CN2037265U - Herringbone blade separating parts and separator - Google Patents
Herringbone blade separating parts and separator Download PDFInfo
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- CN2037265U CN2037265U CN 88206670 CN88206670U CN2037265U CN 2037265 U CN2037265 U CN 2037265U CN 88206670 CN88206670 CN 88206670 CN 88206670 U CN88206670 U CN 88206670U CN 2037265 U CN2037265 U CN 2037265U
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Abstract
The function of centrifugal force is used by the utility model to separete dispersed particles from gases. The utility model discloses a chevron-shaped blade separating component and the separator of the chevron-shaped blade separating component which can be used singly and can also be used by being matched with the separators of other patterns. The chevron-shaped blade separating component and the separator of the chevron-shaped blade separating component can be arranged in equipment or out of the equipment, can be used for gas-liquid or gas-solid separation works and can be made of metallic or non-metallic materials according to the requirements. The utility model has the advantages of simple manufacturing process, compact structure, high efficiency and cabinet appearance. The long-standing problem of low separation efficiency under the state of high voltage is solved. The chevron-shaped blade separating component and the separator of the chevron-shaped blade separating component is suitable for the requirements of gas-liquid or gas-solid separation works of various industries and home application such as the chemical engineering, the metallurgy, the thermal power generation, etc.
Description
Chevron shaped blade separating component of the present invention and separator thereof separate dispersed granules by action of centrifugal force from gas, it belongs to the improvement of cyclone separator.
Precipitation of liquid droplets or to remove the method for dust a lot of from gas, common method has: cyclonic separation, cloth bag filtration, wet film dedusting, refill (or steel wool core) filter, electrostatic precipitation (or demist) or the like.In these methods, can be divided into three fundamental types according to the operating principle of separator: (1) inertia type; (2) centrifugal type; (3) surface type.Yet neither one is that a kind of operation principle of simple utilization is as separating the basis in the separator of practical application.And prior art is very not enough to the research of separator operation principle, particularly their computational methods.The centrifugal type separator is an exception, equally calculate because it can shine cyclone separator, but such calculating also is very approximate.Seeing prior art " the 4th joint separator ", Soviet Union expert A. Д. the Shi Niefu of the Congress writes, and " chemical production machinery and equipment " first volume is translated by Dalian Polytechnic College chemical production machinery and equipment teaching and research room, the publication P234 of Chemical Industry Press～239(1957).Although the extensive use on industrial production of these separation methods also has the more special place of some process conditions, do not resolve the problem of precipitation of liquid droplets or dedusting so far, bring many difficulties to industrial production, for example:
1. the steamdrum exit of steam boiler, an original scroll casing type steam-water separator, the water surface of distance boiling is very near, often because of reasons such as water-drop sputterings, has a large amount of moisture content to enter spiral case in company with steam.When moisture content was too much, separator had little time moisture content is separated, and is brought into jet chimney by steam again.In China, small and medium ammonia synthesis plant all is to be with water saturation steam suddenly with this, directly imports in the reburner, to produce hydrogen.After moisture content entered reburner, the furnace temperature rapid drawdown caused the underproduction.The long-term steam of this band water that uses can cause vanadium catalyst pollution, caking in the reburner again, its performance, life-span is descended greatly, and cause the production capacity of system to reduce.
2. the steam boiler of heat power station is to export saturated vapor by steamdrum earlier, becomes superheated steam after superheat section is overheated, transports to steam turbine.When carrying small amount of moisture secretly in the saturated vapor, superheat section can be with these moisture content vaporizations.If once be with dilutional hyponatremia in the saturated vapor, superheat section has little time whole vaporizations, just has residual water and drips by entrainment with steam in steam turbine.The turbine blade of high-speed cruising runs into this water droplet, is totally unfavorable.Check long-term postrun turbine blade, usually find the phenomenon of being wounded by water droplet.Therefore station boiler also has necessity of improving the steamdrum steam-water separator.
3. the copper washing section of synthesis ammonia plant is with cuprammonia the nitrogen hydrogen under more than 100 atmospheric pressure to be cleaned, and removes pernicious gases such as wherein micro amount of oxygen, carbon monoxide.The exit of cuprammonium washing tower for removing CO is originally that the method for filtering with steel wool stops copper liquid to enter pipeline with air-flow.This filter method effect is bad, " copper tower band liquid " problem often occurs, to the back operation, causes very big threat.
4. traditional hydraulic oil separator, the air velocity of air inlet are 12～15 meter per seconds often, enter separator after, the speed of gas reduces, the droplet in the gas since the effect of gravity gradually sedimentation realize the separation of gas-liquid., gas under high pressure, density is very big, in turbulent motion, these factors are all very unfavorable to natural subsidence again for most gas molecule, so the separation equipment under the high pressure such as oil separate or the ammonia separation equipment also has improved necessity very much.
For overcoming the deficiencies in the prior art, seeking a kind ofly has basis, efficient and simple in structure, working service to remove liquid or cleaner easily, the invention provides a kind of chevron shaped blade separating component (abbreviation separating component) and separator thereof, it can be made according to different process conditions specific designs, thereby can guarantee efficient separation under various operating conditions to have solved long-standing difficult problem.
With several angle steel, channel-section steel or the pipe cut open by row's vertical parallel in the same way and by certain being spaced, shaped steel in adjacent two rows is staggeredly located, be fixed in gas-liquid separate component and the separator thereof formed on base plate and the top board, it is characterized in that, described shaped steel is a kind of chevron shaped blade, chevron shaped blade is also arranged at regular intervals by row's vertical parallel, per two row's chevron shaped blades are one group, two row's chevron shaped blade placement directions in same group are opposite, and second row's everyone the shaped blade both sides adjacent with two chevron shaped blades of last row are fastened mutually, chevron shaped blade is fixed in the framework of being made up of four blocks of sheet materials that has the viscous flow baffle plate, form a chevron shaped blade resolution element (abbreviation resolution element), a resolution element is made up of one group of (or two rows) chevron shaped blade at least, resolution element is formed a chevron shaped blade separating component (abbreviation separating component) with base and top cover, the import UNICOM of the import of separating component and resolution element, the outlet UNICOM of the outlet of separating component and resolution element, separating component or resolution element are installed in the container that has gas inlet and outlet and floss hole, promptly constitute a chevron shaped blade separator; Separating component also can place device interior to use, at this moment, the outlet of separating component connects with the outlet of equipment, the import of separating component and floss hole can be simplified, make first component among the import side of element directly is exposed to the gas of this equipment, the connecting mode of separating component and equipment can adopt welding, riveted joint or Bolt Connection; Separating component can also and the supporting use of separator of other form, form a composite separator; Be simplified structure, also can replace resolution element to form separating component or separator with chevron shaped blade in groups.
In the chevron shaped blade resolution element, a resolution element is made up of one group of (or two rows) chevron shaped blade at least, between every row's chevron shaped blade, and blade all leave suitable gap between row and row, the gap of adjacent two blades of first row is over against the top at the angle of second chevron shaped blade that be interlocked with it of row, air-flow flows into from the gap of first row's blade, run into stopping of second row's blade drift angle, change direction, along first, two liang of two channel flow that the limit forms respectively that row's respective vanes is formed, run into the stopping of drift angle of first row's blade again, flow out by the gap location of second row's blade.When gas changed direction at the drift angle place, droplets entrained or dust in the gas were separated by action of centrifugal force.Aggregation is at the drift angle place, and then along the blade longitudinally, vertical decline discharged up to the framework bottom.
First row's blade of resolution element is an inlet end face, and second row's blade is an exit end face.In the Lower Half of exit end face, the viscous flow baffle plate is installed, the viscous flow baffle plate blocks the Lower Half air-flow of resolution element, and speed reduces, and becomes the stagnant area.When blade comes out drop in the air-flow or dust separation, along the blade vertical landing, when entering the stagnant area, because of air velocity reduces, can safe falling, no longer include the danger that is blown away again by air-flow.Separated drop or dust are discharged to the bottom of separating component or separator through the fluid-tight baffle plate, get rid of through tap then.
On the basis of double-row blades, increase row's number of blade, make air-flow through baffling repeatedly, separating for several times is carried out in changed course, just becomes the multiple blade rows resolution element.
