CN102805947A - Evaporator - Google Patents
Evaporator Download PDFInfo
- Publication number
- CN102805947A CN102805947A CN2012102749059A CN201210274905A CN102805947A CN 102805947 A CN102805947 A CN 102805947A CN 2012102749059 A CN2012102749059 A CN 2012102749059A CN 201210274905 A CN201210274905 A CN 201210274905A CN 102805947 A CN102805947 A CN 102805947A
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- Prior art keywords
- barrel
- heating clamber
- heating chamber
- feed
- evaporator
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Abstract
The invention belongs to the technical field of perfume production appliances, and particularly relates to an evaporator. The evaporator comprises a feed barrel. A feed inlet and sight glasses are arranged on sides of the feed barrel, a gas outlet is arranged on the top of the feed barrel, a heating chamber is arranged at the bottom of the feed barrel, tube sheets are respectively arranged at the upper end and the lower end of the heating chamber, each tube sheet is provided with a large hole and small holes, a large tube matched with each large hole and a tube array matched with the small holes are arranged in the heating chamber, a vapor inlet is arranged on the upper portion of one side wall of the heating chamber, a condensed water outlet is arranged on the lower portion of another side wall of the heating chamber, a liquid outlet barrel is arranged under the heating chamber, and a liquid outlet is arranged at the bottom of the liquid outlet barrel. The evaporator has the advantages that stability of processing environments can be kept easily, evaporation effects are enhanced, and evaporation residues are reduced.
Description
Technical field
The invention belongs to spices and produce the apparatus technical field, relate in particular to a kind of evaporimeter.
Background technology
Spices in process of production; At first be to ferment raw material to obtain zymotic fluid, carry out centrifugal treating to zymotic fluid then, carry out the sedimentation degerming to the suspension in the zymotic fluid; Obtain spices liquid first product then, carry out spices liquid first product rectifying, vacuumize and handle the formation finished product at last.In the production process of whole spices, when spices liquid first product carried out the rectifying evaporation, mostly the evaporimeter of employing was in barrel, to heat direct evaporation at present.This type of evaporimeter exists following defective: when the evaporator evaporation feed liquid, along with continuing of heating, the liquid level of feed liquid descends gradually in the charging basket.By the time the liquid level of feed liquid drops to when exposing heating tube, and can make heating surface (area) (HS diminishing gradually heating this moment, thereby make the effect of heating evaporation reduce, and the evaporation of residual amount increases.Because the heating tube that exposes also in heating, can make whole evaporimeter go wrong, cause whole evaporation technology conditional instability simultaneously.
Summary of the invention
The objective of the invention is to solve above-described technical problem, a kind of evaporimeter is provided, its technical scheme is following:
A kind of evaporimeter comprises barrel, and described barrel sidepiece is provided with charging aperture and visor; The top of described barrel is provided with the gas outlet, and the bottom of described barrel is provided with heating clamber, and described heating clamber top and bottom are provided with tube sheet; Offer macropore and aperture on the described tube sheet, be provided with the bassoon that is complementary with macropore in the described heating clamber, be provided with the tubulation that is complementary with aperture in the described heating clamber; Described heating clamber side wall upper part offers the steam inlet; The lower sidewall of described heating clamber is provided with condensation-water drain, and the below of described heating clamber is provided with out fluid cylinder, and the described bottom that goes out fluid cylinder is provided with liquid outlet.
Optimal way does, described barrel and go out to be connected with circulation pipe between the fluid cylinder.
The present invention at first puts into feed liquid in the barrel through charging aperture in use, and feed liquid enters into out in the fluid cylinder through tubulation and bassoon then.Be incorporated into vapours the whole heating clamber from the steam inlet then.Vapours is full of in the whole heating clamber very soon, begins tubulation in the heating clamber and bassoon are heated.Along with the carrying out of heating, the feed liquid in tubulation and the bassoon constantly is heated to form gas.Gas rises to liquid level with the mode of bubble, and then from the gas outlet at barrel top, goes out.Along with being heated of feed liquid, vapours is also cooled off becomes condensed water, draws from condensation-water drain then.Along with continuing of heating, because the feed liquid of heat rises, cold feed liquid descends, and can form heat in the evaporimeter and rise cold circulation of falling, and makes the feed liquid liquid level constantly descend.The decline situation that simultaneously can observe the feed liquid liquid level through visor determines whether stopping heating.After stopping heating, open liquid outlet, draw evaporation of residual liquid.
The present invention is at barrel and go out to be connected with circulation pipe between the fluid cylinder, makes barrel and go out the heat that also can form feed liquid between the fluid cylinder and rise the cold circulation of falling, and further strengthens evaporation effect.
The tubulation arrangement mode that adopts in the heating clamber of the present invention helps preventing the tubulation obstruction and makes things convenient for the cleaning and dredging tubulation, generally mostly is that bassoon is in the heating clamber center, and tubulation is centrosymmetric around bassoon and evenly distributes then.And the setting of bassoon be for improve and tubulation between the feed liquid cycle efficieny.
The invention has the beneficial effects as follows: when the evaporation feed liquid, when liquid level is in lower position, can also guarantee that the heating surface (area) (HS of liquid level is constant, help keeping the stable of process environments that improve evaporation effect, the evaporation of residual amount reduces.
Description of drawings
Fig. 1 sketch map of the present invention.
Fig. 2 tube plate structure sketch map.
The specific embodiment
Specify embodiment below in conjunction with Fig. 1 and Fig. 2:
A kind of evaporimeter comprises barrel 1, and described barrel 1 sidepiece is provided with charging aperture 2 and visor 3; The top of described barrel 1 is provided with gas outlet 4; The bottom of described barrel 1 is provided with heating clamber 5, and described heating clamber 5 top and bottom are provided with tube sheet 6, offers macropore 61 and aperture 62 on the described tube sheet 6; Be provided with the bassoon 51 that is complementary with macropore 61 in the described heating clamber 5; Be provided with the tubulation 52 that is complementary with aperture 62 in the described heating clamber 5, described heating clamber 5 side wall upper part offer steam inlet 7, and the lower sidewall of described heating clamber 5 is provided with condensation-water drain 8; The below of described heating clamber 5 is provided with out fluid cylinder 9, and the described bottom that goes out fluid cylinder 9 is provided with liquid outlet 91.
Optimal way does, described barrel 1 and go out to be connected with circulation pipe 10 between the fluid cylinder 9.
The present invention at first puts into feed liquid in the barrel 1 through charging aperture 2 in use, and feed liquid enters into out in the fluid cylinder 9 through tubulation 52 and bassoon 51 then.Be incorporated into vapours the whole heating clamber 5 from steam inlet 7 then.Vapours is full of in the whole heating clamber 5 very soon, begins tubulation in the heating clamber 5 52 and bassoon 51 are heated.Along with the carrying out of heating, the feed liquid in tubulation 52 and the bassoon 51 constantly is heated to form gas.Gas rises to liquid level with the mode of bubble, and then from the gas outlet 4 at barrel 1 top, goes out.Along with being heated of feed liquid, vapours is also cooled off becomes condensed water, draws from condensation-water drain 8 then.Along with continuing of heating, because the feed liquid of heat rises, cold feed liquid descends, and can form heat in the evaporimeter and rise cold circulation of falling, and makes the feed liquid liquid level constantly descend.The decline situation that simultaneously can observe the feed liquid liquid level through visor 3 determines whether stopping heating.After stopping heating, open liquid outlet 91, draw evaporation of residual liquid.
Claims (2)
1. an evaporimeter comprises barrel, it is characterized in that; Described barrel sidepiece is provided with charging aperture and visor, and the top of described barrel is provided with the gas outlet, and the bottom of described barrel is provided with heating clamber; Described heating clamber top and bottom are provided with tube sheet, offer macropore and aperture on the described tube sheet, are provided with the bassoon that is complementary with macropore in the described heating clamber; Be provided with the tubulation that is complementary with aperture in the described heating clamber, described heating clamber side wall upper part offers the steam inlet, and the lower sidewall of described heating clamber is provided with condensation-water drain; The below of described heating clamber is provided with out fluid cylinder, and the described bottom that goes out fluid cylinder is provided with liquid outlet.
2. evaporimeter as claimed in claim 1 is characterized in that, described barrel and go out to be connected with circulation pipe between the fluid cylinder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012102749059A CN102805947A (en) | 2012-08-03 | 2012-08-03 | Evaporator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012102749059A CN102805947A (en) | 2012-08-03 | 2012-08-03 | Evaporator |
Publications (1)
Publication Number | Publication Date |
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CN102805947A true CN102805947A (en) | 2012-12-05 |
Family
ID=47229924
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN2012102749059A Pending CN102805947A (en) | 2012-08-03 | 2012-08-03 | Evaporator |
Country Status (1)
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CN (1) | CN102805947A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103721430A (en) * | 2013-12-31 | 2014-04-16 | 浙江诺睿特生物科技有限公司 | Evaporator |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2077739U (en) * | 1990-12-06 | 1991-05-29 | 武汉冷冻机厂 | Horizontal high efficiency tube array condensation evaporator |
CN2629793Y (en) * | 2003-02-20 | 2004-08-04 | 中国石化集团南京化学工业有限公司 | Efficient concentrated crystalliznig evaporator |
CN202724717U (en) * | 2012-08-03 | 2013-02-13 | 浙江诺睿特生物科技有限公司 | Evaporator |
-
2012
- 2012-08-03 CN CN2012102749059A patent/CN102805947A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2077739U (en) * | 1990-12-06 | 1991-05-29 | 武汉冷冻机厂 | Horizontal high efficiency tube array condensation evaporator |
CN2629793Y (en) * | 2003-02-20 | 2004-08-04 | 中国石化集团南京化学工业有限公司 | Efficient concentrated crystalliznig evaporator |
CN202724717U (en) * | 2012-08-03 | 2013-02-13 | 浙江诺睿特生物科技有限公司 | Evaporator |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103721430A (en) * | 2013-12-31 | 2014-04-16 | 浙江诺睿特生物科技有限公司 | Evaporator |
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Application publication date: 20121205 |