CA2218591A1 - Method of conditioning of hydrocarbon fluids and device for embodiment thereof - Google Patents
Method of conditioning of hydrocarbon fluids and device for embodiment thereof Download PDFInfo
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- CA2218591A1 CA2218591A1 CA002218591A CA2218591A CA2218591A1 CA 2218591 A1 CA2218591 A1 CA 2218591A1 CA 002218591 A CA002218591 A CA 002218591A CA 2218591 A CA2218591 A CA 2218591A CA 2218591 A1 CA2218591 A1 CA 2218591A1
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- CA
- Canada
- Prior art keywords
- working wheel
- fluid
- discharge
- stator
- conditioning
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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
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
- C10G31/10—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for with the aid of centrifugal force
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1806—Stationary reactors having moving elements inside resulting in a turbulent flow of the reactants, such as in centrifugal-type reactors, or having a high Reynolds-number
Abstract
Disclosed are a method and apparatus for conditioning hydrocarbon liquids by applying mechanical vibrations before fractionation. The method involves introducing the liquid into a cavity (1) in a rotating wheel (2), expelling the liquid into an annular chamber (4) formed by the wheel and the stator (7) via a series of outlet apertures (8), and removing the liquid. For this process, the following empirical proportions are preferred: R = 1.1614 K/mm; .DELTA.R = 1.1614 B/mm; and n = 3.8396 K-1.5 x 106 revs/min, R being the radius of the peripheral cylindrical surface of the wheel, .DELTA.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
CA 02218~91 1997-10-17 METHOD OF CONDITIONING
OF HYDROCARBON FLUIDS
AND DEVI OE FOR EMBODIMENT THEREOF
BACRGROUND OF THE I~V~NL10N
The present invention relates to technology of preparation of hydrocarbon fluids for their further processing and directly d~als with the method and device for preliminary conditioning of hydrocarbon fluids before their further fractioning, effected by processing with the help of mechanical action.
From the state of art, of a common knowledge are methods of preliminary conditioning of hydrocarbon liquid stock before its fractioning, effected by processing with the help of mechanical action, in particular, by preliminary filtering from undesirable inclusions. Such processing facilitates the process of subsequent fractioning, but has no influence either on the physical properties of the initial hydrocarbon stock or In thi~ context the term "conditioning" implies imparting such phy~ical propertie~ to raw material that are favorable from the point of view of further proce.a~ing .
CA 02218~91 1997-10-17 semi-product, nor on the output of intermediary or finite fractions.
From the state of art is also known a method of fluid processing by means of mechanical vibrations (International Application No. PCT/RU92/00194 dated 1992), which includes the supply of fluid to be processed into the space of the rotating working wheel; the discharge of the fluid from the space of the working wheel through a series of outlet openings made on the peripheral cylindrical surface thereof; intake of the fluid into the stator space through at least one inlet opening made in the stator concentric surface, adjoining the peripheral cylindrical surface of the working wheel with a minimum clearance; whereby a periodical abrupt interruptions of the fluid flowing the output openings of the working wheel are effected, exciting mechanical vibrations therein in the sonic or ultrasonic ranges.
The device embodying the described method of fluid processing comprises a rotor, including a shaft running in bearings; a working wheel connected to a shaft and made as a disc with a peripheral annular wall having cylindrical inner and outer surfaces, wherein a series of openings is made for fluid passage, CA 02218~91 1997-10-17 equidistant along the circumference a stator containing the working wheel, said stator having an intake opening for fluid supply and a discharge opening for fluid outflow and two concentric walls adjoining the peripheral annular wall of the working wheels at both sides with a minimum clearance; in both concentric walls of the stator openings are made for fluid passage, lying in the location plane of the series of openings of the working wheel.
As applied to hydrocarbon fluids, the above-described method and device for fluid processing does not likewise influence their physical properties, with the exception of certain heating., nor the output of intermediary and finite products of subsequent fractioning.
SUM~RY OF THE INVENTION
The present invention is aimed at solving the problem of producing, on the basis of the prior art and own research, such a method of conditioning of hydrocarbon fluids before their subsequent fractioning and such a device for embodiment thereof that would influence the physical properties of hydrocarbon fluid CA 02218~91 1997-10-17 in such a manner as to increase the output of light fractioning products.
This problem is solved, according to the invention, by processing the fluid with the help of mechanical action thereon of the process of rotary motion with a definite linear velocity along a definite radius of rotation with superimposition of vibratory process of a definite frequency.
For this purpose, in the basic embodiment of the method of fluid conditioning are provided: the supply of the fluid to be processed into the space of the rotating working wheel; the discharge of the fluid to be processed from the space of the working wheel into a circular chamber formed by the peripheral cylindrical surface of the working wheel and the concentric surface of the stator through a series of outlet openings arranged on the peripheral cylindrical surface of the working wheel and equidistant along the circumference; the discharge of the fluid from the circular chamber through at least one discharge opening. In this case the radius R of the peripheral cylindrical surface of the working wheel and the rotation frequency n thereof are determined by the number K of the outlet CA 02218~91 1997-10-17 openings of the working wheel ln the range according to empirical relationships R = (1.05 ... 1.28) K (mm) and n = (3.6 4.1) K-l5*106 (r.p.m.).
Beyond the limits of said ranges of parameters the obtainable effect of fluid conditioning, as has been experimentally established, is expressed in an insufficient degree.
In the most preferred embodiment of the method of fluid conditioning the radius R and the rotation frequency n of the working wheel are determined unambiguously by the selected number K of the outlet openings thereof according to empirical relationships R = 1.1614 K (mm) and n = 3.8396 K-l5*106 (r.p.m.).