Outline drawing about the chevron shaped blade resolution element is seen Fig. 1, wherein, and 1 framework, 2 first row's chevron shaped blades, 3 second row's chevron shaped blades, 4 viscous flow baffle plates; Fig. 2 is the side view of double chevron shaped blade resolution element, and Fig. 3 is the AA cutaway view of Fig. 2; Fig. 4 is the side view of many row's chevron shaped blade resolution elements, and Fig. 5 is the BB cutaway view of Fig. 4.
Resolution element is formed a separating component with base and top cover.The import of separating component communicates with the import of resolution element, and the outlet of separating component communicates with the outlet of resolution element.
Be simplified structure, also can replace resolution element to form separating component or separator with chevron shaped blade in groups.
See Fig. 6 and Fig. 7 about " chevron shaped blade separating component ",
Fig. 6 is the single-stage chevron shaped blade separating component, wherein: 1 base, 2 resolution elements, 3 top covers
Fig. 7 is the secondary chevron shaped blade separating component, and wherein: 1 base, 2 one-level resolution elements, 3 secondarys separate resolution element, 4 top covers
When using the multi-stage separation parts to carry out gas-liquid or gas solid separation operation, wherein the resolution element of same gas flow velocity is called one-level, in same separating component, can use the above resolution element serial or parallel connection of one-level, separate in the parts in same level, can adopt identical or different resolution element serial or parallel connection.
In separating component, the effective ventilation area F(millimeter of resolution element
2) be:
F=n(H-h
1) e (millimeter
2)
In the formula: the slit number of n one row's blade
H blade height overall (millimeter)
h
1Viscous flow baffle plate height (millimeter)
E slit width (millimeter)
Gas can be selected different speed for use according to different process conditions by the speed of resolution element.The flow velocity of gas is high more, and centrifugal force suffered when the blade drift angle place that flows through changes direction is just big more, and under normal circumstances separative efficiency is just high more.
In actual applications, can select single-stage or multi-stage separation parts for use according to the process conditions and the needs of medium, and be assembled into corresponding chevron shaped blade separator.For example, the capacity of containers such as the top of scrubbing tower, boiler steamdrum is converted into flow on this container flow break-make face, its flow velocity is very low.But when gas arrives this outlet of container pore, immediately with flow at high speed (flow velocity of general pipeline is about 10 meter per seconds).At the outlet of container place, gas is become at a high speed by low speed, will produce a dust catcher effect, drop that can those low speed flow bands are motionless or dust suction outlet pipe pore.For example, in the time of near the process outlet pore, will change the direction of motion, be inhaled into outlet just at the drop or the dust of sedimentation.In addition, because the interaction of various media in the container drop often occurs and splashes, or the solid particle phenomenon of being got up by throwing.These splash or by the particle of throwing, also are that the low speed flow band is motionless originally, and they can jump into the outlet pore by the effect of external force, then by high velocity gas stream.This class container exit should be selected multistage chevron shaped blade separator for use, and its first order resolution element can be selected the low speed flow resolution element for use.
Separating component or the chevron shaped blade separator that is assembled into by it can become cylindrical separating component or chevron shaped blade separator designs or cube, perhaps other various forms according to the requirement of installation site.When on the circumference of cylindrical separating component, disposing resolution element, can evenly distribute along circumference, also can be interrupted distribution, the layout orientation of adjacent two-stage resolution element can stagger mutually, the profile of resolution element can be made thin box-shaped or tile fragment shape, and the chevron shaped blade in the tile fragment shape resolution element is arranged along circular arc line.As Fig. 6 and Fig. 7 is the separating component of cylinder type.Cuboidal separating component can be made by the resolution element serial or parallel connection that as shown in Figure 1 double or many rows' chevron shaped blade is formed.
Separating component of the present utility model can be selected suitable material for use according to concrete process conditions, makes as metal, plastics, fiberglass, high temperature resistant and/or corrosion resistant masonry etc.
