CN207913773U - A kind of chemical reaction kettle with condensing unit - Google Patents

A kind of chemical reaction kettle with condensing unit Download PDF

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Publication number
CN207913773U
CN207913773U CN201820160012.4U CN201820160012U CN207913773U CN 207913773 U CN207913773 U CN 207913773U CN 201820160012 U CN201820160012 U CN 201820160012U CN 207913773 U CN207913773 U CN 207913773U
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CN
China
Prior art keywords
reaction kettle
substrate
condensing unit
condenser
gas
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
CN201820160012.4U
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Chinese (zh)
Inventor
袁厚华
袁志恩
沈荣
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Shanghai Badefu Industrial Co Ltd
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Shanghai Badefu Industrial 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
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Application filed by Shanghai Badefu Industrial Co Ltd filed Critical Shanghai Badefu Industrial Co Ltd
Priority to CN201820160012.4U priority Critical patent/CN207913773U/en
Application granted granted Critical
Publication of CN207913773U publication Critical patent/CN207913773U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The utility model provides a kind of chemical reaction kettle with condensing unit, including emulsion tank substrate, reaction kettle substrate, emulsion feed pipe, emulsion feed pipe is connected to the feed inlet of the discharge port of emulsion tank substrate, reaction kettle substrate, reaction kettle substrate is provided with gas outlet and liquid inlet, and emulsion tank is provided with air intake;The gas outlet is equipped with circulating condensing unit, circulating condensing unit includes the vertical (type) condenser for being sequentially connected to gas outlet, horizontal condenser, the gas backstreaming pipe that the end of horizontal condenser is equipped with the liquid return tube being connect with the liquid inlet of reaction kettle substrate, is connect with the air intake of emulsion tank, to reach the cooling time for extending gas, increase film-cooled heat, fully use raw material, reduce the loss of raw material, reduce production cost, the discharge capacity for reducing tail gas, reduces the purpose of environmental protection pressure.

Description

A kind of chemical reaction kettle with condensing unit
Technical field
The utility model is related to a kind of chemical reaction kettles with condensing unit.
Background technology
Existing reaction kettle is generally used to complete the processing of industrial chemicals or experiment is used.Especially, it is prepared in lotion In the process, the raw material in emulsion tank is inputted by feed pipe in reaction kettle and is stirred.
However, in practical applications, the volatile unstrpped gas in reaction kettle fails fully to condense on vertical (type) condenser Gas directly discharge outward, increase the loss of raw material, improve production cost, and increase the discharge capacity of tail gas, increase environmental protection Pressure.
Utility model content
The purpose of the utility model is to overcome the deficiencies in the prior art, provide a kind of chemical reaction with condensing unit Kettle, it is simple in structure, raw material is fully used, the loss of raw material is reduced, production cost is reduced, reduces the discharge capacity of tail gas, is reduced Environmental protection pressure.
What the purpose of utility model of the utility model was realized in:A kind of chemical reaction kettle with condensing unit, packet Emulsion tank substrate, reaction kettle substrate, emulsion feed pipe are included, emulsion feed pipe is connected to the discharging of emulsion tank substrate Mouthful, the feed inlet of reaction kettle substrate, wherein the reaction kettle substrate is provided with gas outlet and liquid inlet, emulsion tank substrate be provided with into Gas port;The gas outlet is equipped with circulating condensing unit, and circulating condensing unit includes be sequentially connected to gas outlet vertical cold Condenser, horizontal condenser, the end of horizontal condenser be equipped with the liquid return tube being connect with the liquid inlet of reaction kettle substrate, with The gas backstreaming pipe of the air intake connection of emulsion tank substrate.
It is optimized according to above-mentioned, the reaction kettle substrate, vertical (type) condenser, horizontal condenser, liquid return tube are formed First time gas circulation condenses path.
It is optimized according to above-mentioned, the emulsion tank substrate is equipped with the vertical cooling being connect with external exhaust gas collecting part Device.
It is optimized according to above-mentioned, it is the reaction kettle substrate, vertical (type) condenser, horizontal condenser, gas backstreaming pipe, vertical Cooler, emulsion tank substrate, emulsion feed pipe form second of gas circulation and condense path.
It is optimized according to above-mentioned, the liquid return tube includes liquid reflux rake, liquid reflux U-shaped portion, liquid Reflux rake, liquid reflux U-shaped portion are sequentially connected to horizontal condenser, on reaction kettle substrate.
The utility model has the advantage of:
1) by the respective outer side edges of reaction kettle substrate, vertical (type) condenser, horizontal condenser, liquid return tube, gas is extended The cooling time of body, increase film-cooled heat so that the raw material not being condensed in time in the three-dimensional condenser of reaction kettle substrate Gas when flowing in horizontal condenser, is liquefied, and is back in reaction kettle substrate and participates in processing, fully uses raw material, reduces Production cost;
2) complex reaction kettle substrate, vertical (type) condenser, horizontal condenser, gas backstreaming pipe, upright radiator, emulsion tank base The structure of part, emulsion feed pipe, upright radiator flows through the gas warp that reaction kettle substrate the whole series condensing unit is not liquefied Upright radiator from gas backstreaming pipe to emulsion tank substrate, after being liquefied, be back on emulsion tank substrate and by emulsion into Expects pipe participates in reaction on reaction kettle substrate, reduces the loss of raw material, fully profit raw material to a greater degree, reduces the discharge of tail gas Amount, reduces environmental protection pressure.
Description of the drawings
Attached drawing 1 is the utility model compared with the structural schematic diagram for hanging embodiment.
Specific implementation mode
The utility model will be further described below in conjunction with the accompanying drawings.
With reference to the accompanying drawings shown in 1, the chemical reaction kettle with condensing unit of the utility model, including it is emulsion tank substrate 1, anti- Answer kettle substrate 2, emulsion feed pipe 3.Emulsion feed pipe 3 is connected to the discharge port of emulsion tank substrate 1, reaction kettle substrate 2 feed inlet.Wherein, the reaction kettle substrate 2 is provided with gas outlet and liquid inlet, and emulsion tank substrate 1 is provided with air intake.It is described go out Gas port is equipped with circulating condensing unit, and circulating condensing unit includes the vertical (type) condenser 4 for being sequentially connected to gas outlet, horizontal cold Condenser 5.The end of horizontal condenser 5 is equipped with the liquid return tube 6 and emulsion tank being connect with the liquid inlet of reaction kettle substrate 2 The gas backstreaming pipe 7 of the air intake connection of substrate 1.
It is embodied in, the reaction kettle substrate 2, vertical (type) condenser 4, horizontal condenser 5, liquid return tube 6 form the One time gas circulation condenses path.During reaction kettle substrate 2 reacts, in the three-dimensional condenser of reaction kettle substrate 2 not in time The unstrpped gas being condensed is liquefied when flowing in horizontal condenser 5, and is back in reaction kettle substrate 2 and participates in processing.Prolong It increases film-cooled heat the cooling time for having grown gas, fully uses raw material, reduce production cost.
Wherein, the reaction kettle substrate 2, vertical (type) condenser 4, horizontal condenser 5, gas backstreaming pipe 7, emulsion tank substrate 1, Emulsion feed pipe 3 forms second of gas circulation and condenses path.The emulsion tank substrate 1 is equipped with and external exhaust gas collecting part The upright radiator 8 of connection.When generating the gas for flowing through a whole set of condensing unit of reaction kettle substrate 2 and not being liquefied, unstrpped gas passes through Gas backstreaming pipe 7 after being liquefied, is back on emulsion tank substrate 1 to the upright radiator 8 of emulsion tank substrate 1 and passes through emulsification Liquid feed pipe 3 participates in reaction on reaction kettle substrate 2, to reduce the loss of raw material, fully profit raw material to a greater degree, reduces The discharge capacity of tail gas, reduces environmental protection pressure.
Shown in referring to Fig.1, the liquid return tube 6 includes liquid reflux rake 61, liquid reflux U-shaped portion 62, liquid Reflux rake 61, liquid reflux U-shaped portion 62 are sequentially connected to horizontal condenser 5, on reaction kettle substrate 2.In this way so that in liquid Body return duct 6 allows raw material liq to flow into reaction kettle substrate 2, does not allow unstrpped gas to flee upwards from liquid return tube 6, makes It obtains the raw material being liquefied in horizontal condenser 5 to flow back in reaction kettle substrate 2 by liquid return tube 6, reduces the loss of raw material, Fully profit raw material, reduces the discharge capacity of tail gas, reduces environmental protection pressure.
Above-mentioned specific embodiment is only the preferable specific implementation mode of the utility model effect, all bands with the utility model The structure for having the chemical reaction kettle of condensing unit identical or equivalent, it is within the protection scope of the present utility model.

Claims (5)

1. a kind of chemical reaction kettle with condensing unit, including the charging of emulsion tank substrate (1), reaction kettle substrate (2), emulsion It manages (3), emulsion feed pipe (3) is connected to the feed inlet of the discharge port of emulsion tank substrate (1), reaction kettle substrate (2), It is characterized in that:The reaction kettle substrate (2) is provided with gas outlet and liquid inlet, and emulsion tank substrate (1) is provided with air intake;The outlet Mouthful it is equipped with circulating condensing unit, circulating condensing unit includes the vertical (type) condenser (4) for being sequentially connected to gas outlet, horizontal cold Condenser (5), the end of horizontal condenser (5) be equipped with the liquid return tube (6) being connect with the liquid inlet of reaction kettle substrate (2), The gas backstreaming pipe (7) being connect with the air intake of emulsion tank substrate (1).
2. carrying the chemical reaction kettle of condensing unit according to claim 1, it is characterised in that:The reaction kettle substrate (2), Vertical (type) condenser (4), horizontal condenser (5), liquid return tube (6) form first time gas circulation and condense path.
3. carrying the chemical reaction kettle of condensing unit according to claim 1, it is characterised in that:The emulsion tank substrate (1) Equipped with the upright radiator (8) being connect with external exhaust gas collecting part.
4. carrying the chemical reaction kettle of condensing unit according to claim 3, it is characterised in that:The reaction kettle substrate (2), Vertical (type) condenser (4), horizontal condenser (5), gas backstreaming pipe (7), upright radiator (8), emulsion tank substrate (1), emulsion Feed pipe (3) forms second of gas circulation and condenses path.
5. according to the chemical reaction kettle for carrying condensing unit described in any one of Claims 1-4, it is characterised in that:The liquid Return duct (6) includes liquid reflux rake (61), liquid reflux U-shaped portion (62), liquid reflux rake (61), liquid reflux U-shaped portion (62) is sequentially connected to horizontal condenser (5), on reaction kettle substrate (2).
CN201820160012.4U 2018-01-30 2018-01-30 A kind of chemical reaction kettle with condensing unit Expired - Fee Related CN207913773U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820160012.4U CN207913773U (en) 2018-01-30 2018-01-30 A kind of chemical reaction kettle with condensing unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820160012.4U CN207913773U (en) 2018-01-30 2018-01-30 A kind of chemical reaction kettle with condensing unit

Publications (1)

Publication Number Publication Date
CN207913773U true CN207913773U (en) 2018-09-28

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820160012.4U Expired - Fee Related CN207913773U (en) 2018-01-30 2018-01-30 A kind of chemical reaction kettle with condensing unit

Country Status (1)

Country Link
CN (1) CN207913773U (en)

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Granted publication date: 20180928