CN205443119U - Bio -fertilizer oil expenses melt equipment - Google Patents
Bio -fertilizer oil expenses melt equipment Download PDFInfo
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- CN205443119U CN205443119U CN201521061877.8U CN201521061877U CN205443119U CN 205443119 U CN205443119 U CN 205443119U CN 201521061877 U CN201521061877 U CN 201521061877U CN 205443119 U CN205443119 U CN 205443119U
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- bio
- fertilizer
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- oil
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Abstract
This patent belongs to melting of oils and uses the equipment field, specifically discloses a bio -fertilizer oil expenses melt equipment, including the base, be equipped with on the base and melt the storehouse, still include the steam pipe way, steam pipe says including the section of admitting air, heating section and the play water section that connects gradually, the section of admitting air with melt the storehouse top and be connected, the heating section is the heliciform and is located and melts the storehouse, go out the water section and melt storehouse bottom intercommunication, it is equipped with out oil pipe to melt the storehouse bottom, it is equipped with the oil inlet to melt the storehouse top. This patent application adopts the bio -fertilizer to give birth to that the steam of freedom melts solid -state bio -fertilizer oil expenses in the factory, need not to adopt other energy, and is energy -concerving and environment -protective, with low costs, and water steam temperature is higher than 100 DEG C, and steam pipe says that the heating section is the heliciform, increased with the area of contact of solid -state bio -fertilizer oil expenses, messenger's bio -fertilizer oil expenses that can be quick are melted, have improved work efficiency.
Description
Technical field
This utility model relates to the thawing apparatus field of oils, is specifically related to the thawing equipment of a kind of bio-fertilizer oil.
Background technology
Bio-fertilizer has that nutrient content is high, accessory ingredient is few and the advantage such as physical behavior is good, for balance fertilizing, improves utilization rate of fertilizer, and the stable high yield of promotion crop has highly important effect.But bio-fertilizer is manufacturing and is having a problem that during shipping storage that is exactly easily to lump.Moisture within fertilizer and the constituent of fertilizer itself are two principal elements of fertilizer agglomeration.Moisture within fertilizer mainly has two parts: a part is Free water, i.e. the moisture of manure solids granule internal component absorption under capillary tube or diffusion；Another part is water of crystallization, i.e. intrinsic in fertiliser compounds molecule structure moisture.The existence of these moisture advantageously forms the internal formation with top layer liquid phase of fertiliser granulates, facilitate the formation of brilliant bridge, be conducive to fertiliser granulates inside and the reaction of outer layer component and the decomposition of fertilizer components and recrystallization, and these factors promote the main cause of fertilizer agglomeration just.
Bio-fertilizer caking has had a strong impact on fertilizer efficiency, and gives and store, transport and use brings many difficulties.The ammonium hydrogen carbonate such as lumpd is easy to bale broken in transit, deposits 10 days under the temperature of 26 DEG C-28 DEG C, and nitrogen loss is up to 75.4%.Bio-fertilizer seriously lumps and is difficult to crush, and bio-fertilizer caking is unfavorable to mechanical fertilization, and fritter bio-fertilizer easily blocks shower nozzle, and these are all made troubles to fertilising.So, in bio-fertilizer produces, producer would generally spray one layer of bio-fertilizer oil to prevent bio-fertilizer from luming when manufacturing bio-fertilizer to bio-fertilizer.But the melting point of bio-fertilizer oil is 75-80 DEG C, is solid-state paste at normal temperatures.And sprayed when spraying bio-fertilizer oil by bio-fertilizer for liquid, so needing in process of production bio-fertilizer oil is melted.The method melted includes directly using heating furnace heating and melting or electrical heating to melt.But using heating furnace to melt waste fuel, cause environmental pollution, melting according to electrical heating then wastes electric power, relatively costly.
Utility model content
The purpose of this utility model is to provide the thawing equipment of a kind of bio-fertilizer oil that can economize on resources and rapidly and efficiently can melt bio-fertilizer oil.
For reaching above-mentioned purpose, base case of the present utility model is as follows: the thawing equipment of a kind of bio-fertilizer oil, and including base, described base is provided with thawing storehouse, also includes that steam pipeline, described steam pipeline include air inlet section, bringing-up section and the water exit end being sequentially connected with；Described air inlet section is connected with melting top, storehouse, and described bringing-up section in the shape of a spiral and is positioned at thawing storehouse, and described water exit end connects bottom storehouse with melting；Being provided with flowline bottom described thawing storehouse, top, described thawing storehouse is provided with oil-in.
