CN101843987A - Multi-shaft slag evaporator with arc-shaped end plate - Google Patents
Multi-shaft slag evaporator with arc-shaped end plate Download PDFInfo
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- CN101843987A CN101843987A CN201010199858A CN201010199858A CN101843987A CN 101843987 A CN101843987 A CN 101843987A CN 201010199858 A CN201010199858 A CN 201010199858A CN 201010199858 A CN201010199858 A CN 201010199858A CN 101843987 A CN101843987 A CN 101843987A
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- evaporator
- heat carrier
- arc
- shell
- end plate
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes
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Abstract
The invention relates to the technical field of interlayer exothermal slag evaporation, in particular to a multi-shaft slag evaporator with an arc-shaped end plate, comprising an evaporator shell, a heat carrier shell, a slag inlet, an oil gas outlet, a residue discharging port, a stirring shaft and a stirring component. The evaporator shell consists of a horizontal barrel and an arc-shaped end plate which is firmly connected with two ends of the barrel, the heat carrier shell is sleeved outside the evaporator shell, a heat carrier circulating interlayer is formed between the heat carrier shell and the evaporator shell, and at least two stirring shafts which are respectively provided with the stirring components are installed in parallel inside the evaporator shell. The invention can improve the pressure-bearing performance of the end face of evaporator, the thermal stress generated from the evaporator shell and two ends of the heat carrier shell can be released with high efficiency, and the heat exchange area of evaporator can be maximized, therefore, the operating performance and work efficiency of the equipment are both improved.
Description
Technical field
The present invention relates to interlayer heat release slag charge evaporation technique field, particularly a kind of multi-shaft slag evaporator with arc-shaped end plate.
Background technology
Its housing of interlayer heat release evaporimeter in the past is made of evaporimeter staving and the planar end plate that is connected in the staving two ends, and the evaporimeter staving outside is set with the heat release sandwich shell of bucket body structure.Owing to be subjected to the restriction of evaporimeter shape and structure, cause following defective:, make evaporimeter end face load performance weakness 1. because of its shape of planar end plate; 2. because of its shape of planar end plate, be difficult to discharge the thermal stress that absorption comes from each side; 3. because of the heat release sandwich shell only is looped around on the evaporimeter staving, make the evaporimeter heat exchange area can not realize maximization.
Summary of the invention
The present invention is intended to solve the above-mentioned defective that prior art exists, and provide a kind of load performance that improves the evaporimeter end face, can alleviate the thermal stress that discharges evaporator shell and the generation of heat release sandwich shell two ends, make the heat exchange area of evaporimeter realize maximized multi-shaft slag evaporator with arc-shaped end plate.
The technical scheme that the present invention solves its technical problem employing is:
A kind of multi-shaft slag evaporator with arc-shaped end plate, comprise evaporator shell, heat carrier housing, slag charge inlet, oil gas vent, residue floss hole, shaft, mixing component, described evaporator shell is made of horizontal staving and the arc-shaped end plate that is fixed in these staving two ends, described heat carrier housing is sleeved on this evaporator shell outside, constitute heat carrier between the two and circulate interlayer, be set side by side with two shafts that mixing component is housed respectively in this evaporator shell at least.
The present invention compared with prior art, can improve the load performance of evaporimeter end face, the thermal stress that evaporator shell and heat carrier housing two ends are produced efficiently discharges, and makes the heat exchange area of evaporimeter realize maximization, not only improve the runnability of equipment thus, also improved the operating efficiency of equipment.
Description of drawings
Fig. 1 is a main TV structure schematic diagram of the present invention.
Fig. 2 is a plan structure schematic diagram of the present invention.
Among the figure: evaporimeter staving 1, heat carrier staving 2, FlexbleJoint 3, oil gas vent 4, heating medium outlet 5, evaporimeter staving arc-shaped end plate 6, heat carrier staving arc-shaped end plate 7, axis hole short steel pipes 8, ring flange 9, travelling gear 10, rotating seal component 11, shaft 12, mixing component 13, residue floss hole 14, support 15, heating medium inlet 16, axle sleeve 17, slag charge inlet 18.
The specific embodiment
Below in conjunction with drawings and Examples in detail the present invention is described in detail:
Referring to Fig. 1, Fig. 2, a kind of multi-shaft slag evaporator with arc-shaped end plate, its evaporimeter staving 1 two ends are connected with evaporimeter staving arc-shaped end plate 6, constitute evaporator shell thus; Heat carrier staving 2 is sleeved on evaporimeter staving 1 outside, and two ends are connected with heat carrier staving arc-shaped end plate 7, constitute the heat carrier housing thus; Form heat carrier circulation heat release interlayer between evaporator shell and heat carrier housing, this interlayer is communicated with heating medium inlet 16 and heating medium outlet 5 respectively; Slag charge inlet 18 and oil gas vent 4 pass through heat carrier staving 2 respectively and are communicated with the top of evaporimeter staving 1, and residue floss hole 14 passes through heat carrier staving 2 and is communicated with the bottom of evaporimeter staving 1; Evaporimeter integral body is horizontal installation and by support 15 support fixation, obtains bigger disengagement area with this.
As a kind of preferred structure of the present invention, described evaporator shell and both arc-shaped end plates of heat carrier housing run through axis hole short steel pipes 8 are housed, and ring flange 9 all is equipped with in axis hole short steel pipes 8 outer ends at two ends, and described shaft 12 two ends are passed this axis hole short steel pipes 8 and are installed on the ring flange 9 of axis hole short steel pipes 8 outer ends by the rotating seal component 11 of one end and the axle sleeve 17 of its other end.
At least be set up in parallel two shafts 12 in the described evaporator shell, the alternate mixing component 13 that is equipped with straggly on two shafts 12 of adjacent setting, and mixing component 13 extends to the stirring rotary area of adjacent shaft 12 mutually.The shaft 12 that Fig. 2 provides is two, is horizontally disposed with side by side.
As a kind of preferred structure of the present invention, described mixing component 13 is interrupted paddle forms.Certainly, can also be continuous screw wing form, satisfy needs under the various operating modes with this.
Absorb certain thermal stress in order to discharge, FlexbleJoint 3 is equipped with at the staving middle part of described thermophore housing.
Operation principle:
The oiliness slag charge that will account for its volume 1/2nd ratios of evaporator shell is entered in the evaporator shell by slag charge inlet 18, travelling gear 10 is under the effect of other rotary power equipment, driving two shafts 12 moves mutually, by above-mentioned working condition, not only can make the oiliness slag charge rotate thermally equivalent, a large amount of bonding curing of oiliness slag charge in also can preventing to be heated.
Heat carrier after the boiler heating is constantly entered in the heat carrier housing by heating medium inlet 16, carries out heat release by the oiliness slag charge of evaporator shell to evaporimeter inside, and the heat carrier after heat release constantly escapes and enter boiler by heating medium outlet 5 and continues heating.
Oil content in the oiliness slag charge surmounts under the condition of its boiling range temperature constantly accepting, and with the generating gasification evaporation, the vaporized oil gas oil gas vent 4 of will postponing outwards discharges, and the residue after being finished by steam raising is outwards discharged by residue floss hole 14.
By the arcuate shape of evaporimeter staving arc-shaped end plate 6 and heat carrier staving arc-shaped end plate 7, can improve the pressure of bearing of evaporator shell and heat carrier housing, also the heat exchange area of evaporimeter is realized maximization.
Cross the Cheng Qian in whole implementation, according to the distil process requirement, the outside at slag charge inlet 18 also should be equipped with devices such as valve and feed line; In the outside of oil gas vent 4, also should be equipped with devices such as condenser, fractionating tank and oiliness toxic emission pipeline; In the outside of residue floss hole 14, also should be equipped with devices such as valve.
Claims (3)
1. multi-shaft slag evaporator with arc-shaped end plate, comprise evaporator shell, heat carrier housing, slag charge inlet, oil gas vent, residue floss hole, shaft, mixing component, it is characterized in that, described evaporator shell is made of horizontal staving and the arc-shaped end plate that is fixed in these staving two ends, described heat carrier housing is sleeved on this evaporator shell outside, constitutes heat carrier between the two and circulates interlayer, is set side by side with two shafts that mixing component is housed respectively in this evaporator shell at least.
2. multi-shaft slag evaporator with arc-shaped end plate according to claim 1, it is characterized in that, described evaporator shell and both arc-shaped end plates of heat carrier housing run through the axis hole short steel pipes are housed, and ring flange all is equipped with in the axis hole short steel pipes outer end at two ends, and described shaft two ends are passed this axis hole short steel pipes and are installed on the ring flange of axis hole short steel pipes outer end by the rotating seal component of one end and the axle sleeve of its other end.
3. multi-shaft slag evaporator with arc-shaped end plate according to claim 1 is characterized in that, described mixing component is interrupted paddle form.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201010199858A CN101843987A (en) | 2010-06-11 | 2010-06-11 | Multi-shaft slag evaporator with arc-shaped end plate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201010199858A CN101843987A (en) | 2010-06-11 | 2010-06-11 | Multi-shaft slag evaporator with arc-shaped end plate |
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CN101843987A true CN101843987A (en) | 2010-09-29 |
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CN201010199858A Pending CN101843987A (en) | 2010-06-11 | 2010-06-11 | Multi-shaft slag evaporator with arc-shaped end plate |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103585773A (en) * | 2013-06-07 | 2014-02-19 | 佛山汉维科技有限公司 | Vacuum agitation type energy-saving evaporation device |
CN108159720A (en) * | 2018-03-18 | 2018-06-15 | 唐山山岛石油化学有限公司 | Depressurize the reduction vaporization method of purification of horizontal film evaporator and its organic sludge feed liquid |
CN108585970A (en) * | 2018-07-18 | 2018-09-28 | 无锡子豪环保技术发展有限公司 | A kind of fermenter of organic waste fertilizer machine |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005014667A1 (en) * | 2003-07-24 | 2005-02-17 | Bayer Technology Services Gmbh | Method and device for the elimination of volatile substances from high-viscous media |
CN2889434Y (en) * | 2006-03-24 | 2007-04-18 | 成都凯益工程技术开发有限公司 | Circulated water liquid ammonia evaporator |
CN201105169Y (en) * | 2007-11-09 | 2008-08-27 | 吴国存 | Slag charge helical evaporator |
CN201692670U (en) * | 2010-06-11 | 2011-01-05 | 吴国存 | Arc-shaped end plate multi-shaft slag evaporator |
-
2010
- 2010-06-11 CN CN201010199858A patent/CN101843987A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005014667A1 (en) * | 2003-07-24 | 2005-02-17 | Bayer Technology Services Gmbh | Method and device for the elimination of volatile substances from high-viscous media |
CN2889434Y (en) * | 2006-03-24 | 2007-04-18 | 成都凯益工程技术开发有限公司 | Circulated water liquid ammonia evaporator |
CN201105169Y (en) * | 2007-11-09 | 2008-08-27 | 吴国存 | Slag charge helical evaporator |
CN201692670U (en) * | 2010-06-11 | 2011-01-05 | 吴国存 | Arc-shaped end plate multi-shaft slag evaporator |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103585773A (en) * | 2013-06-07 | 2014-02-19 | 佛山汉维科技有限公司 | Vacuum agitation type energy-saving evaporation device |
CN103585773B (en) * | 2013-06-07 | 2015-07-15 | 佛山汉维科技有限公司 | Vacuum agitation type energy-saving evaporation device |
CN108159720A (en) * | 2018-03-18 | 2018-06-15 | 唐山山岛石油化学有限公司 | Depressurize the reduction vaporization method of purification of horizontal film evaporator and its organic sludge feed liquid |
CN108585970A (en) * | 2018-07-18 | 2018-09-28 | 无锡子豪环保技术发展有限公司 | A kind of fermenter of organic waste fertilizer machine |
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Application publication date: 20100929 |