CN106479536A - Rice straw charcoal production equipment and the technique for producing charcoal - Google Patents
Rice straw charcoal production equipment and the technique for producing charcoal Download PDFInfo
- Publication number
- CN106479536A CN106479536A CN201610203771.XA CN201610203771A CN106479536A CN 106479536 A CN106479536 A CN 106479536A CN 201610203771 A CN201610203771 A CN 201610203771A CN 106479536 A CN106479536 A CN 106479536A
- Authority
- CN
- China
- Prior art keywords
- rice straw
- charcoal
- reaction vessel
- cooler
- temperature
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/04—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition
- C10B57/06—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition containing additives
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
The invention discloses a kind of rice straw charcoal production equipment, including material feeding box, grinder, reaction vessel, discharging supply pipe, cracking case, stove, the first cooler, the second cooler.The present invention discloses a kind of technique for producing charcoal, first rice straw is entered material feeding box through charging aperture, enter back into grinder to be crushed, rice straw after crushing is entered through discharge valve and is processed in reaction vessel, after rice straw after process is cooled down through the first cooler, sending into cracking case by discharging supply pipe carries out Pintsch process, is then conveyed in stove and is carbonized, after rice straw after charing is cooled down through the second cooler, by discharge hole for discharge.Simple production process of the present invention, device therefor energy consumption are low, and cost is less than additive method more than 8%;With short production cycle, production process controllability is strong, and gained charcoal apparent specific gravity is big.
Description
Technical field
The invention belongs to charcoal production equipment and process technical field, is related to a kind of life of rice straw charcoal
Product equipment and the technique for producing charcoal.
Background technology
As crop yield is improved year by year, Rural Urbanization Development and life of farmers level are lifted further,
Agricultural crop straw yield is dramatically increased, and at the same time, stalk progressively declines as the proportion of utilization of firewood, greatly
The superfluous stalk abandoned of amount is in the edge of a field, roadside or irrigation canals and ditches, or burns in the edge of a field, to ecological environment and life,
Property safety brings great hidden danger.China is main Rice Production country, produces substantial amounts of water every year
Rice straw, rice straw are the byproducts that paddy rice shelling obtains gained after seed, the stalk after shelling and attachment
Cured leaf becomes stalk, and most rice straw is arbitrarily abandoned and burned, and causes great environmental pollution,
The quality of life of impact peasant, also results in the significant wastage of resource.
Charcoal be bio-organic materials (living beings) in anoxic or anoxybiotic environment, after high temperature pyrolysis
The solid product of generation.The high-quality energy, soil conditioner is can not only be used for, also can be used as reducing agent, fertilizer
Slow-released carrier and carbon dioxide sequestration agent etc., are widely used to carbon fixation and emission reduction, water source purifying, heavy metal and inhale
Soil improvement etc. is echoed, can be that climate change, environmental pollution and soil function degeneration etc. is complete to a certain extent
Ball hot issue deeply concerned provides solution.Charcoal can also improve agricultural productivity, reduce intensive to carbon
The demand of fertilizer.The pore space structure of charcoal particle very easily assembles nutriment and beneficial microbe, so as to
Make soil become fertile, beneficial to plant growth, realize while volume increase, allowing agricultural have more continuation.Still better
It is that it is locked in carbon in biota, rather than allows it be discharged in the air.Biomass carbonated technology is generally acknowledged
Solve the problems, such as one of possible technique measure of climate change, with raw material sources extensively, low production cost,
Ecological safety, pollution-free, can the distinguishing feature such as spread.