Helical form described in this programme is spiral uprising shape.
Operation principle of the present utility model and have the beneficial effect that by solid-state paste bio-fertilizer through melt top, storehouse oil-in put into thawing storehouse, by steam temperature produced in bio-fertilizer factory production process higher than 100 DEG C, bringing-up section is entered through air inlet section, solid-state bio-fertilizer oil in melting storehouse, is then heated in bringing-up section is moved from top to bottom by bringing-up section at steam.Because the melting point of solid-state bio-fertilizer oil is 75 DEG C-80 DEG C, so steam can melt solid-state bio-fertilizer oil.And steam pipeline bringing-up section is in the shape of a spiral, increase the heating surface area of solid-state bio-fertilizer oil, make solid-state bio-fertilizer oil melt faster.Solid-state bio-fertilizer is discharged through flowline after melting with oil.Steam is then solidified as water in heating process and discharges through outlet pipe.This utility model uses own steam in the raw factory of bio-fertilizer to melt solid-state bio-fertilizer oil, without using other energy, energy-conserving and environment-protective, low cost, and steam temperature is higher than 100 DEG C, steam pipeline bringing-up section is helical form, increase and the contact area of solid-state bio-fertilizer oil, can quickly make bio-fertilizer oil melt, improve work efficiency.
Preferred version one: based on the preferred version of scheme, top, described thawing storehouse is provided with motor；Described motor connects has mixing arm, described mixing arm to be positioned at thawing storehouse.Driven by motor mixing arm rotates and can be stirred the solid-state bio-fertilizer oil in melting process with liquid biological fertilizer oil so that it is mix homogeneously, shortens the thawing time, improves work efficiency.
Preferred version two: the preferably preferred version of, described bringing-up section pitch is less than pipe diameter, bringing-up section pitch is less than pipe diameter, so the pipeline number of turns is made to increase in melting storehouse, duct length increases, add the heating surface area of bio-fertilizer oil, shorten the thawing time, improve work efficiency.
Preferred version three: based on scheme, preferred version one or the preferred version of preferred version two, also include retracting device, described retracting device is connected with water exit end, steam exits into retracting device through water exit end after being solidified as water and recycles, it is to avoid the waste of water resource.
Preferred version four: the preferably preferred version of three, also includes that pump, described pump are connected with flowline, and pump is connected with flowline can melt solution body bio-fertilizer oil quickly extraction in storehouse, improves work efficiency.
Accompanying drawing explanation
Fig. 1 is the structural representation of the thawing apparatus embodiments of this utility model bio-fertilizer oil.
Detailed description of the invention
Below by detailed description of the invention, this utility model is described in further detail:
Reference in Figure of description includes: base 10, thawing storehouse 20, flowline 21, pump 22, oil-in 23, steam pipeline 30, air inlet section 31, bringing-up section 32, water exit end 33, mixing arm 40, recovery bin 50.
Embodiment is the most as shown in Figure 1: the thawing equipment of a kind of bio-fertilizer oil, including base 10, base 10 is installed with thawing storehouse 20, also includes air inlet section 31, bringing-up section 32 and water exit end 33 that steam pipeline 3, steam pipeline 3 include being sequentially connected with；Air inlet section 31 is through melting top, storehouse 20, and bringing-up section 32 in the shape of a spiral and is positioned at thawing storehouse 20, and water exit end 33 is through melting bottom storehouse 20；Melt and bottom storehouse 20, be communicated with flowline 21, melt top, storehouse 20 and offer oil-in 23.Melt top, storehouse 20 and be rotatably connected to mixing arm 40；Mixing arm 40 one end is connected with motor.Solid-state bio-fertilizer oil in melting process can be stirred by mixing arm 40 with liquid biological fertilizer oil so that it is mix homogeneously, shortens the thawing time, improves work efficiency.Bringing-up section 32 pitch is less than pipe diameter, and bringing-up section 32 pitch is less than pipe diameter, so makes the pipeline number of turns increase in melting storehouse 20, and duct length increases, and adds the heating surface area of bio-fertilizer oil, shortens the thawing time, improve work efficiency.The thawing equipment of this bio-fertilizer oil also includes that recovery bin 50, recovery bin 50 are connected with water exit end 33, steam exits into recovery bin 50 through water exit end 33 after being solidified as water and recycles, it is to avoid the waste of water resource.The thawing equipment of this bio-fertilizer oil also includes that pump 22, pump 22 are connected with flowline 21, and pump 22 is connected with flowline 21 can melt liquid bio fertilizer oil quickly extraction in storehouse 20, improves work efficiency.
