CN207019491U - Vapour-recovery unit - Google Patents

Vapour-recovery unit Download PDF

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Publication number
CN207019491U
CN207019491U CN201720669657.6U CN201720669657U CN207019491U CN 207019491 U CN207019491 U CN 207019491U CN 201720669657 U CN201720669657 U CN 201720669657U CN 207019491 U CN207019491 U CN 207019491U
Authority
CN
China
Prior art keywords
tank body
decompression
feed pipe
pipe
hush pipe
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
CN201720669657.6U
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Chinese (zh)
Inventor
张新民
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.)
XINJIANG MODERN PETROCHEMICAL INDUSTRY CO LTD
Original Assignee
XINJIANG MODERN PETROCHEMICAL INDUSTRY 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
Publication date
Application filed by XINJIANG MODERN PETROCHEMICAL INDUSTRY CO LTD filed Critical XINJIANG MODERN PETROCHEMICAL INDUSTRY CO LTD
Priority to CN201720669657.6U priority Critical patent/CN207019491U/en
Application granted granted Critical
Publication of CN207019491U publication Critical patent/CN207019491U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

Vapour-recovery unit technical field is the utility model is related to, is a kind of vapour-recovery unit, it includes tank body, feed pipe, decompression hush pipe and drainage conduit;Tank body is totally enclosed tank body, feed pipe is communicated with the upper end of tank body, the port of export of feed pipe is located at tank interior, the entrance point of hush pipe is depressured together with the port of export closed communication of feed pipe, closed relative to the other end of the decompression hush pipe of decompression hush pipe entrance point, steam vent is distributed with the decompression hush pipe body of decompression hush pipe entrance point, the gross area of all steam vents is more than the cross-sectional area of feed pipe.The utility model reasonable and compact in structure, the utility model can effectively reclaim the high steam for still carrying residual temperature after industrial production utilizes, high steam is set to be discharged after being changed into condensate through drainage conduit, carry out the utilization of next step or concentrate discharge, avoid polluting environment, it also avoid the waste of resource.

