CN206146223U - High -efficient calibration nitrogen appearance condensing equipment - Google Patents
High -efficient calibration nitrogen appearance condensing equipment Download PDFInfo
- Publication number
- CN206146223U CN206146223U CN201620727017.1U CN201620727017U CN206146223U CN 206146223 U CN206146223 U CN 206146223U CN 201620727017 U CN201620727017 U CN 201620727017U CN 206146223 U CN206146223 U CN 206146223U
- Authority
- CN
- China
- Prior art keywords
- heat exchange
- helical guideway
- heat transfer
- exchange disk
- transfer dish
- 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
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model relates to a high -efficient calibration nitrogen appearance condensing equipment, which comprises a housin, ammonia gas inlet, aqueous ammonia export, the comdenstion water entry, condensate outlet, a serial communication port, be equipped with the heat transfer dish in the casing, be equipped with helical guideway in the heat transfer dish, and ammonia gas inlet establishes at the casing top, and communicate with first heat transfer dish helical guideway is marginal, first heat transfer dish helical guideway center is through a pipe and a second heat transfer dish helical guideway center intercommunication, a second heat transfer dish helical guideway edge is through a pipe and a third heat transfer dish helical guideway edge intercommunication, a third heat transfer dish helical guideway center is through a pipe and a fourth heat transfer dish helical guideway center intercommunication, a fourth heat transfer dish helical guideway edge is through pipe and the 5th heat transfer dish helical guideway edge intercommunication, similarly, aqueous ammonia export sets up in the casing bottom and communicates with final heat transfer dish, the comdenstion water entry sets up in the casing lower part, condensate outlet sets up on casing upper portion.
Description
Technical field
The utility model is related to azotometer technical field, more particularly to a kind of high efficiency azotometer condensing unit.
Background technology
Protein determination technology is all widely used in conglomeraties such as food, feeds, the most frequently used protein determination technology
It is exactly Kjeldahl's method, kjeldahl determination device is required for condensing unit, and the condensing unit of general kjeldahl determination device is often
Heat exchange efficiency is low.Accordingly, it would be desirable to technically make improvements.
Utility model content
The utility model aims to solve the problem that the low deficiency of existing azotometer condensing unit heat exchange efficiency, and provides a kind of efficient
Rate azotometer condensing unit.
The utility model for achieving the above object, is employed the following technical solutions：
A kind of described high efficiency azotometer condensing unit, including housing, ammonia entrance, ammoniacal liquor outlet, condensing water inlet,
Condensation-water drain, it is characterised in that heat exchange disk is provided with housing, in heat exchange disk helical guideway is provided with, and ammonia entrance is located at shell
Body top, and connect with first heat exchange valve snail rotation guiding edge, first heat exchange valve snail rotation guideway centreline passes through conduit and the
The connection of two heat exchange valve snail rotation guideway centreline, second heat exchange valve snail rotation guiding edge is by conduit and the 3rd heat exchange valve snail rotation
Guiding edge is connected, and the 3rd heat exchange valve snail rotation guideway centreline revolves guideway centreline and connect by conduit with the 4th heat exchange valve snail,
4th heat exchange valve snail rotation guiding edge revolves guiding edge and connects by conduit with the 5th heat exchange valve snail, by that analogy, ammoniacal liquor
Outlet is arranged on housing bottom and connects with last heat exchange disk, and condensing water inlet is arranged on lower housing portion, condensation-water drain
It is arranged on housing upper.
Hull outside is also provided with heat-insulation layer, in case external environment heat is entered in condensed water, makes condensation effect be deteriorated.
Support column can be also provided between two heat exchange disks that helical guideway edge is connected by conduit, support column is arranged at two
Individual heat exchange disk center position.
The beneficial effects of the utility model are：The utility model arranges spiral shell by arranging heat exchange disk inside heat exchange disk
Rotation guide rail, in certain volume, substantially increases heat exchange efficiency, makes ammonia condensation more efficient.
Description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the internal structure schematic diagram of heat exchange disk of the present utility model.
In figure：1- housings；2- heat exchange disks；3- ammonia entrances；4- ammoniacal liquor is exported；5- condensing water inlets；6- condensation-water drains；
7- support columns.
It is described in detail referring to the drawings below with reference to embodiment of the present utility model.
Specific embodiment
With reference to the accompanying drawings and examples the utility model is described in further detail：
As depicted in figs. 1 and 2, a kind of high efficiency azotometer condensing unit, including housing 1, the outlet of ammonia entrance 3, ammoniacal liquor
4th, condensing water inlet 5, condensation-water drain 6, it is characterised in that heat exchange disk 2 is provided with housing 1, spiral is provided with heat exchange disk 2 and is led
Rail, and ammonia entrance 3 is located at the top of housing 1, and connect with first heat exchange disk 2 helical guideway edge, first heat exchange spiral shell of disk 2
Rotation guideway centreline is connected by conduit with second heat exchange disk 2 helical guideway center, and second heat exchange disk 2 helical guideway edge leads to
Cross conduit to connect with the 3rd heat exchange disk 2 helical guideway edge, the 3rd heat exchange helical guideway of disk 2 is centrally through conduit and the 4th
The connection of individual heat exchange disk 2 helical guideway center, the 4th heat exchange disk 2 helical guideway edge is by conduit and the 5th heat exchange spiral shell of disk 2
Rotation guiding edge connection, by that analogy, ammoniacal liquor outlet 4 is arranged on the bottom of housing 1 and connects with last heat exchange disk 2, condenses
Water inlet 5 is arranged on the bottom of housing 1, and condensation-water drain 6 is arranged on the top of housing 1.
Heat-insulation layer is also provided with outside housing 1, in case external environment heat is entered in condensed water, becomes condensation effect
Difference.
Support column 7 can be also provided between two heat exchange disks 2 that helical guideway edge is connected by conduit, support column 7 is arranged
Exchange heat the center of disk 2 in two, so that overall reach stable state.
Embodiment：Condensed water enters housing 1 from condensing water inlet 5, until the space being full of between housing 1 and each heat exchange disk 2,
Ammonia Jing ammonias entrance 3 is passed through heat exchange disk 2, and Jing after the helical orbit circulation in each heat exchange disk 2, the heat water that is condensed is absorbed into
And ammoniacal liquor is condensed into, discharge from ammoniacal liquor outlet 4.
The utility model is exemplarily described above in conjunction with accompanying drawing, it is clear that the utility model is implemented not to be received
The restriction of aforesaid way, if the various improvement that method design of the present utility model and technical scheme are carried out are employed, or without
Improvement directly applies to other occasions, within protection domain of the present utility model.
Claims (3)
1. a kind of high efficiency azotometer condensing unit, including housing (1), ammonia entrance (3), ammoniacal liquor outlet (4), condensing water inlet
(5), condensation-water drain (6), it is characterised in that heat exchange disk (2) is provided with housing (1), in heat exchange disk (2) helical guideway is provided with,
And ammonia entrance (3) is located at housing (1) top, and connect with first heat exchange disk (2) helical guideway edge, first heat exchange disk
(2) helical guideway is connected centrally through conduit with second heat exchange disk (2) helical guideway center, second heat exchange disk (2) spiral
Guiding edge is connected by conduit with the 3rd heat exchange disk (2) helical guideway edge, the 3rd heat exchange disk (2) helical guideway center
Connected with the 4th heat exchange disk (2) helical guideway center by conduit, the 4th heat exchange disk (2) helical guideway edge passes through conduit
With the 5th heat exchange disk (2) helical guideway edge connect, by that analogy, ammoniacal liquor export (4) be arranged on housing (1) bottom and with most
Latter heat exchange disk (2) connection, condensing water inlet (5) is arranged on housing (1) bottom, and condensation-water drain (6) is arranged on housing (1)
Top.
2. a kind of high efficiency azotometer condensing unit according to claim 1, it is characterised in that also sets outside housing (1)
There is heat-insulation layer, in case external environment heat is entered in condensed water, make condensation effect be deteriorated.
3. a kind of high efficiency azotometer condensing unit according to claim 1, it is characterised in that spiral is connected by conduit
Support column (7) is additionally provided between two heat exchange disk (2) of guiding edge, support column (7) is arranged at two heat exchange disk (2) centre bits
Put.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620727017.1U CN206146223U (en) | 2016-07-12 | 2016-07-12 | High -efficient calibration nitrogen appearance condensing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620727017.1U CN206146223U (en) | 2016-07-12 | 2016-07-12 | High -efficient calibration nitrogen appearance condensing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206146223U true CN206146223U (en) | 2017-05-03 |
Family
ID=58616622
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620727017.1U Expired - Fee Related CN206146223U (en) | 2016-07-12 | 2016-07-12 | High -efficient calibration nitrogen appearance condensing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206146223U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107934987A (en) * | 2017-12-21 | 2018-04-20 | 中冶焦耐(大连)工程技术有限公司 | One kind removes crystallization from wash type ammonia condensing cooling device |
-
2016
- 2016-07-12 CN CN201620727017.1U patent/CN206146223U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107934987A (en) * | 2017-12-21 | 2018-04-20 | 中冶焦耐(大连)工程技术有限公司 | One kind removes crystallization from wash type ammonia condensing cooling device |
| CN107934987B (en) * | 2017-12-21 | 2024-05-14 | 中冶焦耐(大连)工程技术有限公司 | Remove crystallization from washing formula ammonia condensation cooling device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| 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: 20170503 Termination date: 20190712 |