CN205007618U - Condenser pipe with gas -liquid separation - Google Patents

Abstract

The utility model discloses a condenser pipe with gas -liquid separation, during saying, material exchange pipe is equipped with the admission line, admission line fixed connection is on material exchange pipe says, what the upper end of admission line was provided with that the raw materials liquid that is used for preventing the condensation falls into the admission line hinders the liquid lid, it sets up in admission line upper end open -ended top and does not contact with the admission line to hinder the liquid lid. The utility model discloses a material exchange pipe says and is arranged in carrying high temperature raw materials steam and from the former feed liquid of condenser pipe to reaction vessel transport condensation, having set up one section admission line in this material exchange pipe says to the condenser pipe from reaction vessel to set up in admission line top and hinder the liquid lid, make the admitting air and go out liquid and realized the reposition of redundant personnel of condenser pipe, thereby the steam of having avoided gushing takes place to obstruct in material exchange pipe says with the condensation result, has improved condensation efficiency, has also improved the security of installing.

Description

With the condenser pipe of gas-liquid separation device

Technical field

The utility model relates to a kind of condensing unit heating reaction vessel, and more particularly, it relates to a kind of condenser pipe with gas-liquid separation device.

Background technology

Reactor is produced at modern industry, be widely used in particularly materials processing industry, have in reactor a kind of heat reactor materials synthesis processing in time a kind of very important production equipment, owing to adding in thermal response, the raw material of material requested is by thermal evaporation, if reactor is water-tight equipment, along with the raising of material gasification degree, pressure in reactor can be increasing, the still that probably can induce reaction bursts, cause security incident, therefore pressure regulating equipment reactor needing the steam arranged for discharging HTHP in reactor is heated, but the steam in reactor is all the steam after material gasification, if directly steam discharge can be caused the loss and waste of raw material, be unfavorable for saving production cost, therefore we need one can either make feedstock vapor discharge reactor that raw material can not be allowed again directly to spill into wasting decompressor in environment.

Publication number is that the open file of CN202621162U discloses a kind of reactor with condenser pipe, should

Reactor comprises condenser pipe one, condenser pipe two, oral siphon one, oral siphon two, outlet pipe one, outlet pipe two, rectangular support frame one, rectangular support frame two, two rectangular support frames are welded on top cover, oral siphon one and outlet pipe one are supported by rectangular support frame one, oral siphon two and outlet pipe two are supported by rectangular support frame two, two mouths of pipe of condenser pipe one are exposed at outside kettle, and be connected with oral siphon one and outlet pipe one respectively, two mouths of pipe of condenser pipe two are exposed at outside kettle, and be connected with oral siphon two and outlet pipe two respectively, the condenser pipe of such setting, when air pressure rising during raw material liq gasification in reactor, high-temperature steam is pushed in condenser pipe, condenser pipe is connected with oral siphon and outlet pipe, high-temperature steam in condenser pipe is met condensation knot and is become droplet and converge and flow back in reactor via condenser pipe, but the gas rising passway of this condenser pipe and liquid reflux channel are same passage, when reacting violent in reactor, the amount of the steam risen and the liquid of decline is all very large, when the two meets at the mouth of pipe of coupled reaction still and condenser pipe, the situation that gas-liquid is blocked up can be there is, if raw materials used liquid viscosity is higher, gas even can be caused to gush, affect the safe handling of equipment, therefore a kind of condenser pipe that can realize gas-liquid shunting is needed.

Utility model content

For the deficiency that prior art exists, the purpose of this utility model is to provide a kind of condenser pipe with gas-liquid separation device.

For achieving the above object, the utility model provides following technical scheme: a kind of condenser pipe with gas-liquid separation device, comprise condenser pipe, described condenser pipe comprises condensation part and the material for allowing steam rising and liquid fall exchanges pipeline, one end that described material exchanges pipeline is connected with reaction vessel, the other end connects on condensation part, : described material exchanges in pipeline and is provided with admission line, described admission line is connected to material and exchanges on pipeline, the upper port of described admission line is provided with the blocking solution lid for realizing gas-liquid shunting, described blocking solution lid is arranged on the top of admission line upper end open and and has gap between admission line.

Preferably, the outer wall of described admission line is fixedly installed fixed bar, the other end of described fixed bar is fixedly connected on material and exchanges on the inwall of pipeline.

Preferably, described blocking solution lid is cone shape, and the blocking solution caping point of described cone shape is towards condenser pipe.

Preferably, the diameter of the bottom surface of described blocking solution lid is greater than admission line, and the basal diameter of blocking solution lid is less than material exchange pipeline.

Preferably, connection is fixed by connecting rod between described blocking solution lid and admission line.

Compared with prior art the utility model has following advantage: material exchanges pipeline and is used for carrying high temperature feedstock vapor from reaction vessel to condenser pipe and to reaction vessel, carrying the material liquid of condensation from condenser pipe, exchange in pipeline at this material and set up one section of admission line, and blocking solution lid is set above admission line, the air inlet of condenser pipe and fluid is made to achieve shunting, thus avoid the steam of gushing and condensed product and exchange in pipeline at material implode occurs, improve condensation efficiency, also improve the security of device.

Accompanying drawing explanation

The sectional view of Fig. 1 when to be the utility model assemble on the reaction vessel with the condenser pipe of gas-liquid separation device;

Fig. 2 is the partial enlarged drawing of part A in Fig. 1;

The outside drawing of Fig. 3 when to be the utility model assemble on the reaction vessel with the condenser pipe of gas-liquid separation device.

In figure: 1, condenser pipe; 11, blocking solution lid; 12, admission line; 13, fixed bar; 14, material exchanges pipeline; 15, connecting rod; 2, reaction vessel.

Detailed description of the invention

Referring to figs. 1 through Fig. 2, condenser pipe 1 embodiment of the utility model with gas-liquid separation device is described further.

A kind of condenser pipe 1 with gas-liquid separation device, comprise condenser pipe 1, condenser pipe 1 comprises condensation part and the material for allowing steam rising and liquid fall exchanges pipeline 14, one end that material exchanges pipeline 14 is connected with reaction vessel 2, the other end that material exchanges pipeline 14 connects on condensation part, material exchanges in pipeline 14 and is provided with admission line 12, admission line 12 is fixedly connected on material and exchanges on pipeline 14, the upper port of admission line 12 is provided with the blocking solution lid 11 for preventing the raw material liq of condensation from falling into admission line 12, blocking solution lid 11 is arranged on the top of admission line 12 upper end open and does not contact with admission line 12, such structure can make high-temperature steam enter from admission line 12 and pour in condenser pipe 1 from the space between blocking solution lid 11 and admission line 12, and can not with the droplets of feed that falls in condenser pipe 1 to collision, simultaneously, the droplets of feed that condensation falls to drop on blocking solution lid 11 and flows to admission line 12 through blocking solution lid 11 and material exchanges in the space between pipeline 14, flow into reaction vessel 2 via space and proceed reaction, such structure can realize the gas-liquid separation in condensing reflux process well, thus effectively prevent gas-liquid share one Cemented filling time contingent jam, the efficiency of condensing reflux can be improved, the vibrations of springing up of causing and whole device because gas-liquid liquidates can be reduced again, be conducive to the security improving whole device.

Admission line 12 fixed bar 13 is fixedly connected in material exchange pipeline 14, it is concentric that admission line 12 preferably exchanges pipeline 14 with material, the high-temperature steam being so both conducive to rising enters condenser via admission line 12, be conducive to again the raw material liq four that condensation obtains to be scattered back reaction vessel 2, blocking solution lid 11 is fixedly installed on directly over admission line 12 upper port with connecting rod 15, and blocking solution lid 11 is cone shape, blocking solution lid 11 summit of cone shape is towards condenser pipe 1, such blocking solution lid 11 can allow raw material liq thereon flow in the space between material exchanging tube road 14 and admission line 12 through the side of cone shape blocking solution lid 11, the diameter of the bottom surface of blocking solution lid 11 is greater than admission line 12, and the basal diameter of blocking solution lid 11 is less than material exchange pipeline 14, raw material liq can be made like this to fall into material smoothly and to exchange space between pipeline 14 and admission line 12, and admission line 12 can not be fallen into, thus ideally realize gas-liquid separation in pipe.

The above is only preferred embodiment of the present utility model, protection domain of the present utility model be not only confined to above-described embodiment, and all technical schemes belonged under the utility model thinking all belong to protection domain of the present utility model.It should be pointed out that for those skilled in the art, do not departing from the some improvements and modifications under the utility model principle prerequisite, these improvements and modifications also should be considered as protection domain of the present utility model.

Claims (5)

1. the condenser pipe with gas-liquid separation device, comprise condenser pipe, described condenser pipe comprises condensation part and the material for allowing steam rising and liquid fall exchanges pipeline, one end that described material exchanges pipeline is connected with reaction vessel, the other end connects on condensation part, it is characterized in that: described material exchanges in pipeline and is provided with admission line, described admission line is connected to material and exchanges on pipeline, the upper port of described admission line is provided with the blocking solution lid for realizing gas-liquid shunting, described blocking solution lid is arranged on the top of admission line upper end open and and has gap between admission line.

2. the condenser pipe with gas-liquid separation device according to claim 1, is characterized in that: the outer wall of described admission line is fixedly installed fixed bar, and the other end of described fixed bar is fixedly connected on material and exchanges on the inwall of pipeline.

3. the condenser pipe with gas-liquid separation device according to claim 1, is characterized in that: described blocking solution lid is cone shape, and the blocking solution caping point of described cone shape is towards condenser pipe.

4. the condenser pipe with gas-liquid separation device according to claim 3, is characterized in that: the diameter of the bottom surface of described blocking solution lid is greater than admission line, and the basal diameter of blocking solution lid is less than material exchange pipeline.

5. the condenser pipe with gas-liquid separation device according to claim 3, is characterized in that: fix connection by connecting rod between described blocking solution lid and admission line.