In chevron shaped blade separating component, the chevron shaped blade that constitutes resolution element can have different forms, has provided the sectional drawing of the chevron shaped blade of five kinds of patterns commonly used as Fig. 8-12
Fig. 8 is ordinary people's shaped blade sectional drawing
Fig. 9 is the chevron shaped blade sectional drawing that has catch tank
Figure 10 is a broadside chevron shaped blade sectional drawing
Figure 11 is an ordinary masonry chevron shaped blade sectional drawing
Figure 12 is the masonry chevron shaped blade sectional drawing that has catch tank
In Fig. 8-12:
A be chevron shaped blade drift angle (°)
B is the width (millimeter) of chevron shaped blade
C is the length of side (millimeter) of chevron shaped blade
In actual use, can select the blade of different types for use according to the difference of process conditions.For example, if droplets entrained is too many or dust is too light in the air-flow, drop of having separated or dust, when the drift angle place that concentrates at blade vertically descended, the danger that has the air-flow that blown later to take away again can be selected the chevron shaped blade of band catch tank for use.
The resolution element that the broadside blade is formed, long slype is arranged, when gas passes through slype with turbulence state, according to the molecular collision theory, the mist of oil particulate easily and channel side wall collide, and be attached on the wall, make blade separator when carrying out centrifugation, produce again and remove fog effect.Improve the separating effect of synthetic ammonia hydraulic oil separator as selecting broadside chevron shaped blade isolation technics for use.
The chevron shaped blade that in separating component or resolution element, uses, its apex angle is 0～120 °, when adopting tile fragment type resolution element, when blade is arranged along circular arc, be α away from the drift angle of the blade in the center of circle, the drift angle of then adjacent with it nearly lobus cardiacus sheet is an alpha+beta, β equals the corresponding angles in the width of blade b and the center of circle, the length of side of blade is 10～350 millimeters, and vane thickness is 0.3～200 millimeter, and blades height is selected according to actual needs.Also can select the chevron shaped blade that has catch tank for use, the section configuration of its catch tank can be square, rectangle or circle, the manufacturing of chevron shaped blade can adopt pressing or casting to make, need corrosion-resistant or resistant to elevated temperatures separator for some, the gas-solid separator of gas burner exit gas for example, the chevron shaped blade in the separating component can select for use the masonry structure of block refractory material to make.
In separating component, in the bottom of resolution element air inlet side, the fluid-tight baffle plate can be installed, the viscous flow baffle plate of resolution element is installed in the bottom of exhaust side.When the height of chevron shaped blade is H, the height h of viscous flow baffle plate
1=(0.2～0.5) H, the height h of fluid-tight baffle plate
2=(0.05～0.1) H.
The discharge opeing ability can be improved in root of blade and the perforate of framework connection place or the crack or with the blade bed hedgehopping of cracking in the bottom of chevron shaped blade resolution element.When the chevron shaped blade resolution element was used for dedusting, the base plate of the base of framework and the separating component be made up of this resolution element can make the inclined plane, so that banish dust.
The container floor of the chevron shaped blade separator of being made up of chevron shaped blade separating component can be made the stairstepping base, utilizes the vertical plane of ladder to replace the viscous flow baffle plate of resolution element.As the cylindrical separating component of Fig. 7 secondary, the formed ladder of the potential difference between the two-stage resolution element is promptly as the viscous flow baffle plate of previous stage resolution element.In addition, the catch tank of chevron shaped blade, its sectional area can strengthen, so that in groove, add high-voltage conducting wires, or the pectination arresting element, or spray thrower, utilize charge inducing, or ion wind, or humidification improves dedusting or removes fog effect.
Separating component of the present invention can be used for gas-liquid separation or gas solid separation operation.
Chevron shaped blade separating component and separator thereof are that droplets entrained or dust are separated by action of centrifugal force in the gas when utilizing the gas revolution to flow.Its operation principle is identical with cyclone separator.Compare with cyclone separator, the present invention has following advantage:
1. under low gas flow rate, can guarantee the high efficiency of centrifugation.
The cyclone separator of industrial use is usually used in dedusting.The radius of curvature R that air-flow circles round when flowing is different with the diameter of separator, and the diameter of separator is usually in 200～1000 millimeters scopes.Indivedual particular design, the radius of curvature R value can reach 50 millimeters.
The radius of curvature R value of chevron shaped blade separator is minimum, is generally 5～10 millimeters, and minimum of a value can be 1 millimeter.The ratio of cyclone separator and the radius of curvature R value of chevron shaped blade separator can be thought to differ about 50 times.
