, breather pipe is fixedly connected with tank body by through hole, and breather pipe upper end is connected with inlet plenum, and breather pipe lower end is provided with sub-air chamber, sub-air chamber lower end is connected with many blast pipes, and every root blast pipe sidewall is provided with multiple steam vent; Described tank wall is provided with installation cavity, is provided with heater strip in installation cavity; Described tank base is provided with agitator, and agitator connects alternating current generator; Tank body cavity connects cooler and collecting tank successively by tube connector, and described tank base is fixedly connected with blow-off valve.
2. a kind of gas-liquid two-phase chemical reaction tank according to claim 1, is characterized in that: described blast pipe, agitator all use fiberglass manufacture.
3. a kind of gas-liquid two-phase chemical reaction tank according to claim 1, is characterized in that: described heater strip connects AC power.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310733771.7A CN104722250A (en) | 2013-12-21 | 2013-12-21 | Gas-liquid two-phase chemical reaction tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310733771.7A CN104722250A (en) | 2013-12-21 | 2013-12-21 | Gas-liquid two-phase chemical reaction tank |
Publications (1)
Publication Number | Publication Date |
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CN104722250A true CN104722250A (en) | 2015-06-24 |
Family
ID=53447025
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310733771.7A Pending CN104722250A (en) | 2013-12-21 | 2013-12-21 | Gas-liquid two-phase chemical reaction tank |
Country Status (1)
Country | Link |
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CN (1) | CN104722250A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109908854A (en) * | 2019-04-11 | 2019-06-21 | 成武金硕药业化工有限公司 | A kind of preparation system of the phonetic sulphur sulfonamide of jade |
WO2020238499A1 (en) * | 2019-05-30 | 2020-12-03 | 南京杰科丰环保技术装备研究院有限公司 | Gas-liquid phase reactor for preparing sulfite |
-
2013
- 2013-12-21 CN CN201310733771.7A patent/CN104722250A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109908854A (en) * | 2019-04-11 | 2019-06-21 | 成武金硕药业化工有限公司 | A kind of preparation system of the phonetic sulphur sulfonamide of jade |
WO2020238499A1 (en) * | 2019-05-30 | 2020-12-03 | 南京杰科丰环保技术装备研究院有限公司 | Gas-liquid phase reactor for preparing sulfite |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20150624 |