CN205164696U - Reaction system with non -condensable gas eduction gear - Google Patents
Reaction system with non -condensable gas eduction gear Download PDFInfo
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- CN205164696U CN205164696U CN201520831050.4U CN201520831050U CN205164696U CN 205164696 U CN205164696 U CN 205164696U CN 201520831050 U CN201520831050 U CN 201520831050U CN 205164696 U CN205164696 U CN 205164696U
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- condensate
- liquid separator
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- condensable gas
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Abstract
The utility model discloses a reaction system with non -condensable gas eduction gear, the control unit comprises a reaction vessel, reation kettle with rise the steam pipe and be connected, rise the steam pipe and be connected with the top of condenser, the bottom of condenser is connected with vapour and liquid separator's upper end, vapour and liquid separator's lower extreme passes through the condensate back flow to be connected with reation kettle, vapour and liquid separator's upper end is equipped with the non -condensable gas discharge pipe, is equipped with in proper order on the condensate back flow that vapour and liquid separator is connected with reation kettle to look handleless cup I, condensate sample valve and condensate flowmeter, looks handleless cup I and is the U type with the condensate back flow that the condensate sample valve belonged to, is equipped with the non -condensable gas flowmeter on the non -condensable gas discharge pipe in proper order, looks handleless cup II and non -condensable gas sample valve. Adopt the utility model discloses afterwards, the separation efficiency of steam and incoagulable gas obtains the large increase, and condensate that the incoagulable gas was smugglied secretly is no longer than 2% of total amount, and easily measurement, observation, sampling analysis, and the condensation effect is better, the operation and maintenance is more convenient.
Description
Technical field
The utility model belongs to technical field of chemical, is specifically related to a kind of reaction system with on-condensible gas discharger.
Background technology
In Chemical Manufacture, with reactor supporting, need the reflux condensate device of discharging incoagulable gas, its vapours import and the condensate liquid backflow mouth of pipe normally same mouth of pipe, do not have the instrumentations such as flowmeter yet.Although structure is simple, often gas-liquid separation is insufficient, the easy entrained liquids of incoagulable gas, particularly carry lower boiling liquid secretly, be not only difficult to standard and cut metering, and cause loss of material, also easily make condenser pipe fouling even block, add the maintenance workload of condensing unit.
Utility model content
For problems of the prior art, the utility model provides a kind of reaction system with on-condensible gas discharger, and condensation effect is better, operation and maintenance is more convenient.
For solving the problems of the technologies described above, the utility model by the following technical solutions:
A kind of reaction system with on-condensible gas discharger, comprise reactor, described reactor is connected with Steam Pipe, Steam Pipe is connected with the top of condenser, the bottom of condenser is connected with the upper end of gas-liquid separator, the lower end of gas-liquid separator is connected with reactor by condensate liquid return duct, and the upper end of described gas-liquid separator is provided with on-condensible gas discharge pipe.
The condensate liquid return duct that described gas-liquid separator is connected with reactor is provided with successively and looks cup I, condensate liquid sample valve and condensate stream gauge, described in look the condensate liquid return duct at cup I and condensate liquid sample valve place U-shaped.
Described on-condensible gas discharge pipe is provided with on-condensible gas flowmeter successively, looks cup II and on-condensible gas sample valve.
Described condenser adopts shell-and-tube heat exchanger, and this condenser is installed according to vertical.
The beneficial effects of the utility model: after adopting the utility model, the separative efficiency of steam and incoagulable gas is greatly improved, the condensate liquid that incoagulable gas is carried secretly is no more than 2% of total amount, and is easy to metering, observation, sample analysis, and condensation effect is better, operation and maintenance is more convenient.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
As shown in Figure 1, a kind of reaction system with on-condensible gas discharger, comprises reactor, reactor is connected with Steam Pipe, and Steam Pipe is connected with the top of condenser, and condenser tube adopts shell-and-tube heat exchanger, and this condenser is installed according to vertical, be beneficial to heat exchange and fluid flowing.
The bottom of condenser is connected with the upper end of gas-liquid separator, the lower end of gas-liquid separator is connected with reactor by condensate liquid return duct, the upper end of described gas-liquid separator is provided with on-condensible gas discharge pipe, on-condensible gas discharge pipe is provided with successively on-condensible gas flowmeter, looks cup II and on-condensible gas sample valve.
The condensate liquid return duct that gas-liquid separator is connected with reactor is provided with successively and looks cup I, condensate liquid sample valve and condensate stream gauge, described in look the condensate liquid return duct at cup I and condensate liquid sample valve place U-shaped, to install condensate liquid sample valve.
The heat exchange area of condenser of the present utility model and the corresponding ratio of gas-liquid separator are every square metre of corresponding 10-100 liter.
The course of work of the present utility model is as follows: the steam of the band incoagulable gas volatilized from reactor, by Steam Pipe 1, after entering condenser 2 condensation, enters gas-liquid separator 7; Condensate liquid flows out from the bottom of gas-liquid separator 7, through condensate liquid return duct 8, looks cup I 9 and condensate stream gauge 12, is back to reactor 11; Incoagulable gas is discharged from the top of gas-liquid separator 7, through on-condensible gas discharge pipe 4, incoagulable gas flowmeter 6, looks cup II 5, enters incoagulable gas treatment process.Phegma and incoagulable gas are all measured by respective flowmeter, look cup observation, sample valve sample analysis, and can according to the situation of metering, observation and analysis, and the operating condition of adjustment reactor, makes it reach rational operating mode.
Above-described embodiment, just in order to technical conceive of the present utility model and feature are described, its objective is and is one of ordinary skilled in the art can be understood content of the present utility model and implement according to this, can not limit protection domain of the present utility model with this.The change of every equivalence done by the essence of the utility model content or modification, all should be encompassed in protection domain of the present utility model.
Claims (4)
1. the reaction system with on-condensible gas discharger, comprise reactor (11), it is characterized in that: described reactor (11) is connected with Steam Pipe (1), Steam Pipe (1) is connected with the top of condenser (2), the bottom of condenser (2) is connected with the upper end of gas-liquid separator (7), the lower end of gas-liquid separator (7) is connected with reactor (11) by condensate liquid return duct (8), and the upper end of described gas-liquid separator (7) is provided with on-condensible gas discharge pipe (4).
2. the reaction system with on-condensible gas discharger according to claim 1, it is characterized in that: the condensate liquid return duct (8) that described gas-liquid separator (7) is connected with reactor (11) is provided with successively and looks cup I (9), condensate liquid sample valve (10) and condensate stream gauge (12), described in look the condensate liquid return duct at cup I (9) and condensate liquid sample valve (10) place U-shaped.
3. the reaction system with on-condensible gas discharger according to claim 1, is characterized in that: described on-condensible gas discharge pipe (4) is provided with on-condensible gas flowmeter (6) successively, looks cup II (5) and on-condensible gas sample valve (3).
4. the reaction system with on-condensible gas discharger according to claim 1, is characterized in that: described condenser (1) adopts shell-and-tube heat exchanger, and this condenser is installed according to vertical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520831050.4U CN205164696U (en) | 2015-10-26 | 2015-10-26 | Reaction system with non -condensable gas eduction gear |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520831050.4U CN205164696U (en) | 2015-10-26 | 2015-10-26 | Reaction system with non -condensable gas eduction gear |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205164696U true CN205164696U (en) | 2016-04-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520831050.4U Active CN205164696U (en) | 2015-10-26 | 2015-10-26 | Reaction system with non -condensable gas eduction gear |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205164696U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106582478A (en) * | 2016-11-28 | 2017-04-26 | 魏成功 | Circulating reflux device in chemical engineering production |
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2015
- 2015-10-26 CN CN201520831050.4U patent/CN205164696U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106582478A (en) * | 2016-11-28 | 2017-04-26 | 魏成功 | Circulating reflux device in chemical engineering production |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |