CN206337028U - A kind of ammonia water recovery device - Google Patents

A kind of ammonia water recovery device Download PDF

Info

Publication number
CN206337028U
CN206337028U CN201621474917.6U CN201621474917U CN206337028U CN 206337028 U CN206337028 U CN 206337028U CN 201621474917 U CN201621474917 U CN 201621474917U CN 206337028 U CN206337028 U CN 206337028U
Authority
CN
China
Prior art keywords
ammoniacal liquor
ammonia
cooling
recycling
solution
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.)
Active
Application number
CN201621474917.6U
Other languages
Chinese (zh)
Inventor
周传武
何君
钟林云
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.)
Mianyang Di'ao Pharmaceutical Co Ltd
Original Assignee
Mianyang Di'ao Pharmaceutical 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 Mianyang Di'ao Pharmaceutical Co Ltd filed Critical Mianyang Di'ao Pharmaceutical Co Ltd
Priority to CN201621474917.6U priority Critical patent/CN206337028U/en
Application granted granted Critical
Publication of CN206337028U publication Critical patent/CN206337028U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

The utility model discloses a kind of ammonia water recovery device, including be sequentially connected concentration tank, ammoniacal liquor recycling can, heat exchanger and by flow container;The concentration tank is used to be passed through the solution containing ammoniacal liquor, and steam pipe coil is provided with the concentration tank, for being heated to solution, so that the ammoniacal liquor formation ammonia in solution is separated with solution, and is discharged in ammoniacal liquor recycling can;Cooling coil is provided with the ammoniacal liquor recycling can, outside is cased with cooling jacket, cooling coil and cooling jacket are used for common to being cooled down into the ammonia in ammoniacal liquor recycling can, it is allowed to be liquefied as ammoniacal liquor to be stored in ammoniacal liquor recycling can, liquefied ammonia completely is not expelled in heat exchanger for part, is liquefied as being stored into by flow container after ammoniacal liquor by heat exchanger secondary cooling.The utility model is reasonable in design, easy to use, and the rate of recovery of ammoniacal liquor greatly improved, national standard is met.

Description

A kind of ammonia water recovery device
Technical field
The utility model is related to a kind of ammonia water recovery device.
Background technology
Ammoniacal liquor is a kind of low boiling point, the liquid of highly volatile, and highly volatile goes out chlorine in atmosphere, and ammonia is with very strong Excitant.At present, in the industry such as chemical industry and non-ferrous metal metallurgy, desulfurization, dechlorination, denitration can all cause substantial amounts of ammonia to be arranged Release, if not carrying out effective recycling to it, it will cause severe contamination to environment.However, existing ammoniacal liquor is returned Receiving apparatus is only capable of reaching 50~60% to the rate of recovery of ammonia, and the rate of recovery is extremely low, hardly consistent with national standard.
Utility model content
For above-mentioned the deficiencies in the prior art, the utility model provides a kind of ammonia water recovery device, and ammoniacal liquor can be achieved High efficiente callback, meets and reclaims requirement.
To achieve the above object, the technical solution adopted in the utility model is as follows:
A kind of ammonia water recovery device, including be sequentially connected concentration tank, ammoniacal liquor recycling can, heat exchanger and by flow container;It is described Concentration tank is used to be passed through the solution containing ammoniacal liquor, steam pipe coil is provided with the concentration tank, for being heated to solution, so that molten Ammoniacal liquor formation ammonia in liquid is separated with solution, and is discharged in ammoniacal liquor recycling can;Cooler pan is provided with the ammoniacal liquor recycling can Pipe, outside is cased with cooling jacket, and cooling coil and cooling jacket are used for common cold to entering the ammonia progress in ammoniacal liquor recycling can But, it is allowed to be liquefied as ammoniacal liquor to be stored in ammoniacal liquor recycling can, liquefied ammonia completely is not expelled in heat exchanger for part, by exchanging heat Device secondary cooling is liquefied as being stored into by flow container after ammoniacal liquor.
Further, it is described that vavuum pump is also connected with by pipeline by flow container.
Compared with prior art, the utility model has the advantages that:
(1) the utility model is by setting concentration tank, steam pipe coil, ammoniacal liquor recycling can, cooling coil, cooling jacket, changing Hot device and by flow container, can be achieved the once heating of solution, cooling liquid twice, so as to using the characteristic of ammoniacal liquor low boiling point, make molten Ammoniacal liquor in liquid is separated, and is reclaimed.Practice have shown that, the utility model the rate of recovery of ammoniacal liquor can reach 90% with On, fully meet national standard.
(2) the utility model connects a vavuum pump at by flow container by pipeline, consequently, it is possible to before use, it is first right Each tank body carries out vacuumize process, can make to keep vacuum negative pressure condition in each tank body, so as to be easier to ammonia and ammoniacal liquor Flowing, and then optimize the organic efficiency of ammoniacal liquor, and ensure operational safety.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Wherein, reference is corresponding entitled:
1- concentration tanks, 2- steam pipe coils, 3- ammoniacal liquor recycling cans, 4- cooling coils, 5- cooling jackets, 6- heat exchangers, 7- by Flow container.
Embodiment
The utility model is described in further detail with embodiment for explanation below in conjunction with the accompanying drawings, and mode of the present utility model includes But it is not limited only to following examples.
Embodiment
As shown in figure 1, the utility model provides a kind of ammonia water recovery device, it includes concentration tank 1, the ammonia being sequentially connected Water recovery tank 3, heat exchanger 6 and by flow container 7.The concentration tank 1 is used to be passed through the solution containing ammoniacal liquor, provided with steaming in the concentration tank Vapor is passed through in vapour coil pipe 2, steam pipe coil 2, solution can be heated, makes ammoniacal liquor formation ammonia and the solution in solution Separation, and be discharged in ammoniacal liquor recycling can 3.Cooling coil 4 is provided with the ammoniacal liquor recycling can 3, outside is cased with cooling jacket 5, Cooling coil and cooling jacket are passed through refrigerant, carry out instantaneous cooling to the ammonia entered in ammoniacal liquor recycling can jointly, are allowed to liquid Chemical conversion ammoniacal liquor is stored in ammoniacal liquor recycling can 3.And part not completely liquefied ammonia then enter in heat exchanger 6 carry out it is cold again But, ammoniacal liquor is ultimately formed to enter by flow container 7.So once heated, cooling liquid twice, can be achieved the overwhelming majority recovery of ammoniacal liquor (rate of recovery can reach more than 90%).
In addition, the utility model connects a vavuum pump also at by flow container 7 by pipeline, before use, first to each Tank body carries out vacuumize process, to keep vacuum negative pressure condition in each tank body, so that the flowing of ammonia and ammoniacal liquor is easier to, And ensure operational safety.
According to the characteristic of ammonia, by rational structure design, the rate of recovery of ammoniacal liquor greatly improved in the utility model, meets The recovery requirement of ammoniacal liquor.Therefore, the utility model compared with prior art, with substantial feature and progress.
Above-described embodiment is only one of preferred embodiment of the present utility model, be should not be taken to limit of the present utility model Protection domain, it is all body design thought of the present utility model and mentally make have no the change of essential meaning or polishing, The technical problem that it is solved is still consistent with the utility model, should be included in protection domain of the present utility model it It is interior.

Claims (2)

1. a kind of ammonia water recovery device, it is characterised in that including the concentration tank (1) being sequentially connected, ammoniacal liquor recycling can (3), heat exchange Device (6) and by flow container (7);The concentration tank (1) is used to be passed through the solution containing ammoniacal liquor, and steam pipe coil is provided with the concentration tank (2), for being heated to solution, so that the ammoniacal liquor formation ammonia in solution is separated with solution, and it is discharged to ammoniacal liquor recycling can It is interior;Cooling coil (4) is provided with the ammoniacal liquor recycling can (3), outside is cased with cooling jacket (5), cooling coil and cooling jacket For cooling down to entering the ammonia in ammoniacal liquor recycling can jointly, it is allowed to be liquefied as ammoniacal liquor to be stored in ammoniacal liquor recycling can, portion Divide incomplete liquefied ammonia to be expelled in heat exchanger (6), be liquefied as being stored into by liquid after ammoniacal liquor by heat exchanger (6) secondary cooling In tank (7).
2. a kind of ammonia water recovery device according to claim 1, it is characterised in that described also to be passed through pipeline by flow container (7) It is connected with vavuum pump.
CN201621474917.6U 2016-12-29 2016-12-29 A kind of ammonia water recovery device Active CN206337028U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621474917.6U CN206337028U (en) 2016-12-29 2016-12-29 A kind of ammonia water recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621474917.6U CN206337028U (en) 2016-12-29 2016-12-29 A kind of ammonia water recovery device

Publications (1)

Publication Number Publication Date
CN206337028U true CN206337028U (en) 2017-07-18

Family

ID=59304291

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621474917.6U Active CN206337028U (en) 2016-12-29 2016-12-29 A kind of ammonia water recovery device

Country Status (1)

Country Link
CN (1) CN206337028U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111807446A (en) * 2020-07-13 2020-10-23 界首市南都华宇电源有限公司 Device for recovering ammonia in wastewater and using method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111807446A (en) * 2020-07-13 2020-10-23 界首市南都华宇电源有限公司 Device for recovering ammonia in wastewater and using method thereof

Similar Documents

Publication Publication Date Title
WO2016054874A1 (en) Method for extracting bromine from seawater by vacuum distillation
CN204303368U (en) Fixed gas retracting device in a kind of radioactive liquid waste evaporation process
CN204588694U (en) A kind of production system of used in electronic industry hydrofluoric acid
CN206337028U (en) A kind of ammonia water recovery device
CN206176897U (en) Vacuum drying cleaner
CN209431392U (en) Thermal deaerator waste steam recycling system
CN204352578U (en) Alcohol in high concentration recovery tower
CN105271324B (en) A kind of low pressure exhaust steam recycling system
CN105737457B (en) A kind of solvent recovery process
CN208333213U (en) The system of heat reclaim unit and its outer discharge capacity of the steam for reducing boiler thermodynamic system
CN207950720U (en) The system of condensing recovery dinitrogen tetroxide exhaust gas resource
CN203447803U (en) Rectifying device
CN206454298U (en) A kind of chemical industry rectifier unit
CN206281263U (en) A kind of useless air-conditioning refrigerant reclaiming clean device
CN206372543U (en) A kind of low-temperature negative-pressure purifying plant
CN106091719B (en) For the steam condensed water waste heat reclamation set in cryogenic distillation apparatus
CN106517243A (en) High temperature ammonia recovery device
CN207031178U (en) Sewage recorery treatment system
CN103288154B (en) Device and method for recovering metal material surface cleaning agent
CN206793079U (en) A kind of device of butanol weight-removing column top gaseous phase waste heat recovery
CN106440668A (en) Vacuum drying degreasing device
CN203950562U (en) A kind of vaporising device of processing radioactive liquid waste
CN207769768U (en) A kind of naphthalene water reducer condensation reaction equipment
CN207221369U (en) A kind of explosion-proof multistage rectification device of use for laboratory
CN206221042U (en) A kind of diesel-driven generator water body and waste heat from tail gas one retracting device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant