CN102829645A - Novel horizontal evaporative condenser - Google Patents

Novel horizontal evaporative condenser Download PDF

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Publication number
CN102829645A
CN102829645A CN2012103553587A CN201210355358A CN102829645A CN 102829645 A CN102829645 A CN 102829645A CN 2012103553587 A CN2012103553587 A CN 2012103553587A CN 201210355358 A CN201210355358 A CN 201210355358A CN 102829645 A CN102829645 A CN 102829645A
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flange
tube sheet
cylindrical shell
evaporative condenser
pad
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CN2012103553587A
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Chinese (zh)
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张志平
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Individual
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Abstract

The invention discloses a novel horizontal evaporative condenser which belongs to the technical field of chemical instruments. The novel horizontal evaporative condenser comprises a barrel body (1), an end cover, a pipe plate I (22) and heat exchange pipes (26), wherein the barrel body (1) is a cylinder body which is arranged horizontally, the head end of the barrel body (1) is provided with the pipe plate I (22), the tail end of the barrel body (1) is provided with a pipe plate II (38), the heat exchange pipes (26) are arranged between the pipe plate I (22) and the pipe plate II (38) by a plurality of phi12 pull rods (24) and supporting plates (27), the head ends of the heat exchange pipes (26) are fixed on the first group of supporting plates (27) by screws and nuts, the tail ends of the heat exchange pipes (26) are fixed at the inner side of the pipe plate II (38) by screws, and four of the heat exchange pipes (26) are arranged on the pipe plate I (22) and the pipe plate II (38) in a penetrating way. According to the novel horizontal evaporative condenser, CO2 is adopted as a refrigerant, so that the utilization amount of cooling water can be reduced, the pipes after dirt is generated in the pipes can be conveniently cleaned, and the service life of devices is long.

Description

A kind of novel horizontal evaporative condenser
Technical field
The invention belongs to technical field of chemical, be specifically related to a kind of novel horizontal evaporative condenser.
Background technology
Condenser is of wide application in daily life, and the power plant will obtain condensation with the steam that many condensers are discharged turbine; In refrigeration plant, come the refrigeration steam of condensation ammonia and freon and so on condenser.Make hydro carbons and other chemical evapn condensations with condenser in the petro chemical industry.In still-process, be transformed into liquid device to steam and call condenser, all condensers are all taken away the heat of gas or steam and are turned round.
Concerning some application; Gas must be through a long pipe (coiling into solenoid) usually; So that let heat be lost in the air all around, carry steam with metal heat pipe, for the efficient additional heat sink on the pipeline of being everlasting that improves condenser is dispelled the heat with acceleration; Fin is the flat board of processing with good heat-conducting metal, and this type condenser generally also will force air to be walked through fin and the torrid zone with blower fan.
During industrial chemicals is produced, condenser one of the production equipment that is absolutely necessary.Condenser is different by its cooling medium, can be divided into water-cooled, air-cooled type, vaporation-type three major types; Water cooled condenser is divided into open shell and tube conde er, closed shell and tube condenser, tube-in-tube condenser again; Its evaporimeter is divided into horizontal-type evaporator and vertical type evaporator again.Evaporative condenser is when utilizing the outer shower water of coil pipe partly to evaporate in the absorption coil, the heat of high-temperature gas cold-producing medium and make the cold-producing medium in the pipe be cooled to liquid state by gaseous state gradually.Because of the cooling water great majority contain calcium, magnesium ion and acid carbonate.When cooling water flow during, the generation of carbonate is arranged through the metal surface.In addition, the oxygen that is dissolved in the cooling water also can cause metal erosion, forms iron rust.Because the generation of rust deposite, the heat exchange effect descends.The spraying cooling water housing outside of having to when serious is understood cramming when fouling is serious, make the heat exchange effect ineffective.The data of research show that the incrusted deposit thing is huge to the loss influence of heat transmission, can cause the increasing of energy expenditure along with sedimental increase.Even very thin one deck incrustation scale will increase equipment in the operating cost of fouling part more than 40%.Keep not containing the service life that mineral deposit can well improve effect, energy savings, prolongation equipment in the cooling duct, practice thrift production time and expense simultaneously.A lot of problems appear in traditional for a long time cleaning way such as mechanical means (scrape, brush), water under high pressure, Chemical cleaning (pickling) etc. to equipment cleaning the time: can not thoroughly remove deposits such as incrustation scale; Acid solution causes corrosion to form leak to equipment, and residual acid produces anticaustic or underdeposit corrosion to material, finally causes more exchange device; In addition; The cleaning waste liquid is poisonous, needs substantial contribution to carry out wastewater treatment, thereby causes a large amount of manual works, the loss of material.
Summary of the invention
The purpose of this invention is to provide a kind of novel horizontal evaporative condenser, compact conformation, liquid contacts with heating surface, and heat transfer coefficient is high, and the cooling water import and export temperature difference is big, adopts CO 2Make cold-producing medium, thereby reduce the consumption of cooling water, be convenient to clean behind the generation dirt in the pipe, service life of equipment is long.
The present invention realizes through following technical scheme:
A kind of novel horizontal evaporative condenser is made up of cylindrical shell 1, end cap, tube sheet I22 and heat exchanger tube 26; It is characterized in that: described cylindrical shell 1 is the cylinder of horizontal positioned; Its head end is provided with tube sheet I22; Side at tube sheet I22 links together with flat head I21 around a plurality of M24 double-screw bolts that are provided with 8 and M24 nut 9 through a circle; Be provided with a plurality of circular protrusions with the contacted one side of flat head I21; The contacted one side of tube sheet I22 is provided with a plurality of and the suitable pit of circular protrusions, and circular protrusions is connected through pad I10 with pit, makes both be in contact with one another and leaves large-area space between the face; Tail end at cylindrical shell 1 is provided with tube sheet II 38; One side of its tube sheet II 38 links together around a plurality of double-screw bolts that are provided with and nut and flat head II 37 through a circle; Be provided with a plurality of circular protrusions with flat head II 37 contacted one sides; Tube sheet II 38 contacted one sides are provided with a plurality of and the suitable pit of circular protrusions, and circular protrusions is connected through pad II 36 with pit, makes both be in contact with one another and leaves large-area space between the face; Between tube sheet I22 and tube sheet II 38, be provided with a plurality of heat exchanger tubes 26 with support plate 27 through a plurality of Φ 12 pull bars 24; Described Φ 12 pull bars 24 pass distance sink tube 25; Described heat exchanger tube 26 head ends are through on screw and the fixing first group support plate 27 of nut; Its tail end is fixed on the inboard of tube sheet II 38 through screw, wherein has two heat exchanger tubes 26 to run through and is arranged on tube sheet I22 and the tube sheet II 38.
The opposite side upper half plane of described flat head I21 is taken over 16 through Φ 32 and is provided with SO25 flange 2 15, and SO25 flange 2 15 links together through MFM25 pad 1 and M12 bolt 19 and SO25 flange 3 18.
Demifacet is taken over 13 through Φ 76 and is provided with SO65 flange 11 under the opposite side of described flat head I21, and described SO65 flange 11 is provided with SO25 flange 1 through MFM65 pad and screw 12.
Described cylindrical shell 1 head end face of cylinder vertical direction is provided with pipe platform I23 towards the upper part, the position is provided with WN32 flange 1 under advancing, and described WN32 flange 1 is provided with WN32 flange 27 through M16 bolt 4, M16 nut 5 and MFM32 pad 6.
Described cylindrical shell 1 cylindrical side tail end vertical direction is provided with pipe platform II 28 towards the upper part, described pipe platform II 28 is provided with SO25 flange 4 29 through bolt, MFM25 pad 2 31 and nut, on SO25 flange 4 29, also is provided with its blind flange 30; Be provided with pipe platform III 33 at pipe platform II 28 opposite sides, described pipe platform III 33 is provided with SO20 flange 32 through bolt, MFM20 pad 34 and nut, on SO20 flange 32, also is provided with its SO20 blind flange 35.
Described cylindrical shell 1 cylindrical side vertical direction position down is provided with saddle-F2 and saddle-S39.
Be provided with nameplate 41 through nameplate plate 40 and rivet 42 on described cylindrical shell 1 cylindrical side.
Beneficial effect of the present invention:
Described a kind of novel horizontal evaporative condenser; Applied range; Have good condenser apparatus version, technological design control method and parameters of choice, production process can be stablized carry out, and reduce investment outlay, cut down the consumption of energy, increase the business economic benefit again; Compact equipment, the vertical shell-tube type of volume ratio little; Heat transfer coefficient is bigger than vertical package; The cooling water import and export temperature difference is big, and liquid contacts with heating surface, adopts CO 2Make cold-producing medium, reduce the consumption of cooling water; Cylindrical shell 1 inner heat-transfer pipe 26 arranges that in order filling amount is about 40% of the pipe internal volume; Safe and reliable easy to operate, cryogen freezes not can the spalling pipe; The refrigerant liquid face is easy to control, should not deposit dirt in the pipe, also is convenient to clean even produced dirt, makes service life of equipment long.
Description of drawings
Fig. 1 is a front view of the present invention.
Fig. 2 is a left view of the present invention.
Fig. 3 is an A-A cutaway view among Fig. 1.
Among the figure, cylindrical shell 1, saddle-F2, WN32 flange 1, M16 bolt 4, M16 nut 5, MFM32 pad 6, WN32 flange 27, M24 double-screw bolt 8, M24 nut 9, pad I10, SO65 flange 11, MFM65 pad 12, Φ 76 takes over 13, SO25 flange 1, SO25 flange 2 15, Φ 32 take over 16, MFM25 pad 1, SO25 flange 3 18, M12 bolt 19, M12 nut 20, flat head I21, tube sheet I22, pipe platform I23, Φ 12 pull bars 24, distance sink tube 25, heat exchanger tube 26, support plate 27, pipe platform II 28, SO25 flange 4 29, blind flange 30, MFM25 pad 2 31, SO20 flange 32, pipe platform III 33, MFM20 pad 34, SO20 blind flange 35, pad II 36, flat head II 37, tube sheet II 38, saddle-S39, nameplate plate 40, nameplate 41, rivet 42.
The specific embodiment
Below in conjunction with accompanying drawing the present invention is done and to further describe:
The equipment global design requires as follows:
1, design data:
? Tube side Shell side
Design pressure (MPa) 1.0 2.0
Design temperature (C °) -30 -30
Operating pressure (MPa) 1.6 2.4
Operating temperature (C °) -20 -20
Name of material ? CO 2
2, tube sheet sealing surface and housing axis normal, its tolerance is ± 1mm.
3, equipment two ends gradient be controlled at ± 5 ° in.
4, all welding position polishings are handled, and inside and outside fillet is R3.
5, Non-Destructive Testing: according to standard JB/T4730.2-2005, detection method: X ray (A, category-B) requires 100% inspection entirely.
6, pressure test: the water pressure test (shell side) 2.75MPa, gas pressure test (shell side) 1.84MPa, seal (tightness)test (shell side) 2.2MPa.
7, device outer surface carries out anticorrosion and antirust processing, presses JB/T4711-2003 and carries out.
8, tube side is taken over perpendicular to tube sheet, and all take over shell side perpendicular to floor mounted.
Following according to above parameter designing equipment concrete structure:
A kind of novel horizontal evaporative condenser is made up of cylindrical shell 1, end cap, tube sheet I22 and heat exchanger tube 26; Described cylindrical shell 1 is the cylinder of horizontal positioned; Its head end is provided with tube sheet I22; Side at tube sheet I22 links together with flat head I21 around a plurality of M24 double-screw bolts that are provided with 8 and M24 nut 9 through a circle, is provided with a plurality of circular protrusions with the contacted one side of flat head I21, and the contacted one side of tube sheet I22 is provided with a plurality of and the suitable pit of circular protrusions; Circular protrusions is connected through pad I10 with pit, makes both be in contact with one another and leaves large-area space between the face; Tail end at cylindrical shell 1 is provided with tube sheet II 38; One side of its tube sheet II 38 links together around a plurality of double-screw bolts that are provided with and nut and flat head II 37 through a circle; Be provided with a plurality of circular protrusions with flat head II 37 contacted one sides; Tube sheet II 38 contacted one sides are provided with a plurality of and the suitable pit of circular protrusions, and circular protrusions is connected through pad II 36 with pit, makes both be in contact with one another and leaves large-area space between the face; Between tube sheet I22 and tube sheet II 38, be provided with the heat exchanger tube 26 of 264 Φ 16 through a plurality of Φ 12 pull bars 24 and support plate 27; Described Φ 12 pull bars 24 pass distance sink tube 25; Described heat exchanger tube 26 head ends are through on screw and the fixing first group support plate 27 of nut; Its tail end is fixed on the inboard of tube sheet II 38 through screw, wherein has four heat exchanger tubes 26 to run through and is arranged on tube sheet I22 and the tube sheet II 38.
The opposite side upper half plane of described flat head I21 is taken over 16 through Φ 32 and is provided with SO25 flange 2 15, and SO25 flange 2 15 links together through MFM25 pad 1 and M12 bolt 19 and SO25 flange 3 18, is designed with inlet a here.Demifacet is taken over 13 through Φ 76 and is provided with SO65 flange 11 under the opposite side of described flat head I21, and described SO65 flange 11 is provided with SO25 flange 1 through MFM65 pad and screw 12, is designed with gas outlet b here.
Described cylindrical shell 1 head end face of cylinder vertical direction is provided with pipe platform I23 towards the upper part; Advancing down, the position is provided with WN32 flange 1; Described WN32 flange 1 is provided with WN32 flange 27 through M16 bolt 4, M16 nut 5 and MFM32 pad 6, is designed with exhaust outlet c here.Described cylindrical shell 1 cylindrical side tail end vertical direction is provided with pipe platform II 28 towards the upper part; Described pipe platform II 28 is provided with SO25 flange 4 29 through bolt, MFM25 pad 2 31 and nut; On SO25 flange 4 29, also be provided with its blind flange 30, be designed with relief valve port d here; Be provided with pipe platform III 33 at pipe platform II 28 opposite sides, described pipe platform III 33 is provided with SO20 flange 32 through bolt, MFM20 pad 34 and nut, on SO20 flange 32, also is provided with its SO20 blind flange 35, is designed with CO here 2Air inlet e.Described cylindrical shell 1 cylindrical side vertical direction position down is provided with saddle-F2 and saddle-S39, makes things convenient for the horizontal positioned of equipment, the gradient of cylindrical shell 1 is controlled at ± 5 ° in.Be provided with nameplate 41 through nameplate plate 40 and rivet 42 on described cylindrical shell 1 cylindrical side, nameplate 41 subscript exposed installations are equipped with title and relevant design data.
The operation principle of equipment is: when condenser brings into operation, can open exhaust outlet c to get rid of the air in the cooling water pipe, make to be full of cooling water in the pipe; In out of service or when maintenance, can be opened gas outlet b, so that cooling water is all discharged when condenser; When condenser moves, CO 2By cylindrical shell top CO 2Air inlet e gets in the space between condenser tube, condensed CO 2The CO from the cylindrical shell bottom 2Liquid outlet f discharges; Cooling water flows into condenser by the inlet a water inlet pipe of front shroud bottom, and press glide path that water diversion disk forms from bottom to top in pipe order flow last relief valve port d outflow by front shroud top.The equipment applied range has good condenser apparatus version, technological design control method and parameters of choice, production process can be stablized carry out, and reduce investment outlay, cut down the consumption of energy, increase the business economic benefit again; Safe and reliable easy to operate, cryogen freezes not can the spalling pipe; The refrigerant liquid face is easy to control, should not deposit dirt in the pipe, also is convenient to clean even produced dirt, makes service life of equipment long.

Claims (7)

1. a novel horizontal evaporative condenser is made up of cylindrical shell (1), end cap, tube sheet I (22) and heat exchanger tube (26); It is characterized in that: described cylindrical shell (1) is the cylinder of horizontal positioned; Its head end is provided with tube sheet I (22); Side at tube sheet I (22) links together with flat head I (21) around a plurality of M24 double-screw bolts (8) that are provided with and M24 nut (9) through a circle; Be provided with a plurality of circular protrusions with the contacted one side of flat head I (21); The contacted one side of tube sheet I (22) is provided with a plurality of and the suitable pit of circular protrusions, and circular protrusions is connected through pad I (10) with pit, makes both be in contact with one another and leaves large-area space between the face; Tail end at cylindrical shell (1) is provided with tube sheet II (38); One side of its tube sheet II (38) links together around a plurality of double-screw bolts that are provided with and nut and flat head II (37) through a circle; Be provided with a plurality of circular protrusions with the contacted one side of flat head II (37); The contacted one side of tube sheet II (38) is provided with a plurality of and the suitable pit of circular protrusions, and circular protrusions is connected through pad II (36) with pit, makes both be in contact with one another and leaves large-area space between the face; Between tube sheet I (22) and tube sheet II (38), be provided with a plurality of heat exchanger tubes (26) through a plurality of Φ 12 pull bars (24) and support plate (27); Described Φ 12 pull bars (24) pass distance sink tube (25); Described heat exchanger tube (26) head end is through on screw and the fixing first group support plate of nut (27); Its tail end is fixed on the inboard of tube sheet II (38) through screw, wherein has four heat exchanger tubes (26) to run through and is arranged on tube sheet I (22) and the tube sheet II (38).
2. a kind of novel horizontal evaporative condenser according to claim 1; It is characterized in that: the opposite side upper half plane of described flat head I (21) is taken over (16) through Φ 32 and is provided with SO25 flange two (15), and SO25 flange two (15) links together with SO25 flange three (18) through MFM25 pad one (17) and M12 bolt (19); Demifacet is taken over (13) through Φ 76 and is provided with SO65 flange (11) under the opposite side of described flat head I (21), and described SO65 flange (11) is provided with SO25 flange one (14) through MFM65 pad and screw (12).
3. a kind of novel horizontal evaporative condenser according to claim 1; It is characterized in that: the position that described cylindrical shell (1) side head end vertical direction makes progress is provided with pipe platform I (23); Downward position is provided with WN32 flange one (3), and described WN32 flange one (3) is provided with WN32 flange two (7) through M16 bolt (4), M16 nut (5) and MFM32 pad (6).
4. a kind of novel horizontal evaporative condenser according to claim 1; It is characterized in that: described cylindrical shell (1) side tail end vertical direction is provided with pipe platform II (28) towards the upper part; Described pipe platform II (28) is provided with SO25 flange four (29) through bolt, MFM25 pad two (31) and nut, on SO25 flange four (29), also is provided with its blind flange (30); Be provided with pipe platform III (33) at pipe platform II (28) opposite side, described pipe platform III (33) is provided with SO20 flange (32) through bolt, MFM20 pad (34) and nut, on SO20 flange (32), also is provided with its SO20 blind flange (35).
5. a kind of novel horizontal evaporative condenser according to claim 1 is characterized in that: the position that described cylindrical shell 1 lateral vertical is directed downwards is provided with saddle-F (2) and saddle-S (39).
6. a kind of novel horizontal evaporative condenser according to claim 1 is characterized in that: described cylindrical shell 1 one sides are provided with nameplate (41) through nameplate plate (40) and rivet (42).
7. a kind of novel horizontal evaporative condenser according to claim 1; It is characterized in that: described heat exchanger tube (26) is processed by steel pipe, and its cylindrical shell (1), end cap, tube sheet I (22), support plate (27), saddle-F (2) and saddle-S (39) are processed by steel plate.
CN2012103553587A 2012-09-24 2012-09-24 Novel horizontal evaporative condenser Pending CN102829645A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104864734B (en) * 2014-02-23 2017-03-15 参化(上海)能源科技有限公司 Condenser and condensation method

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62242790A (en) * 1986-04-14 1987-10-23 Kubota Ltd Inline type heat exchanger
CN2323337Y (en) * 1997-09-11 1999-06-09 烟台冰轮股份有限公司 Horizontal condenser
CN101140120A (en) * 2007-09-21 2008-03-12 东南大学 Condenser of gravitational force refluxing type ammonia water absorbing refrigerator
CN201706954U (en) * 2010-06-13 2011-01-12 沈观耕 Heat exchange mechanism used for horizontal condenser
CN202204355U (en) * 2011-07-04 2012-04-25 德庆县银龙实业有限公司 Horizontal type heat exchanger
CN202793054U (en) * 2012-09-24 2013-03-13 张志平 Novel horizontal type evaporative condenser

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62242790A (en) * 1986-04-14 1987-10-23 Kubota Ltd Inline type heat exchanger
CN2323337Y (en) * 1997-09-11 1999-06-09 烟台冰轮股份有限公司 Horizontal condenser
CN101140120A (en) * 2007-09-21 2008-03-12 东南大学 Condenser of gravitational force refluxing type ammonia water absorbing refrigerator
CN201706954U (en) * 2010-06-13 2011-01-12 沈观耕 Heat exchange mechanism used for horizontal condenser
CN202204355U (en) * 2011-07-04 2012-04-25 德庆县银龙实业有限公司 Horizontal type heat exchanger
CN202793054U (en) * 2012-09-24 2013-03-13 张志平 Novel horizontal type evaporative condenser

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104864734B (en) * 2014-02-23 2017-03-15 参化(上海)能源科技有限公司 Condenser and condensation method

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Application publication date: 20121219