CN204939304U - A kind of calcium ammonium nitrate Water soluble fertilizer production thickner - Google Patents
A kind of calcium ammonium nitrate Water soluble fertilizer production thickner Download PDFInfo
- Publication number
- CN204939304U CN204939304U CN201520489520.3U CN201520489520U CN204939304U CN 204939304 U CN204939304 U CN 204939304U CN 201520489520 U CN201520489520 U CN 201520489520U CN 204939304 U CN204939304 U CN 204939304U
- Authority
- CN
- China
- Prior art keywords
- evaporator room
- crystallisation chamber
- chamber
- cone
- inlet tube
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Abstract
The utility model relates to a kind of fertilizer production equipment, is a kind of calcium ammonium nitrate Water soluble fertilizer production thickner specifically.Comprise crystallisation chamber, be arranged on the evaporator room of crystallisation chamber upper end, the upper end of evaporator room is provided with venting port, the lower end of evaporator room is provided with the central tube extended in crystallisation chamber inner chamber, the upper end of described crystallisation chamber is provided with return line, and the lower end of crystallisation chamber is provided with discharge nozzle, and evaporator room is provided with inlet tube, interchanger is in series with between inlet tube and return line, the bottom of crystallisation chamber is fixedly installed cone, and the lower end of central tube is with hydraucone, and pyramidal top is arranged in hydraucone.The material that pipe core flows out can disperse to surrounding by cone, is conducive to the formation of xln and improves the mobility of xln, be convenient to form uniform crystalline particle and be easy to realize continuous seepage; Prolong by most of hot steam condensing reflux in evaporator room, can be conducive to save energy, enhances productivity.
Description
Technical field
The utility model relates to a kind of fertilizer production equipment, is a kind of calcium ammonium nitrate Water soluble fertilizer production thickner specifically.
Background technology
The Oslo crystallizer that existing calcium ammonium nitrate Water soluble fertilizer production condensing crystal device mostly adopts chemical industry conventional, its structure is simple, easy to operate, can realize working continuously.Oslo crystallizer utilizes a pipe core to be communicated with crystallisation chamber setting up and down and evaporator room, along with the diameter of production-scale expansion, crystallisation chamber, evaporator room and pipe core is all larger, when pipe core diameter is larger time, material is fallen into after bottom crystallisation chamber by pipe core, cannot spread to surrounding, material is too concentrated, be unfavorable for the formation of xln, or the xln formed is deposited in pipe core mouth of pipe place, can not flow, crystalline particle is uneven, and what impact was produced carries out smoothly; In addition, high-temperature steams a large amount of in production process takes away partial heat and raw materials for production, causes the pollution of energy dissipation and environment.
Summary of the invention
The purpose of this utility model be to provide a kind of xln good fluidity, crystalline particle evenly, save energy, be convenient to quantity-produced calcium ammonium nitrate Water soluble fertilizer production thickner.
For achieving the above object, the utility model is by the following technical solutions:
A kind of calcium ammonium nitrate Water soluble fertilizer production thickner described in the utility model comprises crystallisation chamber, is arranged on the evaporator room of crystallisation chamber upper end, the upper end of described evaporator room is provided with venting port, the lower end of evaporator room is provided with the central tube extended in crystallisation chamber inner chamber, the upper end of described crystallisation chamber is provided with return line, the lower end of crystallisation chamber is provided with discharge nozzle, described evaporator room is provided with inlet tube, interchanger is in series with between described inlet tube and return line, the bottom of described crystallisation chamber is fixedly installed cone, and described cone is hollow cone; The lower end of described central tube is with hydraucone, and described pyramidal top is arranged in hydraucone, with gap between bell-mouthed inwall and cone; With there being the many horizontally disposed prolongs of level in the inner chamber of evaporator room, between inlet tube and venting port, described many prolongs be at least divided into two-layer, be crisscross arranged up and down; Between crystallisation chamber and evaporator room, be provided with communicating pipe, the junction of described communicating pipe and crystallisation chamber is higher than return line, and the junction of described communicating pipe and evaporator room is between inlet tube and prolong.
Adopt after technique scheme, the material that pipe core flows out can disperse to surrounding by cone, is conducive to the formation of xln and improves the mobility of xln, be convenient to form uniform crystalline particle and be easy to realize continuous seepage; Prolong by most of hot steam condensing reflux in evaporator room, can be conducive to save energy, enhances productivity.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model will be further described.
As shown in Figure 1, calcium ammonium nitrate Water soluble fertilizer production thickner described in the utility model comprises crystallisation chamber 1, be arranged on the evaporator room 2 of crystallisation chamber 1 upper end, the upper end of described evaporator room 2 is provided with venting port 3, the lower end of evaporator room 2 is provided with the central tube 4 extended in crystallisation chamber 1 inner chamber, the upper end of described crystallisation chamber 1 is provided with return line 5, the lower end of crystallisation chamber 1 is provided with discharge nozzle 6, described evaporator room 2 is provided with inlet tube 7, interchanger 81 is in series with between described inlet tube 7 and return line 5, the bottom of described crystallisation chamber 1 is fixedly installed cone 8, this cone 8 can be solid conical, also can be hollow cone.The lower end of described central tube 4 is with hydraucone 9, and the top of described cone 8 is arranged in hydraucone 9.With gap between the inwall of hydraucone 9 and cone 8, be convenient to material descending.
In addition, for realizing the recovery of heat energy and material, with there being the many horizontally disposed prolongs 10 of level in the inner chamber of evaporator room 2, between inlet tube 7 and venting port 3, described many prolongs 10 be at least divided into two-layer, be crisscross arranged up and down.Pass into water of condensation in prolong 10 and realize cooling.Run in hot steam uphill process in evaporator room 2 under prolong 10 cooling becomes liquid and fall back in evaporator room.
