CN2589035Y - Float valve and tongue hole combined tray - Google Patents

Float valve and tongue hole combined tray Download PDF

Info

Publication number
CN2589035Y
CN2589035Y CN 02294683 CN02294683U CN2589035Y CN 2589035 Y CN2589035 Y CN 2589035Y CN 02294683 CN02294683 CN 02294683 CN 02294683 U CN02294683 U CN 02294683U CN 2589035 Y CN2589035 Y CN 2589035Y
Authority
CN
China
Prior art keywords
tongue
float valve
otch
liquid
tongue hole
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 02294683
Other languages
Chinese (zh)
Inventor
潘国昌
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing Zehua Chemical Engineering Co ltd
Original Assignee
Beijing Zehua Chemical Engineering Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Beijing Zehua Chemical Engineering Co ltd filed Critical Beijing Zehua Chemical Engineering Co ltd
Priority to CN 02294683 priority Critical patent/CN2589035Y/en
Application granted granted Critical
Publication of CN2589035Y publication Critical patent/CN2589035Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The utility model relates to a float valve and tongue hole combined column tray, which relates to a device which is used for processes of distillation and absorption in oil refining and chemical industry. The main technical feature of the utility model is that a column tray which is arranged between two adjacent circular float valves is upwards punched with a row of tongue holes or notches which are provided with tongue pieces; the jetting direction of each row of tongue holes or notches is consistent, wherein, the jetting direction of each row of tongue holes or notches is perpendicular to the flowing direction of liquid, and the jetting direction two adjacent rows of tongue holes or notches are contrary or the jetting direction of a plurality of rows of tongue holes or notches is the same with the flowing direction of the liquid. Compared with the existing float valve column tray, the opening ratio of the column tray is enlarged, the speed, the voltage drop and the entrainment of valve holes are reduced, the stay time of the liquid on the column tray is extended, the exchange and the mixture of the liquid in the direction which is perpendicular to the flowing direction of the liquid, stagnation regions arranged on both sides of the column tray are eliminated, the height of a foam layer is dropped, and therefore, the efficiency and the productivity of the column tray is effectively raised.

Description

Float valve-tongue hole combined tray
Technical field
The utility model relates to a kind of equipment that is used for oil, chemical industry distillation, absorption process, the structural design of particularly a kind of float valve-tongue hole combined tray.
Background technology
Tower tray is the visual plant that separates homogeneous mixture, and its performance plays great influence to the output of products of separated, quality, energy consumption, cost etc.In existing tower tray technology, circular float valve (float valve that comprises traditional F1 type float valve and valve face band tongue hole) has obtained to use the most widely, but have following defective: it is in working order the time, gas under the type valve block of garden in horizontal direction to around spray, the air-flow of adjacent each valve ejection liquidates mutually, not only aggravates Wu Droplets and carries secretly, and brought radially back-mixing of liquid phase, arc area on this external column plate forms and refluxes and stagnant areas, as shown in Figure 2.These all make permissible load and plate efficiency restricted greatly, requirement such as therefore, this kind tower tray can not satisfy domestic expansion output, improve the quality.
The utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, provides a kind of float valve-tongue hole combined tray, with the last limited load and the tray efficiency of further raising tower tray.
Scheme of the present utility model is as follows: a kind of float valve-tongue hole combined tray, mainly comprise column plate, be arranged on the circular float valve of many rows, inlet weir and downspout on the column plate, it is characterized in that: on the column plate between the circular float valve of every adjacent two rows, all upwards go out a row tongue hole or an otch, tongue piece is arranged on it, the injection direction unanimity of every row's tongue hole or otch, the injection direction of wherein respectively arranging tongue hole or otch is vertical with liquid flow direction, and the injection direction of adjacent two row tongue holes or otch is opposite; Perhaps wherein there is the injection direction of plurality of rows tongue hole or otch identical with liquid flow direction.
Tongue piece described in the utility model is the half garden shape of width 10~25mm, and the tongue piece height h that upwards goes out is 2~8mm. The tongue piece of perhaps upwards going out is made up of tilting section and horizontal segment, and described horizontal segment tongue piece is semicircle, and its tongue piece width is 10~25mm, and tongue piece height h is 2~8mm.
Three of described otch link to each other with column plate, and the otch section is curved or trapezoidal, and its width is 10~25mm, and height h is 2~8mm.
Float valve provided by the utility model-ligulate tongue hole composite plate compared with prior art, has the following advantages and technological progress:
1. enlarged open ratio of plate, reduced valve opening speed, pressure drop Ji Wu Droplets carries secretly.
2. the side direction in tongue hole is sprayed, and makes that liquid layer is tending towards evenly having reduced foam layer height on the tower tray, and reduced mist Droplets and carried secretly, thus the last limited load of raising tower tray.
3. the side direction in tongue hole is sprayed, and has prolonged the time of staying of liquid on column plate, thereby improves the efficient of column plate.
4. the side direction in tongue hole is sprayed, and has strengthened exchange and mixing perpendicular to the liquid on the liquid flow direction, has eliminated the stagnant wake of column plate both sides, makes the concentration homogeneous perpendicular to the liquid flow path direction, thereby has improved plate efficiency.
Description of drawings
Fig. 1 is the structural representation of the F1 float valve of conventional art.
Fig. 2 is the liquid flow point Butut on the F1 float valve tray.
The float valve that Fig. 3 provides for the utility model-tongue hole combined tray floor map.
Fig. 4, Fig. 5 are the stereogram in tongue hole, respectively the structure in two kinds of different tongues holes upwards going out of expression.
Fig. 6 is the stereogram of the otch upwards gone out.
Fig. 7 is the macroscopical liquid flow point Butut on the combined tray of the present utility model.
The specific embodiment
Below in conjunction with drawings and Examples the structure of the present utility model and the course of work are further described.
Fig. 3 is the plane of float valve-tongue hole combined tray, and described combined tray mainly is included in column plate 32, downspout 33, the inlet weir (bubbling promoters) 35 that levels are installed in the tower shell 31 and is arranged on many rows float valve 37 on the column plate.The liquid of a last column plate flows into liquid receiving area 34, flows into bubbling area 36 through inlet weir 35.First row is tongue hole or otch 38 for tongue hole or otch 38, the three rows for float valve 37, the four rows for float valve 37, the second row in the bubbling area, but that its injection direction and second is arranged is opposite, and all the other are analogized in proper order.Do not point to the guidance quality of downspout direction as float valve, then can in bubbling area, arrange plurality of rows tongue hole identical or otch 310, to overcome the gradient of liquid level on the column plate and to lower foam layer height with the liquid flow path direction.
Fig. 4, Fig. 5, Fig. 6 are respectively the solid figure of tongue hole and otch.Tongue hole 41 among Fig. 4 is that column plate is upwards gone out half garden shape tongue piece 41, and the height h of the tip of the tongue is 2-8mm: the tongue hole 52 among Fig. 5 also is half garden shape, and its tongue piece has a horizontal segment 51, and its tip of the tongue height h is 2-8mm.
Fig. 6 upwards goes out projection 61 with column plate, and its three link to each other with column plate, and one side forms otch 62, and the otch section is curved or trapezoidal, and its width is 10~25mm, and height h is 2~8mm.
Embodiment:
In the experiment tower of diameter 1.2m, three blocks of column plates are housed, lower floor is a gas distribution grid, the middle level is a breadboard, the upper strata is the liquid foam entrainment collecting board, on column plate, adopt the nicked float valve of valve face, the performance of having tested this kind float valve-tongue hole combined tray and F1 float valve tray respectively, its technical parameter is as follows:
The wide 200mm of chord downcomer accounts for tower section 11%;
The long 890mm of exit weir, height of weir 50mm;
Air velocity 8~3.6m/s;
Discharge 0.8~112m/h;
Float valve-used tongue the hole width of tongue hole combined tray 15mm, tongue hole height 4mm.
Two kinds of tower trays are carried out contrast test under similarity condition, measured its liquid foam entrainment rate, pressure drop and oxygen desorb plate efficiency.
The contrast test data are: the liquid foam entrainment of float valve-tongue hole combined tray reduces more than 1 times than F1, upper limit stressor C b(promptly representing the production capacity of tower tray) improved 26%, and pressure drop has descended 29%, and efficient has on average improved 24%.

Claims (4)

