CN1181719A - Method of conditioning hydrocarbon liquids and an appts. for carrying out the method - Google Patents
Method of conditioning hydrocarbon liquids and an appts. for carrying out the method Download PDFInfo
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- CN1181719A CN1181719A CN 95197821 CN95197821A CN1181719A CN 1181719 A CN1181719 A CN 1181719A CN 95197821 CN95197821 CN 95197821 CN 95197821 A CN95197821 A CN 95197821A CN 1181719 A CN1181719 A CN 1181719A
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- running wheel
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Abstract
Disclosed are a method an appts. for conditioning hydrocarbon liquids by applying mechanical vibrations before fractionation. The method involves introducing the liquid into a cavity in a rotating wheel, expelling the liquid into an annular chamber formed by the wheel and the stator via a series of outlet apertures, and removing the liquid. For this process the following empirical proportions are prefered : R=1.1614 k/mm; 'DE1TA'R=1.1614 B/mm; and n=3.8396 K -1.5 X106 revs/min, R being the radius of the peripheral cylindrical surface of the wheel, 'DE1TA'R being the radial dimension of the annular chamber, n being the rotation frequency of the wheel, K the number of outlet apertures in the wheel, B an integer in the range 1-K/5.
Description
Background of invention
Handle (in this article the early stage that the present invention relates to hydrocarbon fluid, " processing " speech relates to the implication that makes raw material have the needed physical characteristic of post-processed), particularly a kind of method and apparatus of before hydrocarbon fluid is by fractionation, hydrocarbon fluid being handled by means of mechanism.
In the known technology field, before fractionation, generally hydrocarbon fluid is carried out preliminary treatment by mechanism, particularly remove unwanted field trash by the method for filtering.This filtration treatment greatly facilitates follow-up fractionation operation, can not produce any influence to hydrocarbon raw material or half-finished physical characteristic simultaneously, also can the output of middle or limited fractionation not exerted an influence.
The also known a kind of method with the mechanical oscillation treat liquid of prior art (international patent application no: PCT/RU92/00194,1992) comprises " wanting processed fluid to be provided in the space of running wheel of rotation; Make fluid by being arranged on a series of outlet perforates on the running wheel periphery cylinderical surface, discharge from the space of running wheel; Make fluid pass through at least one inlet drilling and flow into stator space, inlet drilling is set at adjacent with the periphery cylinderical surface of the wheel that turns round and has with it in the stator coaxial surface in minimum gap; Thus, realized periodic, discontinuous interference, and in sound wave or hyperacoustic scope, in fluid stream, excited mechanical oscillation the fluid stream of the outlet perforate of flowing through running wheel.
Embody the device of above-mentioned processing fluid method, comprise the rotor that an axle that rotates is housed in bearing; A running wheel that is connected with axle, it is made into a disk with peripheral annular wall, and this annular wall has columnar inside and outside surface, is provided with a series of perforates that fluid passes through that are used for therein, and these perforates equidistantly distribute along circumference; A stator that is holding the running wheel, said stator has the input perforate and the discharge orifice that is used to discharge fluid that are used to provide fluid, said stator also has two coaxial wall, and the peripheral annular wall of their contiguous running wheels leaves minimum gap in its both sides; All be provided with a perforate as the fluid passage in two coaxial wall of stator at least, these tappings are in the plane, place of a series of perforates of running wheel.
Said apparatus is when handle hydrocarbon fluid, and the meeting convection cell has heat effect to a certain degree, in addition, can not influence other physical characteristics of fluid, also can not produce any influence to the centre or the final products of follow-up fractionation.
Brief introduction of the present invention
The objective of the invention is to, on the basis of prior art and oneself research, solve the problem that produces, a kind of method of before follow-up fractionating step hydrocarbon fluid being handled is proposed, and the device that embodies this method, this method and apparatus can improve the output of lightweight fractionation product to the influence that physical characteristic produced of hydrocarbon fluid.
