CN219628417U - Hydrolytic ammonium carbonate gas fertilizer machine - Google Patents
Hydrolytic ammonium carbonate gas fertilizer machine Download PDFInfo
- Publication number
- CN219628417U CN219628417U CN202321387153.7U CN202321387153U CN219628417U CN 219628417 U CN219628417 U CN 219628417U CN 202321387153 U CN202321387153 U CN 202321387153U CN 219628417 U CN219628417 U CN 219628417U
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- CN
- China
- Prior art keywords
- shell
- reaction tank
- ammonium bicarbonate
- fertilizer machine
- gas fertilizer
- 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.)
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 31
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 title claims abstract description 23
- 239000001099 ammonium carbonate Substances 0.000 title claims abstract description 23
- 235000012501 ammonium carbonate Nutrition 0.000 title claims description 4
- 230000003301 hydrolyzing effect Effects 0.000 title claims description 3
- 238000006243 chemical reaction Methods 0.000 claims abstract description 32
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 claims abstract description 19
- 235000012538 ammonium bicarbonate Nutrition 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 238000009423 ventilation Methods 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 8
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000005096 rolling process Methods 0.000 claims description 2
- 230000001965 increasing effect Effects 0.000 abstract description 5
- 239000002994 raw material Substances 0.000 abstract description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 37
- 239000001569 carbon dioxide Substances 0.000 description 18
- 229910002092 carbon dioxide Inorganic materials 0.000 description 18
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 5
- 235000011114 ammonium hydroxide Nutrition 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 230000007062 hydrolysis Effects 0.000 description 4
- 238000006460 hydrolysis reaction Methods 0.000 description 4
- 230000029553 photosynthesis Effects 0.000 description 4
- 238000010672 photosynthesis Methods 0.000 description 4
- 235000013311 vegetables Nutrition 0.000 description 4
- 235000013399 edible fruits Nutrition 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 244000304217 Brassica oleracea var. gongylodes Species 0.000 description 1
- 240000004160 Capsicum annuum Species 0.000 description 1
- 244000241235 Citrullus lanatus Species 0.000 description 1
- 235000012828 Citrullus lanatus var citroides Nutrition 0.000 description 1
- 244000241257 Cucumis melo Species 0.000 description 1
- 235000015510 Cucumis melo subsp melo Nutrition 0.000 description 1
- 240000008067 Cucumis sativus Species 0.000 description 1
- 235000010799 Cucumis sativus var sativus Nutrition 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000012840 feeding operation Methods 0.000 description 1
- 230000004720 fertilization Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000009469 supplementation Effects 0.000 description 1
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- Fertilizers (AREA)
Abstract
The utility model discloses an ammonium bicarbonate gas fertilizer machine which comprises a machine shell, a reaction tank, a heater and a fan, wherein the reaction tank is arranged in the machine shell, the top of the reaction tank is provided with an exhaust port, the exhaust port is communicated with the fan outside the machine shell through an exhaust pipe, the heater is arranged below the bottom of the reaction tank, and the heater and the fan are respectively and electrically connected with a power switch outside the machine shell. The device has the advantages of wide application range of the raw material ammonium bicarbonate, low cost, affordability for farmers, capability of increasing the yield and efficiency of greenhouse crops, certain economic benefit, and economy, practicality and safety.
Description
Technical Field
The utility model relates to the field of carbon dioxide gas fertilizer preparation equipment, in particular to an ammonium bicarbonate gas fertilizer hydrolysis machine.
Background
In cold seasons, in order to keep a certain crop growth temperature in the greenhouse, the greenhouse is usually closed, the concentration of carbon dioxide in the greenhouse is lower and lower under photosynthesis, so that the photosynthesis of crops in the greenhouse is slower and slower, and even photosynthesis is stopped, and artificial carbon dioxide supplementation is a necessary technology and important measures for promoting and guaranteeing the growth and development of crops and realizing yield and income increase.
The carbon dioxide gas fertilizer application technology in China has been popularized and applied for more than ten years, but the yield increasing effect brought by the carbon dioxide gas fertilizer application on production is not ideal. The carbon dioxide fertilization method adopted at home and abroad mainly has the following eight problems:
the high-pressure liquid carbon dioxide gas fertilizer is adopted, so that the transportation is inconvenient;
the solid dry ice is adopted, so that the cost is high, and the popularization is not easy;
solid particle gas fertilizer is adopted, and carbon dioxide has high specific gravity and small air, so that photosynthesis is not facilitated;
by adopting the combustion method, a gas purifying device must be installed;
the ammonia gas volatilized by adopting an ammonium bicarbonate deep-application method damages crops in a greenhouse;
by adopting a chemical reaction method, the safety problem of burn users or damage to articles of clothing exists;
the gas fertilizer rod is adopted, so that the humidity in the greenhouse is high, and the greenhouse is not easy to burn out;
the carbon dioxide gas is prepared by adopting an electrolysis mode, electricity and water are needed in the use process, chemical raw materials are needed to be added at any time, and the use is complicated.
The development of the application technology is restricted by the measures, such as expensive equipment, complex gas source, complicated and inconvenient use, insignificant use effect and the like. For vast farmer growers in China, the cost is not too high, or the limitation of various conditions is not met, and the actual national conditions of the agricultural development in China are not met.
Disclosure of Invention
Aiming at the problems existing in the prior art, the utility model provides the ammonium bicarbonate gas fertilizer machine for hydrolysis, which is mainly and directly used for heating ammonium bicarbonate produced by factories in water, carbon dioxide gas is produced to be absorbed by plants in greenhouse, the produced ammonia water can be diluted by clear water and can be used as fertilizer, the yield increasing effect of the equipment is good, the fertilizer production cost is low, and the use is safe.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
the hydrolysis ammonium carbonate gas fertilizer machine comprises a shell, a reaction tank, a heater and a fan, wherein the reaction tank is arranged in the shell, an exhaust port is formed in the top of the reaction tank, the exhaust port is communicated to the fan outside the shell through an exhaust pipe, the heater is arranged below the bottom of the reaction tank, and the heater and the fan are respectively and electrically connected with a power switch outside the shell.
Pouring commercial ammonium bicarbonate into a reaction tank of a gas fertilizer machine, adding proper amount of water, heating to 55-58 ℃, stopping heating, and maintaining the temperature for one hour to decompose ammonium bicarbonate into ammonium gas (NH) 3 ) Water (H) 2 O), carbon dioxide (CO) 2 ），CO 2 Is sucked by a fan from an exhaust port and discharged into a greenhouse, NH 3 +H 2 O= NH 3 ·H 2 O, the discharged and collected ammonia water can be used as fertilizer after being diluted.
The further improvement scheme is that the top of the reaction tank is provided with a feed inlet which is communicated with the outside of the shell, and the lower part of the reaction tank is provided with a water outlet which is communicated with the outside of the shell.
The further improvement scheme is that a temperature measuring thermocouple is arranged in the reaction tank and is connected with a temperature control box arranged outside the shell. Keeping proper hydrolysis temperature, and automatically cutting off the temperature controller to stop heating when the temperature is heated to 55-58 ℃.
The further improvement scheme is that a liquid level sensor is arranged on the side wall of the upper part in the reaction tank, and a signal is connected with a liquid level alarm indicator lamp outside the shell. Ensure the gas circulation space formed by the reaction, and feed the proper liquid level in the feedback machine.
Still further improvement scheme is, be equipped with electric switch valve on the drain pipe that the retort outlet is connected, electric switch valve signal connection casing is external power switch. The method is favorable for discharging the hydrolyzed ammonia water after electric control opening.
Still further improvement scheme is, still is equipped with the switch pilot lamp on the casing, and the switch pilot lamp is connected with the switch electricity. The on or off state is clearly indicated.
The further improvement scheme is that the fan is arranged on the top surface of the shell, an air outlet of the fan is connected with a ventilation pipe, and air outlet holes are formed in the ventilation pipe in a rolling mode at intervals. The ventilation pipes are suspended in parallel in the greenhouse, the air is uniformly discharged, the carbon dioxide in the greenhouse is uniformly distributed, and crops are well absorbed.
The further improvement is that the feed inlet is communicated to the top surface of the shell near the edge. Facilitating the feeding operation into the machine.
According to a further improvement scheme, the reaction tank is made of stainless steel.
The further improvement scheme is that the movable wheel is arranged at the bottom of the shell.
Advantageous effects
The commercial ammonium bicarbonate is directly poured into a reaction tank of the device, a proper amount of water is added, the device is heated to a certain temperature, the generated carbon dioxide gas fertilizer is pumped out by a fan and is discharged to all corners in the shed along a ventilation pipe, the carbon dioxide content absorbed by plants in the shed is increased, the ammonia water discharged by the device is diluted by 50 times of clear water and then is used as fertilizer for irrigating crops, the growth vigor of the crops in the shed is obviously improved, and the yield and the efficiency are increased, so that considerable economic benefits are brought to farmers.
Drawings
FIG. 1 is a schematic view of the internal structure of the present utility model;
fig. 2 is an external elevation view of the present utility model.
Detailed Description
As shown in fig. 1 and 2, the utility model comprises a shell 1, a reaction tank 2, a heater 3, a fan 4, a power switch 6, a temperature measuring thermocouple 7 and a temperature control box 8, wherein the reaction tank 2 made of stainless steel is arranged in the shell 1, the top of the reaction tank is provided with an exhaust port 21 and a feed port 22, the feed port 22 is communicated to the position, close to the edge, of the outer top surface of the shell, the exhaust port 22 is communicated to the fan 4 on the outer top surface of the shell through an exhaust pipe 5, the air outlet of the fan 4 is connected with a ventilation pipe 13, the ventilation pipe 13 is provided with air outlet holes in a spacing way, the lower part of the reaction tank 2 is provided with a water outlet 23 which is communicated to the outside of the shell through a water outlet pipe, the heater 3 is arranged below the bottom of the reaction tank 2, the heater 3, the fan 4 and the power switch valve 12 are respectively electrically connected with the power switch 6 outside the shell, and the shell is not provided with a switch indicator 11 which is electrically connected with the power switch 6.
A temperature measuring thermocouple 7 is arranged in the reaction tank 2 and is connected with a temperature control box 8 arranged outside the shell.
The upper side wall in the reaction tank 2 is provided with a liquid level sensor 9 which is connected with a liquid level alarm indicator lamp 10 outside the shell through a signal.
The movable wheel 14 is arranged at the bottom of the shell 1.
The air fertilizer machine is placed in a vegetable greenhouse with the diameter of 100 meters multiplied by 9 meters, 4 kg of ammonium bicarbonate is placed in a reaction tank from a feed inlet, 10 kg of water is added, the temperature is heated to 55-58 ℃, a ventilation pipe with the diameter of 50mm connected to an air outlet of a fan is rolled into 2 small holes with the diameter of 1mm at intervals of 1.5 meters to 3 meters on the ventilation pipe, the ventilation pipe is suspended in the greenhouse in parallel, the temperature is kept for one hour after the power is on, namely, carbon dioxide production is completed, the greenhouse is closed for 2 hours for ventilation, and then ammonia water in the reaction tank is poured into a barrel to be mixed with 50 times of clean water to be used as fertilizer. Compared with the trial observation for 10 days, the color and growth vigor of the vegetables are obviously different from those of the vegetables without carbon dioxide gas fertilizer application, and the effect is very obvious.
After that, the same tests are carried out in kohlrabi, green soy bean, chilli, cucumber and watermelon greenhouses, the effect is very good, the vegetable leaves are rich, green and smooth, the fruit setting rate of the melons is high, the fruits are big, the color is bright, the pulp is thick, and the fruits can be marketed 7-10 days in advance.
The above description is only a preferred embodiment of the present utility model, and the protection scope of the present utility model is not limited to the above examples, and all technical solutions belonging to the concept of the present utility model belong to the protection scope of the present utility model. It should be noted that modifications and adaptations to the present utility model may occur to one skilled in the art without departing from the principles of the present utility model and are intended to be within the scope of the present utility model.
Claims (10)
1. The hydrolytic ammonium carbonate gas fertilizer machine is characterized in that: including casing (1), retort (2), heater (3), fan (4), retort (2) are installed in casing (1), and open at the top has gas vent (21), and gas vent (21) communicate to fan (4) outside the casing through blast pipe (5), and retort (2) bottom below is located in heater (3), fan (4) are electric connection power switch (6) outside the casing respectively.
2. The hydrolyzed ammonium bicarbonate gas fertilizer machine of claim 1, wherein: the top of the reaction tank (2) is provided with a feed inlet (22) which is communicated with the outside of the shell, and the lower part of the reaction tank (2) is provided with a water outlet (23) which is communicated with the outside of the shell.
3. The hydrolyzed ammonium bicarbonate gas fertilizer machine of claim 1, wherein: a temperature measuring thermocouple (7) is arranged in the reaction tank (2) and is connected with a temperature control box (8) arranged outside the shell.
4. The hydrolyzed ammonium bicarbonate gas fertilizer machine of claim 1, wherein: the side wall of the upper part in the reaction tank (2) is provided with a liquid level sensor (9), and a signal is connected with a liquid level alarm indicator lamp (10) outside the shell.
5. The hydrolyzed ammonium bicarbonate gas fertilizer machine of claim 1, wherein: an electric switch valve (12) is arranged on a drain pipe connected with the drain outlet (23) of the reaction tank, and the electric switch valve (12) is in signal connection with a power switch (6) outside the shell.
6. The hydrolyzed ammonium bicarbonate gas fertilizer machine according to claim 1 or 4, wherein: the shell is also provided with a switch indicator lamp (11), and the switch indicator lamp (11) is electrically connected with the power switch (6).
7. The hydrolyzed ammonium bicarbonate gas fertilizer machine of claim 1, wherein: the fan (4) is arranged on the top surface of the shell (1), an air outlet of the fan (4) is connected with a ventilation pipe (13), and air outlet holes are formed in the ventilation pipe (13) in a rolling mode at intervals.
8. The hydrolyzed ammonium bicarbonate gas fertilizer machine of claim 1, wherein: the feed inlet (22) is communicated with the top surface of the shell (1) near the edge.
9. The hydrolyzed ammonium bicarbonate gas fertilizer machine of claim 1, wherein: the reaction tank (2) is made of stainless steel.
10. The hydrolyzed ammonium bicarbonate gas fertilizer machine of claim 1, wherein: the bottom of the shell (1) is provided with a movable wheel (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321387153.7U CN219628417U (en) | 2023-06-02 | 2023-06-02 | Hydrolytic ammonium carbonate gas fertilizer machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321387153.7U CN219628417U (en) | 2023-06-02 | 2023-06-02 | Hydrolytic ammonium carbonate gas fertilizer machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219628417U true CN219628417U (en) | 2023-09-05 |
Family
ID=87809244
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321387153.7U Active CN219628417U (en) | 2023-06-02 | 2023-06-02 | Hydrolytic ammonium carbonate gas fertilizer machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219628417U (en) |
-
2023
- 2023-06-02 CN CN202321387153.7U patent/CN219628417U/en active Active
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