1. float valve-tongue hole combined tray, mainly comprise column plate (32), be arranged on the circular float valve of many rows (37), inlet weir (35) and downspout (33) on the column plate, it is characterized in that: on the column plate between the circular float valve of every adjacent two rows, all upwards go out a row tongue hole or an otch, tongue piece is arranged on it, the injection direction unanimity of every row's tongue hole or otch, the injection direction of wherein respectively arranging tongue hole or otch is vertical with liquid flow direction, and the injection direction of adjacent two row tongue holes or otch is opposite; Perhaps wherein there is the injection direction of plurality of rows tongue hole or otch identical with liquid flow direction.
2. according to the described float valve of claim 1-tongue hole combined tray, it is characterized in that: described tongue piece is the half garden shape of width 10~25mm, and the tongue piece height h that upwards goes out is 2~8mm.
3. according to the described float valve of claim 1-tongue hole combined tray, it is characterized in that: the tongue piece of upwards going out is made up of tilting section and horizontal segment, and described horizontal segment tongue piece is semicircle, and its tongue piece width is 10~25mm, and tongue piece h highly is 2~8mm.
4. according to the described float valve of claim 1-tongue hole combined tray, it is characterized in that: three of described otch link to each other with column plate, and the otch section is curved or trapezoidal, and its width is 10~25mm, and height h is 2~8mm.
CN 02294683 2002-12-30 2002-12-30 Float valve and tongue hole combined tray Expired - Fee Related CN2589035Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 02294683 CN2589035Y (en) 2002-12-30 2002-12-30 Float valve and tongue hole combined tray

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 02294683 CN2589035Y (en) 2002-12-30 2002-12-30 Float valve and tongue hole combined tray

Publications (1)

Publication Number Publication Date
CN2589035Y true CN2589035Y (en) 2003-12-03

Family

ID=33752053

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 02294683 Expired - Fee Related CN2589035Y (en) 2002-12-30 2002-12-30 Float valve and tongue hole combined tray

Country Status (1)

Country Link
CN (1) CN2589035Y (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104958921A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disc-shaped flow-distributing float valve tower disc
CN104958922A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disk-shaped flow division floating valve tray
CN104958920A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disc-shaped floating valve tray
CN104958927A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disk-shaped flow division damping floating valve tray
CN104958926A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disc-shaped damping float valve tower disc
CN104958923A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disc-shaped float valve tower disc
CN112973615A (en) * 2021-03-12 2021-06-18 浙江工业大学 Mixing valve tower plate arranged in high density

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104958921A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disc-shaped flow-distributing float valve tower disc
CN104958922A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disk-shaped flow division floating valve tray
CN104958920A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disc-shaped floating valve tray
CN104958927A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disk-shaped flow division damping floating valve tray
CN104958926A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disc-shaped damping float valve tower disc
CN104958923A (en) * 2015-07-01 2015-10-07 苏州市科迪石化工程有限公司 Disc-shaped float valve tower disc
CN104958920B (en) * 2015-07-01 2017-04-12 苏州润弘贸易有限公司 Disc-shaped floating valve tray
CN112973615A (en) * 2021-03-12 2021-06-18 浙江工业大学 Mixing valve tower plate arranged in high density

Similar Documents

Publication Publication Date Title
US10384147B2 (en) Fluid dispersion unit with directional component vector
CN1066349C (en) High capacity tray for gas-liquid contact apparatus
JPH02277501A (en) Dropping part-tray assembly
CN2589035Y (en) Float valve and tongue hole combined tray
CN106110841B (en) A kind of water absorption tower of methane purification
CN201208542Y (en) Desulfuration spray tower with load regulation and flue gas flow equalizing function
US20160038851A1 (en) Method and system for orifice control of valve pressure drop
CN102861452A (en) Guiding sieve plate float valve tower
CN202410209U (en) Floating valve-tongue hole composite tray of rectification column
CN1194878A (en) Air compounded packing column plate
CN1214842C (en) Impact leakage preventing device of suspending downspout column plate
CN2484098Y (en) Efficient multi-downspout column plate
US3914352A (en) Bubble cap tray
CN204684707U (en) A kind of tongue type float valve tray
CN2805874Y (en) Tower plate with novel inlet weir
CN1142001C (en) Tower plate for gas-liquid mass transfer
CN2676997Y (en) Inclined hole tower tray used for ammonia evaporation tower
CN105944630A (en) Gas distributor and gas distribution system comprising gas distributor
CN1978023A (en) Arrange mode of vapour-liquid mass transfer floating valve tower-board
CN205360640U (en) A floating valve for plate tower
CN219848250U (en) Extraction tower for producing high-concentration hydrogen peroxide
CN2216427Y (en) Conical sieve plate gas-liquid sparger
CN111013178A (en) Stepped liquid circulation bubble tower and method for dispersing gas
CN1424125A (en) Three direction guided valve tower tray
CN1256162C (en) Vapor-liquid mixed high-efficient mass transferring tray with liquid-phase zoning cross current flow

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
DD01 Delivery of document by public notice

Addressee: Zhen Miao

Document name: Notification to Pay the Fees

DD01 Delivery of document by public notice

Addressee: Zhen Miao

Document name: Notification of Termination of Patent Right

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20031203

Termination date: 20111230