According to the present invention, handle fluid by means of mechanism problem is solved, wherein,, be accompanied by to have and determine the overlapping of frequency oscillation action along the rotary movement that a definite radius of turn has definite linear velocity.
For this purpose, in the basic embodiment of the method for this processing fluid, be arranged to: in the space of the running wheel of wanting processed fluid to be provided to rotate; Make the fluid of wanting processed from the space of running wheel, discharge and enter in the annular chamber, this annular chamber is to be formed by the periphery cylinderical surface of running wheel and the coaxial surface of stator, and the discharge of fluid from running wheel space is to realize by a series of outlet perforates that are arranged on the running wheel periphery cylinderical surface.These outlet perforates equidistantly distribute along circumference; Fluid is discharged from annular chamber by at least one discharge orifice.In the case, the radius R of running wheel periphery cylinderical surface and the speed n of running wheel are in following empirical equation scope, are determined by the outlet perforate number K of selected running wheel:
R=(1.05 ... 1.28) K (millimeter), and
N=(3.6 ... 4.1) K
-1.5.10
6(revolution/per minute)
By experiment confirm, surpass said parameter area as, may obtain making the inadequate effect of processing of fluid, this shows that the selection of parameter is unsuitable.
In the most preferred embodiment of the method for handling fluid, the radius R and the speed n of running wheel are according to following empirical equation, give clearly determining by selecting outlet perforate number K:
R=1.1614K (millimeter), and
N=3.8396K
-1.5.10
6(revolution/per minute)
In another preferred embodiment of the method for handling fluid, want processed fluid from annular chamber, to discharge to be discharge orifice to realize by on the coaxial surface that is arranged on stator, this annular chamber is to be formed by the periphery cylinderical surface of running wheel and the coaxial surface of stator, and these discharge orifices are arranged in running wheel rotary course in turn mutually opposed with the outlet perforate of running wheel.
In the basic embodiment of above-mentioned processing fluid, in said parameter range of choice, as experiment is certified, the influence of convection cell physical characteristic, the output of the low boiling fraction of most worthy in follow-up fractional distillation process is greatly improved, that is to say that the method for this processing fluid can be used for actual purpose quite effectively.This effect can realize by the destructive change of the mutual bonding of convection cell on molecular level, and this change is to excite mechanism to be enough to critical frequency and to act on the fluid and to produce the result of harmonic wave in fluid.In the most preferred embodiment of the method for handling fluid, when the clearly value (these parameter values are determined by experiment) of said parameter is chosen, the effects of pretreatment before the fractionation that hydrocarbon fluid is carried out show fullest.In another preferred embodiment of the method for handling fluid, when being discharged in the annular chamber owing to the outlet perforate of taking turns by running when fluid, and when fluid is discharged from annular chamber by being arranged on the discharge orifice on the stator coaxial surface, all there is a comprehensive oscillation action to be applied on the fluid, thereby makes the resulting effect of improvement become possibility.
According to the present invention, the method for handle hydrocarbon fluid only can be implemented by means of the device that hereinafter will set forth, and this constitutes the general purpose intact part that the present invention goes into, and does not really want to be used for other purpose.
Basic embodiment at the device that is used for handling fluid comprises a rotor, and it is adorning an axle that can rotate in bearing; The running wheel that at least one is connected with axle, it is made into the disk that has the peripheral annular wall as same, and annular wall has a columnar outer surface, in this annular wall, along circumference a series of outlet perforates that are used for fluid is set equidistantly; A stator that contains work running wheel, it has the input perforate and the discharge orifice that is used for exhaust fluid that are used to provide fluid; A space that is used to hold the fluid of wanting processed, said space are the peripheral annular walls by this disk and running wheel, and have the input perforate and the stator wall adjacent with the running wheel forms; An annular chamber that is used to hold the fluid of wanting processed, said annular chamber are limited by the peripheral annular wall of running wheel and the coaxial wall of stator diametrically, and are communicated with the discharge orifice that is used for the fluid outflow; The geomery feature of this running wheel and annular chamber is:
R=(1.05 ... 1.28) K (millimeter), herein
K is selected running wheel outlet perforate number,
R is the radius of the outer cylindrical surface of running wheel peripheral annular wall, and
Δ R=(1.05 ... 1.28) B (millimeter) herein
B is 1 ... selected integer in the K/2 scope,
Δ R is the radial dimension of annular chamber,
At the most preferred embodiment of the device that is used for handling fluid, the size of radius R and Δ R is respectively:
R=1.1614K (millimeter),
Δ R=1.1614B (millimeter), herein
B is 1 ... the integer of selecting in the K/5 scope.
In another preferred embodiment of the device that is used for handling fluid, a stator has the space of its coaxial wall of vicinity, and in order to fluid is imported this space from annular chamber, this space is communicated with the discharge orifice that is used for exhaust fluid; The space of this stator is communicated with annular chamber by the discharge orifice that some are arranged in the stator coaxial surface, and these discharge orifices are arranged in the plane, place of running delivery outlet perforate, and equidistantly distributes along circumference; The number of the discharge orifice of annular chamber is 1 ... K.
Can recognize further feature of the present invention from following to the elaborating of the embodiment of the invention.
The accompanying drawing summary
With reference to the embodiment shown in the following schematic diagram, for a more detailed description to the present invention:
Fig. 1 is the Y sectional drawing of the fundamental sum most preferred embodiment of the present invention's device of being used to handle fluid;
Fig. 2 and Fig. 4 are the schematic partial cross sectionals of annular chamber;
Fig. 3 is the Y sectional drawing of one of preferred embodiment that is used to handle the device of fluid.
The present invention describes in detail
According to the basic embodiment (Fig. 1,2) that handles the method for fluid with mechanism, by inlet drilling 3 wanting processed fluid to be provided in the space 1 of running wheel 2 of rotation.In the rotary course of running wheel 2, want processed fluid to be drained into the annular chamber 4 from space 1 by a series of outlet perforates 8, this annular chamber 4 is to be formed by the periphery cylinderical surface 5 of running wheel 2 and the coaxial surface 6 of stator 7, and a series of outlet perforates 8 are to take turns 2 periphery drum surface 5 and along the equidistant setting of circumference along running.Be limited in the processed fluid of wanting in the annular chamber 4, with respect to central shaft 9, when continuing to rotate, be subjected to the effect of mechanical oscillation according to the free fluid rule at it.The vibration of this mechanism is owing to the interaction between the coaxial surface 6 of unit fluid stream that flows out from each outlet perforate 8 of running wheel 2 and stator 7 produces.The fluid of handling is discharged from annular chamber 4 by discharge orifice 10.
The speed n of running wheel 2 and the radius R of its periphery cylinderical surface 5 are in the scope of following empirical equation, the number K of the outlet perforate 8 by selected running wheel 2 and definite:
R=(1.05 ... 1.28) K (millimeter),
N=(3.6 ... 4.1) K
-1.5.10
6(revolution/per minute).
According to the most preferred embodiment of the method for handling fluid, the speed n of radius R and running wheel 2 can be according to following empirical equation, the number K of the outlet perforate 8 by selected running wheel 2 and being determined clearly:
R=1.1614K (millimeter),
N=3.8396K
-1.5.10
6(revolution/per minute).
Another preferred embodiment (Fig. 3-4) according to the method for handling fluid, want the processed discharge of fluid from annular chamber 4, be that by forming on the coaxial surface 6 of stator 7 one, several or a series of discharge orifice 11 realize, annular chamber 4 is to take turns 2 periphery cylinderical surface 5 and the coaxial surface 6 of stator 7 forms by running.During the rotation of running wheel 2, the said discharge orifice 11 of annular chamber 4 is set to mutually opposed with the corresponding outlet perforate 8 of running wheel 2 successively, thereby has caused periodic turbulent flow and corresponding mechanical oscillation in fluid.The fluid that discharge orifice 11 by annular chamber 4 flows out enters in the space 12 of stator 7, and the fluid of disposing passes through discharge orifice 13 discharges from this.
The quantity of the discharge orifice 11 of annular chamber 4 can be selected in the scope from one to K, should be taken into account the increase along with discharge orifice 11 numbers, under the situation that others all remain unchanged, and the corresponding raising of processing volume ability, fluid treatment efficient then reduces.
According to the basic embodiment (Fig. 1,2) of the device of the method that is used to realize described processing fluid, this device comprises a rotor 14, and this rotor 14 is equipped with the axle 15 that can rotate in bearing 16 and 17, and a sealing 18 is being set.Rotor 14 also comprises the running wheel 2 that at least one is connected with axle 15, and it is made into a disk 19 with peripheral annular wall 20, and annular wall 20 has cylindrical external surface 5.A series of outlet perforates 8 that are used for fluid are distributed in the said wall 20 equidistantly along periphery.
The stator 7 that containing running wheel 2 is provided with to providing and wants input perforate 3 that processed fluid uses and be the discharge orifice 10 of the fluid outflow usefulness handled.A space 1 is used to admit and wants processed fluid, and it is by the annular wall 20 of disk 19, running wheel 2 and to have the adjacent wall 21 of the stator 7 of importing perforate 3 formed.An annular chamber 4 is used to admit and wants processed fluid, and annular chamber 4 is limited by the coaxial wall 22 of the annular wall 20 of running wheel 2 with stator 7 diametrically, and is communicated with the discharge orifice 10 that is used to make the fluid handled therefrom to flow out.
The geomery feature-set of running wheel 2 and annular chamber 4 is as follows:
R=(1.05 ... 1.28) K (millimeter),
Δ R=(1.05 ... 1.28) B (millimeter), in addition
K is the selected number of outlet perforate of running wheel,
R is the radius of cylindrical external surface of the peripheral annular wall of running wheel,
B is 1 ... selected integer in the K/2 scope,
Δ R is the radial dimension of annular chamber.
At the most preferred embodiment (Fig. 1,2) of the device that is used for handling fluid, the nominal value of radius R is set at clearly:
R=1.1614K (millimeter),
And the nominal value of radial dimension Δ R is set at:
Δ R=1.1614B (millimeter) is at this.
B is 1 ... selected integer in the K/5 scope.
Another preferred embodiment (Fig. 3,4) according to the device that is used to handle fluid, stator 7 has a space 12, the coaxial wall 22 of its adjacent stator 7, in order to admitting the fluid come out from annular chamber 4, space 12 is communicated with the discharge orifice 13 that is used for the fluid that emission treatment crosses.The space 12 of stator 7 is communicated with annular chamber 4 by discharge orifice 11, and discharge orifice 11 is used for making fluid to discharge from annular chamber 4, makes its inflow space 12 simultaneously, and said discharge orifice 11 is arranged in the coaxial wall 22 of stator 7.Said discharge orifice 11 be arranged in running wheel 2 a series of outlet perforates 8 the distribution plane and equidistantly distribute along circumference.The number of discharge orifice 11 can be from 1 to K setting, and its number surpasses K and is no advantage, because when other situation is identical, above after the K value, impact strength obviously reduces.
Rotor 14 is connected with the drive unit (for example motor 24) that shaft coupling 23 and its have predetermined speed by the transmission mechanism of axle 15.
Rotor can comprise the several running wheels that are assembled on the axle, and said several running wheels sequentially contact along fluid stream.But each running wheel fit on blade.
This device can be made into to have and dams or the internal bypass or the outer bypass of control element, thus with so that the fluid that a part had been handled flow out and enter into its input port and carry out reprocessing from the outlet of this device.
Any position that this device can take up room as a whole.
The number K of the outlet perforate 8 of running wheel 2, can be selected based on desirable forced oscillation frequency in the sound wave scope that in fluid, has inspired, and can be determined K with following empirical formula:
F=63.993K
-0.5(KHz)
Should consider that this device makes as a whole can realize and favourable geomery.
In above-mentioned scope, the physical property of the particular fluid of wanting processed is depended in the selection of B parameter, the especially change of its viscosity and state when its heating, and to consider this device rational geomery as a whole.
Be used for making the selection of fluid, depend on the allowable limit of desirable volume energy power rate and fluid treatment from the number of the discharge orifice 11 of annular chamber 4 outflows.
The outlet perforate 8 of running wheel 2 preferably is set in 1/2 of the circumference spacing between these perforates 8 on the circumference that along R is radius at the width on the circumferencial direction of outer surface 5.The discharge orifice 11 of annular chamber 4 is at the width on the circumferencial direction of coaxial surface 6, no matter the number of discharge orifice 11 how much, preferably is no more than the width of outlet perforate 8.Perforate 8 and 11 shape, preferably consistent as shown in Figure 3, and extend with the direction that is parallel to central shaft 9.
The device that is used to handle fluid according to the present invention moves as follows:
In the basic and illustrated embodiments of this device (Fig. 1,2), processed fluid to be provided in the space 1 of running wheel 2 with the direction shown in the arrow by input perforate 3.With motor 24, by shaft coupling 23 and axle 15, make rotor 14 and running wheel 2 together, rotate with predetermined speed n.In the case, entering the fluid in the space 1 of running wheel 2, under pressure,, entering into the annular chamber 4 that is limited by the coaxial wall 22 of the annular wall 20 of running wheel 2 and stator 7 by a series of outlet perforates 8 in the peripheral annular wall 20 of running wheel 2.The fluid of handling is discharged by discharge orifice 10 with direction shown in the arrow from annular chamber 4, is used for follow-up fractionation and handles.
The running of another preferred embodiment of this device (Fig. 3,4), except wanting processed fluid to leave annular chamber 4 by the discharge orifice 11 in the coaxial wall 22 that is arranged on stator 7, and enter into beyond the space 12 of stator 7, other method of operation was with in the past described all similar.The fluid of handling is discharged by discharge orifice 13 with the direction shown in the arrow from space 12, is used for follow-up fractionation and handles.
Provided in the following form according to the present invention handle fluid method embodiment and be used for the special case (table 1,2) of the device of this embodiment.Wherein, when initial hydrocarbon fluid was handled, the efficient for the treatment of apparatus was corresponding with the raising of the output of lightweight fraction products (gasoline, kerosene, diesel oil).In the given example below, treatment effeciency is to handle in the fuel oil of preparing distillation in the back in mode according to the present invention, when extracting the lightweight fraction once more calculating once more of hydrocarbon raw material (crude oil) is drawn.
Table 1
Example according to Fig. 1,2 embodiment
Processed fluid-fuel oil
The radius R millimeter 140.0 of the periphery cylinderical surface of the outlet perforate number K of name code unit amount running wheel 120 a running wheel
The radial dimension Δ R millimeter 9.3 of inch 5.512 annular chambers
Treatment effeciency-% 6.4 during treatment effeciency-% 1.350% closed circuit service ability G1 kilogram/per minute 32.050% closed circuit operation during the operation of inch 0.366 running wheel speed n revolution/per minute 2920 mechanical oscillation frequency F KHzs 5.840 energy E megajoules 46.8 open type service ability G kilogram/per minutes 64.0 open types
Table 2
Example according to Fig. 3,4 embodiment
Processed fluid-fuel oil
The radius R millimeter 223.0 of the periphery cylinderical surface of the outlet perforate number K of name code unit amount running wheel 192 a running wheel
The radial dimension Δ R millimeter 41.8 of inch 8.780 annular chambers
Treatment effeciency-% 1.1550% closed circuit service ability G1 kg/minute 51.4 treatment effeciencies-% 2.30 when outlet perforate number K1 128 energy E megajoules, 64.8 open type service ability G kilogram/per minutes, 102.8 open types of inch 1.646 running wheel speed n revolution/per minutes 1440 mechanical oscillation frequency F KHzs 4.620 annular chambers are moved
Commercial Application
At chemical industry, oil and other industrial circle, the present invention can be used for for example initially former to hydrocarbon fluid Material or intermediate product carry out the technical finesse before fractionation. This preliminary treatment according to the present invention can be applied to To the crude oil before distilling, the again fuel oil before distillation or the cracking, the gasoline before the catalytic cracking, the stone before reforming The processing of the artificial hydrocarbon fluid before cerebrol and the corresponding fractionation. The integrality of processing mode of the present invention makes this Bright can by with two technical parts pass on the reasonable combination of step, and be applied in the existing fractional distillation process.
By means of being similar purpose (electric power, waterpower, wind-force, machinery, etc.) and particular design Engine, or by means of the section of movement, especially transmission of rotation facility (transporting equipments of hydrocarbon fluid etc.) Part can make the running wheel activate.
Claims (6)
1, a kind of method by means of the mechanism handle hydrocarbon fluid, it comprises:
(1) being provided in the space of the running wheel that is rotating by processed fluid;
(2) wanting processed fluid to discharge and enter the annular chamber from the space of running wheel, this annular chamber is to be formed by the periphery cylinderical surface of said running wheel and the coaxial surface of a stator, wherein
(3) said discharge realizes by a series of outlet perforates, and said a series of outlet perforates are set on the running wheel periphery cylinderical surface, and equidistantly distributes along circumference;
(4) fluid is discharged from said annular chamber by at least one discharge orifice, wherein
(5) size of the radius R of the periphery cylinderical surface of running wheel is according to following empirical equation, determined by the outlet perforate number K of selected said running wheel,
R=(1.05 ... 1.28) K (millimeter),
(6) the speed n of running wheel is determined with said K value according to following empirical equation,
N=(3.6 ... 4.1) K
-1.5.10
6(revolution/per minute).
According to the described a kind of method of handling fluid of claim 1, it is characterized in that 2, the size of the radius R of the periphery cylinderical surface of running wheel is according to following empirical data, the number K of the outlet perforate by selected said running wheel determined,
R=1.1614K (millimeter),
And the speed n of running wheel is according to following empirical formula, determined with the K value,
N=3.836K
-1.5.10
6(revolution/per minute)
3, according to the described a kind of method of handling fluid of claim 2, it is characterized in that, fluid is realized by discharge orifice from the discharge of annular chamber, said annular chamber is to be formed by the periphery cylinderical surface of running wheel and the coaxial surface of stator, said discharge orifice is arranged on the coaxial surface of stator, in said running wheel rotary course, said discharge orifice is in turn mutually opposed with the outlet perforate of running wheel.
4, a kind of device by means of the mechanism handle hydrocarbon fluid, it comprises:
(1) rotor, it is adorning an axle that can rotate in bearing,
(2) at least one running wheel that is connected with axle, it is made into a disk that has the peripheral annular wall, and annular wall has a columnar outer surface, in this annular wall, along circumference a series of outlet perforates that are used for fluid is set equidistantly;
(3) stators that comprising the running wheel, it has the input perforate and the discharge orifice that is used for exhaust fluid that are used to provide fluid;
(4) spaces are used to hold and want processed fluid, and said space is by the annular wall of this disk and running wheel, and have the input perforate and the stator wall adjacent with said running wheel forms;
(5) annular chambers are used to hold and want processed fluid, and it is limited by the peripheral annular wall of running wheel and the coaxial wall of stator diametrically, and is communicated with the discharge orifice that is used for exhaust fluid;
Wherein, the geomery feature-set of running wheel and annular chamber is:
(6) radius R of the cylindrical external surface of the peripheral annular wall of running wheel is set at:
R=(1.05 ... 1.28) K (millimeter), in addition
K is selected running wheel outlet perforate number,
(7) the radial dimension Δ R of annular chamber is set at:
Δ R=(1.05 ... 1.28) B (millimeter), herein
B is a selected integer in 1 to the K/2 scope,
(8) being used to drive rotor makes it by the instrument of being scheduled to the speed rotation.
According to the described a kind of device of handling fluid of claim 4, it is characterized in that 5, the radius R of the cylindrical external surface of the peripheral annular wall of running wheel is set at:
R=1.1614 (millimeter), herein
K is selected running wheel outlet perforate number, and the radial dimension Δ R of annular chamber is set at:
Δ R=1.1614B (millimeter), herein
B is 1 ... selected integer in the K/5 scope.
6, according to the described a kind of device that is used to handle fluid of claim 5, it is characterized in that:
(1) this stator has the space of its coaxial wall of vicinity, and in order to fluid is introduced this space from annular chamber, said space is connected with the discharge orifice that is used for exhaust fluid, at this
(2) space of this stator is communicated with annular chamber by the discharge orifice that is arranged in the stator coaxial wall, said discharge orifice be arranged in running wheel the outlet perforate the plane, place and equidistantly distribute along circumference,
(3) number of the discharge orifice of this annular chamber is set at 1 ... K.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95197821 CN1181719A (en) | 1995-04-18 | 1995-04-18 | Method of conditioning hydrocarbon liquids and an appts. for carrying out the method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95197821 CN1181719A (en) | 1995-04-18 | 1995-04-18 | Method of conditioning hydrocarbon liquids and an appts. for carrying out the method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1181719A true CN1181719A (en) | 1998-05-13 |
Family
ID=5083373
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 95197821 Pending CN1181719A (en) | 1995-04-18 | 1995-04-18 | Method of conditioning hydrocarbon liquids and an appts. for carrying out the method |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104114675A (en) * | 2011-12-07 | 2014-10-22 | 索拉里斯控股有限公司 | Method for processing of liquid hydrocarbon raw materials |
| CN104781535A (en) * | 2012-11-09 | 2015-07-15 | 微系统燃料股份责任有限公司 | A machine for emulsifying fuel oils with water |
| CN111093821A (en) * | 2017-06-14 | 2020-05-01 | 自然资源选矿有限公司 | Method for generating parametric resonance of energy in atoms of chemical elements in a substance |
| US11059018B2 (en) | 2018-05-16 | 2021-07-13 | Dresser-Rand Company | Turbomachine chemical reactor and method for cracking hydrocarbons in a process fluid |
| CN113181857A (en) * | 2021-05-11 | 2021-07-30 | 辽宁活态石油技术有限公司 | Device and method for generating electron acceleration wave through cavitation resonance to change molecular structure |
| US11123702B2 (en) | 2018-09-20 | 2021-09-21 | Dresser-Rand Company | Turbomachine type chemical reactor |
-
1995
- 1995-04-18 CN CN 95197821 patent/CN1181719A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104114675A (en) * | 2011-12-07 | 2014-10-22 | 索拉里斯控股有限公司 | Method for processing of liquid hydrocarbon raw materials |
| CN104114675B (en) * | 2011-12-07 | 2016-05-11 | 索拉里斯控股有限公司 | For the method for processing liquid hydrocarbon feeds |
| CN104781535A (en) * | 2012-11-09 | 2015-07-15 | 微系统燃料股份责任有限公司 | A machine for emulsifying fuel oils with water |
| CN111093821A (en) * | 2017-06-14 | 2020-05-01 | 自然资源选矿有限公司 | Method for generating parametric resonance of energy in atoms of chemical elements in a substance |
| CN111093821B (en) * | 2017-06-14 | 2023-06-27 | 自然资源选矿有限公司 | Method for generating a parametric resonance of energy in atoms of a chemical element in a substance |
| US11059018B2 (en) | 2018-05-16 | 2021-07-13 | Dresser-Rand Company | Turbomachine chemical reactor and method for cracking hydrocarbons in a process fluid |
| US11123702B2 (en) | 2018-09-20 | 2021-09-21 | Dresser-Rand Company | Turbomachine type chemical reactor |
| CN113181857A (en) * | 2021-05-11 | 2021-07-30 | 辽宁活态石油技术有限公司 | Device and method for generating electron acceleration wave through cavitation resonance to change molecular structure |
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