In another preferred embodiment of the method of fluid conditioning the discharge of the fluid to be processed from the circular chamber formed by the peripheral cylindrical surface of the working wheel and concentric surface of the stator is effected through discharge openings arranged of the concentric surface of the stator, which are sequentially arranged opposite CA 02218~91 1997-10-17 to the outlet openings of the working wheel in the course of rotation thereof.
In the described basic embodiment of the method of conditioning of hydrocarbon fluids in said range of selection of parameters, as has been set experimentally, such an influence on fluid physical properties is fundamentally achieved that at its ensuing fractioning the output of most valuable low-boiling fractions essentially increases, namely, to such an extent that it is possible to speak about a rather efficient practical utilization. This effect can be explained, not pretending to an - exhaustive analysis of internal physical processes, by destructive transformation of inner bonds of fluid at a molecular level taking place as a result of initiating influence of mechanical action on the fluid at certain critical frequencies and harmonics thereof. In the most preferred embodiment of the method of fluid conditioning, when said unambiguous values of parameters, determined experimentally, are chosen, the effect of favorable predisposition of hydrocarbon fluid to subsequent fractioning manifests itself at utmost.
CA 02218~91 1997-10-17 Another preferred embodiment of the method of fluid conditioning makes possible to improve the obtainable effect owing to a combined vibratory action exerted upon the fluid at first when the latter is discharged through the ou-tlet openings of the working wheel, then when it is discharged from the circular chamber through the discharge openings made on the stator concentric surface.
The method of conditioning of hydrocarbon fluids, according to the invention, may be embodied only by means of the hereinafter described device, forming an integral part of the inventor's general intention and is not intended for use in other purposes.
The device for fluid conditioning in the basic embodiment thereof comprises a rotor including a shaft running in bearings;
at least one working wheel connected to the shaft and made as a disc with a peripheral annular wall having a cylindrical outer surface, wherein a series of outlet openings is made for fluid, equidistant along the circumference; a stator containing a working wheel having an intake opening for fluid supply and a discharge opening for fluid outflow; a space for the fluid to be CA 02218~91 1997-10-17 processed, said space being formed by the disc and a peripheral annular wall of the working wheel and a stator wall with an intake opening and adjoining thereto; a circular chamber for the fluid to be processed, said c-ircular chamber being restricted in the radial direction by the peripheral annular wall of the working wheel and the stator concentric wall and communicates with the discharge opening for the fluid outflow; the characteristic geometric dimensions of the working wheel and the circular chamber being:
R - (1.05 .... 1.28) K (mm), where K is the selected number of the outlet openings of the working wheel, R is the radius of the outer cylindrical surface of the peripheral annular wall of the working wheel, and ~R = (1.05 ... 1.28) B (mm), where B is the selected integer in the range of 1 ... K/2, ~R is the radial size of the circular chamber.
In the most preferred embodiment of the device for conditioning radius R and size ~R constitute respectively:
R = 1.1614 K (mm), CA 02218~91 1997-10-17 ~R = 1.1614 B (mm), where B is the selected integer in the range of 1 ... K/5.
In another preferred embodiment of the device for conditioning a stator has a space adjoining a concentric wall thereof for fluid intake from a circular chamber communicating with a discharge opening for fluid outflow; the stator space communicating with the circular chamber through the discharge openings made in the stator concentric wall in the arrangement plane of the working wheel outlet openings and equidistant along the circumference; the number of the discharge openings of the circular chamber is 1 ... K.
Other features of the invention will be seen from the following detailed description of embodiments thereof.
CA 02218~91 1997-10-17 BRIEF DESCRIPTION OF THE DR~NINGS
Below the invention is described in more detail by examples of practical embodiment thereof with reference to schematic drawings, wherein:
FIG. 1 is a longitudinal axial section of the device for fluid processing in the basic and most preferred embodiments;
FIG. 2,4 is a partial transverse section of the circular chamber;
FIG. 3 is a longitudinal axial section of the device for fluid processing in one of the preferred embodiments.
DETAILFn DESCRIPTION OF THE lNv~...lON
According to the basic embodiment (FIG. l, 2) of the method of conditioning of hydrocarbon fluid by processing with the help of mechanical action, the fluid to be processed is supplied into the space 1 of the rotating working wheel 2 through the inlet opening 3. During rotation of the working wheel 2 the fluid to be processed is discharged from the space 1 thereof into the CA 02218~91 1997-10-17 circular chamber 4 formed by the peripheral cylindrical surface 5 of the working wheel 2 and the concentric surface 6 of the stator 7 through a series the outlet openings 8 arranged along the peripheral cylindrical surface 5 of the working wheel 2 and equidistant along the circumference. Within the limits of the circular chamber 4 the fluid to be processed, continuing rotation relative to the central axis 9 from the free-flow law, is subjected to the action of mechanical vibrations, caused by the interaction with the concentric surface 6 of the stator 7 of elementary fluid flows flowing out of each outlet opening 8 of the working wheel 2. The processed fluid is discharged from the circular chamber 4 through the discharge opening 10.
The radius R of the peripheral cylindrical surface S and the frequency of rotation n of the working wheel are determined by the selected number K of the outlet openings 8 of the working wheel 2 in the range according to empirical relat-ionships:
R = (1.05 ... 1.28) K (mm), n = (3.6 ... 4.1) K-15*106 (r.p.m.).
According to the most preferred embodiment of the method of conditioning, the radius R and the frequency of rotation n of the CA 02218~91 1997-10-17 working wheel 2 are determined unambiguously by the selected number K of the outlet openings 8 of the working wheel 2 according to empirical relationships:
R = 1.1614 K (mm), n = 3.8396 K-1s*106 (r.p.m.).