The formula of centrifugal force can be written as:
F＝ (m V
2)/(R)
When the particle of carrying secretly in the air-flow was definite value, m was a definite value, and required minimum centrifugal force F also is a certain value.At this moment, the R value is more little, and required air velocity V value is more little.
Suppose the R of cyclone separator
1=50 millimeters, V
1=12 meter per seconds, so, the R of blade separator
2=1 millimeter, V then
2=1.68 meter per seconds can guarantee identical separative efficiency.
2. airflow layer thickness is little in chevron shaped blade separating component and the separator thereof, the separative efficiency height.
The airflow layer thickness of cyclone separator is determined by channel width between shell and the central tube.The airflow layer thickness of single entry cyclone separator is 100～500 millimeters, and the airflow layer thickness of multicyclone is 3 0～100 millimeters.The airflow layer thickness of chevron shaped blade separator, nonmetal blade can be decided to be 50～100 millimeters, and sheet metal punching press blade can be decided to be 1～3 millimeter.The ratio of cyclone separator and the airflow layer thickness of chevron shaped blade separator can be thought to differ about 20 times.
Air-flow droplets entrained or dust under action of centrifugal force, will move along the direction of centrifugal force.Airflow layer thickness is more little, and required mobile distance is short more, and therefore, the separative efficiency of chevron shaped blade separator is than whirlwind separator height.
3. chevron shaped blade separating component and separator thereof can take various ways to improve separative efficiency, and cyclone separator can not be taked similar measure.
(1) low speed resolution element and high-speed separation element can be together in series and become multistage chevron shaped blade separator.
(2) can adopt the blade that has catch tank.
(3) can adopt the stagnant area baffle, keep liquid or dust safety to descend.
4. before can being installed in the outlet of internal tank gas, the simplified apparatus structure, handled easily, cyclone separator is installed under kindred circumstances then following difficulty:
(1) when the outlet of cyclone separator connects with the mouth of pipe of container outlet pipe, other mouth of pipe of cyclone separator then all is exposed in the middle of the atmosphere of internal tank as gas feed, liquid or dust outlet, very easily becomes short circuit, causes discharge opeing row powder difficulty.
(2) import department of cyclone separator will produce the dust catcher effect.On the contrary, the chevron shaped blade separator is installed before the outlet conduit of internal tank, can be solved these difficulties.
5. the minimum gas of flow, cyclone separator can not be handled, and the chevron shaped blade separator can solve.For example, the gas-liquid separation problem under the ammonia production system mesohigh.
In addition, the present invention compares with foregoing prior art, and its advantage is also given prominence to.The preparation of foregoing employing shaped steel is used for the separating component and the separator thereof of gas-liquid separation operation, under the situation that requires processed gas velocity≤0.3 meter per second mainly is to utilize the surface area contacted size of its gas-liquid to guarantee the height of separative efficiency.Thereby, under the certain situation of process conditions, guarantee that separative efficiency is higher, the one, requirement gas speed is low, and the 2nd, the requirement contact surface is long-pending big, and the volume of separator also will be greatly and heavy, and the cost raising.What in fact separator can not be done is excessive, thereby the efficient of its separator operation is generally not really desirable.
In sum, chevron shaped blade separating component of the present invention and separator thereof are a kind of more satisfactory gas-liquid or gas-solid separation equipments in industry at present and the civilian production.
