CN102327748A - Middle and low pressure steam spraying liquefier - Google Patents

Middle and low pressure steam spraying liquefier Download PDF

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Publication number
CN102327748A
CN102327748A CN201110117278A CN201110117278A CN102327748A CN 102327748 A CN102327748 A CN 102327748A CN 201110117278 A CN201110117278 A CN 201110117278A CN 201110117278 A CN201110117278 A CN 201110117278A CN 102327748 A CN102327748 A CN 102327748A
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CN
China
Prior art keywords
steam
feed liquid
liquefier
low pressure
slip
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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.)
Pending
Application number
CN201110117278A
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Chinese (zh)
Inventor
戴拓
陈继锋
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Individual
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Individual
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Publication date
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Priority to CN201110117278A priority Critical patent/CN102327748A/en
Publication of CN102327748A publication Critical patent/CN102327748A/en
Pending legal-status Critical Current

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Abstract

The invention discloses a brand-new middle and low pressure steam spraying liquefier. The purposes that: (1), the liquefier is not blocked, the liquefaction is thorough, and the liquefaction effect is improved, (2), the liquefier is suitable for middle and low pressure steam, and the applied range is improved, and (3), the vibration and the noise are eliminated, are mainly achieved. A dividing device, an impacting device, two steam inlets and two spraying openings are created for the first time; a mixing structure that an inner circular ring and an outer circular ring of slurry are synchronously in contact with steam is uniquely created; the dispersion degree of a feed liquid is improved; the contact surface of the structure with the steam is increased; the microturbulence is enhanced; and the liquefaction effect is further improved. The structure is unique, and the technique and the performance lead over world standards.

Description

The low pressure steam Jet liquefier
Technical field
Patent of the present invention is that a kind of low pressure steam that adopts heats the equipment of liquefaction to slip, is mainly used in the liquefaction of starch milk liquefaction and various feed liquids.
Background technology
External steam Jet liquefier is not suitable for domestic low middle pressure situation, is prone to simultaneously stop up, thereby can not uses.Domestic equipment one is only to be fit to low-pressure steam, and is inapplicable to the mesohigh steam greater than 0.7MPa; The 2nd, the utilization not yet in effect of steam kinetic energy, the liquefaction effect is not ideal enough, causes waste; The 3rd, resistance is big, and power consumption is high.The 4th, need constantly to regulate, just can meet the demands the big and trouble of operation easier.
Summary of the invention
(1) have two steam air intakes (4 and 7) and two steam to spray import, this is world's initiative.Steam advances through spraying formation negative pressure drive feed liquid, promptly aspirates feed liquid, has utilized steam kinetic energy again.Feed liquid is sprayed also can form negative pressure suction steam.Form steam and feed liquid and drive mutually, this also is original creation.
(2) slip flows with circular, and inside and outside annulus contacts with steam simultaneously, has increased the contact area of slip and steam, and this also is original creation, and it helps strengthening microturbulence.
(3) utilization latest modern technological scientific and technological achievement, the segmenting device of setting and crash device are world's initiatives.They mutually combine and reach the dispersion slip, increase the steam contact, strengthen microturbulence, and then have improved the liquefaction effect.
The circular feed liquid structure of (4) two steam injection equipments and formation is fit to that low pressure steam is used and steam kinetic energy effectively utilizes.
The specific embodiment
(1) annulus that forms each other through steam steam inlet pipe 4 and jet blower 5 of slip is with circular outflow.
(2) steam penetrate through steam steam inlet pipe 4 and with slip in annulus contact.
(3) steam that flows into through another steam air intake 7 penetrates and contacts with the slip outer toroid through the gap that inner cone 9 and jet blower 5 form each other.All the other steam are then added by spray-hole 14.
When (4) flowing forward,, strengthened microturbulence on the one hand, promoted that simultaneously collision disperses each other, and then improved the liquefaction effect through segmenting device 10 and crash device 13 with the steam of slip inside and outside circle loop contacts and slip.
(5) steam admission 4 has reasonable clearance not stop up with assurance with jet blower 5 each other.
Description of drawings
Fig. 1 is a low pressure steam Jet liquefier structure chart
Wherein: the 1-feed pipe, 2-expects the chamber, 3-admission flange, 4-steam inlet pipe 1,5-jet blower, 6-vapour chamber, 7-steam inlet pipe 2,8-admission flange, 9-inner cone, 10-segmenting device; 11-discharging chamber, 12-discharging flange, the 13-crash device, the 14-spray-hole, 15-sprays orifice ring, 16-charging aperture flange.

Claims (4)

1. be a kind of brand-new low pressure steam Jet liquefier, be mainly used in the heating liquefaction of starch milk and feed liquid; This equipment is by two steam inlets (4 and 7), 13, one segmenting devices of a crash device, 10 compositions such as grade; Slip is circular when flowing out; Inside and outside annulus contacts with steam respectively, and cuts apart, clashes into through crash device 10 and segmenting device 13, has increased slip microturbulence intensity and feed liquid and steam contact area; Strengthened the liquefaction effect, the reasonably interior external diameter difference of annulus guarantees that slip is not blocked.
2. the inside and outside circle loop contacts of dividing two-way and circular feed liquid according to the steam of 1, two steam inlet of right (4 and 7), the annulus inner and outer diameter forms reasonable clearance, and crash device 13 is installed in this equipment middle and lower part with segmenting device 10, is convenient to cut apart and clash into.
3. according to right 1 and 2, two steam inlets (4 and 7) and two steam injection imports have been created, 10, one crash devices 13 of a segmenting device.
4. according to right 1 and 2, created the inside and outside annulus of feed liquid,, realized for the first time that in the world feed liquid and steam aspirate drive each other simultaneously simultaneously with the steam contact structures; Help utilizing steam kinetic energy and reduce the feed liquid discharge pressure, reduce the feed liquid pressure drop.
CN201110117278A 2011-05-09 2011-05-09 Middle and low pressure steam spraying liquefier Pending CN102327748A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201110117278A CN102327748A (en) 2011-05-09 2011-05-09 Middle and low pressure steam spraying liquefier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201110117278A CN102327748A (en) 2011-05-09 2011-05-09 Middle and low pressure steam spraying liquefier

Publications (1)

Publication Number Publication Date
CN102327748A true CN102327748A (en) 2012-01-25

Family

ID=45479867

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201110117278A Pending CN102327748A (en) 2011-05-09 2011-05-09 Middle and low pressure steam spraying liquefier

Country Status (1)

Country Link
CN (1) CN102327748A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2271536Y (en) * 1996-09-26 1997-12-31 黄武宁 Jet liquefier
WO2008060218A1 (en) * 2006-11-13 2008-05-22 Tetra Laval Holdings & Finance Sa Adjustable steam injector
CN201493115U (en) * 2009-09-01 2010-06-02 兆光生物工程(邹平)有限公司 High-pressure ejector
CN201524565U (en) * 2009-09-01 2010-07-14 兆光生物工程(邹平)有限公司 Low-pressure injection and liquefaction device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2271536Y (en) * 1996-09-26 1997-12-31 黄武宁 Jet liquefier
WO2008060218A1 (en) * 2006-11-13 2008-05-22 Tetra Laval Holdings & Finance Sa Adjustable steam injector
CN201493115U (en) * 2009-09-01 2010-06-02 兆光生物工程(邹平)有限公司 High-pressure ejector
CN201524565U (en) * 2009-09-01 2010-07-14 兆光生物工程(邹平)有限公司 Low-pressure injection and liquefaction device

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Addressee: Chen Jifeng

Document name: Notification to Make Rectification

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Application publication date: 20120125