It can be a kind of with carbon fixation and emission reduction with environmental area that the charcoal produced after biomass carbonated is applied to ecological
Effectively carbon remittance technology, is combined with agriculture, forestry, it is possible to resolve agriculture and forestry organic waste material pollution and greenhouse gas emission
Problem.Charcoal applies farmland, can be effectively improved soil physico-chemical property, increases crop yield, promotes agricultural
Sustainable development.Charcoal is a kind of economically viable mode of fixing carbon dioxide, not only have cured trees
With the carbon dioxide for having been absorbed in crop, its product " biological carbon " is stored in soil, thousand of years all without
Change, while production regenerative resource, soil fertility is also improved, improve crop yield.Raw
Thing charcoal can be embedded in discarded colliery, or in placing into the soil when cultivating.Charcoal landfill also helps improvement soil
Earth drainage system, and 80% or so such as nitric oxide and methane isothermal chamber gas are sealed up for safekeeping in soil, resistance
Stop which to be discharged in air.At present rice straw charcoal production equipment and for produce charcoal technique very
Many, but high energy consumption, long the production cycle, production process poor controllability, cause gained charcoal apparent specific gravity little.
Therefore work out a kind of energy consumption low, cycle is short, the big charcoal production equipment of gained charcoal apparent specific gravity and
For the technique of charcoal is produced, there is important economic benefit and social value in association area.
State Intellectual Property Office's application number 200880013328.X application documents disclose one kind for producing biology
The equipment of charcoal and technique, the equipment include:Reducing mechanism, heater, pressue device and cooling device,
But the high energy consumption of this invention, the charcoal apparent specific gravity for obtaining are little.
Content of the invention
The technical problem to be solved:For current rice straw charcoal production equipment and for giving birth to
The process energy consumption of generation charcoal is high, long the production cycle, and production process poor controllability causes charcoal to produce into
This height, the drawbacks of gained charcoal apparent specific gravity is little, there is provided rice straw charcoal production equipment and be used for
The technique of production charcoal, the equipment and process energy consumption are low, with short production cycle, and production process controllability is strong,
Gained charcoal apparent specific gravity is big.
The present invention employs the following technical solutions realization, a kind of rice straw charcoal production equipment, including
Material feeding box, grinder, reaction vessel, discharging supply pipe, cracking case, stove, the first cooler, second
Cooler, the material feeding box are located above the grinder, and the material feeding box is provided with charging aperture, the crushing
Disintegrating knife is provided with device, is connected by discharge valve between the grinder and reaction vessel, the reaction
Container is provided with heater and pressue device, and the discharging supply pipe is connected between reaction vessel and stove,
First cooler is located on the stove located at the outlet connection of the reaction vessel, the cracking case
Face, the side wall of the stove are additionally provided with discharge nozzle, and second cooler is on discharge nozzle.
Preferably, pressure gauge is additionally provided with the reaction vessel.
Preferably, cracking case side wall is provided with argon inlet mouth.
Preferably, the discharging supply pipe is provided with tail gates near reaction vessel one end, and the other end is provided with brake application
Door, is provided with charging quantity detection sensor in the discharging supply pipe at the upper lock gate position, described enter
Doses detection sensor is used for detecting the inlet amount of cracking case, is examined with the tail gates, upper lock gate and inlet amount
Survey sensor is connected and is provided with MCU, is connected with the MCU and is provided with display screen, and the MCU prestores cracking case and enters
Doses preset data, the MCU is according to the inlet amount Data Control tail gates of charging quantity detection sensor collection
Opening and closing with upper lock gate.
Preferably, the reaction vessel is additionally provided with temperature-detecting device, and the temperature-detecting device is arranged on instead
Answer the exit of container, for detecting the reaction temperature in reaction vessel, the temperature-detecting device with described
MCU is connected with heater.
Preferably, the cracking case is additionally provided with temp measuring system, and the temp measuring system includes that thermo detector and thermometric are visited
Head, the temperature probe are deep in cracking case through the thermometer hole of cracking case, the outside and thermometric of temperature probe
Meter connection.
Preferably, the cracking lower box part is additionally provided with tar catalyst chamber, is provided with tar in the tar catalyst chamber
Catalyst.
Biological straw can produce tar in course of reaction and cracking process, and tar is piled up for a long time, can cause
Pipeline blockage, the blackspot pollution environment of in addition tar gas splash, sooting, smell difficulty are smelt, and impact production is biological
The quality of charcoal, it is nontoxic material that tar catalyst can convert tar.
Preferably, the stove exit is additionally provided with tar separator, is connected with the tar separator and is provided with
Coke tar cracking room, is connected with the coke tar cracking room and is provided with tar exhausting waste gas pipeline.
Although being reacted through catalyst by cracking room product out, a small amount of tar is still had to deposit in stove
, still affect product quality, by tar separator by tar separation out, be sent to coke tar cracking room pair
Tar is made further cracking and is processed, and obtains nontoxic material.
The present invention discloses a kind of technique for producing charcoal, comprises the following steps,
1) water intaking rice straw is put in material feeding box through charging aperture, enters back into grinder, arrange rotating speed be 300~
500r/min is crushed, and after the completion of crushing, the rice straw after crushing is introduced in reaction vessel through discharging
To be reacted, obtained fused mass, pressure is 0.6~0.8Mpa in control reaction vessel, temperature is 160~
180 DEG C, react 1~2h;
2) fused mass for obtaining is cooled to after room temperature through the first cooler, cracking is transported to by discharging supply pipe
In case, at 1000~1200 DEG C, Pintsch process being carried out, while be passed through argon gas being protected, cracking 3~5h;
3) after the completion of waiting to crack, it is transported in stove, control temperature is 600~800 DEG C, carry out carbonizing 1~
2h, is cooled to 23~25 DEG C through the second cooler, is discharged by discharge nozzle, that is, obtain rice straw charcoal.
Preferably, the technique for producing charcoal is comprised the following steps,
1) water intaking rice straw is put in material feeding box through charging aperture, enters back into grinder, and setting rotating speed is 400r/min
Crushed, after the completion of crushing, the rice straw after crushing is introduced in reaction vessel through discharging, control is anti-
It is 0.7Mpa to answer pressure in container, and temperature is 170 DEG C, reacts 1.5h;
2) fused mass for obtaining is cooled to after room temperature through the first cooler, cracking is transported to by discharging supply pipe
In case, at 1100 DEG C, Pintsch process being carried out, while be passed through argon gas being protected, cracking 4h;
3) after the completion of waiting to crack, it is transported in stove, control temperature is 700 DEG C, carries out charing 1.5h, warp
Second cooler is cooled to 24 DEG C, by discharge hole for discharge, that is, obtains rice straw charcoal.
Compared with other production active carbon method, Advantageous Effects are the present invention:
1) simple production process of the present invention, device therefor energy consumption are low, and cost is less than additive method more than 8%;
2) with short production cycle, production process controllability is strong, and gained charcoal apparent specific gravity is big.
Description of the drawings
Further illustrate with reference to the accompanying drawings and detailed description:
Fig. 1 is the structural representation of the rice straw charcoal production equipment of the embodiment of the present invention 1.
Fig. 2 is the structural representation of the rice straw charcoal production equipment of the embodiment of the present invention 2.
Fig. 3 is the structural representation of the rice straw charcoal production equipment of the embodiment of the present invention 3.
Fig. 4 is the frame principle figure that the upper and lower gate of the embodiment of the present invention 2 is opened and closed.
Specific embodiment
Embodiment 1
Fig. 1 gives one embodiment of the present invention, as shown in figure 1, a kind of life of rice straw charcoal
Product equipment, including material feeding box 2, grinder 4, reaction vessel 6, discharging supply pipe 10, cracking case 11, fire
Stove 12, the first cooler 9, the second cooler 13, the material feeding box 2 are located above the grinder 4,
The material feeding box 2 is provided with charging aperture 1, is provided with Disintegrating knife 3 in the grinder 4, the grinder 4 with
It is connected by discharge valve 5 between reaction vessel 6, the reaction vessel 6 is provided with heater 8 and pressurization
Device, the discharging supply pipe 10 are connected between reaction vessel 6 and stove 12, first cooler 9
Located at the outlet connection of the reaction vessel 6, the cracking case 11 is located above the stove 12, institute
The side wall for stating stove 12 is additionally provided with discharge nozzle 14, and second cooler 13 is on discharge nozzle 14.