According to another preferred embodiment (FIG. 3, 4) of the method of conditioning, the discharge of the fluid to be processed from the circular chamber 4 formed by the peripheral cylindrical surface 5 of the working wheel 2 and the concentric surface 6 of the stator 7 is effected through one, several or a series of the discharge openings 11 made on the concentric surface 6 of the stator 7. Said discharge openings 11 of the circular chamber 4 during rotation of the working wheel 2 are sequentially arranged opposite to the corresponding outlet openings 8 of the working wheel 2, causing perlodical disturbances of flow and corresponding mechanical vibrations in the fluid. The fluid passed through the discharge openings of the circular chamber 4 enters the space 12 of the stator 7, wherefrom the processed fluid is let out through the discharge opening 13.
CA 022l8~9l l997- lO- l7 The number of the discharge openings 11 of the circular chamber 4 is selected in the range of one to K, whereat it is taken into account that with the increase of the number of the discharge openings 11, all other things being equal, the process volumetric capacity increases adequately, but the efficiency of conditioning decreases from the point of view of the problem being solved by the invention.
According to the basic embodiment (FIG. 1, 2) of the device for effecting the described method of conditioning, it comprises a rotor 14, containing a shaft 15 running in bearings 16 and 17 and provided with a seal 18. The rotor 14 comprises at least one working wheel 2 connected to the shaft 15 and made as a disc 19 with a peripheral annular wall 20, having a cylindrical outer surface 5. In said wall 20 a series of outlet openings 8 is made for the fluid, equidistant along the circumference.
A stator 7 containing the working wheel 2 is provided with an intake opening 3 for the fluid supply for processing and a discharge opening 10 for letting out the processed fluid. A
space 1 for the admission of the fluid to be processed is formed by the disc 19 and the annular wall 20 of the working wheel 2 and CA 022l8~9l l997- lO- l7 the wall 21 adjoining thereto of the stator 7 with the intake opening 3. A circular chamber 4 for admission of the fluid to be processed is restricted in the radial direction with the annular wall 20 of the working wheel 2 and the concentric wall 22 of the stator 7 and communicates with the discharge opening 10 for letting out the processed fluid.
The characteristic geometric dimenslons of the working wheel 2 and of the circular chamber 4 constitute:
R = (1.05 ... 1.28) K (mm), ~R = (1.05 .... 1.28) B (mm), where K is the selected number of the outlet openings of the working wheel, R is the radius of the cylindrical outer surface of the peripheral annular wall of the working wheel, B is the selected integer in the range of 1 ... K/2, ~R is the radial size of the annular chamber.
In the most preferred embodiment (FIG. 1, 2) of the device for conditioning the nominal value of the radius R constitutes unambiguously R = 1.1614 K (mm), CA 02218~91 1997-10-17 -lS-while the nominal radial size ~R constitutes ~ R = 1.1614 B (mm), where B is the selected integer in the range of 1 ... K/5.
According to another preferred embodiment (FIG. 3, 4) of the device for conditioning the stator 7 has the space 12, adjoining the concentric wall 22 thereof to receive the fluid from the circular chamber 4 communicating with the discharge opening 13 for discharging the processed fluid. The space 12 of the stator 7 communicates with the circular wall 4 through the discharge openings 11 for discharging the fluid from the circular chamber 4 and simultaneously for letting it into the space 12, said discharge openings being made in the concentric wall 22 of the stator 7. Said discharge openings 11 lie in the arrangement plane of a series of the outlet openings 8 of the working wheel 2 and are equidistant along the circumference. The number of the openings 11 constitutes from one to K, their number exceeding K
being not advantageous due to a marked decrease, all other things belng equal, of the intensity of oscillating process.
CA 022l8~9l l997- lO- l7 The rotor 14 is connected through the medium of the shaft 15 and coupling 23 to a driving means thereof with a calculated rotation frequency, such as the electric motor 24.
The rotor may comprise several working wheels fitted on one S shaft, said working wheels being connected sequentially along the fluid flow. Each working wheel can be equipped with vanes.
Provision can be made of the inner or outer by-pass channel with a shut-off-and-control member for reversing a portion of the processed fluid from the outlet of the device to the input thereof for repeated processing.
The device as a whole can occupy any position in space.
The number K of the outlet openings 8 of the working wheel 2 is selected basing on the desired frequency of forced vibrations excited in the fluid in the sonic range, which is determined by empirical relationship F 63 993 K-ls*106 (kHz) taking into account the achievable and advantageous geometric dimensions of the device as a whole.
The value of parameter B is selected in the above-mentioned ranges, depending on physical properties of a particular fluid to CA 02218~91 1997-10-17 be processed, especially on viscosity and nature of change during heating, taking into account reasonable geometric dimensions of the device as a whole.
The number of the discharge openings 11 for fluid letting out from the circular chamber 4 is selected depending on the desirable ratio of volumetric capacity and tolerable degree of conditioning.
The width of the outlet openings 8 of the working wheel 2 in the circumferential direction along the peripheral surface 5 thereof constitutes preferably 1/2 of their circumferential pitch along the circumference of radius R. The width of the discharge openings 11 of the circular chamber 4 in the circumferential direction along the concentric surface 6 thereof, irrespective of their number, should not exceed preferably that of the outlet openings 8. The shape of the openings 8 and 11, as shown in the drawings of FIG. 1 and 3, is preferred uniform, extended in the direction parallel to the central axis 9.
