CN109609204A - Device and method for improving organic matter combustion efficiency - Google Patents
Device and method for improving organic matter combustion efficiency Download PDFInfo
- Publication number
- CN109609204A CN109609204A CN201811369433.9A CN201811369433A CN109609204A CN 109609204 A CN109609204 A CN 109609204A CN 201811369433 A CN201811369433 A CN 201811369433A CN 109609204 A CN109609204 A CN 109609204A
- Authority
- CN
- China
- Prior art keywords
- permanent magnet
- storage tank
- oil storage
- combustion efficiency
- organic matter
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- 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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Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/40—Applying a magnetic field or inclusion of magnets in the apparatus
Abstract
The invention belongs to the technical field of combustion of organic matters such as petroleum and natural gas, and discloses a device and a method for improving the combustion efficiency of the organic matters, which aim to solve the problem of low combustion efficiency of the organic matters in the prior art. The invention can make the magnetic domains of the organic matters consistent through the horizontal, improves the contact area with oxygen and greatly promotes the efficiency of magnetizing the organic matters. The magnetic organic matter is utilized to improve the combustion efficiency, and meanwhile, the secondary pollution is avoided, the improvement of the combustion efficiency of the organic matter is facilitated, and the working procedures are reduced.
Description
Technical field
The present invention relates to the field of combustion technology of the organic matters such as petroleum gas, and in particular to a kind of raising organic compound combustion
The device and method of efficiency.
Background technique
In today of productivity high development, the mankind are increasing to the demand of the energy, and tellurian energy day
Benefit is reduced, and therefore, the utilization efficiency for how improving the energy just becomes people and faces and urgent problem to be solved.Under natural conditions,
With oxygen insufficient contact when organic compound combustion, the efficiency of combustion of organic matter is significantly reduced, the prior art can not solve
State technical problem.
Summary of the invention
The problem of the purpose of the present invention is to solve organic compound combustion low efficiencys in the prior art, provides a kind of burning
Process is less and not will cause the device that secondary pollution improves organic compound combustion efficiency.
In order to achieve the above object, the invention adopts the following technical scheme:
A kind of device improving organic compound combustion efficiency, including oil storage tank, the outlet of oil storage tank are connected with transfer pipeline, delivery pipe
Road is successively arranged circulating pump, the first permanent magnet, the second permanent magnet, control valve and flowmeter along the direction of liquid flowing, and
The outlet of flowmeter and the import of oil storage tank connect, and the magnetic induction line direction of the first permanent magnet is hung down with liquid flow direction vertically downward
Directly, the magnetic induction line direction of the second permanent magnet is identical as liquid flow direction.
Another object of the present invention is to provide a kind of combustion to solve the problems, such as organic compound combustion low efficiency in technology
Burn the method that process is less and not will cause the raising organic compound combustion efficiency of secondary pollution.
A method of organic compound combustion efficiency is improved, is included the following steps；
1) control valve is opened, organic matter is filled it up with into oil storage tank later, covering oil storage tank makes system be in air-tight state, Zhi Houkai
Circulating pump is opened, the speed of recycle oil is adjusted to 0.2 m/s-0.5m/s using control valve, environment temperature is controlled at 25 DEG C -30 DEG C,
The magnetic field strength B of first permanent magnet is 2.5T-3T, and the magnetic field strength B of the second permanent magnet is 2.2T-2.5T；
2) circulatory system entire after the completion to be debugged starts the cycle over operation, runing time t1, and t1=V1/ Sv, wherein V1For storage
Oil tank volume, S are pipeline section product, and v is oil speed；
3) runing time is t1Afterwards, organic matter is thoroughly magnetized, and the burning sample of 1g is taken from organic matter, is measured using calorimetric meter
The changing value of calorimeter temperature before and after organic compound combustion sample combustion, and calculate the combustion heat of burning sample.
Further, liquid first passes around the first permanent magnet, then using the second permanent magnet.
Further, the first permanent magnet and the second permanent magnet are all made of horizontal form and are directly installed on circulatory system tube wall
On.
The present invention compared with the existing technology, have the utility model has the advantages that
The present invention equipped with oil storage tank transfer pipeline on along liquid flowing direction be successively arranged circulating pump, the first permanent magnet,
Second permanent magnet, control valve and flowmeter, and the outlet of flowmeter and the import of oil storage tank connect.This method is using first forever
Magnet, magnetic field strength B is 2.5T-3T, so that the viscosity of organic matter reduces, fogging degree is improved, and is then passing through the second permanent magnetism
Body, magnetic field strength B are 2.2T-2.5T, and organic matter magnetic domain direction becomes in good order after magnetization, is sufficiently recycled
Magnetization, the combustion heat of organic matter further increase.The present invention utilizes the first permanent magnet, takes full advantage of the Lip river logical sequence magnetic of vertical magnetic field
The activation of power, greatly reduces viscosity, the magnetic domain of organic matter can be made consistent by horizontal magnetic field, improved and oxygen
Contact area has been greatly facilitated the efficiency of magnetization organic matter.The present invention is while improving efficiency of combustion using magnetization organic matter
It not will cause secondary pollution.The present invention provides convenience to organic compound combustion efficiency is improved, and reduces process.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the circulatory system of the invention.
Appended drawing reference meaning is as follows: 1. oil storage tanks；2. circulating pump；3. the first permanent magnet；4. the second permanent magnet；5.
Control valve, 6. flowmeters.
Specific embodiment
The present invention will be further explained below with reference to the attached drawings and specific examples.
As shown in Figure 1, a kind of device for improving organic compound combustion efficiency, including oil storage tank 1, the outlet connection of oil storage tank 1
Have a transfer pipeline, on transfer pipeline along the direction of liquid flowing be successively arranged circulating pump 2, the first permanent magnet 3, the second permanent magnet 4,
Control valve 5 and flowmeter 6, and the outlet of flowmeter 6 is connect with the import of oil storage tank 1.First permanent magnet 3, the second permanent magnet 4
It is the adjustable permanent magnet in magnetic field, the magnetic field adjustable extent of the first permanent magnet 3 is 2.5T-3T, and the magnetic field of the second permanent magnet 4 is adjustable
Range is 2.2T-2.5T.
A method of organic compound combustion efficiency is improved, is included the following steps；
1) control valve 5 is opened, organic matter is filled it up with into oil storage tank 1 later, covering oil storage tank 1 makes system be in air-tight state, it
Open circulating pump 2 afterwards, the speed of recycle oil be adjusted to 0.2 m/s-0.5m/s using control valve 5, environment temperature control 25 DEG C-
30 DEG C, the magnetic field strength B of the first permanent magnet 3 is 2.5T-3T, and the magnetic field strength B of the second permanent magnet 4 is 2.2T-2.5T, and first
The magnetic induction line direction of permanent magnet 3 is vertical with liquid flow direction vertically downward, the magnetic induction line direction of the second permanent magnet 4 and liquid flow
Dynamic direction is identical.
2) circulatory system entire after the completion to be debugged starts the cycle over operation, runing time t1, t1=V1/ Sv, wherein V1For
Oil storage tank volume, S are pipeline section product, and v is oil speed.
3) runing time is t1Afterwards, organic matter is thoroughly magnetized, and the burning sample of 1g is taken from organic matter, utilizes calorimeter
The changing value of organic compound combustion sample combustion front and back calorimeter temperature is measured, and calculates the combustion heat of burning sample.
Embodiment 1
1) control valve 5 is opened, benzoic acid is filled it up with into oil storage tank 1 later, covering oil storage tank 1 makes system be in air-tight state, it
Circulating pump 2 is opened afterwards, speed is adjusted to 0.2 m/s using control valve 5, and environment temperature control is at 25 DEG C, the magnetic of the first permanent magnet 3
Field intensity B is 2.5T, and the magnetic field strength B of the second permanent magnet 4 is 2.2T.The magnetic induction line direction of first permanent magnet 3 vertically downward with
Liquid flow direction is vertical, and the magnetic induction line direction of the second permanent magnet 4 is identical as liquid flow direction, and liquid first passes around first forever
Magnet 3, then using the second permanent magnet 4.First permanent magnet 3 and the second permanent magnet 4 are all made of horizontal form and directly clamp
On circulatory system tube wall.
2) circulatory system entire after the completion to be debugged starts the cycle over operation, runing time t1, t1=V1/ Sv, wherein V1For
Oil storage tank volume, S are pipeline section product, and v is oil speed, to guarantee that organic matter is thoroughly magnetized.Take V1For 4m3, pipeline section product S
For 0.1m2, flow velocity v is 0.2m/s, then the time t of entire circulatory system operation1For 200s.
3) after the 200s run, benzoic acid is thoroughly magnetized, and takes the amount of 1g as burning sample, has using the measurement of calorimetric meter
The changing value of machine object burning sample burning front and back calorimeter temperature, and calculate the combustion heat of burning sample.Sample is calculated as follows
The constant volume combustion heat of product.
-m1Qv1-m2Qv2=C△T
In formula: m1The quality of -1g benzoic acid burning sample.
QvlThe constant volume combustion heat of-every gram benzoic acid burning, unit: J/g；
m2- spent igniting yarn quality 0.0026g；
Qv2The constant volume combustion heat-the 3242.6J/g of-every gram nickel wire；
The thermal capacitance 14514.5J/K of C-calorimeter (including inner cylinder water)；
The changing value of calorimeter system temperature 1.96K before and after △ T-benzoic acid sample combustion.
Combustion heat Q is obtained by the temperature gap of measurement benzoic acid burning front and backvFor -2.84KJ/g.
Embodiment 2
1) control valve 5 is opened, benzoic acid is filled it up with into oil storage tank 1 later, covering oil storage tank 1 makes system be in air-tight state, it
Circulating pump 2 is opened afterwards, the speed of recycle oil is adjusted to 0.25m/s using control valve 5, environment temperature is controlled at 28 DEG C, and first forever
The magnetic field strength B of magnet 3 is 2.7T, and the magnetic field strength B of the second permanent magnet 4 is 2.4T.It hangs down in the magnetic induction line direction of first permanent magnet 3
Straight vertical with liquid flow direction downwards, the magnetic induction line direction of the second permanent magnet 4 is identical as liquid flow direction, and liquid passes through first
The first permanent magnet 3 is crossed, then using the second permanent magnet 4.First permanent magnet 3 and the second permanent magnet 4 are all made of horizontal form
Directly it is installed on circulatory system tube wall.
2) circulatory system entire after the completion to be debugged starts the cycle over operation, runing time t1, t1=V1/ Sv, wherein V1For
Oil storage tank volume, S are pipeline section product, and v is oil speed, to guarantee that benzoic acid is thoroughly magnetized.Take V1For 4m3, pipeline section product S
For 0.1m2, flow velocity v is 0.25m/s, then the time t of entire circulatory system operation1For 160s.
3) benzoic acid is thoroughly magnetized after running 160s, is taken the amount of 1g as burning sample, is measured using calorimetric meter organic
The changing value of object burning sample burning front and back calorimeter temperature, and calculate the combustion heat of burning sample.Sample is calculated as follows
The constant volume combustion heat.
The constant volume combustion heat of sample is calculated as follows.
-m1Qv1-m2Qv2=C△T
In formula: m1The quality of -1g benzoic acid burning sample.
QvlThe constant volume combustion heat of-every gram benzoic acid burning, unit: J/g；
m2- spent igniting yarn quality 0.0026g；
Qv2The constant volume combustion heat-the 3242.6J/g of-every gram nickel wire；
The thermal capacitance 14514.5J/K of C-calorimeter (including inner cylinder water)；
The changing value of calorimeter system temperature 2.46K before and after △ T-benzoic acid sample combustion.
Combustion heat Q is obtained by the temperature gap of measurement benzoic acid burning front and backvFor -3.56 KJ//g.
Embodiment 3
1) control valve 5 is opened, benzoic acid is filled it up with into oil storage tank 1 later, covering oil storage tank 1 makes system be in air-tight state, it
Circulating pump 2 is opened afterwards, the speed of recycle oil is adjusted to 0.5m/s using control valve 5, and environment temperature control is at 30 DEG C, the first permanent magnetism
The magnetic field strength B of body 3 is 3T, and the magnetic field strength B of the second permanent magnet 4 is 2.5T.The magnetic induction line direction of first permanent magnet 3 vertically to
Lower vertical with liquid flow direction, the magnetic induction line direction of the second permanent magnet 4 is identical as liquid flow direction, and liquid first passes around the
One permanent magnet 3, then using the second permanent magnet 4.It is direct that first permanent magnet 3 and the second permanent magnet 4 are all made of horizontal form
It is installed on circulatory system tube wall.
2) circulatory system entire after the completion to be debugged starts the cycle over operation, runing time t1, t1=V1/ Sv, wherein V1For
Oil storage tank volume, S are pipeline section product, and v is oil speed, to guarantee that benzoic acid is thoroughly magnetized.Take V1For 4m3, pipeline section product S
For 0.1m2, flow velocity v is 0.5m/s, then the time t of entire circulatory system operation1For 80s.
3) after running 80 s, benzoic acid is thoroughly magnetized, and is taken the amount of 1g as burning sample, is measured using calorimetric meter organic
The changing value of object burning sample burning front and back calorimeter temperature, and calculate the combustion heat of burning sample.Sample is calculated as follows
The constant volume combustion heat.
The constant volume combustion heat of sample is calculated as follows.
-m1Qv1-m2Qv2=C△T
In formula: m1The quality of -1g benzoic acid burning sample.
QvlThe constant volume combustion heat of-every gram benzoic acid burning, unit: J/g；
m2- spent igniting yarn quality 0.0026g；
Qv2The constant volume combustion heat-the 3242.6J/g of-every gram nickel wire；
The thermal capacitance 14514.5J/K of C-calorimeter (including inner cylinder water)；
The changing value of calorimeter system temperature 2.84K before and after △ T-benzoic acid sample combustion.
Combustion heat Q is obtained by the temperature gap of measurement benzoic acid burning front and backvFor -4.12KJ/g.
Embodiment 4
1) control valve 5 is opened, benzoic acid is filled it up with into oil storage tank 1 later, covering oil storage tank 1 makes system be in air-tight state, it
Circulating pump 2 is opened afterwards, speed is adjusted to 0.2 m/s using control valve 5, and environment temperature control is at 25 DEG C, the magnetic of the first permanent magnet 3
Field intensity B is 0T, and the magnetic field strength B of the second permanent magnet 4 is 0T.
2) circulatory system entire after the completion to be debugged starts the cycle over operation, runing time t1, t1=V1/ Sv, wherein V1For
Oil storage tank volume, S are pipeline section product, and v is oil speed.Take V1For 4m3, pipeline section product S is 0.1m2, flow velocity v is 0.2m/s, then
The time t of entire circulatory system operation1For 200s.
3) after the 200s run, benzoic acid is thoroughly magnetized, and takes the amount of 1g as burning sample, has using the measurement of calorimetric meter
The changing value of machine object burning sample burning front and back calorimeter temperature, and calculate the combustion heat of burning sample.
The constant volume combustion heat of sample is calculated as follows.
-m1Qv1-m2Qv2=C△T
In formula: m1The quality of -1g benzoic acid burning sample.
QvlThe constant volume combustion heat of-every gram benzoic acid burning, unit: J/g；
m2- spent igniting yarn quality 0.0026g；
Qv2The constant volume combustion heat-the 3242.6J/g of-every gram nickel wire；
The thermal capacitance 14514.5J/K of C-calorimeter (including inner cylinder water)；
The changing value of calorimeter system temperature 1.45K before and after △ T-benzoic acid sample combustion.
Combustion heat Q is obtained by the temperature gap of measurement benzoic acid burning front and backvFor -2.1KJ/g.
Claims (4)
1. a kind of device for improving organic compound combustion efficiency, including oil storage tank (1), the outlet of oil storage tank (1) are connected with delivery pipe
Road, it is characterized in that: the direction on transfer pipeline along liquid flowing is successively arranged circulating pump (2), the first permanent magnet (3), second forever
Magnet (4), control valve (5) and flowmeter (6), and the outlet of flowmeter (6) is connect with the import of oil storage tank (1), first forever
The magnetic induction line direction of magnet (3) is vertical with liquid flow direction vertically downward, the magnetic induction line direction of the second permanent magnet (4) and liquid
Flow direction is identical.
2. a kind of method for improving organic compound combustion efficiency using device described in claim 1, characterized in that including following step
It is rapid:
1) control valve (5) are opened, organic matter is filled it up with into oil storage tank (1) later, covering oil storage tank (1) makes system be in sealed shape
State opens circulating pump (2) later, the speed of recycle oil is adjusted to 0.2 m/s-0.5m/s, environment temperature control using control valve (5)
System is at 25 DEG C -30 DEG C, and the magnetic field strength B of the first permanent magnet (3) is 2.5T-3T, and the magnetic field strength B of the second permanent magnet (4) is
2.2T-2.5T；
2) circulatory system entire after the completion to be debugged starts the cycle over operation, runing time t1, and t1=V1/ Sv, wherein V1For oil storage
Tank volume, S are pipeline section product, and v is oil speed；
3) after runing time reaches, organic matter is thoroughly magnetized, later combustion of organic matter.
3. a kind of method for improving organic compound combustion efficiency according to claim 1, it is characterized in that: the liquid passes through first
The first permanent magnet (3) are crossed, then using the second permanent magnet (4).
4. a kind of method for improving organic compound combustion efficiency according to claim 1, it is characterized in that: first permanent magnet
(3) and the second permanent magnet (4) is all made of horizontal form and is directly installed on circulatory system tube wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811369433.9A CN109609204B (en) | 2018-11-16 | 2018-11-16 | Device and method for improving organic matter combustion efficiency |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811369433.9A CN109609204B (en) | 2018-11-16 | 2018-11-16 | Device and method for improving organic matter combustion efficiency |
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| CN109609204A true CN109609204A (en) | 2019-04-12 |
| CN109609204B CN109609204B (en) | 2021-07-13 |
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ID=66004694
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