Pressure gauge 7 is additionally provided with the reaction vessel 6.
The cracking 11 side wall of case is provided with argon inlet mouth.
Embodiment 2
Fig. 2 gives the 2nd embodiment of the present invention, as shown in Figure 2, Figure 4 shows, embodiment 2 and embodiment
Unlike 1, the discharging supply pipe 10 is additionally provided with tail gates 15, the other end near 6 one end of reaction vessel
Upper lock gate 16 is provided with, and inlet amount inspection is provided with the discharging supply pipe 10 at 16 position of the upper lock gate
Sensor 17 is surveyed, the charging quantity detection sensor 17 is used for the inlet amount of cracking case 11 to be detected, and described
Tail gates 15, upper lock gate 16 are connected with charging quantity detection sensor 17 and are provided with MCU18, with the MCU18
It is connected and display screen is provided with, the MCU18 prestores cracking 11 inlet amount preset data of case, the MCU18 root
According to charging quantity detection sensor 17 gather inlet amount Data Control tail gates 15 and upper lock gate 16 open and
Close.
The reaction vessel 6 is additionally provided with temperature-detecting device 19, and the temperature-detecting device 19 is arranged on reaction
The exit of container 6, for detecting the reaction temperature in reaction vessel 6, the temperature-detecting device 19 with
The MCU18 is connected with heater 8.
The cracking case 11 is additionally provided with temp measuring system, and the temp measuring system includes thermo detector and temperature probe, institute
State temperature probe to be deep in cracking case 11 through the thermometer hole of cracking case 11, the outside and thermometric of temperature probe
Meter connection.
Remaining is same as Example 1 for embodiment 2.
Embodiment 3
Fig. 3 gives the 3rd embodiment of the present invention, as shown in figure 3, embodiment 3 is with embodiment 2 not
With cracking 11 bottom of case is additionally provided with tar catalyst chamber 21, is provided with the tar catalyst chamber 21
Tar catalyst.
12 exit of the stove is additionally provided with tar separator 23, is connected with the tar separator 23 and is provided with
Coke tar cracking room 22, is connected with the coke tar cracking room 22 and is provided with tar exhausting waste gas pipeline.
Remaining is same as Example 2 for embodiment 3.
Embodiment 4
The present invention discloses a kind of technique for producing charcoal, comprises the following steps,
1) water intaking rice straw is put in material feeding box 2 through charging aperture 1, enters back into grinder 4, is arranged rotating speed and is
400r/min is crushed, and after the completion of crushing, the rice straw after crushing is introduced reaction vessel 6 through discharging
In reacted, obtain fused mass, in control reaction vessel 6, pressure is 0.7Mpa, and temperature is 170 DEG C,
Reaction 1.5h;
2) fused mass for obtaining is cooled to after room temperature through the first cooler 9, is conveyed by discharging supply pipe 10
To in cracking case 11, at 1100 DEG C, Pintsch process being carried out, while be passed through argon gas being protected, cracking 4h;
3) after the completion of waiting to crack, it is transported in stove 12, control temperature is 700 DEG C, carries out charing 1.5h,
24 DEG C are cooled to through the second cooler 13, discharge through discharge nozzle 14, that is, obtain rice straw charcoal.
Embodiment 5
A kind of technique for producing charcoal, comprises the following steps,
1) water intaking rice straw is put in material feeding box 2 through charging aperture 1, enters back into grinder 4, is arranged rotating speed and is
300r/min is crushed, and after the completion of crushing, the rice straw after crushing is introduced reaction vessel 6 through discharging
In reacted, obtain fused mass, in control reaction vessel 6, pressure is 0.6Mpa, and temperature is 160 DEG C,
Reaction 1h;
2) fused mass for obtaining is cooled to after room temperature through the first cooler 9, is conveyed by discharging supply pipe 10
To in cracking case 11, at 1000 DEG C, Pintsch process being carried out, while be passed through argon gas being protected, cracking 3h;
3) after the completion of waiting to crack, it is transported in stove 12, control temperature is 600 DEG C, carries out charing 1h,
23 DEG C are cooled to through the second cooler 13, discharge through discharge nozzle 14, that is, obtain rice straw charcoal.
Embodiment 6
A kind of technique for producing charcoal, comprises the following steps,
1) water intaking rice straw is put in material feeding box 2 through charging aperture 1, enters back into grinder 4, is arranged rotating speed and is
500r/min is crushed, and after the completion of crushing, the rice straw after crushing is introduced reaction vessel 6 through discharging
In reacted, obtain fused mass, in control reaction vessel 6, pressure is 0.8Mpa, and temperature is 180 DEG C,
Reaction 2h;
2) fused mass for obtaining is cooled to after room temperature through the first cooler 9, is conveyed by discharging supply pipe 10
To in cracking case 11, at 1200 DEG C, Pintsch process being carried out, while be passed through argon gas being protected, cracking 5h;
3) after the completion of waiting to crack, it is transported in stove 12, control temperature is 800 DEG C, carries out charing 2h,
25 DEG C are cooled to through the second cooler 13, discharge through discharge nozzle 14, that is, obtain rice straw charcoal.
Test example 1:Charcoal apparent specific gravity is determined
Charcoal that the embodiment of the present invention 4 obtain is taken respectively as experimental group and application number 200880013328.X
The charcoal that obtains of invention as a control group, determine apparent specific gravity, the results are shown in Table 1.
1 charcoal apparent specific gravity of table
After measured, the apparent specific gravity of the charcoal that the present invention is obtained is 1.92-2.04, and application number
The apparent specific gravity of the charcoal that the patent of invention of 200880013328.X is obtained is 1.2-1.38, and the present invention is obtained
Charcoal apparent specific gravity apparently higher than the charcoal obtained with other production equipments and production method.
Test example 2:Charcoal physical characteristic is determined
The charcoal that relatively the present embodiment 4 is obtained and Wooden Biomass and the physical characteristic of coal coke, are as a result shown in
Table 2.
2 charcoal physical characteristic of table and the other materials table of comparisons
Performance of the charcoal that the present invention is obtained in terms of hardness and inflammability is more superior.
By technique productions charcoal of the present invention, the charcoal of high rigidity and high heating value can be obtained, anti-
Answer in container, by heating biological matter at a temperature of 160 to 180, as biomass material main become
/ mono- hemicellulose is pyrolyzed, and lignin keep its framework in the case of with consolidation effect phase interaction
With enhancing intensity whereby.
Test example 3
Compare in the case of technique of the present invention for producing charcoal takes different parameter values and parameter value is not at this
The charcoal physical characteristic obtained in the case of invention scope, the results are shown in Table 3.
3 charcoal physical characteristic of table
As can be seen from the table, change the present invention preparation technology parameter by the apparent specific gravity of charcoal and
Calorific value has a huge impact, and only limits within the scope of the present invention, could obtain apparent specific gravity height,
The high charcoal of calorific value.
Industrial applicibility
By using the charcoal production equipment and process of the present embodiment, efficiently can produce with high rigidity
With the charcoal of golf calorific value, the charcoal can serve as the substitute of coal coke.Produced according to the present embodiment
Charcoal can be used for the cupola furnace of cast iron or ironmaking or the thermal source in blast furnace, reducing agent etc., Yi Jiyong
Make the material using high compression-strength charcoal.
Embodiment described above is only that the preferred embodiment of the present invention is described, not to the present invention's
Scope is defined, and on the premise of without departing from design spirit of the present invention, those of ordinary skill in the art are to this
Various modifications and improvement that the technical scheme of invention is made, all should fall into claims of the present invention determination
In protection domain.
Claims (10)
1. a kind of rice straw charcoal production equipment, it is characterised in that including material feeding box (2), crush
Device (4), reaction vessel (6), discharging supply pipe (10), cracking case (11), stove (12),
First cooler (9), the second cooler (13), described material feeding box (2) are located at grinder (4)
Above, described material feeding box (2) be provided with charging aperture (1), is provided with Disintegrating knife (3) in grinder (4),
It is connected by discharge valve (5) between grinder (4) and reaction vessel (6), the reaction vessel
(6) heater (8) and pressue device are provided with, and discharging supply pipe (10) are connected to reaction vessel
(6) and stove (12) between, described first cooler (9) are located at the outlet of reaction vessel (6)
Place, cracking case (11) are located at stove (12) above, and the side wall of stove (12) also sets
There is discharge nozzle (14), described second cooler (13) are on discharge nozzle (14).
2. rice straw charcoal production equipment according to claim 1, it is characterised in that described anti-
Answer and on container (6), be additionally provided with pressure gauge (7).
3. rice straw charcoal production equipment according to claim 1, it is characterised in that described split
Solution case (11) side wall is provided with argon inlet mouth.
4. rice straw charcoal production equipment according to claim 1, it is characterised in that described go out
Material conveying tube (10) is provided with tail gates (15) near reaction vessel (6) one end, and the other end is provided with upper lock gate
(16), inlet amount inspection is provided with the discharging supply pipe (10) at upper lock gate (16) position
Sensor (17) is surveyed, charging quantity detection sensor (17) is used for detecting the charging of cracking case (11)
Amount, is connected with the tail gates (15), upper lock gate (16) and charging quantity detection sensor (17) and is provided with
MCU (18), is connected with the MCU (18) and is provided with display screen (20), and MCU (18) prestore
Cracking case (11) inlet amount preset data, MCU (18) are adopted according to charging quantity detection sensor (17)
Inlet amount Data Control tail gates (15) of collection and the opening and closing of upper lock gate (16).
5. rice straw charcoal production equipment according to claim 4, it is characterised in that described anti-
The exit of container (6) is answered to be additionally provided with temperature-detecting device (19), for detecting in reaction vessel (6)
Reaction temperature, temperature-detecting device (19) are connected with the MCU (18) and heater (8).
6. rice straw charcoal production equipment according to claim 1, it is characterised in that described split
Temp measuring system is additionally provided with solution case (11), the temp measuring system includes thermo detector and temperature probe, the survey
The thermometer hole that temperature is popped one's head in through cracking case (11) is deep in cracking case (11), and temperature probe is outside and surveys
Temperature meter connection.
7. rice straw charcoal production equipment according to claim 1, it is characterised in that described split
Solution case (11) bottom is additionally provided with tar catalyst chamber (21), is provided with tar and urges in tar catalyst chamber (21)
Agent.
8. rice straw charcoal production equipment according to claim 1, it is characterised in that the fire
Stove (12) exit is additionally provided with tar separator (23), is connected with the tar separator (23) and is provided with
Coke tar cracking room (22), is connected with coke tar cracking room (22) and is provided with tar exhausting waste gas pipeline.