Be embodiments of the invention below
The chevron shaped blade separator that 500 millimeters cuprammonium washing tower for removing CO inner tops of one: 5000 ton/year synthesis ammonia plant φ of embodiment are installed
This separator is mounted in a secondary plain vane separating component of cuprammonium washing tower for removing CO inner top.The outlet of separating component is connected with the outlet of cuprammonium washing tower for removing CO, and the inlet of separating component and leakage fluid dram are exposed to the inside of cuprammonium washing tower for removing CO.Separating component adopts Bolt Connection with connecting of tower.In this secondary separating component:
Separating component height overall: 400 millimeters:
300 millimeters of one-level resolution element barrel diameter: φ
200 millimeters of secondary resolution element barrel diameter: φ
Gas speed: V in the one-level resolution element
1=1 meter per second
Gas speed: V in the secondary resolution element
2=4 meter per seconds
Every grade is separated one group of installation chevron shaped blade (two rows) in the element
Chevron shaped blade height: H=160 millimeter
Viscous flow baffle plate height: h
1=60 millimeters
Viscous flow baffle plate effective length: 100 millimeters
The configuration slit is 12 on the one-level resolution element
The configuration slit is 6 on the secondary resolution element
Blade shape: ordinary people's shaped blade
Vane thickness: 1.2 millimeters
Width of blade: 25 millimeters
First row's blade drift angle: the α in the two-stage resolution element
1=α
2=60 °
The correction angle β of blade in the one-level resolution element
1=10 °
The correction angle β of blade in the secondary resolution element
2=15.6 °
500 millimeters cuprammonium washing tower for removing CO chevron shaped blades of φ separator schematic diagram is seen Figure 13.Wherein, 1 base, 2 one-level resolution elements, 3 secondary resolution elements, 4 safety valves, 5 top covers, 6 gas accesses, 7 gas vents.
Use the comparison of separating component in φ 500 millimeters cuprammonium washing tower for removing CO chevron shaped blades separator and the former design of this tower:
Separating component in the former design of cuprammonium washing tower for removing CO, the employing steel wool filter that has, what have changes steel wool into Pall ring, and changes its title into demister, separator or the like.These are several all to be the principle that adopts filter, with the drop in the divided gas flow.
Copper is washed operation and is carried out in high-pressure bottle, and the physical and chemical performance of gas, liquid all changes to some extent, and cuprammonia may produce precipitation, also may be by oil pollution.Just at operating cuprammonia, may be with hanging drop, splash droplet, foam, variforms such as liquid flooding are in company with giving birth on the air-flow.After ascending liquid enters filter course, may be attached to above the filtering material, the surface area of filtering material is big more, and the liquid that adheres to is many more, adds capillary effect, and this part liquid no longer refluxes.During when filtering material with attached to the liquid lock tower internal channel on the filter material, gas will promote liquid to be continued to rise, and until tower top outlet, forms " band liquid " phenomenon.
The bottom filler is to there being one section void tower between the separator of top in the cuprammonium washing tower for removing CO, and this section void tower itself just has good gas-liquid separation effect, and for example splash droplet or the froth bed certain altitude that all can only rise in void tower just will land or top out.If filter is oversize, void tower is shortened, just may weaken the work of separation usefulness of void tower, make filter become the ladder that drop rises, play the effect that relay is guided and supported.
Cuprammonium washing tower for removing CO adopts the chevron shaped blade separator, is the principle of utilizing whirlwind, with centrifugal force drop is separated by force.The chevron shaped blade separator has the maturity of cyclone separator, reliability, and high efficiency and do not need more renew cartridge or the like advantage has overcome the shortcoming that cyclone separator can not be installed and used simultaneously again in container.The chevron shaped blade separator is minimum with the surface area that gas, liquid contact, can not be at the big quantity of fluid of its surface attachment.The height of chevron shaped blade separator is also very little, replaces original filter with it, can make the void tower height increase by 300～1000 millimeters.Therefore, at the cuprammonium washing tower for removing CO top chevron shaped blade separator is installed and is improved gas-liquid separation efficient, solve the band liquid problem of cuprammonium washing tower for removing CO preferably.
Install the chevron shaped blade resolution element (4) of a low flow velocity at the spiral case inlet place of former K boiler steamdrum scroll casing type steam-water separator (1) additional, see Figure 14, the motionless moisture content of low speed steam flow band such as the water droplet that splashes are separated.Add at the spiral case inlet place again an import water fender (3) make steam flow with higher speed along spiral case inwall eddy flow, will remain water droplet and separate, be collected at the spiral case bottom.Add a following water fender (2) in the spiral case bottom again and prevent that ponding from being taken away by steam flow.Its blade one spiral case composite air flow separator and relevant physical dimension thereof are as follows:
K
41000 millimeters of boiler-steam dome diameter: φ
K
4Boiler-steam dome length: 4000 millimeters
108 millimeters of main steam range diameter: φ
Scroll casing separator height: 200 millimeters
Scroll casing separator is long: 640 millimeters
The chevron shaped blade resolution element adopts one-level to separate
Gas flow rate in the resolution element: V=3 meter per second
The profile of resolution element: thin square type
Resolution element height: 180 millimeters
Resolution element is wide: 60 millimeters
Resolution element is long: 640 millimeters
Viscous flow baffle plate height: 68 millimeters
Blade shape: ordinary people's shaped blade
Blade drift angle: α=60 °
Vane thickness: 3 millimeters
Width of blade: 40 millimeters
Slit width degree between blade: 10 millimeters
Resolution element intra vane row number: 2 rows
Every row's number of blade in the resolution element: 13
Resolution element adopts Bolt Connection with connecting of spiral case.
Former scroll casing separator through on probation on the K boiler, and a container-type separator being installed to observe water entrained by steam situation behind separator of the present invention in the main steam range, is observed through half a year after transforming blade-spiral case composite separator as more, does not find band water.
Description of drawings
Fig. 1. chevron shaped blade resolution element outline drawing.
Wherein: 1 framework, 2 first row's chevron shaped blades, 3 second row's chevron shaped blades, 4 viscous flow baffle plates
The double chevron shaped blade resolution element of Fig. 2 side view
The AA cutaway view of Fig. 3 Fig. 2
Fig. 4 arranges chevron shaped blade resolution element side view more
The BB cutaway view of Fig. 5 Fig. 4
Fig. 6 single-stage chevron shaped blade separating component
Wherein: 1 base, 2 resolution elements, 3 top covers
Fig. 7 secondary chevron shaped blade separating component
Wherein: 1 base, 2 one-level resolution elements, 3 secondary resolution elements, 4 top covers
Fig. 8 ordinary people's shaped blade sectional drawing
Fig. 9 has the chevron shaped blade sectional drawing of catch tank
Figure 10 broadside chevron shaped blade sectional drawing
Figure 11 ordinary masonry chevron shaped blade sectional drawing
Figure 12 has the masonry chevron shaped blade sectional drawing of catch tank
Among Fig. 8-12:
A is the drift angle (degree) of chevron shaped blade
B is the width (millimeter) of chevron shaped blade
C is the length of side (millimeter) of chevron shaped blade
500 millimeters cuprammonium washing tower for removing CO chevron shaped blades of Figure 13 φ separator
Wherein: 1 base, 2 one-level resolution elements, 3 secondary resolution elements, 4 safety valves, 5 top covers, 6 gas accesses, 7. gas vent
Figure 14 blade-spiral case combined gas-liquid separator
Wherein: 1. the scroll casing type steam-water separator partly
2. descend water fender
3. import water fender
4. chevron shaped blade resolution element
Claims (6)
1, with several angle steel, channel-section steel or the pipe that is broken away are arranged in the same way at regular intervals by row's vertical parallel, shaped steel in adjacent two rows is staggeredly located, be fixed in gas-liquid separate component and the separator thereof formed between base plate and the top board, it is characterized in that, described shaped steel is a kind of chevron shaped blade, chevron shaped blade is arranged at regular intervals by row's vertical parallel, per two row's chevron shaped blades are one group, two row's chevron shaped blade placement directions in same group are opposite, and second row's everyone the shaped blade both sides adjacent with two chevron shaped blades of last row are fastened mutually, chevron shaped blade is fixed in the framework of being made up of four blocks of sheet materials that has the viscous flow baffle plate, form a chevron shaped blade resolution element (abbreviation resolution element), a resolution element is made up of lineup's shaped blade at least, resolution element is formed a chevron shaped blade separating component (abbreviation separating component) with base and top cover, the import UNICOM of the import of separating component and resolution element, the outlet UNICOM of the outlet of separating component and resolution element, separating component or resolution element are installed in the container that has gas inlet and outlet and floss hole, promptly constitute a chevron shaped blade separator; Separating component also can place device interior to use, at this moment, the outlet of separating component connects with the outlet of equipment, the import of separating component and floss hole can be simplified, make first component among the import side of element directly is exposed to the gas of this equipment, separating component can adopt welding, riveted joint or nut to connect with the connecting mode of equipment; Resolution element or separating component can also and the supporting use of separator of other form, form a composite separator; Be simplified structure, also can replace resolution element to form separating component or separator with chevron shaped blade in groups.
2, by the described separating component of claim 1, it is characterized in that, the resolution element of same gas flow velocity is called one-level, in same separating component, can use the above resolution element serial or parallel connection of one-level, separate in the parts in same level, can adopt resolution element serial or parallel connection identical or inequality.
3, by the described separating component of claim 1, it is characterized in that, the external form of described separating component can be a cube or cylindrical, when on the circumference of cylindrical separating component, disposing resolution element, can evenly distribute along circumference, also can be interrupted distribution, the layout orientation of adjacent two-stage resolution element can stagger mutually, the profile of resolution element can be made thin box-shaped or tile fragment shape, and the chevron shaped blade in the tile fragment type resolution element is arranged along circular arc line.
4, by the described separating component of claim 1, it is characterized in that separating component can be selected suitable material for use according to concrete process conditions, make as the masonry of metal, plastics, fiberglass, high temperature resistant and/or resistant material etc.
5, by the described separating component of claim 1～4, it is characterized in that, the apex angle of described chevron shaped blade is 0～120 °, when adopting tile fragment shape resolution element, when blade is arranged along circular arc, drift angle away from the blade in the center of circle is α, the drift angle of adjacent with it nearly lobus cardiacus sheet is an alpha+beta, β equals the corresponding angles in the width of blade and the center of circle, the length of side of blade is 10～350 millimeters, vane thickness is 0.3～200 millimeter, the length of blade is selected according to actual needs, also can select the chevron shaped blade that has catch tank for use, and the section configuration of its catch tank can be square, rectangle or circle, the manufacturing of chevron shaped blade can adopt pressing or casting to make, and also can adopt masonry structure.
6, by the described separating component of claim 1～4, it is characterized in that, at the air inlet side lower part of its resolution element, the fluid-tight baffle plate can be installed, the viscous flow baffle plate of resolution element is installed in the bottom of exhaust side, when the height of chevron shaped blade is H, the height h of viscous flow baffle plate
1=(0.2～0.5) H, the height h of fluid-tight baffle plate
2=(0.05～0.1) H, the base plate of separating component can be made the stairstepping base, utilizes the viscous flow baffle plate of the vertical plane replacement resolution element of ladder, also the inclined plane can be made in the base of resolution element framework and the base plate of separating component, so that the rolling dust.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88206670 CN2037265U (en) | 1988-06-10 | 1988-06-10 | Herringbone blade separating parts and separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88206670 CN2037265U (en) | 1988-06-10 | 1988-06-10 | Herringbone blade separating parts and separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2037265U true CN2037265U (en) | 1989-05-10 |
Family
ID=4840821
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 88206670 Expired - Lifetime CN2037265U (en) | 1988-06-10 | 1988-06-10 | Herringbone blade separating parts and separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2037265U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102091493A (en) * | 2010-12-23 | 2011-06-15 | 中色科技股份有限公司 | Combined type method and device for air-liquid separation and purification |
| CN106194842A (en) * | 2016-09-05 | 2016-12-07 | 艾雅迪国际有限公司 | The wind cycling mechanism of air-cooler |
| CN108786367A (en) * | 2018-08-31 | 2018-11-13 | 中冶北方（大连）工程技术有限公司 | A kind of pressure drain gas-liquid separator |
-
1988
- 1988-06-10 CN CN 88206670 patent/CN2037265U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102091493A (en) * | 2010-12-23 | 2011-06-15 | 中色科技股份有限公司 | Combined type method and device for air-liquid separation and purification |
| CN106194842A (en) * | 2016-09-05 | 2016-12-07 | 艾雅迪国际有限公司 | The wind cycling mechanism of air-cooler |
| CN108786367A (en) * | 2018-08-31 | 2018-11-13 | 中冶北方（大连）工程技术有限公司 | A kind of pressure drain gas-liquid separator |
| CN108786367B (en) * | 2018-08-31 | 2023-12-12 | 中冶北方（大连）工程技术有限公司 | Forced drainage gas-liquid separator |
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