The device for conditioning, according to the invention, operates as follows;
CA 022l8~9l l997- lO- l7 In the basic and most preferred embodiments of the device tFIG. 1, 2) the fluid to be processed is supplied through the intake opening 3 into the space 1 of the working wheel 2 in the direction shown by the arrow. The rotor 14 together with the working wheel 2 is set into rotation with the help of the electric motor 24 via the coupling 23 and the shaft 15 with calculated rotation frequency n. In this case the fluid entering the space 1 of the working wheel 2 under pressure leaves the space 1 through a series of the outlet openings 8 made in the peripheral annular wall 20 of the working wheel 2, entering the circular chamber 4 limited with the annular wall 20 of the working wheel 2 and the concentric wall 22 of the stator 7. From the circular chamber 4 the processed fluid is discharged for further processing by fractioning through the discharge opening 10 in the direction shown by the arrow.
In another preferred embodiment the device (FIG. 3, 4) operates similarly to that described above, with the exception that the fluid to be processed leaves the circular chamber 4 and enters the space 12 of the stator 7 through the discharge openings 11 made in the concentric wall 22 of the stator 7. From CA 02218~91 1997-10-17 the space 12 the processed fluid is supplied for further processing with the aim of fractioning through the discharge opening 13 in the direction shown by the arrow.
Below are given particular examples of practical embodiment, according to the invention, of the method of conditioning and device for embodiment thereof (tables 1 and 2). In this case the efficiency of conditioning means relative increase of the output of light fractions (gasoline, kerosene, diesel fuel) when fractioning of the initial hydrocarbon fluid. In the given examples the efficiency of conditioning is determined by recalculation to initial hydrogen stock (raw petroleum) of additional extraction of light fractions from fuel oil subjected to distillation after conditioning, carried out according to the invention.
CA 022l8~9l l997-lO-l7 Table 1. Example of Embodiment According to FIG. 1, 2.
Processed Fluid - Fuel Oil Name Symbol Unit Value Number of working wheel 10 outlet openings K pcs 120 Radius of working wheel peripheral cylindrical R mm 140.0 surface in. 5.512 Radial size of circular~R mm 9.3 chamber in 0.366 Working wheel rotation 20 frequency n r.p.m. 2920 Mechanical vibration frequency F kHz 5.840 25 Energy supplied E MJ 46.8 Capacity at open circulation G kg/min 64.0 30 Efficiency of conditioning at open circulation _ % 1.3 Capacity at 50% enclosedG1 kg/min 32.0 circulation Efficiency of conditioning at 50% enclosed circulation _ % 2.5 . CA 02218~91 1997-10-17 Table 2. Example of Embodiment According to FIG. 3, 4.
Processed Fluid - Fuel Oil Name Symbol Unit Value Number of working wheel outlet openings K pcs 192 Radius of working wheel peripheral cylindrical R mm 223.0 surface in. 8.780 Radial size of circular R mm 41.8 chamber in 1.646 Working wheel rotation frequency n r.p.m. 1440 Mechanical vibration frequency F kHz 4.620 25 Number of circular chamber ~ discharge openings K1 pcs 128 Energy supplied E MJ 64.8 Capacity at open circulation G kg/min 102.8 Efficiency of conditioning at open circulation - % 1.15 Capacity at 50% enclosed circulation G1 kg/min 51.4 Efficiency of conditioning - $ 2.30 '. CA 02218~91 1997-10-17 lN~ .~IAL AppLIt~RTT-TTy The field of industrial application of the invention covers the chemical, petroleum and other branches of industry, associated with technological processing of hydrocarbon fluids -both the initial raw stock and intermediary products of processing - with the aim of conditioning them before subsequent fractioning. Preliminary conditioning can be used, according to the invention, in particular, for crude oil before distillation, fuel oil before repeated distillation or cracking, gas oil before catalytic cracking, naphta before reforming, etc, as well as artificial hydrocarbon fluids before corresponding fractioning.
Integration of the process corresponding to the invention is possible into traditional technological chains of fractioning at a rational combination with transfer operations of hydrocarbon fluids between technological components.
The working wheel can be actuated by means of either a motor specially designed for similar purposes (electric, hydraulic, wind, mechanical, etc.), or of rotating parts of transport facilities for the transportation of hydrocarbon fluids.
OF HYDROCARBON FLUIDS
AND DEVI OE FOR EMBODIMENT THEREOF
BACRGROUND OF THE I~V~NL10N
The present invention relates to technology of preparation of hydrocarbon fluids for their further processing and directly d~als with the method and device for preliminary conditioning of hydrocarbon fluids before their further fractioning, effected by processing with the help of mechanical action.
From the state of art, of a common knowledge are methods of preliminary conditioning of hydrocarbon liquid stock before its fractioning, effected by processing with the help of mechanical action, in particular, by preliminary filtering from undesirable inclusions. Such processing facilitates the process of subsequent fractioning, but has no influence either on the physical properties of the initial hydrocarbon stock or In thi~ context the term "conditioning" implies imparting such phy~ical propertie~ to raw material that are favorable from the point of view of further proce.a~ing .
CA 02218~91 1997-10-17 semi-product, nor on the output of intermediary or finite fractions.
From the state of art is also known a method of fluid processing by means of mechanical vibrations (International Application No. PCT/RU92/00194 dated 1992), which includes the supply of fluid to be processed into the space of the rotating working wheel; the discharge of the fluid from the space of the working wheel through a series of outlet openings made on the peripheral cylindrical surface thereof; intake of the fluid into the stator space through at least one inlet opening made in the stator concentric surface, adjoining the peripheral cylindrical surface of the working wheel with a minimum clearance; whereby a periodical abrupt interruptions of the fluid flowing the output openings of the working wheel are effected, exciting mechanical vibrations therein in the sonic or ultrasonic ranges.
The device embodying the described method of fluid processing comprises a rotor, including a shaft running in bearings; a working wheel connected to a shaft and made as a disc with a peripheral annular wall having cylindrical inner and outer surfaces, wherein a series of openings is made for fluid passage, CA 02218~91 1997-10-17 equidistant along the circumference a stator containing the working wheel, said stator having an intake opening for fluid supply and a discharge opening for fluid outflow and two concentric walls adjoining the peripheral annular wall of the working wheels at both sides with a minimum clearance; in both concentric walls of the stator openings are made for fluid passage, lying in the location plane of the series of openings of the working wheel.
As applied to hydrocarbon fluids, the above-described method and device for fluid processing does not likewise influence their physical properties, with the exception of certain heating., nor the output of intermediary and finite products of subsequent fractioning.
SUM~RY OF THE INVENTION
The present invention is aimed at solving the problem of producing, on the basis of the prior art and own research, such a method of conditioning of hydrocarbon fluids before their subsequent fractioning and such a device for embodiment thereof that would influence the physical properties of hydrocarbon fluid CA 02218~91 1997-10-17 in such a manner as to increase the output of light fractioning products.
This problem is solved, according to the invention, by processing the fluid with the help of mechanical action thereon of the process of rotary motion with a definite linear velocity along a definite radius of rotation with superimposition of vibratory process of a definite frequency.
For this purpose, in the basic embodiment of the method of fluid conditioning are provided: the supply of the fluid to be processed into the space of the rotating working wheel; the discharge of the fluid to be processed from the space of the working wheel into a circular chamber formed by the peripheral cylindrical surface of the working wheel and the concentric surface of the stator through a series of outlet openings arranged on the peripheral cylindrical surface of the working wheel and equidistant along the circumference; the discharge of the fluid from the circular chamber through at least one discharge opening. In this case the radius R of the peripheral cylindrical surface of the working wheel and the rotation frequency n thereof are determined by the number K of the outlet CA 02218~91 1997-10-17 openings of the working wheel ln the range according to empirical relationships R = (1.05 ... 1.28) K (mm) and n = (3.6 4.1) K-l5*106 (r.p.m.).
Beyond the limits of said ranges of parameters the obtainable effect of fluid conditioning, as has been experimentally established, is expressed in an insufficient degree.
In the most preferred embodiment of the method of fluid conditioning the radius R and the rotation frequency n of the working wheel are determined unambiguously by the selected number K of the outlet openings thereof according to empirical relationships R = 1.1614 K (mm) and n = 3.8396 K-l5*106 (r.p.m.).
In another preferred embodiment of the method of fluid conditioning the discharge of the fluid to be processed from the circular chamber formed by the peripheral cylindrical surface of the working wheel and concentric surface of the stator is effected through discharge openings arranged of the concentric surface of the stator, which are sequentially arranged opposite CA 02218~91 1997-10-17 to the outlet openings of the working wheel in the course of rotation thereof.
In the described basic embodiment of the method of conditioning of hydrocarbon fluids in said range of selection of parameters, as has been set experimentally, such an influence on fluid physical properties is fundamentally achieved that at its ensuing fractioning the output of most valuable low-boiling fractions essentially increases, namely, to such an extent that it is possible to speak about a rather efficient practical utilization. This effect can be explained, not pretending to an - exhaustive analysis of internal physical processes, by destructive transformation of inner bonds of fluid at a molecular level taking place as a result of initiating influence of mechanical action on the fluid at certain critical frequencies and harmonics thereof. In the most preferred embodiment of the method of fluid conditioning, when said unambiguous values of parameters, determined experimentally, are chosen, the effect of favorable predisposition of hydrocarbon fluid to subsequent fractioning manifests itself at utmost.
CA 02218~91 1997-10-17 Another preferred embodiment of the method of fluid conditioning makes possible to improve the obtainable effect owing to a combined vibratory action exerted upon the fluid at first when the latter is discharged through the ou-tlet openings of the working wheel, then when it is discharged from the circular chamber through the discharge openings made on the stator concentric surface.
The method of conditioning of hydrocarbon fluids, according to the invention, may be embodied only by means of the hereinafter described device, forming an integral part of the inventor's general intention and is not intended for use in other purposes.
The device for fluid conditioning in the basic embodiment thereof comprises a rotor including a shaft running in bearings;
at least one working wheel connected to the shaft and made as a disc with a peripheral annular wall having a cylindrical outer surface, wherein a series of outlet openings is made for fluid, equidistant along the circumference; a stator containing a working wheel having an intake opening for fluid supply and a discharge opening for fluid outflow; a space for the fluid to be CA 02218~91 1997-10-17 processed, said space being formed by the disc and a peripheral annular wall of the working wheel and a stator wall with an intake opening and adjoining thereto; a circular chamber for the fluid to be processed, said c-ircular chamber being restricted in the radial direction by the peripheral annular wall of the working wheel and the stator concentric wall and communicates with the discharge opening for the fluid outflow; the characteristic geometric dimensions of the working wheel and the circular chamber being:
R - (1.05 .... 1.28) K (mm), where K is the selected number of the outlet openings of the working wheel, R is the radius of the outer cylindrical surface of the peripheral annular wall of the working wheel, and ~R = (1.05 ... 1.28) B (mm), where B is the selected integer in the range of 1 ... K/2, ~R is the radial size of the circular chamber.
In the most preferred embodiment of the device for conditioning radius R and size ~R constitute respectively:
R = 1.1614 K (mm), CA 02218~91 1997-10-17 ~R = 1.1614 B (mm), where B is the selected integer in the range of 1 ... K/5.
In another preferred embodiment of the device for conditioning a stator has a space adjoining a concentric wall thereof for fluid intake from a circular chamber communicating with a discharge opening for fluid outflow; the stator space communicating with the circular chamber through the discharge openings made in the stator concentric wall in the arrangement plane of the working wheel outlet openings and equidistant along the circumference; the number of the discharge openings of the circular chamber is 1 ... K.
Other features of the invention will be seen from the following detailed description of embodiments thereof.
CA 02218~91 1997-10-17 BRIEF DESCRIPTION OF THE DR~NINGS
Below the invention is described in more detail by examples of practical embodiment thereof with reference to schematic drawings, wherein:
FIG. 1 is a longitudinal axial section of the device for fluid processing in the basic and most preferred embodiments;
FIG. 2,4 is a partial transverse section of the circular chamber;
FIG. 3 is a longitudinal axial section of the device for fluid processing in one of the preferred embodiments.
DETAILFn DESCRIPTION OF THE lNv~...lON
According to the basic embodiment (FIG. l, 2) of the method of conditioning of hydrocarbon fluid by processing with the help of mechanical action, the fluid to be processed is supplied into the space 1 of the rotating working wheel 2 through the inlet opening 3. During rotation of the working wheel 2 the fluid to be processed is discharged from the space 1 thereof into the CA 02218~91 1997-10-17 circular chamber 4 formed by the peripheral cylindrical surface 5 of the working wheel 2 and the concentric surface 6 of the stator 7 through a series the outlet openings 8 arranged along the peripheral cylindrical surface 5 of the working wheel 2 and equidistant along the circumference. Within the limits of the circular chamber 4 the fluid to be processed, continuing rotation relative to the central axis 9 from the free-flow law, is subjected to the action of mechanical vibrations, caused by the interaction with the concentric surface 6 of the stator 7 of elementary fluid flows flowing out of each outlet opening 8 of the working wheel 2. The processed fluid is discharged from the circular chamber 4 through the discharge opening 10.
The radius R of the peripheral cylindrical surface S and the frequency of rotation n of the working wheel are determined by the selected number K of the outlet openings 8 of the working wheel 2 in the range according to empirical relat-ionships:
R = (1.05 ... 1.28) K (mm), n = (3.6 ... 4.1) K-15*106 (r.p.m.).
According to the most preferred embodiment of the method of conditioning, the radius R and the frequency of rotation n of the CA 02218~91 1997-10-17 working wheel 2 are determined unambiguously by the selected number K of the outlet openings 8 of the working wheel 2 according to empirical relationships:
R = 1.1614 K (mm), n = 3.8396 K-1s*106 (r.p.m.).
According to another preferred embodiment (FIG. 3, 4) of the method of conditioning, the discharge of the fluid to be processed from the circular chamber 4 formed by the peripheral cylindrical surface 5 of the working wheel 2 and the concentric surface 6 of the stator 7 is effected through one, several or a series of the discharge openings 11 made on the concentric surface 6 of the stator 7. Said discharge openings 11 of the circular chamber 4 during rotation of the working wheel 2 are sequentially arranged opposite to the corresponding outlet openings 8 of the working wheel 2, causing perlodical disturbances of flow and corresponding mechanical vibrations in the fluid. The fluid passed through the discharge openings of the circular chamber 4 enters the space 12 of the stator 7, wherefrom the processed fluid is let out through the discharge opening 13.
CA 022l8~9l l997- lO- l7 The number of the discharge openings 11 of the circular chamber 4 is selected in the range of one to K, whereat it is taken into account that with the increase of the number of the discharge openings 11, all other things being equal, the process volumetric capacity increases adequately, but the efficiency of conditioning decreases from the point of view of the problem being solved by the invention.
According to the basic embodiment (FIG. 1, 2) of the device for effecting the described method of conditioning, it comprises a rotor 14, containing a shaft 15 running in bearings 16 and 17 and provided with a seal 18. The rotor 14 comprises at least one working wheel 2 connected to the shaft 15 and made as a disc 19 with a peripheral annular wall 20, having a cylindrical outer surface 5. In said wall 20 a series of outlet openings 8 is made for the fluid, equidistant along the circumference.
A stator 7 containing the working wheel 2 is provided with an intake opening 3 for the fluid supply for processing and a discharge opening 10 for letting out the processed fluid. A
space 1 for the admission of the fluid to be processed is formed by the disc 19 and the annular wall 20 of the working wheel 2 and CA 022l8~9l l997- lO- l7 the wall 21 adjoining thereto of the stator 7 with the intake opening 3. A circular chamber 4 for admission of the fluid to be processed is restricted in the radial direction with the annular wall 20 of the working wheel 2 and the concentric wall 22 of the stator 7 and communicates with the discharge opening 10 for letting out the processed fluid.
The characteristic geometric dimenslons of the working wheel 2 and of the circular chamber 4 constitute:
R = (1.05 ... 1.28) K (mm), ~R = (1.05 .... 1.28) B (mm), where K is the selected number of the outlet openings of the working wheel, R is the radius of the cylindrical outer surface of the peripheral annular wall of the working wheel, B is the selected integer in the range of 1 ... K/2, ~R is the radial size of the annular chamber.
In the most preferred embodiment (FIG. 1, 2) of the device for conditioning the nominal value of the radius R constitutes unambiguously R = 1.1614 K (mm), CA 02218~91 1997-10-17 -lS-while the nominal radial size ~R constitutes ~ R = 1.1614 B (mm), where B is the selected integer in the range of 1 ... K/5.
According to another preferred embodiment (FIG. 3, 4) of the device for conditioning the stator 7 has the space 12, adjoining the concentric wall 22 thereof to receive the fluid from the circular chamber 4 communicating with the discharge opening 13 for discharging the processed fluid. The space 12 of the stator 7 communicates with the circular wall 4 through the discharge openings 11 for discharging the fluid from the circular chamber 4 and simultaneously for letting it into the space 12, said discharge openings being made in the concentric wall 22 of the stator 7. Said discharge openings 11 lie in the arrangement plane of a series of the outlet openings 8 of the working wheel 2 and are equidistant along the circumference. The number of the openings 11 constitutes from one to K, their number exceeding K
being not advantageous due to a marked decrease, all other things belng equal, of the intensity of oscillating process.
CA 022l8~9l l997- lO- l7 The rotor 14 is connected through the medium of the shaft 15 and coupling 23 to a driving means thereof with a calculated rotation frequency, such as the electric motor 24.
The rotor may comprise several working wheels fitted on one S shaft, said working wheels being connected sequentially along the fluid flow. Each working wheel can be equipped with vanes.
Provision can be made of the inner or outer by-pass channel with a shut-off-and-control member for reversing a portion of the processed fluid from the outlet of the device to the input thereof for repeated processing.
The device as a whole can occupy any position in space.
The number K of the outlet openings 8 of the working wheel 2 is selected basing on the desired frequency of forced vibrations excited in the fluid in the sonic range, which is determined by empirical relationship F 63 993 K-ls*106 (kHz) taking into account the achievable and advantageous geometric dimensions of the device as a whole.
The value of parameter B is selected in the above-mentioned ranges, depending on physical properties of a particular fluid to CA 02218~91 1997-10-17 be processed, especially on viscosity and nature of change during heating, taking into account reasonable geometric dimensions of the device as a whole.
The number of the discharge openings 11 for fluid letting out from the circular chamber 4 is selected depending on the desirable ratio of volumetric capacity and tolerable degree of conditioning.
The width of the outlet openings 8 of the working wheel 2 in the circumferential direction along the peripheral surface 5 thereof constitutes preferably 1/2 of their circumferential pitch along the circumference of radius R. The width of the discharge openings 11 of the circular chamber 4 in the circumferential direction along the concentric surface 6 thereof, irrespective of their number, should not exceed preferably that of the outlet openings 8. The shape of the openings 8 and 11, as shown in the drawings of FIG. 1 and 3, is preferred uniform, extended in the direction parallel to the central axis 9.
The device for conditioning, according to the invention, operates as follows;
CA 022l8~9l l997- lO- l7 In the basic and most preferred embodiments of the device tFIG. 1, 2) the fluid to be processed is supplied through the intake opening 3 into the space 1 of the working wheel 2 in the direction shown by the arrow. The rotor 14 together with the working wheel 2 is set into rotation with the help of the electric motor 24 via the coupling 23 and the shaft 15 with calculated rotation frequency n. In this case the fluid entering the space 1 of the working wheel 2 under pressure leaves the space 1 through a series of the outlet openings 8 made in the peripheral annular wall 20 of the working wheel 2, entering the circular chamber 4 limited with the annular wall 20 of the working wheel 2 and the concentric wall 22 of the stator 7. From the circular chamber 4 the processed fluid is discharged for further processing by fractioning through the discharge opening 10 in the direction shown by the arrow.
In another preferred embodiment the device (FIG. 3, 4) operates similarly to that described above, with the exception that the fluid to be processed leaves the circular chamber 4 and enters the space 12 of the stator 7 through the discharge openings 11 made in the concentric wall 22 of the stator 7. From CA 02218~91 1997-10-17 the space 12 the processed fluid is supplied for further processing with the aim of fractioning through the discharge opening 13 in the direction shown by the arrow.
Below are given particular examples of practical embodiment, according to the invention, of the method of conditioning and device for embodiment thereof (tables 1 and 2). In this case the efficiency of conditioning means relative increase of the output of light fractions (gasoline, kerosene, diesel fuel) when fractioning of the initial hydrocarbon fluid. In the given examples the efficiency of conditioning is determined by recalculation to initial hydrogen stock (raw petroleum) of additional extraction of light fractions from fuel oil subjected to distillation after conditioning, carried out according to the invention.
CA 022l8~9l l997-lO-l7 Table 1. Example of Embodiment According to FIG. 1, 2.
Processed Fluid - Fuel Oil Name Symbol Unit Value Number of working wheel 10 outlet openings K pcs 120 Radius of working wheel peripheral cylindrical R mm 140.0 surface in. 5.512 Radial size of circular~R mm 9.3 chamber in 0.366 Working wheel rotation 20 frequency n r.p.m. 2920 Mechanical vibration frequency F kHz 5.840 25 Energy supplied E MJ 46.8 Capacity at open circulation G kg/min 64.0 30 Efficiency of conditioning at open circulation _ % 1.3 Capacity at 50% enclosedG1 kg/min 32.0 circulation Efficiency of conditioning at 50% enclosed circulation _ % 2.5 . CA 02218~91 1997-10-17 Table 2. Example of Embodiment According to FIG. 3, 4.
Processed Fluid - Fuel Oil Name Symbol Unit Value Number of working wheel outlet openings K pcs 192 Radius of working wheel peripheral cylindrical R mm 223.0 surface in. 8.780 Radial size of circular R mm 41.8 chamber in 1.646 Working wheel rotation frequency n r.p.m. 1440 Mechanical vibration frequency F kHz 4.620 25 Number of circular chamber ~ discharge openings K1 pcs 128 Energy supplied E MJ 64.8 Capacity at open circulation G kg/min 102.8 Efficiency of conditioning at open circulation - % 1.15 Capacity at 50% enclosed circulation G1 kg/min 51.4 Efficiency of conditioning - $ 2.30 '. CA 02218~91 1997-10-17 lN~ .~IAL AppLIt~RTT-TTy The field of industrial application of the invention covers the chemical, petroleum and other branches of industry, associated with technological processing of hydrocarbon fluids -both the initial raw stock and intermediary products of processing - with the aim of conditioning them before subsequent fractioning. Preliminary conditioning can be used, according to the invention, in particular, for crude oil before distillation, fuel oil before repeated distillation or cracking, gas oil before catalytic cracking, naphta before reforming, etc, as well as artificial hydrocarbon fluids before corresponding fractioning.
Integration of the process corresponding to the invention is possible into traditional technological chains of fractioning at a rational combination with transfer operations of hydrocarbon fluids between technological components.
The working wheel can be actuated by means of either a motor specially designed for similar purposes (electric, hydraulic, wind, mechanical, etc.), or of rotating parts of transport facilities for the transportation of hydrocarbon fluids.
Claims (6)
1. A method conditioning of hydrocarbon fluids by processing with the help of mechanical action, comprising (1) supply of the fluid to be processed into a space of a rotating working wheel, (2) discharge of the fluid to be processed from the space of the working wheel into a circular chamber formed by the peripheral cylindrical surface of said working wheel and the concentric surface of a stator, at which (3) said discharge is effected through a series of outlet openings arranged on the peripheral cylindrical surface of the working wheel and equidistant along the circumference, (4) discharge of the fluid from said circular chamber through at least one discharge opening, at which (5) radius R of the peripheral cylindrical surface of the working wheel is determined by selected number E of the outlet openings of said working wheel according to empirical relationship R = (1.05 ... 1.28) K (mm), (6) rotation frequency n of the working wheel is determined by said value K according to empirical relationship n = (3.6 ... 4.1) K-1.5*106 (r.p.m.).
2. The method of conditioning hydrocarbon fluids according to claim 1, wherein the radius R of the peripheral cylindrical surface of the working wheel is determined by the selected number K of the outlet openings of said working wheel according to empirical relationship R = 1.1614 K (mm), while the rotation frequency n of the working wheel is determined by the value K according to empirical relationship n = 3.8396 K-1.5*106 (r.p.m.).
3. The method of conditioning of hydrocarbon fluids according to claim 2, wherein the discharge of the fluid from the circular chamber formed by the peripheral cylindrical surface of the working wheel and the concentric surface of the stator is effected through the discharge openings during rotation of the working wheel sequentially oppose the outlet openings of the working.
4. A device for conditioning of hydrocarbon fluids by processing with the help of mechanical action, comprising (1) a rotor containing a shaft running in bearings, (2) at least one working wheel, connected to a shaft and made as a disc with a peripheral angular wall having a cylindrical outer surface, wherein a series of outlet openings is made for the fluid equidistant along the circumference, (3) a stator containing the working wheel having an intake opening for supply and a discharge opening for discharge of the fluid, (4) a space for the fluid to be processed formed by the disc and the annular wall of the working wheel and a stator wall with an intake opening adjoining said wheel, (5) a circular chamber for the fluid to be processed, which is restricted in the radial direction by the peripheral annular wall of the working wheel and the stator concentric wall, and communicates with the discharge opening for discharge of the fluid, at which the characteristic geometric dimensions of the working wheel and the circular chamber constitute:
( 6 ) radius R of the cylindrical outer surface of the peripheral annular wall of the working wheel R = (1.05 .... 1. 28 ) K (mm), where K is the selected number of the outlet openings of the working wheel, (7) radial size .DELTA.R of the circular chamber .DELTA.R = (1.05 ... 1. 28 ) B (mm), where B is the selected integer in the range of 1 ... K/2, ( 8 ) means for driving the rotor at the calculated rotation frequency.
( 6 ) radius R of the cylindrical outer surface of the peripheral annular wall of the working wheel R = (1.05 .... 1. 28 ) K (mm), where K is the selected number of the outlet openings of the working wheel, (7) radial size .DELTA.R of the circular chamber .DELTA.R = (1.05 ... 1. 28 ) B (mm), where B is the selected integer in the range of 1 ... K/2, ( 8 ) means for driving the rotor at the calculated rotation frequency.
5. The device for conditioning of hydrocarbon fluids according to claim 4, wherein the radius R of the cylindrical outer surface of the peripheral annular wall of the working wheel constitutes R = 1.1614 K (mm), where K is the selected number of the outlet openings of the working wheel, while the radial size .DELTA.R of the circular constitutes .DELTA.R = 1.1614 B (mm), where B is the selected integer in the range of 1 ... K/5.
6. The device for conditioning of hydrocarbon fluids according to claim 5, wherein (1) the stator has a space adjoining the concentric wall thereof for fluid intake from the circular chamber, said space communicating with the discharge opening for discharge of the fluid, at which (2) the stator space communicates with the circular chamber through the discharge openings, made in the stator concentric wall in the arrangement plane of the outlet openings of the working wheel and equidistant along the circumference, (3) the number of the discharge openings of the circular chamber constitutes 1 .... K.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002218591A CA2218591A1 (en) | 1995-04-18 | 1995-04-18 | Method of conditioning of hydrocarbon fluids and device for embodiment thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002218591A CA2218591A1 (en) | 1995-04-18 | 1995-04-18 | Method of conditioning of hydrocarbon fluids and device for embodiment thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2218591A1 true CA2218591A1 (en) | 1996-10-24 |
Family
ID=4161648
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002218591A Abandoned CA2218591A1 (en) | 1995-04-18 | 1995-04-18 | Method of conditioning of hydrocarbon fluids and device for embodiment thereof |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA2218591A1 (en) |
-
1995
- 1995-04-18 CA CA002218591A patent/CA2218591A1/en not_active Abandoned
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| FZDE | Discontinued |