Description

Vapour-recovery unit
Technical field
Vapour-recovery unit technical field is the utility model is related to, is a kind of vapour-recovery unit.
Background technology
At present in the industrial production, many processes are had and use high temperature and high pressure steam, but crosses very much high temperature and high pressure steam and exists Just it is directly discharged to after utilization in atmospheric environment, this some vapor being discharged into atmospheric environment also carries part residual temperature, Atmospheric environment can undoubtedly be polluted, and cause the waste of resource, there is no the device for being capable of effective recovered steam at present.
The content of the invention
The utility model provides a kind of vapour-recovery unit, overcomes the deficiency of above-mentioned prior art, and it can effectively be solved Certainly there is no at present can effectively reclaim the device problem of the steam after industrial production utilizes.
The technical solution of the utility model is realized by following measures:A kind of vapour-recovery unit, including tank body, Feed pipe, decompression hush pipe and drainage conduit;Tank body is totally enclosed tank body, and feed pipe, feed pipe are communicated with the upper end of tank body The port of export be located at tank interior, be depressured the entrance point of hush pipe together with the port of export closed communication of feed pipe, relative to The other end closing of the decompression hush pipe of hush pipe entrance point is depressured, close to the decompression hush pipe body of decompression hush pipe entrance point On be distributed with steam vent, the gross area of all steam vents is more than the cross-sectional area of feed pipe, is provided with the bottom outside of tank body The drainage conduit being connected with tank body, is serially connected with discharge pump in drainage conduit.
Above-mentioned vapour-recovery unit can be made further optimization and/or improvements according to being actually needed:
Here is the further optimization and/or improvements to above-mentioned utility model technical scheme:
The above-mentioned top outer in tank body is provided with the evacuated tube with being connected in tank body, and safety is serially connected with evacuated tube Valve.
The utility model reasonable and compact in structure, the utility model can effectively reclaim the still band after industrial production utilizes There is the high steam of residual temperature, high steam is discharged after being changed into condensate through drainage conduit, carry out utilization or the row of concentration of next step Put, avoid polluting environment, it also avoid the waste of resource.
Brief description of the drawings
Accompanying drawing 1 is the main view perspective structure schematic diagram of the best embodiment of the utility model.
Coding in accompanying drawing is respectively:1 is tank body, and 2 be feed pipe, and 3 be decompression hush pipe, and 4 be steam vent, and 5 be discharge Pipe, 6 be evacuated tube, and 7 be safety valve, and 8 be discharge pump.
Embodiment
The utility model is not limited by following embodiments, can according to the technical solution of the utility model and actual conditions come Determine specific embodiment.
In the utility model, for the ease of description, the description of the relative position relation of each part is according to specification The Butut mode of accompanying drawing 1 is described, such as:The position relationship of upper and lower, left and right etc. is the Butut according to Figure of description Direction determines.
The utility model is further described with reference to embodiment and accompanying drawing:
As shown in Figure 1, the vapour-recovery unit includes tank body 1, feed pipe 2, decompression hush pipe 3 and drainage conduit 5;Tank body 1 is totally enclosed tank body 1, and feed pipe 2 is communicated with the upper end of tank body 1, and the port of export of feed pipe 2 is located inside tank body 1, decompression The entrance point of hush pipe 3 is together with the port of export closed communication of feed pipe 2, relative to the decompression of the decompression entrance point of hush pipe 3 The other end closing of hush pipe 3, steam vent 4, institute are distributed with the body of decompression hush pipe 3 of the decompression entrance point of hush pipe 3 The gross area for having steam vent 4 is more than the cross-sectional area of feed pipe 2, is provided with the bottom outside of tank body 1 and is connected with tank body 1 Drainage conduit 5, discharge pump 8 is serially connected with drainage conduit 5.
The still high steam with residual temperature after industrial production utilizes is recycled in tank body 1 by feed pipe 2, is entered The high steam of feed pipe 2 is then into being depressured in hush pipe 3, because the gross area of all steam vents 4 is more than feed pipe 2 Cross-sectional area, therefore, pressure substantially reduces after high steam is entered in tank body 1, and high steam cooling in tank body 1 is changed into solidifying Tie in water-laid tank body 1, finally discharged by discharge pump 8 through drainage conduit 5.
The utility model can effectively reclaim the high steam for still carrying residual temperature after industrial production utilizes, and steam high pressure Vapour is discharged after being changed into condensate through drainage conduit 5, is carried out the utilization of next step or is concentrated discharge, avoids polluting environment, Avoid the waste of resource.
Above-mentioned vapour-recovery unit can be made further optimization and/or improvements according to being actually needed:
As shown in Figure 1, tank body 1 top outer be provided with the evacuated tube 6 that connects in tank body 1, in evacuated tube 6 It is serially connected with safety valve 7., can the row of opening when the high steam amount of feeding is excessive to be had little time recovery and cause hypertonia in tank body 1 Safety valve 7 on blank pipe 6, by the pressure in tank body 1 through the pressure release of evacuated tube 6, ensure the safety of production, prevent potential safety hazard.
Above technical characteristic constitutes most preferred embodiment of the present utility model, and it has stronger adaptability and optimal implementation Effect, can be according to the non-essential technical characteristic of increase and decrease be actually needed, to meet the needs of different situations.

Claims (2)

1. a kind of vapour-recovery unit, it is characterised in that including tank body, feed pipe, decompression hush pipe and drainage conduit;Tank body is complete The tank body of closing, feed pipe is communicated with the upper end of tank body, and the port of export of feed pipe is located at tank interior, is depressured entering for hush pipe Mouth end is together with the port of export closed communication of feed pipe, relative to the other end of the decompression hush pipe of decompression hush pipe entrance point Closing, steam vent is distributed with the decompression hush pipe body of decompression hush pipe entrance point, the gross area of all steam vents is big In the cross-sectional area of feed pipe, the drainage conduit being connected with tank body is provided with the bottom outside of tank body, is gone here and there in drainage conduit It is connected to discharge pump.
2. vapour-recovery unit according to claim 1, it is characterised in that be provided with and tank body in the top outer of tank body The evacuated tube of interior connection, is serially connected with safety valve in evacuated tube.
CN201720669657.6U 2017-06-09 2017-06-09 Vapour-recovery unit Expired - Fee Related CN207019491U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720669657.6U CN207019491U (en) 2017-06-09 2017-06-09 Vapour-recovery unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720669657.6U CN207019491U (en) 2017-06-09 2017-06-09 Vapour-recovery unit

Publications (1)

Publication Number Publication Date
CN207019491U true CN207019491U (en) 2018-02-16

Family

ID=61484945

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720669657.6U Expired - Fee Related CN207019491U (en) 2017-06-09 2017-06-09 Vapour-recovery unit

Country Status (1)

Country Link
CN (1) CN207019491U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110498021A (en) * 2019-09-06 2019-11-26 威海海洋职业学院 A kind of high-pressure system antispray floor drain apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110498021A (en) * 2019-09-06 2019-11-26 威海海洋职业学院 A kind of high-pressure system antispray floor drain apparatus

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CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180216