9. a kind of technique for producing charcoal, it is characterised in that comprise the following steps,
1) water intaking rice straw is put in material feeding box (2) through charging aperture (1), enters back into grinder (4), if
Put rotating speed to be crushed for 300~500r/min, after the completion of crushing, by the rice straw after crushing through discharging
Be introduced in reaction vessel (6) and reacted, obtain fused mass, in control reaction vessel (6) pressure be 0.6~
0.8Mpa, temperature are 160~180 DEG C, react 1~2h;
2) fused mass for obtaining is cooled to after room temperature through the first cooler (9), by discharging supply pipe (10)
Be transported in cracking case (11), Pintsch process is carried out at 1000~1200 DEG C, while be passed through argon gas carrying out
Protection, cracks 3~5h;
3) after the completion of waiting to crack, it is transported in stove (12), control temperature is 600~800 DEG C, carries out charcoal
Change 1~2h, 23~25 DEG C are cooled to through the second cooler (13), discharged by discharge nozzle (14), obtain final product
To rice straw charcoal.
10. the technique for producing charcoal according to claim 9, it is characterised in that the use
Comprise the following steps in the technique of production charcoal,
1) water intaking rice straw is put in material feeding box (2) through charging aperture (1), enters back into grinder (4), if
Put rotating speed to be crushed for 400r/min, after the completion of crushing, the rice straw after crushing is introduced through discharging anti-
Answer in container (6), in control reaction vessel (6), pressure is 0.7Mpa, temperature is 170 DEG C, reacts 1.5h;
2) fused mass for obtaining is cooled to after room temperature through the first cooler (9), by discharging supply pipe (10)
It is transported in cracking case (11), at 1100 DEG C, Pintsch process is carried out, while be passed through argon gas protected,
Cracking 4h;
3) after the completion of waiting to crack, it is transported in stove (12), control temperature is 700 DEG C, carries out charing 1.5h,
24 DEG C are cooled to through the second cooler (13), are discharged by discharge nozzle (14), that is, obtain rice straw biological
Charcoal.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610203771.XA CN106479536B (en) | 2016-04-01 | 2016-04-01 | Rice straw charcoal production equipment and technique for producing charcoal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610203771.XA CN106479536B (en) | 2016-04-01 | 2016-04-01 | Rice straw charcoal production equipment and technique for producing charcoal |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106479536A true CN106479536A (en) | 2017-03-08 |
CN106479536B CN106479536B (en) | 2019-06-07 |
Family
ID=58238353
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610203771.XA Active CN106479536B (en) | 2016-04-01 | 2016-04-01 | Rice straw charcoal production equipment and technique for producing charcoal |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106479536B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110182782A (en) * | 2019-06-04 | 2019-08-30 | 兰州大学 | A kind of environment-friendly type device preparing straw biological charcoal using hydro-thermal method |
CN113265264A (en) * | 2021-06-15 | 2021-08-17 | 河南省万禾企生物科技有限公司 | Method for preparing straw biochar through low-temperature efficient carbonization |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101486919A (en) * | 2009-02-17 | 2009-07-22 | 北京海润川投资咨询有限公司 | Sectional temperature-controlled fluidized bed type biomass rapid pyrolysis reactor |
CN101519597A (en) * | 2009-03-31 | 2009-09-02 | 王尹平 | Production process for comprehensively utilizing eupatorium adenophorum |
EP2130893A2 (en) * | 2008-06-05 | 2009-12-09 | TerraNova Energy GmbH & Co. KG | Method for producing coal, in particular coal slurry |
CN103173231A (en) * | 2012-06-13 | 2013-06-26 | 罗金 | Double-carbonization type high-temperature carbon firing method |
CN103627415A (en) * | 2012-08-21 | 2014-03-12 | 上海中科岸达节能产品科技有限公司 | Biomass pyrolysis carbonization system equipment |
CN104017590A (en) * | 2014-06-24 | 2014-09-03 | 华南农业大学 | Continuous pyrolysis carbonization method of agricultural and forestal biomasses |
JP5843952B1 (en) * | 2014-12-19 | 2016-01-13 | 株式会社大和三光製作所 | Method and apparatus for semi-carbonizing dried product |
-
2016
- 2016-04-01 CN CN201610203771.XA patent/CN106479536B/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2130893A2 (en) * | 2008-06-05 | 2009-12-09 | TerraNova Energy GmbH & Co. KG | Method for producing coal, in particular coal slurry |
CN101486919A (en) * | 2009-02-17 | 2009-07-22 | 北京海润川投资咨询有限公司 | Sectional temperature-controlled fluidized bed type biomass rapid pyrolysis reactor |
CN101519597A (en) * | 2009-03-31 | 2009-09-02 | 王尹平 | Production process for comprehensively utilizing eupatorium adenophorum |
CN103173231A (en) * | 2012-06-13 | 2013-06-26 | 罗金 | Double-carbonization type high-temperature carbon firing method |
CN103627415A (en) * | 2012-08-21 | 2014-03-12 | 上海中科岸达节能产品科技有限公司 | Biomass pyrolysis carbonization system equipment |
CN104017590A (en) * | 2014-06-24 | 2014-09-03 | 华南农业大学 | Continuous pyrolysis carbonization method of agricultural and forestal biomasses |
JP5843952B1 (en) * | 2014-12-19 | 2016-01-13 | 株式会社大和三光製作所 | Method and apparatus for semi-carbonizing dried product |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110182782A (en) * | 2019-06-04 | 2019-08-30 | 兰州大学 | A kind of environment-friendly type device preparing straw biological charcoal using hydro-thermal method |
CN110182782B (en) * | 2019-06-04 | 2020-04-17 | 兰州大学 | Environment-friendly device for preparing straw biochar by hydrothermal method |
CN113265264A (en) * | 2021-06-15 | 2021-08-17 | 河南省万禾企生物科技有限公司 | Method for preparing straw biochar through low-temperature efficient carbonization |
Also Published As
Publication number | Publication date |
---|---|
CN106479536B (en) | 2019-06-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202030706U (en) | Biomass pyrolyzing furnace | |
CN102583313A (en) | Rural household garbage carbonization method, prepared products using same, and application | |
CN106479536A (en) | Rice straw charcoal production equipment and the technique for producing charcoal | |
Kisiki Nsamba et al. | Designing and performance evaluation of biochar production in a top-lit updraft upscaled gasifier | |
CN104789236A (en) | Internal-combustion type biomass particle material drying, carbonizing and activating integrated furnace | |
CN106040700B (en) | The biological dewatered method of house refuse | |
CN102863975B (en) | Device and method for carbonizing straw | |
CN206157094U (en) | Offal pyrolysis gasification, living beings charcoal preparation system | |
CN104680003A (en) | Prediction method for hydrothermal coke yield | |
CN106824979A (en) | A kind of cooperative disposal method of Cr VI slag and biomass castoff | |
CN201096364Y (en) | Multilevel oxygen feeding type multifunctional biomass dry distillation rapid coke oven | |
CN102786968A (en) | Method for producing machine-made charcoal from Yunnan pipe cone | |
CN206902152U (en) | New rural village biogas feeding mechanism | |
CN202865166U (en) | Dry distillation carbonization furnace with flue pipes | |
CN204661711U (en) | Stalk produces biogas facility | |
CN106834091A (en) | A kind of biomass marsh gas installation for fermenting and preparation method | |
CN104673339B (en) | A kind of device that agricultural crop straw is carried out smokeless carbonization process | |
CN103788974B (en) | Continuous charcoal production equipment and method | |
CN202808711U (en) | Straw carbonizing device | |
CN207362140U (en) | A kind of continuous carbonization device | |
CN202337759U (en) | Biomass gas/biomass carbon preparation system | |
CN206051939U (en) | A kind of biomass regenerate extraction element | |
CN203700275U (en) | Continuous biochar production equipment | |
CN110240966A (en) | A kind of preparation method of agriculture and forestry organic waste material low temperature pyrogenation high heating value granular fuel and a kind of high heating value granular fuel | |
CN203498332U (en) | Rice hull recycling device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |