CN106606919A - Carbonization production ammonia recovery and utilization device - Google Patents
Carbonization production ammonia recovery and utilization device Download PDFInfo
- Publication number
- CN106606919A CN106606919A CN201510703371.0A CN201510703371A CN106606919A CN 106606919 A CN106606919 A CN 106606919A CN 201510703371 A CN201510703371 A CN 201510703371A CN 106606919 A CN106606919 A CN 106606919A
- Authority
- CN
- China
- Prior art keywords
- dissolving
- tower
- screw thread
- inlet pipe
- water inlet
- 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.)
- Pending
Links
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 80
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 40
- 238000003763 carbonization Methods 0.000 title claims abstract description 20
- 238000011084 recovery Methods 0.000 title claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 63
- 230000005540 biological transmission Effects 0.000 claims abstract description 5
- 239000000443 aerosol Substances 0.000 claims description 20
- 230000005520 electrodynamics Effects 0.000 claims description 13
- 208000031481 Pathologic Constriction Diseases 0.000 claims 2
- 210000001215 vagina Anatomy 0.000 claims 2
- 239000003337 fertilizer Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000000605 extraction Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000006199 nebulizer Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
Landscapes
- Fertilizers (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a carbonization production ammonia recovery and utilization device. The device comprises a carbonization tower, a negative pressure pump, a gas transmission pipe, a dissolving tower, a water inlet pipe, an electric valve, a sprayer and a circulating water pump. Compared with the existing ammonia recovery and utilization device, the carbonization production ammonia recovery and utilization device has a simple structure and strong functions, realizes recovery and use of ammonia in a carbonization tower, prevents discharge of ammonia into air, prevents ammonia-caused environment pollution and saves resources.
Description
Technical field
The present invention relates to a kind of recycle device, more particularly to the ammonia that a kind of carbonization production is drawn
Gas recycle device.
Background technology
When carbonization production chemical fertilizer takes out, set with air-introduced machine extraction conduit, thickener and centrifuge etc.
Standby interior ammonia, is vented to air and goes from roof, has both polluted environment, and waste of resource, reflects
In disadvantages described above, it is necessary that designing a kind of Ammonia recovery of carbonization production extraction utilizes device in fact.
The content of the invention
The technical problem to be solved is：The ammonia that a kind of carbonization production is drawn is provided
Recycle device enters asking of causing environmental pollution and data to waste in air solving ammonia
Topic.
To solve above-mentioned technical problem, the technical scheme is that：One kind carbonization production is drawn
Ammonia recovery utilize device, including carbonators, also including negative pressure pump, appendix, dissolving tower,
Water inlet pipe, electrodynamic valve, aerosol apparatus, water circulating pump, described negative pressure pump is located at carbonators top,
Described negative pressure pump is connected with carbonators screw thread, and described appendix is located at negative pressure pump top, institute
The appendix stated is connected with negative pressure pump screw thread, and described dissolving tower is located at appendix right-hand member, described
Dissolving tower be connected with gas transmission pipe screw thread, described water inlet pipe is located at dissolving top of tower center,
Described water inlet pipe is connected with dissolving tower screw thread, and described electrodynamic valve is located at water inlet pipe right-hand member, institute
The electrodynamic valve stated is connected with water inlet pipe screw thread, and described aerosol apparatus are located at water inlet pipe bottom, and institute
The aerosol apparatus stated are located at dissolving tower inner upper end, and described aerosol apparatus water inlet pipe screw thread is connected, institute
The water circulating pump stated is located at dissolving tower inside right-hand member, described water circulating pump and dissolving tower threaded line
Road, and described water circulating pump is connected with injector manifold.
Further, described appendix top is also provided with detector, described detector with it is defeated
Gas-pipe thread is connected.
Further, described dissolving bottom of towe end is additionally provided with drain pipe, described drain pipe and dissolving
Tower is weldingly connected.
