CN2594611Y - Centrifugal vapour-water separating tail-gas recovery - Google Patents

Centrifugal vapour-water separating tail-gas recovery Download PDF

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Publication number
CN2594611Y
CN2594611Y CN 02290728 CN02290728U CN2594611Y CN 2594611 Y CN2594611 Y CN 2594611Y CN 02290728 CN02290728 CN 02290728 CN 02290728 U CN02290728 U CN 02290728U CN 2594611 Y CN2594611 Y CN 2594611Y
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CN
China
Prior art keywords
vapor
water
utility
model
orifice plate
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Expired - Fee Related
Application number
CN 02290728
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Chinese (zh)
Inventor
袁龙新
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Individual
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Individual
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Priority to CN 02290728 priority Critical patent/CN2594611Y/en
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Publication of CN2594611Y publication Critical patent/CN2594611Y/en
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Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a centrifugal vapor-water separating remnant vapor recoverer, which belongs to the field of vapor steam supply matching equipment. The utility model is composed of a recoverer body, a recoverer body cover, an adjusting screw rod, an orifice plate, a guide post, etc. The utility model is characterized in that a cavity of the recoverer body is divided into a vapor-water separating chamber and a condensed water draining chamber by the orifice plate, when used vapor enters the vapor-water separating chamber from a vapor-water entering opening tangent line, a rotating separation is generated; separated condensed water enters the condensed water draining chamber from a water drain hole, thereby, entering a sealed chamber, and is drained by a drain outlet; the opening of the drain outlet can be realized by that the buoyancy of the condensation water lifts a float to make a valve core opened, and the vapor is not drained in company with the water during water drainage; the utility model solves the problems that the separation effect of a vapor-water separation valve in an existing vapor operating line is bad, and much remnant vapor is drained when the water drainage occurs, which reduces the combustion energy of a steam supply boiler furnace. Additionally, the water displacement can be automatically adjusted within a certain range according to the size of the operating vapor quantity, and is suitable for use on various operating lines which are baked by vapor. The utility model has the advantages of simple structure, convenient maintenance, convenient use, and convenient installation.

Description

Centrifugal carbonated drink is separated surplus vapour recover
Affiliated technical field:
The utility model relates to a kind of surplus vapour recover, and particularly a kind of centrifugal carbonated drink is separated surplus vapour recover, belongs to steam steam supply match equipment field.
Background technique:
At present, in the manufacture process of multiple industry, necessary operation is arranged one, to dry product exactly, the thermal source overwhelming majority of oven dry is to utilize steam to enter another container product is toasted, bake process all can produce steam water interface, has a large amount of surplus vapour to be discharged from simultaneously in the process of discharging condensed water.In order to address this problem, extensively employing mode is to load onto a carbonated drink seperating vale in drain opening, its objective is that vapour, water that baking is discharged obtain separating.But this carbonated drink seperating vale separating effect is bad, the defective that has a large amount of surplus vapour to be drained when having draining, and surplus vapour can not be recycled.The reason that produces is a unreasonable structure, cause steam water interface to enter in the valve, produce a large amount of vibrations under the pressure effect of steam, make the ball float (bucket, sheet) that ends valve poorly sealed, a large amount of gases is inevitable discharges simultaneously, existing in addition carbonated drink seperating vale also will have certain vapor pressure, the unimpeded unlatching of ability, the size of discharge capacity can not be regulated in certain scope automatically, therefore causes certain false pressure to container, have unsafe factor, energy consumption is also bigger.
Summary of the invention:
The purpose of this utility model is to provide a kind of employing centrifugal method, stops the defective of existing product, reaches carbonated drink and thoroughly separates, and surplus vapour all reclaims, and eliminates the centrifugal carbonated drink of unsafe factor and separates surplus vapour recover.
The utility model is to realize above-mentioned purpose by following technical solution.
This centrifugal carbonated drink is separated surplus vapour recover and is made up of body, the admission mouth of a river, body lid, adjusting nut, adjusting screw rod, seal washer, steam-expelling port, bolt, spring washer, sealing gasket, orifice plate, directional post, float, spool, valve core case, guide plate, closed chamber, drain opening, water-leaking hole, between valve body and the body cap sealing gasket is housed, connect by the bolt and spring washer circle, it is characterized in that: the middle part of body lid has steam-expelling port, adjusting screw rod and adjusting nut are equipped with in both sides, the lower end of adjusting screw rod is connected with orifice plate, has water-leaking hole on the orifice plate; The top of body is provided with the admission mouth of a river of carbonated drink fluid-mixing, and the bottom has drain opening; Valve core case is equipped with on drain opening top, and directional post is housed in the drain opening, and insert in the center hole of orifice plate the upper end of directional post, and guide plate is equipped with in the lower end, has water-leaking hole on the guide plate, and spool and float and closed chamber are equipped with in the middle part of directional post.
The utility model compared with prior art has following beneficial effect:
The steam water interface that this centrifugal carbonated drink is separated surplus vapour recover enters owing to tangent line, self pressure high speed rotating, steam thoroughly separates, surplus vapour reclaims mouth to be separated with drain opening, the problem that the surplus vapour that flows out when thoroughly having solved draining can not be recycled has been saved the energy of steam widely, and steam is fully used, thoroughly eliminate false the pressure, got rid of unsafe factor.Along with the size of steam consumption can be regulated water displacement automatically in certain scope, and discharging thoroughly.It is simple in structure that this centrifugal carbonated drink is separated surplus vapour recover, installation, use, easy to maintenance.
Description of drawings:
Accompanying drawing is the structural representation that centrifugal carbonated drink is separated surplus vapour recover.
Among the figure: 1 body, the 2 admission mouths of a river, 3 bodies lid, 4 adjusting nuts, 5 adjusting screw rods, 6 seal washers, 7 steam-expelling ports, 8 bolts, 9 spring washers, 10 sealing gaskets, 11 orifice plates, 12 directional posts, 13 floats, 14 spools, 15 valve core cases, 16 guide plates, 17 drain opening, 18 water-leaking holes, 19 closed chambers.
Embodiment:
The utility model is separated by carbonated drink and discharging condensed water two-part constitute, and is provided with surplus vapour and reclaims outlet, condensate drain outlet and prevent that surplus vapour is to the vibrative orifice plate of float and prevent that surplus vapour from entering the closed chamber of drain opening.Its working principle is that the carbonated drink fluid-mixing that roasting plant is discharged reaches carbonated drink separation through centrifugal action, adopts the interlock of float and spool to open and close, and condensed water becomes the U type to discharge through closed chamber, and surplus vapour is recycled.Simultaneously, the supporting gate valve of surplus vapor outlet can be done single drain valve use.
The body (1) that this centrifugal carbonated drink is separated surplus vapour recover is connected with bolt (8) by spring washer (9) with body lid (3), sealing gasket (10) is equipped with for anti-leak-stopping vapour in the junction, body (1) inner chamber becomes the U font, and by being separated into steam-water separation chamber and condensed water drain chamber by adjusting screw rod (5) and the fixing orifice plate (11) of adjusting nut (4).Used steam enters in the steam-water separation chamber by the admission mouth of a river (2) on the top of body (1), because the pressure of self, and produce make at a high speed steam and condensed moisture from, because the proportion difference of carbonated drink, isolated condensed water is entered in the condensed water drain chamber by water-leaking hole (18), and steam is discharged by steam-expelling port (7) and entered in the next container.Spool (14) in the condensed water drain chamber is a normally off, when reaching, isolated condensed water becomes the U type after a certain amount of in the condensed water drain chamber, enter closed chamber (19), because buoyancy function, float (13) is upwards floated, drive on the directional post (12) and move, thereby spool (14) is also moved up, and drain opening (17) is opened, the condensed water in the condensed water drain chamber is discharged by the water-leaking hole (18) on the guide plate (16) by drain opening (17).When the drawdown of condensed water drain chamber, the deadweight of directional post (12), guide plate (16), spool (14) also moves down directional post (12) thereupon, contact with valve core case (15) until spool (14), drain opening (17) is closed, thereby reach this surplus vapour recover can be discharged condensed water, again can be in draining, surplus vapour is not drained, and makes steam can reclaim the purpose that makes full use of.
In order to make surplus vapour recover can be applicable to the production line of various steam consumptions, the discharge amount of condensed water can automatically adjust within the specific limits.Regulating method is that the upper end cover of directional post (12) is inserted in the center hole of orifice plate (11) on a large scale, and be shaped on a boss in the top, regulate the distance size between the boss of orifice plate (11) and directional post (12) upper end by adjusting screw rod (5), promptly may command condensed water discharge amount how much.Do not occur when directional post (12) is slided in drain opening (17) crookedly, a guide plate (16) is equipped with in the lower end of directional post (12).In order to make steam-water separation chamber not leak vapour, seal washer (6) is housed on the adjusting screw rod (5).

Claims (1)

1. a centrifugal carbonated drink is separated surplus vapour recover, it is by body, the admission mouth of a river, the body lid, adjusting nut, adjusting screw rod, seal washer, steam-expelling port, bolt, spring washer, sealing gasket, orifice plate, directional post, float, spool, valve core case, guide plate, closed chamber, drain opening, water-leaking hole is formed, between body and the body lid sealing gasket is housed, and connect by the bolt and spring washer circle, it is characterized in that: the middle part of body lid has a steam-expelling port, adjusting screw rod and adjusting nut are equipped with in both sides, the lower end of adjusting screw rod is connected with an orifice plate, has water-leaking hole on the orifice plate; The top of body is shaped on an admission mouth of a river, the bottom has drain opening, a valve core case is equipped with on drain opening top, directional post is housed in the drain opening, insert in the center hole of orifice plate the upper end of directional post, guide plate is equipped with in the lower end, has water-leaking hole on the guide plate, and spool, float and closed chamber are equipped with in the middle part of directional post.
CN 02290728 2002-12-30 2002-12-30 Centrifugal vapour-water separating tail-gas recovery Expired - Fee Related CN2594611Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 02290728 CN2594611Y (en) 2002-12-30 2002-12-30 Centrifugal vapour-water separating tail-gas recovery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 02290728 CN2594611Y (en) 2002-12-30 2002-12-30 Centrifugal vapour-water separating tail-gas recovery

Publications (1)

Publication Number Publication Date
CN2594611Y true CN2594611Y (en) 2003-12-24

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 02290728 Expired - Fee Related CN2594611Y (en) 2002-12-30 2002-12-30 Centrifugal vapour-water separating tail-gas recovery

Country Status (1)

Country Link
CN (1) CN2594611Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102840438A (en) * 2012-09-06 2012-12-26 江苏永钢集团有限公司 Drainage device for ladle dryer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102840438A (en) * 2012-09-06 2012-12-26 江苏永钢集团有限公司 Drainage device for ladle dryer

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C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee