CN208684822U - A kind of equipment using immersion coal production sodium humate - Google Patents
A kind of equipment using immersion coal production sodium humate Download PDFInfo
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- CN208684822U CN208684822U CN201820921713.5U CN201820921713U CN208684822U CN 208684822 U CN208684822 U CN 208684822U CN 201820921713 U CN201820921713 U CN 201820921713U CN 208684822 U CN208684822 U CN 208684822U
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Abstract
The utility model discloses a kind of equipment using immersion coal production sodium humate, comprising: coal store, collection slurry tank, stock tank, reaction kettle, liquid caustic soda memory, solid-state caustic soda memory, lets out sediment slot, drying extraction pot, steel detritus tank, electric heating conduction oil furnace and autometering packaging machine at water mill.The utility model has green, environmental protection, clean, non-harmful characteristic, can be avoided the sunning of large area land occupation cause sewage toward underground leakage, manually ted be harmful to one's health, the drawbacks such as low output and cost of labor height.In the utility model, feed coal is soaked operation, it is able to suppress the dust pollution of feed coal in process, using electric heating conduction oil furnace entire production process is discharged without gas, the drying extraction sodium humate finished product in closed workshop, dependence and wind for natural environment can be got rid of and rained, product is stained.The utility model is few using equipment, and simple production process, can be mass-produced sodium humate.
Description
Technical field
The utility model relates to industrial chemicals production equipment more particularly to a kind of setting using immersion coal production sodium humate
It is standby.
Background technique
Sodium humate alias natrium humate, rotten sodium are a kind of black crystals soluble easily in water.Contain hydroxyl in sodium humate
Base, quinonyl and carboxyl isoreactivity group, sodium humate have very big internal surface area and stronger absorption, exchange, complexing and
Sequestering power.Sodium humate is industrially applied to ceramic additive, degumming agent, drilling mud adjustment as a kind of additive
Agent, industrial water stabilizer, cement water reducing agent, boiler detergent, ore floatation agent, exhaust gas waste water treating agent, coal briquette bond
In negative battery plate expander, agriculturally it is being applied in compound fertilizer.In addition, sodium humate is gone back in terms of livestock culture
It can be used as feed addictive, synergist be used as in terms of aquaculture.Therefore, sodium humate has a vast market foreground.
Sodium humate be reacted with caustic soda the low magnesium weathered coal of low calcium naturally containing humic acid and passed through processing and made of
High-molecular compound, traditional sodium humate production technology are to make weathering at normal temperature after crushing weathered coal in open-air atmosphere
Coal reacts in the reaction vessel with caustic soda, and then the solid in the solidliquid mixture after reaction precipitates, and extracts upper liquid
Body simultaneously evaporates the solvent in supernatant liquid according to solarization using natural wind and sunlight, and then sodium humate crystal structure is precipitated.
Traditional production technology mainly by sunning be precipitated sodium humate finished product, in traditional production technology, weathered coal and
The reaction rate of caustic soda at normal temperature is slow, and the time for leading to react required is long and reaction is insufficient, results in waste of resources.Liquid
Dry large area land occupation, sunning and evaporation process not only needed for time it is long, but also take up a large area, wind and weather can make
The sodium humate finished product ballooning of dryness in the sun is obtained with rainwater slime flux, pollutes environment.Meanwhile during sunning, contain
The solution of reactant understands some and permeates the ground, and causes underground water pollution.In addition, also needing to employ a large amount of people during sunning
Power stirs the sodium humate after crystallization repeatedly to ensure that final finished product can be dried sufficiently, causes whole production process time-consuming
Longer, production efficiency is low.In addition, during outdoor sunning, since sodium humate finished product is exposed to outdoor environment sunning and phoenix
It is dry, cause the finished product of sodium humate to be easy by contaminateds such as rainwater and dusts storm, and then lead to sodium humate finished product
Quality is low.
It is that environmental consciousness gradually enhances recently as manufacturing enterprise, has enterprise using gas generator or natural gas conduct
The energy produces sodium humate in workshop.Though its various drawback for overcoming traditional processing technology still storing and is feeding intake
Inevasible generation dust, the dust of these coals are flowed with air in the process, the production environment of this enterprise are not only polluted, to public affairs
Environment can also generate a little destruction.Moreover, the production technology heated using the coal gas of gas generator and use natural gas,
There are still the factors that discharge carbon dioxide and CO gas influence environment.
Utility model content
The utility model provides a kind of equipment using immersion coal production sodium humate, is set to closed workshop
It is interior, to solve to generate dust, and the link discharge carbon dioxide in heating during existing sodium humate production equipment feeds intake
The problem of with carbon monoxide gas body pollution environment.
It is provided by the utility model it is a kind of using immersion coal production sodium humate equipment, comprising: coal store, water mill,
Collection slurry tank, reaction kettle, liquid caustic soda memory, solid-state caustic soda memory, lets out sediment slot, drying extraction pot, steel sediment at stock tank
Pond, electric heating conduction oil furnace and autometering packaging machine；
The feed coal entrance top of the coal store is provided with water jet, and the water jet is connected to water source, the coal storage
Feed coal sorter is provided in storehouse；
The outlet of the coal store is connected to by the first conveying device with the entrance of the water mill；
The collection slurry tank includes main tank and bypass tank, and the outlet of the water mill is connected to the entrance of the main tank, described
The first blender and pH value electronic sensor, the bottom of the bottom of the main tank side wall and the bypass pot sidewall are provided in main tank
Portion is connected to, and is provided with the second conveying device in the bypass tank；
The bypass tank is connected to by the second conveying device with one end of the stock tank, and the other end of the stock tank is provided with
Multiple outlets of multiple outlets, the stock tank are connected to the entrance of the reaction kettle respectively；
The water source is also connected to the water mill and stock tank respectively, the liquid caustic soda memory and the storage of solid-state caustic soda
Device is connected to the water mill, collection slurry tank and stock tank respectively；
The second blender and pH value electronic sensor are provided in the reaction kettle, the side wall of the reaction kettle is in vertical side
Multiple first outlets are set up, the bottom of the reaction kettle is set as funnel-shaped structure, the bottom of the funnel-shaped structure
It is provided with second outlet, the side wall at the top of the reaction kettle is provided with multiple thirds outlets, multiple first outlets, the
Two outlets and multiple third outlets are respectively arranged with valve；
Multiple first outlets respectively with it is described drying extraction pot entrance be connected to, the second outlet with it is described let out it is heavy
One end of slag chute is connected to, and the other end for letting out sediment slot is connected to the steel detritus tank, multiple third outlet difference
It is connected to the entrance of the water mill；
It is the structure that semi-circular upper portions are rectangle that the drying extraction pot, which is set as horizontal positioned lower part, the drying extraction
It takes and is axially provided with rotor segment in pot, the front end of the rotor segment is contacted with the inner wall of the drying extraction pot, the baking
The top surface of dry extraction pot offers steam (vapor) outlet, the bottom of the drying extraction pot along the length direction that the drying extracts pot
Discharge port is offered, the discharge port is connected to by third conveying device with the autometering packaging machine, and the discharge port is set
It is equipped with closing device；
The drying extraction pot and steel detritus tank are provided with thermally conductive oil reservoir, the thermally conductive oil reservoir setting of the steel detritus tank
In the skirt section of the steel detritus tank, the oil outlet of the electric heating conduction oil furnace connects with the entrance of the thermally conductive oil reservoir respectively
Logical, the outlet of the thermally conductive oil reservoir is connected to the oil return opening of the electric heating conduction oil furnace respectively.
In one embodiment of the utility model, first conveying device be belt conveyor, bucket elevator or
Screw propeller.
In one embodiment of the utility model, the feed coal sorter is sliding sieve, jaw crusher, roller pair breaking
Machine or hammer mill.
In one embodiment of the utility model, second conveying device is immersible pump.
In one embodiment of the utility model, the third conveying device is belt conveyor.
In one embodiment of the utility model, the entrance of the thermally conductive oil reservoir is respectively arranged at the drying extraction pot
Bottom and steel detritus tank skirt section bottom end, the outlet of the thermally conductive oil reservoir is respectively arranged at drying extraction pot skirt
The top on the top in portion and steel detritus tank skirt section.
Inclined bottom surface setting in one embodiment of the utility model, in the steel detritus tank.
It is provided by the utility model it is a kind of using immersion coal production sodium humate equipment include it is following the utility model has the advantages that
The utility model has green, environmental protection, cleaning, non-harmful characteristic, provided by the utility model to use immersion coal
The equipment for producing sodium humate can be avoided traditional mode of production by sunlight and wind evaporation water and cause black humic acid sodium crystalline solid
Ballooning pollution environment, large area land occupation sunning cause sewage toward underground leakage, manually ted be harmful to one's health, product product
The drawbacks such as matter is unstable, low output and cost of labor height.Additionally it is possible to avoid directly throwing using dry feed coal milling
Material causes coal dust to wave, pollutes environment, being harmful to one's health and being also easy to produce the bad and risk factors such as explosion because coal dust gathers.It can also
Avoid the defect that carbon emission is caused using coal gas or natural gas.In the utility model, feed coal is soaked operation, can effectively be solved
The certainly dust pollution of feed coal in process discharges entire production process without gas using electric heating conduction oil furnace,
Drying extraction sodium humate finished product, can get rid of the dependence for natural environment in closed workshop.The utility model uses
Equipment is few, simple production process, is suitable for producing sodium humate in enormous quantities.
Detailed description of the invention
Fig. 1 is a kind of structural representation of equipment that sodium humate is produced using immersion coal provided by the embodiment of the utility model
Figure；
Fig. 2 is the structural schematic diagram of collection slurry tank provided by the embodiment of the utility model；
Fig. 3 is the structural schematic diagram of reaction kettle provided by the embodiment of the utility model；
Fig. 4 is the structural schematic diagram of steel detritus tank provided by the embodiment of the utility model；
Fig. 5 is the structural schematic diagram of drying extraction pot provided by the embodiment of the utility model；
Fig. 6 is the axial, cross-sectional view of drying extraction pot provided by the embodiment of the utility model.
Figure label indicates:
1- coal store, 2- water mill, 3- collection starch tank, 4- stock tank, 5- reaction kettle, 6- liquid caustic soda memory, 7- solid-state burning
Alkali memory, 8- let out sediment slot, 9- drying extraction pot, 10- steel detritus tank, 11- electric heating conduction oil furnace, 12- automatic gauge
Packing machine, 13- feed coal entrance, 14- water jet, the water source 15-, 16- feed coal sorter, the first conveying device of 17-, 18-
Two conveying devices, 19- first outlet, 20- second outlet, 21- rotor segment, 22- steam (vapor) outlet, 23- discharge port, 24- third
Conveying device, 25- closing device, the thermally conductive oil reservoir of 26-, 27-pH value electronic sensor, 28- main tank, 29- bypass tank, 30- connection
Part, the first blender of 31-, the second blender of 32-, 33- belt pulley, the outlet of 34- third.
Specific embodiment
The utility model is described in further detail with reference to the accompanying drawings and examples.
Referring to Fig. 1, for a kind of knot for the equipment for producing sodium humate using immersion coal provided by the embodiment of the utility model
Structure schematic diagram.
The equipment includes: coal store 1, water mill 2, collection slurry tank 3, stock tank 4, reaction kettle 5, liquid caustic soda memory 6, solid-state
Caustic soda memory 7 lets out sediment slot 8, drying extraction pot 9, steel detritus tank 10, electric heating conduction oil furnace 11 and automatic measuring packing
Machine 12.
Water jet 14 is provided with above the feed coal entrance 13 of the coal store 1, the water jet 14 is connected to water source 15,
Feed coal sorter 16 is provided in the coal store 1.The feed coal sorter 16 is sliding sieve, jaw crusher, breaks to roller
Broken machine or hammer mill.
When dump truck enters coal store 1 and dumps feed coal, it is also easy to produce dust pollution air, in addition, coal is combustible, for a long time
Using pulverizer and Raymond mill etc. to anhydrous dry coal powder, coal dust aggregation, the pyrotechnics of smoking, mechanical friction collision are had naturally
Mars, the spark that issues of electric switch or even electrostatic even mobile phone communication is likely to set off an explosion and fire.Therefore in coal storage
Water jet 14 is set above the feed coal entrance 13 in storehouse 1, to feed coal water spray dust suppression.Feed coal sorter 16 is for removing original
Expect that in coal be stone wood etc., and the bulk crushing in feed coal is extremely adapted with granularity required by water mill 2.
The outlet of the coal store 1 is connected to by the first conveying device 17 with the entrance of the water mill 2.Described first is defeated
Sending device 17 is belt conveyor, bucket elevator or screw propeller.
Feed coal after the sorting of feed coal sorter 16 is delivered in water mill 2 by the first conveying device 17, right
Feed coal is further ground, and keeps its granularity smaller, and lesser granularity can make the contact area of feed coal and caustic soda bigger,
Feed coal and reacting for caustic soda are just more quickly and abundant.
It referring to fig. 2, is the structural schematic diagram of collection slurry tank provided by the embodiment of the utility model.
The collection slurry tank 3 includes main tank 28 and bypass tank 29, and the outlet of the water mill 2 connects with the entrance of the main tank 28
It is logical, the first blender 31 and pH value electronic sensor 27, the bottom of 28 side wall of main tank and institute are provided in the main tank 28
The bottom connection of bypass 29 side wall of tank is stated, is provided with the second conveying device 18 in the bypass tank 29.
The bypass tank 29 is connected to by the second conveying device 18 with one end of the stock tank 4, the other end of the stock tank 4
Multiple outlets are provided with, multiple outlets of the stock tank 4 are connected to the entrance of the reaction kettle 5 respectively.The second conveying dress
18 are set as immersible pump.
The water source 15 is also connected to the water mill 2 and stock tank 4 respectively, and the liquid caustic soda memory 6 and solid-state are burnt
Alkali memory 7 is connected to the water mill 2, collection slurry tank 3 and stock tank 4 respectively.
Feed coal after the sorting of feed coal sorter 16 is delivered in water mill 2 by the first conveying device 17, together
When suitable quantity of water and caustic soda are added into water mill 2, during so that two kinds of raw materials is ground into sodium humate slurries in water mill 2
Carry out combination reaction.Water mill 2 can be set multiple, and the outlet of coal store 1 is connected to multiple water mills 2 respectively.
For more substantially entirely cost can be reduced using raw material, the slurries of the outlet outflow of multiple water mills 2 can be collected,
And high-frequency screen is arranged in the outlet after collecting.The feed coal powder collection in coal slurry is put into water mill 2 again using high-frequency screen,
It is ground to refinement repeatedly, accomplishes raw material using maximization.
Main tank 28 in collection slurry tank 3 is used to collect water mill 2 and the slurries come is ground, and passes through the first blender 31 for coal
Chemical combination is sufficiently stirred in slurry and caustic soda again, and the first blender 31 is driven by belt pulley 33.Main tank 28 and bypass tank 29 are in side wall
Bottom connection is in order to not influence the blender work in main tank 28 in the collection slurry setting bypass tank 29 of tank 3, and coal slurry is in bypass tank
It is delivered in stock tank 4 in 29 by the second conveying device 18.Main tank 28 and bypass tank 29 in collection slurry tank 3 pass through connector 30
It is fixed.
Water source 15 is connected to collection slurry tank 3, for adjusting the concentration of caustic soda reduced in collection slurry tank 3.
Stock tank 4 distributes liquid caustic soda and is delivered in reaction kettle 5 for collecting and shunting coal slurry.
It is provided with pH value electronic sensor 27 in collection slurry tank 3, for the pH value of real-time monitoring slurries, judges that sodium humate is starched
Whether the pH value of liquid has reached optimum response state, due to containing of a certain amount of tiny (or even micron order) in coal slurry
Grain, this particle and caustic soda reaction need the regular hour, and as the reaction time extends, the Ph value of slurries also can wave therewith
It is dynamic.Therefore, liquid caustic soda memory 6 and solid-state caustic soda memory 7 are connected to water mill 2, collection slurry tank 3 and stock tank 4 respectively, mesh
Be at many levels more subtly monitor slurries Ph value variation and be finally adjusted to optimum value.
It is the structural schematic diagram of reaction kettle provided by the embodiment of the utility model referring to Fig. 3.
The second blender 32 and pH value electronic sensor 27 are provided in the reaction kettle 5, the side wall of the reaction kettle 5 exists
Multiple first outlets 19 are provided on vertical direction, the bottom of the reaction kettle 5 is set as funnel-shaped structure, the infundibulate knot
The bottom of structure is provided with second outlet 20, and the side wall close to 5 top of reaction kettle is provided with multiple third outlets 34, Duo Gesuo
It states first outlet 19, second outlet 20 and multiple third outlets 34 and is respectively arranged with valve.
Multiple first outlets 19 are connected to the entrance of the drying extraction pot 9 respectively, the second outlet 20 and institute
One end connection for letting out sediment slot 8 is stated, the other end for letting out sediment slot 8 is connected to the steel detritus tank 10, and multiple described the
Three outlets 34 are connected to the entrance of the water mill 2.
Second blender 32 is driven by belt pulley 33, and the blender in reaction kettle 5 is used for coal slurry and caustic soda is further
Chemical combination is stirred, and reacts feed coal sufficiently with caustic soda under lasting stirring, pH value electronic sensor 27 is used for real-time monitoring
The pH value of coal slurry, to its monitoring pH value the regular hour it is continual and steady conform to quality requirements, that is, represent reaction and complete.
After the reaction was completed, the second blender 32 is closed, to slurries precipitated and separated, though contain humic acid in top layer's clear liquid
Sodium, but its moisture is also more, opens the third outlet 34 on 5 side wall of reaction kettle one by one from top to bottom, the upper layer of reaction kettle is clear
Liquid, which is expelled to, to be continued to play the part of coal grinding in water mill 2.Multiple first outlets 19 are opened, denseer slurries are imported into drying extraction pot 9
Middle evaporation water extracts finished product.First outlet 19 and 34 setting of third outlet is multiple, it can be convenient for the stream of control discharge liquid
Amount, preventing the too urgent sediment for leading to 5 bottom of reaction kettle of slurry flow rate to be mixed into slurries under the active force that liquid flows influences product
Quality.
The reactant sediment of 5 bottom of reaction kettle is assembled by the funnel-shaped structure of reaction kettle 5, sodium humate to be contained
Supernatant liquor discharge after, open second outlet 20 and sediment is expelled to lets out in sediment slot 8, let out sediment slot 8 and sediment is directed at steel
In matter detritus tank 10.
Reaction kettle 5 also can be set it is multiple, to increase yield, and respectively with stock tank 4 and let out sediment slot 8 and be connected to.Reaction
Kettle 5 is arranged aloft, opens valve, and the slurries in reaction kettle 5 can flow to predetermined position from pipeline naturally, saves the energy.
It referring to fig. 4, is the structural schematic diagram of steel detritus tank provided by the embodiment of the utility model.
Detritus tank uses steel, and to prevent the moisture in sediment from penetrating into soil, the bottom angled of steel detritus tank 10 is arranged,
It constitutes dustpan-shaped.
Referring to figs. 5 and 6, the structural schematic diagram of drying extraction pot respectively provided by the embodiment of the utility model and drying
Extract the axial, cross-sectional view of pot.
It is the structure that semi-circular upper portions are rectangle, the drying that the drying extraction pot 9, which is set as horizontal positioned lower part,
Rotor segment 21 is axially provided in extraction pot 9, the front end of the rotor segment 21 and the inner wall of the drying extraction pot 9 connect
Touching, the top surface of the drying extraction pot 9 offer steam (vapor) outlet 22, the drying along the length direction that the drying extracts pot 9
The bottom of extraction pot 9 offers discharge port 23, and the discharge port 23 passes through third conveying device 24 and the automatic measuring packing
Machine 12 is connected to, and the discharge port 23 is provided with closing device 25.The third conveying device 24 is belt conveyor.
The skirt section and bottom of the drying extraction pot 9 are provided with thermally conductive oil reservoir 26, the skirt section of the steel detritus tank 10
It is provided with thermally conductive oil reservoir 26, the oil outlet of the electric heating conduction oil furnace 11 is connected to the entrance of the thermally conductive oil reservoir 26 respectively,
The outlet of the thermally conductive oil reservoir 26 is connected to the oil return opening of the electric heating conduction oil furnace 11 respectively.
The entrance of the thermally conductive oil reservoir 26 is respectively arranged at the bottom for drying extraction pot 9 and the steel detritus tank 10
The bottom end in skirt section, the outlet of the thermally conductive oil reservoir 26 are respectively arranged at the top for drying extraction 9 skirt section of pot and the steel
The top in 10 skirt section of detritus tank.
Can be with non-carbon-emitting using electric heating conduction oil furnace 11, the thermally conductive oil temperature exported is 300 DEG C or so, drying extraction
Take pot 9 and steel detritus tank 10 that thermally conductive oil reservoir 26 is set, the conduction oil after heating is delivered to thermally conductive by electric heating conduction oil furnace 11
It is heated in oil reservoir 26 for drying extraction pot 9 and steel detritus tank 10.
Drying extraction pot 9 also can be set it is multiple, drying extraction pot 9 be used under conditions of heat-conducting oil heating, will contain
Moisture in the slurries of sodium humate gradually evaporates, and vapor is distributed by the steam (vapor) outlet 22 at top, keeps sodium humate de-
Water crystallization, the sodium humate for crystallizing precipitation can be attached to the inner wall surface of drying extraction pot 9, and rotor segment 21 is used for humic acid
Sodium crystal, which is scraped, is transported to the packaging of autometering packaging machine 12 into third conveying device 24 through discharge port 23, after finally packing
Sodium humate be transported in warehouse for finished product and save.
The steam (vapor) outlet 22 at drying extraction pot 9 top is provided with top cover, can when needing to discharge steam opening.
As needed, drying extraction pot 9 can be set to that pot body may be reversed, and rotor segment 21 is used for sodium humate crystal
Directly overturning pot body pours out sodium humate crystal after scraping.When being set as that pot body may be reversed, drying extraction pot 9 is led with electric heating
Hot oil furnace 11 is connected by hose resistant to high temperature.
Steel detritus tank 10 removes the moisture in sediment under the heating condition of conduction oil, and the sediment after drying is high-quality
Organic composite chemical fertilizer, soil can be improved, enhance the lodging tolerance of plant, increase fruit yield, improve fruit quality.It is dry
Sediment after dry is dug out by mechanical equipment to be transported.
Conduction oil to be sent into from the bottom of thermally conductive oil reservoir 26, the mode that top is sent out can be improved the utilization rate of conduction oil,
Thermal losses is reduced, the heat in conduction oil is made full use of to heat for drying extraction pot 9 and steel detritus tank 10.
In conclusion a kind of equipment using immersion feed coal production sodium humate provided by the utility model is with green
Color, environmental protection, cleaning, non-harmful characteristic, the equipment provided by the utility model using immersion feed coal production sodium humate are complete
Traditional mode of production is avoided entirely causes black humic acid sodium crystalline solid ballooning pollution environment, big by sunlight and wind evaporation water
Area land occupation carry out sunning cause sewage toward underground leakage, manually ted be harmful to one's health, product quality is unstable, low output
And the drawbacks such as cost of labor height.Additionally it is possible to avoid directly feeding intake using dry feed coal milling cause coal dust to wave,
Pollution environment is harmful to one's health and is also easy to produce the bad and risk factors such as explosion because coal dust gathers；Also be avoided that using coal gas or
The defect of carbon emission caused by natural gas.In the utility model, feed coal is soaked operation, can effectively solve the problem that feed coal is adding
Dust pollution during work discharges entire production process without gas using electric heating electric heating conduction oil furnace, closed
Workshop in drying extraction sodium humate finished product, the dependence for natural environment can be got rid of.The utility model is few using equipment,
Small, simple production process is invested, is suitable for producing sodium humate in enormous quantities.
The specific embodiment of above-described utility model does not constitute the restriction to scope of protection of the utility model.
Claims (7)
1. a kind of equipment using immersion coal production sodium humate characterized by comprising coal store (1), water mill (2), collection
Slurry tank (3), reaction kettle (5), liquid caustic soda memory (6), solid-state caustic soda memory (7), lets out sediment slot (8), dries stock tank (4)
Dry extraction pot (9), steel detritus tank (10), electric heating conduction oil furnace (11) and autometering packaging machine (12)；
It is provided with water jet (14) above the feed coal entrance (13) of the coal store (1), the water jet (14) and water source
(15) it is connected to, is provided with feed coal sorter (16) in the coal store (1)；
The outlet of the coal store (1) is connected to by the first conveying device (17) with the entrance of the water mill (2)；
Collection slurry tank (3) includes main tank (28) and bypass tank (29), outlet and the main tank (28) of the water mill (2)
Entrance connection, the main tank (28) is interior to be provided with the first blender (31) and pH value electronic sensor (27), the main tank (28)
The bottom of side wall is connected to the bottom of described bypass tank (29) side wall, is provided with the second conveying device in the bypass tank (29)
(18)；
Bypass tank (29) is connected to by the second conveying device (18) with one end of the stock tank (4), the stock tank (4) it is another
One end is provided with multiple outlets, and multiple outlets of the stock tank (4) are connected to the entrance of the reaction kettle (5) respectively；
The water source (15) is also connected to the water mill (2) and stock tank (4) respectively, the liquid caustic soda memory (6) and solid
State caustic soda memory (7) is connected to the water mill (2), collection slurry tank (3) and stock tank (4) respectively；
The second blender (32) and pH value electronic sensor (27), the side of the reaction kettle (5) are provided in the reaction kettle (5)
Wall is provided with multiple first outlets (19) in the vertical direction, and the bottom of the reaction kettle (5) is set as funnel-shaped structure, described
The bottom of funnel-shaped structure is provided with second outlet (20), and the side wall at the top of the reaction kettle (5) is provided with multiple thirds
It exports (34), multiple first outlets (19), second outlet (20) and multiple third outlets (34) are respectively arranged with valve
Door；
Multiple first outlets (19) respectively with it is described drying extraction pot (9) entrance be connected to, the second outlet (20) and
One end connection for letting out sediment slot (8), the other end for letting out sediment slot (8) is connected to the steel detritus tank (10), more
A third outlet (34) is connected to the entrance of the water mill (2)；
It is the structure that semi-circular upper portions are rectangle that drying extraction pot (9), which is set as horizontal positioned lower part, the drying extraction
It takes and is axially provided with rotor segment (21) in pot (9), the front end of the rotor segment (21) is interior with drying extraction pot (9)
Wall contact, the top surface of drying extraction pot (9) offer steam (vapor) outlet along the length direction that the drying extracts pot (9)
(22), the bottom of drying extraction pot (9) offers discharge port (23), and the discharge port (23) passes through third conveying device
(24) it is connected to the autometering packaging machine (12), the discharge port (23) is provided with closing device (25)；
The skirt section and bottom of drying extraction pot (9) are provided with thermally conductive oil reservoir (26), the skirt section of the steel detritus tank (10)
It is also equipped with thermally conductive oil reservoir (26), the oil outlet of the electric heating conduction oil furnace (11) enters with thermally conductive oil reservoir (26) respectively
Mouth connection, the outlet of the thermally conductive oil reservoir (26) is connected to the oil return opening of the electric heating conduction oil furnace (11) respectively.
2. the equipment according to claim 1 using immersion coal production sodium humate, which is characterized in that first conveying
Device (17) is belt conveyor, bucket elevator or screw propeller.
3. the equipment according to claim 1 using immersion coal production sodium humate, which is characterized in that the feed coal point
Select device (16) for sliding sieve, jaw crusher, double-roll crusher or hammer mill.
4. the equipment according to claim 1 using immersion coal production sodium humate, which is characterized in that second conveying
Device (18) is immersible pump.
5. the equipment according to claim 1 using immersion coal production sodium humate, which is characterized in that the third conveying
Device (24) is belt conveyor.
6. the equipment according to claim 1 using immersion coal production sodium humate, which is characterized in that the thermally conductive oil reservoir
(26) entrance is respectively arranged at the bottom of drying extraction pot (9) and the bottom end in the steel detritus tank (10) skirt section, institute
The outlet for stating thermally conductive oil reservoir (26) is respectively arranged at top and the steel detritus tank (10) in drying extraction pot (9) skirt section
The top in skirt section.
7. the equipment according to claim 1 using immersion coal production sodium humate, which is characterized in that the steel sediment
Inclined bottom surface setting in pond (10).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820921713.5U CN208684822U (en) | 2018-06-14 | 2018-06-14 | A kind of equipment using immersion coal production sodium humate |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820921713.5U CN208684822U (en) | 2018-06-14 | 2018-06-14 | A kind of equipment using immersion coal production sodium humate |
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| CN208684822U true CN208684822U (en) | 2019-04-02 |
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| CN201820921713.5U Expired - Fee Related CN208684822U (en) | 2018-06-14 | 2018-06-14 | A kind of equipment using immersion coal production sodium humate |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110317348A (en) * | 2019-08-21 | 2019-10-11 | 四川锐源能环科技有限公司 | A kind of system equipment and method using low calorific value coal production humic acid |
| CN110358111A (en) * | 2019-08-21 | 2019-10-22 | 蒋遂安 | A kind of system and method for coal mining waste harmless resource production humic acid |
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2018
- 2018-06-14 CN CN201820921713.5U patent/CN208684822U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110317348A (en) * | 2019-08-21 | 2019-10-11 | 四川锐源能环科技有限公司 | A kind of system equipment and method using low calorific value coal production humic acid |
| CN110358111A (en) * | 2019-08-21 | 2019-10-22 | 蒋遂安 | A kind of system and method for coal mining waste harmless resource production humic acid |
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