Further, described drain pipe left end is additionally provided with hand-operated valve, described hand-operated valve and draining
Pipe screw thread is connected.
Further, described dissolving tower right-hand member is additionally provided with accumulator tank, and described accumulator tank is square
Enclosed slot.Further, described accumulator tank left end is additionally provided with water pump, described water pump with reclaim
Groove screw thread is connected, and described water pump is connected with draining pipeline.
Compared with prior art, the Ammonia recovery that the carbonization production is drawn utilizes device, is opening
Carbonators to take out and start negative pressure first before chemical fertilizer, and negative pressure pump causes to produce negative pressure in appendix, because
Ammonia by the ammonia suction appendix in carbonators, then can be input to dissolving tower by this by appendix
In, by opening electrodynamic valve so that in the middle water input aerosol apparatus of water inlet pipe, aerosol apparatus are by water
With vaporific ejection, so as to the ammonia in dissolving tower is dissolved well, dissolving rear solution drop
Fall in dissolving tower inner bottom, then ammonia spirit is drawn back in aerosol apparatus by water circulating pump, then
Sprayed by nebulizer solution, fully dissolve ammonia so as to reach, hand-operated valve is opened after dissolving,
Restart water pump, water pump by drain pipe by the ammonia suction accumulator tank for obtaining, so as to reach
Ammonia recovery is utilized, the apparatus structure is simple, powerful, can be by the ammonia in carbonators
Recycle, prevent ammonia from entering in air, so as to avoid ammonia from polluting environment, while saving
Resource.
Description of the drawings
Fig. 1 is the front view that the Ammonia recovery that carbonization production is drawn utilizes device
Fig. 2 is the sectional view for dissolving tower
The negative pressure pump 2 of carbonators 1
Appendix 3 dissolves tower 4
The electrodynamic valve 6 of water inlet pipe 5
The water circulating pump 8 of aerosol apparatus 7
The drain pipe 401 of detector 301
The accumulator tank 403 of hand-operated valve 402
Water pump 404
Specific embodiment
Hereinafter, various specific details are elaborated, to provide to constituting described embodiment
The thorough understanding of the concept on basis.However, it will be apparent to those skilled in the art that institute
The embodiment of description can be in the case of without some or all in these specific details
To put into practice.In other cases, well-known process step is not specifically described.
As shown in Figure 1 and Figure 2, including carbonators 1, negative pressure pump 2, appendix 3, dissolving tower
4th, water inlet pipe 5, electrodynamic valve 6, aerosol apparatus 7, water circulating pump 8, detector 301, draining
Pipe 401, hand-operated valve 402, accumulator tank 403, water pump 404, described negative pressure pump 2 is located at carbon
Change the top of tower 1, described negative pressure pump 2 is connected with the screw thread of carbonators 1, described appendix 3
Positioned at the top of negative pressure pump 2, described appendix 3 is connected with the screw thread of negative pressure pump 2, and described is molten
Solution tower 4 is located at the right-hand member of appendix 3, and described dissolving tower 4 is connected with the screw thread of appendix 3, institute
The water inlet pipe 5 stated is located at the dissolving top center of tower 4, described water inlet pipe 5 and dissolving tower 4
Screw thread is connected, and described electrodynamic valve 6 is located at the right-hand member of water inlet pipe 5, described electrodynamic valve 6 with enter
The screw thread of water pipe 5 is connected, and described aerosol apparatus 7 are located at the bottom of water inlet pipe 5, and described spraying
Device 7 is located at the dissolving inner upper end of tower 4, and the described screw thread of 4 water inlet pipe of aerosol apparatus 5 is connected, institute
The water circulating pump 8 stated is located at the dissolving inside right-hand member of tower 4, described water circulating pump 8 and dissolving tower
4 screw thread circuits, and described water circulating pump 8 is connected with the pipeline of aerosol apparatus 7, described gas transmission
The top of pipe 3 is also provided with detector 301, described detector 301 and the screw thread phase of appendix 3
Even, the described bottom of dissolving tower 4 is additionally provided with drain pipe 401, described drain pipe 401 with it is molten
Solution tower 4 is weldingly connected, and the described left end of drain pipe 401 is additionally provided with hand-operated valve 402, described
Hand-operated valve 402 is connected with the screw thread of drain pipe 401, and the described right-hand member of dissolving tower 4 is additionally provided with recovery
Groove 403, described accumulator tank 403 is square enclosed slot, and the described left end of accumulator tank 403 is also
Water pump 404 is provided with, described water pump 404 is connected with the screw thread of accumulator tank 403, and described water
Pump 404 is connected with the pipeline of drain pipe 401, and the Ammonia recovery that the carbonization production is drawn utilizes device,
Start negative pressure 2 before carbonators 1 takes out chemical fertilizer first opening, negative pressure pump 2 causes appendix
Negative pressure is produced in 3, therefore the ammonia in carbonators 1 can be sucked appendix 3, then by appendix
3 are input to ammonia in dissolving tower 4, by opening electrodynamic valve 6 so that in water inlet pipe 5
In water input aerosol apparatus 7, aerosol apparatus 7 by water with vaporific ejection, so as to will be in dissolving tower 4
Ammonia dissolve well, dissolving rear solution is dropped in the dissolving inner bottom of tower 4, then passes through
Water circulating pump 8 draws back ammonia spirit in aerosol apparatus 7, then is sprayed by the solution of aerosol apparatus 7, from
And reach and fully dissolve ammonia, hand-operated valve 402 is opened after dissolving, restart water pump 404,
Water pump 404 by drain pipe 401 by the ammonia suction accumulator tank 403 for obtaining, so as to reach
Ammonia recovery is utilized, wherein electrodynamic valve 6 is the water inlet and closing for controlling water inlet pipe 5, is detected
Device 301 is to detect whether the ammonia in carbonators 1 is all discharged.
Embodiment described above is only that the preferred embodiment of the present invention is described, and
It is non-that the spirit and scope of the present invention are defined.In the premise without departing from design concept of the present invention
Under, various modifications and improvement that this area ordinary person makes to technical scheme,
Protection scope of the present invention should be dropped into.
Claims (6)
1. the Ammonia recovery that a kind of carbonization production is drawn utilizes device, including carbonators, its
Be characterised by also include negative pressure pump, appendix, dissolving tower, water inlet pipe, electrodynamic valve, aerosol apparatus,
Water circulating pump, described negative pressure pump is located at carbonators top, described negative pressure pump and carbonators spiral shell
Stricture of vagina is connected, and described appendix is located at negative pressure pump top, described appendix and negative pressure pump screw thread
It is connected, described dissolving tower is located at appendix right-hand member, described dissolving tower and gas transmission pipe screw thread phase
Even, described water inlet pipe is located at dissolving top of tower center, described water inlet pipe and dissolving tower spiral shell
Stricture of vagina is connected, and described electrodynamic valve is located at water inlet pipe right-hand member, described electrodynamic valve and water inlet pipe screw thread
It is connected, described aerosol apparatus are located at water inlet pipe bottom, and described aerosol apparatus are located in dissolving tower
Portion upper end, described aerosol apparatus water inlet pipe screw thread is connected, and described water circulating pump is located at dissolving tower
Internal right-hand member, described water circulating pump and dissolving tower screw thread circuit, and described water circulating pump with
Injector manifold is connected.
2. the Ammonia recovery that a kind of carbonization production as claimed in claim 1 is drawn is using dress
Put, it is characterised in that described appendix top is also provided with detector, described detector with
Gas transmission pipe screw thread is connected.
3. the Ammonia recovery that a kind of carbonization production as claimed in claim 2 is drawn is using dress
Put, it is characterised in that described dissolving bottom of towe end is additionally provided with drain pipe, described drain pipe with it is molten
Xie Ta is weldingly connected.
4. the Ammonia recovery that a kind of carbonization production as claimed in claim 3 is drawn is using dress
Put, it is characterised in that described drain pipe left end is additionally provided with hand-operated valve, described hand-operated valve and row
Water pipe thread is connected.
5. the Ammonia recovery that a kind of carbonization production as claimed in claim 4 is drawn is using dress
Put, it is characterised in that described dissolving tower right-hand member is additionally provided with accumulator tank, described accumulator tank is side
Shape closed groove.
6. the Ammonia recovery that a kind of carbonization production as claimed in claim 5 is drawn is using dress
Put, it is characterised in that described accumulator tank left end is additionally provided with water pump, described water pump and accumulator tank
Screw thread is connected, and described water pump is connected with draining pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510703371.0A CN106606919A (en) | 2015-10-26 | 2015-10-26 | Carbonization production ammonia recovery and utilization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510703371.0A CN106606919A (en) | 2015-10-26 | 2015-10-26 | Carbonization production ammonia recovery and utilization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106606919A true CN106606919A (en) | 2017-05-03 |
Family
ID=58613835
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510703371.0A Pending CN106606919A (en) | 2015-10-26 | 2015-10-26 | Carbonization production ammonia recovery and utilization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106606919A (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002263445A (en) * | 2001-03-06 | 2002-09-17 | Tokyo Reikaki Kogyo Kk | Gaseous ammonia removing equipment |
| CN201431850Y (en) * | 2009-05-08 | 2010-03-31 | 湖北三才堂化工科技有限公司 | Ammonia recycling device |
| CN202506309U (en) * | 2012-04-20 | 2012-10-31 | 成都玉龙化工有限公司 | Ammonia washing and recovering device |
| CN202538615U (en) * | 2012-05-07 | 2012-11-21 | 成都玉龙化工有限公司 | Gas washing recovery device of ammonia water storage tank |
| CN203235409U (en) * | 2013-03-13 | 2013-10-16 | 龙南县中利再生资源开发有限公司 | Waste gas collection and treatment device during phosphor waste treatment |
| CN203458955U (en) * | 2013-08-26 | 2014-03-05 | 自贡天和玻璃钢有限责任公司 | Leaked ammonia tail gas recovery system |
| CN204170592U (en) * | 2014-10-21 | 2015-02-25 | 河北科技大学 | A kind of ammonia reveals absorption plant |
| CN205216518U (en) * | 2015-10-26 | 2016-05-11 | 安徽华尔泰化工股份有限公司 | Ammonia recycle device that carbonization production was drawn forth |
-
2015
- 2015-10-26 CN CN201510703371.0A patent/CN106606919A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002263445A (en) * | 2001-03-06 | 2002-09-17 | Tokyo Reikaki Kogyo Kk | Gaseous ammonia removing equipment |
| CN201431850Y (en) * | 2009-05-08 | 2010-03-31 | 湖北三才堂化工科技有限公司 | Ammonia recycling device |
| CN202506309U (en) * | 2012-04-20 | 2012-10-31 | 成都玉龙化工有限公司 | Ammonia washing and recovering device |
| CN202538615U (en) * | 2012-05-07 | 2012-11-21 | 成都玉龙化工有限公司 | Gas washing recovery device of ammonia water storage tank |
| CN203235409U (en) * | 2013-03-13 | 2013-10-16 | 龙南县中利再生资源开发有限公司 | Waste gas collection and treatment device during phosphor waste treatment |
| CN203458955U (en) * | 2013-08-26 | 2014-03-05 | 自贡天和玻璃钢有限责任公司 | Leaked ammonia tail gas recovery system |
| CN204170592U (en) * | 2014-10-21 | 2015-02-25 | 河北科技大学 | A kind of ammonia reveals absorption plant |
| CN205216518U (en) * | 2015-10-26 | 2016-05-11 | 安徽华尔泰化工股份有限公司 | Ammonia recycle device that carbonization production was drawn forth |
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|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170503 |