CN109603727A - It is a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle - Google Patents

It is a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle Download PDF

Info

Publication number
CN109603727A
CN109603727A CN201811310059.5A CN201811310059A CN109603727A CN 109603727 A CN109603727 A CN 109603727A CN 201811310059 A CN201811310059 A CN 201811310059A CN 109603727 A CN109603727 A CN 109603727A
Authority
CN
China
Prior art keywords
water
reaction kettle
pipe
valve
collet
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.)
Withdrawn
Application number
CN201811310059.5A
Other languages
Chinese (zh)
Inventor
鲁晨
徐清
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 University
Original Assignee
Ningbo University
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 University filed Critical Ningbo University
Priority to CN201811310059.5A priority Critical patent/CN109603727A/en
Publication of CN109603727A publication Critical patent/CN109603727A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006Controlling or regulating processes
    • B01J19/0013Controlling the temperature of the process
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/62Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by introduction of halogen; by substitution of halogen atoms by other halogen atoms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00074Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00081Tubes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle, including guide shell, collet water inlet, collet water outlet, water discharging valve, recirculated water valve, water pump, controller 1, heating water tank, air inlet pipe, electrically operated valve, water inlet pipe, outlet pipe, hot-water valve, inlet valve, chlorine inlet, gas distributor, feed pipe, liquid charging stock import, coil inlets, gas vent, safety valve, coil pipe water outlet, coil pipe, liquid outlet, temp-sensing device, reaction kettle ontology, sealing cover, sealing ring, installing port, collet and controller 2.Conversion ratio is too low when the reaction kettle leads to problems such as selectivity too low too low with reaction temperature using the automatic temp controller including collet and coil pipe come generation side reaction when avoiding reaction temperature excessively high, chlorine also is contacted more fully with phenol solution using gas distributor and guide shell simultaneously, is conducive to improve reaction efficiency when synthesis parachlorophenol.

Description

It is a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle
Technical field
The invention belongs to chemical equipment technical fields, and in particular to a kind of synthesis parachlorophenol temperature automatically controlled can react Kettle.
Background technique
Parachlorophenol is a kind of important fine Organic Chemicals, is agriculturally mainly used for synthetic acaricide, removes Careless agent, fungicide, rat poison, mould inhibitor, anti-picloram and plant growth promoter etc., can be used for closing in terms of dye industry At Isosorbide-5-Nitrae-dihydroxy anthraquinone, Isosorbide-5-Nitrae-diamino-anthraquinone, p-aminophenol and quinhydrones etc., can be used for synthesizing 5- in terms of pharmaceutical sector Chlorine-2-hydroxyl sodium benzoate, Chlorophibrinic Acid and other drugs have more wide application prospect.Parachlorophenol Synthesis frequently with using phenol as the chlorine direct chlorination method of raw material.
Process units in the prior art be all using conventional reaction kettle, there is no for the reaction can be temperature automatically controlled Reaction kettle.For example, 105906485 A of Chinese patent CN discloses process units and its production of a kind of high-purity parachlorophenol Technique, the process units include reaction kettle, storage tank, destilling tower, rewinding tank, drainer, vacuum tower, separator, products pot;It should The device of invention is able to produce out the parachlorophenol of high-purity, and high income, and pollution is also fewer, and the device is in logical chlorine Pipeline is equipped with gas flowmeter, can effectively control the air inflow of gas, avoid deep reaction, be equipped at the top of reaction kettle Temperature survey mouth is convenient for temperature detection, prevents side reaction brought by excessively high temperature, influence the purity and quality of product.In 108101750 A of state patent CN proposes a kind of high-purity parachlorophenol preparation process, including 1. chloride process: being with phenol Raw material is first heated to liquid, then to pump quantitative force feed into enamel reaction still, in atmospheric conditions in the way of first quick and back slow It is passed through chlorine, carries out chlorination reaction, the reaction time is 32~38h, obtains chlorophenol;2. rectification working process: chlorophenol is cooling To 55~60 DEG C, composite extractant is then added, is sent into rectifying column is evaporated in vacuo together after mixing evenly, first in steam Flow back 3~3.5h under the conditions of 0.3~0.35MPa of pressure, then in 68~73 DEG C of vacuum degree -0.096~0.098MPa, temperature items Sampling analysis under part receives adjacent benzene chlorophenol;Then 115~120 DEG C of temperature, steam pressure 0.55MPa of adjusting, sampling analysis, And parachlorophenol is received, the invention chlorophenol conversion ratio, yield as made from reasonable process modification all have significantly It improves, and good separating effect, up to 99.4%, comprehensive quality is good for parachlorophenol, o-chlorphenol product purity, is suitble to industrialization Production.In the prior art it is special can temperature automatically controlled reaction kettle for synthesizing parachlorophenol.
Summary of the invention
In view of the above-mentioned drawbacks of the prior art or insufficient, the object of the present invention is to provide a kind of synthesis to chlorobenzene Phenol can temperature automatically controlled reaction kettle.
In order to solve the above technical problems, the technical scheme is that
A kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle, including guide shell (1), collet water inlet (2), collet go out The mouth of a river (3), water discharging valve (4), recirculated water valve (5), water pump (6), controller 1 (7), heating water tank (9), air inlet pipe (11), Electrically operated valve (12), water inlet pipe (13), outlet pipe (14), hot-water valve (15), inlet valve (16), chlorine inlet (17), gas Body distributor (18), feed pipe (19), liquid charging stock import (20), coil inlets (21), gas vent (22), safety valve (23), coil pipe water outlet (24), coil pipe (27), liquid outlet (28), temp-sensing device (29), reaction kettle ontology (30), sealing cover (31), sealing ring (32), installing port (33), collet (34) and controller 2 (35), reaction kettle ontology (30) setting are sealing The lower section for covering (31) is equipped with sealing ring (32) between the sealing cover (31) and reaction kettle ontology (30), the reaction kettle ontology (30) upper left-hand is equipped with liquid charging stock import (20), and the liquid charging stock import (20) is connected to feed pipe (19), described The outside of reaction kettle ontology (30) is equipped with collet (34), and the lower left side of the collet (34) is equipped with collet water inlet (2), the folder The upper right for covering (34) is equipped with collet water outlet (3), the upper left-hand of the sealing cover (31) be equipped with coil inlets (21), Gas vent (22) and two safety valves (23), the upper right of the sealing cover (31) is equipped with installing port (33) and coil pipe is discharged Mouth (24), the temp-sensing device (29) are mounted in reaction kettle ontology (30) by installing port (33) insertion, the temp-sensing device (29) it is electrically connected simultaneously with the input terminal of the input terminal of controller 1 (7) and controller 2 (35), the reaction kettle ontology (30) Inside be equipped with guide shell (1), the guide shell (1) is the cylinder of upper and lower opening, guide shell (1) bottom and reaction kettle ontology (30) direct tube section bottom flushes, which is lower than the height of reaction kettle ontology (30) interior reaction mass, is convenient for Reaction mass forms recycle stream by guide shell (1) in reaction kettle, and the bottom of the reaction kettle ontology (30) is equipped with liquid outlet (28) it is connected to chlorine inlet (17), described chlorine inlet (17) one end with air inlet pipe (11), the chlorine inlet (17) is another The lower end of ring-like gas distributor (18) center internal with guide shell (1) is set to is held to be connected to, the air inlet pipe (11) It is connected to by electrically operated valve (12) with chlorine pot, the output end and electrically operated valve (12) of the controller 2 (35) are electrically connected, just In the working condition by controller 2 (35) control electrically operated valve (12), the gas distributor (18) and guide shell (1) bottom It flushes, guarantees that bubble has sufficiently long motion path in reaction kettle, the coil pipe (27) hovers above on guide shell (1), the disk Pipe (27) both ends are connected to coil inlets (21) and coil pipe water outlet (24) respectively, and the heating water tank (9) is set to reaction The outside of kettle ontology (30), the heating water tank (9) are equipped with water outlet, water inlet end and circulation water inlet, the heating water tank (9) It is internally provided with electric heater (8) and liquidometer (10), the liquidometer (10) is used to detect the liquid level feelings in heating water tank (9) Condition, the controller 1 (7) are mounted on the outside of heating water tank (9), and the output end of the controller 1 (7) and electric heater (8) It is electrically connected, convenient for passing through the working condition of controller 1 (7) control electric heater (8), the collet water inlet (2) and coil pipe Water inlet (21) is connected to the output ends of water inlet pipe (13) simultaneously, the input terminal of the water inlet pipe (13) by hot-water valve (15) with The output end of water pump (6) is connected to, the water outlet of input terminal connection heating water tank (9) of the water pump (6), the heating water tank (9) water inlet end is connected to by inlet valve (16) with external water source, and the collet water outlet (3) and coil pipe water outlet (24) are same The output end of the input terminal of Shi Liantong outlet pipe (14), the outlet pipe (14) leads to drainage position by water discharging valve (4), simultaneously The circulation water inlet that the output end of the outlet pipe (14) passes through recirculated water valve (5) connection heating water tank (9).
Involved electrically operated valve (12) is commercially available;It can also be customized as needed to electrically operated valve specialized factory.
Involved controller 1 (7) and commercially available with controller 2 (35);It can also be fixed to controller specialized factory as needed System.
Involved heating water tank (9) is commercially available;It can also be customized as needed to heating water tank specialized factory.
Preferably, the synthesis parachlorophenol can temperature automatically controlled reaction kettle, wherein the gas distributor (18) Diameter is uniformly provided with along the length direction of gas distribution pipe (25) to be 4~5mm and open up the round venthole (26) of direction upward.
Preferably, the synthesis parachlorophenol can temperature automatically controlled reaction kettle, wherein the sealing ring (32) is poly- four Vinyl fluoride material.
Preferably, the synthesis parachlorophenol can temperature automatically controlled reaction kettle, wherein the guide shell (1), chlorine into Mouth (17), gas distributor (18), liquid charging stock import (20), coil inlets (21), gas vent (22), safety valve (23), coil pipe water outlet (24), coil pipe (27), liquid outlet (28), the measurement protection overcoat of temp-sensing device (29), reaction kettle ontology (30), sealing cover (31) and installing port (33) are corrosion resistant special steel material, the ingredient of the corrosion resistant special steel And mass percent are as follows: carbon 0.02%, chromium 16.5~17.5%, nickel 7%, copper 0.1%, tungsten 0.4%, niobium 0.5%, surplus are Iron, the sum of the above components are 100%.
By adopting the above-described technical solution, the beneficial effects of the present invention are:
1, it is of the present invention synthesis parachlorophenol can temperature automatically controlled reaction kettle use including collet and coil pipe automatic control Warm device is stable to keep the temperature of reaction kettle body interior, and side reaction occurs when avoiding reaction temperature excessively high leads to selective mistake The problems such as conversion ratio is too low when low and reaction temperature is too low, is conducive to controlled syntheses parachlorophenol.
2, it is of the present invention synthesis parachlorophenol can temperature automatically controlled reaction kettle dispersed by gas distributor input Chlorine, and recycle stream is formed in reaction kettle by guide shell, it contacts chlorine more fully with phenol solution, is conducive to mention Reaction efficiency when height synthesis parachlorophenol.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention.
Fig. 2 is the distribution schematic diagram of gas distributor of the present invention.
In figure: 1. guide shells, 2. collet water inlets, 3. collet water outlets, 4. water discharging valves, 5. recirculated water valves, 6. water Pump, 7. controller, 1,8. electric heater, 9. heating water tanks, 10. liquidometers, 11. air inlet pipe, 12. electrically operated valves, 13. water inlet pipes, 14. outlet pipe, 15. hot-water valves, 16. inlet valves, 17. chlorine inlets, 18. gas distributors, 19. feed pipes, 20. liquid Material inlet, 21. coil inlets, 22. gas vents, 23. safety valves, 24. coil pipe water outlets, 25. gas distribution pipes, 26. outlets Hole, 27. coil pipes, 28. liquid outlets, 29. temp-sensing devices, 30. reaction kettle ontologies, 31. sealing covers, 32. sealing rings, 33. installing ports, 34. collet, 35. controllers 2.
Specific embodiment
In order to make the objectives, technical solutions, and advantages of the present invention clearer, the present invention is made below in conjunction with attached drawing It is further to be described in detail.In the following description, descriptions of well-known structures and technologies are omitted, to avoid unnecessarily obscuring Idea of the invention.
Refering to fig. 1, Fig. 2.It is a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle, including guide shell (1), collet water inlet Mouthful (2), collet water outlet (3), water discharging valve (4), recirculated water valve (5), water pump (6), controller 1 (7), heating water tank (9), Air inlet pipe (11), electrically operated valve (12), water inlet pipe (13), outlet pipe (14), hot-water valve (15), inlet valve (16), chlorine Import (17), gas distributor (18), feed pipe (19), liquid charging stock import (20), coil inlets (21), gas vent (22), safety valve (23), coil pipe water outlet (24), coil pipe (27), liquid outlet (28), temp-sensing device (29), reaction kettle ontology (30), sealing cover (31), sealing ring (32), installing port (33), collet (34) and controller 2 (35).The reaction kettle ontology (30) it is arranged between the lower section of sealing cover (31), the sealing cover (31) and reaction kettle ontology (30) and is equipped with sealing ring (32), The upper left-hand of the reaction kettle ontology (30) is equipped with liquid charging stock import (20), the liquid charging stock import (20) and feed pipe (19) it is connected to, the outside of the reaction kettle ontology (30) is equipped with collet (34), and the lower left side of the collet (34) is equipped with collet The upper right of water inlet (2), the collet (34) is equipped with collet water outlet (3), and the upper left-hand of the sealing cover (31) is equipped with The upper right of coil inlets (21), gas vent (22) and two safety valves (23), the sealing cover (31) is equipped with installation Mouth (33) and coil pipe water outlet (24), the temp-sensing device (29) are mounted on reaction kettle ontology (30) by installing port (33) insertion Interior, which is electrically connected with the input terminal of the input terminal of controller 1 (7) and controller 2 (35) simultaneously, described anti- The inside of kettle ontology (30) is answered to be equipped with guide shell (1), the guide shell (1) is the cylinder of upper and lower opening, guide shell (1) bottom It is flushed with reaction kettle ontology (30) direct tube section bottom, which is lower than reaction kettle ontology (30) interior reactant The height of material forms recycle stream, the bottom of the reaction kettle ontology (30) by guide shell (1) convenient for reaction mass in reaction kettle Portion is equipped with liquid outlet (28) and chlorine inlet (17), and described chlorine inlet (17) one end is connected to air inlet pipe (11), the chlorine The lower end of import (17) other end ring-like gas distributor (18) center internal with guide shell (1) is set to is connected to, institute It states air inlet pipe (11) to be connected to by electrically operated valve (12) with chlorine pot, the output end and electrically operated valve of the controller 2 (35) (12) it is electrically connected, convenient for passing through the working condition of controller 2 (35) control electrically operated valve (12), the gas distributor (18) It is flushed with guide shell (1) bottom, guarantees that bubble has sufficiently long motion path in reaction kettle, the coil pipe (27), which hovers above, leads In flow cartridge (1), which is connected to coil inlets (21) and coil pipe water outlet (24) respectively, the heating water tank (9) it is set to the outside of reaction kettle ontology (30), which is equipped with water outlet, water inlet end and circulation water inlet, should Heating water tank (9) is internally provided with electric heater (8) and liquidometer (10), and the liquidometer (10) is for detecting heating water tank (9) level condition in, the controller 1 (7) are mounted on the outside of heating water tank (9), and the output end of the controller 1 (7) With electric heater (8) be electrically connected, convenient for by controller 1 (7) control electric heater (8) working condition, the collet into The mouth of a river (2) is connected to the output end of water inlet pipe (13) with coil inlets (21) simultaneously, and the input terminal of the water inlet pipe (13) passes through Hot-water valve (15) is connected to the output end of water pump (6), the water outlet of input terminal connection heating water tank (9) of the water pump (6), The water inlet end of the heating water tank (9) is connected to by inlet valve (16) with external water source, the collet water outlet (3) and coil pipe Water outlet (24) is connected to the input terminal of outlet pipe (14) simultaneously, and the output end of the outlet pipe (14) is logical by water discharging valve (4) To drainage position, while the output end of the outlet pipe (14) is entered by the recirculated water of recirculated water valve (5) connection heating water tank (9) Mouthful.
Involved electrically operated valve (12) is commercially available;It can also be customized as needed to electrically operated valve specialized factory.
Involved controller 1 (7) and commercially available with controller 2 (35);It can also be fixed to controller specialized factory as needed System.
Involved heating water tank (9) is commercially available;It can also be customized as needed to heating water tank specialized factory.
Preferably, the synthesis parachlorophenol can temperature automatically controlled reaction kettle, wherein the gas distributor (18) Diameter is uniformly provided with along the length direction of gas distribution pipe (25) to be 4~5mm and open up the round venthole (26) of direction upward.
Preferably, the synthesis parachlorophenol can temperature automatically controlled reaction kettle, wherein the sealing ring (32) is poly- four Vinyl fluoride material.
Preferably, the synthesis parachlorophenol can temperature automatically controlled reaction kettle, wherein the guide shell (1), chlorine into Mouth (17), gas distributor (18), liquid charging stock import (20), coil inlets (21), gas vent (22), safety valve (23), coil pipe water outlet (24), coil pipe (27), liquid outlet (28), the measurement protection overcoat of temp-sensing device (29), reaction kettle ontology (30), sealing cover (31) and installing port (33) are corrosion resistant special steel material, the ingredient of the corrosion resistant special steel And mass percent are as follows: carbon 0.02%, chromium 16.5~17.5%, nickel 7%, copper 0.1%, tungsten 0.4%, niobium 0.5%, surplus are Iron, the sum of the above components are 100%.
The operation principle of the present invention is that: feed pipe (19) and liquid charging stock import (20) are first passed through toward reaction kettle ontology (30) Inject a certain amount of phenol solution containing catalyst;Then inlet valve (16) are opened, injection is a certain amount of into heating water tank (9) Water after close inlet valve (16), water discharging valve (4);Then hot-water valve (15) and recirculated water valve (5) are successively opened, is opened Dynamic water pump (6), starting electric heater (8) are warming up to required temperature;Finally start electrically operated valve (12), make chlorine by chlorine into Mouth (17) and gas distributor (18) enter in reaction kettle, and chlorine and phenol solution are in gas distributor (18) and guide shell (1) With the help of come into full contact with, reacted in the presence of a catalyst.The hydrogen chloride gas that reaction generates passes through reaction kettle top Gas vent (22) drain into gas absorption equipment, the liquid reacting product of generation is discharged on demand from liquid outlet (28).Chlorine Category exothermic reaction is reacted with phenol, with the progress of reaction, material in reactor temperature is gradually risen, can pass through controller 1 (7) and controller 2 (35) are adjusted, and control reaction temperature between 50~85 DEG C.When temp-sensing device (29) detects reaction When kettle ontology (30) internal temperature is less than or equal to lower set temperature 1 (such as 55 DEG C), temperature signal is passed into controller 1 (7) and controller 2 (35), so that electric heater (8) and electrically operated valve (12) are kept it turned on.When temp-sensing device (29) are examined When measuring reaction kettle ontology (30) internal temperature higher than set temperature 1, temperature signal is passed to controller 1 by temp-sensing device (29) (7), after controller 1 (7) receives the temperature signal, circulation in reaction kettle coil pipe is reduced by powering off to electric heater (8) The temperature of medium water.When temp-sensing device (29) further detects that reaction kettle ontology (30) internal temperature is higher than higher setting temperature Spend 2 (such as 65 DEG C) when, after controller 2 (35) receives the temperature signal, by close electrically operated valve (12) come prevent chlorine with The generation of exothermic reaction between phenol, to reduce the temperature of solution in reaction kettle ontology.Hot-water valve is kept after reaction (15) open state opens inlet valve (16), water discharging valve (4), is then shut off recirculated water valve (5), electrically operated valve (12) After being cooled down with electric heater (8), liquid reacting product is taken out from the liquid outlet (28) of reaction kettle ontology (30) bottom.
After reaction 30 hours, gas chromatographic analysis, phenol conversion 98.62%, parachlorophenol are carried out to reaction product Ratio with o-chlorphenol is 57:43, and the mass percent of m-Chlorophenol is less than 1%.
The above description is merely a specific embodiment, is not intended to restrict the invention.It is any to be familiar with this technology neck In the technical scope disclosed by the present invention, any changes or substitutions that can be easily thought of by the technical staff in domain, should all cover in the present invention Protection scope within.Therefore, protection scope of the present invention should be based on the protection scope of the described claims.