Between crystallisation chamber 1 and evaporator room 2, be provided with communicating pipe 11, the junction of described communicating pipe 11 and crystallisation chamber 1 is higher than return line 5, and the junction of described communicating pipe 11 and evaporator room 2 is between inlet tube 7 and prolong 10.By communicating pipe 11, the gas in crystallisation chamber 1 can enter in evaporator room 2 smoothly, makes the pressure of crystallisation chamber 1 keep balance.
In work, the material that new material and return line 5 reflux pumps into interchanger 81 by recycle pump 12, and the material after heat exchange enters evaporator room 2 from inlet tube 7, is advanced into crystallisation chamber 14 times along central tube, and the crystal that crystallisation chamber 1 is formed is discharged from discharge nozzle 6.
Claims (1)
1. a calcium ammonium nitrate Water soluble fertilizer production thickner, comprise crystallisation chamber (1), be arranged on the evaporator room (2) of crystallisation chamber (1) upper end, the upper end of described evaporator room (2) is provided with venting port (3), the lower end of evaporator room (2) is provided with the central tube (4) extended in crystallisation chamber (1) inner chamber, the upper end of described crystallisation chamber (1) is provided with return line (5), the lower end of crystallisation chamber (1) is provided with discharge nozzle (6), described evaporator room (2) is provided with inlet tube (7), interchanger (81) is in series with between described inlet tube (7) and return line (5), it is characterized in that: the bottom of described crystallisation chamber (1) is fixedly installed cone (8), described cone (8) is hollow cone, the lower end of described central tube (4) is with hydraucone (9), and the top of described cone (8) is arranged in hydraucone (9), with gap between the inwall of hydraucone (9) and cone (8), with there being the many horizontally disposed prolongs of level (10) in the inner chamber of evaporator room (2), between inlet tube (7) and venting port (3), described many prolongs (10) be at least divided into two-layer, be crisscross arranged up and down, communicating pipe (11) is provided with between crystallisation chamber (1) and evaporator room (2), the junction of described communicating pipe (11) and crystallisation chamber (1) is higher than return line (5), and the junction of described communicating pipe (11) and evaporator room (2) is positioned between inlet tube (7) and prolong (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520489520.3U CN204939304U (en) | 2015-07-09 | 2015-07-09 | A kind of calcium ammonium nitrate Water soluble fertilizer production thickner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520489520.3U CN204939304U (en) | 2015-07-09 | 2015-07-09 | A kind of calcium ammonium nitrate Water soluble fertilizer production thickner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204939304U true CN204939304U (en) | 2016-01-06 |
Family
ID=55006747
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520489520.3U Expired - Fee Related CN204939304U (en) | 2015-07-09 | 2015-07-09 | A kind of calcium ammonium nitrate Water soluble fertilizer production thickner |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204939304U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106621417A (en) * | 2016-11-30 | 2017-05-10 | 深圳市瑞升华科技股份有限公司 | Evaporation and crystallization device |
| CN109422549A (en) * | 2017-08-29 | 2019-03-05 | 贵州芭田生态工程有限公司 | Calcium ammonium nitrate particle preparation system and preparation method |
-
2015
- 2015-07-09 CN CN201520489520.3U patent/CN204939304U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106621417A (en) * | 2016-11-30 | 2017-05-10 | 深圳市瑞升华科技股份有限公司 | Evaporation and crystallization device |
| CN109422549A (en) * | 2017-08-29 | 2019-03-05 | 贵州芭田生态工程有限公司 | Calcium ammonium nitrate particle preparation system and preparation method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203428286U (en) | Wine tank spraying device | |
| CN201710990U (en) | Variable aperture dual-flow sieve-plate tower | |
| CN204939304U (en) | A kind of calcium ammonium nitrate Water soluble fertilizer production thickner | |
| CN101725501B (en) | Gas bubble pump with gas bubble collecting device | |
| CN204428876U (en) | MVR continuous evaporative crystallization system | |
| CN204767575U (en) | Urea aldehyde slowly -releasing fertilizer apparatus for producing | |
| CN203090515U (en) | External circular-reaction extractive distillation integrated device | |
| CN205607186U (en) | Novel phosphorus trichloride condenser | |
| CN205467231U (en) | Novel circulation of plastics extruder water -cooling device | |
| CN103757716A (en) | Energy-saving spinning die head with high heat conduction efficiency for spinning manifold | |
| CN204369595U (en) | A kind of low levels ammonium chloride wastewater stripping recovering device for deamination | |
| CN202322797U (en) | Cooling device for distillation | |
| CN206670435U (en) | A kind of steam and hot water thermal energy storage device | |
| CN206247923U (en) | A kind of novel practical ammoniacal liquor configures condenser | |
| CN205917031U (en) | Phosphoric acid refrigeration cycle water vacuum device | |
| CN204485348U (en) | A kind of thermal coupling is sprayed and flows tower | |
| CN205613072U (en) | Rectifier unit is used in production of energy -efficient type benzene formaldehyde -like | |
| CN203464774U (en) | Condenser used for producing meropenem branched chains | |
| CN208567257U (en) | A kind of water-saving cooling tower | |
| CN204007239U (en) | A kind of being applicable to compared with the tubular heat exchanger of low viscosity material | |
| CN204085238U (en) | A kind of fountain type cooling water pond | |
| CN205007626U (en) | Percolating device | |
| CN201949663U (en) | Novel concentration evaporator | |
| CN204182146U (en) | A kind of vertical falling-film evaporation overflow-type mouth of pipe filming device | |
| CN204246850U (en) | A kind of paraffin oil and the accurate separation system device of carrene |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160106 Termination date: 20180709 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |