CN206037737U - Be applied to high pressure condenser of fluoridation - Google Patents

Be applied to high pressure condenser of fluoridation Download PDF

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Publication number
CN206037737U
CN206037737U CN201620704889.6U CN201620704889U CN206037737U CN 206037737 U CN206037737 U CN 206037737U CN 201620704889 U CN201620704889 U CN 201620704889U CN 206037737 U CN206037737 U CN 206037737U
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China
Prior art keywords
tube
reading
low head
upper cover
inner chamber
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CN201620704889.6U
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Chinese (zh)
Inventor
姜毅
尹连阳
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Dalian Nine Fine Chemical Co Ltd
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Dalian Nine Fine Chemical Co Ltd
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Priority to CN201620704889.6U priority Critical patent/CN206037737U/en
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Abstract

The utility model provides a be applied to high pressure condenser of fluoridation, which comprises a housin, the tube sheet has been connected gradually in the upper end of casing, the upper cover, tube sheet under the lower extreme of casing has connected gradually, the low head, go up the tube sheet and be connected with a branch of heat exchange tube down between the tube sheet, be equipped with the tube side end opening on the low head, it is suitable for reading to be equipped with the tube side on the upper cover, tube side end opening and the tube side inner chamber through the low head suitable for reading, the heat exchange tube, the inner chamber of upper cover is linked together, casing side lower part is equipped with the shell side end opening, it is suitable for reading that the side upper portion of casing is equipped with the shell side, the shell side end opening is linked together with the shell side inner chamber through the casing suitable for reading, the inner chamber of low head be equipped with down the sieve, lower sieve lies in the following of lower tube sheet, pile up the raschig ring that has the nickel material and pack in every heat exchange tube. Compared with the prior art, there is the raschig ring of nickel material to pack owing to distribute in the heat exchange tube, has overcome the high pressure and fluoridized not high, the too big drawback of hydrogen fluoride loss of condenser capture efficiency under the reaction condition, to have reduced manufacturing cost.

Description

It is applied to the high pressure condenser of fluorination reaction
Technical field
This utility model is related to a kind of cold doubtful device, and particularly a kind of high pressure condenser for being applied to fluorination reaction is main to use In fluorination reaction of the picoline quasi-aromatic compound under the pressure of more than 3.0Mpa.
Background technology
Currently used for fluorination reaction high pressure condenser more than exchanged heat using shell and tube, including housing, the upper end of housing according to It is secondary to be connected with upper perforated plate, upper cover, lower perforated plate, low head is connected with turn in the lower end of housing, between upper perforated plate and lower perforated plate It is connected with a branch of heat exchanger tube, upper cover is provided with mouth under tube side, upper cover is provided with that tube side is suitable for reading, and mouth is suitable for reading with tube side under tube side By the inner chamber of low head, heat exchanger tube, upper cover intracavity inter-connection, housing side bottom is provided with mouth under shell side, the side of housing Face top is provided with that shell side is suitable for reading, mouth and the shell side intracavity inter-connection by housing suitable for reading under shell side.The condenser of this structure exists In high pressure fluorination reaction, the effect for trapping fluohydric acid gas is poor, and fluohydric acid gas consumption is larger, consumes many beyond reaction.
The content of the invention
The purpose of this utility model be to provide a kind of simple structure, trapping fluohydric acid gas effect it is good, fluorination hydrogen loss it is few, reduce The high pressure condenser for being applied to fluorination reaction of production cost, overcomes the deficiencies in the prior art.
The high pressure condenser for being applied to fluorination reaction of the present utility model, including housing, is sequentially connected in the upper end of housing There are upper perforated plate, upper cover, lower perforated plate, low head is connected with turn in the lower end of housing, is connected between upper perforated plate and lower perforated plate A branch of heat exchanger tube, low head are provided with mouth under tube side, and upper cover is provided with that tube side is suitable for reading, and under tube side, mouth is suitable for reading by under with tube side The inner chamber of end socket, heat exchanger tube, the intracavity inter-connection of upper cover, housing side bottom are provided with mouth under shell side, the side surface upper part of housing It is provided with that shell side is suitable for reading, mouth and the shell side intracavity inter-connection by housing suitable for reading under shell side;The inner chamber of described low head is provided with down Sieve plate, lower sieve plate are located at below described lower perforated plate, pile up the Raschig ring filler for having nickel material in each heat exchanger tube.
Described lower sieve plate is supported by lower supporting plate, is welded and fixed between lower supporting plate and low head;In upper cover Chamber is provided with upper sieve plate, and upper sieve plate is supported by upper backup pad, is welded and fixed between upper backup pad and upper cover.
The high pressure condenser for being applied to fluorination reaction of the present utility model, compared with prior art, due in heat exchanger tube The Raschig ring filler of nickel material is distributed with, overcomes that condenser arresting efficiency under the conditions of high pressure fluorination reaction is high, fluorination hydrogen loss The drawbacks of losing excessive, reduces production cost.
Description of the drawings
Fig. 1 is the structural representation of this utility model specific embodiment.
Specific embodiment
As shown in Figure 1:8 is cylinder shell, the upper end of housing 8 be connected with turn by bolt upper perforated plate 10, on seal 11.Lower perforated plate 5, low head 4 are connected with turn by bolt in the lower end of housing 8.Connect between upper perforated plate 10 and lower perforated plate 5 There are a branch of many parallel heat exchanger tubes 6.Low head 4 is provided with mouth 1 under tube side, and upper cover 11 is provided with tube side suitable for reading 12, tube side Lower mouth 1 is with tube side suitable for reading 12 by the inner chamber of low head 4, heat exchanger tube 6, the intracavity inter-connection of upper cover 11.8 side lower of housing Mouth 7 under shell side are provided with, the side surface upper part of housing 8 is provided with shell side suitable for reading 9, mouth 7 suitable for reading with shell side 9 is by the interior of housing 8 under shell side Chamber is connected.
The inner chamber of low head 4 is provided with lower sieve plate 3, and lower sieve plate 3 is located at below lower perforated plate 5, piles up in each heat exchanger tube 6 There is the Raschig ring filler of nickel material.
Lower sieve plate 3 is supported by lower supporting plate 2, is welded and fixed between lower supporting plate 2 and low head 4.In upper cover 11 Chamber is provided with upper sieve plate 13, and upper sieve plate 13 is supported by upper backup pad 14, is welded and fixed between upper backup pad 14 and upper cover 11.
As the Raschig ring filler of nickel material is distributed with heat exchanger tube 6, lower section is stopped by lower sieve plate 5, to prevent nickel The Raschig ring filler of material falls.During operation, filled with the Raschig ring filler of nickel material by the fluorination hydrogen fluid of 6 inner chamber of heat exchanger tube Tap is touched, and is increased the fluohydric acid gas of condensation and the contact area of uncooled hydrogen fluoride gas, is dropped low gas velocity, so as to increase heat exchange effect Rate, the effect for strengthening trapping fluohydric acid gas.Overcome that condenser arresting efficiency under the conditions of high pressure fluorination reaction is high, fluorination hydrogen loss Excessive the drawbacks of, reduce production cost.

Claims (2)

1. a kind of high pressure condenser for being applied to fluorination reaction, including housing(8), in housing(8)Upper end be connected with turn Tube sheet(10), upper cover(11), in housing(8)Lower end be connected with lower perforated plate in turn(5), low head(4), upper perforated plate(10)With Lower perforated plate(5)Between be connected with a branch of heat exchanger tube(6), low head(4)It is provided with mouth under tube side(1), upper cover(11)It is provided with Tube side is suitable for reading(12), mouth under tube side(1)It is suitable for reading with tube side(12)By low head(4)Inner chamber, heat exchanger tube(6), upper cover (11)Intracavity inter-connection, housing(8)Side lower is provided with mouth under shell side(7), housing(8)Side surface upper part to be provided with shell side suitable for reading (9), mouth under shell side(7)It is suitable for reading with shell side(9)By housing(8)Intracavity inter-connection;It is characterized in that:Described low head (4)Inner chamber be provided with lower sieve plate(3), lower sieve plate(3)Positioned at described lower perforated plate(5)Below, in each heat exchanger tube(6)Interior heap Product has the Raschig ring filler of nickel material.
2. the high pressure condenser for being applied to fluorination reaction according to claim 1, it is characterised in that:Described lower sieve plate (3)By lower supporting plate(2)Support, lower supporting plate(2)With low head(4)Between be welded and fixed;In upper cover(11)Inner chamber sets There is upper sieve plate(13), upper sieve plate(13)By upper backup pad(14)Support, upper backup pad(14)With upper cover(11)Between weld It is fixed.
CN201620704889.6U 2016-07-06 2016-07-06 Be applied to high pressure condenser of fluoridation Active CN206037737U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620704889.6U CN206037737U (en) 2016-07-06 2016-07-06 Be applied to high pressure condenser of fluoridation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620704889.6U CN206037737U (en) 2016-07-06 2016-07-06 Be applied to high pressure condenser of fluoridation

Publications (1)

Publication Number Publication Date
CN206037737U true CN206037737U (en) 2017-03-22

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620704889.6U Active CN206037737U (en) 2016-07-06 2016-07-06 Be applied to high pressure condenser of fluoridation

Country Status (1)

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CN (1) CN206037737U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020077757A1 (en) * 2018-10-17 2020-04-23 中广核工程有限公司 Passive condenser for nuclear power plant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020077757A1 (en) * 2018-10-17 2020-04-23 中广核工程有限公司 Passive condenser for nuclear power plant

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