Claims (4)

1. it is a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle, including guide shell (1), collet water inlet (2), collet water outlet Mouth (3), water discharging valve (4), recirculated water valve (5), water pump (6), controller 1 (7), heating water tank (9), air inlet pipe (11), electricity Movable valve (12), water inlet pipe (13), outlet pipe (14), hot-water valve (15), inlet valve (16), chlorine inlet (17), gas Distributor (18), feed pipe (19), liquid charging stock import (20), coil inlets (21), gas vent (22), safety valve (23), coil pipe water outlet (24), coil pipe (27), liquid outlet (28), temp-sensing device (29), reaction kettle ontology (30), sealing cover (31), sealing ring (32), installing port (33), collet (34) and controller 2 (35), it is characterised in that: the reaction kettle ontology (30) it is arranged between the lower section of sealing cover (31), the sealing cover (31) and reaction kettle ontology (30) and is equipped with sealing ring (32), The upper left-hand of the reaction kettle ontology (30) is equipped with liquid charging stock import (20), the liquid charging stock import (20) and feed pipe (19) it is connected to, the outside of the reaction kettle ontology (30) is equipped with collet (34), and the lower left side of the collet (34) is equipped with collet The upper right of water inlet (2), the collet (34) is equipped with collet water outlet (3), and the upper left-hand of the sealing cover (31) is equipped with The upper right of coil inlets (21), gas vent (22) and two safety valves (23), the sealing cover (31) is equipped with installation Mouth (33) and coil pipe water outlet (24), the temp-sensing device (29) are mounted on reaction kettle ontology (30) by installing port (33) insertion Interior, which is electrically connected with the input terminal of the input terminal of controller 1 (7) and controller 2 (35) simultaneously, described anti- The inside of kettle ontology (30) is answered to be equipped with guide shell (1), the guide shell (1) is the cylinder of upper and lower opening, guide shell (1) bottom It is flushed with reaction kettle ontology (30) direct tube section bottom, which is lower than reaction kettle ontology (30) interior reactant The height of material forms recycle stream, the bottom of the reaction kettle ontology (30) by guide shell (1) convenient for reaction mass in reaction kettle Portion is equipped with liquid outlet (28) and chlorine inlet (17), and described chlorine inlet (17) one end is connected to air inlet pipe (11), the chlorine The lower end of import (17) other end ring-like gas distributor (18) center internal with guide shell (1) is set to is connected to, institute It states air inlet pipe (11) to be connected to by electrically operated valve (12) with chlorine pot, the output end and electrically operated valve of the controller 2 (35) (12) it is electrically connected, convenient for passing through the working condition of controller 2 (35) control electrically operated valve (12), the gas distributor (18) It is flushed with guide shell (1) bottom, guarantees that bubble has sufficiently long motion path in reaction kettle, the coil pipe (27), which hovers above, leads In flow cartridge (1), which is connected to coil inlets (21) and coil pipe water outlet (24) respectively, the heating water tank (9) it is set to the outside of reaction kettle ontology (30), which is equipped with water outlet, water inlet end and circulation water inlet, should Heating water tank (9) is internally provided with electric heater (8) and liquidometer (10), and the liquidometer (10) is for detecting heating water tank (9) level condition in, the controller 1 (7) are mounted on the outside of heating water tank (9), and the output end of the controller 1 (7) With electric heater (8) be electrically connected, convenient for by controller 1 (7) control electric heater (8) working condition, the collet into The mouth of a river (2) is connected to the output end of water inlet pipe (13) with coil inlets (21) simultaneously, and the input terminal of the water inlet pipe (13) passes through Hot-water valve (15) is connected to the output end of water pump (6), the water outlet of input terminal connection heating water tank (9) of the water pump (6), The water inlet end of the heating water tank (9) is connected to by inlet valve (16) with external water source, the collet water outlet (3) and coil pipe Water outlet (24) is connected to the input terminal of outlet pipe (14) simultaneously, and the output end of the outlet pipe (14) is logical by water discharging valve (4) To drainage position, while the output end of the outlet pipe (14) is entered by the recirculated water of recirculated water valve (5) connection heating water tank (9) Mouthful.
2. as described in claim 1 synthesis parachlorophenol can temperature automatically controlled reaction kettle, which is characterized in that the gas distribution Device (18) is uniformly provided with diameter along the length direction of gas distribution pipe (25) and is 4~5mm and opens up the round venthole of direction upward (26)。
3. as described in claim 1 synthesis parachlorophenol can temperature automatically controlled reaction kettle, which is characterized in that the sealing ring (32) For polytetrafluoroethylene (PTFE) material.
4. as described in claim 1 synthesis parachlorophenol can temperature automatically controlled reaction kettle, which is characterized in that the guide shell (1), Chlorine inlet (17), gas distributor (18), liquid charging stock import (20), coil inlets (21), gas vent (22), safety Valve (23), coil pipe water outlet (24), coil pipe (27), liquid outlet (28), the measurement protection overcoat of temp-sensing device (29), reaction kettle sheet Body (30), sealing cover (31) and installing port (33) are corrosion resistant special steel material, the corrosion resistant special steel at Point and mass percent are as follows: carbon 0.02%, chromium 16.5~17.5%, nickel 7%, copper 0.1%, tungsten 0.4%, niobium 0.5%, surplus are Iron, the sum of the above components are 100%.
CN201811310059.5A 2018-10-23 2018-10-23 It is a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle Withdrawn CN109603727A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811310059.5A CN109603727A (en) 2018-10-23 2018-10-23 It is a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811310059.5A CN109603727A (en) 2018-10-23 2018-10-23 It is a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle

Publications (1)

Publication Number Publication Date
CN109603727A true CN109603727A (en) 2019-04-12

Family

ID=66002733

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811310059.5A Withdrawn CN109603727A (en) 2018-10-23 2018-10-23 It is a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle

Country Status (1)

Country Link
CN (1) CN109603727A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110404485A (en) * 2019-09-02 2019-11-05 铜陵学院 A kind of gas liquid reaction kettle using spherical micropore corundum steam-supplying device
CN113160901A (en) * 2021-03-24 2021-07-23 柳州东风容泰化工股份有限公司 Method and device for improving synthesis rate of chlorophenol

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105688775A (en) * 2016-04-26 2016-06-22 河北工业大学 Reactor with temperature control device
CN105749850A (en) * 2016-05-17 2016-07-13 南京科技职业学院 Special reactor for oriented synthesis of p-chlorotoluene
CN206103897U (en) * 2016-07-21 2017-04-19 中国科学院山西煤炭化学研究所 Controllable temperature water bath reation kettle
CN207446211U (en) * 2017-10-30 2018-06-05 汇智工程科技股份有限公司 Polymeric kettle thermostatic control system
CN207734999U (en) * 2017-12-22 2018-08-17 广东珠江化工涂料有限公司 Reaction kettle exothermic reaction temperature regulating device

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105688775A (en) * 2016-04-26 2016-06-22 河北工业大学 Reactor with temperature control device
CN105749850A (en) * 2016-05-17 2016-07-13 南京科技职业学院 Special reactor for oriented synthesis of p-chlorotoluene
CN206103897U (en) * 2016-07-21 2017-04-19 中国科学院山西煤炭化学研究所 Controllable temperature water bath reation kettle
CN207446211U (en) * 2017-10-30 2018-06-05 汇智工程科技股份有限公司 Polymeric kettle thermostatic control system
CN207734999U (en) * 2017-12-22 2018-08-17 广东珠江化工涂料有限公司 Reaction kettle exothermic reaction temperature regulating device

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
潘传九: "《化工设备机械基础》", 31 July 2002, 化学工业出版社 *
谭蔚: "《化工设备设计基础》", 31 August 2014, 天津大学出版社 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110404485A (en) * 2019-09-02 2019-11-05 铜陵学院 A kind of gas liquid reaction kettle using spherical micropore corundum steam-supplying device
CN113160901A (en) * 2021-03-24 2021-07-23 柳州东风容泰化工股份有限公司 Method and device for improving synthesis rate of chlorophenol
CN113160901B (en) * 2021-03-24 2023-01-03 柳州东风容泰化工股份有限公司 Method and device for improving synthesis rate of chlorophenol

Similar Documents

Publication Publication Date Title
CN109603727A (en) It is a kind of synthesis parachlorophenol can temperature automatically controlled reaction kettle
CN109603710A (en) It is a kind of synthesis p-chlorotoluene can temperature automatically controlled reaction kettle
CN104689763B (en) Oxidizing reaction device and use of oxidizing reaction device
CN110755866A (en) Chemical production is with circulating reation kettle of low energy consumption of high-efficient
CN109593030A (en) A kind of α, the preparation method of alpha-single chloro acetophenone compounds
DK177205B1 (en) Process and apparatus for producing hydrogen from methanol
CN209010425U (en) A kind of tetrahydrofuran reaction separating device
CN218485936U (en) Chlorination reaction device for producing trichloroacetic acid
CN107837781B (en) Reaction kettle for strong exothermic reaction
CN110314618A (en) Sectional integral type solid catalysis continuous reaction apparatus and continuous reaction system
CN103102369B (en) A kind of production method of diethyl ethylphosphate
CN215781617U (en) Chloroethylene high-boiling residue treatment and purification system
CN208742518U (en) Distillation and reflux device in 2,5- dimethoxy dihydrofuran synthetic reaction
CN114210282A (en) Industrial-grade continuous flow photochemical reactor
CN102974281A (en) Apparatus and method for continuous synthesis of long-chain fatty acid methyl esters
CN210303646U (en) Water adding inerting device for oxidation reaction of p-tert-butylbenzoic acid
CN208747974U (en) A kind of distillation and reflux device in 2,5- dimethoxy dihydrofuran synthetic reaction
CN213528673U (en) Reaction device for synthesizing chloroethanol
CN216946813U (en) Production device for alkyl cyanamide
CN219150142U (en) Chloroacetic acid synthesizer
CN103285613B (en) A kind of total reflux reaction distilling apparatus and synthetic method thereof of synthesizing terpinol
CN203990590U (en) Novel intelligent reactor
CN204891860U (en) Reation kettle with circulative cooling function
CN204824676U (en) Methyl alcohol purification system
CN110090602B (en) Hydrogenation reaction system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WW01 Invention patent application withdrawn after publication

Application publication date: 20190412

WW01 Invention patent application withdrawn after publication