In the thawing equipment of this bio-fertilizer oil, steam pipeline is metal tube.Solid-state paste bio-fertilizer is put into thawing storehouse 20 through the oil-in 23 melting top, storehouse 20, steam produced in bio-fertilizer factory production process is entered bringing-up section 32 through air inlet section 31, solid-state bio-fertilizer oil in melting storehouse 20, is then heated in bringing-up section 32 is moved from top to bottom by bringing-up section 32 at steam.Because the melting point of solid-state bio-fertilizer oil is 75 DEG C-80 DEG C, so steam can melt solid-state bio-fertilizer oil.And steam pipeline bringing-up section 32 is in the shape of a spiral, increase the heating surface area of solid-state bio-fertilizer oil, make solid-state bio-fertilizer oil melt faster.Solid-state bio-fertilizer oil is discharged through flowline 21 after melting.Steam is then solidified as water in heating process and discharges through outlet pipe.Solid-state bio-fertilizer oil is melted by the steam during this utility model uses the raw factory of bio-fertilizer to produce, without using other energy, energy-conserving and environment-protective, low cost, and steam temperature is higher than 100 DEG C, steam pipeline bringing-up section 32 is helical form, increase and the contact area of solid-state bio-fertilizer oil, can quickly make bio-fertilizer oil melt, improve work efficiency.
Above-described is only embodiment of the present utility model, and in scheme, the known general knowledge such as concrete structure and characteristic too much describes at this.Should be understood that; for a person skilled in the art, on the premise of without departing from this utility model structure, it is also possible to make some deformation and improvement; these also should be considered as protection domain of the present utility model, and these are all without affecting effect and the practical applicability that this utility model is implemented.The protection domain that this application claims should be as the criterion with the content of its claim, and the detailed description of the invention in description etc. records the content that may be used for explaining claim.
Claims (5)
1. a thawing equipment for bio-fertilizer oil, including base, described base is provided with thawing storehouse, it is characterised in that also include that steam pipeline, described steam pipeline include air inlet section, bringing-up section and the water exit end being sequentially connected with；Described air inlet section is connected with melting top, storehouse, and described bringing-up section in the shape of a spiral and is positioned at thawing storehouse, and described water exit end connects bottom storehouse with melting；Being provided with flowline bottom described thawing storehouse, top, described thawing storehouse is provided with oil-in.
The thawing equipment of bio-fertilizer the most according to claim 1 oil, it is characterised in that top, described thawing storehouse is provided with motor；Described motor connects has mixing arm, described mixing arm to be positioned at thawing storehouse.
The thawing equipment of bio-fertilizer the most according to claim 2 oil, it is characterised in that described bringing-up section pitch is less than pipe diameter.
4. according to the thawing equipment of the bio-fertilizer oil described in any one of claim 1-3, it is characterised in that also include that retracting device, described retracting device are connected with outlet pipe.
The thawing equipment of bio-fertilizer the most according to claim 4 oil, it is characterised in that also include that pump, described pump are connected with flowline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521061877.8U CN205443119U (en) | 2015-12-20 | 2015-12-20 | Bio -fertilizer oil expenses melt equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521061877.8U CN205443119U (en) | 2015-12-20 | 2015-12-20 | Bio -fertilizer oil expenses melt equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205443119U true CN205443119U (en) | 2016-08-10 |
Family
ID=57181064
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521061877.8U Expired - Fee Related CN205443119U (en) | 2015-12-20 | 2015-12-20 | Bio -fertilizer oil expenses melt equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205443119U (en) |
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2015
- 2015-12-20 CN CN201521061877.8U patent/CN205443119U/en not_active Expired - Fee Related
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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: 20160810 Termination date: 20161220 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |